CN107213800A - A kind of novel cross flow rotary ceramic membranous system - Google Patents
A kind of novel cross flow rotary ceramic membranous system Download PDFInfo
- Publication number
- CN107213800A CN107213800A CN201710555413.XA CN201710555413A CN107213800A CN 107213800 A CN107213800 A CN 107213800A CN 201710555413 A CN201710555413 A CN 201710555413A CN 107213800 A CN107213800 A CN 107213800A
- Authority
- CN
- China
- Prior art keywords
- tank body
- cross flow
- rotary ceramic
- pipe
- novel cross
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
-
- 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
- B01D61/18—Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
Abstract
The present invention discloses a kind of novel cross flow rotary ceramic membranous system, including moving cart, tank body is installed above moving cart, and surge tank, the side of moving cart is provided with control system, the rotary ceramic diaphragm group being internally provided with hollow live spindle of tank body, live spindle is connected by swivel joint with surge tank, drain pipe is provided with surge tank, concentrated solution outlet pipe is provided with above the outside tank body of tank body, concentrated solution outlet pipe is connected by adjustable pneumatic valve with control system, feed tube is provided with below the outside tank body of tank body, the feed pump of control raw material liq suction is provided between feed tube and tank body, cleaning device is additionally provided with the side of the outside tank body of tank body.System design of the present invention is simple in construction, easy for installation, and cleaning device is set in system, and periodically ceramic diaphragm, tank interior, valve and pipe fitting can be cleaned.
Description
Technical field
The invention belongs to filtration and separation techniques field, and in particular to a kind of novel cross flow rotary ceramic membranous system.
Background technology
Ceramic membrane filter system, is the accurate ultra filtration cleaning equipment that can be widely applied to various fields.Its core
Heart component inorganic ceramic membrane has excellent heat endurance and hole stability, and intensity is high, resistant to chemical etching, cleaning and regeneration performance
It is good, have both the two-fold advantage for having high efficiency filter and secondary filter, the important new technology separated as secondary filter under harsh conditions.
Existing rotary ceramic membranous system complex structural designs, installation is wasted time and energy, and inconvenient long-time uses the maintenance of rear system
Maintenance.
The content of the invention
The technical problems to be solved by the invention are to provide a kind of novel cross flow rotary ceramic membranous system, the system design
It is simple in construction, it is easy for installation, and cleaning device is set in system, can be periodically to ceramic diaphragm, tank interior, valve and pipe fitting
Cleaned.
In order to solve the above technical problems, the technical solution adopted by the present invention：A kind of novel cross flow rotary ceramic membranous system, its
It is characterised by：Including moving cart, tank body and surge tank, the side of moving cart are installed above the moving cart
Control system, the rotary ceramic diaphragm group being internally provided with hollow live spindle of the tank body, the hollow rotation are installed
Turn one end that main shaft extended to outside tank body and swivel joint is installed, the swivel joint passes through connecting line and the surge tank
Drain pipe is provided with connection, surge tank, concentrated solution outlet pipe is provided with above the outside tank body of tank body, it is described dense
Contracting liquid outlet is connected by adjustable pneumatic valve with the control system, is provided with below the outside tank body of tank body
Feed tube, is provided with the feed pump of control raw material liq suction, in the inside institute of tank body between the feed tube and the tank body
The side for stating tank body is additionally provided with cleaning device.
Further, it is provided with stainless steel purge valve in the cleaning device.
Further, back-blowing device is installed in the surge tank.
Further, concentrated solution outlet connection is additionally provided between the outside tank body and concentrated solution outlet pipe of tank body
Pipe.
Further, the concentrated solution outlet pipe, which is provided with blast pipe, the blast pipe to be provided with, controls blast pipe to open
The stainless steel air bleeding valve of pass.
Further, it is provided with below the outside tank body of tank body on blow-off pipe, the blow-off pipe and is provided with control
The stainless steel blowoff valve of blow-off pipe switch processed.
Further, extend to that be provided with the hollow live spindle outside tank body can be with the deceleration of VFC
Machine, to adjust linear velocity during ceramic diaphragm rotation, makes system reach optimum Working.
Beneficial effects of the present invention：
1) present invention provides a kind of novel cross flow rotary ceramic membranous system, and the system design is simple in construction, easy for installation, has
Maintenance beneficial to later stage work personnel to system；And the system configuration moving cart, it is moved easily and transports；
2) cleaning device is additionally provided with the system, can be with by controlling the switch and closure of purge valve in cleaning device
Periodically tank interior, valve and pipe fitting are cleaned, so as to extend the service life of system；
3) system is additionally provided with hollow live spindle and is connected with surge tank by swivel joint, and the setting of swivel joint can
To improve the separative efficiency of solid particle and liquid；
4) adjustable pneumatic valve is provided between concentrated solution outlet pipe and control system in the system, can sets and adjust
System working pressure, reaches optimal separation effect；
5) back-blowing device is also designed in the system, the solid particle for being attached to ceramic diaphragm outer surface and suspension can be blown open
Thing, coordinates cross-flow filtration structure effectively to extend the service life of ceramic diaphragm.
Brief description of the drawings
Fig. 1 is the schematic device of novel cross flow rotary ceramic membranous system；
Fig. 2 is the part-structure schematic diagram of cross-flow rotary ceramic membranous system.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Embodiment：
A kind of novel cross flow rotary ceramic membranous system, as shown in figure 1, including moving cart 1, moving cart 1 includes and ground
The parallel horizontal stand 1.1 in face and two side stands 1.2 with the oblique of horizontal stand 1.1, the horizontal stand 1.1 of moving cart
Top be provided with tank body 2 and surge tank 3, the side stand 1.2 of moving cart control system 4 be installed, tank body 2 it is interior
Portion is provided with the rotary ceramic diaphragm group 2.2 with hollow live spindle 2.1, and rotary ceramic diaphragm group 2.2 is used for raw material liq
Carry out effective separation of solid and liquid.Live spindle 2.1 is connected by swivel joint 5 with surge tank 3, and liquid is provided with out on surge tank 3
Pipe 3.1, is provided with concentrated solution outlet pipe 2.3 above the outside tank body of tank body 1, and concentrated solution outlet pipe 2.3 passes through adjustable
Pneumatic operated valve 10 is connected with control system 4, in order to which concentrate is led into material box or concentration liquid storage tank from concentrated solution outlet pipe 2.3
In, it is additionally provided with concentrated solution outlet connecting tube 2.7 between the outside tank body 1 and concentrated solution outlet pipe 2.3 of tank body 1.In tank body 1
Outside tank body below be provided with feed tube 2.4, be provided between feed tube 2.4 and tank body 1 control raw material liq suction
Feed pump 6, cleaning device 7 is additionally provided with the side of the inner tanks of tank body 1.The cleaning device 7 is provided with control, and it is switched
Stainless steel purge valve 7.1.
It should be noted that system configuration moving cart in the system, can facilitate the movement and transport of the system；When being
System is in running order, and when feed pump 6 starts, raw material liq is sucked into from feed tube 2.4 in tank body 1, utilizes rotary ceramic
Refined filtration, the ultrafiltration of diaphragm group 2.2, the solid particle in raw material liq and suspension are intercepted in rotary ceramic diaphragm group
2.2 outer surfaces, the filtrate after filtering enters in hollow live spindle 2.1, and enters surge tank 3, Ran Houtong by swivel joint 5
The drain pipe 3.1 for crossing surge tank 3 is discharged.Concentrate drains into material box or concentration liquid storage tank by concentrated solution outlet connecting tube 2.7
In.The setting of swivel joint 5 can improve the separative efficiency of solid particle and liquid in the present invention.
In the system, cleaning device 7 is additionally provided with the side of the inner tanks of tank body 1.The cleaning device 7 is provided with control
Make the stainless steel purge valve 7.1 of its switch.After using some cycles, feed tube 2.4 is closed, while opening stainless steel purge valve
7.1, the cleaning fluid conveyed by external impetus is entered in tank body by stainless steel purge valve 7.1, is sprayed by mouth spray, cleaning rotation
Ceramic diaphragm group 2.2, tank interior, valve and pipe fitting, are then discharged through stainless steel blowoff valve 2.6.1.Set in tank body 1 clear
Cleaning device 7 can be cleaned periodically to rotary ceramic diaphragm group 2.2, tank interior, valve and pipe fitting, so as to extend system
Service life.
It is provided with adjustable pneumatic valve 10 between concentrated solution outlet pipe 2.3 and control system 4, adjustable pneumatic valve 10 can be with
Setting and regulating system operating pressure, so that solid particle reaches optimal separation effect with liquid.
In order to further extend the service life of novel cross flow rotary ceramic membranous system, blowback is installed in the surge tank 3
Device 8, i.e. back-blowing device 8 timing automatic can reversely be blown into clean compressed air, and compressed air is filtered by high-precision pressure regulation
After device filtering, entered by surge tank 3 inside hollow live spindle 2.1, the appearance of rotary ceramic diaphragm group 2.2 is purged from inside to outside
The solid particle and suspension in face, coordinate cross-flow filtration structure effectively to extend the service life of rotary ceramic diaphragm group 2.2.
