CN204396179U - A kind of system of molybdenum concentrate floatation agent recycling - Google Patents
A kind of system of molybdenum concentrate floatation agent recycling Download PDFInfo
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- CN204396179U CN204396179U CN201420784584.1U CN201420784584U CN204396179U CN 204396179 U CN204396179 U CN 204396179U CN 201420784584 U CN201420784584 U CN 201420784584U CN 204396179 U CN204396179 U CN 204396179U
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Abstract
The utility model discloses a kind of system of molybdenum concentrate floatation agent recycling, it comprises roughly selects flotation column, sweeps flotation device, two sweeps flotation device, concentrate pressure-filteration drying device, condensing unit, oily-water seperating equipment and recycling can.By again recycling the kerosene and the oily service efficiency that can improve molybdenum concentrate floatation agent of a small amount of 2# of separating out in concentrate drying sedimentation basin, saving flotation agent, thus having reduce further beneficiation cost.
Description
Technical field:
The utility model relates to the system of flotation agent recycling, particularly relates to a kind of system of molybdenum concentrate floatation agent recycling.
Background technology:
At present, the flotation agent after ore dressing is directly discharged with mine tailing by most molybdenum concntrate ore dressing plant, or the most sale at low prices of the flotation agent reclaimed in molybdenum concntrate dry run gives purchase producer, and recycling, does not cause wastage of material, increases production cost.
Utility model content:
The purpose of this utility model is the system providing a kind of molybdenum concentrate floatation agent recycling.
The purpose of this utility model is implemented by following technology, a kind of system of molybdenum concentrate floatation agent recycling, it comprises roughly selects flotation column, sweeps flotation device, two sweeps flotation device, concentrate pressure-filteration drying device, condensing unit, oily-water seperating equipment and recycling can, the described thick mine tailing slurry outlet roughly selecting flotation column is connected with the described charging aperture sweeping flotation device, described in sweep flotation device the mine tailing slurry outlet that sweeps be connected with described two charging apertures sweeping flotation device; The steam (vapor) outlet of described concentrate pressure-filteration drying device is connected with the air inlet of described condensing unit, the oil-water mixture outlet of described condensing unit is connected with the oil-water mixture import of described oily-water seperating equipment, the flowline of described oily-water seperating equipment is connected with the oil-in pipeline of described recycling can, the oil-out of described recycling can roughly select flotation column respectively by pipeline with described oil-in, described in sweep the oil-in of flotation device and described two oil-ins sweeping flotation device are connected.
Described oily-water seperating equipment comprises open-topped separator main body, the floating block slided up and down is provided with in described separator main body, outlet pipe is provided with bottom described separator main body, described separator main body lower sides is provided with mixed liquor feed tube, described mixed liquor feed tube is provided with liquid feeding pump, described separator main body sidewall above described mixed liquor feed tube is provided with oil gauge pipe, the described separator main body sidewall above described oil gauge pipe import is provided with flowline; Described separator main body top open part is provided with travel switch, and described travel switch and described liquid feeding pump are interlocked, and control the opening and closing of described liquid feeding pump; Oil-water interfaces switch is provided with in described separator main body between described mixed liquor feed tube and described oil gauge pipe, described outlet pipe and described flowline are respectively equipped with out water solenoid valve and go out solenoid, described oil-water interfaces switch respectively with described go out water solenoid valve and described go out solenoid be electrically connected, described oil-water interfaces switch controls the opening and closing of described outlet pipe and described flowline respectively.
The utility model has the advantage of, 1, flotation agent reclaims by the utility model, then the flotation agent of recovery be applied to roughly selecting of flotation and scan operation, reduce 2# oil consumption, while guarantee ore dressing quality, greatly reduce production cost, the cost of raw material more than 200 ten thousand yuan can be saved every year, improve the economic benefit of enterprise; 2, the oily-water seperating equipment structure in the utility model system is simple, and easy to operate, manufacturing cost is low, and operating cost is less, economize energy.
Accompanying drawing illustrates:
Fig. 1 is a kind of system schematic of molybdenum concentrate floatation agent recycling.
Fig. 2 is oily-water seperating equipment structural representation.
Roughly select flotation column 1, sweep flotation device 2, two sweep flotation device 3, concentrate pressure-filteration drying device 4, condensing unit 5, oily-water seperating equipment 6, recycling can 7, oil-water interfaces switch 8, oil gauge pipe 9, flowline 10, outlet pipe 11, goes out water solenoid valve 12, go out solenoid 13, separator main body 14, floating block 15, mixed liquor feed tube 16, liquid feeding pump 17, travel switch 18.
