Laminated heat exchanger

Abstract: A plurality of tube elements (4,5,6,7,7',8,9), each of which is provided with a pair of tanks on one side with these tanks communicating via a heat exchanging medium passage, are laminated. An intake/outlet tank group (100) with intake/outlet portions (40a,40b) is divided into three tank sub groups while a non intake/outlet tank group (200) is not partitioned, constituting a single tank group. The intake/outlet portion (40a,40b) on the intake side is directly connected with the tank sub group at one end in the intake/outlet tank group (100) and at the same time, it communicates with the tank sub group at the other end via a relay pipe (60). Consequently, the coolant that has flowed in through the intake/outlet portion (40a) is induced to the non intake/outlet tank group (200) from the tank sub group at one end via a heat exchanging medium passage and it is also induced to the non intake/outlet tank group (200) from the tank sub group at the other end via the heat exchanging medium passage before the two flows are joined at the center. Then, the coolant reaches the tank sub group at the center in the intake/outlet tank group (100) by travelling through the heat exchanging medium passage again to flow out through the intake/outlet portion (40b) on the output side. By improving the distribution of the heat exchanging medium, the performance of the heat exchanger is enhanced.

Description: The present invention relates to a laminated heat exchanger according to the preamble of claim 1, which can be used, for instance, as a heater core, or an evaporator in an air conditioning system for vehicles. Such a heat exchanger is shown in Fig. 1 of EP - A - 0 271 084. To outline this laminated heat exchanger, an intake piping unit and an outlet piping unit project out adjacent to each other approximately at the center of the front surface in the direction of air flow. The intake piping unit and the outlet piping unit are each formed by bonding formed plates abutted facing each other so that they are internally provided with a first space and a second space and a first space and a second space respectively. Between the intake piping unit and the outlet piping unit, a central tube unit is provided in such a manner that it is clamped between the two units. The central tube unit is provided with a first space and a second space. The first space of the central tube element and the first space of the outlet piping unit are cut off from each other so that the first space of the intake piping unit and the first space of the outlet piping unit 2B are not in communication. Furthermore, adjacent tanks communicate via holes, which are formed in the direction of the lamination. With this, the tanks in this laminated heat exchanger are divided into an intake tank group, a central tank group and an outlet tank group, to effect the flow of heat exchanging medium described below. First, after the heat exchanging medium flows into the intake piping unit to the first space, it travels into the intake tank group. The heat exchanging medium in the intake tank group then travels through the first tube group along its U-shaped flow path to flow into the left half of the central tank group. Then, the heat exchanging medium that has flowed into the left half of the central tank group flows into the right half of the central tank group via the second spaces and of the intake piping unit and the outlet piping unit respectively. The heat exchanging medium, which has thus flowed into the right half of the central tank group, flows through the second tube group along its U-shaped flow path. Then it flows into the outlet tank group. After that, it flows to the left and flows out from the outlet piping unit. However, in a laminated heat exchanger provided with tank groups that effect the flow of heat exchanging medium described above, the heat exchanging medium doses not flow easily in tanks that are far from the intake and outlet piping units, i. e., the tanks that are at the end. The above causes inconsistency in the distribution of heat exchanging medium flowing in the laminated heat exchanger, which, in turn, results in poor temperature distribution of the heat exchanging medium flowing in the tube units, reducing the performance off the laminated heat exchanger. US - A - 5,024,269 discloses a similar laminated heat exchanger as described above. Object of the present invention is to provide a laminated heat exchanger with enhanced performance to improve the distribution of the heat exchanging medium by addressing the problems described above. The above object is achieved by a laminated heat exchanger with the features of claim 1. Preferred embodiments are subject of the subclaims. Preferably, the laminated heat