CN207012618U - First heavy processing system for sewage - Google Patents
First heavy processing system for sewage Download PDFInfo
- Publication number
- CN207012618U CN207012618U CN201720349634.7U CN201720349634U CN207012618U CN 207012618 U CN207012618 U CN 207012618U CN 201720349634 U CN201720349634 U CN 201720349634U CN 207012618 U CN207012618 U CN 207012618U
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- CN
- China
- Prior art keywords
- sedimentation basin
- pipe
- sludge
- sewage
- processing system
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- 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.)
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Abstract
The utility model discloses a kind of first heavy processing system for sewage, including sedimentation basin, the cloth hydroecium in the middle part of sedimentation basin, the water inlet pipe for being communicated in the cloth hydroecium, radome fairing, the delivery port on cloth hydroecium, scrape mud part, the storage mud chamber positioned at sedimentation basin bottom, be communicated in the discharge pipeline of the storage mud chamber, water leg and the outlet pipe being connected with the water leg above sedimentation basin;The radome fairing bottom is set for opening, and the distance h1 of the radome fairing lower openings and sedimentation basin bottom surface is less than the height h2 of sludge in sedimentation basin;The delivery port and the distance h3 of sedimentation basin bottom surface are more than the height h2 of sludge in sedimentation basin.The height h2 of sludge is controlled in the utility model higher than radome fairing lower openings and the distance h1 of sedimentation basin bottom surface so that enter sludge blanket after wastewater influent, double action is caught by the filtering and net of sludge blanket, improve sludgd deposition rate, water outlet band mud rate is reduced, reduces the use of coagulant, reduces cost.
Description
Technical field
The utility model belongs to technical field, more particularly, to a kind of first heavy processing system for sewage.
Background technology
The first heavy processing system of sewage is currently used for, in the running of reality, following weak point be present:Sewage with
Coagulated agent mixing, which need to be set, mixes pond, space-consuming;Sludge interface in pond is not required so that precipitating sludge is formed
Embryonic particle is smaller, easy water outlet band mud, to reduce water outlet band mud phenomenon, certainly will increase coagulated agent dosage, cause to handle
Cost increase.
Utility model content
The utility model is for overcome the deficiencies in the prior art, there is provided a kind of processing cost is low, and sedimentation effect is good to be used for
The first heavy processing system of sewage.
To achieve these goals, the utility model uses following technical scheme:A kind of first heavy processing system for sewage
System, including sedimentation basin, the cloth hydroecium in the middle part of sedimentation basin, the water inlet pipe for being communicated in the cloth hydroecium, radome fairing, located at cloth hydroecium
On delivery port, scrape mud part, the storage mud chamber positioned at sedimentation basin bottom, be communicated in the discharge pipeline of the storage mud chamber, positioned at sedimentation basin
Top water leg and the outlet pipe being connected with the water leg;The radome fairing bottom is set for opening, the radome fairing lower openings
It is less than the height h2 of sludge in sedimentation basin with the distance h1 of sedimentation basin bottom surface;The delivery port and the distance h3 of sedimentation basin bottom surface are big
In the height h2 of sludge in sedimentation basin.The height h2 of sludge is controlled to be higher than radome fairing lower openings and sedimentation basin in the utility model
The distance h1 of bottom surface, the circulation upwards again after sludge blanket in advance after sewage is flowed out by the opening of radome fairing bottom so that warp
The little particle sludge or impurity crossed after flocculation are deposited in sludge blanket in the case where the filtering of sludge blanket catches double action with net, will not
As sewage discharges, sludgd deposition rate is improved, water outlet band mud rate is reduced, reduces the use of coagulant, reduce cost.
Further, the sedimentation basin connection one is used for the sludge interface instrument for detecting the height h2 of sludge in sedimentation basin;Can
Mud height in detection sedimentation basin in real time, when sludge is too high, worker can carry out appropriate spoil disposal operation to sedimentation basin, prevent
Mud height is too high, while sludge is maintained in h2 height;Preferably, h2 for 3/4 of the depth of water in sedimentation basin.
Further, a pipe-line mixer is connected on the water inlet pipe, a chemical feed pipe is connected on the pipe-line mixer;It is logical
Cross chemical feed pipe to add flocculant in pipe-line mixer, flocculated to entering the sewage in pipe-line mixer.
Preferably, the chemical feed pipe encloses outside the pipe-line mixer in the shape of a spiral, pipe-line mixer side wall be provided with
The dosing mouth that the chemical feed pipe is connected;So that flocculant can be sprayed into pipe-line mixer by the different angle of pipe-line mixer
Interior, the mixing with sewage is more abundant, and flocculating effect is more preferable.
Further, the sedimentation basin bottom surface is pyramidal structure, and the mud part of scraping is included on sedimentation basin bottom surface
Cleaning shoe, the drive link being connected with the cleaning shoe, the drive shaft that is connected with the drive link and for driving the drive shaft turns
Actuator;Drive shaft rotates under the drive of actuator, by drive link drive to cleaning shoe drive cleaning shoe using drive shaft as
Center is rotated, and cleaning shoe loosens the sludge scraping on sedimentation basin bottom surface during rotating;Because sedimentation basin bottom surface is cone
Shape structure so that the face contacted with cleaning shoe is inclined-plane, is easy to sludge to be slipped into automatically and stores mud intracavitary.
Or it is further, the drive link is L-shaped structure;Drive shaft is allowd to be arranged on the position of sedimentation basin central part
Put, ensure that cleaning shoe is rotated around sedimentation basin center, it is good to scrape mud effect.
In summary, the utility model is by controlling the height h2 of sludge higher than radome fairing lower openings and sedimentation basin bottom surface
Distance h1 so that enter sludge blanket after wastewater influent, double action caught by the filtering of sludge blanket and net, improves sludgd deposition
Rate, water outlet band mud rate is reduced, reduces the use of coagulant, reduces cost.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of pipe-line mixer of the present utility model.
Embodiment
In order that those skilled in the art are better understood from the utility model, it is real below in conjunction with the utility model
The accompanying drawing in example is applied, clear, complete description is carried out to the technical scheme in the embodiment of the utility model.
As shown in Figure 1-2, a kind of first heavy processing system for sewage, including sedimentation basin 1, the cloth in the middle part of sedimentation basin
Hydroecium 2, the water inlet pipe 3 for being communicated in the cloth hydroecium, radome fairing 4, the delivery port 5 on cloth hydroecium, scrape mud part, positioned at precipitation
The storage mud chamber 7 of pond bottom, it is communicated in the discharge pipeline 8 of the storage mud chamber, water leg 9 and is connected above sedimentation basin with the water leg
Outlet pipe 10;A pipe-line mixer 31 is connected on the water inlet pipe 3, connecting a stainless steel on the pipe-line mixer 31 is made
Chemical feed pipe 32, flocculant put into pipe-line mixer 31 by the chemical feed pipe, after sewage inlet pipe road blender 31 with wadding
Solidifying agent reacts to form short grained flocculate;The flocculant is bodied ferric sulfate;Preferably, the chemical feed pipe 32 is in spiral shell
Rotation shape is enclosed outside the pipe-line mixer 31, and the section of chemical feed pipe 32 can be that semicircular structure is set, directly solid by welding
Surely it is connected to outside pipe-line mixer 31;The side wall of pipe-line mixer 31 is provided with multiple dosing mouths 33, the helically formula of dosing mouth 33
Respectively on the outer surface of pipe-line mixer 31, dosing mouth 33 spaces between uniformly, and chemical feed pipe 3 passes through dosing mouth 33
It is connected with pipe-line mixer 31.
The radome fairing 4 is located on the cloth hydroecium upper position, and the bottom of radome fairing 4 is that opening is set, it is described go out
The mouth of a river 5 is arranged in the sidewall locations of cloth hydroecium, the lower position for extending to delivery port 5 of radome fairing 4, and delivery port 5 is by water distribution
Enter in radome fairing 4 after indoor water output, then flowed out by the opening of the bottom of radome fairing 4;Specifically, the radome fairing 4
Lower openings to the distance of the bottom surface of sedimentation basin 1 is h1, and the height of sludge is h2, the delivery port 5 and sedimentation basin 1 in sedimentation basin 1
The distance of bottom surface is h3, and the depth of water in sedimentation basin is h4;Preferably, described h2 is the 3/4 of h4, described h1<H2, it is described
H3>H2, so as to sewage via 5 water outlet of delivery port when will not be in contact with sludge, but by after the rectification of radome fairing 4 by whole
The opening outflow of 4 bottoms of stream cover, due to h1<H2, then the opening of the bottom of radome fairing 4 be located in sludge blanket, sewage is by radome fairing 4
Sludge blanket is entered to after the opening outflow of bottom, and the little particle flocculate in sewage has been deposited in sludge blanket, is effectively reduced
The water outlet band mud rate of sewage;In order to facilitate the mud height in control sedimentation basin, it is dirty that we are provided with one on the sedimentation basin 1
Mud interface instrument 11, the sludge interface instrument 11 can be detected in real time to the height h2 of sludge in sedimentation basin, when the sludge of display is high
When spending high, worker can keep mud height to maintain water by scraping mud part by the sludge scraping in sedimentation basin except a part
On deep 3/4.
Further, the bottom surface of sedimentation basin 1 is pyramidal structure, and the storage mud chamber is connected with the bottom surface of sedimentation basin 1, described
Discharge pipeline connection is in the side wall for storing mud chamber;The mud part of scraping includes cleaning shoe 61, drive link 62, drive shaft 63 and actuator
64;The cleaning shoe 61 is on sedimentation basin bottom surface, and the drive link 62 is inverted L-shaped, and its one end is connected with cleaning shoe 61,
The other end is connected after extending out to sedimentation basin top with drive shaft;The actuator 64 is motor, drive of the drive shaft in motor
Rotated under dynamic, and then drive the cleaning shoe at sedimentation basin bottom to be moved on the bottom surface of sedimentation basin, scrape sludge so that sludge falls
Enter to mud intracavitary is stored, discharged finally by discharge pipeline.
The upper strata of sedimentation basin is clear liquid, and clear liquid flows into follow-up processing equipment by outlet pipe after being collected by water leg
In.
Obviously, described embodiment is only part of the embodiment of the present utility model, rather than whole embodiments.
Based on the embodiment in the utility model, what those of ordinary skill in the art were obtained under the premise of creative work is not made
Every other embodiment, it should all belong to the scope of the utility model protection.
Claims (6)
1. a kind of first heavy processing system for sewage, including sedimentation basin (1), the cloth hydroecium (2) in the middle part of sedimentation basin, connection
In the water inlet pipe (3) of the cloth hydroecium, radome fairing (4), the delivery port (5) on cloth hydroecium, scrape mud part, under sedimentation basin
The storage mud chamber (7) in portion, the discharge pipeline (8) for being communicated in the storage mud chamber, above sedimentation basin water leg (9) and with the water leg phase
Outlet pipe (10) even;It is characterized in that:Radome fairing (4) bottom is set for opening, and radome fairing (4) lower openings are with sinking
The distance h1 of shallow lake pond (1) bottom surface is less than the height h2 of sedimentation basin (1) interior sludge;The delivery port (5) and sedimentation basin (1) bottom surface
Distance h3 is more than the height h2 of sedimentation basin (1) interior sludge.
2. the first heavy processing system according to claim 1 for sewage, it is characterised in that:Sedimentation basin (1) connection
The one height h2 for detecting sludge in sedimentation basin sludge interface instrument (11).
3. the first heavy processing system according to claim 1 for sewage, it is characterised in that:Connect on the water inlet pipe (3)
A pipe-line mixer (31) is connect, a chemical feed pipe (32) is connected on the pipe-line mixer (31).
4. the first heavy processing system according to claim 3 for sewage, it is characterised in that:The chemical feed pipe (32) is in spiral shell
Rotation shape is enclosed located at the pipe-line mixer (31) outside, and pipe-line mixer (31) side wall is provided with what is be connected with the chemical feed pipe (32)
Dosing mouth (33).
5. the first heavy processing system according to claim 1 for sewage, it is characterised in that:Sedimentation basin (1) bottom surface
For pyramidal structure, the mud part of scraping includes the cleaning shoe (61) on sedimentation basin bottom surface, the transmission connected with the cleaning shoe
Bar (62), the drive shaft (63) being connected with the drive link and the actuator (64) for driving the drive shaft turns.
6. the first heavy processing system according to claim 5 for sewage, it is characterised in that:The drive link (62) is L
Shape structure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720349634.7U CN207012618U (en) | 2017-04-05 | 2017-04-05 | First heavy processing system for sewage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720349634.7U CN207012618U (en) | 2017-04-05 | 2017-04-05 | First heavy processing system for sewage |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207012618U true CN207012618U (en) | 2018-02-16 |
Family
ID=61460315
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720349634.7U Expired - Fee Related CN207012618U (en) | 2017-04-05 | 2017-04-05 | First heavy processing system for sewage |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207012618U (en) |
-
2017
- 2017-04-05 CN CN201720349634.7U patent/CN207012618U/en not_active Expired - Fee Related
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180216 |
|
CF01 | Termination of patent right due to non-payment of annual fee |