CN201537461U - Reverse osmosis type high viscosity liquid filter - Google Patents
Reverse osmosis type high viscosity liquid filter Download PDFInfo
- Publication number
- CN201537461U CN201537461U CN200920220534XU CN200920220534U CN201537461U CN 201537461 U CN201537461 U CN 201537461U CN 200920220534X U CN200920220534X U CN 200920220534XU CN 200920220534 U CN200920220534 U CN 200920220534U CN 201537461 U CN201537461 U CN 201537461U
- Authority
- CN
- China
- Prior art keywords
- viscosity liquid
- bucket
- reverse osmosis
- gauze
- type high
- 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
Links
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a reverse osmosis type high viscosity liquid filter comprising an inner wall barrel, an outer wall barrel, a steel mesh, a gauze, an induction tube and a delivery tube, wherein the steel mesh and the gauze are arranged outside the inner wall barrel; the delivery tube is inserted in the inner wall barrel from the top; the induction tube is arranged at the bottom of the outer wall barrel; and the induction tube is connected with a power source for guiding the high viscosity liquid into the outer wall barrel. By using the reverse osmosis type high viscosity liquid filter, the filtration is fast and complete, the gauze can be replaced quickly, the production efficiency is improved, and a reactor kettle equipment production platform can also be lowered, thus saving equipment cost and labor cost and reducing labor intensity.
Description
Technical field
The utility model relates to the high viscosity liquid filtration art, relates in particular to a kind of reverse osmosis type high-viscosity liquid filter.
Background technology
In the high viscosity liquid production process, need filter high viscosity liquid, to improve the performance of product, therefore filter need be set.
The structural representation of the high-viscosity liquid filter of prior art as shown in Figure 1, comprise: inwall bucket (stainless steel plate mesh) 11, outer wall bucket 14, gauze 13, ingress pipe 16 and delivery line 15, gauze 13 is arranged on inwall bucket 11 inboards, delivery line 15 is arranged on the bottom of outer wall bucket 14, and ingress pipe 16 is arranged on the top of inwall bucket 11.
When using the filter filtration adhesive of this structure, concrete production procedure is: gauze 13 is enclosed within 11 li in stainless steel inwall bucket, then inwall bucket 11 is packed into 14 li in outer wall bucket, and fixing with strainer cover 17.Adhesive flows into inwall bucket 11 by ingress pipe 16, filters through the punching second layer on the filtration of gauze ground floor, the inwall bucket, flows in the outer wall bucket 14, flows out through delivery line 15 then.
The filtered version of this but " from top to bottom ", " from the inside to surface " exists following problem:
1, filtration residue is stayed in the gauze, results in blockage easily, causes filtration insufficient, and the rate of filtration is slow;
2, need to change the gauze that a large amount of residues are housed after filtering, but gauze is easy to and the adhesion of inwall bucket, causes changing difficulty;
3, owing to filter slowly, the requirement height to reactor device fabrication platform has increased production cost.
4, whole filter need be placed certain altitude, derive bonding agent to make things convenient for delivery line.
The utility model content
In view of the problems referred to above of prior art, the purpose of this utility model provide a kind of filtration rapidly, change gauze reverse osmosis type high-viscosity liquid filter easily.
To achieve these goals, the utility model provides a kind of reverse osmosis type high-viscosity liquid filter, comprise inwall bucket, outer wall bucket, steel wire, gauze, ingress pipe and delivery line, it is characterized in that, described gauze is arranged on the outside of described inwall bucket, described delivery line inserts the described inwall bucket from the top, and described ingress pipe is arranged on the bottom of described outer wall bucket, is connected with on the described ingress pipe high viscosity liquid is imported power source in the described outer wall bucket.
As preferably, described steel wire, inwall bucket and outer wall bucket are stainless steel.
As preferably, described power source is for inhaling membrane pump.
As preferably, the outer wall of described inwall bucket is arranged with steel wire, and described gauze net cover is located on the described steel wire.
As preferably, described steel wire is two-layer.
The beneficial effects of the utility model are:
1, the osmosis filtration form of use " from top to bottom ", " from outside to inside ", filtration residue is blocked in outside the gauze, and difficult the obstruction makes filtration rapid and abundant, improved production efficiency.
2, gauze is arranged on the inwall bucket outside, and between gauze and inwall bucket steel wire is set, and makes gauze and inwall bucket can not stick together, and filters fully rapidly.
3, join this filter, can reduce reactor device fabrication platform, thereby save equipment cost and reduce labour intensity, save labour cost.
Description of drawings
Fig. 1 is the structural representation of the high-viscosity liquid filter of prior art.
Fig. 2 is the structural representation of the embodiment of reverse osmosis type high-viscosity liquid filter of the present utility model.
Fig. 3 is that the position of inwall bucket, outer wall bucket, gauze and steel wire among Fig. 2 concerns decomposing schematic representation.
The specific embodiment
Describe embodiment of the present utility model in detail below in conjunction with accompanying drawing.
The position of the inwall bucket among the structural representation of the embodiment of reverse osmosis type high-viscosity liquid filter of the present utility model as shown in Figure 2 and Fig. 2 shown in Figure 3, outer wall bucket, gauze and steel wire concerns decomposing schematic representation, and reverse osmosis type high-viscosity liquid filter comprises:
Wherein, steel wire 12, inwall bucket 11 and outer wall bucket 14 are stainless steel, and power source 18 can be to inhale membrane pump.
Convenient in order to make gauze 13 change, the outer wall of inwall tube 11 sheathed two-layer steel wire 12, the number of plies of steel wire 12 can be chosen as required.
