强化精馏乙醇生产过程中的回收热交换

L. Hariev, I. Riabova
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摘要

传统上,乌克兰生产的大量乙醇用于满足食品、制药和燃料工业的需求。乌克兰拥有生产乙醇的重要原材料基地,这使得该行业成为国家经济中最有前景的行业之一。降低生产成本是乙醇生产商在国内外市场上良性竞争的必要条件。通过对现有企业进行节能现代化改造,降低生产的具体能源成本,为特定行业的发展提供了动力。如今,降低乙醇生产特定能源消耗的方法之一是热流集成法,该方法基于掐头去尾分析,不需要对生产进行全面改造。获取工艺流程数据的依据是乌克兰一家酒精企业关于乙醇主要馏分集中蒸馏装置的设 备和工艺方案的规范性文件以及该装置的能源审计报告。为了对现有工艺进行热集成,选择了乙醇集中蒸馏装置的四个塔:发酵和净化、精馏和甲醇。对装置中这些塔的热平衡和物料平衡进行了计算。为了最大限度地发挥工艺流程的能量潜力,采用了夹层设计原则,并设计了网格图。为了优化热能回收,选择了 ΔТmin - 10 ºС。这就需要使用高能效的热交换设备。在选定的技术流程中,外部公用设施的使用量大幅减少(冷水减少 17.2%,热水减少 12.8%),而且项目的投资回收期较短(约六个月),因此采用这种方法解决问题是合理的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
INTENSIFICATION OF RECOVERY HEAT EXCHANGE IN RECTIFIED ETHYL ALCOHOL PRODUCTION PROCESSES
Traditionally, a lot of ethyl alcohol is produced in Ukraine for the needs of the food, pharmaceutical, and fuel industries. Ukraine has a significant raw material base for the production of ethyl alcohol, which makes this industry one of the most promising for the country's economy. A reduction in the cost of production is a necessary condition for healthy competition of ethanol producers on the domestic and foreign markets. Providing an impetus for the development of the specified industry is the reduction of specific energy costs for production through energy-efficient modernization of existing enterprises. Today, one of the methods of reducing the specific energy consumption for the production of ethyl alcohol is the method of integration of heat flows, which is based on pinch analysis and does not require a total reconstruction of the production. Obtaining data on technological flows was carried out on the basis of the regulatory documentation of the equipment and technological scheme of the installation of the centralized distillation of the main fraction of ethyl alcohol and the report on the energy audit of this installation, which was carried out at one of the alcohol enterprises of Ukraine. For the thermal integration of the existing process, four columns of the centralized ethanol distillation unit were chosen: fermentation and purification, rectification and methanol. The thermal and material balances of these columns of the installation were calculated. To maximize the energy potential of technological flows, the principles of pinch design were used and a grid diagram was designed. To optimize heat energy recovery, ΔТmin – 10 ºС was chosen. This led to the need to use energy-efficient heat exchange equipment. A significant reduction in the use of external utilities (cold by 17.2 % and hot by 12.8 %) for the selected technological flows and the short payback period of the project (about six months) make it reasonable to use this kind of solution to the problem.
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