CN202983662U - Emulsion production device - Google Patents
Emulsion production device Download PDFInfo
- Publication number
- CN202983662U CN202983662U CN 201320021041 CN201320021041U CN202983662U CN 202983662 U CN202983662 U CN 202983662U CN 201320021041 CN201320021041 CN 201320021041 CN 201320021041 U CN201320021041 U CN 201320021041U CN 202983662 U CN202983662 U CN 202983662U
- Authority
- CN
- China
- Prior art keywords
- plc
- measuring tank
- emulsion production
- process units
- material inlet
- 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
Links
- 239000000839 emulsion Substances 0.000 title abstract description 13
- 238000004519 manufacturing process Methods 0.000 title abstract description 10
- 238000007599 discharging Methods 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000003860 storage Methods 0.000 claims abstract description 7
- 238000004945 emulsification Methods 0.000 claims description 12
- 239000002184 metal Substances 0.000 claims description 6
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 abstract description 22
- 239000004925 Acrylic resin Substances 0.000 abstract description 7
- 229920000178 Acrylic resin Polymers 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 6
- 238000001914 filtration Methods 0.000 abstract description 3
- 238000007906 compression Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
- 239000002994 raw material Substances 0.000 description 6
- 238000007792 addition Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000000994 depressed Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
Abstract
The utility model relates to the technical field of water-based acrylic resin emulsion production devices, and provides an emulsion production device. The emulsion production device comprises a reaction still, wherein a material outlet is formed in the bottom portion of the reaction still and a material inlet is formed in the top portion of the reaction still. The material outlet is communicated with a filter device. The top portion of the reaction still is provided with an air compression port. The material inlet is provided with a material storage tank, a material inlet pump, and a measuring tank, wherein the material storage tank, the material inlet pump, and the measuring tank are communicated in sequence. A material inlet valve is arranged on an inlet pipeline of the material inlet pump. A liquid level gauge is arranged on the measuring tank. A material outlet pipeline of the measuring tank is provided with a material outlet valve and a material outlet flow gauge in sequence. The emulsion production device further comprises a programmable logic controller (PLC), wherein the liquid level gauge is connected with an input end of the PLC in an electric mode and the material inlet valve is connected with an output end of the PLC in an electric mode. The emulsion production device can resolve the problems that a filtering process does not exist in an existing industry, material discharging is not thorough, precision of added quantity is poor and the like.
Description
Technical field
The utility model relates to water-borne acrylic resin emulsion production equipment technical field, is specially a kind of emulsion process units.
Background technology
Emulsion acrylic resin is widely used in as a kind of building coating emulsion the production that building coating and technique are used paint.There is following problem in traditional emulsion acrylic resin production technology: one, there is no filter progress, and in the emulsion acrylic resin production process, usually owing to containing various impurity in raw material or auxiliary agent, and cause the quality and performance of finished product to be had a greatly reduced quality; Two, due to the viscosity of emulsion acrylic resin large (being generally 200-3000mpa.s), also have the unclean situation of discharging, residual material not only causes waste, in the building-up process of next batch material, also can further react, generate accessory substance, affect product quality; Three, adopt manually add raw material and auxiliary agent in measuring tank, addition accuracy and rate of addition are difficult to precise control, cause monomer reaction abundant not, considerable influence product quality.
The utility model content
Technical problem to be solved in the utility model is: a kind of emulsion process units is provided, can solves simultaneously the problems referred to above that prior art exists.
For solving the problems of the technologies described above, the utility model provides following technical scheme:
A kind of emulsion process units comprises that the bottom is provided with the reactor that discharging opening, top are provided with charging aperture, and described discharging opening is communicated with filter, and the top of described reactor is provided with compressed air interface; Described charging aperture is provided with storage tank, feed pump and the measuring tank that is communicated with successively, the inlet ductwork of described feed pump is provided with inlet valve, described measuring tank is provided with liquid level gauge, be provided with successively bleeder valve and discharging flow meter on the discharging pipeline of described measuring tank, described emulsion process units also comprises PLC, described liquid level gauge is electrically connected to the input of PLC, and described inlet valve is electrically connected to the output of PLC.
Preferably, described filter is filter vat, and charging aperture place, described filter vat inside is provided with metal screen.
Preferably, described metal screen detachably is arranged in described filter vat.
Preferably, described reactor is provided with agitating device and condensation reflux unit.
after having adopted technique scheme, the beneficial effects of the utility model are: because described discharging opening is communicated with filter, the top of described reactor is provided with compressed air interface, described charging aperture is provided with the storage tank that is communicated with successively, feed pump and measuring tank, the inlet ductwork of described feed pump is provided with inlet valve, described measuring tank is provided with liquid level gauge, be provided with successively bleeder valve and discharging flow meter on the discharging pipeline of described measuring tank, described emulsion process units also comprises PLC, described liquid level gauge is electrically connected to the input of PLC, described inlet valve is electrically connected to the output of PLC, this device can adopt automatic charging and metering, and when discharging, open the compressed air valve, suppress in reactor, the discharging under pressure of emulsion acrylic resin material, and be depressed into and complete filtration by described metal screen in filter vat, therefore, adopt this kind mode reinforced, discharging and filtration, have the following advantages: one, can go out containing various contaminant filters in raw material or auxiliary agent, two, discharging is clean, has not only avoided waste, has also avoided residual material in the building-up process of next batch material, further reacts, and generates accessory substance, affects product quality, three, improved the accuracy of raw material addition.
Description of drawings
Fig. 1 is the utility model example structure schematic diagram;
Wherein, 1, reactor; 2, discharging opening; 3, filter vat; 4, compressed air interface; 5, charging aperture; 6, storage tank; 7, feed pump; 8, measuring tank; 9, inlet valve; 10, liquid level gauge; 11, bleeder valve; 12, discharging flow meter; 13, agitating device; 14, condensation reflux unit.
The specific embodiment
Below in conjunction with accompanying drawing, the specific embodiment of the present utility model is elaborated.
A kind of emulsion process units as shown in Figure 1 comprises that the bottom is provided with the reactor 1 that discharging opening 2, top are provided with charging aperture 5, and discharging opening 2 is communicated with filter vat 3, and the top of reactor 1 is provided with compressed air interface 4.
Charging aperture 5 is provided with storage tank 6, feed pump 7 and the measuring tank 8 that is communicated with successively, the inlet ductwork of feed pump 7 is provided with inlet valve 9, measuring tank 8 is provided with liquid level gauge 10, be provided with successively bleeder valve 11 and discharging flow meter 12 on the discharging pipeline of measuring tank 8, this device also comprises PLC, liquid level gauge 10 is electrically connected to the input of PLC, and inlet valve 9 is electrically connected to the output of PLC.
The inner charging aperture of filter vat 3 place is provided with the metal screen that detachably is arranged in filter vat 3.
Reactor is provided with agitating device 13 and condensation reflux unit 14.
The utlity model has following advantage: one, can go out containing various contaminant filters in raw material or auxiliary agent; Two, discharging is clean, has not only avoided waste, has also avoided residual material in the building-up process of next batch material, further reacts, and generates accessory substance, affects product quality; Three, improved the accuracy of raw material addition.
The utility model is not limited to above-mentioned concrete embodiment, and those of ordinary skill in the art is from above-mentioned design, and without performing creative labour, all conversion of having done are within all dropping on protection domain of the present utility model.
Claims (4)
1. emulsion process units comprises that the bottom is provided with the reactor that discharging opening, top are provided with charging aperture, and it is characterized in that: described discharging opening is communicated with filter, and the top of described reactor is provided with compressed air interface; Described charging aperture is provided with storage tank, feed pump and the measuring tank that is communicated with successively, the inlet ductwork of described feed pump is provided with inlet valve, described measuring tank is provided with liquid level gauge, be provided with successively bleeder valve and discharging flow meter on the discharging pipeline of described measuring tank, described emulsion process units also comprises PLC, described liquid level gauge is electrically connected to the input of PLC, and described inlet valve is electrically connected to the output of PLC.
2. a kind of emulsion process units as claimed in claim 1, it is characterized in that: described filter is filter vat, the inner charging aperture of described filter vat place is provided with metal screen.
3. a kind of emulsion process units as claimed in claim 2, it is characterized in that: described metal screen detachably is arranged in described filter vat.
4. a kind of emulsion process units as claimed in claim 1, it is characterized in that: described reactor is provided with agitating device and condensation reflux unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320021041 CN202983662U (en) | 2013-01-15 | 2013-01-15 | Emulsion production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320021041 CN202983662U (en) | 2013-01-15 | 2013-01-15 | Emulsion production device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202983662U true CN202983662U (en) | 2013-06-12 |
Family
ID=48554888
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320021041 Expired - Fee Related CN202983662U (en) | 2013-01-15 | 2013-01-15 | Emulsion production device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202983662U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110624479A (en) * | 2019-09-24 | 2019-12-31 | 安徽新涛光电科技有限公司 | Configuration control method and system for reaction kettle for preparing organic glass plate |
-
2013
- 2013-01-15 CN CN 201320021041 patent/CN202983662U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110624479A (en) * | 2019-09-24 | 2019-12-31 | 安徽新涛光电科技有限公司 | Configuration control method and system for reaction kettle for preparing organic glass plate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20130612 Termination date: 20190115 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |