CN202410817U - Three-product liquid-solid fluidized bed separator - Google Patents
Three-product liquid-solid fluidized bed separator Download PDFInfo
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- CN202410817U CN202410817U CN201120538018.9U CN201120538018U CN202410817U CN 202410817 U CN202410817 U CN 202410817U CN 201120538018 U CN201120538018 U CN 201120538018U CN 202410817 U CN202410817 U CN 202410817U
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- separation chamber
- chamber
- water supply
- separation
- fluid bed
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Abstract
The utility model relates to a three-product liquid-solid fluidized bed separator, which comprises a top water distribution plate, wherein an inner separation chamber and an outer separation chamber are concentrically arranged on the top water distribution plate; the inner separation chamber is higher than the outer separation chamber, a feeding pipe is arranged in an upper opening of the inner separation chamber; upper openings of the inner separation chamber and the inner separation chamber are respectively provided with an overflow groove, bottoms of the two overflow grooves are provided with overflow ports; lower parts of the inner separation chamber and the outer separation chamber are symmetrically provided with a plurality of discharging holes close to the top water distribution plate, a concentric discharging weir plate is arranged between the inner separation chamber and the outer separation chamber and is positioned on the top water distribution plate; the discharging weir plate is higher than the discharging holes in the lower parts of the inner separation chamber and the outer separation chamber; an inner water supply chamber and an outer water supply chamber are concentrically arranged under the top water distribution plate and correspond to the inner separation chamber and the outer separation chamber; and the inner water supply chamber and the outer water supply chamber are closed and are respectively provided with a water inlet. The utility model can be widely suitable for separating materials which contain more intermediate-density materials and are difficult in separation at high precision.
Description
Technical field
The utility model relates to a kind of separator, and particularly about a kind of Concentrating Field that is used for, the crowd separates to fine grained, to obtain the liquid-solid fluid bed separation machine of three products.
Background technology
Traditional liquid-solid fluid bed separation machine is a square or circular cell body; Water imports in the bucket from the bottom and upwards flows; Material feeds from the staving central upper portion; After being got in the bucket by the material of sorting, have different hindered falling speed owing to particle self granularity and density vary in size, the approaching material crowd of sinking speed and ascending current speed forms more stable interfere with layer in the bucket bottom; Cause and disturb sinking speed in the bed, and big and heavy particle can see through bed and gets into underflow less than the overflow and going out of the fine particle of ascending current speed from top.This shows, traditional liquid-solid fluid bedly can only material that treat sorting be divided into two products, be i.e. overflow product and underflow product.
When by the intermediate density thing in the sorting material more for a long time; During for example for the higher coarse slime of sorting intermediate density thing content; Traditional liquid-solid fluid bed sorting difficulty increases, and sharpness of separation descends, and this moment, this part intermediate density thing was randomized to either overflow or underflow; Can cause overflow product ash content to increase or the reduction of underflow product ash content, cause cleaned coal or tail coal off quality.
Can take two sections separating methods for addressing the above problem, realize through dual mode: a kind of mode is to first section overflow product sorting once more, and another kind of mode is to first section underflow product sorting once more.Because the concentration of first section overflow product is generally lower, if being carried out sorting meeting once more, it cause sorting capability to reduce, therefore generally do not adopt first kind of mode.
Summary of the invention
To the problems referred to above, the purpose of the utility model provide a kind of can be to comprising the three products liquid-solid fluid bed separation machine that the much more difficult sorting materials of intermediate density thing carry out the high accuracy sorting.
For realizing above-mentioned purpose, the utility model is taked following technical scheme: a kind of three products liquid-solid fluid bed separation machine is characterized in that: it comprises that one has the top moisture fabric swatch of through hole, and a separation chamber and an outer separation chamber in one are set on the moisture fabric swatch of top with one heart; Wherein, interior separation chamber is higher than outer separation chamber, and feeding pipe is set in the open topped; Interior separation chamber all is provided with overflow launder outward with outer separation chamber open topped, and two isopipe root all are provided with overfall; Interior separation chamber and outer separation chamber bottom near moisture fabric swatch place, top, all are symmetrical set some discharge gates; Corresponding with interior separation chamber and outer separation chamber, a water supply chamber and an outer water supply chamber in one are set under the moisture fabric swatch of top with one heart; Interior water supply chamber all seals with outer water supply chamber lower end, sets into the mouth of a river respectively, and the corresponding separation chamber of respectively doing for oneself provides ascending current.
