CN206778193U - A kind of automatic backwash formula ceramic membrane filter device - Google Patents
A kind of automatic backwash formula ceramic membrane filter device Download PDFInfo
- Publication number
- CN206778193U CN206778193U CN201720554357.3U CN201720554357U CN206778193U CN 206778193 U CN206778193 U CN 206778193U CN 201720554357 U CN201720554357 U CN 201720554357U CN 206778193 U CN206778193 U CN 206778193U
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- China
- Prior art keywords
- water
- branch pipe
- ceramic membrane
- film component
- water inlet
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
A kind of automatic backwash formula ceramic membrane filter device, including head tank, inlet channel, the dehvery pump on inlet channel, ceramic film component, reflux line and water production pipeline；It is characterized in that：Described ceramic film component is at least three groups, and is dead-end filtration ceramic film component, and described ceramic film component includes a putamina, 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, a backflow branch pipe is also associated with described water inlet pipe, described backflow branch pipe connection reflux line；Described water inlet pipe, backflow branch pipe, valve is designed with production water branch pipe.Automatic backwash formula ceramic membrane filter device described in the utility model, ceramic film component automatic backwash can be realized by valve conversion, without increasing backwashing pump or providing other water sources, effluent quality is more preferable, and ceramic membrane element service life is longer.
Description
Technical field
Ceramic membrane separation field is the utility model is related to, more particularly to a kind of automatic backwash formula ceramic membrane filter device.
Background technology
Ceramic Membranes Separating Technique have good separative efficiency height, effect stability, chemical stability, acid and alkali-resistance, organic solvent-resistant,
Resistance to bacterium, high temperature resistant, antipollution, high mechanical strength, film regenerability is good, separation process is simple, energy consumption is low, simple and convenient operation and maintenance,
Numerous advantages such as film service life length.Ceramic membrane equipment has been successfully applied to food, beverage, plant（Medicine）Object depth processing, biology
The various fields such as medicine, fermentation, fine chemistry industry, available for the separation in technical process, clarification, purifying, concentration, degerming, desalination
Deng.Existing ceramic membrane filter device virtually adds cleaning cost using stop cleaning is needed after a period of time.
The content of the invention
In view of the above-mentioned problems, the purpose of this utility model is that providing one kind can be filled with automatic backwash, increase ceramic membrane
Put the automatic backwash formula ceramic membrane filter device of antifouling property.
To reach above-mentioned purpose, the technical scheme that the utility model is proposed is：A kind of automatic backwash formula ceramic membrane filter dress
Put, including head tank, inlet channel, the dehvery pump on inlet channel, in addition to ceramic film component, reflux line and production water
Pipeline；It is characterized in that：Described ceramic film component is at least three groups, and is dead-end filtration ceramic film component, described ceramics
Membrane module includes a putamina, and ceramic membrane element is provided with described putamina；Described putamina is provided with water inlet and delivery port；Institute
The water inlet stated connects inlet channel by water inlet pipe, and delivery port connects water production pipeline, described water inlet by producing water branch pipe
A backflow branch pipe, described backflow branch pipe connection reflux line are also associated with branch pipe；Described water inlet pipe, backflow branch pipe,
Valve is designed with production water branch pipe.
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.
Preferably, the pore size filter of described ceramic membrane element is 50-800nm.
Using above-mentioned technical proposal, automatic backwash formula ceramic membrane filter device described in the utility model, tool has the advantage that：
Ceramic film component automatic backwash can be realized by valve conversion, without increasing backwashing pump or providing other water sources, water outlet
Water quality is more preferable, and ceramic membrane element service life is longer.
Brief description of the drawings
Fig. 1 is automatic backwash formula ceramic membrane filter device 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, automatic backwash formula ceramic membrane filter device described in the utility model, including head tank 11, water inlet pipe
Road 13, the dehvery pump 12 on inlet channel, ceramic film component 15, reflux line 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 backflow branch pipe 153, described backflow branch pipe 153 connection reflux line 14 are also associated with 155；Described water inlet pipe 155,
Valve 156 is designed with backflow 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.
Preferably, the pore size filter of described ceramic membrane element 152 is 50-800nm.
When specifically used, by taking the device of three groups of ceramic film components in Fig. 1 as an example, when three groups of ceramic film components are all filtering
When, the valve on water inlet pipe and production water branch pipe is opened, and the valve to flow back on branch pipe is closed, and feed liquid so to be filtered is from water inlet
Pipeline enters water inlet pipe, and the feed liquid of permeation ceramic membrane is then by producing in the collection of water branch pipe and water production pipeline；
Self counter flushing of the present utility model is accomplished in the following manner, when one of which ceramic film component needs to clean
When, the valve closed on its water inlet pipe, open the valve on backflow branch pipe, after being especially in the presence of reducer union, the material of rear end
Flow velocity is slack-off；The feed liquid that the membrane module of so other two groups of normal filtrations passes through is by the production water for the ceramic film component for needing to clean
Branch pipe is flow in ceramic film component, realizes the backwash of ceramic membrane element, then be back to reflux line through the branch pipe that flows back and finally receive
Combine in head tank, the automatic backwash of ceramic film component can be achieved through the above way, as needed, we can also lead to
Cross Automated condtrol and realize the purpose that the alternating of automatic backwash is changed.
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 (3)
1. a kind of automatic backwash formula ceramic membrane filter device, including head tank, inlet channel, the dehvery pump on inlet channel,
Also include ceramic film component, reflux line and water production pipeline；It is characterized in that：Described ceramic film component is at least three groups, and
For dead-end filtration ceramic film component, described ceramic film component includes a putamina, ceramic membrane element is provided with described putamina；Institute
The putamina stated is provided with water inlet and delivery port；Described water inlet connects inlet channel by water inlet pipe, and delivery port passes through
A backflow branch pipe is also associated with production water branch pipe connection water production pipeline, described water inlet pipe, described backflow branch pipe connects back to
Flow tube road；Described water inlet pipe, backflow branch pipe, valve is designed with production water branch pipe.
A kind of 2. automatic backwash formula ceramic membrane filter device according to claim 1, it is characterised in that：Described water production pipeline
Being provided with makes the pipeline reducing diameter joint that the pipe diameter of water production pipeline rear end diminishes.
A kind of 3. automatic backwash formula ceramic membrane filter device according to claim 1, it is characterised in that：Described ceramic membrane element
The pore size filter of part is 50-800nm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720554357.3U CN206778193U (en) | 2017-05-18 | 2017-05-18 | A kind of automatic backwash formula ceramic membrane filter device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720554357.3U CN206778193U (en) | 2017-05-18 | 2017-05-18 | A kind of automatic backwash formula ceramic membrane filter device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206778193U true CN206778193U (en) | 2017-12-22 |
Family
ID=60712755
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720554357.3U Expired - Fee Related CN206778193U (en) | 2017-05-18 | 2017-05-18 | A kind of automatic backwash formula ceramic membrane filter device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206778193U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111939768A (en) * | 2020-09-01 | 2020-11-17 | 侯梦斌 | Floating water taking equipment and process |
-
2017
- 2017-05-18 CN CN201720554357.3U patent/CN206778193U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111939768A (en) * | 2020-09-01 | 2020-11-17 | 侯梦斌 | Floating water taking equipment and process |
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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: 20171222 Termination date: 20190518 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |