Heat exchanger
View Patent ↗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. This is significantly advantageous when the heat exchanger is used as an evaporator of a vehicle air conditioning apparatus for which a reduction in the weight of the components and an increase in the performance are demanded.
1. A heat exchanger comprising:
a pair of cylindrical headers vertically arranged at an interval in a radial direction; and a plurality of flat tubes arranged at intervals in an axial direction of the headers, both ends of each of the tubes being connected to the respective headers, the heat exchanger further comprising a plurality of tube groups arranged in an air flow direction, the tube groups comprising the plurality of tubes including the headers at both ends, the heat exchanger exchanging heat of air flowing through a core section formed by the tube groups and heat of a heating medium flowing through a plurality of heating medium flow holes forming flow channels in each of the tubes, wherein
three headers and three tube groups are arranged in the air flow direction to form the core section,
when a width dimension of the tubes is defined as Tw, a flow channel cross-sectional area per tube is defined as S, and the number of heating medium flow holes per tube is defined as N,
the width dimension Tw of the tubes is equal to or greater than 5 mm and equal to or smaller than 11 mm,
N is 3≤N≤5 when 5 mm≤Tw≤6 mm, 4≤N≤5 when 6 mm<Tw≤7 mm, 5≤N≤6 when 7 mm<Tw≤8 mm, 5≤N≤7 when 8 mm<Tw≤9 mm, 6≤N≤8 when 9 mm<Tw≤10 mm, and 7≤N≤9 when 10 mm<Tw≤11 mm, and
the width dimension Tw of the tubes and the flow channel cross-sectional area S satisfy a relationship of −0.002470×Tw 5 +0.09542×Tw 4 −1.436×Tw 3 +10.50×Tw 2 −37.08×Tw+51.31≤S≤0.005616×Tw 5 −0.2314×Tw 4 +3.746×Tw 3 −29.70×Tw 2 +115.4×Tw−173.9.
2. The heat exchanger according to claim 1 , wherein
when a dimension of the core section in the air flow direction is defined as Fd, and an inner diameter of the headers is defined as D,
the dimension Fd of the core section in the air flow direction is equal to or greater than 30 mm and equal to or smaller than 50 mm, and
the dimension Fd of the core section in the air flow direction and the inner diameter D of the headers satisfy a relationship of 0.2081×Fd−1.2487≤D≤0.2081×Fd−0.4162.
3. The heat exchanger according to claim 1 , wherein
a gap between the headers adjacent to each other in the air flow direction among the headers is equal to or greater than 1 mm and equal to or smaller than 3 mm.
4. The heat exchanger according to claim 1 , further comprising
plate-shaped communication members arranged between the headers adjacent to each other in the air flow direction among the headers and configured to allow communication between the headers, wherein
a gap is formed between the headers according to a thickness of the communication members.
5. The heat exchanger according to claim 1 , wherein
the core section comprises first, second, and third tube groups sequentially arranged from the front, the heating medium entered from one end side in the axial direction of the header on one side in an up and down direction of the first tube group flows through the first tube group and flows into the header on another side in the up and down direction of the first tube group, the heating medium flown from the header on the other side in the up and down direction of the first tube group into a part of the header on the one side in the up and down direction of the second tube group flows through a part of the second tube group and flows into the header on the other side in the up and down direction of the second tube group, the heating medium flown into the header on the other side in the up and down direction of the second tube group flows through another part of the second tube group and flows into another part of the header on the one side in the up and down direction of the second tube group, the heating medium flown into the other part of the header on the one side in the up and down direction of the second tube group flows into the header on the one side in the up and down direction of the third tube group, the heating medium entered into the header on the one side in the up and down direction of the third tube group flows through the third tube group and flows into the header on the other side in the up and down direction of the third tube group, and the heating medium flows out from one end side in the axial direction of the header on the other side in the up and down direction of the third tube group.
6. The heat exchanger according to claim 3 , further comprising
plate-shaped communication members arranged between the headers adjacent to each other in the air flow direction among the headers and configured to allow communication between the headers, wherein
a gap is formed between the headers according to a thickness of the communication members.
7. The heat exchanger according to claim 3 , wherein
the core section comprises first, second, and third tube groups sequentially arranged from the front, the heating medium entered from one end side in the axial direction of the header on one side in an up and down direction of the first tube group flows through the first tube group and flows into the header on another side in the up and down direction of the first tube group, the heating medium flown from the header on the other side in the up and down direction of the first tube group into a part of the header on the one side in the up and down direction of the second tube group flows through a part of the second tube group and flows into the header on the other side in the up and down direction of the second tube group, the heating medium flown into the header on the other side in the up and down direction of the second tube group flows through another part of the second tube group and flows into another part of the header on the one side in the up and down direction of the second tube group, the heating medium flown into the other part of the header on the one side in the up and down direction of the second tube group flows into the header on the one side in the up and down direction of the third tube group, the heating medium entered into the header on the one side in the up and down direction of the third tube group flows through the third tube group and flows into the header on the other side in the up and down direction of the third tube group, and the heating medium flows out from one end side in the axial direction of the header on the other side in the up and down direction of the third tube group.
8. The heat exchanger according to claim 2 , wherein
a gap between the headers adjacent to each other in the air flow direction among the headers is equal to or greater than 1 mm and equal to or smaller than 3 mm.
9. The heat exchanger according to claim 2 , further comprising
plate-shaped communication members arranged between the headers adjacent to each other in the air flow direction among the headers and configured to allow communication between the headers, wherein
a gap is formed between the headers according to a thickness of the communication members.
10. The heat exchanger according to claim 2 , wherein
the core section comprises first, second, and third tube groups sequentially arranged from the front, the heating medium entered from one end side in the axial direction of the header on one side in an up and down direction of the first tube group flows through the first tube group and flows into the header on another side in the up and down direction of the first tube group, the heating medium flown from the header on the other side in the up and down direction of the first tube group into a part of the header on the one side in the up and down direction of the second tube group flows through a part of the second tube group and flows into the header on the other side in the up and down direction of the second tube group, the heating medium flown into the header on the other side in the up and down direction of the second tube group flows through another part of the second tube group and flows into another part of the header on the one side in the up and down direction of the second tube group, the heating medium flown into the other part of the header on the one side in the up and down direction of the second tube group flows into the header on the one side in the up and down direction of the third tube group, the heating medium entered into the header on the one side in the up and down direction of the third tube group flows through the third tube group and flows into the header on the other side in the up and down direction of the third tube group, and the heating medium flows out from one end side in the axial direction of the header on the other side in the up and down direction of the third tube group.