抑制水合物冻堵的天然气开井动态模拟研究

doi:10.11885/j.issn.1674-5086.2013.10.31.06

摘要/Abstract

摘要：

针对天然气井工艺管道在开井过程中极易产生水合物冻堵的问题，采用Dynsim 软件建立了开井工况动态模
拟模型，讨论了开井流量、工艺管道敷设方式与保温层厚度、节流调节方案对节流后温度压力的影响，分析了开井过程
中外界热交换的动态变化特征及对开井过程的影响，提出了加热炉前工艺管道优化设计与开井过程水合物优化控制
方案。结果表明：开井流量对水合物生成风险具有重要影响，开井流量越小，水合物生成风险越大，但不管开井流量
如何调整，井口工艺管道内均存在水合物生成风险；在保证下游出口超压在可接受范围的前提下，应通过同时调节各
级节流阀或主要调节二级与三级节流阀来尽量增大开井流量，并配合注醇、加热等方式来避免在工艺管道中生成水合
物；井口至加热炉前的工艺管道宜采用埋地敷设方式，埋地敷设管道无需保温，而架空敷设管道宜加保温措施。

关键词: 天然气井, 开井, 动态模拟, 水合物, 优化设计

Abstract:

The hydrate freeze-plugging phenomenon is easy to occur in pipelines during the open period of natural gas wells
especially for wells with high pressure. The dynamic characteristics and optimal hydrate control schemes during well opening
period，however，have not been studied systematically. So the specific dynamic models have been established to analyze
the dynamic characteristics during well opening period by Dynsim package. The influences of the fluid flowrate，installation
modes of pipelines，thickness of thermal insulation layer as well as throttling regulation schemes on throttling temperature and
pressure during well opening period have been discussed by using the dynamic models. The dynamic characteristics of heat
transfer between fluid in pipelines and ambient environment during well opening period have also been analyzed. In addition，
the optimal control schemes for hydrate inhibition during well opening period and optimization design for pipelines have also
been put forward in the paper. The results demonstrate that the fluid flowrate during well opening period has dramatical influence
on the risk of hydrate formation in pipelines. And no matter how to regulate the fluid flowrate during well opening period，
hydrate formation risk in pipelines exists all the time，especially when the flowrate remains small. In order to avoid hydrate
formation in pipelines，the fluid flowrate during well opening period should be increased as large as possible by regulating
different throttle valves simultaneously or regulating the secondary and tertiary throttle valves mainly. Meanwhile，necessary
measures like alcohol injection or heating should be done to mitigate the risk of hydrate formation. Furthermore，it is suggested
that the pipelines between wellhead and heating furnace should be buried underground without thermal insulation layer，whereas
other overhead pipelines should be covered by thermal insulation layer.

Key words: natural gas well, well opening, dynamic simulation, hydrate, optimization design

中图分类号:

TE375

岑康1 *，江鑫1，杨静2，朱远星1. 抑制水合物冻堵的天然气开井动态模拟研究[J]. 西南石油大学学报(自然科学版), DOI: 10.11885/j.issn.1674-5086.2013.10.31.06.

CEN Kang1*, JIANG Xin1, YANG Jing2, ZHU Yuanxing1. Dynamic Simulation of the Open Process for Natural Gas Wells to#br# Inhibit Hydrate Freeze-plugging[J]. 西南石油大学学报(自然科学版), DOI: 10.11885/j.issn.1674-5086.2013.10.31.06.

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参考文献

[1] 陈赓良. 天然气采输过程中水合物的形成与防止[J]. 天
然气工业，2004，24（8）：89 91.
CHEN Gengliang. Formation and prevention of hydrate
during process of gas exploitation and transmission[J].
Natural Gas Industry，2004，24（8）：89 91.
[2] 胡德芬，侯梅，徐立，等. 高含硫气井集输系统天然气
水合物的防治以川东地区高含硫气井为例[J]. 天
然气工业，2010，30（10）：78 82.
HU Defen，HOU Mei，XU Li，et al. Gas hydrate control
measures for gathering system of high-sulfur gas wells
in eastern Sichuan Basin[J]. Natural Gas Industry，2010，
30（10）：78 82.
[3] 何生厚，曹耀峰. 普光高酸性气田开发[M]. 北京：中国
石化出版社，2010.
[4] 姜志阳，徐艳迪，付国强. 普光高含硫酸性气田主体开
发用管道材料选用[J]. 石油工程建设，2009，35（增）：
4 7.
JIANG Zhiyang，XU Yandi，FU Guoqiang. Pipeline material
selection in main development of Puguang high sulfurous
Gas Field[J]. Petroleum Engineering Construction，
2009，35（S）：4 7.
[5] DEPEW C，MARTINEZ A，COLLODI G，et al. Dynamic
simulation for IGCC process and control design[J]. Hydrocarbon
Processing，1998，77（1）：107 117.
[6] 陈文峰，刘培林，郭洲，等. 复杂物系压力容器安全
阀泄放过程的HYSYS 动态模拟[J]. 天然气与石油，
2010，28（6）：55 58.
CHEN Wenfeng，LIU Peilin，GUO Zhou，et al. HYSYS
dynamic simulation of relief process of complex pressure
vessel safety valve[J]. Natural Gas and Oil，2010，28（6）：
55 58.
[7] Pokki J，Hurme M，Aittanaa J. Dynamic simulation of
the behaviors of pressure relief system[J]. Computers and
Chemical Engineering，2001，25（4）：793 798.
[8] 董兵，魏文韫，帅剑云，等. 蓄能器泄压过程的动态模
拟[J]. 化工机械，2012，39（3）：329 334，346.
DONG Bing，WEI Wenyun，SHUAI Jianyun，et al. Dynamic
simulation on pressure relief process of energy ac
cumulator[J]. Chemical Engineering & Machinery，2012，
39（3）：329 334，346．
[9] 中国石油天然气集团公司人事部. 集输技师培训教
程[M]. 北京：石油工业出版社，2012.
[10] INVENSYS S E. Dynamic Simulation Suite for Dynsim[
R]. 2008.
[11] 贺来宾，杨卫胜，马丽丽. 甲苯歧化装置紧急泄压工
况的模拟研究[J]. 计算机与应用化学，2012，29（4）：
503 506.
HE Laibin，YANG Weisheng，MA Lili. Dynamic simulation
and research of emergent decompression in toluene
disproportionation process[J]. Computers and Applied
Chemistry，2012，29（4）：503 506.
[12] 张永铭，杨焘，刘博，等. 动态模拟在芳烃抽提装置设
计中的应用[J]. 化学工程，2011，39（11）：88 91，98．
ZHANG Yongming，YANG Tao，LIU Bo，et al. Application
of dynsim in design of aromatics extraction unit[J].
Chemical Engineering，2011，39（11）：88 91，98.
[13] 刘云，卢源，伊向艺，等. 天然气水合物预测模型及其
影响因素[J]. 岩性油气藏，2010，22（3）：124 127．
LIU Yun，LU Yuan，YI Xiangyi，et al. Gas hydrate forecasting
model and its influencing factors[J]. Lithological
Reservoirs，2010，22（3）：124 127．
[14] 徐苏燕，康成瑞. 天然气采输过程中水合物防治技术
研究应用[J]. 油气藏评价与开发，2012，2（5）：65 70.
XU Suyan，KANG Chengrui. Research and application of
hydrate prevention and control technology in production
and transportation of natural gas[J]. Reservoir Evaluation
and Development，2012，2（5）：65 70.
[15] 刘祎. 天然气集输与安全[M]. 北京：中国石化出版社，
2010．