4.7 Article

Industrial furnaces with thermochemical waste-heat recuperation by coal gasi fi cation

期刊

ENERGY
卷 221, 期 -, 页码 -

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.energy.2021.119864

关键词

Coal gasification; Thermochemical recuperation; Synthesis gas; Low heating value

资金

  1. Russian Science Foundation [191900327]

向作者/读者索取更多资源

A thermochemical waste-heat recuperation (TCR) system by coal gasification was analyzed through thermodynamic analysis, with heat recuperation degree (HRD) used as an efficiency criterion. The study found heat deficit at specific temperatures, leading to the introduction of gross HRD and net HRD to address this issue.
A thermochemical waste-heat recuperation (TCR) system by coal gasification is considered. Two concepts of TCR were analyzed: gasification with steam and gasification with the steam-flue gas mixture. To determine the effectiveness of using TCR systems by coal gasification, a thermodynamic analysis of the gasification process was carried out in the wide ranges of the operation parameters: a temperature range is 200-1200 degrees C, the steam-to-carbon (S/C) ratio is 0.25-2.0. The thermodynamic analysis has been realized via Aspen HYSYS software. To evaluate the effectiveness of the thermochemical recuperation systems by coal gasification, the heat recuperation degree (HRD) was used as an efficiency criterion of such systems. The algorithm of the calculation of HRD is proposed. It was found in the temperature range up to 700-800 degrees C HRD increases monotonically and reaches its maximum value at 720 degrees C for S/C = 1.0, 810 degrees C at S/C = 0.5 and 930 degrees C at S/C = 0.25. There is a heat deficit when S/C above 1.0 in the inlet reaction mixture. Thus, two types of HRD were introduced e gross HRD and net HRD. The gross HRD shows the relation between the total recovered heat and heat of exhaust gases. The net HRD shows the relation between the total recovered heat without the enthalpy of residual steam and heat of exhaust gases. The maximum net HRD of 0.97 can be achieved at S/C = 1.0 at a temperature of 800 degrees C. The heat transformation coefficient (HTC) was analyzed. An increase in the S/C ratio leads to an increase in HTC. With an increase in the S/C ratio above the stoichiometric ratio, HTC increases slightly. When the S/C ratio increases, the specific low heating value of synthesis gas (per 1 kg of syngas) decreases. (c) 2021 Elsevier Ltd. All rights reserved.

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