taifun 发表于 2023-11-17 00:22:05

请师傅们帮忙检查下HTRI文件

本帖最后由 taifun 于 2023-11-29 18:31 编辑

附一份单壳程4管程油水换热器的HTRI文件,我自己做的结果是换热能力和壳程流速与厂家报告相差甚远。
请师傅帮忙检查完善下,看看与报告不符的原因是什么,谢谢!
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yinquanyu12010 发表于 2023-11-17 00:22:05

{:1110_553:}

dolphin_star 发表于 2023-11-17 00:22:05

能不能把单位换成国际单位呀,这看起来太费劲了

yangtzeliu 发表于 2023-11-17 00:22:05

我看了一下,最大的差别是管数量差很多

feifei飞 发表于 2023-11-17 00:22:05

隔板分布不均,换热管太少,管束间隙等等,很多问题,建议看看软件教程

ftecagan247 发表于 2023-11-17 00:22:05

{:1110_549:}{:1110_553:}

taifun 发表于 2023-11-17 00:22:05

供应商是ITT,给的报告是英文英制单位。

taifun 发表于 2023-11-17 00:22:05

yangtzeliu 发表于 2023-11-17 10:55
我看了一下,最大的差别是管数量差很多

报告中管数量是80啊。

taifun 发表于 2023-11-17 00:22:05

feifei飞 发表于 2023-11-17 11:10
隔板分布不均,换热管太少,管束间隙等等,很多问题,建议看看软件教程

换热管数量与报告一样都是80,管束间隙也是按报告设定的,29/64英寸,隔板间距4英寸,距离入口6英寸,设置上都是按照报告的数据。
换热能力差异主要是在壳程流速上相差很大,报告的壳程流速是2.5英尺/秒,而HTRI计算出的壳程流速差个数量级。

taifun 发表于 2023-11-17 00:22:05

dolphin_star 发表于 2023-11-17 09:17
能不能把单位换成国际单位呀,这看起来太费劲了

主要是想和英制报告数据做个对比。

feifei飞 发表于 2023-11-17 00:22:05

taifun 发表于 2023-11-18 09:17
换热管数量与报告一样都是80,管束间隙也是按报告设定的,29/64英寸,隔板间距4英寸,距离入口6英寸,设 ...

你自己画图布下80根管子看看
页: [1]
查看完整版本: 请师傅们帮忙检查下HTRI文件