SU591684A2 - Corrugated insert for plate heat exchanger - Google Patents

Corrugated insert for plate heat exchanger

Info

Publication number
SU591684A2
SU591684A2 SU762318049A SU2318049A SU591684A2 SU 591684 A2 SU591684 A2 SU 591684A2 SU 762318049 A SU762318049 A SU 762318049A SU 2318049 A SU2318049 A SU 2318049A SU 591684 A2 SU591684 A2 SU 591684A2
Authority
SU
USSR - Soviet Union
Prior art keywords
channel
heat exchanger
plate heat
corrugated insert
insert
Prior art date
Application number
SU762318049A
Other languages
Russian (ru)
Inventor
Евгений Владимирович Дубровский
Original Assignee
Предприятие П/Я А-1665
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 Предприятие П/Я А-1665 filed Critical Предприятие П/Я А-1665
Priority to SU762318049A priority Critical patent/SU591684A2/en
Application granted granted Critical
Publication of SU591684A2 publication Critical patent/SU591684A2/en

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

Description

(54) ГОФРИРОВАННАЯ ВСТАВКА ДЛЯ ПЛАСТИНЧАТОГО ТЕПЛООВМЕННИКА(54) CORRUGATED INSERT FOR PLASTIC HEAT EXCHANGER

налом должна подводитс  к потоку теплоносител , в узком пристенном слое с тем, чтобы она затрачивалась только на его турбулизацию . Именно в этом слое сосредоточено наибольшее термическое сопротивление тепловому потоку в канале.The water should be supplied to the coolant flow in a narrow wall layer so that it is spent only on its turbulization. It is in this layer that the greatest thermal resistance to heat flow in the channel is concentrated.

Профиль канала гофров выполн етс  таким образом, чтобы степень дросселировани  потока теплоносител  характеризовалась отношением гидравлического диаметра d в самом узком сечении канала к гидравлическому диаметру d гладкого участка канала, равным d/d 0,65-0,92. Действительно, масштаб вихревых масс, образуемых за узким сечением канала, а также их место расположени  в пристенном слое определ ютс  отношением d/d 0,65-0,92.The channel profile of the corrugations is designed so that the degree of throttling of the coolant flow is characterized by the ratio of the hydraulic diameter d in the narrowest section of the channel to the hydraulic diameter d of the smooth channel section equal to d / d 0.65-0.92. Indeed, the scale of the vortex masses formed beyond the narrow section of the channel, as well as their location in the near-wall layer, is determined by the ratio d / d 0.65-0.92.

Отношение высоты h канала (гофра) к шагу t ребер (гофров) в гофрированной вставке составл ет h/t 4-6. Значени  диапазона изменени  этого соотношени  обеспечивают благ гопри тные физические услови  образовани  и распространени  в пристенном слое канала турбулентных вихрей за узким его сечением, особенно в угловых зонах 6, так как в канал оделевидного сечени  в угловых зонах по вл ютс  вторичные токи: Эти токи способствуют более ранней турбулизаЦйи течени  в углах. На фоне этого турбулизиро/ 2The ratio of the height h of the channel (corrugation) to the pitch t of the ribs (corrugations) in the corrugated insert is h / t 4-6. The values of the range of variation of this ratio provide favorable physical conditions for the formation and propagation of turbulent vortices in the near-wall layer of the channel beyond its narrow cross section, especially in the corner zones 6, since secondary currents appear in the channel of a clear section in the corner zones: early turbulant currents in the corners. Against the background of this turbulence / 2

ванного течени  в углах образование и развитие турбулентных вихрей за узким сечением канала происходит незатрудненно. В результате сокраш.аютс  энергозатраты на одинаковую интенсификацию теплообмена.At the corners of the flow, the formation and development of turbulent eddies behind a narrow channel section occurs without difficulty. As a result, energy consumption for the same intensification of heat exchange is reduced.

