CN106369982A - Efficient additive processing device - Google Patents
Efficient additive processing device Download PDFInfo
- Publication number
- CN106369982A CN106369982A CN201610742487.XA CN201610742487A CN106369982A CN 106369982 A CN106369982 A CN 106369982A CN 201610742487 A CN201610742487 A CN 201610742487A CN 106369982 A CN106369982 A CN 106369982A
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- China
- Prior art keywords
- inner housing
- steel ball
- rotating shaft
- stirring
- drying machine
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/04—Heating arrangements using electric heating
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Food Science & Technology (AREA)
- Crushing And Pulverization Processes (AREA)
Abstract
The invention discloses an efficient additive processing device. The efficient additive processing device is characterized by comprising a screw conveyor, a drying machine, an intermediate heater, a cyclone separator and an induced draft fan; a feeding hopper is arranged on the screw conveyor, the right end of the drying machine communicates with a hot air pipe, and the intermediate heater is arranged on a pipeline between the drying machine and the cyclone separator; the hot air pipe is branched to form one pipeline to the intermediate heater to serve as a heating source, and a heating coil is wound around a shell of the drying machine; and a humidity detector is arranged on the inner wall of a material collecting hopper at the bottom of the cyclone separator, and a manual valve for discharging is arranged at the bottom of the material collecting hopper.
Description
Technical field
The present invention relates to additive manufacture field is and in particular to a kind of efficient additive processing unit (plant).
Background technology
Additive is a kind of chemical substance that the fields such as chemical industry are commonly used, and existing additive often has drying effect not
The shortcomings of good, humidity control is ineffective, additive granules are excessive is it is therefore necessary to design a kind of efficient additive processing unit (plant).
Content of the invention
For the problems referred to above, the present invention provides a kind of efficient additive processing unit (plant).
The purpose of the present invention employs the following technical solutions to realize:
A kind of efficient additive processing unit (plant), including conveying worm, drying machine, intermediate heater, cyclone separator and
Air-introduced machine, conveying worm is provided with into funnel, the right-hand member of exsiccator is communicated with warm-air pipe, and intermediate heater is arranged on dry
On pipeline between dry machine and cyclone separator, warm-air pipe separates a road pipeline to intermediate heater as heat source, is dried
It is wound with heating coil on the shell of machine；It is provided with moisture detector, aggregate bin on the aggregate bin inwall of cyclone separator bottom
Bottom be provided with the hand-operated valve for blowing.
Have the beneficial effect that the drying machine of the dual-heated by warm-air pipe and heating coil, can effectively improve and effect is dried
Really, the setting of intermediate heater simultaneously also can improve the drying effect of second half section, and the humidity sensor of cyclone separator bottom
The humidity control dynamics of whole device can be improved, simple and practical, it is suitable for promoting the use of.
Brief description
Using accompanying drawing, the invention will be further described, but the embodiment in accompanying drawing does not constitute any limit to the present invention
System, for those of ordinary skill in the art, on the premise of not paying creative work, can also obtain according to the following drawings
Other accompanying drawings.
Fig. 1 is the overall structure diagram of the present invention；
Fig. 2 is the overall structure diagram of wet type high pressure reducing mechanism；
Fig. 3 is the structural representation of main disintegrating apparatus；
Fig. 4 is the structural representation of hydraulic stirring equipment；
Fig. 5 is the structural representation driving in cylinder.
Reference: conveying worm -1；Drying machine -2；Intermediate heater -3；Cyclone separator -4；Air-introduced machine -5；Water
Case -6；Multistage centrifugal hydro pump -7；Mixing chamber -8；Feeder -9；First target body -10；Conducting element -11；Second target body-
12；First control valve -13；Second control valve -14；Accelerating tube -15；Introduce pipe -16；Bifurcation structure -17；Shell body -18；Inner shell
Body -19；First pulverizing steel ball -20；Percussion body -21；First filter screen -22；Inner housing outlet -23；Shell body outlet -24；
First stirring parts -25；Second stirring parts -26；First rotating shaft -27；First stirring rod -28；Second rotating shaft -29；Second stirring rod-
30；Second pulverizing steel ball -31；Protection baffle -32；Pooled portion -33；First furcation -34；Second furcation -35；Casing-
36；Water inlet pipe -37；Outlet pipe -38；Spoke -39；Drive cylinder -40；Bearing holder (housing, cover) -41；Travelling gear -42；Left boss -43；Right
Boss -44；Second filter screen -45；Enter funnel -100；Warm-air pipe -101；Heating coil -102；Aggregate bin -103；Humidity Detection
Device -104；Hand-operated valve -105；Wet type high pressure reducing mechanism -106.
Specific embodiment
The invention will be further described with the following Examples.
Application scenarios 1:
A kind of efficient additive processing unit (plant) as shown in Figure 1, including conveying worm 1, drying machine 2, intermediate heater
3rd, cyclone separator 4 and air-introduced machine 5, conveying worm 1 is provided with into funnel 100, the right-hand member of exsiccator 2 is communicated with hot blast
Pipe 101, intermediate heater 3 is arranged on the pipeline between drying machine 2 and cyclone separator 4, and warm-air pipe 101 separates a road pipeline
To intermediate heater 3 as heat source, the shell of drying machine 2 is wound with heating coil 102；Cyclone separator 4 bottom
Moisture detector 104 is provided with aggregate bin 103 inwall, the bottom of aggregate bin 103 is provided with the hand-operated valve 105 for blowing.
The present invention passes through the drying machine of the dual-heated of warm-air pipe and heating coil, can effectively improve drying effect, with
When intermediate heater setting also can improve the drying effect of second half section, and the humidity sensor of cyclone separator bottom can improve
The humidity control dynamics of whole device, simple and practical, it is suitable for promoting the use of.
Preferably, intermediate heater 3 is pipe heat exchanger.
Preferably, also include wet type high pressure reducing mechanism 106, untreated additive powder pulverizes dress through wet type high pressure
Put 106 broken after, through precipitation, tentatively air-dry after delivered in conveying worm 1 by entering funnel 100, subsequently enter drying machine 2
It is dried, eventually pass after cyclone separator 4 separates and qualified additive powder is discharged by hand-operated valve 105.
Preferably, as Figure 2-3, wet type high pressure reducing mechanism 106 include water tank 6, multistage centrifugal hydro pump 7,
Mixing chamber 8, feeder 9, the first target body 10, conducting element 11, the second target body 12, the first control valve 13, the second control valve 14, master are broken
Broken equipment and hydraulic stirring equipment.Feeder 9 is arranged on mixing chamber 8, enters mixing without broken powder body by feeder 9
In room 8.First target body 10 is arranged on inwall at pipeline turning, and conducting element 11 is obliquely installed and its one end is fixed in the first target body
On 10, the second target body 12 first target body 10 relatively is arranged on inner-walls of duct.Multistage centrifugal hydro pump 7 is by water tank 6
Water is pressurised into supertension, is accelerated by accelerating tube 15 after mixing chamber 8 is mixed with powder body, subsequently clashes into the first target body 10 and carries out just
Step is broken, and is guided by baffle 11 and carry out second-time breakage to the second target body 12, subsequently enters to become owner of disintegrating apparatus by introducing pipe 16.
2 road pipelines are led to, road first control valve 13 enters hydraulic stirring at the centre tap of multistage centrifugal hydro pump 7
Equipment, road second control valve 14 is tangentially entered the left bottom of inner housing 19 by bifurcation structure 17.
Main disintegrating apparatus includes shell body 18, inner housing 19, first pulverizes steel ball 20, percussion body 21, the first filter screen 22, interior
Housing outlet 23, shell body outlet 24, the first stirring parts 25 and the second stirring parts 26.Shell body 18 and inner housing 19 are same
The hollow cylinder of axle setting, the first pulverizing steel ball 20 is arranged on the within the chamber that inner housing 19 is located at the first filter screen 22 left side.Touch
Hit body 21 to be arranged in the top inner wall of inner housing 19, percussion body 21 is inverted bullet, and its cross-sectional axis vertically arranged,
The crushing strength that both sides so can be ensured to greatest extent is unanimously so that the fineness of powder finally obtaining is as far as possible uniform.Introduce
Pipe 16 is connected with inner housing 19 by the bottom minimum point of inner housing 19.Inner housing outlet 23 is arranged on the right side of inner housing 19
Side, the first filter screen 22 is arranged on the middle part of inner housing 19.It is additionally provided with the second pulverizing steel ball between inner housing 19 and shell body 18
31, inner housing outlet 23 has the protection baffle 32 of one section of bending that Open Side Down, and protection baffle 32 is used for protection first
The second pulverizing steel ball 31 that stirring parts 25 and the second stirring parts 26 are not fallen smashes, and is simultaneously used for guiding and is flowed out by inner housing
Mixture moves along the circumferencial direction of shell body 18.In the left side of protection baffle 32, between inner housing 19 and shell body 18 also
It is connected with the second filter screen 45, second pulverizes steel ball 31 is located in the space on the second filter screen 45 right side, and the first filter screen 22 and second is filtered
Net 45 is mainly used in stopping that steel ball passes through.Due to from inner housing outlet 23 mixture kinetic energy out compared to entering inner housing
19 mixture kinetic energy is little, so the weight of the second pulverizing steel ball 31 is set smaller than the weight of the first pulverizing steel ball 20, with
Ensure that the second pulverizing steel ball 31 can be driven.The quality of the second pulverizing steel ball 31 is the 3/5 of the first pulverizing steel ball 20 mass, same
Deng under power consumption up to minimum powder fineness reduce 10% than before not transforming.
As illustrated in figures 4-5, the first stirring parts 25 include first rotating shaft 27 and multiple first stirring rod 28, the second stirring parts 26
Including the second rotating shaft 29 and multiple second stirring rod 30, first rotating shaft 27 and the second rotating shaft 29 are and are horizontally disposed with, the first stirring
Rod 28 and the second stirring rod 30 are respectively perpendicular and are arranged in first rotating shaft 27 and the second rotating shaft 29, and the first stirring rod 28 and second
Stagger arrangement occlusion setting between stirring rod 30, the mode of this stagger arrangement snap-fit arrangement can effectively strengthen crushing effect.Shell body draws
Outlet 24 is communicated in the left side of shell body 18.Bifurcation structure 17 includes pooled portion 33, the first furcation 34 and the second furcation 35,
The lower end of pooled portion 33 is connected with the pipeline of the first control valve 13, and its upper end connects the first furcation 34 and the second furcation
35.First furcation 34 and the second furcation 35 are tangent with inner housing 19 respectively, and both axial length h are equal to the first filter
Net 22 and the distance between inner housing 19 left end h, the combination length introducing pipe 16 with inner housing 19 bottom is equal to the first furcation
34 axial length h, such setting ensure that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement.
In this embodiment, (1) devises a kind of new multi-stage crushing rotating vane type high pressure disintegrating apparatus 3, this reducing mechanism
For the circulating setting of inside and outside steel ball, in the higher inner housing of high pressure water kinetic energy 19, using tangential bifurcation structure 17 with touch
Hit the setting of body 21 so that occurring upper and lower relative motion to produce noticeable effort between mixture to be comminuted and the steel ball of whereabouts
Clash into, this reverse breaking method crushing effect for traditional steel ball trailing type is pulverized greatly reinforces, Er Qie
The driving force of one pulverizing steel ball 20 is to be realized using the intermediate tap pressure of centrifugal multistage pump multiple centrifugal pump, and motor that need not be extra etc. sets
Standby investment, cost substantially reduces；By the setting of inner housing outlet 23 and protection baffle 32, using water under high pressure complementary energy outside
The steel ball carrying out less quality again in shell is pulverized, and the energy of high-pressure hydraulic pump is fully utilized, in equal power consumption
Under accessible smashing fineness greatly improve, second pulverizing steel ball 31 quality be the 3/5 of the first pulverizing steel ball 20 mass, with
Deng under power consumption up to minimum powder fineness reduce 10% than before not transforming；(2) taken into full account the guarantor to mixing plant
Protect the needs with fluid flow characteristics and devise protection baffle 32.(3) devise the bifurcation structure 17 of uniqueness, its cooperation is drawn
Enter the setting of pipe 16 and relative dimensions, can guarantee that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement it is ensured that equipment reliability of operation.
Preferably, hydraulic stirring equipment includes casing 36, water inlet pipe 37, outlet pipe 38, multiple spoke 39, drives cylinder
40, the left end of first rotating shaft 27 and the second rotating shaft 28 is sleeved in the bearing holder (housing, cover) 41 on inner housing outlet 23 side wall, the other end
Through inner housing 19 and extend through casing 36, and the second rotating shaft 28 extends to drive in cylinder 40.Hollow cylindrical form
Driving cylinder 40 be arranged in casing 36, the water inlet pipe 37 being connected with the first control valve 13 pass through casing 36 and with drive cylinder
40 bottom is connected, and the outlet pipe 38 being connected with shell body outlet 24 is connected to the top driving cylinder 40.First rotating shaft
Be provided with travelling gear 42 between the second rotating shaft 29 in 27 right-hand member and casing 36, travelling gear 42 respectively with first rotating shaft 27
It is meshed with the second rotating shaft 29, first rotating shaft 27 and the second rotating shaft 29 are provided with for the groove that engages in engagement place that (in figure is not
Illustrate), and the length of groove is suitable with the width of travelling gear 42.Multiple spokes 39 are distributed in the second rotating shaft 30, and are located at
Drive in cylinder 40.All it is connected with first rotating shaft 27 and the second rotating shaft 29 for ensureing between two rotating shafts and travelling gear 42
The constant left boss in the position of engagement 43 and right boss 44, left boss 43 and right boss 44 are located at the both sides of travelling gear 42 respectively.
As can be seen that the first stirring parts 25 and the second stirring parts 26 are the stirring pairs enabling for a pair to relatively rotate when running, significantly carry
The effect that high stirring is pulverized.
Tangentially entered through bifurcation structure 17 by the unmixed water under high pressure that the centre tap of multistage centrifugal hydro pump 7 comes
Enter 19 in inner housing, drive first to pulverize steel ball 20 along the wall of inner housing 19 from bottom to top movements, the first pulverizing steel
Ball 20 is moved downward with percussion body 21 collision rift at top, simultaneously through the first target body 10 and the broken mixing of the second target body 11
Thing enters in inner housing 19 by introducing pipe 16 from the bottom of inner housing 19, the mixture that moves from bottom to top with move from top to bottom
The first pulverizing steel ball 20 mutually clashes into generation fragmentation, pulverize the driving in pressure for the broken mixture of steel ball 20 through first
Lower tangentially flow in the space between inner housing 19 and shell body 18 from inner housing outlet 23 through the first filter screen 22, drive the
Two pulverize steel ball 31 along the inner surface movement of shell body 18 to be crushed to mixture again, and finally by shell body outlet 24
Flow out.Water under high pressure in the water inlet pipe 37 simultaneously being controlled by the first control valve 13 enters to drive and impacts spoke 39 in cylinder 40, from
And drive the first stirring parts 25 to rotate, and drive the second stirring parts 26 to rotate by travelling gear 42, internal in the way of stirring
Housing outlet 23 mixture out is crushed, drive cylinder 40 in do work after water under high pressure from outlet pipe 38 flow out and with
Shell body outlet 24 mixture out enters next process after converging.
In this embodiment, devise the hydraulic stirring including parts such as spoke 39, water inlet pipe 37, outlet pipes 38 to set
Standby, the power of this mixing plant, and can be with multistage centrifugal also from the centre tap of multistage centrifugal hydro pump 7
The start and stop of high-pressure hydraulic pump 7 and automatic start-stop, eliminate the control program of complexity and the configuration of motor so that crushing effect is strengthened
While run and cost of investment reduce；By the design of travelling gear 42 and the stirring rod of stagger arrangement occlusion, the first stirring parts 25
It is the stirring pair enabling for a pair to relatively rotate when running with the second stirring parts 26, substantially increase the effect that stirring is pulverized.
Application scenarios 2:
A kind of efficient additive processing unit (plant) as shown in Figure 1, including conveying worm 1, drying machine 2, intermediate heater
3rd, cyclone separator 4 and air-introduced machine 5, conveying worm 1 is provided with into funnel 100, the right-hand member of exsiccator 2 is communicated with hot blast
Pipe 101, intermediate heater 3 is arranged on the pipeline between drying machine 2 and cyclone separator 4, and warm-air pipe 101 separates a road pipeline
To intermediate heater 3 as heat source, the shell of drying machine 2 is wound with heating coil 102；Cyclone separator 4 bottom
Moisture detector 104 is provided with aggregate bin 103 inwall, the bottom of aggregate bin 103 is provided with the hand-operated valve 105 for blowing.
The present invention passes through the drying machine of the dual-heated of warm-air pipe and heating coil, can effectively improve drying effect, with
When intermediate heater setting also can improve the drying effect of second half section, and the humidity sensor of cyclone separator bottom can improve
The humidity control dynamics of whole device, simple and practical, it is suitable for promoting the use of.
Preferably, intermediate heater 3 is pipe heat exchanger.
Preferably, also include wet type high pressure reducing mechanism 106, untreated additive powder pulverizes dress through wet type high pressure
Put 106 broken after, through precipitation, tentatively air-dry after delivered in conveying worm 1 by entering funnel 100, subsequently enter drying machine 2
It is dried, eventually pass after cyclone separator 4 separates and qualified additive powder is discharged by hand-operated valve 105.
Preferably, as Figure 2-3, wet type high pressure reducing mechanism 106 include water tank 6, multistage centrifugal hydro pump 7,
Mixing chamber 8, feeder 9, the first target body 10, conducting element 11, the second target body 12, the first control valve 13, the second control valve 14, master are broken
Broken equipment and hydraulic stirring equipment.Feeder 9 is arranged on mixing chamber 8, enters mixing without broken powder body by feeder 9
In room 8.First target body 10 is arranged on inwall at pipeline turning, and conducting element 11 is obliquely installed and its one end is fixed in the first target body
On 10, the second target body 12 first target body 10 relatively is arranged on inner-walls of duct.Multistage centrifugal hydro pump 7 is by water tank 6
Water is pressurised into supertension, is accelerated by accelerating tube 15 after mixing chamber 8 is mixed with powder body, subsequently clashes into the first target body 10 and carries out just
Step is broken, and is guided by baffle 11 and carry out second-time breakage to the second target body 12, subsequently enters to become owner of disintegrating apparatus by introducing pipe 16.
2 road pipelines are led to, road first control valve 13 enters hydraulic stirring at the centre tap of multistage centrifugal hydro pump 7
Equipment, road second control valve 14 is tangentially entered the left bottom of inner housing 19 by bifurcation structure 17.
Main disintegrating apparatus includes shell body 18, inner housing 19, first pulverizes steel ball 20, percussion body 21, the first filter screen 22, interior
Housing outlet 23, shell body outlet 24, the first stirring parts 25 and the second stirring parts 26.Shell body 18 and inner housing 19 are same
The hollow cylinder of axle setting, the first pulverizing steel ball 20 is arranged on the within the chamber that inner housing 19 is located at the first filter screen 22 left side.Touch
Hit body 21 to be arranged in the top inner wall of inner housing 19, percussion body 21 is inverted bullet, and its cross-sectional axis vertically arranged,
The crushing strength that both sides so can be ensured to greatest extent is unanimously so that the fineness of powder finally obtaining is as far as possible uniform.Introduce
Pipe 16 is connected with inner housing 19 by the bottom minimum point of inner housing 19.Inner housing outlet 23 is arranged on the right side of inner housing 19
Side, the first filter screen 22 is arranged on the middle part of inner housing 19.It is additionally provided with the second pulverizing steel ball between inner housing 19 and shell body 18
31, inner housing outlet 23 has the protection baffle 32 of one section of bending that Open Side Down, and protection baffle 32 is used for protection first
The second pulverizing steel ball 31 that stirring parts 25 and the second stirring parts 26 are not fallen smashes, and is simultaneously used for guiding and is flowed out by inner housing
Mixture moves along the circumferencial direction of shell body 18.In the left side of protection baffle 32, between inner housing 19 and shell body 18 also
It is connected with the second filter screen 45, second pulverizes steel ball 31 is located in the space on the second filter screen 45 right side, and the first filter screen 22 and second is filtered
Net 45 is mainly used in stopping that steel ball passes through.Due to from inner housing outlet 23 mixture kinetic energy out compared to entering inner housing
19 mixture kinetic energy is little, so the weight of the second pulverizing steel ball 31 is set smaller than the weight of the first pulverizing steel ball 20, with
Ensure that the second pulverizing steel ball 31 can be driven.The quality of the second pulverizing steel ball 31 is the 4/5 of the first pulverizing steel ball 20 mass, same
Deng under power consumption up to minimum powder fineness reduce 14% than before not transforming.
As illustrated in figures 4-5, the first stirring parts 25 include first rotating shaft 27 and multiple first stirring rod 28, the second stirring parts 26
Including the second rotating shaft 29 and multiple second stirring rod 30, first rotating shaft 27 and the second rotating shaft 29 are and are horizontally disposed with, the first stirring
Rod 28 and the second stirring rod 30 are respectively perpendicular and are arranged in first rotating shaft 27 and the second rotating shaft 29, and the first stirring rod 28 and second
Stagger arrangement occlusion setting between stirring rod 30, the mode of this stagger arrangement snap-fit arrangement can effectively strengthen crushing effect.Shell body draws
Outlet 24 is communicated in the left side of shell body 18.Bifurcation structure 17 includes pooled portion 33, the first furcation 34 and the second furcation 35,
The lower end of pooled portion 33 is connected with the pipeline of the first control valve 13, and its upper end connects the first furcation 34 and the second furcation
35.First furcation 34 and the second furcation 35 are tangent with inner housing 19 respectively, and both axial length h are equal to the first filter
Net 22 and the distance between inner housing 19 left end h, the combination length introducing pipe 16 with inner housing 19 bottom is equal to the first furcation
34 axial length h, such setting ensure that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement.
In this embodiment, (1) devises a kind of new multi-stage crushing rotating vane type high pressure disintegrating apparatus 3, this reducing mechanism
For the circulating setting of inside and outside steel ball, in the higher inner housing of high pressure water kinetic energy 19, using tangential bifurcation structure 17 with touch
Hit the setting of body 21 so that occurring upper and lower relative motion to produce noticeable effort between mixture to be comminuted and the steel ball of whereabouts
Clash into, this reverse breaking method crushing effect for traditional steel ball trailing type is pulverized greatly reinforces, Er Qie
The driving force of one pulverizing steel ball 20 is to be realized using the intermediate tap pressure of centrifugal multistage pump multiple centrifugal pump, and motor that need not be extra etc. sets
Standby investment, cost substantially reduces；By the setting of inner housing outlet 23 and protection baffle 32, using water under high pressure complementary energy outside
The steel ball carrying out less quality again in shell is pulverized, and the energy of high-pressure hydraulic pump is fully utilized, in equal power consumption
Under accessible smashing fineness greatly improve, second pulverizing steel ball 31 quality be the 4/5 of the first pulverizing steel ball 20 mass, with
Deng under power consumption up to minimum powder fineness reduce 14% than before not transforming；(2) taken into full account the guarantor to mixing plant
Protect the needs with fluid flow characteristics and devise protection baffle 32.(3) devise the bifurcation structure 17 of uniqueness, its cooperation is drawn
Enter the setting of pipe 16 and relative dimensions, can guarantee that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement it is ensured that equipment reliability of operation.
Preferably, hydraulic stirring equipment includes casing 36, water inlet pipe 37, outlet pipe 38, multiple spoke 39, drives cylinder
40, the left end of first rotating shaft 27 and the second rotating shaft 28 is sleeved in the bearing holder (housing, cover) 41 on inner housing outlet 23 side wall, the other end
Through inner housing 19 and extend through casing 36, and the second rotating shaft 28 extends to drive in cylinder 40.Hollow cylindrical form
Driving cylinder 40 be arranged in casing 36, the water inlet pipe 37 being connected with the first control valve 13 pass through casing 36 and with drive cylinder
40 bottom is connected, and the outlet pipe 38 being connected with shell body outlet 24 is connected to the top driving cylinder 40.First rotating shaft
Be provided with travelling gear 42 between the second rotating shaft 29 in 27 right-hand member and casing 36, travelling gear 42 respectively with first rotating shaft 27
It is meshed with the second rotating shaft 29, first rotating shaft 27 and the second rotating shaft 29 are provided with for the groove that engages in engagement place that (in figure is not
Illustrate), and the length of groove is suitable with the width of travelling gear 42.Multiple spokes 39 are distributed in the second rotating shaft 30, and are located at
Drive in cylinder 40.All it is connected with first rotating shaft 27 and the second rotating shaft 29 for ensureing between two rotating shafts and travelling gear 42
The constant left boss in the position of engagement 43 and right boss 44, left boss 43 and right boss 44 are located at the both sides of travelling gear 42 respectively.
As can be seen that the first stirring parts 25 and the second stirring parts 26 are the stirring pairs enabling for a pair to relatively rotate when running, significantly carry
The effect that high stirring is pulverized.
Tangentially entered through bifurcation structure 17 by the unmixed water under high pressure that the centre tap of multistage centrifugal hydro pump 7 comes
Enter 19 in inner housing, drive first to pulverize steel ball 20 along the wall of inner housing 19 from bottom to top movements, the first pulverizing steel
Ball 20 is moved downward with percussion body 21 collision rift at top, simultaneously through the first target body 10 and the broken mixing of the second target body 11
Thing enters in inner housing 19 by introducing pipe 16 from the bottom of inner housing 19, the mixture that moves from bottom to top with move from top to bottom
The first pulverizing steel ball 20 mutually clashes into generation fragmentation, pulverize the driving in pressure for the broken mixture of steel ball 20 through first
Lower tangentially flow in the space between inner housing 19 and shell body 18 from inner housing outlet 23 through the first filter screen 22, drive the
Two pulverize steel ball 31 along the inner surface movement of shell body 18 to be crushed to mixture again, and finally by shell body outlet 24
Flow out.Water under high pressure in the water inlet pipe 37 simultaneously being controlled by the first control valve 13 enters to drive and impacts spoke 39 in cylinder 40, from
And drive the first stirring parts 25 to rotate, and drive the second stirring parts 26 to rotate by travelling gear 42, internal in the way of stirring
Housing outlet 23 mixture out is crushed, drive cylinder 40 in do work after water under high pressure from outlet pipe 38 flow out and with
Shell body outlet 24 mixture out enters next process after converging.
In this embodiment, devise the hydraulic stirring including parts such as spoke 39, water inlet pipe 37, outlet pipes 38 to set
Standby, the power of this mixing plant, and can be with multistage centrifugal also from the centre tap of multistage centrifugal hydro pump 7
The start and stop of high-pressure hydraulic pump 7 and automatic start-stop, eliminate the control program of complexity and the configuration of motor so that crushing effect is strengthened
While run and cost of investment reduce；By the design of travelling gear 42 and the stirring rod of stagger arrangement occlusion, the first stirring parts 25
It is the stirring pair enabling for a pair to relatively rotate when running with the second stirring parts 26, substantially increase the effect that stirring is pulverized.
Application scenarios 3:
A kind of efficient additive processing unit (plant) as shown in Figure 1, including conveying worm 1, drying machine 2, intermediate heater
3rd, cyclone separator 4 and air-introduced machine 5, conveying worm 1 is provided with into funnel 100, the right-hand member of exsiccator 2 is communicated with hot blast
Pipe 101, intermediate heater 3 is arranged on the pipeline between drying machine 2 and cyclone separator 4, and warm-air pipe 101 separates a road pipeline
To intermediate heater 3 as heat source, the shell of drying machine 2 is wound with heating coil 102；Cyclone separator 4 bottom
Moisture detector 104 is provided with aggregate bin 103 inwall, the bottom of aggregate bin 103 is provided with the hand-operated valve 105 for blowing.
The present invention passes through the drying machine of the dual-heated of warm-air pipe and heating coil, can effectively improve drying effect, with
When intermediate heater setting also can improve the drying effect of second half section, and the humidity sensor of cyclone separator bottom can improve
The humidity control dynamics of whole device, simple and practical, it is suitable for promoting the use of.
Preferably, intermediate heater 3 is pipe heat exchanger.
Preferably, also include wet type high pressure reducing mechanism 106, untreated additive powder pulverizes dress through wet type high pressure
Put 106 broken after, through precipitation, tentatively air-dry after delivered in conveying worm 1 by entering funnel 100, subsequently enter drying machine 2
It is dried, eventually pass after cyclone separator 4 separates and qualified additive powder is discharged by hand-operated valve 105.
Preferably, as Figure 2-3, wet type high pressure reducing mechanism 106 include water tank 6, multistage centrifugal hydro pump 7,
Mixing chamber 8, feeder 9, the first target body 10, conducting element 11, the second target body 12, the first control valve 13, the second control valve 14, master are broken
Broken equipment and hydraulic stirring equipment.Feeder 9 is arranged on mixing chamber 8, enters mixing without broken powder body by feeder 9
In room 8.First target body 10 is arranged on inwall at pipeline turning, and conducting element 11 is obliquely installed and its one end is fixed in the first target body
On 10, the second target body 12 first target body 10 relatively is arranged on inner-walls of duct.Multistage centrifugal hydro pump 7 is by water tank 6
Water is pressurised into supertension, is accelerated by accelerating tube 15 after mixing chamber 8 is mixed with powder body, subsequently clashes into the first target body 10 and carries out just
Step is broken, and is guided by baffle 11 and carry out second-time breakage to the second target body 12, subsequently enters to become owner of disintegrating apparatus by introducing pipe 16.
2 road pipelines are led to, road first control valve 13 enters hydraulic stirring at the centre tap of multistage centrifugal hydro pump 7
Equipment, road second control valve 14 is tangentially entered the left bottom of inner housing 19 by bifurcation structure 17.
Main disintegrating apparatus includes shell body 18, inner housing 19, first pulverizes steel ball 20, percussion body 21, the first filter screen 22, interior
Housing outlet 23, shell body outlet 24, the first stirring parts 25 and the second stirring parts 26.Shell body 18 and inner housing 19 are same
The hollow cylinder of axle setting, the first pulverizing steel ball 20 is arranged on the within the chamber that inner housing 19 is located at the first filter screen 22 left side.Touch
Hit body 21 to be arranged in the top inner wall of inner housing 19, percussion body 21 is inverted bullet, and its cross-sectional axis vertically arranged,
The crushing strength that both sides so can be ensured to greatest extent is unanimously so that the fineness of powder finally obtaining is as far as possible uniform.Introduce
Pipe 16 is connected with inner housing 19 by the bottom minimum point of inner housing 19.Inner housing outlet 23 is arranged on the right side of inner housing 19
Side, the first filter screen 22 is arranged on the middle part of inner housing 19.It is additionally provided with the second pulverizing steel ball between inner housing 19 and shell body 18
31, inner housing outlet 23 has the protection baffle 32 of one section of bending that Open Side Down, and protection baffle 32 is used for protection first
The second pulverizing steel ball 31 that stirring parts 25 and the second stirring parts 26 are not fallen smashes, and is simultaneously used for guiding and is flowed out by inner housing
Mixture moves along the circumferencial direction of shell body 18.In the left side of protection baffle 32, between inner housing 19 and shell body 18 also
It is connected with the second filter screen 45, second pulverizes steel ball 31 is located in the space on the second filter screen 45 right side, and the first filter screen 22 and second is filtered
Net 45 is mainly used in stopping that steel ball passes through.Due to from inner housing outlet 23 mixture kinetic energy out compared to entering inner housing
19 mixture kinetic energy is little, so the weight of the second pulverizing steel ball 31 is set smaller than the weight of the first pulverizing steel ball 20, with
Ensure that the second pulverizing steel ball 31 can be driven.The quality of the second pulverizing steel ball 31 is the 5/6 of the first pulverizing steel ball 20 mass, same
Deng under power consumption up to minimum powder fineness reduce 17% than before not transforming.
As illustrated in figures 4-5, the first stirring parts 25 include first rotating shaft 27 and multiple first stirring rod 28, the second stirring parts 26
Including the second rotating shaft 29 and multiple second stirring rod 30, first rotating shaft 27 and the second rotating shaft 29 are and are horizontally disposed with, the first stirring
Rod 28 and the second stirring rod 30 are respectively perpendicular and are arranged in first rotating shaft 27 and the second rotating shaft 29, and the first stirring rod 28 and second
Stagger arrangement occlusion setting between stirring rod 30, the mode of this stagger arrangement snap-fit arrangement can effectively strengthen crushing effect.Shell body draws
Outlet 24 is communicated in the left side of shell body 18.Bifurcation structure 17 includes pooled portion 33, the first furcation 34 and the second furcation 35,
The lower end of pooled portion 33 is connected with the pipeline of the first control valve 13, and its upper end connects the first furcation 34 and the second furcation
35.First furcation 34 and the second furcation 35 are tangent with inner housing 19 respectively, and both axial length h are equal to the first filter
Net 22 and the distance between inner housing 19 left end h, the combination length introducing pipe 16 with inner housing 19 bottom is equal to the first furcation
34 axial length h, such setting ensure that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement.
In this embodiment, (1) devises a kind of new multi-stage crushing rotating vane type high pressure disintegrating apparatus 3, this reducing mechanism
For the circulating setting of inside and outside steel ball, in the higher inner housing of high pressure water kinetic energy 19, using tangential bifurcation structure 17 with touch
Hit the setting of body 21 so that occurring upper and lower relative motion to produce noticeable effort between mixture to be comminuted and the steel ball of whereabouts
Clash into, this reverse breaking method crushing effect for traditional steel ball trailing type is pulverized greatly reinforces, Er Qie
The driving force of one pulverizing steel ball 20 is to be realized using the intermediate tap pressure of centrifugal multistage pump multiple centrifugal pump, and motor that need not be extra etc. sets
Standby investment, cost substantially reduces；By the setting of inner housing outlet 23 and protection baffle 32, using water under high pressure complementary energy outside
The steel ball carrying out less quality again in shell is pulverized, and the energy of high-pressure hydraulic pump is fully utilized, in equal power consumption
Under accessible smashing fineness greatly improve, second pulverizing steel ball 31 quality be the 5/6 of the first pulverizing steel ball 20 mass, with
Deng under power consumption up to minimum powder fineness reduce 17% than before not transforming；(2) taken into full account the guarantor to mixing plant
Protect the needs with fluid flow characteristics and devise protection baffle 32.(3) devise the bifurcation structure 17 of uniqueness, its cooperation is drawn
Enter the setting of pipe 16 and relative dimensions, can guarantee that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement it is ensured that equipment reliability of operation.
Preferably, hydraulic stirring equipment includes casing 36, water inlet pipe 37, outlet pipe 38, multiple spoke 39, drives cylinder
40, the left end of first rotating shaft 27 and the second rotating shaft 28 is sleeved in the bearing holder (housing, cover) 41 on inner housing outlet 23 side wall, the other end
Through inner housing 19 and extend through casing 36, and the second rotating shaft 28 extends to drive in cylinder 40.Hollow cylindrical form
Driving cylinder 40 be arranged in casing 36, the water inlet pipe 37 being connected with the first control valve 13 pass through casing 36 and with drive cylinder
40 bottom is connected, and the outlet pipe 38 being connected with shell body outlet 24 is connected to the top driving cylinder 40.First rotating shaft
Be provided with travelling gear 42 between the second rotating shaft 29 in 27 right-hand member and casing 36, travelling gear 42 respectively with first rotating shaft 27
It is meshed with the second rotating shaft 29, first rotating shaft 27 and the second rotating shaft 29 are provided with for the groove that engages in engagement place that (in figure is not
Illustrate), and the length of groove is suitable with the width of travelling gear 42.Multiple spokes 39 are distributed in the second rotating shaft 30, and are located at
Drive in cylinder 40.All it is connected with first rotating shaft 27 and the second rotating shaft 29 for ensureing between two rotating shafts and travelling gear 42
The constant left boss in the position of engagement 43 and right boss 44, left boss 43 and right boss 44 are located at the both sides of travelling gear 42 respectively.
As can be seen that the first stirring parts 25 and the second stirring parts 26 are the stirring pairs enabling for a pair to relatively rotate when running, significantly carry
The effect that high stirring is pulverized.
Tangentially entered through bifurcation structure 17 by the unmixed water under high pressure that the centre tap of multistage centrifugal hydro pump 7 comes
Enter 19 in inner housing, drive first to pulverize steel ball 20 along the wall of inner housing 19 from bottom to top movements, the first pulverizing steel
Ball 20 is moved downward with percussion body 21 collision rift at top, simultaneously through the first target body 10 and the broken mixing of the second target body 11
Thing enters in inner housing 19 by introducing pipe 16 from the bottom of inner housing 19, the mixture that moves from bottom to top with move from top to bottom
The first pulverizing steel ball 20 mutually clashes into generation fragmentation, pulverize the driving in pressure for the broken mixture of steel ball 20 through first
Lower tangentially flow in the space between inner housing 19 and shell body 18 from inner housing outlet 23 through the first filter screen 22, drive the
Two pulverize steel ball 31 along the inner surface movement of shell body 18 to be crushed to mixture again, and finally by shell body outlet 24
Flow out.Water under high pressure in the water inlet pipe 37 simultaneously being controlled by the first control valve 13 enters to drive and impacts spoke 39 in cylinder 40, from
And drive the first stirring parts 25 to rotate, and drive the second stirring parts 26 to rotate by travelling gear 42, internal in the way of stirring
Housing outlet 23 mixture out is crushed, drive cylinder 40 in do work after water under high pressure from outlet pipe 38 flow out and with
Shell body outlet 24 mixture out enters next process after converging.
In this embodiment, devise the hydraulic stirring including parts such as spoke 39, water inlet pipe 37, outlet pipes 38 to set
Standby, the power of this mixing plant, and can be with multistage centrifugal also from the centre tap of multistage centrifugal hydro pump 7
The start and stop of high-pressure hydraulic pump 7 and automatic start-stop, eliminate the control program of complexity and the configuration of motor so that crushing effect is strengthened
While run and cost of investment reduce；By the design of travelling gear 42 and the stirring rod of stagger arrangement occlusion, the first stirring parts 25
It is the stirring pair enabling for a pair to relatively rotate when running with the second stirring parts 26, substantially increase the effect that stirring is pulverized.
Application scenarios 4:
A kind of efficient additive processing unit (plant) as shown in Figure 1, including conveying worm 1, drying machine 2, intermediate heater
3rd, cyclone separator 4 and air-introduced machine 5, conveying worm 1 is provided with into funnel 100, the right-hand member of exsiccator 2 is communicated with hot blast
Pipe 101, intermediate heater 3 is arranged on the pipeline between drying machine 2 and cyclone separator 4, and warm-air pipe 101 separates a road pipeline
To intermediate heater 3 as heat source, the shell of drying machine 2 is wound with heating coil 102；Cyclone separator 4 bottom
Moisture detector 104 is provided with aggregate bin 103 inwall, the bottom of aggregate bin 103 is provided with the hand-operated valve 105 for blowing.
The present invention passes through the drying machine of the dual-heated of warm-air pipe and heating coil, can effectively improve drying effect, with
When intermediate heater setting also can improve the drying effect of second half section, and the humidity sensor of cyclone separator bottom can improve
The humidity control dynamics of whole device, simple and practical, it is suitable for promoting the use of.
Preferably, intermediate heater 3 is pipe heat exchanger.
Preferably, also include wet type high pressure reducing mechanism 106, untreated additive powder pulverizes dress through wet type high pressure
Put 106 broken after, through precipitation, tentatively air-dry after delivered in conveying worm 1 by entering funnel 100, subsequently enter drying machine 2
It is dried, eventually pass after cyclone separator 4 separates and qualified additive powder is discharged by hand-operated valve 105.
Preferably, as Figure 2-3, wet type high pressure reducing mechanism 106 include water tank 6, multistage centrifugal hydro pump 7,
Mixing chamber 8, feeder 9, the first target body 10, conducting element 11, the second target body 12, the first control valve 13, the second control valve 14, master are broken
Broken equipment and hydraulic stirring equipment.Feeder 9 is arranged on mixing chamber 8, enters mixing without broken powder body by feeder 9
In room 8.First target body 10 is arranged on inwall at pipeline turning, and conducting element 11 is obliquely installed and its one end is fixed in the first target body
On 10, the second target body 12 first target body 10 relatively is arranged on inner-walls of duct.Multistage centrifugal hydro pump 7 is by water tank 6
Water is pressurised into supertension, is accelerated by accelerating tube 15 after mixing chamber 8 is mixed with powder body, subsequently clashes into the first target body 10 and carries out just
Step is broken, and is guided by baffle 11 and carry out second-time breakage to the second target body 12, subsequently enters to become owner of disintegrating apparatus by introducing pipe 16.
2 road pipelines are led to, road first control valve 13 enters hydraulic stirring at the centre tap of multistage centrifugal hydro pump 7
Equipment, road second control valve 14 is tangentially entered the left bottom of inner housing 19 by bifurcation structure 17.
Main disintegrating apparatus includes shell body 18, inner housing 19, first pulverizes steel ball 20, percussion body 21, the first filter screen 22, interior
Housing outlet 23, shell body outlet 24, the first stirring parts 25 and the second stirring parts 26.Shell body 18 and inner housing 19 are same
The hollow cylinder of axle setting, the first pulverizing steel ball 20 is arranged on the within the chamber that inner housing 19 is located at the first filter screen 22 left side.Touch
Hit body 21 to be arranged in the top inner wall of inner housing 19, percussion body 21 is inverted bullet, and its cross-sectional axis vertically arranged,
The crushing strength that both sides so can be ensured to greatest extent is unanimously so that the fineness of powder finally obtaining is as far as possible uniform.Introduce
Pipe 16 is connected with inner housing 19 by the bottom minimum point of inner housing 19.Inner housing outlet 23 is arranged on the right side of inner housing 19
Side, the first filter screen 22 is arranged on the middle part of inner housing 19.It is additionally provided with the second pulverizing steel ball between inner housing 19 and shell body 18
31, inner housing outlet 23 has the protection baffle 32 of one section of bending that Open Side Down, and protection baffle 32 is used for protection first
The second pulverizing steel ball 31 that stirring parts 25 and the second stirring parts 26 are not fallen smashes, and is simultaneously used for guiding and is flowed out by inner housing
Mixture moves along the circumferencial direction of shell body 18.In the left side of protection baffle 32, between inner housing 19 and shell body 18 also
It is connected with the second filter screen 45, second pulverizes steel ball 31 is located in the space on the second filter screen 45 right side, and the first filter screen 22 and second is filtered
Net 45 is mainly used in stopping that steel ball passes through.Due to from inner housing outlet 23 mixture kinetic energy out compared to entering inner housing
19 mixture kinetic energy is little, so the weight of the second pulverizing steel ball 31 is set smaller than the weight of the first pulverizing steel ball 20, with
Ensure that the second pulverizing steel ball 31 can be driven.The quality of the second pulverizing steel ball 31 is the 6/7 of the first pulverizing steel ball 20 mass, same
Deng under power consumption up to minimum powder fineness reduce 21% than before not transforming.
As illustrated in figures 4-5, the first stirring parts 25 include first rotating shaft 27 and multiple first stirring rod 28, the second stirring parts 26
Including the second rotating shaft 29 and multiple second stirring rod 30, first rotating shaft 27 and the second rotating shaft 29 are and are horizontally disposed with, the first stirring
Rod 28 and the second stirring rod 30 are respectively perpendicular and are arranged in first rotating shaft 27 and the second rotating shaft 29, and the first stirring rod 28 and second
Stagger arrangement occlusion setting between stirring rod 30, the mode of this stagger arrangement snap-fit arrangement can effectively strengthen crushing effect.Shell body draws
Outlet 24 is communicated in the left side of shell body 18.Bifurcation structure 17 includes pooled portion 33, the first furcation 34 and the second furcation 35,
The lower end of pooled portion 33 is connected with the pipeline of the first control valve 13, and its upper end connects the first furcation 34 and the second furcation
35.First furcation 34 and the second furcation 35 are tangent with inner housing 19 respectively, and both axial length h are equal to the first filter
Net 22 and the distance between inner housing 19 left end h, the combination length introducing pipe 16 with inner housing 19 bottom is equal to the first furcation
34 axial length h, such setting ensure that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement.
In this embodiment, (1) devises a kind of new multi-stage crushing rotating vane type high pressure disintegrating apparatus 3, this reducing mechanism
For the circulating setting of inside and outside steel ball, in the higher inner housing of high pressure water kinetic energy 19, using tangential bifurcation structure 17 with touch
Hit the setting of body 21 so that occurring upper and lower relative motion to produce noticeable effort between mixture to be comminuted and the steel ball of whereabouts
Clash into, this reverse breaking method crushing effect for traditional steel ball trailing type is pulverized greatly reinforces, Er Qie
The driving force of one pulverizing steel ball 20 is to be realized using the intermediate tap pressure of centrifugal multistage pump multiple centrifugal pump, and motor that need not be extra etc. sets
Standby investment, cost substantially reduces；By the setting of inner housing outlet 23 and protection baffle 32, using water under high pressure complementary energy outside
The steel ball carrying out less quality again in shell is pulverized, and the energy of high-pressure hydraulic pump is fully utilized, in equal power consumption
Under accessible smashing fineness greatly improve, second pulverizing steel ball 31 quality be the 6/7 of the first pulverizing steel ball 20 mass, with
Deng under power consumption up to minimum powder fineness reduce 21% than before not transforming；(2) taken into full account the guarantor to mixing plant
Protect the needs with fluid flow characteristics and devise protection baffle 32.(3) devise the bifurcation structure 17 of uniqueness, its cooperation is drawn
Enter the setting of pipe 16 and relative dimensions, can guarantee that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement it is ensured that equipment reliability of operation.
Preferably, hydraulic stirring equipment includes casing 36, water inlet pipe 37, outlet pipe 38, multiple spoke 39, drives cylinder
40, the left end of first rotating shaft 27 and the second rotating shaft 28 is sleeved in the bearing holder (housing, cover) 41 on inner housing outlet 23 side wall, the other end
Through inner housing 19 and extend through casing 36, and the second rotating shaft 28 extends to drive in cylinder 40.Hollow cylindrical form
Driving cylinder 40 be arranged in casing 36, the water inlet pipe 37 being connected with the first control valve 13 pass through casing 36 and with drive cylinder
40 bottom is connected, and the outlet pipe 38 being connected with shell body outlet 24 is connected to the top driving cylinder 40.First rotating shaft
Be provided with travelling gear 42 between the second rotating shaft 29 in 27 right-hand member and casing 36, travelling gear 42 respectively with first rotating shaft 27
It is meshed with the second rotating shaft 29, first rotating shaft 27 and the second rotating shaft 29 are provided with for the groove that engages in engagement place that (in figure is not
Illustrate), and the length of groove is suitable with the width of travelling gear 42.Multiple spokes 39 are distributed in the second rotating shaft 30, and are located at
Drive in cylinder 40.All it is connected with first rotating shaft 27 and the second rotating shaft 29 for ensureing between two rotating shafts and travelling gear 42
The constant left boss in the position of engagement 43 and right boss 44, left boss 43 and right boss 44 are located at the both sides of travelling gear 42 respectively.
As can be seen that the first stirring parts 25 and the second stirring parts 26 are the stirring pairs enabling for a pair to relatively rotate when running, significantly carry
The effect that high stirring is pulverized.
Tangentially entered through bifurcation structure 17 by the unmixed water under high pressure that the centre tap of multistage centrifugal hydro pump 7 comes
Enter 19 in inner housing, drive first to pulverize steel ball 20 along the wall of inner housing 19 from bottom to top movements, the first pulverizing steel
Ball 20 is moved downward with percussion body 21 collision rift at top, simultaneously through the first target body 10 and the broken mixing of the second target body 11
Thing enters in inner housing 19 by introducing pipe 16 from the bottom of inner housing 19, the mixture that moves from bottom to top with move from top to bottom
The first pulverizing steel ball 20 mutually clashes into generation fragmentation, pulverize the driving in pressure for the broken mixture of steel ball 20 through first
Lower tangentially flow in the space between inner housing 19 and shell body 18 from inner housing outlet 23 through the first filter screen 22, drive the
Two pulverize steel ball 31 along the inner surface movement of shell body 18 to be crushed to mixture again, and finally by shell body outlet 24
Flow out.Water under high pressure in the water inlet pipe 37 simultaneously being controlled by the first control valve 13 enters to drive and impacts spoke 39 in cylinder 40, from
And drive the first stirring parts 25 to rotate, and drive the second stirring parts 26 to rotate by travelling gear 42, internal in the way of stirring
Housing outlet 23 mixture out is crushed, drive cylinder 40 in do work after water under high pressure from outlet pipe 38 flow out and with
Shell body outlet 24 mixture out enters next process after converging.
In this embodiment, devise the hydraulic stirring including parts such as spoke 39, water inlet pipe 37, outlet pipes 38 to set
Standby, the power of this mixing plant, and can be with multistage centrifugal also from the centre tap of multistage centrifugal hydro pump 7
The start and stop of high-pressure hydraulic pump 7 and automatic start-stop, eliminate the control program of complexity and the configuration of motor so that crushing effect is strengthened
While run and cost of investment reduce；By the design of travelling gear 42 and the stirring rod of stagger arrangement occlusion, the first stirring parts 25
It is the stirring pair enabling for a pair to relatively rotate when running with the second stirring parts 26, substantially increase the effect that stirring is pulverized.
Application scenarios 5:
A kind of efficient additive processing unit (plant) as shown in Figure 1, including conveying worm 1, drying machine 2, intermediate heater
3rd, cyclone separator 4 and air-introduced machine 5, conveying worm 1 is provided with into funnel 100, the right-hand member of exsiccator 2 is communicated with hot blast
Pipe 101, intermediate heater 3 is arranged on the pipeline between drying machine 2 and cyclone separator 4, and warm-air pipe 101 separates a road pipeline
To intermediate heater 3 as heat source, the shell of drying machine 2 is wound with heating coil 102；Cyclone separator 4 bottom
Moisture detector 104 is provided with aggregate bin 103 inwall, the bottom of aggregate bin 103 is provided with the hand-operated valve 105 for blowing.
The present invention passes through the drying machine of the dual-heated of warm-air pipe and heating coil, can effectively improve drying effect, with
When intermediate heater setting also can improve the drying effect of second half section, and the humidity sensor of cyclone separator bottom can improve
The humidity control dynamics of whole device, simple and practical, it is suitable for promoting the use of.
Preferably, intermediate heater 3 is pipe heat exchanger.
Preferably, also include wet type high pressure reducing mechanism 106, untreated additive powder pulverizes dress through wet type high pressure
Put 106 broken after, through precipitation, tentatively air-dry after delivered in conveying worm 1 by entering funnel 100, subsequently enter drying machine 2
It is dried, eventually pass after cyclone separator 4 separates and qualified additive powder is discharged by hand-operated valve 105.
Preferably, as Figure 2-3, wet type high pressure reducing mechanism 106 include water tank 6, multistage centrifugal hydro pump 7,
Mixing chamber 8, feeder 9, the first target body 10, conducting element 11, the second target body 12, the first control valve 13, the second control valve 14, master are broken
Broken equipment and hydraulic stirring equipment.Feeder 9 is arranged on mixing chamber 8, enters mixing without broken powder body by feeder 9
In room 8.First target body 10 is arranged on inwall at pipeline turning, and conducting element 11 is obliquely installed and its one end is fixed in the first target body
On 10, the second target body 12 first target body 10 relatively is arranged on inner-walls of duct.Multistage centrifugal hydro pump 7 is by water tank 6
Water is pressurised into supertension, is accelerated by accelerating tube 15 after mixing chamber 8 is mixed with powder body, subsequently clashes into the first target body 10 and carries out just
Step is broken, and is guided by baffle 11 and carry out second-time breakage to the second target body 12, subsequently enters to become owner of disintegrating apparatus by introducing pipe 16.
2 road pipelines are led to, road first control valve 13 enters hydraulic stirring at the centre tap of multistage centrifugal hydro pump 7
Equipment, road second control valve 14 is tangentially entered the left bottom of inner housing 19 by bifurcation structure 17.
Main disintegrating apparatus includes shell body 18, inner housing 19, first pulverizes steel ball 20, percussion body 21, the first filter screen 22, interior
Housing outlet 23, shell body outlet 24, the first stirring parts 25 and the second stirring parts 26.Shell body 18 and inner housing 19 are same
The hollow cylinder of axle setting, the first pulverizing steel ball 20 is arranged on the within the chamber that inner housing 19 is located at the first filter screen 22 left side.Touch
Hit body 21 to be arranged in the top inner wall of inner housing 19, percussion body 21 is inverted bullet, and its cross-sectional axis vertically arranged,
The crushing strength that both sides so can be ensured to greatest extent is unanimously so that the fineness of powder finally obtaining is as far as possible uniform.Introduce
Pipe 16 is connected with inner housing 19 by the bottom minimum point of inner housing 19.Inner housing outlet 23 is arranged on the right side of inner housing 19
Side, the first filter screen 22 is arranged on the middle part of inner housing 19.It is additionally provided with the second pulverizing steel ball between inner housing 19 and shell body 18
31, inner housing outlet 23 has the protection baffle 32 of one section of bending that Open Side Down, and protection baffle 32 is used for protection first
The second pulverizing steel ball 31 that stirring parts 25 and the second stirring parts 26 are not fallen smashes, and is simultaneously used for guiding and is flowed out by inner housing
Mixture moves along the circumferencial direction of shell body 18.In the left side of protection baffle 32, between inner housing 19 and shell body 18 also
It is connected with the second filter screen 45, second pulverizes steel ball 31 is located in the space on the second filter screen 45 right side, and the first filter screen 22 and second is filtered
Net 45 is mainly used in stopping that steel ball passes through.Due to from inner housing outlet 23 mixture kinetic energy out compared to entering inner housing
19 mixture kinetic energy is little, so the weight of the second pulverizing steel ball 31 is set smaller than the weight of the first pulverizing steel ball 20, with
Ensure that the second pulverizing steel ball 31 can be driven.The quality of the second pulverizing steel ball 31 is the 7/8 of the first pulverizing steel ball 20 mass, same
Deng under power consumption up to minimum powder fineness reduce 23% than before not transforming.
As illustrated in figures 4-5, the first stirring parts 25 include first rotating shaft 27 and multiple first stirring rod 28, the second stirring parts 26
Including the second rotating shaft 29 and multiple second stirring rod 30, first rotating shaft 27 and the second rotating shaft 29 are and are horizontally disposed with, the first stirring
Rod 28 and the second stirring rod 30 are respectively perpendicular and are arranged in first rotating shaft 27 and the second rotating shaft 29, and the first stirring rod 28 and second
Stagger arrangement occlusion setting between stirring rod 30, the mode of this stagger arrangement snap-fit arrangement can effectively strengthen crushing effect.Shell body draws
Outlet 24 is communicated in the left side of shell body 18.Bifurcation structure 17 includes pooled portion 33, the first furcation 34 and the second furcation 35,
The lower end of pooled portion 33 is connected with the pipeline of the first control valve 13, and its upper end connects the first furcation 34 and the second furcation
35.First furcation 34 and the second furcation 35 are tangent with inner housing 19 respectively, and both axial length h are equal to the first filter
Net 22 and the distance between inner housing 19 left end h, the combination length introducing pipe 16 with inner housing 19 bottom is equal to the first furcation
34 axial length h, such setting ensure that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement.
In this embodiment, (1) devises a kind of new multi-stage crushing rotating vane type high pressure disintegrating apparatus 3, this reducing mechanism
For the circulating setting of inside and outside steel ball, in the higher inner housing of high pressure water kinetic energy 19, using tangential bifurcation structure 17 with touch
Hit the setting of body 21 so that occurring upper and lower relative motion to produce noticeable effort between mixture to be comminuted and the steel ball of whereabouts
Clash into, this reverse breaking method crushing effect for traditional steel ball trailing type is pulverized greatly reinforces, Er Qie
The driving force of one pulverizing steel ball 20 is to be realized using the intermediate tap pressure of centrifugal multistage pump multiple centrifugal pump, and motor that need not be extra etc. sets
Standby investment, cost substantially reduces；By the setting of inner housing outlet 23 and protection baffle 32, using water under high pressure complementary energy outside
The steel ball carrying out less quality again in shell is pulverized, and the energy of high-pressure hydraulic pump is fully utilized, in equal power consumption
Under accessible smashing fineness greatly improve, second pulverizing steel ball 31 quality be the 7/8 of the first pulverizing steel ball 20 mass, with
Deng under power consumption up to minimum powder fineness reduce 23% than before not transforming；(2) taken into full account the guarantor to mixing plant
Protect the needs with fluid flow characteristics and devise protection baffle 32.(3) devise the bifurcation structure 17 of uniqueness, its cooperation is drawn
Enter the setting of pipe 16 and relative dimensions, can guarantee that the first pulverizing steel ball 20 will not produce rotation dead angle, no matter the first pulverizing steel
Which position that ball 20 is located at chamber can keep shuttling movement it is ensured that equipment reliability of operation.
Preferably, hydraulic stirring equipment includes casing 36, water inlet pipe 37, outlet pipe 38, multiple spoke 39, drives cylinder
40, the left end of first rotating shaft 27 and the second rotating shaft 28 is sleeved in the bearing holder (housing, cover) 41 on inner housing outlet 23 side wall, the other end
Through inner housing 19 and extend through casing 36, and the second rotating shaft 28 extends to drive in cylinder 40.Hollow cylindrical form
Driving cylinder 40 be arranged in casing 36, the water inlet pipe 37 being connected with the first control valve 13 pass through casing 36 and with drive cylinder
40 bottom is connected, and the outlet pipe 38 being connected with shell body outlet 24 is connected to the top driving cylinder 40.First rotating shaft
Be provided with travelling gear 42 between the second rotating shaft 29 in 27 right-hand member and casing 36, travelling gear 42 respectively with first rotating shaft 27
It is meshed with the second rotating shaft 29, first rotating shaft 27 and the second rotating shaft 29 are provided with for the groove that engages in engagement place that (in figure is not
Illustrate), and the length of groove is suitable with the width of travelling gear 42.Multiple spokes 39 are distributed in the second rotating shaft 30, and are located at
Drive in cylinder 40.All it is connected with first rotating shaft 27 and the second rotating shaft 29 for ensureing between two rotating shafts and travelling gear 42
The constant left boss in the position of engagement 43 and right boss 44, left boss 43 and right boss 44 are located at the both sides of travelling gear 42 respectively.
As can be seen that the first stirring parts 25 and the second stirring parts 26 are the stirring pairs enabling for a pair to relatively rotate when running, significantly carry
The effect that high stirring is pulverized.
Tangentially entered through bifurcation structure 17 by the unmixed water under high pressure that the centre tap of multistage centrifugal hydro pump 7 comes
Enter 19 in inner housing, drive first to pulverize steel ball 20 along the wall of inner housing 19 from bottom to top movements, the first pulverizing steel
Ball 20 is moved downward with percussion body 21 collision rift at top, simultaneously through the first target body 10 and the broken mixing of the second target body 11
Thing enters in inner housing 19 by introducing pipe 16 from the bottom of inner housing 19, the mixture that moves from bottom to top with move from top to bottom
The first pulverizing steel ball 20 mutually clashes into generation fragmentation, pulverize the driving in pressure for the broken mixture of steel ball 20 through first
Lower tangentially flow in the space between inner housing 19 and shell body 18 from inner housing outlet 23 through the first filter screen 22, drive the
Two pulverize steel ball 31 along the inner surface movement of shell body 18 to be crushed to mixture again, and finally by shell body outlet 24
Flow out.Water under high pressure in the water inlet pipe 37 simultaneously being controlled by the first control valve 13 enters to drive and impacts spoke 39 in cylinder 40, from
And drive the first stirring parts 25 to rotate, and drive the second stirring parts 26 to rotate by travelling gear 42, internal in the way of stirring
Housing outlet 23 mixture out is crushed, drive cylinder 40 in do work after water under high pressure from outlet pipe 38 flow out and with
Shell body outlet 24 mixture out enters next process after converging.
In this embodiment, devise the hydraulic stirring including parts such as spoke 39, water inlet pipe 37, outlet pipes 38 to set
Standby, the power of this mixing plant, and can be with multistage centrifugal also from the centre tap of multistage centrifugal hydro pump 7
The start and stop of high-pressure hydraulic pump 7 and automatic start-stop, eliminate the control program of complexity and the configuration of motor so that crushing effect is strengthened
While run and cost of investment reduce；By the design of travelling gear 42 and the stirring rod of stagger arrangement occlusion, the first stirring parts 25
It is the stirring pair enabling for a pair to relatively rotate when running with the second stirring parts 26, substantially increase the effect that stirring is pulverized.
Finally it should be noted that above example is only in order to illustrating technical scheme, rather than the present invention is protected
The restriction of shield scope, although having made to explain to the present invention with reference to preferred embodiment, those of ordinary skill in the art should
Work as understanding, technical scheme can be modified or equivalent, without deviating from the reality of technical solution of the present invention
Matter and scope.
Claims (3)
1. a kind of efficient additive processing unit (plant), is characterized in that, divides including conveying worm, drying machine, intermediate heater, whirlwind
From device and air-introduced machine, conveying worm is provided with into funnel, the right-hand member of exsiccator is communicated with warm-air pipe, and intermediate heater sets
Put on the pipeline between drying machine and cyclone separator, warm-air pipe separates a road pipeline to intermediate heater as heating heat
Source, the shell of drying machine is wound with heating coil；It is provided with moisture detector on the aggregate bin inwall of cyclone separator bottom,
The bottom of aggregate bin is provided with the hand-operated valve for blowing.
2. a kind of efficient additive processing unit (plant) according to claim 1, is characterized in that, intermediate heater is pipe type heat transfer
Device.
3. a kind of efficient additive processing unit (plant) according to claim 2, is characterized in that, also includes wet type high pressure and pulverizes dress
Put, untreated additive powder after wet type high pressure reducing mechanism crushes, through precipitation, tentatively air-dry after by entering funnel
Deliver in conveying worm, subsequently enter drying machine and be dried, it is qualified to be discharged by hand-operated valve after eventually passing cyclone separator separation
Additive powder.
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|---|---|---|---|
| CN201610742487.XA CN106369982A (en) | 2016-08-26 | 2016-08-26 | Efficient additive processing device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610742487.XA CN106369982A (en) | 2016-08-26 | 2016-08-26 | Efficient additive processing device |
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| CN106369982A true CN106369982A (en) | 2017-02-01 |
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| CN201610742487.XA Pending CN106369982A (en) | 2016-08-26 | 2016-08-26 | Efficient additive processing device |
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Application publication date: 20170201 |