Deconstruction of lignocellulosic biomass with ionic liquids
Open accessAbstract
This paper reviews the application of ionic liquids to the deconstruction and fractionation of lignocellulosic biomass, in a process step that is commonly called pretreatment. It is divided into four parts: the first gives background information on lignocellulosic biomass and ionic liquids; the second focuses on the solubility of lignocellulosic biomass (and the individual biopolymers within it) in ionic liquids; the third emphasises the deconstruction effects brought about by the use of ionic liquids as a solvent; the fourth part deals with practical considerations regarding the design of ionic liquid based deconstruction processes.
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TL;DR
This review surveys ionic liquids for deconstruction and fractionation of lignocellulosic biomass, covering biomass composition, biopolymer solubility, deconstruction effects, and process design. It distinguishes Dissolution and Ionosolv approaches and highlights ionic liquid cost, stability, recycling, water sensitivity, and downstream inhibition as key challenges.
Key findings
- Cellulose solubility in ionic liquids depends strongly on anion hydrogen-bond basicity; high Kamlet-Taft β (>0.8) is apparent, with [C₂C₁im][MeCO₂] dissolving up to 15 wt% Avicel cellulose at 110 °C, while long alkyl/glycol chains or protic cations reduce solubility.
- Lignin solubility varies widely, from virtually insoluble to 30 wt%; e.g. [C₂C₁im][MeCO₂] dissolves 30 wt% Kraft lignin at 90 °C, [C₁C₁im][MeSO₄] and [C₄C₁im][MeSO₄] dissolve 26 wt% at 50 °C, and [C₄C₁im][PF₆] dissolves 0–1 wt%.
- [C₂C₁im][MeCO₂] treatment removes 17–65% lignin and 0–83% hemicellulose depending on feedstock and conditions; softwood is generally less delignified. Saccharification yields after ionic liquid pretreatment vary, e.g. Miscanthus with [C₄C₁im][MeSO₃] gave 98% glucose, [C₄C₁im][HSO₄] 91%, and [C₂C₁im][MeCO₂] 73%; maple with [C₄C₁im][MeCO₂] gave 74% glucose.
- Process challenges include ionic liquid thermal stability: T₀.₀₁/₁₀h for [C₄C₁im][MeCO₂] was measured as 102 °C, implying a maximum process temperature of ca. 90 °C, yet many biomass treatments run above this. Residual ionic liquid inhibits enzymes and yeast; adding 10% v/v ionic liquid decreased cellulase activity by 70–85%, and as little as 0.25% residual [C₂C₁im][MeCO₂] completely inhibited yeast growth and biofuel production.
Methods
- Review article divided into four parts: background on lignocellulosic biomass and ionic liquids; solubility of lignocellulosic biomass and individual biopolymers in ionic liquids; deconstruction effects of ionic liquids as solvents; and practical considerations for ionic liquid based deconstruction processes.
- Synthesizes literature and tabulates ionic liquid properties, cellulose/lignin/lignocellulose solubility, delignification and hemicellulose removal, saccharification yields, lignin recovery, and ionic liquid stability/recycling.
- No new primary experimental data are presented except the authors report an unpublished T₀.₀₁/₁₀h measurement for [C₄C₁im][MeCO₂] as 102 °C.
Limitations
- The paper does not state a formal limitations section; as a review, it notes that data variability and inconsistent protocols complicate quantitative comparison, e.g. cellulose solubility measurements were performed under different temperature, dissolution time, cellulose degree of polymerisation, moisture content, and ionic liquid purity.
- Evident from the text: many cited studies are preliminary, especially ionic liquid recycling studies (often only 1–10 reuses), and the review identifies unresolved scale-up issues including ionic liquid cost, drying/reconcentration energy, water sensitivity, ionic liquid degradation, downstream inhibition, and the absence of commercialised ionic liquid deconstruction processes.
- Evident from the text: the review relies on literature with limited feedstock and ionic liquid coverage; for example, lignin solubility studies are essentially all with imidazolium ionic liquids, and experimental validation of the relative importance of the imidazolium cation for lignin solubilisation is still missing.
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Cites
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Claims the paper makes
0 of 154 cited sources checked · 0 supported · 0 flagged
- Findingcitation
A protic cation prevents cellulose solubilisation entirely in many cases.
“A protic cation prevents cellulose solubilisation entirely in many cases.57,91”
Quote in the paperNot a substantial claim0 of 2 sources checked - Findingown data
The tabulated data show that [C2C1im][MeCO2] is capable of partially removing both hemicellulose and lignin simultaneously.
“Despite these difficulties, the tabulated data show that [C 2 C 1 im][MeCO 2 ] is capable of partially removing both hemicellulose and lignin simultaneously.”
Quote in the paperNot a substantial claim - Findingreasoning
The choice of cation also affects cellulose solubility considerably.
“The choice of cation also affects solubility considerably.”
Quote in the paperNot a substantial claim - Findingnone given
For [C4C1im][HSO4] and its acid-base ionic liquid analogue [C4Him][HSO4], delignification seems more extensive than with [C2C1im][MeCO2].
“For [C 4 C 1 im][HSO 4 ], and also for its acid-base ionic liquid analogue [C 4 Him][HSO 4 ], the delignification seems to be more extensive than with [C 2 C 1 im]-[MeCO 2 ].”
Quote in the paperNot a substantial claim - Findingnone given
Lengthening the alkyl (or glycol) chains on the cation progressively reduces cellulose solubility.
“Lengthening the alkyl (or glycol) chains on the cation progressively reduces cellulose solubility.”
Quote in the paperNot a substantial claim
- Findingown data
The importance of a high Kamlet-Taft β value (>0.8) for cellulose solubility is apparent despite measurements being performed under a variety of conditions.
“Although the measurements were performed under a variety of conditions (e.g.different temperature, dissolution time, cellulose degree of polymerisation, moisture content, ionic liquid purity), which affect the maximum solubility, the importance of a high β value (>0.8) is apparent.”
Quote in the paperSubstantial claim - Findingreasoning
Less extensive delignification and hemicellulose removal is generally achieved for softwood (pine) feedstocks compared to herbaceous and hardwood lignocellulose.
“Less extensive delignification and hemicellulose removal is generally achieved for softwood ( pine) feedstocks compared to herbaceous and hardwood lignocellulose.”
Quote in the paperNot a substantial claim - Findingnone given
Hydroxyl groups on the alkyl chains, which increase the hydrogen-bond acidity of the ionic liquid, also reduce the solubility of cellulose.
“Hydroxyl groups on the alkyl chains, functionalities that increase the hydrogen-bond acidity of the ionic liquid, also reduce the solubility of cellulose.”
Quote in the paperNot a substantial claim - Findingreasoning
[C4C1pyrr][MeCO2], based on an aliphatic ammonium cation, decomposed completely within just 30 h at 120 °C.
“The ionic liquid [C 4 C 1 pyrr][MeCO 2 ], based on an aliphatic (cyclic) ammonium cation, which usually show lower resistance to decomposition than imidazolium cations, decomposed completely within just 30 h at 120 °C.”
Quote in the paperNot a substantial claim - Findingcitation
Wang et al. reused [CvC2C1im]Cl once after a dissolution treatment of 5 wt% pine and did not detect any reduction in performance.
“Wang et al. reused [CvC 2 C 1 im]Cl once after a dissolution treatment of 5 wt% pine and did not detect any reduction in performance.121”
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- Findingcitation
Optimisation of carbohydrate yield after deconstructing wheat straw with a [C2C1im][MeCO2] process using Design of Experiment resulted in an optimal process temperature of 158 °C.
“Optimisation of the carbohydrate yield after deconstructing wheat straw with a [C 2 C 1 im][MeCO 2 ] process using the Design of Experiment (DOE) approach resulted in an optimal process temperature of 158 °C.175”
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- Findingnone given
The majority of biomass deconstruction experiments using these ionic liquids have been performed at temperatures greatly in excess of 90 °C.
“It is important to note that the majority of biomass deconstruction experiments using these ionic liquids have been performed at temperatures greatly in excess of this limit.”
Quote in the paperNot a substantial claim- Rests on an assumption: The majority of biomass deconstruction experiments using [C2C1im][MeCO2] and [C4C1im][MeCO2] have been performed at temperatures greatly in excess of 90 °C.
- Findingcitation
The optimal process temperature of 158 °C for wheat straw was at 50.5 wt% water content.
“This was at 50.5 wt% water content, where the effect of water on the ionic liquid is likely to be considerable.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [175] source
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- Findingcitation
Dissolved cellulose has no effect on the ionic liquid decomposition temperature, even up to 12% cellulose.
“It has been shown that anions that are very nucleophilic, such as chloride and acetate, can lower T onset to around 200 °C, while dissolved cellulose appears to have no effect on the IL decomposition temperature, even up to 12% cellulose.74”
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- Findingown data
The T0.01/10h for [C4C1im][MeCO2] is 102 °C.
“Due to the lack of data in the literature, we measured T 0.01/10 h for [C 4 C 1 im][MeCO 2 ] and determined it as 102 °C.174”
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- Findingcitation
Decomposition of [C2C1im][MeCO2] and [C2C1im]Cl at 100-130 °C was almost complete within 4 months.
“Decomposition of [C 2 C 1 im]-[MeCO 2 ] and [C 2 C 1 im]Cl at 100-130 °C was almost complete within 4 months.177”
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- Findingcitation
Very nucleophilic anions such as chloride and acetate can lower the onset temperature of decomposition of ionic liquids to around 200 °C.
“It has been shown that anions that are very nucleophilic, such as chloride and acetate, can lower T onset to around 200 °C, while dissolved cellulose appears to have no effect on the IL decomposition temperature, even up to 12% cellulose.74”
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- Findingcitation
The economic viability of ionic liquid deconstruction is very sensitive to the efficiency of ionic liquid recycling.
“It has been shown that the economic viability of ionic liquid deconstruction is very sensitive to the efficiency of ionic liquid recycling and therefore decomposition must be avoided.171”
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- Findingcitation
Rogers and co-workers observed 15% weight loss within 10 min when treating bagasse and pine with [C2C1im][MeCO2] at 185 °C.
“Data from deconstruction experiments support this: Rogers and co-workers have observed 15% weight loss within 10 min when treating bagasse and pine with [C 2 C 1 im][MeCO 2 ] at 185 °C.119”
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- Findingcitation
Another study reused [C4C1im]Cl 7 times for fractionation of legume straw with ionic liquid water mixtures.
“Another study reused [C 4 C 1 im]Cl 7 times for fractionation of legume straw with ionic liquid water mixtures.140”
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- Findingcitation
The biomass type plays a role with regard to the energy consumption of grinding, with grasses requiring less grinding energy than woody biomass.
“The biomass type also plays a role with regard to the energy consumption of grinding, with grasses requiring less grinding energy than woody biomass.184”
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- Findingreasoning
Higher pulp recoveries were observed when the ionic liquid was reused.
“In addition, higher pulp recoveries were observed when the ionic liquid was reused, which could be due to less extensive lignin removal.”
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- Findingcitation
Li et al. reused [CvC2C1im]Cl three times for deconstructing 8 wt% Eucalyptus using the Dissolution Process and found that saccharification yields decreased progressively.
“Li et al. reused [CvC 2 C 1 im]Cl three times for deconstructing 8 wt% Eucalyptus using the Dissolution Process and found that the saccharification yields decreased progressively.129b”
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- Findingcitation
More than 10% of the energy contained in willow was required for grinding air-dried chips to a particle size of <1 mm.
“For example, it was shown that more than 10% of the energy contained in willow was required for grinding air-dried chips to a particle size of <1 mm.184”
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- Findingcitation
Rogers and co-workers reused [C2C1im][MeCO2] once after treatment of 4.8 wt% bagasse at 185 °C for 10 min; the delignification efficiency dropped from 63% to 38%.
“Rogers and co-workers reused [C 2 C 1 im][MeCO 2 ] once after treatment of 4.8 wt% bagasse at 185 °C for 10 min; 119 the delignification efficiency dropped from 63% to 38%.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [119] source
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- Findingcitation
A recent study shows that ionic liquids could help to reduce the energy input for grinding wood-derived lignocellulose.
“A recent study shows that ionic liquids could help to reduce the energy input for grinding wood-derived lignocellulose.”
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- Findingcitation
The energy input to grinding for corn stover conversion was estimated to be 1.1% of the energy content of corn stover (0.186 GJ of 17.0 GJ per tonne).
“The energy input to grinding for corn stover conversion was estimated to be 1.1% of the energy content of corn stover (0.186 GJ of 17.0 GJ per tonne).185”
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- Findingcitation
The savings in grinding energy were shown to be due to the lubricating properties of ionic liquids, rather than partial modification of the lignocellulose matrix.
“The savings were shown to be due to the lubricating properties of ionic liquids, rather than partial modification of the lignocellulose matrix.”
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- Findingcitation
Almost quantitative removal of lignin has been achieved with the Ionosolv Process.
“In spite of this, almost quantitative removal of lignin has been achieved.55”
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- Findingcitation
[C2C1im]Cl also affects growth of the yeast, but to a lesser extent.
“The ionic liquid [C 2 C 1 im]Cl also affects growth of the yeast, but to a lesser extent.188”
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- Findingnone given
The ionic liquids used for biomass dissolution are highly hydroscopic.
“The ionic liquids used for biomass dissolution are highly hydroscopic (Fig. 21).”
Quote in the paperSubstantial claim - Findingnone given
Careful analysis of the ionic liquids that are actually used in the chemicals processing industry on a large scale shows that they are mostly based on protic cations, such as [C1Him]+, usually combined with a mineral acid derived anion, such as Cl-.
“Careful analysis of the ionic liquids that are actually used in the chemicals processing industry on a large scale shows that they are mostly based on protic cations, such as [C 1 Him] + , usually combined with a mineral acid derived anion, such as Cl -.”
Quote in the paperNot a substantial claim - Findingnone given
The most effective ionic liquid so far for the Dissolution Process has been [C2C1im][MeCO2].
“The most effective ionic liquid so far has been [C 2 C 1 im][MeCO 2 ].”
Quote in the paperNot a substantial claim - Findingcitation
To date there are no available commercial processes for upgrading lignin into chemicals.
“Although there has very recently been an increased interest in the conversion of lignin into chemicals, 9 to date there are no available commercial processes for this upgrading.”
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- Findingcitation
Water was more effective in removing residual ionic liquid than either pure ethanol or acetone-ethanol mixtures.
“The study found that water was more effective in removing residual ionic liquid than either pure ethanol or acetone-ethanol mixtures.”
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- Findingcitation
Chloride ions also inhibit enzymatic activity in concentrations of less than 1%.
“The chloride ions also inhibit enzymatic activity in concentrations of less than 1%.195”
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- Findingcitation
The first techno-economical analysis modelling of ionic liquid deconstruction has determined that among the investigated variables the order of importance/sensitivity is ionic liquid price > biomass loading > recycling rate.
“The first techno-economical analysis modelling of ionic liquid deconstruction has determined that among the investigated variables the order of importance/ sensitivity is ionic liquid price > biomass loading > recycling rate.171”
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- Findingcitation
As little as 0.25% residual [C2C1im][MeCO2] in the fermentation broth will completely inhibit yeast growth and biofuel production.
“As little as 0.25% residual [C 2 C 1 im][MeCO 2 ] in the fermentation broth will completely inhibit yeast growth and biofuel production.188”
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- Findingnone given
Lignin precipitation requires more water than is generally used to precipitate cellulose from the Dissolution Process solutions.
“Lignin precipitation requires more water than is generally used to precipitate cellulose from the Dissolution Process solutions.”
Quote in the paperNot a substantial claim - Findingcitation
For other applications, ionic liquids have been applied as process solvents on a large scale.
“In spite of this complaint, for other applications, ionic liquids have been applied as process solvents on a large scale.51”
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- Premisecitation
The lignin crust is one of the major obstacles for an energy-efficient biomass deconstruction process.
“The lignin crust has been identified as one of the major obstacles for an energy-efficient biomass deconstruction process.8”
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- Premisecitation
Native lignin prevents access of polysaccharide hydrolases to their substrates.
“Native lignin not only prevents access of polysaccharide hydrolases to their substrates, but modified lignin adhering to the pulp after pretreatment also causes unproductive binding of hydrolases.25”
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- Premisecitation
Lignocellulosic biomass is available at lower cost than starch and sucrose based materials.
“Lignocellulosic biomass is the most abundant plant material on our planet and therefore available in much higher quantities (also due to higher yields per area of land) and at lower cost than starch and sucrose based materials.1c,4”
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- Premisecitation
A major obstacle to competitive lignocellulose utilisation is that cost-effective technologies for processing lignocellulosic material into fuels and chemicals are yet to be commercially developed.
“A major obstacle to competitive lignocellulose utilisation is that cost-effective technologies for processing lignocellulosic material into fuels and chemicals are yet to be commercially developed.6”
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- Premisecitation
Lignocellulosic biomass is the most abundant plant material on our planet.
“Lignocellulosic biomass is the most abundant plant material on our planet and therefore available in much higher quantities (also due to higher yields per area of land) and at lower cost than starch and sucrose based materials.1c,4”
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- Premisenone given
Ionic liquids are applied to the deconstruction and fractionation of lignocellulosic biomass as a pretreatment step.
“This paper reviews the application of ionic liquids to the deconstruction and fractionation of lignocellulosic biomass, in a process step that is commonly called pretreatment.”
Quote in the paperSubstantial claim - Premisecitation
Deconstruction of lignocellulose is likely to account for an important fraction of the energy requirement for biomass processing.
“The deconstruction of lignocellulose is likely to account for an important fraction of the energy requirement for biomass processing.8”
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- Premisecitation
Lignocellulosic biomass is available in much higher quantities than starch and sucrose based materials.
“Lignocellulosic biomass is the most abundant plant material on our planet and therefore available in much higher quantities (also due to higher yields per area of land) and at lower cost than starch and sucrose based materials.1c,4”
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- Premisecitation
The US produces enough lignocellulosic feedstock today to substitute 30% of their liquid transport fuels with biofuels.
“It has been estimated that the US produces enough lignocellulosic feedstock today to substitute 30% of their liquid transport fuels with biofuels.4”
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- Interpretationcitation
Utilisation of lignocellulose as a biofuel feedstock is likely to provide much higher CO2 emission savings than starch- and sucrose-based feedstocks.
“Utilisation of lignocellulose as a biofuel feedstock is likely to provide much higher CO 2 emission savings.2,5”
Quote in the paperNot a substantial claim0 of 2 sources checked - Interpretationnone given
A relatively high lignin content combined with a high guaiacyl to syringyl ratio in the lignin is considered to be the reason for softwood's higher resistance to delignification compared to grass or hardwood biomass.
“A relatively high lignin content combined with a high guaiacyl to syringyl ratio in the lignin is considered to be the reason for its higher resistance to delignification compared to grass or hardwood biomass.”
Quote in the paperNot a substantial claim - Interpretationreasoning
These cross-links must be broken by chemically hydrolysing the ester bonds in order to obtain an effective deconstruction process.
“Thus, these cross-links must be broken by chemically hydrolysing the ester bonds in order to obtain an effective deconstruction process.31”
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- Premisenone given
Ferulic acid can dimerise hemicellulose chains.
“Ferulic acid can also dimerise hemicellulose chains (Fig. 10).”
Quote in the paperNot a substantial claim - Interpretationcitation
Utilisation of pentoses, particularly xylose, will improve the economics of biofuel production.
“The utilisation of the pentoses, particularly xylose, will improve the economics of biofuel production.42”
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- Premisecitation
The ultrastructure of lignocellulose affects the diffusion of chemicals into and out of wood chips during chemical deconstruction.
“This structure also affects the diffusion of chemicals into and out of wood chips during chemical deconstruction.33”
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- Premisecitation
In grasses, lignin-carbohydrate complexes contain ferulic acid.
“In grasses, these lignin-carbohydrate complexes contain ferulic acid (Fig. 9).”
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- Premisereasoning
Softwood is the most recalcitrant lignocellulosic feedstock type.
“Although this feedstock is very abundant, it is also the most recalcitrant feedstock type.”
Quote in the paperNot a substantial claim - Premisecitation
Regenerated cellulose from ionic liquid solutions has significantly accelerated hydrolysis with cellulases compared to native cellulose.
“This also results in significantly accelerated hydrolysis with cellulases compared to native cellulose, 77 an effect that is very attractive in terms of the biorefinery and has sparked interest in the use of cellulose dissolving ionic liquids in lignocellulose deconstruction.”
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- Premisenone given
The extent of cross-linking via lignin-carbohydrate complexes has been correlated with increased cell wall rigidity and resistance to enzymatic digestion.
“The extent of cross-linking via lignin-carbohydrate complexes has been correlated with increased cell wall rigidity and resistance to enzymatic digestion.”
Quote in the paperNot a substantial claim - Premisecitation
In softwood and hardwood, direct complexes between lignin and carbohydrates are present.
“In softwood and hardwood, direct complexes between lignin and carbohydrates are present.32”
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- Premisecitation
Lignin can be a source of compounds that inhibit hydrolases and fermentative organisms, including syringyl aldehyde and vanillic acid.
“Lignin can also be a source of compounds that inhibit hydrolases and fermentative organisms, including syringyl aldehyde and vanillic acid.26”
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- Premisecitation
The ionic liquid anion plays an important role in determining an ionic liquid's ability to dissolve cellulose.
“It has been observed that the ionic liquid anion plays an important role in determining an ionic liquid's ability to dissolve cellulose.69a”
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- Premisecitation
Modified lignin adhering to pulp after pretreatment causes unproductive binding of hydrolases.
“Native lignin not only prevents access of polysaccharide hydrolases to their substrates, but modified lignin adhering to the pulp after pretreatment also causes unproductive binding of hydrolases.25”
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- Premisecitation
Ferulic acid is initially bonded to hemicellulose (arabinoxylan) via ester bonds.
“Ferulic acid is initially bonded to hemicellulose (arabinoxylan) via ester bonds.28”
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- Interpretationreasoning
Traditional paper pulping processes are optimised for high cellulose yield and fibre strength, which does not match the needs of the biorefinery industry.
“These processes are optimised for high cellulose yield and fibre strength, which are required for paper production.This does not match the needs of the biorefinery industry, which needs high quality fermentable sugar solutions at extremely low cost, and highpurity by-product streams that add value.”
Quote in the paperSubstantial claim - Interpretationcitation
Recovery of non-fermentable components as co-products, particularly lignin, will allow multiple revenue streams compared to a single fermentation product.
“In addition, the recovery of non-fermentable components as co-products, particularly lignin, will allow multiple revenue streams compared to a single fermentation product. 1”
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- Premisecitation
A range of ionic liquids, typically with 1,3-dialkylimidazolium cations, are effective cellulose solvents.
“More recently, it has been demonstrated that a range of ionic liquids, typically with 1,3-dialkylimidazolium cations, are also effective cellulose solvents.69”
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- Interpretationcitation
The dissolving power of relevant ionic liquids has been typically attributed to strong hydrogen-bonding interactions between the anions and equatorial hydroxyl groups on cellulose.
“The dissolving power of these relevant ionic liquids has been typically attributed to strong hydrogen-bonding interactions between the anions and equatorial hydroxyl groups on the cellulose.”
Quote in the paperNot a substantial claim - Premisecitation
The order of molecular weight reduction of lignins by ionic liquids was sulfates > lactate > acetate > chloride > phosphates.
“The order of molecular weight reduction was sulfates > lactate > acetate > chloride > phosphates.”
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- Interpretationreasoning
Water tolerance is dependent on the nature of the ionic liquid.
“Therefore it appears, as one might expect, that water tolerance is dependent on the nature of the ionic liquid.”
Quote in the paperSubstantial claim - Premisecitation
The enol ether product was observed as an intermediate when the ionic liquid contained a coordinating anion.
“The enol ether product in Fig. 23 (top) was observed as an intermediate when the ionic liquid contained a coordinating anion.”
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- Premisecitation
The less basic or sometimes even acidic environment of non-acetate ionic liquids can cause more hemicellulose conversion to furfurals and/or humins, which is not seen for the acetate ionic liquids.
“As a potential drawback, the less basic or sometimes even acidic environment of non-acetate ionic liquids can cause more hemicellulose conversion to furfurals and/or humins, which is not seen for the acetate ionic liquids.55”
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- Premisecitation
Differences in reactivity of β-O-4 aryl ether cleavage by hydrogen-bond acidic monoalkylimidazolium ionic liquids depended on the anion.
“Differences in reactivity depending on the anion were observed.”
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- Premisecitation
These findings agree with empirical solvent polarity measurements, which are applied to predict solvent properties, among others, rate constants and solubility.
“These findings also agree with empirical solvent polarity measurements, which are applied to predict solvent properties, among others, rate constants and solubility.46a”
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- Premisecitation
Suitable ionic liquids for cellulose dissolution contain anions that can form strong hydrogen bonds with hydroxyl groups, e.g. chloride, carboxylates, dialkyl phosphates, dialkyl and trialkylphosphonates, and amino acid anions.
“Suitable ionic liquids identified to date contain anions that can form strong hydrogen bonds with hydroxyl groups, e.g.chloride, 69a carboxylates (acetate, formate, propionate, lactate), 78 dialkyl phosphates, dialkyl and trialkylphosphonates 69d and amino acid anions.79”
Quote in the paperSubstantial claim0 of 3 sources checked- cites 69a
Not checked in the free run.
- cites [78] source
Not checked in the free run.
- cites 69d,79
Not checked in the free run.
- Premisecitation
In ionic liquids, particularly those with non-functionalised cations such as dialkylimidazolium, the hydrogen-bond basicity/value of β is primarily influenced by the anion.
“In ionic liquids, particularly those with non-functionalised cations such as dialkylimidazolium, the hydrogen-bond basicity/value of β is primarily influenced by the anion.56”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [56] source
Not checked in the free run.
- Interpretationreasoning
Ionic liquid treatments typically lead to enrichment of cellulose in the recovered solids.
“Therefore, the ionic liquids treatments typically lead to enrichment of cellulose in the recovered solids.”
Quote in the paperNot a substantial claim - Premisecitation
Increased sulfur content of lignin after treatment with ionic liquids with sulfur containing anions such as sulfonates, sulfamates and sulfates has been reported.
“In support of this, an increased sulfur content of the lignin after treatment with ionic liquids with sulfur containing anions such as sulfonates and sulfamates (e.g.[ABS] -and acesulfamate) 52,53 and sulfates ([MeSO 4 ] -and [HSO 4 ] -) 55 has been reported.”
Quote in the paperNot a substantial claim0 of 3 sources checked - Premisecitation
Less coordinating anions such as [BF4]- resulted in elimination of the γ hydroxyl methylene group, forming formaldehyde.
“Less coordinating anions such as [BF 4 ] -resulted in elimination of the γ hydroxyl methylene group, resulting in formation of formaldehyde.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [142] source
Not checked in the free run.
- Premisecitation
Oxidation of Organosolv beech lignin in ionic liquids in the presence of transition metals and molecular oxygen has been demonstrated.
“The oxidation of Organosolv beech lignin in ionic liquids in the presence of transition metals and molecular oxygen has been demonstrated by Stärk et al. 143”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [143] source
Not checked in the free run.
- Premisecitation
Close association between anions and cellulose hydroxyl groups was confirmed by NMR studies on ionic liquid solutions of glucose and cellobiose and molecular dynamics studies of [C2C1im][MeCO2] or [C4C1im]Cl with celloligomers.
“This close association was confirmed by NMR studies on ionic liquid solutions of glucose and cellobiose 81 and molecular dynamics studies of the interaction of [C 2 C 1 im][MeCO 2 ] 82 or [C 4 C 1 im]Cl 83 with celloligomers.”
Quote in the paperSubstantial claim0 of 3 sources checked - Premisecitation
The 1H-NMR spectral shift of the ethanol hydroxyl proton peak in the presence of ionic liquids has been correlated with the cellulose solubilisation power of imidazolium ionic liquids.
“The 1 H-NMR spectral shift of the ethanol hydroxyl proton peak in the presence of ionic liquids has been correlated with the cellulose solubilisation power of imidazolium ionic liquids.84”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [84] source
Not checked in the free run.
- Premisecitation
Ionic liquids with more exotic hydrogen-bond basic anions, such as phosphorthioates or phosphorselenoates, have proven to be less stable than the earlier discoveries.
“Ionic liquids with more exotic hydrogen-bond basic anions, such as phosphorthioates or phosphorselenoates, have proven to be less stable than the earlier discoveries.80”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [80] source
Not checked in the free run.
- Premisecitation
Ionic liquids that dissolve cellulose are characterised by high values for parameters describing solvent hydrogen-bond basicity.
“For cellulose solubility, it was shown that ionic liquids that dissolve cellulose are characterised by high values for parameters describing solvent hydrogen-bond basicity.”
Quote in the paperNot a substantial claim - Premisecitation
An α,β-dehydration reaction was reported for both [C2C1im]Cl and [C2C1im][MeCO2] on a lignin model compound.
“An α,β-dehydration reaction was reported for both ionic liquids.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [135] source
Not checked in the free run.
- Interpretationreasoning
Sulfonate and sulfate containing ionic liquids appear to be currently the most potent ionic liquids in terms of separating cellulose from lignin (and hemicelluloses).
“Therefore sulfonate and sulfate containing ionic liquids appear to be the currently most potent ionic liquids in terms of separating cellulose from lignin (and hemicelluloses).”
Quote in the paperSubstantial claim - Premisecitation
The dehydration of the lignin model compound was significantly faster in [C2C1im][MeCO2] than in [C2C1im]Cl.
“The dehydration was significantly faster in [C 2 C 1 im][MeCO 2 ] than in [C 2 C 1 im]Cl, possibly reflecting the acetate's greater basicity and affinity towards water.141”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [135] source
Not checked in the free run.
- Interpretationreasoning
The T0.01/10h for [C2C1im][MeCO2] is anticipated to be very similar to that of [C4C1im][MeCO2] because their anion and cation core are very similar.
“Since the anion and the cation core are very similar for [C 4 C 1 im][MeCO 2 ] and [C 2 C 1 im][MeCO 2 ], the T 0.01/10 h for [C 2 C 1 im][MeCO 2 ] is anticipated to be very similar.”
Quote in the paperSubstantial claim - Interpretationcitation
Ionic liquid decomposition must be avoided to maintain the economic viability of ionic liquid deconstruction.
“It has been shown that the economic viability of ionic liquid deconstruction is very sensitive to the efficiency of ionic liquid recycling and therefore decomposition must be avoided.171”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [171] source
Not checked in the free run.
- Interpretationreasoning
The maximum process temperature for [C4C1im][MeCO2] and [C2C1im][MeCO2] is about 90 °C.
“This would result in a maximum process temperature of ca.90 °C for both of these very commonly used ionic liquids.”
Quote in the paperSubstantial claim - Interpretationcitation
For [C1C1im][Me2PO4] and [C2C1im][MeCO2], high basicity of anions reduces acidity so much that glucose production cannot be observed.
“The latter two ionic liquids can dissolve cellulose, but the relatively high basicity of their anions, which are both counter-ions of weak acids (with pK a values of 1.29 155 for dimethyl phosphoric acid and 4.76 for acetic acid) reduces the acidity of these solutions so much that glucose production cannot be observed.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 146a
Not checked in the free run.
- Premisecitation
Almost quantitative yield of glucose and cellobiose with very little HMF was achieved when hydrolysing pure cellulose in acidified [C4C1im]Cl with the incremental water method.
“Almost quantitative yield of glucose and cellobiose with very little HMF was achieved when hydrolysing pure cellulose in acidified [C 4 C 1 im]Cl with the incremental water method.149”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [149] source
Not checked in the free run.
- Interpretationreasoning
Lignocellulose deconstruction with ionic liquids will only be successful if the ionic liquid can be recycled, due to the high solvent cost.
“Lignocellulose deconstruction with ionic liquids will only be successful if the ionic liquid can be recycled, due to the high solvent cost.”
Quote in the paperSubstantial claim - Premisenone given
When acidic protons are present in a mixture of proton acceptors, the weaker acid always forms.
“When acidic protons are present in a mixture of proton acceptors the weaker acid always forms.”
Quote in the paperNot a substantial claim - Premisecitation
In ionic liquids with basic anions, such as [C2C1im][MeCO2], hemicellulose remains largely oligomeric, which is typical for alkaline deconstruction processes.
“In ionic liquids with basic anions, such as [C 2 C 1 im][MeCO 2 ], the hemicellulose remains largely oligomeric, 136 which is typical for alkaline deconstruction processes.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [136] source
Not checked in the free run.
- Interpretationreasoning
The decrease of monomer yield at higher water content is probably due to decreased lignocellulose solubility.
“The decrease of the monomer yield at higher water content is probably due to decreased lignocellulose solubility.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 129a
Not checked in the free run.
- Interpretationreasoning
Partial degradation of ionic liquid below Tonset affects recycling efficiency and the properties of the ionic liquid as degradation products accumulate.
“This partial degradation affects the recycling efficiency as well as the properties of the ionic liquid as degradation products accumulate.”
Quote in the paperSubstantial claim - Interpretationreasoning
This gives rise to 'solvent levelling' of acidity, with the ionic liquid anion playing the role of the solvent's basic functional group.
“This gives rise to 'solvent levelling' of the acidity, with the ionic liquid anion playing the role of the solvent's basic functional group.”
Quote in the paperSubstantial claim - Premisecitation
Use of [C4C1im][MeCO2] led to destruction of heterogeneous solid acid catalysts.
“The use of [C 4 C 1 im][MeCO 2 ] led to destruction of the heterogeneous catalysts.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [152]
Not checked in the free run.
- Interpretationcitation
The low monomeric sugar yield in anhydrous acidified ionic liquid is likely due to limited water available, halting hydrolysis at the oligomer stage.
“This is likely due to the limited amount of water available in the anhydrous system, halting the hydrolysis at the oligomer stage.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 129a
Not checked in the free run.
- Premisecitation
In solid acid catalysed hydrolysis, production of short cellulose oligomers was observed rather than complete hydrolysis to monomers.
“Similarly to soluble acids, the production of short cellulose oligomers was observed rather than complete hydrolysis to monomers.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [152]
Not checked in the free run.
- Premisecitation
Best conditions using 1:3 NMP to ionic liquid resulted in 69% total reducing sugar yield and 39% glucose yield.
“The best conditions (using a 1 : 3 ration of NMP to ionic liquid) resulted in a 69% total reducing sugar yield and 39% glucose yield.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [150] source
Not checked in the free run.
- Interpretationreasoning
Performing chemical hydrolysis of cellulose and hemicellulose while dissolved in an ionic liquid has the advantage that glycosidic bonds are more accessible in homogeneous solution, allowing milder hydrolysis conditions.
“Performing the (chemical) hydrolysis of cellulose and hemicellulose while dissolved in an ionic liquid has the advantage that the glycosidic bonds are more accessible in homogenous solution, allowing milder hydrolysis conditions.”
Quote in the paperNot a substantial claim - Interpretationreasoning
The long-term thermal stability of the ionic liquid under process conditions will be important for near-quantitative recycling.
“As already mentioned, the long-term thermal stability of the ionic liquid under process conditions will be important for the near-quantitative recycling.”
Quote in the paperSubstantial claim - Study design and conductcitation
The product solution in the [C4C1im]Cl/NMP hydrolysis study was not analysed for degradation products or lignin.
“The product solution was not analysed for degradation products or lignin.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [150] source
Not checked in the free run.
