CN207102398U - Alkaline brine filter cellulose batch tank - Google Patents
Alkaline brine filter cellulose batch tank Download PDFInfo
- Publication number
- CN207102398U CN207102398U CN201720698468.1U CN201720698468U CN207102398U CN 207102398 U CN207102398 U CN 207102398U CN 201720698468 U CN201720698468 U CN 201720698468U CN 207102398 U CN207102398 U CN 207102398U
- Authority
- CN
- China
- Prior art keywords
- tank body
- cover
- tank
- rotating shaft
- stirring
- 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
Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Alkaline equipment technical field is the utility model is related to, especially a kind of alkaline brine filter cellulose batch tank.This alkaline brine filter cellulose batch tank, including base, base upper surface is provided with tank body, tank body top end cover is provided with cover, and brine inlet and cellulose feed mouth are provided with cover, and tank inner chamber center suspension is provided with rotating shaft, rotating shaft is connected with the motor that drive shaft rotates after stretching out cover, stirring frame is installed, stirring inframe is placed in tank body, stirs and be equipped with some horizontally disposed stirring vanes on two vertical sides of frame in rotating shaft;Discharging opening for the discharging of suspension finished product is installed in the middle part of tank wall.The utility model is simple in construction, it is reasonable in design, raw material enters tank body from brine inlet and cellulose feed mouth respectively, motor-driven rotatable shaft rotates, stir frame to rotate, so as to drive dihedral vane and stirring vane to rotate, the material of tank inner chamber is stirred, suspension finished product is discharged from discharging opening, and whipping performance is good.
Description
Technical field
It the utility model is related to alkaline equipment technical field, especially a kind of alkaline salt for ionic membrane hair manufacture caustic soda
Water filtration cellulose batch tank.
Background technology
Caustic soda is a kind of important chlorine-alkali product, is mainly used as Principles of Chemical Engineering, is widely used in papermaking, spins and make fiber, fertilizer
The field such as soap and detergent, aluminium metallurgy, glass, rubber, plastics, agricultural chemicals, medicine and petroleum refining, occupies important in national economy
Status.Process of caustic soda typically uses ion diaphragm electrolysis, and electrolysis is to carry out the journey to chemically react by means of direct current, when straight
When stream passes through common salt aqueous solution in electrolytic cell, chlorine is produced on anode, hydrogen is produced in solid iron cathode.Ionic membrane method burns
Alkali technique has energy consumption, good product quality, and floor space is small, and automaticity is high, the advantage such as clean environment firendly.In salt solution secondary fine
In system, the suspension in primary brine returns to chelate resin tower produces harmful effect, and quite a few in suspension is that do not have
There is the complete CaCO of sedimentation3、Mg(OH)2、BaSO4Molecule, it is necessary to be filtered to these molecules, traditional mistake
Filter complicated, poor filtration effect.Generally use carbon pipe filter filters to primary brine, and carbon pipe filter needs to coordinate
Cellulose batch tank uses, and traditional cellulose batch tank is complicated, and mixing effect is poor.
Utility model content
The technical problems to be solved in the utility model is:A kind of overcome the deficiencies in the prior art, there is provided alkaline brine filter
With cellulose batch tank.
Technical scheme is used by the utility model solves its technical problem:A kind of alkaline brine filter is matched somebody with somebody with cellulose
Put tank, including base, base upper surface is provided with tank body, and tank body top end cover is provided with cover, be provided with cover brine inlet and
Cellulose feed mouth, the tank inner chamber center suspension are provided with rotating shaft, and rotating shaft is connected with drive shaft rotation after stretching out cover
Motor, stirring frame is provided with rotating shaft, and stirring inframe is placed in tank body, stirs and be equipped with some levels on two vertical sides of frame
The stirring vane of setting;Discharging opening for the discharging of suspension finished product is installed in the middle part of the tank wall.
Further, described stirring four drift angles of frame are mounted on the dihedral vane to external radiation, dihedral vane center
Angle between axle and horizontal line is 45 °.Provided with dihedral vane, tank body corner material can be stirred, improve stirring property
Energy.
