Method for preparing high-concentration calcium chloride solution by decomposing ammonium chloride with lime powder
A technology of calcium chloride solution and lime powder, applied in the direction of calcium/strontium/barium chloride, calcium/strontium/barium halide, etc., can solve the problems of waste, large discharge of waste liquid, pollute the environment, etc., and reduce steam The effect of reducing consumption and emissions
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Embodiment 1
[0021] As shown in the flow chart, add 95% ammonium chloride 300kg / h from the ammonium chloride silo 1 and send the lime powder (CaO content 77.32%) 215kg / h from the lime powder silo 2 into the mixing conveying auger 15 for mixing Then enter the first-stage reactor 3, and add 0.24m at the same time 3 The / h light liquid is fully mixed and partially reacted by stirring, the reaction temperature is 89.5 °C, the excess CaO of lime powder in the first-stage reaction liquid is 9.91%, and it is sent to the top of the first-stage distillation tower 7 by the first-stage delivery pump 4 and from the second-stage distillation tower. The mixed gas of the steam of 8 and ammonia is contacted in countercurrent for heat and mass transfer, the temperature of the first-stage distillate overflowing from the bottom of the first-stage distillation tower 7 is 118.1°C, and the first-stage distillate overflows from the bottom of the first-stage distillation tower The second stage reactor 5 reacts fu...
Embodiment 2
[0023] As shown in the flow chart, add 95% ammonium chloride 300kg / h from the ammonium chloride silo 1 and send the lime powder (CaO content 75.76%) 210kg / h from the lime powder silo 2 into the mixing conveying auger 15 for mixing Then enter the first-stage reactor 3, and add 0.25m 3 The / h light liquid is fully mixed and partially reacted by stirring. The reaction temperature is 79.7 ° C. The excess CaO of lime powder in the first-stage reaction liquid is 5.30%. The mixed gas of steam of 8 and ammonia is contacted in countercurrent for heat and mass transfer, the temperature of the first-stage distillate overflowing from the bottom of the first-stage distillation tower 7 is 117.6°C, and the first-stage distillate overflows from the bottom of the first-stage distillation tower The second stage reactor 5 reacts further, in order to ensure the ammonium chloride decomposition reaction, add 7.8kg / h steam in the second stage reactor 5, the temperature is 114.7 ℃. The reaction liqu...
Embodiment 3
[0025] As shown in the flow chart, add 95% ammonium chloride 200kg / h from ammonium chloride silo 1 and send lime powder (CaO content 80.26%) 128kg / h from lime powder silo 2 into the mixing conveyor auger 15 for mixing Then enter the first-stage reactor 3, and add 0.20m 3 The / h light liquid is fully mixed and partially reacted by stirring. The reaction temperature is 70.7 ° C. The excess CaO of lime powder in the first-stage reaction liquid is 3.21%. The mixed gas of 8 steam and ammonia is contacted in countercurrent for heat and mass transfer. The temperature of the first-stage distillate overflowing from the bottom of the first-stage distillation tower 7 is 117.2°C, and the first-stage distillate overflows from the bottom of the first-stage distillation tower to The second stage reactor 5 reacts further, in order to ensure the ammonium chloride decomposition reaction, add 5.4kg / h steam in the second stage reactor 5, the temperature is 100.8 ℃. The reaction liquid in the sec...
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