CN110052062B - Thickener - Google Patents
Thickener Download PDFInfo
- Publication number
- CN110052062B CN110052062B CN201910463445.6A CN201910463445A CN110052062B CN 110052062 B CN110052062 B CN 110052062B CN 201910463445 A CN201910463445 A CN 201910463445A CN 110052062 B CN110052062 B CN 110052062B
- Authority
- CN
- China
- Prior art keywords
- central cylinder
- thickener
- feeding pipe
- tank
- pipe
- 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.)
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- 239000002562 thickening agent Substances 0.000 title claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 9
- 230000005540 biological transmission Effects 0.000 claims abstract description 4
- 230000005484 gravity Effects 0.000 claims description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 11
- 239000011707 mineral Substances 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 3
- 230000018044 dehydration Effects 0.000 abstract description 2
- 238000006297 dehydration reaction Methods 0.000 abstract description 2
- 238000007790 scraping Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004021 metal welding Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/02—Settling tanks with single outlets for the separated liquid
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Bulkheads Adapted To Foundation Construction (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention belongs to the technical field of material dehydration, and particularly relates to a thickener, which is characterized by comprising a main tank body, a central cylinder arranged in the center of the main tank body, a receiving tank rotationally connected with the central cylinder, a feeding pipe I with the tail part connected with the upper part of the receiving tank, a feeding pipe II with the head part connected with the bottom of the receiving tank, a working bridge rotationally connected with the central cylinder, a transmission device connected with the working bridge, a scraper connected with the working bridge, an overflow pipe arranged in the central cylinder, an underflow tank arranged in the central cylinder and extending downwards to the outside of the main tank body, and four portal holes arranged along the outer circumference of the bottom of the central cylinder, wherein the four portal holes are communicated with the underflow tank. The thickener provided by the invention has a simple structure and reasonable design, can realize the functions of settling coarse-grain minerals in a shallow groove area and settling fine-grain minerals in a deep groove area, and can realize intermittent ore feeding in the same area, so that the influence of continuous ore pulp flow on the settling effect is avoided.
Description
Technical Field
The invention belongs to the technical field of material dehydration, and particularly relates to a thickener.
Background
The thickener is solid-liquid separation equipment based on gravity sedimentation, and generally adopts concrete, wood or metal welding plates as structural materials to build a cylindrical shallow groove with a cone bottom. The ore pulp with the solid weight of 10-20% can be concentrated into the underflow ore pulp with the solid content of 45-55% by gravity sedimentation, and the thickened underflow ore pulp is discharged from a bottom flow port at the bottom of the thickener under the action of a rake which is arranged in the thickener and runs slowly. The upper part of the thickener produces cleaner clarified liquid (overflow) which is discharged from the annular chute at the top. If the content of coarse fraction minerals in ore pulp is more, materials are quickly settled in the central area of a thickener, a pressing harrow phenomenon is easy to generate, and the concentration of underflow is lower in a shallow groove area due to insufficient settlement height, so that the phenomenon has adverse effects on production.
Disclosure of Invention
The invention aims to provide a thickener capable of settling coarse-grained minerals in a shallow tank area and settling fine-grained minerals in a deep tank area.
The aim of the invention is realized by the following technical scheme:
the thickener of the invention is characterized by comprising a main tank body, a central cylinder arranged at the center of the main tank body, a receiving tank arranged at the top of the central cylinder and rotationally connected with the central cylinder through a rotary table, a feeding pipe I with the tail part connected with the upper part of the receiving tank, a feeding pipe II with the head part connected with the bottom of the receiving tank, a working bridge arranged at the upper part of the central cylinder and rotationally connected with the central cylinder, a transmission device connected with the working bridge, a scraper connected with the working bridge through a rake frame, an overflow pipe arranged in the central cylinder, an underflow tank arranged in the central cylinder and downwardly extending to the outside of the main tank body, four portal holes arranged along the outer circumference of the bottom of the central cylinder and communicated with the underflow tank, wherein the bottom of the overflow pipe passes through the underflow tank,
the ore feeding pipe II is supported by the working bridge, an inclined pipe is welded at the tail of the ore feeding pipe II, the length of the inclined pipe, which is at the radial distance from the main groove body to the cofferdam, is 0.9m-1.1m, and the inclined pipe is lower than the upper surface of the cofferdam by 0.9m-1.1m in the vertical direction.
The rotary table comprises a bearing seat fixed on the central cylinder, a bearing arranged on the bearing seat, and the material receiving groove connected with the bearing.
The ore feeding pipe I and the ore feeding pipe II are obliquely arranged according to the gravity gradient of ore pulp.
The bottom surface of the scraping plate is parallel to the bus of the main groove body, and a gap of 95-105 mm is reserved.
