Abstract: An improved heat exchanger (60) includes plural relatively flat conduits (62) adapted to accommodate passage of heat transfer fluid therethrough. Each conduit (62) has inlet and outlet openings, a supply channel (100) communicating with the corresponding inlet opening to direct heat transfer fluid flowing through the corresponding inlet opening into the corresponding conduit (62), a drain channel (102) communicating with the corresponding outlet opening to direct heat transfer fluid out of the corresponding conduit (62) through the corresponding outlet opening, and plural heat transfer channels (92) communicating between the supply and drain channels (100, 102) to direct heat transfer fluid therebetween in a generally transverse direction relative to respective major axes of the supply and drain channels (100, 102). The supply and drain channels (100, 102) each have a substantially greater length and cross-sectional area than the length and cross-sectional area of each heat transfer channel (92).

Abstract: An improved heat exchanger includes plural relatively flat conduits adapted to accommodate passage of heat transfer fluid therethrough. Each conduit has inlet and outlet openings, a supply channel communicating with the corresponding inlet opening to direct heat transfer fluid flowing through the corresponding inlet opening into the corresponding conduit, a drain channel communicating with the corresponding outlet opening to direct heat transfer fluid out of the corresponding conduit through the corresponding outlet opening, and plural heat transfer channels communicating between the supply and drain channels to direct heat transfer fluid therebetween in a generally transverse direction relative to respective major axes of the supply and drain channels. The supply and drain channels each have a substantially greater cross-sectional area than the cross-sectional area of each heat transfer channel.

Abstract: The invention relates to a flat tube for a heat exchanger formed by folding one plate or overlaying two plates, in which long beads (16) are formed in multiple rows on the plate in its longitudinal direction, portions of the plate to which the respective long beads are opposed are formed flat, the tops of the long beads are joined with the flat portions (15) to form a plurality of channels (17) by the long beads and the flat portions, and a plurality of passages (18) which communicate adjacent channels are formed at appropriate parts on the long beads formed in the longitudinal direction of the plate. The invention also relates to a method for producing the above tube.Thus, the plates can have their faces securely engaged, and a heat exchanger having an improved heat-exchanging efficiency can be obtained.

Abstract: A heat exchanger, produced by the insertion of welded pipes into a rib pack, has a good connection between the rib pack and the pipes after expansion of the pipes. An optimal contact of the pipes against the passages in the cooling fins of the rib pack is achieved because the weld base of the welded pipe lies in a recess. The recess is formed by reduction of the wall thickness of a strip material from which the welded pipe is produced.

Abstract: There is disclosed herein a heat exchanger tube having an elongated, generally rectangular member including a planar base, a top, and pair of arcuate opposed side portions interposed between the base and the top. A partition extends from the top to the base to define a pair of fluid passageways, the partition including a pair of opposing, contacting bend portions and a leg portion depending from each of the bend portions which contact the base. Each of the leg portions is disposed at an acute angle relative to a vertical plane and spaced apart a predetermined distance so as define a braze receiving fillet therebetween. A method of manufacturing such a tube is also disclosed.

Abstract: An elongated heat exchanger tube has an internally located stiffener assembly which prevents the deflection of the tube wall due to pressure differentials between the tube internal and external surfaces while allowing the flow of fluid between the areas on opposite sides of the stiffener inside of the tube. The heat exchanger tube can have an elliptical, oval or flat cross-section. The internal stiffener can have a variety of cross-sectional configurations having uniform or non-uniform shapes.