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1溶药搅拌机池宽D池长池深H有效水深含PAC20%折叶浆式444.54混合搅拌机池宽D池长池深H有效水深444.542混合搅拌机池径D池深H有效水深含水98.5%的污泥桶44.53.53溶药搅拌机池宽D池长池深H有效水深含PAC20%折叶浆式1.31.34.54混合搅拌机池宽D池长池深H有效水深1.31.34.54太阳纸业混合搅拌机池径D池深H有效水深含水98.5%的污泥桶47.77.4太阳纸业混合搅拌机池径D池深H有效水深含水98.5%的污泥桶37.97.4桨叶外缘线速度v=1.0~5.0m/s桨叶直径d≥1/3×D线速度(m/s)转速(rpm)搅拌转速n(r/s)1.44.561.388335261.023138921功率准数NpA0.40143877127.234375桨叶直径d≥1/3×D线速度(m/s)转速(rpm)阻力系数C3(0.2~0.5)1.44.561.388335260.5桨叶直径d≥1/3×D线速度(m/s)转速(rpm)阻力系数C3(0.2~0.5)1.44.561.388335260.5桨叶直径d≥1/3×D线速度(m/s)转速(rpm)搅拌转速n(r/s)0.54.5171.88733872.864788979功率准数NpA0.62526402427.85138826桨叶直径d≥1/3×D线速度(m/s)转速(rpm)阻力系数C3(0.2~0.5)0.54.5171.88733870.5桨叶直径d≥1/3×D线速度(m/s)转速(rpm)阻力系数C3(0.2~0.5)1.5450.929581850.5桨叶直径d≥1/3×D线速度(m/s)转速(rpm)阻力系数C3(0.2~0.5)1476.394372770.5液体密度ρ(kg/m3)液体粘度υ(Pa.S)雷诺准数Re=d×d*n*ρ/υ功率准数Np12000.001142110897.1420.401438771BpEb1.3204507950.868750.3878111230.233333333液体密度ρ(kg/m3)角速度ω(rad/s)桨叶数Z层数e12006.42857142921液体密度ρ(kg/m3)角速度ω(rad/s)桨叶数Z层数e12006.42857142921液体密度ρ(kg/m3)液体粘度υ(Pa.S)雷诺准数Re=d×d*n*ρ/υ功率准数Np12000.00114753891.83660.625264024BpEb1.2633164840.8744082840.399781930.083333333液体密度ρ(kg/m3)角速度ω(rad/s)桨叶数Z层数e12001822液体密度ρ(kg/m3)角速度ω(rad/s)桨叶数Z层数e12005.33333333323液体密度ρ(kg/m3)角速度ω(rad/s)桨叶数Z层数e1200824搅拌功率N功率取2倍取最终功率(KW)2.773162875.5463257415.5桨叶宽度b(m)搅拌半径R(m)重力加速度g(m/s2)浆板折角θ0.2333333330.79.8145桨叶宽度b(m)搅拌半径R(m)重力加速度g(m/s2)浆板折角θ0.2333333330.79.8145搅拌功率N功率取2倍取最终功率(KW)0.5509389051.101877811.1桨叶宽度b(m)搅拌半径R(m)重力加速度g(m/s2)浆板折角θ0.0833333330.259.8145桨叶宽度b(m)搅拌半径R(m)重力加速度g(m/s2)浆板折角θ0.250.759.8145桨叶宽度b(m)搅拌半径R(m)重力加速度g(m/s2)浆板折角θ0.1666666670.59.8145sinθ搅拌功率N(KW)0.7071067813.155363838sinθ搅拌功率N(KW)功率取2倍取最终功率(KW)0.7071067813.1553638386.3107276767.5功率取1.5倍4.7330457575.5sinθ搅拌功率N(KW)0.7071067810.804939755sinθ搅拌功率N(KW)功率取2倍取最终功率(KW)0.7071067817.63202138215.2640427615sinθ搅拌功率N(KW)功率取2倍取最终功率(KW)0.7071067814.5226793379.04535867411
本文标题:搅拌机功率计算
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