CN108525391A - A kind of efficiency material dewatering system - Google Patents
A kind of efficiency material dewatering system Download PDFInfo
- Publication number
- CN108525391A CN108525391A CN201810688759.1A CN201810688759A CN108525391A CN 108525391 A CN108525391 A CN 108525391A CN 201810688759 A CN201810688759 A CN 201810688759A CN 108525391 A CN108525391 A CN 108525391A
- Authority
- CN
- China
- Prior art keywords
- inspissator
- chamber
- enriched chamber
- overflow
- discharge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000000463 material Substances 0.000 title claims abstract description 34
- 239000012141 concentrate Substances 0.000 claims abstract description 10
- 239000004576 sand Substances 0.000 claims abstract description 8
- 239000000203 mixture Substances 0.000 claims description 4
- 241000196324 Embryophyta Species 0.000 abstract description 16
- 230000005540 biological transmission Effects 0.000 abstract description 4
- 238000012216 screening Methods 0.000 abstract description 3
- 241001391944 Commicarpus scandens Species 0.000 abstract description 2
- 208000019901 Anxiety disease Diseases 0.000 description 1
- 241001503485 Mammuthus Species 0.000 description 1
- 230000036506 anxiety Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
Abstract
The invention discloses a kind of efficiency material dewatering systems, it includes cyclone group, dewatering screen and inspissator, the feed inlet of the cyclone group receives the tailing in ore dressing plant, enriched chamber and overflow chamber are equipped in the inspissator, the overflow chamber is separated by downflow weir and enriched chamber, the material receiving port of the enriched chamber bottom connects the overflow port of cyclone group, dewatering screen is sent into the concentrate outlet of enriched chamber side after being mixed with the material of the sand setting of cyclone group outlet discharge, the ore pulp of the discharge outlet discharge of overflow chamber returns to ore dressing plant, the oversize of the dewatering screen discharge is sent into dry row's tailings impoundment place by belt conveyor, screenings flows into the enriched chamber of inspissator.Present invention inspissator greatly reduces the floor space of equipment, and transmission parts are not present in inspissator, it is not easy to break down instead of traditional concentrator.The system has well solved conventional materials dewatering system and has taken up a large area and the problem of high failure rate, be particularly suitable for small-sized ore dressing plant and use.
Description
Technical field
The present invention relates to a kind of material dewatering systems suitable for being used in the workshop in small-sized ore dressing plant, belong to isolation technics
Field.
Background technology
Material dewatering system is the equipment being separated by solid-liquid separation to material, usually by cyclone, dewatering screen and concentrator
Composition, the overflow substance of cyclone and the concentrated equipment of the screenings of dewatering screen carry out secondary concentration, and the underflow product after concentration is given
Enter dewatering screen to be carried out dehydrating.
Currently, the concentrator of material dewatering system used in ore dressing plant is generally concentrator, concentrator processing capacity is big, structure
It makes simply, easy to operate, power consumption is less, and technical indicator is preferable, but it takes up a large area, and is only applicable to mammoth mill,
It in the middle-size and small-size ore dressing plant of workshop land used anxiety and is not suitable for, and concentrator, there are transmission parts, failure rate is relatively high.
Invention content
It is an object of the invention to be directed to the drawback of the prior art, it is efficient to provide that a kind of floor space is small, failure rate is low
Material dewatering system, to meet the use needs in small-sized ore dressing plant.
To achieve the above object, the present invention adopts the following technical scheme that：
A kind of efficiency material dewatering system, composition include cyclone group, dewatering screen and inspissator, the charging of the cyclone group
Mouth receives the tailing in ore dressing plant, and enriched chamber and overflow chamber are equipped in the inspissator, and the overflow chamber passes through downflow weir and concentrates
Room separates, and the material receiving port of the enriched chamber bottom connects the overflow port of cyclone group, the concentrate outlet of enriched chamber side and eddy flow
Dewatering screen is sent into after the material mixing of the sand setting outlet discharge of device group, the ore pulp of the discharge outlet discharge of overflow chamber returns to ore dressing plant,
The oversize of the dewatering screen discharge is sent into dry row's tailings impoundment place by belt conveyor, and screenings flows into the concentration of inspissator
Room.
Above-mentioned efficiency material dewatering system, the drainage line being connected with the outlet of the concentrate of the enriched chamber of inspissator are equipped with
Densimeter.
The longitudinal section of above-mentioned efficiency material dewatering system, the enriched chamber of the inspissator is wide at the top and narrow at the bottom trapezoidal.
The side wall of above-mentioned efficiency material dewatering system, the inspissator is equipped with access hole.
Present invention inspissator greatly reduces equipment instead of traditional concentrator while ensureing processing capacity
Floor space, and inspissator be not present transmission parts, it is not easy to break down.The system has well solved conventional materials
Dewatering system takes up a large area and the problem of high failure rate, is particularly suitable for middle-size and small-size ore dressing plant and uses.
Description of the drawings
The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments.
Fig. 1 is the structural schematic diagram of the present invention.
It is marked in figure as follows：1, ore dressing plant, 2, dry row's tailings impoundment place, 3, cyclone group, 4, overflow pipe, 5, sand setting
Pipeline, 6, dewatering screen, 7, belt conveyor, 8, inspissator, 9, concentrate outlet, 10, discharge outlet, 11, access hole, 12, material receiving port,
13, downflow weir, 14, enriched chamber, 15, densimeter, 16, overflow chamber, 17, drainage pipeline, 18, drainage line.
Specific implementation mode
Funnel under a kind of sieve of small with floor space simple inspissator substitution dewatering screen without transmission parts of the present invention is dense
Contracting device is dehydrated recovery system with dewatering screen component material, to provide a kind of saving occupation of land, the good material dewatering of dehydrating effect
System.
Referring to Fig. 1, the invention mainly comprises cyclone group 3, dewatering screen 6, belt conveyor 7, inspissator 8,13 and of downflow weir
Densimeter 15.Wherein, enriched chamber 14 and overflow chamber 16 are equipped in inspissator 8.
The tailing in ore dressing plant 1 is connected with the material feeding end of cyclone group 3, the overflow port of cyclone group 3 by overflow pipe 4 with
The material receiving port 12 of 14 bottom of enriched chamber of inspissator connects, and the spigot of cyclone group 3 passes through sand setting pipeline 5 and dewatering screen 6
Material feeding end connects, inspissator 8 in the underface of dewatering screen 6, undersize material gravity flow flow into inspissator 8 enriched chamber 14 carry out it is dense
Contracting, enriched chamber 14 concentrate outlet 9 discharge material mixed with the sand setting of cyclone group 3 by drainage line 18 after feed it is de-
The material feeding end of water sieve 6 is equipped with densimeter 15 in the drainage line 18 of enriched chamber 14, and the discharge outlet 10 of overflow chamber 16 passes through draining
Pipeline 17 is connected with ore dressing plant 1, and product is sent by belt conveyor 7 to dry row's tailings impoundment place 20 on the sieve of dewatering screen 6.
The present invention the course of work be：Mill tailings enter cyclone group 3 and are concentrated, and overflow pulp feeds inspissator
Secondary concentration is carried out in 8, the sand setting product of cyclone group 3 feeds dewatering screen 6, and oversize passes through sieve after the dehydration of dewatering screen 6
Upper product belt conveyor 7 feeds dry row's tailings impoundment place 2, and undersize, which flows automatically, feeds the enriched chamber 14 of inspissator 8.Ore pulp passes through
After enriched chamber 14 concentrates, overflow flows into overflow chamber 16, then after the discharge of discharge outlet 10, is returned by the drainage pipeline 17 being attached thereto
It is back to ore dressing plant 1 and circulates in utilization, the overflow production concentration for returning to ore dressing plant 1 is 5% ~ 6%.Material after the concentration of concentrated room 14
It is carried out by 9 discharge of concentrate outlet, then through feeding dewatering screen 6 after the sand setting product mix of drainage line 18 and cyclone group 3
It is dehydrated again, densimeter 15 is installed in drainage line 18, to control discharge concentration.
Present invention inspissator has saved floor space, and because of it instead of funnel and concentrator under the sieve of dewatering screen
It is simple in structure easy, reduce maintenance capacity and equipment operating cost.It is the configuration of the present invention is simple, highly practical, it is suitable for land area
Nervous small-sized ore dressing plant and sewage treatment industry.
Claims (4)
1. a kind of efficiency material dewatering system, characterized in that composition includes cyclone group（3）, dewatering screen（6）And inspissator
（8）, the cyclone group（3）Feed inlet receive ore dressing plant（1）Tailing, the inspissator（8）It is interior to be equipped with enriched chamber（14）
The overflow chamber and（16）, the overflow chamber（16）Pass through downflow weir（13）With enriched chamber（14）Separate, the enriched chamber（14）Bottom
Material receiving port（12）Connect cyclone group（3）Overflow port, enriched chamber（14）The concentrate of side exports（9）With cyclone group（3）
Sand setting outlet discharge material mixing after be sent into dewatering screen（6）, overflow chamber（16）Discharge outlet（10）The ore pulp of discharge returns
Ore dressing plant（1）, the dewatering screen（6）The oversize of discharge passes through belt conveyor（7）It is sent into dry row's tailings impoundment place（2）, sieve
Lower logistics enters inspissator（8）Enriched chamber（14）.
2. a kind of efficiency material dewatering system according to claim 1, characterized in that with inspissator（8）Enriched chamber
（14）Concentrate outlet（9）Connected drainage line（18）It is equipped with densimeter（15）.
3. a kind of efficiency material dewatering system according to claim 1 or 2, characterized in that the inspissator（8）Concentration
Room（14）Longitudinal section be it is wide at the top and narrow at the bottom trapezoidal.
4. a kind of efficiency material dewatering system according to claim 3, characterized in that the inspissator（8）Side wall on
Equipped with access hole（11）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810688759.1A CN108525391A (en) | 2018-06-28 | 2018-06-28 | A kind of efficiency material dewatering system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810688759.1A CN108525391A (en) | 2018-06-28 | 2018-06-28 | A kind of efficiency material dewatering system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108525391A true CN108525391A (en) | 2018-09-14 |
Family
ID=63487499
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810688759.1A Pending CN108525391A (en) | 2018-06-28 | 2018-06-28 | A kind of efficiency material dewatering system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108525391A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201384871Y (en) * | 2009-01-21 | 2010-01-20 | 山东省环境保护科学研究设计院 | Whirl type reaction precipitator |
| CN203389378U (en) * | 2013-08-02 | 2014-01-15 | 大连玉源环境工程有限公司 | Efficient sludge-discharging radial-flow sedimentation basin |
| CN107224757A (en) * | 2017-06-07 | 2017-10-03 | 常州鼎众冷暖设备工程有限公司 | One planting sand water waterpower separates clean water device |
| CN107321493A (en) * | 2017-07-17 | 2017-11-07 | 首钢集团有限公司 | A kind of tailings glass system |
| CN208512058U (en) * | 2018-06-28 | 2019-02-19 | 唐山陆凯科技有限公司 | A kind of efficiency material dewatering system |
-
2018
- 2018-06-28 CN CN201810688759.1A patent/CN108525391A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201384871Y (en) * | 2009-01-21 | 2010-01-20 | 山东省环境保护科学研究设计院 | Whirl type reaction precipitator |
| CN203389378U (en) * | 2013-08-02 | 2014-01-15 | 大连玉源环境工程有限公司 | Efficient sludge-discharging radial-flow sedimentation basin |
| CN107224757A (en) * | 2017-06-07 | 2017-10-03 | 常州鼎众冷暖设备工程有限公司 | One planting sand water waterpower separates clean water device |
| CN107321493A (en) * | 2017-07-17 | 2017-11-07 | 首钢集团有限公司 | A kind of tailings glass system |
| CN208512058U (en) * | 2018-06-28 | 2019-02-19 | 唐山陆凯科技有限公司 | A kind of efficiency material dewatering system |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180914 |