CN206762706U - A kind of twin shaft mixing reactor in the same direction - Google Patents
A kind of twin shaft mixing reactor in the same direction Download PDFInfo
- Publication number
- CN206762706U CN206762706U CN201720425683.4U CN201720425683U CN206762706U CN 206762706 U CN206762706 U CN 206762706U CN 201720425683 U CN201720425683 U CN 201720425683U CN 206762706 U CN206762706 U CN 206762706U
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- chuck
- housing
- agitating
- same direction
- medium
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Abstract
The utility model provides a kind of twin shaft mixing reactor in the same direction, more particularly to disappearing fibre spinning equipment field, including transmission device, housing, chuck, support end seat, support base and 2 agitating shafts, the both ends of the housing are fixed with the support end seat, the outside of the housing is provided with the chuck, the chuck lower end is provided with the support base, the agitating shaft is located in the housing, the both ends of the agitating shaft are located in the support end seat, one end of the agitating shaft is connected with the transmission device, the transmission device includes reducing motor, driving gear and driven gear, the driving gear is connected with the reducing motor, the driving gear is provided with 2 driven gears, the driven gear and the stirring axis connection.The utility model has simple in construction, and production efficiency is high, and the advantages of fiber is rotten will not occur during stirring.
Description
Technical field
The utility model belongs to disappearing fibre spinning equipment field, more particularly to a kind of twin shaft mixing reactor in the same direction.
Background technology
At present, the mixed dissolution for solving disappearing fibre spinning is mainly passed through thermal medium in a mixer, and is stirred
Mix to realize that the dissolving of fiber mixes, such as, blade dryer can reach this effect, but because the stirring of blade dryer is cut
It is excessively strong to cut effect, disappearing fibre can be made to go bad.
Patent horizontal-type biaxial stirred reactor (publication No.：CN203525716U, date of publication：2014-04-09), disclose
A kind of horizontal-type biaxial stirred reactor, including housing, enclosure interior set agitating shaft, and one end of the mixing shaft passes through shaft coupling and transmission
Device is connected, and shield is set on the outside of transmission device；Housing upper sets steam inlet, waste gas outlet, triggers water inlet, thermometer
Mouth, material inlet and observation panel.The utility model is provided simultaneously with mixing, stirred, reacting and the stirring of the horizontal-type biaxial of conveying capacity
Reactor apparatus.Service life is grown, and reduces the use cost of equipment, and equipment extends exhaust gas volumn drain time, substantially reduced
Vent gas treatment difficulty and investment.Traditional intermittent production is improved to consecutive production, production efficiency is greatly improved, and
And reached the requirement of energy-conserving and environment-protective, but the utility model can not be applicable the mixed dissolution of disappearing fibre spinning.
Therefore, it is badly in need of that a kind of production efficiency is high, fiber rotten twin shaft mixing reactor in the same direction will not occurs during stirring.
Utility model content
The problem of shear action is too strong during in order to solve to mix, and disappearing fibre can go bad, mesh of the present utility model
Be to provide a kind of twin shaft mixing reactor in the same direction, the advantages of fiber is rotten will not occur when having that production efficiency is high, and stirring.
The utility model provides following technical scheme：
A kind of twin shaft mixing reactor in the same direction, including transmission device, housing, chuck, support end seat, support base and 2
Agitating shaft, the both ends of the housing are fixed with the support end seat, and the outside of the housing is provided with the chuck, under the chuck
End is provided with the support base, and the agitating shaft is located in the housing, and the both ends of the agitating shaft are located at the support end seat
On, one end of the agitating shaft is connected with the transmission device, and the transmission device includes reducing motor, driving gear and driven
Gear, the driving gear are connected with the reducing motor, and the driving gear is provided with 2 driven gears, the driven tooth
Wheel and the stirring axis connection.
The transmission device drives the agitating shaft, the driven tooth rotation with the driving gear and the driven gear
Dynamic direction is identical, and the rotation direction of the agitating shaft is also identical, and the agitating shaft of rotating Vortex makes material roll procedure
In, the effect of kneading material is realized, without producing excessive shear action, makes material that fiber will not occur in heating process
It is rotten.
Preferably, enclosing cover is provided with above the housing, material inlet, first medium mouth is sequentially provided with the outer cover outer wall
Exported with volatilization gas, volatilization gas outlet is arranged on the centre position of the enclosing cover, the housing be additionally provided with it is described
The first medium pipe that first medium mouth is connected, the first medium pipe are located at the top of the agitating shaft.
Preferably, some punching pipes are provided with the chuck, the punching pipe and the chuck are vertical, the chuck bottom
Outer wall is provided with second medium pipe and material outlet, and the material outlet is located at one end of the chuck, the second medium pipe
It is provided with second medium mouth.The first medium mouth can be used as thermal medium entrance or cold medium to export, the second medium
Mouth can be used as cold medium entrance or thermal medium outlet.
Preferably, the punching pipe is divided equally in the chuck and is distributed.The punching pipe is carrying out stay bolt to the chuck
While reinforcement, the turbulence effects of thermal medium or cold medium in the chuck are increased.
Preferably, the agitating shaft includes institute's spindle nose, central siphon, hollow blade and agitating paddle, and the central siphon both ends are provided with institute
Spindle nose is stated, the central siphon is provided with some hollow blades, and the both ends of the hollow blade are fixed with the agitating paddle, described
Agitating paddle is U-shaped.
Preferably, the angle value between the agitating paddle and the hollow blade is 15-30 degree.The hollow blade and institute
Stating agitating paddle has appropriate angle, and the agitating paddle advances to convey material, makes in material roll procedure, will not produce excessive cut
The effect of cutting, also greatly reduce the rotten degree of fiber.
The beneficial effects of the utility model are：It is simple in construction；Production efficiency is high；Fiber will not occur during stirring to go bad.
Brief description of the drawings
Accompanying drawing is used for providing further understanding to of the present utility model, and a part for constitution instruction, with this practicality
New embodiment is used to explain the utility model together, does not form to limitation of the present utility model.In the accompanying drawings：
Fig. 1 is the utility model structure chart；
Fig. 2 is the utility model inside configuration structure chart；
Fig. 3 is agitating shaft structure chart described in the utility model；
Fig. 4 is driving gear described in the utility model and the driven gear engagement figure；
Agitating shaft stirring figure when Fig. 5 is utility model works；
In figure mark for：1st, transmission device；11st, reducing motor；12nd, driving gear；13rd, driven gear；2nd, housing；3rd, it is outer
Lid；31st, material inlet；32nd, first medium mouth；33rd, volatilization gas exports；34th, first medium pipe；4th, chuck；41st, punching pipe；
42nd, second medium pipe；43rd, second medium mouth；44th, stream outlet；5th, end seat is supported；6th, support base；7th, agitating shaft；71st, axle
Head；72nd, central siphon；73rd, hollow blade；74th, agitating paddle.
Embodiment
As Figure 1-5, a kind of twin shaft mixing reactor in the same direction, including transmission device 1, housing 2, chuck 4, support end seat
5th, support base 6 and 2 agitating shafts 7, the both ends of housing 2 are fixed with support end seat 5, and the outside of housing 2 is provided with chuck 4, chuck 4
Lower end is provided with support base 6, and agitating shaft 7 is located in housing 2, and the both ends of agitating shaft 7 are located in support end seat 5, and the one of agitating shaft 7
End is connected with transmission device 1, and transmission device 1 includes reducing motor 11, driving gear 12 and driven gear 13, driving gear 12 and
Reducing motor 11 is connected, and driving gear 12 is provided with 2 driven gears 13, and driven gear 13 is connected with agitating shaft 7.
Transmission device 1 drives agitating shaft 7, the direction phase that driven gear 13 rotates with driving gear 12 and driven gear 13
Together, the rotation direction of agitating shaft 7 is also identical, and the agitating shaft 7 of rotating Vortex realizes kneading material in material roll procedure is made
Effect, without producing excessive shear action, makes material that fiber will not occur in heating process and goes bad.
The top of housing 2 is provided with enclosing cover 3, and material inlet 31, first medium mouth 32 and Volatile Gas are sequentially provided with the outer wall of enclosing cover 3
Body outlet 33, volatilization gas outlet 33 are arranged on the centre position of enclosing cover 3, and housing 2 is additionally provided with to be connected with first medium mouth 32
First medium pipe 34, first medium pipe 34 is located at the top of agitating shaft 7.
Some punching pipes 41 are provided with chuck 4, punching pipe 41 and chuck 4 are vertical, and the bottom outer wall of chuck 4 is provided with second and is situated between
Matter pipe 42 and material outlet 44, material outlet 44 are located at one end of chuck 4, and second medium pipe 42 is provided with second medium mouth 43,
Punching pipe 41 is divided equally in chuck 4 to be distributed.Punching pipe 41 is provided with chuck 4, punching pipe 41 is carrying out stay bolt reinforcement to chuck 4
Meanwhile increase the turbulence effects of thermal medium or cold medium in chuck 4.
Agitating shaft 7 includes spindle nose 71, central siphon 72, hollow blade 73 and agitating paddle 74, and the both ends of central siphon 72 are provided with spindle nose 71, axle
Pipe 72 is provided with some hollow blades 73, and the both ends of hollow blade 73 are fixed with agitating paddle 74, and agitating paddle 74 is U-shaped.
Angle value between agitating paddle 74 and hollow blade 73 is 15-30 degree, and hollow blade 73 has suitably with agitating paddle 74
Angle, agitating paddle 74 advance to convey material, make in material roll procedure, will not produce excessive shear action, also subtract significantly
The rotten degree of few fiber.
First medium mouth 32 can be used as thermal medium entrance or cold medium to export, and second medium mouth 43 can be used as cold Jie
Matter entrance or thermal medium outlet.
The utility model application method：Enter after material mixing from material inlet 31 in housing 2, thermal medium is from first medium
Mouth 32 or cold medium enter in chuck 4 from second medium mouth 43, start reducing motor 11, and reducing motor 11 rotates, and drive actively
Gear 12 rotates, and driving gear 12 drives driven gear 13 to rotate, and driven gear 13 drives agitating shaft 7 to rotate, driven gear 13
Rotation direction it is identical, the rotation direction of agitating shaft 7 is also identical, and the hollow blade 73 and agitating paddle 74 on agitating shaft 7 have necessarily
Angle, agitating shaft 7 rotate when, material carry out kneading mixing, pass through the impetus of the agitating paddle 74 on agitating shaft 7, material
Moved from material inlet 31 to material outlet 44, final finished is discharged from material outlet 44, and material is raw during hybrid reaction
Into volatilization gas by volatilization gas outlet 33 discharge reactors, in order that material reacts at a suitable temperature, in chuck 4
The thermal medium or cold medium being passed through on interior, thermal medium enter from first medium mouth 32, and second medium mouth 43 flows out, cold medium from
Second medium mouth 43 enters, and first medium mouth 32 flows out.
Preferred embodiment of the present utility model is the foregoing is only, is not limited to the utility model, although ginseng
The utility model is described in detail according to previous embodiment, for those skilled in the art, it still can be with
Technical scheme described in foregoing embodiments is modified, or equivalent substitution is carried out to which part technical characteristic.It is all
Within the spirit and principles of the utility model, any modification, equivalent substitution and improvements made etc., this practicality should be included in
Within new protection domain.
Claims (6)
1. a kind of twin shaft mixing reactor in the same direction, it is characterised in that including transmission device, housing, chuck, support end seat, support
Base and 2 agitating shafts, the both ends of the housing are fixed with the support end seat, and the outside of the housing is provided with the chuck,
The chuck lower end is provided with the support base, and the agitating shaft is located in the housing, and the both ends of the agitating shaft are located at institute
State in support end seat, one end of the agitating shaft is connected with the transmission device, and the transmission device includes reducing motor, active
Gear and driven gear, the driving gear are connected with the reducing motor, and the driving gear is provided with 2 driven gears,
The driven gear and the stirring axis connection.
2. a kind of twin shaft mixing reactor in the same direction according to claim 1, it is characterised in that be provided with above the housing outer
Cover, material inlet, first medium mouth and volatilization gas outlet are sequentially provided with the outer cover outer wall, the volatilization gas outlet is set
Put the first medium pipe for being additionally provided with the centre position of the enclosing cover, the housing and being connected with the first medium mouth, institute
State the top that first medium pipe is located at the agitating shaft.
3. a kind of twin shaft mixing reactor in the same direction according to claim 1, it is characterised in that be provided with the chuck some
Punching pipe, the punching pipe and the chuck are vertical, and chuck bottom outer wall is provided with second medium pipe and material outlet, institute
One end that material outlet is located at the chuck is stated, the second medium pipe is provided with second medium mouth.
4. a kind of twin shaft mixing reactor in the same direction according to claim 3, it is characterised in that the punching pipe is in the folder
It is uniformly distributed in set.
5. a kind of twin shaft mixing reactor in the same direction according to claim 1, it is characterised in that the agitating shaft includes institute's axle
Head, central siphon, hollow blade and agitating paddle, the central siphon both ends are provided with the spindle nose, and the central siphon is provided with some described hollow
Blade, the both ends of the hollow blade are fixed with the agitating paddle, and the agitating paddle is U-shaped.
6. a kind of twin shaft mixing reactor in the same direction according to claim 5, it is characterised in that the agitating paddle and the sky
Angle value between lobus cardiacus piece is 15-30 degree.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720425683.4U CN206762706U (en) | 2017-04-21 | 2017-04-21 | A kind of twin shaft mixing reactor in the same direction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720425683.4U CN206762706U (en) | 2017-04-21 | 2017-04-21 | A kind of twin shaft mixing reactor in the same direction |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206762706U true CN206762706U (en) | 2017-12-19 |
Family
ID=60635450
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720425683.4U Expired - Fee Related CN206762706U (en) | 2017-04-21 | 2017-04-21 | A kind of twin shaft mixing reactor in the same direction |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206762706U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112391187A (en) * | 2019-08-16 | 2021-02-23 | 宝武炭材料科技有限公司 | Oxidation device for producing high-softening-point asphalt |
-
2017
- 2017-04-21 CN CN201720425683.4U patent/CN206762706U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112391187A (en) * | 2019-08-16 | 2021-02-23 | 宝武炭材料科技有限公司 | Oxidation device for producing high-softening-point asphalt |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171219 Termination date: 20180421 |
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| CF01 | Termination of patent right due to non-payment of annual fee |