The upper part of the bottom launder is of a funnel structure, a wide opening of the funnel is tangent to the central cylinder, and the elevation of the tangent line is lower than 1.4m-1.6m of the cofferdam.
The invention has the advantages that:
the thickener provided by the invention has a simple structure and reasonable design, can realize the functions of settling coarse-grain minerals in a shallow groove area and settling fine-grain minerals in a deep groove area, and can realize intermittent ore feeding in the same area, so that the influence of continuous ore pulp flow on the settling effect is avoided.
Drawings
Fig. 1 is a schematic structural view of the present invention.
Fig. 2 is a top view of fig. 1 of the present invention.
Detailed Description
Specific embodiments of the present invention are further described below with reference to the accompanying drawings.
As shown in fig. 1 and 2, the thickener of the present invention is characterized by comprising a main tank body 1, a central cylinder 7 arranged at the center of the main tank body 1, a receiving tank 5 arranged at the top of the central cylinder 7 and rotationally connected with the central cylinder 7 through a rotary table 6, a feeding pipe i 10 with the tail connected with the upper part of the receiving tank 5, a feeding pipe ii 11 with the head connected with the bottom of the receiving tank 5, a working bridge 2 arranged at the upper part of the central cylinder 7 and rotationally connected with the central cylinder 7, a transmission device 4 connected with the working bridge 2, a scraper 3 connected with the working bridge 2 through a rake frame, an overflow pipe 8 arranged inside the central cylinder 7, four gate-shaped holes arranged along the outer circumference of the bottom of the central cylinder 7 and communicated with the underflow tank 9, an overflow pipe 8 passing through the underflow tank 9 and leaving a connecting pipe flange,
the ore feeding pipe II 11 is supported by the working bridge 2, and an inclined pipe is welded at the tail of the ore feeding pipe II 11, the length of the inclined pipe, which is positioned at the radial distance of the main groove body 1, from the cofferdam is 0.9m to 1.1m, and the inclined pipe is lower than the upper surface of the cofferdam by 0.9m to 1.1m in the vertical direction. The ore feeding pipe I10 and the ore feeding pipe II 11 are obliquely arranged according to the gravity gradient of ore pulp, the tail part of the ore feeding pipe I10 is inserted into the upper part of the receiving groove 5, and the high point of the ore feeding pipe II 11 is connected with the bottom of the receiving groove 5.
The rotary table 6 comprises a bearing seat fixed on the central cylinder 7, a bearing arranged on the bearing seat, and the material receiving groove 5 is connected with the bearing.
The bottom surface of the scraping plate 3 is parallel to the bus of the main groove body 1, and a gap of 95mm-105mm is reserved.
The upper part of the underflow groove 9 is of a funnel structure, a wide opening of the funnel is tangent to the central cylinder 7, the elevation of the tangent is lower than 1.4m-1.6m of the cofferdam, a narrow opening of the funnel is connected with a pipeline,
when the invention is applied, ore pulp is fed into the receiving groove 5 through the ore feeding pipe I10, the driving device 4 drives the working bridge 2 to rotate, the receiving groove 5 rotates together with the ore feeding pipe II 11, materials are fed into the main groove body 1 along the circumferential direction through the ore feeding pipe II 11, ore pulp heavy and coarse fraction minerals are deposited in the shallow groove circumferential area of the main groove body 1, fine fraction minerals are deposited in the deep groove, clarified water overflows from a gate-shaped hole of the central cylinder 7 to the underflow groove 9 to be discharged, and the scraping plate 3 rakes the underflow into the underflow groove 9 and conveys the underflow to a designated position through a pump. The invention has simple structure, realizes that coarse-grain minerals are precipitated in the shallow groove area and fine-grain minerals are precipitated in the deep groove area of the thickener, and along with the rotation of the working bridge 2, the feeding pipe II 11 continuously feeds materials into the circumference area of the shallow part of the main groove body 1, and the same area intermittently feeds ores, thereby being beneficial to clarification of ore pulp.
Claims (5)
1. The thickener is characterized by comprising a main tank body, a central cylinder arranged at the center of the main tank body, a receiving tank arranged at the top of the central cylinder and rotationally connected with the central cylinder through a rotary table, a feeding pipe I with the tail part connected with the upper part of the receiving tank, a feeding pipe II with the head part connected with the bottom of the receiving tank, a working bridge arranged at the upper part of the central cylinder and rotationally connected with the central cylinder, a transmission device connected with the working bridge, a scraper connected with the working bridge through a rake frame, an overflow pipe arranged in the central cylinder, an underflow tank arranged in the central cylinder and downwardly extending to the outside of the main tank body, four portal holes arranged along the outer circumference of the bottom of the central cylinder, wherein the four portal holes are communicated with the underflow tank, the bottom of the overflow pipe passes through the underflow tank,
the ore feeding pipe II is supported by the working bridge, an inclined pipe is welded at the tail of the ore feeding pipe II, the length of the inclined pipe, which is at the radial distance from the main groove body to the cofferdam, is 0.9m-1.1m, and the inclined pipe is lower than the upper surface of the cofferdam by 0.9m-1.1m in the vertical direction.
2. The thickener of claim 1, wherein the rotary table comprises a bearing seat fixed on the central cylinder, a bearing arranged on the bearing seat, and the material receiving groove is connected with the bearing.
3. The thickener of claim 1, wherein the feeding pipe I and the feeding pipe II are arranged obliquely according to the gravity gradient of the ore pulp.
4. The thickener of claim 1, wherein the bottom surface of the scraper is parallel to the bus bar of the main tank body and has a gap of 95mm-105 mm.
5. The thickener of claim 1, wherein the upper part of the bottom launder is of a funnel structure, a wide opening of the funnel is tangent to the central cylinder, and the elevation of the tangent line is lower than 1.4m-1.6m of the cofferdam.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910463445.6A CN110052062B (en) | 2019-05-30 | 2019-05-30 | Thickener |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910463445.6A CN110052062B (en) | 2019-05-30 | 2019-05-30 | Thickener |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110052062A CN110052062A (en) | 2019-07-26 |
CN110052062B true CN110052062B (en) | 2024-03-08 |
Family
ID=67325158
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910463445.6A Active CN110052062B (en) | 2019-05-30 | 2019-05-30 | Thickener |
Country Status (1)
Country | Link |
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CN (1) | CN110052062B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN118294051B (en) * | 2024-04-08 | 2025-03-28 | 恒丰泰精密机械股份有限公司 | A thickener detection structure with stable support |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08266812A (en) * | 1995-03-30 | 1996-10-15 | Ito Seisakusho:Kk | Precipitator |
CN204395547U (en) * | 2015-01-06 | 2015-06-17 | 中国矿业大学 | Rotational-flow high-efficient deep cone thickener |
CN104815765A (en) * | 2015-04-14 | 2015-08-05 | 昆明理工大学 | Centrifugal classification equipment of micro-fine particle level materials |
CN104826372A (en) * | 2015-04-29 | 2015-08-12 | 淮北市中芬矿山机器有限责任公司 | Material evenly distributing device of flow stabilizing cylinder of central transmission thickener |
CN207012619U (en) * | 2017-06-14 | 2018-02-16 | 马钢(集团)控股有限公司 | A kind of concentrator |
CN108049440A (en) * | 2018-02-05 | 2018-05-18 | 中冶北方(大连)工程技术有限公司 | Dry type tailing back production mixing plant |
CN207614416U (en) * | 2017-11-25 | 2018-07-17 | 彝良驰宏矿业有限公司 | A kind of peripheral-traction concentrator circle chemicals dosing plant |
CN210114861U (en) * | 2019-05-30 | 2020-02-28 | 中冶北方(大连)工程技术有限公司 | Thickener |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI114899B (en) * | 2001-06-25 | 2005-01-31 | Outokumpu Oy | Process and apparatus for sedimentation and / or thickening of sludge |
-
2019
- 2019-05-30 CN CN201910463445.6A patent/CN110052062B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08266812A (en) * | 1995-03-30 | 1996-10-15 | Ito Seisakusho:Kk | Precipitator |
CN204395547U (en) * | 2015-01-06 | 2015-06-17 | 中国矿业大学 | Rotational-flow high-efficient deep cone thickener |
CN104815765A (en) * | 2015-04-14 | 2015-08-05 | 昆明理工大学 | Centrifugal classification equipment of micro-fine particle level materials |
CN104826372A (en) * | 2015-04-29 | 2015-08-12 | 淮北市中芬矿山机器有限责任公司 | Material evenly distributing device of flow stabilizing cylinder of central transmission thickener |
CN207012619U (en) * | 2017-06-14 | 2018-02-16 | 马钢(集团)控股有限公司 | A kind of concentrator |
CN207614416U (en) * | 2017-11-25 | 2018-07-17 | 彝良驰宏矿业有限公司 | A kind of peripheral-traction concentrator circle chemicals dosing plant |
CN108049440A (en) * | 2018-02-05 | 2018-05-18 | 中冶北方(大连)工程技术有限公司 | Dry type tailing back production mixing plant |
CN210114861U (en) * | 2019-05-30 | 2020-02-28 | 中冶北方(大连)工程技术有限公司 | Thickener |
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CN110052062A (en) | 2019-07-26 |
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