首页|超临界CO2管输首站增压方式优选

超临界CO2管输首站增压方式优选

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超临界CO2 管输增压方式的优选对CO2 捕集、利用与封存技术的经济性评价具有重要影响.以将常温、常压下输量为 500 万t/a 的CO2 在首站增压至 14 MPa 为例,应用Aspen HYSYS软件建立了2 种n+1多级增压工艺流程进行过程模拟,对比了不同增压方式以及不同增压级数下的总费用现值.结果表明,取首站运行时间为30 a,基准折现率为8%,在n取值4、5、6的增压级数下,压缩机+泵组合增压工艺流程相较于压缩机多级增压工艺流程能分别降低新建首站总费用现值5.51%、5.85%和6.03%.研究结果可为超临界CO2 管输首站增压方式选择提供参考.
Comparison and Selection of Pressurization Process of Supercritical CO2 Pipeline Transportation in First Station
The comparison and selection of process flow for supercritical CO2 pipeline transportation has a significant impact on the economy evaluation of CO2 capture,utilization and storage technology.As an illustration,two types of n+1 multistage pressurization process flows were established.The pressurization process from normal temperature and pressure to 14 MPa of CO2 with a capacity of 5×106 t/a was simulated.The present value of the total cost of the first station under different pressurization processes and different numbers of pressurization stages was compared.The results indicate that under conditions of an operation time of 30 years,a base discount rate of 8%,and pressurization stages of 4,5,and 6,the present value of the total cost of the new supercritical CO2 pipeline first station can be reduced by 5.51%,5.85%,and 6.03%respectively,by the n+1 compressor+pump combination pressurization process as compared with the n+1 compressor multistage pressurization process.The findings of the research may provide a reference point for the pressurization method of the first station on a supercritical CO2 pipeline.

CO2transportationsupercriticalpressurizationprocess flowcomparison and selection

马启钊、张瑛、李淼、李林、于徽、陈廷鑫、史瑶、马宇航

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中国石油天然气股份有限公司 新疆油田工程技术研究院(监理公司),新疆 克拉玛依 830060

中国石油天然气股份有限公司 新疆油田玛湖勘探开发项目部,新疆 克拉玛依 830060

新疆大学 化工学院,新疆 乌鲁木齐 830000

CO2 输送 超临界 增压 工艺流程 优选

2024

石油化工设备
兰州石油机械研究所,中国石油和石油化工设备工业协会

石油化工设备

影响因子:0.465
ISSN:1000-7466
年,卷(期):2024.53(5)