Method using extraction agent and hydrochloric acid acidolysis technology to efficiently leach K, Ca, Mg and P from P and K associated ore
A technology of phosphorus-potassium associated ore and extractant, which is applied in the industrial field, can solve the problems of high reaction temperature, long reaction time, hindering the acid hydrolysis process, etc., and achieves the effect of reducing the reaction temperature and reducing the corrosion damage and reducing the reaction time.
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Embodiment 1
[0020] A method for efficiently leaching K, Ca, Mg, P from phosphorus and potassium associated ore by using extraction agent and hydrochloric acid acid hydrolysis technology, comprising the steps of: weighing 20g of phosphorus and potassium associated ore, CaF 2 1.8g, 22.5% (mass concentration) HCl68ml, tributyl phosphate 2ml, put into a three-necked flask in turn, heat up, start stirring, react at 75°C for 4h, wash and filter with water, and obtain a leaching solution containing K, Ca, Mg, and P.
[0021] Determination of K in the leaching solution by atomic absorption spectrometry + , Ca 2+ , Mg 2+ content, using the ammonium molybdate titration method to determine the H in the leach solution 3 PO 4 The content of calculated and obtained employing the present embodiment method to process phosphorus-potassium associated ore, wherein the leaching rate of phosphorus reaches 98.3%; The leaching rate of potassium is 96.2%; The leaching rate of Ca is 97.5%; The leaching rate of...
Embodiment 2
[0023] A method for efficiently leaching K, Ca, Mg, P from phosphorus and potassium associated ore by using extraction agent and hydrochloric acid acid hydrolysis technology, comprising the steps of: weighing 20g of phosphorus and potassium associated ore, CaF 2 3.0g, 52ml of 30% (mass concentration) HCl, and 2.5ml of n-heptanol were put into a three-necked flask in turn, heated up, started to stir, reacted at 80°C for 3h, washed with water and filtered to obtain a leaching solution containing K, Ca, Mg, and P.
[0024] Determination of K in the leaching solution by atomic absorption spectrometry + , Ca 2+ , Mg 2+ content, using the ammonium molybdate titration method to determine the H in the leach solution 3 PO 4 The content of calculated and obtained employing the present embodiment method to process phosphorus and potassium associated ore, wherein the leaching rate of phosphorus reaches 99.1%; The leaching rate of potassium is 98.5%; The leaching rate of Ca is 98.4%; Th...
Embodiment 3
[0026] A method for efficiently leaching K, Ca, Mg, P from phosphorus and potassium associated ore by using extraction agent and hydrochloric acid acid hydrolysis technology, comprising the steps of: weighing 20g of phosphorus and potassium associated ore, CaF 2 1.2g, 65ml of 27% HCl (mass concentration), 2.5ml of polyether polyol MN-1000, put them into a three-necked flask in turn, raise the temperature, start stirring, react at 70°C for 4h, wash and filter with water, and obtain K, Ca, Mg, P Leaching solution.
[0027] Determination of K in the leaching solution by atomic absorption spectrometry + , Ca 2+ , Mg 2+ content, using the ammonium molybdate titration method to determine the H in the leach solution 3 PO 4 The content of calculated and obtained employing the present embodiment method to process phosphorus and potassium associated ore, wherein the leaching rate of phosphorus reaches 99.5%; The leaching rate of potassium is 97.8%; The leaching rate of Ca is 99.3%; ...
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