exchanger according to the present invention is constituted by laminating tube elements, each of which is formed by fitting together a pair of formed plates, with a pair of tanks at one end and a heat exchanging medium passage that communicates between the pair of tanks, alternately with fins over a plurality of levels, with the pairs of tanks formed, by lamination, to constitute separate tank groups, i.e., an intake / outlet tank group and a non intake / outlet tank group. The intake / outlet tank group is further divided into three tank sub groups by two non communicating portions while the non intake / outlet tank group constitutes one tank group which is in communication throughout with no partitions. One intake / outlet portion is provided in one of the tank sub groups that is at one end of the intake / outlet tank group and is connected to the tank sub group at the other end via a means for relay. The other intake / outlet portion is provided in the tank sub group which is in the center of the intake / outlet tank group. In the laminated heat exchanger structured as described above, heat exchanging medium flows into the tank sub groups at both ends in the intake / outlet tank group from the one intake / outlet portion, then travels upwards from the intake / outlet tank sub groups at both ends through heat exchanging medium passage groups at both ends. It then travels downward through the heat exchanging medium passage groups and the two flow paths of the heat exchanging medium are joined at the non intake / outlet tank group to travel upward from the center of the non intake / outlet tank group through the heat exchanging medium passage group. It then travels downward through the heat exchanging medium passage group to reach the central tank sub group of the intake / outlet tank group and flows out through the other intake / outlet portion. Another example of the laminated heat exchanger is constituted by laminating tube elements, each of which is formed by fitting together two formed plates, with a pair of tanks at one end and a heat exchanging medium passage that communicates between the pair of tanks, alternately with fins over a plurality of levels, with the pairs of tanks formed, by lamination, to constitute separate tank groups, i.e., an intake / outlet tank group and a non intake / outlet tank group. The intake / outlet tank group is further divided into three tank sub groups by two non communicating portions while the non intake / outlet tank group is further divided into two tank sub groups by one non communicating portion provided in the tube element located between the two non communicating portions. One intake / outlet portion is provided in one of the tank sub groups that is at one end of the intake / outlet tank group and is connected to the tank group at the other end via a means for relay. The other intake / outlet portion is provided in the tank sub group which is in the center of the intake / outlet tank group. In the laminated heat exchanger structured as described above, heat exchanging medium flows, for instance, from the one intake / outlet portion into the tank sub groups at both ends of the intake / outlet tank group, then travels upwards from the intake / outlet tank sub groups at both ends through heat exchanging medium passage groups at both ends. It then travels downward through the heat exchanging medium passage groups and the two flow paths of the heat exchanging medium flow separately into the left tank sub group and the right tank sub group of the non intake / outlet tank group. The two flow paths of the heat exchanging medium then travel upward from those tank sub groups through the two heat exchanging medium passage groups in the center which are separate from each other. They then travel downward through the two heat exchanging medium passage groups to reach the central tank sub group of the intake / outlet tank group to be joined, before flowing out from the other intake / outlet portion. FIG. 1 illustrates the overall structure of the laminated heat exchanger in the first embodiment according to the present invention; FIG. 2 illustrates the laminated heat exchanger above viewed from the end with the tanks; FIG. 3 is a cross section of the laminated heat exchanger above through line II at the end with the tanks; FIGs. 4 - 9 illustrate the formed plates used in the laminated heat exchanger above; FIGs. 10A - 10H illustrate plates for intake / outlet portion formation which constitute the intake / outlet portions in the laminated heat exchanger above; FIG. 11 illustrates the flow of heat exchanging medium in the laminated heat exchanger above; FIG. 12 illustrates the laminated heat exchanger in a second embodiment according to the present invention, viewed from the end with the tanks; FIG. 13 illustrates formed plates used in the laminated heat exchanger above; FIG. 14 illustrates the flow of heat exchanging medium in the laminated heat exchanger above; FIG. 15 illustrates the overall structure of the laminated heat exchanger which employs intake / outlet portions structured differently from those in the first embodiment; and FIG. 16 illustrates the laminated heat exchanger above, viewed from the end with the tanks. The following is an explanation of the embodiments according to the present invention in reference to the drawings. FIGs. 1 - 11 show the first embodiment of the laminated heat exchanger 1 according to the present invention. As shown in FIGs. 1 and 2, this laminated heat exchanger 1 is constituted by laminating a plurality of types of tube elements 4, 5, 6, 7, 7', 8 and 9 and corrugated fins 10 alternately over a plurality of levels (21 levels, for instance). The core of the heat exchanger is formed by providing the second tube element 5 between the laminated first tube elements 4 at the seventh from the center, providing the third tube element 6 at the second place counting toward the center from the second tube element 5, and providing the fourth tube element 7, the sixth tube element 8 and the fifth tube element 7', located fourth, fifth and sixth respectively from the center toward the left. At the same time, a seventh tube element 9 and an end plate 2 or 3, are provided at each end in the direction of the lamination . Plates for intake / outlet portion formation 41, 42, 43 and 44 which constitute intake / outlet portions 40a, 40b to be explained later, are provided between the fourth tube element 7 and the sixth tube element 8 and between the sixth tube element 8 and the fifth tube element 7'. The first tube element 4, the second tube element 5, the third tube element 6, the fourth tube element 7, the fifth tube element 7', the sixth tube element 8 and the seventh tube element 9 are all approximately rectangular and the first tube element 4 is constituted by adjoining two formed plates 11 and 11, shown in FIG. 4, face-to-face at their brazing margins, 19 and 19. The formed plates 11 which constitute the first tube element 4 are constituted of a clad material whose main constituent is aluminum, which is clad with brazing material. As shown in FIG. 4, each formed plate 11 is provided with a pair of distended portions for tank formation 13a and 14a located toward one end in the direction of the length, each of which, in turn, is provided with a communicating hole 12. A projection 15 extends from approximately the center between the distended portions for tank formation 13a and 14a toward the non tank side and a distended portion for passage formation 16, which is formed approximately U-shaped and which communicates with the distended portions for tank formation 13a and 14a, is formed around the projection 15. In addition, an indented portion 18, which is indented toward the inside is formed between the distended portion for tank formation 13a and the distended portion for tank formation 14a. The first tube element 4 is constituted by bonding the two formed plates 11 described above, abutted to each other flush. Toward one end of the first tube element 4, a pair of tanks 13 and 14 are formed, constituted of the distended portions for tank formation 13a and 14a which face opposite each other. Toward the inside, a heat exchanging medium passage 20, which is approximately U-shaped, is constituted with two of the distended portions for passage formation 16 facing opposite each other. The tank 13 and the tank 14 communicate via the heat exchanging medium passage 20 and between the tank 13 and the tank 14, a groove 21 is constituted with the indented portion 18. The second tube element 5, which is provided at a position that is third from the end plate 2 of the laminated heat exchanger 1, is constituted by bonding a formed plate 25, shown in FIG. 5, and a formed plate 26, shown in FIG. 6, abutted flush to each other. The formed plate 25 is similar to the formed plate 11 in its basic form and material. However, it does not have the indented portion 18 between its distended portion for tank formation 13a' and its distended portion for tank formation 14a. Instead, the distended portion for tank formation 13a', which is provided with a fitting hole 27 for fitting a relay pipe 60 and a communicating hole 12, distends into the area where the indented portion would otherwise be, to form an elongated circular shape. The other formed plate 26, too, is similar to the formed plate 11 in its basic form and material. However, it also does not have an indented portion. Instead, the distended portion for tank formation 13a", which is provided with a communicating hole 12, distends to the area where the indented portion would otherwise be, to form an elongated circular shape. The second tube element 5 is constituted by abutting the formed plate 25 and the formed plate 26 flush to each other, and toward its lower end, the tanks 14 are formed from the distended portions for tank formation 14a and 14a which face opposite each other. At the same time, a tank 13' is constituted from the distended portion for tank formation 13a' of the formed plate 25 and the distended portion for tank formation 13a" of the formed plate 26. Note that the fitting hole 27 of the tank 13' opens toward a passage 35, to be explained later. The third tube element 6, which is provided at a position that is second toward the center from the second tube element 5, is constituted by bonding the formed plate 11 shown in FIG. 4 abutted flush to a formed plate 28, shown in FIG. 7, whose distended portion for tank formation 13a"' is not provided with a communicating hole 12 but only with a shallow impression. The third tube element 6 is constituted by abutting the formed plate 28 and the formed plate 11 flush to each other, and toward its lower end, a tank 14 is formed from the distended portions for tank formation 14a and 14a which face opposite each other. A blind tank 13'' is constituted from the distended portion for tank formation 13a of the formed plate 11 and the distended portion for tank formation 13a"' of the formed plate 28. With this, since the communicating holes 12 do not communicate between the first tube elements 4 and 4 which clamp the third tube element 6, heat exchanging medium does not flow through. The fourth tube element 7, which is provided at a position that is fourth toward the end plate 3 from the central tube element 4, is constituted by bonding flush to each other the formed plate 11, shown in FIG. 4, and a formed plate 30, shown in FIG. 8, which is provided with a communicating hole 12 and a flat plate portion 13b that does not have a distended portion for tank formation. The fifth tube element 7', which is provided at the sixth position toward the end plate 3 from the central tube element 4, is constituted by bonding flush to each other the formed plate 11 shown in FIG. 4 and a formed plate 31, shown in FIG. 9, which is provided with a communicating hole 12 and a flat plate portion 13b that does not have a distended portion for tank formation. In other words the fifth tube element 7' is a mirror image of the fourth tube element 7. The fourth tube element 7 is constituted by bonding the formed plate 30 and the formed plate 11 flush to each other and the fifth tube element 7' is constituted by bonding the formed plate 31 and the formed plate 11 flush to each other. As shown in FIG. 2, half-tanks 13''' are formed in the fourth tube element 7 and the fifth tube element 7'. The sixth tube element 8, which is provided between the fourth tube element 7 and the fifth tube element 7' is constituted by bonding the formed plate 30 and the formed plate 31 flush to each other. By bonding these formed plates 30 and 31 flush to each other, a straight flat plate 32, which is provided with no tanks but is provided only with a communicating hole 12, is formed toward the front surface in the direction of the air flow at the sixth tube element 8, as shown in FIG. 2. Note that the seventh tube element 9 is constituted by blocking off the formed plate 11 with a flat plate. Consequently, when the core of the heat exchanger is formed by laminating the first tube elements 4, the second tube element 5, the third tube element 6, the fourth tube element 7, the fifth tube element 7' and the sixth tube element 8 alternately with the fins 10 over a plurality of levels, and by providing the seventh tube element 9 and the end plates 2 and 3 at the two ends, a passage 35 that extends in the direction of the lamination is formed and also, two spaces, to be explained below, which enclose two intake / outlet portions 40a, 40b are formed. The intake / outlet portions 40a and 40b are constituted by bonding together the four plates for intake / outlet portion formation 41, 42, 43 and 44, which form an approximate L-shape, in that order in the direction of the lamination. As shown in FIGs. 10A and 10B, the plate for intake / outlet portion formation 41 is provided with a distended portion for passage formation 45 that is, in turn, provided with a communicating hole 12 located toward the bottom portion to communicate with the communicating hole 12 of the fourth tube element 7 and it is also provided with a brazing margin 46 to come in contact with the plate for intake / outlet portion formation 42 at its peripheral edge. The plate for intake / outlet portion formation 42 is formed approximately symmetrically to the plate for intake / outlet portion formation 41 as shown in FIGs. 10C and 10D, except that its distended portion for passage formation 47 becomes deeper toward the top and another communicating hole 48 is formed toward the upper end of the distended portion for passage formation 47. A heat exchanging medium passage 53 is formed when the plate for intake / outlet portion formation 41 and the plate for intake / outlet portion formation 42 are abutted flush to each other. This heat exchanging medium passage 53 has a width which allows its lower end portion to fit between the fourth tube element 7 and the sixth tube element 8 while its upper end portion distends toward the end plate 3 rather than toward the sixth tube element 8. The plate for intake / outlet portion formation 43, as shown in FIGs. 10E and 10F, is provided with a distended portion 50 with an intake / outlet hole 49 and a distended portion for passage formation 52 with an intake / outlet hole 51. At the lower end of the distended portion for passage formation 52, a communicating hole 12'' is provided, which communicates with the communicating hole 12 of the fourth tube element 7. As shown in FIGs. 10G and 10H, the plate for intake / outlet portion formation 44 is an approximately flat plate, which blocks off the distended portion for passage formation 52 of the plate for intake / outlet portion formation 43. The plate for intake / outlet portion formation 44 is provided with a communicating hole 48 for communicating between the intake / outlet hole 49 of the plate for intake / outlet portion formation 43 and the communicating hole 48 of the plate for intake / outlet portion formation 42, and a fitting hole 57, into which the relay pipe to be described below, is fitted. However, it is not provided with a communicating hole 12. A heat exchanging medium passage 54 is formed when the plate for intake / outlet portion formation 43 and the plate for intake / outlet portion formation 44 are bonded flush to each other. This heat exchanging medium passage 54 has a width which allows its lower end portion to fit between the sixth tube element 8 and the fifth tube element 7'. Consequently, when the intake / outlet portions 40a and 40b are assembled, the intake / outlet hole 49, the distended portion 50 and the heat exchanging medium passage 53 communicate with the tank 13''' of the fourth tube element 7, and the intake / outlet hole 51 and the heat exchanging medium passage 54 communicate with the tank 13''' of the fifth tube element 7'. Note that a block-type mounting plate for an expansion valve (not shown) can be connected on the side where the intake / outlet holes 49 and 51 of the intake / outlet portion 40a are provided. In the structure described above, the laminated heat exchanger 1 is divided by the separated tanks 13 and 14, into an intake / outlet tank group 100 and a non intake / outlet tank group 200. The intake / outlet tank group 100 is further divided into three tank sub groups A, B and C by the third tube element 6 which is provided with a non communicating portion and the plate for intake / outlet portion formation 44. Note that the non intake / outlet tank group 200 constitutes one tank group with all the tanks 14 communicating with one another. As a result, since the intake / outlet tank group 100 is divided into three portions and the non intake / outlet tank group 200 is in communication throughout, the heat exchanging medium passage is also divided into three heat exchanging medium passage sub groups E, F and G. By giving the laminated heat exchanger 1 such a split structure, heat exchanging medium flowing in from the intake / outlet hole 51 travels through two major flow paths. The first flow path for the heat exchanging medium has the heat exchanging medium flowing in from the intake / outlet hole 51 and then being sent from the heat exchanging medium passage 54 to the tank sub group A, which is partitioned by a great number of first tube elements 4 and the plate for intake / outlet portion formation 44 of the intake / outlet tank group 100. In this first path, the heat exchanging medium then travels upward through the heat exchanging medium passage sub group E of the first tube elements 4 constituting the tank sub group A. Then it travels downward before reaching the left end of the non intake / outlet tank group 200. Since this non intake / outlet tank group 200 constitutes one tank group, the heat exchanging medium that has flowed in, travels inside the tanks to reach the center, and then from the tank group between the third tube element 6 and the sixth tube element 8, travels upward through the heat exchanging medium passage sub group F. It then travels downward before reaching the tank sub group B of the intake / outlet tank group 100. The tank sub group B