IP Library Granted Patent US 11,619,427
Granted Patent B2
US 11,619,427 · App. 17/885,168 · Granted Apr 4, 2023

Heat exchanger and heat pump system having same

Inventors: Yutaka Shibata (Osaka, JP); Mitsuharu Numata (Osaka, JP); Tomoki Hirokawa (Osaka, JP); Hirokazu Fujino (Osaka, JP)
Assignee: DAIKIN INDUSTRIES, LTD.
F25B39/00F28D9/00F28F9/22F28F2260/02
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Quick Facts
Patent No.
US 11,619,427
App. No.
17/885,168
Granted
Apr 4, 2023
Kind
B2
Abstract

A heat exchanger includes: first layers each including first flow channels that are microchannels; and second layers each including second flow channels that are microchannels. The first layers and the second layers constitute a lamination. Heat is exchanged by performing either of: liquid evaporation in the first flow channels and gas condensation in the second flow channels, or liquid evaporation in the second flow channels and gas condensation in the first flow channels. The lamination includes: a first liquid transport pore that is in fluid communication with the first flow channels; and a second liquid transport pore that is in fluid communication with the second flow channels.

Claims (41)

1. A heat exchanger, comprising:

first layers each comprising first flow channels that are microchannels; and

second layers each comprising second flow channels that are microchannels, wherein

the first layers and the second layers constitute a lamination,

heat is exchanged by performing either of:

liquid evaporation in the first flow channels and gas condensation in the second flow channels, or

liquid evaporation in the second flow channels and gas condensation in the first flow channels,

the lamination comprises:

a first liquid transport pore that is in fluid communication with the first flow channels; and

a second liquid transport pore that is in fluid communication with the second flow channels,

in a case where the liquid evaporation is performed in the first flow channels,

the heat exchanger comprises a distribution member in the first liquid transport pore,

the distribution member:

uniformly distributes a fluid containing a liquid as an evaporation source to the first layers,

has a gap, along a longitudinal direction of the distribution member, between the distribution member and the first liquid transport pore that comprises one end constituting a fluid inlet section for the fluid, and

is a tubular member that is sealed at both ends and that comprises:

a returning pore at a proximal position that is proximal to a proximal end of the distribution member to the fluid inlet section along the longitudinal direction; and

a redirecting pore at a distal position that is proximal to a distal end of the distribution member from the fluid inlet section along the longitudinal direction, and

in a case where the liquid evaporation is performed in the second flow channels,

the heat exchanger comprises a distribution member in second liquid transport pore,

the distribution member:

uniformly distributes a fluid containing a liquid as an evaporation source to the second layers,

has a gap, along a longitudinal direction of the distribution member, between the distribution member and the second liquid transport pore that comprises one end constituting a fluid inlet section for the fluid, and

is a tubular member that is sealed at both ends and that comprises:

a returning pore at a proximal position that is proximal to a proximal end of the distribution member to the fluid inlet section along the longitudinal direction; and

a redirecting pore at a distal position that is proximal to a distal end of the distribution member from the fluid inlet section along the longitudinal direction.

2. The heat exchanger according to claim 1 , wherein an opening area of the returning pore is smaller than an opening area of the redirecting pore.

3. The heat exchanger according to claim 1 , wherein the first flow channels and the second flow channels extend in a horizontal direction.

4. The heat exchanger according to claim 1 , wherein each of fluids flowing in the first layers and the second layers is a CFC refrigerant or a natural refrigerant, independently.

5. The heat exchanger according to claim 2 , wherein the first flow channels and the second flow channels extend in a horizontal direction.

6. The heat exchanger according to claim 2 , wherein each of fluids flowing in the first layers and the second layers is a CFC refrigerant or a natural refrigerant, independently.

7. The heat exchanger according to claim 3 , wherein each of fluids flowing in the first layers and the second layers is a CFC refrigerant or a natural refrigerant, independently.

8. The heat exchanger according to claim 5 , wherein each of fluids flowing in the first layers and the second layers is a CFC refrigerant or a natural refrigerant, independently.

9. A heat pump system comprising the heat exchanger according to claim 1 .

10. A heat pump system comprising the heat exchanger according to claim 2 .

11. A heat pump system comprising the heat exchanger according to claim 3 .

12. A heat pump system comprising the heat exchanger according to claim 4 .

13. A heat pump system comprising the heat exchanger according to claim 5 .

14. A heat pump system comprising the heat exchanger according to claim 6 .

15. A heat pump system comprising the heat exchanger according to claim 7 .

16. A heat pump system comprising the heat exchanger according to claim 8 .

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2022
From: SHIBATA, YUTAKA; NUMATA, MITSUHARU; HIROKAWA, TOMOKI; FUJINO, HIROKAZU
To: DAIKIN INDUSTRIES, LTD.
Reel/Frame 060920/0550 →
Priority Claims (1)
JP JP2020-021017 · Feb 10, 2020 · national
Continuity (2)
Continuation PCTJP2021004960 · Feb 10, 2021
Related Publication 20220381487A1 · Dec 1, 2022