2016
DOI: 10.1021/acs.iecr.5b04249
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Investigation and Performance Improvement of the Propane Precooling Cycle in the Propane Precooled Mixed Refrigerant Cycle Liquefaction Process

Abstract: This study aims to improve the performance of the propane precooling cycle used for precooling of both natural gas and mixed refrigerant in the Propane Precooled Mixed Refrigerant Cycle (PPMRC) in an LNG plant. The unit is simulated by Aspen HYSYS version 7.3 for optimization of the propane precooling cycle to provide the minimum energy consumption of the propane compressors and the two air-coolers. The effect of subcooling temperature in the propane air-cooler, the number of compression stages in the propane … Show more

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Cited by 16 publications
(5 citation statements)
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“…Because the C3/MRC combines the advantages of MRC and cascade refrigeration cycle, it is currently the most dynamic liquefaction process in the world. Both the APCI and Shell of the United States have their own patents in this process [27,28].…”
Section: Propane Mixed-refrigerant Cycle (C3/mrc)mentioning
confidence: 99%
“…Because the C3/MRC combines the advantages of MRC and cascade refrigeration cycle, it is currently the most dynamic liquefaction process in the world. Both the APCI and Shell of the United States have their own patents in this process [27,28].…”
Section: Propane Mixed-refrigerant Cycle (C3/mrc)mentioning
confidence: 99%
“…SMR CYCLE CONFIGURATIONS This section considers the liquefaction of a natural gas stream for the production of LNG at a small scale (1 MTPA). The natural gas stream is adapted from the work of Fahmy et al, 32 and the details are given in Table S1 in the Supporting Information.…”
Section: Case Study I: Thorough Optimization Of Thementioning
confidence: 99%
“…In this case study, the natural gas stream data are presented in Table , based on the work of Fahmy et al and LNG production is assumed to be 1 MTPA. The three SMR configurations are to be optimized to minimize the shaft work required to cool and liquefy the natural gas stream from 25 °C (298.15 K) to its target temperature of −161.0 °C (112.15 K).…”
Section: Case Study: Problem Definition and Optimization Strategymentioning
confidence: 99%
“…In this case study, the natural gas stream data are presented in Table 8, based on the work of Fahmy et al 45 and LNG production is assumed to be 1 MTPA. The three SMR Cooling and liquefaction of the natural gas stream is assumed at a constant pressure of 63 bar.…”
Section: Case Study: Problem Definition Andmentioning
confidence: 99%