CN203803227U - Novel diatomite membrane coating filtering device - Google Patents
Novel diatomite membrane coating filtering device Download PDFInfo
- Publication number
- CN203803227U CN203803227U CN201420172706.1U CN201420172706U CN203803227U CN 203803227 U CN203803227 U CN 203803227U CN 201420172706 U CN201420172706 U CN 201420172706U CN 203803227 U CN203803227 U CN 203803227U
- Authority
- CN
- China
- Prior art keywords
- pipeline
- filter
- valve
- diatomite
- agitator tank
- 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 - Lifetime
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 239000012528 membrane Substances 0.000 title claims abstract description 13
- 238000001914 filtration Methods 0.000 title claims abstract description 11
- 239000011248 coating agent Substances 0.000 title abstract 3
- 238000000576 coating method Methods 0.000 title abstract 3
- 239000007788 liquid Substances 0.000 claims abstract description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 17
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000005406 washing Methods 0.000 claims description 20
- 229910000831 Steel Inorganic materials 0.000 claims description 14
- 239000010959 steel Substances 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 10
- 239000000706 filtrate Substances 0.000 claims description 8
- 230000008676 import Effects 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000003792 electrolyte Substances 0.000 description 14
- 238000000034 method Methods 0.000 description 7
- 238000005457 optimization Methods 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 239000011889 copper foil Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002362 mulch Substances 0.000 description 3
- 239000002985 plastic film Substances 0.000 description 3
- 229920006255 plastic film Polymers 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000008092 positive effect Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a novel diatomite membrane coating filtering device. The novel diatomite membrane coating filtering device comprises a filter, an agitating tank, a tail liquid groove, a pure liquid tank, a liquid supply pump A and a liquid supply pump B, wherein a water inlet of the filter is led out through a pipeline and then is divided into a first pipeline and a second pipeline; the first pipeline is connected with an outlet of the tail liquid groove through the liquid supply pump A; the second pipeline is connected with the outlet of the agitating tank through the liquid supply pump B; a middle water outlet of the filter is connected with an inlet of the agitating tank through a third pipeline; the water outlet of the filter is led out through a pipeline and then is divided into three paths including a fourth pipeline, a fifth pipeline and a sixth pipeline; the fourth pipeline is provided with a fourth valve and is connected with the inlet of the tail liquid groove; the fifth pipeline is provided with a fifth valve and is connected to the agitating tank; the sixth pipeline passes through a sixth valve and then is divided into a seventh pipeline and an eighth pipeline; the seventh pipeline is connected with the inlet of the pure liquid groove; the eighth pipeline is connected to the inlet of the tail liquid groove; diatomite and active carbon are agitated by the agitating tank to form a filtering membrane to filter liquid in the tail liquid groove.
Description
Technical field
The utility model relates to diatomite filtration technical field, in particular a kind of novel diatomite overlay film filter.
Background technology
In electronics Copper Foil production process, need to use a large amount of electrolyte, and existing electrolyte filtering diatomite filtration system used, complex structure, overhead time is long, and labour intensity is large, complicated operation, normal appearance feeds in raw material unsuccessfully, and filter effect is undesirable.And active carbon is very good adsorbent, there are countless Small Holes gaps, surface area is huge, and growth has a large amount of microorganisms, and it has the double grading of physical absorption and chemisorbed.Diatomite particle granularity is less, and plastic film mulch is effective, but the loss of flood peak is large, so just makes the cycle of operation shorter.Therefore, be badly in need of a kind of active carbon and diatomite powder being mixed to form to filter membrane, liquid is filtered, both brought into play the advantage of diatomite as new type filter aid, also well made up the loss of flood peak large, the fast shortcoming that lost efficacy, after processing, liquid not only has positive effect on turbidity, in removing liquid, aspect organic matter, also has positive effect.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, thus provide a kind of simple in structure, the operating time is short, labour intensity is little, can utilize diatomite and active carbon to carry out the novel diatomite overlay film filter that online plastic film mulch is filtered liquid such as electrolyte.
