CN103225963A - Efficient ripple thin-walled condensing heat exchanger - Google Patents

Efficient ripple thin-walled condensing heat exchanger Download PDF

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Publication number
CN103225963A
CN103225963A CN2013101383247A CN201310138324A CN103225963A CN 103225963 A CN103225963 A CN 103225963A CN 2013101383247 A CN2013101383247 A CN 2013101383247A CN 201310138324 A CN201310138324 A CN 201310138324A CN 103225963 A CN103225963 A CN 103225963A
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heat exchanger
thin
heat
tube
heat exchange
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CN2013101383247A
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吴国存
冯斌
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Abstract

The invention relates to a heat exchanger, in particular to an efficient ripple thin-walled condensing heat exchanger, which comprises a heat exchanger casing and a heat exchanging core tube arranged inside the heat exchanger casing, and is characterized in that the heat exchanging core tube is a thin-walled ripple tube; the thickness of the tube wall of the thin-walled ripple tube ranges from 0.1% to 1.2% times of the inner diameter of the tube body, and the height of wave crest of the thin-walled ripple tube is 10-50 times of the thickness of the tube wall of the thin-walled ripple tube; and infill is arranged inside the ripple tube. The efficient ripple thin-walled condensing heat exchanger has remarkable effects that the heat exchanging efficiency of the heat exchanger can be increased to a large extent through a heat exchanging surface provided with an oversized heat exchanging area and formed by the tube wall of the ripple tube; and an ultrathin heat exchanging surface formed by the tube wall of the ripple tube not only has the capability of preventing out of circularity and recessing under exogenic action, but also can increase the heat exchanging efficiency of the heat exchanger to a large extent, and further has the function of absorbing heat stress efficiently.

Description

Efficient corrugated thin-wall condensing heat exchanger
Technical field
The present invention relates to heat exchanger, especially a kind of efficient corrugated thin-wall condensing heat exchanger.
Background technology
At present, though condensing heat exchanger is of a great variety, form is different, determine the principal element of its heat exchange efficiency all to be: 1. big more by the ratio of the circulation volume of heat exchange journey and heat exchange area, its heat exchange efficiency is high more; 2. heat-transfer surface is thin more, and its heat exchange efficiency is high more.
Prevailing heat exchanger, it is made up of a cylindrical heat exchange core pipe inside by the heat exchange journey, one end of cylindrical heat exchange core pipe is entered the mouth by heat transferring medium, the other end of cylindrical heat exchange core pipe is exported by heat transferring medium, thick steel pipe of suit outside cylindrical heat exchange core pipe and form heat exchanger shell, the two ends of heat exchanger shell are recessed into and are connected with the two ends of cylindrical heat exchange core pipe, be communicated with the outlet of heat transferring medium inlet and heat transferring medium respectively at the two ends of heat exchanger shell, thus cylindrical heat exchange core pipe outside with the inner heat exchange journey that exports perforation with heat transferring medium inlet and heat transferring medium that forms of heat exchanger shell.
Circulated in by heat transferring medium by the heat exchange journey, heat transferring medium circulates in the heat exchange journey, between by heat transferring medium and heat transferring medium under the potential difference of the temperature difference, will be passed through heat-transfer surface that the tube wall by cylindrical heat exchange core pipe constitutes by the heat in the temperature difference between heat transferring medium and the heat transferring medium and thermaltransmission mode by the medium conduction transmits heat to the other side.
The heat exchange efficiency of conventional heat exchanger down is not only relevant, also relevant with the thickness of heat-transfer surface with the heat exchange area under the circulation volume, the heat exchanger under equal circulation volume, and heat exchange area is big more, the thickness of heat-transfer surface is thin more, and its heat exchange efficiency is high more.
Under the structure of above-mentioned heat exchanger, certainly lead to following drawback:
1. under the prerequisite of equal latus rectum, equal length, the heat exchange area minimum that constitutes by the tube wall of cylindrical heat exchange core pipe.
It is relatively poor that the tube wall of 2. cylindrical heat exchange core pipe bears the intensity of unidirectional external force, under the effect of unidirectional external force, make it that circle and depression take place to lose easily, must (for example be supported with thicker tube wall, if cylindrical heat exchange core pipe is that a circulation diameter is the steel pipe of 100mm, then pipe thickness is about 4.5mm), form thicker heat-transfer surface thus, and thicker heat-transfer surface must cause certain obstruction for the heat transmission by the medium conduction.
3. cylindrical heat exchange core pipe does not possess the function that absorbs thermal stress substantially.
For solving above-mentioned drawback, adopt the heat exchange core pipe of bellows structure more.But how to improve the heat exchange efficiency of corrugated tube heat exchanger, still do not have preferred plan at present.
Summary of the invention
The present invention is intended to solve the problem that the described heat exchanger of background technology exists, but and provides a kind of ultra-thin heat-transfer surface, super large heat exchange area efficient absorption thermal stress and inside to be provided with the efficient corrugated thin-wall condensing heat exchanger of obturator.
The present invention solves its technical problem and adopts following technical scheme:
A kind of efficient corrugated thin-wall condensing heat exchanger, comprise heat exchanger shell, place the heat exchange core pipe in the heat exchanger shell, it is characterized in that, described heat exchange core pipe is a thin-wall corrugated tube, the pipe thickness of described thin-wall corrugated tube is in 1.2% to 0.1% scope of internal diameter of tube body, the height of crest is in 8 to 20 times of scopes of pipe thickness, and bellows interior is provided with obturator.
Adopt the present invention of technique scheme, its outstanding effect is: by the heat-transfer surface of the super large heat exchange area that is made of the bellows tube wall, can significantly improve the heat exchange efficiency of heat exchanger, by the ultra-thin heat-transfer surface that constitutes by the bellows tube wall, not only has the ability that prevents to lose circle and depression under external force, also can significantly improve the heat exchange efficiency of heat exchanger, also possess and absorb thermal stress duty efficiently, be provided with obturator by bellows interior, can improve to greatest extent by the ratio of heat exchange journey circulation volume and heat exchange area, finally realize the purpose of high efficient heat exchanging.
The technical scheme that realizes the object of the invention also can have following preferred version:
Described thin-wall corrugated tube is by stainless acid resistant steel machine-shaping.
The obturator of described thin-wall corrugated tube inside is provided with the obturator support.
Described thin-wall corrugated tube outer setting has the body support.
Description of drawings
Fig. 1 is an embodiment of the invention structural representation.
Fig. 2 is the section structure schematic diagram of the embodiment of the invention.
Fig. 3 is the bellows partial enlarged drawing.
Among the figure: by heat transferring medium inlet 1, heat transferring medium outlet 2, heat exchange core pipe 3, heat exchanger shell 4, body support 5, obturator 6, obturator support 7, by heat transferring medium outlet 8, heat transferring medium inlet 9, crest 10, trough 11.
The specific embodiment
Further set forth the present invention below by embodiment, purpose only is to understand better content of the present invention.
Referring to accompanying drawing, in the present embodiment, heat exchange core pipe 3 is that a diameter dimension repeatedly size variation takes place and forms undulatory tubular body, the position that diameter dimension is big is referred to as crest 10, the position that diameter dimension is little is referred to as trough 11, the thickness of crest 10 and trough 11 is basic identical, and their thickness is the pipe thickness of bellows 1.The tube wall of heat exchange core pipe 3 is heat-transfer surfaces, and the pipe thickness of heat exchange core pipe 3 is a heat-transfer surface thickness, and the tube wall area of heat exchange core pipe 3 is heat exchange areas.
Be communicated with heat exchange core pipe 3 two ends respectively by heat transferring medium inlet 1 with by heat transferring medium outlet 8, heat exchange core pipe 3 inner formations are by the heat exchange journey; Outside heat exchange core pipe 3, be set with heat exchanger shell 4, the two ends of heat exchanger shell 4 recessed and with heat exchange core pipe 3 two ends by heat transferring medium inlet 1 be connected by the outer end of heat transferring medium outlet 8, be communicated with heat transferring medium inlet 9 and heat transferring medium outlet 2 with its internal communication respectively at the two ends of heat exchanger shell 4, thus heat exchange core pipe 3 outside with the heat exchanger shell 4 inner heat exchange journeys that connect with heat transferring medium inlet 9 and heat transferring medium outlet 2 that form.
In the present embodiment, heat exchange core pipe 3 is by stainless acid resistant steel machine-shaping, and its internal diameter of tube body is 80 ㎜, and pipe thickness is 0.6 ㎜, and crest 10 highly is 8 ㎜, and pipe thickness is 0.75% of an internal diameter of tube body, and crest 10 highly is 13 times of pipe thickness.Thin-wall corrugated tube inside is provided with obturator 6, and obturator 6 can improve by the ratio of heat exchange journey circulation volume and heat exchange area, thereby the heat exchange efficiency of heat exchanger is further enhanced.
In the present embodiment, obturator 6 is provided with obturator support 7.Obturator support 7 can make obturator 6 be positioned at heat exchange core pipe 3 inner optimum positions, so that by the heat transferring medium heat exchange of circulating more uniformly, optimize the heat exchange property of heat exchanger in by the heat exchange journey.
In the present embodiment, heat exchange core pipe 3 outer setting have body support 5.Equally, body support 5 can make heat exchange core pipe 3 be positioned at heat exchanger shell 4 inner optimum positions, so that heat exchange core pipe 3 bottoms in the heat exchange journey have sufficient heat transferring medium circulation heat exchange, further optimizes the heat exchange property of heat exchanger.
In the present embodiment, heat exchange core pipe 3 Corrosion Protections of being made by stainless acid resistant steel are stronger, can not shorten the service life of heat exchanger because of the corrosion of ultra-thin heat-transfer surface.
The heat exchange core pipe 3 of said structure has the heat exchange area of super large, especially the heat-transfer surface of superthin structure, can significantly improve the heat exchange efficiency of heat exchanger, and have and prevent that under external force heat exchange core pipe 3 from losing the ability of circle and depression, possess to absorb thermal stress duty efficiently.
The description of the foregoing description is not the restriction to technical solution of the present invention, any according to the present invention design done only for pro forma but not substantial equivalent transformation all should be considered as technical scheme category of the present invention.

Claims (4)

1. efficient corrugated thin-wall condensing heat exchanger, comprise heat exchanger shell, place the heat exchange core pipe in the heat exchanger shell, it is characterized in that, described heat exchange core pipe is a thin-wall corrugated tube, the pipe thickness of described thin-wall corrugated tube is in 1.2% to 0.1% scope of internal diameter of tube body, the height of crest is in 8 to 20 times of scopes of pipe thickness, and bellows interior is provided with obturator.
2. efficient corrugated thin-wall condensing heat exchanger according to claim 1 is characterized in that described thin-wall corrugated tube is by stainless acid resistant steel machine-shaping.
3. efficient corrugated thin-wall condensing heat exchanger according to claim 1 is characterized in that the obturator of described thin-wall corrugated tube inside is provided with the obturator support.
4. efficient corrugated thin-wall condensing heat exchanger according to claim 1 is characterized in that described thin-wall corrugated tube outer setting has the body support.
CN2013101383247A 2013-04-22 2013-04-22 Efficient ripple thin-walled condensing heat exchanger Pending CN103225963A (en)

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CN2013101383247A CN103225963A (en) 2013-04-22 2013-04-22 Efficient ripple thin-walled condensing heat exchanger

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106955558A (en) * 2017-05-16 2017-07-18 福建龙净环保股份有限公司 A kind of condensing duster
CN109883240A (en) * 2019-03-25 2019-06-14 中国空气动力研究与发展中心超高速空气动力研究所 A kind of high-temperature cooler circular cross-section shell structure and its design method
CN115432906A (en) * 2022-09-15 2022-12-06 北京工业大学 A jet flow bellows type sludge drying device

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2336312Y (en) * 1998-09-09 1999-09-01 海尔集团公司 Casing heat exchanger
CN2517530Y (en) * 2002-01-10 2002-10-23 秦皇岛市宇田科技有限公司 Wax Liquid cooling box
CN2867258Y (en) * 2005-12-12 2007-02-07 郎风 Annular parallel-flow heat exchanger
CN201503228U (en) * 2009-10-22 2010-06-09 山东爱客多热能科技有限公司 Heat accumulation type heating heat exchanger
CN101782340A (en) * 2009-01-15 2010-07-21 王智慧 Multi-stage type high-efficiency bellows waste heat recovery device
CN203177682U (en) * 2013-04-22 2013-09-04 吴国存 Efficient corrugated thin-walled condensing heat exchanger

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2336312Y (en) * 1998-09-09 1999-09-01 海尔集团公司 Casing heat exchanger
CN2517530Y (en) * 2002-01-10 2002-10-23 秦皇岛市宇田科技有限公司 Wax Liquid cooling box
CN2867258Y (en) * 2005-12-12 2007-02-07 郎风 Annular parallel-flow heat exchanger
CN101782340A (en) * 2009-01-15 2010-07-21 王智慧 Multi-stage type high-efficiency bellows waste heat recovery device
CN201503228U (en) * 2009-10-22 2010-06-09 山东爱客多热能科技有限公司 Heat accumulation type heating heat exchanger
CN203177682U (en) * 2013-04-22 2013-09-04 吴国存 Efficient corrugated thin-walled condensing heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106955558A (en) * 2017-05-16 2017-07-18 福建龙净环保股份有限公司 A kind of condensing duster
CN106955558B (en) * 2017-05-16 2024-05-28 福建龙净环保股份有限公司 Condensing dust remover
CN109883240A (en) * 2019-03-25 2019-06-14 中国空气动力研究与发展中心超高速空气动力研究所 A kind of high-temperature cooler circular cross-section shell structure and its design method
CN115432906A (en) * 2022-09-15 2022-12-06 北京工业大学 A jet flow bellows type sludge drying device

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Application publication date: 20130731