CN204211495U - A kind of chemical industry process former of bentonite sodium metallization processes - Google Patents
A kind of chemical industry process former of bentonite sodium metallization processes Download PDFInfo
- Publication number
- CN204211495U CN204211495U CN201420490590.6U CN201420490590U CN204211495U CN 204211495 U CN204211495 U CN 204211495U CN 201420490590 U CN201420490590 U CN 201420490590U CN 204211495 U CN204211495 U CN 204211495U
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- axles
- sodium
- reactive tank
- moisture control
- control storehouse
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- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
The utility model discloses a kind of chemical industry process former of bentonite sodium metallization processes, comprise reactive tank, moisture control storehouse and working chamber, the bottom of described reactive tank is provided with moisture control storehouse and working chamber successively, hopper and liquid adding bottle are set above the charging opening of described reactive tank, No. two axles are provided with in described reactive tank, No. two axles connect an outside motor, and No. two axle surfaces are provided with several stirrer gears; Inside, described moisture control storehouse arranges No. three axles, and No. three axles are provided with several breaks up rod.By reactive tank, wilkinite and sodium liquid hybrid reaction are obtained sodium-ionized bentonite, then sodium-ionized bentonite humidity is regulated by moisture control storehouse, utilize simultaneously and break up bastinade and to fall apart sodium-ionized bentonite, sodium-ionized bentonite is made to be dispersed into small-particle, then taken away portion of water by blower fan, thus make sodium-ionized bentonite have better viscosity and toughness.
Description
Technical field
The utility model relates to a kind of chemical industry process former, specifically a kind of chemical industry process former of bentonite sodium metallization processes.
Background technology
Sodium bentonite is broad-spectrum Chemicals, is to prepare bentonite basic raw material.The preparation of sodium bentonite adds 1Va` in the raw material wilkinite that calcic, magnesium etc. are higher, obtained to displace these ions.A kind of new working method is by through crushing raw ore, mix with light ash in duplex stirring mixer, in duplex reactor, stand shearing strain with certain pressure again and complete ion exchange reaction, then through shining thousand, after grinding, namely produce qualified sodium bentonite; This new processing method production efficiency is higher, but its weak point is: complete the material after ion exchange reaction not of uniform size, the air dry time is long, ted trouble and easily cause the pollution of material, and merely through the reaction of duplex stirring mixer also not exclusively, these defects cause the production time to lengthen on the one hand, and the quality of product is lower on the other hand.
Utility model content
The purpose of this utility model is the chemical industry process former providing a kind of bentonite sodium metallization processes, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of chemical industry process former of bentonite sodium metallization processes, comprise reactive tank, moisture control storehouse and working chamber, the bottom of described reactive tank is provided with moisture control storehouse and working chamber successively, hopper and liquid adding bottle are set above the charging opening of described reactive tank, No. two axles are provided with in described reactive tank, No. two axles connect an outside motor, and No. two axle surfaces are provided with several stirrer gears; Inside, described moisture control storehouse arranges No. three axles, and No. three axles are provided with several breaks up rod, the side in described moisture control storehouse is provided with fan housing, fan housing is by pipeline connecting fan, and in fan housing, heating unit is set, be provided with material toggling roller between described moisture control storehouse and working chamber, material toggling roller is connected on No. four axles; Screw-blade is provided with in described working chamber, screw-blade is arranged on an axle, and an axle is driven by No. two motors and connects, and side, working chamber arranges forming board, forming board is provided with several through holes, a described axle, connects each other by pulley belt between No. four axles and No. three axles.
As further program of the utility model: a described axle, No. two axles, No. three axles, No. four axles are all coated with layers of chrome.
Compared with prior art, the beneficial effects of the utility model are: by reactive tank, wilkinite and sodium liquid hybrid reaction are obtained sodium-ionized bentonite, then sodium-ionized bentonite humidity is regulated by moisture control storehouse, utilize simultaneously and break up bastinade and to fall apart sodium-ionized bentonite, sodium-ionized bentonite is made to be dispersed into small-particle, then taken away portion of water by blower fan, thus make sodium-ionized bentonite have better viscosity and toughness; Eventually pass extruding and the stirring of working chamber, make last shaping have the particulate state sodium-ionized bentonite of fine viscosity and toughness, the process-cycle is short, and is convenient to transport and segmentation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: forming board 1, axle 2, screw-blade 3, material toggling roller 4, blower fan 5, fan housing 6, moisture control storehouse 7, heating unit 8, No. two axles 9, stirrer gear 10, liquid adding bottle 11, hopper 12, charging opening 13, motor 14, reactive tank 15, No. three axles 16, break up rod 17, No. four axles 18, No. two motors 19, working chamber 20.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1, in the utility model embodiment, a kind of chemical industry process former of bentonite sodium metallization processes, comprise reactive tank 15, moisture control storehouse 7 and working chamber 20, the bottom of described reactive tank 15 is provided with moisture control storehouse 7 and working chamber 20 successively, hopper 12 and liquid adding bottle 11 are set above the charging opening 13 of described reactive tank 15, the wilkinites such as wilkinite are added by hopper 12, liquid adding bottle 11 adds sodium liquid, No. two axles 9 are provided with in described reactive tank 15, No. two axles 9 connect an outside motor 14, and No. two axle 9 surfaces are provided with several stirrer gears 10, after fully mixing after stirrer gear 10 stirs from the wilkinites such as the wilkinite that charging opening 13 enters and sodium liquid, enter moisture control storehouse 7,
Inside, described moisture control storehouse 7 arranges No. three axles 16, and No. three axles 16 are provided with several breaks up rod 17, break up rod 17 by the rotation drive of No. three axles 16 to break up mixing the sodium-ionized bentonite be bonded together in reactive tank 15, the side in described moisture control storehouse 7 is provided with fan housing 6, fan housing 6 is by pipeline connecting fan 5, and in fan housing 6, heating unit 8 is set, accelerate to break up scattering and disappearing of rear sodium-ionized bentonite internal moisture by hot blast, the humidity of quick adjustment sodium-ionized bentonite, avoid the excessive phenomenon that cannot be shaped of the humidity of sodium-ionized bentonite, when the moisture proportion of sodium-ionized bentonite reaches requirement, the wind-force discrepancy working chamber 20 that will be fixed, material toggling roller 4 is provided with between described moisture control storehouse 7 and working chamber 20, material toggling roller 4 is connected on No. four axles 18, sodium-ionized bentonite is clashed into by material toggling roller 4 high-speed rotation, increase the viscosity of sodium-ionized bentonite,
Screw-blade 3 is provided with in described working chamber 20, screw-blade 3 is arranged on an axle 2, an axle 2 is driven by No. two motors 19 and connects, thus drive screw-blade 3 sodium-ionized bentonite to be pushed to forming board 1 place of side, working chamber 20 setting, forming board 1 is provided with several through holes, finally makes sodium-ionized bentonite from through hole extrusion molding;
Describedly to connect each other by pulley belt between an axle 2, No. four axles 18 and No. three axles 16, thus complete the driving of single motor-driven, reduce equipment cost, a described axle 2, No. two axles 9, No. three axles 16, No. four axles 18 are all coated with layers of chrome, avoid wilkinite and sodium corrosion, cause damage.
Principle of work of the present utility model is: by reactive tank 15, wilkinite and sodium liquid hybrid reaction are obtained sodium-ionized bentonite, then sodium-ionized bentonite humidity is regulated by moisture control storehouse 7, utilization is simultaneously broken up rod 17 and is broken up sodium-ionized bentonite, sodium-ionized bentonite is made to be dispersed into small-particle, then taken away portion of water by blower fan 5, thus make sodium-ionized bentonite have better viscosity and toughness; Eventually pass extruding and the stirring of working chamber 20, make last shaping have the particulate state sodium-ionized bentonite of fine viscosity and toughness, thus be convenient to transport and segmentation.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (2)
1. the chemical industry process former of a bentonite sodium metallization processes, comprise reactive tank, moisture control storehouse and working chamber, it is characterized in that, the bottom of described reactive tank is provided with moisture control storehouse and working chamber successively, hopper and liquid adding bottle are set above the charging opening of described reactive tank, be provided with No. two axles in described reactive tank, No. two axles connect an outside motor, and No. two axle surfaces are provided with several stirrer gears; Inside, described moisture control storehouse arranges No. three axles, and No. three axles are provided with several breaks up rod, the side in described moisture control storehouse is provided with fan housing, fan housing is by pipeline connecting fan, and in fan housing, heating unit is set, be provided with material toggling roller between described moisture control storehouse and working chamber, material toggling roller is connected on No. four axles; Screw-blade is provided with in described working chamber, screw-blade is arranged on an axle, and an axle is driven by No. two motors and connects, and side, working chamber arranges forming board, forming board is provided with several through holes, a described axle, connects each other by pulley belt between No. four axles and No. three axles.
2. the chemical industry process former of a kind of bentonite sodium metallization processes according to claim 1, is characterized in that, a described axle, No. two axles, No. three axles, No. four axles are all coated with layers of chrome.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420490590.6U CN204211495U (en) | 2014-08-28 | 2014-08-28 | A kind of chemical industry process former of bentonite sodium metallization processes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420490590.6U CN204211495U (en) | 2014-08-28 | 2014-08-28 | A kind of chemical industry process former of bentonite sodium metallization processes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204211495U true CN204211495U (en) | 2015-03-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420490590.6U Expired - Fee Related CN204211495U (en) | 2014-08-28 | 2014-08-28 | A kind of chemical industry process former of bentonite sodium metallization processes |
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| CN (1) | CN204211495U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106426546A (en) * | 2016-09-12 | 2017-02-22 | 淮阴工学院 | Integrated continuous production type clay dissociation-modification-drying method |
| CN112978745A (en) * | 2021-04-15 | 2021-06-18 | 许世国 | Production equipment and production process of sodium modified bentonite |
| CN117228680A (en) * | 2023-11-13 | 2023-12-15 | 建平慧营化工有限公司 | Bentonite sodium modification device |
-
2014
- 2014-08-28 CN CN201420490590.6U patent/CN204211495U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106426546A (en) * | 2016-09-12 | 2017-02-22 | 淮阴工学院 | Integrated continuous production type clay dissociation-modification-drying method |
| CN112978745A (en) * | 2021-04-15 | 2021-06-18 | 许世国 | Production equipment and production process of sodium modified bentonite |
| CN117228680A (en) * | 2023-11-13 | 2023-12-15 | 建平慧营化工有限公司 | Bentonite sodium modification device |
| CN117228680B (en) * | 2023-11-13 | 2024-01-26 | 建平慧营化工有限公司 | Bentonite sodium modification device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| DD01 | Delivery of document by public notice |
Addressee: HANGZHOU XIEHONG TECHNOLOGY CONSULTING CO., LTD. Document name: Notification to Go Through Formalities of Registration |
|
| DD01 | Delivery of document by public notice |
Addressee: Wang Fei Document name: Notification of Passing Examination on Formalities |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150318 Termination date: 20170828 |