CN203990638U - Cathode electrophoresis dope reaction unit - Google Patents
Cathode electrophoresis dope reaction unit Download PDFInfo
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- CN203990638U CN203990638U CN201420485525.4U CN201420485525U CN203990638U CN 203990638 U CN203990638 U CN 203990638U CN 201420485525 U CN201420485525 U CN 201420485525U CN 203990638 U CN203990638 U CN 203990638U
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- reactor body
- condenser
- reaction unit
- collecting tank
- transverse axis
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Abstract
The utility model proposes a kind of cathode electrophoresis dope reaction unit, belong to chemical machinery field.It comprises reactor body, motor and condenser, described motor be positioned at reactor body directly over, condenser is positioned at the side top of reactor body, reactor bodies top is provided with charging aperture, bottom is provided with discharging opening, under described motor, be connected with shaft, described shaft stretches in reactor body, the bottom of described shaft is provided with stirring transverse axis, the two ends of described stirring transverse axis are respectively arranged with paddle, described paddle and described stirring transverse axis are 30~45 ° of angles, with vertical direction angle of inclination be 30 °; Described condenser comprises two parts, is respectively the liquid collecting tank of superposed condenser pipe and bottom, and described liquid collecting tank outside is coated with heat-insulation layer, and described liquid collecting tank below is provided with outlet, and described outlet is communicated with reactor body by pipeline; This reaction unit have stir, reacting balance and discharging advantage easily.
Description
Technical field
The utility model relates to a kind of cathode electrophoresis dope reaction unit, belongs to chemical mechanical equipment field.
Background technology
Electrophoretic coating, as the novel low pollution of a class, the coating of high anticorrosive property, has been widely used in the application of the parts such as automobile, automatic vehicle, steamer, household electrical appliances.In the actual one-tenth product process of cathode electrophoresis dope, the synthetic of binder resin need to carry out in reactor, because material viscosity is larger, in stirring reaction process, traditional agitating device can cause mixing of materials inhomogeneous, and phegma fluctuation is larger, thereby the carrying out of impact reaction and the quality of product, in discharge process, can only discharge by the gravity of material self, discharge process is consuming time longer, the carrying out that impact is produced.
Utility model content
In order to solve problems of the prior art, the utility model proposes a kind of cathode electrophoresis dope reaction unit, the paddle of this reaction unit is 30 °-45 ° of angles with stirring transverse axis, with vertical direction angle of inclination be 30 °, thereby reach mixing of materials evenly, the effect of reacting balance and acceleration discharging.
Its technical solution comprises:
A kind of cathode electrophoresis dope reaction unit, it comprises reactor body, motor and condenser, described motor be positioned at reactor body directly over, condenser is positioned at the side top of reactor body, the top of described reactor body is provided with charging aperture, bottom is provided with discharging opening, under described motor, be connected with shaft, described shaft stretches in reactor body, the bottom of described shaft is provided with stirring transverse axis, the two ends of described stirring transverse axis are respectively arranged with paddle, described paddle and described stirring transverse axis are 30~45 ° of angles, with vertical direction angle of inclination be 30 °, described condenser comprises two parts, is respectively the liquid collecting tank of superposed condenser pipe and bottom, and described liquid collecting tank outside is coated with heat-insulation layer, and described liquid collecting tank below is provided with outlet, and described outlet is communicated with reactor body by pipeline.
Described pipeline is provided with the flowmeter for controlling fluid flow.
Described reactor body below is provided with heating jacket layer.
Described paddle is set to rectangle, its material selection steel plate.
The useful technique effect that the utility model brings:
The utility model proposes a kind of cathode electrophoresis dope reaction unit, this reaction unit comprises motor, condenser and reactor body, this volume surrounding of reactor is provided with heating jacket layer, inside is provided with shaft, and shaft bottom is provided with stirring transverse axis, stirs transverse axis two ends and is respectively equipped with paddle, paddle is rectangular steel plates, paddle with stir transverse axis be 30 °-45 ° of angles, with vertical direction angle of inclination be 30 °, bottom is provided with discharging opening.In the time that reaction is carried out, paddle can produce two power to coating in whipping process, one of them power is the axial-rotation power moving in a circle by coating by shaft, and another one power is the power that allows coating continue to move downward, and coating is because pressure-acting continues to move downward, after at the bottom of contact still, rebound upwards, impel coating to mix, therefore can not produce dead angle, and in the time of discharging, because dope viscosity is larger, the downward power of paddle can be accelerated coating and discharge from bottom discharge mouth.
Outlet below liquid collecting tank is communicated with reactor body by pipeline, and is provided with flowmeter on pipeline, passes back into the liquid of reactor body by flowmeter control, reduces fluctuation, ensures that reacting balance carries out.
Brief description of the drawings
Below in conjunction with accompanying drawing, the utility model is done to further clear complete explanation:
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the utility model mixing part top view;
In figure, 1, motor, 2, reactor body, 3, nitrogen tube, 4, heating jacket layer, 5, discharging opening, 6, condenser, 7, liquid collecting tank, 8, flowmeter, 9, shaft, 10, paddle, 11, stir transverse axis.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is done to further clear, complete explanation.
As Fig. 1, shown in Fig. 2, the utility model, a kind of cathode electrophoresis dope reaction unit, it comprises reactor body 2, be arranged on the motor 1 directly over reactor body 2 and be arranged on the condenser 6 of reactor body 2 sides tops, this outer middle and lower part of reactor body 2 is provided with heating jacket layer 4, heating jacket layer 4 heats reactor body 2 by outside heating steam, reactor body 2 tops are provided with charging aperture, reactor body 2 sidewalls are provided with nitrogen tube 3, required nitrogen enters reactor body 2 inside by nitrogen tube 3, reactor body 2 bottoms are provided with discharging opening 5, product is from discharging opening 5 extraction.
Structural similarity in above-mentioned motor 1 and prior art, motor 1 below is connected with shaft 9, motor 1 drives shaft 9 to rotate by its inner driving mechanism, coating below at least will be stretched in the bottom of shaft 9, shaft 9 bottoms are connected with stirs transverse axis 11, stirs transverse axis 11 two ends and is connected with respectively paddle 10, and paddle 10 is preferably rectangular steel plates, paddle 10 is 30 °~45 ° of angles with stirring transverse axis 11, and paddle 10 is 30 ° with vertical direction angle of inclination; In the time that reaction is carried out, paddle 10 can produce two power to coating in whipping process, one of them power is the axial-rotation power moving in a circle by coating by shaft, and another one power is the power that allows coating continue to move downward, and coating is because pressure-acting continues to move downward, after at the bottom of contact still, rebound upwards, impel coating to mix, therefore can not produce dead angle, and in the time of discharging, because dope viscosity is larger, the downward power of paddle can be accelerated coating and discharge from bottom discharge mouth 5.
Above-mentioned condenser 6 comprises top condenser pipe and bottom liquid collecting tank 7, liquid collecting tank 7 outsides are provided with heat-insulation layer, when the liquid getting off when condensation enters liquid collecting tank 7, due to the insulation effect of heat-insulation layer, can reduce the loss of heat, the outlet of liquid collecting tank 7 belows is communicated with reactor body 2 by pipeline, on pipeline, be provided with flowmeter 8, control by flowmeter 8 liquid that passes back into reactor body 2, reduce fluctuation, ensure that reacting balance carries out.
The cardinal principle method of work of above-mentioned cathode electrophoresis dope reaction unit is as follows:
First, in reactor body 2, pass into nitrogen by nitrogen tube 3, open charging aperture and add material in reactor body 2, open motor 1 and stir;
Then, in heating jacket layer 4, passing into heating steam heats, along with the carrying out of reaction, Partial Liquid Phase heat absorption in material becomes gas phase, gas phase enters condenser 6, the condensed liquid phase that becomes, enters liquid collecting tank 7, and in liquid collecting tank 7, liquid phase passes back into reactor body 2 by flowmeter 8 with certain flow velocity;
Finally, after question response completes, material is by discharging opening 5 extraction.
It should be noted that, under the instruction of this description, those skilled in the art can also make such or such variation, such as equivalent way, or obvious mode of texturing.Above-mentioned variation pattern all should be within protection domain of the present utility model.
Claims (4)
1. a cathode electrophoresis dope reaction unit, it comprises reactor body, motor and condenser, described motor be positioned at reactor body directly over, condenser is positioned at the side top of reactor body, the top of described reactor body is provided with charging aperture, bottom is provided with discharging opening, it is characterized in that: under described motor, be connected with shaft, described shaft stretches in reactor body, the bottom of described shaft is provided with stirring transverse axis, the two ends of described stirring transverse axis are respectively arranged with paddle, described paddle and described stirring transverse axis are 30~45 ° of angles, with vertical direction angle of inclination be 30 °, described condenser comprises two parts, is respectively the liquid collecting tank of superposed condenser pipe and bottom, and described liquid collecting tank outside is coated with heat-insulation layer, and described liquid collecting tank below is provided with outlet, and described outlet is communicated with reactor body by pipeline.
2. cathode electrophoresis dope reaction unit according to claim 1, is characterized in that: described pipeline is provided with the flowmeter for controlling fluid flow.
3. cathode electrophoresis dope reaction unit according to claim 1, is characterized in that: described reactor body below is provided with heating jacket layer.
4. cathode electrophoresis dope reaction unit according to claim 1, is characterized in that: described paddle is set to rectangle, its material selection steel plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420485525.4U CN203990638U (en) | 2014-08-20 | 2014-08-20 | Cathode electrophoresis dope reaction unit |
Applications Claiming Priority (1)
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CN201420485525.4U CN203990638U (en) | 2014-08-20 | 2014-08-20 | Cathode electrophoresis dope reaction unit |
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CN203990638U true CN203990638U (en) | 2014-12-10 |
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CN201420485525.4U Expired - Fee Related CN203990638U (en) | 2014-08-20 | 2014-08-20 | Cathode electrophoresis dope reaction unit |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
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CN105087918A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Non-ammonia-leakage type copper mine efficient chemical combination leaching device |
CN105087928A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Total-ammonia recovery type copper mine efficient chemical combination leaching device |
CN105087920A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Environment-friendly efficient copper mine combination leaching device with reverse-cone sieve disc |
CN105087923A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Cyclone separation environment-friendly copper mine efficient chemical combination leaching device |
CN105087922A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Cyclone separation ammonia total-recycle-type copper mine efficient chemical combination leaching device |
CN105087917A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Environment-friendly copper mine efficient chemical combination leaching device |
CN105087921A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Effective counter-cone sieve plate ammonia full-recycling type copper mine combined leaching device |
CN105112653A (en) * | 2015-10-07 | 2015-12-02 | 吉首大学 | Reverse cone sieve disk ammonia leakage-free efficient chemical combination leaching device of copper ore |
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2014
- 2014-08-20 CN CN201420485525.4U patent/CN203990638U/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105087918A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Non-ammonia-leakage type copper mine efficient chemical combination leaching device |
CN105087928A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Total-ammonia recovery type copper mine efficient chemical combination leaching device |
CN105087920A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Environment-friendly efficient copper mine combination leaching device with reverse-cone sieve disc |
CN105087923A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Cyclone separation environment-friendly copper mine efficient chemical combination leaching device |
CN105087922A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Cyclone separation ammonia total-recycle-type copper mine efficient chemical combination leaching device |
CN105087917A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Environment-friendly copper mine efficient chemical combination leaching device |
CN105087921A (en) * | 2015-10-07 | 2015-11-25 | 吉首大学 | Effective counter-cone sieve plate ammonia full-recycling type copper mine combined leaching device |
CN105112653A (en) * | 2015-10-07 | 2015-12-02 | 吉首大学 | Reverse cone sieve disk ammonia leakage-free efficient chemical combination leaching device of copper ore |
CN105087918B (en) * | 2015-10-07 | 2017-09-29 | 吉首大学 | The efficient chemical combination leaching device of ammonia No leakage formula copper mine |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141210 Termination date: 20150820 |
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EXPY | Termination of patent right or utility model |