CN202626000U - Drying and purifying treatment device of urban sludge and industrial sludge - Google Patents
Drying and purifying treatment device of urban sludge and industrial sludge Download PDFInfo
- Publication number
- CN202626000U CN202626000U CN 201220265091 CN201220265091U CN202626000U CN 202626000 U CN202626000 U CN 202626000U CN 201220265091 CN201220265091 CN 201220265091 CN 201220265091 U CN201220265091 U CN 201220265091U CN 202626000 U CN202626000 U CN 202626000U
- Authority
- CN
- China
- Prior art keywords
- cylindrical barrel
- outlet
- sludge
- barrel body
- high speed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Abstract
The utility model relates to a drying and purifying treatment device of urban sludge and industrial sludge. The drying and purifying treatment device of the urban sludge and the industrial sludge comprises a drying machine, a mechanical sludge crushing machine, a high speed thermal current pipeline nozzle, a rotation shaft, a helix guide plate, a hot gas fume pipeline inlet port, a dry sediment outlet and an airflow outlet, wherein the drying machine is a cylindrical barrel body, an outlet of the mechanical sludge crushing machine is connected with a sludge inlet of the front end of the cylindrical barrel body, and an air outlet of the high speed thermal current pipeline nozzle is connected with an air inlet on the cylindrical barrel body. The rotation shaft is located on a center shaft of the cylindrical barrel body, the helix guide plate is arranged on the rotation shaft, and the hot gas fume pipeline inlet port is arranged on the front end of the cylindrical barrel body along the tangential direction of the cylindrical barrel body. The dry sediment outlet is arranged on a lower portion of the rear end of the cylindrical barrel body, and the airflow outlet is arranged on an upper portion of the rear end of the cylindrical barrel body. The drying and purifying treatment device of the urban sludge and the industrial sludge has the advantages of being simple in structure, small in size, saving in energy, improved in efficiency, and increased in treatment capacity and the like.
Description
Technical field
The utility model relates to a kind of mummification and purifying processing device, relates in particular to a kind of city and industrial sludge mummification and purifying processing device.
Background technology
Contain various nutrient elements and organic compositions capable of using such as a large amount of nitrogen, phosphorus, potassium in city and the industrial sludge; Also contain simultaneously poisonous, deleterious pathogenic bacteria, the organism of Dioxins, difficult degradation (polychlorobiphenyl etc.), heavy metal (copper, chromium, arsenic, mercury, cadmium etc.) material.Mud is not if handle, contaminate environment not only, and cause the waste of resource.
Also there are a lot of defectives in present domestic sludge treatment equipment, and like bulky, power consumption is high, and treatment process is complicated, the height of cost.
The utility model content
The utility model technical problem to be solved provides a kind of city and industrial sludge mummification and purifying processing device; Overcome existing sludge treatment device bulky; Power consumption is high, and treatment process is complicated, the height of cost; Cause great majority still to handle accumulation, landfill situation, the defective of contaminate environment.
The technical scheme that the utility model solves the problems of the technologies described above is following: a kind of city and industrial sludge mummification and purifying processing device; Comprise desiccation machine, mud mechanical crusher, high speed hot gas flow plumbing nozzle, turning axle, spiral deflector, thermal chimney road admission port, the outlet of dried slag, air stream outlet; Said desiccation machine is a cylindrical barrel, and the outlet of said mud mechanical crusher links to each other with mud inlet on the said cylindrical barrel front portion; Inlet mouth links to each other on said high speed hot gas flow duct injection mouth air outlet and the said cylindrical barrel; Said high speed hot gas flow plumbing nozzle is located on the said cylindrical barrel along said cylindrical barrel tangential direction; And be positioned near the mud inlet, said mud inlet is provided with said inlet mouth is vertical; Said turning axle is positioned on the hub of said cylindrical barrel; Said spiral deflector is arranged on the said turning axle; Said thermal chimney road admission port is arranged on the front portion of said cylindrical barrel, and along the tangential direction setting of cylindrical barrel; Said dried slag outlet is arranged on the below at said cylindrical barrel rear portion, and said air stream outlet is arranged on the top at the rear portion of said cylindrical barrel.The gas flow rate of said high speed hot gas flow plumbing nozzle ejection is 100 to 600 meter per seconds.Said mud mechanical crusher is that the splash mechanical crusher is got rid of in centrifugal throwing.
The beneficial effect of the utility model is: get into mechanical crusher through extruding; Because through the shape mud that splashes after the Mechanical Crushing; Be set at simultaneously that high speed hot gas flow plumbing nozzle on the desiccation machine ejects high temperature (100 to 800 degrees centigrade), (100 to 600 meter per second) gas shock is broken for the more tiny mud of particle once more at a high speed, the mud after the secondary breaking is adding that carrying that hot flue gas that the thermal chimney road that is provided with on the cylindrical barrel gets into forms whirlwind shape hot gas flow down, passes through the spiral deflector that is provided with on the turning axle and advance at the internal rotation of cylindrical barrel; Further dry mud; Discharge through the outlet of overdrying slag at last, this apparatus structure is simple, and volume is little; Energy-conservation and efficient improves greatly, and treatment capacity increases.
On the basis of technique scheme, the utility model can also be done following improvement.
Further, also comprise scraper plate, said scraper plate is fixed on the said turning axle, is provided with at interval with said spiral deflector.
Further, said high speed hot gas flow plumbing nozzle is provided with one or more along said cylindrical barrel tangential direction.
Further, said spiral deflector is arranged on a plurality of planes in the said cylindrical barrel; Each plane of said spiral deflector is provided with two of propeller-like, three or four blades.
Description of drawings
Fig. 1 is the front view of a kind of city of the utility model and industrial sludge mummification and purifying processing device;
Fig. 2 is Fig. 1 diagrammatic cross-section;
In the accompanying drawing, the list of parts of each label representative is following:
1, mud mechanical crusher, 2, high speed hot gas flow nozzle, 3, desiccation machine, 4, hot gas approach, 5, spiral deflector, 6, turning axle, 7, the outlet of dried slag, 8, scraper plate, 9, air stream outlet.
Embodiment
Below in conjunction with accompanying drawing the principle and the characteristic of the utility model are described, institute gives an actual example and only is used to explain the utility model, is not the scope that is used to limit the utility model.
Like Fig. 1,2 said cities and industrial sludge mummification and purifying processing device; Comprise desiccation machine 3, mud mechanical crusher 1, high speed hot gas flow plumbing nozzle 2, turning axle 6, spiral deflector 5, thermal chimney road admission port 4, dried slag outlet 7, air stream outlet 9; Said desiccation machine 3 is a cylindrical barrel, and the mud inlet on the outlet of said mud mechanical crusher 1 and the said cylindrical barrel front portion links to each other;
Inlet mouth links to each other on the air outlet of said high speed hot gas flow duct injection mouth 2 and the said cylindrical barrel; Said high speed hot gas flow plumbing nozzle 2 is located on the said cylindrical barrel along said cylindrical barrel tangential direction; And be positioned near the mud inlet, said mud inlet is provided with said inlet mouth is vertical; Mud can be broken into the mud of fine particle shape under the high temperature and high speed jet impingement function, increased the mud heat interchanging area, has improved mummification speed.
Said turning axle 6 is positioned on the said cylindrical barrel hub; Said spiral deflector 5 is arranged on the said turning axle 6; Said thermal chimney road 4 admission ports are arranged on the rear portion of said cylindrical barrel, and along the tangential direction setting of cylindrical barrel; Said dried slag outlet 7 is arranged on the below at said cylindrical barrel rear portion; Said air stream outlet is arranged on the top at the rear portion of said cylindrical barrel.Also comprise scraper plate 8, said scraper plate 8 is fixed on the said turning axle 6, is provided with at interval with said spiral deflector 5.
The gas flow rate of said high speed hot gas flow plumbing nozzle 2 ejections is the high temperature fluid of 100 to 600 meter per seconds; With the mud granule head-on crash; Add under the energy that is produced at a high speed at high temperature, moisture content instant vaporization adsorbed in the mud or that comprise is reached the mummification purpose.
Said high speed hot gas flow plumbing nozzle 2 is provided with one or more along said cylindrical barrel tangential direction.Said spiral deflector 5 is arranged on a plurality of planes in the said cylindrical barrel; Said spiral deflector 5 each plane are provided with two of propeller-like, three or four blades.
Working process: mud gets into mechanical crusher through extruding; Because through the shape mud that splashes after the Mechanical Crushing; Be set at simultaneously that high speed hot gas flow plumbing nozzle on the desiccation machine ejects high temperature (100 to 800 degrees centigrade), (100 to 600 meter per second) gas shock is broken for the more tiny mud of particle once more at a high speed, the mud after the secondary breaking is adding that carrying that hot flue gas that the thermal chimney road that is provided with on the cylindrical barrel gets into forms whirlwind shape hot gas flow down, passes through the spiral deflector that is provided with on the turning axle and advance at the internal rotation of cylindrical barrel; Further dry mud; Discharge through the outlet of overdrying slag at last, this apparatus structure is simple, and volume is little; Energy-conservation and efficient improves greatly, and treatment capacity increases.
The above is merely the preferred embodiment of the utility model, and is in order to restriction the utility model, not all within the spirit and principle of the utility model, any modification of being done, is equal to replacement, improvement etc., all should be included within the protection domain of the utility model.
Claims (4)
1. a city and industrial sludge mummification and purifying processing device; It is characterized in that; Comprise desiccation machine, mud mechanical crusher, high speed hot gas flow plumbing nozzle, turning axle, spiral deflector, thermal chimney road admission port, the outlet of dried slag, air stream outlet; Said desiccation machine is a cylindrical barrel, and the outlet of said mud mechanical crusher links to each other with mud inlet on the said cylindrical barrel front portion; Inlet mouth links to each other on said high speed hot gas flow duct injection mouth air outlet and the said cylindrical barrel; Said high speed hot gas flow plumbing nozzle is located on the said cylindrical barrel along said cylindrical barrel tangential direction; And be positioned near the mud inlet, said mud inlet is provided with said inlet mouth is vertical; Said turning axle is positioned on the hub of said cylindrical barrel; Said spiral deflector is arranged on the said turning axle; Said thermal chimney road admission port is arranged on the front portion of said cylindrical barrel, and along the tangential direction setting of cylindrical barrel; Said dried slag outlet is arranged on the below at said cylindrical barrel rear portion, and said air stream outlet is arranged on the top at the rear portion of said cylindrical barrel.
2. according to the said city of claim 1 and industrial sludge mummification and purifying processing device, it is characterized in that, also comprise scraper plate, said scraper plate is fixed on the said turning axle, is provided with at interval with said spiral deflector.
3. according to the said city of claim 1 and industrial sludge mummification and purifying processing device, it is characterized in that said high speed hot gas flow plumbing nozzle is provided with one or more along said cylindrical barrel tangential direction.
4. according to the said city of claim 1 and industrial sludge mummification and purifying processing device, it is characterized in that said spiral deflector is arranged on a plurality of planes in the said cylindrical barrel; Each plane of said spiral deflector is provided with two of propeller-like, three or four blades.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220265091 CN202626000U (en) | 2012-06-06 | 2012-06-06 | Drying and purifying treatment device of urban sludge and industrial sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220265091 CN202626000U (en) | 2012-06-06 | 2012-06-06 | Drying and purifying treatment device of urban sludge and industrial sludge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202626000U true CN202626000U (en) | 2012-12-26 |
Family
ID=47379220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220265091 Expired - Fee Related CN202626000U (en) | 2012-06-06 | 2012-06-06 | Drying and purifying treatment device of urban sludge and industrial sludge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202626000U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109809671A (en) * | 2019-03-04 | 2019-05-28 | 程京生 | A kind of sludge treating system and method |
| CN112146355A (en) * | 2020-09-22 | 2020-12-29 | 施美 | Low temperature sludge drying-machine of high-efficient environmental protection |
| CN112358152A (en) * | 2020-03-12 | 2021-02-12 | 北京航天试验技术研究所 | Oil sludge drying device, working method and production line with device |
| CN112479544A (en) * | 2019-09-12 | 2021-03-12 | 广州新致晟环保科技有限公司 | Vertical sludge drier and method for drying sludge by using same |
-
2012
- 2012-06-06 CN CN 201220265091 patent/CN202626000U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109809671A (en) * | 2019-03-04 | 2019-05-28 | 程京生 | A kind of sludge treating system and method |
| CN112479544A (en) * | 2019-09-12 | 2021-03-12 | 广州新致晟环保科技有限公司 | Vertical sludge drier and method for drying sludge by using same |
| CN112358152A (en) * | 2020-03-12 | 2021-02-12 | 北京航天试验技术研究所 | Oil sludge drying device, working method and production line with device |
| CN112146355A (en) * | 2020-09-22 | 2020-12-29 | 施美 | Low temperature sludge drying-machine of high-efficient environmental protection |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202626000U (en) | Drying and purifying treatment device of urban sludge and industrial sludge | |
| CN107596796A (en) | Multistage VOCs exhaust gas processing devices | |
| CN202893122U (en) | Flue gas cleaning device | |
| CN103601355A (en) | Spiral sludge drier | |
| CN203653402U (en) | Loop coil type sludge dryer | |
| CN203635019U (en) | Spray paint waste gas treatment device | |
| CN205115263U (en) | Utilize sludge drying equipment of low temperature flue gas | |
| CN202387241U (en) | Device for purifying and treating high-temperature flue gas containing persistent organic pollutants | |
| CN205088089U (en) | A oar formula stirring drying device for mummification mud | |
| CN204320230U (en) | A kind of when slurry-spraying pelletizing carries out to chemical fertilizer the tail cigarette of generation carry out the system of dedusting | |
| CN102008889B (en) | Compound type exhaust gas purification and deodorization device | |
| CN201609640U (en) | Tail water body structure for guiding airflow to tangentially impact liquid level to form moist airflow | |
| CN201101987Y (en) | Dust-removing heat-exchanger | |
| CN203653406U (en) | Special roller dryer for sludge | |
| CN205851055U (en) | A kind of circulation breaking drier | |
| CN206996146U (en) | A kind of novel environment friendly shaft furnace | |
| CN206051604U (en) | The low concentration wastewater that a kind of high efficiency of energy is utilized strengthens vaporising device | |
| CN201016550Y (en) | Portable double helix sludge drying apparatus | |
| CN108043543A (en) | Material powders temperature adjustment processing unit and its a variety of application methods | |
| CN203253352U (en) | Absorption device for desulfurization and dust removal | |
| CN201815240U (en) | Combined exhaust gas purifying and deodorizing device | |
| CN203253264U (en) | Waste treatment device of combustion furnace | |
| CN206404559U (en) | A kind of novel coating exhaust treatment system | |
| CN202724943U (en) | Multifunction dust remover | |
| CN103521018A (en) | Dedusting cooling tower for polyester resin production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20131126 Address after: 100029, 501C, room 1, 39 Anding Road, Beijing, Chaoyang District Patentee after: BEIJING MING SHUN TAK CENTER ENVIRONMENTAL EQUIPMENT CO., LTD. Address before: At the China University of Petroleum No. 18 Beijing city Changping district development plan 102249 Road Patentee before: Xi Yang |
|
| 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: 20121226 Termination date: 20210606 |