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机构地区:[1]岳阳市化工蓄电池厂,岳阳414000 [2]岳阳师范学院,岳阳414000
出 处:《现代化工》2002年第1期41-42,44,共3页Modern Chemical Industry
摘 要:介绍了复分解三步循环法生产硝酸钾的生产工艺。和四步法生产硝酸钾工艺比较 ,减少了加料步骤 ,在反应溶液中加入助剂后使溶液中硝酸钾结晶率提高 2 0 %以上。经检测产品质量组成为K2 O 43 0 1 %~ 45 68% ,N 1 3 80 %~ 1 4 2 0 % ,Cl0 3 %~ 2 1 5 % ,H2 O 1 98%~ 3 45 %The process of double decomposition three-step circulation for potassium nitrate production was introduced. Compared with the four-step process, feeding steps in the new process were reduced and the crystallization rate of potassium nitrate was increased by over 20% after adding assistants into the reaction solution. Tests show that the mass fraction was 43.01%-45.68% for K2O, 13.80%-14.20% for N, 0.3% -2.15% for Cl and 1.98% -3.45% for H2O.
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