Thermoeconomic analysis of novel hydrogen liquefaction assisted by absorption refrigeration utilizing heat from Brayton cycle

L. Rahadiyan, M. Aziz, N. Nasruddin
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Abstract

Current research presents a novel method for reducing the energy consumption of hydrogen liquefaction through heat recovery of hydrogen liquefier. An ammonia absorption refrigeration cycle on the hydrogen precooling utilizes the heat generated by the compressor intercooler and aftercooler of the reverse Brayton cycle of hydrogen liquefier to precool hydrogen feedstock. The system is analyzed from exergy, energy, and economic perspective. The results are compared with the reference case without a heat recovery system. The proposed system can reduce SEC (specific energy consumption) from 7.37 kWh/kgLH2 to 6.23 kWh/kgLH2 and exergy efficiency improvement from 55.2% to 60.90%. The economic analysis shows that the levelized cost of energy to produce 5.07 tons/day of liquid hydrogen for the reference and novel case is 5.88 USD/kgLH2 and 5.03 USD/kgLH2, respectively. The results imply that the proposed method can be a reference for designing an integrated hydrogen liquefaction system to minimize energy consumption.
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利用布雷顿循环热量的吸收式制冷辅助新型氢液化的热经济分析
目前的研究提出了一种通过氢液化器热回收降低氢液化能耗的新方法。氢气预冷氨吸收式制冷循环利用氢气液化器反向布雷顿循环压缩机中间冷却器和后冷却器产生的热量来预冷氢气原料。从放热、能量和经济角度对该系统进行了分析。结果与没有热回收系统的参考案例进行了比较。建议的系统可将 SEC(比能耗)从 7.37 kWh/kgLH2 降至 6.23 kWh/kgLH2,将放能效率从 55.2% 提高到 60.90%。经济分析表明,在参考案例和新型案例中,生产 5.07 吨/天液氢的平准化能源成本分别为 5.88 美元/千克液氢2 和 5.03 美元/千克液氢2。结果表明,所提出的方法可作为设计综合氢液化系统的参考,以最大限度地降低能耗。
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