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On Hydrogen Sulfide Evolution and Scavenging within SAGD Steam Chambers

机译:在SAGD蒸汽室内硫化氢进化和清除

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In the Steam-Assisted Gravity Drainage (SAGD) thermal recovery process, high pressure and high temperature saturated-steam is injected into a bitumen-bearing oil sands formation. For most operations, the steam temperature ranges from about 200 to 260?C and thus under these conditions, the bitumen, in the presence of high temperature steam condensate, undergoes hydrous pyrolysis, i.e. aquathermolysis, yielding acid gases such as hydrogen sulfide and carbon dioxide. Current SAGD thermal reservoir simulation models in the literature often take into account complex spatial heterogeneity of the geology and oil composition and the physics of heat transfer, multiphase flow, gas solubility effects, and viscosity variations with temperature, however, few have taken the chemistry of SAGD into account. Here, we have added aquathermolysis reactions to thermal reservoir simulation model to understand reactive zones in the SAGD process and how the process generates acid gases via aquathermolysis. Given the requirement to constrain or handle sulfur emissions from thermal recovery processes, it is necessary to understand both the physical and chemical sides of the processes. Here, we have explored the possibility of triggering the Claus process underground for in situ scavenging of hydrogen sulfide during SAGD. The application of the research results is specifically to SAGD although the results could be extended to Cyclic Steam Stimulation as well. The results demonstrate that SAGD is not only a physical process that operates largely under gravity drainage but that it is also a chemically reactive process which generates hydrogen sulfide and carbon dioxide. The results also demonstrate that hydrogen sulfide generation reactions occur where there is sufficient heat, water, and oil and thus, the reactive zones are mainly at the edges of the steam chamber and in the liquid pool that sits above the production well. Injecting very small amount of sulfur dixode along with steam could result in initiation of Claus reaction underground resulting into conversion of hydrogen sulfide into liquid sulfur. The results of this study are significant given regulated emission limits of hydrogen sulfide from SAGD operations in Alberta, Canada, and moreover, the ability to potentially reduce emissions by altering the operating strategy or through in situ hydrogen sulfide scavengers offers an elegant way to meet these regulations.
机译:在蒸汽辅助重力引流(SAGD)热回收过程中,将高压和高温饱和蒸汽注入含沥青油砂层中。对于大多数操作,蒸汽温度范围为约200至260℃,因此在这些条件下,沥青在高温蒸汽冷凝物的存在下,经历含水热解,即含水溶解,产生耐硫化氢和二氧化碳等酸性气体。当前的SAGD热储层在文献中的仿真模型通常考虑到地质和油组成的复杂空间异质性和传热,多相流动,气体溶解度效应和温度的粘度变化,然而,很少有化学SAGD考虑。在这里,我们已经添加了对热储存器模拟模型的Aquathermoly istics反应,以了解SAGD过程中的反应区以及该过程如何通过Aquather溶解产​​生酸性气体。鉴于要求从热回收过程中约束或处理硫排放,有必要了解该过程的物理和化学侧面。在这里,我们已经探讨了在SAGD期间触发地下触发地下克劳斯过程的可能性。研究结果的应用具体是SAGD,尽管结果也可以扩展到循环蒸汽刺激。结果表明,SAGD不仅是物理过程,该物理过程在很大程度上在重力引流下工作,但它也是产生硫化氢和二氧化碳的化学反应过程。结果还表明,硫化氢产生反应发生足够的热量,水和油,因此,反应区主要处于蒸汽室的边缘和坐在生产井上之上的液体池中。注入非常少量的硫Dixode以及蒸汽可导致在地下引发Claus反应,从而将硫化氢转化为液态硫。本研究的结果是亚伯塔省,加拿大的SAGD操作的硫化氢硫化氢的受调节排放限制,并且通过改变操作策略或通过原位硫化氢清除剂来潜在地减少排放的能力提供了优雅的方式来满足这些法规。

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