CN202844994U - Oil cooling system for resin-synthetized reaction kettle - Google Patents
Oil cooling system for resin-synthetized reaction kettle Download PDFInfo
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- CN202844994U CN202844994U CN 201220570483 CN201220570483U CN202844994U CN 202844994 U CN202844994 U CN 202844994U CN 201220570483 CN201220570483 CN 201220570483 CN 201220570483 U CN201220570483 U CN 201220570483U CN 202844994 U CN202844994 U CN 202844994U
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Abstract
The utility model discloses an oil cooling system for resin-synthetized reaction kettle. The oil cooling system comprises a reaction kettle, an oil cooling tank, an oil heating tank, a condenser, and a water cooling pond, wherein the reaction kettle, the reaction kettle, the oil heating tank, the condenser and the reaction kettle are orderly connected through a pipeline to form a loop; the oil cooling tank is connected with the reaction kettle through the pipeline; meanwhile, another pipeline is also arranged on the oil heating tank to be connected with the reaction kettle; the water cooling pond is respectively provided with a water outlet pipe and a water inlet pipe to be connected to the condenser; and an expansion tank is arranged above the oil heating tank and connected through the pipeline. The oil heating tank and the oil cooling tank are added to the oil cooling system; the expansion tank is arranged to prevent the danger that the oil heating tank blasts when the oil overflows the oil heating tank; conduction oil in an interlayer of the reaction kettle is released to an empty can when the matter inside the reaction kettle is to cooled after reaction; cold oil inside the oil cooling tank is input into the interlayer of the reaction kettle by a pump and then a circulating loop is formed through the condenser. Therefore, the cooling time is effectively shortened; the production efficiency is improved, and the quality of the product is also ensured.
Description
Technical field
The utility model relates to a kind of cooling device, specifically refers to a kind of oil cooling system for the synthetic reactor of resin.
Background technology
In chemical process, cooling generally is to adopt running water, and the cost of water is not high, cool off also comparatively fast, and still, when the temperature of technological requirement was higher when resin was synthetic (above 100 ℃), the interior interior medium of cooling coil of reactor just can not be water but oil.And the method for the common usefulness of oil cooling is exactly that interior conduction oil and the conduction oil in the water-cooled reactor interlayer of reactor interlayer of oil cooling mixed, perhaps the conduction oil in the coil pipe cools off first conduction oil by condensing tower (fixing a price for matter with running water), then remove again to cool off the interior material of reactor with cooled conduction oil, it is longer that the shortcoming of these two kinds of methods is exactly cool time, efficient is low, product quality can not get ensureing, and increases the cost of product.
The utility model content
The purpose of this utility model is to provide a kind of and shortens cool time, the oil cooling system of the reactor that is used for production of resins that can guarantee product quality and production safety simultaneously of enhancing productivity.
To achieve these goals, the utility model has adopted following technical scheme:
A kind of oil cooling system for the synthetic reactor of resin, comprise reactor, cold oil tank, deep fat tank, condenser and water cooling pond, described reactor, condenser and reactor connect by pipeline successively and form a loop, described cold oil tank is connected with described reactor by pipeline, simultaneously, described deep fat tank is provided with another pipeline and is connected with described reactor, and described water cooling pond is respectively equipped with an outlet pipe and a water inlet pipe is connected with described condenser.
Further, the top of described deep fat tank is provided with an expansion slot, and described deep fat tank is connected by pipeline with described expansion slot.
Further, described expansion slot places the top of described reactor.
The utility model increases cold oil tank and deep fat tank on the reactor next door, the deep fat tank connects a tubule to the expansion slot on reactor top, in order to avoid the conduction oil in the reactor expands because of excess Temperature, avoided when the deep fat tank can not load will explosion danger, when substance reaction in the reactor is complete will lower the temperature the time, just the conduction oil in the interlayer of reactor is put in the deep fat tank, with pump the cold oil in the cold oil tank is inputted the reactor interlayer again, by condenser, make condenser and reactor form a closed circuit again.Cooling will be very fast like this, thereby effectively shorten cool time, improved the quality that production efficiency has also guaranteed product.
Description of drawings
Fig. 1 is structure chart of the present utility model.
The specific embodiment
Now by reference to the accompanying drawings, describe the utility model in detail.
