Method for measuring microcellular plate-type membrane porosity
A measurement method and porosity technology, which is applied in the field of accurate determination of the porosity of membrane materials, can solve problems such as laborious, time-consuming, and large error in results, and achieve the effects of simple measurement equipment, accurate measurement values, and low cost
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Embodiment 1
[0039] A. to SO 2 / Air mixed gas-clear water is the measurement test system, and the German sulfonated polyethersulfone flat membrane experiment membrane is selected, and its volume porosity is known to be 72.0%; SO 2 The flow rate of air / air mixture is 400L / h, the flow rate of clear water absorption liquid is 24L / h, when the two phases are in direct contact, the gas phase inlet and outlet concentrations measured by the pararosaniline method are: C g1 =126.86ppm, C g2 =98.04ppm, known SO 2 / Henry coefficient H of the air mixture-clean water system A =24.2, calculated by formula (1), (2), (3): K G =1.997×10 -3 , so as to obtain point P, and draw the linear relationship between the total mass transfer coefficient of the mass transfer system and the membrane porosity image 3 ;
[0040] B. After adding the side membrane, under the same experimental conditions as step A, measure SO according to the method of step 1 2 The inlet and outlet concentrations of / air mixture are C...
Embodiment 2
[0042] A. Change the experimental membrane to be tested into the polyacrylonitrile flat membrane of Zhejiang University Membrane Engineering Company. It is known that its volume porosity is 40.0%. Other conditions are the same as in Example 1, so its total mass transfer coefficient - membrane porosity The linear relationship diagram of the rate is also the same as that of Example 1 image 3 unanimous.
[0043] B. Add the side film to be treated, record the gas phase inlet and outlet concentrations by the method of embodiment 1 and be respectively: C g1 '=126.86ppm, C g2 '=111.01ppm, calculate K G '=0.843×10 -3 ,exist image 3 The M2 point is obtained, and its corresponding porosity value is 41.8%.
Embodiment 3
[0045] A. change the liquid phase flow velocity in embodiment 1 into 32L / h, other conditions are all unchanged, when two phases directly contact, record gas phase inlet and outlet concentration to be respectively: C g1 =126.86ppm, C g2 = 95.13 ppm. Calculate K G =2.276×10 -3 , from which the linear relationship between total mass transfer coefficient and membrane porosity is plotted Figure 4 .
[0046] B. After adding the side membrane, under the same experimental conditions as in step A, the gas phase inlet and outlet concentrations measured according to A are: C g1 '=126.86ppm, C g2 '=102.38ppm, K is calculated G '=1.592×10 -3 . According to K G ’ has a value of Figure 4 The M3 point can be determined in , and its corresponding porosity value is 70.3%. This value is in good agreement with the value of Example 1.
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