CN209411875U - A kind of reaction unit with metazoa decrement excess sludge - Google Patents
A kind of reaction unit with metazoa decrement excess sludge Download PDFInfo
- Publication number
- CN209411875U CN209411875U CN201822235478.9U CN201822235478U CN209411875U CN 209411875 U CN209411875 U CN 209411875U CN 201822235478 U CN201822235478 U CN 201822235478U CN 209411875 U CN209411875 U CN 209411875U
- Authority
- CN
- China
- Prior art keywords
- sludge
- area
- decrement
- metazoa
- mud
- 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.)
- Active
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Abstract
The utility model belongs to the technical field using biotechnology processing sludge, and in particular to a kind of reaction unit with metazoa decrement excess sludge.A kind of reaction unit with metazoa decrement excess sludge provided by the utility model includes sludge aging area, sludge conditioning area, three, mud decrement area functional area, a kind of reaction unit with metazoa decrement excess sludge provided by the utility model, it is capable of providing metazoa and suitably dissolves oxygen environment, sludge aging has been further speeded up simultaneously, realize the excess sludge treatment process based on metazoa, it is environmental and ecological, it is without secondary pollution, sludge after processed may be implemented unit sludge amount and reduce 60% or more, and the whole rhythm of the device is compact, capital construction and operating cost are low, occupied area is small, operation is simple, stability is preferable, continuous operation and unattended function can be achieved.
Description
Technical field
The utility model belongs to the technical field using biotechnology processing sludge, and in particular to a kind of to be subtracted with metazoa
Measure the reaction unit of excess sludge.
Background technique
The processing of China's sanitary wastewater and industrial wastewater mostly uses greatly activated sludge process, and there is capital expenditure to save, handle for it
The good advantage of effect, but it always exists a maximum drawback, that is, it can generate in the process of running a large amount of remaining dirty
Mud.In traditional activated sludge process, every degradation 1kg BOD5(Biochemical Oxygen Demand, five biochemical aerobic
Amount) excess sludge that about 15-100L can be generated, for handling or the expense for the treatment of excess sludge accounts for about sewage treatment total cost
25%-65%, the expense that European countries are used to handle excess sludge every year is as high as 2,800,000,000 RMB.It is clear that any
The measure for advantageously reducing excess sludge will all bring huge economic benefit.
Secondly, various Treatment of Sludge and the fund that method of disposal needs are huge, at present in the world at 80% or more sewage
Manage factory's application is Wastewater Treated by Activated Sludge Process sewage, and such as in America and Europe, Treatment of Sludge capital cost accounts for sewage treatment plant's total capital investment cost
Ratio is up to 60-70%.In recent years, wastewater treatment in China factory sharply increases, and corresponding surplus sludge volume is also increasing, and
The excess sludge disposition means in China are mainly landfill, burning and compost or he uses, and these types of method, which all exists, to be difficult to overcome
Technical bottleneck, sludge treatment ability lags far behind the actual needs of sludge treatment, especially this year, with some new environments
The promulgation and implementation of method, the depth and range require sewage treatment are all significantly increased, and inevitably result in the yield of excess sludge
It is increasing, meanwhile, excess sludge disposition of keeping under strict control is tightened by country, all realizes strictly from sludge entrucking-transport and disposition each stage
Monitoring, supply falls short of demand in sludge transport disposition market, and the operating cost of sewage treatment plant increases substantially, the processing and disposition of sludge
The a great problem of environmental area will be become.The demand urgent in face of this needs to develop a kind of sludge reduction process, realizes dirty
Mud source reduction.Existing multiple technologies are used for sludge reduction at present, mainly use physical chemistry or biological means, mainly
It destroys cell combination water or melts born of the same parents' technology, it is subsequent to still need to add a large amount of medicament and filter press dehydration.
Its attention, the predation digestion on biological (sludge organism chain top) after directly utilizing, from food
Chain pyramid it can be seen that, energy from bottom to food chain top transmit during, 90% or more is all distributed with form of heat
Fall, to reduce sludge yield from source.In actual operation, pig kiss wheel animalcule and erythema wooden dipper body worm are reported and can largely bite
Sludge is eaten, notably under the action of them, sludge concentration is down to 3000mg/L from 10000mg/L in the time.But at present this
Kind method is merely resting on the laboratory research stage, and engineer application is less.Therefore, according to these metazoa metabolic characteristics, originally
Utility model has devised a kind of reaction unit with metazoa decrement excess sludge, and it is remaining to be suitable for urban wastewater treatment firm
In sludge engineer application.
Utility model content
In order to solve the problems in the existing technology, subtracted the purpose of this utility model is to provide a kind of with metazoa
Measure the reaction unit of excess sludge.Reaction unit provided by the utility model with metazoa decrement excess sludge, Neng Gouti
Oxygen environment is suitably dissolved for metazoa, while having further speeded up sludge aging, is realized surplus based on metazoa
Remaining sludge handling process, it is environmental and ecological, it is without secondary pollution, it is processed after sludge may be implemented unit sludge amount reduce 60% with
On, while the whole rhythm of the device is compact, capital construction and operating cost are low, occupied area is small, operation is simple, and stability is preferable,
Continuous operation and unattended function can be achieved.
To achieve the above object, the utility model adopts the following technical solutions:
A kind of reaction unit with metazoa decrement excess sludge, including sludge aging area, sludge conditioning area, sludge subtract
Measure three, area functional area;The sludge aging area be cyclic structure, as the outer wall of whole device, the sludge conditioning area and
Mud decrement area is located inside the sludge aging area.
Further, the sludge aging area is provided with water inlet pipe, and enters mud pipe and sludge aging separate section;It is described into
Mud pipe is connect from the top in sludge aging area with sludge aging area;The water inlet pipe is located at the top of whole device and subtracts with sludge
Amount area is connected;The sludge aging separates the side of section close to enters mud pipe, and the other side is close to sludge conditioning area mud inlet;Institute
It states sludge aging area and helical regions is arranged to certain slope, acted on by gradient plug-flow, guarantee that sludge enters sludge aging
Qu Houneng is mobile according to clockwise direction, and enters sludge conditioning area from the enters mud pipe in sludge conditioning area, in the process, passes through
Extend sludge age and reduce dissolved oxygen and quickly allows sludge aging.
Further, the sludge conditioning area is provided with sludge conditioning area mud inlet and sludge conditioning area aeration plate;It is described
Sludge conditioning area mud inlet is located at the bottom in sludge conditioning area, and sludge aging area is connected with sludge conditioning area;The sludge
Regulatory region aeration plate is located at sludge conditioning area bottom;The regulatory region aeration plate is rotary mixing aerator, guarantees to flow into sludge tune
The sludge in section area can obtain certain stirring, be uniformly mixed, while can improve the content of dissolved oxygen.
Further, the mud decrement area is disposed with plate membrane control from top to bottom, and water level controller is rear lively
Object packing area is reduced aeration tube, sludge pipe;The decrement aeration tube uses micropore aeration pipe, can guarantee that mud decrement area obtains
Sufficiently aeration, considerably increases the content of dissolved oxygen, is suitble to the growth and breeding of metazoa, living by the metabolism of metazoa
Dynamic, excess sludge is reduced;The water level controller and plate membrane are used to control the water level of whole device.
Further, the reaction unit with metazoa decrement excess sludge further includes blower, and the blower passes through
Pipeline is connected respectively at the sludge conditioning aeration plate in sludge conditioning area with the decrement aeration tube in mud decrement area, is subtracted by sludge
The flowmeter measured on area's aeration tube and sludge conditioning area aeration plate carries out air quantity adjusting.
Further, the reaction unit with metazoa decrement excess sludge, the metazoa include pig kiss wheel
Worm and erythema wooden dipper body worm.
A kind of operational process of reaction unit with metazoa decrement excess sludge provided by the utility model are as follows: sludge
Sludge aging area is flowed into from enters mud pipe, since sludge aging area is arranged to helical regions with certain slope, so sludge passes through
Gradient plug-flow, from sludge conditioning area, mud inlet enters sludge conditioning area, under sludge conditioning area aeration plate aeration effect, inflow
Sludge obtains certain stirring, and dissolved oxygen is improved, and uniformly mixed sludge spills into mud decrement from sludge conditioning area
Area, by the abundant aeration of decrement area aeration tube, dissolved oxygen is greatly increased, and metazoa obtains sufficient growth and breeding, is led to
The metabolic activity of metazoa is crossed, excess sludge is reduced, and controls entire reactor with water level controller and plate membrane
Water level.When sludge concentration is excessively high, water inlet pipe can be passed through, the sludge that proper amount of clear water dilutes mud decrement area is added.When sludge quantity mistake
There is exception in big or system, can pass through the sludge pipe in mud decrement area and sludge is discharged.Decrement area aeration tube and sludge conditioning area expose
The air quantity of gas disk is provided by blower, and is equipped with flowmeter and is carried out flow adjusting.
