Heat exchanger with adjacent inlets and outlets

Abstract

A heat exchange device includes a center manifold disposed between a first and second section, each of the first and second sections including flow passages configured for heat exchange between heat exchange fluid within the flow passages and fluid external of the flow passages. Each of the flow passages have a first end and a second end, and wherein adjacent ends of adjacent flow passages direct fluid flow in the same direction.

Claims

1. A heat exchange device, comprising: a center manifold disposed between a first and second section, each of the first and second sections including flow passages configured to exchange heat between heat exchange fluid within the flow passages and fluid external of the flow passages, wherein each of the flow passages have a first end and a second end, and wherein adjacent ends of adjacent flow passages each direct fluid flow in opposite directions; a plurality of separator plates arranged within the center manifold, wherein the inlet and the outlet of each flow passage is separated one of the plurality of separator plates, wherein the plurality of separator plates are connected to one another by arcuate segments arranged at alternating ends of the separator plates along a height of the manifold section, wherein the inlet and the outlet of adjacent flow passages is separated by one of the plurality of separator plates; and a plurality of angled center manifold plates arranged within the center manifold, wherein each of the angled center manifold plates are angled or curved to alter a static pressure profile throughout the center manifold and make more uniform distribution of flow among channels of the flow passages, wherein a downstream end of each angled abuts and arcuate segment connecting adjacent separator plates, and wherein the angled center manifold plates are asymmetrically distributed within the center manifold such that a first group of separator plates are connected by arcuate segments that are abutted by an end of an angled center manifold plate, and a second group of separator plates are connected by arcuate segments that are not abutted by an angled center manifold plate.

2. The heat exchange device of claim 1, wherein the first end includes a fluid inlet directing flow from the center manifold into the flow passage and the second end includes a fluid outlet directing flow from the flow passage to the center manifold.

3. The heat exchange device of claim 2, wherein the fluid inlet and the fluid outlet of adjacent flow passages are opposite in flow direction of one another.

4. The heat exchange device of claim 1, further comprising a plurality of separators within the center manifold configured to separate ends of adjacent flow passages in which fluid flow is in the opposite direction.

5. The heat exchange device of claim 1, wherein each of the first and second sections include core sections in a stacked arrangement made up of secondary heat transfer structures attached to parting sheets.

6. The heat exchange device of claim 5, wherein each of the flow passages includes secondary heat transfer structures within the flow passage and secondary heat transfer structures extending from the flow passage configured to effect heat transfer.

7. The heat exchange device of claim 5, wherein the fins and flow passages form a solid matrix configured to limit relative motion within the device and resultant wear.

8. The heat exchange device of claim 1, wherein the plurality of inlets and outlets inlets and outlets of alternate along a height of a heat exchanger stack of the first section and the second section of the heat exchange device.

9. The heat exchange device as recited in claim 1, wherein the manifold section includes more separator plates than angled center manifold plates.

10. A heat exchange device, comprising: a center manifold disposed between a first and second section, each of the first and second sections including flow passages configured to exchange heat between heat exchange fluid within the flow passages and fluid external of the flow passages, wherein each of the flow passages have a first end with an inlet and a second end with an outlet that alternate along a height of the heat exchanger, and wherein adjacent ends of adjacent flow passages direct fluid flow in the same direction; and a plurality of separator plates arranged within the center manifold, wherein the plurality of separator plates are connected to one another by arcuate segments arranged at alternating ends of the separator plates along a height of the manifold section, wherein the inlet and the outlet of each flow passage is separated by one of the plurality of separator plates, wherein the inlet and the outlet of adjacent flow passages is separated by one of the plurality of separator plates; and a plurality of angled center manifold plates arranged within the center manifold, wherein each of the angled center manifold plates are angled or curved to alter a static pressure profile throughout the center manifold and make more uniform distribution of flow among channels of the flow passages, wherein the angled center manifold plates are asymmetrically distributed within the center manifold, such that a first group of separator plates are connected by arcuate segments that are abutted by an end of an angled center manifold plate, and a second group of separator plates are connected by arcuate segments that are abutted by an angled center manifold plate.

11. The heat exchange device of claim 10, wherein the first group and the second group are separate and distinct from each other.

12. The heat exchange device of claim 11, wherein the first group is larger than the second group.

13. The heat exchange device of claim 11, wherein the first group is wider than the second group.

14. The heat exchange device of claim 11, wherein the first group and the second group do not overlap.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) So that those skilled in the art to which the subject disclosure appertains will readily understand how to make and use the devices and methods of the subject disclosure without undue experimentation, preferred embodiments thereof will be described in detail herein below with reference to certain figures, wherein:

(2) FIG. 1 is a perspective view of a heat exchange device, showing first and second sections and a center manifold;

(3) FIG. 2 is a cross-sectional perspective view of a flow passage of each of the first and second sections of FIG. 1, showing a bend at the outer edge of the heat exchange device;

(4) FIG. 3 is a cross-sectional perspective view taken along line 3-3 of the center manifold of FIG. 1, showing the angled center manifold plates;

(5) FIG. 4 is a cross-sectional schematic view of one embodiment of the flow directions of heat exchange device of FIG. 1, showing adjacent inlet and outlets directing flow in opposite direction; and

(6) FIG. 5 is a cross-sectional schematic view of an exemplary embodiment of the flow directions of the heat exchange device of FIG. 1, showing adjacent inlet and outlets directing flow in the same direction.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(7) Reference will now be made to the drawings wherein like reference numerals identify similar structural features or aspects of the subject disclosure. For purposes of explanation and illustration, and not limitation, a partial view of an exemplary embodiment of a heat exchange device in accordance with the disclosure is shown in FIG. 1 and is designated generally by reference character 100. Other embodiments of the heat exchange device in accordance with the disclosure, or aspects thereof, are provided in FIGS. 2-5, as will be described. The systems and methods described herein can be used in turbine engines exposed to high pressure and high temperatures, for example in aerospace application.

(8) With reference to FIG. 1, a heat exchange device 100 in accordance with the present disclosure is shown. The device includes a first section 102 and a second section 104. The first and second sections 102, 104 are two identical heat exchanger plate core sections each made up of flow passages 110 configured for heat exchange between heat exchange fluid within the flow passages 110 and fluid external of the fluid passages 110 are separated by parting sheets 136. With continued reference to FIGS. 1 and 2, each of the flow passages 110 includes a bend or loop 130 at the outer edges of the device 100 to return the fluid to the center manifold 106. The bulk of the heat transfer occurs within the flow passages 110 of the first and second sections 102, 104. Secondary heat elements such as fins 132 (see FIG. 2) are included within each of the flow passages 110 and fins 134 extend from the flow passages 110. The fins 132 and 134 act as heat transfer elements and form a solid matrix to provide thermal and structural connection.

(9) With reference to FIGS. 4 and 5, exemplary embodiments of the flow configuration within flow passages 110 of the present disclosure heat exchange device 100 are shown. FIG. 4 shows one embodiment, in which inlets 12 and outlets 14 alternate along the height of the heat exchanger stack. Separator plates 18 are required to separate each inlet 12 and outlet 14 to separate the inlet and outlet fluid flows. A second embodiment is shown in FIG. 5, in which two inlets 120 and two outlets 122 are adjacent to each other. More specifically, adjacent inlets 120, 122 of adjacent flow passages 110 direct fluid flow in the same direction. The exemplary embodiment shown in FIG. 5 reduces the number of cooling layers in which heat is transferred from inlets 120 to outlets 122 at lower temperature via mixing of cooling flows passing over the parting sheets 136 between the adjacent inlets 120 and outlets 122, and via thermal conduction along cold side fins 134 thereby increasing overall thermal effectiveness of the device, allowing an approximate 10% reduction in weight and volume of the device while meeting a given set of performance requirements. A plurality of separators 140 (shown schematically) are included within the center manifold 106 configured to separate inlets and outlets 122, 120 of flow passages 110 in which fluid flows in the opposite direction. This reduces the number of separators, compared to the embodiment in FIG. 4, to segregate inlet and outlet flows in the manifold, further reducing weight of the device. The separators 140 may be angled or curved to achieve a static pressure profile throughout the manifold resulting in nearly uniform distribution of flow among the channels in each flow passage, with resultant high thermal effectiveness for the device.

(10) The center manifold 106 is configured to allow high pressure fluid to enter the manifold 106 at first side 112, pass into the flow passages 102, 104 on either side of the manifold 106, and return to the manifold 106 to exit the manifold 106 at a second side 114. More specifically, the center manifold 106 includes a first plenum 112a at one end and a second plenum 114a on an opposing end. Each of the flow passages 106 includes a fluid inlet 120 and a separate fluid outlet 122 (see FIG. 2) leading to and from the center manifold 106, respectively. Fluid flows into the first plenum 114a of the center manifold 106, passes through a respective inlet 120 of a flow passage 110, follows a bend/loop 130 of the flow passage 106, enters the center manifold 106 again through the outlet 122 and then exits the center manifold 106 through the second plenum 114a. The design for the first and second sections 102, 104 and the center manifold 106 facilitate installation of the proposed heat exchange device 100 in place of an existing tube-shell unit.

(11) As shown in FIG. 3, a cross-sectional view of the center manifold 100 illustrating angled center manifold plates 138. The flow rate of hot fluid flowing (illustrated with arrows) within the center manifold 100 varies as a function of a distance along a flow length of the manifold in both the inlet and outlet sections of the center manifold 100. The cross-sectional area increases with increased flow in regions of both the inlet and outlet manifolds to reduce pressure drop as well as to achieve a more uniform static pressure distribution along the flow length of the manifold 100 that helps to achieve more uniform distribution of flow among each flow passage bend 130. This in turn improves the overall thermal effectiveness of the device relative to a manifold configuration with nearly uniform manifold inlet and outlet cross-sectional flow areas.

(12) The methods and systems of the present disclosure, as described above and shown in the drawings, provide for a heat exchange device with superior properties including a directing fluid of adjacent ends of a flow passages in the same direction. While the apparatus and methods of the subject disclosure have been shown and described with reference to preferred embodiments, those skilled in the art will readily appreciate that changes and/or modifications may be made thereto without departing from the scope of the subject disclosure.