CN105854769A - Bentonite modifying agent preparation device - Google Patents
Bentonite modifying agent preparation device Download PDFInfo
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- CN105854769A CN105854769A CN201610366705.4A CN201610366705A CN105854769A CN 105854769 A CN105854769 A CN 105854769A CN 201610366705 A CN201610366705 A CN 201610366705A CN 105854769 A CN105854769 A CN 105854769A
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- Prior art keywords
- tank body
- feed pieces
- section
- shaft
- preparation facilities
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- 239000000440 bentonite Substances 0.000 title claims abstract description 30
- 229910000278 bentonite Inorganic materials 0.000 title claims abstract description 30
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title claims abstract description 26
- 239000003795 chemical substances by application Substances 0.000 title abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 48
- 238000007599 discharging Methods 0.000 claims description 24
- 239000003607 modifier Substances 0.000 claims description 18
- 230000007935 neutral effect Effects 0.000 claims description 13
- 235000013312 flour Nutrition 0.000 claims description 3
- 238000003756 stirring Methods 0.000 abstract description 20
- 230000000694 effects Effects 0.000 abstract description 15
- 238000012986 modification Methods 0.000 abstract description 3
- 230000004048 modification Effects 0.000 abstract description 3
- 150000003512 tertiary amines Chemical class 0.000 description 11
- 239000000203 mixture Substances 0.000 description 9
- 238000007790 scraping Methods 0.000 description 9
- 239000006185 dispersion Substances 0.000 description 5
- 238000010943 off-gassing Methods 0.000 description 5
- 239000000376 reactant Substances 0.000 description 5
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical class ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 3
- 239000010410 layer Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 229910052901 montmorillonite Inorganic materials 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- -1 borate ester Chemical class 0.000 description 1
- 239000002734 clay mineral Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 229940050176 methyl chloride Drugs 0.000 description 1
- 229910052756 noble gas Inorganic materials 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1862—Stationary reactors having moving elements inside placed in series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/006—Baffles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention provides a bentonite modifying agent preparation device which comprises a first tank body, a second tank body communicated with the first tank body and a third tank body communicated with the second tank body, wherein the first tank body is provided with a first feeding component, a second feeding component and a discharge hole; the first tank is internally provided with a stirring shaft I; the stirring shaft I penetrates through the bottom of the first tank body so as to be connected with the motor; the stirring shaft I is provided with a hollow section which is arranged at the stirring shaft I and is provided with an opening at the top end; the shaft wall of the hollow section is provided with a discharge hole; the outlet of the first feeding component is opposite to that of the second feeding component, and a mixed discharge hole is formed between the two outlets; the mixed discharge hole is aligned to the opening of the hollow section. By virtue of improving the material feeding mode, a stirring effect on materials is achieved; meanwhile, the stirring shaft is improved, so that the stirring efficiency is greatly improved, the quality of the modifying agent is improved, and the bentonite modification effect is relatively good.
Description
Technical field
The present invention 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 composition silicate.This mineral is the inorganic matter of natural nano level interlamellar spacing; sheet interlayer spacing about tens nanometer; there is special water absorption, hydroplasticity, caking property and stronger ion exchangeable etc.; being one of current range of application is the widest, economic worth is higher clay mineral, 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 bentonite is modified.
The most a lot of about to bentonite modified research, if the patent of invention of Patent No. CN102660159A is 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, the preparation of modifying agent is also even more important, 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, so the highest to the equipment requirements used in modifying agent preparation, due to factors such as stirrings in preparation process, often lead to can't meet the quality requirement.
Summary of the invention
It is an object of the invention to provide Bentonite modifier preparation facilities, for the preparation of modifying agent, bentonite modified quality can be improved.
The present invention adopts the following technical scheme that: Bentonite modifier preparation facilities, 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.
Technique scheme, the preparation of modifying agent uses two kinds of different materials to enter through two feed pieces, the exit position of two feed pieces of regulation, enables material to be sufficiently mixed, and Bentonite modifier raw material the most all uses 16 tertiary amines, 18 tertiary amines, for thick, this feeding manner, then by between on shaft one arrange discharge opening, material is thrown away and mixes, this thick material can be mixed evenly, react more abundant.
As preferably, described first feed pieces and the second feed pieces all include the portion that feeds intake arranging dog-house being arranged on outside described first tank body, are positioned at the feeder that described first tank body is outer, and 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 leading section of the reclaiming plate of described first feed pieces is positioned at above the reclaiming plate of described second feed pieces, by dropping into the reclaiming plate of the second feed pieces from the reclaiming plate of the first feed pieces, material can be broken up, play peptizaiton, thus preferably mix homogeneously.
As preferably, the angle of inclination of described first feed pieces braking section is more than the angle of inclination of described second feed pieces braking section, the speed that the speed that in first feed pieces, material drops drops more than material in the second feed pieces, ensure that material can stop in the second feed pieces, material drops into the reclaiming plate of the second feed pieces from the reclaiming plate of the first feed pieces, can break up material, dispersion, stopping mixing on the reclaiming plate of the second feed pieces, mixed effect is more preferable.
As preferably, it is provided with first below the feeder of described first feed pieces and falls plate, it is provided with second below the feeder of described second feed pieces and falls plate, described first leading section falling plate is positioned at below described first feed pieces reclaiming plate, and 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 repeatedly fall, breaks up, mix, and 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, fall certain degree of depth, it is unlikely to again the material impact power to next layer excessive, break up out completely, it is ensured that the exposure of two kinds of materials, be 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, 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, it is unlikely to immediately from falling plate landing, but through mixing section, strengthen mixed effect, described mixing section is provided with wave flour mixed with adulterants, 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, formation stream, and material below is broken up, mixed.
As preferably, the first charging aperture being positioned at described second tank body top it is provided with on described second tank body, between described discharging opening and described first charging aperture, there is difference in height, the second charging aperture and the 3rd charging aperture is also set up on described second tank body, it is provided with shaft two in described second tank body, described shaft two is hollow structure, and the inner chamber of described shaft two connects the air inlet pipe being positioned at outside described second tank body, and the axial wall of described shaft two is provided with gas outlet.
Such scheme, second tank body adds the third raw material, by arranging the difference in height between discharging opening and the first charging aperture, just can play material and break up, act on during charging, by the air inlet pipe outside the second tank body, if using gas raw material, such as the chloromethanes in Bentonite modifier, just it is passed through methyl chloride gas, it it is the mode added materials, the most this addition manner, can impact the material of the inside again, immixture, improves the efficiency of reaction；Without gas raw material, noble gas can be used, there is 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, improves 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 more preferable mixed effect.
As preferably, described shaft two includes axial direction part and is arranged on the traversing section of described axial direction part end, described traversing section includes base portion, the stop part being arranged on described base portion front end and neutral portion, by neutral portion, material is broken up, in particular for thick material, play more preferable mixed effect.
As preferably, described base portion and described stop part are provided with the gas passage communicating and communicating with the inner chamber of described shaft two, and 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 the width of described stop part, and the dispersion to material is more abundant.
As preferably, the axial direction part of described shaft two arranging stirring parts and the second scraping blade, the outgassing direction of the gas outlet inside described second scraping blade is parallel to described second scraping blade.
As preferably, described stirring parts includes the second paddle being parallel to each other that the root being connected with described shaft two is connected with described root, and described second paddle is provided with perforation.
By implementing technique scheme, the present invention has a following beneficial effect: the present invention is directed to bentonite modified during the preparation of modifying agent, reasonable in design, by improving the addition manner to material, make it that material is had stirring action, shaft is improved simultaneously, be greatly improved stirring efficiency, improve the quality of modifying agent, more preferable to alta-mud modification effect.
Accompanying drawing explanation
Accompanying drawing 1Structural representation for one embodiment of the inventionFigure；
Accompanying drawing 2For the first tank interior signal in one embodiment of the inventionFigure；
Accompanying drawing 3For the second tank body signal in one embodiment of the inventionFigure。
Detailed description of the invention
Below in conjunction withAccompanying drawingAnd specific embodiment, the present invention is described in further detail.
Embodiment 1:
A kind of Bentonite modifier preparation facilities, asAccompanying drawing 1Shown in, including first tank body the 1, second tank body 2 being sequentially communicated connection.The structure of the first tank body 1 is such asAccompanying drawing 2Shown in, it is provided with and is 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 as a example by 16 tertiary amines and 18 tertiary amines, in first tank body 1, shaft 1 is set, shaft 1 is connected through the bottom of the first tank body 1 with motor, shaft 1 has the hollow section of the opening on a top being arranged on shaft 1, discharge opening 131 is set on the axial wall of hollow section, outer wall is provided with paddle and axially arranged scraping blade, some through holes it are provided with on paddle, depending on number is according to the area of paddle and the viscosity of stirring thing, area is the biggest, viscosity is the biggest, the most.
The structure of the second tank body 2 is such asAccompanying drawing 3Shown in, it is provided with multiple second charging aperture 22 and is positioned at first charging aperture 21 on the second tank body 2 top, second charging aperture 22 adds raw water, first charging aperture 21 adds the mixture of tertiary amine in the first tank body 1, the discharging direction of the second different charging apertures 22 has two to intersect, the present embodiment the second charging aperture 22 arranges two, and material is separately introduced, and improves reaction efficiency.Between discharging opening 14 and the first charging aperture 21, there is difference in height, it is provided with shaft 23 in second tank body 2, shaft 23 is hollow structure, the inner chamber of shaft 23 connects the air inlet pipe 4 being positioned at outside described second tank body 2, gas outlet 31 it is provided with, the non-parallel setting of outgassing direction of gas outlet 31 on the axial wall of shaft 23.
The outlet of the first feed pieces 11 and the outlet of described second feed pieces 12 are oppositely arranged, form mixing discharging opening between the two, being directed at the opening of described hollow section, material enters from first, second feeder, can tentatively mix in both exits, blended discharging opening enters the hollow section of shaft 1, under the rotation of shaft 1, throw away through discharge opening 131, carry out secondary mixing, again under the stirring of shaft 1, finally mix.First feed pieces 11 and the second feed pieces 12 all include the portion that feeds intake 111 arranging dog-house being arranged on outside described first tank body 1, it is positioned at the feeder 112 of the first tank body 1, feeder 112 has the braking section 1121 being positioned at front end, braking section 1121 makes material the most quickly drop, the time being fully contacted to the material of two feed pieces outlets, and first the angle of inclination of feed pieces 11 braking section 1121 more than the angle of inclination of the second feed pieces 12 braking section 1121, preferably, 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 above the reclaiming plate of described 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 leading section falling plate 113 is positioned at below described first feed pieces 11 reclaiming plate 1122, and the second leading section falling plate 114 is positioned at the described first lower section falling plate 113.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, and described traversing section 33 includes base portion 331, the stop part 332 being arranged on described base portion 331 front end and neutral portion 333；Stop part 332 and neutral portion 333 are 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 are provided with the gas passage 334 communicating and communicating with the inner chamber of described shaft 23, and 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.The first feed pieces 11 and the second feed pieces 12 being separately added into two kinds of reactants it is provided with on first tank body 1, it is provided with on first tank body 1 and is 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 as a example by 16 tertiary amines and 18 tertiary amines, in first tank body 1, shaft 1 is set, shaft 1 is connected through the bottom of the first tank body 1 with motor, shaft 1 has the hollow section of the opening on a top being arranged on shaft 1, discharge opening 131 is set on the axial wall of hollow section, outer wall is provided with paddle and axially arranged scraping blade, some through holes it are provided with on paddle, depending on number is according to the area of paddle and the viscosity of stirring thing, area is the biggest, 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, second charging aperture 22 adds raw water, first charging aperture 21 adds the mixture of tertiary amine in the first tank body 1, the discharging direction of the second different charging apertures 22 has three to intersect, the present embodiment the second charging aperture 22 arranges three, material is separately introduced, and improves reaction efficiency.Between discharging opening 14 and the first charging aperture 21, there is difference in height, it is provided with shaft 23 in second tank body 2, shaft 23 is hollow structure, the inner chamber of shaft 23 connects the air inlet pipe 4 being positioned at outside described second tank body 2, gas outlet 31 it is provided with, the non-parallel setting of outgassing direction of gas outlet 31 on the axial wall of shaft 23.
The outlet of the first feed pieces 11 and the outlet of described second feed pieces 12 are oppositely arranged, form mixing discharging opening between the two, being directed at the opening of described hollow section, material enters from first, second feeder, can tentatively mix in both exits, blended discharging opening enters the hollow section of shaft 1, under the rotation of shaft 1, throw away through discharge opening 131, carry out secondary mixing, again under the stirring of shaft 1, finally mix.First feed pieces 11 and the second feed pieces 12 all include the portion that feeds intake 111 arranging dog-house being arranged on outside described first tank body 1, it is positioned at the feeder 112 of the first tank body 1, feeder 112 has the braking section 1121 being positioned at front end, braking section 1121 makes material the most quickly drop, the time being fully contacted to the material of two feed pieces outlets, and first the angle of inclination of feed pieces 11 braking section 1121 more than the angle of inclination of the second feed pieces 12 braking section 1121, preferably, 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 above the reclaiming plate of described 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 leading section falling plate 113 is positioned at below described first feed pieces 11 reclaiming plate 1122, and the second leading section falling plate 114 is positioned at the described first lower section falling plate 113.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, it is unlikely to immediately from falling plate landing, but through mixing section, strengthen mixed effect, 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, and described traversing section 33 includes base portion 331, the stop part 332 being arranged on described base portion 331 front end and neutral portion 333；Stop part 332 and neutral portion 333 are 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 are provided with the gas passage 334 communicating and communicating with the inner chamber of described shaft 23, and gas passage 334 is provided with the second gas outlet.Arranging stirring parts and the second scraping blade on the axial direction part of shaft 23, the outgassing direction of the gas outlet inside described second scraping blade is parallel to described second scraping blade.Stirring parts includes the second paddle being parallel to each other that the root being connected with described shaft 23 is connected with described root, and described second paddle is provided with perforation.
Claims (10)
- null1. Bentonite modifier preparation facilities，Including the first tank body (1) and the second tank body (2) of communicating with described first tank body (1)，It is provided with the first feed pieces (11) on described first tank body (1)、Second feed pieces (12) and discharging opening (14)，The first charging aperture (21) being positioned at described second tank body (2) top it is provided with on described second tank body (2)，It is characterized in that，The first feed pieces (11) and the second feed pieces (12) it is provided with on described first tank body (1)，In described first tank body (1), shaft one (13) is set，Described shaft one (13) is connected through the bottom of described first tank body (1) with motor，Described shaft one (13) has the hollow section of the opening on a top being arranged on described shaft one (13)，Discharge opening (131) is set on the axial wall of described hollow section，The outlet of described first feed pieces (11) and the outlet of described second feed pieces (12) are oppositely arranged，Form mixing discharging opening between the two，Described mixing discharging opening is directed at the opening of described hollow section；Between described discharging opening (14) and described first charging aperture (21), there is difference in height, the second charging aperture (22) is also set up on described second tank body (2), the shaft two (3) of interior sky it is provided with in described second tank body (2), the inner chamber of described shaft two (3) connects the air inlet pipe (4) being positioned at described second tank body (2) outward, and 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 characterized in that, described shaft two (3) includes axial direction part (32) and is arranged on the traversing section (33) of described axial direction part (32) end, and described traversing section (33) includes base portion (331), the stop part (332) being arranged on described base portion (331) front end and neutral portion (333).
- Bentonite modifier preparation facilities the most according to claim 2, it is characterized in that, described base portion (331) and described stop part (332) are provided with the gas passage (334) communicating and communicating with the inner chamber of described shaft two (3), and described gas passage (334) is provided with the second gas outlet.
- Bentonite modifier preparation facilities the most according to claim 1, it is characterised in that the discharging direction of different the second charging apertures (22) 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) are 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 characterized in that, described first feed pieces (11) and the second feed pieces (12) all include being arranged on the outer portion that feeds intake (111) arranging dog-house of described first tank body (1), are positioned at the feeder (112) of described first tank body (1), and 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 characterized in that, the lower wall of described braking section (1121) extends reclaiming plate (1122), and the leading section of the reclaiming plate of described first feed pieces (11) is positioned at above the reclaiming plate of described second feed pieces (12).
- Bentonite modifier preparation facilities the most according to claim 6, it is characterised in that the angle of inclination of described first feed pieces (11) braking 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 characterized in that, feeder (112) lower section of described first feed pieces (11) is provided with first and falls plate (113), feeder (112) lower section of described second feed pieces (11) is provided with second and falls plate (114), described first leading section falling plate (113) is positioned at described first feed pieces (11) reclaiming plate (1122) lower section, and 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 characterized in that, described first, second falls breeze way, mixing section and the discharging section that plate (113,114) all includes setting gradually along Flow of Goods and Materials direction, described mixing section is provided with wave flour mixed with adulterants, and described mixing section is obliquely installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610366705.4A CN105854769B (en) | 2016-05-30 | 2016-05-30 | Bentonite modifier preparation facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610366705.4A CN105854769B (en) | 2016-05-30 | 2016-05-30 | Bentonite modifier preparation facilities |
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| Publication Number | Publication Date |
|---|---|
| CN105854769A true CN105854769A (en) | 2016-08-17 |
| CN105854769B CN105854769B (en) | 2018-02-02 |
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| CN201610366705.4A Active CN105854769B (en) | 2016-05-30 | 2016-05-30 | Bentonite modifier preparation facilities |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114471317A (en) * | 2022-02-09 | 2022-05-13 | 山东畜牧兽医职业学院 | Low-fat ice cream processing equipment |
| CN114768730A (en) * | 2022-05-07 | 2022-07-22 | 上海蕙黔化工科技有限公司 | A mixing device that is used for gas phase method oxo process dimethyl carbonate |
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| US1375406A (en) * | 1919-07-02 | 1921-04-19 | Merrell Soule Co | Agitator |
| CN87103450A (en) * | 1986-05-12 | 1988-03-23 | 三菱重工业株式会社 | The equipment that is used for Treatment Solution or processing mud solution |
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| CN114471317A (en) * | 2022-02-09 | 2022-05-13 | 山东畜牧兽医职业学院 | Low-fat ice cream processing equipment |
| CN114768730A (en) * | 2022-05-07 | 2022-07-22 | 上海蕙黔化工科技有限公司 | A mixing device that is used for gas phase method oxo process dimethyl carbonate |
| CN114768730B (en) * | 2022-05-07 | 2023-11-21 | 上海蕙黔新材料科技有限公司 | Mixing device for synthesizing dimethyl carbonate by gas phase method carbonyl |
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|---|---|
| CN105854769B (en) | 2018-02-02 |
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