CN206814539U - A kind of organic waste-water treating apparatus - Google Patents
A kind of organic waste-water treating apparatus Download PDFInfo
- Publication number
- CN206814539U CN206814539U CN201720555315.1U CN201720555315U CN206814539U CN 206814539 U CN206814539 U CN 206814539U CN 201720555315 U CN201720555315 U CN 201720555315U CN 206814539 U CN206814539 U CN 206814539U
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- water
- pipeline
- branch pipe
- production
- concentrated
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Abstract
A kind of organic waste-water treating apparatus, including raw water tank, inlet channel, dehvery pump；Also include ceramic film component, concentrated water pipeline and water production pipeline；Described ceramic film component is at least three groups, and described ceramic film component includes a putamina, and ceramic membrane element is provided with described putamina；Described putamina is provided with water inlet and delivery port；Described water inlet connects inlet channel by water inlet pipe, and delivery port connects water production pipeline by producing water branch pipe, and a concentrated water branch pipe, described concentrated water branch pipe connection concentrated water pipeline are also associated with described water inlet pipe；Described water inlet pipe, concentrated water branch pipe, valve is designed with production water branch pipe；The pore size filter of described ceramic membrane element is 2 50nm；The water inlet of described concentration pipeline connection Fenton oxidation device, the production mouth of a river of described Fenton oxidation device connects raw water tank by reflux line.Organic waste-water treating apparatus described in the utility model, have the advantages that treatment effeciency height, waste water can be with reuses.
Description
Technical field
Sewage-treatment plant is the utility model is related to, more particularly to a kind of organic waste-water treating apparatus.
Background technology
Organic wastewater is exactly the waste water based on organic pollution, and organic wastewater easily causes Water Eutrophication, hazard ratio
It is larger.Containing organic matters such as substantial amounts of carbohydrate, fat, albumen, celluloses in these waste water, if directly discharged, meeting
Cause seriously to pollute.The membrane separation device of sewage disposal is currently used for, in use, is carried out clearly after being typically necessary shutdown
Wash, this virtually adds the cost and treatment effeciency of sewage disposal.
The content of the invention
In view of the above-mentioned problems, the purpose of this utility model is that providing one kind reaches efficient process organic wastewater, realizes useless
The organic waste-water treating apparatus of Water circulation.
To reach above-mentioned purpose, the technical scheme that the utility model is proposed is：A kind of organic waste-water treating apparatus, including
Raw water tank, inlet channel, the dehvery pump on inlet channel；Also include ceramic film component, concentrated water pipeline and water production pipeline；Its
It is characterised by：Described ceramic film component is at least three groups, and is dead-end filtration ceramic film component, described ceramic film component bag
A putamina is included, ceramic membrane element is provided with described putamina；Described putamina is provided with water inlet and delivery port；Described water inlet
Mouthful inlet channel is connected by water inlet pipe, delivery port by produce water branch pipe connect water production pipeline, on described water inlet pipe also
It is connected with a concentrated water branch pipe, described concentrated water branch pipe connection concentrated water pipeline；Described water inlet pipe, concentrated water branch pipe, production water branch pipe
On be designed with valve；The pore size filter of described ceramic membrane element is 2-50nm；Described concentration pipeline connection Fenton oxidation device
Water inlet, the production mouth of a river of described Fenton oxidation device passes through reflux line and connects raw water tank.
Preferably, described water production pipeline is provided with the pipeline reducing diameter for making the pipe diameter of water production pipeline rear end diminish and connect
Head.
Using above-mentioned technical proposal, organic waste-water treating apparatus described in the utility model, tool has the advantage that：
1) organic wastewater is filtered by separating the ceramic film component that aperture is 2-50nm, and production water meets Treated sewage reusing requirement,
Concentrated water can remove most of organic matter by Fenton advanced oxidation, and concentrated rear oxidation efficiency improves；
2) ceramic film component automatic backwash, without increasing backwashing pump or providing other water sources, ceramic membrane element uses the longevity
Order longer.
Brief description of the drawings
Fig. 1 is organic waste-water treating apparatus schematic diagram described in the utility model.
Embodiment
With reference to the accompanying drawings and detailed description, the utility model is described further.
