CN201735239U - Separation plate type filter capable of realizing thorough reverse flushing of filter cores - Google Patents
Separation plate type filter capable of realizing thorough reverse flushing of filter cores Download PDFInfo
- Publication number
- CN201735239U CN201735239U CN2010202151179U CN201020215117U CN201735239U CN 201735239 U CN201735239 U CN 201735239U CN 2010202151179 U CN2010202151179 U CN 2010202151179U CN 201020215117 U CN201020215117 U CN 201020215117U CN 201735239 U CN201735239 U CN 201735239U
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- Prior art keywords
- valve
- filter
- separation plate
- filter core
- filter cores
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- 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
- 238000000926 separation method Methods 0.000 title abstract 7
- 238000011010 flushing procedure Methods 0.000 title abstract 2
- 239000007788 liquid Substances 0.000 claims abstract description 49
- 238000007599 discharging Methods 0.000 claims description 9
- 125000006850 spacer group Chemical group 0.000 claims description 2
- 239000012065 filter cake Substances 0.000 abstract description 15
- 238000007664 blowing Methods 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 5
- 239000012792 core layer Substances 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a separation plate type filter capable of realizing the thorough reverse flushing of filter cores, which comprises a casing, wherein a separation plate is arranged at the inner side of the casing, a clean liquid outlet valve, a gas back blowing valve and an atmospheric valve are respectively connected with a clean liquid cavity arranged above the separation plate, a turbidity liquid inlet valve, a pollution discharge valve and a thorough discharge valve are respectively connected with a turbidity liquid cavity arranged under the separation plate, a plurality of filter cores positioned in the turbidity liquid cavity are arranged on the separation plate, the clean liquid cavity arranged at the upper part and the turbidity liquid cavity arranged at the lower part are communicated through the filter cores, core pipes are arranged at the inner sides of the filter cores, the lower ends of the core pipes are positioned at the lower parts of inner cavities of the filter cores, gaps are formed between the outer sides of the core pipes and the inner walls of the filter cores, the core pipes are communicated with the clean liquid cavity and the inner cavities of the filter cores, and a balance opening valve is arranged on the casing under the separation plate. The utility model has the advantages of thorough filter cake removal, no residual, time saving, labor saving and no need of manual operation.
Description
Technical field
The utility model relates to a kind of filter, and particularly a kind of filter core backwash clapboard type filter completely that makes is mainly used in turbid liquid is filtered.
Background technology
At present, in chemical industry or other industrial processes, often need the turbid liquid that produce be filtered, existing filter mostly is iris type, its structure is: comprise the housing that has loam cake, in the housing inboard dividing plate is arranged, the dividing plate top is the clear liquid chamber, the dividing plate below is turbid sap cavity, the clear liquid chamber of dividing plate top is connected with the purified liquor outlet valve respectively, the filter washing water inlet valve, the blow-back valve, atmospheric valve, the turbid sap cavity of dividing plate below is connected with turbid liquid inlet valve respectively, blowoff valve, dirt discharging valve, the a plurality of filter cores that are positioned at turbid sap cavity are installed on dividing plate, and the clear liquid chamber of top is connected by filter core with the turbid sap cavity of below.The turbid liquid that enters in the turbid sap cavity from turbid liquid inlet valve during work enters the clear liquid chamber by filter core, and the clear liquid after the filtration is discharged housing from the purified liquor outlet valve, and filter residue is intercepted at cartridge surface.Along with the carrying out of filtering, filter residue at the filter core outer surface constantly thickens and forms filter cake, filtration resistance constantly increases, the clear liquid flow constantly reduces, close turbid liquid inlet valve and stop to filter when the pressure reduction between turbid sap cavity and the clear liquid chamber reaches when setting value when dropping to the lower limit rated value (or purified liquor outlet flow), filter core is counter to be cleaned to crossing.During anti-the cleaning, need close turbid liquid inlet valve and purified liquor outlet valve earlier, open atmospheric valve and dirt discharging valve, the liquid in the housing is discharged, close atmospheric valve and dirt discharging valve then.Open blowoff valve, in the clear liquid chamber, be blown into gas from the blow-back valve then, gas more after filtration in-core side-blown promptly blow to filter cake laterally attached to the filter core outside, it is come off, gas and filter cake are discharged by blowoff valve.The filter of this structure has following shortcoming: after the part filter cake on the cartridge surface is blown off, when filter core does not have the lip-deep penetrating area in cake district greater than the gas access sectional area, gas begins to pass filter core from no cake district, the gas purging power that causes carrying on the cartridge surface of filter cake zone reduces greatly, the less power of blowing is not enough so that the filter cake at other positions breaks away from cartridge surface, can not remove whole filter cakes completely.In order to remove whole filter cakes, must carry out manually-operated, very trouble wastes time and energy.
Summary of the invention
The purpose of this utility model provide a kind of thorough removal filter cake, not residual, need not manual work make filter core backwash clapboard type filter completely, overcome the deficiencies in the prior art.
