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首页> 外文期刊>Journal of Cleaner Production >Techno-economic and environmental evaluation of aldehyde-assisted chemical looping separation technology in coal-based and biomass-based ethylene glycol purification
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Techno-economic and environmental evaluation of aldehyde-assisted chemical looping separation technology in coal-based and biomass-based ethylene glycol purification

机译:基于煤基和生物质基乙二醇纯化的醛辅助化学循环分离技术的技术经济和环境评价

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摘要

The application of aldehyde-assisted chemical looping separation technology in the separation of ethylene glycol (EG) and 1,2-butanediol (1,2-BDO) azeotropic mixture from coal-based and biomass-based crude ethylene glycol refining process can relax the operation conditions of the 1,2-BDO removal column and EG refining column, save energy, increase the yield of EG and guarantee the quality of EG product. Formaldehyde (FA), acetaldehyde (AA) and prolyl aldehyde (PA) are feasible reactants and assessment of the opportunities and challenges of different aldehyde-assisted processes before industrial application is necessary. In this paper, the mole composition of EG and 1,2-BDO in the distillate from the 1,2-BDO removal column was optimized. FA, AA, and PA-assisted chemical-looping separation processes (FA-ACLSP, AA-ACLSP and PA-ACLSP) were developed and simulated to provide fundamental data for the techno-economic and environmental evaluation. Results show that PAACLSP has significant economic and technical advantages (the yield of polyester-grade EG is 94.42% and the internal rate of return is 137.28%). However, it suffers from high potential environmental impacts (PEIs) and liquid discharge (the input and output PEIs and liquid discharge per kilogram of EG per hour are 4.87, 2.95 and 0.538). AA-ACLSP has zero liquid discharge and is truly environmentally friendly. FA-ACLSP faces a tough challenge in industrial application because of the large energy consumption and waste discharge (the internal rate of return is 4.63% and the liquid discharge per kilogram of EG per hour is 4.161). Finally, the discussion and analysis of different processes are illustrated to guide commercialization.
机译:醛辅助化学循环分离技术在乙二醇(例如)和1,2-丁二醇(1,2-Bdo)共沸混合物中的分离在煤基和生物质基粗乙二醇精炼过程中的分离可以放松1,2-BDO去除柱和例如炼油柱,节省能量,增加EG的产量并保证产品的质量,增加了炼油柱的操作条件。甲醛(Fa),乙醛(AA)和脯氨酰醛(PA)是可行的反应物,并且在工业申请之前对不同醛辅助过程的机会和挑战的评估。在本文中,优化了来自1,2-BDO去除塔中馏出物中的摩尔组合物和1,2-BDO的优化。开发和模拟FA,AA和PA辅助化学环循环分离过程(FA-ACLSP,AA-ACLSP和PA-ACLSP),以提供技术经济和环境评估的基本数据。结果表明,PAACLSP具有显着的经济和技术优势(聚酯级的产量为94.42%,内部返回率为137.28%)。然而,它受到高潜在的环境影响(PEI)和液体放电(每小时每千克的输入和输出PEI和液体放电是4.87,2.95和0.538)。 AA-ACLSP具有零液体排放,真正环保。由于大量的能量消耗和废物放电,FA-ACLSP面临着工业应用中的艰难挑战(内部回报率为4.63%,每小时每小时的液体放电为4.161)。最后,说明了不同过程的讨论和分析以指导商业化。

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  • 来源
    《Journal of Cleaner Production 》 |2021年第1期| 127675.1-127675.12| 共12页
  • 作者单位

    Tianjin Univ Sch Chem Engn & Technol Natl Engn Res Ctr Distillat Technol Collaborat Innovat Ctr Chem Sci & Engn Tianjin Tianjin 300072 Peoples R China|Univ Surrey Dept Chem & Proc Engn Guildford GU27XH Surrey England;

    Tianjin Univ Sch Chem Engn & Technol Natl Engn Res Ctr Distillat Technol Collaborat Innovat Ctr Chem Sci & Engn Tianjin Tianjin 300072 Peoples R China;

    Tianjin Univ Sch Chem Engn & Technol Natl Engn Res Ctr Distillat Technol Collaborat Innovat Ctr Chem Sci & Engn Tianjin Tianjin 300072 Peoples R China;

    Tianjin Univ Sch Chem Engn & Technol Natl Engn Res Ctr Distillat Technol Collaborat Innovat Ctr Chem Sci & Engn Tianjin Tianjin 300072 Peoples R China;

    Univ Surrey Dept Chem & Proc Engn Guildford GU27XH Surrey England;

    Tianjin Univ Sch Chem Engn & Technol Natl Engn Res Ctr Distillat Technol Collaborat Innovat Ctr Chem Sci & Engn Tianjin Tianjin 300072 Peoples R China;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Ethylene glycol; Techno-economic; Environmental; Chemical-looping; 1; 2-Butanediol;

    机译:乙二醇;技术经济;环境;化学环;1;2-丁二醇;

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