CN204380530U - The spray silk purging system of hollow-fibre membrane - Google Patents
The spray silk purging system of hollow-fibre membrane Download PDFInfo
- Publication number
- CN204380530U CN204380530U CN201420726344.6U CN201420726344U CN204380530U CN 204380530 U CN204380530 U CN 204380530U CN 201420726344 U CN201420726344 U CN 201420726344U CN 204380530 U CN204380530 U CN 204380530U
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- Prior art keywords
- silk
- hollow
- fibre membrane
- spinning head
- cleaning fluid
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Abstract
The utility model provides the spray silk purging system of the hollow-fibre membrane that a kind of service efficiency is high, and it has: silk slurry supplying tank, and its supply is starched as the silk of the material of hollow-fibre membrane; Spinning head, itself and silk are starched supplying tank and are connected, and the silk slurry of ejection silk slurry supplying tank supply forms hollow-fibre membrane; Cleaning fluid tank, its spinning head connects, and to spinning head supply cleaning fluid, and cleaning fluid tank is connected with pressure source via pressure controller.
Description
Technical field
The utility model relates to a kind of spray silk purging system of hollow-fibre membrane.
Background technology
Hollow Fiber Membrane Separation Technology is a kind of new and high technology grown up at mid-twentieth century, because hollow-fibre membrane to have the characteristic of selectively penetrating and diffusion to some gas component, and effective film area is maximum, isolated by filtration efficiency is high, easy cleaning, structure is simple, easy to operate, do not produce the reasons such as secondary pollution in production process, thus be widely used in such as pharmacy, brewage, food and drink, chemical industry, recycling municipal sewage, hospital, community wastewater can be separated with solution such as productive life sewage disposal such as, papermaking, the concentrated and isolation technics of purifying.
Such hollow fiber film assembly is made up of housing, end socket, end cap and hollow-fibre membrane usually.Wherein, hollow-fibre membrane is critical component, and its profile is rectangular threadiness, and a large amount of hollow-fibre membrane sealings in the housing.When producing so fibrous hollow-fibre membrane, usually utilize the spray silk system of hollow-fibre membrane.The spray silk system of hollow-fibre membrane is formed primarily of silk slurry supplying tank and spinning head, from silk slurry supplying tank shape spinning head supply silk slurry, forms hollow-fibre membrane.
But in process of production, the silk slurry of the remnants in spinning head runs into steam and solidifies, and blocks the spinneret orifice of spinning head thus.Therefore, usually in process of production, need regular replacing spinning head to clean, the spinning head blocked is put into boil cleaning fluid make silk starch fusing from spinning head discharge, spinning head is cleaned.But, need in this case constantly to change spinning head, can not produce continuously, the service efficiency of spinning head is low, and such cleaning is very loaded down with trivial details, needs the cost time of one or two hour, thus the man-hour of operating personnel increases, total production efficiency is low.
Utility model content
The utility model proposes for problems of the prior art, its object is to provide the spray silk purging system of the hollow-fibre membrane that a kind of service efficiency is high.
Following technical scheme is adopted for realizing the purpose of this utility model.
The spray silk purging system of the hollow-fibre membrane of technical scheme 1, has: silk slurry supplying tank, and its supply is starched as the silk of the material of hollow-fibre membrane; Spinning head, itself and described silk are starched supplying tank and are connected, and the silk slurry spraying the supply of described silk slurry supplying tank forms hollow-fibre membrane; Cleaning fluid tank, spinning head described in it connects, and to spinning head supply cleaning fluid, and described cleaning fluid tank is connected with pressure source via pressure controller.
The spray silk purging system of the hollow-fibre membrane of technical scheme 2, in the spray silk purging system of the hollow-fibre membrane of technical scheme 1, described silk slurry supplying tank is connected with described spinning head through filter.
The spray silk purging system of the hollow-fibre membrane of technical scheme 3, in the spray silk purging system of the hollow-fibre membrane of technical scheme 2, described cleaning fluid tank is connected with described spinning head via described filter.
The spray silk purging system of the hollow-fibre membrane of technical scheme 4, in the spray silk purging system of the hollow-fibre membrane any one of technical scheme 1 to 3, described cleaning fluid tank is connected with heating source by temperature controller.
Compared with prior art, the utility model has following beneficial effect.
According to the spray silk purging system of the hollow-fibre membrane of technical scheme 1, spinning head connects the cleaning fluid tank with cleaning fluid, at the end of production, closedown spinning head and silk are starched and are supplied tank connected pipeline, open spinning head and the tank connected pipeline of cleaning fluid, cleaning fluid flows into spinning head, the silk slurry of the solidification in spinning head is dissolved and flows out from spinning head, reach the effect of on-line cleaning spinning head.Now, after being produced by spinning head, can clean immediately, avoid changing spinning head during regenerative ratio, reduce spinning head replacing construction, on-line cleaning spinning head can be realized and carry out quantity-produced object, improve the service efficiency of spinning head, improve productivity ratio.
In addition, according to the spray silk purging system of the hollow-fibre membrane of technical scheme 2, silk slurry supplying tank is connected with spinning head through filter, can produce thus after filter wire slurry, thus can the high-quality hollow-fibre membrane of production department.
In addition, according to the spray silk system of the hollow-fibre membrane of technical scheme 3, cleaning fluid tank is connected with spinning head through filter, thus can simultaneously filter rinsed, thus can enhance productivity.
In addition, according to the spray silk purging system of the hollow-fibre membrane of technical scheme 4, cleaning fluid tank is connected with heating source by temperature controller, can regulate the temperature of the cleaning fluid in cleaning fluid tank thus, remain the temperature of best dissolving silk slurry, thus maintain best cleaning performance all the time.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the spray silk purging system representing hollow-fibre membrane of the present utility model.
Fig. 2 is the schematic diagram of the another way of the spray silk purging system representing hollow-fibre membrane of the present utility model.
Fig. 3 is the schematic diagram of the another mode of the spray silk purging system representing hollow-fibre membrane of the present utility model.
Fig. 4 is the schematic diagram of a mode again of the spray silk purging system representing hollow-fibre membrane of the present utility model.
Detailed description of the invention
Below, the spray silk purging system of the hollow-fibre membrane as an example of the present utility model is described based on accompanying drawing.
Fig. 1 is the schematic diagram of the spray silk purging system representing hollow-fibre membrane of the present utility model.
As shown in Figure 1, the spray silk purging system of hollow-fibre membrane of the present utility model has: silk slurry supplying tank 10, and its supply is starched as the silk of the material of hollow-fibre membrane; Spinning head 20, itself and silk are starched supplying tank 10 and are connected, and the silk slurry that ejection silk slurry supplying tank 10 supplies forms hollow-fibre membrane; Cleaning fluid tank 30, it is connected with spinning head 20, supplies cleaning fluid to spinning head 20, and cleaning fluid tank 30 is connected 40 via pressure controller with pressure source.
Specifically, silk slurry supplying tank is connected with spinning head via open and close valve, and cleaning fluid tank is connected with spinning head via open and close valve in addition, and cleaning fluid pipe can be connected with pressure source via pressure controller
According to the spray silk purging system of above-mentioned hollow-fibre membrane, spinning head connects the cleaning fluid tank with cleaning fluid, at the end of production, closedown spinning head and silk are starched and are supplied tank connected pipeline, open spinning head and the tank connected pipeline of cleaning fluid, cleaning fluid flows into spinning head, the silk slurry of the solidification in spinning head is dissolved and flows out from spinning head, reach the effect of on-line cleaning spinning head.Now, after being produced by spinning head, can clean immediately, avoid changing spinning head during regenerative ratio, reduce spinning head replacing construction, on-line cleaning spinning head can be realized and carry out quantity-produced object, improve the service efficiency of spinning head, improve productivity ratio.
In addition, as shown in Figure 2, silk slurry supplying tank 10 can be connected with spinning head 20 through filter 50.Can produce after filter wire slurry thus, thus can the high-quality hollow-fibre membrane of production department.
In addition, as described in Figure 3, cleaning fluid tank 30 can be connected with spinning head 20 through filter 50, thus can simultaneously filter rinsed, thus can enhance productivity.
In addition, as shown in Figure 4, cleaning fluid tank 30 can be connected with heating source and heater 60 by temperature controller.The temperature of the cleaning fluid in cleaning fluid tank can be regulated thus, remain the temperature of best dissolving silk slurry, thus maintain best cleaning performance all the time.
Above the spray silk purging system of the hollow-fibre membrane of preferred embodiment of the present utility model is illustrated, but, the utility model is not limited to above-mentioned concrete embodiment, only otherwise depart from the scope of claim, can carry out various distortion or change.The utility model comprises various distortion within the scope of the claims and change.
Claims (4)
1. a spray silk purging system for hollow-fibre membrane, is characterized in that,
Have:
Silk slurry supplying tank, its supply is starched as the silk of the material of hollow-fibre membrane;
Spinning head, itself and described silk are starched supplying tank and are connected, and the silk slurry spraying the supply of described silk slurry supplying tank forms hollow-fibre membrane;
Cleaning fluid tank, it is connected with described spinning head, and to spinning head supply cleaning fluid, and described cleaning fluid tank is connected with pressure source via pressure controller.
2. the spray silk purging system of hollow-fibre membrane according to claim 1, is characterized in that, described silk slurry supplying tank is connected with described spinning head through filter.
3. the spray silk purging system of hollow-fibre membrane according to claim 2, it is characterized in that, described cleaning fluid tank is connected with described spinning head via described filter.
4. the spray silk purging system of hollow-fibre membrane according to any one of claim 1 to 3, it is characterized in that, described cleaning fluid tank is connected with heating source by temperature controller.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420726344.6U CN204380530U (en) | 2014-11-27 | 2014-11-27 | The spray silk purging system of hollow-fibre membrane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420726344.6U CN204380530U (en) | 2014-11-27 | 2014-11-27 | The spray silk purging system of hollow-fibre membrane |
Publications (1)
Publication Number | Publication Date |
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CN204380530U true CN204380530U (en) | 2015-06-10 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420726344.6U Expired - Fee Related CN204380530U (en) | 2014-11-27 | 2014-11-27 | The spray silk purging system of hollow-fibre membrane |
Country Status (1)
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CN (1) | CN204380530U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105671653A (en) * | 2016-04-07 | 2016-06-15 | 天津华清健坤膜科技有限公司 | Hollow fiber spinning nozzle or spinning plate washing device and application method |
CN110685023A (en) * | 2018-07-05 | 2020-01-14 | 宁波方太厨具有限公司 | Spinneret cleaning device and method |
-
2014
- 2014-11-27 CN CN201420726344.6U patent/CN204380530U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105671653A (en) * | 2016-04-07 | 2016-06-15 | 天津华清健坤膜科技有限公司 | Hollow fiber spinning nozzle or spinning plate washing device and application method |
CN105671653B (en) * | 2016-04-07 | 2018-07-31 | 天津华清健坤膜科技有限公司 | A kind of hollow fiber spinneret or cleaning device for spinning plate and application method |
CN110685023A (en) * | 2018-07-05 | 2020-01-14 | 宁波方太厨具有限公司 | Spinneret cleaning device and method |
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Legal Events
Date | Code | Title | Description |
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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: 20150610 Termination date: 20181127 |
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CF01 | Termination of patent right due to non-payment of annual fee |