CN203315808U - Rapid single-layer settler - Google Patents
Rapid single-layer settler Download PDFInfo
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- CN203315808U CN203315808U CN2013200580332U CN201320058033U CN203315808U CN 203315808 U CN203315808 U CN 203315808U CN 2013200580332 U CN2013200580332 U CN 2013200580332U CN 201320058033 U CN201320058033 U CN 201320058033U CN 203315808 U CN203315808 U CN 203315808U
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- juice
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- settler
- cylindrical shell
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Abstract
The utility model aims at providing a rapid single-layer settler. The rapid single-layer settler comprises a juice passing pipe, a barrel and a juice outlet pipe, wherein an annular juice inlet groove is formed in the upper part inside the barrel, and the juice passing pipe passes through the wall of the barrel and is communicated with the annular juice inlet groove; more than two annular baffles are arranged in the barrel below the annular juice inlet groove. Sugar juice slowly and uniformly flows into the lower part of the barrel through the annular juice inlet groove so as to greatly reduce the risk that the sugar juice entering the settler impacts the bottom of the settler; the annular baffles are used for ensuring that the sugar juice stably settles in each annular baffle and is free of the influence of sugar juice flow. The rapid single-layer settler works stably and has the good juicing quality; the retention time of the sugar juice in the settler is shorter than that of the sugar juice in other settles; discharged sludge is solid, the quantity of the sludge is reduced, and the quantity of reflux is aslo reduced, and the burden of later-period filtration and retreatment is eased.
Description
Technical field
The utility model relates to a kind of solid-liquid separating equipment of the field application of refining sugar, and is specifically related to a kind of individual layer accelerated clarifier.
Background technology
The old-fashioned Multilayer precipitator of the most employings of the defeco-sulfitated juice settler in current domestic sugar refinery, part sugar refinery also adopts some single-layer settlers in recent years, as cylindrical shape single-layer settler, cylinder type parallel flow setting vessel.Because being all relies on the self gravitation sedimentation, the as easy as rolling off a log amount of being subject to processing and process conditions change and turn over the problem at the end, job insecurity.
Parallel flow setting vessel has been installed straight hydraulic barrier in body, syrup advance juice mouth and juice opening all at the top of body, syrup, from advancing the juice mouth and entering body, must be flowed by the passage through between hydraulic barrier, then arrives juice opening.This device has the effect of the convection current of the syrup of preventing in body.But rely on the self gravitation sedimentation because remain, when the syrup treating capacity changes, still can turn over the problem at the end.
The drum type brake single-layer settler is the principal mode that current sugar refinery is used, and by arranging into juice groove and juice outlet groove guiding syrup, relies on the self gravitation sedimentation, and the complete hollow of mid portion, easily be subject to fluctuation and process conditions impact.
The gravitational settling of syrup in settler is subject to the impact of the factors such as self temperature, process conditions and treating capacity, thereby cause syrup that convection current and disturbance occur in settler and cause the mud layer particle rolling settled down, go out the juice muddiness when serious and carry mud granule secretly, affect carrying out and the product quality of follow-up workshop section.
Therefore, sugar refinery settler easily turns over end problem now, job insecurity, and subsider juice turbidity and colour are higher, inefficiency, the time of staying is long, and the mud juice amount is large and rare, causes that sugar loss is serious.
The utility model content
The utility model aims to provide a kind of individual layer accelerated clarifier, effectively solves existing settler inefficiency, job insecurity, and the time of staying is long and easily turn over the defect such as the end.
Individual layer accelerated clarifier described in the utility model, comprised juice pipe, cylindrical shell, juice yield tube, and the top in described cylindrical shell is provided with annular and advances the juice groove, and described juice pipe excessively advances the juice groove through barrel with annular and is connected; Bottom in cylindrical shell is provided with the ring baffle more than two, and the lower openings that annular is advanced the juice groove is positioned at the below of ring baffle.
Described ring baffle be take the center of circle of cylindrical shell in the center of circle is distributed in cylindrical shell.
Top in described cylindrical shell is provided with interior annular juice outlet groove and outer ring juice outlet groove; Interior annular juice outlet groove is positioned at the ring baffle top, and annular is advanced the inner ring of juice groove; The outer ring juice outlet groove is positioned at the ring baffle top, and annular is entered juice groove outer ring.
Described interior annular juice outlet groove is set to one group or two groups.
Described outer ring juice outlet groove is set to one group or two groups.
Described cylindrical shell bottom is connected with tapered solid collection bucket.
In described solid collection bucket, mud-scraping apparatus is installed.
Described solid collection bucket bottom is connected with the solids-enriched bucket, and solids-enriched bucket bottom is provided with the mud juice pipe.
