Method for recovering iodine from industrial byproduct containing KI
A technology for by-product and iodine recovery, applied in the field of iodine recovery, can solve the problems of low recovery rate and high iodine production cost, and achieve the effects of short reaction time, reduced equipment investment and low reaction temperature
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Embodiment 1
[0040] This embodiment combines the attached figure 1 The present invention is further described in detail:
[0041] In raw material liquid preparation device 1, be raw material with the industrial by-product that contains KI, with from I 2 The filtered mother liquor of the crystallization tank reaction system is used as a solvent, and the preparation concentration is a raw material solution of 8.5mol / L, which is the same as the original concentration;
[0042] The prepared raw material liquid is transported to the raw material liquid storage tank 3 by the acid-resistant pump I2 for standby, and the raw material liquid in the storage tank 3 is added to the KH with stirring and temperature control functions by the acid-resistant pump II4 2 PO 4 In the crystallization kettle 5, under the condition that the stirring rate is controlled at 4r / min and the reaction temperature is controlled at 3°C, KH is added in a steady flow. 2 PO 4 Crystal modifier Ⅰ and industrial grade wet-p...
Embodiment 2
[0048] Use industrial by-products containing KI as raw materials to 2 The filtered mother liquor of the reactant system of the crystallization tank is used as a solvent to prepare a raw material solution with a concentration of 3.0mol / L, which is the same as the original concentration;
[0049] The prepared raw material liquid is transported to the raw material liquid storage tank by the acid-resistant pump I for standby, and the raw material liquid in the storage tank is added to the KH with stirring and temperature control functions by the acid-resistant pump II 2 PO 4 In the crystallization tank, under the condition that the stirring rate is controlled at 8r / min and the reaction temperature is controlled at 20°C, add KH at a steady flow. 2 PO 4 Crystal modifier Ⅰ and industrial grade wet-process phosphoric acid, KH 2 PO 4 The amount of crystal modifier I is 0.30‰ of the total mass of the raw material liquid in the kettle, and its composition is composed of cetyl alcohol...
Embodiment 3
[0055] Use industrial by-products containing KI as raw materials to 2 The filtered mother liquor of the reactant system of the crystallization tank is used as a solvent to prepare a raw material solution with a concentration of 4.0mol / L, which is the same as the original concentration;
[0056] The prepared raw material liquid is transported to the raw material liquid storage tank by the acid-resistant pump I for standby, and the raw material liquid in the storage tank is added to the KH with stirring and temperature control functions by the acid-resistant pump II 2 PO 4 In the crystallization tank, under the condition that the stirring rate is controlled at 6r / min and the reaction temperature is controlled at 15°C, add KH at a steady flow. 2 PO 4 Crystal modifier Ⅰ and industrial grade wet-process phosphoric acid, KH 2 PO 4 The amount of crystal modifier I is 0.20‰ of the total mass of the raw material liquid in the kettle, and its composition is composed of cetyl alcohol...
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