Make filter core backwash clapboard type filter completely, comprise housing, in the housing inboard dividing plate is arranged, the clear liquid chamber of dividing plate top is connected with purified liquor outlet valve, blow-back valve, atmospheric valve respectively, the turbid sap cavity of dividing plate below is connected with turbid liquid inlet valve, blowoff valve, dirt discharging valve respectively, the a plurality of filter cores that are positioned at turbid sap cavity are installed on dividing plate, and the clear liquid chamber is connected by filter core with turbid sap cavity; The inboard of described filter core is provided with the core pipe, and the lower end of core pipe is positioned at the inner chamber bottom of filter core, forms the gap between the outside of core pipe and the inwall of filter core, and the core pipe is communicated with the inner chamber of clear liquid chamber and filter core; Below the housing upper spacer, be connected to the balance port valve.
Make filter core backwash clapboard type filter completely, during the blowback operation, open atmospheric valve simultaneously by the turbid liquid of balance port valve discharge housing internal upper part earlier, make turbid liquid liquid level consistent with balance port valve height, filter core below major part is immersed in the turbid liquid, close dirt discharging valve, atmospheric valve, blowoff valve and dirt discharging valve all are in closed condition, in housing, be blown into gas by the blow-back valve, gas is introduced into the clear liquid chamber, enter filter core inner chamber bottom along the core pipe again, gas oppositely passes the cake layer in the filter core layer and the filter core outside under pressure, enter turbid sap cavity, the bubble disturbance liquid of floating upward quickly produces flow-disturbing, the motive force of flow-disturbing forces filter cake to break away from filter core, gas self-balancing mouth valve behind the flow-disturbing drains into outside the housing, last all filter cake impurity can be discharged from blowoff valve, reach the purpose of the filter cake of all having removed the filter core outside completely, not residual, need not to open the artificial operation of thoroughly cleaning filter core of big blind flange, and reduced the equipment operation, change expenses such as pad and maintenance of equipment, removed installation, suppress, a series of links such as leak test, time saving and energy saving.
Description of drawings
Fig. 1 is the structural representation of the utility model specific embodiment;
Fig. 2 is a filter core structural representation partly shown in Figure 1.
The specific embodiment
As shown in Figure 1, 2: 1 housing, be fixed with dividing plate 2 in housing 1 inboard, dividing plate 2 is divided into two parts up and down with the inner chamber of housing 1, and the top is clear liquid chamber 17, and the below is turbid sap cavity 18.The clear liquid chamber 17 of dividing plate 2 tops is connected with purified liquor outlet valve 8, blow-back valve 11, atmospheric valve 10 respectively, and the turbid sap cavity 18 of dividing plate 2 belows is connected with turbid liquid inlet valve 7, blowoff valve 6, dirt discharging valve 5 respectively; The a plurality of filter cores 4 that are positioned at turbid sap cavity 18 are installed on dividing plate 2, and the clear liquid chamber 17 of top is connected by filter core 4 with the turbid sap cavity 18 of below.Filter core 4 comprises the link 13 of top and the bottom 16 of below, is filtration members 14 between link 13 and bottom 16, is processed with screw thread on the link 13 or fixedlys connected with dividing plate 2 with flange.Be provided with core pipe 15 in the inboard of filter core 4, can be between the upper end of core pipe 15 and the link 13 and be threaded, the lower end of core pipe 15 is positioned at the inner chamber bottom of filter core 4, i.e. the inner chamber bottom of filtration members 14.Form gap 12 between the inwall of the outside of core pipe 15 and filter core 4, core pipe 15 is communicated with the inner chamber of clear liquid chamber 17 and filter core 4; Be positioned on the housing 1 dividing plate 2 below be connected to balance port valve 3, the height of balance port valve 3 is between the top of filter core 4 below the dividing plate 2.
During backwash, earlier emit the turbid liquid that is positioned at balance port valve 3 tops by balance port valve 3, open atmospheric valve 10 simultaneously, make turbid liquid liquid level highly consistent with balance port valve 3, the filter core major part is immersed in the turbid liquid, dirt discharging valve 5, atmospheric valve 10, blowoff valve 6 all is in closed condition, in housing 1, be blown into gas by blow-back valve 11, gas is introduced into clear liquid chamber 17, enter filter core inner chamber bottom along core pipe 15 again, gas oppositely passes the cake layer in the filter core layer and the filter core outside under pressure, enter turbid sap cavity 18, the bubble disturbance liquid of floating upward quickly produces flow-disturbing then, and the motive force of flow-disturbing forces filter cake to break away from filter core, gas self-balancing mouth valve 3 behind the flow-disturbing drains into outside the housing, and last all filter cake impurity is discharged from blowoff valve.
Filter washing water inlet valve 9 is installed above housing 1, during blowback, also can utilizes this valve in housing 1, to charge into cleaning fluid, utilize cleaning fluid to produce flow-disturbing and carry out the blowback cleaning.
Claims (1)
1. one kind makes filter core backwash clapboard type filter completely, comprise housing (1), in housing (1) inboard dividing plate (2) is arranged, the clear liquid chamber (17) of dividing plate (2) top is connected with purified liquor outlet valve (8), blow-back valve (11), atmospheric valve (10) respectively, the turbid sap cavity (18) of dividing plate (2) below is connected with turbid liquid inlet valve (7), blowoff valve (6), dirt discharging valve (5) respectively, the a plurality of filter cores (4) that are positioned at turbid sap cavity (18) are installed on dividing plate (2), and clear liquid chamber (17) are connected by filter core (4) with turbid sap cavity (18); It is characterized in that: the inboard of described filter core (4) is provided with core pipe (15), the lower end of core pipe (15) is positioned at the inner chamber bottom of filter core (4), form gap (12) between the inwall of the outside of core pipe (15) and filter core (4), core pipe (15) is communicated with the inner chamber of clear liquid chamber (17) and filter core (4); Be connected to balance port valve (3) in the below of housing (1) upper spacer (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202151179U CN201735239U (en) | 2010-06-04 | 2010-06-04 | Separation plate type filter capable of realizing thorough reverse flushing of filter cores |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202151179U CN201735239U (en) | 2010-06-04 | 2010-06-04 | Separation plate type filter capable of realizing thorough reverse flushing of filter cores |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201735239U true CN201735239U (en) | 2011-02-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202151179U Expired - Fee Related CN201735239U (en) | 2010-06-04 | 2010-06-04 | Separation plate type filter capable of realizing thorough reverse flushing of filter cores |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201735239U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102274650A (en) * | 2011-07-26 | 2011-12-14 | 合肥三番水处理设备有限公司 | Highly-integrated hollow fiber column filter |
| CN107469427A (en) * | 2017-09-22 | 2017-12-15 | 上海炼升化工股份有限公司 | A kind of filter plant and its operating method |
| CN107626132A (en) * | 2017-10-24 | 2018-01-26 | 王家骐 | The high-performance back purge system of beam tube type filter |
| CN108905342A (en) * | 2018-09-30 | 2018-11-30 | 陕西燎原净化设备有限公司 | A kind of filter core self-cleaning filter device |
| CN109420373A (en) * | 2017-08-28 | 2019-03-05 | 北京奥博水处理有限责任公司 | Self-cleaning filter |
| CN113599882A (en) * | 2021-09-08 | 2021-11-05 | 安泰环境工程技术有限公司 | Filtering device and filtering method for reducing nuclear power filtering solid waste amount |
-
2010
- 2010-06-04 CN CN2010202151179U patent/CN201735239U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102274650A (en) * | 2011-07-26 | 2011-12-14 | 合肥三番水处理设备有限公司 | Highly-integrated hollow fiber column filter |
| CN109420373A (en) * | 2017-08-28 | 2019-03-05 | 北京奥博水处理有限责任公司 | Self-cleaning filter |
| CN107469427A (en) * | 2017-09-22 | 2017-12-15 | 上海炼升化工股份有限公司 | A kind of filter plant and its operating method |
| CN107626132A (en) * | 2017-10-24 | 2018-01-26 | 王家骐 | The high-performance back purge system of beam tube type filter |
| CN108905342A (en) * | 2018-09-30 | 2018-11-30 | 陕西燎原净化设备有限公司 | A kind of filter core self-cleaning filter device |
| CN113599882A (en) * | 2021-09-08 | 2021-11-05 | 安泰环境工程技术有限公司 | Filtering device and filtering method for reducing nuclear power filtering solid waste amount |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: SHAANXI CHUANGLIAN INDUSTRY TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: XING ZHAOJIE Effective date: 20150310 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 116000 DALIAN, LIAONING PROVINCE TO: 710075 XI'AN, SHAANXI PROVINCE |
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| TR01 | Transfer of patent right |
Effective date of registration: 20150310 Address after: 710075 Shaanxi city of Xi'an province high tech Zone Tang Yan Lu Nan Duan Tong Da International Building 1 Building 1 unit 11705 room Patentee after: SHAANXI CHUANGLIAN INDUSTRIAL TECHNOLOGY CO., LTD. Address before: 116000, No. 7, building three, unit 6H, Welcome Road, Ganjingzi District, Liaoning, Dalian, China Patentee before: Xing Zhaojie |
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| DD01 | Delivery of document by public notice |
Addressee: SHAANXI CHUANGLIAN INDUSTRIAL TECHNOLOGY CO., LTD. Document name: Notification to Pay the Fees |
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| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: SHAANXI CHUANGLIAN INDUSTRIAL TECHNOLOGY CO., LTD. Document name: Notification of Termination of Patent Right |
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| DD01 | Delivery of document by public notice | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110209 Termination date: 20170604 |
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| CF01 | Termination of patent right due to non-payment of annual fee |