Comparison of low temperature mixed refrigerant cycles for separation systems
Open accessAbstract
Numerous mixed refrigerant cycles (MRCs) were developed in the past several decades in different applications. In this paper, two sets of low temperature MRCs are developed and simulated for a typical olefin plant utilizing a mixture of methane, ethane, propane and nitrogen as cycle working fluid to replace the pure ethylene refrigeration cycle that is used in conjunction with propylene refrigeration cycle in conventional plants. The key parameters of the cycles including mixture compositions and operating pressure levels are optimized to meet the objective of minimum shaftwork in compressor. The results show that different cycle configuration has different optimal mixture composition and low and high operating pressures. The results of exergy analysis reveal that the main location of the exergy loss in the cycles is the heat exchanger system. Also, the Carnot factor versus heat flow diagram is provided to identify the distribution of inefficiencies in the heat exchangers for each cycle. The simulation results show that MRCs can improve the thermodynamic performance of refrigeration system using the optimal working fluid mixture composition, optimal high and low operating pressures and optimal arrangement of the cycle components. Copyright © 2008 John Wiley & Sons, Ltd.
The claims and statistics of this paper haven’t been checked yet.
Run the check — free, no account needed. It reads the open-access text and checks the sources it cites.
Integrity signals
Registry
Cites
Statistics
Claims the paper makes
The claims and statistics of this paper haven’t been checked yet.
Run the check — free, no account needed. It reads the open-access text and checks the sources it cites.
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?
The essential instruments in the targeting phase of CPEA are exergy composite diagrams (ECCs) and exergy grand composite diagrams (EGCCs), which are obtained by replacing the temperature axis in the CCs and GCCs with the Carnot factor.
“The essential instruments in the targeting phase of CPEA are exergy composite diagrams (ECCs) and exergy grand composite diagrams (EGCCs), which are obtained by replacing the temperature axis in the CCs and GCCs with the Carnot factor .283,307−310”
From Strategies To Improve the Performance of Hydrogen Storage Systems by Liquefaction Methods: A Comprehensive Review (2023) · cites this paper as [283]
Section 5 (page not available in our copy) says that replacing temperature with the Carnot factor in composite curves produces exergy composite curves (ECCs), which the authors use in an exergy-loss targeting analysis. The paper discusses grand composite curves separately in Section 2, but the passages do not describe exergy grand composite curves (EGCCs) or identify ECCs and EGCCs together as essential instruments in CPEA targeting. (LLM, conf=0.87)
Experimental — accuracy not yet measured
Self-check
Percentages, sums and reported differences re-computed from the paper’s own numbers.
The self-check needs the paper’s full text.
Cites
Gong, M. Q., Wu, J. F., & Luo, E. G. (2004) · Cryogenics · doi:10.1016/j.cryogenics.2004.05.004 · Cited by 83 · see citing works
Exergy analysis of multistage cascade low temperature refrigeration systems used in olefin plants
Mafi, M., Naeynian, S. M. M., & Amidpour, M. (2009) · International Journal of Refrigeration · doi:10.1016/j.ijrefrig.2008.05.008 · Cited by 73 · see citing works
Self-citation
Flagged first, then by citations
Research works printed but not linked: 19
- Gong M, Wu J, Luo E, Qi Y, Zhou Y. Study of the single- stage mixed-gases refrigeration cycle for cooling tempera- ture-distributed heat loads. International Journal of Thermal Science 2004; 43:31-41. DOI: 10.1016/S1290- 0729(03)00097-8. · DOI
- Haberschill P, Gay L, Aubouin P, Lallemand M. Perfor- mance prediction of a refrigerating machine using R-407C: the effect of the circulating composition on system performance. International Journal of Energy Research 2002; 26:1295-1311. DOI: 10.1002/er.817. · DOI
- Fleming J, Bwalya C, Dempster W. The testing and evaluation of trial refrigerants: Part 1. System description. International Journal of Energy Research 2000; 24:1217-1241. DOI: 10.1002/1099-114X(200011)24:14 o1217::AID-ER64743.0.CO;2-U. M. MAFI, M. AMIDPOUR AND S. M. M. NAEYNIAN 376 Copyright r 2008 John Wiley & Sons, Ltd. Int. J. Energy Res. 2009; 33:358-377 DOI: 10.1002/er 1099114x, 2009, 4, Downloaded from https://onlinelibrary.wiley.com/doi/10.1002/er.1480 by Mount Vernon Nazarene University, Wiley Online Library on [26/08/2026]. See the Terms and Conditions (https://onlinelibrary.wiley.com/terms-and-conditions) on Wiley Online Library for rules of use; OA articles are governed by the applicable Creative Commons License · DOI
- Fleming J, Bwalya A, Dempster W. The testing and evaluation of trial refrigerants: Part 2. The practical use of measured data. International Journal of Energy Research 2000; 24:1243-1256. DOI: 10.1002/1099-114X(200011)24: 14o1243::AID-ER649>3.0.CO;2-J. · DOI
- Sami S, Zhou Y. Numerical prediction of heat pump dynamic behaviour using ternary non-azeotropic refriger- ant mixtures. International Journal of Energy Research 1995; 19:19-35. DOI: 10.1002/er.4440190105. · DOI
- Sami S, Kita R. Behaviour of new refrigerant mixtures under magnetic field. International Journal of Energy Research 2005; 29:1205-1213. DOI: 10.1002/er.1090. · DOI
- Sami S, Aucoin S. Behaviour of refrigerant mixtures with gas/liquid injection. International Journal of Energy Research 2003; 27:1265-1277. DOI: 10.1002/er.941. · DOI
- Stegou-Sagia A, Paignigiannis N. Exergy losses in refrigerating systems. A study for performance compar- isons in compressor and condenser. International Journal of Energy Research 2003; 27:1067-1078. DOI: 10.1002/ er.936. · DOI
- Alexeev A, Thiel A, Harberstoh Ch, Quack H. Study of behavior in the heat exchanger of a mixed gas Joule-Thom- son cooler. Advances in Cryogenics Engineering 2000;45: 307-315.