Be the course of work (other similar high viscosity liquid filter process is identical with the adhesive filter process) that reverse osmosis type high-viscosity liquid filter is used in the example explanation below with the adhesive:
Gauze net cover is located on the steel wire 12, then inwall bucket 11 is packed into 14 li in outer wall bucket, and fixing with strainer cover 17.Adhesive will be drawn in the outer wall bucket 14 by power source 18 through ingress pipe 16, arrive in the inwall bucket 11 through the punching on gauze 13, steel wire 12, the inwall bucket 11, and delivery line 15 is extracted adhesive out.Thereby make adhesive enter from the below, extract out the top.
For easy to use, reverse osmosis type high-viscosity liquid filter can be arranged on the dolly 10, be convenient to move and use.
" from top to bottom " of this reverse osmosis type, the filtered version of " from outside to inside " have following benefit:
1, the osmosis filtration form of use " from top to bottom ", " from outside to inside ", filtration residue is blocked in outside the gauze, and difficult the obstruction makes filtration rapid and abundant, improved production efficiency.
2, gauze is arranged on the inwall bucket outside, and between gauze and inwall bucket steel wire is set, and makes that gauze and inwall bucket are more ventilative, and it is fully filtered.
3, owing to filter rapidly, can reduce reactor device fabrication platform, thereby save equipment cost and reduce labour intensity, save labour cost.
Above embodiment is an exemplary embodiment of the present utility model only, is not used in restriction the utility model, and protection domain of the present utility model is defined by the claims.Those skilled in the art can make various modifications or be equal to replacement the utility model in essence of the present utility model and protection domain, this modification or be equal to replacement and also should be considered as dropping in the protection domain of the present utility model.
Claims (6)
1. reverse osmosis type high-viscosity liquid filter, comprise inwall bucket, outer wall bucket, steel wire, gauze, ingress pipe and delivery line, it is characterized in that, described steel wire, gauze are arranged on the outside of described inwall bucket, described delivery line inserts the described inwall bucket from the top, described ingress pipe is arranged on the bottom of described outer wall bucket, is connected with on the described ingress pipe high viscosity liquid is imported power source in the described outer wall bucket.
2. reverse osmosis type high-viscosity liquid filter according to claim 1 is characterized in that, described steel wire, inwall bucket and outer wall bucket are stainless steel.
3. reverse osmosis type high-viscosity liquid filter according to claim 1 is characterized in that, described power source is for inhaling membrane pump.
4. reverse osmosis type high-viscosity liquid filter according to claim 1 is characterized in that the outer wall of described inwall bucket is arranged with steel wire, and described gauze net cover is located on the described steel wire.
5. reverse osmosis type high-viscosity liquid filter according to claim 1 is characterized in that, described steel wire is two-layer.
6. reverse osmosis type high-viscosity liquid filter according to claim 1 is characterized in that, described high viscosity liquid goes out on advancing under in filter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200920220534XU CN201537461U (en) | 2009-10-30 | 2009-10-30 | Reverse osmosis type high viscosity liquid filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200920220534XU CN201537461U (en) | 2009-10-30 | 2009-10-30 | Reverse osmosis type high viscosity liquid filter |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201537461U true CN201537461U (en) | 2010-08-04 |
Family
ID=42588912
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN200920220534XU Expired - Lifetime CN201537461U (en) | 2009-10-30 | 2009-10-30 | Reverse osmosis type high viscosity liquid filter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201537461U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105026019A (en) * | 2012-11-16 | 2015-11-04 | Oasys水有限公司 | Draw solutions and draw solute recovery for osmotically driven membrane processes |
-
2009
- 2009-10-30 CN CN200920220534XU patent/CN201537461U/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105026019A (en) * | 2012-11-16 | 2015-11-04 | Oasys水有限公司 | Draw solutions and draw solute recovery for osmotically driven membrane processes |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107758891A (en) | A kind of purifier with sewage pre-treatment device | |
CN205684416U (en) | A kind of Chinese medicine circulation cleaning washing trough | |
CN202700276U (en) | Drawer type activated carbon filter | |
CN201537461U (en) | Reverse osmosis type high viscosity liquid filter | |
CN205613080U (en) | Draw tank bottoms side combination filter equipment | |
CN101797478B (en) | Reverse osmosis type high-viscosity liquid filter | |
CN201603422U (en) | Compressed air recoiling device of multifunctional extraction tank | |
CN204675906U (en) | A kind of oily-water seperating equipment of catering trade | |
CN203874561U (en) | Back-washing filter system | |
CN205683635U (en) | A kind of biological extraction liquid defecator | |
CN207654759U (en) | A kind of drainage type oil water separator | |
CN202829733U (en) | Water purifier | |
CN204745843U (en) | Kinetic energy back flush filter | |
CN207886773U (en) | A kind of water circulating filter processing unit | |
CN204058088U (en) | Simple sewage strumbox device | |
CN208362030U (en) | A kind of domestic sewage purification device | |
CN209092803U (en) | A kind of oily-water seperating equipment of restaurant's kitchen waste water | |
CN202968280U (en) | Sewage treatment pool | |
CN207886805U (en) | Novel extraction filter device | |
CN201427011Y (en) | Liquid purification structure | |
CN206255912U (en) | Biological pulsation pond is used in a kind of low energy consumption, high-efficiency sewage treatment | |
CN201008771Y (en) | Centrifugal-type, net-type integrated water-sand segregator | |
CN201596466U (en) | Reverse osmosis type high-viscosity fluid ultrafilter | |
CN103951011A (en) | Glass fiber reinforced plastic integrated oil-water separation device for dining kitchen waste water | |
CN203625156U (en) | Sewage treatment equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20100804 Effective date of abandoning: 20091030 |