SU616521A1 - Heat-exchanging pipe - Google Patents
Heat-exchanging pipeInfo
- 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
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)
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)
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 |
-
1977
- 1977-03-29 SU SU772469481A patent/SU616521A1/en active
Cited By (9)
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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