CN206396031U - A kind of city domestic sewage handles plant excess sludge deep dehydration system - Google Patents
A kind of city domestic sewage handles plant excess sludge deep dehydration system Download PDFInfo
- Publication number
- CN206396031U CN206396031U CN201621075005.1U CN201621075005U CN206396031U CN 206396031 U CN206396031 U CN 206396031U CN 201621075005 U CN201621075005 U CN 201621075005U CN 206396031 U CN206396031 U CN 206396031U
- Authority
- CN
- China
- Prior art keywords
- sludge
- excess sludge
- domestic sewage
- city domestic
- deep dehydration
- 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
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Plant excess sludge deep dehydration system, including Centrafugal speed accelerator, ultrasonic cavitation dehydrator, sedimentation basin, filter press are handled the utility model discloses a kind of city domestic sewage.Compared with prior art, the utility model destroys the flocculation structure of sludge using Centrafugal speed accelerator, the sedimentation effect and muddy water for improving sludge have divided effect, and the cell wall structure and capillary pipe structure destroyed using ultrasonic combined Hydrodynamic Cavitation Technology in excess sludge, the difficult capillary water removed and intracellular water is set to be changed into the surface water easily removed, it is high with dewatering efficiency, simple system, it is easy to operational management, the technical advantage of non-secondary pollution.
Description
Technical field
The utility model is related to a kind of sludge dehydration device, belongs to fixed-end forces technical field, more particularly to a kind of life of city
Sewage disposal plant excess sludge deep dehydration system living.
Background technology
City domestic sewage processing plant excess sludge is the accessory substance of Wastewater Treated by Activated Sludge Process city domestic sewage, yield
Greatly, moisture content is high, turns into a main source of municipal solid wastes at present, there is the anxiety in " sludge besieged city ", still, we
It is a kind of potential energy and resource, if can be rationally sharp simultaneously it is also seen that containing substantial amounts of organic matter in excess sludge
With, you can turn waste into wealth.Under resource and the energy increasingly overall situation of shortage, city domestic sewage processing plant excess sludge will be
The preparation of the energy and resource furnishes ample material, in recent years, the energy and recycling of excess sludge of municipal sewage plant
It is with considerable scale, such as, burning electricity generation is carried out by raw material of excess sludge, using excess sludge as raw material, passes through anaerobic fermentation
Obtain hydrogen-rich fuel methane etc..But, there is also some problems during the recovery energy of excess sludge, such as, remain
The calorific value of remaining sludge is too low, and recovery energy cost is higher, and economic benefit is poor, and this is primarily due to China's city domestic sewage
Processing plant excess sludge content of organics is relatively low, and moisture content is higher, if it is aqueous to reduce sludge by suitable technical measures
Rate, so as to reduce the heat loss of excess sludge burning process, improves the economic benefit that sludge incineration generates electricity, may advantageously facilitate residue
The recovery energy of sludge.Moisture in excess sludge is roughly divided into four classes：Void among particles water, accounts for sludge water content
70%, typically separated with concentration method；Some small capillaries are formed between mud granule, the water being filled with claims capillary water, about
20% is accounted for, can be using supercentrifuge dehydration, negative pressure or positive-pressure filtering machine dehydration（Dehydration cost is too high）；The absorption water quilt of particle
Absorption accounts for 7% or so, can removed with heating in particle surface；It is present in inside mud granule or in microbial cell
Water is referred to as internal water, accounts for the 3% of sludge, can remove intracellular water or high-temperature heating method, freezing using bioanalysis destruction cell membrane
Method is removed.By prior art as can be seen that still lacking the device of systematization, realize that the synchronization of all kinds of moisture content in excess sludge is gone
Remove.
Utility model content
The purpose of this utility model is that the defect overcome present in existing excess sludge dehydration technique, and provides a kind of
City domestic sewage handles plant excess sludge deep dehydration system.
The utility model is achieved through the following technical solutions above-mentioned purpose：Centrafugal speed accelerator 1, ultrasound-cavitation dehydrator
2nd, sedimentation basin 3, filter press 4.Described Centrafugal speed accelerator 1 is by charging aperture 10, spiral case flow diverter 11, cylinder 12, cone 13, spoil disposal
Mouth 14 is constituted；Ultrasound-cavitation dehydrator 2 is made up of sleeve pipe 20, supersonic generator 21, sludge cavitation device 22；Sludge cavitation device
22 by screw joint casing 221, jet blower 222, molten air chamber 223, pipe joint 224, air intake duct 225, check valve 226, trunnion
227th, increaser 228, adpting flange 229 are constituted, and sedimentation basin 3 is constituted provided with enters mud pipe 31, drainpipe 32, discharge pipeline 33；Charging
Mouth 10 is connected with spiral case flow diverter 11 using bolt seal, and spiral case flow diverter 11 is connected with cylinder 12 using bolt seal, cylinder
12 are connected with cone 13 using flange seal, and the bottom of cone 13 is tangentially welded with mud discharging mouth 14, and mud discharging mouth 14 is with being threadedly coupled
Sleeve pipe 221 is connected using thread seal, and screw joint casing 221 is connected with jet blower 222 by thread seal；Jet blower 222
It is connected with molten air chamber 223 by thread seal；Inclined pipe joint 224 is provided with molten air chamber 223；Pipe joint 224 and air-breathing
Pipe 225 is connected in thread seal mode；Molten air chamber 223 is connected with trunnion 227 with thread seal；Trunnion 227 and increaser 228 with
Thread seal is connected；Increaser 228 is tightly connected with enters mud pipe 31 by adpting flange 229.Sleeve pipe 20 and sludge cavitation device 22
It is coaxial to be arranged concentrically, and the outside of sludge cavitation device 22 is enclosed on, supersonic generator 21 is arranged at sleeve pipe 20 and sludge cavitation
Between device 22 and the inwall of sleeve pipe 20 is fixedly installed in, sleeve pipe 20 is welded and fixed with sludge cavitation device 22 using grizzly bar.
Further, it is 4 that the internal diameter of described screw joint casing 221 is beneficial with the ratio between the described internal diameter of jet blower 222:
1~3:1。
Further, the internal diameter of described screw joint casing 221 is not less than 150mm.
Further, the length of described molten air chamber 223 and the length ratio of described jet blower 222 are beneficial for 1:1.8~1:
1.5。
Further, it is 2.2 that the internal diameter of described molten air chamber 223 is beneficial with the ratio between the described internal diameter of trunnion 227:1~2.6:
1。
Further, it is 1 that the internal diameter of described trunnion 227 is beneficial with the ratio between the end internal diameter of increaser 228:6~1:8.
Further, the length of described molten air chamber 223, the length of described trunnion 227, described increaser 228
Length ratio benefit is 1:1.5:3.
Further, the inclination angle benefit of described pipe joint 224 is at 30 ° ~ 40 °.
Further, described check valve 226 is installed on described air intake duct 225.
Further, described filter press 4 preferably uses chamber filter press.
Further, described sedimentation basin 3 preferably uses swash plate tube settler.
The beneficial effects of the utility model are：The utility model provides a kind of city domestic sewage processing plant excess sludge
Deep dehydration system, compared with prior art, it enters in sludge cavitation device after being accelerated by Centrafugal speed accelerator is carried out at cavitation
Reason, while realizing the destruction of capillary wall and the destruction of cell membrane in excess sludge under Hydrodynamic cavitation and ultrasonic irradiation, makes
Capillary water and intracellular combination water in excess sludge are discharged, and carry out mud-water separation in sedimentation basin afterwards, separating obtained
Excess sludge can be that deep dehydration can be achieved after press filtration, meanwhile, the sludge dewatering system need not add chemical agent, be difficult production
Raw secondary pollution, the recycling sludge utilization ways after processing extensively, have a good application prospect.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the utility model Centrafugal speed accelerator structural representation.
Fig. 3 is the utility model ultrasound-cavitation evaporator structure schematic diagram.
Fig. 4 is the utility model sleeve pipe, sludge cavitation device, supersonic generator scheme of installation.
Fig. 5 is the utility model sludge cavitation device configuration schematic diagram.
In Fig. 1 ~ 5：1- Centrafugal speed accelerators, 2- ultrasounds-cavitation dehydrator, 3- sedimentation basins, 4- filter presses, 10- charging apertures,
11- spiral cases flow diverter, 12- cylinders, 13- cones, 14- mud discharging mouths, 20- sleeve pipes, 21- supersonic generators, 22- sludge cavitations
Device, 221- screw joint casings, 222- jet blowers, the molten air chambers of 223-, 224- pipe joints, 225- air intake ducts, 226- check valves,
227- trunnions, 228- increasers, 229- adpting flanges, 31- enters mud pipes, 32- drainpipes, 33- discharge pipelines.L1The length of-molten air chamber
Degree, L2- jet blower length, L3The length of-trunnion, L4The length of increaser, α-pipe joint inclination angle, D1- screw joint casing it is interior
Footpath, D2Internal diameter, the D of-jet blower3Internal diameter, the D of-molten air chamber4Internal diameter, the D of-trunnion5The end internal diameter of-increaser.
Embodiment
1 ~ 5 the utility model is described in further detail below in conjunction with the accompanying drawings：
As shown in Figure 1 and 2：1- Centrafugal speed accelerators, 2- ultrasounds-cavitation dehydrator, 3- sedimentation basins, 4- filter presses, 10- chargings
Mouth, 11- spiral cases flow diverter, 12- cylinders, 13- cones, 14- mud discharging mouths, 20- sleeve pipes, 21- supersonic generators, 22- sludge are empty
Change device, 221- screw joint casings, 222- jet blowers, the molten air chambers of 223-, 224- pipe joints, 225- air intake ducts, 226- check valves,
227- trunnions, 228- increasers, 229- adpting flanges, 31- enters mud pipes, 32- drainpipes, 33- discharge pipelines.
As shown in Fig. 1 ~ 5：Excess sludge enters described spiral case flow diverter 11, excess sludge warp through described charging aperture 10
Entered after the drainage of spiral case flow diverter 11 with tangential direction in cylinder 12, rotation moves downwardly to cone 13 in cylinder 12, with
Excess sludge rotates in cone 13 to be moved downward, and the speed of excess sludge is gradually lifted, to excess sludge during 13 bottom of cone
Speed reaches maximum, now, and excess sludge enters ultrasound-cavitation dehydrator 2 by mud discharging mouth 14 through the high speed of screw joint casing 221
In, sprayed at a high speed in molten air chamber 223 by jet blower 222, at the same time, excess sludge enters at a high speed molten air chamber 223, makes molten air chamber
223 show negative pressure state, therefore, and air is entered in molten air chamber 223 with spraying at a high speed through air intake duct 225 by check valve 226
Excess sludge be sufficiently mixed, the excess sludge being mixed with gas-solid water tri-state enters in trunnion 227 therewith, in trunnion 227
End, the excess sludge containing large quantity of air enter increaser 228 in, now, due to sharply increasing for flow section, flow velocity
Rapid reduction, cavitation processes are completed in the drastically change procedure of flow velocity, and the bubble being mixed into excess sludge is being grown up and buried in oblivion
During capillary water and born of the same parents in destruction, excess sludge are produced to the capillary pipe structure in excess sludge and cell wall structure
Interior water is converted into interstitial water and absorption water, because excess sludge enters after ultrasound-cavitation dehydrator 2, all the time by ultrasonic amplitude
Penetrate, destroyed more complete of cell membrane and capillary, capillary water and intracellular water can more thoroughly be released to Free water, residue
Moisture in sludge is more easy to remove, afterwards, and excess sludge mixture enters after increaser 228, and molten air chamber 223 is again by air-breathing
Air produces swabbing action to pipe 225 to external world, cavitation processes is continued progress, realizes the continuous cavitation processing of excess sludge, surpasses
Excess sludge after sound-cavitation process enters to enter in sedimentation basin 3 with admixture with the Free water discharged through enters mud pipe 31
Row muddy water initial gross separation, supernatant is discharged by drainpipe 32 and is back to water process link and handled, and the sludge after precipitation is then
Enter through discharge pipeline 33 in filter press 4 and carry out filter-press dehydration, because the cell membrane and capillary in excess sludge are entirely destroyed,
The main surface water to be easy to press filtration removing of moisture in excess sludge is present, therefore moisture content drastically drops after excess sludge press filtration
It is low, realize that city domestic sewage handles the target of plant excess sludge deep dehydration.
The utility model destroys the flocculation structure of sludge using Centrafugal speed accelerator, improves the sedimentation effect and muddy water point of sludge
Effect, and the cell wall structure and capillary pipe structure that are destroyed using ultrasonic combined Hydrodynamic Cavitation Technology in excess sludge,
The difficult capillary water removed and intracellular water is changed into the surface water easily removed, substantially increase sludge dewatering efficiency, have compressed dirt
Mud amount, meanwhile, during system operation, the addition of no chemical agent is not likely to produce secondary pollution, and the chemical property of sludge changes
Become little, be conducive to its follow-up recycling.
Claims (6)
1. a kind of city domestic sewage handles plant excess sludge deep dehydration system, it is characterised in that：Including：Centrafugal speed accelerator
（1）, ultrasound-cavitation dehydrator（2）, sedimentation basin（3）, filter press（4）, charging aperture（10）, spiral case flow diverter（11）, cylinder
（12）, cone（13）, mud discharging mouth（14）, sleeve pipe（20）, supersonic generator（21）, sludge cavitation device（22）, threaded connecting sleeve
Pipe（221）, jet blower（222）, molten air chamber（223）, pipe joint（224）, air intake duct（225）, check valve（226）, trunnion
（227）, increaser（228）, adpting flange（229）, enters mud pipe（31）, drainpipe（32）, discharge pipeline（33）；Its middle charging aperture
（10）With spiral case flow diverter（11）Connected using bolt seal, spiral case flow diverter（11）With cylinder（12）Connected using bolt seal
Connect, cylinder（12）With cone（13）Connected using flange seal, cone（13）Bottom is tangentially welded with mud discharging mouth（14）, spoil disposal
Mouthful（14）With screw joint casing（221）Connected using thread seal, screw joint casing（221）With jet blower（222）Pass through
Thread seal is connected, jet blower（222）With molten air chamber（223）Connected by thread seal, molten air chamber（223）On be provided with inclination
Pipe joint（224）, pipe joint（224）With air intake duct（225）Connected in thread seal mode, molten air chamber（223）With trunnion
（227）Connected with thread seal, trunnion（227）With increaser（228）Connected with thread seal, increaser（228）With enters mud pipe
（31）Pass through adpting flange（229）It is tightly connected, sleeve pipe（20）With sludge cavitation device（22）It is coaxial to be arranged concentrically, and it is enclosed on dirt
Mud cavitation device（22）Outside, supersonic generator（21）It is arranged at sleeve pipe（20）With sludge cavitation device（22）Between and fixed peace
Loaded on sleeve pipe（20）Inwall, sleeve pipe（20）With sludge cavitation device（22）It is welded and fixed using grizzly bar.
2. a kind of city domestic sewage processing plant excess sludge deep dehydration system according to claim 1, it is characterized in that：
Described Centrafugal speed accelerator is made up of described charging aperture, spiral case flow diverter, cylinder, cone, mud discharging mouth.
3. a kind of city domestic sewage processing plant excess sludge deep dehydration system according to claim 1, it is characterized in that：
Described ultrasound-cavitation dehydrator is made up of described sleeve pipe, supersonic generator, sludge cavitation device.
4. a kind of city domestic sewage processing plant excess sludge deep dehydration system according to claim 1, it is characterized in that：
Described sludge cavitation device by described screw joint casing, jet blower, molten air chamber, pipe joint, air intake duct, check valve, trunnion,
Increaser, adpting flange composition.
5. a kind of city domestic sewage processing plant excess sludge deep dehydration system according to claim 1, it is characterized in that：
Described sedimentation basin preferably uses swash plate tube settler.
6. a kind of city domestic sewage processing plant excess sludge deep dehydration system according to claim 1, it is characterized in that：
The described press filtration principles of action use chamber filter press.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621075005.1U CN206396031U (en) | 2016-09-23 | 2016-09-23 | A kind of city domestic sewage handles plant excess sludge deep dehydration system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621075005.1U CN206396031U (en) | 2016-09-23 | 2016-09-23 | A kind of city domestic sewage handles plant excess sludge deep dehydration system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206396031U true CN206396031U (en) | 2017-08-11 |
Family
ID=59507735
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621075005.1U Expired - Fee Related CN206396031U (en) | 2016-09-23 | 2016-09-23 | A kind of city domestic sewage handles plant excess sludge deep dehydration system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206396031U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108046550A (en) * | 2017-11-28 | 2018-05-18 | 四川理工学院 | A kind of excess sludge ultrasound rotational flow, which is combined, cracks technique |
| CN114804551A (en) * | 2022-03-25 | 2022-07-29 | 中瑞(苏州)资源环境科技有限公司 | One-stop method for sludge disposal and resource utilization for ecological restoration |
-
2016
- 2016-09-23 CN CN201621075005.1U patent/CN206396031U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108046550A (en) * | 2017-11-28 | 2018-05-18 | 四川理工学院 | A kind of excess sludge ultrasound rotational flow, which is combined, cracks technique |
| CN114804551A (en) * | 2022-03-25 | 2022-07-29 | 中瑞(苏州)资源环境科技有限公司 | One-stop method for sludge disposal and resource utilization for ecological restoration |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102992559B (en) | Method for comprehensively utilizing anaerobic digestion and carbonization of municipal sludge | |
| CN102730912B (en) | Integrated sewage-sludge treatment method | |
| CN102921695A (en) | Water-sorting resource, harmlessness and natural-derivation recycling eco-system of municipal domestic wastes | |
| WO2015149519A1 (en) | Radial-flow-type hydrothermal reactor for sludge pyrohydrolysis treatment | |
| CN202945139U (en) | Sludge dewatering device | |
| CN206396031U (en) | A kind of city domestic sewage handles plant excess sludge deep dehydration system | |
| CN103724056A (en) | Hydrothermal carbonization-based value added disposing method for household garbage | |
| CN109368953A (en) | A kind of processing method and processing device of riverway sludge | |
| CN205295098U (en) | Mud resourceful treatment device | |
| CN102815847B (en) | Method for producing organic fertilizer by processing biological sludge, and sludge dewatering granulator | |
| CN104083918A (en) | Screw squeezing dewaterer | |
| CN101007743A (en) | Garbage methane processing and resource utilization machine set | |
| Huang et al. | Research on the experiment of the enhancement removal of fine sand by hydrocyclone in sewage treatment plant | |
| CN202898107U (en) | Water distribution device for anaerobic sludge reactors | |
| CN107434343A (en) | Method without Matter Transfer in mechanical agitation Treatment of Sludge anaerobic reactor and reactor | |
| CN104096394A (en) | Screw pressing dewaterer for sludge dewatering | |
| CN208327776U (en) | A kind of novel residual active sludge carbon source recyclable device | |
| CN207608472U (en) | A kind of city domestic sewage residual sludge reduction device | |
| CN207552307U (en) | A kind of island rubbish biological mass-energy processing system | |
| CN206721005U (en) | Without mechanical agitation Treatment of Sludge anaerobic reactor | |
| CN206328286U (en) | A kind of city sewage deep treatment device | |
| CN205575774U (en) | Efficient D -UASB reactor | |
| CN206645981U (en) | A kind of municipal sludge deodorization decrement processing apparatus | |
| CN207259356U (en) | A kind of energy-efficient continuous radial-flow sludge rapid subsidence storehouse | |
| CN220745675U (en) | Sludge fine silt separation equipment |
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: 20170811 Termination date: 20180923 |