Air-cooled radiator assembly for oil-filled electrical quipment

Information

  • Patent Application
  • 20090277611
  • Publication Number
    20090277611
  • Date Filed
    April 20, 2009
    15 years ago
  • Date Published
    November 12, 2009
    15 years ago
Abstract
A radiator section of a radiator is provided that has a plate that defines a plurality of ducts for the flow of a fluid therethrough. A first one of the ducts has only four convex ridges and only two concave furrows. Also, a second one of the ducts located closer to a longitudinal centerline of the plate than the first duct has only eight convex ridges and only six concave furrows.
Description
FIELD OF THE INVENTION

This invention is directed towards heat exchangers and, more specifically, radiator assemblies for use with fluid sealed electrical apparatuses.


BACKGROUND OF THE INVENTION

Radiator assemblies for oil-filled electrical apparatuses have been widely used and are available in a number of different shapes and cooling configurations. Radiator assemblies are frequently needed for electrical equipment which use oil to transfer heat from electrical equipment. The oil is directed to an oil-filled radiator which is cooled by the passage of ambient air over the radiator surface.


In one type of oil-filled radiators, such as those marketed by the assignee of this patent application under the Flexoplate® trademark, radiators provide a recirculation loop to cool oil which is in contact with the electrical equipment. As the oil is heated by the electrical equipment, it expands due to the increase in temperature. The volume of oil likewise increases along with a reduction in the oil density. The hot, low-density oil will rise to the top of the electrical equipment and flows through a connecting passage into an upper region of a radiator. The hot oil transfers heat to the radiator which is subsequently transferred into the surrounding ambient air. As the oil cools, the oil flows by gravity to the bottom of the radiator undergoing additional cooling as the oil passes through the radiator. The oil is then directed back into the electrical apparatus.


One deficiency within the prior art is a failure on the part of both the purchasers and some manufacturers of radiator cooling products to fully integrate the specific cooling needs with the end radiator product. At one extreme, purchasers of radiator products may expend resources acquiring a radiator that has excessive cooling capacity and in so doing expend more money than is required to bring about efficient cooling. At the other extreme, a radiator product may be acquired which under performs with respect to the electrical transformer. In such cases, auxiliary fans or oil pumps are utilized to increase air flow or oil flow across or through the radiator at considerable expense that could have been avoided by proper matching of the radiator to the cooling needs. There is a further need in the industry to maximize the heat dissipation capability of a transformer radiator such that the most economical radiator can be provided to achieve the desired cooling.


Accordingly, there remains room for variation and improvement within the art.


SUMMARY OF THE INVENTION

It is one aspect of at least one of the present embodiments to provide for an air-cooled radiator for oil-filled electrical equipment in which the oil inlet and the oil outlet for the oil flow have an increased diameter.


It is a further aspect of at least one embodiment of the present invention to provide for a heat exchange plate of the radiator having an increased hydraulic diameter with respect to the same perimeter profile, thereby reducing the friction factor for the oil flow.


It is further aspect of at least one of the present embodiments to provide for a radiator assembly providing a larger neck region of the radiator associated with the inlet header and a similar enlargement of the neck on the exit header of the radiator, thereby reducing the resistance of flow to the circulating oil.


It is yet another aspect of at least one embodiment of the present invention to provide for an optimized plate spacing within the radiator assembly, the optimized plate spacing providing for an increased hydraulic diameter of the plate for a given perimeter while reducing the friction factor for the external flow of air.


It is yet another aspect of at least one of the present embodiments of the present invention to provide for a ripple pattern for a radiator assembly, the ripple pattern providing a greater hydraulic diameter with respect to oil flow and increasing the ability of the exterior of the ripple pattern to dissipate heat to surrounding ambient air.


It is yet a further aspect of at least one of the present embodiments of the present invention to provide for a radiator assembly for cooling heated oil in which for a given size radiator, provides for greater heat dissipation while using less material than radiators of the similar type found in the prior art.


These and other features, aspects, and advantages of the present invention will become better understood with reference to the following description and appended claims.





BRIEF DESCRIPTION OF THE DRAWINGS

A fully enabling disclosure of the present invention, including the best mode thereof to one of ordinary skill in the art, is set forth more particularly in the remainder of the specification, including reference to the accompanying drawings.



FIG. 1 is a perspective view of a radiator section attached to portions of an inlet and outlet header in accordance with one exemplary embodiment.



FIG. 2 is a cross-sectional view taken along line 2-2 of FIG. 1.



FIG. 3 is a perspective view of a pair of radiator sections attached to portions of an inlet and outlet header in accordance with a prior design.



FIG. 4 is a cross-sectional view taken along line 4-4 of FIG. 3.