With reference to accompanying drawing 1, a kind of oil cooling system for the synthetic reactor of resin, comprise reactor 1, cold oil tank 2, deep fat tank 3, condenser 4, water cooling pond 5 and expansion slot 6, water cooling pond 5 is respectively equipped with an outlet pipe 51 and a water inlet pipe 52 is connected with condenser 4, the deep fat that enters condenser 4 is carried out condensation, reactor 1, condenser 4 and reactor 1 connect by pipeline successively and form a loop, cold oil tank 2 is connected with reactor 1 by pipeline, simultaneously, deep fat tank 3 is provided with pipeline and is connected with reactor 1, for the safety that guarantees to produce, above deep fat tank 3, be provided with expansion slot 6, deep fat tank 3 and expansion slot 6 are connected by pipeline, when the oil temperature in the reactor 1 is too high, deep fat can be disposed to deep fat tank 3, when the deep fat in the deep fat tank 3 makes liquid level rise because of excess Temperature, the deep fat that overflows in the deep fat tank 3 can enter in the expansion slot 6 by pipeline, and in order to improve further security performance, expansion slot 3 places the top of reactor 1.
When actual production, reactor 1 is synthetic complete just to be disposed to deep fat tank 3 to the conduction oil in reactor 1 interlayer, the cold oil in the cold oil tank 2 is input in reactor 1 interlayer again.When cold oil is flowed through reactor 1 owing to the material temperature is high in the still reason so that the cold oil temperature can obviously raise, at this moment the oil of reactor condenser 4 and the reactor 1 of can flowing through forms a closed circuit, water in the condenser 4 can reduce, the temperature of oil in the oil cooling service pipe, reduce the temperature of condenser 4 self by water cooling pond 5 again.Thereby so consist of two circulations and reach the purpose that reduces material temperature in the still.
Above-described the utility model embodiment does not consist of the restriction to the utility model protection domain.Any modification of within spirit of the present utility model and principle, doing, be equal to and replace and improvement etc., all should be included within the claim protection domain of the present utility model.
Claims (3)
1. oil cooling system that is used for the synthetic reactor of resin, comprise reactor, cold oil tank, condenser and water cooling pond,, described water cooling pond is respectively equipped with an outlet pipe and a water inlet pipe is connected with described condenser, it is characterized in that, also comprised the deep fat tank; Described reactor, condenser and reactor connect by pipeline successively and form a loop, and described cold oil tank is connected with described reactor by pipeline, and simultaneously, described deep fat tank also is provided with pipeline and is connected with described reactor.
2. according to claim 1 a kind of oil cooling system for the synthetic reactor of resin is characterized in that the top of described described deep fat tank is provided with an expansion slot, and described deep fat tank is connected by pipeline with described expansion slot.
3. according to claim 2 a kind of oil cooling system for the synthetic reactor of resin is characterized in that described expansion slot places the top of described reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220570483 CN202844994U (en) | 2012-10-31 | 2012-10-31 | Oil cooling system for resin-synthetized reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220570483 CN202844994U (en) | 2012-10-31 | 2012-10-31 | Oil cooling system for resin-synthetized reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202844994U true CN202844994U (en) | 2013-04-03 |
Family
ID=47976233
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220570483 Expired - Fee Related CN202844994U (en) | 2012-10-31 | 2012-10-31 | Oil cooling system for resin-synthetized reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202844994U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103666748A (en) * | 2013-12-11 | 2014-03-26 | 绩溪县翰徽农业开发有限公司 | Circulating oil supply system for processing tea-seed oil |
| CN106225235A (en) * | 2016-08-29 | 2016-12-14 | 镇江市三维电加热器有限公司 | Cold and hot oil combined-circulation electric heater system |
| CN110117360A (en) * | 2019-06-25 | 2019-08-13 | 福建中庚环境技术有限公司 | A kind of MC nylon industry metaplasia production complete set of equipments |
| CN113639511A (en) * | 2021-08-25 | 2021-11-12 | 常州化工设计院有限公司 | Emergency cooling device for heat-conducting oil heating reaction kettle |
-
2012
- 2012-10-31 CN CN 201220570483 patent/CN202844994U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103666748A (en) * | 2013-12-11 | 2014-03-26 | 绩溪县翰徽农业开发有限公司 | Circulating oil supply system for processing tea-seed oil |
| CN106225235A (en) * | 2016-08-29 | 2016-12-14 | 镇江市三维电加热器有限公司 | Cold and hot oil combined-circulation electric heater system |
| CN110117360A (en) * | 2019-06-25 | 2019-08-13 | 福建中庚环境技术有限公司 | A kind of MC nylon industry metaplasia production complete set of equipments |
| CN113639511A (en) * | 2021-08-25 | 2021-11-12 | 常州化工设计院有限公司 | Emergency cooling device for heat-conducting oil heating reaction kettle |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 528333 Shunde province science and Technology Industrial Park, Foshan,, Sha Sha Industrial Zone, No. five Hui Road, No. 13 Patentee after: Guangdong Kodest Chemical Industry Co., Ltd. Address before: 528333 Shunde province science and Technology Industrial Park, Foshan,, Sha Sha Industrial Zone, No. five Hui Road, No. 13 Patentee before: Guangdong Kodest Chemical Industry Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130403 Termination date: 20201031 |
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| CF01 | Termination of patent right due to non-payment of annual fee |