CN208525929U - A kind of solid-liquid is from separator - Google Patents
A kind of solid-liquid is from separator Download PDFInfo
- Publication number
- CN208525929U CN208525929U CN201820727939.1U CN201820727939U CN208525929U CN 208525929 U CN208525929 U CN 208525929U CN 201820727939 U CN201820727939 U CN 201820727939U CN 208525929 U CN208525929 U CN 208525929U
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- China
- Prior art keywords
- slurry
- solid
- separator
- nozzle
- leakage sieve
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Abstract
The utility model discloses a kind of solid-liquids from separator, including clear liquid separating tank (8), slurry nozzle is provided in the clear liquid separating tank (8), at least two pieces of inclined leakage sieve plates (7) are disposed with below slurry nozzle, one end of leakage sieve plate (7) is that inclined mud is enriched with plate (6), it is provided with flooding nozzle (18) above the other end, the inclination angle of leakage sieve plate (7) is less than the inclination angle of mud enrichment plate (6).The utility model, which uses gravity and impulse force collective effect, to be realized and is separated by solid-liquid separation, and low energy consumption, only more compared with natural subsidence several agitating paddles and pumps, but energy consumption is to separate far below mechanism filter-pressing, and separative efficiency can be adjusted by control valve inlet velocity.
Description
Technical field
The utility model relates to sieve plate, enrichment plate and the nozzles in a kind of equipment for separating liquid from solid, especially clear liquid separating tank
Structure.
Background technique
It is frequently necessary to be separated by solid-liquid separation in modern industrial production, frequently with mechanism filter-pressing separation and settling tank natural subsidence
Separate two ways；The high, high production cost using mechanism filter-pressing separating energy consumption；It is separated using settling tank natural subsidence, is seldom disappeared
The energy is consumed, cost is minimum, but the time is long, is unfavorable for continuous production.Under current environment, drop is all being sought originally by Chemical Manufacture enterprise
The approach of synergy can either guarantee that device normally produces, and also reduces production cost, a set of while can take into account separating rate
Solid-liquid separation system with energy consumption is the target that enterprise is pursued.
Summary of the invention
Technical problem to be solved by the utility model is: providing a kind of solid-liquid from separator, meet enterprise's separation of solid and liquid
Demand, combine low cost and low energy consumption, disengaging time is slightly slow compared with mechanism filter-pressing, but significantly faster than natural subsidence,
And energy consumption is lower compared to mechanism filter-pressing.
The technical solution of the utility model is as follows:
A kind of solid-liquid is provided with slurry nozzle, slurry from separator, including clear liquid separating tank, the clear liquid separating tank
At least two pieces of inclined leakage sieve plates are disposed with below spout, one end of leakage sieve plate is that inclined mud is enriched with plate, separately
Flooding nozzle is provided with above one end, the inclination angle of leakage sieve plate is less than the inclination angle of mud enrichment plate.
Preferably, the inclination angle of the leakage sieve plate is 30 degree, and the inclination angle of the mud enrichment plate is 40 degree.
Preferably, the leakage sieve plate includes the grating of more parallel intervals distribution, is connected between grating by reinforcing rib,
Leakage sieve plate upper surface is equipped with the different sieve of two layers of mesh number.
Preferably, the slurry nozzle has multiple, and position height is consistent, is spaced apart along leakage sieve plate width direction.
Preferably, the flooding nozzle is flat spout, flooding nozzle and slurry nozzle through pipeline and slurry collecting tank
Connection, and slurry delivery pump and slurry control valve are provided on pipeline.
Preferably, valve, the slurry nozzle and slurry pipeline transport are provided between the flooding nozzle and slurry delivery pump
Valve is provided between pump.
Preferably, agitating paddle is equipped in the slurry collecting tank.
Preferably, the mud enrichment plate is trapezoidal, and wider one end is connected with leakage sieve plate, and narrow end is through pipeline
It is connected to slurry collecting slot, and is provided with mud valve on pipeline.
Preferably, agitating paddle is provided in the slurry collecting slot, slurry collecting slot is pumped through slurry control valve, slurry transportation
It is connect with cinder field.
Preferably, the clear liquid separation trench bottom is connected to through clear liquid control valve with clear liquid delivery pump.
The utility model compared with prior art, uses gravity and impulse force collective effect realizes and be separated by solid-liquid separation that low energy consumption,
Only more compared with natural subsidence several agitating paddles and pumps, but much separated less than mechanism filter-pressing.Separative efficiency passes through regulating valve
Door inlet velocity adjusts.
Detailed description of the invention
Fig. 1 is the equipment for separating liquid from solid schematic diagram of the utility model；
Fig. 2 is the equipment for separating liquid from solid working state schematic representation of the utility model；
Fig. 3 is the clear liquid separating tank top view in the utility model；
Fig. 4 is the leakage sieve plate section enlarged diagram of a-quadrant in Fig. 1；
Fig. 5~7 are flooding nozzle main view, vertical view and the side view of B area in Fig. 1；
Fig. 8 is the enlarged diagram in the region C in Fig. 3.
Specific embodiment
As shown in Figure 1, being a kind of solid-liquid from separator, which includes that sequentially connected slurry is collected from separator
Slot 17, clear liquid separating tank 8 and slurry collecting slot 20.
Clear liquid separating tank 8 is provided with the leakage sieve plate 7 at two pieces of 30 degree of parallel inclinations angle, inclination angle here from top to bottom
Refer to the bottom surface angle of leakage sieve plate 7 Yu clear liquid separating tank 8.Incline with 40 degree the lower one end in the position of each piece of leakage sieve plate 7
The mud enrichment plate 6 at oblique angle connects, and flooding nozzle 18 is arranged above higher one end in position.8 bottom clear liquid of clear liquid separating tank goes out
Clear liquid control valve 9 and clear liquid delivery pump 10 are provided on mouth pipeline.
The first agitating paddle 16 is provided in slurry collecting tank 17, and the grout outlet of slurry collecting tank 17 is provided with slurry control
Valve 15 and slurry delivery pump 14 processed, slurry delivery pump 14 are connect with slurry nozzle and flooding nozzle 18 respectively through pipeline, rinse spray
There are two mouth 18 is total, second layer valve 12 and third layer valve 13, the pipe of slurry nozzle are each configured on respective pipeline
Road is configured with first layer valve 11.
The second agitating paddle 3 is provided in slurry collecting slot 20, and slurry collecting slot 20 passes through on two pipelines and pipeline
First mud valve 4 and the second mud valve 5 are connect with the mud enrichment plate 6 in clear liquid separating tank 8 respectively.Slurry collecting slot 20
Slurry outlet pipeline on be provided with slurry control valve 2 and slurry transportation pump 1.
As shown in figure 3, being the top view of clear liquid separating tank 8, wherein it can be seen that slurry nozzle has 3, and position height one
It causes, is spaced apart along 7 width direction of leakage sieve plate.Mud enrichment plate 6 is trapezoidal, and wider one end is connected with leakage sieve plate 7,
Its narrow end is connected to through pipeline with slurry collecting slot 20.
Shown in as shown in Figure 4 and Figure 8, leakage sieve plate 7 includes the grating 72 of more parallel intervals distribution, is led between grating 72
It crosses reinforcing rib 19 to be connected, 7 upper surface of leakage sieve plate is equipped with the different sieve 71 of two layers of mesh number, for example, the mesh number of outermost layer strainer
For 60 mesh, the mesh number of inner screen is 100 mesh.
As shown in Fig. 5~7, the spout of flooding nozzle 18 is in flat, and the free end width of its spout is maximum.
As shown in Fig. 2, being the working principle of the present apparatus:
Slurry is sent into clear liquid separating tank 8 by slurry delivery pump 15 by slurry in slurry collecting tank 17, and slurry passes through clear liquid
The 8 first layer valve 11 of top 3 of separating tank, which falls, enters 7 primary filtration of first layer leakage sieve plate；Contain solid phase and liquid in slurry
Phase, solid phase are gradually collected under gravity and slurry fraction impulse force on mud enrichment plate 6, pass through the first mud valve of time switch
Door 4, discharges it into slurry collecting slot 20.The filtrate for carrying out primary filtration enters second layer leakage sieve plate 7, carries out second of solid-liquid
Separation, mud collect on mud enrichment plate 6, and filtrate enters 8 bottom of clear liquid separating tank, is sent by clear liquid delivery pump 10 next
A process.Mud is then unified to enter slurry collecting slot 20, sends to cinder field stockpiling by slurry transportation pump 1.
When equipment runs a period of time, mud is enriched on leakage sieve plate 7 and mud enrichment plate 6, forms part and agglomerate, this
When need to be cleaned, close first layer valve 11, open second layer valve 12 and third layer valve 13, slurry is rushed by flat
Wash 18 jet cleaning sieve 71 of nozzle and mud enrichment plate 6.
Claims (10)
1. a kind of solid-liquid is from separator, it is characterised in that: including clear liquid separating tank (8), setting in the clear liquid separating tank (8)
There is slurry nozzle, is disposed at least two pieces of inclined leakage sieve plates (7), one end of leakage sieve plate (7) below slurry nozzle
Plate (6) are enriched with for inclined mud, are provided with flooding nozzle (18) above the other end, the inclination angle of leakage sieve plate (7) is less than mud
The inclination angle of slurry enrichment plate (6).
2. a kind of solid-liquid according to claim 1 is from separator, it is characterised in that: the inclination of the leakage sieve plate (7)
Angle is 30 degree, and the inclination angle of mud enrichment plate (6) is 40 degree.
3. a kind of solid-liquid according to claim 1 is from separator, it is characterised in that: the leakage sieve plate (7) includes more
The grating (72) of root parallel interval distribution, is connected between grating (72), leakage sieve plate (7) upper surface is equipped with by reinforcing rib (19)
The different sieve of two layers of mesh number (71).
4. a kind of solid-liquid according to claim 1 is from separator, it is characterised in that: the slurry nozzle have it is multiple, and
Position height is consistent, and along leakage sieve plate (7), width direction is spaced apart.
5. a kind of solid-liquid according to claim 1 is from separator, it is characterised in that: the flooding nozzle (18) is flat
Shape spout, flooding nozzle (18) and slurry nozzle are connected to through pipeline with slurry collecting tank (17), and it is defeated that slurry is provided on pipeline
Send pump (14) and slurry control valve (15).
6. a kind of solid-liquid according to claim 5 is from separator, it is characterised in that: the flooding nozzle (18) and slurry
It is provided with valve between delivery pump (14), is provided with valve between the slurry nozzle and slurry delivery pump (14).
7. a kind of solid-liquid according to claim 5 is from separator, it is characterised in that: is set in the slurry collecting tank (17)
There is agitating paddle.
8. a kind of solid-liquid according to claim 1 is from separator, it is characterised in that: mud enrichment plate (6) is in ladder
Shape, wider one end are connected with leakage sieve plate (7), and narrow end is connected to through pipeline with slurry collecting slot (20), and on pipeline
It is provided with mud valve.
9. a kind of solid-liquid according to claim 7 is from separator, it is characterised in that: is set in the slurry collecting slot (20)
It is equipped with agitating paddle, slurry collecting slot (20) is connect through slurry control valve (2), slurry transportation pump (1) with cinder field.
10. a kind of solid-liquid according to claim 1 is from separator, it is characterised in that: clear liquid separating tank (8) bottom
It is connected to through clear liquid control valve (9) with clear liquid delivery pump (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820727939.1U CN208525929U (en) | 2018-05-16 | 2018-05-16 | A kind of solid-liquid is from separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820727939.1U CN208525929U (en) | 2018-05-16 | 2018-05-16 | A kind of solid-liquid is from separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208525929U true CN208525929U (en) | 2019-02-22 |
Family
ID=65393598
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820727939.1U Expired - Fee Related CN208525929U (en) | 2018-05-16 | 2018-05-16 | A kind of solid-liquid is from separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208525929U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355382A (en) * | 2018-05-16 | 2018-08-03 | 贵州开磷集团矿肥有限责任公司 | A kind of solid-liquid is from separator |
| CN110404309A (en) * | 2019-07-18 | 2019-11-05 | 无锡德林海环保科技股份有限公司 | Blue algae slurry enrichment facility |
-
2018
- 2018-05-16 CN CN201820727939.1U patent/CN208525929U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355382A (en) * | 2018-05-16 | 2018-08-03 | 贵州开磷集团矿肥有限责任公司 | A kind of solid-liquid is from separator |
| CN110404309A (en) * | 2019-07-18 | 2019-11-05 | 无锡德林海环保科技股份有限公司 | Blue algae slurry enrichment facility |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190222 Termination date: 20210516 |