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Process Simulation and Cost Evaluation of Carbon Membranes for CO2 Removal from High-Pressure Natural Gas

机译:高压天然气脱碳碳膜的工艺模拟与成本估算

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摘要

Natural gas sweetening is required to remove the acid gas CO2 to meet gas grid specifications. Membrane technology has a great potential in this application compared to the state-of-the-art amine absorption technology. Carbon membranes are of particular interest due to their high CO2/CH4 selectivity of over 100. In order to document the advantages of carbon membranes for natural gas (NG) sweetening, HYSYS simulation and cost evaluation were conducted in this work. A two-stage carbon membrane process with recycling in the second stage was found to be technically feasible to achieve >98% CH4 with <2% CH4 loss. The specific natural gas processing cost of 1.122 × 10−2 $/m3 sweet NG was estimated at a feed pressure of 90 bar, which was significantly dependent on the capital-related cost. Future work on improving carbon membrane performance is required to increase the competitiveness of carbon membranes for natural gas sweetening.
机译:需要天然气脱硫以除去酸性气体CO2以满足气网规格。与最先进的胺吸收技术相比,膜技术在该应用中具有巨大潜力。碳膜因其对CO2 / CH4的高选择性超过100而特别受关注。为了证明碳膜在天然气(NG)脱硫中的优势,在这项工作中进行了HYSYS模拟和成本评估。发现在第二阶段进行再循环的两阶段碳膜工艺在技术上是可行的,以实现> 98%的CH4和<2%的CH4损失。在90巴的进料压力下,估算天然气的单位天然气加工成本为1.122×10 −2 $ / m 3 甜NG,这在很大程度上取决于资本-相关费用。需要提高碳膜性能的未来工作,以提高碳膜在天然气脱硫中的竞争力。

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