IP Library Granted Patent US 11,226,158
Granted Patent B2
US 11,226,158 · App. 16/371,392 · Granted Jan 18, 2022

Heat exchanger fractal splitter

Inventor: James Streeter (Torrington, CT)
Assignee: HAMILTON SUNDSTRAND CORPORATION
F28D1/0246F28D1/047
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Quick Facts
Patent No.
US 11,226,158
App. No.
16/371,392
Granted
Jan 18, 2022
Kind
B2
Abstract

A flow manifold for a heat exchanger core includes a number of fractal flow splitters arranged in a grid pattern of layers each fluidly connected to a corresponding first circuit layer, a flow plenum having a number of flow channels that are fluidly connected to an associated fractal flow splitter, one or more flow dividing vanes located in each flow channel thereby dividing the associated flow channel into two or more sub-channels, and an outer manifold surrounding the fractal flow splitters and configured to direct a first circuit flow into or out of the heat exchanger core. Each fractal flow splitter has an open end and a plenum end, and provides a transition from the open end to the flow plenum.

Claims (40)

1. A flow manifold for a heat exchanger core, the heat exchanger core comprising alternating first circuit layers and second circuit layers, the flow manifold comprising:

a plurality of fractal flow splitters arranged in a grid pattern that comprises a plurality of vertical layers, each of the plurality of vertical layers fluidly connected to a corresponding first circuit layer, wherein two or more of the plurality of fractal flow splitters are in each vertical layer;

a plurality of flow channels, each flow channel being fluidly connected to an associated fractal flow splitter;

a plurality of flow dividing vanes, each disposed within a flow channel and configured to divide the associated flow channel into two or more sub-channels; and

an outer manifold surrounding the plurality of fractal flow splitters and configured to direct a first circuit flow into, or out of, the flow manifold;

wherein:

each of the plurality of fractal flow splitters defines an open end and a plenum end, and is configured to provide a transition from the open end to one of the plurality of fluid flow channels;

each of the plurality of fractal flow splitters is configured to direct a portion of the first circuit flow toward, or away from, one or more of the plurality of flow dividing vanes, thereby directing flow into, or away from, the two or more sub-channels;

each of the plurality of fractal flow splitters defines a flow splitter length;

the flow splitter length ranges from 0.03-0.5 inch (0.8-13 mm);

each of the plurality of flow dividing vanes at least partially enters the corresponding fractal flow splitter, defining an entrance length;

a ratio of the entrance length to the flow splitter length defines a protrusion ratio;

the protrusion ratio ranges from 10-80%;

each of the open ends has a circular, oval, oblong, or elliptical shape;

two adjacent first circuit layers define a vertical spacing; and

the vertical spacing ranges from 0.075-0.5 inch (1.9-13 mm).

2. The flow manifold of claim 1 , wherein:

the heat exchanger core defines a first circuit flow axis;

the flow manifold defines a manifold flow axis;

the flow manifold changes a direction of the first circuit flow from the manifold flow axis to the first circuit flow axis by an angle that ranges from 0-120 deg.

3. The flow manifold of claim 2 , wherein the flow manifold changes the direction of the first circuit flow from the manifold flow axis to the first circuit flow axis by an angle that is about 90 deg.

4. The flow manifold of claim 1 , wherein the vertical spacing ranges from 0.2-0.3 inch (5-7.5 mm).

5. The flow manifold of claim 1 , wherein:

the flow channel defines a flow channel width; and

the flow channel width ranges between 0.03-0.5 inch (0.8-13 mm).

6. The flow manifold of claim 5 , wherein the flow channel width ranges from 0.08-0.125 inch (2-3.2 mm).

7. The flow manifold of claim 1 , wherein:

the fractal flow splitter open end defines an outside diameter (OD); and

the outside diameter ranges from 0.04-0.5 inch (1-13 mm).

8. The flow manifold of claim 7 , wherein the outside diameter ranges from 0.06-0.1 inch (1.5-2.5 mm).

9. The flow manifold of claim 1 , wherein:

the flow dividing vane defines a vane thickness; and

the vane thickness ranges from 0.003-0.2 inch (0.08-5 mm).

10. The flow manifold of claim 1 , comprising one or more materials selected from the group consisting of: nickel, aluminum, titanium, copper, iron, cobalt, and alloys thereof.

11. The flow manifold of claim 1 , wherein the protrusion ratio ranges from 30-60%.

12. The flow manifold of claim 1 , wherein:

the heat exchanger core comprises a plurality of core channels;

each of the plurality of core channels has a sinuous shape defining a peak-to-peak amplitude and a wavelength; and

a ratio of the peak-to-peak amplitude to wavelength ranges from 0.05-0.3.

13. A heat exchanger, comprising at least one of the flow manifolds of claim 1 .

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 1, 2019
From: STREETER, JAMES
To: HAMILTON SUNDSTRAND CORPORATION
Reel/Frame 048753/0762 →
Continuity (1)
Related Publication 20200309459A1 · Oct 1, 2020
Cited By (2)
US 12,516,893 US 12,624,899