doi: 10.3850/978-981-08-7614-2_IMPRES037


Performance of Natural Gas Liquefaction Cycle using C3H8, N2O and N2


Won Jae Choi1, Seung Taek Oh1, Chang Hyo Son1, Jung In Yoon1,a, Ho Saeng Lee2, Sang Gyu Lee3 and Keun Hyung Choi3

1Dept. of Refrigeration & Air-conditioning Engineering, Pukyong National University, Busan 608-739, Korea.

ayoonji@pknu.ac.kr

2KORDI, Jungwang-myeon, Goseong-gun, Gangwon-do, 219-822, Korea

3KOGAS, Dongchun-Dong, Yeonsu-Gu, Incheon, 406-130, Korea

ABSTRACT

This paper presents a new natural gas liquefaction cycle which utilizes propane (C3H8), nitrogen monoxide (N2O), and nitrogen gas (N2) cycles. A liquefaction cycle with staged compression was designed and simulated using HYSYS software for improving cycle efficiency. This included a cascade cycle with a three-stage compression consisting of a C3H8, a N2O and a N2 cycle. These cycles were compared with an optimized staged compression process. The Compressor work, specific energy, and COP (Coefficient of Performance) of the cascade cycles were compared and analyzed. The new C3H8, N2O and N2 liquefaction cycle is also compared to other natural gas liquefaction cycles including the Phillips optimized cascade cycle and a multi-staged cascade cycle using a Propane, Ethylene and Methane. The COP (Coefficient of Performance) of the new cascade cycle which utilizes a three-stage compression process is 25% higher than that of basic single-stage cycle. Also, the new liquefaction cycle requires less power for the same liquefied natural gas (LNG) quantity produced by other methods. For example, up to 14.3% less power is consumed using the new method as opposed to the Phillips optimized cascade cycle under the same conditions of feed gas composition and liquefaction rate.

Keywords: Liquefaction, Cryogenic, LNG, Cascade, Refrigerating cycle.



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