Cleaning agent for polyacrylamide contaminated films, and cleaning method thereof
A technology of polyacrylamide and cleaning agent, which is applied in the field of cleaning agent for polyacrylamide polluted membranes, which can solve the problems of difficult cleaning and reuse of filter membranes, shortened service life, secondary pollution of water bodies, etc., and achieves short cleaning time and clean Thorough, surface-structured effect
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[0022] A cleaning agent for polyacrylamide polluted membranes, including a pre-soaking solution before using the membrane and a cleaning solution after using the membrane, the pre-soaking solution is a soluble anionic polymer aqueous solution with a mass concentration of 0.01-10wt%, The cleaning liquid is an aqueous solution containing 0.01-8wt% sodium hydroxide and 0.01-6wt% soluble anionic polymer, and the soluble anionic polymer is sodium alginate or sodium polyacrylate. Its cleaning method comprises the following steps:
[0023] (1) Pre-soaking treatment
[0024] Soak the filter membrane in a soluble anionic polymer solution with a mass concentration of 0.01-10wt% for 3-12 hours to form a layer of soluble pre-protective layer on the surface of the membrane to protect the surface of the membrane from damage by cleaning agents, in which the soluble anionic polymer Sodium alginate or sodium polyacrylate;
[0025] (2) Filtration process
[0026] Take the filter membrane obt...
Embodiment 1
[0030] A PS hollow fiber ultrafiltration membrane with a cut molecular weight of 5 million was selected and soaked in a sodium polyacrylate solution with a mass concentration of 0.1% for 3 hours, and was taken out and applied to the water purification process of the waterworks. After the untreated water is flocculated and precipitated by the water plant, the supernatant will have a little residual polyacrylamide flocculant and other impurities, and the pre-soaked PS hollow fiber ultrafiltration membrane will be used to deeply purify the tap water, that is Continue to filter the supernatant after flocculation and precipitation. The initial pure water flux of the membrane is 350 L / (m 2 *h), for the filtration of tap water supernatant after flocculation and sedimentation, the initial filtration flux is 190 L / (m 2 *h), through the filtration backflush process, after a period of filtration, the equilibrium filtration flux of the membrane is 30 L / (m 2 *h), compared with the initia...
Embodiment 2
[0032] The PES microfiltration flat membrane module with a pore size of 0.1 μm is selected, and the initial pure water flux of the membrane is 700 L / (m 2 *h), soak in sodium alginate solution with a mass concentration of 0.05% for 3 hours, and then filter with a mass concentration of 10 -6 (g / L) polyacrylamide (PAM) aqueous solution. The flux of initial filtration PAM is 250 L / (m 2 *h), after a period of filtration, the equilibrium filtration flux of the membrane is 20 L / (m 2 *h) When compared with the initial filtration PAM flux, the filtration flux decays by about 92%, the filtration is stopped, and the membrane is seriously polluted. The aqueous solution containing 0.3wt% NaOH and 0.06wt% sodium polyacrylate was used to clean the polluted membrane for 60 minutes; after cleaning, the pure water flux of the membrane was 885 L / (m 2 *h), a recovery rate of 126% compared to the initial pure water flux. Soak the above-mentioned PES microfiltration flat membrane module that ha...
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