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首页> 外文期刊>Journal of the Japan Petroleum Institute >Upgrading of Heavy Oil by Hydrogenation through Partial Oxidation and Water-gas Shift Reaction in Supercritical Water
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Upgrading of Heavy Oil by Hydrogenation through Partial Oxidation and Water-gas Shift Reaction in Supercritical Water

机译:超临界水中部分氧化加水煤气变换反应加氢提质重油

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摘要

Partial oxidation of hydrocarbons including heavy oil in supercritical water forms CO and CO2, which undergoes the water-gas shift reaction to form active hydrogen and then hydrogenation of heavy oil proceeds. In the case of partial oxidation of hydrocarbons and bitumen in supercritical water, the selectivity for partial oxidative products such as CO increased with increasing water density. In the case of hydrogenation of heavy oil in supercritical water through the water-gas shift reaction, reverse water-gas shift reaction and decomposition of formic acid that is a reaction intermediate of the water-gas shift reaction, coke formation was suppressed compared to that in only supercritical water. The main factors for suppressing coke formation were as follows: high water density improving the reactivity of hydrogen source in the oil-rich phase that enhanced hydrogenation of asphal-tene core, direct injection of hydrogen source into the oil-rich phase increasing the concentration of active hydrogen in that phase, and coexisting gases with supercritical water facilitating the extraction of coke precursor from the oil-rich phase. The upgrading of heavy oil through a series of partial oxidation and hydrogenation reactions in supercritical water proceeded in the presence of catalyst and possible optimum conditions were proposed.
机译:在超临界水中,包括重油在内的碳氢化合物的部分氧化会生成CO和CO2,然后进行水煤气变换反应以形成活性氢,然后进行重油的氢化。在超临界水中烃和沥青被部分氧化的情况下,部分氧化产物(如CO)的选择性随水密度的增加而增加。通过水煤气变换反应,水煤气变换反应的逆反应和作为水煤气变换反应的反应中间产物的甲酸的分解,在超临界水中使重油氢化的情况,与之相比,抑制了焦炭的生成。仅在超临界水中。抑制焦炭形成的主要因素如下:高水密度提高了富油相中氢源的反应性,从而增强了沥青烯芯的氢化,将氢源直接注入富油相中,从而增加了焦炭的浓度。该相中的活性氢,以及与超临界水共存的气体,有助于从富油相中提取焦炭前体。在催化剂的存在下,通过在超临界水中进行一系列的部分氧化和氢化反应,对重油进行提质,并提出了可能的最佳条件。

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