As shown in figure 1, organic waste-water treating apparatus described in the utility model, including raw water tank 11, inlet channel 13, set
In the dehvery pump 12 on inlet channel, in addition to ceramic film component 15, concentrated water pipeline 14 and water production pipeline 16；Wherein, ceramic membrane
Component 15 is three groups（As needed, can also set more multigroup）, and be dead-end filtration ceramic film component, ceramic film component 15 wraps
A putamina 151 is included, ceramic membrane element 152 is provided with putamina 151；Putamina 15 is provided with water inlet and delivery port；Water inlet passes through
Water inlet pipe 155 connects inlet channel 13, and delivery port connects water production pipeline 16, described water inlet pipe by producing water branch pipe 154
A concentrated water branch pipe 153, described concentrated water branch pipe 153 connection concentrated water pipeline 14 are also associated with 155；Described water inlet pipe 155,
Valve 156 is designed with concentrated water branch pipe 153, production water branch pipe 154；Water production pipeline 16 is provided with the pipeline for making the rear end of water production pipeline 16
The pipeline reducing diameter joint 17 that diameter diminishes, production water branch pipe 16 connect production water pot 18, and concentrated water pipeline 14 connects Fenton oxidation device 19
Water inlet, the production mouth of a river of Fenton oxidation device 19 connect raw water tank 1 by reflux line 20；Further, ceramic membrane element 152
Pore size filter is 2-50nm.
When specifically used, the pending organic wastewater in raw water tank, it is pumped into by dehvery pump through inlet channel, water inlet pipe
In ceramic film component, the pore size filter of the ceramic membrane element in ceramic film component is 2-50nm, can retain most of organic dirt
Thing is contaminated, production water enters in production water pot through water production pipeline, can meet Treated sewage reusing requirement；Due to using dead-end filtration ceramic membrane group
Part, waste water can be made to reach higher concentration；When one of which ceramic film component needs cleaning, close on its water inlet pipe
Valve, the valve on backflow branch pipe is opened, after being especially in the presence of reducer union, the feed velocity of rear end is slack-off；So other two
Group treats that the production water that the ceramic film component of normal filtration passes through flow to ceramic membrane by the production water branch pipe for the ceramic film component for needing to clean
In component, the backwash of ceramic membrane element is realized, then concentrated water pipeline is back to through concentrated water branch pipe, Fenton oxidation device of then intaking again
Middle carry out advanced oxidation, the organic matter in degrading waste water；Waste water after Fenton oxidation is back in raw water tank through reflux line again,
Circulating filtration and oxidation can be achieved, as needed, we can also realize the alternating of automatic backwash by Automated condtrol
The purpose of replacing.
Although specifically showing and describing the utility model with reference to preferred embodiment, those skilled in the art should
This is understood, is not departing from the spirit and scope of the present utility model that appended claims are limited, in form and details
On the utility model is made a variety of changes, be the scope of protection of the utility model.
Claims (2)
1. a kind of organic waste-water treating apparatus, including raw water tank, inlet channel, the dehvery pump on inlet channel；Also include
Ceramic film component, concentrated water pipeline and water production pipeline；It is characterized in that：Described ceramic film component is at least three groups, and is dead end
Ceramic for filtration membrane module, described ceramic film component include a putamina, ceramic membrane element are provided with described putamina；Described film
Shell is provided with water inlet and delivery port；Described water inlet connects inlet channel by water inlet pipe, and delivery port is by producing water branch
A concentrated water branch pipe, described concentrated water branch pipe connection concentrated water pipeline are also associated with pipe connection water production pipeline, described water inlet pipe；
Described water inlet pipe, concentrated water branch pipe, valve is designed with production water branch pipe；The pore size filter of described ceramic membrane element is 2-
50nm；The water inlet of described concentrated water pipeline connection Fenton oxidation device, the production mouth of a river of described Fenton oxidation device passes through return duct
Road connects raw water tank.
A kind of 2. organic waste-water treating apparatus according to claim 1, it is characterised in that：Described water production pipeline is provided with
Make the pipeline reducing diameter joint that the pipe diameter of water production pipeline rear end diminishes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720555315.1U CN206814539U (en) | 2017-05-18 | 2017-05-18 | A kind of organic waste-water treating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720555315.1U CN206814539U (en) | 2017-05-18 | 2017-05-18 | A kind of organic waste-water treating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206814539U true CN206814539U (en) | 2017-12-29 |
Family
ID=60756360
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720555315.1U Expired - Fee Related CN206814539U (en) | 2017-05-18 | 2017-05-18 | A kind of organic waste-water treating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206814539U (en) |
-
2017
- 2017-05-18 CN CN201720555315.1U patent/CN206814539U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171229 Termination date: 20190518 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |