Abstract: Problem to be Solved To provide a heat exchanger that can increase the performance by setting an optimal number of tube groups in a configuration where each of the tube groups is provided with headers. Solution The number of arrays of tube groups of a core section 2 is set to three rows. The number N of heating medium flow holes 21 per tube is set for each width dimension Tw of tubes 20, and the tubes 20 are formed such that the width dimension Tw of the tubes and a flow channel cross-sectional area S satisfy a relationship of S1?S?S2. Therefore, the number of arrays of the tube groups in the core section 2 can be set to an optimal number of arrays for improving the endothermic capacity and reducing the weight, and sufficient refrigerant flow rate and pressure resistance can be secured. As a result, even when there is a restriction on the size of the entire heat exchanger, a light high-performance heat exchanger can be configured.

Abstract: Problem to be Solved To provide a heat exchanger that can increase the performance by setting an optimal number of tube groups in a configuration where each of the tube groups is provided with headers. Solution The number of arrays of tube groups of a core section 2 is set to three rows. The number N of heating medium flow holes 21 per tube is set for each width dimension Tw of tubes 20, and the tubes 20 are formed such that the width dimension Tw of the tubes and a flow channel cross-sectional area S satisfy a relationship of S1?S?S2. Therefore, the number of arrays of the tube groups in the core section 2 can be set to an optimal number of arrays for improving the endothermic capacity and reducing the weight, and sufficient refrigerant flow rate and pressure resistance can be secured. As a result, even when there is a restriction on the size of the entire heat exchanger, a light high-performance heat exchanger can be configured.

Abstract: Provided are a heat exchanger capable of providing sufficient heat exchange capability even with heat transfer tubes having a reduced outer diameter, and a heat pump device using the same. The heat transfer tubes has an outer diameter D in a range of 5 mm?D?6 mm, has a thickness t in a range of 0.05×D?t?0.09×D, are disposed at a vertical pitch L1 in a range of 3×D?L1?4.2×D, and are disposed at a longitudinal pitch L2 in a range of 2.6×D?L2?3.64×D. A sufficiently increased heat exchange rate per unit weight is obtainable with the heat exchanger.

Abstract: A heat exchanger having a plurality of heat-transfer tubes arrayed at intervals in vertical and anteroposterior directions and arranged so that an equilateral triangle is formed by lines connecting the centers of heat-transfer tubes located vertically and anteroposteriorly adjacent to each other; and a plurality of heat-transfer corrugated fins arranged at intervals in an axial direction of the heat-transfer tubes, characterized in that when an external diameter of each of the heat-transfer tubes is V1; a vertical pitch of the heat-transfer tubes is V2, a fin pitch of the heat-transfer corrugated fins is V3, a fin plate thickness of each of the heat-transfer corrugated fins is V4, and a corrugate height of the heat-transfer corrugated fins is V5, any one of V2, V3 and V5 is set within a given range.

Abstract: A heat exchanger having a plurality of heat-transfer tubes arrayed at intervals in vertical and anteroposterior directions and arranged so that an equilateral triangle is formed by lines connecting the centers of heat-transfer tubes located vertically and anteroposteriorly adjacent to each other; and a plurality of heat-transfer corrugated fins arranged at intervals in an axial direction of the heat-transfer tubes, characterized in that when an external diameter of each of the heat-transfer tubes is V1; a vertical pitch of the heat-transfer tubes is V2, a fin pitch of the heat-transfer corrugated fins is V3, a fin plate thickness of each of the heat-transfer corrugated fins is V4, and a corrugate height of the heat-transfer corrugated fins is V5, any one of V2, V3 and V5 is set within a given range.

Abstract: Provided are a heat exchanger capable of providing sufficient heat exchange capability even with heat transfer tubes having a reduced outer diameter, and a heat pump device using the same. The heat transfer tubes has an outer diameter D in a range of 5 mm?D?6 mm, has a thickness t in a range of 0.05×D?t?0.09×D, are disposed at a vertical pitch L1 in a range of 3×D?L1?4.2×D, and are disposed at a longitudinal pitch L2 in a range of 2.6×D?L2?3.64×D. A sufficiently increased heat exchange rate per unit weight is obtainable with the heat exchanger.

Abstract: A heat exchanger includes a pipe having an opening formed therein, and an insert positioned within the pipe. The heat exchanger also includes a cap member for sealing the opening, and a support member for resiliently supporting the insert. Specifically, the support member is positioned between the insert and the cap member.

Abstract: A heat exchanger includes a pipe having an opening formed therein, and an insert positioned within the pipe. The heat exchanger also includes a cap member for sealing the opening, and a support member for resiliently supporting the insert. Specifically, the support member is positioned between the insert and the cap member.

Abstract: A subcooling-type condenser includes a refrigerant condensation core and a subcooling core for supercooling refrigerant condensed by the refrigerant condensation core. A header portion corresponding to an entrance portion of the subcooling core is formed as a liquid refrigerant storage portion, and a capacity of the header Vh is set within a range of 100 cc≦Vh≦250 cc. Thus, subcooling-type condenser having a desired re-liquefaction function without using a separately formed liquid tank may be achieved, thereby reducing the condenser's size and cost.

Abstract: A subcooling-type condenser includes a refrigerant condensation core and a subcooling core for supercooling refrigerant condensed by the refrigerant condensation core. A header portion corresponding to an entrance portion of the subcooling core is formed as a liquid refrigerant storage portion, and a capacity of the header Vh is set within a range of 100 cc≦Vh≦250 cc. Thus, subcooling-type condenser having a desired re-liquefaction function without using a separately formed liquid tank may be achieved, thereby reducing the condenser's size and cost.

Abstract: A condenser equipped with a receiver includes an inlet portion for refrigerant of the receiver opening in an axial direction of the receiver; an outlet portion for refrigerant of the condenser communicating with the inlet portion of the receiver; and an insertion portion provided on either the inlet portion or the outlet portion. The insertion portion is inserted into the outlet portion or the inlet portion, and the inlet portion and the outlet portion are brought into contact with each other to make a gastight condition between the inlet portion and the outlet portion. In this structure, the workability for attaching the receiver to the condenser and detaching the receiver from the condenser may be improved. Moreover, the strength for fixing the receiver to the condenser may be increased.

Abstract: A multi-flow type heat exchanger includes a pair of headers and a plurality of heat transfer tubes interconnecting the headers. The flow direction of the heat exchange medium through the whole of the heat transfer tubes is only one direction. A flow division parameter &ggr; is defined as a ratio of a resistance parameter &bgr; of the heat transfer tubes to a resistance parameter &agr; of an entrance side header and is set to at least about 0.5. The flow division parameter is calculated, such that &ggr;=&bgr;/&agr;, where &bgr;=Lt/(Dt·n), and &agr;=Lh/Dh. The equation variables are defined as follows: Lt equals a length of each tube, Dt equals a hydraulic diameter of one tube, n equals a number of tubes, Lh equals a length of an entrance side header, and Dh equals a hydraulic diameter of the header. The flow division from the header to the tubes may be chosen at an optimum condition, and the heat exchanger may have superior performance.

Abstract: A heat exchanger includes a tank having a pipe insertion hole disposed in a tank wall and a fluid pipe connected to the tank wall for introducing a fluid into the tank or discharging the fluid from the tank. The tank wall has a burr formed around the pipe insertion hole extending toward an interior of the tank. The fluid pipe has a flange formed on its periphery by bending the fluid pipe onto itself. An end portion of the fluid pipe is inserted into the pipe insertion hole so that the flange contacts an outer surface of the tank wall, and the inserted end portion is expanded and caulked together with the burr. A brazing material may be fixed between the flange and the tank wall during brazing even during vibration. The length of the pipe inserted into the tank may be minimized. The contact area between the fluid pipe and the tank is thereby enlarged.

Abstract: A header of a heat exchanger includes a seat member having bent portions on its end portions, a tank member having side walls on its end portions, and a pair of caps sealing the open ends of a barrel formed from the seat member and the tank member. Each side wall has a free end portion bent inwardly by an amount substantially equal to a thickness of the bent portion. The inner surface of each bent portion and the outer surface of each offset free end portion are joined to form the barrel. Thus, protrusions on the exterior shape of the formed barrel are eliminated, thereby eliminating contours from the shape of each cap provided on each open end of the barrel.

Abstract: A heat exchanger includes a pair of header pipes, each having an end closed by a header cap; a plurality of heat transfer tubes interconnecting the header pipes; a plurality of fins; a side fin disposed on the outer surface of at least one of the outermost heat transfer tubes; and a side plate disposed on the outer surface of the side fin. The header cap comprises a header pipe connecting portion and a portion extending toward the side fin and side plate and having a concave portion engaged with the side fin and side plate. The header pipe and the side fin and side plate are connected to each other by the header cap; in particular, by the extended portion of the header cap, when assembled and brazed. The rotational shifting of the header pipe and the positional shifting of the side fin and side plate in the brazing process are prevented by the structure of the header cap.

Abstract: A heat exchanger includes reservoirs spaced apart from each other and a plurality of parallel heat transfer tubes fluidly connecting the reservoirs. An end portion of each heat transfer tube is connected to at least one of the reservoirs so that the end portion does not project into the interior of the reservoir. Thus, the dimension of the reservoir in the axial direction of the tubes and a proper volume of heat transfer medium may be minimized. Further, pressure loss can be reduced because there are no projecting tubes in the reservoirs to obstruct the flow of the heat transfer medium. Moreover, the strength of the connection between the tubes and the reservoirs can be increased because more contacting surface area is provided for making the connection, for example by brazing.

Abstract: A heat exchanger includes a header having tube insertion holes and heat transfer tubes, wherein each of the heat transfer tubes has an end portion inserted into a corresponding tube insertion hole. A burr is formed on a wall of the header around each tube insertion hole to extend in a direction toward an interior of the header. The burr has a bent tip portion formed by bending at least a part of a tip portion of the burr inwardly. A tip of the end portion of each heat transfer tube inserted into a corresponding tube insertion hole contacts with the bent tip portion of the burr. The bent tip portion of the burr seals a gap formed between an outer surface of the inserted end portion of the tube and an inner surface of the burr when the header and the tubes are assembled and brazed, thereby preventing leakage of a heat exchange fluid through such a gap. The insertion depth of the tube is reduced by the bent tip portion of the burr, thereby decreasing pressure loss in the header.

Abstract: A heat exchanger includes a tank having a pipe insertion hole disposed in a tank wall and a fluid pipe connected to the tank wall for introducing a fluid into the tank or discharging the fluid from the tank. The tank wall has a burr formed around the pipe insertion hole extending toward an interior of the tank. The fluid pipe has a flange formed on its periphery by bending the fluid pipe onto itself. An end portion of the fluid pipe is inserted into the pipe insertion hole so that the flange contacts an outer surface of the tank wall, and the inserted end portion is expanded and caulked together with the burr. A brazing material may be fixed between the flange and the tank wall during brazing even during vibration. The length of the pipe inserted into the tank may be minimized. The contact area between the fluid pipe and the tank is thereby enlarged.

Abstract: A heat exchanger, such as a condenser for use in an automobile air conditioning system includes inlet and outlet union elements. Each inlet and outlet union element includes a union joint and a pipe member having one end secured to a header pipe. The other end of the pipe member is temporarily connected to the union joint before a brazing process of the condenser is carried out. Couplers are provided to effect the temporary connection.

Abstract: A method of making a heat exchanger including header pipes, flat tubes extending between the header pipes and fin units extending between the flat tubes. The header pipes include a plurality of holes on one side thereof for accepting the flat tubes. On the opposite side of the header pipes is at least one slit in which a partition plate is inserted. During the formation of the header pipe, a pair of projections are formed on the ends of the slit. After the partition plate is inserted into the header pipe, the projections are bent until they engage the partition plate thereby fixedly securing the partition plate within the header pipe.