The water inlet of water supply chamber is arranged on its bottom centre in above-mentioned; The water inlet of outer water supply chamber is symmetricly set on its sidewall.
In above-mentioned between separation chamber and the outer separation chamber, on the moisture fabric swatch of top, a concentric discharge weir plate is set, the discharge gate of separation chamber and outer separation chamber bottom in the discharge weir plate is higher than.
The discharge gate of separation chamber and outer separation chamber bottom all is provided with the gate of a control flow in above-mentioned.
The discharge gate of separation chamber and outer separation chamber bottom is two in above-mentioned, and the line of interior separation chamber two discharge gates is vertical each other with the line of outer separation chamber two discharge gates.
Separation chamber and outer separation chamber in above-mentioned, and interior water supply chamber all is cylindric with outer water supply chamber.
The utility model is owing to take above technical scheme; It has the following advantages: 1, the utility model is owing to adopt two separate separation chamber; Utilize the hindered falling speed of different densities in the ascending current, granularity particle different; Therefore combined sorting material to be selected can increase substantially sharpness of separation, particularly can solve the sorting problem to the coal that selects like the difficulty that comprises more intermediate density thing.2, the utility model is owing to adopt two separate, isolation separation chamber's combined sorting materials to be selected; Through first section and second section sorting; Obtain: first section overflow, second section overflow and second section underflow, compare with traditional screening installation, can product of more than enough acquisition.3, the discharge gate gate of the underflow of two separation chamber of the utility model is independent separately; Interior outer water chamber is also independent separately; Therefore can control the quality of final products through the aperture of regulating ascending water speed and gate; Can be mixed into final overflow product according to its quality and first section overflow product like second section overflow product, also can be separately as middle product, its controllable quality ability is significantly strengthened.4, the utility model packing density sensor and PID control system as required to control product quality more accurately, has certain extended capability.The utility model can be widely used for the sorting of material, particularly to comprising the material of the more difficult choosing of intermediate density thing, like the sorting of coal.
Description of drawings
Fig. 1 is the structural representation of the utility model
Fig. 2 is the vertical view at the utility model A-A place
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is carried out detailed description.
As shown in Figure 1, the utility model comprises that one has the top moisture fabric swatch 1 of through hole, and a separation chamber 2 and an outer separation chamber 3 in one are set on the top moisture fabric swatch 1 with one heart.Wherein, interior separation chamber 2 than outer separation chamber 3 height, is provided with feeding pipe 4 as first section separation chamber in the open topped.Interior separation chamber 2 open topped are provided with 21, the first sections overflow launder 21 bottoms of first section overflow launder outward first section overfall 22 are set, as first section overflow outlet; Interior separation chamber 2 bottoms near top moisture fabric swatch 1 place, are symmetrical set some discharge gates 23, as first section apex, are example with two only among the figure, but are not limited thereto.Outer separation chamber 3 is as second section separation chamber, and open topped is provided with 31, the second sections overflow launder 31 bottoms of second section overflow launder outward second section overfall 32 is set, as second section overflow outlet; Outer separation chamber 3 bottoms near top moisture fabric swatch 1 place, are symmetrical set some discharge gates 33, as second section apex, are example with two only among the figure, but are not limited thereto.
In view of treating that sorting material density is formed, the difference of granularmetric composition; During sorting, ascending current speed required in the inside and outside separation chamber 2,3 is also different, therefore; Corresponding with interior separation chamber 2 and outer separation chamber 3, top moisture fabric swatch is provided with a water supply chamber 5 and an outer water supply chamber 6 in one for 1 time with one heart.Inside and outside water supply chamber 5,6 lower ends are all sealed, and are respectively arranged with water inlet, and the corresponding separation chamber of respectively doing for oneself provides ascending current, is independent of each other.
