CN108726674A - Anaerobic reactor and waste-water anaerobic treatment process - Google Patents
Anaerobic reactor and waste-water anaerobic treatment process Download PDFInfo
- Publication number
- CN108726674A CN108726674A CN201710241490.8A CN201710241490A CN108726674A CN 108726674 A CN108726674 A CN 108726674A CN 201710241490 A CN201710241490 A CN 201710241490A CN 108726674 A CN108726674 A CN 108726674A
- Authority
- CN
- China
- Prior art keywords
- reative cell
- mud
- anaerobic reactor
- sludge
- cleaning shoe
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2866—Particular arrangements for anaerobic reactors
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/22—Eliminating or preventing deposits, scale removal, scale prevention
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The invention discloses a kind of anaerobic reactor and waste-water anaerobic treatment process, anaerobic reactor includes tank body and mud scraper, and there is reative cell, reative cell to have waste water inlet and methane outlet in tank body, the bottom surface of reative cell is equipped with mud-collecting slot, and the sludge outlet being connected to mud-collecting slot is equipped in the wall of tank body；Mud scraper includes cleaning shoe and driving device, and cleaning shoe is located at the bottom of reative cell, and the sludge on the bottom surface by reative cell scrapes in mud-collecting slot, and driving device is located at the bottom of tank body and is connected with cleaning shoe, for driving cleaning shoe to rotate.The anaerobic reactor and waste-water anaerobic treatment process of the present invention, it is low without stirring, consuming energy, and sludge and waste water good mixing effect, reduce anaerobic reactor bottom stirring dead zone, substantially increases water treatment effect.
Description
Technical field
The present invention relates to environmental technology fields, and in particular, to a kind of anaerobic reactor and waste water for handling waste water
Anaerobic treatment process.
Background technology
Anaerobic reactor is the commonly used equipment for handling waste water, and anaerobic sludge of the anaerobic reactor inside is by waste water
In COD processing be converted to biogas.Contain impurity, such as fiber (cow dung water), stalk etc. in waste water.In order to will be inside fiber etc.
COD be converted to biogas much more as possible, to generate certain upflow velocity in anaerobic reactor, improve Anaerobic Treatment effect
Fruit, waste water are usually pre-processed without fiber before entering in anaerobic reactor.Waste water is with anaerobic sludge mixing uniformity
An important factor for influencing treatment effect, improves treatment effect, in anaerobic reaction in order to enable waste water is uniformly mixed with anaerobic sludge
It is usually stirred in device.However, there is a problem of respective using the method that stirring improves mixed effect, there are improved need
It asks.
Invention content
The application is made to the discovery of following facts and problem and understanding based on inventor：
The stirring of anaerobic reactor has following several agitating modes：(1) compressed gas stirs：By into anaerobic reactor
Conveying compressed gas is stirred.This agitating mode is the problem is that high energy consumption, the security requirement to anaerobic reactor
It is high.(2) circulating pump stirs：The waste water of anaerobic reactor internal upper part is pumped into the lower part in anaerobic reactor by circulating pump,
For generating upward flow velocity, to rush waste water and sludge upwards, there is also stirring dead zones for this circulating pump agitating mode.
(3) mechanical agitation, i.e., be arranged stirrer paddle in anaerobic reactor, and stirrer paddle is led to by being located at the motor at the top of anaerobic reactor
Cross transmission shaft driving rotation.It needs to drive stirrer paddle by long transmission shaft due to being located at the motor at the top of anaerobic reactor,
Since the height of anaerobic reactor is usually larger, there is vibration greatly, the unstable problem of stirrer paddle.Stirrer paddle distance
The distance of anaerobic reactor inner bottom surface is usually the one third of anaerobic reactor height, if stirrer paddle apart from inner bottom surface too
Closely, then the loss of energy is stirred, energy consumption and cost are increased, if stirrer paddle is too far apart from inner bottom surface, anaerobic reactor bottom holds
Easily there is stirring dead zone (region that can not be stirred to), influences mixed effect.
Further, since sludge is easy to be deposited on the inner bottom surface of anaerobic reactor, traditional agitating mode can not be fine
Ground stirs the sludge on inner bottom surface, to influence the mixed effect of sludge and waste water.
Present invention recognize that it is above-mentioned tradition stirring there are the problem of, it is intended to solve at least to a certain extent in the related technology
One of the technical issues of.For this purpose, the present invention proposes a kind of anaerobic reactor and waste-water anaerobic treatment process, the anaerobic reactor and
Waste-water anaerobic treatment process is low without stirring, consuming energy, and sludge and waste water good mixing effect, reduces anaerobic reactor bottom
Dead zone is stirred, water treatment effect is substantially increased.
Anaerobic reactor according to the ... of the embodiment of the present invention, including：
Tank body, the tank body is interior, and there is reative cell, the reative cell to have waste water inlet and methane outlet, the reative cell
Bottom surface be equipped with mud-collecting slot, be equipped with the sludge outlet being connected to the mud-collecting slot in the wall of the tank body；
Mud scraper, the mud scraper include cleaning shoe and driving device, and the cleaning shoe is located at the bottom of the reative cell,
For scraping the sludge on the bottom surface of the reative cell in the mud-collecting slot, the driving device is located at the bottom of the tank body
And be connected with the cleaning shoe, for driving the cleaning shoe to rotate.
Waste-water anaerobic treatment process according to the ... of the embodiment of the present invention, including：
Waste water is supplied in the reative cell of anaerobic reactor to be detested waste water using the indoor sludge of reaction
Oxygen processing；
Sludge on the bottom surface of the reative cell is scraped in the mud-collecting slot being located on the bottom surface using mud scraper, it is described to scrape
Mud machine includes cleaning shoe and is located at the anaerobic reactor bottom for driving the driving device of the cleaning shoe；
The reative cell is discharged in sludge in the mud-collecting slot.
Anaerobic reactor and waste-water anaerobic treatment process according to the ... of the embodiment of the present invention, by mud scraper by reative cell bottom
Sludge scrape in mud-collecting slot, avoid sludge in the deposition of reative cell bottom, improve sludge and waste water mixed effect, and nothing
Agitating device need to be set, the problem of traditional agitating mode is brought is overcome.Since the driving device of driving mud scraper is located at tank body
Bottom, without being connected with mud scraper by long transmission shaft, mud scraper operates steadily, and vibration and noise are small.
Description of the drawings
Fig. 1 is the schematic diagram of anaerobic reactor according to a first embodiment of the present invention.
Fig. 2 is the schematic diagram of anaerobic reactor according to a second embodiment of the present invention.
Fig. 3 is the schematic diagram of anaerobic reactor according to a third embodiment of the present invention.
Fig. 4 is the schematic top plan view of anaerobic reactor according to the ... of the embodiment of the present invention.
Fig. 5 is the schematic diagram of anaerobic reactor according to a fourth embodiment of the present invention.
Specific implementation mode
The embodiment of the present invention is described below in detail, examples of the embodiments are shown in the accompanying drawings.Below with reference to
The embodiment of attached drawing description is exemplary, it is intended to for explaining the present invention, and is not considered as limiting the invention.
As shown in Figs 1-4, anaerobic reactor according to the ... of the embodiment of the present invention includes tank body 1 and mud scraper 4.
Specifically, the inner cavity of tank body 1 forms reative cell 11.Reative cell 11 is equipped with waste water inlet 2 and methane outlet 3, waste water
It is transported in reative cell 11 by waste water inlet 2, the biogas generated in reative cell 11 is discharged by methane outlet 3.Reative cell 11
Bottom surface be equipped with mud-collecting slot 6, mud-collecting slot 6 is used to collect sludge on the bottom surface of reative cell 11.Here, term " collection " refers to scraping
Sludge on the bottom surface of reative cell 11 is scraped and is focused in mud-collecting slot 6 by mud machine 4.
Mud scraper 4 includes cleaning shoe 41 and driving device 5.Cleaning shoe 41 be located at the bottom of reative cell 11 and with reative cell 11
Bottom surface and peripheral wall be spaced apart preset distance, for the sludge on the bottom surface of reative cell 11 to be scraped in mud-collecting slot 6.Driving device
5 are located at the bottom of tank body 1 and are connected with cleaning shoe 41, for driving cleaning shoe 41 to rotate.When cleaning shoe 41 rotates, by reative cell
The sludge of 11 bottom scrapes in mud-collecting slot 6, prevents the sludge settling in reative cell 11 in the bottom of reative cell 11.It is collected into collection
At least part sludge in mud groove 6 may return to the top of reative cell 11, and in other words, the sludge in mud-collecting slot 6 can be complete
Portion loops back to the top of reative cell 11, can also a part return reative cell 11 top, a part discharge.
