Mixed acid nitration synthesis continuous production process and device
A mixed acid, continuous technology, applied in the direction of ammonia compounds, feeding devices, chemical/physical/physicochemical processes, etc., can solve the problems of polynitrates and oxidation, prone to combustion, explosion, small size of micro-reaction channels, etc. Achieve the effects of simple process flow, large heat release and low equipment investment
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Embodiment 1
[0022] O-methyl-N-nitroisourea 30kg and 100kg of CO 2 The liquid is mixed in the mixing tank, the temperature of the mixing tank is 15°C, and the pressure is 5.2MPa; the mixed material enters the reactor continuously at a flow rate of 13kg / h, the temperature in the reactor is 15°C, and the pressure is 5.0MPa Mixed acid is added in the mixed acid storage tank by HNO3:H2SO4=3:1 (mol), and mixed acid enters into the reactor continuously with the flow rate of 9.6kg / h and reacts with ammonium sulfamate to generate ammonium dinitramide. CO 2 The gas continuously enters the bottom of the reactor at a flow rate of 8Nm3 / h as the power of the reactor. The generated ammonium dinitramide and unreacted mixed acid are continuously extracted from the upper part of the reactor with a flow rate of 12.6kg / h by the product discharge pump; the unreacted CO 2 The discharge from the top of the reactor is compressed and condensed into CO by the compressor and condenser 2 The liquid is returned to...
Embodiment 2
[0024] Ammonium sulfamate 9.7kg and 44kg of CO 2 The liquid is mixed in the mixing tank, the temperature of the mixing tank is -40°C, and the pressure is 1.2MPa; the mixed material enters the reactor continuously at a flow rate of 5.37kg / h, the temperature in the reactor is -40°C, and the pressure 1.0MPa; mixed acid according to HNO 3 :H 2 SO 4 =5:1 (mol) is added in the mixed acid storage tank, and the mixed acid continuously enters the reactor with a flow rate of 5kg / h to react with ammonium sulfamate to generate ammonium dinitramide. CO 2 The gas continuously enters the bottom of the reactor at a flow rate of 5Nm3 / h as the power of the reactor. The ammonium dinitramide and unreacted mixed acid are continuously extracted from the reactor top with a flow rate of 6kg / h by the product discharge pump; 2 The discharge from the top of the reactor is compressed and condensed into CO by the compressor and condenser 2 The liquid is returned to the ingredients tank.
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