Analyzing the Hydrogen Supply Cost of Various Scenarios for A Blue Hydrogen Supply Chain Between Korea and Australia

Jiwon Cho, Namhwa Kim, Hyundon Shin
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Abstract

Two scenarios were assumed to analyze the unit price of hydrogen implementation and build a blue hydrogen supply chain between Australia and Korea. Scenario 1 was the case of the unit price for transporting blue hydrogen produced at steam methane reforming (SMR) facilities in Australia to South Korea by three methods. Scenario 2 was the case of the unit price of hydrogen produced through domestic SMR facilities with CO 2 sequestration in Korea and Australia, respectively. Considering the various implementations and the unit price depending on the technology level and process efficiency, Monte Carlo simulation was used to calculate the implementation unit prices statistically. For scenario 1, the results were $12.4/kgH 2 (liquid hydrogen), $6.3/kgH 2 (ammonia), and $13.8/kgH 2 (liquid organic hydrogen carrier, LOHC). For scenario 2, they were $21.5/kgH 2 (Australia) and $13.7/kgH 2 (Korea), depending on CCS site location. This analysis showed that the implementation of blue hydrogen as ammonia in Australia is the most feasible option.
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分析韩国和澳大利亚之间蓝色氢气供应链各种方案的氢气供应成本
为分析氢气实施的单价并在澳大利亚和韩国之间建立蓝色氢气供应链,假设了两种情况。情景 1 是通过三种方法将澳大利亚蒸汽甲烷重整(SMR)设施生产的蓝色氢气运输到韩国的单价。情景 2 是分别在韩国和澳大利亚通过带有二氧化碳封存的国内 SMR 设施生产的氢的单价。考虑到不同的实施方式以及取决于技术水平和工艺效率的单价,采用蒙特卡罗模拟法对实施单价进行了统计计算。方案 1 的结果为 12.4 美元/千克氢 2(液氢)、6.3 美元/千克氢 2(氨)和 13.8 美元/千克氢 2(液态有机载氢体,LOHC)。对于情景 2,根据二氧化碳捕集与封存地点的不同,分别为 21.5 美元/千克氢 2(澳大利亚)和 13.7 美元/千克氢 2(韩国)。该分析表明,在澳大利亚采用蓝氢作为氨是最可行的方案。
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