Efficiency Study of a Natural Gas Liquefier Using Precooling Driven by Organic Rankine Cycle

Cover Page


Cite item

Full Text

Open Access Open Access
Restricted Access Access granted
Restricted Access Subscription or Fee Access

Abstract

Technical and energy analyses of small-scale liquefied natural gas (LNG) plants using a precooling cycle based on the organic Rankine cycle (ORC) were conducted. The first step of the research included modeling and optimization of the natural gas mixed-refrigerant (MR) liquefaction cycle with propane vapor-compression cycle (VCR) precooling. Calculations were used to determine the value of heat and energy flows under various environmental conditions. The second step of the research included a simulation of ORC cycles using values of high-potential heat obtained earlier. The minimum possible cooling temperature was determined as the intersection point between the required cooling capacity and the possible cooling capacity of the ORC–VCR system. Performance data of ORC–VCR-type refrigerators using natural refrigerants were obtained and analyzed, and optimal operational modes were determined. The applicability of the ORC–VCR type refrigerators was considered using obtained data. The potential cost–benefit of the ORC–VCR systems was compared with those of traditional propane VCR systems.

AIMS: Feasibility study of ORC–VCR systems for the preliminary cooling of an autonomous small-scale plant for natural gas liquefaction plants.

MATERIALS AND METHODS: Natural gas liquefaction cycles and ORC–VCR cycles were simulated using the Aspen HYSYS software. Further optimization and parameter selection were performed using the MATLAB module Global Optimization Toolbox.

RESULTS: The cost–benefit value of the ORC–VCR precooling systems compared with the classic propane VCR refrigerators was found to be up to 15%, depending on the type of the Rankine cycle used and the type of working substance.

CONCLUSIONS: The authors analyzed the feasibility of ORC–VCR systems for the preliminary cooling of autonomous small-scale LNG plants. The application of ORC–VCR refrigerators using high-potential heat of exhaust gases from a diesel generator or an electric generator reduced the consumption of natural gas and specific costs of LNG production. The cost–benefit value compared with those of classic propane VCR refrigerators was up to 15%, depending on the type of the Rankine cycle used and the type of working substance.

Full Text

Restricted Access

About the authors

Sofia V. Maslikova

Bauman Moscow State Technical University

Email: maslikova@bmstu.ru
ORCID iD: 0009-0002-9326-6491
SPIN-code: 3513-1800

graduate student

Russian Federation, Moscow

Alexander S. Krotov

Bauman Moscow State Technical University

Email: krotov@bmstu.ru
ORCID iD: 0000-0001-9671-8890
SPIN-code: 4165-8154

assistant professor, Ph.D. of Engineering Sciences

Russian Federation, Moscow

Georgii M. Kosenko

Bauman Moscow State Technical University

Email: kosenko@bmstu.ru
ORCID iD: 0009-0006-4885-6678
SPIN-code: 2674-8335

graduate student

Russian Federation, Moscow

Pavel R. Sitnikov

Bauman Moscow State Technical University

Author for correspondence.
Email: spr18ea332@student.bmstu.ru
ORCID iD: 0009-0000-0960-4108

student

Russian Federation, Moscow

Vsevolod O. Novikov

Bauman Moscow State Technical University

Email: novikovvo@student.bmstu.ru
ORCID iD: 0009-0007-9710-8008

student

Russian Federation, Moscow

References

  1. Yin QS, Li HY, Fan QH, Jia LX. Economic Analysis of Mixed refrigerant Cycle and Nitrogen Expander Cycle in Small Scale Natural Gas Liquefier. AIP Conference Proceedings. 2008;985:1159.
  2. Pearson SF. Uses of Hydrocarbon Refrigerants. In: Proceedings of the IIR Conference on Applications for Natural Refrigerants. Aarhus: IIF/IIR; 1996:439–446. doi: 10.1063/1.2908467
  3. Voronov VA, Leonov VP, Apsit KA. Use of heat-utilizing vehicle refrigerating machine using diesel engine waste heat. Chemical and petroleum engineering. 2022;57:997–1007. doi: 10.1007/s10556-022-01037-9
  4. Zhao J, Ma X, Grekhov L, Denisov A. Specific features of diesel fuel supply under ultra-high pressure. Applied Thermal Engineering. 2020;179:115699. doi: 10.1016/j.applthermaleng.2020.115699
  5. Antanenkova IS, Koroleva AP, Frantsuzov MS, et al. Designing the Main Heat-Transfer Equipment of an ORC-System for the Internal Combustion Engines of Shipboard Installations. Thermal Engineering. 2021;68(1):25–36. doi: 10.1134/S0040601520120010
  6. Kostenko AA, Leonov VP, Rosenoer TM, et al. Using the Direct and Reverse Rankine Cycles to Create a Water-Cooling Chiller Running on Waste Heat. Chemical and Petroleum Engineering. 2016;51:778–782. doi: 10.1007/s10556-016-0121-9
  7. Aphornratana S, Sriveerakul T. Analysis of a combined Rankine–vapour–compression refrigeration cycle. Energy Conversion and Management. 2010;51:2557–2564. doi: 10.33422/5ist.2018.12.111
  8. Rawat KS, Khulve H, Pratihar AK. Thermodynamic Analysis of Combined ORC-VCR System Using Low Grade Thermal Energy. International Journal for Research in Applied Science & Engineering Technology (IJRASET). 2015;3:515–522. Accessed: 22.05.2024. Available from: https://www.ijraset.com/fileserve.php?FID=3025
  9. Bao J. Organic Rankine Cycle for Recovery of Liquefied Natural Gas (LNG) Cold Energy. In: Organic Rankine Cycle Technology for Heat Recovery. Enhua Wang: IntechOpen; 2018. doi: 10.5772/intechopen.77990
  10. Astolfi M, Fantolini AM, Valenti G, et al. Cryogenic ORC to Enhance the Efficiency of LNG Regasification Terminals. Energy Procedia. 2017;129:42–49. doi: 10.1016/j.egypro.2017.09.177
  11. Krotov A, Kolesnikov A, Samokhvalov Y, et al. Research of mixed refrigerant cycle for liquefaction of natural gas depending on ambient conditions and its regulation. In: Proceedings of the 25th IIR International Congress of Refrigeration, August 24-30, 2019, Montreal, Canada. Montreal; 2019:401–407. doi: 10.18462/iir.icr.2019.0980
  12. Narasimhan NL, Venkatarathnam G. A method for estimating the composition of the mixture to be charged to get the desired composition in circulation in a single stage JT refrigerator operating with mixtures. Cryogenics. 2010;50(2):93–101. doi: 10.1016/J.CRYOGENICS.2009.12.004
  13. Bychkov EG, Makarov BA, Yakovlev VI, et al. Comparative Analysis of Equations of State for Calculating the Thermodynamic Properties of a Vapour-Liquid Multicomponent Refrigerant Blend Comprising the Working Fluid of a Low-Temperature Throttling Refrigeration Unit. Chemical and Petroleum Engineering. 2020;56(5–6):393–402. doi: 10.1007/s10556-020-00786-9
  14. Zuev OA, Garanov SA, Ivanova EV, Karpukhin AS. Investigation of the efficiency of autocascade and cascade heat pumps in cold climate. Chemical and petroleum engineering. 2020;56:448–455. doi: 10.1007/s10556-020-00793-w
  15. Krotov A, Samokhvalov Y, Verkhovny A, Vasilyev A. Closed cycle cryosurgical device with phase separator and mixed refrigerant. Refrigeration Science and Technology. 2019;F147717:287–292. doi: 10.18462/iir.cryo.2019.0067

Supplementary files

Supplementary Files
Action
1. JATS XML
2. Fig. 1. Simplified diagram of a small-scale natural gas liquefaction plant.

Download (48KB)
3. Fig. 2. Simplified diagram of the suggested small-scale natural gas liquefaction plant.

Download (56KB)
4. Fig. 3. Intersection point of the required cooling capacity curve and possible cooling capacity curve for the ORC–VCR system for summer conditions.

Download (71KB)
5. Fig. 4. Schemes of the VCR system (left) and ORC–VCR (right).

Download (61KB)
6. Fig. 5. Power consumption of the different precooling cycles.

Download (88KB)
7. Fig. 6. Annual gas consumption for electricity generation for different precooling cycles.

Download (61KB)

Copyright (c) 2023 Eco-Vector

Creative Commons License
This work is licensed under a Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International License.

This website uses cookies

You consent to our cookies if you continue to use our website.

About Cookies