CN202089877U - Spiral batch-type sludge extruding dewaterer - Google Patents
Spiral batch-type sludge extruding dewaterer Download PDFInfo
- Publication number
- CN202089877U CN202089877U CN2011200894345U CN201120089434U CN202089877U CN 202089877 U CN202089877 U CN 202089877U CN 2011200894345 U CN2011200894345 U CN 2011200894345U CN 201120089434 U CN201120089434 U CN 201120089434U CN 202089877 U CN202089877 U CN 202089877U
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- mud
- mandrel
- extruding
- filter cylinder
- intermittent type
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Abstract
A spiral batch-type sludge extruding dewaterer comprises a mandrel 7 which is driven by a motor 2 through a transmission device, and two ends of the mandrel are respectively installed on corresponding support seats. Helical blades 8 which are equal in screw pitches and located in a filter drum 9 are arranged on the mandrel 7, one end of the filter drum 9 is communicated with a sludge outlet 14 through a clamp ring 6 capable of adjusting opening of the end port, and the other end of the filter drum 9 is provided with a sludge inlet 10. A sludge extruding cavity between the mandrel 7 and the filter drum 9 is divided into at least two variable volume cavities and an equal volume cavity by the helical blades 8, and the variable volume cavities and the equal volume cavity are arranged along the axial direction of the mandrel 7 at intervals. The volume of each variable volume cavity is decreased stage by stage from the direction of the sludge inlet 10 to the direction of the sludge outlet 14, and the length of a section of screw pitch is a stage. Moisture content of sludge which is dewatered by adopting the dewaterer is low, and the spiral batch-type sludge extruding dewaterer is easy to maintain, small in occupied area and low in running cost and can continuously work for 24 hours.
Description
Technical field
The utility model relates to the dewatering processing device of mud that sewage disposal produces.
Background technology
After sewage work's sewage disposal, can produce a large amount of mud.The water ratio of mud is between 95%~98%.Sewage work all adopts the mechanical dehydration mode to sludge dewatering at present, and dewatering machine has vacuum belt machine, centrifuge, plate-and-frame filter press, belt filter press etc.Adopt these mechanical dehydrations, the water ratio of mud is reduced between 78%~82%, and occupation area of equipment is big, operating environment is poor, and the maintenance amount is big, the running cost height.
The utility model content
The technical problems to be solved in the utility model is, defective at the prior art existence, a kind of spiral intermittent type mud extruding-desiccation machine is provided, adopt the moisture percentage in sewage sludge low (60%) after this equipment dewaters, the easy care maintenance, floor space is little, and running cost is relatively low, can work in continuous 24 hours.
The technical solution of the utility model is, described spiral intermittent type mud extruding-desiccation machine comprises that two ends are installed on the corresponding supporting base respectively and by the mandrel of electric motor by actuator drives, this mandrel is provided with the uniform pitch screw-blade that is arranged in filter cylinder, the clamp ring of filter cylinder one end through regulating this end port aperture is communicated with mud mouth, and the other end of described filter cylinder is provided with mud inlet; It is characterized in that the mud extrusion chamber between mandrel and the filter cylinder is divided at least two by described screw-blade and becomes cavity volumes and isometric(al) chamber, and become cavity volume and isometric(al) chamber axially alternately along mandrel; The volume edge that becomes cavity volume is reduced step by step by the direction of mud inlet towards mud mouth, and a joint pitch length is an one-level.
Below the utility model made further specify.
Referring to Fig. 1, working process of the present utility model and know-why are, mandrel 7 rotates under electric motor 2 drives, and the screw-blade 8 on the mandrel 7 promotes to advance to mud mouth 14 extruding from the mud that mud inlet 10 is come in, and the water of extruding in the process of advancing flows out from the aperture on the filter cylinder 9; Regulate the spacing between clamp ring 6 and filter cylinder 9 ports, can regulate squeeze pressure in the filter cylinder, with the mass dryness fraction of mud.The volume that becomes cavity volume successively decreases along the mud direct of travel, and mud is compressed in cavity, and moisture is separated in mud; The isometric(al) chamber can make the intermolecular gap of mud keep no longer being compressed, and keeps the unimpeded outflow of moisture; Second section volume that becomes cavity volume successively decreases once more, mud is compressed therein again, and second isometric(al) chamber makes the intermolecular gap of mud keep once more not being compressed; By that analogy, make mud reach required water ratio.
