Method for preparing composite flocculant
A composite flocculant and inorganic flocculant technology, applied in the direction of flocculation/sedimentation water/sewage treatment, etc., can solve the problems of water quality not meeting discharge standards, slow separation speed of flocs, poor treatment effect, etc., and achieve high oil removal efficiency , The amount of scum generation is reduced, and the effect of cost reduction
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Embodiment 1
[0010] In a 1 liter reactor, add 350g of diethylenetriamine, heat up to 100°C under stirring, pass in 300g of propylene oxide, control the temperature at 115-125°C, add it in 2 hours, keep it at 110°C for one hour, and cool A substituted amine A is formed.
[0011] Add 250g of polyethylene glycol with a molecular weight of 1000 to a 1000ml three-necked flask with stirring, thermometer and reflux tube, and then add 200g of 3-chloro-1,2-epoxypropane in 2 hours. The reaction temperature is 90-110 ℃, the reaction is completed at about 90 ℃ for 1 hour, the product is adduct B.
[0012] Add 150g of amine substitute A into a 500ml flask, stir and heat to 100°C, add 100g of adduct B in portions. The reaction temperature is 110-120°C, the reaction time is 2 hours, and the reactant is neutralized with 50 ml industrial hydrochloric acid after cooling.
Embodiment 2
[0014] At room temperature, 130ml of the product of Example 1 and 100ml of 50% (weight) polyferric sulfate solution are added to the reactor, and then 10ml of water and 8ml of isopropanol are added, and the finished product is stirred evenly.
Embodiment 3
[0016] At room temperature, 100 ml of the polymer of Example 1 and 70 ml of 30% (weight) polyaluminum chloride solution were added to the reactor, and about 10 ml of water and 9 ml of isopropanol were added. Stir evenly to be the finished product.
[0017] The application effect evaluation of the above-mentioned flocculant is carried out by the conventional bottle test method, and the dosage range of the flocculant is 10-3000ppm according to the composition and stability of oily sewage. The flocculants of the present invention all show good demulsification performance and oil removal effect, and the technical cost is low.
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