| 50万t/a催化裂化装置MIP工艺改造总结 |
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| 引用本文： | 王共和,郝新宇.50万t/a催化裂化装置MIP工艺改造总结[J].企业技术开发,2011(17):39-40. |
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| 作者姓名： | 王共和 郝新宇 |
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| 作者单位： | 陕西延长石油(集团)有限责任公司永坪炼油厂; |
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| 摘 要： | 装置MIP工艺技术及其相关改造后,汽油烯烃降低了15个体积单位以上,可以达到30个体积单位以下,汽油的研究法辛烷值(RON)为88以上,装置汽柴油收率达到72%～73%,液化气收率达到12%～13%,比技改前都有所提高。
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| 关 键 词： | 催化裂化 MIP工艺 汽油烯烃 辛烷值 |
Summary on the MIP process modification of 500 000 tons/year catalytic cracking unit |
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| WANG Gong-he,HAO Xin-yu Co.,Ltd.,Yanchuan,Shaanxi ,China.Summary on the MIP process modification of 500 000 tons/year catalytic cracking unit[J].Technological Development of Enterprise,2011(17):39-40. |
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| Authors: | WANG Gong-he HAO Xin-yu Co Ltd Yanchuan Shaanxi China |
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| Institution: | WANG Gong-he,HAO Xin-yu (Yongping Refinery of Shaanxi Yanchang Petroleum(Group)Co.,Ltd.,Yanchuan,Shaanxi 717208,China) |
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| Abstract: | After the corresponding transformation of the equipment MIP process technic,the gasoline olefin has been reduced by over 15 volume units and it can reach to below 30 volume units,the Research Octane Number(RON)of petrol is over 88,the yield gasoline and diesel of the equipment achieves 72%～73%,and the liquid gas uield achieves 12%～13%,which are all improved than themselves before technical transformation. |
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| Keywords: | catalytic cracking MIP process gasoline olefin octane number |
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