CN203183793U - Rotating-disc-type pressure filter - Google Patents
Rotating-disc-type pressure filter Download PDFInfo
- Publication number
- CN203183793U CN203183793U CN 201320122737 CN201320122737U CN203183793U CN 203183793 U CN203183793 U CN 203183793U CN 201320122737 CN201320122737 CN 201320122737 CN 201320122737 U CN201320122737 U CN 201320122737U CN 203183793 U CN203183793 U CN 203183793U
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- filter
- chassis
- top cover
- rotating disk
- rotating
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Abstract
The utility model belongs to the field of solid-liquid separation, and discloses a rotating-disc-type pressure filter. The rotating-disc-type pressure filter comprises a slurry inlet, a gas inlet, a top cover, a middle rotating disc, sealing plates, clapboard strips, a chassis, a filtrate outlet and a filter cake outlet, wherein a pore passage is formed in the top cover and is communicated with the slurry inlet and the gas inlet respectively, a pore passage of the chassis is covered by a perforated plate and filter cloth and then is communicated with the filtrate outlet and the filter cake outlet respectively, the top cover and the chassis are fixed, the middle rotating disc is driven by a transmission device to continuously rotate between the top cover and the chassis, the sealing plates are arranged on the upper end and the lower end of the middle rotating disc, and the clapboard strips are distributed inside the middle rotating disc and rotate along with the intermediate rotating disc. The filter provided by the utility model can continuously operate and is low at rotating speed and good in leakproofness, and the filtering area of the pressure filter is exponentially enlarged.
Description
Technical field
The utility model relates to a kind of solid-liquid separating equipment, particularly a kind of continous way filter press.
Background technology
Filtration is a chemical enginnering process the most basic.Usually be that the interception part is handled slurry with the filter cloth, the liquid under the effect of external force in the slurry becomes filtrate by the filter cloth duct, and the solid particle in the slurry is trapped within becomes filter cake on the filter cloth, thereby realizes Separation of Solid and Liquid.
The traditional filtering machine is representative with plate and frame filter press and rotary drum vacuum filter.Plate and frame filter press mainly is made up of frame, filter plate, filter frame and hold down gag etc., and plate and frame are done quadrate more, and left and right corner all has circular hole on filter plate, the frame, assembles and compress the duct that the back constitutes Flow of Goods and Materials, and the both sides of frame form the filter chamber coated with filter cloth.Slurry enters the filter chamber during filtration under certain differential pressure action, and filtrate is converged discharge from the bottom, and filter cake is stayed in the filter chamber, treat that filter cake is full of the filter chamber after, namely stop to filter.Rotary drum vacuum filter mainly is made up of rotary drum, dispensing head, slurry tank etc., the rotary drum outer surface is made of porous plate, filter cloth covers thereon, rotary drum inside is separated into several not connected fan-shaped lattice chambers, each lattice chamber has the interior duct of pipeline and hollow shaft to be connected, and the duct in the hollow shaft feeds on the rolling disc that is positioned at axle head and rotates with the axis vertically, rolling disc and fixed disk closely cooperate becomes dispensing head, be divided into several arc grooves on the fixed disk of dispensing head, communicate with vacuum tube, washing lotion groove, compressed air line respectively.When rotary drum turned round, because the effect of dispensing head just forms vacuum or pressurization respectively in the fan-shaped lattice, controlled filter was operated carrying out smoothly of each stage.
Plate and frame filter press intermittently operated of the prior art, efficient is lower; Rotary drum vacuum filter relies on to vacuumize and is motive force, and differential pressure is limited.
The utility model content
The utility model provides a kind of rotating disc type pressing filter, and is little with the filter motive force that solves continued operation in the prior art, and the problem that the big filter of motive force can not continued operation.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is:
A kind of rotating disc type pressing filter is characterized in that: comprise slurry import, gas feed, top cover, middle rotating disk, sealing plate, separator strip, chassis, filtrate (liquid and filtered solid outlet.Having the duct on the top cover is connected with slurry import, gas feed respectively, on the duct on chassis coated with porous plate and filter cloth, be connected with filtrate (liquid and filtered solid outlet respectively again, top cover and chassis all maintain static, middle rotating disk is rotated between top cover and chassis continuously by actuator drives, rotating disk is divided into several fan-shaped cavities in the middle of described, and the separator strip between the fan-shaped cavity and top cover and chassis form several sealed compartments.
A kind of rotating disc type pressing filter of the utility model, it is further characterized in that: preferably 16~24 of described fan-shaped cavities, preferably 16~24 of described sealed compartments.
A kind of rotating disc type pressing filter of the utility model, it is further characterized in that: form on the rotating disk separator strip in the middle of the sealing between described each sealed compartments is pressed in by the sealing plate on top cover and the chassis.
A kind of rotating disc type pressing filter of the utility model, it is further characterized in that: the rotating speed of rotating disk can be regulated by gear in the middle of described, and being generally 30~60 changes/hour.
A kind of rotating disc type pressing filter of the utility model, it is further characterized in that: the material of sealing plate can select for use metal or nonmetallic materials to make.The material of filter cloth can select for use metal or nonmetallic materials to make.
When rotating disk rotates in the middle of transmission device drives, slurry begins to enter continuously each sealed compartments, under the promotion of operating pressure, most of filtrate in the slurry is passed the district of filter just filter cloth to filtrate (liquid, a small amount of filtrate goes to the press filtration district with sealed compartments, further press filtration under the gas pressure effect, and residue filtrate is passed press filtration district filter cloth and is pooled to filtrate (liquid, be trapped in filter cake in the sealed compartments and be rotated further filtered solid outlet and come off voluntarily by gravity, finish the filtration operation.
The filter that the utility model provides, but continued operation, rotating speed is low, good airproof performance, filter area significantly improves, and filter capacity significantly strengthens, and has dwindled the specification of traditional filtering machine greatly, saved occupation area of equipment, be applicable to that petroleum chemical industry, fertilizer industry, plastic industry, rubber industry, pharmaceutical industry etc. have any one technical process of the requirement of filtering.
Description of drawings
Fig. 1 is the front view of the utility model rotating disc type pressing filter;
Fig. 2 is the vertical view of the utility model rotating disc type pressing filter.
Reference numeral shown in the figure: the import of 1-slurry, 2-gas feed, rotating disk in the middle of the 3-top cover, 4-, 5-chassis, 6-filtrate (liquid, 7-filtered solid outlet, 8-porous plate, 9-filter cloth, 10-transmission device, 11-fan-shaped cavity, 12-separator strip, 13-sealing plate.
The specific embodiment
Below in conjunction with accompanying drawing the utility model rotating disc type pressing filter is described in further detail.
As shown in Figure 1, the utility model rotating disc type pressing filter comprises slurry import 1, gas feed 2, top cover 3, middle rotating disk 4, chassis 5, filtrate (liquid 6 and filtered solid outlet 7.Having the duct on the top cover 3 is connected with slurry import 1, gas feed 2 respectively, on the duct on chassis 5 coated with porous plate 8 and filter cloth 9, be connected with filtrate (liquid 6 and filtered solid outlet 7 respectively again, top cover 3 and chassis 5 all maintain static, and middle rotating disk 4 is driven between top cover 3 and chassis 5 by transmission device 10 and rotates continuously.Middle rotating disk 4 is divided into several fan-shaped cavities 11, and the separator strip 12 between the fan-shaped cavity 11 forms several sealed compartments with top cover 3 and chassis 5.
When rotating disk 4 rotates in the middle of transmission device 10 drives, slurry begins to enter continuously each sealed compartments, under the promotion of operating pressure, most of filtrate in the slurry is passed the district of filter just filter cloth 9 to filtrate (liquid 6, a small amount of filtrate goes to the press filtration district with sealed compartments, further press filtration under the gas pressure effect, residue filtrate is passed press filtration district filter cloth 9 and is pooled to filtrate (liquid 6, is trapped in filter cake in the sealed compartments and is rotated further filtered solid outlet 7 and comes off voluntarily by gravity.Sealed compartments is carrying slurry, and the moving circle of revolution all passes through zones such as charging, press filtration, discharging respectively, as required, also can set up zones such as washing, drying.
By changing the position of sealed compartments, can change the ratio in zones such as charging, press filtration, discharging.
In the middle of being pressed in by the sealing plate 13 on top cover 3 and the chassis 5, sealing between each compartment forms on the rotating disk separator strip 12.In middle rotating disk 4 continuous rotary courses, separator strip 12 contacts with sealing plate 13 all the time.The material of sealing plate 13 can select for use metal or nonmetallic materials to make.The material of filter cloth 9 can select for use metal or nonmetallic materials to make.
The rotating speed of middle rotating disk 4 can be regulated by gear, and being generally 30~60 changes/hour.
Claims (7)
1. rotating disc type pressing filter, comprise the slurry import, gas feed, top cover, middle rotating disk, the chassis, filtrate (liquid and filtered solid outlet, it is characterized in that: have on the described top cover duct respectively with the slurry import, gas feed is connected, on the duct on chassis coated with porous plate and filter cloth, be connected with filtrate (liquid and filtered solid outlet respectively again, top cover and chassis all maintain static, middle rotating disk is rotated between top cover and chassis continuously by actuator drives, rotating disk is divided into several fan-shaped cavities in the middle of described, and the separator strip between the fan-shaped cavity and top cover and chassis form several sealed compartments.
2. filter according to claim 1, it is characterized in that: described fan-shaped cavity is 16~24.
3. filter according to claim 1, it is characterized in that: described sealed compartments is 16~24.
4. filter according to claim 1 is characterized in that: form on the rotating disk separator strip in the middle of the sealing between described each sealed compartments is pressed in by the sealing plate on top cover and the chassis.
5. filter according to claim 4 is characterized in that: the upper and lower end of rotating disk in the middle of described sealing plate is positioned at, rotated with middle rotating disk the inside of rotating disk in the middle of separator strip was distributed in.
6. filter according to claim 1 is characterized in that: the rotating speed of rotating disk can be regulated by gear in the middle of described.
7. filter according to claim 6 is characterized in that: in the middle of described the rotating speed of rotating disk be 30~60 change/hour.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320122737 CN203183793U (en) | 2013-03-11 | 2013-03-11 | Rotating-disc-type pressure filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320122737 CN203183793U (en) | 2013-03-11 | 2013-03-11 | Rotating-disc-type pressure filter |
Publications (1)
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CN203183793U true CN203183793U (en) | 2013-09-11 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201320122737 Expired - Lifetime CN203183793U (en) | 2013-03-11 | 2013-03-11 | Rotating-disc-type pressure filter |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104492138A (en) * | 2014-12-21 | 2015-04-08 | 重庆市家顶翔食品有限公司 | Plate-and-frame filter |
CN106746148A (en) * | 2017-03-17 | 2017-05-31 | 成都源蓉科技有限公司 | A kind of magnetic loading precipitation filtration, purification system |
CN108840478A (en) * | 2018-07-10 | 2018-11-20 | 白忠海 | A kind of environment-friendly metal waste liquid recovery apparatus |
-
2013
- 2013-03-11 CN CN 201320122737 patent/CN203183793U/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104492138A (en) * | 2014-12-21 | 2015-04-08 | 重庆市家顶翔食品有限公司 | Plate-and-frame filter |
CN106746148A (en) * | 2017-03-17 | 2017-05-31 | 成都源蓉科技有限公司 | A kind of magnetic loading precipitation filtration, purification system |
CN108840478A (en) * | 2018-07-10 | 2018-11-20 | 白忠海 | A kind of environment-friendly metal waste liquid recovery apparatus |
CN108840478B (en) * | 2018-07-10 | 2021-09-17 | 苏州乐米凡电气科技有限公司 | Environment-friendly metal waste liquid recovery unit |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term |
Granted publication date: 20130911 |
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CX01 | Expiry of patent term |