Alkyl phosphinate polymer, and preparation method and application thereof
A technology of alkyl phosphinate and polymer, which is applied in the field of organic phosphinate polymer and its preparation, and can solve problems such as limited flame retardant effect, high hydrochloric acidity, and damage to mechanical properties of materials
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Embodiment 1
[0045] First, an Al polymer of dialkylphosphinic acid is prepared. For this, a mixture of 150 kg of sodium hypophosphite and 750 kg of deionized water was charged into a 2000 L jacketed pressure reactor. Once the reaction mixture had been heated to 100°C, acetylene was added to the reactor through a pressure relief valve set at 0.3 MPa until saturated. Dissolve 2.0kg of 2,2,-azobis(2-methylpropylamidine) dihydrochloride (or V50) in 200kg of water, and stir the solution continuously at a temperature of 100-105°C Add evenly to this mixture. A total of 18.5kg of acetylene was consumed. Acetylene was replaced by ethylene, which was added to the reactor through a pressure reducing valve set at 0.6 MPa until saturated. The catalyst is fed uniformly into the mixture at a temperature of 100-105°C. Total reaction 10h. Consumption of ethylene 39.6kg. The reactor was depressurized, and after cooling to 80 °C. Within 2 hours, add 290kg concentration of 50wt% Al-containing 2 o 3 1...
Embodiment 2
[0047] First, an Al polymer of dialkylphosphinic acid is prepared. For this, a mixture of 150 kg of sodium hypophosphite and 750 kg of deionized water was charged into a 2000 L jacketed pressure reactor. Once the reaction mixture had been heated to 100°C, acetylene was added through a pressure relief valve set at 0.3 MPa until saturation was reached in the reactor. A solution of 2.0kg of 2,2,-azobis(2-methylpropylamidine) dihydrochloride (or V50) in 200kg of water was uniformly fed to the in the mixture. A total of 9.2kg of acetylene was consumed. Acetylene was replaced by ethylene, which was added through a pressure reducing valve set at 0.6 MPa until saturation was reached in the reactor. The catalyst is fed uniformly into the mixture at a temperature of 100-105°C. Total reaction 10h. Consumption of ethylene 59.7kg. The reactor was depressurized, and after cooling to 80 °C. Within 2 hours, add 290kg of 50wt% Al-containing 2 o 3 16.53wt% A1 2 (SO 4 ) 3 aqueous sol...
Embodiment 3
[0049] First, an Al polymer of dialkylphosphinic acid is prepared. For this, a mixture of 150 kg of sodium hypophosphite and 750 kg of deionized water was charged into a 2000 L jacketed pressure reactor. Once the reaction mixture had been heated to 100°C, acetylene was added through a pressure relief valve set at 0.3 MPa until saturation was reached in the reactor. A solution of 2.0 kg of potassium persulfate in 200 kg of water was uniformly fed into the mixture under continuous stirring at a temperature of 100-105°C. A total of 12.9kg of acetylene was consumed. Acetylene was replaced by ethylene, which was added through a pressure reducing valve set at 0.6 MPa until saturation was reached in the reactor. The catalyst is fed uniformly into the mixture at a temperature of 100-105°C. Total reaction 10h. Consumption of ethylene 51.8kg. The reactor was depressurized, and after cooling to 80 °C. Within 2 hours, add 290kg of 50wt% Al-containing 2 o 3 16.53wt% A1 2 (SO 4 ) ...
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