A kind of initiating method for acrylamide aqueous solution polymerization
An aqueous solution polymerization and acrylamide technology, which is applied in the field of high molecular polymer synthesis technology, can solve the problems of difficulty in obtaining a polymer product, a large difference in the light intensity of the glue block, and a decrease in light transmittance, and achieves low residual monomer and consumption saving. , the effect of improving utilization
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Embodiment 1
[0023] Add 1600kg of industrial-grade acrylamide (40%), 200kg of 2-acryloyloxyethyltrimethylammonium chloride (80%), and 1200kg of deionized water into the batching kettle, and add 2-hydroxy-4'-(2 -Hydroxyethoxy)-2-methylpropiophenone 9kg, azobisisobutylimidazoline hydrochloride 0.03kg, azobisisobutylamidine hydrochloride 0.6kg, azobisisobutyronitrile 0.3kg, azobisisobutyronitrile Disodium diamine tetraacetate, after mixing evenly, add hydrochloric acid to adjust the pH value to 3.5, cool down to 2°C, after deoxygenation, continuously feed the material to the closed belt conveyor polymer belt with ultraviolet lamp, after passing the conveyor belt, the rubber block is formed , and then through rubber cutting, granulation, drying, and grinding to obtain a cationic polyacrylamide product with a molecular weight of 6.5-8 million, a residual monomer of 300-800 ppm, and a dissolution time of 26-32 minutes.
Embodiment 2
[0025] Add 800kg of industrial-grade acrylamide (40%), 1600kg of 2-acryloyloxyethyltrimethylammonium chloride (80%), and 600kg of deionized water into the batching kettle, and add 2-hydroxy-4'-(2 -Hydroxyethoxyl group)-2-methyl propiophenone 12kg, azobisisobutyryl imidazoline hydrochloride 0.08kg, azobisisobutyromidine hydrochloride 0.5kg, azobisisobutyronitrile 0.3kg, azobisisobutyronitrile Disodium diamine tetraacetate 1kg, after mixing evenly, add hydrochloric acid to adjust the pH value to 3.5, cool down to 4°C, after deoxygenation, continuously feed to the closed belt conveyor polymer belt with ultraviolet lamp, after passing the conveyor belt, the rubber block Forming, cutting, granulating, drying and grinding to obtain a cationic polyacrylamide product with a molecular weight of 2 million to 4 million, a residual monomer of 300-500 ppm, and a dissolution time of 23-28 minutes.
Embodiment 3
[0027] Add 1980kg of industrial grade acrylamide (30%), 340kg of acrylic acid (70%), and 290kg of deionized water into the batching kettle, adjust the pH value to 6.0, consume 390kg of NaOH (32%), and then add the initiator 2-hydroxyl-2 - 0.6kg of methyl-1-phenyl-1-acetone, 0.03kg of azobisisobutylimidazoline hydrochloride, 0.3kg of azobisisobutyromidine hydrochloride, 0.2kg of azobisisobutyronitrile, Disodium diamine tetraacetate 1kg, after mixing evenly, add hydrochloric acid or liquid caustic soda to adjust the pH value to 6.0, cool down to 2°C, after deoxygenation, continuously feed to the closed belt conveyor polymer belt with ultraviolet lamp, and pass through the conveyor belt After the rubber block is formed, the anionic polyacrylamide product is obtained after cutting, granulating, drying and grinding, with a molecular weight of 8-12 million, a residual monomer of 400-800ppm, and a dissolution time of 30-45min.
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