Concentrated solution outlet pipe 2.3, which is provided with, is provided with the stainless of control blast pipe switch on blast pipe 2.5, blast pipe 2.5
Steel air bleeding valve 2.5.1, discharges the air in tank body 1 during for system boot.
It is provided with the present invention below the outside tank body of tank body 1 on blow-off pipe 2.6, blow-off pipe 2.6 and is provided with control
The stainless steel blowoff valve 2.6.1 of blow-off pipe switch.In course of normal operation, stainless steel blowoff valve 2.6.1 is closed, and works as cleaning device
After 7 open, cleaning liquid is cleaned to tank interior, valve and pipe fitting, after cleaning is finished, and opens stainless steel blowoff valve
2.6.1, sewage cleaning finished flows out from stainless steel blowoff valve 2.6.1.
In the present invention, extend to be provided with the hollow live spindle outside tank body can with the reductor 9 of VFC, with
Just linear velocity when regulation rotary ceramic diaphragm group 2.2 rotates, makes system reach optimum Working.
In the system, valve and pipe fitting use foodstuff sanitation-stage stainless steel material, can apply to fine chemistry industry, medicine with
And food service industry is separated by filtration.
The foregoing is only a specific embodiment of the invention, but protection scope of the present invention is not limited thereto, any
Those familiar with the art the invention discloses technical scope in, change or replacement can be readily occurred in, should all be contained
Cover within protection scope of the present invention.Therefore, protection scope of the present invention should be based on the protection scope of the described claims.
Claims (7)
1. a kind of novel cross flow rotary ceramic membranous system, it is characterised in that：Including moving cart, the top of the moving cart is pacified
Equipped with tank body and surge tank, the side of moving cart is provided with control system, and the tank body is internally provided with hollow rotation
Turn the rotary ceramic diaphragm group of main shaft, one end that the hollow live spindle is extended to outside tank body is provided with swivel joint, institute
State swivel joint to be connected with the surge tank by connecting line, the surge tank is provided with drain pipe, in the outside institute of tank body
State and concentrated solution outlet pipe is provided with above tank body, the concentrated solution outlet pipe passes through adjustable pneumatic valve and the control system
Connection, is provided with feed tube below the outside tank body of tank body, control is provided between the feed tube and the tank body
The feed pump of raw material liq suction processed, cleaning device is additionally provided with the side of tank body described in the inside of tank body.
2. a kind of novel cross flow rotary ceramic membranous system according to claim 1, it is characterised in that：Set in the cleaning device
It is equipped with stainless steel purge valve.
3. a kind of novel cross flow rotary ceramic membranous system according to claim 1, it is characterised in that：Installed in the surge tank
There is back-blowing device.
4. a kind of novel cross flow rotary ceramic membranous system according to claim 1, it is characterised in that：Described in the outside of tank body
Concentrated solution outlet connecting tube is additionally provided between tank body and the concentrated solution outlet pipe.
5. a kind of novel cross flow rotary ceramic membranous system according to claim 1, it is characterised in that：The concentrated solution outlet pipe
It is provided with the stainless steel air bleeding valve that control blast pipe switch is provided with blast pipe, the blast pipe.
6. a kind of novel cross flow rotary ceramic membranous system according to claim 1, it is characterised in that：Described in the outside of tank body
The stainless steel blowoff valve that control of sewage disposal pipe switch is provided with blow-off pipe, the blow-off pipe is provided with below tank body.
7. a kind of novel cross flow rotary ceramic membranous system according to claim 1, it is characterised in that：Extend to outside tank body
Being provided with the hollow live spindle can be with the reductor of VFC.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710555413.XA CN107213800A (en) | 2017-07-10 | 2017-07-10 | A kind of novel cross flow rotary ceramic membranous system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710555413.XA CN107213800A (en) | 2017-07-10 | 2017-07-10 | A kind of novel cross flow rotary ceramic membranous system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107213800A true CN107213800A (en) | 2017-09-29 |
Family
ID=59952878
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710555413.XA Pending CN107213800A (en) | 2017-07-10 | 2017-07-10 | A kind of novel cross flow rotary ceramic membranous system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107213800A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111217348A (en) * | 2018-11-24 | 2020-06-02 | 飞潮（无锡）过滤技术有限公司 | Process for washing and concentrating lithium iron phosphate powder slurry by using rotary ceramic membrane |
| CN113813908A (en) * | 2021-10-22 | 2021-12-21 | 上海安赐环保科技股份有限公司 | Integrated reaction and separation system, process and application |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104592036A (en) * | 2014-12-24 | 2015-05-06 | 上海安赐机械设备有限公司 | Nitrobenzene/dinitrobenzene catalyst recovery device and recovery method thereof |
| CN104923081A (en) * | 2015-07-02 | 2015-09-23 | 徐永恒 | Rotating disc type dynamic membrane separating assembly |
| CN106422468A (en) * | 2016-10-31 | 2017-02-22 | 刘国敏 | Cross-flow backflushing ceramic membrane liquid ammonia deoiling filtering device |
-
2017
- 2017-07-10 CN CN201710555413.XA patent/CN107213800A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104592036A (en) * | 2014-12-24 | 2015-05-06 | 上海安赐机械设备有限公司 | Nitrobenzene/dinitrobenzene catalyst recovery device and recovery method thereof |
| CN104923081A (en) * | 2015-07-02 | 2015-09-23 | 徐永恒 | Rotating disc type dynamic membrane separating assembly |
| CN106422468A (en) * | 2016-10-31 | 2017-02-22 | 刘国敏 | Cross-flow backflushing ceramic membrane liquid ammonia deoiling filtering device |
Non-Patent Citations (1)
| Title |
|---|
| 蔡仁良等: "《过程装备密封技术》", 31 May 2006, 北京：化学工业出版社 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111217348A (en) * | 2018-11-24 | 2020-06-02 | 飞潮（无锡）过滤技术有限公司 | Process for washing and concentrating lithium iron phosphate powder slurry by using rotary ceramic membrane |
| CN113813908A (en) * | 2021-10-22 | 2021-12-21 | 上海安赐环保科技股份有限公司 | Integrated reaction and separation system, process and application |
| CN113813908B (en) * | 2021-10-22 | 2023-09-22 | 上海安赐环保科技股份有限公司 | Integrated reaction and separation system, process and application |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2020042379A1 (en) | Exhaust spray tower | |
| CN204208383U (en) | A kind of cyclone type dedusting steam-water separator | |
| CN107213800A (en) | A kind of novel cross flow rotary ceramic membranous system | |
| CN207237438U (en) | Bio-pharmaceuticals isolates and purifies filtration apparatus | |
| CN206845218U (en) | A kind of coal mine dedusting device | |
| CN203075750U (en) | Coarse-fine integrated filter unit | |
| CN210842858U (en) | Energy-saving and efficient dust collector | |
| CN219944052U (en) | Dust removal equipment | |
| CN202289763U (en) | Intake deduster with membrane | |
| CN104117252A (en) | High efficient vacuum water-bath deduster | |
| CN203777804U (en) | Automatic filter with a swirling device | |
| CN207913978U (en) | Self-cleaning double fluid atomizing lance | |
| CN207641186U (en) | One kind being used for the molding dust-extraction unit of operation towel film | |
| CN207342299U (en) | A kind of self-cleaning filter with sewage treatment | |
| CN109261382A (en) | A kind of cyclone dust collectors | |
| CN103920337B (en) | With the automatic filter of swirl-flow devices | |
| CN209378660U (en) | A kind of vertical deduster of drop stream | |
| CN210114931U (en) | Automatic dust removal device | |
| CN204017586U (en) | High-efficiency vacuum wet dust collector | |
| CN205150531U (en) | Jar is switched in vacuum | |
| CN203852972U (en) | Dust removal sprayer and dust removing device | |
| CN207929674U (en) | Ultra-clean contactless cleaning system | |
| CN208893702U (en) | A kind of disassembly and wash free paint filter device | |
| CN206008148U (en) | Waterpower torsion couple automatic cleaning screen filter | |
| CN209602140U (en) | One kind removing carbon blower fan apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: Room 472, 1180 Nanting Highway, Zhuanghang Town, Fengxian District, Shanghai, 20149 Applicant after: FEICHAO (SHANGHAI) ENVIRONMENTAL TECHNOLOGY Co.,Ltd. Address before: Room 472, 1180 Nanting Highway, Zhuanghang Town, Fengxian District, Shanghai, 20149 Applicant before: SHANGHAI RUNMING PRECISION TECHNOLOGY Co.,Ltd. |
|
| CB02 | Change of applicant information | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170929 |
|
| WD01 | Invention patent application deemed withdrawn after publication |