Phosphate rock flotation collector and preparation method thereof
A collector and phosphate rock technology, applied in flotation, solid separation, etc., to achieve the effects of improving concentrate grade and recovery rate, improving economic benefits, and reducing types
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Embodiment 1
[0049] A phosphate rock flotation collector is prepared from components in the following weight ratios:
[0050] Y 20,
[0051] S 80,
[0052] Described Y is made up of the component of following weight ratio:
[0053] Dodecylamine 60,
[0054] Mixed amine 20,
[0055] Hydrochloric acid 20,
[0056] Described S is made up of the component of following weight ratio:
[0057] Oleic Acid 40,
[0058] Benzyl hydroxamic acid 20,
[0059] caustic soda 30,
[0060] sulfuric acid 10,
[0061] Among the above raw materials, dodecylamine {CH 3 —(CH 2 ) 10 —CH 2 NH 2}, mixed amine {R—NH 2}, R is C 17~20 Alkyl, oleic acid {C 17 h 33 COOH}, benzyl hydroxamic acid {C 7 h 7 NO 2}, hydrochloric acid {HCl}, caustic soda {NaOH}, and sulfuric acid are commercially available products.
[0062] Preferably, the purity of the dodecylamine ≥ 95%, the purity of the mixed amine ≥ 95%, the mass percentage concentration of the hydrochloric acid ≥ 35%, the purity of the oleic acid ≥ 9...
Embodiment 2
[0074] A phosphate rock flotation collector is prepared from components in the following weight ratios:
[0075] Y 70,
[0076] S 30,
[0077] Described Y is made up of the component of following weight ratio:
[0078] Dodecylamine 30,
[0079] Mixed amine 40,
[0080] Hydrochloric acid 30,
[0081] Described S is made up of the component of following weight ratio:
[0082] Oleic acid 20,
[0083] Benzyl hydroxamic acid 40,
[0084] caustic soda 20,
[0085] sulfuric acid 20,
[0086] Among the above raw materials, dodecylamine {CH 3 —(CH 2 ) 10 —CH 2 NH 2}, mixed amine {R—NH 2}, R is C 17~20 Alkyl, oleic acid {C 17 h 33 COOH}, benzyl hydroxamic acid {C 7 h 7 NO 2}, hydrochloric acid {HCl}, caustic soda {NaOH}, and sulfuric acid are commercially available products.
[0087] Preferably, the purity of the dodecylamine ≥ 95%, the purity of the mixed amine ≥ 95%, the mass percentage concentration of the hydrochloric acid ≥ 35%, the purity of the oleic acid ≥ 9...
Embodiment 3
[0095] A phosphate rock flotation collector is prepared from components in the following weight ratios:
[0096] Y 40,
[0097] S60,
[0098] Described Y is made up of the component of following weight ratio:
[0099] Dodecylamine 45,
[0100] Mixed amine 35,
[0101] Hydrochloric acid 25,
[0102] Described S is made up of the component of following weight ratio:
[0103] Oleic Acid 30,
[0104] Benzyl hydroxamic acid 30,
[0105] caustic soda 25,
[0106] sulfuric acid 15,
[0107] Among the above raw materials, dodecylamine {CH 3 —(CH 2 ) 10 —CH 2 NH 2}, mixed amine {R—NH 2}, R is C 17~20 Alkyl, oleic acid {C 17 h 33 COOH}, benzyl hydroxamic acid {C 7 h 7 NO 2}, hydrochloric acid {HCl}, caustic soda {NaOH}, and sulfuric acid are commercially available products.
[0108] Preferably, the purity of the dodecylamine ≥ 95%, the purity of the mixed amine ≥ 95%, the mass percentage concentration of the hydrochloric acid ≥ 35%, the purity of the oleic acid ≥ 95...
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