In the foregoing description, the water inlet 51 of interior water supply chamber 5 can be arranged on its bottom centre.The water inlet 61 of outer water supply chamber 6 can be symmetricly set on its sidewall.
In the foregoing description; Inside and outside separation chamber 2, between 3, a concentric discharge weir plate 7 can also be set on top moisture fabric swatch 1, discharge weir plate 7 is higher than the discharge gate 23,33 of inside and outside separation chamber 2,3 bottoms; Purpose is the direction of motion of first section underflow of control; Make first section underflow separation chamber 3 outside the top entering of discharge weir plate 7, thereby avoid first section underflow directly to import second section underflow, cause the streams short circuit.
In the foregoing description, the discharge gate 23,33 of inside and outside separation chamber 2,3 is provided with the gate of a control flow.
In the foregoing description, the line of 3 liang of discharge gates 33 of the line of 2 liang of discharge gates 23 of interior separation chamber and outer separation chamber is vertical each other, and purpose is to avoid first section underflow just to get into second section underflow without the abundant sorting of outer separation chamber 3.
In the foregoing description, inside and outside separation chamber 2,3 and inside and outside water supply chamber 5,6 all are cylindric.
The utility model device is in use:
First section entry and second section entry respectively in water inlet 51,61 gets into water supply chamber 5 and outside water supply chamber 6; Two strands of current get into corresponding interior separation chamber 2 and outer separation chamber 3 respectively through top moisture fabric swatch 1, interior separation chamber 2 with outside two strands of different ascending currents of separation chamber's 3 formation flow velocitys.At this moment, treat that sorting material feeds interior separation chamber 2, i.e. first section separation chamber from top to bottom from feeding pipe 4; The acting in conjunction that receives ascending current and particle gravity sub-elects two products, i.e. first section overflow and first section underflow, and the first section overflow that is generated discharged through overflow launder 21 and overfall 22; First section underflow then discharged through discharge gate 23, and imports outer separation chamber 3, i.e. second section separation chamber through discharge weir plate 7; Material as second section; Sorting once more, the second section overflow that is generated discharged through overflow launder 31 and overfall 32, and second section underflow then discharged through discharge gate 33.So far, material is accomplished twice sorting, obtains three products, is respectively first section overflow product, second section overflow product and second section underflow product.Wherein, second section overflow product can be mixed into final overflow product according to its quality and first section overflow product, also can use as middle product separately.
Above-mentioned each embodiment only is used to explain the utility model; Wherein the structure of each parts, connected mode etc. all can change to some extent; Every equivalents of on the basis of the utility model technical scheme, carrying out and improvement all should not got rid of outside the protection domain of the utility model.
Claims (10)
1. three products liquid-solid fluid bed separation machine, it is characterized in that: it comprises that one has the top moisture fabric swatch of through hole, and a separation chamber and an outer separation chamber in one are set on the moisture fabric swatch of said top with one heart; Wherein, said interior separation chamber is higher than said outer separation chamber, and feeding pipe is set in the open topped; Separation chamber and said outer separation chamber open topped all are provided with overflow launder outward in said, and two said isopipe root all are provided with overfall; Separation chamber and said outer separation chamber bottom in said near moisture fabric swatch place, said top, all are symmetrical set some discharge gates; Corresponding with said interior separation chamber and said outer separation chamber, a water supply chamber and an outer water supply chamber in one are set under the moisture fabric swatch of said top with one heart; Water supply chamber and said outer water supply chamber lower end are all sealed in said, set into the mouth of a river respectively, and the corresponding separation chamber of respectively doing for oneself provides ascending current.
2. a kind of three products liquid-solid fluid bed separation machine as claimed in claim 1 is characterized in that: the water inlet of water supply chamber is arranged on its bottom centre in said; The water inlet of said outer water supply chamber is symmetricly set on its sidewall.
3. a kind of three products liquid-solid fluid bed separation machine as claimed in claim 1; It is characterized in that: between said interior separation chamber and the said outer separation chamber; On the moisture fabric swatch of said top; One concentric discharge weir plate is set, said discharge weir plate be higher than said in the discharge gate of separation chamber and said outer separation chamber bottom.
4. a kind of three products liquid-solid fluid bed separation machine as claimed in claim 2; It is characterized in that: between said interior separation chamber and the said outer separation chamber; On the moisture fabric swatch of said top; One concentric discharge weir plate is set, said discharge weir plate be higher than said in the discharge gate of separation chamber and said outer separation chamber bottom.
5. like claim 1 or 2 or 3 or 4 described a kind of three products liquid-solid fluid bed separation machines, it is characterized in that: the discharge gate of separation chamber and said outer separation chamber bottom all is provided with the gate of a control flow in said.
6. like claim 1 or 2 or 3 or 4 described a kind of three products liquid-solid fluid bed separation machines; It is characterized in that: the discharge gate of separation chamber and said outer separation chamber bottom is two in said, and the line of said interior separation chamber two discharge gates is vertical each other with the line of said outer separation chamber two discharge gates.
7. a kind of three products liquid-solid fluid bed separation machine as claimed in claim 5; It is characterized in that: the discharge gate of separation chamber and said outer separation chamber bottom is two in said, and the line of said interior separation chamber two discharge gates is vertical each other with the line of said outer separation chamber two discharge gates.
8. like claim 1 or 2 or 3 or 4 or 7 described a kind of three products liquid-solid fluid bed separation machines, it is characterized in that: separation chamber and said outer separation chamber in said, and said interior water supply chamber and said outer water supply chamber all are cylindric.
9. a kind of three products liquid-solid fluid bed separation machine as claimed in claim 5 is characterized in that: separation chamber and said outer separation chamber in said, and said interior water supply chamber and said outer water supply chamber all are cylindric.
10. a kind of three products liquid-solid fluid bed separation machine as claimed in claim 6 is characterized in that: separation chamber and said outer separation chamber in said, and said interior water supply chamber and said outer water supply chamber all are cylindric.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120538018.9U CN202410817U (en) | 2011-12-20 | 2011-12-20 | Three-product liquid-solid fluidized bed separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120538018.9U CN202410817U (en) | 2011-12-20 | 2011-12-20 | Three-product liquid-solid fluidized bed separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202410817U true CN202410817U (en) | 2012-09-05 |
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ID=46735614
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201120538018.9U Withdrawn - After Issue CN202410817U (en) | 2011-12-20 | 2011-12-20 | Three-product liquid-solid fluidized bed separator |
Country Status (1)
| Country | Link |
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| CN (1) | CN202410817U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102441479A (en) * | 2011-12-20 | 2012-05-09 | 华北科技学院 | Liquid and solid fluidized bed sorting machine for three products and working method thereof |
| CN104549708A (en) * | 2014-12-30 | 2015-04-29 | 中国矿业大学 | Spiral up-flow type liquid-solid fluidized bed separation equipment and method |
| CN111450984A (en) * | 2020-04-16 | 2020-07-28 | 谢艳梅 | Underflow continuous quantitative discharge three-product interference bed separator |
-
2011
- 2011-12-20 CN CN201120538018.9U patent/CN202410817U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102441479A (en) * | 2011-12-20 | 2012-05-09 | 华北科技学院 | Liquid and solid fluidized bed sorting machine for three products and working method thereof |
| CN102441479B (en) * | 2011-12-20 | 2014-03-05 | 华北科技学院 | Liquid and solid fluidized bed sorting machine for three products and working method thereof |
| CN104549708A (en) * | 2014-12-30 | 2015-04-29 | 中国矿业大学 | Spiral up-flow type liquid-solid fluidized bed separation equipment and method |
| CN111450984A (en) * | 2020-04-16 | 2020-07-28 | 谢艳梅 | Underflow continuous quantitative discharge three-product interference bed separator |
| CN111450984B (en) * | 2020-04-16 | 2021-09-24 | 谢艳梅 | Underflow continuous quantitative discharge three-product interference bed separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20120905 Effective date of abandoning: 20140305 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20120905 Effective date of abandoning: 20140305 |