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

机译:蒸汽注入过程中使用氢供体和催化剂原位重油的实验研究

摘要

Experiments were conducted to investigate the feasibility of in situ upgrading ofheavy oil by the use of an orgametallic catalyst and a hydrogen donor (tetralin). Theexperiments used a vertical injection cell into which a mixture of sand, water, and Jobooil was thoroughly mixed and packed. Two types of runs were conducted: a run wherethe tetralin and catalyst were mixed within the mixture before packing into the cell, andthe other was conducted by injecting a slug of the tetralin-catalyst solution beforecommencing with the steam injection. The Jobo oil used had an oil gravity of 12.4? APIand a viscosity of 7800 cp at 30?C. The injection cell was placed in a vacuum jacket andset to a reservoir temperature of 50?C. Superheated steam at 273?C was then injectedinto the injection cell at a rate of 5.5 cc/min (cold water equivalent). The cell outletpressure was maintained at 500 psig. Produced liquid samples were collectedperiodically through a series of separators. The produced oil was divided into two halvesand several measurements and analyses were carried out on them. These includedviscosity, density, elemental analysis and liquid composition. Experimental results indicated that tetralin alone was a worthy additive andincreased recovery by 15% compared to that of pure steam. The premixed tetralincatalystrun showed improved recovery to that of pure steam by 20%. Experiments alsoshowed that, when the tetralin-catalyst solution was injected rather than mixed, theresults were equivalent to tetralin injection runs. Oil production acceleration wasdisplayed by all the runs with tetralin and tetralin-catalyst but was more pronounced withthe 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(四氢萘)原位提质重油的可行性。实验使用垂直注入池,将沙子,水和Jobooil的混合物充分混合并包装在其中。进行两种运行:将四氢萘酚和催化剂在混合物中混合后再填充到电池中,另一种通过在注入蒸汽之前注入一段四氢萘催化剂溶液进行。所用的Jobo油的油重为12.4? API和30°C时的粘度为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。然后以5.5 cc / min(冷水当量)的速度将273°C的过热蒸汽注入注入室。池出口压力保持在500 psig。通过一系列的分离器定期收集产生的液体样品。将产生的油分为两半,并对其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,与纯蒸汽相比,单独的四氢萘是值得添加的添加剂,回收率提高了15%。预混合的四氢化萘催化剂运行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,但是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
  • 年度 2008
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  • 原文格式 PDF
  • 正文语种 en_US
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