CN202924891U - Sludge drying belt filter press - Google Patents
Sludge drying belt filter press Download PDFInfo
- Publication number
- CN202924891U CN202924891U CN 201220654086 CN201220654086U CN202924891U CN 202924891 U CN202924891 U CN 202924891U CN 201220654086 CN201220654086 CN 201220654086 CN 201220654086 U CN201220654086 U CN 201220654086U CN 202924891 U CN202924891 U CN 202924891U
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- belt
- filter press
- sludge
- sludge drying
- conveying belt
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Abstract
The utility model discloses a sludge drying belt filter press which consists of a belter filter press and a drying machine, wherein the belt filter press consists of a filter press frame, a filter press drive motor, an upper filter belt, a tension device, a filtrate collecting pipe and a lower filter belt; and the drying machine consists of a lower conveyor belt, a drying machine frame, a conveyor belt drive motor, a collecting cover and an upper conveying belt. According to the utility model, the sludge drying belt filter press is directly dried and heated through intermediate temperature, the heat transfer area of the sludge conveyor belt is large, and the moisture content of the sludge is reduced from about 98-99% to about 45-55%, so that the moisture content of the sludge is reduced obviously; furthermore, the sludge drying belt filter press is provided with an air circulation system, so that the moisture evaporated by the sludge is quickly taken away; in addition, the sludge drying belt filter press can automatically operate and is operated conveniently; and a totally closed system adopted by the utility model can be used for reducing the secondary pollution of the sludge, so that resource utilization requirements can be reached.
Description
Technical field
The utility model relates to a kind of sludge drying belt filter press, belongs to the environmental protection technical field of sludge treatment.
Background technology
The quantity discharged of urban industry waste water and sanitary sewage is increasing, and treatment rate of domestic sewage also improves year by year, and the sludge yield of municipal sewage plant also sharply increases.When adopting biological method to dispose of sewage, can produce a large amount of residue organic sludges, the mud that these organic contents are very high must in time obtain treatment and disposal, otherwise can cause secondary pollution, and the final settling mode of mud mainly adopts: landfill, agricultural, drying and incineration.Due to industrial development, the heavy metal content most cases in mud all exceeds standard, can't directly carry out agriculturally, and simultaneously due to constantly the dwindling of landfill yard area, the mud shipment distance is more and more remoter again.Though and mud is through processed, its water ratio is still higher, causes landfill yard to be difficult to accept, so cause can't landfill or the landfill expense constantly rise.Traditional method for sludge treatment namely carries out simply mechanicalness and concentrates and processed in sewage work, can not satisfy processing requirements and the cleanup standard of present stage.
The composition of sewage sludge is very complicated, except containing a large amount of moisture, also contains a large amount of useful resources, and the mud through after mummification can apply to land reclamation, building materials utilization etc.The sludge drying mode has: natural air drying, direct heating and indirect heating.How to reduce the water ratio of mud, reduce energy consumption, this is the gordian technique of sludge treatment.
The utility model content
The purpose of this utility model is to overcome the shortcoming and defect of above-mentioned prior art, and a kind of sludge drying belt filter press is provided, and can further reduce moisture percentage in sewage sludge, has the direct mummification of middle temperature, the characteristics that level of automation is high.
The purpose of this utility model is achieved through the following technical solutions: a kind of sludge drying belt filter press, be comprised of belt filter press and desiccation machine, it is characterized in that: described belt filter press is made of pressure filter rack, pressure filter drive-motor, upper strainer, tightening device, filtrate collection pipe and lower filter belt; Described desiccation machine is made of lower conveying belt, desiccation machine frame, conveying belt drive-motor, collecting hood and upper conveyor belt.
Medicine mixing device is installed in described belt filter press upper end.
Described conveying belt drive-motor connects upper conveyor belt and lower conveying belt with transmission chain.
Further, described lower conveying belt mud outlet end is provided with the dewatered sludge receiving tank, and the dewatered sludge receiving tank connects worm conveyor.
The utility model principle of work: after sewage work's settling tank mud tentatively concentrates, be 98%～99% mud suction medicine mixing device with water ratio with sludge pump, add the flocculation medicament in medicine mixing device, sludge flocculation enters belt filter press after becoming particle, mud and filtrate are at upper strainer sharp separation, mud is strainer and the further press filtration of lower filter belt contact part on entering, and water ratio drops to 80%～85%.mud after press filtration further reduces water ratio in sludge drying machine, hot blast enters sludge drying machine from the hot blast import, the conveying belt drive-motor drives lower conveying belt and upper conveyor belt rotates, mud flows on two conveying belt, hot blast sees through successively lower conveying belt and upper conveyor belt and takes away water vapor, water ratio drops to 45%～55%, after mummification, mud is collected at the dewatered sludge receiving tank, then mud transfers out from worm conveyor, the hot blast that contains moisture is collected in collecting hood, discharge from hot-blast outlet, the part waste gas circulation is got back to the hot blast import, contain moisture waste gas through condensation and process up to standard after discharging.
In sum, the beneficial effects of the utility model are: directly mummification of temperature in employing, and direct heating, the heat transfer area of mud conveying belt is large, can make general moisture percentage in sewage sludge be about 98%～99% and be reduced to 45%～55% left and right, has obviously reduced the water content of mud; And be furnished with air circulation system, take away rapidly the moisture of mud evaporation; Sludge drying and belt filter press can automatic operatings, and be easy to operate; The utility model adopts totally-enclosed system, has reduced the secondary pollution of mud, can arrive the requirement of recycling.
Description of drawings
Fig. 1 facade structures figure of the present utility model;
Fig. 2 vertical view of the present utility model.
The title of mark in accompanying drawing: 1-pressure filter rack; 2-pressure filter drive-motor; 3-upper strainer; 4-medicine mixing device; 5-tightening device; 6-filtrate collection pipe; 7-lower filter belt; 8-dewatered sludge receiving tank; 9-worm conveyor; The import of 10-hot blast; 11-lower conveying belt; 12-controlling box; 13-desiccation machine frame; 14-conveying belt drive-motor; 15-collecting hood; 16-hot-blast outlet; 17-upper conveyor belt.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, but embodiment of the present utility model is not limited only to this.
Embodiment: as depicted in figs. 1 and 2, a kind of sludge drying belt filter press, be comprised of belt filter press and desiccation machine, described belt filter press is made of pressure filter rack 1, pressure filter drive-motor 2, upper strainer 3, tightening device 5, filtrate collection pipe 6 and lower filter belt 7; Described desiccation machine is made of lower conveying belt 11, desiccation machine frame 13, conveying belt drive-motor 14, collecting hood 15 and upper conveyor belt 17.
Described conveying belt drive-motor 14 use transmission chains connect upper conveyor belt 17 and lower conveying belt 11.
Further, described lower conveying belt 11 mud outlet ends are provided with dewatered sludge receiving tank 8, and dewatered sludge receiving tank 8 connects worm conveyor 9.
During the utility model operation work: after sewage work's settling tank mud tentatively concentrates, be 98%～99% mud suction medicine mixing device 4 with water ratio with sludge pump, add the flocculation medicament in medicine mixing device 4, sludge flocculation enters belt filter press after becoming particle, mud and filtrate are at upper strainer sharp separation, mud is strainer 3 and the lower filter belt 7 further press filtrations of contact part on entering, and water ratio drops to 80%～85%.mud after press filtration further reduces water ratio in sludge drying machine, hot blast enters sludge drying machine from hot blast import 10, conveying belt drive-motor 14 drives lower conveying belt 11 and upper conveyor belt 17 rotates, mud flows on two conveying belt, hot blast sees through successively lower conveying belt 11 and upper conveyor belt 17 and takes away water vapor, water ratio drops to 45%～55%, after mummification, mud is collected at dewatered sludge receiving tank 8, then mud transfers out from worm conveyor 9, the hot blast that contains moisture is collected in collecting hood 15, discharge from hot-blast outlet 16, the part waste gas circulation is got back to the hot blast import, contain moisture waste gas through condensation and process up to standard after discharging.
Directly mummification of temperature during the sludge drying belt filter press adopts, direct heating, the heat transfer area of mud conveying belt is large, the results show: can make general moisture percentage in sewage sludge be about 98%～99% and be reduced to 45%～55% left and right, obviously reduce the water content of mud.
As mentioned above, just can realize preferably the utility model.
Claims (4)
1. sludge drying belt filter press, be comprised of belt filter press and desiccation machine, it is characterized in that: described belt filter press is made of pressure filter rack (1), pressure filter drive-motor (2), upper strainer (3), tightening device (5), filtrate collection pipe (6) and lower filter belt (7); Described desiccation machine is made of lower conveying belt (11), desiccation machine frame (13), conveying belt drive-motor (14), collecting hood (15) and upper conveyor belt (17).
2. a kind of sludge drying belt filter press as claimed in claim 1, is characterized in that: described belt filter press upper end installation medicine mixing device (4).
3. a kind of sludge drying belt filter press as claimed in claim 1, it is characterized in that: described conveying belt drive-motor (14) connects upper conveyor belt (17) and lower conveying belt (11) with transmission chain.
4. a kind of sludge drying belt filter press as claimed in claim 1, it is characterized in that: described lower conveying belt (11) mud outlet end is provided with dewatered sludge receiving tank (8), and dewatered sludge receiving tank (8) connects worm conveyor (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220654086 CN202924891U (en) | 2012-12-03 | 2012-12-03 | Sludge drying belt filter press |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220654086 CN202924891U (en) | 2012-12-03 | 2012-12-03 | Sludge drying belt filter press |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202924891U true CN202924891U (en) | 2013-05-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220654086 Expired - Fee Related CN202924891U (en) | 2012-12-03 | 2012-12-03 | Sludge drying belt filter press |
Country Status (1)
| Country | Link |
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| CN (1) | CN202924891U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104958956A (en) * | 2015-07-02 | 2015-10-07 | 天津霍普环保科技有限公司 | Cleaning device for filter belt of sludge electroosmosis dewatering machine |
| CN105036515A (en) * | 2015-09-08 | 2015-11-11 | 陕西沃升机械制造有限公司 | Heat roller filter-pressing type sludge dewatering and drying integrated machine |
| CN109133561A (en) * | 2017-06-19 | 2019-01-04 | 乔丙年 | Mud drying device |
| CN109467301A (en) * | 2019-01-03 | 2019-03-15 | 深圳市钰杰环保工程有限公司 | A kind of continuous high-efficient shield slurry dewatering system |
| CN110845114A (en) * | 2019-12-20 | 2020-02-28 | 中原晟启新能源装备有限公司 | Continuous sludge dewatering and drying system |
-
2012
- 2012-12-03 CN CN 201220654086 patent/CN202924891U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104958956A (en) * | 2015-07-02 | 2015-10-07 | 天津霍普环保科技有限公司 | Cleaning device for filter belt of sludge electroosmosis dewatering machine |
| CN105036515A (en) * | 2015-09-08 | 2015-11-11 | 陕西沃升机械制造有限公司 | Heat roller filter-pressing type sludge dewatering and drying integrated machine |
| CN105036515B (en) * | 2015-09-08 | 2017-03-22 | 陕西沃升机械制造有限公司 | Heat roller filter-pressing type sludge dewatering and drying integrated machine |
| CN109133561A (en) * | 2017-06-19 | 2019-01-04 | 乔丙年 | Mud drying device |
| CN109467301A (en) * | 2019-01-03 | 2019-03-15 | 深圳市钰杰环保工程有限公司 | A kind of continuous high-efficient shield slurry dewatering system |
| CN110845114A (en) * | 2019-12-20 | 2020-02-28 | 中原晟启新能源装备有限公司 | Continuous sludge dewatering and drying system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ANHUI FUWEN NEW ENERGY CO., LTD. Free format text: FORMER OWNER: CHENGDU YUANCHUANG ENVIRONMENTAL ENGINEERING CO., LTD. Effective date: 20130626 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 610000 CHENGDU, SICHUAN PROVINCE TO: 230031 HEFEI, ANHUI PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130626 Address after: 230031, No. 2 A Road, Yaohai Industrial Park, Hefei, Anhui, China Patentee after: Anhui Fuwen New Energy Co., Ltd. Address before: 610000 Sichuan city of Chengdu province Wuhou District Temple Red Street No. 9 of No. 605 Patentee before: Chengdu Yuanchuang Environmental Engineering Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130508 Termination date: 20151203 |
|
| EXPY | Termination of patent right or utility model |