四乙酰乙二胺

反应条件: temp:100.01; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 1500 g (14 mol) of sodium hypophosphite monohydrate are dissolved in 7.5 kg of water and initially charged in a 16 l steel-enamel jacketed pressure reactor. After heating the reaction mixture to 100° C., a reducing valve set to 6 bar is used to introduce ethylene into the reactor up to saturation. While stirring constantly at an ethylene pressure of 6 bar and a temperature of 100-110° C., a solution of 22 g (1 mol %) of sodium percarbonate and 16 g of tetraacetylethylenediamine in 300 g of water is metered in homogeneously. At a conversion of ethylene of 85%, the metered addition of sodium percarbonate and tetraacetylethylenediamine is stopped and the reactor is decompressed. After cooling to about 90° C., 3000 g (4.67 mol of aluminum) of a 46% aqueous solution of Al2(SO4)3.14 H2O is added within 60 minutes. Subsequently, the resulting solid was filtered off, washed with 2 l of hot water and dried at 130° C. under reduced pressure. The resulting mixture comprises diethylphosphinic acid aluminum(III) salt and ethylphosphonous acid aluminum(III) salt in a ratio of 79.5% by weight of diethylphosphinic acid aluminum(III) salt and 20.5% by weight of ethylphosphonous acid aluminum(III) salt (95.9% yield). a reducing valve set to 6 bar a temperature of 100-110° C. After cooling to about 90° C. Subsequently, the resulting solid was filtered off washed with 2 l of hot water dried at 130° C. under reduced pressure

反应条件: temp:100.01; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 1500 g (14 mol) of sodium hypophosphite monohydrate are dissolved in 7.5 kg of water and initially charged in a 16 l steel-enamel jacketed pressure reactor. After heating the reaction mixture to 100° C., a reducing valve set to 6 bar is used to introduce ethylene into the reactor up to saturation. While stirring constantly at an ethylene pressure of 6 bar and a temperature of 100-110° C., a solution of 22 g (1 mol %) of sodium percarbonate and 16 g of tetraacetylethylenediamine in 300 g of water is metered in homogeneously. At a conversion of ethylene of 85%, the metered addition of sodium percarbonate and tetraacetylethylenediamine is stopped and the reactor is decompressed. After cooling to about 90° C., 3000 g (4.67 mol of aluminum) of a 46% aqueous solution of Al2(SO4)3.14 H2O is added within 60 minutes. Subsequently, the resulting solid was filtered off, washed with 2 l of hot water and dried at 130° C. under reduced pressure. The resulting mixture comprises diethylphosphinic acid aluminum(III) salt and ethylphosphonous acid aluminum(III) salt in a ratio of 79.5% by weight of diethylphosphinic acid aluminum(III) salt and 20.5% by weight of ethylphosphonous acid aluminum(III) salt (95.9% yield). a reducing valve set to 6 bar a temperature of 100-110° C. After cooling to about 90° C. Subsequently, the resulting solid was filtered off washed with 2 l of hot water dried at 130° C. under reduced pressure

反应条件: temp:100.01; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 1500 g (14 mol) of sodium hypophosphite monohydrate are dissolved in 7.5 kg of water and initially charged in a 16 l steel-enamel jacketed pressure reactor. After heating the reaction mixture to 100° C., a reducing valve set to 6 bar is used to introduce ethylene into the reactor up to saturation. While stirring constantly at an ethylene pressure of 6 bar and a temperature of 100-110° C., a solution of 22 g (1 mol %) of sodium percarbonate and 16 g of tetraacetylethylenediamine in 300 g of water is metered in homogeneously. At a conversion of ethylene of 85%, the metered addition of sodium percarbonate and tetraacetylethylenediamine is stopped and the reactor is decompressed. After cooling to about 90° C., 3000 g (4.67 mol of aluminum) of a 46% aqueous solution of Al2(SO4)3.14 H2O is added within 60 minutes. Subsequently, the resulting solid was filtered off, washed with 2 l of hot water and dried at 130° C. under reduced pressure. The resulting mixture comprises diethylphosphinic acid aluminum(III) salt and ethylphosphonous acid aluminum(III) salt in a ratio of 79.5% by weight of diethylphosphinic acid aluminum(III) salt and 20.5% by weight of ethylphosphonous acid aluminum(III) salt (95.9% yield). a reducing valve set to 6 bar a temperature of 100-110° C. After cooling to about 90° C. Subsequently, the resulting solid was filtered off washed with 2 l of hot water dried at 130° C. under reduced pressure

反应条件: temp:100.01; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 1500 g (14 mol) of sodium hypophosphite monohydrate are dissolved in 7.5 kg of water and initially charged in a 16 l steel-enamel jacketed pressure reactor. After heating the reaction mixture to 100° C., a reducing valve set to 6 bar is used to introduce ethylene into the reactor up to saturation. While stirring constantly at an ethylene pressure of 6 bar and a temperature of 100-110° C., a solution of 22 g (1 mol %) of sodium percarbonate and 16 g of tetraacetylethylenediamine in 300 g of water is metered in homogeneously. At a conversion of ethylene of 85%, the metered addition of sodium percarbonate and tetraacetylethylenediamine is stopped and the reactor is decompressed. After cooling to about 90° C., 3000 g (4.67 mol of aluminum) of a 46% aqueous solution of Al2(SO4)3.14 H2O is added within 60 minutes. Subsequently, the resulting solid was filtered off, washed with 2 l of hot water and dried at 130° C. under reduced pressure. The resulting mixture comprises diethylphosphinic acid aluminum(III) salt and ethylphosphonous acid aluminum(III) salt in a ratio of 79.5% by weight of diethylphosphinic acid aluminum(III) salt and 20.5% by weight of ethylphosphonous acid aluminum(III) salt (95.9% yield). a reducing valve set to 6 bar a temperature of 100-110° C. After cooling to about 90° C. Subsequently, the resulting solid was filtered off washed with 2 l of hot water dried at 130° C. under reduced pressure