首页|不同相态下CO2管道输送技术经济评价分析

不同相态下CO2管道输送技术经济评价分析

Economic evaluation and analysis of CO2 pipeline transportation technologies under different phases

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目的 为助力实现"双碳"目标,明确不同相态下CO2 管道输送的适应性和经济性.方法 以中国石油西南油气田碳酸盐岩气藏CCUS-EGR关键技术研究为背景,优化建立了气相、液相以及超临界相 3种相态的CO2 管道输送经济性估算模型,分析了流速、输送距离以及输送量对相对总成本的影响.结果 ①最低输送成本气相管道最高,液相管道次之,超临界相管道最低;②气相经济流速为 3.0~4.0 m/s,液相经济流速为 1.0~1.8 m/s,超临界相经济流速为 2.0~2.4 m/s;③在不同输送距离下,相对总成本随着输送距离的增加而增大;④在不同输送量下,相对总成本随着输送量的增加而增大,DN200以上规格的管道输送成本随输送量变化增长较慢,DN100的管道输送成本随输送量变化很大.结论 通过建立CO2 管道输送经济性估算模型,分析不同相态下的CO2 管道输送经济性,为CO2 管道输送工程建设提供充分的依据和参考.
Objective To support achieving the"dual carbon"goals by clarifying the adaptability and economic feasibility of CO2 pipeline transportation under different phases.Methods This study is set against research on key CCUS-EGR technologies in the carbonate gas reservoirs of PetroChina Southwest Oil and Gas Field.We optimized and established economic estimation models for CO2 pipeline transportation in three phases:gas phase,liquid phase,and supercritical phase.The impacts of flow rate,transportation distance,and transportation volume on the relative total cost were analyzed.Results The findings indicate that:first,the minimum transportation costs follow the order:gas phase pipeline>liquid phase pipeline>supercritical pipeline;second,the economical flow rate ranges are 3.0-4.0 m/s for gas phase,1.0-1.8 m/s for liquid phase,and 2.0-2.4 m/s for supercritical phase;third,the relative total cost increases with transportation distance at different conveying distances;fourth,the relative total cost also increases with transportation volume at different throughput,where the transportation cost for pipe diameters above DN200 rises slowly with volume,whereas the cost for DN100 diameter pipes varies significantly with volume.Conclusion By establishing an economic estimation model for CO2 pipeline transportation and analyzing its economic feasibility under different phases,this study provides a solid basis and reference for constructing CO2 pipeline transportation projects.

CCUSCO2 pipelinepipeline process calculationphase stateeconomic analysis

杨继忠、戴万能、李茜、刘恩斌、计维安、钟华

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中国石油西南油气田公司集输工程技术研究所

西南石油大学石油与天然气工程学院

CCUS CO2管道 管道工艺计算 相态 经济性分析

中国石油天然气股份有限公司油气与新能源分公司科技项目中国石油天然气股份有限公司西南油气田分公司科研项目

2023YQX10503ZK20230312-01

2024

石油与天然气化工
西南油气田分公司天然气研究院 西南油气田公司重庆天然气净化总厂

石油与天然气化工

北大核心
影响因子:0.805
ISSN:1007-3426
年,卷(期):2024.53(5)