|本期目录/Table of Contents|

[1]张胜,蒲万芬,刘冬冬,等.蒸汽吞吐生产过程中CO产出超标原因分析 ——以红山油田为例[J].中国安全生产科学技术,2016,12(8):153-157.[doi:10.11731/j.issn.1673-193x.2016.08.026]
　ZHANG Sheng,PU Wanfen,LIU Dongdong,et al.Cause analysis on excess production of carbon monoxide in cyclic steam stimulation process-Taking Hongshan Oilfield as example[J].JOURNAL OF SAFETY SCIENCE AND TECHNOLOGY,2016,12(8):153-157.[doi:10.11731/j.issn.1673-193x.2016.08.026]
点击复制

蒸汽吞吐生产过程中CO产出超标原因分析 ——以红山油田为例
分享到：

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

卷:
12
期数:
2016年8期
页码:
153-157
栏目:
现代职业安全卫生管理与技术
出版日期:
2016-08-30

文章信息/Info

Title:
Cause analysis on excess production of carbon monoxide in cyclic steam stimulation process-Taking Hongshan Oilfield as example
作者:
张胜1; 蒲万芬2; 刘冬冬1; 于倩1; 杨洋2
（1. 克拉玛依红山油田有限责任公司， 新 疆 克拉玛依 834000；2.西南石油大学 国家重点实验室，四川 成都 610500）
Author(s):
ZHANG Sheng1;  PU Wanfen2;  LIU Dongdong1;  YU Qian1;  YANG Yang2
(1. Karamay Hongshan Oilfield Co. Ltd., Karamay Xinjiang 834000, China; 2. State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation, Southwest Petroleum University, Chengdu Sichuan 610500, China)
关键词:
蒸汽吞吐; 一氧化碳; 超标; 原因
Keywords:
cyclic steam stimulation;  carbon monoxide;  excess production;  cause
分类号:
X937
DOI:
10.11731/j.issn.1673-193x.2016.08.026
文献标志码:
A
摘要:
针对红山油田蒸汽吞吐生产过程中一氧化碳产出浓度超标的问题，开展了实验研 究，分析了反应温度、水油质量比、反应时间、储层矿物等因素对于一氧化碳产出浓度 的影响。结果表明：反应温度的升高、水油比的减少、反应时间的减少均会使一氧化碳 产出浓度上升，但造成红山油田生产过程中一氧化碳产出浓度超标的主要原因是红山油 田地层岩石矿物对水气转换反应的催化能力不足，加入对水气转换反应具有催化能力的 药剂可以降低一氧化碳产出浓度。
Abstract:
To solve the problem of excess production of carbon monoxide in cyclic steam stimulation process in Hongshan Oilfield, the corresponding laboratory study was conducted. The effect of reaction temperature, water/oil mass ratio, reaction time and rock minerals on production concentration of carbon monoxide was investigated. The results showed that all the increase of reaction temperature, the reduction of water/oil mass ratio and the reduction of reaction time promoted the increase of production concentration of carbon monoxide. However, the main cause of excess production of carbon monoxide in Hongshan oilfield is that the lack of catalytic capability of rock minerals in strata of Hongshan Oilfield to the water-gas shift reaction. The addition of agent which has the catalytic capability to the water-gas shift reaction can decrease the production concentration of carbon monoxide.

参考文献/References:

［1］Mousavi S M, Masoudi R, Ataei A. Evaluation of Steam Flooding and Cyclic Steam Stimulation (CSS) for a Fractured Carbonate Heavy Oil Reservoir ［C］. Bangkok, Thailand: IPTC International Petroleum Technology Conference, 2011.
［2］王洋, 蒋平, 张建强,等. 气体辅助蒸汽吞吐研究进展 ［J］. 精细石油化工进展 , 2012, 13（6）：6-11. WANG Yang, JIANG Ping, ZHANG Jianqiang, et al. Research progress of gas assisted cyclic steam stimulation ［J］. Advances in Fine Petrochemicals, 2012, 13 (6): 6-11.
［3］Tewari R D, Abdalla F, Lutfi H G, et al. Successful Cyclic Steam Stimulation Pilot in Heavy Oilfield of Sudan ［C］. Kuala Lumpur, Malaysia: SPE Enhanced Oil Recovery Conference, 2011.
［4］Elias R, Powell T, Medizade M. An Analysis of Cyclic Steam Stimulation Projects in the California Opal A Diatomite ［C］. Garden Grove, California, USA: SPE Western Regional Meeting. Society of Petroleum Engineers, 2015.
［5］刘文章. 特稠油，超稠油油藏热采开发模式综述 ［J］. 特种油气藏，1998，5（ 3）：1-7. LIU Wenzhang. An overview on thermal development mode of super viscous crude oil and extra viscous crude oil reservoir ［J］. Special Oil & Gas Reservoirs, 1998, 5 (3): 1-7.
［6］Wayne Monnery. Dealing with H2S in Heavy Oil Thermal Projects ［C］. Calgary, Alberta, Canada: SPE International Thermal Operations and Heavy Oil Symposium, 2005.
［7］武萍. 超稠油开发硫化氢成因分析及治理技术 ［J］. 中外能源，2013，18（6） ：49-52. Wu Ping. Genesis analysis and treatment technology for hydrogen sulfide in super heavy crude oil exploitation ［J］. Sino-Global Energy, 2013. 18 (6): 49-52.
［8］刘小群, 江宏富, 姚文锐. 硫化氢脱除技术研究进展 ［J］. 安徽化工，2004， 30（5）：33-37. LIU Xiaojiang, JIANG Hongfu, YAO Wenrui. Development study on removing hydrogen sulfide ［J］. Anhui Chemical Engineering, 2004, 30 (5): 33-37.
［9］Clark P D, Hyne J B. Steam-oil chemical reactions: mechanisms for the aquathermolysis of heavy oil ［J］. Aostra J Res, 1984, 1(1): 15-20.
［10］Callaghan C A. Kinetics and catalysis of the water-gas-shift reaction: A microkinetic and graph theoretic approach ［D］. Worcester: Worcester Polytechnic Institute, 2006.
［11］房德仁, 刘中民, 杨越,等. 制备溶液pH对CuO-ZnO/Al2O3催化剂前体物相及其CO 水汽变换反应活性的影响［J］. 石油化工, 2005, 34(11):1032-1036. FANG Deren, LIU Zhongmin, YANG Yue, et al. Influence of precipitation pH on phase composition of catalyst (CuO-ZnO/Al2O3) precursors and activity of catalyst in CO water gas reaction［J］. Petroleum Chemical Engineering, 2005, 34(11):1032-1036.
［12］林性贻, 殷玲, 范言,等. Al2O3改性CuO/Fe2O3催化剂水煤气变换反应性能［J］ . 物理化学学报, 2015, 31(4):757-763. LIN Xingyi, YIN Ling, FAN Yan, et al. Performance of Al2O3-Modified CuO/Fe2O3 catalysts in the water-gas shift reaction ［J］. Acta Physico- Chimica Sinica , 2015, 31(4): 757-763.

相似文献/References:

备注/Memo

备注/Memo:
红山油田公司横向项目
更新日期/Last Update: 2016-08-30