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    • 3. 发明公开
    • FIN-AND-TUBE TYPE HEAT EXCHANGER, AND ITS RETURN BEND PIPE
    • RÜCKLAUFBOGENROHRGERIPPTERROHRWÄRMETAUSCHER
    • EP2042825A1
    • 2009-04-01
    • EP07790611.3
    • 2007-07-11
    • Kobelco&materials Copper Tube, Ltd.
    • TAKAHASHI, HiroyukiHABA, TsuneoISHIBASHI, Akihiko
    • F28D1/047F25B1/00F25B39/02F28F1/40
    • F28F1/40F25B39/02F25B2500/01F25B2500/09F28D1/0477F28F1/32F28F1/42F28F1/422F28F9/0246F28F9/26
    • The invention provides a fin-and-tube heat exchanger using a return bend tube that allows further enhancement of the evaporative performance of the heat exchanger. The fin-and-tube heat exchanger, where a refrigerant is supplied inside tubing, has a hairpin tube portion where a plurality of hairpin tubes are arranged, a return bend tube portion where there are arranged a plurality of return bend tubes joined to respective hairpin tube ends of the hairpin tube portion, and a fin portion comprising a plurality of fins arranged at a predetermined spacing on the outer surface of the hairpin tubes. The heat exchanger comprises first grooves formed on the tube inner surface of the return bend tube. A first groove pitch (P1) of the first grooves in a cross section perpendicular to a tube axis, and a second groove pitch (P2) of spiral-shaped second grooves formed on the inner surface of the hairpin tube in a cross section perpendicular to a tube axis, satisfy a groove pitch ratio (P1/P2) of 0.65 to 2.2, while a first groove cross-sectional area (S1) per groove of the first grooves in a cross section perpendicular to the tube axis, and a second groove cross-sectional area (S2) per groove of the second grooves in a cross section perpendicular to the tube axis satisfy a groove cross-sectional area ratio (S1/S2) of 0.3 to 3.6.
    • 本发明提供了一种使用回弯管的翅片管式热交换器,其允许进一步提高热交换器的蒸发性能。 在管内供给制冷剂的翅片管式热交换器具有设置有多个发夹管的发夹管部分,其中布置有多个返回弯管并连接到相应的发夹 所述发夹管部分的管端部和翅片部分包括在所述发夹管的外表面上以预定间隔布置的多个翅片。 热交换器包括形成在返回弯管的管内表面上的第一槽。 在垂直于管轴线的横截面中的第一槽的第一槽间距(P1)和形成在发夹管的内表面上的螺旋状第二槽的第二槽间距(P2),垂直于 管轴线满足0.65〜2.2的槽间距比(P1 / P2),而与管轴垂直的截面中的第一槽的槽的第一槽横截面积(S1)和第二槽 在与管轴垂直的截面中,第二槽的槽的截面积(S2)满足0.3〜3.6的槽截面积比(S1 / S2)。