Membrane cleaning agent for starch wastewater treatment and preparation method thereof
A technology for starch wastewater and membrane cleaning agent, applied in chemical instruments and methods, membrane technology, semi-permeable membrane separation, etc., can solve the problems of membrane surface pollution, system paralysis, membrane module fouling and blocking, etc., to shorten cleaning time, restore The effect of filtering flux and reducing energy consumption
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Embodiment 1
[0013] Sodium hydroxide 28%, sodium silicate 3.5%, sodium polyphosphate 5.5%, sodium carbonate 4%, zircoaluminate coupling agent 0.1%, ammonium zirconium carbonate 0.05%, nonionic surfactant AES 0.15%, Sodium dodecylbenzenesulfonate 4.3%, fatty alcohol polyoxyethylene ether sulfate 0.5%, acrylonitrile-butadiene-styrene copolymer 0.4%, EDTA disodium salt 6%, diatomaceous earth 3.5%, 5% ethanol, and 39% water are sequentially added into a stirred reactor according to the listed order of the above components, and stirred at room temperature and normal pressure for 4 hours at the same time to obtain the finished product. After cleaning the membrane surface pollutants test, it is measured that the water production of the membrane before and after the membrane cleaning is increased from 115m 3 / h returns to 150m 3 / h, the product water flux of the unused new reverse osmosis membrane is 153m 3 / h.
Embodiment 2
[0015] Sodium hydroxide 32%, sodium silicate 3%, sodium polyphosphate 5%, sodium carbonate 4.5%, zircoaluminate coupling agent 0.18%, ammonium zirconium carbonate 0.07%, nonionic surfactant AES 0.2%, Sodium dodecylbenzene sulfonate 3%, fatty alcohol polyoxyethylene ether sulfate 0.6%, acrylonitrile-butadiene-styrene copolymer 0.45%, edetate disodium salt 4%, diatomaceous earth 3%, 4% ethanol, and 40% water are sequentially added into a stirred reactor according to the listed order of the above components, and stirred at room temperature and normal pressure for 8 hours at the same time to obtain the finished product. After cleaning the membrane surface pollutants test, it is measured that the water production of the membrane before and after the membrane cleaning is increased from 117m 3 / h returns to 158m 3 / h, the product water flux of the unused new reverse osmosis membrane is 158m 3 / h.
Embodiment 3
[0017] Sodium hydroxide 33%, sodium silicate 2%, sodium polyphosphate 4%, sodium carbonate 3%, zircoaluminate coupling agent 0.3%, ammonium zirconium carbonate 0.1%, nonionic surfactant AES 0.3%, Sodium dodecylbenzenesulfonate 3%, fatty alcohol polyoxyethylene ether sulfate 0.7%, acrylonitrile-butadiene-styrene copolymer 0.6%, ethylenediaminetetraacetic acid disodium salt 2%, diatomaceous earth 4%, 4% ethanol, 43% water, according to the listed order of the above components, add them into a stirred reactor in sequence, and stir at room temperature and normal pressure for 5 hours at the same time to obtain the finished product. After cleaning the membrane surface pollutants test, it is measured that the water production of the membrane before and after the membrane cleaning is increased from 117m 3 / h returns to 141m 3 / h, the product water flux of the unused new reverse osmosis membrane is 143m 3 / h.
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