CN206622105U - A kind of ink resin special reactor - Google Patents
A kind of ink resin special reactor Download PDFInfo
- Publication number
- CN206622105U CN206622105U CN201720357929.9U CN201720357929U CN206622105U CN 206622105 U CN206622105 U CN 206622105U CN 201720357929 U CN201720357929 U CN 201720357929U CN 206622105 U CN206622105 U CN 206622105U
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- China
- Prior art keywords
- reactor
- big
- small
- agitating shaft
- controller
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Abstract
The utility model discloses a kind of ink resin special reactor,Including reactor shell,Controller,Small reactor agitating shaft,Swing stirring vane and big reactor,Controller is provided with kettle reactor shell,Small reactor and big reactor,Controller uses PLC,The lower end of small reactor is connected by reactor connector with big reactor,Small reactor agitating shaft is provided with small reactor,The upper end of small reactor is additionally provided with small liquid tank and small powder tank,Big reactor agitating shaft is provided with big reactor and swings stirring vane,The upper end of big reactor is additionally provided with big liquid tank and big powder tank,The utility model adapts to the processing of obstructed production conditions by two reactors of size,And both can also be used cooperatively,And it is Automatic Control in process,Relative to artificial,Add its machining accuracy and operating efficiency,Stirring vane is swung by being set in big reactor,So that accelerate reaction speed and efficiency.
Description
Technical field
The utility model belongs to ink resin processing equipment field, is related to a kind of reactor, and in particular to a kind of ink tree
Fat special reactor.
Background technology
Resin typically refer to it is heated after be softened or melted scope, have liquidity preference, normal temperature under external force during softening
Under be solid-state, semisolid, can also be the organic polymer of liquid sometimes.In a broad aspect, plastic products processing can be used as former
Any high-molecular compound of material is referred to as resin.Resin be manufacture plastics primary raw material, also be used for coating processed, binder,
Insulating materials etc., synthetic resin in the industrial production, are widely used in the separation and purifying of impurities in liquid, there is macroporous absorption
Resin, ion exchange resin and some are resin dedicated.
The raw material in production of resins is manual control at present, but such a mode wastes time and energy, and often occurs that raw material is added
Or situation about adding less, it is difficult to accurate measurement raw material, easily malfunctions, poor accuracy, so that the quality of naval stores can not ensure,
Qualification rate is relatively low, and for different working conditions, the amount of processing is also different, and a kind of reactor of quantitative volumetric can not meet not
Same working condition.So I develops a kind of ink resin special reactor.
Utility model content
In order to solve above-mentioned problem, the utility model provides a kind of ink resin special reactor.
The utility model is to be achieved through the following technical solutions：
A kind of ink resin special reactor, including reactor shell, controller, small reactor agitating shaft, swing stirring
Blade and big reactor, controller, small reactor and big reactor are provided with the kettle reactor shell, the controller is adopted
With PLC, the small reactor and big reactor are fixed on kettle reactor enclosure, the small reaction by reactor fixator
The lower end of kettle is connected by reactor connector with big reactor, and the upper end of the small reactor is installed with small reactor driving electricity
Machine, the output shaft of the small reactor motor are connected to the small reactor agitating shaft in small reactor, the small reactor
Upper end be additionally provided with small liquid tank and small powder tank；The upper end of the big reactor is provided with big reactor motor, institute
The output shaft for stating big reactor motor is connected to big reactor agitating shaft in big reactor, the upper end of the big reactor
It is additionally provided with big liquid tank and big powder tank；Blade is equipped with the small reactor agitating shaft and big reactor agitating shaft, institute
The blade stated on big reactor agitating shaft is arranged in a crossed manner with swinging stirring vane, and the swing stirring vane is consolidated by mounting flange
It is scheduled on the inwall of big reactor, the swing stirring vane is connected by swinging ball with oscillating vane seat, the swing leaf
Bar limits the both sides for swinging stirring vane by limit spring, and the oscillating vane seat is fixedly connected with mounting flange.
Preferably, the output end of the small liquid tank, small powder tank, big liquid tank and big powder tank is mounted on metering control
System switch, four measure control switches are connected to controller by wire.
Preferably, the small liquid tank and big liquid tank are connected by liquid conducting pipes with liquid material storage tank, institute
State the side that liquid material storage tank is placed on reactor shell.
Preferably, the side of the reactor shell is provided with control panel, and the control panel is connected by data wire
Controller.
Preferably, the lower end of the kettle reactor shell is propped up on the ground by bottom seat.
Preferably, the lower end of the big reactor is provided with discharge gate, and the discharge gate is connected to controller by wire.
Compared with prior art, the beneficial effects of the utility model are：The utility model passes through two reactors of size
To adapt to the processing of obstructed production conditions, and both can also be used cooperatively, and be Automatic Control in process, phase
For artificial, its machining accuracy and operating efficiency are added, stirring vane is swung by being set in big reactor so that
Accelerate reaction speed and efficiency.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model；
Fig. 2 is the structural representation of swing stirring vane of the present utility model.
In figure：1st, bottom seat；2nd, reactor shell；3rd, controller；4th, control panel；5th, reactor connector；6th, it is small anti-
Answer kettle；7th, small reactor agitating shaft；8th, small reactor motor；9th, measure control switchs；10th, small liquid tank；11st, liquid is defeated
Send pipeline；12nd, small powder tank；13rd, big liquid tank；14th, big powder tank；15th, big reactor motor；16th, liquid material is deposited
Storage tank；17th, big reactor agitating shaft；18th, stirring vane is swung；19th, reactor fixator；20th, big reactor；21st, discharge gate；
22nd, limit spring；23rd, ball is swung；24th, oscillating vane seat；25th, mounting flange.
Embodiment
The utility model is described in further detail with embodiment below in conjunction with the accompanying drawings：
As shown in Figure 1-2, a kind of ink resin special reactor, including reactor shell 2, controller 3, small reactor stir
Mix axle 7, swing stirring vane 18 and big reactor 20, controller 3, small reactor 6 and big anti-are provided with kettle reactor shell 2
Kettle 20 is answered, controller 3 uses PLC, and small reactor 6 and big reactor 20 are mutually permanently connected and gone back by reactor fixator 19
It is fixed on inside kettle reactor shell 2, the lower end of small reactor 6 is connected by reactor connector 5 with big reactor 20 so that
Small reactor 6 can connect use with big reactor 20, and the upper end of small reactor 6 is installed with small reactor motor 8, small anti-
Answer the output shaft of kettle motor 8 to be connected to small reactor agitating shaft 7 in small reactor 6, by small reactor agitating shaft 7 plus
Fast response speed, the upper end of small reactor 6 are additionally provided with small liquid tank 10 and small powder tank 12, pass through small liquid tank 10 and starch
Last tank 12 is fed to small reactor 6；The upper end of big reactor 20 is provided with big reactor motor 15, big reactor driving electricity
The output shaft of machine 15 is connected to the big reactor agitating shaft 17 in big reactor 20, is accelerated by big reactor agitating shaft 17 big anti-
The reaction speed of material in kettle 20 is answered, the upper end of big reactor 20 is additionally provided with big liquid tank 13 and big powder tank 14, by big
Liquid tank 13 and big powder tank 14 are fed to big reactor 20, are all provided with small reactor agitating shaft 7 and big reactor agitating shaft 17
Have a blade, blade on big reactor agitating shaft 17 and to swing stirring vane 18 arranged in a crossed manner, swing stirring vane 18 pass through it is solid
Determine flange 25 to be fixed on the inwall of big reactor 20, reaction speed can be accelerated by swinging stirring vane 18, swing stirring vane
18 are connected by swinging ball 23 with oscillating vane seat 24, and oscillating vane seat 24 is limited by limit spring 22 and swings stirring vane
18 both sides, oscillating vane seat 24 are fixedly connected with mounting flange 25, small liquid tank 10, small powder tank 12, the and of big liquid tank 13
The output end of big powder tank 14 is mounted on measure control switch 9, and accurately controlling material by measure control switch 9 inputs
Amount, four measure control switches 9 are connected to controller 3 by wire, and small liquid tank 10 and big liquid tank 13 are conveyed by liquid
Pipeline 11 is connected with liquid material storage tank 16, and liquid material storage tank 16 is placed on the side of reactor shell 2, outside reactor
The side of shell 2 is provided with control panel 4, can pay close attention to or control the response situation in reactor by control panel 4, control
Panel 4 is connected to controller 3 by data wire, the lower end of kettle reactor shell 2 by bottom seat 1 on the ground, big reaction
The lower end of kettle 20 is provided with discharge gate 21, and discharge gate 21 is connected to controller 3 by wire, and reaction can be discharged by discharge gate 21
The material of completion excludes from discharge gate 21, and discharge gate 21 can be by setting in control panel 4, and controls its switch by controller
Amount and switch time.
Operation principle：When small yield, liquid and powder are provided to small reactor 6 by small liquid tank 10 and small powder tank 12
Last material, the amount of blanking can be accurately controlled in the measure control switch 9 of 12 times installations of small liquid tank 10 and small powder tank, then
Drive small reactor agitating shaft 7 in small reactor 6 to rotate by small reactor motor 8, installed on small reactor agitating shaft 7
There is blade, by the rotation of small reactor agitating shaft 7, and the blade of upper installation can stir material in small reactor 6 so that add
Fast response speed；If if the big processing of yield, provided by big liquid tank 13 and big powder tank 14 to big reactor 20
Liquid and powder material, it is big anti-then by driving big reactor motor 15 to allow big reactor agitating shaft 17 to rotate
Answer and be also equipped with blade on kettle agitating shaft 17, be additionally provided with big reactor 20 and swing stirring vane 18, swing stirring vane 18
It is to be connected by swinging ball 23 with oscillating vane seat 24, the other end of oscillating vane seat 24 is fixed on greatly by mounting flange 25
The inwall of reactor 20, it is to be slidably connected to swing ball 23 and oscillating vane seat 24 so that swings the opposing oscillatory leaf of stirring vane 18
Bar 24 can do oscillating motion, and the both sides of oscillating vane seat 24 swing the two of stirring vane 18 by limit spring 22 to limit
Side, original position is returned to by the restoring force of limit spring 22 in swing process so as to swing stirring vane 18, stirred
During material, by the stirring of big reactor agitating shaft 17, material can rotate in big reactor 20 so that promote
Swing stirring vane 18 and do oscillating motion, swing stirring vane 18 and recovery motion is done by the limit spring 22 of both sides so that add
The speed stirred soon, reaction efficiency is improved, is passed through after having stirred material.
General principle, principal character and advantage of the present utility model has been shown and described above.The technical staff of the industry
It should be appreciated that the utility model is not restricted to the described embodiments, the simply explanation described in above-described embodiment and specification is originally
The principle of utility model, on the premise of the spirit and scope of the utility model is not departed from, the utility model also has various change
And improvement, these changes and improvements are both fallen within claimed the scope of the utility model.The utility model requires protection scope
By appended claims and its equivalent thereof.
Claims (6)
1. a kind of ink resin special reactor, including reactor shell (2), controller (3), small reactor agitating shaft (7), pendulum
Dynamic stirring vane (18) and big reactor (20), it is characterised in that：Controller (3), small is provided with the reactor shell (2)
Reactor (6) and big reactor (20), the controller (3) use PLC, and the small reactor (6) and big reactor (20) are logical
Cross reactor fixator (19) and be fixed on kettle reactor shell (2) inside, the lower end of the small reactor (6) is connected by reactor
Connect device (5) to be connected with big reactor (20), the upper end of the small reactor (6) is installed with small reactor motor (8), described
The output shaft of small reactor motor (8) is connected to the small reactor agitating shaft (7) in small reactor (6), the small reaction
The upper end of kettle (6) is additionally provided with small liquid tank (10) and small powder tank (12)；The upper end of the big reactor (20) is provided with greatly
Reactor motor (15), the output shaft of the big reactor motor (15) are connected to big anti-in big reactor (20)
Kettle agitating shaft (17) is answered, the upper end of the big reactor (20) is additionally provided with big liquid tank (13) and big powder tank (14)；It is described
Blade is equipped with small reactor agitating shaft (7) and big reactor agitating shaft (17), on the big reactor agitating shaft (17)
Blade is arranged in a crossed manner with swinging stirring vane (18), and the swing stirring vane (18) is fixed on big anti-by mounting flange (25)
On the inwall for answering kettle (20), the swing stirring vane (18) is connected by swinging ball (23) with oscillating vane seat (24), institute
State oscillating vane seat (24) and the both sides for swinging stirring vane (18), the oscillating vane seat (24) are limited by limit spring (22)
It is fixedly connected with mounting flange (25).
A kind of 2. ink resin special reactor according to claim 1, it is characterised in that：The small liquid tank (10),
The output end of small powder tank (12), big liquid tank (13) and big powder tank (14) is mounted on measure control switch (9), four institutes
State measure control switch (9) and controller (3) is connected to by wire.
A kind of 3. ink resin special reactor according to claim 1, it is characterised in that：The small liquid tank (10) and
Big liquid tank (13) is connected by liquid conducting pipes (11) with liquid material storage tank (16), the liquid material storage tank
(16) it is placed on the side of reactor shell (2).
A kind of 4. ink resin special reactor according to claim 1, it is characterised in that：The reactor shell (2)
Side control panel (4) is installed, the control panel (4) is connected to controller (3) by data wire.
A kind of 5. ink resin special reactor according to claim 1, it is characterised in that：The kettle reactor shell
(2) propped up on the ground by bottom seat (1) lower end.
A kind of 6. ink resin special reactor according to claim 1, it is characterised in that：The big reactor (20)
Lower end is provided with discharge gate (21), and the discharge gate (21) is connected to controller (3) by wire.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720357929.9U CN206622105U (en) | 2017-04-07 | 2017-04-07 | A kind of ink resin special reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720357929.9U CN206622105U (en) | 2017-04-07 | 2017-04-07 | A kind of ink resin special reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206622105U true CN206622105U (en) | 2017-11-10 |
Family
ID=60207845
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720357929.9U Expired - Fee Related CN206622105U (en) | 2017-04-07 | 2017-04-07 | A kind of ink resin special reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206622105U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108079929A (en) * | 2018-01-31 | 2018-05-29 | 四川普思瑞新材料有限公司 | A kind of production of resins system |
| CN109078354A (en) * | 2018-09-23 | 2018-12-25 | 天津市艾碘科技股份有限公司 | A kind of industrial coarse iodine recycling agitating device |
| CN113648955A (en) * | 2021-09-01 | 2021-11-16 | 东营益美得化工有限公司 | Plasticizer esterification reaction device |
-
2017
- 2017-04-07 CN CN201720357929.9U patent/CN206622105U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108079929A (en) * | 2018-01-31 | 2018-05-29 | 四川普思瑞新材料有限公司 | A kind of production of resins system |
| CN108079929B (en) * | 2018-01-31 | 2023-08-15 | 四川普思瑞新材料有限公司 | Resin production system |
| CN109078354A (en) * | 2018-09-23 | 2018-12-25 | 天津市艾碘科技股份有限公司 | A kind of industrial coarse iodine recycling agitating device |
| CN113648955A (en) * | 2021-09-01 | 2021-11-16 | 东营益美得化工有限公司 | Plasticizer esterification reaction device |
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Legal Events
| 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: 20171110 Termination date: 20190407 |
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| CF01 | Termination of patent right due to non-payment of annual fee |