- Linnhoff B, Dhole VR. Shaftwork targets for low temperature process design. Chemical Engineering Science 1992; 4(8):2081-2091.
- Lee GC. Optimal design and analysis of refrigeration systems for low-temperature processes. Ph.D. Thesis, UMIST, U.K., 2001.
- Wu GD. Design and retrofit of integrated refrigeration systems. Ph.D. Thesis, UMIST, U.K., 2000.
- Kanoglu M, Dincer I, Rosen M. Performance analysis of gas liquefaction cycles. International Journal of Energy Research 2008; 32:35-43. DOI: 10.1002/er.1333. · DOI
- Mehrpooya M, Jarrahian A, Pishvaie MR. Simulation and exergy-method analysis of an industrial refrigeration cycle used in NGL recovery units. International Journal of Energy Research 2006; 30:1336-1351. DOI: 10.1002/ er.1256. · DOI
- Cao W, Lu X, Lin W, Gu A. Parameter comparison of two small-scale natural gas liquefaction processes in skid-mounted packages. Journal of Applied Thermal Engi- neering 2006; 26:898-904. DOI: 10.1016/j.applthermaleng. 2005.09.014. · DOI
- Remeljej CW, Hoadley AFA. An exergy analysis of small- scale liquefied natural gas (LNG) liquefaction processes. Journal of Energy 2006; 31:1669-1683. DOI: 10.1016/ j.energy.2005.09.005. · DOI
- Kanoglu M. Exergy analysis of multistage cascade refrig- eration cycle used for natural gas liquefaction. International Journal of Energy Research 2002; 26:763-774. DOI: 10.1002/er.814. · DOI
- Smith R. Chemical Process Design and Integration. Wiley: New York, 2004.
- Reid RC, Prausnitz JM, Poling BE. The Properties of Gases and Liquids (4th edn). McGraw-Hill, 1987.
Cited by
Sorted by citations
Ghorbani, B., Zendehboudi, S., Saady, N. M. C., Duan, X., & Albayati, T. M. (2023) · ACS Omega · doi:10.1021/acsomega.3c01072 · Cited by 121 · see citing works
- Authors
- Mafi, M., Amidpour, M., & Mousavi Naeynian, S. M.
- Affiliations
- K. N. Toosi University of Technology (IR)
- Corresponding author
- Amidpour, M.
- ORCID
- Venue
- International Journal of Energy Research
- Publisher
- Hindawi Limited
- Published
- 2009-03-25
- Volume
- 33
- Issue
- 4
- Pages
- 358-377
- ISSN
- 0363-907X (ISSN-L)
- 1099-114X
- OpenAlex
- W1965607045
- Cited by
- 16
- References
- 2
- Citations by year
- 2026: 1 · 2025: 2 · 2024: 1 · 2023: 1 · 2022: 2 · 2021: 3 · 2020: 1 · 2018: 2 · 2017: 1 · 2014: 1
- FWCI
- 0.71
- Type
- journal article
- Language
- en
- Open access
- bronze
- doi.org
- Locations
- International Journal of Energy Research (publishedVersion)
- Topics
- Physical Sciences › Engineering › Mechanical Engineering › Refrigeration and Air Conditioning Technologies
- Physical Sciences › Engineering › Mechanical Engineering › Thermodynamic and Exergetic Analyses of Power and Cooling Systems
- Physical Sciences › Engineering › Control and Systems Engineering › Process Optimization and Integration
- Keywords
- mixed refrigerant cycle, low-temperature refrigeration, olefin separation, exergy analysis, cycle configuration
About these checks
Registry, retraction, Cites and statistics results are computed, not judged, with one exception: a printed reference that no index lists is read once by a model before it counts as a citation error. Claims are extracted by a model and kept only when their quote appears verbatim in the text; each cited source is then checked, with a model’s help, for whether it says what the claim relies on. Those verdicts can be wrong — read the claim’s quote and the cited source before relying on one.
Statistics and arithmetic are recomputed, not judged.
Confidence bands are shown only for fields calibrated on our annotated test set. None is calibrated yet, so no band is shown.
What counts as a claim ›How we measure confidence ›How we check this ›
Are you an author, or do you see a problem with this page? Request a review