Heat exchanger

Patent metadata

Field	Value
Publication number	US-9689620-B2
Application number	US-201013382989-A
Country	US
Kind code	B2
Filing date	Jul 9, 2010
Priority date	Jul 14, 2009
Publication date	Jun 27, 2017
Grant date	Jun 27, 2017

Abstract

Disclosed is a heat exchanger that can more efficiently transfer heat between a heat-exchange fluid and an object with which heat is to be exchanged. A heat exchanger ( 1 ) can transfer heat between a heat-exchange fluid flowing through flow paths (R 1 ) and a fluid with which heat is to be exchanged flowing through other flow paths (R 2 ) by means of the flow path structure member ( 10 ) (a first metal sheet ( 11 ) and a second metal sheet ( 12 )) in which the flow paths (R 1 and R 2 ) are formed. The flow paths (R 1 and R 2 ) are formed so that the side surfaces thereof are not straight and so that the depths thereof change along the flow direction.

First claim

The invention claimed is:

1. A heat exchanger for performing heat exchange between a heat-exchange fluid flowing through a flow path having a pair of opposing side surfaces and a heat-exchange object located outside the flow path, wherein
the pair of opposing side surfaces of the flow path are formed with alternating pairs of recessed portions and pairs of protruding portions,
the flow path is further formed by a planar surface positioned between a pair of the pairs of recessed portions and extending downstream along the flow path from the pair of recessed portions to a position between a downstream pair of protruding portions of the pairs of protruding portions, and
the flow path being formed such that a distance between the downstream pair of protruding portions of the pair of side surfaces is narrower than a distance between the pair of recessed portions along a flow direction, and depths of the flow path at all locations between the pair of recessed portions, as measured from the planar surface at the position between the pair of recessed portions, is smaller than depths of the flow path at all locations between the downstream pair of protruding portions, as measured from the planar surface at the position between the downstream pair of the protruding portions of the pair of side surfaces.

2. The heat exchanger according to claim 1 , wherein the flow path is formed such that an area of a cross section orthogonal to the flow direction is constant.

3. The heat exchanger according to claim 1 , wherein the flow path is formed such that the alternating pairs of recessed portions and pairs of protruding portions of the opposing side surfaces are rectangular in shape.

4. A heat exchanger for performing heat exchange between a heat-exchange fluid flowing through a flow path having a pair of opposing side surfaces and a heat-exchange object located outside the flow path, wherein
the pair of opposing side surfaces of the flow path are formed with alternating pairs of recessed portions and pairs of protruding portions,
the flow path is further formed by a planar surface positioned between a pair of the pairs of recessed portions and extending downstream along the flow path from the pair of recessed portions to a position between a downstream pair of protruding portions of the pairs of protruding portions, and
the flow path being formed such that a distance between the downstream pair of protruding portions of the pair of side surfaces is narrower than a distance between the pair of recessed portions along a flow direction, a depth of the flow path between the pair of recessed portions, as measured from the planar surface at the position between the pair of recessed portions, is smaller than a depth of the flow path between the downstream pair of protruding portions, as measured from the planar surface at the position between the downstream pair of the protruding portions of the pair of side surfaces, and a change from the distance between the pair of recessed portions to the narrower distance between the protruding portions occurs at a common location where the depth changes from the smaller depth between the protruding portions to the depth between the downstream protruding portions.

5. The heat exchanger according to claim 4 , wherein the flow path is formed such that an area of a cross section orthogonal to the flow direction is constant.

6. The heat exchanger according to claim 4 , wherein the flow path is formed such that the alternating pairs of recessed portions and pairs of protruding portions of the opposing side surfaces are rectangular in shape.

Assignees

• Yamada Sayaka
• Higashi Yasuo
• Nishimura Makoto
• Yoshida Tatsuo
• Noishiki Koji
• Kobe Steel Ltd

Inventors

• Yamada Sayaka
• Higashi Yasuo
• Nishimura Makoto
• Yoshida Tatsuo
• Noishiki Koji

Classifications

• F28D9/0037 Primary

  the conduits for the other heat-exchange medium also being formed by paired plates touching each other (F28D9/0043 takes precedence) · CPC title

• F28F13/02

  by influencing fluid boundary (boundary-layer control in general F15D) · CPC title

• F28F13/12

  by creating turbulence, e.g. by stirring, by increasing the force of circulation (F28F13/08 takes precedence) · CPC title

• F28F3/048

  in the form of ribs integral with the element or local variations in thickness of the element, e.g. grooves, microchannels · CPC title

• F28F13/08

  by varying the cross-section of the flow channels · CPC title