CN204227975U - Heat-energy recovering apparatus - Google Patents
Heat-energy recovering apparatus Download PDFInfo
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- CN204227975U CN204227975U CN201420624021.6U CN201420624021U CN204227975U CN 204227975 U CN204227975 U CN 204227975U CN 201420624021 U CN201420624021 U CN 201420624021U CN 204227975 U CN204227975 U CN 204227975U
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- heat
- exchanging component
- cold fluid
- zone
- liberation
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Abstract
A kind of heat-energy recovering apparatus, comprise zone of heat liberation, cold fluid pass and heat-exchanging component, described zone of heat liberation and described cold fluid pass be arranged in parallel, one end of described heat-exchanging component is located in described zone of heat liberation, the other end of described heat-exchanging component is located in described cold fluid pass, described heat-exchanging component comprises copper pipe and is located at the multiple copper sheets on described copper pipe, and multiple described copper sheet is arranged along the axially spaced-apart of described copper pipe.Above-mentioned heat-energy recovering apparatus, after hot fluid enters zone of heat liberation, hot fluid transfers heat to heat-exchanging component, temperature reduces, one end that heat is positioned at zone of heat liberation one end from heat-exchanging component is positioned at cold fluid pass toward heat-exchanging component is transmitted, meanwhile, after cold fluid enters cold fluid pass, cold fluid absorbs thermal temperature from heat-exchanging component and raises.Thus the heat of hot fluid is delivered to need on the cold fluid of raised temperature, make used heat be recycled utilization, economize energy, reduce production cost.
Description
Technical field
The utility model relates to energy saver field, particularly relates to a kind of heat-energy recovering apparatus.
Background technology
More existing equipment can produce a large amount of heats in use.To the process of these heats, what have directly can only get rid of waste heat, effectively can not recycle used heat, cannot improve energy consumption problem, and cost pressure is too large.What have then carries out oxidation processes acquisition thermal energy by residual solvent, but the method cost costly.
Utility model content
Given this, be necessary to provide a kind of cost lower, can the heat-energy recovering apparatus of effectively reclaiming waste heat.
A kind of heat-energy recovering apparatus, comprise zone of heat liberation, cold fluid pass and heat-exchanging component, described zone of heat liberation and described cold fluid pass be arranged in parallel, one end of described heat-exchanging component is located in described zone of heat liberation, the other end of described heat-exchanging component is located in described cold fluid pass, described heat-exchanging component comprises copper pipe and is located at the multiple copper sheets on described copper pipe, and multiple described copper sheet is arranged along the axially spaced-apart of described copper pipe.
Wherein in an embodiment, the thickness of described copper sheet is 0.4mm ~ 0.6mm.
Wherein in an embodiment, described copper sheet is ring-type, and described copper sheet is sheathed on outside described copper pipe, and the internal edge of described copper sheet is fixed on the outer surface of described copper pipe.
Wherein in an embodiment, each described copper sheet extends along the circumference of described copper pipe.
Wherein in an embodiment, the distance between adjacent described copper sheet is 2mm ~ 3mm.
Wherein in an embodiment, described heat-exchanging component is at least two, and the distance between adjacent described heat-exchanging component is 31mm ~ 36mm.
Above-mentioned heat-energy recovering apparatus, after hot fluid enters zone of heat liberation, hot fluid transfers heat to heat-exchanging component, temperature reduces, one end that heat is positioned at zone of heat liberation one end from heat-exchanging component is positioned at cold fluid pass toward heat-exchanging component is transmitted, meanwhile, after cold fluid enters cold fluid pass, cold fluid absorbs thermal temperature from heat-exchanging component and raises.Thus the heat of hot fluid is delivered to need on the cold fluid of raised temperature, make used heat be recycled utilization, economize energy, reduce production cost.
Accompanying drawing explanation
Fig. 1 is the cross-sectional view of the heat-energy recovering apparatus of an embodiment.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage more clear, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
Refer to Fig. 1, the heat-energy recovering apparatus 100 of an embodiment, comprise zone of heat liberation 10, cold fluid pass 20 and heat-exchanging component 30.Zone of heat liberation 10 and cold fluid pass 20 be arranged in parallel.One end of heat-exchanging component 30 is located in zone of heat liberation 10, and the other end of heat-exchanging component 30 is located in cold fluid pass 20.Multiple copper sheets 34 that heat-exchanging component 30 comprises copper pipe 32 and is located on copper pipe 32, multiple copper sheet 34 is arranged along the axially spaced-apart of copper pipe 32.
For circulating with the hot fluid of used heat in zone of heat liberation 10.Hot fluid can be liquid, also can be gaseous state.Zone of heat liberation 10 comprises entrance point 12 and the port of export 14.Hot fluid enters zone of heat liberation 10 from entrance point 12, after transferring heat to heat-exchanging component 30, flows out zone of heat liberation 10 from the port of export 14.For the cold fluid that circulates in cold fluid pass 20.Cold fluid can be liquid, also can be gaseous state.Cold fluid pass 10 comprises entrance point 22 and the port of export 24.Cold fluid enters cold fluid pass 20 from entrance point 22, after absorbing heat, flows out cold fluid pass 20 from the port of export 24 from heat-exchanging component 30.
Heat-exchanging component 30 is at least two.Distance between adjacent heat-exchanging component 30 can be 31mm ~ 36mm.When distance between the heat-exchanging component 30 that heat-exchanging component 30 quantity is more and adjacent is suitable, heat exchange efficiency is higher.Be appreciated that the quantity of heat-exchanging component 30 can be arranged according to actual needs.Copper sheet between adjacent heat-exchanging component 30 staggers setting, better transfers heat to heat-exchanging component 30 to enable the heat of the hot fluid in type of thermal communication path 10.In the present embodiment, heat-exchanging component 30 can according to 6 × 4 Heterogeneous Permutations.Namely the quantity of heat-exchanging component is 24, and 24 heat-exchanging components are divided into 4 rows, often arranges 6, heat-exchanging component 24 Heterogeneous Permutation of adjacent two rows.
The internal diameter of copper pipe 32 is 8mm ~ 10mm, and the external diameter of copper pipe 32 is 10mm ~ 12mm.Copper pipe 32 closed at both ends.
In the present embodiment, copper sheet 34 is ring-type.Copper sheet 34 is sheathed on outside copper pipe 32.The internal edge of copper sheet 34 is fixed on the outer surface of copper pipe 32.Be appreciated that copper sheet 34 also can other shapes such as semi-annular shape or sheet.The bearing of trend of copper sheet 34 is parallel to the axial direction of zone of heat liberation 10.That is, the bearing of trend of copper sheet 34 is parallel to the flow direction of fluid.In the present embodiment, copper sheet 34 extends along the circumference of copper pipe 32.When the bearing of trend of copper sheet 34 is parallel to the flow direction of fluid, the flow resistance of copper sheet 34 pairs of fluids is less.
The thickness of copper sheet 34 can be 0.4mm ~ 0.6mm.Specifically in the present embodiment, the thickness of copper sheet 34 is 0.5mm.Distance between adjacent copper sheet 34 can be 2mm ~ 3mm.Specifically in the present embodiment, the distance between adjacent copper sheet 34 is 3mm.When copper sheet 34 is ring-type, the internal diameter of copper sheet 34 is 10mm ~ 12mm.The external diameter of copper sheet 34 is 30mm ~ 35mm.The internal diameter of copper sheet 34 is equal with the external diameter of copper pipe 32.
When above-mentioned heat-energy recovering apparatus 100 works, hot fluid enters zone of heat liberation 10 from the entrance point 12 of zone of heat liberation 10.After hot fluid enters zone of heat liberation 10, transfer heat to the heat-exchanging component 30 in zone of heat liberation 10, the port of export 14 again from zone of heat liberation 10 after cooling flows out.One end that heat is positioned at zone of heat liberation 10 one end from heat-exchanging component 30 is positioned at cold fluid pass 10 toward heat-exchanging component 30 is transmitted.Meanwhile, cold fluid enters cold fluid pass 20 from the entrance point 22 of cold fluid pass 20.After cold fluid enters cold fluid pass 20, absorb heat from the heat-exchanging component 30 in cold fluid pass 20, the port of export 24 again from cold fluid pass after intensification flows out.
Above-mentioned heat-energy recovering apparatus 100, after hot fluid enters zone of heat liberation 10, hot fluid transfers heat to heat-exchanging component 30, temperature reduces, one end that heat is positioned at zone of heat liberation 10 one end from heat-exchanging component 30 is positioned at cold fluid pass 10 toward heat-exchanging component 30 is transmitted, meanwhile, after cold fluid enters cold fluid pass 20, cold fluid absorbs thermal temperature from heat-exchanging component 30 and raises.Thus the heat of hot fluid is delivered to need on the cold fluid of raised temperature, make used heat be recycled utilization, economize energy, reduce production cost.
Above-mentioned heat-energy recovering apparatus 100, the heat of the waste hot gas of the temperature 90 DEG C ~ 200 DEG C baking oven can discharged carries out effective recycling, thus makes equipment reach energy-saving effect.This apparatus structure is simple, easy to operate, can be applicable to the market demand and the use of large portion equipment.
The above is only preferred embodiment of the present utility model; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (6)
1. a heat-energy recovering apparatus, it is characterized in that, comprise zone of heat liberation, cold fluid pass and heat-exchanging component, described zone of heat liberation and described cold fluid pass be arranged in parallel, one end of described heat-exchanging component is located in described zone of heat liberation, the other end of described heat-exchanging component is located in described cold fluid pass, and described heat-exchanging component comprises copper pipe and is located at the multiple copper sheets on described copper pipe, and multiple described copper sheet is arranged along the axially spaced-apart of described copper pipe.
2. heat-energy recovering apparatus as claimed in claim 1, it is characterized in that, the thickness of described copper sheet is 0.4mm ~ 0.6mm.
3. heat-energy recovering apparatus as claimed in claim 1, it is characterized in that, described copper sheet is ring-type, and described copper sheet is sheathed on outside described copper pipe, and the internal edge of described copper sheet is fixed on the outer surface of described copper pipe.
4. heat-energy recovering apparatus as claimed in claim 1, it is characterized in that, each described copper sheet extends along the circumference of described copper pipe.
5. heat-energy recovering apparatus as claimed in claim 1, it is characterized in that, the distance between adjacent described copper sheet is 2mm ~ 3mm.
6. heat-energy recovering apparatus as claimed in claim 1, it is characterized in that, described heat-exchanging component is at least two, and the distance between adjacent described heat-exchanging component is 31mm ~ 36mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420624021.6U CN204227975U (en) | 2014-10-24 | 2014-10-24 | Heat-energy recovering apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420624021.6U CN204227975U (en) | 2014-10-24 | 2014-10-24 | Heat-energy recovering apparatus |
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| Publication Number | Publication Date |
|---|---|
| CN204227975U true CN204227975U (en) | 2015-03-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420624021.6U Active CN204227975U (en) | 2014-10-24 | 2014-10-24 | Heat-energy recovering apparatus |
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| CN (1) | CN204227975U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109269330A (en) * | 2018-10-30 | 2019-01-25 | 江苏龙净节能科技有限公司 | A kind of three-stage heat pipe rotational flow heat exchanger |
-
2014
- 2014-10-24 CN CN201420624021.6U patent/CN204227975U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109269330A (en) * | 2018-10-30 | 2019-01-25 | 江苏龙净节能科技有限公司 | A kind of three-stage heat pipe rotational flow heat exchanger |
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