Method for producing type I ammonium polyphosphate with high degree of polymerization
An ammonium polyphosphate, high degree of polymerization technology, applied in phosphates, phosphorus oxyacids, chemical instruments and methods, etc., can solve problems such as unfavorable industrialization promotion, harsh reaction conditions, high energy consumption, etc., and achieve easy control of the production process. , The color of the product is white, and the effect of effective use is realized.
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Embodiment 1
[0018] 1000.0g of urea phosphate and 113.9g of urea were added to the reaction kettle, ammonia was passed through and mixed, and the materials were melted, foamed and polycondensed. The reaction temperature was 220°C, the reaction pressure was 0.06MPa, and the reaction time was 80 minutes. After finishing, the obtained product was pulverized to obtain I-type ammonium polyphosphate, the average degree of polymerization of the product was 56, and the ammonia-containing tail gas used 40% P 2 O 5 The wet-process phosphoric acid is absorbed to obtain ammonium dihydrogen phosphate.
Embodiment 2
[0020] 1000.0g of urea phosphate and 113.9g of urea were added to the reaction kettle, ammonia was passed through and mixed, and the materials were melted, foamed and polycondensed. The reaction temperature was 280°C, the reaction pressure was 0.1MPa, and the reaction time was 150 minutes. After finishing, the obtained product was pulverized to obtain I-type ammonium polyphosphate, the average degree of polymerization of the product was 145, and the ammonia-containing tail gas used 25% P 2 O 5 The wet purification of phosphoric acid is absorbed to obtain ammonium dihydrogen phosphate.
Embodiment 3
[0022] 900.0 g of urea phosphate, 100.0 g of ammonium dihydrogen phosphate, and 159.9 g of urea were added to the reaction kettle, followed by ammonia flow and mixing, and the materials were melted, foamed, and polycondensed. The reaction time was 140 minutes. After the reaction, the obtained product was pulverized to obtain I-type ammonium polyphosphate. The average degree of polymerization of the product was 109. After the ammonia-containing tail gas was treated with solid sodium hydroxide, it was returned to the reactor as an ammonia gas source.
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