CN206996572U - Florfenicol is produced with to stirring formula reactor - Google Patents

Florfenicol is produced with to stirring formula reactor Download PDF

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Publication number
CN206996572U
CN206996572U CN201720660782.0U CN201720660782U CN206996572U CN 206996572 U CN206996572 U CN 206996572U CN 201720660782 U CN201720660782 U CN 201720660782U CN 206996572 U CN206996572 U CN 206996572U
Authority
CN
China
Prior art keywords
inner bag
kettle
gear
rotating shaft
stirring
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201720660782.0U
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Chinese (zh)
Inventor
袁庆
康先禄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ZHEJIANG KANGMU PHARMACEUTICAL CO Ltd
Original Assignee
ZHEJIANG KANGMU PHARMACEUTICAL CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ZHEJIANG KANGMU PHARMACEUTICAL CO Ltd filed Critical ZHEJIANG KANGMU PHARMACEUTICAL CO Ltd
Priority to CN201720660782.0U priority Critical patent/CN206996572U/en
Application granted granted Critical
Publication of CN206996572U publication Critical patent/CN206996572U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

It the utility model is related to reactor.A kind of Florfenicol production is with to stirring formula reactor, agitator including kettle and in kettle, the agitator includes rotating shaft and is connected to the puddler of rotating shaft, the kettle is provided with charging aperture and air admission hole, characterized in that, the inner bag rotational structure that inner bag is rotatably connected in the kettle and drives inner bag to rotate, the puddler are located in the inner bag, the rotation direction of the inner bag and the rotation direction of rotating shaft are on the contrary, the inwall of the inner bag is provided with stirring vane.A kind of good Florfenicol production of tearing effects when the utility model provides stirring solves the problems, such as that existing reactor synchronization is merely able to as unidirectional stirring with to stirring formula reactor.

Description

Florfenicol is produced with to stirring formula reactor
Technical field
Reactor, more particularly to a kind of production of Florfenicol be the utility model is related to stirring formula reactor.
Background technology
Reactor is the kettle for physically or chemically reacting, and by the structure design and parameter configuration to kettle, is realized The heating of technological requirement, evaporation, the mixture function of cooling and low high speed.Reactor is by kettle, kettle cover, chuck, agitator, transmission The compositions such as device, gland seal device, supporting are formed, and charging aperture and discharging opening are provided with the kettle that kettle and kettle cover are formed.
Chinese Patent Application No. be 2009100199921, publication date is on January 11st, 2012, entitled " self-adjustable is fast A kind of reactor is disclosed in the patent document of fast reactor ".
It can be related to gas liquid reaction during preparing Florfenicol by reactor.The principle of gas liquid reaction at present is gas Body is fully contacted with liquid, and under certain reaction condition, gas-liquid, which reacts, generates target compound, existing reaction When kettle carries out gas liquid reaction, it is that air tube is sent directly into reactor and venthole is maintained at below liquid level, opens simultaneously The Gas Stirring that dynamic agitator will be fed into is uniform, is reacted with liquid, and this method has the following disadvantages:Air duct only has One venthole, although there is agitator stirring, it can not also ensure that gas is evenly distributed in a kettle, thus the gas in reactor Body local concentration is too high, causes the increase of side reaction, the yield reduction of target compound.Synchronization is court when agitator stirs One direction stirring has been what is instantaneously unidirectionally stirred, and unidirectional stirring is small to being stirred tear edge caused by object.
Utility model content
A kind of good Florfenicol production of tearing effects when first purpose of the present utility model aims to provide stirring is used To stirring formula reactor, solve the problems, such as that existing reactor synchronization is merely able to as unidirectional stirring.
Second purpose of the present utility model is intended to further provide for a kind of dissipating for gas raw material on the basis of first purpose Effect good Florfenicol production is opened with to stirring formula reactor, solving existing reactor gas raw material not dispersion effect difference Problem.
Above technical problem is that solved by following technical proposal:A kind of production of Florfenicol with to stirring formula reactor, Agitator including kettle and in kettle, the agitator include rotating shaft and are connected to the puddler of rotating shaft, the kettle Provided with charging aperture, it is characterised in that the inner bag rotational structure that inner bag is rotatably connected in the kettle and drives inner bag to rotate, institute State puddler to be located in the inner bag, the rotation direction of the inner bag and the rotation direction of rotating shaft are on the contrary, the inwall of the inner bag It is provided with stirring vane.Inner bag and the rotation direction of inner bag and agitating roller are set on the contrary, the raw materials of two flow directions are in intersection's meeting Tear edge is produced, tearing effects during so as to improve stirring.
Preferably, the inner bag rotational structure includes first gear, second gear and ring gear, the first gear is same Axis connection is in the rotating shaft, and the second gear and first gear mesh together, and the ring gear is connected to the inner bag Inner surface on, the second gear meshes together with the ring gear.Inner bag and agitator realize common power source.
Preferably, the bottom wall inner surface of the kettle is provided with the spindle nose being vertically arranged, the bottom wall outer surface of the inner bag is provided with Axle sleeve, the axle sleeve are set on the spindle nose, and the plane bearing of support inner bag is provided between the spindle nose and axle sleeve.Load-carrying is imitated Fruit is good.
Preferably, surround air distribution cavity between the inner bag and kettle, the inner bag is communicated with air distribution cavity and described interior At least three venthole of courage inner space, the kettle are provided with the air admission hole that supplied gas raw material enters, and the air admission hole is located at institute State air distribution cavity.In use, gas enters air distribution cavity through air admission hole, then enter through multiple ventholes in inner bag, it is more due to setting Individual venthole, uniformity when gas flows out are more preferable.Realize second goal of the invention.
Preferably, the air admission hole is arranged on the bottom wall of the kettle, the venthole is arranged on the inner bag Bottom wall, the aperture area of the venthole is less than 2 square millimeters.The uniformity of outlet can be improved.
The utility model tool has the advantage that:Degree of scattering when gas raw material enters reactor is good;Material can be divided into Two parts and produce the different rotation in direction, so as to produce tear effect, be advantageous to the broken of solid material.
Brief description of the drawings
Fig. 1 is schematic diagram of the present utility model.
In figure:Kettle 1, charging aperture 11, air admission hole 18, spindle nose 19, plane bearing 191, agitator 2, rotating shaft 21, puddler 22nd, driving structure 3, motor 31, driving gear 32, driven gear 33, inner bag 4, axle sleeve 41, flanging 42, sealing ring 43, stirring Blade 44, air distribution cavity 45, venthole 46, inner bag rotational structure 5, first gear 51, second gear 52, ring gear 53.
Embodiment
The utility model is further described with embodiment below in conjunction with the accompanying drawings.
Referring to Fig. 1, a kind of production of Florfenicol is including kettle 1, agitator 2, driving structure 3, interior with to stirring formula reactor Courage 4 and inner bag rotational structure 5.
The roof of kettle 1 is provided with charging aperture 11.The bottom wall of kettle 1 is provided with air admission hole 18.On the bottom wall inner surface of kettle 1 Provided with spindle nose 19.Spindle nose 19 vertically extends.The top braces of spindle nose 19 have plane bearing 191.
Inner bag 4 is located in kettle 1.Inner bag 4 is the cylindrical structure of open upper end.The bottom wall outer surface of inner bag 4 is provided with axle sleeve 41.Axle sleeve 41 is set on spindle nose 19.Axle sleeve 41, which is supported on plane bearing 191, realizes rotation connection of the inner bag 4 with kettle 1. The upper end of inner bag 4 is provided with flanging 42.Flanging 42 is linked together by sealing ring 43 with the rotary seal of kettle 1.Inner bag 4 Inwall is provided with stirring vane 44.Air distribution cavity 45 is surrounded between inner bag 4 and kettle 1.The bottom wall of inner bag 4 is provided with 36 ventholes 46, the setting of venthole causes inner bag bottom wall to form grid harden structure.Venthole 46 connects air distribution cavity and inner bag inner space.Go out The aperture area of stomata is less than 2 square millimeters.Air admission hole 18 is located at air distribution cavity 45.
Agitator 2 is located in kettle 1.Agitator 2 includes rotating shaft 21 and is connected to some of rotating shaft.Rotating shaft 21 is rotatablely connected In kettle 1.Rotating shaft 21 is vertically extending.Puddler 22 is welded in rotating shaft 21.Puddler 22 is located in inner bag 4.Puddler Along the projection of rotating shaft axial direction with projection radially and circumferentially all staggering along rotating shaft of the stirring vane along rotating shaft axial direction.
Driving structure 3 includes motor 31, the driving gear 32 for being arranged at motor power output shaft and engaged with driving gear Driven gear 33 together.Driven gear 33 is fixed on the upper end of rotating shaft 21, and driven gear 33 and rotating shaft 21 are coaxial.
Inner bag rotational structure 5 includes first gear 51, second gear 52 and ring gear 53.First gear 51 it is coaxially connected In rotating shaft 21.Second gear 52 is rotatably connected on the roof of kettle 1.Second gear 52 and first gear mesh together.It is interior Gear ring 53 is fixed on the inner peripheral surface of inner bag 4.Ring gear 53 and second gear 52 mesh together.First gear 51, the second tooth The diameter parallel of wheel 52 and ring gear 53.The annexation causes the rotation of the rotation direction of inner bag and rotating shaft when agitator rotates In the opposite direction.
In use, solid material enters inner bag through charging aperture.Gas raw material enters air distribution cavity through air admission hole, then from outlet Hole enters in inner bag.
Motor 31 drives driving gear 32 to rotate, driving gear 32 drives driven gear 33 to rotate, driven gear driving turns Axle rotates, and rotating shaft driving agitating roller and first gear rotate, and first gear drives ring gear to rotate by second gear, ring gear Inner bag is driven to rotate, inner bag driving fan blade rotates.During rotation the rotation direction of inner bag with agitating roller rotation direction on the contrary, So that the material some in inner bag rotates clockwise, some rotates counterclockwise, tear edge is produced at cross-flow along animal body is reversed To promote the fragmentation of solid material.

Claims (5)

1. a kind of Florfenicol production is with to stirring formula reactor, including kettle and the agitator in kettle, the agitator Including rotating shaft and the puddler of rotating shaft is connected to, the kettle is provided with charging aperture, it is characterised in that be rotatablely connected in the kettle The inner bag rotational structure for having inner bag and driving inner bag to rotate, the puddler are located in the inner bag, the rotation side of the inner bag To the rotation direction with rotating shaft on the contrary, the inwall of the inner bag is provided with stirring vane.
2. Florfenicol production according to claim 1 is with to stirring formula reactor, it is characterised in that the inner bag rotates knot Structure includes first gear, second gear and ring gear, and the first gear is coaxially connected in the rotating shaft, the second gear Mesh together with first gear, the ring gear is connected on the inner surface of the inner bag, and the second gear is the same as described interior Gear ring meshes together.
3. Florfenicol production according to claim 1 or 2 is with to stirring formula reactor, it is characterised in that the kettle Bottom wall inner surface is provided with the spindle nose being vertically arranged, and the bottom wall outer surface of the inner bag is provided with axle sleeve, and the axle sleeve is set in the spindle nose On, the plane bearing for supporting inner bag is provided between the spindle nose and axle sleeve.
4. Florfenicol according to claim 1 or 2 production is with to stirring formula reactor, it is characterised in that the inner bag and Air distribution cavity is surrounded between kettle, the inner bag is communicated with air distribution cavity and at least three venthole of the inner bag inner space, institute State kettle and be provided with the air admission hole that supplied gas raw material enters, the air admission hole is located at the air distribution cavity.
5. Florfenicol production according to claim 4 is with to stirring formula reactor, it is characterised in that the air admission hole is set On the bottom wall of the kettle, the venthole is arranged on the bottom wall of the inner bag, and the aperture area of the venthole is 2 squares Millimeter is following.
CN201720660782.0U 2017-06-08 2017-06-08 Florfenicol is produced with to stirring formula reactor Expired - Fee Related CN206996572U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720660782.0U CN206996572U (en) 2017-06-08 2017-06-08 Florfenicol is produced with to stirring formula reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720660782.0U CN206996572U (en) 2017-06-08 2017-06-08 Florfenicol is produced with to stirring formula reactor

Publications (1)

Publication Number Publication Date
CN206996572U true CN206996572U (en) 2018-02-13

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Application Number Title Priority Date Filing Date
CN201720660782.0U Expired - Fee Related CN206996572U (en) 2017-06-08 2017-06-08 Florfenicol is produced with to stirring formula reactor

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110171117A (en) * 2019-06-10 2019-08-27 浙江宏途电气科技有限公司 Pvc pipe manufacturing process for cable protection pipe production

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110171117A (en) * 2019-06-10 2019-08-27 浙江宏途电气科技有限公司 Pvc pipe manufacturing process for cable protection pipe production
CN110171117B (en) * 2019-06-10 2021-10-29 浙江宏途电气科技有限公司 PVC pipe manufacturing process for cable protection pipe production

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CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180213

Termination date: 20200608