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Optimal waste stream discharge temperature selection for dryer operations using thermo-economic assessment

机译:利用热经济评估为干燥机运行选择最佳的废气排放温度

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摘要

A typical drying process that has liquid and gas discharge streams has been analysed and the impact of selecting various combinations of soft temperatures on heat recovery, utility targets, area targets, capital cost and total cost is reported. The method is based on the plus-minus principle and traditional pinch analysis methods for utility, area and capital cost targeting with the modification of using a ΔT contribution. Results show that there is significant benefit from optimising discharge temperatures for total cost. To achieve minimum energy consumption and total cost, heat recovery from the dryer exhaust air is necessary. Heat recovery from liquid heat sources is shown to be preferable over gas streams due to a higher film coefficient resulting in less heat exchanger area and capital cost. There is also value in making process modifications, such as combining streams or removing small streams to be solely heated by utility, to reduce the number of network heat exchangers. For the best case, the discharge temperatures of the leaving streams are 18.0 °C for water condensate (liquid stream) and 52.4 °C for the exhaust air (gas stream).
机译:分析了具有液体和气体排放流的典型干燥过程,并报告了选择软温的各种组合对热回收,效用目标,面积目标,资金成本和总成本的影响。该方法基于加减法原理和针对公用事业,面积和资本成本目标的传统捏分析方法,并修改了使用ΔT的贡献。结果表明,为总成本优化排放温度具有显着优势。为了实现最低的能耗和总成本,必须从干燥机废气中回收热量。由于较高的薄膜系数导致较小的热交换器面积和较低的投资成本,因此从液体热源回收的热量显示出比气流更可取。在进行工艺修改(例如合并流或除去仅由公用事业加热的小流)以减少网络热交换器的数量方面,也具有价值。最好的情况是,对于水冷凝物(液体流),排出流的排出温度为18.0°C,对于废气(气体流),排出温度为52.4°C。

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