CN201770641U - Unsaturated polyester resin production device - Google Patents
Unsaturated polyester resin production device Download PDFInfo
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- CN201770641U CN201770641U CN2010202746057U CN201020274605U CN201770641U CN 201770641 U CN201770641 U CN 201770641U CN 2010202746057 U CN2010202746057 U CN 2010202746057U CN 201020274605 U CN201020274605 U CN 201020274605U CN 201770641 U CN201770641 U CN 201770641U
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- polyester resin
- unsaturated polyester
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- measurement device
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Abstract
The utility model relates to the technical field of unsaturated polyester resin, in particular to an unsaturated polyester resin production device, which comprises a first tank, a second tank, a meter, a reactor, a dilution kettle and a receiver. The first tank and the second tank are connected with the meter connected with the reactor, the reactor is connected with the dilution kettle, and the reactor is further connected with the receiver. The unsaturated polyester resin production device in simple structure is used to effectively improve the production efficiency and increase the yield, the size of the reactor can be set according to the size of a factory, and the unsaturated polyester resin production device is convenient in structural maintenance.
Description
Technical field
The utility model relates to a kind of production equipment, relates in particular to a kind of production equipment of unsaturated polyester resin.
Background technology
Nineteen forty-two begins unsaturated polyester resin and has obtained large-scale application industrial.The processing performance of unsaturated polyester resin is good, at room temperature, can adopt different cure system curing moldings, and is of light color at the normal pressure compacted under, so can make light color or multiple chromatic goods, can adopt multiple measure to improve its processing performance simultaneously.In the prior art, be used for the production unit of unsaturated polyester resin, great majority can't reach the large vol suitability for industrialized production, and the extensive needs on the domestic industry can not enough be provided.
The utility model content
The technical problems to be solved in the utility model is: the existing production unit great majority that are used to mend saturated polyester resin can't reach the large vol suitability for industrialized production, and a kind of production equipment of unsaturated polyester resin is provided.
In order to overcome the defective that exists in the background technology, the technical scheme that its technical problem that solves the utility model adopts is: the utility model comprises groove one, groove two, gauger, reactor, dilution still and receptor, described groove one is connected gauger with groove two, described gauger ligation still, described reactor connects the dilution still, and described reactor also is connected with receptor.
According to another embodiment of the present utility model, comprise that further described reactor is provided with thermal measurement device and vacuum pressure gauge.
According to another embodiment of the present utility model, further comprise between being connected of described reactor and receptor being provided with fractional column, vertical (type) condenser and horizontal condenser, be provided with the thermal measurement device between the connection of described vertical (type) condenser and horizontal condenser.
According to another embodiment of the present utility model, comprise that further described dilution still is provided with thermal measurement device and thermal measurement device, also connects reflux exchanger on the described dilution still.
According to another embodiment of the present utility model, comprise that further described receptor is provided with vacuum pressure gauge.
The beneficial effects of the utility model are: of the present utility model simple in structure, and this structure effectively raises production efficiency, strengthened turnout, and the size of reactor can be formulated according to the size of factory, and structural maintenance of the present utility model is convenient.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is a structural representation of the present utility model;
Wherein: 1, groove one, 2, groove two, 3, gauger, 4, fractional column, 5, upright condenser, 6, horizontal condenser, 7, receptor, 8, reactor, 9, vacuum pressure gauge, 10, vacuum pressure gauge, 13, thermal measurement device, 14, the thermal measurement device, 15, the thermal measurement device, 16, the thermal measurement device.
Embodiment
In conjunction with the accompanying drawings the utility model is described in further detail now.These accompanying drawings are the synoptic diagram of simplification, basic structure of the present utility model only is described in a schematic way, so it only show the formation relevant with the utility model.
Fig. 1 is a structural representation of the present utility model, comprise groove 1, groove 22, gauger 3, reactor 8, dilution still 11 and receptor 7 among the figure, described groove 1 is connected gauger 3 with groove 22, described gauger 3 ligation stills 8, described reactor 8 connects dilution still 11, and described reactor 8 also is connected with receptor 7.Groove 1 and groove 22 are placed propylene glycol and ethylene glycol respectively, weigh by gauger 3, enter reactor 8, reactor 8 is key equipments of synthetic unsaturated polyester resin, be provided with coil pipe and chuck in the reactor 8, can be for heating or cooling effect, dilution still 11 plays the effect of dilution, unsaturated polyester and linking agent dilute in the dilution still, form unsaturated polyester resin, receptor 7 is distillate storage tankss, has the reactivity of reaction later stage when vacuumizing simultaneously concurrently, of the present utility model simple in structure, also improved production efficiency simultaneously.
Described reactor 8 is provided with thermal measurement device 13 and vacuum pressure gauge 9.Thermal measurement device 13 and vacuum pressure gauge 9 effectively show the situation in the reaction process, increase work efficiency.
Be provided with fractional column 4, vertical (type) condenser 5 and horizontal condenser 6 between being connected of described reactor 8 and receptor 7, be provided with thermal measurement device 16 between the connection of described vertical (type) condenser 5 and horizontal condenser 6.
Described dilution still 11 is provided with thermal measurement device 14 and thermal measurement device 15, also connects reflux exchanger 12 on the described dilution still 11.The situation that steam overflowed when reflux exchanger 12 had effectively prevented dilution still 11 interior unsaturated polyesters and linking agent mixing has improved production efficiency.
Described receptor 7 is provided with vacuum pressure gauge 10.Vacuum pressure gauge 10 effectively shows the situation in the reaction process, increases work efficiency.
With above-mentioned foundation desirable embodiment of the present utility model is enlightenment, and by above-mentioned description, the related work personnel can carry out various change and modification fully in the scope that does not depart from this utility model technological thought.The technical scope of this utility model is not limited to the content on the specification sheets, must determine its technical scope according to the claim scope.
Claims (5)
1. the production equipment of a unsaturated polyester resin, comprise groove one (1), groove two (2), gauger (3), reactor (8), dilution still (11) and receptor (7), it is characterized in that: described groove one (1) is connected gauger (3) with groove two (2), described gauger (3) ligation still (8), described reactor (8) connects dilution still (11), and described reactor (8) also is connected with receptor (7).
2. the production equipment of unsaturated polyester resin as claimed in claim 1, it is characterized in that: described reactor (8) is provided with thermal measurement device (13) and vacuum pressure gauge (9).
3. the production equipment of unsaturated polyester resin as claimed in claim 1, it is characterized in that: be provided with fractional column (4), vertical (type) condenser (5) and horizontal condenser (6) between being connected of described reactor (8) and receptor (7), be provided with thermal measurement device (16) between the connection of described vertical (type) condenser (5) and horizontal condenser (6).
4. the production equipment of unsaturated polyester resin as claimed in claim 1, it is characterized in that: described dilution still (11) is provided with thermal measurement device (14) and thermal measurement device (15), also connects reflux exchanger (12) on the described dilution still (11).
5. the production equipment of unsaturated polyester resin as claimed in claim 1, it is characterized in that: described receptor (7) is provided with vacuum pressure gauge (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202746057U CN201770641U (en) | 2010-07-29 | 2010-07-29 | Unsaturated polyester resin production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202746057U CN201770641U (en) | 2010-07-29 | 2010-07-29 | Unsaturated polyester resin production device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201770641U true CN201770641U (en) | 2011-03-23 |
Family
ID=43750480
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202746057U Expired - Fee Related CN201770641U (en) | 2010-07-29 | 2010-07-29 | Unsaturated polyester resin production device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201770641U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104629031A (en) * | 2015-01-30 | 2015-05-20 | 宜兴市兴合树脂有限公司 | Unsaturated polyester resin production DCS system |
| CN104672397A (en) * | 2015-03-11 | 2015-06-03 | 镇江利德尔复合材料有限公司 | Highly-efficient unsaturated resin production device |
| CN108499487A (en) * | 2018-03-19 | 2018-09-07 | 江苏大力士投资有限公司 | A kind of production system and its production method of unsaturated-resin |
-
2010
- 2010-07-29 CN CN2010202746057U patent/CN201770641U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104629031A (en) * | 2015-01-30 | 2015-05-20 | 宜兴市兴合树脂有限公司 | Unsaturated polyester resin production DCS system |
| CN104672397A (en) * | 2015-03-11 | 2015-06-03 | 镇江利德尔复合材料有限公司 | Highly-efficient unsaturated resin production device |
| CN104672397B (en) * | 2015-03-11 | 2023-10-20 | 镇江利德尔复合材料有限公司 | High-efficient apparatus for producing of unsaturated resins |
| CN108499487A (en) * | 2018-03-19 | 2018-09-07 | 江苏大力士投资有限公司 | A kind of production system and its production method of unsaturated-resin |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110323 Termination date: 20110729 |