Dehydration and upgrading system for high-water-content material
US-2022379317-A1 · Dec 1, 2022 · US
US12115539B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12115539-B2 |
| Application number | US-201917043600-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 24, 2019 |
| Priority date | Mar 14, 2019 |
| Publication date | Oct 15, 2024 |
| Grant date | Oct 15, 2024 |
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A wide-size-fraction flotation system and process includes feeding coal slime to be floated into a stirrer, adding water to the floating coal slime in the stirrer, stirring, then feeding same into a grading cyclone through a first feeding pump for pre-grading; after grading of the coal slime in the grading cyclone, feeding overflow in the grading cyclone into a flotation column through a second feeding pump for flotation, discharging flotation tailings through an underflow port of the flotation column, collecting flotation concentrates through an overflow port of the flotation column and feeding same into a bubble generator through a fourth feeding pump, and the flotation concentrates passing through the bubble generator and being fed from the bottom of a hydraulic flotation machine; and feeding underflow in the grading cyclone into the hydraulic flotation machine through a third feeding pump, for flotation and recovery.
Opening claim text (preview).
The invention claimed is: 1. A wide size fraction flotation process for coal washing and ash removal, comprising the following steps: in step 1: feeding coal slime to be floated into an agitator, adding water into the agitator, agitating and mixing the floating coal slime with the water to a homogeneous state, and feeding the mixture into a classifying cyclone by a first feeding pump for pre-classifying; in step 2: after the coal slime is classified in the classifying cyclone, feeding the overflow from the classifying cyclone into a flotation column by a second feeding pump for flotation, discharging the flotation tailings through an underflow port of the flotation column, while collecting the flotation concentrate through an overflow port of the flotation column and feeding the collected flotation concentrate into a bubble generator by a fourth feeding pump, and feeding the flotation concentrate into a hydraulic flotation machine through the bottom of the hydraulic flotation machine via the bubble generator; and in step 3: after the coal slime is classified in the classifying cyclone, feeding the underflow in the classifying cyclone into a hydraulic flotation machine by a third feeding pump for recovery by flotation. 2. The wide size fraction flotation process according to claim 1 , wherein the foaming agent is one or a combination of pine oil, cresol oil, terpineol, methyl isobutyl carbinol, methyl amyl alcohol, triethyl-1-alkane, sodium alkylbenzene sulfonate, alkyl sodium sulfate, polyethylene glycol ether and polyalcohol ether; and the collecting agent is one or a combination of kerosene and diesel oil. 3. The wide size fraction flotation process according to claim 1 , wherein in the step 2, when the flotation concentrate passes through the bubble generator, a certain amount of collecting agent and foaming agent are added and supplied to the hydraulic flotation machine as rising water flow of the hydraulic flotation machine to form a foaming layer. 4. The wide size fraction flotation process according to claim 3 , wherein in the step 3, the coarse coal slime underflow fed from the classifying cyclone is separated in the foaming layer in the hydraulic flotation machine, the flotation concentrate is collected through the overflow port of the hydraulic flotation machine, while the flotation tailings are discharged from the underflow port of the hydraulic flotation machine. 5. The wide size fraction flotation process according to claim 3 , wherein in the step 3, the coarse coal slime underflow fed from the classifying cyclone is separated in the foaming layer in the hydraulic flotation machine, the flotation concentrate is collected through the overflow port of the hydraulic flotation machine, while the flotation tailings are discharged from the underflow port of the hydraulic flotation machine. 6. The wide size fraction flotation process according to claim 3 , wherein the foaming agent is one or a combination of pine oil, cresol oil, terpineol, methyl isobutyl carbinol, methyl amyl alcohol, triethyl-1-alkane, sodium alkylbenzene sulfonate, alkyl sodium sulfate, polyethylene glycol ether and polyalcohol ether; and the collecting agent is one or a combination of kerosene and diesel oil.
Pneumatic {(mixing gases or vapours with liquids B01F23/20)} · CPC title
using centrifugal forces · CPC title
specially adapted for coal · CPC title
Combinations of wet processes or apparatus with other processes or apparatus, e.g. for dressing ores or garbage · CPC title
by sink-float separation · CPC title
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