CN104258620A - Huff-puff solid-liquid separator - Google Patents
Huff-puff solid-liquid separator Download PDFInfo
- Publication number
- CN104258620A CN104258620A CN201410481170.6A CN201410481170A CN104258620A CN 104258620 A CN104258620 A CN 104258620A CN 201410481170 A CN201410481170 A CN 201410481170A CN 104258620 A CN104258620 A CN 104258620A
- Authority
- CN
- China
- Prior art keywords
- strainer
- filter
- running roller
- strap
- roller
- 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.)
- Granted
Links
Abstract
The invention relates to a huff-puff solid-liquid separator, which belongs to the technical field of filter pressing technologies. The huff-puff solid-liquid separator is mainly characterized in that rollers are distributed in an triangular shape in a stander, wherein each roller is driven by a motor, one end part of a filter strap A which is reversely wound on an upper roller is reversely wound on a right lower roller, and one end part of a filter strap B which is forwardly wound on a lower left roller is reversely wound on a right lower roller; both the filter strap A and the filter strap B are respectively formed by a stainless steel sheet and a piece of filter cloth which is compounded on the stainless steel sheet, a plurality of filter holes which are formed at intervals in the longitudinal direction and transverse direction are formed in the middle stainless steel sheet, two sides of each transverse filter hole in the filter strap A are respectively provided with a semispherical projection, and the stainless steel sheets on the filter strap A and the filter strap B are opposite to each other. The huff-puff solid-liquid separator is simple in structure, favorable for saving energy and reducing the consumption and applicable to the dehydration of starch, plant residue slurry, industrial and municipal sludge, ore slag tailing sludge and the like, the content of water of a material can reach about 40 percent after the material is dehydrated once, a great amount of energy and a great amount of time can be reduced when the material is re-roasted, the practicability is very high, and the technical effect is prominent.
Description
Technical field
The present invention relates to a kind of throughput type solid-liquid seperator, the mixture for the solid-liquid having certain solid content is effectively separated, and deep removal liquid obtains liquid or solid product, belongs to pressure filtering technique technical field.
Background technology
Like product in the market has: (1) band press filter dewatering machine, the structure of this product is strainer along with running roller rotates, press filtration is produced when the mixture being placed in the solid-liquid on strainer contacts with running roller, the major defect of this series products is: the drainage time not considering material when A, design, the pressure pop-off that linear contact lay produces, can not effectively dewater.So the material liquid holdup after dehydration is still too high, usually also needs deep dehydration; Trouble changed by B, filter bag; C, due to assembly too many, maintenance of equipment rate is high.Be all with band press filter dewatering machine as manioc waste dehydration, after dehydration, moisture content is still about 75%, and also need deep dehydration during recycling, baking is normal selection.Dewatering efficiency is low, dehydration cost and dehydration energy high.(2) high-dryness filter, the major defect of this product is: A, be subject to warehouse length and diameter manufacturing capacity restriction, output is large not; B, manufacturing cost are high.
Summary of the invention
The object of this invention is to provide a kind of throughput type solid-liquid seperator, solve existing band press filter dewatering machine because of structural factor, the drainage time of material is short, be close to the pressure pop-off that linear contact lay produces between strainer and running roller, there is the deficiency that can not effectively dewater, changing existing strainer with being close to linear contact lay between running roller by the present invention is that face contacts, realize deep dehydration, greatly reduce the material liquid holdup after dehydration, improve dewatering efficiency low, reduce dehydration cost and dehydration energy.
The object of the invention is to be achieved through the following technical solutions, a kind of throughput type solid-liquid seperator, comprise frame, hopper in frame, running roller in frame and strainer, the motor of drive roller wheel, it is characterized in that, running roller in frame is three, be triangularly arranged, every root running roller drives through motor respectively, and strainer A mono-end of reverse winding on upper end running roller 1 is reverse to be wrapped on the running roller 2 of lower right, and strainer B mono-end that the running roller 3 of lower left is forward wound around is reverse to be wrapped on the running roller 2 of lower right; Strainer A, strainer B are formed by stainless sheet steel with the filter cloth of its compound, the stainless sheet steel at middle part have some in length and breadth to filter opening alternately, on strainer A, the both sides of each horizontal filter opening have dome-type projection, and the stainless sheet steel 4 on strainer A, strainer B is relative.
Described strainer A, fixing with running roller of strainer B two ends are wound around some circles.
Solid-liquid of the present invention is separated fully, and structure is simple, is conducive to saving energy and reduce the cost, purposes widely, is applicable to starch dehydrating, the dehydration of the plant slag oars such as cassava, Ipomoea batatas, potato residues, kelp residue, bean dregs, vinasse, industry and municipal sludge dehydration, slag tail mud dehydration etc.Use the disposable dehydration of the present invention that the moisture content of material can be allowed to reach about 40%, then will save a large amount of energy and time when toasting, the field effects such as the dehydration of above-mentioned starch dehydrating, the dregs of a decoction, industrial sludge dehydration, dewatering whole stillage are substantially identical.The present invention has very strong practicality and outstanding technique effect.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is the right TV structure schematic diagram of Fig. 1;
Fig. 3 is the structural representation of strainer A center line one end in the present invention;
Fig. 4 is the left TV structure schematic diagram of Fig. 3;
Fig. 5 is the structural representation of strainer B center line one end in the present invention;
Fig. 6 is the right TV structure schematic diagram of Fig. 5;
In figure, 1 running roller, 2 running rollers, 3 running rollers, 4 stainless sheet steels, 5 filter clothes, 6 dome-types are protruding, 7 filter openings,
8 frames, 9 hoppers, 10,11 motors, A, B strainer.
Detailed description of the invention
Further illustrate the present invention in conjunction with the accompanying drawings and embodiments, as shown in Figure 1, 2, the present invention includes the hopper 9 in frame 8, three running rollers in frame 8 and corresponding strainer, drive the motor of each running roller, three running roller settings triangular in shape in frame 8, every root running roller drives through motor respectively, strainer A mono-end of reverse winding on upper end running roller 1 is reverse to be wrapped on the running roller 2 of lower right, and strainer B mono-end that the running roller 3 of lower left is forward wound around is reverse to be wrapped on the running roller 2 of lower right; Strainer A, strainer B are formed by stainless sheet steel 4 with the filter cloth 5 of its compound, the stainless sheet steel 4 at middle part have some in length and breadth to filter opening 7 alternately, on strainer A, the both sides of each horizontal filter opening 7 have dome-type projection 6, stainless sheet steel 4 on strainer A, strainer B is relative, stainless sheet steel 4 on the relative strainer B of the side that namely on strainer A, stainless sheet steel 4 has a dome-type projection 6.Dome-type protruding 6 forms the space between filter plate, and be beneficial to liquid and flow out from both sides, meanwhile, dome-type projection 6 is easy to the relative displacement of having slided between filter plate.Filter cloth on strainer A, strainer B 5 is relative.
As seen in figures 3-6, the length of strainer A, strainer B makes as required, and fixing with running roller of its two ends is wound around some circles.Each filter opening 7 on strainer A, strainer B is alternate.
During work, strainer A one end is reverse to be fastened on running roller 1, strainer B one end is forward fastened on running roller 3, strainer A, the other end of B is all reverse to be fastened on running roller 2, during charging, running roller 2 is driving wheel, running roller 1, 3 is driven, material in hopper 9 is added on the filter cloth 5 of strainer B, running roller 2 starts rear strainer A, B moves, material is at strainer A, formed sandwich between B, and rolled by running roller 2 gradually, when running roller 1, the strainer A of 3, B is discharged into when limiting position and stops, running roller 2 works on and tightens up under the control of controlling organization, because curling generation normal pressure and shearing force acting in conjunction are on material, liquid in material is fully separated out, achieve the goal.After certain hour, running roller 1,3 is driving wheel, and running roller 2 is driven, and reversing allows the material after dewatering spue, and a work period completes.Under the condition guaranteeing stainless sheet steel 4 on the relative strainer B of the side that stainless sheet steel 4 on strainer A has a dome-type projection 6, strainer A, B can exchange on running roller 1,3.
Claims (2)
1. a throughput type solid-liquid seperator, comprise frame, hopper in frame, the running roller in frame and strainer, the motor of drive roller wheel, it is characterized in that, running roller in frame is three, is triangularly arranged, and every root running roller drives through motor respectively, strainer A mono-end of the upper reverse winding of upper end running roller (1) is reverse to be wrapped on the running roller (2) of lower right, and strainer B mono-end that the running roller (3) of lower left is forward wound around is reverse to be wrapped on the running roller (2) of lower right; Strainer A, strainer B are formed by stainless sheet steel (4) with the filter cloth (5) of its compound, the stainless sheet steel (4) at middle part have some in length and breadth to filter opening (7) alternately, on strainer A, the both sides of each horizontal filter opening (7) have dome-type projection (6), and the stainless sheet steel (4) on strainer A, strainer B is relative.
