Method for producing sodium dihydrogen phosphate and sodium chloride by purifying crude product sodium pyrophosphate
A technology of sodium dihydrogen phosphate and sodium pyrophosphate, applied in chemical instruments and methods, phosphorus compounds, alkali metal chlorides, etc., can solve the problems of slow dissolution of crude sodium pyrophosphate, small device processing capacity, and high viscosity of the solution , to achieve the effect of reducing the amount of wastewater produced, the amount of treatment is large, and the cost of treatment is high
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Embodiment 1
[0045] A method for purifying crude product sodium pyrophosphate to produce sodium dihydrogen phosphate and sodium chloride
[0046] In this process scheme, the content of sodium dihydrogen phosphate in the mother liquor after sodium dihydrogen phosphate crystallization is high, and the consumption of phosphoric acid is relatively large, but because the hydration amount of sodium dihydrogen phosphate is small and the mother liquor is recycled, the overall cost is also advantageous. This process scheme is especially suitable for enterprises with supporting devices of pentasodium phosphate and hexabias.
[0047] 1. Ingredients: At the initial start-up, mix the crude sodium pyrophosphate and water in the hydrolysis tank (hydrolysis tank) according to the mass ratio of 1:1, and add phosphoric acid dropwise to control the pH value of the mixed material at 3.5.
[0048] In the continuous operation process, the crude product sodium pyrophosphate and mechanically applied process water...
Embodiment 2
[0065] A device for purifying crude sodium pyrophosphate to produce sodium pyrophosphate and sodium chloride. The bottom of the hydrolysis kettle 1 is connected to the filter A2; the filter device A2 is connected to the heat exchanger 4, and the heat exchanger 4 is connected to the mixer 6, and the mixer 6 is connected with filter C 7, filter C 7 is connected with crystallization kettle 8, crystallization kettle 8 is connected with filter B 9, filter B 9 is connected with material washing device B 10, and material washing device B 10 is connected to sodium pyrophosphate Deep refining device 11.
[0066] Filter B 9 and material washing device B 10 are connected to heat exchanger 4 through pipelines respectively, and heat exchanger 4 is connected to heater 12 through connecting water storage tank 5 again, and heater 12 is connected to hydrolysis kettle 1.
[0067] Filter A 2 bottom is connected with material washing device A 3 through pipeline, and material washing device A 3 is...
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