Anaerobic reactor according to the ... of the embodiment of the present invention can will be anti-by the way that mud scraper 4 is arranged in the bottom of reative cell 11
It answers the sludge on the bottom surface of room 11 to scrape in mud-collecting slot 6, avoids sludgd deposition in the bottom of reative cell 11, moreover, mud is scraped in driving
The driving device 5 of plate 41 is also provided in the lower part of tank body 1 rather than the top of tank body 1, and there is no need to by long transmission shaft and scraping mud
Plate 41 is connected, and with small vibration, mud scraper operates steadily.The sludge being collected into mud-collecting slot 6 may return in reative cell 11, and useless
Water mixes.Anaerobic reactor according to the ... of the embodiment of the present invention as a result, is stirred to react the dirt of room bottom without traditional agitating device
Mud solves the above problem that traditional agitating mode is brought.
Below with reference to the accompanying drawings anaerobic reactor according to the specific embodiment of the invention is described.
As shown in Figure 1, in some embodiments, there is reative cell 11, reative cell 11 to have 2 He of waste water inlet in tank body 1
Methane outlet 3.The bottom surface of reative cell 11 is equipped with mud-collecting slot 6, sludge on the bottom surface for collecting reative cell 11.Mud scraper 4 wraps
Cleaning shoe 41 and driving device 5 are included, cleaning shoe 41 is for scraping the sludge on the bottom surface of reative cell 11 in mud-collecting slot 6.Scrape mud
Plate 41 is arranged adjacent to the bottom surface of reative cell 11, such as distance of the lower edge apart from the bottom surface of reative cell 11 of cleaning shoe 41 is less than 100
Millimeter.Driving device 5 is located at the bottom of tank body 1 and is connected with cleaning shoe 41, for driving cleaning shoe 41 to rotate.
Preferably, the rotating speed of cleaning shoe 41 be, for example, less than 5 turns/per hour, but it is not limited to this.In the embodiment of the present invention
In, as long as the rotating speed of cleaning shoe 41 allows cleaning shoe 41 to scrape the sludge on the bottom surface of reative cell 11 but does not play substantially
Stirring action.It will be understood to those skilled in the art that if to realize stirring, the mixing component for stirring for example stirs
The rotating speed for mixing blade is typically greater than scheduled value.However, in an embodiment of the present invention, the effect of cleaning shoe 41 is for scraping
Sludge on dynamic reative cell bottom surface, rather than for stirring action, therefore, anaerobic reactor according to the ... of the embodiment of the present invention does not have
The problem of anaerobic reactor stirred being needed with the presence of tradition.
In the example depicted in fig. 1, driving device 5 is hydraulic motor, to which driving device 5 can be immersed in waste water,
Without sealing, simplify structure.Driving device 5 can drive with the power plant outside tank body 1.
In further embodiments, as shown in Fig. 2, anaerobic reactor further includes circulating pump 7, the entrance and collection of circulating pump 7
The sludge outlet of mud groove 6 is connected to, and the outlet of circulating pump 7 is connected to the top of reative cell 11, and circulating pump 7 is used for will be in mud-collecting slot 6
At least part sludge pumping be recycled to the top of reative cell 11, to improve the mixed effect of sludge and waste water, improve useless
The treatment effect of water.
Circulating pump 7 can be arranged outside tank body 1.The entrance of circulating pump 7 is connected to the sludge outlet of mud-collecting slot 6, cycle
The outlet of pump 7 is connected to the top of reative cell 11.Collect entrance of at least part sludge in mud-collecting slot 6 from circulating pump 7
Into circulating pump 7, by the pump action of circulating pump 7, sludge enters from the outlet of circulating pump in reative cell, is mixed with waste water,
To which waste water is uniformly mixed with sludge, treatment effect improves.
In some instances, circulating pump 7 is along the tangential by sludge pumping to the top of reative cell 11 of reative cell 11.Namely
It says, the opening (or nozzle or nozzle direction) on the reative cell 11 being connected with circulating pump 7 is along the tangential of reative cell 11, sludge edge
It is tangential to spray into reative cell 11, so that the waste water in reative cell 11 is rotated in a circumferential direction movement, to avoid wastewater surface floating material
Accumulation, and waste water is uniformly mixed with sludge, and water treatment effect is more preferable.It is highly preferred that sludge is supplied to instead by circulating pump 7
The liquid level on the top of room 11 is answered in the following, to which the mixing of sludge and waste water be better achieved.
