CN108380054A - The emptier of waste emulsified mixture hyperfiltration treatment - Google Patents
The emptier of waste emulsified mixture hyperfiltration treatment Download PDFInfo
- Publication number
- CN108380054A CN108380054A CN201810436977.6A CN201810436977A CN108380054A CN 108380054 A CN108380054 A CN 108380054A CN 201810436977 A CN201810436977 A CN 201810436977A CN 108380054 A CN108380054 A CN 108380054A
- Authority
- CN
- China
- Prior art keywords
- pipeline
- ultrafiltration
- ultrafiltration system
- emptier
- solenoid valve
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/20—Accessories; Auxiliary operations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/145—Ultrafiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/12—Specific discharge elements
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- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention relates to a kind of emptier of waste emulsified mixture hyperfiltration treatment, it is characterized in that:Including pipeline, one end of the pipeline connects ultrafiltration system pipeline, and the other end of pipeline connects ultrafiltration system ultrafiltration circulating tank, ball valve of the installation in normally open and the solenoid valve with ultrafiltration system coordinated signals on pipeline.The pipeline is attached installation by elbow.The upper end capping of one end connection ultrafiltration system pipeline of the pipeline.The emptier of waste emulsified mixture hyperfiltration treatment of the present invention, pass through solenoid valve in pipeline and ultrafiltration system coordinated signals, solenoid valve is closed when ultrafiltration system is run, solenoid valve opens connection ultrafiltration circulating tank when ultrafiltration system empties stoste in pipeline, ultrafiltration circulating tank belongs to non-pressure vessel, and internal pressure is equal with atmospheric pressure, and auxiliary accelerates stoste in emptying ultrafiltration system, scavenging period is saved, ejected wash water intractability is reduced.
Description
Technical field
The present invention relates to a kind of emptier of waste emulsified mixture hyperfiltration treatment, belong to technical field of environment protection equipment.
Background technology
Ultrafiltration system is a kind of system for being demulsified to stoste by ultrafiltration membrane pipe, removing a large amount of greasy dirts in stoste.
But since ultrafiltration membrane pipe can adhere to remaining greasy dirt while a large amount of greasy dirts in removing emulsion in membrane tube,
So needing to clean ultrafiltration membrane pipe after used a period of time, and need first to empty the stoste in pipeline if cleaning, such as
It is longer that no ultrafiltration system pipeline emptying auxiliary piping then empties the required time, and can not drain stoste, can both cause in this way be
System cleaning total time used lengthens, and will also result in the pollution of ejected wash water, increases ejected wash water intractability.
Invention content
The purpose of the present invention is overcoming the deficiencies in the prior art, a kind of emptying of waste emulsified mixture hyperfiltration treatment is provided
Device reduces ultrafiltration system emptying time, is cleaned convenient for ultrafiltration system.
According to technical solution provided by the invention, the emptier of the waste emulsified mixture hyperfiltration treatment, it is characterized in that:Including
One end of pipeline, the pipeline connects ultrafiltration system pipeline, the other end connection ultrafiltration system ultrafiltration cycle of ultrafiltration system pipeline
Tank, ball valve of the installation in normally open and the solenoid valve with ultrafiltration system coordinated signals on pipeline.
Further, the pipeline is attached installation by elbow.
Further, the upper end capping of one end connection ultrafiltration system pipeline of the pipeline.
Further, the ball valve is arranged close to ultrafiltration system pipeline side, and solenoid valve is arranged close to ultrafiltration system
Ultrafiltration circulating tank side.
Further, the other end of the pipeline is connected to flushes with the head cover of ultrafiltration circulatory system ultrafiltration circulating tank.
The emptier of waste emulsified mixture hyperfiltration treatment of the present invention is controlled by solenoid valve in pipeline and ultrafiltration system linkage
System, solenoid valve is closed when ultrafiltration system is run, and solenoid valve opens connection ultrafiltration circulating tank when ultrafiltration system empties stoste in pipeline,
Ultrafiltration circulating tank belongs to non-pressure vessel, and internal pressure is equal with atmospheric pressure, and auxiliary accelerates stoste in emptying ultrafiltration system, saves clear
It washes the time, reduces ejected wash water intractability.
Description of the drawings
Fig. 1 is the structural schematic diagram of the emptier of waste emulsified mixture hyperfiltration treatment of the present invention.
Fig. 2 is layout drawing of the emptier of waste emulsified mixture hyperfiltration treatment of the present invention in ultrafiltration system.
Reference sign:1- pipelines, 2- elbows, 3- ball valves, 4- solenoid valves, 5- ultrafiltration systems pipeline, 6- ultrafiltration systems
Ultrafiltration circulating tank.
Specific implementation mode
With reference to specific attached drawing, the invention will be further described.
As shown in Figure 1 and Figure 2, the emptier of waste emulsified mixture hyperfiltration treatment of the present invention includes pipeline 1, and pipeline 1 passes through
Elbow 2 is attached installation;The upper end capping of one end connection ultrafiltration system pipeline 5 of the pipeline 1, ultrafiltration system pipeline 5
The other end connects ultrafiltration system ultrafiltration circulating tank 6, and mounting ball valve 3 and solenoid valve 4 on pipeline 1, ball valve 3 are in normally open,
Solenoid valve 4 and ultrafiltration system coordinated signals.
The ball valve 3 is arranged close to 5 side of ultrafiltration system pipeline, and solenoid valve 4 is arranged close to ultrafiltration system ultrafiltration and follows
6 side of ring tank.
The other end of the pipeline 1 is connected to be flushed with the head cover of ultrafiltration circulatory system ultrafiltration circulating tank 6, is not inserted into ultrafiltration
In circulatory system ultrafiltration circulating tank 6.
The course of work of the emptier of waste emulsified mixture hyperfiltration treatment of the present invention is as follows:The present invention stops in ultrafiltration system
Only used when stoste in operation emptying pipeline, ball valve 3 be in normally open, and solenoid valve 4 needs to close when maintenance, solenoid valve 4 and
Ultrafiltration system coordinated signals, solenoid valve 4 is closed when ultrafiltration system is run, solenoid valve 4 when ultrafiltration system is out of service
In the open state, auxiliary ultrafiltration system pipeline 5 is emptied, and solenoid valve 4 is closed after emptying and is noted to ultrafiltration system pipeline
Enter clear water to be cleaned.
Ultrafiltration system pipeline needs to clean the membrane tube in system after operation a period of time, and the present invention is in ultrafiltration
Solenoid valve is closed when system operation, to reach system normal use;Solenoid valve is opened when ultrafiltration system pipeline need to clean, makes pipe
Road top peak is connected with air, and to auxiliary piping rapid deflation stoste, then additional clean water is cleaned, and is subtracted with reaching
Few purpose for cleaning consumed total time.The solenoid valve of the present invention can operate with system operation and make coordinated signals simultaneously, be used for
The automatic control of system will not aggravate the burden of user without increasing extra operation when operation.
Claims (5)
1. a kind of emptier of waste emulsified mixture hyperfiltration treatment, it is characterized in that:Including pipeline(1), the pipeline(1)One end connect
Connect ultrafiltration system pipeline(5), ultrafiltration system pipeline(5)The other end connect ultrafiltration system ultrafiltration circulating tank(6), in pipeline(1)
Upper ball valve of the installation in normally open(3)With the solenoid valve with ultrafiltration system coordinated signals(4).
2. the emptier of waste emulsified mixture hyperfiltration treatment as described in claim 1, it is characterized in that:The pipeline(1)By curved
Head(2)It is attached installation.
3. the emptier of waste emulsified mixture hyperfiltration treatment as described in claim 1, it is characterized in that:The pipeline(1)One end
Connect ultrafiltration system pipeline(5)Upper end capping.
4. the emptier of waste emulsified mixture hyperfiltration treatment as described in claim 1, it is characterized in that:The ball valve(3)It is mounted on
Close to ultrafiltration system pipeline(5)Side, solenoid valve(4)It is arranged close to ultrafiltration system ultrafiltration circulating tank(6)Side.