Detailed description of the invention:
Embodiment 1: a kind of system of molybdenum concentrate floatation agent recycling, it comprises roughly selects flotation column 1, sweeps flotation device 2, two and sweep flotation device 3, concentrate pressure-filteration drying device 4, condensing unit 5, oily-water seperating equipment 6 and recycling can 7, sweep flotation device 2 and two to sweep flotation device 3 and be pneumatic flotation cell, concentrate pressure-filteration drying device 4 comprises frame filter press and electromagnetic drying machine, and condensing unit 5 is screen collector.The thick mine tailing slurry outlet roughly selecting flotation column 1 is connected with the charging aperture sweeping flotation device 2, and the charging aperture that mine tailing slurry outlet and two sweeps flotation device 3 that sweeps sweeping flotation device 2 is connected; The steam (vapor) outlet of concentrate pressure-filteration drying device 4 is connected with the air inlet of condensing unit 5, the oil-water mixture outlet of condensing unit 5 is connected with the oil-water mixture import of oily-water seperating equipment 6, the flowline of oily-water seperating equipment 6 is connected with the oil-in pipeline of recycling can 7, and the oil-in that the oil-out of recycling can 7 sweeps flotation device 3 respectively by pipeline and the oil-in roughly selecting flotation column 1, the oil-in and two that sweeps flotation device 2 is connected.
Oily-water seperating equipment 6 comprises open-topped separator main body 14, the floating block 15 slided up and down is provided with in separator main body 14, outlet pipe 11 is provided with bottom separator main body 14, separator main body 14 lower sides is provided with mixed liquor feed tube 16, mixed liquor feed tube 16 is provided with liquid feeding pump 17, separator main body 14 sidewall above mixed liquor feed tube 16 is provided with oil gauge pipe 9, separator main body 14 sidewall above oil gauge pipe 9 import is provided with flowline 10; Separator main body 14 is built with oil-water mixture to be separated, and oil water mixture enters in separator main body 14 from the mixed liquor feed tube 16 of separator main body 14 bottom, and liquid feeding pump 17 provides the power of feed liquor; Separator main body 14 open top can keep separator main body 14 internal gas pressure to balance, and ensures liquid proper flow; Oil gauge pipe 9 in separator main body 14 upper portion side wall is used to indicate the height of oil level in separator main body 14, and oil gauge pipe 9 is the transparent glass tube be communicated with separator main body 14, the convenient height observing oil level; Flowline 10 is pipelines that after oil water mixture is separated, oil flows out, and outlet pipe 11 is passages that after oil water mixture is separated, water flows out.
Separator main body 14 top open part is provided with travel switch 18, and travel switch 18 and liquid feeding pump 17 are interlocked, and controls the opening and closing of liquid feeding pump 17; Oil-water interfaces switch 8 is provided with in separator main body 14 between mixed liquor feed tube 16 and oil gauge pipe 9, outlet pipe 11 and flowline 10 are respectively equipped with out water solenoid valve 12 and go out solenoid 13, oil-water interfaces switch 8 respectively with go out water solenoid valve 12 and go out solenoid 13 to be electrically connected, oil-water interfaces switch 8 controls the opening and closing of outlet pipe 11 and flowline 10 respectively.
The course of work is: first open liquid feeding pump 17, oil-water mixture constantly enters in separator main body 14 by mixed liquor feed tube 16, in separator main body 14, floating block 15 constantly rises with liquid level, when floating block 15 contacts the travel switch 18 of separator main body 14 top open part, switch motion, interlocking liquid feeding pump 17, controls to close mixed liquor feed tube 16, stops injecting liquid to separator main body 14;
After feed liquor, in separator main body 14, oil-water mixture liquid level is in released state, starts the oil-water interfaces switch 8 on separator main body 14 lower sides, if detection place liquid is oil, then control flowline 10 goes out solenoid 13, open flowline 10, isolated oil flows out through flowline 10, in this process, constantly fuel head is observed by oil gauge pipe 9, when fuel head is too low, closes oil-water interfaces switch 8, open liquid feeding pump 17 and be again filled with mixed liquor; If detection place liquid is water, control outlet pipe 11 goes out water solenoid valve 12, open outlet pipe 11, isolated water flows out through outlet pipe 11, along with continuously outflowing of water, oil level declines, and when pasta drops to detection place, then oil-water interfaces switch 8 controls flowline 10 goes out solenoid 13, open flowline 10, isolated oil flows out through flowline 10, in this process, constantly observes fuel head by oil gauge pipe 9, when fuel head is too low, close oil-water interfaces switch 8, open liquid feeding pump 17 and be again filled with mixed liquor, circulate successively.
Claims (1)
1. the system of a molybdenum concentrate floatation agent recycling, it is characterized in that, it comprises roughly selects flotation column, sweeps flotation device, two sweeps flotation device, concentrate pressure-filteration drying device, condensing unit, oily-water seperating equipment and recycling can, the described thick mine tailing slurry outlet roughly selecting flotation column is connected with the described charging aperture sweeping flotation device, described in sweep flotation device the mine tailing slurry outlet that sweeps be connected with described two charging apertures sweeping flotation device; The steam (vapor) outlet of described concentrate pressure-filteration drying device is connected with the air inlet of described condensing unit, the oil-water mixture outlet of described condensing unit is connected with the oil-water mixture import of described oily-water seperating equipment, the flowline of described oily-water seperating equipment is connected with the oil-in pipeline of described recycling can, the oil-out of described recycling can roughly select flotation column respectively by pipeline with described oil-in, described in sweep the oil-in of flotation device and described two oil-ins sweeping flotation device are connected;
Described oily-water seperating equipment comprises open-topped separator main body, the floating block slided up and down is provided with in described separator main body, outlet pipe is provided with bottom described separator main body, described separator main body lower sides is provided with mixed liquor feed tube, described mixed liquor feed tube is provided with liquid feeding pump, described separator main body sidewall above described mixed liquor feed tube is provided with oil gauge pipe, the described separator main body sidewall above described oil gauge pipe import is provided with described flowline; Described separator main body top open part is provided with travel switch, and described travel switch and described liquid feeding pump are interlocked, and control the opening and closing of described liquid feeding pump; Oil-water interfaces switch is provided with in described separator main body between described mixed liquor feed tube and described oil gauge pipe, described outlet pipe and described flowline are respectively equipped with out water solenoid valve and go out solenoid, described oil-water interfaces switch respectively with described go out water solenoid valve and described go out solenoid be electrically connected, described oil-water interfaces switch controls the opening and closing of described outlet pipe and described flowline respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420784584.1U CN204396179U (en) | 2014-12-12 | 2014-12-12 | A kind of system of molybdenum concentrate floatation agent recycling |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420784584.1U CN204396179U (en) | 2014-12-12 | 2014-12-12 | A kind of system of molybdenum concentrate floatation agent recycling |
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| CN204396179U true CN204396179U (en) | 2015-06-17 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104475271A (en) * | 2014-12-12 | 2015-04-01 | 内蒙古中西矿业有限公司 | System and method for recycling molybdenum concentrate flotation agent |
| CN105381870A (en) * | 2015-12-10 | 2016-03-09 | 中国地质科学院矿产综合利用研究所 | Beneficiation and enrichment method for molybdenum oxide ore |
| CN110259734A (en) * | 2019-05-29 | 2019-09-20 | 徐州工程学院 | A kind of hydraulic oil container |
-
2014
- 2014-12-12 CN CN201420784584.1U patent/CN204396179U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104475271A (en) * | 2014-12-12 | 2015-04-01 | 内蒙古中西矿业有限公司 | System and method for recycling molybdenum concentrate flotation agent |
| CN105381870A (en) * | 2015-12-10 | 2016-03-09 | 中国地质科学院矿产综合利用研究所 | Beneficiation and enrichment method for molybdenum oxide ore |
| CN105381870B (en) * | 2015-12-10 | 2018-07-10 | 中国地质科学院矿产综合利用研究所 | Beneficiation and enrichment method for molybdenum oxide ore |
| CN110259734A (en) * | 2019-05-29 | 2019-09-20 | 徐州工程学院 | A kind of hydraulic oil container |
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Address after: 012300, the Inner Mongolia Autonomous Region County, Wulanchabu, Zhuozi large elm Township, big Su Village Patentee after: Inner Mongolia Guocheng Industrial Co., Ltd Address before: 012300, the Inner Mongolia Autonomous Region County, Wulanchabu, Zhuozi large elm Township, big Su Village Patentee before: INNER MONGOLIA ZHONGXI MINING Co.,Ltd. |