|本期目录/Table of Contents|

[1]苗青,殷布泽,王鑫,等.含杂质超临界CO2输送管道停输再启动瞬态特性研究*[J].中国安全生产科学技术,2024,20(5):43-49.[doi:10.11731/j.issn.1673-193x.2024.05.006]
 MIAO Qing,YIN Buze,WANG Xin,et al.Study on transient characteristics of shutdown and restart of supercritical CO2 pipeline containing impurities[J].JOURNAL OF SAFETY SCIENCE AND TECHNOLOGY,2024,20(5):43-49.[doi:10.11731/j.issn.1673-193x.2024.05.006]
点击复制

含杂质超临界CO2输送管道停输再启动瞬态特性研究*
分享到:

《中国安全生产科学技术》[ISSN:1673-193X/CN:11-5335/TB]

卷:
20
期数:
2024年5期
页码:
43-49
栏目:
学术论著
出版日期:
2024-05-31

文章信息/Info

Title:
Study on transient characteristics of shutdown and restart of supercritical CO2 pipeline containing impurities
文章编号:
1673-193X(2024)-05-0043-07
作者:
苗青殷布泽王鑫聂超飞李玉星李其抚胡其会
(1.国家石油天然气管网集团有限公司科学技术研究总院分公司,河北 廊坊 065000;
2.中国石油大学(华东) 储运与建筑工程学院,山东 青岛 266500;
3.中国石油技术开发有限公司,北京 100020)
Author(s):
MIAO Qing YIN Buze WANG Xin NIE Chaofei LI Yuxing LI Qifu HU Qihui
(1.Science and Technology Research Institute,National Oil and Natural Gas Pipeline Network Group Company Limited,Langfang Hebei 065000,China;
2.College of Pipeline and Civil Engineering,China University of Petroleum (East China),Qingdao Shandong 266500,China;
3.China Petroleum Technology and Development Corporation,Beijing 100020,China)
关键词:
OLGA含杂质CO2停输再启动安全停输时间
Keywords:
OLGA impure CO2' target="_blank" rel="external">">2 shutdown and restart safety shutdown time
分类号:
X937
DOI:
10.11731/j.issn.1673-193x.2024.05.006
文献标志码:
A
摘要:
为研究超临界CO2管道停输后管内温度压力和相态变化规律,以国内某CO2管道为研究对象,利用OLGA软件开展停输再启动瞬态数值模拟,探究不同工况及工质对管道停输再启动过程的影响。研究结果表明:在保证相态不变且下游用户流量不变的情况下,流量越大,最大停输时间越短,且管道中前部和管道高点较其他位置先出现相变;在相同工况下,H2和N2等非极性杂质的存在会使CO2的相包线向上移动,最大停输时间减少;而H2S和CO等极性杂质的存在会使CO2的相包线向下移动,最大停输时间增加;停输再启动过程中,如果所含杂质的密度小于纯CO2的密度,则含有该类型杂质的管道恢复稳定运行状态所需时间短于纯CO2工质管道。研究结果可为相关单位制定CO2管道设计方案和安全停输预案提供参考。
Abstract:
To study the change law of temperature,pressure,and phase inside the supercritical CO2 pipeline after shutdown,taking a domestic CO2 pipeline as the research object,the OLGA software was used to conduct the transient numerical simulation of shutdown and restart,and the influence of different operating conditions and working medium on the pipeline shutdown and restart process was explored.The results show that when remaining the phase state and downstream user flow rate unchanged,the larger the flow rate,the shorter the maximum shutdown time,and the phase transition occurs first at the mid-front part and high points of the pipeline.Under the same operating conditions,the existence of non-polar impurities such as H2 and N2 can cause the phase envelope of CO2 to move upwards,reducing the maximum shutdown time,while the polar impurities such as H2S and CO can cause the phase envelope of CO2 to move downwards,increasing the maximum shutdown time.During the shutdown and restart process,if the density of contained impurities is less than that of pure CO2,the time required for pipelines containing this type of impurities to restore the stable operation status is shorter than that of pure CO2 pipeline.The research results can provide guidance and suggestions for related organizations to develop the CO2 pipeline design and safety shutdown plans.

参考文献/References:

[1]黄维和,李玉星,陈朋超.碳中和愿景下中国二氧化碳管道发展战略[J].天然气工业,2023,43(7):1-9.HUANG Weihe,LI Yuxing,CHEN Pengchao.China’s CO2 pipeline development strategy under the strategy of carbon neutrality[J].Natural Gas Industry,2023,43(7):1-9.
[2]郭克星,闫光龙,张阿昱,等.CO2捕集、利用与封存技术及CO2管道研究现状与发展[J].天然气与石油,2023,41(1):28-40.GUO Kexing,YAN Guanglong,ZHANG Ayu.Status quo and development of the research on CO2 capture,utilization and storage technology and CO2 pipeline[J].Natural Gas and Oil,2023,41(1):28-40.
[3]胡鑫杰,许仁辞.基于SPS的原油管道最大再启动压力增加值分析[J].管道技术与设备,2020(3):11-16.HU Xinjie,XU Renci.Analysis of maximum restart pressure increment of crude oil pipeline based on SPS[J].Pipeline Technique and Equipment,2020(3):11-16.
[4]程诚.油气长输管道安全经济效益评价模型及应用[J].中国安全生产科学技术,2021,17(增刊1):56-61.CHENG Cheng.Safety and economic benefit evaluation model of long-distance oil and gas pipelineand its application[J].Journal of Safety Science and Technology,2021,17(Supplement 1):56-61.
[5]王帅,何玉玉,龙相琪,等.基于启动压力的稠油停输海管再启动与置换对策[J].延安大学学报(自然科学版),2022,41(2):105-110.WANG Shuai,HE Yuyu,LONG Xiangqi,et al.Restart and replacement countermeasures of shutdown subsea pipeline for heavy oil water mixed transportation based on restart pressure[J].Journal of Yan’an University (Natural Science Edition),2022,41(2):105-110.
[6]杨金威,潘婷,周翔,等.中亚天然气管道乌国段AB/C线联合运行方案比选[J].油气储运,2021,40(5):596-600.YANG Jinwei,PAN Ting,ZHOU Xiang,et al.Comparison between joint operation schemes for Lines AB/C of Central Asia-China Gas Pipeline in Uzbekistan[J].Oil & Gas Storage and Transportation,2021,40(5):596-600.
[7]陈兵,房启超,白世星.含杂质超临界CO2输送管道的停输影响因素[J].天然气化工(C1化学与化工),2020,45(3):84-89.CHEN Bing,FANG Qichao,BAI Shixing.Research on the factors influencing the shutdown of the transport pipeline of supercritical CO2 containing impurities[J].Natural Gas Chemical Industry,2020,45(3):84-89.
[8]陈兵,徐梦林,房启超,等.超临界含杂质CO2管网停输再启动对水合物生成的影响[J].石油与天然气化工,2022,51(4):43-50.CHEN Bing,XU Menglin,FANG Qichao,et al.Effect of supercritical impurity-containing CO2 pipe network shutdown and restarting conditions on hydrate generation[J].Chemical Engineering of Oil & Gas,2022,51(4):43-50.
[9]李顺丽,潘红宇,李玉星,等.放空管设计对超临界CO2管道放空影响研究[J].中国安全生产科学技术,2015,11(11):101-105.LI Shunli,PAN Hongyu,LI Yuxing,et al.Study on influence of blow-down pipe design on blow-down of supercritical CO2 pipeline[J].Journal of Safety Science and Technology,2015,11(11):101-105.
[10]赵青,李玉星.杂质对管道输送CO2相特性的影响规律[J].油气储运,2014,33(7):734-739,743.ZHAO Qing,LI Yuxing.Impact of impurities on the phase behavior of CO2 in pipeline transportation[J].Oil & Gas Storage and Transportation,2014,33(7):734-739,743.
[11]刘敏.超临界二氧化碳管道输送瞬变特性研究[D].青岛:中国石油大学(华东),2015.
[12]KUNZ O,WAGNER W.The GERG-2008 wide-range equation of state for natural gases and other mixtures:an expansion of GERG-2004[J].Journal of Chemical and Engineering Data:the ACS Journal for Data,2012,57(11):3032-3091.
[13]李欣泽,袁亮,张超,等.超临界CO2管道瞬态输送工艺研究进展及方向[J].大庆石油地质与开发,2024,43(1):22-32.LI Xinze,YUAN Liang,ZHANG Chao.Research progress and direction on transient transportation process of supercritical CO2 pipeline[J].Petroleum Geology & Oilfield Development in Daqing,2024,43(1):22-32.
[14]吕家兴.复杂地形超临界CO2管道输送工艺技术研究[D].北京:中国石油大学(北京),2023.
[15]闫光龙,郭克星,牛爱军,等.CO2管道设计的热力学挑战[J].石油管材与仪器,2023,9(3):95-100.YAN Guanglong,GUO Kexing,NIU Aijun,et al.Thermodynamic challenges of CO2 pipeline design[J].Petroleum Tubular Goods & Instruments,2023,9(3):95-100.

相似文献/References:

[1]杨亚吉,曲兆光,王文光,等.基于瞬态特性的海底长输天然气管道泄漏规律研究[J].中国安全生产科学技术,2023,19(6):119.[doi:10.11731/j.issn.1673-193x.2023.06.017]
 YANG Yaji,QU Zhaoguang,WANG Wenguang,et al.Research on leakage law of submarine long-distance gas pipeline based on transient characteristics[J].JOURNAL OF SAFETY SCIENCE AND TECHNOLOGY,2023,19(5):119.[doi:10.11731/j.issn.1673-193x.2023.06.017]

备注/Memo

备注/Memo:
收稿日期: 2023-12-15
* 基金项目: 国家石油天然气管网集团有限公司科技专项项目(SSCC202107)
作者简介: 苗青,本科,高级工程师,主要研究方向为油气储运工艺和新能源输送技术。
通信作者: 李玉星,博士,教授,主要研究方向为天然气、氢气、二氧化碳管道输送理论与安全保障。
更新日期/Last Update: 2024-05-30