is provided with the intake / outlet hole 49 of the intake / outlet portion 40b and the heat exchanging medium flows out through this intake / outlet hole 49. Now, the flow of heat exchanging medium through the second flow path has the heat exchanging medium flowing in from the intake / outlet hole 51, and then travelling through the relay pipe 60 from the heat exchanging medium passage 54 to enter the tank sub group C which is partitioned by the third tube element 6. The heat exchanging medium that has entered the tank sub group C first travels upward and then downward through the heat exchanging medium passage sub group G, and reaches the right end of the non intake / outlet tank group 200. The heat exchanging medium which has thus flowed into the non intake / outlet tank group 200 flows through the tanks until it reaches the center. It then joins the first flow path of heat exchanging medium described earlier and, together, they travel first upward and then downward through the heat exchanging medium passage sub group F before reaching the tank sub group 13 of the intake / outlet tank group 100, to flow out through the intake / outlet hole 49. This means that the flow of heat exchanging medium constitutes a so-called 6-pass flow. While the explanation has been given with the assumption that the heat exchanging medium flows in through the intake / outlet hole 51 and out through the intake / outlet hole 49, the flow is not limited to that direction. The heat exchanging medium may enter through the intake / outlet hole 49 and flow out through the intake / outlet hole 51. In that case, the flow of the heat exchanging medium will run in the opposite direction from the arrows in FIG. 11. Next, as a second embodiment of the present invention, the laminated heat exchanger 1 which is structured so that the two flows of heat exchanging medium run separately from beginning to end, effected by using an eighth tube element 58, is explained in reference to FIGs. 12 - 14. Note that the structures of the first through seventh tube elements, the end plates, the intake / outlet portions and the relay pipe are identical to those described earlier, and that the same reference numbers are assigned to them. Therefore, their explanation is omitted here. As shown in FIG. 12, the eighth tube element 58 is provided, for instance, at a central position in the direction of lamination, and is structured by bonding the formed plate 11, shown in FIG. 4, and a formed plate 56, shown in FIG. 13, flush to each other. The formed plate 56 is provided in such a manner that it is positioned at the center in the direction of lamination of the laminated heat exchanger 1 and its basic form is similar to that of the formed plate 11 except that it is provided with no communicating hole 12 at the distended portion for tank formation 14a but is provided with a shallow impression. In other words, it is a mirror image of the third tube element 6 described earlier. The eighth tube element 58 is constituted by abutting the formed plate 56 and the formed plate 11 flush to each other, and toward its lower end, the tanks 13 are formed from the distended portions for tank formation 13a and 13a, which face opposite each other and a blind tank 14' is constituted from the distended portion for tank formation 14a of the formed plate 11 and the distended portion for tank formation 14a' of the formed plate 56. With this, since the communicating holes 12 do not communicate between the first tube elements 4 and 4, which clamp the eighth tube element 58, the non intake / outlet tank group 200 is divided into two parts and the heat exchanging medium does not flow between the tank sub groups H and J. With the structure described above, in addition to the structural features of the laminated heat exchanger 1 in the earlier embodiment, the non intake / outlet tank group 200 is divided into two parts; the left and the right tank sub groups, with the eighth tube element 58 at the center. Consequently, the heat exchanging medium passage group F is divided into two heat exchanging medium passage sub groups F 1 and F 2 to ensure that the two flows of the heat exchanging medium flow entirely separately until the end. The first flow path for heat exchanging medium has the heat exchanging medium flowing in from the intake / outlet hole 51 and then being sent from the heat exchanging medium passage 54 to the tank sub group A, which is partitioned by a great number of first tube elements 4 and the plate for intake / outlet portion formation 44 of the intake / outlet tank group 100. In this first path, the heat exchanging medium then travels upward through the heat exchanging medium passage group E of the first tube elements 4 constituting the tank sub group A and then it travels