摘要
常减压装置是原油深度加工的基础,同时也是炼油企业用能大户。针对国内某企业的常减压装置,应用流程模拟软件Aspen HYSYS,建立装置的换热网络模型。以加工原油性质、初馏塔、常压塔、减压塔模拟过程参数及常减压装置对产品质量的要求作为换热网络调整的基础参数,利用Aspen Pinch软件,对装置原有换热网络进行夹点分析,根据原油常减压装置内部冷、热物流特点,分析装置用能瓶颈,得出换热网络初底原油的最高理论换热终温。按照消除原换热物流跨夹点传热、中高温位热源多次合理利用、调整换热效率偏低的设备、现有设备布置变动小、投资省的原则,对换热网络进行改造优化。通过换热流程优化调整,初底油进常压加热炉温度由原来的278℃提高到288℃;降低常压炉加热负荷及燃料消耗,可节省加热炉负荷约60×10~4kcal/h,装置能耗降低约0.7kg标油/t,折合每年创造效益约126万元。
The atmospheric and vacuum unit is basic equipment in crude oil deep processing and is also a ma-jor energy consumer in a refinery.Technicians used the process simulation software,Aspen HYSYS,to establish a heat exchanger network model for a domestic oil refiner ′ s atmospheric and vacuum unit.Using crude oil properties,primary tower,atmospheric tower and vacuum tower simulation process parameters and the require-ments of the atmospheric and vacuum unit on product quality as the basic parameters used in the adjustment of the heat exchanger network as well as the Aspen Pinch software,they conducted a pinch point analysis for the existing heat exchanger network of the atmospheric and vacuum unit.Based on the characteristics of the unit′ s internal cold and hot streams,these technicians analyzed the bottlenecks affecting the efficient use of energy in the unit and calculated the highest theoretical end temperature for heat exchange for initial bot-toms in the heat exchanger network.Based on the principles of eliminating original cross-pinch point heat transfer of heat exchange streams,utilizing high and medium-temperature heat sources in a repeated and rational manner,replacing equipment with low heat exchange efficiencies and minimizing changes in equipment arrangement and capital investment,they optimized the heat exchanger network.As a result of the optimization of the heat exchange process,the temperature of initial bottoms entering the atmospheric heating furnace has increased to 288℃ from 278℃.As a result of the declines in the heating load on the atmospheric furnace and fuel consumption,heating furnace load savings could reach around 60 ×10~4kcal/h and the atmospheric and vacuum unit′ s energy use could drop some 0.7kg of oil equivalent per ton.Annual energy savings reach about 1.26 million yuan.
作者
张继东
孟硕
张海滨
田文爽
Zhang Jidong Meng Shuo Zhang Haibin Tian Wenshuang(CNOOC Energy Conservation ＆ Pollution Monitor Center,Tianjin 30045)
出处
《中外能源》
CAS
2017年第1期90-96,共7页
Sino-Global Energy
关键词
常减压装置
夹点技术
换热网络
优化
atmospheric and vacuum unit
pinch-point technology
heat exchanger network
optimization
作者简介
张继东，硕士，工程师，2014年毕业于中国石油大学（北京）化学工程与工艺专业，主要从事石油石化领域的节能减排、炼油化工装置的模拟与优化工作。E-mail：zhangjd13@cnooc．com．cn
