freepeople性欧美熟妇, 色戒完整版无删减158分钟hd, 无码精品国产vα在线观看DVD, 丰满少妇伦精品无码专区在线观看,艾栗栗与纹身男宾馆3p50分钟,国产AV片在线观看,黑人与美女高潮,18岁女RAPPERDISSSUBS,国产手机在机看影片

正文內(nèi)容

13068噸每年苯一甲苯連續(xù)精餾裝置工藝設(shè)計(jì)_課程設(shè)計(jì)-展示頁(yè)

2024-09-08 19:03本頁(yè)面
  

【正文】 ..............................................................6 ..........................................................................................................7 ..............................................................................................................7 4 三、 精餾塔設(shè)計(jì) .......................................................................................................................7 工藝條件的確定 ...............................................................................................................7 ...............................................................................................7 ...............................................................................................................8 ...........................................................................................................9. 精餾塔物料恒算 ................................................................................................................9 ....................................................................................................................9 、塔底產(chǎn)品的平均摩爾量 ................................................................9 ....................................................................9 塔板數(shù)計(jì)算 ........................................................................................................................9 ...............................................................................................................9 XY曲線 ................................................................................................................9 Rmin........................................................................................................................10 ..............................................................................................................11 ..............................................................................................11 ET......................................................................................................11 ..........................................................................................................11 塔的精餾段操作工藝條件及計(jì)算 .................................................................................12 mP............................................................................................................12 ......................................................................................................12 ..............................................................................................13 ..........................................................................................................14 ..........................................................................................15 ..................................................................................................16 精餾塔的塔體工藝尺寸計(jì)算 .........................................................................................17 R1=.................................................................................................17 、液相負(fù)荷: ..............................................................................17 Vs和 Ls計(jì)算 ................................................................................................17 ..............................................................................................................18 ..........................................................................................19 、塔底空間 ......................................................................................................20 DH.....................................................................................................20 空間 B....................................................................................................20 1H ...................................................................................................20 2H .............................................................................................20. 、塔總高度 ...................................................................................................20 . F1 型浮閥塔板設(shè)計(jì) (以塔頂?shù)诙K為例) ......................................................20 .................................................................................................................22 ..................................................................................23 ..................................................................................................23 ..........................................................................23 ..................................................................................................................24 ..........................................................................................................24 ..............................................................................................24 5 ......................................................................................................24 ..............................................................................................................25 ..............................................................................................25 ..............................................................................................................26 液相負(fù)荷下限線 .............................................................................................26 ..........................................................................................................26 四、 裝置熱衡算確定熱換器(以一秒計(jì)算為例) .......................................................27 塔頂冷凝器
點(diǎn)擊復(fù)制文檔內(nèi)容
環(huán)評(píng)公示相關(guān)推薦
文庫(kù)吧 www.dybbs8.com
備案圖鄂ICP備17016276號(hào)-1