Method for floatation of apatite using collector prepared from illegal cooking oils
A collector and gutter oil technology, applied in flotation, solid separation, etc., can solve the problems of no research reports, etc., and achieve the effects of simple process flow, improved competitiveness, and reduced production costs
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Embodiment 1
[0066] Example 1 Preparation of collector I
[0067] The waste oil is centrifuged to remove suspended solids, a certain amount of water is added to remove colloidal substances, dried and dehydrated, the clay is decolorized, and then hydrolyzed by adding sodium hydroxide, the reaction temperature is 60-80 ° C, the reaction time is 60 minutes, the amount of sodium hydroxide It is 2% of the quality of waste oil, after cooling the obtained hydrolyzate, use petroleum ether extraction, wherein the upper layer is a non-saponifiable matter, and the lower layer is a saponified matter; taking the saponified matter of the lower layer and adding a certain amount of hydrochloric acid with a mass concentration of 10% solution, so that the weight ratio of the mixed fatty acid and the mixed fatty acid sodium salt in the product is 1:1, that is, the collector I is obtained.
Embodiment 2
[0068] Example 2 Preparation of collector II
[0069] The waste oil is centrifuged to remove suspended solids, a certain amount of water is added to remove colloidal substances, dried and dehydrated, the clay is decolorized, and then sodium hydroxide is added for hydrolysis. The reaction temperature is 50-70 ° C, the reaction time is 70 minutes, and the amount of sodium hydroxide For 4% of the quality of waste oil, after cooling the obtained hydrolyzate, use petroleum ether to extract, wherein the upper layer is a non-saponifiable matter, and the lower layer is a saponified matter; The saponification of the lower layer is added to a certain amount of hydrochloric acid with a mass concentration of 8%. solution, so that the weight ratio of the mixed fatty acid and the mixed fatty acid sodium salt in the product is 1:10, that is, the collector II of the present invention is obtained.
Embodiment 3
[0070] Example 3 Preparation of collector III
[0071] The waste oil was centrifuged to remove suspended solids, a certain amount of water was added to remove colloidal substances, dried and dehydrated, the clay was decolorized, and then sodium hydroxide was added for hydrolysis. The reaction temperature was 70-90 ° C, the reaction time was 30 minutes, and the amount of sodium hydroxide It is 5% of the quality of the waste oil, after cooling the obtained hydrolyzate, use petroleum ether extraction, wherein the upper layer is a non-saponifiable matter, and the lower layer is a saponified matter; The saponified matter of the lower layer is added a certain amount of mass concentration and is 12% hydrochloric acid solution, so that the weight ratio of the mixed fatty acid and the mixed fatty acid sodium salt in the product is 10:1, that is, the collector III is obtained.
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