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

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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.

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作者简介

Sofia Maslikova

Bauman Moscow State Technical University

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

graduate student

俄罗斯联邦, Moscow

Alexander Krotov

Bauman Moscow State Technical University

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

assistant professor, Ph.D. of Engineering Sciences

俄罗斯联邦, Moscow

Georgii Kosenko

Bauman Moscow State Technical University

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

graduate student

俄罗斯联邦, Moscow

Pavel Sitnikov

Bauman Moscow State Technical University

编辑信件的主要联系方式.
Email: spr18ea332@student.bmstu.ru
ORCID iD: 0009-0000-0960-4108

student

俄罗斯联邦, Moscow

Vsevolod Novikov

Bauman Moscow State Technical University

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

student

俄罗斯联邦, Moscow

参考

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2. Fig. 1. Simplified diagram of a small-scale natural gas liquefaction plant.

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3. Fig. 2. Simplified diagram of the suggested small-scale natural gas liquefaction plant.

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

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

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6. Fig. 5. Power consumption of the different precooling cycles.

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7. Fig. 6. Annual gas consumption for electricity generation for different precooling cycles.

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