A method for preparing solid-type water-soluble polymers induced by ultraviolet light
A technology of water-soluble polymers and ultraviolet light, which is applied in the field of preparation of solid water-soluble polymers induced by ultraviolet light, which can solve the problems of increased risk, increased production costs, and high strength
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Embodiment 1
[0027] Add deionized water 3262kg in batching tank, acrylamide (functional monomer) 4725kg of 40% concentration, acryloyloxyethyltrimethyl ammonium chloride (functional monomer) 1012kg of 80% concentration; Cosolvent urea 50kg; Chelating agent EDTA-2Na1Kg, chain transfer agent isopropanol 5kg mix homogeneously, obtain prepolymerization liquid;
[0028] Cool the pre-polymerization solution to 0°C, adjust the pH of the polymerization solution to 4.5; then use the feeding pump to transfer the pre-polymerization solution to the top of the packed tower at a flow rate of 3 tons / h, and open the nitrogen gas under the packed tower for oxygen removal; After completion, enter the static mixer and mix with 20% concentration 2-hydroxyl-2-methyl-1-phenyl-1-propanone (photoinitiator) at a flow rate of 1.2kg / h to form a polymerization solution;
[0029] Put the polymerization liquid into the polymerization device, use 254nm wavelength ultraviolet light at the light intensity of 0.6mw / cm2 at ...
Embodiment 2
[0031]Add 2900kg of deionized water in the batching tank, 4500kg of acrylamide (functional monomer) of 40% concentration, 612kg of diallyl dimethyl ammonium chloride (functional monomer) of 60% concentration, methyl Acryloyl propyltrimethylammonium chloride (functional monomer) 810kg; Cosolvent urea 70kg; Cosolvent industrial salt 50kg, chelating agent EDTA-2Na 1Kg, crosslinking agent (SA80) 36kg mix homogeneously, obtain pre-polymerized liquid;
[0032] Cool the pre-polymerization solution to 15°C, adjust the pH of the polymerization solution to 6.3; then use the feeding pump to transfer the polymerization solution to the top of the packed tower at a flow rate of 3 tons / h, and open the nitrogen gas under the packed tower for deoxygenation; deoxygenation is completed After entering the static mixer and mixing with the 1-hydroxycyclohexyl phenyl ketone (photoinitiator) solution of 10% concentration of 1.5kg / h flow rate and the azo initiator va044 solution of 1% concentration of ...
Embodiment 3
[0035] In batching tank, add deionized water 2250kg, acrylamide 6700kg of 40% concentration, industrial salt 120kg, chelating agent EDTA-2Na 1.2Kg, chain transfer agent isopropanol 9kg mix homogeneously, obtain prepolymerized liquid;
[0036] Cool the pre-polymerization solution to 0°C, adjust the pH of the polymerization solution to 4.0; then use the feeding pump to transfer the polymerization solution to the top of the packed tower at a flow rate of 2.5 tons / h, and open the nitrogen gas under the packed tower for deoxygenation; deoxygenation is completed After entering the static mixer with a 20% concentration of 2,4,6-trimethylbenzoyl-diphenylphosphine oxide (photoinitiator) solution with a flow rate of 3.2kg / h and a 1% solution with a flow rate of 18kg / h The concentration of azo initiator va044 solution is mixed into a polymerization solution;
[0037] Put the polymerization liquid into the polymerization device for polymerization, and use 254nm wavelength ultraviolet ligh...
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Abstract
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