【正文】 ………………………………………………………………………………………………………………………………………………………………………………………………………二、概述………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………三、罐體及傳熱裝置的設(shè)計……………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………四、攪拌裝置及附件設(shè)計…………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………五、傳動裝置設(shè)計及部分其它裝置選型設(shè)計……………………………………………………………………………………………………………………………………………………………………………… V帶設(shè)計…………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………六、剩余其它裝置選型設(shè)計…………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………七、設(shè)計總結(jié)………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………………八、公稱容積30 m3纈氨酸發(fā)酵罐設(shè)計裝配圖（附圖）九、參考文獻(xiàn)………………………………………………………………一、設(shè)計任務(wù)書公稱容積纈氨酸發(fā)酵罐設(shè)計項目名稱參數(shù)或指標(biāo)工作壓力罐內(nèi)夾套（蛇管）內(nèi)工作溫度罐內(nèi)≤121℃夾套（蛇管）內(nèi)≤150℃工作介質(zhì)罐內(nèi)輕微腐蝕性物料夾套內(nèi)蒸汽組別6裝料量（m3）26傳熱面積（m2）39攪拌器型式直葉圓盤渦輪攪拌器轉(zhuǎn)速/rmp200攪拌軸功率kw其它夾套換熱時，至少應(yīng)裝四塊擋板（根據(jù)需要設(shè)置）罐體材料16Mn?。谎b料系數(shù)?。煌L(fēng)管通風(fēng)比（通氣速率/發(fā)酵液體積）取 發(fā)酵液密度為，最大粘度；初始水溫.接管建議（推薦）：出料口冷凝液出口蒸汽進(jìn)口溫度計插口視鏡進(jìn)料口人孔手孔壓縮空氣入口，完成設(shè)計說明書。：罐的圓柱體部分體積和上下封頭體積之和