Claims (3)

1.Гофрированна  вставка дл  пластинчатого теплообменника по авт. св. № 336489, отличающа с  тем, что, с целью интенсификации теплообмена двухсторонние асимметричные выточки выполнены скругленными с радиусом сопр жени , равным 1 - 10 толшинам гофра.1. Corrugated insert for a plate heat exchanger according to ed. St. No. 336489, characterized in that, in order to intensify heat exchange, two-sided asymmetrical undercuts are rounded with a radius of conjugation of 1 to 10 corrugation thicknesses. 2.Вставка по п, 1. отличающа с  тем,-что каждый сужаюшийс  участок канала выполнен с гидравлическим диаметром, составл ющим2. The insert according to claim 1. 1. wherein each narrowed section of the channel is made with a hydraulic diameter constituting 0,65-0,92 гидравлического диаметра гладкого участка канала.0,65-0,92 hydraulic diameter of the smooth section of the channel. 3.Вставка по п. 1, отличающа с  тем, что канал имеет высоту, равную 4-6 шагам гофров .3. The insert according to claim 1, characterized in that the channel has a height equal to 4-6 steps of the corrugations. Источники информации, прин тые во внимание при экспертизе;Sources of information taken into account in the examination; 1. Авторское свидетельство № 336489, кл. F 28 F 3/02, 1969.1. Copyright certificate № 336489, cl. F 28 F 3/02, 1969. ТT АBUT
SU762318049A 1976-01-30 1976-01-30 Corrugated insert for plate heat exchanger SU591684A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU762318049A SU591684A2 (en) 1976-01-30 1976-01-30 Corrugated insert for plate heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU762318049A SU591684A2 (en) 1976-01-30 1976-01-30 Corrugated insert for plate heat exchanger

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
SU336489 Addition

Publications (1)

Publication Number Publication Date
SU591684A2 true SU591684A2 (en) 1978-02-05

Family

ID=20646825

Family Applications (1)

Application Number Title Priority Date Filing Date
SU762318049A SU591684A2 (en) 1976-01-30 1976-01-30 Corrugated insert for plate heat exchanger

Country Status (1)

Country Link
SU (1) SU591684A2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4420039A (en) * 1980-02-07 1983-12-13 Dubrovsky Evgeny V Corrugated-surface heat exchange element
US5473508A (en) * 1994-05-31 1995-12-05 At&T Global Information Solutions Company Focused CPU air cooling system including high efficiency heat exchanger
RU2450230C2 (en) * 2009-12-07 2012-05-10 Евгений Владимирович Дубровский Corrugated insert for plate heat exchanger
RU2575378C2 (en) * 2012-04-23 2016-02-20 ГЕА ЭКОФЛЕКС ГмбХ Plate-type heat exchanger
RU2576404C2 (en) * 2012-04-23 2016-03-10 ГЕА ЭКОФЛЕКС ГмбХ Plate-type heat exchanger
US9410462B2 (en) 2008-08-06 2016-08-09 Sven Melker Nilsson Channel system
US9441523B2 (en) 2008-04-18 2016-09-13 Sven Melker Nilsson Channel system with internal flow director and turbulence generator

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4420039A (en) * 1980-02-07 1983-12-13 Dubrovsky Evgeny V Corrugated-surface heat exchange element
US5473508A (en) * 1994-05-31 1995-12-05 At&T Global Information Solutions Company Focused CPU air cooling system including high efficiency heat exchanger
US9441523B2 (en) 2008-04-18 2016-09-13 Sven Melker Nilsson Channel system with internal flow director and turbulence generator
US9410462B2 (en) 2008-08-06 2016-08-09 Sven Melker Nilsson Channel system
RU2450230C2 (en) * 2009-12-07 2012-05-10 Евгений Владимирович Дубровский Corrugated insert for plate heat exchanger
RU2575378C2 (en) * 2012-04-23 2016-02-20 ГЕА ЭКОФЛЕКС ГмбХ Plate-type heat exchanger
RU2576404C2 (en) * 2012-04-23 2016-03-10 ГЕА ЭКОФЛЕКС ГмбХ Plate-type heat exchanger

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