CN204694120U - A kind of titanium coil heat exchanger - Google Patents
A kind of titanium coil heat exchanger Download PDFInfo
- Publication number
- CN204694120U CN204694120U CN201520270531.2U CN201520270531U CN204694120U CN 204694120 U CN204694120 U CN 204694120U CN 201520270531 U CN201520270531 U CN 201520270531U CN 204694120 U CN204694120 U CN 204694120U
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- CN
- China
- Prior art keywords
- heat exchange
- apotheca
- hot gas
- heat
- fluid flow
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- Expired - Fee Related
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of titanium coil heat exchanger, comprise tank body, the lower end of tank body is provided with hot air intake, upper end is provided with cold air outlet, this tank interior is provided with hot gas apotheca, heat-exchanging chamber and cold air apotheca from bottom to up successively, and hot gas apotheca has a hot gas conditioning chamber, and the side of this hot gas apotheca is provided with out liquid interface, the side of heat-exchanging chamber is provided with feed liquor interface, goes out between liquid interface and feed liquor interface and is provided with heat exchange fluid flow tube; Be provided with spiral heat exchange tube in heat-exchanging chamber, described spiral heat exchange tube hovers above heat exchange fluid flow tube, and the inner side of spiral heat exchange tube is provided with towards the jet spray orifice of heat exchange fluid flow tube.The utility model is novel in design, greatly increases the transformation efficiency of heat, solves the problem that the heat exchanger effectiveness of existing heat exchanger is low.
Description
Technical field
The utility model relates to a kind of titanium coil heat exchanger.
Background technology
At present, heat exchanger has been widely used in industrial production, the major function of heat exchanger is that the hot waste gas of industrial production generation and the stoste of preprocessing are carried out heat exchange, and then can accomplish preheating stoste, greatly increases the utilization rate of industrial energy.
Existing heat exchanger is in the certain limitation used or exist, and the heat exchange efficiency of existing heat exchanger when carrying out heat exchange is lower, and energy utilization rate is lower.
Utility model content
The utility model, in order to solve the above-mentioned deficiency of prior art, proposes a kind of titanium coil heat exchanger.
In order to solve the problems of the technologies described above, the utility model is by the following technical solutions: a kind of titanium coil heat exchanger, it is characterized in that: comprise tank body, the lower end of described tank body is provided with hot air intake, upper end is provided with cold air outlet, this tank interior is provided with hot gas apotheca from bottom to up successively, heat-exchanging chamber, with cold air apotheca, described hot gas apotheca has a hot gas conditioning chamber, the upper end gas collection shower nozzle of described hot gas conditioning chamber, the side of this hot gas apotheca is provided with out liquid interface, the side of described heat-exchanging chamber is provided with feed liquor interface, describedly go out, between liquid interface and feed liquor interface, heat exchange fluid flow tube is installed, be provided with spiral heat exchange tube in described heat-exchanging chamber, described spiral heat exchange tube hovers above heat exchange fluid flow tube, and the inner side of spiral heat exchange tube is provided with towards the jet spray orifice of heat exchange fluid flow tube, and the lower end of this spiral heat exchange tube is connected with described hot gas apotheca, described cold air apotheca is connected with the heat-exchanging chamber of below.
Compared with prior art, the utility model greatly increases heat exchanger effectiveness, hot waste gas is reasonably allocated in three chambers by the utility model, reasonably distribute the utilization of hot waste gas, wherein hot gas apotheca can stockpile a large amount of hot waste gas, the hot gas conditioning chamber arranged can be vented the safe air pressure that can ensure in hot gas apotheca, hot waste gas directly can be sprayed onto on heat exchange fluid flow tube by spray orifice by the spiral heat exchange tube in heat-exchanging chamber, have passed rate of heat exchange widely, and wherein, the flow direction of hot waste gas is contrary with the flow direction of pre-warmed liquid stream, add area and the time of heat exchange, and then substantially increase rate of heat exchange.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with drawings and Examples, utility model is described in detail.
As shown in Figure 1, the titanium coil heat exchanger that the utility model proposes, comprises tank body 1, and the lower end of described tank body is provided with hot air intake 2, upper end is provided with cold air outlet 3, and this tank interior is provided with hot gas apotheca 4, heat-exchanging chamber 5 and cold air apotheca 6 from bottom to up successively.
Hot gas apotheca 4 has a hot gas conditioning chamber 7, the upper end gas collection shower nozzle 8 of hot gas conditioning chamber 7, and its side is provided with a control valve 14, ensures the stable gas pressure of its inside.The side of hot gas apotheca 4 is provided with out liquid interface 9, goes out liquid interface 9 horizontally set, extends through hot gas apotheca inner.The side of heat-exchanging chamber 5 is provided with feed liquor interface 10, feed liquor interface 10 and go out liquid interface 9 corresponding to be also horizontally set, to go out between liquid interface 9 and feed liquor interface 10 and be provided with heat exchange fluid flow tube 11; Be provided with spiral heat exchange tube 12 in heat-exchanging chamber 5, spiral heat exchange tube 12 hovers above heat exchange fluid flow tube 11, and the inner side of spiral heat exchange tube 12 is provided with towards the jet spray orifice 13 of heat exchange fluid flow tube 11, and the lower end of this spiral heat exchange tube 12 is connected with described hot gas apotheca 4; Cold air apotheca 6 is connected with the heat-exchanging chamber 5 of below.
In the utility model, hot waste gas enters into hot gas apotheca 4 from hot air intake 2, in hot gas apotheca 4 inner accumulated, accumulate to a timing, flow out from gas collection shower nozzle 8, the lower end of heat exchange fluid flow tube 11 faces the hot gas of gas collection shower nozzle ejection, after hot waste gas collects in hot gas apotheca 4, discharge from spiral heat exchange tube 12, when hot waste gas is walked and is flowed in spiral heat exchange tube 12, spraying from spray orifice 13 slowly, towards heat exchange fluid flow tube 11 between the hot waste gas of ejection, directly carry out heat exchange, finally collect and rise in cold air apotheca 6, can discharge from cold air outlet 3 again.Liquid stream in heat exchange fluid flow tube 11 wherein from top to bottom, with the bulk flow of hot waste gas to contrary.
Hot waste gas is reasonably allocated in three chambers by the utility model, reasonably distribute the utilization of hot waste gas, wherein hot gas apotheca can stockpile a large amount of hot waste gas, the hot gas conditioning chamber arranged can be vented the safe air pressure that can ensure in hot gas apotheca, hot waste gas directly can be sprayed onto on heat exchange fluid flow tube by spray orifice by the spiral heat exchange tube in heat-exchanging chamber, have passed rate of heat exchange widely, and wherein, the flow direction of hot waste gas is contrary with the flow direction of pre-warmed liquid stream, add area and the time of heat exchange, and then substantially increase rate of heat exchange.
Above-described embodiment only have expressed several embodiment of the present utility model, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the utility model the scope of the claims.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the utility model patent and protection domain should be as the criterion with appended claims.
Claims (1)
1. a titanium coil heat exchanger, it is characterized in that: comprise tank body (1), the lower end of described tank body is provided with hot air intake (2), upper end is provided with cold air outlet (3), this tank interior is provided with hot gas apotheca (4) from bottom to up successively, heat-exchanging chamber (5), with cold air apotheca (6), described hot gas apotheca (4) has a hot gas conditioning chamber (7), upper end gas collection shower nozzle (8) of described hot gas conditioning chamber (7), the side of this hot gas apotheca (4) is provided with out liquid interface (9), the side of described heat-exchanging chamber (5) is provided with feed liquor interface (10), describedly go out, between liquid interface (9) and feed liquor interface (10), heat exchange fluid flow tube (11) is installed, spiral heat exchange tube (12) is provided with in described heat-exchanging chamber (5), described spiral heat exchange tube (12) hovers above heat exchange fluid flow tube (11), and the inner side of spiral heat exchange tube (12) is provided with towards the jet spray orifice (13) of heat exchange fluid flow tube (11), the lower end of this spiral heat exchange tube (12) is connected with described hot gas apotheca (4), described cold air apotheca (6) is connected with the heat-exchanging chamber (5) of below.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520270531.2U CN204694120U (en) | 2015-04-30 | 2015-04-30 | A kind of titanium coil heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520270531.2U CN204694120U (en) | 2015-04-30 | 2015-04-30 | A kind of titanium coil heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204694120U true CN204694120U (en) | 2015-10-07 |
Family
ID=54234398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520270531.2U Expired - Fee Related CN204694120U (en) | 2015-04-30 | 2015-04-30 | A kind of titanium coil heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204694120U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108662937A (en) * | 2018-05-30 | 2018-10-16 | 庐山市环绿时代农业科技开发有限公司 | A kind of heat transmission equipment |
-
2015
- 2015-04-30 CN CN201520270531.2U patent/CN204694120U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108662937A (en) * | 2018-05-30 | 2018-10-16 | 庐山市环绿时代农业科技开发有限公司 | A kind of heat transmission equipment |
| CN108662937B (en) * | 2018-05-30 | 2020-09-15 | 庐山市环绿时代农业科技开发有限公司 | Heat exchange equipment |
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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: 20151007 Termination date: 20170430 |