After entering the juice groove with the syrup of the abundant hybrid reaction of flocculant by the annular of crossing the juice pipe and enter settler, advance the juice groove via annular and slowly and equably divide inflow cylindrical shell bottom, greatly reduce the syrup that newly enters settler and impact the risk of the mud juice of settler bottom, simultaneously, solid particle larger in this process is lowered into the solid collection bucket at Action of Gravity Field, by mud-scraping apparatus, is scraped into the solids-enriched bucket and is concentrated; When syrup slowly rises arrival ring baffle zone, the working curved surface of ring baffle can flow and be stopped the syrup of non-radioactive line direction, follow the mobile tiny solid particle of syrup assembles on working curved surface, form larger particle, return to the mud juice enrichment region, newly do not entered the syrup impact also to the syrup of having carried out sedimentation simultaneously protective effect is provided, make syrup stable settlement in each ring baffle, be not subject to the mobile impact of syrup; The application of these two structures has effectively increased the sinking speed of syrup, effectively reduces the risk of turning over the end, and syrup is through after the ring baffle zone, pure and impure separation, and clear juice slowly rises, and from interior juice outlet groove and juice yield tube, discharges.
The design of interior juice outlet groove and outer juice outlet groove makes the discharge that syrup can uniform and stable, and increases the speed that syrup is discharged, thereby avoids the time of staying of syrup long, the loss of minimizing sugar.
The solid collection bucket of cylindrical shell bottom and the combination of mud-scraping apparatus, can scrape solid particle into the solids-enriched bucket effectively, and then discharged by the mud juice pipe, can promote the concentrated of solid particle can prevent that again precipitating sludge backflow from affecting the sedimentation of syrup.
In sum, the utility model working stability, go out the juice quality good, the time of staying of syrup in settler is shorter than other settlers, and institute's blowdown mud is solid, and the mud amount reduces, capacity of returns also reduces thereupon, and the burden that alleviates the later stage filtration and process, have a good application prospect.
The accompanying drawing explanation
Fig. 1 is profile of the present utility model.
Fig. 2 is top view of the present utility model.
Sequence number in figure and the structure of each several part and title are as follows:
1 was the juice pipe, and 2 is cylindrical shell, and 3 is juice yield tube, and 4 advance the juice groove for annular, and 5 is ring baffle, and 6 is interior annular juice outlet groove, and 7 is the solid collection bucket, and 8 is mud-scraping apparatus, and 9 is the solids-enriched bucket, and 10 is the mud juice pipe, and 11 is flocculation reactor, and 12 is the outer ring juice outlet groove.
The specific embodiment
As shown in Figures 1 and 2, the utility model comprised juice pipe 1, cylindrical shell 2, juice yield tube 3, and the tops in described cylindrical shell 2 are provided with annular and advance juice groove 4, and described juice pipe 1 excessively advances juice groove 4 through barrel with annular and is connected; Bottom in cylindrical shell 2 is provided with the ring baffle 5 more than two, and the lower openings that annular is advanced juice groove 4 is positioned at the below of ring baffle 5.
Top in described cylindrical shell 2 is provided with interior annular juice outlet groove 6 and outer ring juice outlet groove 12; Interior annular juice outlet groove 6 is positioned at ring baffle 5 tops, and annular is advanced the inner ring of juice groove 4; Outer ring juice outlet groove 12 is positioned at ring baffle 5 tops, and annular is entered juice groove 4 outer rings.
Described cylindrical shell 2 bottoms are connected with tapered solid collection bucket 7, in described solid collection bucket 7, mud-scraping apparatus 8 are installed, and described solid collection bucket 7 bottoms are connected with solids-enriched bucket 9, and solids-enriched bucket 9 bottoms are provided with mud juice pipe 10.
Below in conjunction with embodiment, the utility model is further illustrated.
The course of work of the present utility model is as follows:
Syrup through passing through juice pipe 1 after flocculation reactor 11 and flocculant reaction mixing, the annular that enters settler is advanced juice groove 4, advance juice groove 4 via annular and slowly and equably divide inflow cylindrical shell 2 bottoms, solid particle larger in this process is lowered into solid collection bucket 7 at Action of Gravity Field, and scrape into solids-enriched bucket 9 and concentrated by mud-scraping apparatus 8, then by mud juice pipe 10, discharged;
Syrup slowly rises while arriving ring baffle 5 regional, the working curved surface of ring baffle 5 can flow and be stopped the syrup of non-radioactive line direction, follow the mobile tiny solid particle of syrup assembles on working curved surface, form larger particle, return to solid collection bucket 7, newly do not entered the syrup impact also to the syrup of having carried out sedimentation simultaneously protective effect is provided, make syrup stable settlement in each ring baffle, be not subject to the mobile impact of syrup;
Syrup is through after the zone of ring baffle 5, pure and impure separation, and clear juice slowly rises, and in arriving, when juice outlet groove 6 and outer juice outlet groove 12 height, enters interior juice outlet groove 6 and outer juice outlet groove 12, through juice yield tube 3, discharges.
Claims (8)
1. an individual layer accelerated clarifier, comprised juice pipe (1), cylindrical shell (2), juice yield tube (3), it is characterized in that: the top in described cylindrical shell (2) is provided with annular and advances juice groove (4), and described juice pipe (1) excessively advances juice groove (4) through barrel with annular and is connected; Bottom in cylindrical shell (2) is provided with the ring baffle (5) more than two, and the lower openings that annular is advanced juice groove (4) is positioned at the below of ring baffle (5).
2. individual layer accelerated clarifier as claimed in claim 1 is characterized in that: described ring baffle (5) be take the center of circle of cylindrical shell (2) in the center of circle is distributed in cylindrical shell (2).
3. individual layer accelerated clarifier as claimed in claim 1 is characterized in that: the top in described cylindrical shell (2) is provided with interior annular juice outlet groove (6) and outer ring juice outlet groove (12); Interior annular juice outlet groove (6) is positioned at ring baffle (5) top, and annular is advanced the inner ring of juice groove (4); Outer ring juice outlet groove (12) is positioned at ring baffle (5) top, and annular is entered juice groove (4) outer ring.
4. individual layer accelerated clarifier as claimed in claim 3, it is characterized in that: described interior annular juice outlet groove (6) is set to one group or two groups.
5. individual layer accelerated clarifier as claimed in claim 3, it is characterized in that: described outer ring juice outlet groove (12) is set to one group or two groups.
6. as any one described individual layer accelerated clarifier of claim 1～5, it is characterized in that: described cylindrical shell (2) bottom is connected with tapered solid collection bucket (7).
7. individual layer accelerated clarifier as claimed in claim 6, is characterized in that: mud-scraping apparatus (8) is installed in described solid collection bucket (7).
8. individual layer accelerated clarifier as claimed in claim 7, it is characterized in that: described solid collection bucket (7) bottom is connected with solids-enriched bucket (9), and solids-enriched bucket (9) bottom is provided with mud juice pipe (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200580332U CN203315808U (en) | 2013-02-01 | 2013-02-01 | Rapid single-layer settler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200580332U CN203315808U (en) | 2013-02-01 | 2013-02-01 | Rapid single-layer settler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203315808U true CN203315808U (en) | 2013-12-04 |
Family
ID=49655210
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013200580332U Expired - Fee Related CN203315808U (en) | 2013-02-01 | 2013-02-01 | Rapid single-layer settler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203315808U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104611474A (en) * | 2015-01-21 | 2015-05-13 | 南宁苏格尔科技有限公司 | Sugar-manufacturing single-layer precipitator control system |
| CN107164569A (en) * | 2017-05-20 | 2017-09-15 | 米易华森糖业有限责任公司 | It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour |
| CN110745927A (en) * | 2019-11-18 | 2020-02-04 | 宜兴市荣盛达环保有限公司 | Coupling separation device for removing SS (suspended substance) in catalytic cracking flue gas desulfurization wastewater |
| CN111001196A (en) * | 2019-12-25 | 2020-04-14 | 上海宝钢磁业有限公司 | System for recycling cold rolling acid to regenerate acid-containing slurry and method for recycling cold rolling acid |
| WO2021104105A1 (en) * | 2019-11-26 | 2021-06-03 | 广西叶茂机电自动化有限责任公司 | System and process for pretreating sugarcane juice before membrane filtration |
| CN113877253A (en) * | 2021-10-25 | 2022-01-04 | 湖南贵威生物科技有限公司 | Quick settling separator |
-
2013
- 2013-02-01 CN CN2013200580332U patent/CN203315808U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104611474A (en) * | 2015-01-21 | 2015-05-13 | 南宁苏格尔科技有限公司 | Sugar-manufacturing single-layer precipitator control system |
| CN107164569A (en) * | 2017-05-20 | 2017-09-15 | 米易华森糖业有限责任公司 | It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour |
| CN110745927A (en) * | 2019-11-18 | 2020-02-04 | 宜兴市荣盛达环保有限公司 | Coupling separation device for removing SS (suspended substance) in catalytic cracking flue gas desulfurization wastewater |
| WO2021104105A1 (en) * | 2019-11-26 | 2021-06-03 | 广西叶茂机电自动化有限责任公司 | System and process for pretreating sugarcane juice before membrane filtration |
| CN111001196A (en) * | 2019-12-25 | 2020-04-14 | 上海宝钢磁业有限公司 | System for recycling cold rolling acid to regenerate acid-containing slurry and method for recycling cold rolling acid |
| CN113877253A (en) * | 2021-10-25 | 2022-01-04 | 湖南贵威生物科技有限公司 | Quick settling separator |
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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: 20131204 Termination date: 20220201 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |