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1,4-丁二醇生产工艺及其换热网络优化

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针对混合C5原料联产顺酐和苯酐的1,4-丁二醇生产工艺存在能耗高的缺陷,通过对生产工艺的模拟,并采用夹点技术,分析和优化了 1,4-丁二醇生产工艺的能耗,并进一步对换热网络进行集成和优化,达到了节能效果.研究结果表明:节省热公用工程10 239.3 kW和冷公用工程21 683.2 kW,换热单元数由原来44个减少为32个,降低了设备成本.
Optimization of the production process and heat exchange network of 1,4-butanediol
For the defect of high energy consumption in the process of 1,4-butanediol co-producing maleic anhydride and phthalic anhydride using mixed C5 as raw materials,the energy consumption of the 1,4-butanediol production process was analyzed and optimized through the simulation and the pinch point technology,and the heat exchange network was further integrated and optimized to achieve energy-saving effects.The research results showed that 10 239.3 kW of heat utility and 21 683.2 kW of cold utility were saved,and equipment costs were decreased because the number of heat exchange units was reduced from 44 to 32.

1,4-butanediolenergy integrationheat exchange network

张悦、郝家悦、胡泽汇、邓陈陈、穆罕穆德·亚新、李书珍

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上海应用技术大学化学与环境工程学院,上海 201418

白沙瓦大学化学科学研究所,白沙瓦25120

1,4-丁二醇 能量集成 换热网络

2024

应用技术学报
上海应用技术学院

应用技术学报

影响因子:0.195
ISSN:2096-3424
年,卷(期):2024.24(4)