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设计〔论文〕题目:
列管式换热器的设计
目录
1前言························································3
2设计任务及操作条件··············································3
3列管式换热器的工艺设计·········································3
3.1换热器设计方案确实定··········································3
3.2物性数据确实定················································4
3.3平均温差的计算················································4
3.4传热总系数K确实定············································4
3.5传热面积A确实定··············································6
3.6主要工艺尺寸确实定············································6
3.6.1管子的选用·················································6
3.6.2管子总数n和管程数Np确实定··································6
3.6.3校核平均温度差?tm及壳程数Ns·································7
3.6.4传热管排列和分程方法········································7
3.6.5壳体内径··················································7
3.6.6折流板····················································7
3.7核算换热器传热能力及流体阻力··································7
热量核算···················································7
3.7.2换热器压降校核·············································9
4列管式换热器机械设计············································10
4.1壳体壁厚的计算················································10
4.2换热器封头选择················································10
4.3其他部件······················································11
5课程设计评价·····················································11
5.1可靠性评价····················································11
5.2个人感想······················································11
6参考文献··························································11
附表换热器主要结构尺寸和计算结果·······························12
1前言
换热器〔英语翻译:heatexchanger〕,是将热流体的局部热量传递给冷流体的设备,又称热交换器。换热器是化工、石油、动力、食品及其它许多工业部门的通用设备,在生产中占有重要地位。在化工生产中换热器可作为加热器、冷却器、冷凝器、蒸发器和再沸器等,应用更加广泛。换热器种类很多,但根据冷、热流体热量交换的原理和方式根本上可分三大类即:间壁式、混合式和蓄热式。
列管式换热器工业上使用最广泛的一种换热设备。其优点是单位体积的传热面积、处理能力和操作弹性大,适应能力强,尤其在高温、高压和大型装置中采用更为普遍。列管式换热器主要有以下几个类型:固定管板式换热器、浮头式换热器、U形管式
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