CN205760949U - A kind of organobentonite preparation facilities - Google Patents
A kind of organobentonite preparation facilities Download PDFInfo
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- CN205760949U CN205760949U CN201620503337.9U CN201620503337U CN205760949U CN 205760949 U CN205760949 U CN 205760949U CN 201620503337 U CN201620503337 U CN 201620503337U CN 205760949 U CN205760949 U CN 205760949U
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Abstract
This utility model relates to a kind of organobentonite preparation facilities, and including the preparation facilities of modifying agent, bentonitic reducing mechanism and modifying agent and bentonitic mixing arrangement, described preparation facilities includes the second tank body that the first tank body communicates with described first tank body；The first feed pieces, the second feed pieces and discharging opening it is provided with on first tank body, in described first tank body, shaft one is set, described shaft one has the hollow section of the opening on a top being arranged on described shaft one, on the axial wall of described hollow section, discharge opening is set, the outlet of described first and second feed pieces is oppositely arranged, and forms mixing discharging opening between the two.This utility model preparation facilities is reasonable in design, by improving the addition manner to material so that it is material is had stirring action, improves shaft simultaneously, is greatly improved stirring efficiency, improves the quality of modifying agent, more preferable to alta-mud modification effect.
Description
Technical field
This utility model belongs to a kind of bentonite preparation field, relates to a kind of organobentonite preparation facilities.
Background technology
Bentonite is also referred to as montmorillonite, is the mineral being mainly made up of montmorillonite.The main component of montmorillonite is comprehensive silicon
Hydrochlorate.This mineral is the inorganic matter of natural nano level interlamellar spacing, sheet interlayer spacing about tens nanometer, have special water absorption,
Hydroplasticity, caking property and stronger ion exchangeable etc., be the clay mineral that current range of application is the widest, economic worth is higher
One of, it has been widely used in the every field such as metallurgy, machinery, oil, chemical industry, macromolecular material and environmental conservation.But
Due to the surface active of bentonite micropowder, its compatibility in polymer matrix and dispersion existing problems.So needing swollen
Profit soil is modified.
At present much about to bentonite modified research, as Patent No. CN102660159A utility model patent in
A kind of modified superfine preparation method for bentonite, the modified superfine bentonite of preparation and application thereof disclosed in JIUYUE in 2012 12 days,
Use borate ester modifying agent, solve Ultra-fine Bentonite and the compatibility of macromolecular material and dispersion problem.
During to alta-mud modification, preparation and the modifying agent of modifying agent are even more important with bentonitic reaction,
At present, modifying agent many employings tertiary amine is prepared with water and chloromethanes, for the effect of modifying agent, uses two kinds of different tertiary amines
Mixing, because the toughness of tertiary amine is high, thus the highest, owing to stirring in preparation process to the equipment requirements used in modifying agent preparation
The factor such as mix, often lead to can't meet the quality requirement.
In the course of processing, bentonite need pulverize, levigate, with the higher bentonite of prepared quality, meet the need of purposes
, at present, undesirable to bentonitic crushing effect, the Chinese utility model patent such as Publication No. 202096975U discloses
A kind of gear crusher for bentonite, crushing effect is poor, inefficient so that bentonitic production cost increases.
Utility model content
The purpose of this utility model is to provide a kind of organobentonite preparation facilities, and modifying agent is now made, and modified effect is good, greatly
The big stirring efficiency improved in preparation process, improves the quality of modifying agent, more preferable to alta-mud modification effect, leads to bentonite
Cross pulverize, alternate cycles of sieving, good crushing effect, collect in time pulverizing the bentonite of particle diameter of achieving the goal, improve and pulverize effect
Rate, strengthens the reaction effect of bentonite and modifying agent, improves bentonite quality.
This utility model adopts the following technical scheme that: a kind of organobentonite preparation facilities, including the preparation of modifying agent
Device, bentonitic reducing mechanism and modifying agent and bentonitic mixing arrangement, described preparation facilities include the first tank body and
The second tank body that described first tank body communicates；The coarse pulverization knot that reducing mechanism includes feeding structure, is connected with described feeding structure
Structure and the finely divided structure being connected with described coarse pulverization structure, described first tank body is provided with the first feed pieces, second enters
Material parts and discharging opening, arrange shaft one in described first tank body, described shaft one is through the bottom of described first tank body
Being connected with motor, described shaft one has the hollow section of the opening on a top being arranged on described shaft one, described hollow
Arranging discharge opening on the axial wall of section, the outlet of described first feed pieces and the outlet of described second feed pieces are oppositely arranged,
Forming mixing discharging opening between the two, described mixing discharging opening is directed at the opening of described hollow section.
Technique scheme, the preparation of modifying agent uses two kinds of different materials to enter through two feed pieces, regulates two
The exit position of feed pieces, enables material to be sufficiently mixed, Bentonite modifier raw material the most all use 16 tertiary amines, 18
Tertiary amine, for thick, this feeding manner, then by between on shaft one arrange discharge opening, material is thrown away into
Row mixing, can mix evenly this thick material, react more abundant.
As preferably, described coarse pulverization structure includes that coarse pulverization tank, described coarse pulverization tank are provided with charging aperture and are positioned at institute
State the discharging opening of coarse pulverization pot bottom, it is characterised in that be provided with in described coarse pulverization tank the first crushing part, be arranged on described
Screening part below first crushing part, described screening part includes base, the peace being fixed on described coarse pulverization tank
The grade screening structure being contained on described base, the actuator driving described grade screening structure to rotate, described grade screening knot
Structure includes surrounding columned one-level screening net and being arranged on described one-level screening in the cylinder that net surrounds and surrounding cylinder
Two grades of shape screen nets and are arranged on the suction tubes in the cylinder that described two grades of screening nets surround.
Technique scheme, thick bentonite pulverizes successively through coarse pulverization structure, finely divided structure, and coarse pulverization is tied
Structure is pulverized, is sieved, and the bentonite of the particle diameter that achieves the goal, from postsearch screening net filtration, reclaims through suction tube and collects, and particle diameter is unsatisfactory for
Require, screen net, the screening of two grades of screening nets through one-level, fall in tank, reclaim through discharging opening, again put into pulverizing；Existing
Grinding be all to be crushed to purpose particle diameter together, another rising is reclaimed, and grinding efficiency is low, this design of this programme, can be timely
Reclaim the target bentonite pulverized, improve grinding efficiency, it is ensured that Grinding Quality.
As preferably, described first feed pieces and the second feed pieces all include being arranged on setting outside described first tank body
Putting the portion that feeds intake of dog-house, be positioned at the feeder that described first tank body is outer, described feeder has the braking section being positioned at front end.
Braking section makes material the most quickly drop, the time being fully contacted to the material of two feed pieces outlets.
As preferably, the lower wall of described braking section extends reclaiming plate, the front end of the reclaiming plate of described first feed pieces
Portion is positioned at above the reclaiming plate of described second feed pieces, by dropping into the second feeder from the reclaiming plate of the first feed pieces
The reclaiming plate of part, can break up material, plays peptizaiton, thus preferably mix homogeneously.
As preferably, the angle of inclination of described first feed pieces braking section is more than described second feed pieces braking section
Angle of inclination, the speed that the speed that in the first feed pieces, material drops drops more than material in the second feed pieces, it is ensured that thing
Material can stop in the second feed pieces, and material drops into the discharging of the second feed pieces from the reclaiming plate of the first feed pieces
Plate, can break up material, dispersion, stops mixing on the reclaiming plate of the second feed pieces, and mixed effect is more preferable.
As preferably, it is provided with first below the feeder of described first feed pieces and falls plate, described second feeder
Being provided with second below the feeder of part and fall plate, described first leading section falling plate is positioned at described first feed pieces discharging
Below plate, the second leading section falling plate is positioned at the described first lower section falling plate.This programme arranges and falls plate, and material can be many
Secondary falling, break up, mix, mixed effect is more preferably.
As preferably, the reclaiming plate end of described second feed pieces is 5-15 to the vertical distance that described first falls plate
, the material of last layer can fall on next layer of material, falls certain degree of depth, is unlikely to again the material impact to next layer
Power is excessive, breaks up out completely, it is ensured that the exposure of two kinds of materials, is beneficial to mixing.
As preferably, the angle of inclination of described second feed pieces braking section is 40-50 °.
As preferably, described first, second falls breeze way that plate all includes setting gradually, mixed along Flow of Goods and Materials direction
Closing section and discharging section, breeze way makes material drop to fall on plate, be unlikely to immediately from falling plate landing, but through mixing
Section, strengthens mixed effect, and described mixing section is provided with wave flour mixed with adulterants, and mixed effect can more preferably, and described mixing section is obliquely installed.
As preferably, the outer wall of described shaft one is provided with paddle and axially arranged scraping blade.
As preferably, described paddle being provided with some through holes, during stirring, partial material passes through hole, is formed
Material stream, breaks up material below, mixes.
As preferably, the cylindrical outer surface that described one-level screening net surrounds is provided with some separations of horizontally set
Plate, described demarcation strip is along the circumferencial direction distribution of described one-level screening net.Ensure that the bentonite of purpose particle diameter can abundant warp
Cross screening to be recovered, be unlikely to be not able to do in time through first screening net just fall into discharging opening.
As preferably, described screening part also includes that one end is fixed on described coarse pulverization tank, the other end is from described
The end of two grades of screening nets penetrates the supporting spring in the cylinder that described two grades of screening nets surround, and the acting surface of described supporting spring is upward.
Supporting spring is set, it is ensured that reaching to collect the bentonite required can at utmost be collected, and will not repeat to fall into discharging opening.
As preferably, along the length direction of described supporting spring, the middle part indent of described supporting spring acting surface forms collector groove, more
Convenient collection.
As preferably, the discharge gate of described coarse pulverization pot bottom connects described feeding structure and/or described first smashing portion
Part, puts into pulverizing again.
As preferably, described first crushing part includes being arranged on a pair compression roller above described screening part, from two
The two panels passed between individual described compression roller has the extruding crushing piece of certain flexibility, is formed for thing between two panels extruding crushing piece
The material channel that material passes through.By compression roller, by extruding crushing piece, material is pulverized, crushing effect can be improved.
As preferably, described material channel includes the entrance leading to outside described coarse pulverization tank, through two described extruding
Extruded segment between roller and the discharging section below described extruded segment.
As preferably, in described extruded segment, it is enclosed with pulverizing steel ball, improves crushing effect.
As preferably, from described extruded segment to described discharging section, the particle diameter of described pulverizing steel ball is gradually reduced, crushing effect
More preferably.
As preferably, described entrance is provided with vibrations and pulverizes rod, improves crush efficiency, improves crushing effect.
By implementing technique scheme, this utility model has following beneficial effect: this utility model is by controlling
The quality of modifying agent and to bentonitic Grinding Quality, improves prepared bentonite quality: preparation facilities designs
Rationally, by improving the addition manner to material so that it is material is had stirring action, shaft is improved, significantly simultaneously
Improve stirring efficiency, improve the quality of modifying agent, more preferable to alta-mud modification effect；Bentonite is pulverized by reducing mechanism
Levigate, by pulverizing, alternate cycles of sieving, good crushing effect, the bentonite pulverizing the particle diameter that achieves the goal is collected in time, improve
Crush efficiency, reduces and pulverizes cost, improves grinding efficiency.
Accompanying drawing explanation
Accompanying drawing 1 is the preparation facilities structural representation of modifying agent in this utility model one embodiment；
Accompanying drawing 2 is the first tank interior sectional view in this utility model one embodiment；
Accompanying drawing 3 is coarse pulverization tank schematic diagram in this utility model one embodiment；
Accompanying drawing 4 is the cross-sectional schematic of coarse pulverization tank in this utility model one embodiment.
Detailed description of the invention
Below in conjunction with the accompanying drawings and specific embodiment, this utility model is described in further detail.
Embodiment 1:
A kind of organobentonite preparation facilities, including the preparation facilities of modifying agent, bentonitic reducing mechanism and modification
Agent and bentonitic mixing arrangement, described preparation facilities includes the second tank body that the first tank body 1 communicates with described first tank body 1
3；Reducing mechanism includes feeding structure, the coarse pulverization structure being connected with described feeding structure and is connected with described coarse pulverization structure
Finely divided structure, the structure of the first tank body 1 as shown in Figure 1, is provided with the first charging being separately added into two kinds of reactants
Parts 11 and the second feed pieces 12, raw material 16 tertiary amine of such as Bentonite modifier and 18 tertiary amines, set in the first tank body 1
Putting shaft 1, shaft 1 is connected through the bottom of the first tank body 1 with motor, and shaft 1 has one and is arranged on and stirs
Mix the hollow section of the opening on the top of axle 1, the axial wall of hollow section arranges discharge opening 131, described first feed pieces 11
The outlet of outlet and described second feed pieces 12 is oppositely arranged, and forms mixing discharging opening between the two, is directed at described hollow section
Opening, material enters from first, second feeder, can tentatively mix in both exits, and blended discharging opening enters
Enter the hollow section of shaft 1, under the rotation of shaft 1, throw away through discharge opening 131, carry out secondary mixing, then stirring
Mix under the stirring of axle 1, finally mix.First feed pieces 11 and the second feed pieces 12 all include being arranged on described
The portion that feeds intake 111 arranging dog-house outside first tank body 1, being positioned at the feeder 112 of the first tank body 1, feeder 112 has position
In the braking section 1121 of front end, braking section 1121 makes material the most quickly drop, and fills to the material of two feed pieces outlets
The time that tap is touched.
The lower wall of braking section 1121 extends reclaiming plate 1122, and the leading section of the reclaiming plate of the first feed pieces 11 is positioned at institute
State above the reclaiming plate of the second feed pieces 12；It is provided with first below the feeder 112 of the first feed pieces 11 and falls plate
113, it is provided with second below the feeder 112 of the second feed pieces 11 and falls plate 114, first falls the position, front end of plate 113
Below described first feed pieces 11 reclaiming plate 1122, the second leading section falling plate 114 is positioned at described first and falls plate 113
Lower section.Reclaiming plate 1122 end of the second feed pieces 12 is 5-15, this enforcement to the vertical distance that first falls plate 113
Example selects 8cm.First, second falls plate as shown in Figure 3, all includes the breeze way set gradually along Flow of Goods and Materials direction
1131, mixing section 1132 and discharging section 1133, described mixing section 1132 is provided with wave flour mixed with adulterants, and mixing section 1132 tilts to set
Put.
Coarse pulverization structure includes that coarse pulverization tank 2, coarse pulverization tank 2 are provided with charging aperture 201 and are positioned at the discharging opening of bottom
202, it is provided with the first crushing part 21 in coarse pulverization tank 2, is arranged on the screening part 22 below the first crushing part 21, screening
The grade screening knot that parts 22 include the base 222 being fixed on described coarse pulverization tank 2 tank body, are arranged on described base 222
Structure 221, driving the actuator 223 that described grade screening structure 221 rotates, grade screening structure 221 includes surrounding columned
One-level screening net 2211 screens in the cylinder that net 2211 surrounds with being arranged on described one-level and surrounds columned two grades of sieves
Network selection 2212 and be arranged on the suction tubes 2213 in two grades of screening cylinders of surrounding of nets 2212, suction tube 2213 links negative pressure
Generator.The cylindrical outer surface that one-level screening net 2211 surrounds is provided with three pieces of demarcation strips 2214 of horizontally set, described
Demarcation strip 2214 is along the circumferencial direction distribution of described one-level screening net 2211.
First crushing part 21 includes being arranged on a pair compression roller 211 above described screening part 22, from two extruding
The two panels extruding crushing piece 212 passed between roller 211, forms, between two panels extruding crushing piece 212, the material passed through for material and leads to
Road 213, entrance 2131 that material channel 213 includes leading to outside described coarse pulverization tank 2, through two described compression rollers 211 it
Between extruded segment 2132 and discharging section 2133 below described extruded segment 2132, be enclosed with pulverizing steel ball in extruded segment 2132, from
Described extruded segment 2132 is gradually reduced to described discharging section 2133, the particle diameter pulverizing steel ball.
Embodiment 2:
A kind of organobentonite preparation facilities, including the preparation facilities of modifying agent, bentonitic reducing mechanism and modification
Agent and bentonitic mixing arrangement, described preparation facilities includes the second tank body that the first tank body 1 communicates with described first tank body 1
3；Reducing mechanism includes feeding structure, the coarse pulverization structure being connected with described feeding structure and is connected with described coarse pulverization structure
Finely divided structure, the structure of the first tank body 1 as shown in Figure 1, is provided with the first charging being separately added into two kinds of reactants
Parts 11 and the second feed pieces 12, raw material 16 tertiary amine of such as Bentonite modifier and 18 tertiary amines, set in the first tank body 1
Putting shaft 1, shaft 1 is connected through the bottom of the first tank body 1 with motor, and shaft 1 has one and is arranged on and stirs
Mix the hollow section of the opening on the top of axle 1, the axial wall of hollow section arranges discharge opening 131, described first feed pieces 11
The outlet of outlet and described second feed pieces 12 is oppositely arranged, and forms mixing discharging opening between the two, is directed at described hollow section
Opening, material enters from first, second feeder, can tentatively mix in both exits, and blended discharging opening enters
Enter the hollow section of shaft 1, under the rotation of shaft 1, throw away through discharge opening 131, carry out secondary mixing, then stirring
Mix under the stirring of axle 1, finally mix.First feed pieces 11 and the second feed pieces 12 all include being arranged on described
The portion that feeds intake 111 arranging dog-house outside first tank body 1, being positioned at the feeder 112 of the first tank body 1, feeder 112 has position
In the braking section 1121 of front end, braking section 1121 makes material the most quickly drop, and fills to the material of two feed pieces outlets
The time that tap is touched.
The lower wall of braking section 1121 extends reclaiming plate 1122, and the leading section of the reclaiming plate of the first feed pieces 11 is positioned at institute
State above the reclaiming plate of the second feed pieces 12；It is provided with first below the feeder 112 of the first feed pieces 11 and falls plate
113, it is provided with second below the feeder 112 of the second feed pieces 11 and falls plate 114, first falls the position, front end of plate 113
Below described first feed pieces 11 reclaiming plate 1122, the second leading section falling plate 114 is positioned at described first and falls plate 113
Lower section.Reclaiming plate 1122 end of the second feed pieces 12 is 5-15, this enforcement to the vertical distance that first falls plate 113
Example selects 8cm.First, second falls plate as shown in Figure 3, all includes the breeze way set gradually along Flow of Goods and Materials direction
1131, mixing section 1132 and discharging section 1133, described mixing section 1132 is provided with wave flour mixed with adulterants, and mixing section 1132 tilts to set
Put.
Coarse pulverization structure includes that coarse pulverization tank 2, coarse pulverization tank 2 are provided with charging aperture 201 and are positioned at the discharging opening of bottom
202, it is provided with the first crushing part 21 in coarse pulverization tank 2, is arranged on the screening part 22 below the first crushing part 21, screening
The grade screening knot that parts 22 include the base 222 being fixed on described coarse pulverization tank 2 tank body, are arranged on described base 222
Structure 221, driving the actuator 223 that described grade screening structure 221 rotates, grade screening structure 221 includes surrounding columned
One-level screening net 2211 screens in the cylinder that net 2211 surrounds with being arranged on described one-level and surrounds columned two grades of sieves
Network selection 2212 and be arranged on the suction tubes 2213 in two grades of screening cylinders of surrounding of nets 2212, suction tube 2213 links negative pressure
Generator.The cylindrical outer surface that one-level screening net 2211 surrounds is provided with three pieces of demarcation strips 2214 of horizontally set, described
Demarcation strip 2214 is along the circumferencial direction distribution of described one-level screening net 2211.Screening part also include one end be fixed on described slightly
Pulverize on tank 2 tank body, the other end penetrates, from the end of described two grades of screening nets 2212, the circle that described two grades of screening nets 2212 surround
Supporting spring 224 in cylinder, the acting surface of described supporting spring 224 is upward.
First crushing part 21 includes being arranged on a pair compression roller 211 above described screening part 22, from two extruding
The two panels extruding crushing piece 212 passed between roller 211, forms, between two panels extruding crushing piece 212, the material passed through for material and leads to
Road 213, entrance 2131 that material channel 213 includes leading to outside described coarse pulverization tank 2, through two described compression rollers 211 it
Between extruded segment 2132 and discharging section 2133 below described extruded segment 2132, be enclosed with pulverizing steel ball in extruded segment 2132, from
Described extruded segment 2132 is gradually reduced to described discharging section 2133, the particle diameter pulverizing steel ball.
Claims (10)
1. an organobentonite preparation facilities, including the preparation facilities of modifying agent, bentonitic reducing mechanism and modifying agent
With bentonitic mixing arrangement, described preparation facilities includes the second tank that the first tank body (1) communicates with described first tank body (1)
Body (3)；Reducing mechanism include feeding structure, the coarse pulverization structure being connected with described feeding structure and with described coarse pulverization structure phase
Finely divided structure even, it is characterised in that be provided with the first feed pieces (11) and the second feeder on described first tank body (1)
Part (12), arranges shaft one (13) in described first tank body (1), described shaft one (13) is through described first tank body (1)
Bottom be connected with motor, described shaft one (13) has in the opening on a top being arranged on described shaft one (13)
Dead band, the axial wall of described hollow section arranges discharge opening (131), and the outlet of described first feed pieces (11) and described second is entered
The outlet of material parts (12) is oppositely arranged, and forms mixing discharging opening between the two, and described mixing discharging opening is directed at described hollow section
Opening；Described coarse pulverization structure includes that coarse pulverization tank (2), described coarse pulverization tank (2) are provided with charging aperture (201) and are positioned at institute
State the discharging opening (202) of coarse pulverization tank (2) bottom, be provided with the first crushing part (21) in described coarse pulverization tank (2), be arranged on
The screening part (22) of described first crushing part (21) lower section.
A kind of organobentonite preparation facilities, it is characterised in that described screening part (22) includes
The grade screening structure be fixed on the base (222) on described coarse pulverization tank (2) tank body, being arranged on described base (222)
(221), driving described grade to screen the actuator (223) that structure (221) rotates, described grade screening structure (221) includes enclosing
Become columned one-level screening net (2211) and be arranged on described one-level and screen in net (2211) cylinder that surrounds and surround
Columned two grades are screened net (2212) and are arranged on the suction tubes in the cylinder that described two grades of screenings net (2212) surround
(2213).
A kind of organobentonite preparation facilities, it is characterised in that described first feed pieces (11)
All include being arranged on the outer portion that feeds intake (111) that dog-house is set of described first tank body (1) with the second feed pieces (12), be positioned at
Feeder (112) in described first tank body (1), described feeder (112) has the braking section (1121) being positioned at front end.
A kind of organobentonite preparation facilities, it is characterised in that under described braking section (1121)
Wall extends reclaiming plate (1122), and the leading section of the reclaiming plate of described first feed pieces (11) is positioned at described second feed pieces
(12) above reclaiming plate.
A kind of organobentonite preparation facilities, it is characterised in that described first feed pieces (11)
Feeder (112) lower section be provided with first and fall plate (113), feeder (112) lower section of described second feed pieces (11)
Being provided with second and fall plate (114), the described first leading section falling plate (113) is positioned at the discharging of described first feed pieces (11)
Plate (1122) lower section, the second leading section falling plate (114) is positioned at the described first lower section falling plate (113).
A kind of organobentonite preparation facilities, it is characterised in that described one-level screening net (2211)
The cylindrical outer surface surrounded is provided with some demarcation strips (2214) of horizontally set, and described demarcation strip (2214) is along described
The circumferencial direction distribution of one-level screening net (2211).
A kind of organobentonite preparation facilities, it is characterised in that described screening part also includes one
End is fixed on described coarse pulverization tank (2) tank body, the other end penetrates described two grades from the end of described two grades of screenings net (2212)
Supporting spring (224) in the cylinder that screening net (2212) surrounds, the acting surface of described supporting spring (224) is upward.
A kind of organobentonite preparation facilities, it is characterised in that described first crushing part (21)
Including being arranged on a pair compression roller (211) of described screening part (22) top, passing between two described compression rollers (211)
Two panels extruding crushing piece (212), form the material channel (213) passed through for material between two panels extruding crushing piece (212).
A kind of organobentonite preparation facilities, it is characterised in that described material channel (213) wraps
Include and lead to described coarse pulverization tank (2) entrance (2131) outward, the extruded segment between two described compression rollers (211)
(2132) discharging section (2133) and below described extruded segment (2132).
A kind of organobentonite preparation facilities, it is characterised in that in described extruded segment (2132)
Being enclosed with pulverizing steel ball, from described extruded segment (2132) to described discharging section (2133), the particle diameter of described pulverizing steel ball gradually subtracts
Little.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620503337.9U CN205760949U (en) | 2016-05-30 | 2016-05-30 | A kind of organobentonite preparation facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620503337.9U CN205760949U (en) | 2016-05-30 | 2016-05-30 | A kind of organobentonite preparation facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205760949U true CN205760949U (en) | 2016-12-07 |
Family
ID=59978425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620503337.9U Active CN205760949U (en) | 2016-05-30 | 2016-05-30 | A kind of organobentonite preparation facilities |
Country Status (1)
| Country | Link |
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| CN (1) | CN205760949U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797640A (en) * | 2016-05-30 | 2016-07-27 | 浙江红宇新材料股份有限公司 | Organic bentonite preparing device |
| CN107597386A (en) * | 2017-10-10 | 2018-01-19 | 湖州壤之沃生物技术有限公司 | A kind of reducing mechanism for bentonite production |
-
2016
- 2016-05-30 CN CN201620503337.9U patent/CN205760949U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105797640A (en) * | 2016-05-30 | 2016-07-27 | 浙江红宇新材料股份有限公司 | Organic bentonite preparing device |
| CN105797640B (en) * | 2016-05-30 | 2018-07-27 | 浙江红宇新材料股份有限公司 | A kind of organobentonite preparation facilities |
| CN107597386A (en) * | 2017-10-10 | 2018-01-19 | 湖州壤之沃生物技术有限公司 | A kind of reducing mechanism for bentonite production |
| CN107597386B (en) * | 2017-10-10 | 2019-07-09 | 湖州壤之沃生物技术有限公司 | A kind of grinding device for bentonite production |
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