CN205340768U - Reaction waste heat utilization equipment - Google Patents
Reaction waste heat utilization equipment Download PDFInfo
- Publication number
- CN205340768U CN205340768U CN201521058823.6U CN201521058823U CN205340768U CN 205340768 U CN205340768 U CN 205340768U CN 201521058823 U CN201521058823 U CN 201521058823U CN 205340768 U CN205340768 U CN 205340768U
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- China
- Prior art keywords
- heat exchanger
- reaction
- coil pipe
- reactor
- delivery outlet
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Abstract
The utility model discloses a reaction waste heat utilization equipment, including reactor and heat exchanger, the heat exchanger is the box of a rectangle, is equipped with the coil pipe in the inside of heat exchanger, and the input port and the raw materials import of coil pipe are connected, and delivery outlet and a pipeline of coil pipe are connected, a pipeline's delivery outlet ligation ware, and the reactor and input port connection no. Two pipeline, the heat exchanger is connected to no. Two pipeline's delivery outlet, still is equipped with the product export on the heat exchanger. The utility model discloses can make the reacted product cool off rapidly to the heat that utilizes the product to produce in process of production simultaneously heats in order to make the raw materials can proceed the reaction the raw materials, guarantees that the circulation of whole reaction is gone on, reaches the energy can be saved, effective use of energy's purpose.
Description
Technical field
This utility model relates to pre-heat reclamation device, and specifically a kind of residual heat of reaction utilizes device.
Background technology
Common many exothermic reactions, heating is needed before reaction, because product temperature raises during reaction, after reaction, products obtained therefrom needs cooling, such as radical polymerization, radical polymerization is combined into and causes with free radical, make the ever-increasing polyreaction of chain growth (chain growth) free radical, also known as radical polymerization, polyaddition reaction, the overwhelming majority is as raw material by the vinyl monomer containing unsaturated double-bond, by opening the double bond in monomer molecule, in the intermolecular additive reaction being repeated repeatedly, many monomers are coupled together, form macromole, it is mainly used in the addition polymerization of alkene class, the most frequently used method producing free radical is the oxidoreduction decomposition reaction of the decomposes of initiator or two component initiators, heating can also be used, ultraviolet irradiation, high-energy irradiation, the methods such as electrolysis and plasma initiation produce free radical.Here it is typically need the exothermic reaction of certain initiation temperature, product can be lowered the temperature by natural cooling after preparation completes, and so will result in the waste that the energy is bigger, causes certain puzzlement to whole course of reaction.
Summary of the invention
The purpose of this utility model is in that to provide a kind of residual heat of reaction to utilize device, with the problem solving to propose in above-mentioned background technology.
For achieving the above object, this utility model provides following technical scheme:
A kind of residual heat of reaction utilizes device, including reactor and heat exchanger, described heat exchanger is the casing of a rectangle, being provided with coil pipe in the inside of heat exchanger, the input port of coil pipe is connected with material inlet, and the delivery outlet of coil pipe and a conveyance conduit connect, the delivery outlet coupled reaction device of a number conveyance conduit, the input port with No. two conveyance conduits of reactor is connected, and the delivery outlet of No. two conveyance conduits connects heat exchanger, is additionally provided with products export on heat exchangers.
As further program of the utility model: the inside of described reactor is provided with agitating device.
As further program of the utility model: the interior surface of described coil pipe, conveyance conduit, reactor, No. two conveyance conduits and heat exchanger is all coated with Teflon coating.
Compared with prior art, this utility model can make reacted product cool down rapidly, and utilize the heat that product produces in process of production simultaneously, it is heated raw material promoting raw material to can continue to react, ensure that the circulation of whole reaction carries out, reach to save the purpose of the energy, effective use of energy sources.
Accompanying drawing explanation
Fig. 1 is the structural representation that residual heat of reaction utilizes device.
In figure: 1-reactor, 2-material inlet, 3-products export, number conveyance conduit of 4-, 5-heat exchanger, 6-coil pipe, No. bis-conveyance conduits of 7-.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model, rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of this utility model protection.
Refer to Fig. 1, in this utility model embodiment, a kind of residual heat of reaction utilizes device, including reactor 1 and heat exchanger 5, described heat exchanger 5 is the casing of a rectangle, it is provided with coil pipe 6 in the inside of heat exchanger 5, the input port of coil pipe 6 is connected with material inlet 2, the delivery outlet of coil pipe 6 and a conveyance conduit 4 connect, the delivery outlet coupled reaction device 1 of a number conveyance conduit 4, the input port with No. two conveyance conduits 7 of reactor 1 is connected, and the delivery outlet of No. two conveyance conduits 7 connects heat exchanger 5, is additionally provided with products export 3 on heat exchanger 5.The inside of described reactor 1 is provided with agitating device, if agitating device can promote the carrying out of reaction.The interior surface of 6, conveyance conduit 4 of described coil pipe, 1, No. two conveyance conduits 7 of reactor and heat exchanger 5 is all coated with Teflon coating, it is possible to avoid pipeline and container to be corroded.
In the process used, raw material word material inlet 2 enters coil pipe, after carrying out once heating, raw material enters into the inside of reactor 1 by a conveyance conduit 4, react, product after reaction enters into the inside of heat exchanger 5, the outside of coil pipe 6, owing to carrying out heat release in the process of reaction, so product now carries substantial amounts of heat, coil pipe 6 is heated by these heats, enable newly entering to absorb heat to the raw material within coil pipe 6 and react, whole reaction forms an effective cyclic process, contribute to carrying out for a long time of reaction, and heat will not be caused waste.
This utility model can make reacted product cool down rapidly, and utilize the heat that product produces in process of production simultaneously, it is heated raw material promoting raw material to can continue to react, it is ensured that the circulation of whole reaction carries out, reaches to save the purpose of the energy, effective use of energy sources.
It is obvious to a person skilled in the art that this utility model is not limited to the details of above-mentioned one exemplary embodiment, and when without departing substantially from spirit of the present utility model or basic feature, it is possible to realize this utility model in other specific forms.Therefore, no matter from which point, embodiment all should be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims rather than described above, it is intended that all changes in the implication of the equivalency dropping on claim and scope included in this utility model.Any accompanying drawing labelling in claim should be considered as the claim that restriction is involved.
In addition, it is to be understood that, although this specification is been described by according to embodiment, but not each embodiment only comprises an independent technical scheme, this narrating mode of description is only for clarity sake, description should be made as a whole by those skilled in the art, and the technical scheme in each embodiment through appropriately combined, can also form other embodiments that it will be appreciated by those skilled in the art that.
Claims (3)
1. a residual heat of reaction utilizes device, including reactor and heat exchanger, it is characterized in that, described heat exchanger is the casing of a rectangle, is provided with coil pipe in the inside of heat exchanger, the input port of coil pipe is connected with material inlet, the delivery outlet of coil pipe and a conveyance conduit connect, the delivery outlet coupled reaction device of a conveyance conduit, and the input port with No. two conveyance conduits of reactor is connected, the delivery outlet of No. two conveyance conduits connects heat exchanger, is additionally provided with products export on heat exchangers.
2. a kind of residual heat of reaction according to claim 1 utilizes device, it is characterised in that the inside of described reactor is provided with agitating device.
3. a kind of residual heat of reaction according to claim 1 utilizes device, it is characterised in that the interior surface of described coil pipe, conveyance conduit, reactor, No. two conveyance conduits and heat exchanger is all coated with Teflon coating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521058823.6U CN205340768U (en) | 2015-12-18 | 2015-12-18 | Reaction waste heat utilization equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521058823.6U CN205340768U (en) | 2015-12-18 | 2015-12-18 | Reaction waste heat utilization equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205340768U true CN205340768U (en) | 2016-06-29 |
Family
ID=56169614
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521058823.6U Expired - Fee Related CN205340768U (en) | 2015-12-18 | 2015-12-18 | Reaction waste heat utilization equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205340768U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109647321A (en) * | 2019-01-18 | 2019-04-19 | 江苏海企技术工程股份有限公司 | A kind of energy saving thermal chlorination reaction unit for methane chloride |
| CN110385093A (en) * | 2019-07-05 | 2019-10-29 | 江苏海阳化纤有限公司 | A kind of resistance of eutectic is high to spin the ultralow viscous nylon 6 slice polyplant of property and operating method |
| CN111715174A (en) * | 2020-06-28 | 2020-09-29 | 安徽威驰化工有限责任公司 | Heat exchange packed tower and method for producing surfactant |
-
2015
- 2015-12-18 CN CN201521058823.6U patent/CN205340768U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109647321A (en) * | 2019-01-18 | 2019-04-19 | 江苏海企技术工程股份有限公司 | A kind of energy saving thermal chlorination reaction unit for methane chloride |
| CN110385093A (en) * | 2019-07-05 | 2019-10-29 | 江苏海阳化纤有限公司 | A kind of resistance of eutectic is high to spin the ultralow viscous nylon 6 slice polyplant of property and operating method |
| CN111715174A (en) * | 2020-06-28 | 2020-09-29 | 安徽威驰化工有限责任公司 | Heat exchange packed tower and method for producing surfactant |
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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: 20160629 Termination date: 20201218 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |