The DOI matches its Crossref record; 55 of the 59 references it cites were found in a registry or an index.
Introducing and energy analysis of a novel cryogenic hydrogen liquefaction process configuration
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In the citing paper
“If H2 liquefaction is carried out without catalytic conversion of o- to p-H2, the ortho isomer will be at a higher concentration than its equilibrium concentration and will thus spontaneously convert to the para isomer, generating a significant amount of heat [50].”
From Strategies to recover and minimize boil-off losses during liquid hydrogen storage (2023) · cites this paper as [50]
In the citing paper
“In the second stage, the pre-cooled H2 passes through a heat exchanger to reach 30 K through a cryocooling system, which operates with refrigeration cycles such as the helium reverse Brayton cycle (possibly with H2 as well, but there is a minimum temperature limitation [80]) or the H2 Claude cycle [79].”
From Strategies to recover and minimize boil-off losses during liquid hydrogen storage (2023) · cites this paper as [79]
In the citing paper
“To give figures, liquefying H2 from ambient conditions theoretically and ideally requires about 10 times more energy than LNG, i.e., 3.92 kWh/kg LH2 versus 0.31 kWh/kg LNG [79].”
From Strategies to recover and minimize boil-off losses during liquid hydrogen storage (2023) · cites this paper as [79]
In the citing paper
“The Claude process has higher liquefaction efficiency and lower power consumption than the L–H process.170”
From Strategies To Improve the Performance of Hydrogen Storage Systems by Liquefaction Methods: A Comprehensive Review (2023) · cites this paper as [170]
In the citing paper
“The results showed that the developed process’ SEC decreased from 4.410 to 4.022 kWh/kgLH2 compared to the basic plant,170 and its exergy efficiency increased from 55.47% to 73.75%.”
From Strategies To Improve the Performance of Hydrogen Storage Systems by Liquefaction Methods: A Comprehensive Review (2023) · cites this paper as [170]
In the citing paper
“Mehrpooya et al. used the CCs in multistream heat exchangers to reduce the SEC in H2 liquefaction systems.71,92,170,313−315”
From Strategies To Improve the Performance of Hydrogen Storage Systems by Liquefaction Methods: A Comprehensive Review (2023) · cites this paper as [170]
Citations
Cites
A New Two-Constant Equation of State
Peng, D., & Robinson, D. B. (1976) · Industrial & Engineering Chemistry Fundamentals · doi:10.1021/i160057a011 · Cited by 13,112
Equilibrium constants from a modified Redlich-Kwong equation of state
Soave, G. S. (1972) · Chemical Engineering Science · doi:10.1016/0009-2509(72)80096-4 · Cited by 6,447
The Exergy Method of Thermal Plant Analysis
(1985) · Elsevier eBooks · doi:10.1016/c2013-0-00894-8 · Cited by 2,935
(2009) · doi:10.1016/j.ijhydene.2010.02.109 · Cited by 369
(2014) · CRC Press eBooks · doi:10.1201/b17226 · Cited by 235
An exergy analysis of small-scale liquefied natural gas (LNG) liquefaction processes
Remeljej, C. W., & Hoadley, A. (2005) · Energy · doi:10.1016/j.energy.2005.09.005 · Cited by 232
Mehrpooya, M., Sharifzadeh, M. M. M., & Rosen, M. A. (2015) · Energy · doi:10.1016/j.energy.2015.07.101 · Cited by 210
Self-citationTimmerhaus, K. D., & Flynn, T. M. (1989) · Springer eBooks · doi:10.1007/978-1-4684-8756-5 · Cited by 205
Advanced exergetic analysis of five natural gas liquefaction processes
Vatani, A., Mehrpooya, M., & Palizdar, A. (2013) · Energy Conversion and Management · doi:10.1016/j.enconman.2013.11.050 · Cited by 196
Self-citationHandbook of Process Integration (PI). Minimisation of Energy and Water Use, Waste and Emissions
Trafczyński, M. (2014) · Journal of Cleaner Production · doi:10.1016/j.jclepro.2014.04.010 · Cited by 195
Source composite curve for waste reduction
Bandyopadhyay, S. K. (2006) · Chemical Engineering Journal · doi:10.1016/j.cej.2006.08.007 · Cited by 187
Mohammadi, A., & Mehrpooya, M. (2016) · Journal of Cleaner Production · doi:10.1016/j.jclepro.2016.08.057 · Cited by 139
Self-citationAnsarinasab, H., Mehrpooya, M., & Mohammadi, A. (2017) · Journal of Cleaner Production · doi:10.1016/j.jclepro.2017.01.014 · Cited by 134
Self-citationLarge-scale hydrogen liquefier utilising mixed-refrigerant pre-cooling
Berstad, D., Stang, J., & Nekså, P. (2010) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2010.02.001 · Cited by 131
Energy and exergy analyses of five conventional liquefied natural gas processes
Vatani, A., Mehrpooya, M., & Palizdar, A. (2014) · International Journal of Energy Research · doi:10.1002/er.3193 · Cited by 131
Self-citationProposal of an innovative, high-efficiency, large-scale hydrogen liquefier
Valenti, G., & Macchi, E. (2008) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2008.03.044 · Cited by 125
Mehrpooya, M., Sharifzadeh, M. M. M., & Rosen, M. A. (2016) · Energy · doi:10.1016/j.energy.2015.12.008 · Cited by 122
Self-citationMehrpooya, M., Dehghani, H., & Moosavian, S. M. A. (2015) · Journal of Power Sources · doi:10.1016/j.jpowsour.2015.11.103 · Cited by 121
Self-citationConceptual design of a high efficiency large capacity hydrogen liquefier
Quack, H. (2002) · AIP Conference Proceedings · doi:10.1063/1.1472029 · Cited by 121
Optimal operation of a large-scale liquid hydrogen plant utilizing mixed fluid refrigeration system
Krasae-in, S. (2014) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2014.02.046 · Cited by 118
Krasae-in, S., Stang, J. H., & Neksa, P. (2010) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2010.08.062 · Cited by 117
Liquid hydrogen fuel system design and demonstration in a small long endurance air vehicle
Stroman, R. O., Schuette, M. W., Swider‐Lyons, K. E., Rodgers, J. A., & Edwards, D. J. (2014) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2014.05.065 · Cited by 113
Mehrpooya, M., Kalhorzadeh, M., & Chahartaghi, M. (2015) · Journal of Cleaner Production · doi:10.1016/j.jclepro.2015.12.058 · Cited by 107
Self-citationPrediction of standard chemical exergy by a three descriptors QSPR model
Gharagheizi, F., & Mehrpooya, M. (2007) · Energy Conversion and Management · doi:10.1016/j.enconman.2007.04.005 · Cited by 102
Self-citationGeothermal energy use in absorption precooling for Claude hydrogen liquefaction cycle
Kanoglu, M., Yilmaz, C., & Abusoglu, A. (2016) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2016.04.068 · Cited by 102
Economics of hydrogen production and liquefaction by geothermal energy
Yılmaz, C., Kanoğlu, M., Bolattürk, A., & Gadalla, M. A. E. (2011) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2011.06.037 · Cited by 99
Novel LNG-Based Integrated Process Configuration Alternatives for Coproduction of LNG and NGL
Mehrpooya, M., Hossieni, M., & Vatani, A. (2014) · Industrial & Engineering Chemistry Research · doi:10.1021/ie502370p · Cited by 90
Self-citationYazdanfar, J., Mehrpooya, M., Yousefi, H., & Palizdar, A. (2015) · Energy Conversion and Management · doi:10.1016/j.enconman.2015.03.076 · Cited by 88
Self-citationExergy analysis of C2+ recovery plants refrigeration cycles
Tirandazi, B., Mehrpooya, M., Vatani, A., & Moosavian, S. M. A. (2010) · Process Safety and Environmental Protection · doi:10.1016/j.cherd.2010.10.006 · Cited by 85
Self-citationGeothermal energy use in hydrogen liquefaction
KANOGLU, M., DINCER, I., & ROSEN, M. (2007) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2007.06.006 · Cited by 84
Comparison criteria for large-scale hydrogen liquefaction processes
Berstad, D., Stang, J., & Nekså, P. (2009) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2008.11.058 · Cited by 83
Advanced exergoeconomic evaluation of single mixed refrigerant natural gas liquefaction processes
Mehrpooya, M., & Ansarinasab, H. (2015) · Journal of Natural Gas Science and Engineering · doi:10.1016/j.jngse.2015.07.019 · Cited by 79
Self-citationLowesmith, B. J., Hankinson, G., & Chynoweth, S. (2014) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2014.08.002 · Cited by 77
Exergoeconomic evaluation of single mixed refrigerant natural gas liquefaction processes
Mehrpooya, M., & Ansarinasab, H. (2015) · Energy Conversion and Management · doi:10.1016/j.enconman.2015.04.038 · Cited by 77
Self-citationMehrpooya, M., Bahramian, P., Pourfayaz, F., & Rosen, M. A. (2016) · Sustainable Energy Technologies and Assessments · doi:10.1016/j.seta.2016.10.003 · Cited by 75
Self-citationEnergy and advanced exergy analysis of an existing hydrocarbon recovery process
Mehrpooya, M., Lazemzade, R., Sadaghiani, M. S., & Parishani, H. (2016) · Energy Conversion and Management · doi:10.1016/j.enconman.2016.06.069 · Cited by 72
Self-citationAdvanced exergoeconomic analysis of the multistage mixed refrigerant systems
Mehrpooya, M., & Ansarinasab, H. (2015) · Energy Conversion and Management · doi:10.1016/j.enconman.2015.07.026 · Cited by 70
Self-citationThermal design of multi-stream heat exchangers
Picón‐Núñez, M., Polley, G. T., & Medina-Flores, M. (2002) · Applied Thermal Engineering · doi:10.1016/s1359-4311(02)00074-1 · Cited by 66
Yahya, S. (2010) · Cited by 65
Valenti, G., Macchi, E., & Brioschi, S. (2012) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2012.04.050 · Cited by 53
Concept of Building Medium-Capacity Hydrogen Liquefiers with Helium Refrigeration Cycle
Kuz'menko, I. F., Morkovkin, I. M., & Gurov, E. I. (2004) · Chemical and Petroleum Engineering · doi:10.1023/b:cape.0000024144.92081.aa · Cited by 50
Fernandes, A., Woudstra, T., & Aravind, P. V. (2015) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2015.01.136 · Cited by 46
Thermodynamic analysis of a new renewable energy based hybrid system for hydrogen liquefaction
Ratlamwala, T. A. H., Dincer, I., Gadalla, M. A., & Kanoglu, M. (2012) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2012.09.036 · Cited by 43
Development of a small-scale hydrogen liquefaction system
Garceau, N., Baik, J. H., Lim, C. M., Kim, S. C., Oh, I., & Karng, S. W. (2015) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2015.06.135 · Cited by 41
Exergy and exergoeconomic evaluation of gas separation process
Ghorbani, B., Salehi, G., Amidpour, M., & Hamedi, M. H. (2012) · Journal of Natural Gas Science and Engineering · doi:10.1016/j.jngse.2012.05.001 · Cited by 41
Krasae-in, S., Bredesen, A. M., Stang, J., & Nekså, P. (2010) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2010.09.005 · Cited by 38
Compressor Handbook: Principles and Practice
Giampaolo, A. (2010) · Cited by 35
Small-scale hydrogen liquefaction with a two-stage Gifford–McMahon cycle refrigerator
Nakano, A., Maeda, T., Ito, H., Masuda, M., Kawakami, Y., Kato, A., Tange, M., Takahashi, T., & Matsuo, M. (2010) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2010.05.104 · Cited by 33
STUDY OF LARGE HYDROGEN LIQUEFACTION PROCESS
Matsuda, H., & Nagami, M. (1997) · Cited by 31
(2005) · Elsevier eBooks · doi:10.1016/b978-0-7506-6273-4.x5000-4 · Cited by 22
Shahram, T., Abbasabadi, A. B., Ghasemi, N., Javadian, H., Mashhadi, S., Fattahi, M., Arian, Y. R., & Maddah, H. (2014) · Journal of Natural Gas Science and Engineering · doi:10.1016/j.jngse.2014.11.019 · Cited by 21
Nelium, a Refrigerant with High Potential for the Temperature Range between 27 and 70 K
Quack, H. H., Haberstroh, C., Seemann, I., & Klaus, M. (2015) · Physics Procedia · doi:10.1016/j.phpro.2015.06.031 · Cited by 20
Price, S. J. W., & Sapiano, H. J. (1979) · Canadian Journal of Chemistry · doi:10.1139/v79-111 · Cited by 12
Low-Capacity Hydrogen Liquefier with a Helium Cycle
Belyakov, V. V., Krakovskii, B. D., Popov, O. M., Step, G. K., & Udut, V. N. (2002) · Chemical and Petroleum Engineering · doi:10.1023/a:1019692103797 · Cited by 11
Fernandes, A., Woudstra, T., & Aravind, P. V. (2015) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2015.11.043 · Cited by 4
Research works printed but not linked: 1
- Mehdi Mehrpooya, 2015, Optimum design and exergy analysis of a novel cryogenic air separation process with LNG (liquefied natural gas) cold energy utilization, Energy, 90, 2047, 10.1016/j.energy.2015.07.101 · DOI
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Wijayanta, A. T., Oda, T., Purnomo, C. W., Kashiwagi, T., & Aziz, M. (2019) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2019.04.112 · Cited by 595
Hydrogen liquefaction and storage: Recent progress and perspectives
Zhang, T., Uratani, J. M., Huang, Y., Xu, L., Griffiths, S., & Ding, Y. (2023) · Renewable and Sustainable Energy Reviews · doi:10.1016/j.rser.2023.113204 · Cited by 590
(2018) · doi:10.1016/j.apenergy.2017.12.033 · Cited by 429
Self-citationBosu, S., & Rajamohan, N. (2023) · International Journal of Hydrogen Energy · doi:10.1016/j.ijhydene.2023.01.344 · Cited by 267
Metadata
- Authors
- Sadaghiani, M. S., & Mehrpooya, M.
- Affiliations
- University of Tehran (IR)
- Corresponding author
- Mehrpooya, Mehdi
- ORCID
- Mehrpooya, Mehdi
- Venue
- International Journal of Hydrogen Energy
- Publisher
- Elsevier BV
- Published
- 2017-03
- Volume
- 42
- Issue
- 9
- Pages
- 6033-6050
- ISSN
- 0360-3199 (ISSN-L)
- OpenAlex
- W2587279559
- Cited by
- 266
- References
- 59
- Citations by year
- 2026: 33 · 2025: 39 · 2024: 42 · 2023: 41 · 2022: 33 · 2021: 28 · 2020: 16 · 2019: 16 · 2018: 10 · 2017: 8
- FWCI
- 10.63
- Type
- journal article
- Language
- en
- Open access
- closed
- Locations
- International Journal of Hydrogen Energy (publishedVersion)
- Topics
- Physical Sciences › Engineering › Mechanical Engineering › Thermodynamic and Exergetic Analyses of Power and Cooling Systems
- Physical Sciences › Engineering › Aerospace Engineering › Spacecraft and Cryogenic Technologies
- Physical Sciences › Engineering › Mechanical Engineering › Refrigeration and Air Conditioning Technologies
- Keywords
- hydrogen liquefaction, cryogenic liquefaction, refrigerant mixtures, two-stage refrigeration cycle, energy analysis, exergy analysis, coefficient of performance, exergy efficiency, heat exchanger design, expander design, power consumption
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