CN205700563U - Bentonite modifier preparation facilities - Google Patents
Bentonite modifier preparation facilities Download PDFInfo
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- CN205700563U CN205700563U CN201620503349.1U CN201620503349U CN205700563U CN 205700563 U CN205700563 U CN 205700563U CN 201620503349 U CN201620503349 U CN 201620503349U CN 205700563 U CN205700563 U CN 205700563U
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Abstract
The open a kind of Bentonite modifier preparation facilities of this utility model, including the first tank body, the second tank body communicated with described first tank body and the 3rd tank body communicated with described second tank body, it is provided with the first feed pieces on described first tank body, second feed pieces and discharging opening, in described first tank body, shaft one is set, described shaft one is connected through the bottom of described first tank body with motor, 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 feed pieces and the outlet of described second feed pieces are oppositely arranged, form mixing discharging opening between the two, described mixing discharging opening is directed at the opening of described hollow section.This utility model is 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 relates to a kind of process equipment, especially Bentonite modifier 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.
The most a lot of about to bentonite modified research, if the patent of invention of Patent No. CN102660159A is in 2012
Disclosed on JIUYUE 12, a kind of modified superfine preparation method for bentonite, the modified superfine bentonite of preparation and application thereof, use
Borate ester modifying agent, solves Ultra-fine Bentonite and the compatibility of macromolecular material and dispersion problem.
During to alta-mud modification, the preparation of modifying agent is also even more important, at present, modifying agent many employings tertiary amine with
Water and chloromethanes are prepared, and for the effect of modifying agent, use two kinds of different tertiary amines mixing, because the toughness of tertiary amine
Height, thus the highest to the equipment requirements used in modifying agent preparation, due to factors such as stirrings in preparation process, often lead to quality
Do not reach requirement.
Utility model content
The purpose of this utility model is to provide Bentonite modifier preparation facilities, for the preparation of modifying agent, can improve
Bentonite modified quality.
This utility model adopts the following technical scheme that: Bentonite modifier preparation facilities, including the first tank body with described
The second tank body that first tank body communicates and the 3rd tank body communicated with described second tank body, described first tank body is provided with first
Feed pieces, the second feed pieces and discharging opening, arrange shaft one in described first tank body, described shaft one is through described
The bottom of the first tank body is connected with motor, and described shaft one has in the opening on a top being arranged on described shaft one
Dead band, the axial wall of described hollow section arranges discharge opening, the outlet of described first feed pieces and described second feed pieces
Outlet is oppositely arranged, and forms mixing discharging opening between the two, and described mixing discharging opening is directed at the opening of described hollow section；Described go out
Between material mouth and described first charging aperture, there is difference in height, described second tank body also sets up the second charging aperture and the 3rd charging
Mouthful, it being provided with shaft two in described second tank body, described shaft two is hollow structure, and the inner chamber of described shaft two connects
There is the air inlet pipe being positioned at outside described second tank body, the axial wall of described shaft two is provided with gas outlet.
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 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.
Such scheme, the second tank body adds the third raw material, by arranging the height between discharging opening and the first charging aperture
Difference, just can play material during charging and break up, act on, by the air inlet pipe outside the second tank body, if using gas raw material, and example
Such as the chloromethanes in Bentonite modifier, just it is passed through methyl chloride gas, is the mode added materials, the most this interpolation side
Formula, can impact the material of the inside again, immixture, improves the efficiency of reaction；Without gas raw material, can use
Noble gas, has the effect of stirring mixed material.
As preferably, described second charging aperture is be arranged on described second tank body tank skin multiple, multiple comes in simultaneously,
Improve in the material that the dispersibility of material, especially material enter thickness.
As preferably, the non-parallel setting of outgassing direction of the gas outlet on described shaft two, play and preferably mix effect
Really.
As preferably, described shaft two includes axial direction part and is arranged on the traversing section of described axial direction part end, described horizontal stroke
Include base portion, the stop part being arranged on described base portion front end and neutral portion to section, by neutral portion, material is broken up, especially
It is for thick material, plays more preferable mixed effect.
As preferably, described base portion and described stop part are provided with and communicate and communicate with the inner chamber of described shaft two
Gas passage, described gas passage is provided with the second gas outlet, plays more preferable mixed effect.
As preferably, the discharging direction of the second different charging apertures at least two intersect, play preferably dispersion,
Mixed effect.