5. the emptier of waste emulsified mixture hyperfiltration treatment as described in claim 1, it is characterized in that:The pipeline(1)It is another
End is connected to and ultrafiltration circulatory system ultrafiltration circulating tank(6)Head cover flush.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810436977.6A CN108380054A (en) | 2018-05-09 | 2018-05-09 | The emptier of waste emulsified mixture hyperfiltration treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810436977.6A CN108380054A (en) | 2018-05-09 | 2018-05-09 | The emptier of waste emulsified mixture hyperfiltration treatment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108380054A true CN108380054A (en) | 2018-08-10 |
Family
ID=63071440
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810436977.6A Pending CN108380054A (en) | 2018-05-09 | 2018-05-09 | The emptier of waste emulsified mixture hyperfiltration treatment |
Country Status (1)
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CN (1) | CN108380054A (en) |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6186903A (en) * | 1984-10-03 | 1986-05-02 | Asahi Chem Ind Co Ltd | Ultrafiltration apparatus |
RU1792729C (en) * | 1989-06-14 | 1993-02-07 | Rabinovich Aleksandr L | Technique used in treating oil emulsions-containing sewage |
DE29818701U1 (en) * | 1998-10-22 | 1999-02-11 | Industrie-Filtration INDUFILT GmbH, 37079 Göttingen | Device for processing an emulsion |
MD3096F1 (en) * | 2005-12-28 | 2006-07-31 | Universitatea De Stat Din Moldova | Plant for water-oil emulsion separation by ultrafiltration |
JP2007301544A (en) * | 2006-05-12 | 2007-11-22 | Takahashi Kinzoku Kk | Membrane type oil-water separator, membrane washing method, washing system using membrane type oil-water separator, and oil-water separating system of water-soluble coolant liquid |
CN203971767U (en) * | 2014-07-25 | 2014-12-03 | 湖北武当金鼎制药有限公司 | Traditional Chinese medicine injection production ultrafiltration system |
CN204874531U (en) * | 2015-07-20 | 2015-12-16 | 江苏普华克胜药业有限公司 | Draw equipment of pig eyeball ammonia iodine peptide |
CN205575983U (en) * | 2016-04-21 | 2016-09-14 | 天津康源生物技术有限公司 | Novel automatic concentrated desalination degerming system of albumen liquid |
CN205676198U (en) * | 2016-06-08 | 2016-11-09 | 天津海普尔膜科技有限公司 | A kind of oil emulsion automated programming system |
FR3038854A1 (en) * | 2015-07-15 | 2017-01-20 | S D E - Savoy Desinfection Environnement | INSTALLATION FOR CLEANING WASTE RECEPTACLES |
CN106861442A (en) * | 2017-04-14 | 2017-06-20 | 湖南北控威保特环境科技股份有限公司 | The purging system and cleaning method of a kind of tubular ultrafiltration membrane module |
CN208526320U (en) * | 2018-05-09 | 2019-02-22 | 无锡格物环保技术有限公司 | The emptier of waste emulsified mixture hyperfiltration treatment |
-
2018
- 2018-05-09 CN CN201810436977.6A patent/CN108380054A/en active Pending
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6186903A (en) * | 1984-10-03 | 1986-05-02 | Asahi Chem Ind Co Ltd | Ultrafiltration apparatus |
RU1792729C (en) * | 1989-06-14 | 1993-02-07 | Rabinovich Aleksandr L | Technique used in treating oil emulsions-containing sewage |
DE29818701U1 (en) * | 1998-10-22 | 1999-02-11 | Industrie-Filtration INDUFILT GmbH, 37079 Göttingen | Device for processing an emulsion |
MD3096F1 (en) * | 2005-12-28 | 2006-07-31 | Universitatea De Stat Din Moldova | Plant for water-oil emulsion separation by ultrafiltration |
JP2007301544A (en) * | 2006-05-12 | 2007-11-22 | Takahashi Kinzoku Kk | Membrane type oil-water separator, membrane washing method, washing system using membrane type oil-water separator, and oil-water separating system of water-soluble coolant liquid |
CN203971767U (en) * | 2014-07-25 | 2014-12-03 | 湖北武当金鼎制药有限公司 | Traditional Chinese medicine injection production ultrafiltration system |
FR3038854A1 (en) * | 2015-07-15 | 2017-01-20 | S D E - Savoy Desinfection Environnement | INSTALLATION FOR CLEANING WASTE RECEPTACLES |
CN204874531U (en) * | 2015-07-20 | 2015-12-16 | 江苏普华克胜药业有限公司 | Draw equipment of pig eyeball ammonia iodine peptide |
CN205575983U (en) * | 2016-04-21 | 2016-09-14 | 天津康源生物技术有限公司 | Novel automatic concentrated desalination degerming system of albumen liquid |
CN205676198U (en) * | 2016-06-08 | 2016-11-09 | 天津海普尔膜科技有限公司 | A kind of oil emulsion automated programming system |
CN106861442A (en) * | 2017-04-14 | 2017-06-20 | 湖南北控威保特环境科技股份有限公司 | The purging system and cleaning method of a kind of tubular ultrafiltration membrane module |
CN208526320U (en) * | 2018-05-09 | 2019-02-22 | 无锡格物环保技术有限公司 | The emptier of waste emulsified mixture hyperfiltration treatment |
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