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Temperature–Pressure Swing Process for Reactive Carbon Capture and Conversion to Methanol: Techno-Economic Analysis and Life Cycle Assessment
Environmental Science & Technology ( IF 10.8 ) Pub Date : 2024-07-24 , DOI: 10.1021/acs.est.4c02589
Jonathan A Martin 1 , Eric C D Tan 1 , Daniel A Ruddy 1 , Jennifer King 1 , Anh T To 1
Affiliation  

A model was developed to conduct techno-economic analysis (TEA) and life cycle assessment (LCA) for reactive carbon capture (RCC) and conversion of carbon dioxide (CO2) to methanol. This RCC process is compared to a baseline commercialized flue gas CO2 hydrogenation process. An ASPEN model was combined with existing TEA and LCA models into a larger TEA/LCA framework in Python. From preliminary experimental data, the model found a levelized cost of $0.79/kg methanol for the baseline process and $0.99/kg for the RCC process. The cradle-to-gate carbon intensity of the baseline process was 0.50 kg-CO2e/kg-methanol, compared to 0.55 kg-CO2e/kg-methanol for the RCC process. However, water consumption for RCC (10.21 kg-H2O/kg-methanol) is greatly reduced compared to the baseline (12.89 kg-H2O/kg-methanol). Future improvements in hydrogen electrolysis costs will benefit the RCC. A target H2/methanol mass ratio of 0.26 was developed for RCC laboratory experiments to reduce methanol cost below the baseline. If a ratio of 0.24 can be achieved, a levelized cost of $0.76/kg methanol is projected, with a carbon intensity of 0.42 kg-CO2e/kg-methanol.

中文翻译:


活性碳捕获和甲醇转化的温度-压力摆动过程:技术经济分析和生命周期评估



开发了一个模型来对反应性碳捕获(RCC)和二氧化碳(CO 2 )转化为甲醇进行技术经济分析(TEA)和生命周期评估(LCA)。该 RCC 工艺与基准商业化烟道气 CO 2加氢工艺进行了比较。 ASPEN 模型与现有的 TEA 和 LCA 模型组合成 Python 中更大的 TEA/LCA 框架。根据初步实验数据,该模型发现基准工艺的甲醇平均成本为 0.79 美元/千克,RCC 工艺的平均成本为 0.99 美元/千克。基线工艺的从摇篮到大门的碳强度为 0.50 kg-CO 2 e/kg-甲醇,而 RCC 工艺的碳强度为 0.55 kg-CO 2 e/kg-甲醇。然而,与基线(12.89 kg-H 2 O/kg-甲醇)相比,RCC的水消耗量(10.21 kg-H 2 O/kg-甲醇)大大减少。未来氢电解成本的改善将使 RCC 受益。为 RCC 实验室实验制定了 0.26 的目标 H 2 /甲醇质量比,以将甲醇成本降低到基线以下。如果能够达到 0.24 的比率,预计平均成本为 0.76 美元/kg 甲醇,碳强度为 0.42 kg-CO 2 e/kg-甲醇。
更新日期:2024-07-24
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