SU616521A1 - Heat-exchanging pipe - Google Patents

Heat-exchanging pipe

Info

Publication number
SU616521A1
SU616521A1 SU772469481A SU2469481A SU616521A1 SU 616521 A1 SU616521 A1 SU 616521A1 SU 772469481 A SU772469481 A SU 772469481A SU 2469481 A SU2469481 A SU 2469481A SU 616521 A1 SU616521 A1 SU 616521A1
Authority
SU
USSR - Soviet Union
Prior art keywords
pipe
grooves
groove
heat
helix
Prior art date
Application number
SU772469481A
Other languages
Russian (ru)
Inventor
Владимир Тихонович Буглаев
Владимир Иванович Калентьев
Валерий Сергеевич Казаков
Петр Петрович Рыженко
Валерий Ильич Судаков
Original Assignee
Брянский Институт Транспортного Машиностроения
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 Брянский Институт Транспортного Машиностроения filed Critical Брянский Институт Транспортного Машиностроения
Priority to SU772469481A priority Critical patent/SU616521A1/en
Application granted granted Critical
Publication of SU616521A1 publication Critical patent/SU616521A1/en

Links

Description

(54) ТЕПЛООБМЕННАЯ ТРУБА(54) HEAT EXCHANGE PIPE

Изобретение относитс  к теплотехнике а точнее к конденсаторам с конденсацией пара из паровоздушной смеси ни наружной поверхности труб, с движением охлаж дающей жидкости внутри труб. Известны теплообменные трубы, снабженные на наружной поверхности канавкой треугольного профил  в виде спирали 1. Однако такие трубы обладают низким коэффициентом теплоотдачи, так как их наружна  поверхность не имеет гладких участков, канавки трубы заполн ютс  пленкой конденсата. Без конденсатной пленки работают лишь вершины между соседними канавками) не оказываю существенного вли ни  на теплопередачу от пара к воде. Цель изобретени  - повышение коэффицИента теплоотдачи. Это достигаетс  тем, что шаг спирали равен Двойной ширине канавки, глубина которой tie пре 1шает 0,5 толшинь стен ки трубы. При эгом профиль канавок представл ет собой равносторонний треугольник, то повышает эффективность теплопередачи за счет отсутстви  пленки конденсата на поверхности трубы. На чертеже изображена предлагаема  теплосбменна  труба, общий вид. Теплообменна  труба имеет гладкую внутреннюю поверхность 1. На наружной поверхности трубы выполнены канавки 2 треугольного профил  в виде спирали, между которыми образованы спиральные цилиндрические по ски 3. Шаг спирали равен двойной ширине канавки, при этом ширина по скОв 3 равна ширине канавок 2 по верху, глубина канавок не превышает 0,5 толщины стенки трубы. Угол при вершине 4 канавок 2 составл ет прибли- зительно 60 . Труба может быть цельнот нута , канавки образованы нарезкой или накаткой, профиль канавок представл ет собой равносторонний треугольник. При работе трубы через нее пропускаетс  охлаждающа  вода, снаружи поперёкThe invention relates to heat engineering, and more specifically to condensers with steam condensation from an air-steam mixture or the outer surface of pipes, with the movement of cooling fluid inside the pipes. Heat transfer tubes are known that are provided on the outer surface with a groove of a triangular profile in the form of a spiral 1. However, such pipes have a low heat transfer coefficient, since their outer surface does not have smooth sections, the pipe grooves are filled with a condensate film. Without a condensate film, only vertices between adjacent grooves work) have no significant effect on heat transfer from steam to water. The purpose of the invention is to increase the heat transfer coefficient. This is achieved by the fact that the pitch of the helix is equal to the double width of the groove, whose depth of tie exceeds 0.5 the thickness of the pipe wall. With this, the groove profile is an equilateral triangle, which increases the efficiency of heat transfer due to the absence of a film of condensate on the surface of the pipe. The drawing shows the proposed heat exchange pipe, a general view. The heat exchange pipe has a smooth inner surface 1. On the outer surface of the pipe there are grooves 2 of a triangular profile in the form of a spiral, between which spiral cylindrical skirts 3 are formed. The pitch of the helix is equal to twice the width of the groove, while the width of shear 3 is equal to the width of the grooves 2 along the top, the depth of the grooves does not exceed 0.5 pipe wall thickness. The angle at the apex of the 4 grooves 2 is approximately 60. The pipe can be chickpea whole, the grooves are formed by cutting or knurling, the profile of the grooves is an equilateral triangle. During the operation of the pipe, cooling water is passed through it, across the outside

оси трубы О1к;хоаиг пер или паровоздушна  с.месь.O1k pipe axes; hoaig pen or vapor-air seam.

