Method for preparing industrial-grade and food-grade phosphoric acid by emulsification extraction and purification of wet-process phosphoric acid
A wet-process phosphoric acid, industrial-grade technology, applied in chemical instruments and methods, phosphorus compounds, inorganic chemistry, etc., can solve the problems of high price of barium carbonate/barium hydroxide, fine barium sulfate particles, and increased product cost, and achieves economical efficiency. The effect of removing the filtration and separation process, shortening the production cycle and improving the utilization rate
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Embodiment 1
[0027] Embodiment 1: Preparation of technical grade phosphoric acid
[0028] In the present embodiment, the composition of raw material wet-process phosphoric acid used is as follows:
[0029]
[0030] Process steps such as figure 1 As shown, the sequence is primary decolorization, emulsification extraction, emulsification washing, emulsification stripping, arsenic and heavy metal removal, secondary decolorization, and concentration adjustment.
[0031] (1) One decolorization
[0032] The primary decolorization process is carried out in a primary decolorization tank, the decolorizing agent is ozone, the addition amount is 0.3% of the mass of phosphoric acid, the reaction temperature is 50°C, and the reaction time is 40 min.
[0033] (2) Emulsion extraction
[0034] The emulsification extraction process extracts the phosphoric acid after primary decolorization, using the mixture of tributyl phosphate and kerosene as the extractant, the volume percentage of kerosene is 40%...
Embodiment 2
[0049] Embodiment 2: Preparation of food-grade phosphoric acid
[0050] In the present embodiment, the composition of raw material wet-process phosphoric acid used is as follows:
[0051]
[0052] Process steps such as figure 1 As shown, the sequence is primary decolorization, emulsification extraction, emulsification washing, emulsification stripping, concentration, de-arsenic and heavy metal removal, secondary deep decolorization, defluorination and concentration adjustment.
[0053] (1) One decolorization
[0054] The primary decolorization process is carried out in a primary decolorization tank, the decolorant is ozone, the addition amount is 3% of the mass of phosphoric acid, the reaction temperature is 60°C, and the reaction time is 10 min.
[0055] (2) Emulsion extraction
[0056] The emulsification extraction process extracts the phosphoric acid after a decolorization, using the mixture of tributyl phosphate and kerosene as the extractant, the volume percentage o...
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