In other specific examples, as shown in figure 5, tank body 1 include cement bottom wall and be located on cement bottom wall and under
Hold open metal upper tank body.The outer peripheral edge of cement bottom wall extends outwardly beyond the outer peripheral edge of metal upper tank body.In cement bottom wall
Equipped with sludge out pipe 12, one end of sludge out pipe 12 is connected with the sludge outlet of mud-collecting slot 6 and the entrance phase of the other end and circulating pump 7
Even.
Preferably, the draw ratio of sludge out pipe 12 is less than 40：1.Inventor is had found by largely studying with engineering practice, dirty
Fiber etc. may be contained in mud, in the case where the caliber of sludge out pipe 12 is certain, when sludge out pipe is more than certain length, sludge out pipe
12 are particularly easy to block, and sludge out pipe 12 blocks and is very difficult to clear up later, not only influences wastewater treatment, and increase dimension
Protect cost.For this purpose, by the way that the draw ratio of sludge out pipe 12 is limited to less than predetermined value, blockage problem can be well solved.
As described above, distance of the lower edge of cleaning shoe 41 apart from the bottom surface of reative cell 11 is less than 100 millimeters.In order to preferably
Sludge on the bottom wall of reative cell 11 is scraped in mud-collecting slot 6, the lower edge of cleaning shoe 41 uses up the bottom wall away from reative cell 11 as far as possible
It is close, preferred distance is less than 100 millimeters.
As noted previously, as without making scraper plate without with substantial stirring action, the rotating speed of cleaning shoe 41 be less than 5 turns/
Hour.Hereby it is achieved that sludge scrapes, and energy consumption reduces.
In other optional examples, as shown in figure 5, mud scraper 4 further includes truss 42.Cleaning shoe 41 and 42 phase of truss
Even, it can be equipped on truss 42 for being rolled with the rolling of Auxiliary support truss 42 and cleaning shoe 41 on the bottom surface of reative cell 11
Wheel.
In order to which the service life and raising that increase cleaning shoe 41 scrape mud effect, the lower edge of cleaning shoe 41 can be equipped with and react
The elastic sheet rubber 411 of the bottom surface Elastic Contact of room 11.Cleaning shoe 41 carry out rotation scrape mud when, elastic sheet rubber 41 with react
The bottom wall of room 11 contacts, and improves and scrapes mud effect, and can play cushioning effect, prevent damage reative cell 11 bottom surface and
The damage of mud scraper.
In other optional examples, as shown in figure 5, can be as far as possible by the reaction of large area for the ease of cleaning shoe 41
Sludge scrapes in mud-collecting slot 6 on the sludge of 11 bottom wall of room, and the outer rim of cleaning shoe 41 extends outwardly beyond the outer rim of mud-collecting slot 6.
Preferably, the interior sidewall surface of mud-collecting slot 6 is the inclined-plane tilted down outward, as a result, on the bottom wall of reative cell 11
Sludge is easier to flow in mud-collecting slot 6.
In other optional examples, driving device 5 includes hydraulic motor, and mud scraper 4 further includes central axle sleeve 43.Scrape mud
Plate 41 is mounted on central axle sleeve 43, is rotated with the rotation of central axle sleeve 43.Hydraulic motor 5 is located in central axle sleeve 43 and liquid
The output shaft of pressure motor is connected with central axle sleeve 43 to drive central axle sleeve 43 to rotate.
In other optional examples, as shown in figure 3, anaerobic reactor further includes air supply pipe 8, air supply pipe 8 is used for institute
Conveying gas in central axle sleeve 43 is stated so as to scheduled pressure be kept in central axle sleeve 43, to avoid the waste water in reative cell 11
Into in central axle sleeve 43, the service life of driving device 5 is substantially increased, motor may be used in driving device 5 at this time.
In other optional examples, as shown in figure 5, driving device 5 includes hydraulic motor or motor, mud scraper 4 also wraps
Include central axle sleeve 43.Cleaning shoe 41 is mounted in central axle sleeve 43, and sealing shroud 44, and sealing shroud are additionally provided in central axle sleeve 43
44 top and periphery wall are spaced apart with central axle sleeve 43.For example, the lower end of sealing shroud 44 is located on the bottom wall of reative cell 11, liquid
Pressure motor or motor are located in sealing shroud 44.The output shaft of hydraulic motor or motor passes through upper end and the central axle sleeve of sealing shroud 44
43 are connected.
