CN201728010U - High-pressure carbon fiber melt filter - Google Patents
High-pressure carbon fiber melt filter Download PDFInfo
- Publication number
- CN201728010U CN201728010U CN2010202654233U CN201020265423U CN201728010U CN 201728010 U CN201728010 U CN 201728010U CN 2010202654233 U CN2010202654233 U CN 2010202654233U CN 201020265423 U CN201020265423 U CN 201020265423U CN 201728010 U CN201728010 U CN 201728010U
- Authority
- CN
- China
- Prior art keywords
- filter
- carbon fiber
- valve
- fiber melt
- pressure carbon
- 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.)
- Expired - Fee Related
Links
- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 17
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 17
- 238000007599 discharging Methods 0.000 claims description 27
- 238000010079 rubber tapping Methods 0.000 claims description 6
- 238000005070 sampling Methods 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000010924 continuous production Methods 0.000 abstract 1
- 238000001914 filtration Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000007380 fibre production Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
Abstract
The utility model discloses a high-pressure carbon fiber melt filter, mainly solving the problem that the existing carbon fiber melt filter can not be produced continuously and the filter core is inconvenient to be cleaned. The high-pressure carbon fiber melt filter is characterized in that the structure comprises two filter chambers (2); feed switching valves (6) are respectively arranged at the lower ends of the two filter chambers (2), discharge switching valves (7) are respectively on the discharge end covers (4) of the two filter chambers (2), a backwash valve (8) is arranged on each discharge switching valve (7) and used for controlling a discharge passage (9) and a backwash pipe (10) in the discharge end cover (4) to be switched on or off. The high-pressure carbon fiber melt filter is improved in the background technology, the double-cylinder structure of two filter chambers is adopted, three-way feed and discharge switching valves are used for switching, one filter chamber is switched quickly into another while the production process is not stopped, and the filter chamber not in service is washed once the backwash valve is opened, thereby the utility model is characterized by continuous production, convenient cleaning of the filter core, and high work efficiency.
Description
Technical field:
The utility model relates to used filter, especially the high pressure carbon fiber melt filter in a kind of carbon fiber production.
Background technology:
Existing carbon fiber fondant filter mainly is made up of frame, filter chamber and charging and discharging valve, and the filter chamber upper end is provided with installing plate and discharging end cap, and filter core was installed on the installing plate, and the lower end of filter chamber communicates with inlet valve, and the discharging end cap communicates with bleeder valve.Filter chamber is one, is the single cylinder structure, because the filter core of crossing in the filter chamber needs to clean in use for some time, the breaks in production of so just having to can not be carried out production continuously.When the cleaning and filtering core, need pull down and could clean crossing filter core, inconvenience during cleaning, the length that expends time in influences ordinary production.
The utility model content:
Existing carbon fiber fondant filter can not be produced continuously and the deficiency of cleaning and filtering core inconvenience in order to overcome, the utility model provides a kind of high pressure carbon fiber melt filter, this high pressure carbon fiber melt filter improves under background technology, adopt the twin-tub structure of 2 filter chambers to utilize threeway charging and discharging transfer valve to switch mutually, under the situation that does not stop to produce, switch to another filter chamber fast from a filter chamber, opening backwash valve can clean idle filter chamber, have can produce continuously, the cleaning and filtering core is convenient and the characteristics of high efficiency.
The technical solution of the utility model is: this high pressure carbon fiber melt filter comprises frame and filter chamber, the filter chamber upper end is provided with installing plate and discharging end cap, filter core was installed on the installing plate, filter chamber is 2, the lower end of 2 filter chambers is provided with the charging transfer valve, and the discharge end of 2 filter chambers is covered with the discharging transfer valve; Described discharging transfer valve is provided with backwash valve, and backwash valve can be controlled the tapping channel in the discharging end cap and the break-make of backwash tube.
Described charging transfer valve is provided with the blowdown baiting valve.
Described discharging transfer valve is provided with the exhaust gas sampling valve.
The beneficial effects of the utility model are: owing to take such scheme, when producing, a filter chamber job, another filter chamber is standby; When needs cleaning and filtering core, switch to standby filter chamber by threeway charging and discharging transfer valve, under the situation that does not stop to produce, the filter core of crossing that stops up is cleaned, can uninterruptedly produce continuously.And when the cleaning and filtering core, only need open backwash valve, the tapping channel in the discharging end cap can be connected with the backwash tube in the external world, and the high pressure washing liquid in the backwash tube oppositely entered filter core and rinses out the dirt that filters outer core, clear Xian's process is quick and convenient, high efficiency.
Description of drawings:
Accompanying drawing 1 is a structure cutaway view of the present utility model;
Accompanying drawing 2 is right views of Fig. 1;
Accompanying drawing 3 is vertical views of Fig. 2.
1-frame among the figure, the 2-filter chamber, the 3-installing plate, 4-discharging end cap, 5-crosses filter core, 6-charging transfer valve, 7-discharging transfer valve, 8-backwash valve, 9-tapping channel, 10-backwash tube, 11-blowdown baiting valve, 12-exhaust gas sampling valve.
