Electrolytic cell diaphragm for chlor-alkali industry and preparation method thereof
A chlor-alkali industry and electrolytic cell technology, applied in the field of ion exchange membranes, can solve problems such as increased membrane resistance and increased cell pressure, and achieve the effects of reducing adhesion, reducing cell voltage, and reducing energy consumption
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Embodiment 1
[0034] (1) Perfluorosulfonic acid resin with IEC=1.08mmol / g and perfluorocarboxylic acid resin with IEC=0.98mmol / g are combined into perfluoroion exchange resin base membrane by co-extrusion casting, wherein perfluorosulfonic acid resin The thickness of the acid resin layer is 90 microns, and the thickness of the perfluorocarboxylic acid resin layer is 7 microns to obtain a perfluorinated ion exchange membrane precursor.
[0035] (2) under the temperature of 180 ℃, under the pressure of 120 tons, the perfluorinated ion-exchange membrane precursor that makes in the step (1) uses superpressure machine to carry out superpressure treatment with the speed of 45 meters per minute, superpressure After the pressure treatment, the perfluorinated ion exchange membrane precursor was immersed in a mixed aqueous solution containing 18wt% dimethyl sulfoxide and 20wt% NaOH at 85°C for 80 minutes to transform into a perfluorinated ion exchange membrane with ion exchange function.
[0036] (3)...
Embodiment 2
[0050] (1) The perfluorosulfonic acid resin of IEC=0.93mmol / g and the perfluorocarboxylic acid resin of IEC=0.95mmol / g are combined into a perfluoroion exchange resin base membrane by co-extrusion casting, wherein the perfluorosulfonic acid resin The thickness of the acid resin layer is 150 microns, the thickness of the perfluorocarboxylic acid resin layer is 8 microns, and the precursor of the perfluorinated ion exchange membrane is obtained.
[0051] (2) under the temperature of 200 ℃, under the pressure of 100 tons, with the perfluorinated ion exchange membrane precursor that makes in the step (1), carry out overpressure treatment with the speed of 45 m / min using overpressure machine, overpressure After pressure treatment, the precursor of the perfluorinated ion exchange membrane was immersed in a mixed aqueous solution containing 15wt% dimethyl sulfoxide and 20wt% NaOH at 80°C for 80 minutes to transform into a perfluorinated ion exchange membrane with ion exchange function...
Embodiment 3
[0063] (1) Perfluorosulfonic acid resin with IEC=1.3mmol / g and perfluorocarboxylic acid resin with IEC=1.22mmol / g are combined into perfluoroion exchange resin base membrane by co-extrusion casting, wherein perfluorosulfonic acid resin The thickness of the acid resin layer is 150 microns, and the thickness of the perfluorocarboxylic acid resin layer is 10 microns to obtain a perfluorinated ion exchange membrane precursor.
[0064] (2) under the temperature of 190 ℃, under the pressure of 100 tons, with the perfluorinated ion exchange membrane precursor that makes in the step (1), carry out overpressure treatment with the speed of 45 m / min using overpressure machine, overpressure After the pressure treatment, the precursor of the perfluorinated ion exchange membrane was immersed in a mixed aqueous solution containing 15 wt% dimethyl sulfoxide and 15 wt% NaOH at 80°C for 80 minutes to transform into a perfluorinated ion exchange membrane with ion exchange function.
[0065] (3) ...
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