Preferably, sealing shroud 44 has air supply opening, for the supply gas into sealing shroud so as to be kept in sealing shroud 44 pre-
Fixed pressure is to avoid the waste water in reative cell 11 from entering in sealing shroud 44.
Preferably, the lower end of sealing shroud 44 is located in the bottom wall of reative cell 11, air supply opening and the bottom wall for being located at reative cell 11
The interior and air supply channel suitable for being connected with external air source or air supply pipe 8 are connected.
In other optional examples, mud-collecting slot 6 can be the single annular groove of the circumferentially extending along tank body 1, can also
For along multiple slots of the circumferentially-spaced distribution of tank body 1.Preferably, circulating pump 7 be with it is single or multiple.
In other optional examples, the bottom surface of reative cell 11 can be divided into multiple areas Gua Ni, correspondingly, mud scraper be with
Multiple areas Gua Ni are corresponding multiple, and at least provided with a mud-collecting slot 6 in each areas Gua Ni.
In other optional examples, the top of reative cell 11 is equipped with cycle nozzle 9, and outlet and the cycle of circulating pump 7 are sprayed
First 9 are connected.
Preferably, the waste water nozzle for being injected to waste water in reative cell 11 is additionally provided at waste water inlet 2.
Preferably, waste water is tangentially supplied to the indoor ullage of reaction by waste water nozzle.Waste water nozzle is by waste water edge
In the tangential penetrating reative cell 11 of reative cell 11, the waste water of penetrating causes the waste water in reative cell 11 to rotate in a circumferential direction movement,
The accumulation of Sludge Surface floating material is avoided, and waste water is uniformly mixed with sludge, water treatment effect is more preferable.
Waste-water anaerobic treatment process according to the ... of the embodiment of the present invention is briefly described below.
Waste-water anaerobic treatment process according to the ... of the embodiment of the present invention, waste water is supplied in the reative cell of anaerobic reactor,
To carry out Anaerobic Treatment to waste water using the indoor sludge of reaction.
Sludge on the bottom surface of reative cell is scraped in the mud-collecting slot being located on the bottom surface of reative cell using mud scraper, mud scraper
Including cleaning shoe and it is located at driving device of the anaerobic reactor bottom for driving cleaning shoe.
The reative cell is discharged in sludge in mud-collecting slot.
Preferably, at least part sludge being discharged out of described mud-collecting slot is pumped into institute along the tangential of the reative cell
State the top of reative cell.
Preferably, at least part sludge is pumped into above the indoor liquid level of reaction, and the waste water is by along described
Reative cell is tangentially supplied in the reative cell.
The sludge of reative cell bottom is scraped collection by waste-water anaerobic treatment process according to the ... of the embodiment of the present invention by mud scraper
In mud groove, a part of sludge may loop to reative cell top, improve sludge and waste water mixed effect, and it is not necessary that stirring is arranged
Device overcomes the problem of traditional agitating mode is brought.Since the driving device of driving mud scraper is located at tank base, without logical
Long transmission shaft is connected with mud scraper, and mud scraper operates steadily, and vibration and noise are small.
The waste-water anaerobic treatment process of the embodiments of the present invention, it is low without stirring, consuming energy, and sludge and waste water mixing
Effect is good, reduces anaerobic reactor bottom stirring dead zone (region that can not be stirred to), substantially increases wastewater treatment effect
Fruit.
In the description of the present invention, it is to be understood that, term "center", " longitudinal direction ", " transverse direction ", " length ", " width ",
" thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom" "inner", "outside", " up time
The orientation or positional relationship of the instructions such as needle ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " be orientation based on ... shown in the drawings or
Position relationship is merely for convenience of description of the present invention and simplification of the description, and does not indicate or imply the indicated device or element must
There must be specific orientation, with specific azimuth configuration and operation, therefore be not considered as limiting the invention.
In addition, term " first ", " second " are used for description purposes only, it is not understood to indicate or imply relative importance
Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include at least one this feature.In the description of the present invention, the meaning of " plurality " is at least two, such as two, three
It is a etc., unless otherwise specifically defined.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " fixation " etc.
