石化技术与应用2024,Vol.42Issue(5) :364-370.DOI:10.19909/j.cnki.ISSN1009-0045.2024.05.0364

天然气脱硫脱碳和脱水工艺的节能模拟与优化

Energy-saving simulation and optimization of natural gas desulfurization and decarbonization and dehydration process

张生安 温欣 陈星 刘桂莲
石化技术与应用2024,Vol.42Issue(5) :364-370.DOI:10.19909/j.cnki.ISSN1009-0045.2024.05.0364

天然气脱硫脱碳和脱水工艺的节能模拟与优化

Energy-saving simulation and optimization of natural gas desulfurization and decarbonization and dehydration process

张生安 1温欣 2陈星 2刘桂莲1
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作者信息

  • 1. 西安交通大学 化学工程与技术学院,陕西 西安 710049
  • 2. 中国石油长庆油田分公司 第一采气厂,陕西 榆林 718500
  • 折叠

摘要

针对某 450 万m3/d天然气净化装置,利用Aspen HYSYS软件对天然气脱硫脱碳和脱水工艺进行建模,基于夹点技术分析天然气净化装置的换热网络节能潜力和不合理换热之处,基于灵敏度分析操作参数节能潜力,确定甲基二乙醇胺(MDEA)和三甘醇(TEG)溶剂的最佳循环量.结果表明:通过夹点技术分析,天然气净化装置换热网络的节能潜力为 307.80 kW,占现行加热公用工程和冷却公用工程消耗量的4.97%,5.65%;通过灵敏度分析,MDEA和TEG的循环量分别取 95.00,5.00 m3/h,操作参数优化的最大节能潜力为 2 527.95 kW,占现行加热公用工程和冷却公用工程消耗量的 40.86%,46.43%;通过换热网络改造和操作参数优化,装置最大节能量为 2 795.41 kW,占现行加热和冷却公用工程消耗量的 45.18%,51.34%;2 种节能优化方案可节省操作费用 144.72 万元/a,回收期为 0.174 a.

Abstract

For a natural gas purification plant with a capacity of 4.5 million m3/d,Aspen HYSYS soft-ware was used to model the natural gas desulfuriza-tion,decarbonization,and dehydration processes.Based on the pinch technology,the energy-saving potentials and unreasonable heat transfer of the heat exchange network of the process were analyzed.Based on the operational energy-saving potentials through sensitivity analysis,the optimal cycle flow rate of MDEA and TEG solvents could be deter-mined.The results showed that the energy-saving potentials of the natural gas purification plant′s heat exchange network was 307.80 kW,corresponding to 4.97%and 5.65%of the current heating and cooling utilities consumption.Through sensitivity analysis,the cycle flow rate of MDEA and TEG were 95.00 m3/h and 5.00 m3/h,and the maximum energy-saving potentials of operation parameter optimization was 2 527.95 kW,accounting for 40.86%and 46.43%of the current heating and cooling utilities consump-tion.According to the heat exchange network retrofit and the optimization of operating parameters,the maximum energy-saving values of the process was 2 795.41 kW,corresponding to 45.18%and 51.34%of the current heating and cooling utilities consump-tion.For the proposed two energy-saving optimiza-tion schemes,the annual operating cost savings was 1 447.2 thousand Yuan/a,and the recovery period was 0.174 a.

关键词

天然气净化/脱硫脱碳/脱水/节能分析/夹点技术/灵敏度分析/模拟优化

Key words

natural gas purification/desulfuriza-tion and decarbonization/dehydration/energy-sav-ing analysis/pinch technology/sensitivity analysis/simulation and optimization

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基金项目

国家自然科学基金资助项目(22078259)

出版年

2024
石化技术与应用
兰州石化公司石油化工研究院

石化技术与应用

CSTPCD
影响因子:0.491
ISSN:1009-0045
参考文献量8
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