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反應器直徑和高度的計算

來(lái)源: 時(shí)間:2012-11-21 14:19:40 瀏覽次數:

1、長(cháng)徑比對攪拌功率的影響:在轉速不變的情況下,PD5(其中D---攪拌器直徑,P——攪拌功率),P隨釜體直徑的增大,而增加很多,減小長(cháng)徑比只能無(wú)謂地損耗一些攪拌功率。因此一般情況下,長(cháng)經(jīng)比應選擇大一些。

在已知攪拌器的操作容積后,首先要選擇罐體適宜的長(cháng)徑比(H/Di),以確定罐體直徑和高度。選擇罐體長(cháng)徑比主要考慮以下兩方面因素:

    1、長(cháng)徑比對攪拌功率的影響:在轉速不變的情況下,PD5(其中D---攪拌器直徑,P——攪拌功率),P隨釜體直徑的增大,而增加很多,減小長(cháng)徑比只能無(wú)謂地損耗一些攪拌功率。因此一般情況下,長(cháng)經(jīng)比應選擇大一些。
    2、長(cháng)徑比對傳熱的影響:當容積一定時(shí),H/Di越高,越有利于傳熱。
    長(cháng)徑比的確定通常采用經(jīng)驗值.即表1

表1  罐體長(cháng)徑比經(jīng)驗表

種類(lèi)

罐體物料類(lèi)型

H/Di

一般攪拌罐

液—固或液—液相物料

1--1.3

氣—液相物料

1--2

發(fā)酵罐類(lèi)

1.7--2.5

 

在確定了長(cháng)徑比和裝料系數之后,先忽略罐底容積,此時(shí)

        

                                (3—9)

將上式計算結果圓整成標準直徑,代入下式得出罐體高度

       

                          (3—10)

其中  v--封頭容積

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