As preferably, described stop part and described neutral portion are arranged alternately, and the width in described neutral portion is less than described resistance
The width of stopper, the dispersion to material is more abundant.
As preferably, the axial direction part of described shaft two arranges stirring parts and the second scraping blade, near described second scraping blade
The outgassing direction of the gas outlet of inner side is parallel to described second scraping blade.
As preferably, described stirring parts includes that the root being connected with described shaft two is mutual with what described root was connected
The second parallel paddle, described second paddle is provided with perforation.
By implementing technique scheme, this utility model has following beneficial effect: this utility model is for swelling
During land reform, the preparation of modifying agent, reasonable in design, by improving the addition manner to material so that it is have stirring to make to material
With, shaft is improved simultaneously, be greatly improved stirring efficiency, improve the quality of modifying agent, to alta-mud modification effect
More preferably.
Accompanying drawing explanation
Accompanying drawing 1 is the structural representation of this utility model one embodiment；
Accompanying drawing 2 is the first tank interior schematic diagram in this utility model one embodiment；
Accompanying drawing 3 is the second tank body schematic diagram 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 Bentonite modifier preparation facilities, as shown in Figure 1, including the first tank body 1, second being sequentially communicated connection
Tank body 2.The structure of the first tank body 1 as shown in Figure 2, is provided with the first feed pieces 11 being separately added into two kinds of reactants
With the second feed pieces 12 and discharging opening 14, reactant, as a example by 16 tertiary amines and 18 tertiary amines, arranges in the first tank body 1 and stirs
Mixing axle 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 shaft
The hollow section of the opening on the top of 1, the axial wall of hollow section arranges discharge opening 131, and outer wall is provided with paddle and axially sets
The scraping blade put, paddle is provided with some through holes, depending on number is according to the area of paddle and the viscosity of stirring thing, and face
Long-pending the biggest, viscosity is the biggest, the most.
The structure of the second tank body 2 as shown in Figure 3, is provided with multiple second charging aperture 22 and is positioned at the second tank body 2
First charging aperture 21 on top, the second charging aperture 22 adds raw water, and the first charging aperture 21 adds the mixed of tertiary amine in the first tank body 1
Compound, the discharging direction of the second different charging apertures 22 has two to intersect, and the present embodiment the second charging aperture 22 arranges two,
Material is separately introduced, and improves reaction efficiency.Between discharging opening 14 and the first charging aperture 21, there is difference in height, set in the second tank body 2
Being equipped with shaft 23, shaft 23 is hollow structure, and the inner chamber of shaft 23 connects to have and is positioned at outside described second tank body 2
Air inlet pipe 4, the axial wall of shaft 23 is provided with gas outlet 31, the non-parallel setting of outgassing direction of gas outlet 31.
The outlet of the first feed pieces 11 and the outlet of described second feed pieces 12 are oppositely arranged, and are formed mixed between the two
Closing discharging opening, be directed at the opening of described hollow section, material enters from first, second feeder, can carry out in both exits
Preliminary mixing, blended discharging opening enters the hollow section of shaft 1, under the rotation of shaft 1, through discharge opening 131
Throw away, carry out secondary mixing, then under the stirring of shaft 1, finally mix.First feed pieces 11 and second is entered
Material parts 12 all include the portion that feeds intake 111 arranging dog-house being arranged on outside described first tank body 1, are positioned at the first tank body 1
Feeder 112, feeder 112 has the braking section 1121 being positioned at front end, and braking section 1121 makes material the most quickly drop, gives
The time that the material of two feed pieces outlet is fully contacted, and the angle of inclination of the first feed pieces 11 braking section 1121 is more than
The angle of inclination of the second feed pieces 12 braking section 1121, it is preferable that the angle of inclination of the second feed pieces 12 braking section 1121 is
40-50 °, the present embodiment is set to 45 °.
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.The reclaiming plate end of the second feed pieces is 5-15 to the vertical distance that described first falls plate, and the present embodiment is
8cm。
Shaft 23 includes axial direction part 32 and is arranged on the traversing section 33 of described axial direction part 32 end, described traversing section 33
The stop part 332 including base portion 331, being arranged on described base portion 331 front end and neutral portion 333；Stop part 332 and neutral portion 333
It is arranged alternately, and the width in neutral portion 333 is less than the width of stop part 332；Base portion 331 and stop part 332 be provided with communicate and
The gas passage 334 communicated with the inner chamber of described shaft 23, gas passage 334 is provided with the second gas outlet.
Embodiment 2:
A kind of Bentonite modifier preparation facilities, including first tank body the 1, second tank body 2 being sequentially communicated connection.First tank
It is provided with the first feed pieces 11 and the second feed pieces 12 being separately added into two kinds of reactants on body 1, the first tank body 1 is arranged
Having and be separately added into the first feed pieces 11 of two kinds of reactants and the second feed pieces 12 and discharging opening 14, reactant is with 16
As a example by tertiary amine and 18 tertiary amines, shaft 1 is set in first tank body 1, shaft 1 through the first tank body 1 bottom with
Motor is connected, and shaft 1 has the hollow section of the opening on a top being arranged on shaft 1, on the axial wall of hollow section
Arranging discharge opening 131, outer wall is provided with paddle and axially arranged scraping blade, and paddle is provided with some through holes, number
Depending on area according to paddle and the viscosity of stirring thing, area is the biggest, and viscosity is the biggest, the most.
It is provided with multiple second charging aperture 22 on second tank body 2 and is positioned at first charging aperture 21 on the second tank body 2 top, the
Two charging apertures 22 add raw water, and the first charging aperture 21 adds the mixture of tertiary amine in the first tank body 1, the second different charging apertures
The discharging direction of 22 has three to intersect, and the present embodiment the second charging aperture 22 arranges three, and material is separately introduced, and improves reaction
Efficiency.Between discharging opening 14 and the first charging aperture 21, there is difference in height, in the second tank body 2, be provided with shaft 23, shaft two
3 is hollow structure, and the inner chamber of shaft 23 connects the air inlet pipe 4 being positioned at outside described second tank body 2, the axial wall of shaft 23
On be provided with gas outlet 31, the non-parallel setting of outgassing direction of gas outlet 31.
The outlet of the first feed pieces 11 and the outlet of described second feed pieces 12 are oppositely arranged, and are formed mixed between the two
Closing discharging opening, be directed at the opening of described hollow section, material enters from first, second feeder, can carry out in both exits
Preliminary mixing, blended discharging opening enters the hollow section of shaft 1, under the rotation of shaft 1, through discharge opening 131
Throw away, carry out secondary mixing, then under the stirring of shaft 1, finally mix.First feed pieces 11 and second is entered
Material parts 12 all include the portion that feeds intake 111 arranging dog-house being arranged on outside described first tank body 1, are positioned at the first tank body 1
Feeder 112, feeder 112 has the braking section 1121 being positioned at front end, and braking section 1121 makes material the most quickly drop, gives
The time that the material of two feed pieces outlet is fully contacted, and the angle of inclination of the first feed pieces 11 braking section 1121 is more than
The angle of inclination of the second feed pieces 12 braking section 1121, it is preferable that the angle of inclination of the second feed pieces 12 braking section 1121 is
40-50 °, the present embodiment is set to 45 °.
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.First, second falls breeze way, mixing section and the discharging section that plate all includes setting gradually along Flow of Goods and Materials direction,
Breeze way makes material drop to fall on plate, be unlikely to immediately from falling plate landing, but through mixing section, strengthens mixing effect
Really, described mixing section is provided with wave flour mixed with adulterants, and mixed effect can more preferably, and described mixing section is obliquely installed.
Shaft 23 includes axial direction part 32 and is arranged on the traversing section 33 of described axial direction part 32 end, described traversing section 33
The stop part 332 including base portion 331, being arranged on described base portion 331 front end and neutral portion 333；Stop part 332 and neutral portion 333
It is arranged alternately, and the width in neutral portion 333 is less than the width of stop part 332；Base portion 331 and stop part 332 be provided with communicate and
The gas passage 334 communicated with the inner chamber of described shaft 23, gas passage 334 is provided with the second gas outlet.Shaft 23
Axial direction part on stirring parts and the second scraping blade are set, the outgassing direction of the gas outlet inside described second scraping blade is parallel to institute
State the second scraping blade.Stirring parts includes be parallel to each other second that the root being connected with described shaft 23 is connected with described root
Paddle, described second paddle is provided with perforation.
Claims (10)
1. Bentonite modifier preparation facilities, including the first tank body (1) and the second tank body of communicating with described first tank body (1)
(2), described first tank body (1) is provided with the first feed pieces (11), the second feed pieces (12) and discharging opening (14), described
The first charging aperture (21) being positioned at described second tank body (2) top it is provided with, it is characterised in that described on second tank body (2)
Arranging shaft one (13) in one tank body (1), described shaft one (13) passes bottom and the motor phase of described first tank body (1)
Even, described shaft one (13) has the hollow section of the opening on a top being arranged on described shaft one (13), described hollow
On the axial wall of section, discharge opening (131) is set, the outlet of described first feed pieces (11) and described second feed pieces (12)
Outlet is oppositely arranged, and forms mixing discharging opening between the two, and described mixing discharging opening is directed at the opening of described hollow section；Described go out
Between material mouth (14) and described first charging aperture (21), there is difference in height, described second tank body (2) also sets up the second charging aperture
(22), being provided with the shaft two (3) of interior sky in described second tank body (2), the inner chamber of described shaft two (3) connects to have and is positioned at
Described second tank body (2) air inlet pipe (4) outward, the axial wall of described shaft two (3) is provided with gas outlet (31).
Bentonite modifier preparation facilities the most according to claim 1, it is characterised in that described shaft two (3) includes axle
To section (32) and the traversing section (33) that is arranged on described axial direction part (32) end, described traversing section (33) includes base portion (331), sets
Put the stop part (332) in described base portion (331) front end and neutral portion (333).
Bentonite modifier preparation facilities the most according to claim 2, it is characterised in that described base portion (331) and described resistance
Stopper (332) is provided with the gas passage (334) communicating and communicating with the inner chamber of described shaft two (3), described gas passage
(334) the second gas outlet it is provided with.
Bentonite modifier preparation facilities the most according to claim 1, it is characterised in that different the second charging apertures (22)
Discharging direction at least two intersect.
Bentonite modifier preparation facilities the most according to claim 2, it is characterised in that described stop part (332) and described
Neutral portion (333) is arranged alternately, and the width in described neutral portion (333) is less than the width of described stop part (332).
Bentonite modifier preparation facilities the most according to claim 1, it is characterised in that described first feed pieces (11) and
Second feed pieces (12) all includes being arranged on the outer portion that feeds intake (111) arranging dog-house of described first tank body (1), is positioned at institute
Stating the feeder (112) in the first tank body (1), described feeder (112) has the braking section (1121) being positioned at front end.
Bentonite modifier preparation facilities the most according to claim 6, it is characterised in that the lower wall of described braking section (1121)
Extending reclaiming plate (1122), the leading section of the reclaiming plate of described first feed pieces (11) is positioned at described second feed pieces
(12) above reclaiming plate.
Bentonite modifier preparation facilities the most according to claim 6, it is characterised in that described first feed pieces (11) subtracts
The angle of inclination of speed section (1121) is more than the angle of inclination of described second feed pieces (12) braking section (1121).
Bentonite modifier preparation facilities the most according to claim 1, it is characterised in that described first feed pieces (11)
Feeder (112) lower section is provided with first and falls plate (113), and feeder (112) lower section of described second feed pieces (11) sets
Being equipped with second and fall plate (114), the described first leading section falling plate (113) is positioned at described first feed pieces (11) reclaiming plate
(1122) lower section, the second leading section falling plate (114) is positioned at the described first lower section falling plate (113).
Bentonite modifier preparation facilities the most according to claim 9, it is characterised in that described first, second falls plate
(113,114) all include breeze way, mixing section and the discharging section set gradually along Flow of Goods and Materials direction, and described mixing section is arranged
Wave flour mixed with adulterants, described mixing section is had to be obliquely installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620503349.1U CN205700563U (en) | 2016-05-30 | 2016-05-30 | Bentonite modifier preparation facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620503349.1U CN205700563U (en) | 2016-05-30 | 2016-05-30 | Bentonite modifier preparation facilities |
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| Publication Number | Publication Date |
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| CN205700563U true CN205700563U (en) | 2016-11-23 |
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| CN201620503349.1U Active CN205700563U (en) | 2016-05-30 | 2016-05-30 | Bentonite modifier preparation facilities |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854769A (en) * | 2016-05-30 | 2016-08-17 | 浙江红宇新材料股份有限公司 | Bentonite modifying agent preparation device |
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2016
- 2016-05-30 CN CN201620503349.1U patent/CN205700563U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105854769A (en) * | 2016-05-30 | 2016-08-17 | 浙江红宇新材料股份有限公司 | Bentonite modifying agent preparation device |
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