Subfreezing heat exchanger with separate melt fluid

Abstract

A heat exchanger includes a first side opposite a second side and a third side opposite a fourth side and a cold layer with an inlet at the first side of the heat exchanger, an outlet at the second side of the heat exchanger, and a cold passage extending from the inlet to the outlet. The heat exchanger also includes a hot layer with an inlet manifold at the third side of the heat exchanger extending between the first side and the second side, an outlet manifold at the fourth side of the heat exchanger opposite the inlet manifold and extending between the first side and the second side, a hot passage extending from the inlet manifold to the outlet manifold, and a tube on the first side of the heat exchanger extending from the third side to the fourth side.

Description

BACKGROUND

The present disclosure relates to heat exchangers, and in particular to plate-fin crossflow heat exchangers.

Heat exchangers are often used to transfer heat between two fluids. For example, in aircraft environmental control systems, heat exchangers may be used to transfer heat between a relatively hot air source (e.g., bleed air from a gas turbine engine) and a relatively cool air source (e.g., ram air). Some heat exchangers, often referred to as plate-fin heat exchangers, include a plate-fin core having multiple heat transfer sheets arranged in layers to define air passages there between. Closure bars seal alternating inlets of hot air and cool air inlet sides of the core. Accordingly, hot air and cool air are directed through alternating passages to form alternating layers of hot and cool air within the core. Heat is transferred between the hot and cool air via the heat transfer sheets that separate the layers. In addition, to facilitate heat transfer between the layers, each of the passages can include heat transfer fins, often formed of a material with high thermal conductivity (e.g., aluminum), that are oriented in the direction of the flow within the passage. The heat transfer fins increase turbulence and a surface area that is exposed to the airflow, thereby enhancing heat transfer between the layers.

In some applications, heat exchangers can be exposed to extremely cold temperatures. When a heat exchanger is exposed to extremely cold temperatures ice accretion can occur. When there is ice accretion on a heat exchanger the ice accretion can result in restricting airflow into or out of the heat exchanger, thereby increasing the pressure loss across the heat exchanger and decreasing heat transfer performance.

SUMMARY

In one example, a heat exchanger includes a first side opposite a second side and a third side opposite a fourth side. The third side and the fourth side extend from the first side to the second side. The heat exchanger also includes a cold layer with an inlet at the first side of the heat exchanger and an outlet at the second side of the heat exchanger. The cold layer also includes a cold passage extending from the inlet to the outlet. The heat exchanger also includes a hot layer with an inlet manifold at the third side of the heat exchanger extending between the first side and the second side and an outlet manifold at the fourth side of the heat exchanger opposite the inlet manifold and extending between the first side and the second side. The hot layer also includes a hot passage extending from the inlet manifold to the outlet manifold and a tube on the first side of the heat exchanger extending from the third side to the fourth side.

In another example, a heat exchanger includes a first side opposite a second side and a third side opposite a fourth side, wherein the third side and the fourth side extend from the first side to the second side. The heat exchanger also includes a cold layer with a first closure bar on the third side extending from the first side to the second side, a second closure bar on the fourth side extending from the first side to the second side, and a cold passage between the first closure bar and the second closure bar, wherein the cold passage includes an inlet on the first side. The heat exchanger also includes a hot layer adjacent the cold layer. The hot layer includes a third closure bar on the second side extending from the third side to the fourth side, a closure tube on the first side extending from the third side to the fourth side. The closure tube includes a heating fluid passage extending from the third side to the fourth side. The hot layer also includes a hot passage between the third closure bar and the closure tube. The hot passage includes an inlet on the third side and an outlet on the fourth side.

In another example, a method of preventing ice accretion on a cold inlet of a cold layer of a heat exchanger includes directing a cold flow through the cold inlet of the cold layer at a first side of the heat exchanger and out a cold outlet of the cold layer at a second side of the heat exchanger. The method also includes directing a hot flow through a hot inlet header of a hot layer at a third side of the heat exchanger and out the hot outlet header of the hot layer at the fourth side of the heat exchanger. The method also includes directing a heating fluid through a tube located on the first side of the heat exchanger. The heating fluid heats the cold inlet of the cold layer of the heat exchanger.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a perspective view of a core of a heat exchanger.

FIG. 2 is a schematic diagram of one example of a hot layer of the heat exchanger.

FIG. 3 is a schematic diagram showing another example of the hot layer of the heat exchanger.

DETAILED DESCRIPTION

The present disclosure relates to a heat exchanger. The heat exchanger includes a cold layer and a hot layer. The hot layer includes a closure tube with a heating fluid passage configured to prevent ice accretion on the inlet of the cold layer. The heat exchanger will be described below with reference to FIGS. 1-3.

FIG. 1 is a perspective view of an example of a core of heat exchanger 10. Heat exchanger 10 includes core 11. Core 11 includes first side 12, second side 14, third side 16, fourth side 18, first cold layer 20a, second cold layer 20b, first hot layer 40a, second hot layer 40b, and parting sheets (43a, 43b, 43c, 43d, and 43e). First cold layer 20a includes first cold inlet 22a, first cold outlet 24a, first lower closure bar 26a, second lower closure bar 28a, a plurality of first cold fins 30a, and first cold passages 32a. First hot layer 40a includes a plurality of first hot fins 45a, first hot passages 46a, third lower closure bar 48a, first closure tube 50a. First closure tube 50a includes first heating fluid passage 56a. Second cold layer 20b includes second cold inlet 22b, second cold outlet 24b, first upper closure bar 26b, second upper closure bar 28b, a plurality of second cold fins 30b, and second cold passages 32b. Second hot layer 40b includes a plurality of second hot fins 45b, second hot passages 46b, third upper closure bar 48b, second closure tube 50b. Second closure tube 50b includes second heating fluid passage 56b.

First cold layer 20a is adjacent to first hot layer 40a and first cold layer 20a is separated from first hot layer 40a by parting sheet 43b. First hot layer 40a is also adjacent to second cold layer 20b and first hot layer 40a is separated from second cold layer 20b by parting sheet 43c. Second cold layer 20b is also adjacent second hot layer 40b. Second cold layer 20b is separated from second hot layer by parting sheet 43d. Each of parting sheets (43b, 43c, and 43d) are configured to enable heat transfer between their contiguous and adjacent layers. Parting sheet 43a is adjacent to first cold layer 20a opposite of parting sheet 43b. Parting sheet 43e is adjacent to second hot layer 40b opposite of parting sheet 43d.

First cold inlet 22a and second cold inlet 22b of first cold layer 20a and second cold layer 20b, respectively, are on first side 12 and extend between third side 16 and fourth side 18 of core 11 of heat exchanger 10. First cold outlet 24a and second cold outlet 24b of first cold layer 20a and second cold layer 20b, respectively, are on second side 14 and extend between third side 16 and fourth side 18 of heat exchanger 10. First lower closure bar 26a and first upper closure bar 26b are on third side 16 and extend from first side 12 to second side 14. Second lower closure bar 28a and second upper closure bar 28b are opposite first lower closure bar 26a and first upper closure bar 26b, respectively, and are on fourth side 18 extending from first side 12 to second side 14. Plurality of first cold fins 30a and plurality of second cold fins 30b extend through first cold layer 20a and second cold layer 20b, respectively, between first end 12 and second end 14 and are spaced apart from each other between third side 16 and fourth side 18. First lower closure bar 26a, second lower closure bar 28a, plurality of first cold fins 30a, parting sheet 43a, and parting sheet 43b define first cold passages 32a. First upper closure bar 26b, second upper closure bar 28b, plurality of second cold fins 30b, parting sheet 43c, and parting sheet 43d define second cold passages 32b. First cold passages 32a and second cold passages 32b each extend between first side 12 and second side 14.

Third lower closure bar 48a and third upper closure bar 48b are on second side 14 and extend between third side 16 and fourth side 18. Third lower closure bar 48a is between parting sheet 43b and parting sheet 43c. Third upper closure bar 48b is between parting sheet 43d and parting sheet 43e. First closure tube 50a and second closure tube 50b are on first side 12, opposite of third lower closure bar 48a and third upper closure bar 48b, respectively, and extend between first side 12 and second side 14. First closure tube 50a is between parting sheet 43b and parting sheet 43c. First closure tube 50a functions as a closure bar for first hot layer 40a. Second closure tube 50b is between parting sheet 43d and parting sheet 43e. Second closure tube 50b functions as a closure bar for second hot layer 40b. Plurality of first hot fins 45a and plurality of second hot fins 45b are spaced between third lower closure bar 48a and third upper closure bar 48b and first closure tube 50a and second closure tube 50b, respectively, and extends between third side 16 and fourth side 18. Third lower closure bar 48a, first closure tube 50a, plurality of first hot fins 45a, parting sheet 43b, and parting sheet 43c define first hot passages 46a in first hot layer 40a. Third upper closure bar 48b, second closure tube 50b, plurality of second hot fins 45b, parting sheet 43d, and parting sheet 43e define second hot passages 46b in second hot layer 40b. In the example shown in FIG. 1, first hot passages 46a and second hot passages 46b are configured to direct hot airflow from third side 16 to fourth side 18. In another example, first hot passages 46a and second hot passages 46b can be configured to direct hot airflow from fourth side 18 to third side 16. All of core 11 of heat exchanger 10 is made from material(s) with high thermal conductivity to encourage heat transfer between cold layers (20a and 20b) and hot layers (40a and 40b).

As shown in FIG. 1, first hot layer 40a can be stacked between first cold layer 20a and second cold layer 20b, and second cold layer 20b can be stacked between first hot layer 40a and second hot layer 40b. In the example of FIG. 1, first closure tube 50a and second closure tube 50b are configured to prevent ice accretion on first cold inlet 22a and second cold inlet 22b of first cold layer 20a and second cold layer 20b, respectively. In another example, the number of cold layers and the number of hot layers can be modified to adjust the heat transfer capabilities of heat exchanger 10.

Core 11 of heat exchanger 10 is manufactured by stacking parting sheet 43a, first cold layer 20a, parting sheet 43b, first hot layer 40a, parting sheet 43c, second cold layer 20b, parting sheet 43d, second hot layer 40b, and parting sheet 43e, then brazing the layers together in a furnace. First cold layer 20a is made by placing first lower closure bar 26a on third side 16 and second lower closure bar 28a on fourth side 18. Then, the plurality of first cold fins 30a are spaced apart from each other between first lower closure bar 26a and second lower closure bar 28a and extending between first side 12 and second side 14. Parting sheet 43b is then placed on top of first lower closure bar 26a and second lower closure bar 28a to complete first cold layer 20a. Next, first hot layer 40a is made by placing third lower closure bar 48a on top of parting sheet 43b on second side 14 and extending between third side 16 and fourth side 18. Then, first closure tube 50a is placed on top of parting sheet 43b opposite of third lower closure bar 48a on first side 12 extending between third side 16 and fourth side 18. Plurality of first hot fins 45a are then placed on top of parting sheet 43b, spaced from one another between third lower closure bar 48a and first closure tube 50a and extending between third side 16 and fourth side 18. Parting sheet 43c is then placed atop third closure lower bar 48a, first closure tube 50a, and the plurality of first hot fins 45a to complete first hot layer 40a. Second cold layer 20b is made by placing first upper closure bar 26b on third side 16 and second upper closure bar 28b on fourth side 18. Then, the plurality of second cold fins 30b are spaced apart from each other between first upper closure bar 26b and second upper closure bar 28b and extending between first side 12 and second side 14. Parting sheet 43d is then placed on top of first upper closure bar 26b and second upper closure bar 28b to complete second cold layer 20b. Next, second hot layer 40b is made by placing third upper closure bar 48b on top of parting sheet 43d on second side 14 and extending between third side 16 and fourth side 18. Then, second closure tube 50b is placed on top of parting sheet 43d opposite of third upper closure bar 48b on first side 12 extending between third side 16 and fourth side 18. The plurality of second hot fins 45b are then placed on top of parting sheet 43d, spaced from one another between third upper closure bar 48b and second closure tube 50b and extending between third side 16 and fourth side 18. Parting sheet 43e is then placed atop third lower closure bar 48a, first closure tube 50a, and the plurality of first hot fins 45a to complete first hot layer 40a. Core 11 is then loaded into a furnace with braze foil inserted into each of the joints of core 11 to braze core 11 into one unitary, monolithic component.

First heating fluid passage 56a and second heating fluid passage 56b are contained within first closure tube 50a and second closure tube 50b, respectively, and extend between third side 16 and fourth side 18. In the example shown in FIG. 1, first closure tube 50a and second closure tube 50b are rectangular tubes. In another example, first closure tube 50a and second closure tube 50b can be cylindrical tubes, triangular tubes, or any other shape that fits between parting sheets (43b, 43c, 43d, and 43e) and accommodates first heating fluid passage 56a and second heating fluid passage 56b. First heating fluid passage 56a and second heating fluid passage 56b will be discussed in greater detail below with reference to FIGS. 2 and 3.

FIG. 2 is a schematic diagram of first hot layer 40a in core 11 of heat exchanger 10. Although the following discussion relates to first hot layer 40a, it is to be understood that the following disclosure equally applies to second hot layer 40b. Heat exchanger 10 also includes tube inlet manifold 52, tube outlet manifold 54, heating fluid system 59, inlet manifold 61, and outlet manifold 63. Heating fluid system 59 includes first fluid supply line 60, second fluid supply line 62, temperature control valve 64, flow control valve 66, check valve 68, first fluid source 70, second fluid source 72, and regulated heating fluid line 74.

Tube inlet manifold 52 is connected to first closure tube 50a on third side 16. Tube outlet manifold 54 is connected to first closure tube 50a on fourth side 18. First heating fluid passage 56a fluidically connects tube inlet manifold 52 and tube outlet manifold 54. Tube inlet manifold 52 is configured to direct a heating fluid from regulated heating fluid line 74 into first heating fluid passage 56a. Tube outlet manifold 54 receives the heating fluid after the heating fluid traverses first heating fluid passage 56a. First heating fluid passage 56a is configured to contain and transport the heating fluid, which flows from inlet manifold 52 to outlet manifold 54 and transfers heat through first closure tube 50a to first cold inlet 22a and second cold inlet 22b of first cold layer 20a and second cold layer 20b, respectively. The preceding discussion regarding first closure tube 50a is to be understood as equally applying to second closure tube 50b.

Inlet manifold 61 of first hot layer 40a is on third side 16 and extends between first side 12 and second side 14. Inlet manifold 61 is configured to receive the hot fluid via an inlet of inlet manifold 61 (not shown) and direct the hot fluid into first hot passages 46a. Outlet manifold 63 is on fourth side 18, opposite of inlet manifold 61, and extends between first side 12 and second side 14. Outlet manifold 63 is fluidically connected to inlet manifold 61 via first hot passages 46a of first hot layer 40a. Outlet manifold 63 receives the hot fluid after the hot fluid traverses first hot passages 46a and directs the hot fluid to an outlet (not shown) on outlet manifold 63. The preceding discussion regarding first hot layer 40a and first hot passages 46a is to be understood as equally applying to second hot layer 40b and second hot passages 46b.

First closure tube 50a, tube inlet manifold 52, tube outlet manifold 54, first fluid supply line 60, second fluid supply line 62, temperature control valve 64, flow control valve 66, check valve 68, first fluid source 70, second fluid source 72, and regulated heating fluid line 74 are all fluidically connected. Likewise, second closure tube 50b, tube inlet manifold 52, tube outlet manifold 54, first fluid supply line 60, second fluid supply line 62, temperature control valve 64, flow control valve 66, check valve 68, first fluid source 70, second fluid source 72, and regulated heating fluid line 74 are all fluidically connected. First fluid supply line 60 and second fluid supply line 62 carry fluids of different temperatures from first fluid source 70 and second fluid source 72 respectively. For instance, in one example first fluid source 70 could be a hot fluid source, e.g., from a hot side of a turbine or any other hot components of an engine, and second fluid source 72 could be a cold fluid source, e.g., from a cold side of a ram air heat exchanger or any other cold components of the engine. In another example, first fluid source 70 could contain a cold fluid, e.g., from a cold side of a ram air heat exchanger or any other cold components of the engine, and second fluid source 72 could contain a hot fluid, e.g., from a hot side of a turbine or any other hot components of an engine.

Temperature control valve 64 controls the quantity of fluid from first fluid supply line 60 and second fluid supply line 62 to control the temperature of the heating fluid (not shown) that flows through first closure tube 50a and second closure tube 50b. After temperature control valve 64 determines the temperature of the heating fluid (not shown), flow control valve 66 determines the rate at which the heating fluid flows into regulated heating fluid line 74 and ultimately through first closure tube 50a and second closure tube 50b. Temperature control valve 64 works in concert with flow control valve 66 to determine the melting capacity of the heating fluid (not shown) as it flows through first closure tube 50a and second closure tube 50b. Check valve 68 prevents the heating fluid from flowing back into first fluid source 70, thereby preventing contamination of the system.

In operation a first fluid (not shown) flows through first fluid supply line 60 and a second fluid (not shown) flows through second fluid supply line 62. Temperature control valve 64 determines the quantity of each the first fluid and the second fluid to control the heating fluid temperature. The fluid flows through flow control valve 66, which determines the quantity of the heating fluid that flows through first closure tube 50a and second closure tube 50b. From flow control valve 66, the fluid flows through tube inlet manifold 52, first closure tube 50a and second closure tube 50b, and out tube outlet manifold 54. While the heating fluid flows through first closure tube 50a and second closure tube 50b, the heating fluid's heat is transferred through first closure tube 50a and second closure tube 50b, thereby preventing or melting ice accretion on the above or below first inlet 22a and second inlet 22b of first cold layer 20a and second cold layer 20b, respectively.

FIG. 2 shows an alternative design where inlet manifold 61 and tube inlet manifold 52 are one unitary, monolithic component and where outlet manifold 63 and tube outlet manifold 54 are one unitary, monolithic component. In each of the above examples, inlet manifold 61 and tube inlet manifold 52 are fluidically isolated from one another and outlet manifold 63 and tube outlet manifold 54 are fluidically isolated from one another. When inlet manifold 61 and tube inlet manifold 52 are one unitary, monolithic component they can be additively manufactured. Likewise, when outlet manifold 63 and tube outlet manifold 54 are one unitary, monolithic component they can be additively manufactured. Core 11 is manufactured, as described above with FIG. 1. Then, the additively manufactured unitary, monolithic component including inlet manifold 61 and tube inlet manifold 52 can be attached to core 11 of heat exchanger 10 by welding, brazing, or any other method of mechanically coupling two metals. Similarly, the additively manufactured unitary, monolithic component including outlet manifold 63 and tube outlet manifold 54 can be attached to core 11 of heat exchanger 10 by welding, brazing, or any other method of mechanically coupling two metals.

FIG. 3 is schematic view of another example of first hot layer 40a of heat exchanger 10. First hot layer 40a includes fourth closure bar 49. In the example shown in FIG. 3, fourth closure bar 49 is on first side 12 of heat exchanger 10 extending between third side 16 and fourth side 18. First closure tube 50a is attached to fourth closure bar 49. First closure tube 50a can be attached to fourth closure bar by welding, brazing, or any other way of mechanically coupling two metals. The preceding discussion regarding first closure tube 50a is to be understood as equally applying to second closure tube 50b.

The example shown in FIG. 3 shows an alternative design where inlet manifold 61 and tube inlet manifold 52 are each solitary components and where outlet manifold 63 and tube outlet manifold 54 are each solitary components. In the above examples, inlet manifold 61 and tube inlet manifold 52 are fluidically isolated from one another and outlet manifold 63 and tube outlet manifold 54 are fluidically isolated from one another.

After core 11 is manufactured, as described above with FIG. 1, inlet manifold 61 and outlet manifold 63 are attached to core 11 and first cold layer 20a and second cold layer 20b will likewise have an inlet manifold (not shown) and an outlet manifold (not shown) attached thereto. Tube inlet manifold 52 and tube outlet manifold 54 are attached to first closure tube 50a and second closure tube 50b. Then, tube inlet manifold 52 is attached to heating fluid system 59 via regulated heating fluid line 74.

Discussion of Possible Embodiments

The following are non-exclusive descriptions of possible embodiments of the present invention.

A heat exchanger includes a first side opposite a second side and a third side opposite a fourth side. The third side and the fourth side extend from the first side to the second side. The heat exchanger also includes a cold layer with an inlet at the first side of the heat exchanger and an outlet at the second side of the heat exchanger. The cold layer also includes a cold passage extending from the inlet to the outlet. The heat exchanger also includes a hot layer with an inlet manifold at the third side of the heat exchanger extending between the first side and the second side and an outlet manifold at the fourth side of the heat exchanger opposite the inlet manifold and extending between the first side and the second side. The hot layer also includes a hot passage extending from the inlet manifold to the outlet manifold and a tube on the first side of the heat exchanger extending from the third side to the fourth side.

The heat exchanger of the preceding paragraph can optionally include, additionally and/or alternatively, any one or more of the following features, configurations and/or additional components:

wherein the cold layer further comprises: a first closure bar on the third side extending from the first side to the second side; a second closure bar on the fourth side extending from the first side to the second side; a plurality of fins between the first closure bar and the second closure bar extending from the first side to the second side; and a plurality of cold passages defined by the first closure bar, the second closure bar, and the plurality of fins of the cold layer;

wherein the hot layer further comprises: a third closure bar on the second side of the heat exchanger extending from the third side to the fourth side; a plurality of fins between the tube and the third closure bar extending from the third side to the fourth side; a plurality of passages defined by the tube, the third closure bar, and the plurality of fins of the hot layer;

further comprising: a second cold layer; and a second hot layer, wherein: the second cold layer is stacked between the hot layer and the second hot layer; the second hot layer is stacked between the cold layer and the second cold layer; and the second hot layer comprises a second tube on the first side of the heat exchanger and extending from the third side to the fourth side;

further comprising: a first fluid supply line configured to contain a first fluid; a second fluid supply line configured to contain a second fluid; and a control valve, wherein the control valve is fluidically connected to the first fluid supply line and the second fluid supply line, and wherein the control valve determines a quantity of the first fluid and quantity of the second fluid that flows into the tube of the hot layer and the tube of the second hot layer;

wherein the tube of the hot layer comprises: a tube inlet manifold on the third side of the heat exchanger; and a tube outlet manifold on the fourth side of the heat exchanger, wherein the tube of the hot layer fluidically connects the tube inlet manifold and the tube outlet manifold;

wherein the tube inlet manifold and the inlet manifold of the hot layer are a unitary, monolithic component, and wherein the tube inlet manifold and the inlet manifold of the hot layer are additively manufactured;

wherein the tube outlet manifold and the outlet manifold of the hot layer are one unitary, monolithic component, and wherein the tube outlet manifold and the outlet manifold of the hot layer are additively manufactured;

wherein the hot layer further comprises: a third closure bar on the second side of the heat exchanger extending from the third side to the fourth side; a fourth closure bar on the first side of the heat exchanger extending from the third side to the fourth side, wherein the tube is attached to the fourth closure bar; a plurality of fins between the third closure bar and the fourth closure bar extending from the third side to the fourth side; and a plurality of passages defined by the third closure bar, the fourth closure bar, and the plurality of fins of the hot layer extending from the third side to the fourth side;

further comprising: a first fluid supply line configured to contain a first fluid; a second fluid supply line configured to contain a second fluid; and a control valve, wherein the control valve is fluidically connected to the first fluid supply line and the second fluid supply line, and wherein the control valve determines a quantity of the first fluid and a quantity of the second fluid that flows into he tube of the hot layer;

wherein the tube of the hot layer comprises: a tube inlet manifold on the third side of the heat exchanger; and a tube outlet manifold on the fourth side of the heat exchanger, wherein the tube of the hot layer fluidically connects the tube inlet manifold and the tube outlet manifold;

wherein the tube inlet manifold and the inlet manifold of the hot layer are a unitary, monolithic component, and wherein the tube inlet manifold and the inlet manifold of the hot layer are additively manufactured; and

wherein the tube outlet manifold and the outlet manifold of the hot layer are one unitary, monolithic component, and wherein the tube outlet manifold and the outlet manifold of the hot layer are additively manufactured.

In another example, a heat exchanger includes a first side opposite a second side and a third side opposite a fourth side, wherein the third side and the fourth side extend from the first side to the second side. The heat exchanger also includes a cold layer with a first closure bar on the third side extending from the first side to the second side, a second closure bar on the fourth side extending from the first side to the second side, and a cold passage between the first closure bar and the second closure bar, wherein the cold passage includes an inlet on the first side. The heat exchanger also includes a hot layer adjacent the cold layer. The hot layer includes a third closure bar on the second side extending from the third side to the fourth side, a closure tube on the first side extending from the third side to the fourth side. The closure tube includes a heating fluid passage extending from the third side to the fourth side. The hot layer also includes a hot passage between the third closure bar and the closure tube. The hot passage includes an inlet on the third side and an outlet on the fourth side.

The heat exchanger of the preceding paragraph can optionally include, additionally and/or alternatively, any one or more of the following features, configurations and/or additional components:

wherein the heat exchanger further comprises: an inlet manifold on the third side of the heat exchanger; and an outlet manifold on the fourth side of the heat exchanger, wherein the closure tube fluidically connects the inlet manifold and the outlet manifold;

wherein the hot layer further comprises: an inlet manifold on the third side; and an outlet manifold on the fourth side, wherein the inlet manifold and the outlet manifold extend between the first side and the second side;

wherein the inlet manifold of the hot layer and the inlet manifold of the closure tube are one unitary, monolithic component, and wherein the inlet manifold of the hot layer and the inlet manifold of the closure tube are additively manufactured; and

wherein the outlet manifold of the hot layer and the outlet manifold of the closure tube are one unitary, monolithic component, and wherein the outlet manifold of the hot layer and the outlet manifold of the closure tube are additively manufactured.

In another example, a method of preventing ice accretion on a cold inlet of a cold layer of a heat exchanger includes directing a cold flow through the cold inlet of the cold layer at a first side of the heat exchanger and out a cold outlet of the cold layer at a second side of the heat exchanger. The method also includes directing a hot flow through a hot inlet header of a hot layer at a third side of the heat exchanger and out the hot outlet header of the hot layer at the fourth side of the heat exchanger. The method also includes directing a heating fluid through a tube located on the first side of the heat exchanger. The heating fluid heats the cold inlet of the cold layer of the heat exchanger.

The method of the preceding paragraph can optionally include, additionally and/or alternatively, any one or more of the following features, configurations and/or additional components:

further comprising: controlling a temperature of the heating fluid via a temperature control valve, wherein the temperature control valve determines a quantity of a first fluid and a quantity of a second fluid that are mixed to form the heating fluid; and controlling heat transfer in the first side of the heat exchanger by controlling a flow of the heating fluid via a flow control valve between the tube and the temperature control valve.

While the invention has been described with reference to an exemplary embodiment(s), it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment(s) disclosed, but that the invention will include all embodiments falling within the scope of the appended claims.

Claims

1. A heat exchanger comprising: a first side opposite a second side;a third side opposite a fourth side, wherein the third side and the fourth side extend from the first side to the second side;a cold layer comprising: an inlet at the first side of the heat exchanger;an outlet at the second side of the heat exchanger; anda cold passage extending from the inlet to the outlet;a hot layer comprising: a hot layer inlet manifold at the third side of the heat exchanger extending between the first side and the second side;a hot layer outlet manifold at the fourth side of the heat exchanger opposite the inlet manifold and extending between the first side and the second side;a hot passage extending from the inlet manifold to the outlet manifold; anda tube on the first side of the heat exchanger extending from the third side to the fourth side, wherein the tube extends fully parallel with the hot passage extending from the inlet manifold to the outlet manifold;a tube inlet manifold on the third side of the heat exchanger, wherein the tube inlet manifold is fluidically connected to the tube, the tube inlet manifold and the hot layer inlet manifold are a unitary, monolithic component, and the tube inlet manifold and the hot layer inlet manifold are additively manufactured; anda tube outlet manifold on the fourth side of the heat exchanger, wherein the tube outlet manifold is fluidically connected to the tube, the tube outlet manifold and the hot layer outlet manifold are one unitary, monolithic component, and the tube outlet manifold and the hot layer outlet manifold are additively manufactured;wherein the tube fluidic ally connects the tube inlet manifold to the tube outlet manifold, the tube inlet manifold is fluidically isolated from the hot layer inlet manifold, and the tube outlet manifold is fluidically isolated from the hot layer outlet manifold;a second hot layer comprising a second tube on the first side of the heat exchanger and extending from the third side to the fourth side; anda second cold layer, the second cold layer stacked between the hot layer and the second hot layer.

2. The heat exchanger of claim 1, wherein the cold layer further comprises: a first closure bar on the third side extending from the first side to the second side;a second closure bar on the fourth side extending from the first side to the second side;a plurality of fins between the first closure bar and the second closure bar extending from the first side to the second side; anda plurality of cold passages defined by the first closure bar, the second closure bar, and the plurality of fins of the cold layer.

3. The heat exchanger of claim 2, wherein the hot layer further comprises: a third closure bar on the second side of the heat exchanger extending from the third side to the fourth side;a plurality of fins positioned between the tube and the third closure bar extending from the third side to the fourth side; anda plurality of hot passages defined by the tube, the third closure bar, and the plurality of fins of the hot layer.

4. The heat exchanger of claim 1, further comprising: a first fluid supply line configured to contain a first fluid; a second fluid supply line configured to contain a second fluid; and a control valve, wherein the control valve is fluidically connected to the first fluid supply line and the second fluid supply line, and wherein the control valve determines a quantity of the first fluid and a quantity of the second fluid that flows into the tube of the hot layer and the second tube of the second hot layer.

5. The heat exchanger of claim 2, wherein the hot layer further comprises: a third closure bar on the second side of the heat exchanger extending from the third side to the fourth side;a fourth closure bar on the first side of the heat exchanger extending from the third side to the fourth side, wherein the tube is attached to the fourth closure bar;a plurality of fins between the third closure bar and the fourth closure bar extending from the third side to the fourth side; anda plurality of passages defined by the third closure bar, the fourth closure bar, and the plurality of fins of the hot layer extending from the third side to the fourth side.

6. The heat exchanger of claim 5, further comprising: a first fluid supply line configured to contain a first fluid;a second fluid supply line configured to contain a second fluid; anda control valve, wherein the control valve is fluidically connected to the first fluid supply line and the second fluid supply line, and wherein the control valve determines a quantity of the first fluid and a quantity of the second fluid that flows into the tube of the hot layer.

7. A heat exchanger comprising: a first side opposite a second side;a third side opposite a fourth side, wherein the third side and the fourth side extend from the first side to the second side;a cold layer comprising: a first closure bar on the third side extending from the first side to the second side;a second closure bar on the fourth side extending from the first side to the second side; anda cold passage between the first closure bar and the second closure bar, wherein the cold passage comprises an inlet on the first side;a hot layer adjacent the cold layer, the hot layer comprising: a third closure bar on the second side extending from the third side to the fourth side;a closure tube on the first side extending from the third side to the fourth side, wherein the closure tube comprises a heating fluid passage extending from the third side to the fourth side, such that the heating fluid passage is parallel with the third closure bar from the third side to the fourth side; anda hot passage between the third closure bar and the closure tube, wherein the hot passage comprises an inlet on the third side and an outlet on the fourth side;a control valve fluidly coupled to the closure tube of the hot layer, wherein a first fluid supply line is configured to transfer a first fluid to the control valve and a second fluid supply line is configured to transfer a second fluid to the control valve, and wherein the first fluid and the second fluid flow through the control valve before flowing into the closure tube;a second hot layer comprising a second closure tube on the first side of the heat exchanger and extending from the third side to the fourth side; anda second cold layer, the second cold layer stacked between the hot layer and the second hot layer.

8. The heat exchanger of claim 7, wherein the heat exchanger further comprises: an inlet manifold on the third side of the heat exchanger; andan outlet manifold on the fourth side of the heat exchanger, wherein the hot passage fluidically connects the inlet manifold and the outlet manifold, and wherein the inlet manifold and the outlet manifold extend between the first side and the second side.

9. The heat exchanger of claim 8, wherein the hot layer further comprises: a tube inlet manifold on the third side; anda tube outlet manifold on the fourth side, wherein the closure tube of the hot layer fluidically connects the tube inlet manifold and the tube outlet manifold.

10. The heat exchanger of claim 9, wherein the tube inlet manifold and the inlet manifold of the hot layer are one unitary, monolithic component, and wherein the tube inlet manifold and the inlet manifold are additively manufactured.

11. The heat exchanger of claim 9, wherein the tube outlet manifold and the outlet manifold of the hot layer are one unitary, monolithic component, and wherein the tube outlet manifold and the outlet manifold of the hot layer are additively manufactured.

12. A method of preventing ice accretion on an inlet of one or more cold layers of a heat exchanger comprising: directing a cold flow through an inlet of a first cold layer and through an inlet of a second cold layer at a first side of the heat exchanger and out an outlet of the first cold layer and out an outlet of the second cold layer at a second side of the heat exchanger;directing a hot flow through an inlet manifold and into a first hot layer and a second hot layer at a third side of the heat exchanger and out an outlet manifold of the first hot layer and the second hot layer at a fourth side of the heat exchanger;directing a heating fluid through a first tube located on the first side of the heat exchanger, wherein the heating fluid heats the inlet of the first cold layer of the heat exchanger, and wherein the first tube is positioned perpendicular to the cold flow flowing through the inlet of the first cold layer from the third side of the heat exchanger to the fourth side of the heat exchanger; anddirecting the heating fluid through a second tube of the second hot layer, the second tube located on the first side of the heat exchanger, wherein the second tube is positioned perpendicular to the cold flow flowing through the inlet of the second cold layer from the third side of the heat exchanger to the fourth side of the heat exchanger;wherein a temperature control valve is fluidly coupled to the first tube;wherein a first fluid supply line is configured to transfer a first fluid to the temperature control valve and a second fluid supply line is configured to transfer a second fluid to the temperature control valve to control a temperature of the heating fluid flowing through the first tube;wherein the first fluid and the second fluid flow through the control valve before flowing into the first tube; andwherein the second cold layer is stacked between the first hot layer and the second hot layer.

13. The method of claim 12, wherein the temperature control valve determines a quantity of the first fluid and a quantity of the second fluid that are mixed to form the heating fluid.