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北方煤矿矿井乏风余热回收换热器设计与试验

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在煤矿乏风余热利用领域,换热器乏风风阻利用不充分,导致传热系数通常较低。针对以上问题,基于乏风压降不高于200 Pa的限制条件,进行了煤矿乏风余热利用换热器的设计。提出了基于换热管压降约束的圆管顺排设计方法,分析获得了竖-横向管心距比为 5∶8 的圆管顺排结构的换热器;二次开发了基于Excel VBA的多变量寻优、多方案比对的自动化方案决策工具,实现了陕煤榆林红柳林煤矿二号风井换热器等 3 个换热器近百个设计方案的选优,并在柠条塔煤矿南翼风井和红柳林煤矿二号风井完成了建造安装。红柳林煤矿二号风井安装的圆管顺排换热器的数据采集与分析表明,与合阳煤矿方管堆砌换热器传热系数 17 W/(m2·K)相比,其传热系数提升了近 76%,达到 30 W/(m2·K);与红柳林煤矿原二号风井口锅炉年运行能耗 7。65×106 kWh相比,节约了近 81%,仅为 1。47×106 kWh。圆管顺排换热器年实际热回收量为 1。79×106 kWh,柠条塔煤矿南翼风井换热器年实际热回收量为 1。16×106 kWh。将圆管顺排换热器在北方地区所有煤矿广泛推广后,预计每年可回收热能 1。09×1010 kWh,减少 8。64×106 t二氧化碳、2。36×106 t碳粉尘、2。6×105 t二氧化硫、1。3×105 t氮氧化物的排放。
Design and Testing of Heat Exchanger for Waste Heat Recovery from Exhaust Air in Northern Coal Mines
In the field of waste heat utilization from exhaust air in coal mines,the insufficient utilization of the resistance of heat exchangers leads to generally low heat transfer coefficients.To address this issue,a design for a heat exchanger for waste heat recovery from exhaust air in coal mines was developed under the constraint that the pressure drop of the exhaust air does not exceed 200 Pa.A circular tube arrangement design method based on constraints of pressure drop in heat exchange tubes was proposed,and a heat exchanger with a vertical-horizontal tube spacing ratio of 5∶8 was analyzed.An automated decision-making tool for multi-variable optimization and multi-scheme comparison was further developed based on Excel VBA,enabling the selection of optimal design schemes from nearly a hundred design alternatives for three heat exchangers,including the heat exchanger for the No.2 air shaft of the Yulin Hongliulin Coal Mine in Shaanxi Province.Construction and installation were completed at the southern air shaft of the Ningtiaota Coal Mine and the No.2 air shaft of the Hongliulin Coal Mine.Data collection and analysis from the circular tube arrangement heat exchanger installed at the No.2 air shaft of the Hongliulin Coal Mine indicated that,compared to the heat transfer coefficient of 17 W/(m2·K)for the rectangular tube stacked heat exchanger at the Heyang Coal Mine,the heat transfer coefficient increased by nearly 76%,reaching 30 W/(m2·K).Additionally,compared to the annual energy consumption of 7.65×106 kWh for the original boiler at the No.2 air shaft of the Hongliulin Coal Mine,the system achieved a reduction of nearly 81%,resulting in only 1.47×106 kWh.The actual annual thermal recovery of the circular tube arrangement heat exchanger was 1.79×106 kWh,while the annual actual thermal recovery of the heat exchanger at the southern air shaft of the Ningtiaota Coal Mine was 1.16×106 kWh.With the widespread promotion of the circular tube arrangement heat exchanger across all coal mines in northern regions,it is expected that approximately 1.09×1010 kWh of thermal energy can be recovered annually,resulting in a reduction of emissions by 8.64×10⁶ tons of carbon dioxide,2.36×106 tons of carbon dust,2.6×105 tons of sulfur dioxide,and 1.3×105 tons of nitrogen oxides.

energy saving and emission reductioncoal mine exhaust airpressure drop limitwaste heat utilizationparameter optimization

罗小明、雒宵、杨成、摆志国、丁文捷

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宁夏大学机械工程学院,宁夏 银川 750021

节能减排 煤矿乏风 压降限值 余热利用 参数寻优

宁夏自然科学基金项目企业委托课题

2020AACO302222641

2024

宁夏工程技术
宁夏大学

宁夏工程技术

影响因子:0.185
ISSN:1671-7244
年,卷(期):2024.23(3)
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