| 120万吨/年柴油加氢精制装置系统完善改造 |
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| 引用本文： | 周景伦,安进堂. 120万吨/年柴油加氢精制装置系统完善改造[J]. 石油化工应用, 2009, 28(5): 77-79 |
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| 作者姓名： | 周景伦 安进堂 |
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| 作者单位： | 中国石油兰州石化分公司炼油厂,甘肃,兰州,730060 |
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| 摘 要： | 介绍兰州石化公司炼油厂1.2Mt/a柴油加氢精制装置建成后生产中所发现的问题,针对这些问题进行技术改造,在改动不大的原则下,合理利用了原装置的大部分工艺设备。改造后,基本解决了分馏系统热源不足问题,为高压分离器液面控制提供了可靠依据,使装置运行周期大大延长。装置经过近两年的平稳运行表明技术改造是成功的。
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| 关 键 词： | 分馏 技术改造 高压分离器 运行周期 |
System perfect reformation of 1.2Mt/a diesel hydrogenation is refined to equip |
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| ZHOU Jinglun,AN Jintang. System perfect reformation of 1.2Mt/a diesel hydrogenation is refined to equip[J]. Petrochemical Industry Application, 2009, 28(5): 77-79 |
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| Authors: | ZHOU Jinglun AN Jintang |
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| Affiliation: | Oilrefinary Processing Plant of Lanzhou Petrochemical Comprany;PetroChina;Lanzhou Gansu 730060;China |
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| Abstract: | Introduce the orchid state petrochemical company the refined device of the diesel hydrogenation of the oil refinery 1.2 Mt/a is to these problems built up young man to produce a medium problem discover,carry on a technique reformation,is change to move under the not great principle,the reasonable made use of big and parts of craft equipmentses of original equipment.After reform,it was basic to solved separately the Liu system hot source not enough problem and separated the machine liquid noodles control to ... |
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| Keywords: | fractionation technological transformation high pressure separator operational cycle |
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