2. throughput type solid-liquid seperator according to claim 1, is characterized in that, described strainer A, strainer B two ends and running roller are fixing is wound around some circles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410481170.6A CN104258620B (en) | 2014-09-20 | 2014-09-20 | Throughput type solid-liquid seperator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410481170.6A CN104258620B (en) | 2014-09-20 | 2014-09-20 | Throughput type solid-liquid seperator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104258620A true CN104258620A (en) | 2015-01-07 |
| CN104258620B CN104258620B (en) | 2016-02-10 |
Family
ID=52150269
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410481170.6A Expired - Fee Related CN104258620B (en) | 2014-09-20 | 2014-09-20 | Throughput type solid-liquid seperator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104258620B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111888823A (en) * | 2020-07-24 | 2020-11-06 | 咸宁市农业科学院 | Water-saving sweet potato starch extractor |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2141317Y (en) * | 1991-11-14 | 1993-09-01 | 冶金工业部建筑研究总院 | Horizontal double-belt type filting machine |
| CN1081474C (en) * | 1996-10-30 | 2002-03-27 | 潘尼维斯公司 | Separating device |
| EP1403223A1 (en) * | 2001-05-14 | 2004-03-31 | Suzuki, Kiyoshi | Sludge concentrating method and device |
| CN200987932Y (en) * | 2006-12-27 | 2007-12-12 | 鞍钢股份有限公司 | Emulsion vacuum filter for cold rolling unit |
| CN202061866U (en) * | 2011-03-04 | 2011-12-07 | 王元华 | Dirt disposer |
| CN102489062A (en) * | 2011-11-28 | 2012-06-13 | 嘉兴绿方舟环保设备有限公司 | Solid-liquid separator |
| CN202460267U (en) * | 2012-02-29 | 2012-10-03 | 贵州天福化工有限责任公司 | Bag type vacuum filter |
| CN202893048U (en) * | 2012-11-19 | 2013-04-24 | 瓮福（集团）有限责任公司 | Improved extrusion roller of belt filter press |
| CN204121855U (en) * | 2014-09-20 | 2015-01-28 | 扬州海笑环保科技有限公司 | Throughput type solid-liquid seperator |
-
2014
- 2014-09-20 CN CN201410481170.6A patent/CN104258620B/en not_active Expired - Fee Related
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2141317Y (en) * | 1991-11-14 | 1993-09-01 | 冶金工业部建筑研究总院 | Horizontal double-belt type filting machine |
| CN1081474C (en) * | 1996-10-30 | 2002-03-27 | 潘尼维斯公司 | Separating device |
| EP1403223A1 (en) * | 2001-05-14 | 2004-03-31 | Suzuki, Kiyoshi | Sludge concentrating method and device |
| CN200987932Y (en) * | 2006-12-27 | 2007-12-12 | 鞍钢股份有限公司 | Emulsion vacuum filter for cold rolling unit |
| CN202061866U (en) * | 2011-03-04 | 2011-12-07 | 王元华 | Dirt disposer |
| CN102489062A (en) * | 2011-11-28 | 2012-06-13 | 嘉兴绿方舟环保设备有限公司 | Solid-liquid separator |
| CN202460267U (en) * | 2012-02-29 | 2012-10-03 | 贵州天福化工有限责任公司 | Bag type vacuum filter |
| CN202893048U (en) * | 2012-11-19 | 2013-04-24 | 瓮福（集团）有限责任公司 | Improved extrusion roller of belt filter press |
| CN204121855U (en) * | 2014-09-20 | 2015-01-28 | 扬州海笑环保科技有限公司 | Throughput type solid-liquid seperator |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111888823A (en) * | 2020-07-24 | 2020-11-06 | 咸宁市农业科学院 | Water-saving sweet potato starch extractor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104258620B (en) | 2016-02-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN208757060U (en) | A kind of high-efficiency sewage processing filter press | |
| CN207240943U (en) | A kind of high-efficiency helical extruding-desiccation machine | |
| CN215137550U (en) | Vacuum dehydrator | |
| CN104258620B (en) | Throughput type solid-liquid seperator | |
| CN204121855U (en) | Throughput type solid-liquid seperator | |
| CN206337139U (en) | A kind of novel high-pressure belt type sludge deep dehydrator | |
| CN201785297U (en) | High-efficiency energy-saving belt type sludge concentrating and pressing integrated drying machine | |
| CN104524846B (en) | Wedge shape supercharging sawtooth groove double dewatering squeezes belt filter press | |
| CN202876505U (en) | Permeable pressing roller and belt filter press | |
| CN104759134A (en) | Solid-liquid separator | |
| CN204346056U (en) | A kind of screw extruder for extrusion dehydration | |
| CN206896968U (en) | large belt filter press | |
| CN203678133U (en) | Vacuum filter with pressure filtration function | |
| CN204395590U (en) | Wedge shape supercharging sawtooth groove double dewatering squeezes belt filter press | |
| CN214962470U (en) | Industrial fruit and vegetable belt type squeezer | |
| CN202246371U (en) | Stripped concentration and pressing integral machine | |
| CN207786090U (en) | A kind of efficient high usage filter | |
| CN201093849Y (en) | Novel belt type compression filter-press dewatering integrated machine | |
| CN203170095U (en) | High-efficiency energy-saving belt type filter press | |
| CN210438608U (en) | Belt type concentration filter press | |
| CN201926254U (en) | Dehydration equipment for starch residue | |
| CN208468975U (en) | The production line of quick-frozen food flexible package PET composite membrane | |
| CN201250163Y (en) | Circulating squeeze dewatering device | |
| CN202456332U (en) | Drying press for cassava dreg | |
| CN204522457U (en) | A kind of equipment for separating liquid from solid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| 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: 20160210 Termination date: 20160920 |