Poly silicon phosphorus aluminum ferrous chloride and preparation method thereof
A technology of polysilicon phosphoaluminum chloride and phosphate rock powder, which is applied in the treatment of water, sewage or sludge, and wastewater fields, can solve problems such as failure to detect technical solutions, and achieve the best effect of stable performance
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Embodiment 1
[0037] Example 1, take 95kg of industrially synthesized hydrochloric acid converted into a mass concentration of 100%, add it to the reaction tank, add 50kg of phosphate rock powder under constant stirring, then add 80kg of gibbsite, steam heating to control the temperature of the reaction tank at 100-110°C In between, after 2 hours of reaction, pressure filtration is carried out. After pressure filtration, the semi-finished product is added to the reaction tank again, cooled to 50-70°C, and 140kg of calcium aluminate powder is added under constant stirring, and 635kg of water is gradually added. Timely control the flow rate so that the temperature of the solution is controlled in the range of 80-100°C. At this time, the amount of water converted from the amount of steam should be deducted from the total amount of water. React for 1 hour to separate the liquid and slag. In this example, natural sedimentation is used to obtain 920 kg of finished filtrate.
Embodiment 2
[0038] Example 2, take 145kg of industrially synthesized hydrochloric acid converted into a mass concentration of 100%, add it to the reaction tank, add 100kg of phosphate rock powder under constant stirring, then add 120kg of gibbsite, steam heating to control the temperature of the reaction tank at 100-110°C In between, press filter after 2 hours of reaction, add the semi-finished product to the reaction tank after the press filter, cool to 50-70°C, add 110kg of calcium aluminate powder under constant stirring, and gradually add 525kg of water, add water Timely control the flow rate so that the temperature of the solution is controlled in the range of 80-100°C. At this time, the amount of water converted from the amount of steam should be deducted from the total amount of water. React for 3 hours to separate the liquid and slag. In this example, pressure filtration is used to obtain 890kg of finished filtrate.
Embodiment 3
[0039] Example 3, take 100kg of industrially synthesized hydrochloric acid converted into a mass concentration of 100%, add it to the reaction tank, add 60 kg of phosphate rock powder under constant stirring, then add 85 kg of gibbsite, and steam heating to control the temperature of the reaction tank at 100-110 ° C In between, after 2 hours of reaction, pressure filtration is carried out. After pressure filtration, the semi-finished product is added to the reaction tank again, cooled to 50-70°C, and 135kg of calcium aluminate powder is added under constant stirring, and 620kg of water is gradually added. Timely control the flow rate, so that the solution temperature is controlled in the range of 80-100 ° C. At this time, the amount of water converted from the amount of steam should be deducted from the total amount of water. React for 2 hours to separate the liquid and slag. In this example, centrifugation is used to obtain 910 kg of finished filtrate.
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