CN200945400Y - Ceramic vacuum sulfur foam filter - Google Patents
Ceramic vacuum sulfur foam filter Download PDFInfo
- Publication number
- CN200945400Y CN200945400Y CN 200620083011 CN200620083011U CN200945400Y CN 200945400 Y CN200945400 Y CN 200945400Y CN 200620083011 CN200620083011 CN 200620083011 CN 200620083011 U CN200620083011 U CN 200620083011U CN 200945400 Y CN200945400 Y CN 200945400Y
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- hopper
- ceramic vacuum
- filter machine
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Abstract
The utility model relates to a ceramic vacuum filter, in particular to a ceramic vacuum sulfur foam filter that disposes elementary sulfur and water separation and makes desulphurization solution used recyclingly and also prevents the environment from being polluted by the elementary sulfur sewage. The ceramic vacuum sulfur foam filter has a frame (10) which is characterized in that the frame (10) is provided with a feed trough (14) which is provided inside with a drum (7); the periphery of the drum (7) is fixed with at least one grade of filter disk (12) which is connected with a distributing moving disk (5) through a water outlet pipe (6); one end of the distributing moving disk (5) is provided with a distributing fasting disk (4); one end of the distributing fasting disk (4) is connected with a liquid-discharging tank (3) through a pipe, and the other end of the liquid-discharging tank (3) is communicated with a vacuum pump (1) through a pipe; one end of the drum (7) is connected with a driving device (9) through a shaft coupling (8).
Description
(1) technical field: the utility model relates to a kind of ceramic vacuum filter, especially a kind of the sulphur foam is carried out elemental sulfur and moisture from processing, recycles doctor solution, and prevents the ceramic vacuum sulphur foamed filter machine of elemental sulfur sewage pollution environment.
(2) background technology: chemical field adopts Steam Heating evaporation sulphur foam to carry out the processed elemental sulfur usually; But it is too high to reclaim the elemental sulfur cost, and doctor solution can not reclaim usefulness again, wastes very greatly, and environmental pollution is also serious.At present, also do not search out other energy-saving consumption-reducing, the processing method of stopping to pollute and equipment.
(3) summary of the invention: the purpose of this utility model is to overcome the deficiency of above-mentioned prior art and the ceramic vacuum sulphur foamed filter machine that a kind of energy-saving consumption-reducing is provided, stops to pollute.The ceramic wafer of this equipment utilization microcellular structure, and utilize the pressure differential on ceramic wafer two sides separates the elemental sulfur solid particle in the sulphur foam with water, solved the difficult problem that sulphur foam that industries such as chemical fertilizer produce coal combustion is handled.
The purpose of this utility model can be achieved through the following technical solutions: ceramic vacuum sulphur foamed filter machine, a frame 10 is arranged, it is characterized in that: frame 10 is provided with a hopper 14, be provided with cylinder 7 in the hopper 14, be fixed with one-level ceramic filter disk 12 at least around the cylinder 7, ceramic filter disk 12 is connected with distributing Moving plate 5 by water outlet connecting pipe 6, distribute an end of Moving plate 5 to be provided with distribution price fixing 4, distribute an end of price fixing 4 to connect a Drainage tank 3 by pipeline, Drainage tank 3 opposite sides are communicated with a vavuum pump 1 by pipeline; The other end of cylinder 7 is connected with drive unit 9 by shaft coupling 8.A plurality of ceramic wafers 1201 constitute ceramic filter disk 12 on the same axis by being positioned at, and a plurality of ceramic wafers are communicated with by water outlet connecting pipe 6.Ceramic wafer 1201 is sector structure, forms a plurality of passages 1202 that catchment between its former and later two plate faces 1203, and there is a collector pipe 1204 its underpart, and collector pipe 1204 is communicated with the passage 1202 that catchments, and collector pipe 1,204 one ends are connected with water outlet connecting pipe 6.The diameter of the passage 1202 that catchments on 1201 of the ceramic wafers is between 2 microns one 15 microns.The lower end of hopper 14 is provided with receiving hopper 16.Be provided with liquid level gauge 11 in the hopper 14.Atmosphere transfer valve 17, vacuum transfer valve 2 are housed on the Drainage tank 3.Distribute Moving plate 5 to be provided with a plurality of through holes 501, distribute price fixing 4 to be provided with arc gully- hole 401 and 402, circular clean-out opening 403.
Compared with the prior art the utility model has following good effect: the utility model is the advanced technology and the equipment of sulphur foam processing aspect, utilize the ceramic wafer of microcellular structure, and utilize the pressure differential on ceramic wafer two sides, elemental sulfur solid particle in the sulphur foam is separated with water, solved the difficult problem that industries such as chemical fertilizer are handled the sulphur foam of coal combustion generation; When having solved chemical field and adopting Steam Heating evaporation sulphur foam to carry out the processed elemental sulfur usually, waste very greatly, the problem that environmental pollution is serious, and energy-saving consumption-reducing, energy consumption only account for 10% of legacy equipment; Because the utility model adopts the ceramic wafer of microcellular structure to handle the sulphur foam, isolated filtrate is as clear as crystal, and the solids content in it is almost nil, has stopped pollution; Water content in the sulphur foamed filter that use the utility model filters is lower, and water content only is 35-45%, can fully recycle.
(4) description of drawings: Fig. 1 is the structural representation of ceramic vacuum sulphur foamed filter machine
Fig. 2 is the A-A cross-sectional view of Fig. 1
Fig. 3 is the structural representation of ceramic wafer 1201
Fig. 4 is the B-B cross-sectional view of the ceramic wafer 1201 of Fig. 3
Fig. 5 is the C-C cross-sectional view of the distribution Moving plate 5 of Fig. 1
Fig. 6 is the D-D cross-sectional view of the distribution price fixing 4 of Fig. 1
(5) specific embodiment: describe the utility model in detail below in conjunction with accompanying drawing, and provide an embodiment:
Referring to Fig. 1, Fig. 2, Fig. 3, shown in Figure 4, vacuum filter of the present utility model has a structural steel frame open frame 10, and described frame lower is provided with the hopper 14 of a semicircle tubular, is provided with liquid level gauge 11 in this hopper, is used for controlling the liquid level of sulphur foam.This foam hopper one end is provided with Drainage tank 3, and this Drainage tank one side is connected with distributing price fixing 4, and opposite side is communicated with a vavuum pump 1 by pipeline, and this vavuum pump is made of the pump housing, motor etc.; Be equipped with on the described frame 10 to design in a cylinder 7, multistage ceramic filter disk 12, the present embodiment three grades of ceramic filter disks 12 are arranged, also can design one-level, secondary or more than three grades, ceramic filter disk 12 is made up of polylith ceramic wafer 1201, ceramic filter disk 12 is made of 12 ceramic wafers 1201 in the utility model, one end of the collector pipe 1204 of ceramic wafer 1201 is connected with 12 water outlet connecting pipes 6, distribute Moving plate 5 to be connected with distributing price fixing 4, the other end of cylinder 7 is connected with drive unit 9 by shaft coupling 8.
Referring to Fig. 1, Fig. 5, shown in Figure 6, distribute Moving plate 5 and distribute price fixing 4 minute surfaces to contact, distribute Moving plate 5 and the faying face that distributes price fixing 4 to have high fineness, can not occur when rotating relatively leaking and the pressure loss.Distribute Moving plate 5 and cylinder 7 one ends to link together, play rotation with one, distribution price fixing 4 is connected with Drainage tank 3 one sides and bonds together.Referring to Fig. 5, distribute price fixing 4 to be provided with 401,402 and circular clean-out openings 403 of two arc gully-holes, this arc gully- hole 401 and 402 is communicated with Drainage tank 3, and this circle clean-out opening 403 is communicated with a pipe blow-through through hole 501, is used for the cleaning of ceramic wafer 1201.Distribute on the Moving plate 5 equidistantly to be provided with 12 through holes 501, this through hole is used for installing water outlet connecting pipe 6.
Referring to Fig. 3 and Fig. 4, ceramic wafer 1201 is a sector structure, former and later two plate faces 1203 that its top is microcellular structure, form the passage 1202 that catchments between the plate face, the collector pipe 1204 in its underpart, this collector pipe and the channel connection that catchments, this pipe end that catchments is used for being connected with the water outlet connecting pipe.Micro-pore diameter on the ceramic plate is between 2 microns-15 microns.In the present embodiment, constituting a ceramic filter disk 12 by 12 ceramic wafers 1201 is installed on the cylinder 7, at an equidistant circle or the multi-turn ceramic filter disk 12 of arranging of these cylinder 7 upper edge axis directions, ceramic wafer 1201 on it is on the same axis, and a plurality of ceramic wafers 1201 that water outlet connecting pipe 6 will be positioned on the same axis are communicated with.Referring to Fig. 1 and Fig. 2, in the present embodiment, the both sides of described each ceramic filter disk 12 all are provided with scraper 13, this scraper 13 adopt scrape from the mode elemental sulfur that will be bonded on the ceramic wafer 1201 separate with ceramic wafer 1201, collect receiving hopper 16 then.Dump skip 16 is equipped with in the lower end of hopper 7, is used for collecting elemental sulfur.For ceramic wafer 1201 is more cleaned supersonic generator 15 is installed in hopper 14, its ultrasonic wave that sends can cleaning ceramic plate 1201.
During the utility model work, in hopper 14, add the sulphur foam, start drive unit 9 and drive cylinder 7 uniform rotation, start vavuum pump 1.In the rotation process of cylinder 7, distribute the moving week of through hole 501 revolutions on the Moving plate 5 all will to overlap respectively once with arc gully-hole 401,402 and the circular clean-out opening 403 on distributing price fixing 4, be in when overlapping the position, ceramic wafer 1201 is communicated with Drainage tank 3, by ceramic wafer 1201 inside and outside pressure differentials the sulphur foam in the hopper 14 is adsorbed on ceramic wafer 1201 surfaces, and water wherein sucks Drainage tank 3 discharges and reclaims.Be adsorbed on ceramic wafer 1201 lip-deep elemental sulfurs when rotating to scraper 13 positions with cylinder 7, by scraper 13 scrape from and reclaim.The later ceramic wafer 1201 of discharging can produce micropore and stop up, and can use water under high pressure or steam clean.When the through hole 501 on distributing Moving plate 5 and circular clean-out opening 403 on the distribution price fixing 4 are in and overlap the position, water under high pressure or steam enter in the passage 1202 that catchments of ceramic wafer 1201 by water outlet connecting pipe 6, and ejection from inside to outside, finish the task that micropore is cleaned, guarantee the equipment operate as normal.
Claims (8)
1, ceramic vacuum sulphur foamed filter machine, a frame (10) is arranged, it is characterized in that: frame (10) is provided with a hopper (14), be provided with cylinder (7) in the hopper (14), be fixed with one-level ceramic filter disk (12) at least around the cylinder (7), ceramic filter disk (12) is connected with distributing Moving plate (5) by water outlet connecting pipe (6), distribute an end of Moving plate (5) to be provided with distribution price fixing (4), distribute an end of price fixing (4) to connect a Drainage tank (3) by pipeline, Drainage tank (3) opposite side is communicated with a vavuum pump (1) by pipeline, and the other end of cylinder (7) is connected with drive unit (9) by shaft coupling (8).
2, ceramic vacuum sulphur foamed filter machine according to claim 1 is characterized in that: a plurality of ceramic wafers (1201) constitute ceramic filter disk (12) on the same axis by being positioned at, and a plurality of ceramic wafers are communicated with by water outlet connecting pipe (6).
3, ceramic vacuum sulphur foamed filter machine according to claim 1 and 2, it is characterized in that: ceramic wafer (1201) is sector structure, form a plurality of passages that catchment (1202) between its former and later two plate faces (1203), there is a collector pipe (1204) its underpart, collector pipe (1204) is communicated with the passage that catchments (1202), and collector pipe (1204) one ends are connected with water outlet connecting pipe (6).
4, ceramic vacuum sulphur foamed filter machine according to claim 3, it is characterized in that: the diameter of the passage that catchments (1202) on ceramic wafer (1201) face is between 2 microns to 15 microns.
5, ceramic vacuum sulphur foamed filter machine according to claim 1, it is characterized in that: the lower end of hopper (14) is provided with receiving hopper (16).
6, ceramic vacuum sulphur foamed filter machine according to claim 1 is characterized in that: be provided with liquid level gauge (11) in the hopper (14).
7, ceramic vacuum sulphur foamed filter machine according to claim 1 is characterized in that: atmosphere transfer valve (17), vacuum transfer valve (2) are housed on the Drainage tank (3).
8, ceramic vacuum sulphur foamed filter machine according to claim 1 is characterized in that: distribute Moving plate (5) to be provided with a plurality of through holes (501), distribute price fixing (4) to be provided with arc gully-hole (401) and (402), circular clean-out opening (403).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620083011 CN200945400Y (en) | 2006-04-13 | 2006-04-13 | Ceramic vacuum sulfur foam filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620083011 CN200945400Y (en) | 2006-04-13 | 2006-04-13 | Ceramic vacuum sulfur foam filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200945400Y true CN200945400Y (en) | 2007-09-12 |
Family
ID=38732461
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620083011 Expired - Fee Related CN200945400Y (en) | 2006-04-13 | 2006-04-13 | Ceramic vacuum sulfur foam filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200945400Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107227185A (en) * | 2017-07-11 | 2017-10-03 | 江苏苏港和顺生物科技有限公司 | A kind of filtration integrated equipment of biogas production wet desulphurization elemental sulfur |
| CN108176131A (en) * | 2018-02-06 | 2018-06-19 | 东莞市德林环保科技有限公司 | A kind of nano ceramics filter device and its technique for applying |
-
2006
- 2006-04-13 CN CN 200620083011 patent/CN200945400Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107227185A (en) * | 2017-07-11 | 2017-10-03 | 江苏苏港和顺生物科技有限公司 | A kind of filtration integrated equipment of biogas production wet desulphurization elemental sulfur |
| CN107227185B (en) * | 2017-07-11 | 2023-06-23 | 江苏盐城港盐农循环农业有限公司 | Wet desulfurization elemental sulfur filtering integrated equipment for biogas production |
| CN108176131A (en) * | 2018-02-06 | 2018-06-19 | 东莞市德林环保科技有限公司 | A kind of nano ceramics filter device and its technique for applying |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070912 Termination date: 20120413 |