Term shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral；Can be that machinery connects
It connects, can also be to be electrically connected or can communicate each other；It can be directly connected, can also indirectly connected through an intermediary, it can be with
It is the interaction relationship of the connection or two elements inside two elements, unless otherwise restricted clearly.For this field
For those of ordinary skill, the specific meanings of the above terms in the present invention can be understood according to specific conditions.
In the present invention unless specifically defined or limited otherwise, fisrt feature can be with "above" or "below" second feature
It is that the first and second features are in direct contact or the first and second features pass through intermediary mediate contact.Moreover, fisrt feature exists
Second feature " on ", " top " and " above " but fisrt feature be directly above or diagonally above the second feature, or be merely representative of
Fisrt feature level height is higher than second feature.Fisrt feature second feature " under ", " lower section " and " below " can be
One feature is directly under or diagonally below the second feature, or is merely representative of fisrt feature level height and is less than second feature.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show
The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example
Point is included at least one embodiment or example of the invention.In the present specification, schematic expression of the above terms are not
It must be directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be in office
It can be combined in any suitable manner in one or more embodiments or example.In addition, without conflicting with each other, the skill of this field
Art personnel can tie the feature of different embodiments or examples described in this specification and different embodiments or examples
It closes and combines.
Although the embodiments of the present invention has been shown and described above, it is to be understood that above-described embodiment is example
Property, it is not considered as limiting the invention, those skilled in the art within the scope of the invention can be to above-mentioned
Embodiment is changed, changes, replacing and modification.
Claims (20)
1. a kind of anaerobic reactor, which is characterized in that including：
Tank body, the tank body is interior, and there is reative cell, the reative cell to have waste water inlet and methane outlet, the bottom of the reative cell
Face is equipped with mud-collecting slot, and the sludge outlet being connected to the mud-collecting slot is equipped in the wall of the tank body；
Mud scraper, the mud scraper include cleaning shoe and driving device, and the cleaning shoe is located at the bottom of the reative cell, is used for
Sludge on the bottom surface of the reative cell is scraped in the mud-collecting slot, the driving device be located at the bottom of the tank body and with
The cleaning shoe is connected, for driving the cleaning shoe to rotate.
2. anaerobic reactor according to claim 1, which is characterized in that further include circulating pump, the entrance of the circulating pump
It is connected to the sludge outlet, the outlet of the circulating pump is connected to the top of the reative cell, will be in the mud-collecting slot
At least part sludge pumping is to the top of the reative cell.
3. anaerobic reactor according to claim 2, which is characterized in that the circulating pump will along the tangential of the reative cell
The sludge pumping is to the reative cell top.
4. anaerobic reactor according to claim 2, which is characterized in that the tank body includes cement bottom wall and is located at described
On the cement bottom wall and metal upper tank body of open at its lower end, the outer peripheral edge of the cement bottom wall extends outwardly beyond tank on the metal
The outer peripheral edge of body, is equipped with sludge out pipe in the cement bottom wall, and one end of the sludge out pipe is connected and another with the sludge outlet
End is connected with the entrance of the circulating pump.
5. anaerobic reactor according to claim 4, which is characterized in that the draw ratio of the sludge out pipe is less than 40：1.
6. anaerobic reactor according to any one of claims 1-5, which is characterized in that the lower edge distance of the cleaning shoe
The distance of the bottom surface of the reative cell is less than 100 millimeters.
7. according to the anaerobic reactor described in any one of claim 1-6, which is characterized in that the rotating speed of the cleaning shoe is less than
5 turns/hour.
8. according to the anaerobic reactor described in any one of claim 1-7, which is characterized in that the mud scraper further includes purlin
Frame, the cleaning shoe are connected with the truss, and the truss is equipped with for being rolled on the bottom surface of the reative cell to assist
The idler wheel of the truss and the cleaning shoe, the lower edge of the cleaning shoe is supported to be equipped with the bottom surface Elastic Contact with the reative cell
Elastic sheet rubber.
9. according to the anaerobic reactor described in any one of claim 1-8, which is characterized in that the outer rim of the cleaning shoe is outside
The outer rim of the mud-collecting slot is extended beyond, the interior sidewall surface of the mud-collecting slot is the inclined-plane tilted down outward.
10. according to the anaerobic reactor described in any one of claim 1-9, which is characterized in that the driving device includes liquid
Pressure motor, the mud scraper further include central axle sleeve, and the cleaning shoe is mounted on the central axle sleeve, and the hydraulic motor is set
In the central axle sleeve and the output shaft of the hydraulic motor is connected with the central axle sleeve to drive the central axle sleeve to turn
It is dynamic.
11. anaerobic reactor according to claim 10, which is characterized in that further include air supply pipe, the air supply pipe is used for
Gas is conveyed into the central axle sleeve so as to keep scheduled pressure in the central axle sleeve to avoid in the reative cell
Waste water enter the central axle sleeve in.
12. according to the anaerobic reactor described in any one of claim 1-11, which is characterized in that the driving device includes liquid
Pressure motor or motor, the mud scraper further include central axle sleeve, and the cleaning shoe is mounted in the central axle sleeve, the center
Sealing shroud is equipped in axle sleeve, the top of the sealing shroud and periphery wall are spaced apart with the central axle sleeve, under the sealing shroud
End is located on the bottom wall of the reative cell, and the hydraulic motor or motor are located in the sealing shroud, the hydraulic motor or electricity
The output shaft of machine passes through the upper end of the sealing shroud to be connected with the central axle sleeve, and the sealing shroud is with for the sealing
Supply gas in set is so as to keep scheduled pressure to avoid the indoor waste water of reaction from entering sealing in the sealing shroud
Air supply opening in set.
13. anaerobic reactor according to claim 12, which is characterized in that the lower end of the sealing shroud is located at the reaction
In the bottom wall of room, the air supply opening and be located in the bottom wall of the reative cell and the air supply channel suitable for being connected with external air source or
Air supply pipe is connected.
14. according to the anaerobic reactor described in any one of claim 1-13, which is characterized in that the mud-collecting slot is along described
The single annular groove of the circumferentially extending of tank body or for along multiple slots of the circumferentially-spaced distribution of the tank body, the circulating pump be with
It is single or multiple.
15. according to the anaerobic reactor described in any one of claim 1-14, which is characterized in that the bottom surface of the reative cell point
For multiple areas Gua Ni, the mud scraper is corresponding multiple with multiple areas Gua Ni, in each areas Gua Ni at least provided with
One mud-collecting slot.
16. anaerobic reactor according to claim 2, which is characterized in that the top of the reative cell is equipped with cycle nozzle,
The outlet of the circulating pump is connected with the cycle nozzle, is equipped at the waste water inlet for waste water to be injected to the reaction
Indoor waste water nozzle.
17. anaerobic reactor according to claim 16, which is characterized in that the waste water nozzle tangentially supplies waste water
To the indoor ullage of reaction.
18. a kind of waste-water anaerobic treatment process, which is characterized in that including：
Waste water is supplied in the reative cell of anaerobic reactor to be carried out at anaerobism to waste water using the indoor sludge of reaction
Reason；
Sludge on the bottom surface of the reative cell is scraped in the mud-collecting slot being located on the bottom surface using mud scraper, the mud scraper
Including cleaning shoe and it is located at driving device of the anaerobic reactor bottom for driving the cleaning shoe；
The reative cell is discharged in sludge in the mud-collecting slot.
19. waste-water anaerobic treatment process according to claim 18, which is characterized in that further including will be out of described mud-collecting slot
At least part sludge of discharge is along the top for being tangentially pumped into the reative cell of the reative cell.
20. waste-water anaerobic treatment process according to claim 19, which is characterized in that at least part sludge is pumped
It is sent to above the indoor liquid level of reaction, the waste water is by being tangentially supplied in the reative cell along the reative cell.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710241490.8A CN108726674A (en) | 2017-04-13 | 2017-04-13 | Anaerobic reactor and waste-water anaerobic treatment process |
| PCT/CN2017/107904 WO2018188317A1 (en) | 2017-04-13 | 2017-10-26 | Anaerobic reactor and anaerobic wastewater treatment process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710241490.8A CN108726674A (en) | 2017-04-13 | 2017-04-13 | Anaerobic reactor and waste-water anaerobic treatment process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108726674A true CN108726674A (en) | 2018-11-02 |
Family
ID=63923721
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710241490.8A Withdrawn CN108726674A (en) | 2017-04-13 | 2017-04-13 | Anaerobic reactor and waste-water anaerobic treatment process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108726674A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101475297A (en) * | 2008-01-01 | 2009-07-08 | 庄维健 | Anaerobic fermentation method for treating garbage by using wastewater |
| CN102616930A (en) * | 2012-04-19 | 2012-08-01 | 徐富 | Methane air floating anaerobic reactor |
| CN202671366U (en) * | 2012-05-24 | 2013-01-16 | 深圳市启明环境技术有限公司 | Cross-flow anaerobic sludge bed reactor |
| CN103752051A (en) * | 2014-01-20 | 2014-04-30 | 扬州澄露环境工程有限公司 | Hydraulic driving type tank-bottom mud scraper |
| CN103803705A (en) * | 2014-01-26 | 2014-05-21 | 浙江德安科技股份有限公司 | Novel sewage treatment device |
| CN205472934U (en) * | 2016-03-24 | 2016-08-17 | 湖北美源环保科技有限公司 | Biochemical sewage treatment plant of anaerobism |
| CN206843182U (en) * | 2017-04-13 | 2018-01-05 | 帕克环保技术(上海)有限公司 | Anaerobic reactor |
-
2017
- 2017-04-13 CN CN201710241490.8A patent/CN108726674A/en not_active Withdrawn
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101475297A (en) * | 2008-01-01 | 2009-07-08 | 庄维健 | Anaerobic fermentation method for treating garbage by using wastewater |
| CN102616930A (en) * | 2012-04-19 | 2012-08-01 | 徐富 | Methane air floating anaerobic reactor |
| CN202671366U (en) * | 2012-05-24 | 2013-01-16 | 深圳市启明环境技术有限公司 | Cross-flow anaerobic sludge bed reactor |
| CN103752051A (en) * | 2014-01-20 | 2014-04-30 | 扬州澄露环境工程有限公司 | Hydraulic driving type tank-bottom mud scraper |
| CN103803705A (en) * | 2014-01-26 | 2014-05-21 | 浙江德安科技股份有限公司 | Novel sewage treatment device |
| CN205472934U (en) * | 2016-03-24 | 2016-08-17 | 湖北美源环保科技有限公司 | Biochemical sewage treatment plant of anaerobism |
| CN206843182U (en) * | 2017-04-13 | 2018-01-05 | 帕克环保技术(上海)有限公司 | Anaerobic reactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101452392B1 (en) | Anaerobic digestion tank | |
| WO2018188317A1 (en) | Anaerobic reactor and anaerobic wastewater treatment process | |
| CN206843182U (en) | Anaerobic reactor | |
| KR101276405B1 (en) | Vacuum drum type sludge concentration apparatus with enhanced dehydration function | |
| CN110282837B (en) | Pump station forebay quality of water emergency treatment system | |
| CN103657168A (en) | Peripheral transmission sludge suction method and suction dredge adopting gas stripping device | |
| CN104707371A (en) | Novel mechanical stirring clarification tank | |
| CN108726674A (en) | Anaerobic reactor and waste-water anaerobic treatment process | |
| CN100343181C (en) | Middle arranged sedimentation tank | |
| CN105836850A (en) | High efficiency autocontrol electro-fenton decontamination equipment | |
| CN212740865U (en) | Sewage treatment plant carbon source supplementing device | |
| CN208898575U (en) | A kind of magnetic-coagulation efficient sedimentation tank sewage disposal system | |
| CN106145447A (en) | A kind of sewage-treatment plant and the method processing sewage thereof | |
| KR101155615B1 (en) | Rabbit hole prevention and sludge discharge device of circular sedimentation basin | |
| CN202508960U (en) | Sludge treatment device combining ultrasonic and anoxic/oxic digestion | |
| CN204582626U (en) | A kind of novel accelerator | |
| CN205495411U (en) | Wear -resisting churn of high strength for building engineering | |
| CN208104155U (en) | A kind of system handling synthetic leather wastewater | |
| CN215667291U (en) | Water treatment adds medicine and mixes equalizing basin | |
| CN220976630U (en) | Intelligent high-efficient dephosphorization equipment | |
| CN220745470U (en) | Paint removal wastewater treatment device | |
| CN214916079U (en) | Intelligent control lime feeding device | |
| CN209652100U (en) | A kind of system using Lime And Sewage Sludge production wet desulphurization agent | |
| KR102298527B1 (en) | Anaerobic digestion system equipped with an integrated circulation system combined with gas mixer and grinding pump, and control method of the same | |
| US10988396B2 (en) | Method and apparatus for anaerobic sludge digestion mixing and heat exchange |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20181102 |
|
| WW01 | Invention patent application withdrawn after publication |