CN201441845U - Concentration tank impurity separator in solid pipeline transportation - Google Patents
Concentration tank impurity separator in solid pipeline transportation Download PDFInfo
- Publication number
- CN201441845U CN201441845U CN2009200094997U CN200920009499U CN201441845U CN 201441845 U CN201441845 U CN 201441845U CN 2009200094997 U CN2009200094997 U CN 2009200094997U CN 200920009499 U CN200920009499 U CN 200920009499U CN 201441845 U CN201441845 U CN 201441845U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- overflow
- concentration tank
- concentration basin
- impurity separator
- 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.)
- Expired - Fee Related
Links
- 239000012535 impurity Substances 0.000 title claims abstract description 26
- 239000007787 solid Substances 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000000084 colloidal system Substances 0.000 claims abstract description 10
- 239000007788 liquid Substances 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 3
- 230000032258 transport Effects 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 7
- 239000011148 porous material Substances 0.000 abstract description 5
- 239000000919 ceramic Substances 0.000 abstract description 4
- 238000005115 demineralization Methods 0.000 abstract description 3
- 230000002328 demineralizing effect Effects 0.000 abstract description 3
- 239000002002 slurry Substances 0.000 abstract 2
- 239000012530 fluid Substances 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 241000209094 Oryza Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- -1 diabase Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000000247 postprecipitation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a concentration tank impurity separator in solid pipeline transportation, which comprises a concentration tank, a slurry inlet pipeline, an underflow pump-in pipeline and an underflow pump. The concentration tank is provided with the impurity separator. The impurity separator comprises an adjusting water inlet pipeline, an overflow groove and an overflow tank; the overflow groove is circular and arranged at the mouth of the concentration tank; the water in the adjusting water inlet pipeline is communicated into the concentration tank; fluid, particles and colloid overflowing from the mouth of the concentration tank flow into the overflow groove; the overflow groove is provided with a hole; and the overflow tank is communicated with the overflow groove through the hole. The concentration tank impurity separator in solid pipeline transportation can separate particles which are easy to block pores from the slurry, so as to ensure that the demineralization is high-efficiency and stable and the pores of a filter plate of a ceramic filter are not blocked.
Description
Technical field
The utility model relates to impurity separator of concentrated tank, especially relates to the device that concentration basin impurity separates in the solid pipeline transportation.
Background technology
In with pipeline transportation solid material field, can carry the material of different medium with pipeline, the material of different medium, especially solid material all must carry out processed and could export as finished product.
In real work, the material dewatering difficulty that has.For example: carry iron ore concentrate with pipeline, if when containing mineral such as diabase, clay in the iron ore concentrate, if fail particulate in the ore pulp is removed clean processing stage of in the concentration basin, particulate is very easy to stop up the filter pore of ceramic filter in this ore pulp, cause water separation capability to reduce, moisture raises, thereby influences demineralization technology.
Summary of the invention
The utility model has designed impurity separator of concentrated tank in a kind of solid pipeline transportation, and it can remove objectionable impurities such as the particulate in the ore pulp, colloid clean.
In order to solve the technical problem of above-mentioned existence, the utility model has adopted following scheme:
Impurity separator of concentrated tank in a kind of solid pipeline transportation comprises that concentration basin, ore pulp enter pipeline, underflow pumps into pipeline and underflow pump.On concentration basin, be provided with impurity separating device.Impurity separating device comprises that regulating water enters pipeline, overflow ditch and overflow launder, and the overflow ditch becomes ring type, is positioned at the Chi Kou place of concentration basin, and adjusting water enters ducted water and leads in the concentration basin; The liquid, particulate and the colloid that overflow from concentration basin Chi Kou flow into the overflow ditch, are provided with the hole on the overflow ditch, and overflow launder is communicated with described overflow ditch by described hole.
Impurity separator of concentrated tank compared with prior art has following beneficial effect in this solid pipeline transportation:
Because the utility model is provided with impurity separating device on concentration basin, can from ore pulp, separate stopping up the pore particulate in the ore pulp easily, thereby guarantee demineralization ability efficient stable, guarantee that also the filter pore of ceramic filter is not blocked.
Description of drawings
Fig. 1: the vertical view of impurity separator of concentrated tank in the transportation of the utility model solid pipeline;
Fig. 2: the front view of impurity separator of concentrated tank in the transportation of the utility model solid pipeline.
