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加氢装置运行全周期高压换热器垢阻计算与应用效果
引用本文:姚立松,穆海涛.加氢装置运行全周期高压换热器垢阻计算与应用效果[J].石油炼制与化工,2012,43(12):55-58.
作者姓名:姚立松  穆海涛
作者单位:中国石化青岛炼油化工有限责任公司
摘    要:采用MATLAB软件,跟踪计算某炼油厂蜡油加氢装置高压换热器运行3年来的垢阻。计算结果表明, 运行期间高压换热器结垢速率可控,运行末期总垢阻为1.2×10-3(m2.K)/W。生产中根据结垢速率逐渐将阻垢剂加注浓度由100 μg/g下调至25~35 μg/g,单周期节约阻垢剂成本约1 159万元。此外,基于ASPEN软件的换热器模块计算理论,构造采用ASPEN软件计算换热器垢阻的方法。

关 键 词:加氢装置  高压换热器  垢阻  换热系数
收稿时间:2012-04-09
修稿时间:2012-06-13

CALCULATION OF FOULING IN HIGH-PRESSURE HEAT EXCHANGER OF A HYDROGENATION UNIT FOR THE WHOLE OPERATION CYCLE AND APPLICATION EFFECT
Yao Lisong,Mu Haitao.CALCULATION OF FOULING IN HIGH-PRESSURE HEAT EXCHANGER OF A HYDROGENATION UNIT FOR THE WHOLE OPERATION CYCLE AND APPLICATION EFFECT[J].Petroleum Processing and Petrochemicals,2012,43(12):55-58.
Authors:Yao Lisong  Mu Haitao
Affiliation:(SINOPEC Qingdao Refining & Chemical Company,Qingdao,Shandong266500)
Abstract:With MATLAB software, the fouling of high-pressure heat exchanger in a gas oil hydrogenation unit was calculated throughout 3-year operation. The calculation results showed that the fouling rate of heat exchanger during operation was controllable; at the final stage of operation, the total resistance of scale was 1.2×10-3 (m2?K)/W. Based on the calculation results of fouling rate, the injection of scale inhibitor during operation was gradually reduced from 100 μg/g to 25-35μg/g, so that in this single operation cycle, the cost saving of scale inhibitor reached 11.59 MRMB. Besides, a fouling calculation method of heat exchanger based on ASPEN PLUS software and film coefficient theory was set up and the accuracy of this method was discussed as well.
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