The specific embodiment:
The utility model is described in further detail below in conjunction with accompanying drawing:
By Fig. 1 in conjunction with Fig. 2, shown in Figure 3, this high pressure carbon fiber melt filter comprises frame 1 and filter chamber 2, filter chamber 2 upper ends are provided with installing plate 3 and discharging end cap 4, filter core 5 was installed on the installing plate 3, filter chamber 2 is 2, the discharging end cap 4 that the lower end of 2 filter chambers 2 is provided with 6,2 filter chambers 2 of charging transfer valve is provided with discharging transfer valve 7; Described discharging transfer valve 7 is provided with backwash valve 8, and backwash valve 8 can be controlled the break-make of tapping channel 9 and backwash tube 10 in the discharging end cap 4.When producing, filter chamber 2 job, another filter chamber 2 is standby; When needs cleaning and filtering core 5, switch to standby filter chamber 2 by threeway charging and discharging transfer valve (6,7), under the situation that does not stop to produce, the filter core 5 of crossing that stops up is cleaned, can uninterruptedly produce continuously.And when cleaning and filtering core 5, only need open backwash valve 8, the tapping channel 9 in the discharging end cap 4 can be connected with the backwash tube 10 in the external world, and the high pressure washing liquid in the backwash tube 10 oppositely entered the dirt that filter core 5 rinsed out filter core 5 outer walls, clear Xian's process is quick and convenient, high efficiency.
In conjunction with shown in Figure 2, described charging transfer valve 6 is provided with blowdown baiting valve 11 by Fig. 1.When backwash filter core 5, can open blowdown baiting valve 11, give off flushing liquor and dirt.
In conjunction with shown in Figure 2, described discharging transfer valve 7 is provided with exhaust gas sampling valve 12 by Fig. 1.In the ordinary production, can take a sample or emission gases by exhaust gas sampling valve 12.
Claims (3)
1. high pressure carbon fiber melt filter, comprise frame (1) and filter chamber (2), filter chamber (2) upper end is provided with installing plate (3) and discharging end cap (4), filter core (5) was installed on the installing plate (3), it is characterized in that: filter chamber (2) is 2, the lower end of 2 filter chambers (2) is provided with charging transfer valve (6), and the discharging end cap (4) of 2 filter chambers (2) is provided with discharging transfer valve (7); Described discharging transfer valve (7) is provided with backwash valve (8), and backwash valve (8) can be controlled the break-make of tapping channel (9) and backwash tube (10) in the discharging end cap (4).
2. high pressure carbon fiber melt filter according to claim 1 is characterized in that: described charging transfer valve (6) is provided with blowdown baiting valve (11).
3. high pressure carbon fiber melt filter according to claim 1 and 2 is characterized in that: described discharging transfer valve (7) is provided with exhaust gas sampling valve (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202654233U CN201728010U (en) | 2010-07-16 | 2010-07-16 | High-pressure carbon fiber melt filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202654233U CN201728010U (en) | 2010-07-16 | 2010-07-16 | High-pressure carbon fiber melt filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201728010U true CN201728010U (en) | 2011-02-02 |
Family
ID=43519169
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202654233U Expired - Fee Related CN201728010U (en) | 2010-07-16 | 2010-07-16 | High-pressure carbon fiber melt filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201728010U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102166448A (en) * | 2011-03-10 | 2011-08-31 | 温州宇丰化纤机械有限公司 | Full-automatic melt filter |
| CN102716608A (en) * | 2012-06-08 | 2012-10-10 | 温州宇丰化纤机械有限公司 | Automatic back washing carbon fiber filter |
| CN102921228A (en) * | 2012-10-30 | 2013-02-13 | 宁波大发化纤有限公司 | Vertical type double-cylinder filter for polyester spinning |
| CN105396353A (en) * | 2015-12-18 | 2016-03-16 | 浙江宇丰机械有限公司 | High-viscosity material full-automatic backwashing coarse-filtration system |
-
2010
- 2010-07-16 CN CN2010202654233U patent/CN201728010U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102166448A (en) * | 2011-03-10 | 2011-08-31 | 温州宇丰化纤机械有限公司 | Full-automatic melt filter |
| CN102166448B (en) * | 2011-03-10 | 2012-11-28 | 温州宇丰化纤机械有限公司 | Full-automatic melt filter |
| CN102716608A (en) * | 2012-06-08 | 2012-10-10 | 温州宇丰化纤机械有限公司 | Automatic back washing carbon fiber filter |
| CN102716608B (en) * | 2012-06-08 | 2014-12-10 | 温州宇丰化纤机械有限公司 | Automatic back washing carbon fiber filter |
| CN102921228A (en) * | 2012-10-30 | 2013-02-13 | 宁波大发化纤有限公司 | Vertical type double-cylinder filter for polyester spinning |
| CN105396353A (en) * | 2015-12-18 | 2016-03-16 | 浙江宇丰机械有限公司 | High-viscosity material full-automatic backwashing coarse-filtration system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160526 Address after: 325000 office building, Pearl River Road Administrative Committee, Binhai Economic Zone, Wenzhou economic and Technological Development Zone, Zhejiang 5108, China Patentee after: ZHEJIANG YUFENG MACHINERY CO., LTD. Address before: 325013 No. 516, Airport Avenue, Longwan District, Zhejiang, Wenzhou Patentee before: Wenzhou Yufeng Chemical Fiber Machinery Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110202 Termination date: 20180716 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |