CN201894882U - Continuous material washing device - Google Patents
Continuous material washing device Download PDFInfo
- Publication number
- CN201894882U CN201894882U CN 201020603953 CN201020603953U CN201894882U CN 201894882 U CN201894882 U CN 201894882U CN 201020603953 CN201020603953 CN 201020603953 CN 201020603953 U CN201020603953 U CN 201020603953U CN 201894882 U CN201894882 U CN 201894882U
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- Prior art keywords
- kettle
- continuous washing
- washing device
- material continuous
- filter core
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Abstract
A continuous material washing device comprises a kettle, a stirring mechanism and a metal filter element. A material inlet is arranged on the upper portion of the kettle, a material outlet is disposed on the lower portion of the kettle, the stirring mechanism consists of a transmission device and a stirring blade, the stirring blade extends into the kettle, one end of the metal filter element extends to the lower side of an inner liquid surface of the kettle, the other end of the metal filter element is connected with a vacuum buffer tank via a pipeline, and the vacuum buffer tank is connected with a vacuum system. The continuous material washing device realizes continuous completion of filtering and washing, is simple in structure, convenient in operation and maintenance and low in labor intensity, basically avoids material loss, and more effectively solves problems in an existing washing method.
Description
Technical field
The utility model relates to the material filtering washing facility, particularly is used for a kind of material continuous washing device of fine granular materials filtration washing.
Background technology
At present, that the fine granular materials filtration washing mainly adopts is centrifugal, mode of washing is realized, shortcoming such as this method exists labour intensity big, and loss of material is serious.
Chinese patent 200720090834.1 discloses a kind of fine granular materials filtration washing dewatering drying device.This device is provided with the subfeeder that is communicated with water main on the sheet frame of filter one side, the inboard is laid with a plurality of limbers around the sheet frame, water main be parallel with set up give tracheae and steam pipe, the sheet frame of filter opposite side is provided with branch drain, and be communicated with two main sewers respectively at interval, be parallel with vacuum tube on one of them main sewer, be provided with the feed arm that is communicated with the feed house steward, be parallel with jet water spout on the feed house steward in isolation frame one side.
Chinese patent CN201105183 discloses a kind of horizontal ultrafine powder filtering, washing and drying press integrated machine.This equipment comprises cylindrical shell, be arranged on the top filter mechanism in the cylindrical shell and the charging aperture that is complementary, top filtrate (liquid, bottom filtrate (liquid, drain, spray liquid import, cylindrical shell crouches to put and is arranged on the guide rail, move with guide rail and to cooperate, end in the relative cartridge openings of guide rail fixedly installs a tubular body frame, in the body frame, be provided with rotating bottom filter, the bottom filter is communicated with bottom filtrate (liquid on being arranged on the body frame, cylindrical shell and body frame are sealed and matched by clip mechanism, the bottom filter place the top filter mechanism below.
Chinese patent CN201399285 discloses a kind of filtration washing two-in-one device that is applicable to the extraction recovery of crystal in the medication chemistry industry, it comprises storage tank, filter, receive crystalline cone, be provided with inlet at the storage tank top, the air inlet that is provided with at the storage tank sidewall, be provided with leakage fluid dram in the storage tank bottom, the leakage fluid dram of described storage tank is connected by the filter of branch line and storage tank lower end, the filter wall lower end is provided with liquid outlet, the filter wall upper end is provided with back blow port, a through type tubular porous filter elements is housed in the filter, and the filter admission chamber is connected with the sap cavity that goes out of filter by the capillary micropore on the tubular porous filter elements barrel.
Chinese patent CN201020296 discloses the crystal filtration washing device of a kind of totally-enclosed, the filtration that can finish the crystallization suspension simultaneously, washing, and it is applied to the isolated by filtration of crystallization suspension in the chemical field and the washing of gained crystal product.It mainly is made up of conical end socket, cylinder, cover plate, bearing support, feed pipe, clear water inlet tube, mother liquor overflow pipe, wash water inlet tube, filtrate exit pipe, vomit pipe, compressed air inlet pipe, cleaning eye, filter screen mechanism, agitator, agitator, shaft, seal box, shaft joint, frame, reductor, top manhole, side manhole, support pad seat, angle ring, base bearing etc.
Mainly there are following some shortcomings in above-mentioned existing filter washing equipment: complex structure, and inconvenient operation, material loss is many, the plant maintenance difficulty.
Summary of the invention
The purpose of this utility model provides a kind of material continuous washing device, realizes filtering cleaning and finishes continuously, and simple in structure, easy to operate, easy to maintenance, material is lossless substantially, and labour intensity is little, has better solved in the existing washing to go wrong.
For achieving the above object, the technical solution of the utility model is:
A kind of material continuous washing device, it comprises, kettle, its top is provided with material inlet, and the bottom is provided with material outlet; Rabbling mechanism comprises transmission device and stirrer paddle, and stirrer paddle stretches in the kettle; Metal filtration filter core, one end stretch under the interior liquid level of kettle, and an other end connects a vacuum buffer tank by pipeline, and this vacuum buffer tank connects a vacuum system.
Further, described metal filtration filter core stretches into from the kettle top, or stretches into from the kettle side, or stretches into from autoclave body bottom.
Described metal filtration filter element filtering grade is 1～1000 μ m.
Again, the utility model is also established a blowback pipeline that connects Compressed Gas and is connected in described metal filtration filter core.
Described kettle is selected strap clamp cover or strap clamp cover kettle not for use according to different service conditions.
Described stirrer paddle is oar formula or turbine open-type or disc turbine formula.
In addition, described transmission device has speed adjusting gear.
Described transmission device is a motor.
Described metal filtration filter core adopts the metal sintering pipe.
A pressure pipeline that is connected with Compressed Gas is also inserted on described kettle top.
Material enters in the still from the kettle import, be issued at stirring action and mix, realize of the filtration of metal filtration filter core by vacuum system or supercharging (pressurization) system to material, filtrate is discharged from the filter core mouth, waits after liquid acquires a certain degree in the still, stops to filter, in kettle, add the washing medium, carry out stirring and washing, repeated multiple times is gone centrifugal or drying equipment after making final material reach requirement.
Simultaneously, the metal filtration filter core is provided with blowback system, and blowback filter core under the bad situation of filter effect improves and filters.
The utility model compared with prior art has the following advantages:
1. the utility model kettle was established the metal filtration filter core, realized filtering, cleaned and finish continuously.
2. long service life.Owing to adopted the metal filtration filter core, be convenient to clean and blowback, repeatedly repeated regeneration increases the washing still service life greatly.
3. commutativity is good, maintenance cost is low.Metal filtration filter core of the present utility model is interchangeable element independently, and manufacturing cost is lower, replacing is convenient.
4. applicability is wide.According to selecting for use of filter core grade, the washing still all is suitable for from micron order to millimetre-sized washing material particle diameter.
5. serviceability temperature height.Because what adopt is the metal filtration filter core, improved serviceability temperature.
6. strainability is good.Because of making cartridge surface be not easy to produce particle packing bridging phenomenon under the stirring action, simultaneously filter core also there is souring, strainability is improved greatly.
Description of drawings
Fig. 1 is the structural representation of the utility model one embodiment.
The specific embodiment
Referring to Fig. 1, a kind of material continuous washing of the utility model device, it comprises, kettle 1, its top is provided with material inlet 11, inlet for pressurised gas 12, and the bottom is provided with material outlet 13; Rabbling mechanism 2 comprises transmission device 21 and stirrer paddle 22, and stirrer paddle 22 stretches in the kettle 1; Under metal filtration filter core 3, one end filter end stretched into liquid level in the kettle 1 from autoclave body bottom, an other end connected a vacuum buffer tank 4 by pipeline, and this vacuum buffer tank 4 connects a vacuum system 5.
Described metal filtration filter core stretches into from the kettle top, or stretches into from the kettle side, or stretches into from autoclave body bottom.In the present embodiment, under metal filtration filter element filtering end stretches into liquid level in the kettle 1 from autoclave body bottom.Metal filtration filter element filtering grade is 1～1000 μ m.Described metal filtration filter core adopts the metal sintering pipe.
Again, the utility model is also established a blowback pipeline 6 that connects Compressed Gas by the flange described metal filtration filter core that is threaded.
Described kettle is selected strap clamp cover or strap clamp cover kettle not for use according to different service conditions.
Described stirrer paddle is oar formula or turbine open-type or disc turbine formula.
In addition, described transmission device has speed adjusting gear, and in the present embodiment, described transmission device is a motor.
Material enters in the still from material inlet, running is stirred, after reaching even mixing, filter by the metal filtration filter core in autoclave body bottom extend into kettle, undertaken the filter core pulse cleaning by the filter core blowback system when the filter core filtration resistance increases, another road is connected with vacuum buffer tank and is connected realization filtrate with vacuum system discharges.
Can insert the pressure pipeline that is connected with Compressed Gas at kettle top inlet for pressurised gas simultaneously as required during filtration and carry out supercharging, add strong filter.After the filtration, add washing medium and wash, the repeated multiple times washing, requirement touches the mark.
Claims (10)
1. a material continuous washing device is characterized in that, comprise,
Kettle, its top is provided with material inlet, and the bottom is provided with material outlet;
Rabbling mechanism comprises transmission device and stirrer paddle, and stirrer paddle stretches in the kettle;
Metal filtration filter core, one end stretch under the interior liquid level of kettle, and an other end connects a vacuum buffer tank by pipeline, and this vacuum buffer tank connects a vacuum system.
2. material continuous washing device as claimed in claim 1 is characterized in that described metal filtration filter core stretches into from the kettle top, or stretches into from the kettle side, or stretches into from autoclave body bottom.
3. material continuous washing device as claimed in claim 1 or 2 is characterized in that, described filter core filtration grade is 1～1000 μ m.
4. material continuous washing device as claimed in claim 1 or 2 is characterized in that, also establishes a blowback pipeline that connects Compressed Gas and is connected in described metal filtration filter core.
5. material continuous washing device as claimed in claim 1 is characterized in that, described kettle is strap clamp cover or strap clamp cover kettle not.
6. material continuous washing device as claimed in claim 1 is characterized in that, described stirrer paddle is oar formula or turbine open-type or disc turbine formula.
7. material continuous washing device as claimed in claim 1 is characterized in that described transmission device has speed adjusting gear.
8. as claim 1 or 7 described material continuous washing devices, it is characterized in that described transmission device is a motor.
9. material continuous washing device as claimed in claim 1 or 2 is characterized in that, described metal filtration filter core adopts the metal sintering pipe.
10. as claim 1 or 5 described material continuous washing devices, it is characterized in that a pressure pipeline that is connected with Compressed Gas is also inserted on described kettle top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020603953 CN201894882U (en) | 2010-11-12 | 2010-11-12 | Continuous material washing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020603953 CN201894882U (en) | 2010-11-12 | 2010-11-12 | Continuous material washing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201894882U true CN201894882U (en) | 2011-07-13 |
Family
ID=44252801
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201020603953 Expired - Fee Related CN201894882U (en) | 2010-11-12 | 2010-11-12 | Continuous material washing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201894882U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104128151A (en) * | 2014-07-31 | 2014-11-05 | 贵州远盛钾业科技有限公司 | Neutralization reaction kettle |
| CN104857752A (en) * | 2015-05-23 | 2015-08-26 | 施婷婷 | Rapid pressure filtering device for propolis |
| CN111498521A (en) * | 2020-04-22 | 2020-08-07 | 上海森松制药设备工程有限公司 | Self-cleaning type powder feeding machine |
| CN113082809A (en) * | 2021-04-09 | 2021-07-09 | 东方电气集团科学技术研究院有限公司 | Bubbling stirring type nano powder cleaning and filtering device and method |
| CN114917676A (en) * | 2022-05-17 | 2022-08-19 | 恒丰泰精密机械股份有限公司 | A two unification agitated vessel of filtration washing for preparing lithium cell cathode material |
-
2010
- 2010-11-12 CN CN 201020603953 patent/CN201894882U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104128151A (en) * | 2014-07-31 | 2014-11-05 | 贵州远盛钾业科技有限公司 | Neutralization reaction kettle |
| CN104128151B (en) * | 2014-07-31 | 2016-05-04 | 贵州远盛钾业科技有限公司 | A kind of neutralization reaction still |
| CN104857752A (en) * | 2015-05-23 | 2015-08-26 | 施婷婷 | Rapid pressure filtering device for propolis |
| CN111498521A (en) * | 2020-04-22 | 2020-08-07 | 上海森松制药设备工程有限公司 | Self-cleaning type powder feeding machine |
| CN113082809A (en) * | 2021-04-09 | 2021-07-09 | 东方电气集团科学技术研究院有限公司 | Bubbling stirring type nano powder cleaning and filtering device and method |
| CN114917676A (en) * | 2022-05-17 | 2022-08-19 | 恒丰泰精密机械股份有限公司 | A two unification agitated vessel of filtration washing for preparing lithium cell cathode material |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110713 Termination date: 20111112 |