CN206624766U - A kind of sludge high-drying integrating device - Google Patents
A kind of sludge high-drying integrating device Download PDFInfo
- Publication number
- CN206624766U CN206624766U CN201720166091.5U CN201720166091U CN206624766U CN 206624766 U CN206624766 U CN 206624766U CN 201720166091 U CN201720166091 U CN 201720166091U CN 206624766 U CN206624766 U CN 206624766U
- Authority
- CN
- China
- Prior art keywords
- crawler belt
- negative
- sludge
- pressure
- integrating device
- 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
- 239000010802 sludge Substances 0.000 title claims abstract description 53
- 238000001035 drying Methods 0.000 title claims abstract description 21
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims abstract description 13
- 230000008676 import Effects 0.000 claims abstract description 4
- 239000004744 fabric Substances 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 8
- 230000005611 electricity Effects 0.000 claims description 6
- 238000005370 electroosmosis Methods 0.000 claims description 6
- 230000000694 effects Effects 0.000 claims description 5
- 239000004809 Teflon Substances 0.000 claims description 3
- 229920006362 Teflon® Polymers 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 3
- 230000001360 synchronised effect Effects 0.000 claims description 3
- 238000011026 diafiltration Methods 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 11
- 230000008569 process Effects 0.000 abstract description 6
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 230000008901 benefit Effects 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000018044 dehydration Effects 0.000 description 4
- 238000006297 dehydration reaction Methods 0.000 description 4
- 239000010865 sewage Substances 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
It the utility model is related to a kind of sludge high-drying integrating device.Described integrating device includes sludge import, electric osmose permeable system, disintegrating machine, negative-pressure microwave system, pedestal and control device, described pedestal fixes on the ground, described electric osmose permeable system, disintegrating machine, negative-pressure microwave system are separately fixed on pedestal, and described electric osmose permeable system is sequentially connected disintegrating machine and negative-pressure microwave system.The utility model combines electric osmose permeable system, negative pressure system, microwave system, the characteristics of using three kinds of techniques in sludge handling process, the advantage of technique is combined, improve the drying efficiency of sludge, energy consumption is reduced, can be by the sludge dewatering of 80% moisture content to 40%.
Description
Technical field
It the utility model is related to a kind of sludge drying treatment equipment, more particularly to a kind of sludge high-drying integrating device.
Background technology
As the requirement to environment is improved in China, China increasingly payes attention to the processing to sewage, increased rapidly in recent years
Sewage disposal requirement will produce substantial amounts of biological sludge, and how can deal carefully with these sludge, turn into sewage disposal
Environmental problem urgently to be resolved hurrily.
Sludge is to be formed by the suspended solid in water through the cementing cohesion of various modes, loosely organized, in irregular shape, its
Specific surface area is high with porosity, and water content is high, and dehydration property is poor.There is branch and the network structure of similar appearance in appearance.It is dirty
Moisture percentage in sewage sludge caused by water treatment plant may be up to 99%, quality and bulky, is unfavorable for transporting and handles disposal, it is necessary to drop
Its low moisture content.
Moisture percentage in sewage sludge is down to 80% from 95%, and sludge volume reduces 75%, is down to 50% from 80%, volume will reduce 60% again.
When the moisture content of sludge is higher, his calorific value is lower, and when moisture content is less than 50%, sludge is just adapted to burn.And contain in sludge
There are a large amount of microbial cells and organic colloidal matter, mechanical dehydration difficulty.The moisture content of sludge is to restrict sludge treatment and utilization
Key issue, and the desiccation link of sludge be specific resistance to filtration system power consumption key link.
The heat and mass of sludge heat drying is mainly manifested in following two process：
First, evaporation process：The moisture of surface of material vaporizes, and the steam partial pressure in medium steams higher than the water of surface of material
Air pressure, therefore moisture moves into medium from surface of material；
Second, diffusion process：Diffusion process is with vaporizing closely related mass transport process.When surface of material moisture is evaporated
Fall, the humidity of surface of material is less than material interior humidity, at this time, it may be necessary to the motive force of heat by moisture from interior shifting to table
Face.
Above-mentioned two process continuously alternately, substantially reflects dry mechanism.It is it can thus be seen that dry
Dry is by surface water vapor, and moisture enters medium and internal water spreads, and the two are mutually auxiliary from material interior shifting to outside for moisture
The process coordinated is completed.
Existing sludge drying technique energy consumption is generally larger, and sludge drying is inefficient, and moisture content reduces unobvious.
Utility model content
The problem of the utility model is larger in order to solve traditional sludge drying process energy consumption, and sludge drying is inefficient, is carried
The dirt that a kind of drying efficiency is high, compact-sized, stable, energy utilization rate is high, dehydrating effect is obvious, operation energy consumption is low is supplied
The high desiccation integrating device of mud.
The technical solution of the utility model is：Described integrating device include sludge import, electric osmose permeable system, disintegrating machine,
Negative-pressure microwave system, pedestal and control device, described pedestal fix on the ground, described electric osmose permeable system, disintegrating machine, bear
Pressure microwave system is separately fixed on pedestal, and described electric osmose permeable system is sequentially connected disintegrating machine and negative-pressure microwave system.
Described electric osmose permeable system includes drive device, pressure roller, support roller, trolley, upper crawler belt, filter cloth, lower crawler belt, tensioning
Device, dc source, percolate collector, the upper crawler belt are arranged on lower crawler belt top, drive device be arranged on crawler belt and
Lower crawler belt both ends, pressure roller are arranged in crawler belt, and support roller is arranged in lower crawler belt；Filter cloth is arranged on crawler belt and lower crawler belt table
Face, it is synchronized with the movement by fast pulley and upper crawler belt, lower crawler belt, tensioning apparatus is connected with filter cloth；Dc source passes through trolley point
It is not connected with upper crawler belt, lower crawler belt；Percolate collector is arranged on below lower crawler belt.
Described negative-pressure microwave system includes charging aperture, conveyer belt system, microwave generator, surge tank, vavuum pump, discharging
Mouthful, the charging aperture, microwave generator, surge tank, vavuum pump are separately positioned on negative-pressure microwave system top；The conveyer belt system
System is arranged in negative-pressure microwave system, including conveyer belt support roller and conveyor drive arrangement；Discharging opening is arranged on negative-pressure microwave system
System lower section.
Between described upper crawler belt and lower crawler belt the wedge shape space for sludge preliminary hydro-extraction is provided with sludge entrance.
Described dc source is powered with upper crawler belt, lower crawler belt respectively by trolley, and upper crawler belt leads to positive electricity, and lower crawler belt leads to
Negative electricity, form electro-osmosis effect.
Described vavuum pump produces negative pressure to being evacuated in negative-pressure microwave system in negative-pressure microwave system.
Described conveyer belt system is made up of teflon material.
The utility model combines electric osmose permeable system, negative pressure system, microwave system, using three kinds of techniques at sludge
The characteristics of during reason, the advantage of technique is combined, improve the drying efficiency of sludge, reduce energy consumption, can be aqueous by 80%
The sludge dewatering of rate is to 40%.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
1 is drive device in figure, and 2 be pressure roller, and 3 be tugboat, and 4 be trolley, and 5 be upper crawler belt, and 6 be filter cloth, and 7 be lower shoe
Band, 8 be tensioning apparatus, and 9 be disintegrating machine, and 10 be charging aperture, and 11 be conveyer belt system, and 12 be microwave generator, and 13 be surge tank,
14 be vavuum pump, and 15 be dc source, and 16 be control device, and 17 be percolate collector, and 18 be pedestal, 19 discharging openings.
Embodiment
A kind of sludge high-drying integrating device, described integrating device include sludge import, electric osmose permeable system, disintegrating machine 9,
Negative-pressure microwave system, pedestal 18 and control device 16, described pedestal 18 fix on the ground, described electric osmose permeable system, break
Broken machine 9, negative-pressure microwave system are separately fixed on pedestal 18, and described electric osmose permeable system is sequentially connected disintegrating machine 9 and negative pressure is micro-
Wave system is united.
Described electric osmose permeable system includes drive device 1, pressure roller 2, support roller 3, trolley 4, upper crawler belt 5, filter cloth 6, lower shoe
Band 7, tensioning apparatus 8, dc source 15, percolate collector 17, the upper crawler belt 5 are arranged on the lower top of crawler belt 7, drive device
1 is arranged on crawler belt 5 and the lower both ends of crawler belt 7, and pressure roller 2 is arranged in crawler belt 5, and support roller 3 is arranged in lower crawler belt 7；Filter cloth 6 is set
Put in upper crawler belt 5 and the lower surface of crawler belt 7, be synchronized with the movement by fast pulley and upper crawler belt 5, lower crawler belt 7, tensioning apparatus 8 and filter cloth 6
Connection；Dc source 15 is connected with upper crawler belt 5, lower crawler belt 7 respectively by trolley 4；Percolate collector 17 is arranged on lower shoe
The lower section of band 7.
Described negative-pressure microwave system includes charging aperture 10, conveyer belt system 11, microwave generator 12, surge tank 13, true
Empty pump 14, discharging opening 19, the charging aperture 10, microwave generator 12, surge tank 13, vavuum pump 14 are separately positioned on negative-pressure microwave
System top；The conveyer belt system 11 is arranged in negative-pressure microwave system, including conveyer belt support roller and conveyor drive arrangement；
Discharging opening 19 is arranged on below negative-pressure microwave system.
Between described upper crawler belt 5 and lower crawler belt 7 wedge shape space for sludge preliminary hydro-extraction is provided with sludge entrance.
Described dc source 15 is powered with upper crawler belt 5, lower crawler belt 7 respectively by trolley 4, and upper crawler belt 5 leads to positive electricity, under
Crawler belt 7 leads to negative electricity, forms electro-osmosis effect.
Described vavuum pump 14 produces negative pressure to being evacuated in negative-pressure microwave system in negative-pressure microwave system.
Described conveyer belt system 11 is made up of teflon material.
At work, wet mud is introduced into electric osmose permeable system to the present apparatus, as lower crawler belt 7 travels forward, upper crawler belt 5 with
Wedge area between lower crawler belt 7 is extruded for the first time, drives crawler belt to enter sludge by pressure roller 2, support roller 3 into parallel zone afterwards
Row dehydration, at the same time, dc source 15 makes the upper positively charged of crawler belt 5, lower crawler belt 7 negatively charged by trolley 4, the water in sludge
Divide and extruding with departing under electro-osmosis double action with sludge, the effect of dehydration can be reached, percolate collector 17 is in lower shoe
The lower section of band 7 is collected to water；Sludge after electric osmose permeable system by entering disintegrating machine 9, the sludge powdering after broken
Negative-pressure microwave system is entered by charging aperture 10；Powdery sludge is distributed in negative-pressure microwave system on conveyer belt system 11, is led to
Conveyer belt system 11 is crossed to travel forward；During forward, microwave caused by microwave generator 12 carries out desiccation to sludge, with
This simultaneously, vavuum pump 14 is evacuated to negative-pressure microwave internal system, and dust and the foul smell that on the one hand internal system is floated suction out, separately
On the one hand internal system is in negative pressure state, be advantageous to the removal of sludge reclaimed water, the gas that vavuum pump 14 is extracted out is by buffering
Discharged after tank 13；Sludge discharges negative-pressure microwave system after conveyer belt system 11 from discharging opening 19, and central control system 16 can be completed
Control to the present apparatus.
Claims (7)
- A kind of 1. sludge high-drying integrating device, it is characterised in that：Described integrating device includes sludge import, electro-osmosis system System, disintegrating machine, negative-pressure microwave system, pedestal and control device, described pedestal fix on the ground, described electro-osmosis system System, disintegrating machine, negative-pressure microwave system are separately fixed on pedestal, and described electric osmose permeable system is sequentially connected disintegrating machine and negative pressure is micro- Wave system is united.
- A kind of 2. sludge high-drying integrating device according to claim 1, it is characterised in that：Described electric osmose permeable system bag Include drive device, pressure roller, support roller, trolley, upper crawler belt, filter cloth, lower crawler belt, tensioning apparatus, dc source, leachate collection Device, the upper crawler belt are arranged on lower crawler belt top, and drive device is arranged on crawler belt and lower crawler belt both ends, and pressure roller is arranged on shoe In band, support roller is arranged in lower crawler belt；Filter cloth is arranged on crawler belt and lower track surface, passes through fast pulley and upper crawler belt, lower shoe Band is synchronized with the movement, and tensioning apparatus is connected with filter cloth；Dc source is connected with upper crawler belt, lower crawler belt respectively by trolley；Diafiltration Collection is arranged on below lower crawler belt.
- A kind of 3. sludge high-drying integrating device according to claim 1, it is characterised in that：Described negative-pressure microwave system Including charging aperture, conveyer belt system, microwave generator, surge tank, vavuum pump, discharging opening, the charging aperture, microwave generator, Surge tank, vavuum pump are separately positioned on negative-pressure microwave system top；The conveyer belt system is arranged in negative-pressure microwave system, bag Include conveyer belt support roller and conveyor drive arrangement；Discharging opening is arranged on below negative-pressure microwave system.
- A kind of 4. sludge high-drying integrating device according to claim 2, it is characterised in that：Described upper crawler belt and lower shoe Between band the wedge shape space for sludge preliminary hydro-extraction is provided with sludge entrance.
- A kind of 5. sludge high-drying integrating device according to claim 2 or 4, it is characterised in that：Described dc source It is powered respectively with upper crawler belt, lower crawler belt by trolley, upper crawler belt leads to positive electricity, and lower crawler belt leads to negative electricity, forms electro-osmosis effect.
- A kind of 6. sludge high-drying integrating device according to claim 3, it is characterised in that：Described vavuum pump is to negative pressure It is evacuated in microwave system, negative pressure is produced in negative-pressure microwave system.
- A kind of 7. sludge high-drying integrating device according to claim 3, it is characterised in that：Described conveyer belt system by Teflon material is made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720166091.5U CN206624766U (en) | 2017-02-23 | 2017-02-23 | A kind of sludge high-drying integrating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720166091.5U CN206624766U (en) | 2017-02-23 | 2017-02-23 | A kind of sludge high-drying integrating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206624766U true CN206624766U (en) | 2017-11-10 |
Family
ID=60211630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720166091.5U Expired - Fee Related CN206624766U (en) | 2017-02-23 | 2017-02-23 | A kind of sludge high-drying integrating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206624766U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106865943A (en) * | 2017-02-23 | 2017-06-20 | 扬州博越生态技术有限公司 | A kind of sludge high-drying integrating device |
-
2017
- 2017-02-23 CN CN201720166091.5U patent/CN206624766U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106865943A (en) * | 2017-02-23 | 2017-06-20 | 扬州博越生态技术有限公司 | A kind of sludge high-drying integrating device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104803577B (en) | A kind of quick-dehydration device of High water cut mud | |
| CN206661910U (en) | A kind of refuse disposal installation easy to remove | |
| CN206624766U (en) | A kind of sludge high-drying integrating device | |
| CN107777853A (en) | Double dry method sludge treatment equipments | |
| CN106865943A (en) | A kind of sludge high-drying integrating device | |
| CN204769825U (en) | Centralized rubbish washs categorised facility | |
| CN202968346U (en) | Conducting tube type sludge drying machine | |
| CN211394160U (en) | Sewage treatment and discharge device for livestock breeding | |
| CN205214041U (en) | A high -efficient drying device for beef processing | |
| CN203393456U (en) | Wet-cloth vacuum dewatering machine | |
| CN217628075U (en) | Municipal sludge treatment system | |
| CN110395873A (en) | A kind of city sludge van-type Minton dryer | |
| CN203678133U (en) | Vacuum filter with pressure filtration function | |
| CN215667688U (en) | Solar sludge drying oven | |
| CN211770902U (en) | Sludge dewatering device | |
| CN212152053U (en) | Sludge electroosmosis deep dehydration coupling dehumidification drying device | |
| CN205090383U (en) | Domestic waste microwave mummification system | |
| CN211419963U (en) | Stepped energy-saving high-dryness electroosmosis sludge dewatering device and system | |
| CN207143076U (en) | A kind of bipacking-auger sludge temporary storage tank | |
| CN206970443U (en) | Electromagnetic energy quick sterilization sludge dehumidifying desiccation line | |
| CN207056703U (en) | For handling the reducing mechanism of house refuse | |
| CN111992570A (en) | Large kitchen garbage disposer | |
| CN205412379U (en) | Cauldron formula pressure filtration drying machine | |
| CN212222775U (en) | Energy-saving sludge treatment system | |
| CN214422492U (en) | Tower type process device for drying sludge fuel |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20171110 |