IP Library Granted Patent US 9,989,276
Granted Patent B2
US 9,989,276 · App. 14/255,419 · Granted Jun 5, 2018

Condensate drainage device for heat exchanger

Inventors: Karl P. Kroetsch (Williamsville, NY); Kenneth R. Handley, III (Lockport, NY); Sourav Chowdhury (Lockport, NY); Lawrence P. Scherer (Lockport, NY); Scott B. Lipa (Snyder, NY); David G. Schmidt (East Amherst, NY)
Assignee: MAHLE International GmbH
F24F13/222F25B39/04F25D21/14F28D1/05366F28F17/005F24F2013/227F25D2321/146
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Quick Facts
Patent No.
US 9,989,276
App. No.
14/255,419
Granted
Jun 5, 2018
Kind
B2
Abstract

A condensate drainage enhancing device is provided for an evaporator. An integrally molded plastic part snap fits around the conventional lower manifold, with rails maintained in tight engagement with the front and rear edges of the refrigerant flow tubes. These interrupt the meniscus films of columns of retained water that would otherwise form and, which instead drains down ribs that depend from the rails.

Claims (17)

1. A cross flow heat exchanger comprising:

a plurality of horizontally spaced, parallel and vertically oriented tubes configured to provide a fluid path for an inner fluid flowing at a temperature at which entrained water condenses out of air flowing across and between the tubes, the tubes having front edges being coplanar and rear edges being coplanar,

a lower horizontal manifold, into which the front edges and rear edges enter, the lower manifold oriented along a manifold axis with a tube to tube spacing causing condensed water to become entrapped in condensate columns of a height between the tubes with meniscus films on the lower manifold, presented to the front and rear tube edges, and

a condensate drainage enhancing device having

a horizontal first rail extending along the manifold axis at an uppermost height of the condensate drainage enhancing device and contacting the front edges of the tubes at a location below the height of the condensate columns and contacting the meniscus films, and,

a plurality of first drainage ribs depending below and downward from the first rail, evenly spaced apart from each other along the manifold axis by empty gaps, and oriented to extend away from the front edges to provide a drainage path for condensed water out of the columns,

a second horizontal rail at the uppermost height of the condensate drainage enhancing device, extending along the manifold axis and contacting the rear edges of the tubes at a location below the height of the condensate columns and having second drainage ribs depending below and downward from the second rail that are oriented to extend away from the rear edges,

wherein the first drainage ribs describe a curved path originating from the first rail outward in a direction away from the second drainage ribs.

2. The cross flow heat exchanger according to claim 1 ,

wherein the first drainage ribs that describe the curved path originating from the first rail and extending first outward in the direction away from the axis and from the second drainage ribs, then extend downward, and finally inward toward the second drainage ribs.

3. The cross flow heat exchanger according to claim 1 , further comprising a second horizontal rail, extending at the uppermost height along the axis on a second side opposite the first side parallel to the first rail, the second horizontal rail having second drainage ribs depending downward therefrom and below the second horizontal rail, wherein the second drainage ribs describe a curved path, originating from the second rail, first outward in a direction away from the first drainage ribs, then downward, and finally inward toward the first drainage ribs.

4. The cross flow heat exchanger according to claim 3 , in which the first and second drainage ribs depending from the first and second rails are joined at their lower ends to a central keel running parallel to and beneath the axis and spaced from the first and second rails by the first and second drainage ribs.

5. The cross flow heat exchanger according to claim 4 , in which the lower manifold that has a width greater than the distance between the first and second rails when the condensate drainage enhancing device is not attached to the tubes of the heat exchanger, and in which the drainage ribs are flexibly joined to the keel with a free state separation between the first drainage ribs and the second drainage ribs when the drainage device is not attached to the tubes of the heat exchanger, which is somewhat less than in an installed position so that the horizontal rails may snap fit over the lower manifold.

6. The cross flow heat exchanger according to claim 5 , in which at least one edge of the first or second drainage ribs is concave in cross section to enhance drainage.

7. The cross flow heat exchanger according to claim 4 , in which at least one edge of the first or second drainage ribs is concave in cross section to enhance drainage.

8. The cross flow heat exchanger according to claim 3 , in which at least one edge of the first or second drainage ribs is concave in cross section to enhance drainage.

9. The cross flow heat exchanger according to claim 1 , in which at least one edge of the first and second drainage ribs is concave in cross section to enhance drainage.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 29, 2016
From: DELPHI TECHNOLOGIES, INC.
To: MAHLE INTERNATIONAL GMBH
Reel/Frame 037640/0036 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 9, 2014
From: KROETSCH, KARL P.; HANDLEY, KENNETH R., III; CHOWDHURY, SOURAV; SCHERER, LAWRENCE P.; LIPA, SCOTT B.; SCHMIDT, DAVID G.
To: DELPHI TECHNOLOGIES, INC.
Reel/Frame 032855/0972 →
Continuity (1)
Related Publication 20150300680A1 · Oct 22, 2015