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CN2149598Y - Drop-cross-section tubular heat exchanger - Google Patents

Drop-cross-section tubular heat exchanger Download PDF

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Publication number
CN2149598Y
CN2149598Y CN 92219327 CN92219327U CN2149598Y CN 2149598 Y CN2149598 Y CN 2149598Y CN 92219327 CN92219327 CN 92219327 CN 92219327 U CN92219327 U CN 92219327U CN 2149598 Y CN2149598 Y CN 2149598Y
Authority
CN
China
Prior art keywords
heat exchanger
drop
shaped tube
drop shaped
cross
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN 92219327
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Chinese (zh)
Inventor
季中
李庆领
任建勋
南新双
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
QINGDAO CHEMICAL COLLEGE
Original Assignee
QINGDAO CHEMICAL COLLEGE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by QINGDAO CHEMICAL COLLEGE filed Critical QINGDAO CHEMICAL COLLEGE
Priority to CN 92219327 priority Critical patent/CN2149598Y/en
Application granted granted Critical
Publication of CN2149598Y publication Critical patent/CN2149598Y/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model discloses a drop-shaped pipe heat exchanger, in particular to a recuperative heat exchanger whose basic heat transfer element is the drop-shaped pipe. The cross section of the drop-shaped pipe of the heat exchanger is formed by four sections of arc lines. The utility model has the advantages of high heat transfer coefficient, small flow resistance, low operating cost, easy processing, convenient manufacturing, high efficiency, energy saving, and material saving, and is the updated element of the prior and the future pipe heat exchangers.

Description

Drop-cross-section tubular heat exchanger
The utility model is the drop shaped tube heat exchanger.
Technical field is under the utility model: the heat-exchange device that heat exchange medium does not directly contact.
The drop shaped tube heat exchanger is to be the high-efficiency and energy-saving type dividing wall type heat exchanger of basic heat transfer element with drop shaped tube.
It is basic heat transfer element that existing pipe heat exchanger adopts pipe more.But because the fluid from outside cross-current is when crossing pipe, flow condition is not good, portion abscission zone broad, and the average heat transfer coefficient that causes the pipe outside is lower and flow resistance is higher.Afterwards, it is found that the heat transfer of some shape tubes and resistance performance were better than pipe, therefore, in some heat exchanger, begun to use shape tubes such as flat tube and elliptical tube.But still there is the low and high shortcoming of flow resistance of the coefficient of heat transfer in all non-best performance pipe of using of shape tube now, needs further improvement.
The drop shaped tube that the utility model proposed, its cross-sectional profiles line is near streamlined.By theory analysis as can be known, streamlined body has minimum form drag; Therefore, the external drag performance of drop shaped tube is better than other any cast.Simultaneously, theory analysis and experimental result all confirm: fluid is horizontal when plunderring drop shaped tube, under lower Reynolds number, " separate bubble " just can occur and reach " turbulent flow is attached again " phenomenon, and this phenomenon significantly improves the average heat transfer coefficient of drop shaped tube and resistance reduces greatly.In addition, consider easily manufacturedly, drop shaped tube and stream tube are incomplete same again.So drop shaped tube had both had the premium properties of streamline tube, have again and implement characteristics easily, have broad application prospects.
Goal of the invention of the present utility model is to overcome pipe and the shortcoming of other shape tube as heat transfer element the time; Improve the heat transfer coefficient of pipe heat exchanger, reduce flow resistance; Thereby saving tubing reduces operating cost, energy savings.
The cross-sectional profiles line of drop shaped tube is made up of four sections camber lines.Fig. 1 is the drop shaped tube cross sectional representation.Wherein, the radius of curvature of stem camber line is R 1The radius of curvature of afterbody camber line is R 2The radius of curvature of middle two sections camber lines is R 3Distance between the head and the tail two camber line centers of curvature is C.The correlation of each size is: R 1=(12~5) R 2R 3〉=10R 1Comprising R 3Be infinitely-great special circumstances; C=(15~5) R 1Fig. 2 is the operation principle schematic diagram of drop shaped tube heat exchanger.During the work of drop shaped tube heat exchanger, cold and hot fluid flows through the medial and lateral of drop shaped tube respectively.One of type of flow as shown in Figure 2, A represents cold fluid among the figure, B represents hot fluid.
The utility model is implemented convenient, and is easy to manufacture.During enforcement, according to the different application occasion, the material of drop shaped tube can adopt carbon steel, steel alloy (comprising stainless steel, titanium and titanium alloy etc.), copper, aluminium, zinc and alloy thereof, and nonmetallic materials such as graphite (comprising graphite plastic), polytetrafluoroethylene (PTFE), polystyrene, polyvinyl chloride, glass.The drop shaped tube of metal and nonmetallic materials can adopt the special equipment one-shot forming; The also available pipe roll forming of metal drop shaped tube.Drop shaped tube can adopt welding, expanded joint, expanded and welded tube joint to connect with connecting of tube sheet or glued joint.The enforcement of other parts is identical with common pipe heat exchanger.
The utility model is compared with the pipe heat exchanger of present use, has series of advantages: at first be coefficient of heat transfer height; Next is that flow resistance is low; The 3rd is that heat exchange area is big; Be the easy compact arrangement of tube bank once more; Be to have advantages such as the dust stratification amount is few at last.In the reynolds number range of using always in industry, the coefficient of heat transfer of drop shaped tube is higher by about 30% than corresponding pipe; And resistance has only about 1/3rd of pipe.For this reason, if replace the pipe that has now in the heat exchanger with drop shaped tube, its energy-saving effect is significant.With the boiler economizer is example, if the economizer of nearly 300,000 boilers in the whole nation all changes the drop shaped tube heat exchanger into, only considers that then resistance reduces by one, the annual degree more than 1,000,000,000 that just can economize on electricity; Consider that economizer only accounts for the very little part of industrial heat exchange device, consider that the economic benefit of more then using drop shaped tube is huge because the material that the drop shaped tube augmentation of heat transfer is brought is saved.

Claims (1)

1, a kind of heat exchange medium not directly the contact the drop shaped tube heat exchanger, it is characterized in that the cross section of drop shaped tube is made up of four sections camber lines; The radius of curvature R of stem camber line 1Radius of curvature R for the afterbody camber line 21.2 to 5 times, the radius of curvature R of middle two camber lines 3Radius of curvature R for the stem camber line 1More than 10 times, head and the tail two camber line center of curvature spacing C be stem camber line radius of curvature R 11.5 to 5 times, i.e. R 1=(1.2~5) R 2, R 3〉=10R 1, C=(1.5~5) R 1
CN 92219327 1992-07-11 1992-07-11 Drop-cross-section tubular heat exchanger Expired - Lifetime CN2149598Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 92219327 CN2149598Y (en) 1992-07-11 1992-07-11 Drop-cross-section tubular heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 92219327 CN2149598Y (en) 1992-07-11 1992-07-11 Drop-cross-section tubular heat exchanger

Publications (1)

Publication Number Publication Date
CN2149598Y true CN2149598Y (en) 1993-12-15

Family

ID=33766581

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 92219327 Expired - Lifetime CN2149598Y (en) 1992-07-11 1992-07-11 Drop-cross-section tubular heat exchanger

Country Status (1)

Country Link
CN (1) CN2149598Y (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101943535A (en) * 2010-09-29 2011-01-12 浙江金宸三普换热器有限公司 Oblate pipe and fin structure for parallel flow heat exchanger
CN102052876A (en) * 2010-12-16 2011-05-11 昆明理工大学 Novel heat transfer tube for low-temperature flue gas waste heat reclamation
CN102538538A (en) * 2011-11-10 2012-07-04 华北电力大学 Resistance-reducing base-tube fin tube bundle of air condenser
CN102607313A (en) * 2012-03-08 2012-07-25 双良节能系统股份有限公司 Direct air-cooling condenser finned tube
CN102607311A (en) * 2012-03-08 2012-07-25 双良节能系统股份有限公司 Heat exchange base tube for direct air-cooling condenser
CN102692144A (en) * 2012-02-02 2012-09-26 吴植仁 Novel flat-tube air cooler
CN102865758A (en) * 2012-08-31 2013-01-09 大连葆光节能空调设备厂 Heat exchanger special for sewage source thermal pump
CN102878842A (en) * 2012-10-24 2013-01-16 中国航天科技集团公司第五研究院第五一0研究所 Novel initiative jet cooling device
CN106288912A (en) * 2016-08-03 2017-01-04 海信(山东)空调有限公司 A kind of micro-channel heat exchanger and air-conditioner
CN108240701A (en) * 2016-12-26 2018-07-03 美的集团股份有限公司 Combustion gas liquid heating and gas heater
CN111237939A (en) * 2020-03-05 2020-06-05 成都医洁净环境科技有限公司 Cross-contamination-preventing waste heat recycling digital fresh air disinfection unit
CN113251828A (en) * 2021-05-07 2021-08-13 东南大学 Water drop grooving type winding pipe type heat exchanger
CN113476922A (en) * 2021-07-29 2021-10-08 万彪 Textile printing and dyeing wastewater treatment equipment and treatment method thereof

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101943535A (en) * 2010-09-29 2011-01-12 浙江金宸三普换热器有限公司 Oblate pipe and fin structure for parallel flow heat exchanger
CN102052876A (en) * 2010-12-16 2011-05-11 昆明理工大学 Novel heat transfer tube for low-temperature flue gas waste heat reclamation
CN102538538A (en) * 2011-11-10 2012-07-04 华北电力大学 Resistance-reducing base-tube fin tube bundle of air condenser
CN102692144B (en) * 2012-02-02 2016-01-20 吴植仁 A kind of new flat tube air cooler
CN102692144A (en) * 2012-02-02 2012-09-26 吴植仁 Novel flat-tube air cooler
CN102607313A (en) * 2012-03-08 2012-07-25 双良节能系统股份有限公司 Direct air-cooling condenser finned tube
CN102607311A (en) * 2012-03-08 2012-07-25 双良节能系统股份有限公司 Heat exchange base tube for direct air-cooling condenser
CN102865758A (en) * 2012-08-31 2013-01-09 大连葆光节能空调设备厂 Heat exchanger special for sewage source thermal pump
CN102878842A (en) * 2012-10-24 2013-01-16 中国航天科技集团公司第五研究院第五一0研究所 Novel initiative jet cooling device
CN106288912A (en) * 2016-08-03 2017-01-04 海信(山东)空调有限公司 A kind of micro-channel heat exchanger and air-conditioner
CN108240701A (en) * 2016-12-26 2018-07-03 美的集团股份有限公司 Combustion gas liquid heating and gas heater
CN111237939A (en) * 2020-03-05 2020-06-05 成都医洁净环境科技有限公司 Cross-contamination-preventing waste heat recycling digital fresh air disinfection unit
CN113251828A (en) * 2021-05-07 2021-08-13 东南大学 Water drop grooving type winding pipe type heat exchanger
CN113476922A (en) * 2021-07-29 2021-10-08 万彪 Textile printing and dyeing wastewater treatment equipment and treatment method thereof

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GR01 Patent grant
C17 Cessation of patent right
CX01 Expiry of patent term