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
A phosphorus and potassium associated ore and extraction agent technology, applied in the industrial field, can solve the problems of hindering the acidolysis process, long reaction time, high reaction temperature, etc., and achieve the effects of reducing reaction time, alleviating corrosion hazards, reducing reaction temperature and
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
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) HCl 68ml, 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, 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, 30% (mass concentration) HCl 52ml, n-heptanol 2.5ml, put into a three-necked flask in turn, heat up, start stirring, react at 80°C for 3h, wash and filter with water, and obtain a leaching solution containing K, Ca, Mg, 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%; The leaching rate of Mg ...
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%;...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More