A method for treating waste water produced by hydrochloric acid method to produce calcium hydrogen phosphate
A technology of calcium hydrogen phosphate and hydrochloric acid method, applied in the field of phosphorus chemical industry, can solve the problems of low added value of calcium chloride, limited phosphate fertilizer output, small market demand, etc., and achieve the effect of comprehensive comprehensive utilization
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Embodiment 1
[0027] The present embodiment relates to the comprehensive utilization method of waste water in the calcium hydrogen phosphate production process, comprises the following steps:
[0028] 1) The waste water containing 20% calcium chloride and the ammonia water containing 30% ammonia produced in the production process of calcium hydrogen phosphate are reacted in the reaction tank according to the volume ratio of 1:1.5, and the feed rate of ammonia water is controlled to be 3.5 during the reaction process. m 3 / h, the stirring speed in the reaction tank is 12 rpm, the stirring power of the stirrer should ensure that the reaction liquid reacts in a turbulent state, and the Reynolds number is guaranteed to be 1.5×10 4 ~2.0×10 4 , the reaction time was controlled at 20 minutes to generate a mixed liquid.
[0029] 2) The mixed liquid from the reaction tank enters the settling tank, adjust the pH value of the mixed liquid to 10-11 with 30% ammonia water, and then add flocculant po...
Embodiment 2
[0032] 1) The waste water containing 20% calcium chloride and the ammonia water containing 30% ammonia produced by the production of calcium hydrogen phosphate are reacted in the reaction tank according to the volume ratio of 1:5. During the reaction, the feed rate of ammonia water is controlled to be 3.8m 3 / h, the stirring speed in the reaction tank is 13 rpm, the stirring power of the stirrer should ensure that the reaction liquid reacts in a turbulent state, and the Reynolds number is guaranteed to be 1.5×10 4 ~2.0×10 4 , the reaction time was controlled at 25 minutes to generate a mixed liquid.
[0033] 2) The mixed solution from the reaction tank enters the settling tank, adjust the pH value of the mixed solution to 10.5 with 30% ammonia water, and then add flocculant polyacrylamide, the molecular weight of polyacrylamide is 5 million to 6 million, during the addition process, polyacrylamide Firstly dilute the mixture with water to 60% volume percentage, and then pass...
Embodiment 3
[0036] 1) The waste water containing 20% calcium chloride and the ammonia water containing 30% ammonia produced by the production of calcium hydrogen phosphate are reacted in the reaction tank according to the volume ratio of 1:2.5. During the reaction, the feeding speed of ammonia water is controlled to be 4m 3 / h, the stirring speed in the reaction tank is 15 rpm, the stirring power of the stirrer should ensure that the reaction liquid reacts in a turbulent state, and the Reynolds number is guaranteed to be 1.5×10 4 ~2.0×10 4 , the reaction time was controlled at 30 minutes to generate a mixed liquid.
[0037] 2) The mixed solution from the reaction tank enters the settling tank, adjust the pH value of the mixed solution to 11 with 30% ammonia water, and then add the flocculant polyacrylamide, the molecular weight of the polyacrylamide is 5 to 6 million, during the addition process, the polyacrylamide Dilute the mixture to 58% by volume with water first, and then pass the...
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