원문정보
초록
영어
The purpose of this analytic study is to design and examine an efficient hydrogen liquefaction cycle by using a pre-cooler. The liquefaction cycle is primarily comprised of a pre-cooler and a refrigerator. The fed hydrogen gas is cooled down from ambient temperature (300 K) to the pre-cooling coolant temperature (either 77 K or 120 K approximately) through the pre-cooler. There are two pre-cooling methods: a single pre-coolant pre-cooler and a cascade pre-cooler which uses two levels of pre-coolants. After heat exchanging with the pre-cooler, the hydrogen gas is further cooled and finally liquefied through the refrigerator. The working fluids of the potential pre-cooling cycle are selected as liquid nitrogen and liquefied natural gas. A commercial software Aspen HYSYS is utilized to perform the numerical simulation of the proposed liquefaction cycle. Efficiency is compared with respect to the various conditions of the heat exchanging part of the pre-cooler. The analysis results show that the cascade method is more efficient, and the heat exchanging part of the pre-coolers should have specific UA ratios to maximize both spatial and energy efficiencies. This paper presents the quantitative performance of the pre-cooler in the hydrogen liquefaction cycle in detail, which shall be useful for designing an energy-efficient liquefaction system.
목차
1. INTRODUCTION
2. ANALYTICAL METHOD
2.1. Efficiency Enhancement by Reutilizing Cold Exergy of Boil-off Pre-coolant
2.2. Efficiency Enhancement by Pre-cooling Method
3. RESULTS AND DISCUSSION
3.1. Results of Efficiency Enhancement by Reutilizing the Cold Exergy of Boil-off Pre-coolant
3.2. Results of Efficiency Enhancement by the Pre-cooling Method
4. CONCLUSIONS
ACKNOWLEDGMENT
REFERENCES