On Kinetics of Upgrading Reactions by Supercritical Water Technology of Highly Sour Qayara Crude Oil over an Activated Carbon-Based Catalyst

Saba A. Gheni, Mohammed H. Mohammed, K. Hamad, Hassan M. Hmood
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Abstract

Currently clean energy and zero emission fuel is a priority as there is a growing level of pollutants in air, sea and soil. Also, the conventional Iraqi crude oil is going to deplete according to the statistical analysis. Thus, methods of upgrading should attract attention in Iraqi fuel sector. The method of supercritical fluids (SCF) is one of the advanced approaches to upgrade the unconventional crude oil and removal of high levels of sulfur compounds. The present work aims at developing a kinetic model for upgrading reactions by supercritical water technology of a sour Iraqi crude oil. This aim was achieved via conducting sets of experiments in a hydrothermal autoclave reactor over a cobalt/activated carbon catalyst. The AC was used as a support for Co as an active metal. A set of upgrading kinetics experiments were applied at different temperatures (290-350 °C) and reaction times (0-45 min). Upon evaluation of the prepared catalysts for kinetics of upgrading by supercritical water technology, it was found that the process flows pseudo first order mechanism. Also, the activation energy of the chemical reaction was found to be 204.1 kJ/mol which is much less compared to previous studies
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活性炭基催化剂上高酸性Qayara原油超临界水提质反应动力学研究
目前,清洁能源和零排放燃料是一个优先事项,因为空气、海洋和土壤中的污染物水平越来越高。另外,据统计分析,伊拉克的常规原油也将逐渐枯竭。因此,改进的方法应引起伊拉克燃料部门的注意。超临界流体法(SCF)是非常规原油改造和去除高硫化合物的先进方法之一。本工作旨在建立超临界水技术对伊拉克含硫原油进行提质反应的动力学模型。这一目标是通过在钴/活性炭催化剂上的水热压釜反应器中进行的一系列实验来实现的。作为活性金属的钴被用作载体。在不同温度(290 ~ 350℃)和反应时间(0 ~ 45 min)下进行了一组升级动力学实验。通过对制备的催化剂进行超临界水技术提质动力学评价,发现该工艺符合准一级机理。同时,该化学反应的活化能为204.1 kJ/mol,大大低于前人的研究结果
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