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中深层煤炭地下气化的气化腔安全宽度计算方法

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煤炭地下气化是目前温度最高(超过 1200℃)的化石能源非常规开发方式,中深层(本文指埋深 800~1500 m)煤炭地下气化在提高气化压力、降低地质安全风险方面优势明显,科学预测气化腔安全宽度对保障气化稳定运行十分重要,由于目前基于可控注入点后退(CRIP)工艺的气化腔安全宽度计算方法尚未建立,为保证现场试验顺利实施,需要开展针对性研究.气化腔顶板"裸露"在气化腔后会受到高温影响,通过数值模拟方法研究了压应力约束条件下岩石内部热应力产生位置以及颗粒、基质热膨胀系数差异对热应力大小的影响规律,结合高温处理后的岩石电镜扫描结果,查明了高温下岩石热损伤机理.根据CRIP气化工艺造腔特点,建立了考虑高温影响的气化腔顶板薄板模型,结合"关键层"理论提出了气化腔安全宽度计算方法.研究表明:岩石热损伤是岩石物理化学反应与热应力互相促进、共同作用的结果,高温下岩石发生不规则变形,岩石热损伤引起的微观结构变化是导致岩石力学性质、物理性质变化的根本原因.岩石的最大拉张热应力出现在颗粒界面或热膨胀系数较小的颗粒中,颗粒与基质热膨胀系数比值在[0.01~1)时,最大拉张热应力随颗粒热膨胀系数减小而快速增加.泥岩加热到 200℃时开始出现微裂隙;加热到 400℃时裂隙发育更加明显,主要是沿颗粒边缘破裂;加热到 600~800℃时,裂隙数量增多、尺寸变大;加热到 1000℃时,除出现较大裂隙外,还产生了大量孔隙;1200℃时裂隙连通性明显增加,气孔发育较大.由于高温的影响,薄板模型的步距准数不再是定值,需要根据气化腔顶板热破坏范围与顶板硬岩层的空间位置关系确定具体数值.气化腔安全宽度受温度影响,在研究算例中,砂岩顶板在35、1000℃时安全宽度计算结果分别为34.3 m和14.1 m,相差达 58.9%,泥岩顶板在 35、1000℃时安全宽度计算结果分别为 16.7 m和 15.9 m,相差 4.8%.最后从降低顶板垮落风险、有利于气化控制角度,提出了煤层纵向靶区位置的确定方法,当煤层厚度超过气化腔安全宽度一半时,建议将水平井纵向靶区设计在距离煤顶不超过气化腔安全宽度一半的位置.
Calculation method of safe width of gasification cavity for medium-deep underground coal gasification
Underground coal gasification is currently the highest-temperature(over 1200℃)unconventional development method for fossil energy.Underground gasification of coal in the medium-deep(refer to the depth of 800~1500 m in this paper)has obvious advant-ages in improving the gasification pressure and reducing the geological safety risks.Scientific prediction of safe width of gasification cav-ity is important to ensure stable gasification operation.Since the method of calculating the safe width of gasification cavity based on Con-trolled Retreat Injection Point(CRIP)process has not yet been established,targeted research is needed to ensure the smooth implementa-tion of field tests.Once the top plate of the gasification cavity is"exposed"to high temperature behind the gasification cavity.The genera-tion position of thermal stresses inside the rock and the influence law of differences in the thermal expansion coefficient of particles and matrix on the magnitude of thermal stresses were studied by numerical simulation under compressive stress constraints.the thermal dam-age mechanism of rock under high temperature was clarified combined with the scanning electron microscope results of rock after high temperature treatment.According to the characteristics of CRIP gasification process,a thin plate model of gasification cavity roof consid-ering the influence of high temperature was established,and a method for calculating the safe width of the gasification cavity was pro-posed in combination with the theory of"key layer".The study revealed that,rock thermal damage was caused by the interaction and syn-ergy of rock physicochemical reactions and thermal stress,and the rock undergone irregular deformation at high temperatures.Microstruc-tural changes of rock caused by the thermal damage were the fundamental cause of changes in rock mechanical and physical properties.The maximum tensile thermal stress in rock occurred at the grain interfaces or in grains with small coefficient of thermal expansion.The maximum tensile thermal stress increased rapidly with decreasing the thermal expansion coefficient of the grain when the ratio of the thermal expansion coefficient of the grain to that of the matrix is in the range of[0.01-1).The microcracks of mudstone was developed when heated to 200℃,the crack development was more obvious when heated to 400℃,which mainly along the edge of the particles rup-ture.The number of cracks was increased and the size was larger when heated to 600-800℃.The larger cracks and numerous pores were formed when heated to 1000℃.The crack connectivity increased significantly at 1200℃,and the stomatal development was larger.Due to the effect of high temperature,the step constant for the thin plate model is no longer a constant,and specific values need to be determ-ined based on the extent of thermal damage to the roof of gasification cavity and the location of the hard rock layer on the top plate.The safe width of gasification cavity was affected by temperature.In the study,the calculated safe widths of sandstone roof at 35 and 1000℃ were 34.3 m and 14.1 m,respectively,with a difference of 58.9%.while the safe widths at 35 and 1000℃ were 16.7 m and 15.9 m,re-spectively,with a 4.8%difference.Lastly,a method of determining the longitudinal target area of coal seam was proposed from the per-spective of reducing the risk of roof collapse and improving gasification control.When the coal seam thickness exceeded half of the gasi-fication cavity safe width,it was suggested to design the longitudinal target area of horizontal well at a location not more than half of the safe width of gasification cavity from the top of the coal.

underground coal gasificationcontrolled retracting injection point processgasification cavitythermal stressthermal dam-agethin plate modelspan criterionsafety width

东振、任博、陈艳鹏、赵宇峰、陈浩、陈姗姗、薛俊杰、张梦媛、易海洋、吴瀚琦

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中国石油勘探开发研究院,北京 100083

中国矿业大学深部岩土力学与地下工程国家重点实验室,江苏徐州 221116

华北科技学院建筑工程学院,河北廊坊 065201

中国石油天然气股份有限公司储气库分公司,北京 100101

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煤炭地下气化 可控注入点后退工艺 气化腔 热应力 热损伤 薄板模型 步距准数 安全宽度

中国石油科技攻关计划重大项目中国石油天然气集团有限公司软科学研究计划

2019E-2520230118-4

2024

煤炭科学技术
煤炭科学研究总院

煤炭科学技术

CSTPCD北大核心
影响因子:2.095
ISSN:0253-2336
年,卷(期):2024.52(2)
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