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多周期常减压蒸馏装置换热网络用能变化与柔性优化

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常减压蒸馏装置能耗在整个炼油厂中最高,优化其换热网络是节能的有效手段.考虑到所加工油品会发生变化,以往针对特定原油设计的换热网络在处理其他原油时表现不再最优.提出一种多周期柔性优化方法:首先对不同原油周期进行流程模拟,随后模拟现行换热网络,辨识夹点位置偏移,发现不合理用能发生位置,通过改变管路结构并调节换热匹配,提高换热网络柔性,消除部分共有的跨夹点传热.在某炼油厂的应用结果表明,多周期柔性设计可在周期1、周期2、周期3、周期4分别节约1 421,880,3 842,3 421 kW的加热炉热负荷和等量的冷却负荷.对多周期换热网络用能变化规律的深入研究和柔性设计,可为炼油厂节能降耗做出更大贡献.
ENERGY VARIATION AND FLEXIBILITY OPTIMIZATION OF MULTI-PERIOD ATMOSPHERIC AND VACUUM DISTILLATION UNIT HEAT EXCHANGER NETWORK
The energy consumption of atmospheric and vacuum distillation unit is the highest in refinery,and the optimization of heat exchanger network is an effective means of energy saving.Given the variability of crude oils,heat exchanger network that was previously designed for specific crude oils is no longer optimal for other crude oils.A multi-period flexible optimization method was proposed:firstly,Aspen Plus was used to simulate the process of different crude oil periods;then pinch design method was adopted and Aspen Energy Analyzer was used to simulate the current heat exchanger network,identify the pinch position offset,find the unreasonable energy use,and eliminate some common cross-pinch heat transfer by changing the pipeline structure and adjusting the heat transfer matching.The application results in a refinery showed that the multi-period flexible design could save 1 421,880,3 842 and 3 421 kW of heating furnace heat load and equivalent cooling water heat load in period 1,2,3 and 4,respectively.Further study and flexible design of multi-period heat exchanger network can make greater contribution to energy saving and consumption reduction in refineries.

atmospheric and vacuum distillationprocess simulationheat exchanger networkpinching techniquemulti-periodflexibilityoptimization

刘泽坤、刘绍东、赵卫东、王彧斐

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中国石油大学(北京),北京 102249

中国石油塔里木油田分公司

常减压蒸馏 流程模拟 换热网络 夹点技术 多周期 柔性 优化

国家自然科学基金国家自然科学基金

2202281622078358

2024

石油炼制与化工
中国石油化工股份有限公司石油化工科学研究院

石油炼制与化工

CSTPCD北大核心
影响因子:0.825
ISSN:1005-2399
年,卷(期):2024.55(6)
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