CN203123841U - Multi-unit integrated detection equipment - Google Patents
Multi-unit integrated detection equipment Download PDFInfo
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- CN203123841U CN203123841U CN 201320110438 CN201320110438U CN203123841U CN 203123841 U CN203123841 U CN 203123841U CN 201320110438 CN201320110438 CN 201320110438 CN 201320110438 U CN201320110438 U CN 201320110438U CN 203123841 U CN203123841 U CN 203123841U
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- checkout equipment
- pipeline
- putamina
- integrated checkout
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Abstract
The utility model discloses multi-unit integrated detection equipment, comprising a membrane housing in which a membrane core is contained, and a pipeline and a feed liquid tank connected with each other, wherein the pipeline is connected with the two ends of the membrane housing through two distribution pipes, respectively; the feed liquid tank is connected with the two ends of the membrane housing through two concentrated liquid return pipes, respectively; and valves are arranged on all the distribution pipes and the concentrated liquid return pipes. The multi-unit integrated detection equipment has the characteristics that the valves on each distribution pipe and each concentrated liquid return pipe are controlled to be opened and closed so that forward cleaning and backward cleaning of the membrane core are realized; and therefore, pollutants in the membrane core can be removed thoroughly, the service life of the membrane core can be effectively prolonged and the working efficiency can be improved.
Description
Technical field
The utility model relates to water treatment field, is specifically related to the integrated checkout equipment of a kind of multiple-unit.
Background technology
Film is as a kind of macromolecule chemical material, existing separation, concentrate, purification and desalination function, features such as efficient, energy-saving and environmental protection, molecular level filtration are arranged again, be widely used in industries such as sewage recycling, desalinization, brackish water desalination, ultra-pure water.Membrane technology is acknowledged as one of most important new technology of 21 century.
Membrane separation technique mainly comprises micro-filtration, ultrafiltration, nanofiltration and counter-infiltration.The maximum technology barrier that the application industry of film separation is at present promoted is the pollution of film.After film resolution element film core uses a period of time, owing to process exists and being in contact with one another and pollution has been taken place for the crown_interception of material of material, filter effect obviously descends, separating effect also changes, need clean it, remove the pollutant of absorption or combination, membrane component/film core performance is recovered, guarantee its separating effect.The cleaning way of the membrane component/film core that pollutes mainly is to use cleaning agent to clean in the equipment cocycle at present, or takes off membrane component/film core off-line soaking and washing.
China utility model patent CN202700376U discloses a kind of reverse osmosis membrane on-line auto-cleaning system, comprise the pipe blow-through that links to each other with the counter-infiltration system inlet channel, be provided with security personnel's filter, scavenging pump, purge tank on the described pipe blow-through successively, described counter-infiltration system water producing pipe road is provided with a cleaning reflux line and links to each other with purge tank.The utility model adopts online film cleaning technique, saves hand labor, can fast, in time solve membrane pollution problem, overcomes the shortcoming that the off-line film cleans.But pipe blow-through of the present utility model only links to each other with an end of film core, thus this purging system can only folk prescription to cleaning film core, can not remove the pollutant in the film core up hill and dale, inefficiency.
Summary of the invention
The utility model purpose provides the integrated checkout equipment of a kind of multiple-unit, can positive and negative two-way cleaning film core, can remove the pollutant in the film core more up hill and dale, and prolong the service life of film core effectively, increase work efficiency.
For achieving the above object, the technical solution adopted in the utility model is: the integrated checkout equipment of a kind of multiple-unit, comprise the putamina of ccontaining film core, continuous pipeline and material liquid tank, described pipeline utilizes two distributing pipes to link to each other with the two ends of described putamina respectively, described material liquid tank utilizes two concentrate feed back pipes to link to each other with the two ends of described putamina respectively, is equipped with valve on described distributing pipe and the concentrate feed back pipe.
The integrated checkout equipment of above-mentioned multiple-unit comprises 2～6 described putaminas.
In the technique scheme, at least one end of described putamina is provided with the punishment in advance mouth, and the distributing pipe that arranges with end has the input and output material arm that links to each other with the punishment in advance mouth with concentrate feed back pipe, and this input and output material arm is provided with valve.
In the technique scheme, be provided with permeate conduits between an end of described putamina and the material liquid tank, this permeate conduits is provided with flowmeter.
In the technique scheme, described distributing pipe is provided with flowmeter.
In the technique scheme, described pipeline is provided with temp probe.
In the technique scheme, described pipeline is provided with bag filter and pump.
In the technique scheme, the side of described pipeline is parallel with the bypass of binder flow container and pipeline, and this bypass is provided with valve.
Further technical scheme, described putamina upper and lower settings is provided with the film core of upper and lower settings in it.
Further technical scheme, the integrated checkout equipment of described multiple-unit comprise 4 cun putaminas, 6 cun putaminas, 8 cun putaminas and integral type putamina.
Because technique scheme is used, the advantage that the utility model compared with prior art has is:
1. the utility model is realized forward and reverse cleaning of film core by the switching of the valve on each distributing pipe of control and the concentrate feed back pipe, can remove the pollutant in the film core more up hill and dale, prolongs the service life of film core effectively, increases work efficiency.
2. the utility model comprises a plurality of putaminas, compares with the system of the independent detection of single group film core in the past, saves the space, saves resource, and pump, material liquid tank, support and electric cabinet etc. can share, and can realize the detection of a plurality of film cores by switch valve.
3. the utility model is provided with flowmeter at distributing pipe, can see the contaminated degree of membrane core intuitively by the reading of flowmeter; If paint detection, if the flowmeter muddiness illustrates film core seepage; Also be provided with flowmeter in permeate conduits, can clean the reading of forward and backward flowmeter by contrast, clearly know wash result.
4. the utility model is provided with temp probe at pipeline, utilizes temp probe to detect former liquid temp, and is shown on the interior instrument board of electric cabinet, and after running temperature was set in arrival, the checkout equipment automatic shutdown protection was in case the too high damage film of temperature core.
5. the utility model is provided with bag filter at pipeline, removes larger particles in the stoste etc. in advance, the diaphragm core.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment one;
Fig. 2 is the fundamental diagram of embodiment one;
Wherein: 1,4 cun putaminas; 2, pipeline; 3, material liquid tank; 4, go up distributing pipe; 5, following distributing pipe; 6, go up concentrate feed back pipe; 7, following concentrate feed back pipe, 8, valve; 9, go up the input and output material arm; 10, following input and output material arm; 11, permeate conduits; 12, flowmeter; 13, temp probe; 14, bag filter; 15, pump; 16, bypass; 17, Pressure gauge.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further described:
Embodiment one: shown in Fig. 1,2, the integrated checkout equipment of a kind of multiple-unit, 4 cun, 6 cun, 8 cun and the putamina of 4 upper and lower settings of integral type comprising ccontaining film core, detection system common pump, material liquid tank, support and the electric cabinet etc. of 4 film cores, compare with the system of the independent detection of single group film core in the past, save the space, save resource, can realize the detection of a plurality of film cores by switch valve.
Detection system with 4 cun film cores is that example further describes the integrated checkout equipment of this multiple-unit, comprise 4 cun putaminas 1, the pipeline 2 and the material liquid tank 3 that link to each other, described pipeline 2 utilizes upward, and distributing pipe 4 links to each other with the upper/lower terminal of described 4 cun putaminas 1 respectively with following distributing pipe 5, described material liquid tank 3 utilizes upward, and concentrate feed back pipe 6 links to each other with the upper/lower terminal of described 4 cun putaminas 1 respectively with following concentrate feed back pipe 7, described upper and lower distributing pipe is equipped with valve 8 on the upper and lower concentrate feed back pipe.Said structure is realized forward and reverse cleaning of film core by the switching of the valve on each distributing pipe of control and the concentrate feed back pipe, can remove the pollutant in the film core more up hill and dale, prolongs the service life of film core effectively, increases work efficiency.
The upper end of described 4 cun putaminas 1 is provided with the punishment in advance mouth, and the last distributing pipe 4 that arranges with end has the last input and output material arm 9 that links to each other with last punishment in advance mouth with last concentrate feed back pipe 6, and input and output material arm 9 is provided with valve on this.
The lower end of described 4 cun putaminas 1 is provided with down the punishment in advance mouth, and the following distributing pipe 5 that arranges with end has the following input and output material arm 10 that links to each other with following punishment in advance mouth with following concentrate feed back pipe 7, and this time input and output material arm 10 is provided with valve.
Be provided with permeate conduits 11 between the upper end of described 4 cun putaminas 1 and the material liquid tank 3, the flexible pipe that permeate conduits 11 is selected easy connection for use and is easy to observe which is provided with flowmeter 12.Be equipped with flowmeter on the described upper and lower distributing pipe.Said structure can be seen the contaminated degree of membrane core intuitively by the reading of the flowmeter on the upper and lower distributing pipe; If paint detection, if the flowmeter muddiness illustrates film core seepage; Also be provided with flowmeter in permeate conduits, can clean the reading of forward and backward flowmeter by contrast, clearly know wash result.
The bottom of described 4 cun putaminas 1 is provided with blowoff valve, makes things convenient for blowdown.
Described pipeline 2 is provided with temp probe 13, utilizes temp probe to detect former liquid temp, and is shown on the interior instrument board of electric cabinet, and after running temperature was set in arrival, the cleaning device automatic shutdown protection was in case the too high damage film of temperature core.
Described pipeline 2 is provided with bag filter 14 and pump 15.Utilize bag filter, remove larger particles in the stoste etc. in advance, the diaphragm core.
The integrated checkout equipment utilization of this multiple-unit is by the button on the control cabinet, the start and stop of control pump 15.
The both sides of bag filter 14 are equipped with Pressure gauge 17 on the pipeline 2, are used for testing respectively bag filter import and export pressure; Also be provided with Pressure gauge on the upper and lower distributing pipe, be used for test membrane core import and export pressure.
The side of described pipeline 2 is parallel with the bypass 16 of binder flow container 3 and pipeline 2, and this bypass 16 is provided with valve, the valve wide open during start in the bypass 16, after close gradually.
The integrated checkout equipment of above-mentioned multiple-unit is arranged on the chassis, and 4 rollers are installed in the below on chassis, and wherein 2 is directional wheel, and 2 is universal wheel, convenient mobile.
The glide path of feed liquid is as described below when utilizing the present embodiment forward to clean 4 cun film cores:
At first, stoste is from material liquid tank 3 flow through pipeline 2, pump 15, bag filter 14, distributing pipe 5 and input and output material arm 10 down down, flows into 4 cun putaminas 1 via punishment in advance mouth down; Then, the see through liquid mouth of liquid from 4 cun putamina 1 upper ends that see through that sees through the film core flows into permeate conduits 11, finally is back to material liquid tank 3; Simultaneously, the concentrate that does not see through the film core flows into from last punishment in advance mouth goes up input and output material arm 9, is back to material liquid tank 3 by last concentrate feed back pipe 6, finishes forward and cleans.
When forward cleans, pipeline 2, down distributing pipe 5, down input and output material arm 10, permeate conduits 11, go up the valve opening on input and output material arm 9 and the last concentrate feed back pipe 6, all the other valve closings.
The glide path of feed liquid is as described below when utilizing present embodiment oppositely to clean 4 cun film cores:
At first, stoste from material liquid tank 3 flow through pipeline 2, pump 15, bag filter 14, go up distributing pipe 4 and go up input and output material arm 9, flow into 4 cun putaminas 1 via last punishment in advance mouth; Then, the see through liquid mouth of liquid from 4 cun putamina 1 upper ends that see through that sees through the film core flows into permeate conduits 11, finally is back to material liquid tank 3; Simultaneously, through concentrate input and output material arm 10 under the punishment in advance mouth flows into down of film core, be back to material liquid tank 3 by following concentrate feed back pipe 7, finish reverse cleaning.
When oppositely cleaning, pipeline 2, go up distributing pipe 4, go up input and output material arm 9, permeate conduits 11, the valve opening on input and output material arm 10 and the following concentrate feed back pipe 7 down, all the other valve closings.
The circuit design that all the other film cores detect and operation require and 4 cun identical permeate conduits of film core, in the present embodiment, be provided with two trunk lines and a main permeate conduits, the upper and lower punishment in advance mouth of each putamina links to each other with trunk line through valve respectively, the liquid mouth that sees through of each putamina is connected with flexible pipe respectively with between the flowmeter, and links to each other with main permeate conduits.
The above is preferred embodiment of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from principle described in the utility model; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (10)
1. integrated checkout equipment of multiple-unit, comprise the putamina of ccontaining film core, continuous pipeline and material liquid tank, it is characterized in that, described pipeline utilizes two distributing pipes to link to each other with the two ends of described putamina respectively, described material liquid tank utilizes two concentrate feed back pipes to link to each other with the two ends of described putamina respectively, is equipped with valve on described distributing pipe and the concentrate feed back pipe.
2. the integrated checkout equipment of multiple-unit according to claim 1 is characterized in that, comprises 2～6 described putaminas.
3. the integrated checkout equipment of multiple-unit according to claim 1 and 2, it is characterized in that, at least one end of described putamina is provided with the punishment in advance mouth, and the distributing pipe that arranges with end has the input and output material arm that links to each other with the punishment in advance mouth with concentrate feed back pipe, and this input and output material arm is provided with valve.
4. the integrated checkout equipment of multiple-unit according to claim 1 and 2 is characterized in that, is provided with permeate conduits between an end of described putamina and the material liquid tank, and this permeate conduits is provided with flowmeter.
5. the integrated checkout equipment of multiple-unit according to claim 1 and 2 is characterized in that, described distributing pipe is provided with flowmeter.
6. the integrated checkout equipment of multiple-unit according to claim 1 and 2 is characterized in that, described pipeline is provided with temp probe.
7. the integrated checkout equipment of multiple-unit according to claim 1 and 2 is characterized in that, described pipeline is provided with bag filter and pump.
8. the integrated checkout equipment of multiple-unit according to claim 1 and 2 is characterized in that, the side of described pipeline is parallel with the bypass of binder flow container and pipeline, and this bypass is provided with valve.
9. the integrated checkout equipment of multiple-unit according to claim 1 is characterized in that, described putamina upper and lower settings is provided with the film core of upper and lower settings in it.
10. according to claim 2 or the integrated checkout equipment of 9 described multiple-units, it is characterized in that, comprise 4 cun putaminas, 6 cun putaminas, 8 cun putaminas and integral type putamina.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320110438 CN203123841U (en) | 2013-03-12 | 2013-03-12 | Multi-unit integrated detection equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320110438 CN203123841U (en) | 2013-03-12 | 2013-03-12 | Multi-unit integrated detection equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203123841U true CN203123841U (en) | 2013-08-14 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320110438 Expired - Fee Related CN203123841U (en) | 2013-03-12 | 2013-03-12 | Multi-unit integrated detection equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203123841U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103623706A (en) * | 2013-11-20 | 2014-03-12 | 株洲时代新材料科技股份有限公司 | Device for detecting flat filtering membrane element |
| CN110523289A (en) * | 2019-09-11 | 2019-12-03 | 上海丰信环保科技有限公司 | A kind of detection device and its application method of the on-line checking reverse-osmosis membrane element performance of simplicity |
-
2013
- 2013-03-12 CN CN 201320110438 patent/CN203123841U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103623706A (en) * | 2013-11-20 | 2014-03-12 | 株洲时代新材料科技股份有限公司 | Device for detecting flat filtering membrane element |
| CN103623706B (en) * | 2013-11-20 | 2015-08-12 | 株洲时代新材料科技股份有限公司 | For the checkout gear of flat panel filter membrane component |
| CN110523289A (en) * | 2019-09-11 | 2019-12-03 | 上海丰信环保科技有限公司 | A kind of detection device and its application method of the on-line checking reverse-osmosis membrane element performance of simplicity |
| CN110523289B (en) * | 2019-09-11 | 2021-07-27 | 上海丰信环保科技有限公司 | Simple and convenient detection equipment for detecting performance of reverse osmosis membrane element on line and use method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130814 Termination date: 20180312 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |