CN206276378U - A kind of reactor stirring vane for synthesizing hexanicit - Google Patents

A kind of reactor stirring vane for synthesizing hexanicit Download PDF

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Publication number
CN206276378U
CN206276378U CN201621166433.5U CN201621166433U CN206276378U CN 206276378 U CN206276378 U CN 206276378U CN 201621166433 U CN201621166433 U CN 201621166433U CN 206276378 U CN206276378 U CN 206276378U
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CN
China
Prior art keywords
gag lever
lever post
stirring vane
chute
tank body
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Expired - Fee Related
Application number
CN201621166433.5U
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Chinese (zh)
Inventor
朱理伟
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Weifang Sheng Yu Pharmaceutical Ltd By Share Ltd
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Weifang Sheng Yu Pharmaceutical Ltd By Share Ltd
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Filing date
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Priority to CN201621166433.5U priority Critical patent/CN206276378U/en
Application granted granted Critical
Publication of CN206276378U publication Critical patent/CN206276378U/en
Expired - Fee Related legal-status Critical Current
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Abstract

A kind of reactor stirring vane for synthesizing hexanicit, including reactor tank body, the sleeve pipe being installed in reactor tank body, two drive devices for being vertically arranged and being rotated relative to the symmetrically arranged stirring vane of sleeve pipe and drive sleeve are rotated vertically, also include:The drive rod being plugged in sleeve pipe, the support for being installed on reactor tank body upper end and the motor for being installed on support and being connected with drive rod are slided vertically.With the carrying out of stirring, motor drives drive rod rotation, so as to gag lever post drive mechanism drives gag lever post I and gag lever post II to be moved along chute I and chute II respectively, now stirring vane deflects motion by axle center of the rotating shaft of middle part, the stirring vane of deflection can not only produce the stirring eddy flow of circumferencial direction in whipping process, axial stirring eddy flow can also be produced, so as to gradually step up the uniformity of the stirring of raw material, the production efficiency and product quality of hexanicit are improve.

Description

A kind of reactor stirring vane for synthesizing hexanicit
Technical field
The utility model is related to reactor technical field, and in particular to a kind of reactor stirring of synthesis hexanicit Blade.
Background technology
Need to use reactor during synthetically produced hexanicit to carry out, the stirring vane one in reactor As use paddle blade or anchor formula blade, the stirring eddy flow direction of the generation in its whipping process is changeless, therefore Being sufficiently mixed between raw material is not well positioned to meet, so as to cause low production efficiency, the drawbacks of synthesis waste production is high.
The content of the invention
The utility model is in order to overcome the shortcomings of above technology, there is provided a kind of to be changed stirring according to reaction The reactor stirring vane of the synthesis hexanicit of blade deflection angle.
The utility model overcomes the technical scheme that its technical problem is used to be:
A kind of reactor stirring vane for synthesizing hexanicit, including reactor tank body, vertical rotation are installed on instead Answer the sleeve pipe in kettle tank body, two be vertically arranged and rotated relative to the symmetrically arranged stirring vane of sleeve pipe and drive sleeve Drive device, also includes:The drive rod being plugged in sleeve pipe, the support and peace for being installed on reactor tank body upper end are slided vertically Loaded on the motor being connected on support and with drive rod, the middle part of the stirring vane is installed by axis of rotation In on sleeve pipe, the stirring vane upper and lower ends are horizontally disposed with limited location bar I and gag lever post II, described sleeve pipe upper and lower ends respectively Twist it is provided with chute I and chute II from top to bottom respectively, the gag lever post I is slided and is plugged in chute I, described spacing Bar II is slided and is plugged in chute II, and gag lever post drive mechanism is provided with the drive rod, spacing when motor is rotated Bar drive mechanism drives gag lever post I and gag lever post II to be moved along chute I and chute II respectively.
Above-mentioned drive device includes the stirring motor for being installed on reactor tank body upper end, the chain being installed on motor output shaft Take turns II, be installed on cannula tip and the chain wheel I on the outside of reactor tank body, chain is passed through between the chain wheel I and chain wheel II Drive connection.
Above-mentioned gag lever post drive mechanism includes being coaxially disposed splined shaft in drive rod lower end, slided by splined hole and insert In the slide bar on splined shaft and the jaw I and jaw II of slide bar upper and lower ends are respectively arranged at, the jaw I is slided and is plugged in In chute I and gag lever post I is located in the slot of jaw I, the jaw II is slided and is plugged in chute II and gag lever post II is located at In the slot of jaw II.
In order to prevent raw material to be bonded on the inwall of reactor tank body, the outboard end of above-mentioned stirring vane is vertically solid Surely there is rubber slab, the outboard end of the rubber slab is in contact with the inwall of reactor tank body.
The beneficial effects of the utility model are:After raw material is added in reactor tank body, the rotation of drive device drive sleeve Turn, so that stirring vane is stirred in reactor tank body, with the carrying out of stirring, motor drives drive rod rotation, So as to gag lever post drive mechanism drives gag lever post I and gag lever post II to be moved along chute I and chute II respectively, now stirring vane with The rotating shaft of middle part deflects motion for axle center, and the stirring vane of deflection can not only produce circumference side in whipping process To stirring eddy flow, additionally it is possible to produce axial direction stirring eddy flow, so as to gradually step up the uniformity of the stirring of raw material, work as stirring After uniform, motor is rotated backward, and stirring vane is recovered to vertical state, the circumferencial direction that now stirring vane is produced Eddy flow need to only ensure that chemical reaction occurs between raw material, therefore improve the production efficiency and product matter of hexanicit Amount.
Brief description of the drawings
Fig. 1 is main view cross-sectional view of the present utility model;
Fig. 2 is sleeve pipe portion structure schematic diagram of the present utility model;
Fig. 3 is drive rod portion structure schematic diagram of the present utility model;
In figure, the 1. chain 8. of 2. support of reactor tank body, 3. motor, 4. sleeve pipe, 5. drive rod, 6. chain wheel I 7. The chute of II 14. chute of stirring motor 9. chain wheel II, 10. stirring vane, 11. rotating shaft, 12. gag lever post, I 13. gag lever post I 15. The rubber slab of II 16. jaw, I 17. jaw, II 18. splined shaft, 19. slide bar 20..
Specific embodiment
Below in conjunction with the accompanying drawings 1, accompanying drawing 2, accompanying drawing 3 are described further to the utility model.
A kind of reactor stirring vane for synthesizing hexanicit, including reactor tank body 1, vertical rotation are installed on instead The sleeve pipe 4, two in kettle tank body 1 is answered to be vertically arranged and relative to the symmetrically arranged stirring vane 10 of sleeve pipe 4 and drive sleeve 4 The drive device of rotation, also includes:Slide vertically be plugged in sleeve pipe 4 drive rod 5, be installed on the upper end of reactor tank body 1 Support 2 and the motor 3 for being installed on support 2 and being connected with drive rod 5, the middle part of stirring vane 10 passes through Rotating shaft 11 is rotated and is installed on sleeve pipe 4, and the upper and lower ends of stirring vane 10 are horizontally disposed with limited location bar I 12 and gag lever post II respectively 13, the upper and lower ends of sleeve pipe 4 are twist provided with chute I 14 and chute II 15 from top to bottom respectively, and gag lever post I 12 is slided It is plugged in chute I 14, gag lever post II 13 is slided and is plugged in chute II 15, and gag lever post driving machine is provided with drive rod 5 Structure, when motor 3 is rotated, gag lever post drive mechanism drives gag lever post I 12 and gag lever post II 13 respectively along chute I 14 Moved with chute II 15.After raw material is added in reactor tank body 1, drive device drive sleeve 4 rotates, so that paddle Piece 10 is stirred in reactor tank body 1, and with the carrying out of stirring, motor 3 drives drive rod 5 to rotate, so that spacing Bar drive mechanism drives gag lever post I 12 and gag lever post II 13 to be moved along chute I 14 and chute II 15 respectively, now paddle , with the rotating shaft 11 of middle part for axle center deflects motion, the stirring vane 10 of deflection not only can be with whipping process for piece 10 Produce circumferencial direction stirring eddy flow, additionally it is possible to produce axial direction stirring eddy flow, so as to gradually stepped up raw material stirring it is equal Even property, after stirring, motor 3 is rotated backward, and stirring vane 10 is recovered to vertical state, now stirring vane 10 The eddy flow of the circumferencial direction of generation need to only ensure that chemical reaction occurs between raw material, therefore improve the life of hexanicit Produce efficiency and product quality.
Drive device can be following structure, and it includes being installed on the stirring motor 8 of the upper end of reactor tank body 1, is installed on Chain wheel II 9 on the output shaft of motor 8, it is installed on the top of sleeve pipe 4 and positioned at the chain wheel I 6 in the outside of reactor tank body 1, chain wheel I 6 It is connected by chain 7 between chain wheel II 9.Stirring motor 8 is rotated, and its drive sprocket II 9 is rotated, and chain wheel II 9 passes through 7 drive sprocket of chain I 6 is rotated, so that sleeve pipe 4 drives stirring vane 10 to rotate, realizes the mixing of raw material.
Gag lever post drive mechanism can be following structure, and it includes being coaxially disposed splined shaft 18 in the lower end of drive rod 5, logical Cross splined hole slide the slide bar 19 being plugged on splined shaft 18 and the jaw I 16 that is respectively arranged at the upper and lower ends of slide bar 19 and Jaw II 17, the slip of jaw I 16 is plugged in chute I 14 and gag lever post I 12 is located in the slot of jaw I 16, jaw II 17 slips are plugged in chute II 15 and gag lever post II 13 is located in the slot of jaw II 17.Motor 3 is rotated, its drive Dynamic drive rod 5 is rotated, and drive rod 5 is rotated by splined shaft 18 with moving slide-bar 19, because jaw I 16 and jaw II 17 are in chute I 14 and chute II 15 in slide, therefore slide bar 19 be side rotation the above-below direction stretching motion of edge drive rod 5, while slide bar 19 because jaw I 16 and the holding of jaw II 17 are in chute I 14 and chute II 15, and it does not fall out.Jaw I 16 and fork First II 17 when sliding, and it drives the gag lever post I 12 and gag lever post II 13 that are located in jaw I 16 and jaw II 17 along cunning Groove I 14 and chute II 15 are slided, and realize the deflection of stirring vane 10.
Further, the outboard end of stirring vane 10 is vertically fixed with rubber slab 20, the outboard end of rubber slab 20 Inwall with reactor tank body 1 is in contact.When stirring vane 10 is rotated, rubber slab 20 is by the original on the inwall of reactor tank body 1 Material can strike off, and preventing raw material to be bonded on inwall causes the situation for influenceing reaction efficiency to occur.

Claims (4)

1. a kind of reactor stirring vane for synthesizing hexanicit, including reactor tank body(1), vertically rotate be installed on it is anti- Answer kettle tank body(1)In sleeve pipe(4), two be vertically arranged and relative to sleeve pipe(4)Symmetrically arranged stirring vane(10)And Drive sleeve(4)The drive device of rotation, it is characterised in that also include:Slide vertically and be plugged in sleeve pipe(4)In drive rod (5), be installed on reactor tank body(1)The support of upper end(2)And it is installed on support(2)Upper and and drive rod(5)Drive connection Motor(3), the stirring vane(10)Middle part pass through rotating shaft(11)Rotation is installed on sleeve pipe(4)On, it is described Stirring vane(10)Upper and lower ends are horizontally disposed with limited location bar I respectively(12)And gag lever post II(13), described sleeve pipe(4)Upper and lower two End is twist provided with chute I from top to bottom respectively(14)With chute II(15), the gag lever post I(12)Slip is plugged in cunning Groove I(14)In, the gag lever post II(13)Slip is plugged in chute II(15)In, the drive rod(5)On be provided with gag lever post Drive mechanism, works as motor(3)During rotation, gag lever post drive mechanism drives gag lever post I(12)And gag lever post II(13)Respectively Along chute I(14)With chute II(15)Motion.
2. it is according to claim 1 synthesis hexanicit reactor stirring vane, it is characterised in that:The driving Device includes being installed on reactor tank body(1)The stirring motor of upper end(8), be installed on motor(8)Chain wheel II on output shaft (9), be installed on sleeve pipe(4)Top and positioned at reactor tank body(1)The chain wheel I in outside(6), the chain wheel I(6)With chain wheel II (9)Between pass through chain(7)Drive connection.
3. it is according to claim 1 and 2 synthesis hexanicit reactor stirring vane, it is characterised in that:It is described Gag lever post drive mechanism includes being coaxially disposed in drive rod(5)The splined shaft of lower end(18), by splined hole slide be plugged in flower Key axle(18)On slide bar(19)And it is respectively arranged at slide bar(19)The jaw I of upper and lower ends(16)And jaw II(17), institute State jaw I(16)Slip is plugged in chute I(14)In and gag lever post I(12)Positioned at jaw I(16)Slot in, the jaw II (17)Slip is plugged in chute II(15)In and gag lever post II(13)Positioned at jaw II(17)Slot in.
4. it is according to claim 3 synthesis hexanicit reactor stirring vane, it is characterised in that:The stirring Blade(10)Outboard end be vertically fixed with rubber slab(20), the rubber slab(20)Outboard end and reactor tank body (1)Inwall be in contact.
CN201621166433.5U 2016-11-02 2016-11-02 A kind of reactor stirring vane for synthesizing hexanicit Expired - Fee Related CN206276378U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621166433.5U CN206276378U (en) 2016-11-02 2016-11-02 A kind of reactor stirring vane for synthesizing hexanicit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621166433.5U CN206276378U (en) 2016-11-02 2016-11-02 A kind of reactor stirring vane for synthesizing hexanicit

Publications (1)

Publication Number Publication Date
CN206276378U true CN206276378U (en) 2017-06-27

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107213861A (en) * 2017-07-28 2017-09-29 德清县东来化学有限公司 A kind of liquid barium zinc heat stabilizer production reactor
CN107213860A (en) * 2017-07-28 2017-09-29 德清县东来化学有限公司 A kind of reactor for producing liquid barium zinc heat stabilizer
CN107252669A (en) * 2017-07-28 2017-10-17 德清县东来化学有限公司 Automatic charging reactor is used in a kind of liquid barium zinc heat stabilizer production
CN107262004A (en) * 2017-07-28 2017-10-20 德清县东来化学有限公司 A kind of liquid barium zinc heat stabilizer production reactor of good antiscale property

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107213861A (en) * 2017-07-28 2017-09-29 德清县东来化学有限公司 A kind of liquid barium zinc heat stabilizer production reactor
CN107213860A (en) * 2017-07-28 2017-09-29 德清县东来化学有限公司 A kind of reactor for producing liquid barium zinc heat stabilizer
CN107252669A (en) * 2017-07-28 2017-10-17 德清县东来化学有限公司 Automatic charging reactor is used in a kind of liquid barium zinc heat stabilizer production
CN107262004A (en) * 2017-07-28 2017-10-20 德清县东来化学有限公司 A kind of liquid barium zinc heat stabilizer production reactor of good antiscale property

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

Granted publication date: 20170627

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