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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Optimal design of process configuration for a cascade coproduction system to produce furnace off-gas-based clean fuels and chemicals
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Optimal design of process configuration for a cascade coproduction system to produce furnace off-gas-based clean fuels and chemicals

机译:级联联合生产系统的工艺配置的优化设计,以生产基于炉废气的清洁燃料和化学品

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摘要

Previous studies have shown that methanol, dimethyl ether and fuel oil are the products of the conversion of furnace off-gas. A coproduction system for clean fuel and chemicals was studied in this paper to find a proper way to use furnace off-gas. First, a new perspective on the chemical cascade coproduction system was proposed. The effective atom yield and process exergy loss were integrated to evaluate the material conversion and energy utilization of the coproduction system. Four schemes with different process configurations were later built to produce methanol, dimethyl ether and fuel oil from furnace off-gas. The effects of the configuration and basic processes on the material conversion and energy utilization were analyzed with the evaluation method of the chemical cascade coproduction system. The work shows that the differences in the effective atom yield and exergy loss are attributable to the process configurations, and a suitable approach is proposed to consider the exergy loss and effective atom yield of the process, especially the latter, which is more meaningful for comparison than carbon emissions. The exergy loss, effective atom yield, energy consumption and carbon emission of the optimal scheme are calculated to be 128.86 kW, 0557, 592.15 kW and 238.09 kg CO2/h, respectively. (C) 2016 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:先前的研究表明,甲醇,二甲醚和燃料油是炉废气转化的产物。本文研究了一种用于清洁燃料和化学药品的联合生产系统,以找到使用炉窑废气的正确方法。首先,提出了有关化学级联联产系统的新观点。集成了有效原子产率和过程本能损失,以评估联产系统的材料转化和能量利用。后来建立了四个具有不同工艺配置的方案,以从炉废气中生产甲醇,二甲醚和燃料油。通过化学级联联产系统的评价方法,分析了结构和基本工艺对材料转化和能量利用的影响。研究表明,有效原子产率和有效能损失的差异可归因于工艺流程的配置,提出了一种适当的方法来考虑过程的有效能损失和有效原子产率,尤其是后者,这对于比较是有意义的。比碳排放。计算得出的最佳方案的火用损失,有效原子产率,能源消耗和碳排放分别为128.86 kW,0557、592.15 kW和238.09 kg CO2 / h。 (C)2016化学工程师学会。由Elsevier B.V.发布。保留所有权利。

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