Центры lioHfK-HcauHK пара возникают в гюршинах 4 спирал1ЛГо1х канавок 2s как наиболее охлаждйнных по сравнению с удаленными от поверхности 1 по сками 3. Образующиес  в центрах конденсации капли за счет поверхностного нат жен   увлекают конденсат с по сков 3 и удаленных от вершины 4 участков канавок 2, укрупн ютс  и срываютс  с трубы. Пленка конденсата на поверхности трубы не образуетс .The centers of lioHfK-HcauHK steam appear in the gyr-shears 4 helix1LGohx grooves 2s as the most cooled compared to the remote from surface 1 strip 3. The droplets formed in the condensation centers draw the condensate from the sandwich 3 and 4 sections removed from the top of the grooves 2 are enlarged and broken off the pipe. No condensate film is formed on the pipe surface.

Благодар  работе наружной поверхнооти трубы без пленки и конденсата KoaJHфициенг теплоотдачи от пара   паровоздути ной смеси к охлаждаемой стенке трубы повышаетс  на 6О -7О%оDue to the operation of the outer surface of the pipe without a film and condensate, the heat transfer from the steam-air mixture to the cooled pipe wall increases by 6 ~ -7 0% o

Claims (2)

Формула изобрегйни Isobregin formula 1,Тбплообменна  труба, преммущесч. венно конденсатора, снабженна  на наружной повархности канавкой треуг олького профил  Е виде спирали, о т л и ч а ia«1, Tbploobmenna pipe, premturnesch. of the condenser, provided on the external surface with a groove of a three-sided profile E in the form of a helix, about щ а   с   тем, что, с целью повышени  ковг фициента теплоотдачи, шаг спирали равен двойной ширшю канавки, глубина которой не превышает Одб толщины стен ки трубы.This is due to the fact that, in order to increase the heat transfer coefficient of the heat source, the pitch of the helix is equal to the double width of the groove, the depth of which does not exceed the maximum wall thickness of the pipe. 2.Труба по п„ 1, о т л и ч а ю щ а  с   TeMj что профиль .канавок представл ет собой равносторонний треугольни2. A pipe according to Clause 1, of which there is a TeMj that the profile of the grooves is an equilateral triangle. Источники информации, пргш тые во внимание при экспертизе:Sources of information taken into account in the examination: 1о Авторское свидетельство СССР № 423547, кл, F 28 F 1/10, 1972.1 USSR author's certificate No. 423547, class, F 28 F 1/10, 1972.
SU772469481A 1977-03-29 1977-03-29 Heat-exchanging pipe SU616521A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU772469481A SU616521A1 (en) 1977-03-29 1977-03-29 Heat-exchanging pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU772469481A SU616521A1 (en) 1977-03-29 1977-03-29 Heat-exchanging pipe

Publications (1)

Publication Number Publication Date
SU616521A1 true SU616521A1 (en) 1978-07-25

Family

ID=20702270

Family Applications (1)

Application Number Title Priority Date Filing Date
SU772469481A SU616521A1 (en) 1977-03-29 1977-03-29 Heat-exchanging pipe

Country Status (1)

Country Link
SU (1) SU616521A1 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8091621B2 (en) 2006-01-19 2012-01-10 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8191258B2 (en) 2006-01-19 2012-06-05 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8281489B2 (en) 2006-01-19 2012-10-09 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8434227B2 (en) 2006-01-19 2013-05-07 Modine Manufacturing Company Method of forming heat exchanger tubes
US8438728B2 (en) 2006-01-19 2013-05-14 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8561451B2 (en) 2007-02-01 2013-10-22 Modine Manufacturing Company Tubes and method and apparatus for producing tubes
US8683690B2 (en) 2006-01-19 2014-04-01 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8726508B2 (en) 2006-01-19 2014-05-20 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US9038267B2 (en) 2010-06-10 2015-05-26 Modine Manufacturing Company Method of separating heat exchanger tubes and an apparatus for same

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8091621B2 (en) 2006-01-19 2012-01-10 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8191258B2 (en) 2006-01-19 2012-06-05 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8281489B2 (en) 2006-01-19 2012-10-09 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8434227B2 (en) 2006-01-19 2013-05-07 Modine Manufacturing Company Method of forming heat exchanger tubes
US8438728B2 (en) 2006-01-19 2013-05-14 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8683690B2 (en) 2006-01-19 2014-04-01 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8726508B2 (en) 2006-01-19 2014-05-20 Modine Manufacturing Company Flat tube, flat tube heat exchanger, and method of manufacturing same
US8561451B2 (en) 2007-02-01 2013-10-22 Modine Manufacturing Company Tubes and method and apparatus for producing tubes
US9038267B2 (en) 2010-06-10 2015-05-26 Modine Manufacturing Company Method of separating heat exchanger tubes and an apparatus for same

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