Compared with prior art, a kind of reaction unit with metazoa decrement excess sludge provided by the utility model is used
It has the advantage that
(1) a kind of reaction unit with metazoa decrement excess sludge provided by the utility model, is provided with certain slope
The sludge aging area of degree is extended sludge age while reducing dissolved oxygen by the gradient plug-flow when sludge passes through sludge aging area
Content, can allow sludge quick aging, and aging and solution wadding sludge are easy to be ingested by metazoa, be conducive to the place of subsequent sludge
Reason.
(2) a kind of reaction unit with metazoa decrement excess sludge provided by the utility model, in sludge aging area
With increase sludge conditioning area among mud decrement area, reduce anaerobic sludge and the dissolved oxygen in mud decrement area impacted so that aging
Sludge enter mud decrement area after, although dissolved oxygen increase, without additional organic matter, it is suitable that this not only provides metazoa
Oxygen environment is dissolved, while having further speeded up sludge aging.
(3) a kind of reaction unit with metazoa decrement excess sludge provided by the utility model, considerably reduces
The operating cost of coagulated agent dosage and filter press, operation is simple, and stability is preferable, while realizing based on metazoa
Excess sludge treatment process, it is environmental and ecological, it is without secondary pollution, it can be achieved that continuous operation and unattended function.
Detailed description of the invention
Fig. 1 is the sectional view of utility model device;
Fig. 2 is the top view of utility model device;
Fig. 3 is the side view of utility model device;
In figure: 1, enters mud pipe, 2, water inlet pipe, 3, sludge aging area, 4, metazoa packing area, 5, mud decrement area, 6,
Decrement area aeration tube, 7, sludge pipe, 8, sludge conditioning area aeration plate, 9, blower, 10, sludge conditioning area mud inlet, 11, sludge tune
Save area, 12, plate membrane, 13, sludge aging separate section, 14, water level controller.
Specific embodiment
Below by way of the description of specific embodiment, the utility model is described in further detail, but this is not practical to this
Novel limitation, those skilled in the art's basic thought according to the present utility model, can make various modifications or improvements, still
Without departing from the basic thought of the utility model, it both is within the protection scope of the present invention.
A kind of reaction unit with metazoa decrement excess sludge provided by the utility model mainly includes sludge aging
Area 3, sludge conditioning area 11,5 three zones area, mud decrement area.The sludge aging area 3 is cyclic structure, as whole device
Outer wall, the sludge conditioning area 11 and mud decrement area 5 are located inside the sludge aging area 3.
The sludge aging area 3 is provided with water inlet pipe 2, and enters mud pipe 1 and sludge aging separate section 3;The enters mud pipe 1
It is connect from the top in sludge aging area 3 with sludge aging area 3;The water inlet pipe 2 is located at the top of whole device and subtracts with sludge
Amount area 5 is connected;The sludge aging separates the side of section 13 close to enters mud pipe 1, and the other side is close to sludge conditioning area into mud
Mouth 10;The sludge aging area 3 is arranged to helical regions with certain slope, is acted on by gradient plug-flow, guarantees that sludge enters
Can be mobile according to clockwise direction behind sludge aging area 3, and enter sludge conditioning area 11 from sludge conditioning area mud inlet 10, herein
In the process, sludge aging is quickly allowed by extending sludge age and reducing dissolved oxygen.
The sludge conditioning area 11 is provided with sludge conditioning area mud inlet 10 and sludge conditioning area aeration plate 8;The sludge
Regulatory region mud inlet 10 is located at the bottom in sludge conditioning area 11, and sludge aging area 3 is connected with sludge conditioning area 11;The dirt
Mud regulatory region aeration plate 8 is located at 11 bottom of sludge conditioning area;Sludge conditioning area aeration plate 8 is rotary mixing aerator, is guaranteed
The sludge for flowing into sludge conditioning area 11 can obtain certain stirring, be uniformly mixed, while can improve the content of dissolved oxygen.
The mud decrement area 5 is disposed with plate membrane 12, water level controller 14, metazoa packing area from top to bottom
4, it is reduced aeration tube 6, sludge pipe 7;The decrement aeration tube 6 uses micropore aeration pipe, can guarantee that mud decrement area 5 obtains sufficiently
Aeration, considerably increases the content of dissolved oxygen, is suitble to the growth and breeding of metazoa, by the metabolic activity of metazoa, remains
Remaining sludge is reduced;The metazoa includes pig kiss wheel animalcule and erythema wooden dipper body worm;The water level controller 14 and plate membrane
12 are used to control the water level of whole device.
The reaction unit with metazoa decrement excess sludge further includes blower 9, and the blower 9 is distinguished by pipeline
It is connected in the sludge conditioning aeration plate 8 in sludge conditioning area 11 with the decrement aeration tube 6 in mud decrement area 5, passes through mud decrement
Flowmeter on area's aeration tube 6 and sludge conditioning area aeration plate 8 carries out air quantity adjusting.
A kind of operational process of reaction unit with metazoa decrement excess sludge provided by the utility model are as follows: sludge
Sludge aging area 3 is flowed into from enters mud pipe 1, since sludge aging area 3 is arranged to helical regions with certain slope, so sludge is logical
Gradient plug-flow is crossed, enters sludge conditioning area 11, the aeration effect of aeration plate 8 in sludge conditioning area from sludge conditioning area mud inlet 10
Under, the sludge of inflow obtains certain stirring, and dissolved oxygen is improved, and uniformly mixed sludge is overflowed from sludge conditioning area 11
To mud decrement area 5, by the abundant aeration of decrement area aeration tube 6, dissolved oxygen is greatly increased, and metazoa obtains adequately
Growth and breeding, by the metabolic activity of metazoa, excess sludge is reduced, and with water level controller 14 and plate membrane 12
Control the water level of entire reactor.When sludge concentration is excessively high, water inlet pipe 2 can be passed through proper amount of clear water is added and dilute mud decrement area 5
Sludge.When sludge quantity is excessive or system occurs abnormal, the sludge pipe 7 in mud decrement area 5 can be passed through, sludge is discharged.Decrement area exposes
The air quantity of tracheae 6 and sludge conditioning area aeration plate 8 is provided by blower 9, and is equipped with flowmeter and is carried out flow adjusting.
The above embodiments are only illustrative of the principle and efficacy of the utility model, and not for limitation, this is practical new
Type.Any person skilled in the art can all carry out above-described embodiment under the spirit and scope without prejudice to the utility model
Modifications and changes.Therefore, such as those of ordinary skill in the art without departing from the revealed essence of the utility model
All equivalent modifications or change completed under mind and technical idea, should be covered by the claim of the utility model.
Claims (6)
1. a kind of reaction unit with metazoa decrement excess sludge, which is characterized in that including sludge aging area, sludge conditioning
Area, three, mud decrement area functional area, the sludge aging area is cyclic structure, as the outer wall of whole device, the dirt
Mud regulatory region and mud decrement area are located inside the sludge aging area;
The sludge aging area is provided with water inlet pipe, and enters mud pipe and sludge aging separate section;The enters mud pipe is old from sludge
The top for changing area is connect with sludge aging area;The water inlet pipe is located at the top of whole device and is connected with mud decrement area;
The sludge aging separates the side of section close to enters mud pipe, and the other side is close to sludge conditioning area mud inlet;
The sludge conditioning area is provided with sludge conditioning area mud inlet and sludge conditioning area aeration plate;The sludge conditioning area is into mud
Mouth is located at the bottom in sludge conditioning area, and sludge aging area is connected with sludge conditioning area;The sludge conditioning area aeration plate position
In sludge conditioning area bottom;
The mud decrement area is disposed with plate membrane control, water level controller, metazoa packing area, decrement from top to bottom
Aeration tube, sludge pipe;
The reaction unit with metazoa decrement excess sludge further includes blower;The blower and pipeline is respectively at sludge
The sludge conditioning aeration plate of regulatory region is connected with the decrement aeration tube in mud decrement area, passes through mud decrement area aeration tube and dirt
Flowmeter on mud regulatory region aeration plate carries out air quantity adjusting.
2. as described in claim 1 with the reaction unit of metazoa decrement excess sludge, which is characterized in that the sludge is old
Change area and helical regions are arranged to certain slope.
3. as described in claim 1 with the reaction unit of metazoa decrement excess sludge, which is characterized in that the regulatory region
Aeration plate is rotary mixing aerator.
4. as described in claim 1 with the reaction unit of metazoa decrement excess sludge, which is characterized in that the water level control
Device processed and plate membrane are used to control the water level of whole device.
5. as described in claim 1 with the reaction unit of metazoa decrement excess sludge, which is characterized in that the decrement exposes
Tracheae is micropore aeration pipe.
6. as described in claim 1 with the reaction unit of metazoa decrement excess sludge, which is characterized in that lively after described
Object includes pig kiss wheel animalcule and erythema wooden dipper body worm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201822235478.9U CN209411875U (en) | 2018-12-28 | 2018-12-28 | A kind of reaction unit with metazoa decrement excess sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201822235478.9U CN209411875U (en) | 2018-12-28 | 2018-12-28 | A kind of reaction unit with metazoa decrement excess sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
CN209411875U true CN209411875U (en) | 2019-09-20 |
Family
ID=67941347
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201822235478.9U Active CN209411875U (en) | 2018-12-28 | 2018-12-28 | A kind of reaction unit with metazoa decrement excess sludge |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN209411875U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109455813A (en) * | 2018-12-28 | 2019-03-12 | 肇庆市鹏凯环保装备有限公司 | A kind of reaction unit with metazoa decrement excess sludge |
-
2018
- 2018-12-28 CN CN201822235478.9U patent/CN209411875U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109455813A (en) * | 2018-12-28 | 2019-03-12 | 肇庆市鹏凯环保装备有限公司 | A kind of reaction unit with metazoa decrement excess sludge |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Yuan et al. | Woodchips as sustained-release carbon source to enhance the nitrogen transformation of low C/N wastewater in a baffle subsurface flow constructed wetland | |
CN103880248B (en) | A kind of coking wastewater processing system and treatment process | |
CN107381961A (en) | A kind of processing system of decentralized type sewage and the processing method using the processing system | |
CN107473471B (en) | Sewage purification treatment device | |
CN207175585U (en) | Compound biochemical reactor | |
CN102329043B (en) | Method for treating and printing and dyeing wastewater by using hydrolysis tank | |
CN106830542A (en) | UASB two-stage A/O coagulating treatments pig farm biogas slurry system | |
CN106946403A (en) | UASB two-stage A/O coagulating treatments pig farm biogas slurry technique | |
CN204490603U (en) | The reaction unit of phosphate from sewage is efficiently removed without anaerobic phosphorus release | |
CN209411875U (en) | A kind of reaction unit with metazoa decrement excess sludge | |
CN206607071U (en) | A kind of sewage treatment unit based on water treatment agent and ceramic membrane | |
CN205347142U (en) | Aquaculture wastewater treatment system | |
CN209872704U (en) | Device for low-energy-consumption high-efficiency enhanced treatment of printing and dyeing wastewater | |
CN205710290U (en) | A kind of integrated sewage water purifier | |
CN204752492U (en) | Integration membrane biological reaction device | |
CN208649042U (en) | Sewage treatment unit | |
CN207192920U (en) | Highly effective anaerobic reaction dephosphorization equipment | |
CN109455813A (en) | A kind of reaction unit with metazoa decrement excess sludge | |
CN105884146A (en) | Rural distributed wastewater treatment system | |
CN210595462U (en) | Double-chamber artificial rapid infiltration sewage purification system | |
CN209583911U (en) | A kind of laboratory integration waste water treatment system | |
CN208667382U (en) | A kind of biological water purification device | |
CN208980415U (en) | A kind of built-in solid-phase carbon source denitrification packed column reactor | |
CN208038125U (en) | Device for removing total nitrogen in sewage | |
CN202322576U (en) | Sludge minimizing system with high efficiency and low consumption |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address |
Address after: 526238 No. 2, Gangnan street, high tech Industrial Development Zone, Zhaoqing City, Guangdong Province Patentee after: Guangdong Pengkai Intelligent Equipment Manufacturing Co.,Ltd. Address before: 526060 No.2, Wende 3rd Street, Gaoxin District, Zhaoqing City, Guangdong Province Patentee before: ZHAOQING PENGKAI ENVIRONMENTAL PROTECTION EQUIPMENT Co.,Ltd. |
|
CP03 | Change of name, title or address |