Heat exchanger

Patent metadata

Field	Value
Publication number	US-9625214-B2
Application number	US-201214360779-A
Country	US
Kind code	B2
Filing date	Nov 28, 2012
Priority date	Nov 30, 2011
Publication date	Apr 18, 2017
Grant date	Apr 18, 2017

Abstract

In a heat exchanger, a plate member of a tank portion includes a first fluid communication passage through which a first tank space communicates with first tubes, and a second fluid communication passage through which a second tank space communicates with second tubes. Either an upstream first tube group of the first tubes or a downstream first tube group of the first tubes, whichever is larger in a pressure loss of the first fluid, configures a higher pressure loss first tube group, and the other first tube group smaller in the pressure loss of the first fluid configures a lower pressure loss first tube group. A flow channel resistance between the higher pressure loss first tube group and the first tank space is smaller than a flow channel resistance between the lower pressure loss first tube group and the first tank space.

First claim

The invention claimed is:

1. A heat exchanger, comprising:
a heat exchange portion in which first tubes through which a first fluid flows and second tubes through which a second fluid flows are stacked, the heat exchange portion performing heat exchange among the first fluid, the second fluid and a third fluid;
a tank portion including:
an inlet side first tank space is connected to a first inlet pipe and communicates with the first tubes to distribute the first fluid to the first tubes, an outlet side first tank space is connected to a first outlet pipe and communicates with the first tubes to collect the first fluid from the first tubes, and
an inlet side second tank space is connected to a second inlet pipe and communicates with the second tubes to distribute the second fluid to the second tubes, an outlet side second tank space is connected to a second outlet pipe and communicates with the second tubes to collect the second fluid from the second tubes;
a third fluid passage formed between adjacent tubes of the first tubes and the second tubes, the third fluid flowing through the third fluid passage; and
an outer fin arranged in the third fluid passage, the outer fin facilitating heat exchange between the first fluid and the third fluid and heat exchange between the second fluid and the third fluid and enabling heat transfer between the first fluid flowing in the first tubes and the second fluid flowing in the second tubes, wherein
the heat exchange portion includes an upstream heat exchange portion, and a downstream heat exchange portion arranged downstream of the upstream heat exchange portion in a flow direction of the third fluid,
the first tubes are arranged in both the upstream heat exchange portion and the downstream heat exchange portion,
the second tubes are arranged in at least one of the upstream heat exchange portion or the downstream heat exchange portion,
one of the first tubes of the upstream heat exchange portion overlaps with one of the first tubes of the downstream heat exchange portion in the flow direction of the third fluid, and another of the first tubes of the downstream heat exchange portion overlaps with one of the second tubes of the upstream heat exchange portion in the flow direction of the third fluid,
the tank portion includes a plate member arranged to close the inlet side first tank space, the outlet side first tank space, the inlet side second tank space and the outlet side second tank space from a side of the first and second tubes,
the plate member is provided with a first fluid communication passage as a through-hole through which the inlet side first tank space and the outlet side first tank space communicates with the first tubes, and a second fluid communication passage as a through-hole through which the inlet side second tank space and the outlet side second tank space communicates with the second tubes,
the first tubes in the upstream heat exchange portion configures an upstream first tube group, and the first tubes in the downstream heat exchange portion configures a downstream first tube group,
either the upstream first tube group or the downstream first tube group, whichever is larger in pressure loss of the first fluid, configures a higher pressure loss first tube group,
either the upstream first tube group or the downstream first tube group, whichever is smaller in pressure loss of the first fluid, configures a lower pressure loss first tube group, and
a flow channel resistance between the higher pressure loss first tube group and the inlet side first tank space is smaller than a flow channel resistance between the lower pressure loss first tube group and the inlet side first tank space.

2. The heat exchanger according to claim 1 , wherein
the inlet side first tank space is arranged to be nearer to the higher pressure loss first tube group than to the lower pressure loss first tube group in the flow direction of the third fluid, and
the inlet side first tank space communicates with the higher pressure loss first tube group through a communication passage in the first fluid communication passage, and at least a part of an opening portion of the communication passage is opened toward the first tubes and is disposed to overlap with an opening end surface of the first tubes in a direction perpendicular to the opening end surface.

3. The heat exchanger according to claim 2 , wherein
the first tubes are arranged so that the first fluid flowing within the first tubes has a flow rate component in a direction of a gravitational force,
the first fluid is a refrigerant,
the first fluid which has been subjected to heat exchange with the third fluid at least once in the heat exchange portion is introduced into the inlet side first tank space, and
the inlet side first tank space is located on the higher pressure loss first tube group.

4. The heat exchanger according to claim 2 , being used as an evaporator that evaporates the first fluid, wherein
the outlet side first tank space is arranged to be nearer to the lower pressure loss first tube group side than to the higher pressure loss first tube group side in the flow direction of the third fluid.

5. The heat exchanger according to claim 1 , wherein
the number of the first tubes included in the higher pressure loss first tube group is smaller than that in the lower pressure loss first tube group.

6. The heat exchanger according to claim 1 , wherein
the higher pressure loss first tube group configures the upstream first tube group, and the lower pressure loss first tube group configures the downstream first tube group.

7. The heat exchanger according to claim 1 , wherein
the heat exchange portion has three or more first fluid paths, and each of the first fluid paths has one or more of the first tubes interposed between the inlet side first tank space and the outlet side first tank space,
the first fluid paths are coupled to each other in series in a flow pathway of the first fluid, and each of the first fluid paths allows the first fluid to flow therein oppositely in the direction of the gravitational force to adjacent another of the first fluid paths in the flow pathway,
the first fluid paths include an upward flow first fluid path in which the first fluid flows upward in the direction of the gravitational force, and
the upward flow first fluid path is smaller in stack width of the first tubes of the first fluid paths in the stacking direction of the first tubes than any other adjacent first fluid path in the flow pathway of the first fluid.

8. The heat exchanger according to claim 1 , wherein
the first fluid and the second fluid are heat media flowing in different fluid circulation circuits.

9. The heat exchanger according to claim 1 , being used as an evaporator that evaporates a refrigerant in a vapor compression refrigerant cycle, wherein
the first fluid is the refrigerant of the refrigerant cycle,
the second fluid is a heat medium which absorbs the quantity of heat that an external heat source possesses, and
the third fluid is air.

10. The heat exchanger according to claim 1 , being used as a condenser that condenses a refrigerant in a vapor compression refrigerant cycle, wherein
the first fluid is the refrigerant of the refrigerant cycle,
the second fluid is a heat medium which absorbs the quantity of heat that an external heat source possesses, and
the third fluid is air.

11. The heat exchanger according to claim 1 , being used for a vehicle cooling system, wherein
the first fluid is a heat medium which absorbs the quantity of heat that a first in-vehicle device associated with a heat generation during actuation possesses,
the second fluid is a heat medi

Assignees

• Denso Corp

Inventors

• Katoh Yoshiki

Classifications

• F28D1/0435

  Combination of units extending one behind the other (F28D1/0452 takes precedence) · CPC title

• F28D1/05366 Primary

  Assemblies of conduits connected to common headers, e.g. core type radiators · CPC title

• F28D1/05391

  with multiple rows of conduits or with multi-channel conduits combined with a particular flow pattern, e.g. multi-row multi-stage radiators · CPC title

• B60H1/00328

  of the liquid-air type · CPC title

• F28F2009/0287

  having passages for different heat exchange media · CPC title