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Hydrogenation of Heavy Oil through Partial Oxidation in Supercritical Water

Hydrogenation of Heavy Oil through Partial Oxidation in Supercritical Water
超临界水部分氧化重油加氢
批准号:
09450281
负责人:
ARAI Kunio
金额:
$9.09万
依托单位:
依托单位国家:
日本
项目类别:
Grant-in-Aid for Scientific Research (B)
财政年份:
1997
资助国家:
日本
项目状态:
已结题
起止时间:
1997 至 1998

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中文摘要
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英文摘要
We have developed a hydrogenation process of heavy oil through partial oxidation in supercritical water. For the development of the process, partial oxidation of hydrocarbon and water-gas shift (WGS) reaction in supercritical water are key reactions. In this research, we conducted the basic study of these reactions. The results are as follows.1) Study on partial oxidation of hydrocarbon in supercritical waterPartial oxidation of n-hexadecane (n-C_<16>) in supercritical water was conducted using batch reactors at 400゚C and the effect of water density on the partial oxidation of n-C16 was investigated, In the result, the selectivity of CO formation increased with increasing water density.Partial oxidation of methanol and methane in supercritical water was also conducted using a flow apparatus at 380゚C - 400゚C of reaction temperatures and 10 MPa - 25 MPa of reaction pressures. At lower conversion and higher water density, the selectivity of CO formation increased.2) Measurement of reactio … More n rate of water-gas shift (WGS) reaction in supercritical waterThe reaction rate of WGS reaction in supercritical water was measured using a flow apparatus at 380゚C - 400゚C of reaction temperatures and 10 MPa - 30 MPa of reaction pressures. The rate of WGS reaction was changed specifically at the critical point of water and increased slightly with increasing water density.3) Study on catalytic hydrogenation of hydrocarbons through WGS reaction in supercritical waterCatalytic hydrogenation of hydrocarbons (naphthalene, carbazole, heavy oil, and so on) through WGS reaction in supercritical water was investigated using batch reactors. The rate of catalytic hydrogenation of hydrocarbons under SCW+CO atmosphere was higher than that under SCW+H_2 atmosphere. Furthermore, the rate of catalytic hydrogenation of hydrocarbons under SCW + CO_2 +H_2 atmosphere was higher than that under SCW+h_2 atmosphere. These results suggest that WGS reaction provides an active species for a catalytic hydrogenation of hydrocarbon in supercritical water.The above results indicate that catalytic hydrogenation through partial oxidation and water-gas shift reaction in supercritical water is an effective method for hydrogenation of hydrocarbons. Less
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Sato et al.: "Partial Oxidation of Hydroearbon and Carbon and Water-Gas Shift Reaction in Supercritical Water" Proceedings of the 6th Japan-China Symposium on Coal and C_1 chemistry. 232-235 (1998)
佐藤等:《超临界水中碳氢化合物的部分氧化与水煤气变换反应》第六届日中煤与C_1化学研讨会论文集。
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Adschiri.T et al.: "Catalytic hydrogenating desulfurization of heavy oil through part al oxidation in Supercritical water" Proceedings 9th international conference on coal science. (印刷中).
Adschiri.T 等人:“通过超临界水部分氧化实现重油催化加氢脱硫”第九届国际煤炭科学会议论文集(正在出版)。
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14
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    • 项目类别:
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    • 财政年份:
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    • 项目类别:
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