SU964422A2 - Heat exchanging surface - Google Patents

Heat exchanging surface Download PDF

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Publication number
SU964422A2
SU964422A2 SU813257433A SU3257433A SU964422A2 SU 964422 A2 SU964422 A2 SU 964422A2 SU 813257433 A SU813257433 A SU 813257433A SU 3257433 A SU3257433 A SU 3257433A SU 964422 A2 SU964422 A2 SU 964422A2
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SU
USSR - Soviet Union
Prior art keywords
heat exchanging
exchanging surface
pipes
heat exchange
heat transfer
Prior art date
Application number
SU813257433A
Other languages
Russian (ru)
Inventor
Борис Васильевич Анипко
Юрий Митрофанович Дедусенко
Александр Васильевич Быков
Владимир Павлович Лещин
Игорь Леонидович Иванов
Original Assignee
Институт Проблем Машиностроения Ан Усср
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Application filed by Институт Проблем Машиностроения Ан Усср filed Critical Институт Проблем Машиностроения Ан Усср
Priority to SU813257433A priority Critical patent/SU964422A2/en
Application granted granted Critical
Publication of SU964422A2 publication Critical patent/SU964422A2/en

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Description

(54) ТЕПЛООБМЕННАЯ ПОВЕРХНОСТЬ(54) HEAT EXCHANGE SURFACE

Изобретение относитс  к теплообменной аппаратуре и может быть использовано в знергетической промышленности .The invention relates to heat exchange equipment and can be used in the energy industry.

Известны теплообменные поверхности дл  систем кондиционировани  воз духа, содержащие расположенные параллельными р дами трубы с поперечным пластинчатым оребрением, выполненным в виде желобов, смещенных в смежных р дах на полшага и обращенЦых выпуклостью в разные стороны tl.Heat transfer surfaces are known for air-conditioning systems that contain pipes arranged in parallel rows with transverse plate fins made in the form of grooves displaced in adjacent rows by half a step and facing convexity in different directions tl.

Недостатком известной поверхности  вл етс  низкий коэффициент теплоотда и к теплоносителю, протекающему в межтрубном.пространстве.A disadvantage of the known surface is the low coefficient of heat transfer to the coolant flowing in the annular space.

Цель изобретени  - интенсификаци  теплообмена.The purpose of the invention is to intensify heat transfer.

Указанна  цель достигаетс  тем, что трубы имеют вогнутый профиль с радиусом кривизны, составл ющим 0,65-0,9 длины их дуги, и в смежных р дах обращены вогнутост ми в противоположные стороны.This goal is achieved by the fact that the pipes have a concave profile with a radius of curvature of 0.65-0.9 times the length of their arc, and in adjacent rows are turned towards the opposite sides by concavities.

На чертеже схематично изображена, предлагаема  теплообменна  поверхность . The drawing schematically shows the proposed heat exchange surface.

Теплообменна  поверхность содержит расположенные параллельными р дами 1 и 2 трубы 3 с поперечнымThe heat exchange surface contains pipes 3 arranged in parallel rows 1 and 2 with transverse

пластинчатым оребрением 4, выполненным в виде желобов, смещенных в смежных р дах 1 и 2 на полшага и обра|щенных вогнутостью в разные стороны. Трубы 3 имеют вогнутый профиль с радиусом кривизны, составл ющим 0,65-0,9 длины их дуги, и в смежных р дах 1 и 2 обращены вогнутост ми в противоположные стороны. Желоба вы10 полнены с радиусом кривизны,, составл ющим 0,6-0,7 длины их дуги.lamellar fins 4, made in the form of grooves, displaced in adjacent rows 1 and 2 by half a step and inverted in opposite directions. The pipes 3 have a concave profile with a radius of curvature of 0.65-0.9 times the length of their arc, and in adjacent rows 1 and 2 are turned in opposite directions by concavities. The gutters are filled with a radius of curvature that is 0.6-0.7 in the length of their arc.

Теплоноситель циркулирует по трубам 3 и отдает тепло потоку воздуха,The coolant circulates through the pipes 3 and gives off heat to the air flow,

15 который в поперечном направлении омывает теплообменную поверхность, проход  по каналам, образованным вогнутой поверхностью трубок 3 и пластинчатого оребрени  4. За счет15 which in the transverse direction washes the heat exchange surface, the passage through the channels formed by the concave surface of the tubes 3 and the plate fins 4. Due to

20-вогнутости труб 3 и оребрени  4, в каналах дл  воздуха создаютс  вихревые течени , повышающие коэффициент теплоотдачи к воздуху.20-concavity of the tubes 3 and the fins 4, eddy currents are created in the air channels, increasing the heat transfer coefficient to the air.

Выполнение труб с радиусом кривгиз25 ны 0,65-0,9 от длины их дуг и ориентирование их в смежных р дах вогнутост ми в противоположные стороны увеличивает коэффициент теплоотдачи и интенсифицирует теплообмен The making of pipes with a radius of curvature of 0.65-0.9 from the length of their arcs and their orientation in adjacent rows with concavities in opposite directions increases the heat transfer coefficient and intensifies the heat exchange

30 в целом.30 overall.

Claims (1)

1. Авторское свидетельство СССР 589532, кл. F 28 F 1/24, 1974. 1. USSR author's certificate 589532, cl. F 28 F 1/24, 1974.
SU813257433A 1981-03-06 1981-03-06 Heat exchanging surface SU964422A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU813257433A SU964422A2 (en) 1981-03-06 1981-03-06 Heat exchanging surface

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU813257433A SU964422A2 (en) 1981-03-06 1981-03-06 Heat exchanging surface

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
SU589532 Addition

Publications (1)

Publication Number Publication Date
SU964422A2 true SU964422A2 (en) 1982-10-07

Family

ID=20946530

Family Applications (1)

Application Number Title Priority Date Filing Date
SU813257433A SU964422A2 (en) 1981-03-06 1981-03-06 Heat exchanging surface

Country Status (1)

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SU (1) SU964422A2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5501270A (en) * 1995-03-09 1996-03-26 Ford Motor Company Plate fin heat exchanger
US6151949A (en) * 1999-08-25 2000-11-28 Visteon Global Technologies, Inc. Method of manufacturing a flat corrugated tube
US6249968B1 (en) 1999-08-25 2001-06-26 Visteon Global Technologies, Inc. Method of making a robust gosper fin heat exchanger
GB2413706A (en) * 2004-04-29 2005-11-02 Hewlett Packard Development Co Heat exchanger and liquid cooling system
US11225807B2 (en) 2018-07-25 2022-01-18 Hayward Industries, Inc. Compact universal gas pool heater and associated methods

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5501270A (en) * 1995-03-09 1996-03-26 Ford Motor Company Plate fin heat exchanger
US6151949A (en) * 1999-08-25 2000-11-28 Visteon Global Technologies, Inc. Method of manufacturing a flat corrugated tube
US6249968B1 (en) 1999-08-25 2001-06-26 Visteon Global Technologies, Inc. Method of making a robust gosper fin heat exchanger
GB2413706A (en) * 2004-04-29 2005-11-02 Hewlett Packard Development Co Heat exchanger and liquid cooling system
US7142424B2 (en) 2004-04-29 2006-11-28 Hewlett-Packard Development Company, L.P. Heat exchanger including flow straightening fins
US11225807B2 (en) 2018-07-25 2022-01-18 Hayward Industries, Inc. Compact universal gas pool heater and associated methods
US11649650B2 (en) 2018-07-25 2023-05-16 Hayward Industries, Inc. Compact universal gas pool heater and associated methods

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