- Premisecitation
Lignocellulose deconstruction with ionic liquids typically involves heating well above 100 °C, with up to 190 °C reported.
“Lignocellulose deconstruction with ionic liquids typically involves heatingin many studies well above 100 °C (up to 190 °C has been reported).52,119”
Quote in the paperNot a substantial claim0 of 2 sources checked - Interpretationreasoning
One repeat is not sufficient to assess performance on an industrial scale where many cycles will be necessary to make an ionic liquid deconstruction process viable.
“Although this is a start, one repeat is not sufficient to assess performance on an industrial scale where many cycles will be necessary to make an ionic liquid deconstruction process viable.”
Quote in the paperSubstantial claim - Interpretationreasoning
It is likely that the extractable organic small molecules will be found in the filtrate.
“It is also likely that this is where the extractable organic small molecules will be found (oils, acetic acid, ferulic acid, vanillin, other small lignin fragments, furfurals, levulinic acid etc.).”
Quote in the paperNot a substantial claim - Interpretationreasoning
It is by cation design that an ionic liquid could be optimised for washing.
“Therefore, it is by cation design that an ionic liquid could be optimised for washing.”
Quote in the paperNot a substantial claim - Interpretationcitation
The preliminary observations that fractionation and, in some cases, the saccharification are somewhat adversely affected by repeated use of the ionic liquid suggests that a clean-up step is likely to be necessary.
“The preliminary observations that fractionation and, in some cases, the saccharification are somewhat adversely affected by repeated use of the ionic liquid suggests that a clean-up step is likely to be necessary.”
Quote in the paperSubstantial claim - Premisecitation
The larger the ratio between initial and final particle size, the more mechanical energy is required for the size reduction, all other conditions being equal.
“However, the larger the ratio between initial and final particle size, the more mechanical energy is required for the size reduction, all other conditions being equal.183”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [183] source
Not checked in the free run.
- Interpretationreasoning
These studies show results for the changing performance of the ionic liquids in the process step in which they were used, not the condition of the ionic liquid solution that was being recycled.
“These studies show results for the changing performance of the ionic liquids in the process step in which they were used, not the condition of the ionic liquid solution that was being recycled.”
Quote in the paperSubstantial claim - Interpretationcitation
Hardwoods and softwoods may require prohibitive quantities of energy to grind to fine powders.
“In contrast, hardwoods and softwoods may require prohibitive quantities of energy to grind to fine powders.183,186”
Quote in the paperSubstantial claim0 of 2 sources checked - Interpretationcitation
For the Ionosolv and Dissolution Processes, it is important that the cellulose fraction be as free of ionic liquid as possible to avoid unwanted deactivation of the saccharification enzymes or toxicity to the fermenting microorganisms.
“For the Ionosolv, as well as the Dissolution Process, it is important that the cellulose fraction be as free of ionic liquid as possible to avoid unwanted deactivation of the saccharification enzymes 162 or toxicity to the fermenting microorganisms.188”
Quote in the paperSubstantial claim0 of 2 sources checked - Premisereasoning
Water can be added to the ionic liquid phase to precipitate the dissolved lignin for further processing or incineration.
“Water can be added to the ionic liquid phase to precipitate the dissolved lignin for further processing or incineration.52,53,55”
Quote in the paperNot a substantial claim0 of 3 sources checked - Premisereasoning
The solubility of cellulose in the ionic liquids used in the Dissolution Process is sensitive to the presence of water.
“As has been noted above, the solubility of cellulose in the ionic liquids used in the Dissolution Process is sensitive to the presence of water.”
Quote in the paperSubstantial claim - Interpretationreasoning
Even the lower end of the 90-160 °C temperature range coincides with some degradation of [C2C1im][MeCO2] on these timescales.
“Even the lower end of this temperature range coincides with some degradation of [C 2 C 1 im][MeCO 2 ] on these timescales (see above).”
Quote in the paperSubstantial claim - Interpretationnone given
The ability to sell the lignin and/or its products will heavily impact on the process costs.
“In addition, the ability to sell the lignin and/or its products will heavily impact on the process costs.”
Quote in the paperSubstantial claim - Interpretationreasoning
For the Ionosolv Process to be viable, it will be necessary to reconcentrate the ionic liquid for reuse.
“For the Ionosolv Process to be viable, it will be necessary to reconcentrate the ionic liquid for reuse.”
Quote in the paperSubstantial claim - Interpretationreasoning
Protic ionic liquids are much cheaper than those with fully alkylated cations used in most academic laboratories.
“This makes these ionic liquids much cheaper than those with fully alkylated cations (e.g.[C 2 C 1 im] + in [C 2 C 1 im][MeCO 2 ]) used in most academic laboratories.”
Quote in the paperNot a substantial claim - Interpretationreasoning
Since good cellulose solubility has been related to the ionic liquid anion's β value in the same way as its hydrophilicity, we cannot see a way to address the water problem through ionic liquid design.
“Since good cellulose solubility (Fig. 18) has been related to the ionic liquid anion's β value in the same way as its hydrophilicity (Fig. 21), we cannot see a way to address this problem through ionic liquid design.”
Quote in the paperSubstantial claim - Interpretationreasoning
The relatively acidic nature of the ionic liquid keeps the dissolved lignin in fully protonated form (phenol groups rather than phenolates), making water precipitation possible.
“This is made possible by the relatively acidic nature of the ionic liquid, which keeps the dissolved lignin in fully protonated form ( phenol groups rather than phenolates).”
Quote in the paperSubstantial claim - Interpretationreasoning
Unless drying is a prominent feature of the process, the build-up of water in the ionic liquid will lead to levels that will prevent cellulose dissolution and hence stop the process.
“Unless drying is a prominent feature of the process, the build-up of water in the ionic liquid will lead to levels that will prevent cellulose dissolution and hence stop the process.”
Quote in the paperSubstantial claim- Rests on an assumption: Raw biomass typically contains about 50% water and even thoroughly air-dried biomass typically contains around 5-10 wt% residual moisture.
- Interpretationreasoning
Deconstruction with ionic liquid will only be viable if its advantages outweigh the drawbacks of ionic liquids, most prominently the cost of ionic liquids relative to the value of the substrate processed by them.
“However, deconstruction with ionic liquid will only be viable if its advantages outweigh the drawbacks of ionic liquids, most prominently the cost of ionic liquids relative to the value of the substrate processed by them.”
Quote in the paperSubstantial claim- Rests on an assumption: Ionic liquids are the most expensive solvents currently under investigation for lignocellulose deconstruction.
- Interpretationnone given
A major and widely highlighted advantage of the ionic liquid Dissolution Process compared to other pretreatment options is its ability to decrystallise the cellulose portion of lignocellulosic biomass and simultaneously disrupt the lignin and hemicellulose network.
“As already mentioned, a major and widely highlighted advantage of the ionic liquid Dissolution Process compared to other pretreatment options is its ability to decrystallise the cellulose portion of lignocellulosic biomass and simultaneously disrupt the lignin and hemicellulose network.”
Quote in the paperSubstantial claim
- May combine two claims. 67
- Classified as probably not a substantial claim. 54
- The quote only partly states this claim. 1
May combine two claims.
FindingreasoningThe overall trend is that a higher temperature or a longer treatment time results in more lignin and hemicellulose removal.
“The overall trend is that a higher temperature or a longer treatment time results in more lignin and hemicellulose removal.”
Quote in the paperNot a substantial claimMay combine two claims.
Findingnone givenLignin removal was reported to be between 17% and 65%, while hemicellulose removal varied between 0% and 83%.
“Lignin removal was reported to be between 17% and 65%, while hemicellulose removal varied between 0% and 83%.”
Quote in the paperNot a substantial claimMay combine two claims.
FindingcitationAn increase of the water content in the system appears to lead to less delignification and lower subsequent saccharification yields.
“An increase of the water content in the system appears to lead to less delignification (and also to lower subsequent saccharification yields).55”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [55] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing).
FindingcitationOhno and co-workers reported rapid dissolution (5 min) of 15 wt% cellulose in aqueous solutions of tetrabutylphosphonium hydroxide and tetrabutylammonium hydroxide containing 40-50% water by weight at room temperature.
“Interestingly, Ohno and co-workers recently reported the rapid dissolution (5 min) of 15 wt% cellulose in aqueous solutions of tetrabutylphosphonium hydroxide, [(C 4 ) 4 P]OH, and tetrabutylammonium hydroxide, [(C 4 ) 4 N]OH, containing 40-50% water by weight at room temperature.102”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [102] source
Not checked in the free run.
May combine two claims.
Findingown dataLignin solubility seems strongly affected by the choice of anion, although hydrogen-bond basicity does not need to be as high as for cellulose; some mid-range basic ionic liquids seem to be better solvents for lignin than their more hydrogen-bond basic relatives.
“As with cellulose, the solubility seems to be strongly affected by the choice of anion, although hydrogen-bond basicity does not need to be as high as for cellulose; some mid-range basic ionic liquids seem to be better solvents for lignin than their more hydrogen-bond basic relatives (Fig. 19).”
Quote in the paperSubstantial claimMay combine two claims.
FindingcitationWu et al. increased biomass loading stepwise from 4.8 wt% to 50 wt% for [C2C1im][MeCO2] at 125 °C for 1 h and observed that lignin removal decreased substantially from 44% to 8%.
“They increased the loading stepwise from 4.8 wt% up to 50 wt% for [C 2 C 1 im]-[MeCO 2 ] at 125 °C for 1 h and observed that lignin removal decreased substantially from 44% to 8%.123a”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 123a
Not checked in the free run.
May combine two claims.
Findingnone givenReported delignification and hemicellulose removal for chloride based ionic liquids are significantly lower than achieved with other ionic liquids under the conditions applied, coupled with very low glucose yields after enzymatic saccharification.
“The reported delignification and hemicellulose removal are significantly lower than achieved with other ionic liquids under the conditions applied.These were coupled with very low glucose yields after enzymatic saccharification.”
Quote in the paperSubstantial claimMay combine two claims.
Findingown dataDecomposition of [C2C1im][MeCO2] is much slower at 60 °C below Tonset, but still detectable.
“The decomposition is much slower at 60 °C below T onset , but still detectable (Fig. 26).”
Quote in the paperNot a substantial claimMay combine two claims.
Findingcitation[C2C1im]Cl and [C4C1im]Cl are long-term stable at 120 °C and show signs of decomposition at 140 °C.
“[C 2 C 1 im]Cl and [C 4 C 1 im]Cl are longterm stable at 120 °C and show signs of decomposition at 140 °C.176”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [176] source
Not checked in the free run.
May combine two claims.
FindingcitationThe type of both cation and anion influences the temperature of decomposition of ionic liquids, with a strong effect of the anion.
“It has been found that the type of both cation and anion influences the temperature of decomposition, 169 but there is a strong effect of the anion.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [169] source
Not checked in the free run.
May combine two claims.
FindingcitationTonset is only an indicator of ionic liquid stability under process conditions, because significant mass loss occurs below Tonset.
“If the stability of an ionic liquid under process conditions is of interest, T onset is only an indicator, as significant mass loss occurs below T onset (Fig. 26).170”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [170] source
Not checked in the free run.
May combine two claims.
FindingcitationMethanesulfonate based ionic liquids [C2C1im][MeSO3] and [C4C1im][MeSO3] are stable at 140 °C and only slowly degrade at 200 °C.
“The same study showed methanesulfonate based ionic liquids [C 2 C 1 im][MeSO 3 ] and [C 4 C 1 im][MeSO 3 ] to be stable at 140 °C and to only slowly degrade at 200 °C.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [176] source
Not checked in the free run.
May combine two claims.
FindingcitationAn increase of the amount of recovered pulp was observed after the 4th cycle; the lignin content in the recovered solid remained constant over the course of the experiment.
“An increase of the amount of recovered pulp was observed after the 4th cycle; the lignin content in the recovered solid remained constant over the course of the experiment.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [140] source
Not checked in the free run.
May combine two claims.
FindingcitationBrandt et al. detected varying amounts of monomeric hemicellulose and furfurals in liquors of [C4C1im][MeSO4], [C4C1im][HSO4] and [C4C1im][MeSO3] after treatment of Miscanthus with fresh ionic liquid, the quantities detected depending on the ionic liquid acidity and the treatment length.
“Brandt et al. detected varying amounts of monomeric hemicellulose and furfurals in liquors of [C 4 C 1 im][MeSO 4 ], [C 4 C 1 im][HSO 4 ] and [C 4 C 1 im][MeSO 3 ] after treatment of Miscanthus with fresh ionic liquid, the quantities detected depending on the ionic liquid acidity and the treatment length.55”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [55] source
Not checked in the free run.
May combine two claims.
FindingcitationWu et al. reused [C2C1im][MeCO2] 10 times at 4.8 wt% corn stover loading at 125 °C; the saccharification yield was unaffected, as was the decrystallisation of the cellulose, but less lignin was extracted in the last cycle compared to the first one (44% reduced to 20%).
“Wu et al. reused [C 2 C 1 im][MeCO 2 ] 10 times at 4.8 wt% corn stover loading at 125 °C.The saccharification yield was unaffected, as was the decrystallisation of the cellulose, but less lignin was extracted in the last cycle compared to the first one (44% reduced to 20%).”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
FindingcitationFrancisco et al. found that adsorption of glucose onto zeolites from ionic liquid water mixtures and subsequent desorption into water could be used for removing sugars from the ionic liquid liquor.
“Francisco et al. found that adsorption of glucose onto zeolites from ionic liquid water mixtures and subsequent desorption into water could be used for removing sugars from the ionic liquid liquor.180”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [180] source
Not checked in the free run.
May combine two claims.
FindingcitationLan et al. fractionated bagasse into cellulose, hemicelluloses and lignin four times with the same batch of [C4C1im]Cl; the delignification efficiency dropped slightly, the saccharification yield was not investigated.
“Lan et al. fractionated bagasse into cellulose, hemicelluloses and lignin four times with the same batch of [C 4 C 1 im]Cl.178 The delignification efficiency dropped slightly, the saccharification yield was not investigated.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [178]
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing).
FindingreasoningMost studies in the ionic liquid pretreatment field use finely milled biomass for their experiments, due to pronounced particle size effects on the solubilisation.
“Most studies in the ionic liquid pretreatment field use finely milled biomass for their experiments, due to pronounced particle size effects on the solubilisation.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
FindingcitationBrennan et al. devised an extraction method for glucose and xylose recovery from [C2C1im][MeCO2] using boronates such as naphthalene-2-boronate.
“Brennan et al. have devised an extraction method for glucose and xylose recovery from [C 2 C 1 im][MeCO 2 ] using boronates such as naphthalene-2-boronate.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [182] source
Not checked in the free run.
May combine two claims.
FindingcitationShill et al. attempted to lower the energy use for drying the ionic liquid after dissolution of Miscanthus by re-concentrating diluted ionic liquids with K3PO4, but saw a negative effect on saccharification yields after reuse.
“Shill et al. have attempted to lower the energy use for drying the ionic liquid after dissolution of Miscanthus by re-concentrating diluted ionic liquids with the inorganic salt potassium phosphate (K 3 PO 4 ), but saw a negative effect on saccharification yields after reuse.181”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [181] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
FindingcitationViell and Marquardt reported the breaking up of air-dried beech wood chips into individual cell walls under dissolving conditions; this was accomplished by vigorous stirring for 2 h.
“As an alternative, Viell and Marquardt reported the breaking up of air-dried beech wood chips into individual cell walls under dissolving conditions; 116 this was accomplished by vigorous stirring for 2 h.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [116] source
Not checked in the free run.
May combine two claims.
FindingcitationThe non-baseline power consumption for grinding pine chips was significantly reduced (up to 75%), while a finer powder was obtained, by adding the ionic liquid before the grinding.
“The non-baseline power consumption for grinding pine chips was significantly reduced (up to 75%), while a finer powder was obtained, by adding the ionic liquid before the grinding.187”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [187] source
Not checked in the free run.
Probably not a substantial claim: may not pass S4 (based).
Findingnone givenNo reported work has considered the direct use of the filtrate solution.
“No reported work has considered the direct use of this solution.”
Quote in the paperNot a substantial claimMay combine two claims.
FindingcitationAn advantage of the Dissolution Process is the recovery of the majority of the hemicelluloses with the pulp, although along with some lignin, as the delignification in this process is not complete.
“An advantage of the Dissolution Process is the recovery of the majority of the hemicelluloses with the pulp, although along with some lignin, as the delignification in this process is not complete.109,136”
Quote in the paperNot a substantial claim0 of 2 sources checkedMay combine two claims.
Findingnone givenCellulose has extremely low water solubility, and the water content of acetate and chloride based ionic liquids has been observed to have the single greatest impact on the cellulose solubility.
“Cellulose has extremely low water solubility, and the water content of acetate and chloride based ionic liquids has been observed to have the single greatest impact on the cellulose solubility.”
Quote in the paperSubstantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
FindingcitationOne case of deconstruction of corn stover with an [C2C1im][MeCO2]/N-methylpyrrolidone mixture has been reported.
“One case of deconstruction of corn stover with an [C 2 C 1 im]-[MeCO 2 ]/N-methylpyrrolidone mixture has been reported.193”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [193] source
Not checked in the free run.
May combine two claims.
Findingnone givenThe pretreatment in the Dissolution Process is typically conducted by heating the biomass-ionic liquid mixture to 90-160 °C for 3-16 hours, at which point the majority (or entirety) of the biomass is dissolved in the ionic liquid and partial lignin and hemicellulose removal from the lignocellulose has occurred.
“The pretreatment is typically conducted by heating the biomass-ionic liquid mixture to 90-160 °C for 3-16 hours, at which point the majority (or entirety) of the biomass is dissolved in the ionic liquid and partial lignin and hemicellulose removal from the lignocellulose has occurred.”
Quote in the paperNot a substantial claimMay combine two claims.
FindingcitationWhile disruption of the lignin and hemicellulose network is a prerequisite for enzymatic saccharification to occur to a significant extent, the changed crystallinity of the cellulose also has a measurable positive impact on the speed of saccharification.
“While the latter is a prerequisite for enzymatic saccharification to occur to significant extent, the changed crystallinity of the cellulose also has a measurable positive impact on the speed of saccharification.76a”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 76a
Not checked in the free run.
May combine two claims.
FindingcitationSome ionic liquids with protic cations may not be applicable in the Dissolution Process due to their increased hydrogen-bond acidity, although others have been shown to be good cellulose solvents.
“Unfortunately, some ionic liquids with protic cations may not be applicable in the Dissolution Process due to their increased hydrogen-bond acidity, although others have been shown to be good cellulose solvents.78b”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites 78b
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing).
Findingown dataIn the studies of lignin and hemicellulose removal by [C2C1im][MeCO2] compiled in Table 5, the biomass loading was in the range of 5-8%.
“The biomass loading in these studies was in the range of 5-8%.”
Quote in the paperNot a substantial claimMay combine two claims.
FindingcitationThe ionic liquid cation was identified as the main cause of cell toxicity, as control experiments with inorganic acetate and chloride salts did not lead to the same level of inhibition.
“The ionic liquid cation was identified as the main cause of cell toxicity, as control experiments with inorganic acetate and chloride salts did not lead to the same level of inhibition.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [188] source
Not checked in the free run.
Probably not a substantial claim: may not pass S2 (checkable), S3 (load-bearing).
PremisecitationUtilisation of lignin is highly desirable for the economic viability of any future biorefinery.
“In addition, the utilisation of the non-carbohydrate fraction, lignin, 9 is highly desirable for the economic viability of any future biorefinery.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [9] source
Not checked in the free run.
Classified as probably not a substantial claim.
PremisereasoningAn additional deconstruction step (pretreatment) is required to bring sugar polymers into a form suitable for hydrolysis and subsequent fermentation.
“In order to access the carbohydrates in the biomass for biological conversion, an additional deconstruction step (also commonly called pretreatment or pre-treatment) is required to bring the sugar polymers into a form suitable for hydrolysis and subsequent fermentation.”
Quote in the paperSubstantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based). May combine two claims.
Premisenone givenGrass lignin can usually be extracted by aqueous alkali, which is not effective on softwood.
“Grass lignin can usually be extracted by aqueous alkali, which is not effective on softwood.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
Premisenone givenRemoval of lignin is usually a combination of chemical fragmentation and the ability of the liquor to solvate the modified lignin fragments.
“The removal of lignin is usually a combination of chemical fragmentation and the ability of the liquor to solvate the modified lignin fragments.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
PremisecitationSaccharification can be catalysed by chemicals or enzymes; enzymes are usually preferred due to their higher selectivity.
“The saccharification can be catalysed by chemicals 41 or enzymes; enzymes are usually preferred due to their higher selectivity.17”
Quote in the paperNot a substantial claim0 of 2 sources checkedProbably not a substantial claim: may not pass S3 (load-bearing).
PremisecitationIonic liquids have been investigated as solvents for the processing of biomass.
“They have found a number of industrial applications 51 and have also been investigated as solvents for the processing of biomass.10”
Quote in the paperNot a substantial claim0 of 2 sources checkedProbably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
PremisecitationHarsher conditions are usually required for softwood delignification and strong nucleophiles such as sulfide or sulfite ions are added to aid lignin removal and prevent lignin recondensation.
“Therefore, harsher conditions are usually required and strong nucleophiles such as sulfide (S 2-, in Kraft pulping) or sulfite ([HSO 3 ] -) ions are added to aid lignin removal and prevent lignin recondensation.34”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [34] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Premisenone givenCellulose is the most abundant polymer in lignocellulose (35-50%).
“Cellulose is the most abundant polymer in lignocellulose (35-50%).”
Quote in the paperNot a substantial claimClassified as probably not a substantial claim.
PremisereasoningVarying chemical composition and structural differences between lignocellulose types affect their amenability to deconstruction.
“The varying chemical composition (e.g.lignin composition and content) and structural differences (e.g.cell wall thickness and pore size) between the lignocellulose types affects their amenability to deconstruction, therefore the effects of each lignocellulose deconstruction method should be assessed on a number of feedstocks.”
Quote in the paperSubstantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
PremisecitationThe current industrially most developed lignocellulose treatment processes are in the area of paper production.
“The current industrially most developed lignocellulose treatment processes are therefore in the area of paper production.40”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [40] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing), S4 (based). May combine two claims.
Premisenone givenHardwoods have more complex structures than softwoods, containing large water-conducting pores or vessels surrounded by narrower fibre cells.
“Hardwoods have more complex structures than softwoods, containing large waterconducting pores or vessels that are surrounded by narrower fibre cells (Fig. 13).”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
Premisenone givenHardwood lignin is made up of guaiacyl and syringyl units and the main hemicellulose sugar is xylose.
“The lignin is made up of guaiacyl and syringyl units and the main hemicellulose sugar is not mannose but xylose.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Premisenone givenPerennial bioenergy grasses are more resistant to lignocellulose deconstruction than annual grasses such as straws.
“but they are more resistant to lignocellulose deconstruction than annual grasses such as straws.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
Premisenone givenThe focus of biomass deconstruction processes is the preparation of carbohydrates (mainly cellulose) from lignocellulose in a form that can be readily metabolised by fermenting microorganisms.
“The focus of those working on biomass deconstruction processes is thus the preparation of carbohydrates (mainly cellulose) from lignocellulose in a form that can be readily metabolised by fermenting microorganisms.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
Premisenone givenMost chemical deconstruction methods modify lignin by hydrolysing its ether bonds, but only some remove it from the pulp.
“Most chemical deconstruction methods modify lignin by hydrolysing its ether bonds, but only some remove it from the pulp (e.g.Organosolv pulping, some base treatments, sulfite pretreatment and pulping, Kraft pulping).”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based). The quote only partly states this claim.
Premisenone givenDirect lignin-carbohydrate complexes in softwood and hardwood are thought to be formed during lignification when hydroxyl groups of carbohydrates react with electrophilic ketone methide intermediates of growing lignin polymer chains.
“It is thought that they are formed during lignification, when hydroxyl groups of carbohydrates react with electrophilic ketone methide intermediates of the growing lignin polymer chains.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
PremisecitationSignificant instability of the NMO/cellulose solution above 90 °C and redox activity of the NMO have been viewed as problems.
“Nevertheless, significant instability of the NMO/cellulose solution above 90 °C and redox activity of the NMO have been viewed as problems, 67 which could be addressed by the use of more stable cellulose dissolving ionic liquids.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [67] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing).
Premisenone givenTo gain access to cellulose, the lignin-hemicellulose shield must be broken up, usually by a chemical method at elevated temperature and often also elevated pressure.
“To gain access to the cellulose the lignin-hemicellulose shield must be broken up (Fig. 15), usually by a chemical method at elevated temperature and often also elevated pressure.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
PremisecitationDuring lignification, ferulic acid's aromatic ring can be incorporated into the growing lignin network by participating in radical polymerisation.
“During lignification, its aromatic ring can be incorporated into the growing lignin network by participating in the radical polymerisation reaction.29”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [29] source
Not checked in the free run.
May combine two claims.
PremisecitationThe ordering of regenerated cellulose is reduced compared to the initial state and it is transformed into cellulose II.
“The ordering of the regenerated cellulose is reduced compared to the initial state and it is transformed into cellulose II.75,76”
Quote in the paperSubstantial claim0 of 2 sources checkedProbably not a substantial claim: may not pass S3 (load-bearing).
Premisecitation1-ethylpyridiniumchloride, [C2pyr]Cl, can dissolve cellulose.
“It has been known for some time that 1-ethylpyridiniumchloride, [C 2 pyr]Cl, can dissolve cellulose.68”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [68] source
Not checked in the free run.
May combine two claims.
PremisecitationThe Viscose process uses toxic and highly flammable CS2 and produces large amounts of waste products, which has fuelled the search for a more benign replacement.
“This process uses toxic and highly flammable CS 2 and produces large amounts of waste products, which has fuelled the search for a more benign replacement.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [65] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Premisenone givenStraws are usually, of all feedstocks, the least resistant to deconstruction.
“Straws are usually, of all feedstocks, the least resistant to deconstruction.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
PremisecitationThe Lyocell process is a true dissolution process using NMO and an improvement in terms of health and environmental impact.
“The Lyocell process is a true dissolution process using NMO and an improvement in terms of health and environmental impact.66”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [66] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing).
PremisecitationPerennial bioenergy grasses such as Miscanthus and switchgrass can achieve high yields per area of land and year.
“Perennial bioenergy grasses such as Miscanthus and switchgrass have the advantage that high yields per area of land and year can be achieved.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [38] source
Not checked in the free run.
May combine two claims.
PremisecitationOnly a few solvents are able to dissolve crystalline cellulose fibrils, e.g. NMO or concentrated phosphoric acid, none of which are applied in lignocellulose processing.
“Only a few solvents are able to dissolve the crystalline polymer fibrils, e.g.N-methylmorpholine-N-oxide (NMO) 63 or concentrated phosphoric acid, 64 none of which are applied in lignocellulose processing.”
Quote in the paperSubstantial claim0 of 2 sources checkedMay combine two claims.
InterpretationcitationCellulose dissolution is an industrially attractive application of ionic liquids due to good solubilities (5-20 wt%, depending on ionic liquid and conditions), competitive properties of regenerated cellulose, increased stability of ionic liquid cellulose solutions, and low toxicity of certain relevant ionic liquids.
“Cellulose dissolution is an industrially attractive application of ionic liquids, due to good solubilities (5-20 wt%, depending on the ionic liquid and the conditions), the competitive properties of cellulose reprecipitated from the ionic liquid solutions, 73 the increased stability of ionic liquid cellulose solutions 74 and the low toxicity of certain relevant ionic liquids (for example, [C 2 C 1”
Quote in the paperSubstantial claim0 of 2 sources checkedMay combine two claims.
PremisecitationVirtually all pretreatment options induce chemical changes in both hemicellulose and lignin, while cellulose usually remains largely chemically unchanged.
“Virtually all pretreatment options induce chemical changes in both hemicellulose and lignin, for example polymer fragmentation, chemical transformation or functionalization, while the cellulose usually remains largely chemically unchanged (NB: structural modifications of cellulose have been observed).”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [76] source
Not checked in the free run.
May combine two claims.
PremisecitationThe empirical Kamlet-Taft model and the quantum mechanical COSMO-RS model have been used most frequently to predict or explain the solubility of cellulose (and other biopolymers) in ionic liquids, while few literature data exist for Hansen solubility parameters of ionic liquids.
“The empirical Kamlet-Taft model 69c,d and the quantum mechanical COSMO-RS model 88 have been used most frequently to predict or explain the solubility of cellulose (and other biopolymers) in ionic liquids, while few literature data exist for Hansen solubility parameters of ionic liquids.89”
Quote in the paperNot a substantial claim0 of 3 sources checkedProbably not a substantial claim: may not pass S3 (load-bearing).
PremisecitationSeveral empirical and semi-empirical polarity scales have been used to explain and predict solubility of biomolecules and biopolymers in solvents, for example Hansen solubility parameters, COSMO-RS and Kamlet-Taft polarity parameters.
“Several empirical and semi-empirical polarity scales have been used to explain and predict solubility of biomolecules and biopolymers in solvents, for example the Hansen solubility parameters, 21,85 COSMO-RS 86 and the Kamlet-Taft polarity parameters.87”
Quote in the paperNot a substantial claim0 of 4 sources checkedMay combine two claims.
PremisecitationMore strongly hydrogen bond-basic anions (Cl-, Br-, [HSO4]-) resulted in higher yields of β-O-4 cleavage products than weakly basic anions, as well as in different routes.
“More strongly hydrogen bond-basic anions (Cl -, Br -and [HSO 4 ] -) resulted in higher yields of the cleavage products than weakly basic anions, as well as in different routes.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [142] source
Not checked in the free run.
May combine two claims.
PremisecitationThe functional group of the anion determined the effect on lignin fragmentation rather than its size, while the cation did not play a significant role.
“The functional group of the anion determined the effect rather than its size, while the cation did not play a significant role.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [134] source
Not checked in the free run.
May combine two claims.
PremisecitationThe main product of Organosolv beech lignin oxidation in ionic liquids was 2,6-dimethoxy-1,4-benzoquinone; vanillin, syringaldehyde and other less abundant oxidised aromatic fragments were also identified.
“The main product was 2,6-dimethoxy-1,4-benzoquinone; vanillin, syringaldehyde and other less abundant oxidised aromatic fragments were also identified.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [143] source
Not checked in the free run.
May combine two claims.
InterpretationcitationRecovery of only around 50% of bagasse feedstock and production of a pulp highly enriched in cellulose suggests that removal of both lignin and hemicellulose is considerable with [C2C1im][ABS].
“However, recovery of only around 50% of the bagasse feedstock and production of a pulp that appears to be highly enriched in cellulose suggests that removal of both lignin and hemicellulose is considerable with this ionic liquid.52”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [52] source
Not checked in the free run.
May combine two claims.
PremisecitationTotal time requirement for two-stage simultaneous dissolution/saccharification plus enzymatic saccharification was 3.5-5 h, significantly shorter than enzymatic saccharification alone but with similar selectivity.
“The total time requirement was 3.5-5 h (0.5-1 h for the dissolution/acid hydrolysis and 3-4 h for the enzymatic hydrolysis) which is significantly shorter than enzymatic saccharification alone but with a similar selectivity.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [154] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Interpretationnone givenDissolved impurities may reduce the performance of the ionic liquid in subsequent cycles.
“Other considerations are reactions of ionic liquids with the lignocellulose, which would also affect the recycling rate as well as the quality of the pulp, and dissolved impurities which may reduce the performance of the ionic liquid in subsequent cycles.”
Quote in the paperNot a substantial claimMay combine two claims.
PremisecitationMacroreticulated resins functionalized with sulfonic groups such as Amberlyst 15DRY are compatible with viscous solutions and sufficiently acidic for cellulose hydrolysis in ionic liquids.
“It was concluded that macroreticulated resins functionalized with sulfonic groups (-SO 3 H) such as Amberlyst 15DRY, which have a large surface area, are compatible with viscous solutions and sufficiently acidic for the reaction to occur.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [152]
Not checked in the free run.
May combine two claims.
PremisecitationUsing corn stover as substrate, Binder and Raines achieved glucose yield of 70-80% and HMF yield of 10% or less under optimised conditions.
“Using corn stover as a substrate, the yield of glucose under optimised conditions was 70-80% and the HMF yield was 10% or less.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites 146a
Not checked in the free run.
May combine two claims.
PremisecitationIn hydrolysis of cellulose in [C4C1im]Cl/NMP with water and sulfuric acid, the hydrolysis temperature was only 70 °C and the co-solvent accelerated dissolution substantially, although hydrolysis was slower.
“The hydrolysis temperature was only 70 °C and the presence of the co-solvent accelerated the dissolution substantially, although hydrolysis was slower.”
Quote in the paperNot a substantial claim0 of 1 sources checked- cites [150] source
Not checked in the free run.
May combine two claims.
PremisecitationOnly acids with pKa < 1.0 resulted in appreciable cellobiose hydrolysis in [C2C1im]Cl, showing strong acids are needed for fast hydrolysis in chloride ionic liquids.
“It was shown that only the use of acids with a pK a < 1.0 resulted in appreciable hydrolysis, showing that strong acids need to be used to achieve fast hydrolysis in chloride ionic liquids.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites [151] source
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
PremisecitationSubsequent studies have shown that acidic protons contained in solid catalyst are released into ionic liquid and hydrolysis rate is proportional to H+ concentration in liquid phase.
“This study suggested that the cellulose hydrolysis proceeds on the surface of the resin, while subsequent studies have shown that the acidic protons contained in the solid catalyst are released into the ionic liquid and that the hydrolysis rate is proportional to the H + concentration in the liquid phase.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Interpretationnone givenAt 50.5 wt% water content, the effect of water on the ionic liquid is likely to be considerable.
“This was at 50.5 wt% water content, where the effect of water on the ionic liquid is likely to be considerable.”
Quote in the paperNot a substantial claimMay combine two claims.
PremisecitationSecondary hydrolysis in diluted ionic liquid increased monomer yield to up to 30%, supporting that cellulose after acidic dissolution in ionic liquids is mostly oligomeric.
“A secondary hydrolysis in diluted ionic liquid increased the monomer yield to up to 30%, supporting the explanation that the cellulose after acidic dissolution in ionic liquids is mostly oligomeric.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 129a
Not checked in the free run.
May combine two claims.
PremisecitationIonic liquid treatment is accompanied by significant hemicellulose depolymerisation, as are other deconstruction methods.
“Ionic liquid treatment is accompanied by significant hemicellulose depolymerisation, 120,136 as are other deconstruction methods.”
Quote in the paperNot a substantial claim0 of 2 sources checkedMay combine two claims.
Interpretationnone givenReactions of ionic liquids with lignocellulose would affect the recycling rate as well as the quality of the pulp.
“Other considerations are reactions of ionic liquids with the lignocellulose, which would also affect the recycling rate as well as the quality of the pulp, and dissolved impurities which may reduce the performance of the ionic liquid in subsequent cycles.”
Quote in the paperNot a substantial claimMay combine two claims.
PremisecitationIn Sievers et al. study, although solubilisation of pine flour in [C4C1im]Cl with sulfuric acid was close to 100% at 120 °C within 2 h, the yield of monomeric sugars was low.
“Although the solubilisation was close to 100% at 120 °C within 2 h, the yield of monomeric sugars was low.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 129a
Not checked in the free run.
May combine two claims.
PremisecitationSeveral ionic liquids containing chloride anions were effective in generating glucose from cellulose, while [C2C1im][NO3], [C4C1im][BF4], [C1C1im][Me2PO4] and [C2C1im][MeCO2] did not result in detectable glucose.
“While several ionic liquids containing chloride anions were effective in generating glucose from cellulose, the ionic liquids [C 2 C 1 im][NO 3 ], [C 4 C 1 im][BF 4 ], [C 1 C 1 im][Me 2 PO 4 ] and [C 2 C 1 im][MeCO 2 ] did not result in the formation of detectable amounts of glucose.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 146a
Not checked in the free run.
May combine two claims.
InterpretationcitationFor [C2C1im][NO3] and [C4C1im][BF4], inability to dissolve cellulose inhibits acid access to glycosidic bonds and prevents hydrolysis.
“For the first two ionic liquids, it is suggested that their inability to dissolve the polymer inhibits access of the acid to the glycosidic bonds and thus prevents hydrolysis.”
Quote in the paperSubstantial claim0 of 1 sources checked- cites 146a
Not checked in the free run.
Probably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
PremisereasoningBefore any thermal deconstruction of lignocellulosic biomass, a milling or grinding step is necessary.
“Before any thermal deconstruction of lignocellulosic biomass, a milling or grinding step is necessary.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based). May combine two claims.
Interpretationnone givenAlthough grinding costs are saved, the energy required for drying harvested biomass to 7-10% moisture, and thoroughly drying the ionic liquid, must be accounted for.
“Although grinding costs are saved, the energy required for drying harvested biomass to 7-10% moisture, and thoroughly drying the ionic liquid, must be accounted for.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S4 (based).
Interpretationnone givenRegardless of how successfully the ionic liquid is separated from the cellulose, it is likely that some of the ionic liquid will pass into subsequent process operations.
“Regardless of how successfully the ionic liquid is separated from the cellulose, it is likely that some of the ionic liquid will pass into subsequent process operations.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Premisenone givenMilling increases the surface area of the lignocellulosic substrate.
“Milling increases the surface area of the lignocellulosic substrate.”
Quote in the paperNot a substantial claimClassified as probably not a substantial claim.
InterpretationreasoningThe particle size reduction process is an important target for optimisation, especially in the case of woody biomass.
“The particle size reduction process is an important target for optimisation, especially in the case of woody biomass.”
Quote in the paperSubstantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Interpretationnone givenThe small number of papers in the literature that use the Ionosolv Process approach indicates that it is unlikely to have yet been optimised.
“The small number of papers in the literature that use the Ionosolv Process approach indicates that it is unlikely to have yet been optimised.”
Quote in the paperNot a substantial claimMay combine two claims.
InterpretationreasoningThe almost quantitative lignin removal is likely due to the presence of mid-range nucleophilic, neutral or acidic anions in the ionic liquids employed by the Ionosolv Process; these seem to act as catalytic delignifiers and possibly reagents.
“This is likely due to the presence of mid-range nucleophilic, neutral or acidic anions in the ionic liquids employed by the Ionosolv Process; these seem to act as catalytic delignifiers and possibly reagents.”
Quote in the paperNot a substantial claimMay combine two claims.
Interpretationnone givenThe ionic liquid solutions being recycled may contain ionic liquid decomposition products, biomass decomposition products and most likely both.
“These solutions may contain ionic liquid decomposition products, biomass decomposition products and most likely both.”
Quote in the paperSubstantial claimClassified as probably not a substantial claim. May combine two claims.
InterpretationreasoningSince the fractionation ability of an ionic liquid is dominated by the nature of the anion, it is likely that this will determine the anion selection.
“Since the fractionation ability of an ionic liquid is dominated by the nature of the anion, it is likely that this will determine the anion selection.”
Quote in the paperSubstantial claimProbably not a substantial claim: may not pass S3 (load-bearing).
InterpretationreasoningThe higher pulp recoveries could be due to less extensive lignin removal.
“In addition, higher pulp recoveries were observed when the ionic liquid was reused, which could be due to less extensive lignin removal.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based). May combine two claims.
Interpretationnone givenThe filtrate will contain lignin and probably some hemicelluloses.
“The filtrate will contain lignin and probably some hemicelluloses.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Interpretationnone givenDuring recycling, the ionic liquid is likely to experience a build-up of carbohydrate monomers and oligomers, furfurals, organic acids, lignin fragments, inorganic salts and other solutes that are released during the pretreatment.
“During recycling, the ionic liquid is likely to experience a build-up of carbohydrate monomers and oligomers, furfurals, organic acids, lignin fragments, inorganic salts and other solutes that are released during the pretreatment.”
Quote in the paperNot a substantial claimMay combine two claims.
InterpretationreasoningProtic ionic liquids are also distillable and hence much more easily recycled than the ionic liquids with fully alkylated cations.
“The protic ionic liquids are also distillable and hence much more easily recycled than the ionic liquids with fully alkylated cations.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
InterpretationreasoningThe use of distillable acid-base ionic liquids may be a solution to solute accumulation, although distillation of the ionic liquid after each cycle is likely to be uneconomical.
“The use of distillable acid-base ionic liquids may be a solution to this problem, although distillation of the ionic liquid after each cycle is likely to be uneconomical.”
Quote in the paperNot a substantial claimMay combine two claims.
InterpretationreasoningAlthough the recovered ionic liquid does not need to be fully dried (as ca.20% water is required for the pretreatment step), reconcentration is still likely to be a highly energy intensive step and has the potential to be a process-limiting problem.
“Although the recovered ionic liquid does not need to be fully dried (as ca.20% water is required for the pretreatment step), this is still likely to be a highly energy intensive step and has the potential to be a process-limiting problem.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based).
Interpretationnone givenThe incorporation of ionic liquid components into lignin or cellulose pulp could hamper the economic viability of ionic liquid deconstruction by reducing the maximum recovery as well as the value of the recovered pulp and the lignin.
“For example, the incorporation of ionic liquid components into lignin or cellulose pulp could hamper the economic viability of ionic liquid deconstruction by reducing the maximum recovery as well as the value of the recovered pulp and the lignin.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S2 (checkable). May combine two claims.
InterpretationreasoningThe design of less inhibitory ionic liquids could be beneficial, as extensive washing will worsen the process economics due to a large, possibly environmentally harmful waste water stream.
“The design of less inhibitory ionic liquids could be beneficial, as extensive washing will worsen the process economics due to a large, possibly environmentally harmful waste water stream.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S2 (checkable), S3 (load-bearing).
InterpretationreasoningReduction in the price of ionic liquids used for deconstruction of biomass is essential if this is to become commercial reality.
“Notwithstanding this, reduction in the price of ionic liquids used for deconstruction of biomass is essential if this is to become commercial reality.”
Quote in the paperNot a substantial claim- Rests on an assumption: Ionic liquids are the most expensive solvents currently under investigation for lignocellulose deconstruction.
Probably not a substantial claim: may not pass S3 (load-bearing). May combine two claims.
InterpretationreasoningThe degradation of [C2C1im][MeCO2] during Dissolution Process pretreatment has yet to be studied in detail, but has the potential to be a process-limiting problem.
“This has yet to be studied in detail, but has the potential be a process-limiting problem.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S4 (based).
Interpretationnone givenThe filtrate (precipitation solvent + ionic liquid) contains dissolved lignin, some hemicelluloses and the organic extractives.
“The filtrate ( precipitation solvent + ionic liquid) contains dissolved lignin, some hemicelluloses and the organic extractives.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S2 (checkable), S3 (load-bearing). May combine two claims.
InterpretationreasoningOther separation procedures, such as solvent extraction, will probably be used to minimize solute accumulation and to ensure the ionic liquid remains sufficiently clean for repeated recycling, with distillation only being used when this cleaning fails.
“Therefore, other separation procedures, such as solvent extraction, will probably be used to minimize solute accumulation and to ensure the ionic liquid remains sufficiently clean for repeated recycling, with distillation only being used when this cleaning fails.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S2 (checkable), S3 (load-bearing), S4 (based).
Interpretationnone givenThe possibility of removing lignin with the ionic liquid and recovering a separate, possibly more valuable lignin fraction is an attractive feature.
“The possibility of removing lignin with the ionic liquid and recovering a separate, possibly more valuable lignin fraction is also an attractive feature.”
Quote in the paperNot a substantial claimProbably not a substantial claim: may not pass S3 (load-bearing), S4 (based). May combine two claims.
Interpretationnone givenA less frequently mentioned advantage of ionic liquids is their low volatility, making it possible to pretreat biomass at atmospheric pressure even at temperatures surpassing the boiling point of water, as well as the ability to handle a non-odorous and relatively safe liquor compared to volatile solvents or sulfide containing aqueous solutions.
“A less frequently mentioned advantage of ionic liquids is their low volatility, making it possible to pretreat biomass at atmospheric pressure even at temperatures surpassing the boiling point of water, as well as the ability to handle a non-odorous and relatively safe liquor compared to volatile solvents or sulfide containing aqueous solutions.”
Quote in the paperNot a substantial claimMay combine two claims.
InterpretationreasoningThe energy costs of drying the ionic liquid have to be assessed and have the potential to be a process-limiting problem.
“The energy costs of this drying have to be assessed and have the potential to be a process-limiting problem.”
Quote in the paperSubstantial claim
The paper relies on this without support.
Lignocellulose is a composite material with cellulose, hemicellulose and lignin making up ca.90% of dry matter.
“It is a composite material, with three biopolymers, cellulose, hemicellulose and lignin, making up ca.90% of the dry matter.”
The paper relies on this without support.
Lignocellulose contains up to 60-70 wt% sugars/carbohydrates but is not utilised for food production.
“It contains up to 60-70 wt% sugars/carbohydrates but is not utilised for food production.”
The paper relies on this without support.
Hemicellulose and lignin are covalently cross-linked in lignocellulose.
“Hemicellulose and lignin are not only entangled, but also covalently cross-linked.”
The paper relies on this without support.
High hydrogen bond basicity is associated with reduced ionic liquid stability.
“as it has been shown that high hydrogen bond basicity is associated with reduced ionic liquid stability.”
The paper relies on this without support.
Water is essential for stabilising the organic hydroxide salt, which would decompose upon drying.
“as the water is essential for stabilising the organic hydroxide salt, which would decompose upon drying.”
The paper relies on this without support.
The hemicellulose component in lignocellulosic biomass is 25-30% and large enough to be of significant economic value.
“The hemicellulose component in lignocellulosic biomass (25-30%) is large enough to be of significant economic value.”
The paper relies on this without support.
Currently most important fermentative organisms (e.g. yeast) are not yet able to utilise all hemicellulose sugars.
“Although currently most important fermentative organisms (e.g.yeast) are not yet able to utilise all hemicellulose sugars, this is likely to change in the near future by introduction of genetically engineered strains, 161 therefore high recovery of hemicellulose sugars is also desirable.”
The paper relies on this without support.
Raw biomass typically contains about 50% water and even thoroughly air-dried biomass typically contains around 5-10 wt% residual moisture.
“Raw biomass is wet, typically containing 50% water and even thoroughly airdried biomass typically contains around 5-10 wt% residual moisture.”
The paper relies on this without support.
Ionic liquids are the most expensive solvents currently under investigation for lignocellulose deconstruction.
“Ionic liquids are the most expensive solvents that are currently under investigation for lignocellulose deconstruction.”
The paper relies on this without support.
Acetate is a metabolic inhibitor of most yeast systems.
“Acetate is a proven metabolic inhibitor of most yeast systems.”
The paper relies on this without support.
The majority of biomass deconstruction experiments using [C2C1im][MeCO2] and [C4C1im][MeCO2] have been performed at temperatures greatly in excess of 90 °C.
“It is important to note that the majority of biomass deconstruction experiments using these ionic liquids have been performed at temperatures greatly in excess of this limit.”
The paper relies on this without support.
The 3,5-dinitrosalicylic acid (DNS) assay is not specific for glucose nor for monomers.
“Studies using 3,5-dinitrosalicylic acid (DNS) were not considered for this table, as this assay is not specific for glucose nor for monomers”
Claims other papers make about this one
Each is checked against this paper’s own text: does it say what the citing paper says it does?
Carbon materials derived from biopolymers have made considerable progress in recent years, especially in the development of molecular sieves, as photocatalyst supports and adsorbents for the storage of natural gas.
“Carbon materials derived from biopolymers have made considerable progress in recent years, especially in the development of molecular sieves, as photocatalyst supports and adsorbents for the storage of natural gas.26,34,35”
From Sustainable hybrid photocatalysts: titania immobilized on carbon materials derived from renewable and biodegradable resources (2016) · cites this paper as [34]
Carbonization of a carefully designed polymer provides opportunities to control the pore size, pore volume and bulk density of the ensuing carbon.
“Carbonization of the carefully designed polymer provides opportunities in controlling the pore size, pore volume and bulk density of the ensuing carbon, which are important characteristics in the aforementioned applications.26,34,35”
From Sustainable hybrid photocatalysts: titania immobilized on carbon materials derived from renewable and biodegradable resources (2016) · cites this paper as [34]
Self-check
Percentages, sums and reported differences re-computed from the paper’s own numbers.
Each contradiction between two passages listed here was confirmed by an independent check.
Reported lignin-removal range omits a table value
MinorThe text says lignin removal with [C 2 C 1 im][MeCO 2 ] reached at most 65%, but Table 5 reports 69% for switchgrass.
“Lignin removal was reported to be between 17% and 65%, while hemicellulose removal varied between 0% and 83%.”
“| | 160 °C | 3 h | 85 | 69 | 77 | 138 |”
Miscanthus precipitate yield conflicts with Table 8
MinorThe text reports a precipitate yield over 60% of the original lignin content for [C 4 C 1 im][HSO 4 ] treatment of Miscanthus, whereas Table 8 lists 47% for that ionic liquid and feedstock.
“They reported a precipitate yield of over 60 wt% of the lignin content of untreated Miscanthus after pretreatment with [C 4 C 1 im][HSO 4 ] water mixtures.”
“| [C 4 C 1 im][HSO 4 ] (20% water) [C 4 C 1 im][MeSO 4 ] a (20% water) | | 120 °C 120 °C | 22 h 26 h | Water Water | 47% 43% | 55 55 |”
Cites
Room-Temperature Ionic Liquids: Solvents for Synthesis and Catalysis. 2
Hallett, J. P., & Welton, T. (2011) · Chemical Reviews · doi:10.1021/cr1003248 · Cited by 12,581 · see citing works
Self-citationRoom-Temperature Ionic Liquids. Solvents for Synthesis and Catalysis
Welton, T. (1999) · Chemical Reviews · doi:10.1021/cr980032t · Cited by 11,866 · see citing works
Self-citationFeatures of promising technologies for pretreatment of lignocellulosic biomass
MOSIER, N. (2005) · Bioresource Technology · doi:10.1016/j.biortech.2004.06.025 · Cited by 6,251 · see citing works
The Path Forward for Biofuels and Biomaterials
Ragauskas, A. J., Williams, C. K., Davison, B. H., Britovsek, G., Cairney, J., Eckert, C. A., Frederick, W. J., Hallett, J. P., Leak, D. J., Liotta, C. L., et al. (2006) · Science · doi:10.1126/science.1114736 · Cited by 5,741 · see citing works
Self-citationApplications of ionic liquids in the chemical industry
Plechkova, N. V., & Seddon, K. R. (2008) · Chem. Soc. Rev. · doi:10.1039/b006677j · Cited by 5,686 · see citing works
Use of U.S. Croplands for Biofuels Increases Greenhouse Gases Through Emissions from Land-Use Change
Searchinger, T., Heimlich, R., Houghton, R. A., Dong, F., Elobeid, A., Fabiosa, J., Tokgoz, S., Hayes, D., & Yu, T.-H. (2008) · Science · doi:10.1126/science.1151861 · Cited by 4,888 · see citing works
Dissolution of Cellose with Ionic Liquids
Swatloski, R. P., Spear, S. K., Holbrey, J. D., & Rogers, R. D. (2002) · Journal of the American Chemical Society · doi:10.1021/ja025790m · Cited by 4,735 · see citing works
Boerjan, W., Ralph, J., & Baucher, M. (2003) · Annual Review of Plant Biology · doi:10.1146/annurev.arplant.54.031902.134938 · Cited by 4,504 · see citing works
The Catalytic Valorization of Lignin for the Production of Renewable Chemicals
Zakzeski, J., Bruijnincx, P. C. A., Jongerius, A. L., & Weckhuysen, B. M. (2010) · Chemical Reviews · doi:10.1021/cr900354u · Cited by 4,468 · see citing works
Klamt, A. (1995) · The Journal of Physical Chemistry · doi:10.1021/j100007a062 · Cited by 4,194 · see citing works
Ionic Liquid (Molten Salt) Phase Organometallic Catalysis
Dupont, J., de Souza, R. F., & Suarez, P. A. Z. (2002) · Chemical Reviews · doi:10.1021/cr010338r · Cited by 3,753 · see citing works
Nishiyama, Y., Langan, P. A., & Chanzy, H. (2002) · Journal of the American Chemical Society · doi:10.1021/ja0257319 · Cited by 3,041 · see citing works
Parvulescu, V. I., & Hardacre, C. (2007) · Chemical Reviews · doi:10.1021/cr050948h · Cited by 2,373 · see citing works
Jason, P. H., & Tom, W. (2011) · Chemical Reviews · Cited by 2,270 · see citing works
Metal Chlorides in Ionic Liquid Solvents Convert Sugars to 5-Hydroxymethylfurfural
Zhao, H., Holladay, J. E., Brown, H., & Zhang, Z. C. (2007) · Science · doi:10.1126/science.1141199 · Cited by 1,997 · see citing works
Air and water stable 1-ethyl-3-methylimidazolium based ionic liquids
Wilkes, J. S., & Zaworotko, M. J. (1992) · Journal of the Chemical Society, Chemical Communications · doi:10.1039/c39920000965 · Cited by 1,883 · see citing works
Fast solvent screening via quantum chemistry: COSMO‐RS approach
Eckert, F., & Klamt, A. (2002) · AIChE Journal · doi:10.1002/aic.690480220 · Cited by 1,831 · see citing works
Welton, T. (2004) · Coordination Chemistry Reviews · doi:10.1016/j.ccr.2004.04.015 · Cited by 1,610 · see citing works
Self-citationvan Rantwijk, F., & Sheldon, R. A. (2007) · Chemical Reviews · doi:10.1021/cr050946x · Cited by 1,561 · see citing works
Ionic Liquids and Their Interaction with Cellulose
Pinkert, A., Marsh, K. N., Pang, S., & Staiger, M. P. (2009) · Chemical Reviews · doi:10.1021/cr9001947 · Cited by 1,508 · see citing works
Cellulose: the structure slowly unravels
O'sullivan, A. C. (1997) · Cellulose · doi:10.1023/a:1018431705579 · Cited by 1,501 · see citing works
Cammarata, L., Kazarian, S. G., Salter, P. A., & Welton, T. (2001) · Physical Chemistry Chemical Physics · doi:10.1039/b106900d · Cited by 1,441 · see citing works
Self-citationIonic liquid processing of cellulose
Wang, H., Gurau, G., & Rogers, R. D. (2012) · Chemical Society Reviews · doi:10.1039/c2cs15311d · Cited by 1,369 · see citing works
Dissolution of cellulose with ionic liquids and its application: a mini-review
Zhu, S., Wu, Y., Chen, Q., Yu, Z., Wang, C., Jin, S., Ding, Y., & Wu, G. (2006) · Green Chemistry · doi:10.1039/b601395c · Cited by 1,260 · see citing works
Enzymatic conversion of lignocellulose into fermentable sugars: challenges and opportunities
Jørgensen, H., Kristensen, J. B., & Felby, C. (2007) · Biofuels, Bioproducts and Biorefining · doi:10.1002/bbb.4 · Cited by 1,143 · see citing works
Net energy of cellulosic ethanol from switchgrass
Schmer, M. R., Vogel, K. P., Mitchell, R. B., & Perrin, R. K. (2008) · Proceedings of the National Academy of Sciences · doi:10.1073/pnas.0704767105 · Cited by 1,067 · see citing works
Li, C., Knierim, B., Manisseri, C., Arora, R., Scheller, H. V., Auer, M., Vogel, K. P., Simmons, B. A., & Singh, S. (2009) · Bioresource Technology · doi:10.1016/j.biortech.2009.10.066 · Cited by 1,045 · see citing works
Structure formation of regenerated cellulose materials from NMMO-solutions
Fink, H.-P., Weigel, P., Purz, H. J., & Ganster, J. (2001) · Progress in Polymer Science · doi:10.1016/s0079-6700(01)00025-9 · Cited by 1,025 · see citing works
Deconstruction of Lignocellulosic Biomass to Fuels and Chemicals
Chundawat, S. P. S., Beckham, G. T., Himmel, M. E., & Dale, B. E. (2011) · Annual Review of Chemical and Biomolecular Engineering · doi:10.1146/annurev-chembioeng-061010-114205 · Cited by 1,017 · see citing works
Acid-based hydrolysis processes for ethanol from lignocellulosic materials: A review
Taherzadeh, M. J., & Karimi, K. (2007) · BioResources · doi:10.15376/biores.2.3.472-499 · Cited by 1,010 · see citing works
Sun, N., Rahman, M., Qin, Y., Maxim, M. L., Rodríguez, H., & Rogers, R. D. (2009) · Green Chemistry · doi:10.1039/b822702k · Cited by 988 · see citing works
Dissolution of Wood in Ionic Liquids
Kilpeläinen, I., Xie, H., King, A. W. T., Granström, M., Heikkinen, S., & Argyropoulos, D. S. (2007) · Journal of Agricultural and Food Chemistry · doi:10.1021/jf071692e · Cited by 943 · see citing works
Lee, S. H., Doherty, T. V., Linhardt, R. J., & Dordick, J. S. (2008) · Biotechnology and Bioengineering · doi:10.1002/bit.22179 · Cited by 942 · see citing works
Recent progress in the chemistry of wood hemicelluloses
Timell, T. E. (1967) · Wood Science and Technology · doi:10.1007/bf00592255 · Cited by 874 · see citing works
Saeman, J. F. (1945) · Industrial & Engineering Chemistry · doi:10.1021/ie50421a009 · Cited by 818 · see citing works
Fort, D. A., Remsing, R. C., Swatloski, R. P., Moyna, P., Moyna, G., & Rogers, R. D. (2006) · Green Chemistry · doi:10.1039/b607614a · Cited by 815 · see citing works
FitzPatrick, M., Champagne, P., Cunningham, M. F., & Whitney, R. A. (2010) · Bioresource Technology · doi:10.1016/j.biortech.2010.06.125 · Cited by 810 · see citing works
On the mechanism of dissolution of cellulose
Lindman, B., Karlström, G., & Stigsson, L. (2010) · Journal of Molecular Liquids · doi:10.1016/j.molliq.2010.04.016 · Cited by 792 · see citing works
Cellulose dissolution with polar ionic liquids under mild conditions: required factors for anions
Fukaya, Y., Hayashi, K., Wada, M., & Ohno, H. (2008) · Green Chem. · doi:10.1039/b713289a · Cited by 775 · see citing works
High-throughput screening for ionic liquids dissolving (ligno-)cellulose
Zavrel, M., Bross, D., Funke, M., Büchs, J., & Spieß, A. C. (2009) · Bioresource Technology · doi:10.1016/j.biortech.2008.11.052 · Cited by 696 · see citing works
Poplar as a feedstock for biofuels: A review of compositional characteristics
Sannigrahi, P., Ragauskas, A. J., & Tuskan, G. A. (2010) · Biofuels, Bioproducts and Biorefining · doi:10.1002/bbb.206 · Cited by 688 · see citing works
Grinding performance and physical properties of wheat and barley straws, corn stover and switchgrass
Mani, S., Tabil, L. G., & Sokhansanj, S. (2004) · Biomass and Bioenergy · doi:10.1016/j.biombioe.2004.03.007 · Cited by 680 · see citing works
Homogeneous Acetylation of Cellulose in a New Ionic Liquid
Wu, J., Zhang, J., Zhang, H., He, J., Ren, Q., & Guo, M. (2004) · Biomacromolecules · doi:10.1021/bm034398d · Cited by 648 · see citing works
Inhibition of cellulase, xylanase and β-glucosidase activities by softwood lignin preparations
Berlin, A., Balakshin, M. Y., Gilkes, N. R., Kadla, J. F., Maximenko, V., Kubo, S., & Saddler, J. N. (2006) · Journal of Biotechnology · doi:10.1016/j.jbiotec.2006.02.021 · Cited by 636 · see citing works
Ohno, H., & Fukumoto, K. (2007) · Accounts of Chemical Research · doi:10.1021/ar700053z · Cited by 630 · see citing works
Reviving the carbohydrate economy via multi-product lignocellulose biorefineries
Zhang, Y.-H. P. (2008) · Journal of Industrial Microbiology & Biotechnology · doi:10.1007/s10295-007-0293-6 · Cited by 622 · see citing works
Fractionating recalcitrant lignocellulose at modest reaction conditions
Zhang, Y. P., Ding, S., Mielenz, J. R., Cui, J., Elander, R. T., Laser, M., Himmel, M. E., McMillan, J. R., & Lynd, L. R. (2007) · Biotechnology and Bioengineering · doi:10.1002/bit.21386 · Cited by 589 · see citing works
Dissolution and forming of cellulose with ionic liquids
Kosan, B., Michels, C., & Meister, F. (2008) · Cellulose · doi:10.1007/s10570-007-9160-x · Cited by 585 · see citing works
Dissolution of lignocellulosic materials and its constituents using ionic liquids—A review
Mäki‐Arvela, P., Anugwom, I., Virtanen, P., Sjöholm, R. E., & Mikkola, J. (2010) · Industrial Crops and Products · doi:10.1016/j.indcrop.2010.04.005 · Cited by 581 · see citing works
Enhancement of cellulose saccharification kinetics using an ionic liquid pretreatment step
Dadi, A. P., Varanasi, S., & Schall, C. A. (2006) · Biotechnology and Bioengineering · doi:10.1002/bit.21047 · Cited by 574 · see citing works
Enzyme catalysis in ionic liquids
Kragl, U., Eckstein, M. F., & Kaftzik, N. (2002) · Current Opinion in Biotechnology · doi:10.1016/s0958-1669(02)00353-1 · Cited by 572 · see citing works
Medronho, B., Romano, A., Miguel, M. G., Stigsson, L., & Lindman, B. (2012) · Cellulose · doi:10.1007/s10570-011-9644-6 · Cited by 567 · see citing works
Ionic Liquid as a Green Solvent for Lignin
Pu, Y., Jiang, N., & Ragauskas, A. J. (2007) · Journal of Wood Chemistry and Technology · doi:10.1080/02773810701282330 · Cited by 548 · see citing works
Depolymerization of Cellulose Using Solid Catalysts in Ionic Liquids
Rinaldi, R., Palkovits, R., & Schüth, F. (2008) · Angewandte Chemie International Edition · doi:10.1002/anie.200802879 · Cited by 539 · see citing works
Understanding the polarity of ionic liquids
Rani, M. A. A., Brant, A., Crowhurst, L., Dolan, A., Lui, M. Y.-Y., Hassan, N. H., Hallett, J. P., Hunt, P. A., Niedermeyer, H., Perez‐Arlandis, J. M., et al. (2011) · Physical Chemistry Chemical Physics · doi:10.1039/c1cp21262a · Cited by 524 · see citing works
Self-citationBrunecky, R., Selig, M. J., Vinzant, T. B., Himmel, M. E., Lee, D., Blaylock, M. J., & Decker, S. R. (2011) · Biotechnology for Biofuels · doi:10.1186/1754-6834-4-1 · Cited by 512 · see citing works
Characterization of milled wood lignin and ethanol organosolv lignin from miscanthus
Hage, R. E., Brosse, N., Chrusciel, L., Sanchez, C., Sannigrahi, P., & Ragauskas, A. J. (2009) · Polymer Degradation and Stability · doi:10.1016/j.polymdegradstab.2009.07.007 · Cited by 510 · see citing works
Fukaya, Y., Sugimoto, A., & Ohno, H. (2006) · Biomacromolecules · doi:10.1021/bm060327d · Cited by 504 · see citing works
‘Cradle-to-grave’ assessment of existing lignocellulose pretreatment technologies
Sousa, L. D. C., Chundawat, S. P. S., Balan, V., & Dale, B. E. (2009) · Current Opinion in Biotechnology · doi:10.1016/j.copbio.2009.05.003 · Cited by 497 · see citing works
Fermentable sugars by chemical hydrolysis of biomass
Binder, J. B., & Raines, R. T. (2010) · Proceedings of the National Academy of Sciences · doi:10.1073/pnas.0912073107 · Cited by 496 · see citing works
Regenerating cellulose from ionic liquids for an accelerated enzymatic hydrolysis
Zhao, H., Jones, C. L., Baker, G. A., Xia, S., Olubajo, O., & Person, V. N. (2009) · Journal of Biotechnology · doi:10.1016/j.jbiotec.2008.08.009 · Cited by 492 · see citing works
Determination of the Structure of Cellulose II
Kolpak, F. J., & Blackwell, J. (1976) · Macromolecules · doi:10.1021/ma60050a019 · Cited by 491 · see citing works
Ionic liquid pretreatment of lignocellulosic biomass with ionic liquid–water mixtures
Brandt, A., Ray, M. J., To, T. Q., Leak, D. J., Murphy, R. J., & Welton, T. (2011) · Green Chemistry · doi:10.1039/c1gc15374a · Cited by 491 · see citing works
Self-citationSolubility of Carbohydrates in Ionic Liquids
Zakrzewska, M. E., Bogel-Łukasik, E., & Bogel-Łukasik, R. (2010) · Energy & Fuels · doi:10.1021/ef901215m · Cited by 490 · see citing works
Thermal degradation studies of alkyl-imidazolium salts and their application in nanocomposites
Awad, W. H., Gilman, J. W., Nyden, M. R., Harris, R. H. J., Sutto, T. E., Callahan, J. H., Trulove, P. C., DeLong, H. C., & Fox, D. M. (2003) · Thermochimica Acta · doi:10.1016/s0040-6031(03)00334-4 · Cited by 485 · see citing works
Designing enzyme-compatible ionic liquids that can dissolve carbohydrates
Zhao, H., Baker, G. A., Song, Z., Olubajo, O., Crittle, T. D., & Peters, D. (2008) · Green Chemistry · doi:10.1039/b801489b · Cited by 467 · see citing works
Pan, X., Gilkes, N. R., Kadla, J. F., Pye, K., Saka, S., Gregg, D. J., Ehara, K., Xie, D., Lam, D., & Saddler, J. N. (2006) · Biotechnology and Bioengineering · doi:10.1002/bit.20905 · Cited by 457 · see citing works
Ralph, J., Grabber, J. H., & Hatfield, R. D. (1995) · Carbohydrate Research · doi:10.1016/0008-6215(95)00237-n · Cited by 450 · see citing works
Acid in ionic liquid: An efficient system for hydrolysis of lignocellulose
Li, C., Wang, Q., & Zhao, Z. K. (2007) · Green Chemistry · doi:10.1039/b711512a · Cited by 447 · see citing works
Xu, A., Wang, J., & Wang, H. (2010) · Green Chem. · doi:10.1039/b916882f · Cited by 439 · see citing works
Cheng, G., Varanasi, P., Li, C., Liu, H., Melnichenko, Y. B., Simmons, B. A., Kent, M. S., & Singh, S. (2011) · Biomacromolecules · doi:10.1021/bm101240z · Cited by 437 · see citing works
Single-step conversion of cellulose to 5-hydroxymethylfurfural (HMF), a versatile platform chemical
Su, Y., Brown, H. M., Huang, X., Zhou, X.-D., Amonette, J. E., & Zhang, Z. C. (2009) · Applied Catalysis A: General · doi:10.1016/j.apcata.2009.04.002 · Cited by 436 · see citing works
Advances on biomass pretreatment using ionic liquids: An overview
Tadesse, H., & Luque, R. (2011) · Energy & Environmental Science · doi:10.1039/c0ee00667j · Cited by 434 · see citing works
Tan, S. S. Y., MacFarlane, D. R., Upfal, J., Edye, L. A., Doherty, W. O. S., Patti, A. F., Pringle, J. M., & Scott, J. L. (2009) · Green Chemistry · doi:10.1039/b815310h · Cited by 429 · see citing works
Sun, N., Rodríguez, H., Rahman, M., & Rogers, R. D. (2010) · Chemical Communications · doi:10.1039/c0cc03990j · Cited by 417 · see citing works
Ionic liquid salt-induced inactivation and unfolding of cellulase from Trichoderma reesei
Turner, M. B., Spear, S. K., Huddleston, J. G., Holbrey, J. D., & Rogers, R. D. (2003) · Green Chemistry · doi:10.1039/b302570e · Cited by 386 · see citing works
Room temperature ionic liquids as emerging solvents for the pretreatment of lignocellulosic biomass
Mora‐Pale, M., Meli, L., Doherty, T. V., Linhardt, R. J., & Dordick, J. S. (2011) · Biotechnology and Bioengineering · doi:10.1002/bit.23108 · Cited by 384 · see citing works
Development and implementation of integrated biomass supply analysis and logistics model (IBSAL)
Sokhansanj, S., Kumar, A., & Turhollow, A. (2006) · Biomass and Bioenergy · doi:10.1016/j.biombioe.2006.04.004 · Cited by 374 · see citing works
Li, Q., He, Y.-C., Xian, M., Jun, G., Xu, X., Yang, J., & Li, L. (2009) · Bioresource Technology · doi:10.1016/j.biortech.2009.02.040 · Cited by 362 · see citing works
Techno‐economic analysis of a lignocellulosic ethanol biorefinery with ionic liquid pre‐treatment
Klein‐Marcuschamer, D., Simmons, B. A., & Blanch, H. W. (2011) · Biofuels Bioproducts and Biorefining · doi:10.1002/bbb.303 · Cited by 362 · see citing works
Understanding the Interactions of Cellulose with Ionic Liquids: A Molecular Dynamics Study
Liu, H., Sale, K. L., Holmes, B. M., Simmons, B. A., & Singh, S. (2010) · The Journal of Physical Chemistry B · doi:10.1021/jp9117437 · Cited by 351 · see citing works
Zhu, J. Y., Pan, X., & Zalesny, R. S. (2010) · Applied Microbiology and Biotechnology · doi:10.1007/s00253-010-2654-8 · Cited by 350 · see citing works
INNOVATIVE APPLICATIONS OF IONIC LIQUIDS AS “GREEN” ENGINEERING LIQUIDS
Zhao, H. (2006) · Chemical Engineering Communications · doi:10.1080/00986440600586537 · Cited by 343 · see citing works
Thermal Degradation of Ionic Liquids at Elevated Temperatures
Baranyai, K. J., Deacon, G. B., MacFarlane, D. R., Pringle, J. M., & Scott, J. L. (2004) · Australian Journal of Chemistry · doi:10.1071/ch03221 · Cited by 338 · see citing works
Moreau, C., Finiels, A., & Vanoye, L. (2006) · Journal of Molecular Catalysis A Chemical · doi:10.1016/j.molcata.2006.03.046 · Cited by 334 · see citing works
The effect of the ionic liquid anion in the pretreatment of pine wood chips
Brandt, A., Hallett, J. P., Leak, D. J., Murphy, R. J., & Welton, T. (2010) · Green Chemistry · doi:10.1039/b918787a · Cited by 333 · see citing works
Self-citationInstantaneous dissolution of cellulose in organic electrolyte solutions
Rinaldi, R. (2010) · Chemical Communications · doi:10.1039/c0cc02421j · Cited by 330 · see citing works
Ionic liquid solvent properties as predictors of lignocellulose pretreatment efficacy
Doherty, T. V., Mora‐Pale, M., Foley, S. E., Linhardt, R. J., & Dordick, J. S. (2010) · Green Chemistry · doi:10.1039/c0gc00206b · Cited by 324 · see citing works
Lignin Extraction from Straw by Ionic Liquids and Enzymatic Hydrolysis of the Cellulosic Residues
Fu, D., Mazza, G., & Tamaki, Y. (2010) · Journal of Agricultural and Food Chemistry · doi:10.1021/jf903616y · Cited by 315 · see citing works
Ionic liquid pretreatment of cellulosic biomass: Enzymatic hydrolysis and ionic liquid recycle
Shill, K., Padmanabhan, S., Xin, Q., Prausnitz, J. M., Clark, D. S., & Blanch, H. W. (2010) · Biotechnology and Bioengineering · doi:10.1002/bit.23014 · Cited by 315 · see citing works
Yield and spatial supply of bioenergy poplar and willow short-rotation coppice in the UK
Aylott, M. J., Casella, E., Tubby, I., Street, N. R., Smith, P., & Taylor, G. (2008) · New Phytologist · doi:10.1111/j.1469-8137.2008.02396.x · Cited by 301 · see citing works
Cadoche, L., & López, G. D. (1989) · Biological Wastes · doi:10.1016/0269-7483(89)90069-4 · Cited by 290 · see citing works
Role of Solvent Parameters in the Regeneration of Cellulose from Ionic Liquid Solutions
Hauru, L. K. J., Hummel, M., King, A. W. T., Kilpeläinen, I., & Sixta, H. (2012) · Biomacromolecules · doi:10.1021/bm300912y · Cited by 288 · see citing works
Dinand, E., Vignon, M., Chanzy, H., & Heux, L. (2002) · Cellulose · doi:10.1023/a:1015877021688 · Cited by 285 · see citing works
About the structure of cellulose: debating the Lindman hypothesis
Glasser, W. G., Atalla, R. H., Blackwell, J., Brown, R. M., Burchard, W., French, A. D., Klemm, D., & Nishiyama, Y. (2012) · Cellulose · doi:10.1007/s10570-012-9691-7 · Cited by 285 · see citing works
Energy requirement for comminution of biomass in relation to particle physical properties
Miao, Z., Grift, T. E., Hansen, A. C., & Ting, K. C. (2011) · Industrial Crops and Products · doi:10.1016/j.indcrop.2010.12.016 · Cited by 279 · see citing works
Rheological Properties of Cellulose/Ionic Liquid Solutions: From Dilute to Concentrated States
Gericke, M., Schlufter, K., Liebert, T., Heinze, T., & Budtova, T. (2009) · Biomacromolecules · doi:10.1021/bm801430x · Cited by 276 · see citing works
Kumler, W. D., & Eiler, J. J. (1943) · Journal of the American Chemical Society · doi:10.1021/ja01252a028 · Cited by 274 · see citing works
Pan, X., Xie, D., Gilkes, N. R., Gregg, D. J., & Saddler, J. N. (2005) · Applied Biochemistry and Biotechnology · doi:10.1385/abab:124:1-3:1069 · Cited by 272 · see citing works
Acid‐Catalyzed Conversion of Sugars and Furfurals in an Ionic‐Liquid Phase
Sievers, C., Musin, I. R., Marzialetti, T. G., Olarte, M. V., Agrawal, P. K., & Jones, C. W. (2009) · ChemSusChem · doi:10.1002/cssc.200900092 · Cited by 256 · see citing works
From wood to fuels: Integrating biofuels and pulp production
Ragauskas, A. J., Nagy, M., Kim, D. H., Eckert, C. A., Hallett, J. P., & Liotta, C. L. (2006) · Industrial Biotechnology · doi:10.1089/ind.2006.2.55 · Cited by 256 · see citing works
Self-citationThermal degradation of cyano containing ionic liquids
Wooster, T. J., Johanson, K. M., Fraser, K. J., MacFarlane, D. R., & Scott, J. L. (2006) · Green Chemistry · doi:10.1039/b606395k · Cited by 255 · see citing works
Willför, S. M., Sundberg, K., Tenkanen, M., & Holmbom, B. R. (2007) · Carbohydrate Polymers · doi:10.1016/j.carbpol.2007.08.006 · Cited by 251 · see citing works
Cellulose Solvents – Remarkable History, Bright Future
Liebert, T. (2010) · ACS Symposium Series · doi:10.1021/bk-2010-1033.ch001 · Cited by 250 · see citing works
Fox, D. M., Awad, W. H., Gilman, J. W., Maupin, P. H., De Long, H. C., & Trulove, P. C. (2003) · Green Chemistry · doi:10.1039/b308444b · Cited by 246 · see citing works
Qiu, Z., Aita, G. M., & Walker, M. S. (2012) · Bioresource Technology · doi:10.1016/j.biortech.2012.04.070 · Cited by 246 · see citing works
The integration of green chemistry into future biorefineries
H. Clark, J., E. I. Deswarte, F., & J. Farmer, T. (2009) · Biofuels, Bioproducts and Biorefining · doi:10.1002/bbb.119 · Cited by 241 · see citing works
Yeast metabolic engineering for hemicellulosic ethanol production
Van Vleet, J., & Jeffries, T. (2009) · Current Opinion in Biotechnology · doi:10.1016/j.copbio.2009.06.001 · Cited by 241 · see citing works
Ionic liquids for biofuel production: Opportunities and challenges
Liu, C.-Z., Wang, F., Stiles, A. R., & Guo, C. (2012) · Applied Energy · doi:10.1016/j.apenergy.2011.11.031 · Cited by 236 · see citing works
Distillable Acid–Base Conjugate Ionic Liquids for Cellulose Dissolution and Processing
King, A. W. T., Asikkala, J., Mutikainen, I., Järvi, P., & Kilpeläinen, I. (2011) · Angewandte Chemie International Edition · doi:10.1002/anie.201100274 · Cited by 234 · see citing works
Oxidative Depolymerization of Lignin in Ionic Liquids
Stark, K. H., Taccardi, N., Bösmann, A., & Wasserscheid, P. (2010) · ChemSusChem · doi:10.1002/cssc.200900242 · Cited by 232 · see citing works
Ionic liquid tolerant hyperthermophilic cellulases for biomass pretreatment and hydrolysis
Datta, S., Holmes, B. M., Park, J. I., Chen, Z., Dibble, D., Hadi, M. Z., Blanch, H. W., Simmons, B. A., & Sapra, R. (2010) · Green Chemistry · doi:10.1039/b916564a · Cited by 229 · see citing works
Glucose Solvation by the Ionic Liquid 1,3-Dimethylimidazolium Chloride: A Simulation Study
Youngs, T. G. A., Hardacre, C., & Holbrey, J. D. (2007) · The Journal of Physical Chemistry B · doi:10.1021/jp076728k · Cited by 228 · see citing works
Li, W., Sun, N., Stoner, B., Jiang, X., Lü, X., & Rogers, R. D. (2011) · Green Chemistry · doi:10.1039/c1gc15522a · Cited by 226 · see citing works
The Potential of C4Perennial Grasses for Developing a Global BIOHEAT Industry
Samson, R., Mani, S., Boddey, R. M., Sokhansanj, S., Quesada, D., Urquiaga, S. S., Reis, V. M., & Lem, C. H. (2005) · Critical Reviews in Plant Sciences · doi:10.1080/07352680500316508 · Cited by 221 · see citing works
Lan, W., Liu, C., & Sun, R. (2011) · Journal of Agricultural and Food Chemistry · doi:10.1021/jf201508g · Cited by 216 · see citing works
The Lignol Approach to Biorefining of Woody Biomass to Produce Ethanol and Chemicals
Arato, C., Pye, E. K., & Gjennestad, G. (2005) · Applied Biochemistry and Biotechnology · doi:10.1385/abab:123:1-3:0871 · Cited by 214 · see citing works
Enzymatic in situ saccharification of cellulose in aqueous-ionic liquid media
Kamiya, N., Matsushita, Y., Hanaki, M., Nakashima, K., Narita, M., Goto, M., & Takahashi, H. (2008) · Biotechnology Letters · doi:10.1007/s10529-008-9638-0 · Cited by 207 · see citing works
Rinaldi, R., Meine, N., vom Stein, J., Palkovits, R., & Schüth, F. (2010) · ChemSusChem · doi:10.1002/cssc.200900281 · Cited by 201 · see citing works
Pinkert, A., Goeke, D. F., Marsh, K. N., & Pang, S. (2011) · Green Chemistry · doi:10.1039/c1gc15671c · Cited by 199 · see citing works
Cellulose extraction from wood chip in an ionic liquid 1-allyl-3-methylimidazolium chloride (AmimCl)
Wang, X., Li, H., Cao, Y., & Tang, Q. (2011) · Bioresource Technology · doi:10.1016/j.biortech.2011.05.064 · Cited by 198 · see citing works
Thermal stability of ionic liquids assessed by potentiometric titration
Meine, N., Benedito, F. L., & Rinaldi, R. (2010) · Green Chemistry · doi:10.1039/c0gc00091d · Cited by 197 · see citing works
Genetic Improvement of Willow for Bioenergy and BiofuelsFree Access
Karp, A., Hanley, S. J., Trybush, S. O., Macalpine, W., Pei, M., & Shield, I. (2011) · Journal of Integrative Plant Biology · doi:10.1111/j.1744-7909.2010.01015.x · Cited by 196 · see citing works
Remsing, R. C., Hernandez, G., Swatloski, R. P., Massefski, W. W., Rogers, R. D., & Moyna, G. (2008) · The Journal of Physical Chemistry B · doi:10.1021/jp8042895 · Cited by 193 · see citing works
Ionic liquids in the biorefinery: a critical assessment of their potential
Stark, A. (2010) · Energy & Environmental Science · doi:10.1039/c0ee00246a · Cited by 193 · see citing works
Aqueous ionic liquid pretreatment of straw
Fu, D., & Mazza, G. (2011) · Bioresource Technology · doi:10.1016/j.biortech.2011.04.049 · Cited by 191 · see citing works
Enzyme activities in cocoa beans during fermentation
Hansen, C. E., del Olmo, M., & Burri, C. (1998) · Journal of the Science of Food and Agriculture · doi:10.1002/(sici)1097-0010(199806)77:2 · Cited by 188 · see citing works
Influence of water on the dissolution of cellulose in selected ionic liquids
Mazza, M., Catana, D.-A., Vaca‐García, C., & Cecutti, C. (2008) · Cellulose · doi:10.1007/s10570-008-9257-x · Cited by 184 · see citing works
Use of ionic liquids in converting lignocellulosic material to biofuels
Vancov, T., Alston, A.-S., Brown, T. C., & McIntosh, S. R. (2012) · Renewable Energy · doi:10.1016/j.renene.2012.02.033 · Cited by 181 · see citing works
Preparation and polymerization of new organic molten salts; N-alkylimidazolium salt derivatives
Hirao, M., Ito, K., & Ohno, H. (2000) · Electrochimica Acta · doi:10.1016/s0013-4686(99)00334-5 · Cited by 179 · see citing works
Viscosity of Cellulose−Imidazolium-Based Ionic Liquid Solutions
Sescousse, R., Le, K. A., Ries, M. E., & Budtova, T. (2010) · The Journal of Physical Chemistry B · doi:10.1021/jp1024203 · Cited by 178 · see citing works
Study on the Solubility of Cellulose in Aqueous Alkali Solution by Deuteration IR and 13C NMR
Kamida, K., Okajima, K., Matsui, T., & Kowsaka, K. (1984) · Polymer Journal · doi:10.1295/polymj.16.857 · Cited by 177 · see citing works
Abe, M., Fukaya, Y., & Ohno, H. (2012) · Chemical Communications · doi:10.1039/c2cc16203b · Cited by 176 · see citing works
Ionic Liquids for Electrochemical Devices
HAGIWARA, R., & LEE, J. S. (2007) · Electrochemistry · doi:10.5796/electrochemistry.75.23 · Cited by 174 · see citing works
Factors Affecting Wood Dissolution and Regeneration of Ionic Liquids
Li, B., Asikkala, J., Filpponen, I., & Argyropoulos, D. S. (2010) · Industrial & Engineering Chemistry Research · doi:10.1021/ie901560p · Cited by 172 · see citing works
Kline, L. M., Hayes, D. G., Womac, A. R., & Labbé, N. (2010) · BioResources · doi:10.15376/biores.5.3.1366-1383 · Cited by 170 · see citing works
Lawoko, M., Henriksson, G., & Gellerstedt, G. (2006) · Holzforschung · doi:10.1515/hf.2006.025 · Cited by 164 · see citing works
Vanoye, L., Fanselow, M., Holbrey, J. D., Atkins, M. P., & Seddon, K. R. (2009) · Green Chemistry · doi:10.1039/b817882h · Cited by 158 · see citing works
Guo, Z., Lue, B., Thomasen, K., Meyer, A. S., & Xu, X. (2007) · Green Chemistry · doi:10.1039/b709786g · Cited by 158 · see citing works
Ionic-Liquid-Phase Hydrolysis of Pine Wood
Sievers, C., Olarte, M. V., Marzialetti, T. G., Musin, I. R., Agrawal, P. K., & Jones, C. W. (2009) · Industrial & Engineering Chemistry Research · doi:10.1021/ie801174x · Cited by 156 · see citing works
Tailored Media for Homogeneous Cellulose Chemistry: Ionic Liquid/Co‐Solvent Mixtures
Gericke, M., Liebert, T. F., Seoud, O. A. E., & Heinze, T. J. (2011) · Macromolecular Materials and Engineering · doi:10.1002/mame.201000330 · Cited by 156 · see citing works
Enhanced enzymatic hydrolysis of sugarcane bagasse by N-methylmorpholine-N-oxide pretreatment
Kuo, C.-H., & Lee, C.-K. (2009) · Bioresource Technology · doi:10.1016/j.biortech.2008.07.001 · Cited by 156 · see citing works
The Ultrastructure of Wood from a Solubility Parameter Point of View
Hansen, C. M., & Björkman, A. (1998) · Holzforschung · doi:10.1515/hfsg.1998.52.4.335 · Cited by 155 · see citing works
Kuhlmann, E., Himmler, S., Giebelhaus, H., & Wasserscheid, P. (2007) · Green Chem. · doi:10.1039/b611974c · Cited by 150 · see citing works
Ouellet, M., Datta, S., Dibble, D., Tamrakar, P., Benke, P. I., Li, C., Singh, S., Sale, K. L., Adams, P. D., Keasling, J. D., et al. (2011) · Green Chemistry · doi:10.1039/c1gc15327g · Cited by 148 · see citing works
The effect of ionic liquid cation and anion combinations on the macromolecular structure of lignins
George, A., Tran, K. L. T., Morgan, T. J., Benke, P. I., Berrueco, C., Lorente, E., Wu, B., Keasling, J. D., Simmons, B. A., & Holmes, B. M. (2011) · Green Chemistry · doi:10.1039/c1gc15543a · Cited by 146 · see citing works
Facile pretreatment of lignocellulosic biomass at high loadings in room temperature ionic liquids
Wu, H., Mora‐Pale, M., Miao, J., Doherty, T. V., Linhardt, R. J., & Dordick, J. S. (2011) · Biotechnology and Bioengineering · doi:10.1002/bit.23266 · Cited by 142 · see citing works
Seeberger, A., Andresen, A.-K., & Jess, A. (2009) · Physical Chemistry Chemical Physics · doi:10.1039/b909624h · Cited by 141 · see citing works
Cox, B. J., Jia, S., Zhang, Z. C., & Ekerdt, J. G. (2011) · Polymer Degradation and Stability · doi:10.1016/j.polymdegradstab.2011.01.011 · Cited by 137 · see citing works
Engel, P., Mladenov, R., Wulfhorst, H., Jäger, G., & Spiess, A. C. (2010) · Green Chemistry · doi:10.1039/c0gc00135j · Cited by 137 · see citing works
Köhler, S., Liebert, T., Schöbitz, M., Schaller, J., Meister, F., Günther, W., & Heinze, T. (2007) · Macromolecular Rapid Communications · doi:10.1002/marc.200700529 · Cited by 136 · see citing works
Understanding the impact of ionic liquid pretreatment on eucalyptus
Çetinkol, Ö. P., Dibble, D. C., Cheng, G., Kent, M. S., Knierim, B., Auer, M., Wemmer, D. E., Pelton, J. G., Melnichenko, Y. B., Ralph, J., et al. (2010) · Biofuels · doi:10.4155/bfs.09.5 · Cited by 135 · see citing works
Modeling interactions between lignocellulose and ionic liquids using DFT-D
Janesko, B. G. (2011) · Physical Chemistry Chemical Physics · doi:10.1039/c1cp20072k · Cited by 135 · see citing works
Thermostability of imidazolium ionic liquids as direct solvents for cellulose
Wendler, F., Todi, L.-N., & Meister, F. (2012) · Thermochimica Acta · doi:10.1016/j.tca.2011.11.015 · Cited by 134 · see citing works
A facile method for the recovery of ionic liquid and lignin from biomass pretreatment
Dibble, D., Li, C., Sun, L., George, A., Cheng, A., Çetinkol, Ö. P., Benke, P. I., Holmes, B. M., Singh, S., & Simmons, B. A. (2011) · Green Chemistry · doi:10.1039/c1gc15111h · Cited by 134 · see citing works
Electrospun nanosized cellulose fibers using ionic liquids at room temperature
Freire, M. G., Teles, A. R. R., Ferreira, R. A. S., Carlos, L. D., Lopes-da-Silva, J. A., & Coutinho, J. A. P. (2011) · Green Chemistry · doi:10.1039/c1gc15930e · Cited by 132 · see citing works
Arora, R., Manisseri, C., Li, C., Ong, M. D., Scheller, H. V., Vogel, K. P., Simmons, B. A., & Singh, S. (2010) · BioEnergy Research · doi:10.1007/s12155-010-9087-1 · Cited by 132 · see citing works
Modelling cellulose solubilities in ionic liquids using COSMO-RS
Kahlen, J., Masuch, K., & Leonhard, K. (2010) · Green Chemistry · doi:10.1039/c0gc00200c · Cited by 130 · see citing works
Pottkämper, J., Barthen, P., Ilmberger, N., Schwaneberg, U., Schenk, A., Schulte, M. M., Ignatíev, N., & Streit, W. R. (2009) · Green Chemistry · doi:10.1039/b820157a · Cited by 129 · see citing works
Optimization of processing conditions for the pretreatment of wheat straw using aqueous ionic liquid
Fu, D., & Mazza, G. (2011) · Bioresource Technology · doi:10.1016/j.biortech.2011.06.023 · Cited by 119 · see citing works
Kuhlmann, E., Himmler, S., Giebelhaus, H., & Wasserscheid, P. (2007) · ChemInform · doi:10.1002/chin.200730193 · Cited by 118 · see citing works
Zhu, J., Zhu, W., O’Bryan, P. J., Dien, B. S., Tian, S., Gleisner, R., & Pan, X. (2010) · Applied Microbiology and Biotechnology · doi:10.1007/s00253-009-2408-7 · Cited by 114 · see citing works
Recovery of Sugars from Ionic Liquid Biomass Liquor by Solvent Extraction
Brennan, T. C. R., Datta, S., Blanch, H. W., Simmons, B. A., & Holmes, B. M. (2010) · BioEnergy Research · doi:10.1007/s12155-010-9091-5 · Cited by 110 · see citing works
Gross, A. S., Bell, A. T., & Chu, J. (2011) · The Journal of Physical Chemistry B · doi:10.1021/jp202415v · Cited by 100 · see citing works
High glucose yields from the hydrolysis of cellulose dissolved in ionic liquids
Morales-delaRosa, S., Campos-Martin, J. M., & Fierro, J. L. G. (2012) · Chemical Engineering Journal · doi:10.1016/j.cej.2011.11.061 · Cited by 94 · see citing works
Reaction behavior of wood in an ionic liquid, 1-ethyl-3-methylimidazolium chloride
Miyafuji, H., Miyata, K., Saka, S., Ueda, F., & Mori, M. (2009) · Journal of Wood Science · doi:10.1007/s10086-009-1020-x · Cited by 93 · see citing works
Design of Cellulose Dissolving Ionic Liquids Inspired by Nature
Ohira, K., Abe, Y., Kawatsura, M., Suzuki, K., Mizuno, M., Amano, Y., & Itoh, T. (2012) · ChemSusChem · doi:10.1002/cssc.201100427 · Cited by 92 · see citing works
Torr, K. M., Love, K. T., Çetinkol, Ö. P., Donaldson, L. A., George, A., Holmes, B. M., & Simmons, B. A. (2012) · Green Chemistry · doi:10.1039/c2gc16362d · Cited by 91 · see citing works
Imidazolium Ionic Liquids as Solvents for Cerium(IV)-Mediated Oxidation Reactions
Hasan, M., Bodor, A., Lantos, D., Horváth, I. T., Vos, D. E. D., & Binnemans, K. (2006) · The Journal of Organic Chemistry · doi:10.1021/jo061909o · Cited by 87 · see citing works
Selective extraction of hemicelluloses from spruce using switchable ionic liquids
Anugwom, I., Mäki-Arvela, P., Virtanen, P., Willför, S., Sjöholm, R., & Mikkola, J.-P. (2012) · Carbohydrate Polymers · doi:10.1016/j.carbpol.2011.10.006 · Cited by 84 · see citing works
Qian, X., Ding, S., Nimlos, M. R., Johnson, D. K., & Himmel, M. E. (2005) · Macromolecules · doi:10.1021/ma051683b · Cited by 78 · see citing works
Himmler, S., Hörmann, S., van Hal, R., Schulz, P. S., & Wasserscheid, P. (2006) · Green Chemistry · doi:10.1039/b601583b · Cited by 77 · see citing works
Xie, H., Shen, H., Gong, Z., Wang, Q., Zhao, Z. K., & Bai, F. (2012) · Green Chemistry · doi:10.1039/c2gc00033d · Cited by 75 · see citing works
King, A. W. T., Parviainen, A., Karhunen, P., Matikainen, J., Hauru, L. K. J., Sixta, H., & Kilpeläinen, I. (2012) · RSC Advances · doi:10.1039/c2ra21287k · Cited by 75 · see citing works
Intraprotoplasmic feruloylation of arabinoxylans in Festuca arundinacea cell cultures
Myton, K., & Fry, S. (1994) · Planta · doi:10.1007/bf00201809 · Cited by 75 · see citing works
Marques, A. P., Evtuguin, D. V., Magina, S., Amado, F. M. L., & Prates, A. (2009) · Journal of Wood Chemistry and Technology · doi:10.1080/02773810903207754 · Cited by 75 · see citing works
Activation of lignocellulosic biomass by ionic liquid for biorefinery fractionation
Labbé, N., Kline, L. M., Moens, L., Kim, K., Kim, P. C., & Hayes, D. G. (2012) · Bioresource Technology · doi:10.1016/j.biortech.2011.10.062 · Cited by 74 · see citing works
Thermal Decomposition Study of Isolated Lignin Using Temperature Modulated TGA
Kubo, S., & Kadla, J. F. (2008) · Journal of Wood Chemistry and Technology · doi:10.1080/02773810802124928 · Cited by 71 · see citing works
Disintegration and dissolution kinetics of wood chips in ionic liquids
Viell, J., & Marquardt, W. (2011) · Holzforschung · doi:10.1515/hf.2011.072 · Cited by 65 · see citing works
Esterification in Ionic Liquids: The Influence of Solvent Basicity
Wells, T. P., Hallett, J. P., Williams, C. K., & Welton, T. (2008) · The Journal of Organic Chemistry · doi:10.1021/jo8005864 · Cited by 65 · see citing works
Self-citationSathitsuksanoh, N., Zhu, Z., & Zhang, Y.-H. P. (2012) · Cellulose · doi:10.1007/s10570-012-9719-z · Cited by 63 · see citing works
Auxenfans, T., Buchoux, S., Djellab, K., Avondo, C., Husson, E., & Sarazin, C. (2012) · Carbohydrate Polymers · doi:10.1016/j.carbpol.2012.05.101 · Cited by 63 · see citing works
Zoia, L., King, A., & Argyropoulos, D. (2011) · Journal of Agricultural and Food Chemistry · doi:10.1021/jf103615e · Cited by 62 · see citing works
Self-Repairing DNA Based on a Reductive Electron Transfer through the Base Stack
Schwögler, A., Burgdorf, L. T., & Carell, T. (2000) · Angewandte Chemie International Edition · doi:10.1002/1521-3773(20001103)39:21 · Cited by 59 · see citing works
Efficient acid-catalyzed hydrolysis of cellulose in organic electrolyte solutions
Zhang, Z., Liu, B., & Zhao, Z. (. (2012) · Polymer Degradation and Stability · doi:10.1016/j.polymdegradstab.2012.01.010 · Cited by 55 · see citing works
Solubility and rate of dissolution for Miscanthus in hydrophilic ionic liquids
Padmanabhan, S., Kim, M., Blanch, H. W., & Prausnitz, J. M. (2011) · Fluid Phase Equilibria · doi:10.1016/j.fluid.2011.06.034 · Cited by 55 · see citing works
Dissolving lignocellulosic biomass in a 1-butyl-3-methylimidazolium chloride–water mixture
Wei, L., Li, K., Ma, Y., & Hou, X. (2012) · Industrial Crops and Products · doi:10.1016/j.indcrop.2011.12.012 · Cited by 54 · see citing works
Gross, A. S., Bell, A. T., & Chu, J. (2012) · Physical Chemistry Chemical Physics · doi:10.1039/c2cp40417f · Cited by 50 · see citing works
Kubo, S., Hashida, K., Yamada, T., Hishiyama, S., Magara, K., Kishino, M., Ohno, H., & Hosoya, S. (2008) · Journal of Wood Chemistry and Technology · doi:10.1080/02773810802124845 · Cited by 46 · see citing works
Dialkyl Phosphate-Related Ionic Liquids as Selective Solvents for Xylan
Froschauer, C., Hummel, M., Laus, G., Schottenberger, H., Sixta, H., Weber, H. K., & Zuckerstätter, G. (2012) · Biomacromolecules · doi:10.1021/bm300582s · Cited by 46 · see citing works
An Integrated Catalytic Approach to Fermentable Sugars from Cellulose
Rinaldi, R., Engel, P., Büchs, J., Spiess, A. C., & Schüth, F. (2010) · ChemSusChem · doi:10.1002/cssc.201000153 · Cited by 45 · see citing works
Dorn, S., Wendler, F., Meister, F., & Heinze, T. (2008) · Macromolecular Materials and Engineering · doi:10.1002/mame.200800153 · Cited by 44 · see citing works
Pretreatment of microcrystalline cellulose in organic electrolyte solutions for enzymatic hydrolysis
Tian, X.-F., Fang, Z., Jiang, D., & Sun, X.-Y. (2011) · Biotechnology for Biofuels · doi:10.1186/1754-6834-4-53 · Cited by 44 · see citing works
Mai, N. L., Nguyen, N., Kim, J.-I., Park, H., Lee, S., & Koo, Y. (2011) · Journal of Chromatography A · doi:10.1016/j.chroma.2011.12.030 · Cited by 41 · see citing works
Alkanolamine Ionic Liquids and Their Inability To Dissolve Crystalline Cellulose
Pinkert, A., Marsh, K. N., & Pang, S. (2010) · Industrial & Engineering Chemistry Research · doi:10.1021/ie101250v · Cited by 41 · see citing works
The Affinities of Organic Solvents in Biological Systems
Hansen, C. M., & Andersen, B. H. (1988) · American Industrial Hygiene Association Journal · doi:10.1080/15298668891379783 · Cited by 40 · see citing works
Soaking of pine wood chips with ionic liquids for reduced energy input during grinding
Brandt‐Talbot, A., Erickson, J. K., Hallett, J. P., Murphy, R. J., Potthast, A., Ray, M. J., Rosenau, T., Schrems, M., & Welton, T. (2012) · Green Chemistry · doi:10.1039/c2gc15663f · Cited by 40 · see citing works
Self-citationBrereton, N. J., Pitre, F. E., Ray, M. J., Karp, A., & Murphy, R. J. (2011) · Biotechnology for Biofuels · doi:10.1186/1754-6834-4-13 · Cited by 40 · see citing works
Extraction of lignins from aqueous–ionic liquid mixtures by organic solvents
Xin, Q., Pfeiffer, K., Prausnitz, J. M., Clark, D. S., & Blanch, H. W. (2012) · Biotechnology and Bioengineering · doi:10.1002/bit.24337 · Cited by 37 · see citing works
Ionic liquids in enzymatic catalysis and biochemical methods of analysis: Capabilities and prospects
Muginova, S. V., Galimova, A. Z., Polyakov, A. E., & Shekhovtsova, T. N. (2010) · Journal of Analytical Chemistry · doi:10.1134/s1061934810040027 · Cited by 36 · see citing works
Flagged first, then by citations
2 of the 214 references couldn’t be matched to a known paper.
Research works printed but not linked: 7
- Meng, 2012, e-Polymers, 028, 1
- King, 2011, Angew. Chem., Int. Ed., 50, 6301, 10.1002/anie.201100274 · DOI
- Gericke, 2011, Macromol. Mater. Eng., 296, 483, 10.1002/mame.201000330 · DOI
- Padmanabhan, 2011, Fluid Phase Equilib., 309, 89, 10.1016/j.fluid.2011.06.034 · DOI
- Padmanabhan, 2011, Fluid Phase Equilib., 309, 89, 10.1016/j.fluid.2011.06.034 · DOI
- McDonough, 1993, Tappi J., 186
- Mäki-Arvela, 2012, Int. J. Chem. Eng., 674761
Cited by
Sorted by citations
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Bui, M., Adjiman, C. S., Bardow, A., Anthony, E. J., Boston, A., Brown, S., Fennell, P. S., Fuss, S., Galindo, A., Hackett, L. A., et al. (2018) · Energy & Environmental Science · doi:10.1039/c7ee02342a · Cited by 4,374 · see citing works
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Wang, S., Dai, G., Yang, H., & Luo, Z. (2017) · Progress in Energy and Combustion Science · doi:10.1016/j.pecs.2017.05.004 · Cited by 2,613 · see citing works
Chemicals from lignin: an interplay of lignocellulose fractionation, depolymerisation, and upgrading
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Kan, T., Strezov, V., & Evans, T. J. (2016) · Renewable and Sustainable Energy Reviews · doi:10.1016/j.rser.2015.12.185 · Cited by 2,239 · see citing works
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Rinaldi, R., Jastrzebski, R., Clough, M. T., Ralph, J., Kennema, M., Bruijnincx, P. C. A., & Weckhuysen, B. M. (2016) · Angewandte Chemie International Edition · doi:10.1002/anie.201510351 · Cited by 2,140 · see citing works
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Xu, C., Paone, E., Rodríguez‐Padrón, D., Luque, R., & Mauriello, F. (2020) · Chemical Society Reviews · doi:10.1039/d0cs00041h · Cited by 1,049 · see citing works
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Ionic liquids: Promising green solvents for lignocellulosic biomass utilization
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Chemocatalytic hydrolysis of cellulose into glucose over solid acid catalysts
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Clough, M. T., Geyer, K., Hunt, P. A., Mertes, J., & Welton, T. (2013) · Physical Chemistry Chemical Physics · doi:10.1039/c3cp53648c · Cited by 259 · see citing works
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Lindman, B., Medronho, B., Alves, L., Costa, C., Edlund, H., & Norgren, M. (2017) · Physical Chemistry Chemical Physics · doi:10.1039/c7cp02409f · Cited by 249 · see citing works
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Green chemistry, catalysis and valorization of waste biomass
Sheldon, R. A. (2016) · Journal of Molecular Catalysis A Chemical · doi:10.1016/j.molcata.2016.01.013 · Cited by 213 · see citing works
Loow, Y.-L., Wu, T. Y., Yang, G. H., Ang, L. Y., New, E. K., Siow, L. F., Jahim, J. M., Mohammad, A. W., & Teoh, W. H. (2017) · Bioresource Technology · doi:10.1016/j.biortech.2017.07.165 · Cited by 211 · see citing works
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Lou, R., Ma, R., Lin, K.-T., Ahamed, A., & Zhang, X. (2019) · ACS Sustainable Chemistry & Engineering · doi:10.1021/acssuschemeng.8b05816 · Cited by 208 · see citing works
Veisi, H., Öztürk, T., Karmakar, B., Tamoradi, T., & Hemmati, S. (2020) · Carbohydrate Polymers · doi:10.1016/j.carbpol.2020.115966 · Cited by 207 · see citing works
RetractedProcessing and valorization of cellulose, lignin and lignocellulose using ionic liquids
Xia, Z., Li, J., Zhang, J., Zheng, X., Zhang, J. P., & Zhang, J. P. (2020) · Journal of Bioresources and Bioproducts · doi:10.1016/j.jobab.2020.04.001 · Cited by 203 · see citing works
Structural changes in lignins isolated using an acidic ionic liquid water mixture
Brandt‐Talbot, A., Chen, L., van Dongen, B. E., Welton, T., & Hallett, J. P. (2015) · Green Chemistry · doi:10.1039/c5gc01314c · Cited by 201 · see citing works
Self-citationPretreatment of Lignocellulosic Biomass with Ionic Liquids and Ionic Liquid-Based Solvent Systems
Hou, Q., Ju, M., Li, W., Liu, L., Chen, Y., & Yang, Q. (2017) · Molecules · doi:10.3390/molecules22030490 · Cited by 201 · see citing works
Zhang, J., Wang, Y., Zhang, L., Zhang, R., Liu, G., & Cheng, G. (2013) · Bioresource Technology · doi:10.1016/j.biortech.2013.10.009 · Cited by 199 · see citing works
- Authors
- Brandt, A., Gräsvik, J., Hallett, J. P., & Welton, T.
- Affiliations
- Umeå University (SE)
- Imperial College London (GB)
- Corresponding author
- Welton, Tom
- Venue
- Green Chemistry
- Publisher
- Royal Society of Chemistry (RSC)
- Published
- 2013
- Volume
- 15
- Issue
- 3
- Pages
- 550
- ISSN
- 1463-9262 (ISSN-L)
- 1463-9270
- OpenAlex
- W2166219224
- Semantic Scholar
- 3bb1c838477a538886acfa02e851d8079e8c1051
- Cited by
- 1,557
- References
- 214
- Citations by year
- 2026: 61 · 2025: 92 · 2024: 81 · 2023: 101 · 2022: 115 · 2021: 159 · 2020: 154 · 2019: 141 · 2018: 130 · 2017: 164 · 2016: 130 · 2015: 113 · 2014: 85 · 2013: 30 · 2012: 1
- FWCI
- 41.71
- Type
- journal article
- Language
- en
- Open access
- bronze
- doi.org
- Locations
- Green Chemistry (publishedVersion)
- Funders
- Engineering and Physical Sciences Research Council (EP/K014676/1)
- Topics
- Physical Sciences › Engineering › Biomedical Engineering › Biofuel production and bioconversion
- Physical Sciences › Chemical Engineering › Catalysis › Ionic liquids properties and applications
- Physical Sciences › Engineering › Biomedical Engineering › Catalysis for Biomass Conversion
- Keywords
- ionic liquids, lignocellulosic biomass, biomass pretreatment, biomass deconstruction, biomass fractionation, process design
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