CN203342483U - Ceramic filter - Google Patents
Ceramic filter Download PDFInfo
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- CN203342483U CN203342483U CN 201320369897 CN201320369897U CN203342483U CN 203342483 U CN203342483 U CN 203342483U CN 201320369897 CN201320369897 CN 201320369897 CN 201320369897 U CN201320369897 U CN 201320369897U CN 203342483 U CN203342483 U CN 203342483U
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Abstract
The utility model discloses a ceramic filter. A tube rotating wheel is a barrel-shaped wheel body which is formed by fixedly connecting a plurality of communicated and connected tube bodies; a first rotary joint and a second rotary joint are communicated and connected with the tube bodies on the tube rotating wheel; a connecting sheet is fixed on the tube rotating wheel; a ceramic plate is fixed on the connecting sheet; a passage is formed on the connecting plate, and communicated and connected with the ceramic plate and the tube rotating wheel; the first rotary joint and the second rotary joint are respectively communicated and connected with a liquid discharging tank by a pipeline; the liquid discharging tank is communicated and connected with an air inlet of a vacuum pump; the liquid discharging tank is communicated and connected with a liquid inlet of a filtrate pump; a liquid outlet of the filtrate pump is communicated and connected with a filtrate storage tank by a pipeline; a scraper is fixed on a rack; the front part of the scraper is opposite to the side surface of the ceramic plate; and the rear part of the scraper is opposite to a belt conveyor. The ceramic filter has no filter cloth filtration, has high vacuum degree, high filter cake drying performance, and clear and transparent filtrate, saves the energy consumption by over 80% in comparison with other filter devices, and has low installation cost.
Description
Technical field:
The utility model relates to the solid-liquid separating equipment technical field, more specifically to a kind of ceramic filter.It can be widely used in the industries such as metallurgy, chemical industry, coal, mine, generating, coloured, environmental protection, sewage disposal.
Background technology:
The problem existed in current vacuum filter operation has: the filtered fluid muddiness, can not recycle, and can not directly discharge; The problems such as equipment energy consumption is large, automaticity is low, equipment operating cost height.
The utility model content:
The purpose of this utility model is exactly the deficiency for prior art, and a kind of ceramic filter is provided, and its no filter-fabric filters; Vacuum is high, and the filtration cakes torrefaction performance is good, and filtrate is as clear as crystal, with other filter plant phase specific energy consumption, saves approximately more than 80%, and mounting cost is low.
Technology solution of the present utility model is as follows:
Ceramic filter, comprise main shaft reducing motor and vavuum pump, is fixed with main shaft reducing motor, vavuum pump and slurry tank on frame, and the slurry feed pipe, facing to slurry tank, forms overfall on slurry tank;
Rotor is comprised of pipe runner, the first swivel joint, the second swivel joint, brace and ceramic wafer, be connected with from right to left the first swivel joint, pipe runner and the second swivel joint in the rotating shaft of main shaft reducing motor in turn, pipe runner several bodys that connect mutually of serving as reasons are fixed together the tubular wheel body of composition, the first swivel joint connects mutually with the second swivel joint and the body on the pipe runner, be fixed with brace on the pipe runner, be fixed with ceramic wafer on brace, form passage on brace and connect mutually with ceramic wafer and pipe runner;
The first swivel joint connects respectively pipeline with the second swivel joint and connects mutually with Drainage tank, Drainage tank connects mutually by pipeline and the air inlet of vavuum pump, Drainage tank connects mutually by pipeline and the inlet of filtrate pump, and the liquid outlet of filtrate pump connects the filtrate holding vessel by pipeline;
Scraper is fixed on frame, and the front portion of scraper is facing to the side of ceramic wafer, and the rear portion of scraper is facing to belt conveyor.
The bottom of described slurry tank is fixed with the ultrasonic oscillator of ultrasonic cleaner, and the diluted acid tank is taken over runner by device for cleaning pipeline, on diluted acid tank and the pipeline that connects mutually of pipe runner, Pressure gauge, flowmeter, electromagnetic distribution valve and hand-operated valve is installed.
Described stirring motor is fixed on frame, and stirring motor drives agitator and rotates, and agitator is placed in slurry tank.
The beneficial effects of the utility model are:
1, its no filter-fabric filters; Vacuum is high, and the filtration cakes torrefaction performance is good; 2, filtrate is as clear as crystal; 3, with other filter plant phase specific energy consumption, save approximately more than 80%; 4, automaticity is high, continued operation, and the high performance series type adopts procedure auto-control, automatic feed, automatically cleans, and reduces labor intensity of operating staff, reduces operating personnel's quantity; 5, working environment is clean, pollution-free; Filtrate is limpid, can recycle, and reduces discharge; 6, compact equipment, complete machine adopts microcomputer optimized design, rational in infrastructure, dependable performance, main drive disk assembly adopts non-maintaining design, reduces downtime rate, and the cell body rake adopts stainless steel structure, guarantees to reach its service life more than 10 years; 7, mounting cost is low.
The accompanying drawing explanation:
Fig. 1 is structural representation of the present utility model;
The top view that Fig. 2 is Fig. 1 rotor and slurry tank part;
The side view that Fig. 3 is Fig. 1 rotor and slurry tank part;
Fig. 4 is operation principle key diagram of the present utility model.
The specific embodiment:
Embodiment: see shown in Fig. 1 to 4, ceramic filter, comprise main shaft reducing motor 1 and vavuum pump 2, is fixed with main shaft reducing motor 1, vavuum pump 2 and slurry tank 4 on frame 3, and slurry feed pipe 18, facing to slurry tank 4, forms overfall 4 on slurry tank 4;
The first swivel joint 52 connects respectively pipeline with the second swivel joint 53 and connects mutually with Drainage tank 6, Drainage tank 6 connects mutually by pipeline and the air inlet of vavuum pump 7, Drainage tank 6 connects mutually by pipeline and the inlet of filtrate pump 8, and the liquid outlet of filtrate pump 8 connects filtrate holding vessel 9 by pipeline;
The bottom of described slurry tank 4 is fixed with the ultrasonic oscillator of ultrasonic cleaner 12, diluted acid tank 13 is taken over runner 51 by device for cleaning pipeline, on diluted acid tank 13 and the pipeline that connects mutually of pipe runner 51, Pressure gauge 14, flowmeter 15, electromagnetic distribution valve 16 and hand-operated valve 17 is installed.
Described stirring motor 19 is fixed on frame 3, and stirring motor 19 drives agitator and rotates, and agitator is placed in slurry tank 4.
Operation principle: ceramic filter uses ceramic capillarity: when vacuumizing, can only allow water pass through, air and mineral particle can't pass through, and guarantee the principle without vacuum leak, have greatly reduced energy consumption and material moisture.Therefore ceramic filter is the solid-liquid separating equipment of New-generation efficient energy-saving.
As shown in Figure 4, put into slurries by slurry feed pipe 18 in slurry tank 4,7 pairs of Drainage tanks 6 of vavuum pump vacuumize, Drainage tank 6 forms negative pressure by pipeline to pipe runner 51,51 pairs of runners of pipe have the ceramic wafer 55 of micropore to form negative pressure, water enters pipe runner 51 from ceramic wafer 55, and the mineral matter in water and impurity just are adsorbed to the surface formation filter cake of ceramic wafer 55.Filter cake is scraped by scraper 10, then on scraper 10 flows to the conveyer belt of belt conveyor 11, sees off.
After filter cake of every suction, by vavuum pump 7, oppositely in Drainage tank 6, pressurize, filtrate can be flowed out by the micropore on ceramic wafer 55, to ceramic wafer 55 is counter, cleans like this.
After ceramic wafer 55 is used a period of time, (being generally 7-12 hour), the micropore of ceramic wafer 55 is because of the blocked filter efficiency that reduces gradually, for the micropore that guarantees ceramic wafer 55 unobstructed, enable the mixing purging system, start ultrasonic cleaner 12, open electromagnetic distribution valve 16 and hand-operated valve 17 and inject diluted acid to pipe runner 51, the effect of the ultrasonic oscillator by diluted acid and ultrasonic cleaner 12, ceramic wafer 55 is carried out to pickling and Ultrasonic Cleaning, guarantee the service life of ceramic wafer, can reach more than 10 years service life of the present utility model.
Claims (3)
1. ceramic filter, comprise main shaft reducing motor (1) and vavuum pump (2), it is characterized in that: be fixed with main shaft reducing motor (1), vavuum pump (2) and slurry tank (4) on frame (3), slurry feed pipe (18), facing to slurry tank (4), forms overfall (4) on slurry tank (4);
Rotor (5) is by pipe runner (51), the first swivel joint (52), the second swivel joint (53), brace (54) and ceramic wafer (55) form, be connected with from right to left the first swivel joint (52) in the rotating shaft of main shaft reducing motor (1) in turn, pipe runner (51) and the second swivel joint (53), pipe runner (51) several bodys that connect mutually of serving as reasons are fixed together the tubular wheel body of composition, the first swivel joint (52) connects mutually with the second swivel joint (53) and the body on pipe runner (51), be fixed with brace (54) on pipe runner (51), be fixed with ceramic wafer (55) on brace (54), forming passage on brace (54) connects mutually with ceramic wafer (55) and pipe runner (51),
The first swivel joint (52) connects respectively pipeline with the second swivel joint (53) and connects mutually with Drainage tank (6), Drainage tank (6) connects mutually by pipeline and the air inlet of vavuum pump (7), Drainage tank (6) connects mutually by pipeline and the inlet of filtrate pump (8), and the liquid outlet of filtrate pump (8) connects filtrate holding vessel (9) by pipeline;
It is upper that scraper (10) is fixed on frame (3), and the front portion of scraper (10) is facing to the side of ceramic wafer (55), and the rear portion of scraper (10) is facing to belt conveyor (11).
2. ceramic filter according to claim 1, it is characterized in that: the bottom of slurry tank (4) is fixed with the ultrasonic oscillator of ultrasonic cleaner (12), diluted acid tank (13) is taken over runner (51) by device for cleaning pipeline, on diluted acid tank (13) and the pipeline that connects mutually of pipe runner (51), Pressure gauge (14), flowmeter (15), electromagnetic distribution valve (16) and hand-operated valve (17) is installed.
3. ceramic filter according to claim 1 is characterized in that: it is upper that stirring motor (19) is fixed on frame (3), and stirring motor (19) drives agitator and rotates, and agitator is placed in slurry tank (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320369897 CN203342483U (en) | 2013-06-25 | 2013-06-25 | Ceramic filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320369897 CN203342483U (en) | 2013-06-25 | 2013-06-25 | Ceramic filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203342483U true CN203342483U (en) | 2013-12-18 |
Family
ID=49742425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320369897 Expired - Fee Related CN203342483U (en) | 2013-06-25 | 2013-06-25 | Ceramic filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203342483U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105749606A (en) * | 2016-05-06 | 2016-07-13 | 无锡市同至人机械设备制造有限公司 | Efficient disc filter cloth dehydrator |
| CN105879467A (en) * | 2016-06-14 | 2016-08-24 | 湖州核汇机械有限公司 | Filter mechanism for ceramic filter |
| CN108786242A (en) * | 2018-06-12 | 2018-11-13 | 铜陵市绿美星环保建材有限公司 | The cleaning plant of solid matter in a kind of sewage disposal process |
| CN117138435A (en) * | 2023-10-23 | 2023-12-01 | 核工业(烟台)建设工程有限公司 | Ceramic filter for mining and fine selection |
-
2013
- 2013-06-25 CN CN 201320369897 patent/CN203342483U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105749606A (en) * | 2016-05-06 | 2016-07-13 | 无锡市同至人机械设备制造有限公司 | Efficient disc filter cloth dehydrator |
| CN105879467A (en) * | 2016-06-14 | 2016-08-24 | 湖州核汇机械有限公司 | Filter mechanism for ceramic filter |
| CN108786242A (en) * | 2018-06-12 | 2018-11-13 | 铜陵市绿美星环保建材有限公司 | The cleaning plant of solid matter in a kind of sewage disposal process |
| CN117138435A (en) * | 2023-10-23 | 2023-12-01 | 核工业(烟台)建设工程有限公司 | Ceramic filter for mining and fine selection |
| CN117138435B (en) * | 2023-10-23 | 2023-12-26 | 核工业(烟台)建设工程有限公司 | Ceramic filter for mining and fine selection |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131218 Termination date: 20170625 |