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Experimental investigation of in situ upgrading of heavy oil by using a hydrogen donor and catalyst during stream injection.

机译:在射流过程中通过使用氢供体和催化剂对重油进行原位提质的实验研究。

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摘要

Experiments were conducted to investigate the feasibility of in situ upgrading of heavy oil by the use of an orgametallic catalyst and a hydrogen donor (tetralin). The experiments used a vertical injection cell into which a mixture of sand, water, and Jobo oil was thoroughly mixed and packed. Two types of runs were conducted: a run where the tetralin and catalyst were mixed within the mixture before packing into the cell, and the other was conducted by injecting a slug of the tetralin-catalyst solution before commencing with the steam injection. The Jobo oil used had an oil gravity of 12.4° API and a viscosity of 7800 cp at 30°C. The injection cell was placed in a vacuum jacket and set to a reservoir temperature of 50°C. Superheated steam at 273°C was then injected into the injection cell at a rate of 5.5 cc/min (cold water equivalent). The cell outlet pressure was maintained at 500 psig. Produced liquid samples were collected periodically through a series of separators. The produced oil was divided into two halves and several measurements and analyses were carried out on them. These included viscosity, density, elemental analysis and liquid composition.;Experimental results indicated that tetralin alone was a worthy additive and increased recovery by 15% compared to that of pure steam. The premixed tetralincatalyst run showed improved recovery to that of pure steam by 20%. Experiments also showed that, when the tetralin-catalyst solution was injected rather than mixed, the results were equivalent to tetralin injection runs. Oil production acceleration was displayed by all the runs with tetralin and tetralin-catalyst but was more pronounced with the availability of catalyst.
机译:进行实验以研究通过使用有机金属催化剂和氢供体(四氢化萘)进行重油原位提质的可行性。实验使用垂直注入池,其中将沙子,水和Jobo油的混合物充分混合并填充。进行两种类型的运行:一种运行,其中将四氢萘酚和催化剂在混合物中混合,然后填充到电池中;另一种通过在注入蒸汽之前注入一小段四氢化萘催化剂溶液进行。所用的Jobo油的油重为API的12.4°,在30°C下的粘度为7800 cp。将进样池放置在真空夹套中,并设定为50°C的储存器温度。然后将273°C的过热蒸汽以5.5 cc / min(冷水当量)的速率注入注入室。池出口压力保持在500 psig。通过一系列分离器定期收集产生的液体样品。将产生的油分为两半,并对它们进行了几次测量和分析。这些包括粘度,密度,元素分析和液体组成。;实验结果表明,单独的四氢萘是一种有价值的添加剂,与纯蒸汽相比,回收率提高了15%。预混合四氢化萘催化剂运行显示出比纯蒸汽的回收率提高了20%。实验还表明,当注射四氢化萘催化剂溶液而不是混合时,结果等同于四氢化萘注射过程。用四氢化萘和四氢化萘催化剂进行的所有运行均显示出产油加速,但在催化剂的可获得性方面更为明显。

著录项

  • 作者

    Mohammad, Ahmad A. A.;

  • 作者单位

    Texas A&M University.;

  • 授予单位 Texas A&M University.;
  • 学科 Engineering Petroleum.
  • 学位 Ph.D.
  • 年度 2008
  • 页码 199 p.
  • 总页数 199
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 石油、天然气工业;
  • 关键词

  • 入库时间 2022-08-17 11:38:34

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