downward before reaching the left end of the non intake / outlet tank group 200. The non intake / outlet tank group 200 is partitioned by the eighth tube element 58 and the heat exchanging medium travels upward from one of the tank sub groups H through the heat exchanging medium passage sub group F 1 then downward to reach the tank sub group B of the intake / outlet tank group 100. The heat exchanging medium that has reached the tank sub group B then flows out through the intake / outlet portion 40b. Now, the flow of heat exchanging medium through the second flow path has the heat exchanging medium flowing in from the intake / outlet hole 51, and then travelling through the relay pipe 60 from the heat exchanging medium passage 54 to enter the tank sub group C, which is partitioned by the third tube element 6. The heat exchanging medium that has entered the tank sub group C then travels first upward and then downward through the heat exchanging medium passage group G, and enters the tank sub group J at the right end of the non intake / outlet tank group 200. Once out of the tank sub group J, the heat exchanging medium travels upward and then downward through the heat exchanging medium passage group F 2 before reaching the tank sub group B of the intake / outlet tank group 100, where it joins the first flow of the heat exchanging medium described earlier to flow out through the intake / outlet portion 40b. In this manner, a so-called 8-pass flow is effected. Note that, while, in this embodiment, too, the heat exchanging medium flows in through the intake / outlet hole 51 and out through the intake / outlet hole 49, the flow path is not limited to that direction. The heat exchanging medium may enter through the intake / outlet hole 49 and flow out through the intake / outlet hole 51. In that case, the flow of the heat exchanging medium will run in the opposite direction from the arrows in FIG. 14. Furthermore, the intake / outlet portions 40a and 40b described earlier do not necessarily have to be constituted by bonding the plates for intake / outlet portion formation 41, 42, 43 and 44 in that order. Although not shown in the figures, the intake / outlet portions 40a and 40b with the plates for intake / outlet portion formation 41' through 44' which are actually the plates for intake / outlet portion formation 41 through 44 facing the opposite direction, may be used. Note that the structure is identical to that disclosed in the first embodiment except for the assembling direction of the intake / outlet portions 40a and 40b. The same reference numbers are assigned to identical parts and their explanation is omitted. Moreover, instead of assembling the four plates for intake / outlet portion formation 41 through 44 for the intake / outlet portions 40a and 40b, separate intake / outlet portions may be structured, as shown in FIGs. 15 and 16, i.e., an intake / outlet portion 61a, formed by bonding the plates for intake / outlet portion formation 62 and 63 flush to each other and an intake / outlet portion 61b formed by bonding the plates for intake / outlet portion formation 64 and 65 flush to each other. In that case, the intake / outlet portion 61b must have an extended end projecting to the passage 35 to accommodate bonding to the relay pipe 60 and also must have a fitting hole toward the relay pipe though this ist not illustrated. As has been explained, according to the present invention, a six- or eight-pass flow of the heat exchanging medium is formed overall, and the heat exchanging medium is made to flow along two separate paths from the intake to the outlet. As a result, the area where the heat exchanging medium flows is expanded compared to the 4-pass flow system in the prior art, ensuring that the heat exchanging medium reaches every part of the laminated heat exchanger, improving the heat exchanging efficiency and, as a result, enhancing the performance of the heat exchanger.

Claims: Laminated heat exchanger (1) comprising a plurality of tube elements (4, 5, 6, 7, 7', 8, 9, 58), each of which is formed by fitting together a pair of formed plates and each of which is provided with a pair of tanks (13, 13', 13", 13"', 14, 14') at one end thereof and a heat exchanging medium passage (20) communicating between the pair of tanks (13, 13', 13", 13"', 14, 14'), and a plurality of fins (10) laminated alternately with the tube elements (4, 5, 6, 7, 7', 8, 9, 58) over a plurality of levels, wherein a pair of tank groups comprising an intake / outlet tank group (100) and a non intake / outlet tank group (200) is constituted by laminating the pair of tanks (13, 13', 13", 13"', 14, 14'), wherein the intake / outlet tank group (100) is divided into tank sub groups (A, B, C), which are connected to intake / outlet portions (40a, 40b, 61a, 61b), characterized in that the intake / outlet tank group (100) is divided into three tank sub groups (A, B, C) by two non communicating portions (6, 44), and that one intake / outlet portion (40a, 61a) is provided in one of the three tank sub groups (A, B, C) located at one end of the intake / outlet tank group (100) and is connected to the other of the three tank sub groups (A, B, C) located at the other end of the intake / outlet tank group (100) via a relay means (60), and another intake / outlet portion (40b, 61b) is provided in the tank sub group (B) located in a center of the intake / outlet tank group (100). Laminated heat exchanger according to claim 1, characterized in that the tanks (14) of the non intake / outlet tank group (200) are interconnected without any partitions. Laminated heat exchanger according to claim 2, characterized in that separate flow paths of heat exchanging medium are provided from one intake / outlet portion (40a, 61a) into the tank sub groups (A, C) at both ends of the intake / outlet tank group (100), wherein the flow paths then extend upwards through heat exchanging medium passages (20) of tube elements (4, 5, 6, 7, 7', 8, 9, 58) connected to the intake / outlet tank sub groups (A, C) and constituting passage sub groups (E, G) and downwards through these heat exchanging medium passages (20) and are joined at the non intake / outlet tank group (200) to extend upwards through heat exchanging medium passages (20) of tube elements (4, 5, 6, 7, 7', 8, 9, 58) connected to the central tank sub group (B) and constituting a passage sub group (F) and downwards through these heat exchanging medium passages (20) for reaching the central tank sub group (B) being connected to the other intake / outlet portion (40b, 61b). Laminated heat exchanger according to claim 1, characterized in that the non intake / outlet tank group (200) is divided into two tank sub groups (H, J) by one non communicating portion provided in one tube element (58) which is located between the two non communicating portions (6, 44) of the intake / outlet tank group (100). Laminated heat exchanger according to claim 4, characterized in that separate flow paths of heat exchanging medium are provided from one intake / outlet portion (40a, 61a) into the tank sub groups (A, C) at both ends of the intake / outlet tank group (100), wherein the flow paths then extend upwards through heat exchanging medium passages (20) of tube elements (4, 5, 6, 7, 7', 8, 9, 58) connected to the intake / outlet tank sub groups (A, C) and constituting passage sub groups (E, G) and downwards through these heat exchanging medium passages (20) into the tank sub groups (H, J) of the non intake / outlet tank group (200) to extend upwards through heat exchanging medium passages (20) of tube elements (4, 5, 6, 7, 7', 8, 9, 58) connected to the central tank sub group (B) and constituting passage sub groups (F1, F2) and downwards through these heat exchanging medium passages (20) into the central tank sub group (B) being connected to the other intake / outlet portion (40b, 61b). Laminated heat exchanger according to any one of the preceding claims, characterized in that the intake / outlet portions (40a, 40b, 61a, 61b) are each constituted by bonding two roughly L-shaped plates (41 - 44, 41' - 44', 62 - 65) for intake / outlet portion formation and by providing these plates (41 - 44, 41' - 44', 62 - 65) bonded between the tube elements (4, 5, 6, 7, 7', 8, 9, 58) in the intake / outlet tank group (100) in a clamped condition. Laminated heat exchanger according to any one of the preceding claims, characterized in that the intake / outlet portions (40a, 40b) are adjacent to each other, wherein one intake / outlet portion (40a) is provided with two intake / outlet holes (49, 51), in which heat exchanging medium can flow in or out, and with a heat exchanging medium passage (52) for interconnecting the intake / outlet tank sub groups (A, C) with an intake / outlet hole (51) on a coolant inflow side, and wherein the other intake / outlet portion (40b) is provided with a communicating hole (48), which communicates with the intake / outlet hole (49). on the coolant outflow side of the one intake / outlet portion (40a), and with a heat exchanging medium passage (47) for interconnecting the other intake / outlet tank sub group (B) with the communicating hole (48).

Inventors: INOUE SEIJI, KINUGASA TAKASHI, NISHIHITA KUNIHIKO, INOUE, SEIJI, KINUGASA, TAKASHI, NISHIHITA, KUNIHIKO, Inoue, Seiji, c/o Zexel Corp. Konan Factory, Kinugasa, Takashi, c/o Zexel Corp. Konan Factory, Nishihita, Kunihiko, c/o Zexel Corp. Konan Factory
Applicants: ZEXEL CORP, ZEXEL CORPORATION
Application year: 1995
Main classification: F28D1
IPC codes: F28F9, F25B39, F28D1