Further, described motor output end is provided with reductor, and output end of reducer is connected with rotating shaft, can install
Production requirement sets mixing speed.
Further, described motor is arranged on cover by electric machine support.
Further, described inner tank wall is provided with helical form flow guide bar, improves whipping performance.
The beneficial effects of the utility model are:The utility model is simple in construction, reasonable in design, and raw material is respectively from brine inlet
Enter tank body with cellulose feed mouth, motor-driven rotatable shaft rotates, and stirring frame rotates, so as to drive dihedral vane and stirring vane
Rotate, the material of tank inner chamber is stirred, suspension finished product is discharged from discharging opening, and whipping performance is good.
Brief description of the drawings
The utility model is further illustrated below in conjunction with the accompanying drawings.
Fig. 1 is structural representation of the present utility model.
1. tank body in figure, 2. dihedral vanes, 3. brine inlets, 4. cellulose feed mouths, 5. stirring frames, 6. discharging openings, 7.
Stirring vane, 8. bases, 9. rotating shafts, 10. reductors, 11. motors, 12. electric machine supports, 13. covers, 14. flow guide bars.
Embodiment
The utility model is further described presently in connection with accompanying drawing.These accompanying drawings are simplified schematic diagram only to show
Meaning mode illustrates basic structure of the present utility model, therefore it only shows the composition relevant with the utility model.
Alkaline brine filter cellulose batch tank as shown in Figure 1, including base 8, the upper surface of base 8 are provided with tank body
1, the top end cover of tank body 1 is provided with cover 13, and brine inlet 3 and cellulose feed mouth 4, the lumen centers of tank body 1 are provided with cover 13
Suspension is provided with rotating shaft 9, and rotating shaft 9 is connected with the motor 11 that drive shaft 9 rotates after stretching out cover 13, stirring is provided with rotating shaft 9
Frame 5, stirring frame 5 are built in tank body 1, stir and are equipped with some horizontally disposed stirring vanes 7 on two vertical sides of frame 5;
Discharging opening 6 for the discharging of suspension finished product is installed in the middle part of the side wall of tank body 1.
Stirring 5 four drift angles of frame are mounted on dihedral vane 2 to external radiation, the central shaft of dihedral vane 2 and horizontal line it
Between angle be 45 °.
The output end of motor 11 is provided with reductor 10, and the output end of reductor 10 is connected with rotating shaft 9;Motor 11 passes through motor branch
Frame 12 is arranged on cover 13;The inwall of tank body 1 is provided with helical form flow guide bar 14.
Salt solution brine inlet 3 after filtering enters tank body 1, and cellulosic material enters tank body 1, electricity from cellulose feed mouth 4
The drive shaft 9 of machine 11 rotates, and stirring frame 5 rotates, so as to drive dihedral vane 2 and stirring vane 7 to carry out the material in tank body 1
Stirring, suspension finished product are discharged from discharging opening 6.
Using it is above-mentioned according to desirable embodiment of the present utility model as enlightenment, pass through above-mentioned description, related work people
Member can carry out various changes and amendments in the range of without departing from this item utility model technological thought completely.This item is real
The content being not limited to new technical scope on specification, it is necessary to which its technology is determined according to right
Property scope.
Claims (5)
- A kind of 1. alkaline brine filter cellulose batch tank, it is characterised in that:Including base(8), base(8)Install upper surface There is tank body(1), tank body(1)Top end cover is provided with cover(13), cover(13)On brine inlet is installed(3)With cellulose feed mouth (4), the tank body(1)Lumen centers suspension is provided with rotating shaft(9), rotating shaft(9)Stretch out cover(13)After be connected with drive shaft(9) The motor of rotation(11), rotating shaft(9)On stirring frame is installed(5), stir frame(5)It is built in tank body(1), stir frame(5)Two Some horizontally disposed stirring vanes are equipped with individual vertical side(7);The tank body(1)It is provided with the middle part of side wall for suspended The discharging opening of liquid finished product discharging(6).
- 2. alkaline brine filter cellulose batch tank according to claim 1, it is characterised in that:Described stirring frame (5)Four drift angles are mounted on the dihedral vane to external radiation(2), dihedral vane(2)Angle between central shaft and horizontal line For 45 °.
- 3. alkaline brine filter cellulose batch tank according to claim 1, it is characterised in that:Described motor(11) Output end is provided with reductor(10), reductor(10)Output end and rotating shaft(9)Connection.
- 4. alkaline brine filter cellulose batch tank according to claim 1, it is characterised in that:Described motor(11) Pass through electric machine support(12)Installed in cover(13)On.
- 5. alkaline brine filter cellulose batch tank according to claim 1, it is characterised in that:Described tank body(1) Inwall is provided with helical form flow guide bar(14).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720698468.1U CN207102398U (en) | 2017-06-15 | 2017-06-15 | Alkaline brine filter cellulose batch tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720698468.1U CN207102398U (en) | 2017-06-15 | 2017-06-15 | Alkaline brine filter cellulose batch tank |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207102398U true CN207102398U (en) | 2018-03-16 |
Family
ID=61595082
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720698468.1U Expired - Fee Related CN207102398U (en) | 2017-06-15 | 2017-06-15 | Alkaline brine filter cellulose batch tank |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207102398U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115212744A (en) * | 2022-08-04 | 2022-10-21 | 江苏方达正塬电子材料科技有限公司 | High-viscosity colloidal material pretreatment device |
-
2017
- 2017-06-15 CN CN201720698468.1U patent/CN207102398U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115212744A (en) * | 2022-08-04 | 2022-10-21 | 江苏方达正塬电子材料科技有限公司 | High-viscosity colloidal material pretreatment device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103060834B (en) | A kind of technological process of electrolytic sulfite | |
CN205361210U (en) | Novel storage vat stirring device | |
CN109763137A (en) | A kind of device for production water supply javelle water | |
CN207102398U (en) | Alkaline brine filter cellulose batch tank | |
CN103058248B (en) | Equipment and process for preparing nano calcium carbonate by gypsum | |
CN106976894A (en) | A kind of method that lithium chloride electricity conversion directly prepares lithium carbonate | |
CN210973907U (en) | Micro-reaction device for preparing nano calcium carbonate | |
CN214047548U (en) | On-spot jar of papermaking method reconstituted tobacco coating liquid | |
CN104151859B (en) | A kind of device of indigo Product recycling mixed base | |
CN213652668U (en) | System for preparing sodium hypochlorite by fly ash | |
CN210480892U (en) | Complete device for producing magnesium hydroxide from magnesium chloride lime milk | |
CN203128220U (en) | Equipment for producing nano calcium carbonate from gypsum | |
CN107675201A (en) | The preparation method of electrolytic manganese dioxide | |
CN210906157U (en) | Pyrolytic reaction cauldron of lithium carbonate production usefulness | |
CN205398130U (en) | Carbide slag preparation industry naoh reaction unit | |
CN218579703U (en) | Acidic oxidation high-potential water generator | |
CN206064191U (en) | A kind of sodium silicate solid dissolving apparatus | |
CN215388048U (en) | Purification device is used in calcium hydrate production | |
CN208292789U (en) | A kind of device preparing fungicide | |
CN206381856U (en) | Sodium sulfite make-up tank | |
CN220860703U (en) | Concentrated device that separates out of lithium carbonate crystal | |
CN211725746U (en) | Condensation kettle for producing polyamide resin | |
CN216418557U (en) | Slurry purifying device capable of efficiently discharging slag | |
CN213793158U (en) | Alkali washing kettle for producing organic fluoride | |
CN202752019U (en) | Precipitation reactor for producing silica |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180316 Termination date: 20180615 |
|
CF01 | Termination of patent right due to non-payment of annual fee |