Description of reference numerals:
The 1-concentration basin; 2-overflow ditch; The 3-ore pulp enters pipeline; 4-concentration basin bottom; 5-regulates water and enters pipeline; The 6-overflow launder; The 7-underflow pumps into pipeline; 8-underflow pump.
The specific embodiment
Below in conjunction with Fig. 1 and Fig. 2, the utility model is described further:
Impurity separator of concentrated tank in a kind of solid pipeline transportation comprises that concentration basin 1, ore pulp enter pipeline 3, underflow pumps into pipeline 7 and underflow pump 8, is provided with impurity separating device on concentration basin 1.
Impurity separating device comprises that regulating water enters pipeline 5, overflow ditch 2 and overflow launder 6, and 2 one-tenths ring types of described overflow ditch are positioned at the Chi Kou place of concentration basin 1, and the water that adjusting water enters in the pipeline 5 leads in the described concentration basin 1; The liquid, particulate and the colloid that overflow from concentration basin 1 Chi Kou flow into the described overflow ditch 2, are provided with the hole on overflow ditch 2, and overflow launder 6 is communicated with overflow ditch 2 by the hole.Operation principle is as follows: during concentration basin 1 work, ore pulp enters pipeline 3 and regulates water and enters pipeline 5 and open simultaneously, enters that ore pulp contains particle and colloid in the concentration basin 1, and the proportion of this particle and colloid is littler than the proportion of water, so be suspended in waterborne.It is to strengthen spillway discharge that adjusting water enters the effect that adds production adjusting water in the pipeline 5, makes the sufficient overflow of particles suspended and colloid, and water that overflows from concentration basin 1 and particles suspended and colloid flow in the annular overflow ditch 2.Its principle just as rice washing, after impurity suspends in the rice washing process, all overflows in order to make impurity, just need add big yield.The solution that contains particle and colloid that enters into overflow ditch 2 enters into accident pool by overflow launder 6, pulls away with the mud car through post precipitation.
And the part of dehydration pumps into pipeline 7 by underflow easily, after concentration basin 1 bottom flows into underflow pump 8, sends into ceramic filter dehydration back again and exports as finished product.
Though described the utility model by above most preferred embodiment; but it is not in order to limit the utility model; under the situation that does not deviate from the utility model spirit and essence thereof; those skilled in the art can make various corresponding changes and distortion according to the utility model, but these corresponding changes or distortion all should belong to the protection domain of the utility model claim.
Claims (2)
1. impurity separator of concentrated tank during a solid pipeline transports comprises that concentration basin (1), ore pulp enter pipeline (3), underflow pumps into pipeline (7) and underflow pump (8), it is characterized in that: be provided with impurity separating device on described concentration basin (1); Described impurity separating device comprises that regulating water enters pipeline (5), overflow ditch (2) and overflow launder (6), described overflow ditch (2) becomes ring type, be positioned at the Chi Kou place of described concentration basin (1), the water that described adjusting water enters in the pipeline (5) leads in the described concentration basin (1); The liquid, particulate and the colloid that overflow from described concentration basin (1) Chi Kou flow into the described overflow ditch (2), are provided with the hole on described overflow ditch (2), and described overflow launder (6) is communicated with described overflow ditch (2) by described hole.
2. impurity separator of concentrated tank in the solid pipeline transportation according to claim 1, it is characterized in that: described overflow ditch (2) is connected with accident pool.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200094997U CN201441845U (en) | 2009-04-10 | 2009-04-10 | Concentration tank impurity separator in solid pipeline transportation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200094997U CN201441845U (en) | 2009-04-10 | 2009-04-10 | Concentration tank impurity separator in solid pipeline transportation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201441845U true CN201441845U (en) | 2010-04-28 |
Family
ID=42546523
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200094997U Expired - Fee Related CN201441845U (en) | 2009-04-10 | 2009-04-10 | Concentration tank impurity separator in solid pipeline transportation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201441845U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102166437A (en) * | 2011-04-08 | 2011-08-31 | 湖州金泰科技股份有限公司 | V-shaped water-collecting upflow sedimentation tank |
-
2009
- 2009-04-10 CN CN2009200094997U patent/CN201441845U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102166437A (en) * | 2011-04-08 | 2011-08-31 | 湖州金泰科技股份有限公司 | V-shaped water-collecting upflow sedimentation tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100428 Termination date: 20170410 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |