立式氣液分離器計(jì)算

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,"立式重力氣液分離器計(jì)算

VerticalGravityGasLiquidSeparatorCaculation

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,"項(xiàng)目說(shuō)明：

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,1基礎(chǔ)數(shù)據(jù)BasicData,,,,,,,

,氣體介質(zhì)名稱(chēng),,,水蒸氣,,,,

,液體介質(zhì)名稱(chēng),,,冷凝水,,,,

,氣體流量Q,,,2000,m3/hour,,,

,液體流量W,,,50,Kg/hour,,,

,氣體密度ρg,,,0.75,Kg/m3,,,

,氣體黏度μg,,,1.25127E-05,Pa*s,,,

,液體密度ρl,,,1000,Kg/m3,,,

,液滴直徑d,,,200.00,μm,Or,2.00E-04,m

,,,,,,100－350μm,,

,2Re計(jì)算,,,,,,,

,0.001<Re<1,沉降速度Ut,,1.7391,m/s,Stoke定律,,

,,Re,,20.8486,,FALSE,,

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,1<Re<1000,沉降速度Ut,,0.8814,m/s,Allen定律,,

,,Re,,10.5664,,TRUE,,

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,1000<Re<100000,沉降速度Ut,,2.8132,m/s,牛頓定律,,

,,Re,,33.7245,,FALSE,,

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,最終確定Re,,,10.5664,,,,

,最終沉降速度Ut,,,2.8132,m/s,,,

,3汽液分離器結(jié)構(gòu)計(jì)算,,,,,,,

,3.1汽液分離器直徑D,,,,,,,

,Dmin,,,501.27,mm,圓整,550.00,mm

,,,,,,,0.55,m

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,3.2氣相段高度H1,,,,,,,

,系數(shù)C,,,1.2,,0.8－1.2,,

,H1,,,601.52,m/s,圓整,650.00,mm

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,3.3液位計(jì)可視高度H3,,,,,,,

,液位計(jì)可視范圍內(nèi)液體量控制時(shí)間t,,,10,min,5－10min,,

,H3,,,35.08,mm,圓整,36.00,mm

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,3.4液相段直邊高度H4,,,,,,,

,封頭容積V1,,,0.02,m3,標(biāo)準(zhǔn)橢圓封頭V=0.131D3,,

,被分離液體停留時(shí)間t,,,5,hour,2－8hour,,

,H4,,,960.53,m,圓整,961.00,mm

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,3.5入口管管徑d1,,,,,,,

,氣體在入口管內(nèi)流速U≤,,,36.51,m/s,ρl*U2≤1000Pa,,

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,入口管管徑d1,,,139.21,mm,圓整,150.00,mm

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,入口管底部至最高液面高度H2,,,150,mm,150－200mm,,

,3.6出口管管徑,,,,,,,

,氣體在出口管內(nèi)流速Ug≤,,,25,m/s,,,

,出氣管管徑d2,,,168.24,mm,圓整,200.00,mm

,液體在出口管內(nèi)流速Ul≤,,,1,m/s,0.5－1.5,,

,出液管管徑d3,,,133.01,mm,圓整,150.00,mm

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