冒泡压力与精度的换算
乙二醇张异丙醇张Po mm水柱力温度修正力高H PaD平 μmDmax μm冒泡压最大孔径力S dyn/cmS dyn/cmS dyn/cm标准下压力平均孔径μμ75023.405℃22.861.16142.30151.07235023.0410℃22.45215.7840.3342.82380022.7815℃22.2359.0524.2425.73110022.2720℃21.799.0487.8893.29440021.8625℃21.3434.9520.0121.2490021.4530℃20.982.20105.88112.41160021.0435℃20.5157.4355.2858.69380021.2432℃20.7385.0622.6023.99160021.0934℃20.55157.0455.4258.83160021.6527℃21.1152.9556.9060.41不同温度
下异丙醇表面张力和密度：
ＴＡＰ2Ｔ
Ａ Ｐ
℃DYN/CM3g/CM3℃
DYN/CM2g/CM3
５ ２２．８００．７９８０２３ ２１．４
０．７８５５ ６ ２２．７００．７９７４２４ ２１．３５０．７８４５
７ ２２．６５０．７９６７２５ ２１．３００．７８３８ ８ ２２．６００．７９６０２６ ２１．２００．７８３０ ９ ２２．５００．７９５５２７ ２１．１００．７８２０ １０ ２２．４５０．７９５０２８ ２１．０００．７８１２ １１ ２２．４００．７９４５２９ ２０．９５０．７８００ １２ ２２．３５０．７９４０３０ ２０．９００．７７９０ １３ ２２．３００．７９３５３１ ２０．８００．７７８５ １４ ２２．２００．７９３０３２ ２０．７００．７７７５ １５ ２２．１００．７９２５３３ ２０．６００．７７６８
１６ ２２．０００．７９１５３４ ２０．５５０．７７６１ １７ ２１．９５０．７９１１３５ ２０．５００．７７５５ １８ ２１．９００．７９０１３６ ２０．４５０．７７５０ １９ ２１．８００．７８９５３７ ２０．４００．７７４５ ２０ ２１．７００．７８８５３８ ２０．３００．７７４１ ２１ ２１．６００．７８７５３９ ２０．２００．７７３８ ２２ ２１．５００．７８６５４０ ２０．１００．７７３５
(表面涨力小计算精度低,温度高涨力小)
β100时精β100时精度β100时精度度β100时精度β100时精度β100时精度化学纤维μ玻璃纤维μ不锈钢纤维金属网纤维μm棉木纤维μmmμmm粉末烧结μm29.1754.0731.3158.0691.0728.298.2715.338.8716.4625.818.024.979.215.339.8915.514.8218.0133.3919.3335.8556.2417.474.107.604.408.1612.813.9821.7140.2423.2943.2067.7621.0511.3321.0112.1622.5635.3810.994.638.594.979.2214.474.4911.3621.0612.1922.6135.4711.0211.6621.6212.5223.2236.4211.31注:单通β20
相当多通β100
乙二醇在20℃时22.27异丙醇在20℃时21.7系数
A=21.7/22.27=0.974
3℃时与20℃比值1.065
冒泡压力换算过滤精度
