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作 者:黄佳 江航[1] 赵长虹 周明辉[1] 赵慧龙[2] 孙盈盈[1] 邢向荣[2] 吕柏林[2] 樊铖 HUANG Jia;JIANG Hang;ZHAO Changhong;ZHOU Minghui;ZHAO Huilong;SUN Yingying;XING Xiangrong;LYU Bolin;FAN Cheng(State Key Laboratory of Enhanced Oil Recovery,Research Institute of Petroleum Exploration&Development,China National Petroleum Corporation,Beijing 100083,China;Fengcheng Field Operation District,PetroChina Xinjiang Oilfield Company,Karamay 834000,China;School of Chemistry and Chemical Engineering,Beijing Institute of Technology,Beijing 100081,China)
机构地区:[1]中国石油勘探开发研究院提高石油采收率国家重点实验室,北京100083 [2]中国石油新疆油田公司风城油田作业区,新疆克拉玛依834000 [3]北京理工大学化学与化工学院,北京100081
出 处:《中国粉体技术》2020年第1期68-74,共7页China Powder Science and Technology
基 金:国家“十三五”科技重大专项,编号:2016ZX05012;中国石油天然气集团公司技术研发基金项目,编号:2016A-0901
摘 要:为探讨固体稠油的原位改质降黏技术,提高采收率,对其中关键因素催化剂进行研究。分别采用油溶性催化剂环烷酸铁与水溶性纳米催化剂硝酸铁,对新疆油田中的稠油固体进行改质降黏,并采用集总的分布式活化能模型(DAEM)模型对稠油固体热解过程进行分析。结果表明:环烷酸铁和硝酸铁独立作为催化剂时,对于稠油固体的降黏率分别到56.29%,45.40%;两者复配使用时,降黏率可达到97%,复配协同作用有助于集成各自优势。In order to study in-situ modification and viscosity reduction technology of solid heavy oil and improve oil re covery,the most critical factor catalyst was studied.Iron naphthenate,an oil-soluble catalyst,and ferric nitrate,a water soluble catalyst,were employed,and their separate and combined effects on viscosity reduction were evaluated.The re sults showed that,the viscosity of heavy oil was reduced by 56.29%and 45.40%respectively when the two were used as separate catalyst,while the viscosity was significantly reduced by 97%when the two catalysts were combined.The dis tributed activation energy model(DAEM)was employed to analyze the pyrolysis process of heavy oil and the synergistic effect of the catalysts helps to integrate the advantages of the two catalysts.
关 键 词:稠油固体 催化降黏 复配催化剂 分布式活化能模型 热解动力学
分 类 号:TE39[石油与天然气工程—油气田开发工程]
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