首页|重芳烃轻质化精馏系统操作压力的优化

重芳烃轻质化精馏系统操作压力的优化

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精馏是化工中重要的工艺单元,其能耗在装置中占据一定的比例.简述压力对精馏工艺的影响,通过适当调节精馏压力达到节能降耗目的.以国内某重质芳烃轻质化开发项目的脱C6/C7塔为例,通过提高脱C6/C7塔压力由0.1 MPa(g)至1.05 MPa(g),提高塔顶冷凝温度,精馏系统可多副产1.20 MPa(g)蒸汽,进而提高经济效益.从整个精馏系统进行考察能源消耗情况,利用化工模拟软件ASPEN进行核算.经计算表明,脱C6/C7塔压力优化后,系统可多副产1.20 MPa蒸汽11.53 t/h,年节约运行费用637.33万元,投资增加221.7万元,经济效益十分显著.
Optimization of operating pressure in heavy aromatics lightening distillation system
Distillation is an important unit operation in the chemical industry,and its energy consumption accounts for a significant proportion of the plant's total.Briefly describes the impact of pressure on the distillation process and how adjusting the distillation pressure appropriately can achieve the goal of energy saving and consumption reduction.Taking the C6/C7 removal tower of a domestic heavy aromatics lightening development project as an example,by increasing the pressure of the C6/C7 removal tower from 0.1 MPa(g)to 1.05 MPa(g)and raising the condenser temperature at the top of the tower,the distillation system can produce an additional 1.20 MPa(g)steam,thereby improving economic benefits.The energy consumption of the entire distillation system is examined,and the chemical simulation software ASPEN is used for accounting.Calculations show that after the pressure optimization of the C6/C7 removal tower,the system can produce an additional 1.20 MPa steam at a rate of 11.53 t/h,saving operational costs of 6.373 3 million yuan per year,with an increase in investment of 2.217 million yuan,resulting in very significant economic benefits.

distillation separation systemlightening of heavy aromatic hydrocarbonsenergy-saving optimizationASPEN

刘亭引

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福建福海创石油化工有限公司,福建 漳州 363216

精馏分离系统 重质芳烃轻质化 节能优化 ASPEN

2024

节能
辽宁省科学技术情报研究所 辽宁省能源研究会

节能

影响因子:0.295
ISSN:1004-7948
年,卷(期):2024.43(6)
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