The utility model is achieved through the following technical solutions:
A kind of novel diatomite overlay film filter, comprise filter, also comprise agitator tank, tail washings groove, clean liquid bath, solution feed pump A, solution feed pump B, described agitator tank is used for stirring diatomite and active carbon, described filter is provided with water inlet, delivery port and middle delivery port, the water inlet of described filter is divided into the first pipeline and the second pipeline two-way after piping is drawn, the first pipeline is connected with the outlet of described tail washings groove by described solution feed pump A, described the first pipeline is provided with the first valve, the second pipeline is connected with the outlet of described agitator tank by described solution feed pump B, described the second pipeline is provided with the second valve, the middle delivery port of described filter is connected with the import of described agitator tank by the 3rd pipeline, and described the 3rd pipeline is provided with the 3rd valve, the delivery port of described filter is divided into the 4th pipeline after piping is drawn, the 5th pipeline and the 6th pipeline three tunnels, described the 4th pipeline is provided with the 4th valve and is connected with the entrance of described tail washings groove, described the 5th pipeline is provided with the 5th valve and is connected to described agitator tank, described the 6th pipeline is provided with the 6th valve as total valve, described the 6th pipeline is divided into again the 7th pipeline after described the 6th valve, the 8th pipeline two-way, described the 7th pipeline is provided with the 7th valve and is connected to the entrance of described clean liquid bath, described the 8th pipeline is provided with the 8th valve and is connected to the entrance of described tail washings groove, solution feed pump A, solution feed pump B and a plurality of valve all can independently be controlled, by solution feed pump B, the diatomite stirring through described agitator tank and active carbon are squeezed in described filter and formed filter membrane, thereby the liquid in described tail washings groove is filtered.
As the further optimization of technique scheme, described filter is plate frame filter.
Further optimization as technique scheme, the filtration fraction of described plate frame filter comprises multi-layer planar filter element, every layer of dull and stereotyped filter element comprises sheet frame, stainless (steel) wire, described sheet frame is that stainless steel sheet frame and its have surrounded the structure that profile is regular polygon, described sheet frame both sides are coated with stainless (steel) wire, the stainless (steel) wire of described sheet frame and its both sides has surrounded the space that holds diatomite and active carbon filter pulp, forms pie filter membrane, and the bottom of described sheet frame is provided with the filtrate drain pipe flowing out for filtrate.
As the further optimization of technique scheme, described sheet frame has surrounded the structure that profile is regular octagonal.
As the further optimization of technique scheme, described stainless (steel) wire is 400 orders.
As the further optimization of technique scheme, the top of described agitator tank is provided with stirring motor.
The utility model has the following advantages compared to existing technology:
1, the novel diatomite overlay film filter that the utility model provides, can utilize diatomite and active carbon to carry out online plastic film mulch and form dynamic filter membrane, thereby the liquid such as electrolyte are filtered, hold back thus suspended particle in filter liquide and other germs/bacteria etc., there is good drainage, adsorption effect, guaranteed the filter effect of the liquid such as electrolyte.
2, the novel diatomite overlay film filter that the utility model provides, power consumption is little, simple in structure, and price is low, and filter area is large, and proof pressure is high;
3, the novel diatomite overlay film filter that the utility model provides, simple to operate, avoided reinforced failed heavy industry.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is dull and stereotyped filter element side structure schematic diagram of the present utility model.
The specific embodiment
Below embodiment of the present utility model is elaborated; the present embodiment is implemented take technical solutions of the utility model under prerequisite; provided detailed embodiment and concrete operating process, but protection domain of the present utility model is not limited to following embodiment.
A novel diatomite overlay film filter, comprises filter 2, also comprises agitator tank 1, tail washings groove 3, clean liquid bath 4, solution feed pump A5, solution feed pump B6, and agitator tank 1 is for stirring diatomite and active carbon, and the top of agitator tank 1 is provided with stirring motor.Filter 2 is provided with water inlet, delivery port and middle delivery port, the water inlet of filter 2 is divided into the first pipeline 10 and the second pipeline 20 two-way after piping is drawn, the first pipeline 10 is connected with the outlet of tail washings groove 3 by solution feed pump A5, the first pipeline 10 is provided with the first valve 101, the second pipeline 20 is connected with the outlet of agitator tank 1 by solution feed pump B6, and the second pipeline 20 is provided with the second valve 201, the middle delivery port of filter 2 is connected with the import of agitator tank 1 by the 3rd pipeline 30, and the 3rd pipeline 30 is provided with the 3rd valve 301, the delivery port of filter 2 is divided into the 4th pipeline 40 after piping is drawn, the 5th pipeline 50 and the 6th pipeline 60San road, the 4th pipeline 40 is provided with the 4th valve 401 and is connected with the entrance of tail washings groove 3, the 5th pipeline 50 is provided with the 5th valve 501 and is connected to agitator tank 1, the 6th pipeline 60 is provided with the 6th valve 601 as total valve, the 6th pipeline 60 is divided into again the 7th pipeline 70 after the 6th valve 601, the 8th pipeline 80 two-way, the 7th pipeline 70 is provided with the 7th valve 701 and is connected to the entrance of clean liquid bath 4, the 8th pipeline 80 is provided with the 8th valve 801 and is connected to the entrance of tail washings groove 3, solution feed pump A5, solution feed pump B6 and a plurality of valve all can independently be controlled, by solution feed pump B6, the diatomite stirring through agitator tank 1 and active carbon are squeezed into the interior formation filter membrane of filter 2, thereby the liquid in tail washings groove 3 is filtered.
Referring to Fig. 2, filter 2 is plate frame filter.The filtration fraction of plate frame filter comprises multi-layer planar filter element 21, every layer of dull and stereotyped filter element 21 comprises sheet frame 211, stainless (steel) wire 212, sheet frame 211 has surrounded the structure that profile is regular polygon for stainless steel sheet frame and its, and this regular polygon structure can be the structure of regular octagonal.Sheet frame 211 both sides are coated with stainless (steel) wire 212, stainless (steel) wire is 400 orders, sheet frame 211 has surrounded with the stainless (steel) wire 212 of its both sides the space that holds diatomite and active carbon filter pulp, forms pie filter membrane, and the bottom of sheet frame 211 is provided with the filtrate drain pipe 213 flowing out for filtrate.
Before work starts, in this filter, all pumps and valve are all closed condition.During work, the liquid that needs are filtered packs tail washings groove 3 into, the present embodiment filters the electrolyte of using in electronics Copper Foil production process, electrolyte is packed in tail washings groove 3, first open on solution feed pump A5 on the first pipeline 10, the first valve 101, the 6th pipeline 60 as the 6th valve 601 of total valve and the 8th valve 801 on the 8th pipeline, make to form a circulation in tail washings groove 3 and filter 2, will in filter 2, fill with electrolyte.Then open the 3rd valve 301 on the 3rd pipeline 30, after the gas in filter 2 is discharged, electrolyte enters in agitator tank 1, closes the 3rd valve 301 when the liquid level of electrolyte reaches 2/3 position in agitator tank 1; Then when closing solution feed pump A5, the first valve 101 and the 6th valve 601, open the 5th valve 501 on solution feed pump B6, the second valve 201 and the 5th pipeline 50 on the second pipeline 20, so that filter 2 forms a circulation with agitator tank 1; Then different size diatomite is dropped in agitator tank 1 in order, open stirring motor in agitator tank 1 and carry out high-speed stirred, after diatomite is uniformly dispersed, open agitator tank 1 bottom valve, the point solution liquid suspending circulates in filter 2 and agitator tank 1, final clarification, illustrate that diatomite is adsorbed on the stainless (steel) wire 212 of multi-layer planar filter element 21 of filter 2 completely, sheet frame 211 has surrounded with the stainless (steel) wire 212 of its both sides the space that holds diatomite and active carbon filter pulp, form pie filter membrane, the bottom of sheet frame 211 is provided with the filtrate drain pipe 213 flowing out for filtrate.With diatomite adding method, equally in agitator tank 1, add active carbon, after electrolyte liquid clarification in agitator tank 1, when opening solution feed pump A5, the first valve 101 and the 6th valve 601, close solution feed pump B6, the second valve 201 and the 5th valve 501; Until electrolyte, at circulating filtration between tail washings groove 3 and filter 2, after 1 hour, open the 7th valve 701 on the 7th pipeline 70, close the 8th valve 801 on the 8th pipeline 80 simultaneously, make electrolyte after filter 2 filters, flow into clean liquid bath 4 from tail washings groove 3, then from clean liquid bath 4, electrolyte is provided to the raw paper tinsel operation of Copper Foil.The 4th valve 401 on the 4th pipeline 40 is that while changing diatomite and active carbon, discharge opeing is used.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all any modifications of doing within spirit of the present utility model and principle, be equal to and replace and improvement etc., within all should being included in protection domain of the present utility model.
Claims (6)
1. a novel diatomite overlay film filter, comprise filter, it is characterized in that: also comprise agitator tank, tail washings groove, clean liquid bath, solution feed pump A, solution feed pump B, described agitator tank is used for stirring diatomite and active carbon, described filter is provided with water inlet, delivery port and middle delivery port, the water inlet of described filter is divided into the first pipeline and the second pipeline two-way after piping is drawn, the first pipeline is connected with the outlet of described tail washings groove by described solution feed pump A, described the first pipeline is provided with the first valve, the second pipeline is connected with the outlet of described agitator tank by described solution feed pump B, described the second pipeline is provided with the second valve, the middle delivery port of described filter is connected with the import of described agitator tank by the 3rd pipeline, and described the 3rd pipeline is provided with the 3rd valve, the delivery port of described filter is divided into the 4th pipeline after piping is drawn, the 5th pipeline and the 6th pipeline three tunnels, described the 4th pipeline is provided with the 4th valve and is connected with the entrance of described tail washings groove, described the 5th pipeline is provided with the 5th valve and is connected to described agitator tank, described the 6th pipeline is provided with the 6th valve as total valve, described the 6th pipeline is divided into again the 7th pipeline after described the 6th valve, the 8th pipeline two-way, described the 7th pipeline is provided with the 7th valve and is connected to the entrance of described clean liquid bath, described the 8th pipeline is provided with the 8th valve and is connected to the entrance of described tail washings groove, solution feed pump A, solution feed pump B and a plurality of valve all can independently be controlled, by solution feed pump B, the diatomite stirring through described agitator tank and active carbon are squeezed in described filter and formed filter membrane, thereby the liquid in described tail washings groove is filtered.
2. a kind of novel diatomite overlay film filter as claimed in claim 1, is characterized in that: described filter is plate frame filter.
3. a kind of novel diatomite overlay film filter as claimed in claim 2, it is characterized in that: the filtration fraction of described plate frame filter comprises multi-layer planar filter element, every layer of dull and stereotyped filter element comprises sheet frame, stainless (steel) wire, described sheet frame is that stainless steel sheet frame and its have surrounded the structure that profile is regular polygon, described sheet frame both sides are coated with stainless (steel) wire, the stainless (steel) wire of described sheet frame and its both sides has surrounded the space that holds diatomite and active carbon filter pulp, form pie filter membrane, the bottom of described sheet frame is provided with the filtrate drain pipe flowing out for filtrate.
4. a kind of novel diatomite overlay film filter as claimed in claim 3, is characterized in that: described sheet frame has surrounded the structure that profile is regular octagonal.
5. a kind of novel diatomite overlay film filter as claimed in claim 4, is characterized in that: described stainless (steel) wire is 400 orders.
6. a kind of novel diatomite overlay film filter as claimed in claim 5, is characterized in that: the top of described agitator tank is provided with stirring motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420172706.1U CN203803227U (en) | 2014-04-10 | 2014-04-10 | Novel diatomite membrane coating filtering device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420172706.1U CN203803227U (en) | 2014-04-10 | 2014-04-10 | Novel diatomite membrane coating filtering device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203803227U true CN203803227U (en) | 2014-09-03 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420172706.1U Expired - Lifetime CN203803227U (en) | 2014-04-10 | 2014-04-10 | Novel diatomite membrane coating filtering device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203803227U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112657449A (en) * | 2019-10-15 | 2021-04-16 | 立邦涂料（中国）有限公司 | Continuous production method and equipment of aqueous electrophoretic resin |
-
2014
- 2014-04-10 CN CN201420172706.1U patent/CN203803227U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112657449A (en) * | 2019-10-15 | 2021-04-16 | 立邦涂料（中国）有限公司 | Continuous production method and equipment of aqueous electrophoretic resin |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 230001 Anhui city of Chizhou Province Economic and Technological Development Zone Qingxi road and road intersection and Patentee after: Anhui Tongguan copper foil Group Co.,Ltd. Address before: 230001 Anhui city of Chizhou Province Economic and Technological Development Zone Qingxi road and road intersection and Patentee before: ANHUI TONGGUAN COPPER FOIL Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140903 |