4.7 Article

An innovative high energy efficiency-based process enhancement of hydrogen liquefaction: Energy, exergy, and economic perspectives

期刊

FUEL
卷 320, 期 -, 页码 -

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2022.123964

关键词

Hydrogen liquefaction; HFO based mixed refrigerants; Process enhancement; Specific energy consumption; Exergy efficiency

资金

  1. UNIST (Ulsan National Institute of Science and Technology) [1.220038.01]

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Hydrogen liquefaction is an effective and viable solution to increase energy contents for storage and transportation. This study proposes a precooling cycle that reduces energy consumption by using unique HFO-based mixed refrigerants to lower the temperature of gaseous H-2. The results show a significant reduction in specific energy consumption and an increase in exergy efficiency compared to the base cases. The economic evaluation also demonstrates the feasibility of the proposed process.
Hydrogen liquefaction can be one of the effective and viable solutions to enhance its energy contents for storage and transportation purposes. However, liquefaction of H-2 is highly energy intensive where precooling is the most significant energy consumption section (similar to 50% of overall process) due to huge reduction in temperature (25 to-159.4 degrees C). In this context, in proposed study the precooling cycle is split into two cycles for reducing the energy consumption, 1) Hydrofluoroolefin-based mixed refrigerant stream which reduces the H-2 temperature to -30 degrees C and 2) Mixed refrigerant stream which tends to reduce the H-2 temperature up to-159.4 degrees C. This is the first study which utilizes the four refrigeration cycles with unique selection of HFO-based mixed refrigerants in precooling section to reduce the gaseous H-2 temperature. Results of proposed study reveal that the specific energy consumption of proposed process was reduced by 55.2 % and 29.5%, as compared to base case-I (10.15 kWh/kgLH(2)) and base case-II (6.45 kWh/kgLH(2)), respectively. The exergy efficiency of the proposed process was increased by 67%. In addition, results of economic evaluation depicted that the total annualized cost of proposed process was obtained as $1.89 x 10(6)/y where the CAPEX has share of similar to 71.7% in total cost of project. The estimated unit production cost was recorded as $5.18/kg of LH2 at the capacity of 1TPD. The simplicity and less energy consumption of proposed model built a basis for its development to commercial scale adoption.

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