CN108380054A - The emptier of waste emulsified mixture hyperfiltration treatment - Google Patents

The emptier of waste emulsified mixture hyperfiltration treatment Download PDF

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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
Application number
CN201810436977.6A
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Chinese (zh)
Inventor
嵇伟峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuxi's Environmental Protection Technology Co Ltd
Original Assignee
Wuxi's Environmental Protection Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Wuxi's Environmental Protection Technology Co Ltd filed Critical Wuxi's Environmental Protection Technology Co Ltd
Priority to CN201810436977.6A priority Critical patent/CN108380054A/en
Publication of CN108380054A publication Critical patent/CN108380054A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/20Accessories; Auxiliary operations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/145Ultrafiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/12Specific 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

The emptier of waste emulsified mixture hyperfiltration treatment
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.
CN201810436977.6A 2018-05-09 2018-05-09 The emptier of waste emulsified mixture hyperfiltration treatment Pending CN108380054A (en)

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)

Country Link
CN (1) CN108380054A (en)

Citations (12)

* Cited by examiner, † Cited by third party
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

Patent Citations (12)

* Cited by examiner, † Cited by third party
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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