低温法费-托合成油加氢提质CFH~L技术开发及工业应用 |
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引用本文: | 吴昊,胡志海,聂红,贺小亮.低温法费-托合成油加氢提质CFH~L技术开发及工业应用[J].石油炼制与化工,2017,48(3):1-4. |
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作者姓名: | 吴昊 胡志海 聂红 贺小亮 |
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作者单位: | 1. 中国石化石油化工科学研究院;
2. 陕西未来能源化工有限公司; |
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摘 要: | 介绍了中国石化石油化工科学研究院开发的低温法费-托合成油加氢提质CFH~L技术及工业应用情况,考察了操作条件对异构加氢裂化反应效果的影响。结果表明,反应温度、氢分压、体积空速对异构加氢裂化反应效果影响显著,氢油体积比影响较小。CFH~L技术工业应用结果表明,稳定加氢柴油馏分十六烷值为81,凝点小于-20℃;异构加氢裂化柴油馏分选择性为82.2%,异构裂化柴油馏分十六烷值为76,凝点为-53℃。
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关 键 词: | 费-托合成油 加氢提质 异构裂化 工业化 |
收稿时间: | 2016-07-18 |
CFHL TECHNOLOGY FOR LOW TEMPERATURE F-T SYNTHETIC OIL HYDROUPGRADING AND ITS INDUSTRIAL APPLICATION |
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Abstract: | This paper introduced the RIPP`s low temperature F-T synthetic oil hydro-upgrading CFHL technology and its commercialization. The operating conditions on the effect of iso-hydrocracking reactions were explored. The results show that temperature, hydrogen pressure and space velocity significantly influence the iso-hydrocracking reaction, while the effect of H2/oil ratio is much less. The industrial application of CFHL shows that the cetane number of the hydrotreated diesel is 81 and the freezing point is below -20 ℃. The selectivity of iso-hydrocracking diesel exceeds 82.2%, while the cetane number of iso-hydrocracking diesel is 76 with a freezing point below -53 ℃. |
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Keywords: | F-T synthetic oil hydroupgrading isocracking industrialization |
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