CN204494796U - Boiler conduction oil heat exchange oil supply system - Google Patents
Boiler conduction oil heat exchange oil supply system Download PDFInfo
- Publication number
- CN204494796U CN204494796U CN201520067214.0U CN201520067214U CN204494796U CN 204494796 U CN204494796 U CN 204494796U CN 201520067214 U CN201520067214 U CN 201520067214U CN 204494796 U CN204494796 U CN 204494796U
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- China
- Prior art keywords
- boiler
- heat exchanger
- outlet
- heat
- oil
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- 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
- 230000008676 import Effects 0.000 claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 abstract description 10
- 230000009466 transformation Effects 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 29
- 229920006337 unsaturated polyester resin Polymers 0.000 description 8
- 238000000034 method Methods 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a kind of boiler conduction oil heat exchange oil supply system, it is characterized in that it includes boiler (1), the outlet of boiler (1) is divided into multiple-way duct by Heat-transfer Oil Pump (2) and is connected to each equipment, wherein a road pipeline is connected with the outer circulation import of heat exchanger (3), the outer circulation outlet of heat exchanger (3) is connected to described boiler (1), the connecting pipe of Heat-transfer Oil Pump (2) with heat exchanger (3) outer circulation import is provided with valve (4), the Inner eycle outlet of described heat exchanger (3) is connected with the heat conductive oil inlet of reactor (8), the conduction oil outlet of described reactor (8) is connected with the Inner eycle import of described heat exchanger (3).The utility model is simple and practical, can carry out transformation and use in present boiler foundation, no longer needs to use separately platform boiler for specific products, has effectively saved production equipment cost.
Description
Technical field
The utility model relates to a kind of oil supply system being applicable to specific reactor oil and requiring.
Background technology
Unsaturated polyester resin technique functions comes from Sweden, after only improving and optimizing, is commercially produced in nineteen forty-one first by the U.S..And domesticly to start late, just started the production having small lot in 1958, after within 1966, Changzhou building materials 253 factory causes the production technology and eqUipment of unsaturated polyester resin from Britain, unsaturated polyester resin just starts commercialized development at home.Through the development of decades, be that the glass fiber reinforced plastics product of matrix penetrates into all trades and professions with unsaturated polyester resin, play a part more and more important in national economy every field.But generally speaking, the production technology of domestic unsaturated polyester resin also lags far behind advanced international standard, aspects such as being in particular in that production technology falls behind, being simply equipped, technical merit is low.Since entering 21st century, along with the fast development of domestic and international trade, the phenomenon that the production technology level of domestic unsaturated polyester resin product falls behind displays at once.Such severe situation forces domestic unsaturated polyester resin manufacturing enterprise to update, optimize production facility and technique, to increase the competitiveness with external colleague.
Current existing unsaturated polyester resin manufacturer is in production of resins process, specific products requires that temperature of reaction kettle can not be too high, as 160 DEG C, and boiler conduction oil is out 240 DEG C, because existing boiler can not adapt to this temperature requirement, so when encountering this situation, be all generally the independent boiler of increase by, thus also just add cost.
Summary of the invention
The purpose of this utility model is exactly for above-mentioned the deficiencies in the prior art, provides a kind of simple and practical, effectively reduces the boiler conduction oil heat exchange oil supply system of equipment cost.
For achieving the above object, the technical solution adopted in the utility model is as follows:
A kind of boiler conduction oil changes heat utilization system, it is characterized in that it includes boiler, the outlet of boiler is divided into multiple-way duct by Heat-transfer Oil Pump and is connected to each equipment, wherein a road pipeline is connected with the outer circulation import of heat exchanger, the outer circulation outlet of heat exchanger is connected to described boiler, the connecting pipe of Heat-transfer Oil Pump and heat exchanger outer circulation import is provided with valve, the Inner eycle outlet of described heat exchanger is connected with the heat conductive oil inlet of reactor, and the conduction oil outlet of described reactor is connected with the Inner eycle import of described heat exchanger.
The connecting line cocycle pump of described reactor conduction oil outlet and the import of described heat exchanger Inner eycle.
Described heat exchanger Inner eycle outlet is provided with thermal detector with reactor heat conductive oil inlet connecting line, and the signal output part of thermal detector is connected with the defeated input of attemperating unit, and described attemperating unit controls the aperture of described valve.
The beneficial effects of the utility model have:
Simple and practical, transformation can be carried out use in present boiler foundation, no longer need to use separately platform boiler for specific products, effectively saved production equipment cost.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail:
As shown in Figure 1, the utility model it include boiler 1, the outlet of boiler 1 is divided into multiple-way duct by Heat-transfer Oil Pump 2 and is connected to each equipment, and wherein a road pipeline is connected with the outer circulation import of heat exchanger 3, and the outer circulation outlet of heat exchanger 3 is connected to described boiler 1.Heat-transfer Oil Pump 2 with the connecting pipe of heat exchanger 3 outer circulation import are provided with valve 4.The Inner eycle outlet of heat exchanger 3 is connected with the heat conductive oil inlet of the reactor 8 producing specific products, and the conduction oil outlet of reactor 8 is connected with the Inner eycle import of heat exchanger 3.The connecting line cocycle pump 5 of the outlet of reactor 8 conduction oil and the import of heat exchanger 3 Inner eycle, thus form an independent oil circuit.The outlet of heat exchanger 3 Inner eycle with reactor 8 heat conductive oil inlet connecting line are provided with thermal detector 6, and the signal output part of thermal detector 6 is connected with the defeated input of attemperating unit 7, and described attemperating unit 7 controls the aperture of described valve 4.Heat exchanger 3 can adopt tube heat exchanger.
The course of work of the present utility model is as follows:
From boiler 1,240 DEG C of conduction oils out arrive heat exchanger 3 through Heat-transfer Oil Pump 2, in heat exchanger 3 by heat exchange after return boiler 1 and reuse.Oil Guide stream in the independent oil circuit of reactor 8, when flowing through heat exchanger 3, carries out heat exchange with the high temperature heat conductive oil of coming in boiler 1, makes its temperature increase to about 160 DEG C, for reactor 8.Thermal detector 6 carries out thermometric to the conduction oil of process, see the instructions for use whether reaching 160 DEG C, if do not reached, then feed back signal to attemperating unit 7, attemperating unit 7 by-pass valve control 4, makes the high temperature heat conductive oil increased flow capacity flowing to heat exchanger 3, otherwise, then reduce the aperture of valve 4, thus the conduction oil temperature ensureing to flow to reactor 8 is all in and needs in scope.
Other undeclared part that the utility model relates to is same as the prior art.
Claims (3)
1. a boiler conduction oil heat exchange oil supply system, it is characterized in that it includes boiler (1), the outlet of boiler (1) is divided into multiple-way duct by Heat-transfer Oil Pump (2) and is connected to each equipment, wherein a road pipeline is connected with the outer circulation import of heat exchanger (3), the outer circulation outlet of heat exchanger (3) is connected to described boiler (1), the connecting pipe of Heat-transfer Oil Pump (2) with heat exchanger (3) outer circulation import is provided with valve (4), the Inner eycle outlet of described heat exchanger (3) is connected with the heat conductive oil inlet of reactor (8), the conduction oil outlet of described reactor (8) is connected with the Inner eycle import of described heat exchanger (3).
2. boiler conduction oil heat exchange oil supply system according to claim 1, is characterized in that the connecting line cocycle pump (5) of the outlet of described reactor (8) conduction oil and described heat exchanger (3) Inner eycle import.
3. boiler conduction oil heat exchange oil supply system according to claim 1, it is characterized in that the outlet of described heat exchanger (3) Inner eycle is provided with thermal detector (6) with reactor (8) heat conductive oil inlet connecting line, the signal output part of thermal detector (6) is connected with the defeated input of attemperating unit (7), and described attemperating unit (7) controls the aperture of described valve (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520067214.0U CN204494796U (en) | 2015-01-30 | 2015-01-30 | Boiler conduction oil heat exchange oil supply system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520067214.0U CN204494796U (en) | 2015-01-30 | 2015-01-30 | Boiler conduction oil heat exchange oil supply system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204494796U true CN204494796U (en) | 2015-07-22 |
Family
ID=53574106
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520067214.0U Expired - Fee Related CN204494796U (en) | 2015-01-30 | 2015-01-30 | Boiler conduction oil heat exchange oil supply system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204494796U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104633931A (en) * | 2015-01-30 | 2015-05-20 | 宜兴市兴合树脂有限公司 | Boiler heat-conducting oil heat exchange oil supply system |
-
2015
- 2015-01-30 CN CN201520067214.0U patent/CN204494796U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104633931A (en) * | 2015-01-30 | 2015-05-20 | 宜兴市兴合树脂有限公司 | Boiler heat-conducting oil heat exchange oil supply system |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150722 |