| 200万吨/年加氢精制装置运行总结 |
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| 引用本文： | 郑佰龙,张海峰.200万吨/年加氢精制装置运行总结[J].广州化工,2011,39(16):152-153,197. |
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| 作者姓名： | 郑佰龙 张海峰 |
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| 作者单位： | 中国石油辽阳石化公司炼油厂,辽宁辽阳,111003 |
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| 摘 要： | 装置开车经历几个重要阶段后进入装置的试生产阶段,经过两个月的运行调试装置达到平稳运行。对装置负荷情况、设备运行情况进行考核。通过考核情况可以确认装置设备能满足100%负荷生产的要求,汽提塔、分馏塔基本达到设计参数,满足实际生产要求。
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| 关 键 词： | 加氢精制 催化剂 柴油 装置 运行 |
Summary on the Operation of 2 Mt/a Hydrogenation Unit |
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| ZHENG Bai-long,ZHANG Hai-feng.Summary on the Operation of 2 Mt/a Hydrogenation Unit[J].GuangZhou Chemical Industry and Technology,2011,39(16):152-153,197. |
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| Authors: | ZHENG Bai-long ZHANG Hai-feng |
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| Affiliation: | (Petrochina Liaoyang Petrochemical Company Refinery,Liaoning Liaoyang 111003,China) |
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| Abstract: | Through several important stages,the device into pre-production stage,it ran smoothly after two months.The loads of equipment and operation were assessed.It can confirmed that the device equipments ability satisfy 100% burden produce of request and the vapor lift tower and cent the Liu tower attained design parameter basically,and satisfied actual produce request. |
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| Keywords: | hydrogenation catalyst diesel unit operation |
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