As known from the above, the utility model is a kind of spiral intermittent type mud extruding-desiccation machine, adopts the moisture percentage in sewage sludge after this equipment dewaters can be low to moderate 60%, the easy care maintenance, and floor space is little, and running cost is relatively low, can work in continuous 24 hours.
Description of drawings
Fig. 1 is the spiral intermittent type mud extruding-desiccation machine structural representation of a kind of embodiment of utility model.
In the drawings:
The 1-support, the 2-electric motor, the 3-step-down gear,
4,5,11, the 12-supporting seat, the 6-clamp ring, the 7-mandrel,
The 8-screw-blade, the 9-filter cylinder, the 10-mud inlet,
The 13-washing nozzle, the 14-mud mouth.
Embodiment
As shown in Figure 1, the mandrel 7 that described spiral intermittent type mud extruding-desiccation machine comprises that two ends are installed in respectively on the corresponding supporting base and driven by transmission mechanism (step-down gear 3) by electric motor 2, this mandrel 7 is provided with the uniform pitch screw-blade 8 that is arranged in filter cylinder 9, the clamp ring 6 of filter cylinder 9 one ends through regulating this end port aperture is communicated with mud mouth 14, and the other end of described filter cylinder 9 is provided with mud inlet 10; It is characterized in that the mud extrusion chamber between mandrel 7 and the filter cylinder 9 is divided at least two by described screw-blade 8 and becomes cavity volumes and isometric(al) chamber, and become cavity volume and the isometric(al) chamber is arranged along mandrel axially alternate (replacing); The volume edge that becomes cavity volume is reduced step by step by the direction of mud inlet 10 towards mud mouth 14, and a joint pitch length is an one-level.
Mandrel 7 is a tapering spindle, and screw-blade 8 is welded on and constitutes an integral body on the mandrel 7, is contained in the filter cylinder 9.Whole filter cylinder and mandrel frame are on supporting seat 4,5,11,12, and the big end of mandrel 7 links to each other with electric motor 2 and step-down gear 3.The small end of mandrel 7 is established mud inlet, and the outside of filter cylinder 9 is provided with washing nozzle 13, to clean the obstruction of filter cylinder 9 apertures.
Described mud inlet 10 becomes cavity volume with first and is communicated with.
Described change cavity volume is made up of the screw-blade place mud extrusion chamber of three joint pitch length.
The volume in described isometric(al) chamber equates with adjacent one-level cavity volume in adjacent previous stage (left side among Fig. 1) the change cavity volume.
The above and below of described filter cylinder 9 is arranged washing nozzle 13 respectively.
Described filter cylinder 9 is for being distributed with the cylindrical shell of ostium excurrens on the barrel.
The upper end of described mud inlet 10 be larger caliber in last positive taper, the position that mud inlet 10 is connected with filter cylinder 9 be larger caliber under back taper.
Be equipped with on the described clamp ring 6 and scrape slice.
Claims (8)
1. spiral intermittent type mud extruding-desiccation machine, comprise that two ends are installed on the corresponding supporting base respectively and by the mandrel (7) of electric motor (2) by actuator drives, this mandrel (7) is provided with the uniform pitch screw-blade (8) that is arranged in filter cylinder (9), clamp ring (6) the same mud mouth (14) of filter cylinder (9) one ends through regulating this end port aperture is communicated with, and the other end of described filter cylinder (9) is provided with mud inlet (10); It is characterized in that the mud extrusion chamber between mandrel (7) and the filter cylinder (9) is divided at least two by described screw-blade (8) and becomes cavity volumes and isometric(al) chamber, and become cavity volume and isometric(al) chamber axially alternately along mandrel (7); The volume edge that becomes cavity volume is reduced step by step by the direction of mud inlet (10) towards mud mouth (14), and a joint pitch length is an one-level.
2. according to the described spiral intermittent type of claim 1 mud extruding-desiccation machine, it is characterized in that described mud inlet (10) becomes cavity volume with first and is communicated with.
3. according to claim 1 or 2 described spiral intermittent type mud extruding-desiccation machines, it is characterized in that described change cavity volume is made up of screw-blade (8) the place mud extrusion chamber of three joint pitch length.
4. according to claim 1 or 2 described spiral intermittent type mud extruding-desiccation machines, it is characterized in that the volume in isometric(al) chamber equates with adjacent one-level cavity volume in the adjacent previous stage change cavity volume.
5. according to claim 1 or 2 described spiral intermittent type mud extruding-desiccation machines, it is characterized in that, arrange washing nozzle (13) respectively in the above and below of described filter cylinder (9).
6. according to claim 1 or 2 described spiral intermittent type mud extruding-desiccation machines, it is characterized in that described filter cylinder (9) is for being distributed with the cylindrical shell of ostium excurrens on the barrel.
7. according to claim 1 or 2 described spiral intermittent type mud extruding-desiccation machines, it is characterized in that, the upper end of described mud inlet (10) be larger caliber in last positive taper, the position that filter cylinder connects be larger caliber under back taper.
8. according to claim 1 or 2 described spiral intermittent type mud extruding-desiccation machines, it is characterized in that, be equipped with on the described clamp ring (6) and scrape slice.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011200894345U CN202089877U (en) | 2011-03-30 | 2011-03-30 | Spiral batch-type sludge extruding dewaterer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011200894345U CN202089877U (en) | 2011-03-30 | 2011-03-30 | Spiral batch-type sludge extruding dewaterer |
Publications (1)
Publication Number | Publication Date |
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CN202089877U true CN202089877U (en) | 2011-12-28 |
Family
ID=45364958
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2011200894345U Expired - Fee Related CN202089877U (en) | 2011-03-30 | 2011-03-30 | Spiral batch-type sludge extruding dewaterer |
Country Status (1)
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CN (1) | CN202089877U (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105110598A (en) * | 2015-09-11 | 2015-12-02 | 山东晨钟机械股份有限公司 | High-dryness sludge extrusion dewatering equipment main shaft |
CN108479363A (en) * | 2018-04-13 | 2018-09-04 | 宁波清智环保科技有限公司 | Environmentally friendly emission-control equipment |
CN110999815A (en) * | 2019-12-24 | 2020-04-14 | 贵州锦屏生态鹅业发展有限公司 | Semi-dry type bionic farm |
CN112870808A (en) * | 2021-04-22 | 2021-06-01 | 焦华丽 | Sewage sludge environment-friendly recovery device |
CN113998860A (en) * | 2021-11-17 | 2022-02-01 | 江苏京源环保股份有限公司 | Multifunctional combined mud discharging device |
CN114315066A (en) * | 2022-01-13 | 2022-04-12 | 潍坊学院 | High-water-content sludge treatment system |
-
2011
- 2011-03-30 CN CN2011200894345U patent/CN202089877U/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105110598A (en) * | 2015-09-11 | 2015-12-02 | 山东晨钟机械股份有限公司 | High-dryness sludge extrusion dewatering equipment main shaft |
CN105110598B (en) * | 2015-09-11 | 2018-07-03 | 山东晨钟机械股份有限公司 | High mass dryness fraction sludge extrusion dehydration machine spindle |
CN108479363A (en) * | 2018-04-13 | 2018-09-04 | 宁波清智环保科技有限公司 | Environmentally friendly emission-control equipment |
CN110999815A (en) * | 2019-12-24 | 2020-04-14 | 贵州锦屏生态鹅业发展有限公司 | Semi-dry type bionic farm |
CN112870808A (en) * | 2021-04-22 | 2021-06-01 | 焦华丽 | Sewage sludge environment-friendly recovery device |
CN112870808B (en) * | 2021-04-22 | 2023-05-05 | 河南凯源水务科技有限公司 | Environment-friendly sewage sludge recovery device |
CN113998860A (en) * | 2021-11-17 | 2022-02-01 | 江苏京源环保股份有限公司 | Multifunctional combined mud discharging device |
CN114315066A (en) * | 2022-01-13 | 2022-04-12 | 潍坊学院 | High-water-content sludge treatment system |
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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 |
Granted publication date: 20111228 Termination date: 20150330 |
|
EXPY | Termination of patent right or utility model |