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["[" ["Apresse! Por favor,帮忙计算一下大概需要多大的换热面积??", "Fluxo de nitró gás 30 m3/h, "Temperatura 1 " "Pressão kPa" "Conteúdo de丁同 500 "经后降温至4 " "再经过二级深冷至- 5 " "把丁同都冷却下来" "还请帮忙计算一级、perímetro de换热器大概需要多少面积。" "换热器材质、循环水规格都没有" "换热器可以34" "循环水上水38回回水38" "计算" "溶剂含量很小" "主要是氮气" "这个工况打算采用什么传热元件?常规光管设计会比较大" "若考虑我这内展翅片换热的话" "还需要核实其他一些设计参数" "站内留个联系方式交流" "你你确定- 5 " "一定一定温度下丁同的饱和蒸气压是一定的吧? " "一定温度下饱和蒸汽压是一定7 " " " "但是混合气体中" " 5 " " " "绝对很低的" " " " "按组分含量计算出来为 4 " " " "低于饱和蒸汽压" " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " " kukpa kuk k

2020-09-10View Original

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氮气流量2000m3/h 温度100℃,压力10kpa,含10000mg/m3丁同,经过一级循环冷却水循环后降温至40℃左右,再经过二级深冷至-10℃左右,把丁同都冷却下来,还请帮忙算下一级、二级换热器大概需要多少面积。
Reply #22020-09-11
换热器材质、循环水规格都没有
Reply #32020-09-11
换热器可以304,循环水上水32 回水38计算
Reply #42020-09-12
溶剂含量很小,主要是氮气,这个工况打算采用什么传热元件?常规光管设计会比较大,若考虑我这内展翅片换热的话,还需要核实其他一些设计参数,站内留个联系方式交流。
Reply #52020-09-16
你确定-10℃可以冷却下来?氮气含量这么高,丁同含量非常低,丁同气体组分所占的分压也很低,对应的露点也很低,冷凝需要很低的温度,用ASPEN模拟的按含量20kg,需要-60℃才能冷下来19kg
Reply #62020-09-17
跟分压没关系吧? 一定温度下丁同的饱和蒸气压是一定的吧?
Reply #72020-09-17
一定温度下饱和蒸汽压是一定的,-10℃时的丁同的饱和蒸汽压是1.7kpa,但是混合气体中,110Kpa绝压压力下丁同的分压是很低的,按组分含量计算出来为0.4kpa,低于饱和蒸汽压,是不会冷凝的,如果是纯组分丁同,110Kpa肯定会冷凝,但是气相中含有大量的不凝性气体N2,就相应的降低了丁同的压力,要么继续降低温度,降低饱和蒸汽压,要么提高压力,达到-10℃下的饱和蒸汽压
Reply #82020-09-18
循环水显然冷凝不下来,冷冻水冷下来的可能性都不大,开始分压那么低,全冷下来直接不可能,深冷可能好一点。

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