DESCRIPTION OF THE PREFERRED EMBODIMENT

Reference will now be made in detail to the embodiments of the invention, one or more examples of which are set forth below. Each example is provided by way of explanation of the invention, not limitation of the invention. In fact, it will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the scope or spirit of the invention. For instance, features illustrated or described as part of one embodiment can be used on another embodiment to yield a still further embodiment. Thus, it is intended that the present invention cover such modifications and variations as come within the scope of the appended claims and their equivalents. Other objects, features, and aspects of the present invention are disclosed in the following detailed description. It is to be understood by one of ordinary skill in the art that the present discussion is a description of exemplary embodiments only and is not intended as limiting the broader aspects of the present invention, which broader aspects are embodied in the exemplary constructions.


In describing the various figures herein, the same reference numbers are used throughout to describe the same material, apparatus, or process pathway. To avoid redundancy, detailed descriptions of much of the apparatus once described in relation to a figure is not repeated in the descriptions of subsequent figures, although such apparatus or process is labeled with the same reference numbers.


It is to be understood that the ranges mentioned herein include all ranges located within the prescribed range. As such, all ranges mentioned herein include all sub-ranges included in the mentioned ranges. For instance, a range from 100-200 also includes ranges from 110-150, 170-190, and 153-162. Further, all limits mentioned herein include all other limits included in the mentioned limits. For instance, a limit of up to 7 also includes a limit of up to 5, up to 3, and up to 4.5.


A variety of radiators are known to be used for the cooling of transformer oil. Such radiators include the radiator assembly seen in U.S. Pat. No. 4,019,572 assigned to Westinghouse Electric Corporation and U.S. Pat. No. 3,153,447 assigned to Tranter Manufacturing, Inc., and which are incorporated herein by reference.


The equation which governs heat dissipated from a transformer radiator may be expressed as:






Q=U*A*ΔT


where Q is the heat dissipated; U is the heat transfer co-efficient; A is the heat transfer surface area; and ΔT is the effective temperature difference between the oil and the air.


Heretofore, manufacturers have often stressed the heat transfer area value (A) while ignoring other portions of the equation that may also contribute to the most efficient radiator design for a desired purpose. For instance, ignoring that there may be wide variations in ΔT depending upon placement of the radiators, climate factors, as well as subtle influences on radiator design that may affect the heat transfer co-efficient value (U).


Based upon the above formula and factors, the present design may be directed to improvements to a natural convection radiator which can bring about an improvement (increase) of the heat transfer co-efficient for the entire radiator performance. These improvements, combined with a more thorough understanding of the deployment conditions for the radiator, allow for the most efficient pairing of an efficient radiator product to the desired cooling needs of an electrical transformer.


As set forth in FIGS. 1 and 2, a radiator section 10 of a passive radiator is provided for use with an electrical transformer oil bath. From the various factors which are discussed below, it should be understood that other variables exist which may affect the thermal performance of radiator constants. For instance, in the example set forth below, the width 110 of a plate 20 of 21.25 inches is held constant as is the effective length 112 of 19.75 inches. Further, it is readily understood by one of ordinary skill in the art that, to the extent the plate geometry is otherwise constant, changing the width 110 of the plate 20 or changing the length 112 of the plate 20 can bring about changes in the heat transfer efficiency. For instance, changes to the width 110 of the plate 20 can bring about improvements with respect to ambient air flow relative to the plate 20 but such changes are quickly diluted by diminishing returns in terms of efficiency versus increased commercial cost of materials. Similarly, increasing the length 112 or height of a radiator (as measured by the center-to-center distance between headers 12 and 14) increases the contact interval between the oil and the ambient air and increases the residence time of the oil within the radiator. Again, changes to this particular geometry of the radiator can easily create changes in which the cost of bringing about the change far exceeds the incremental increase in overall thermal efficiency.


As is known and appreciated in the art, variations in the length 112 or height of a radiator are usually constrained by the design of the associated electrical equipment, such as a transformer, and as such, radiator dimensions are often set within a very narrow range. As is commonly employed, radiator designs typically will use the largest length 112 available given the limitations of the electrical equipment design. As set forth below, given a specific size or footprint limitation for a radiator, it has been found that significant improvements in the amount of heat that can be dissipated can be achieved by altering features of the radiation design. As noted, oftentimes the design modification allows for increased efficiency of the radiator in a same sized space while using less material which contributes to manufacturing efficiency.


As best seen in reference to FIG. 1, it has been found beneficial to increase the inlet header 12 size and outlet header 14 sizes to a diameter of 5 inches. In this regard, the diameter 16 of the inlet header 12 is 5 inches, and the diameter 18 of the outlet header 14 is likewise 5 inches although the diameters 16 and 18 may be different in other exemplary embodiments. As seen in reference to FIG. 1, the 5 inch header size allows for a reduced pressure drop for the resulting oil bath fluid flow. As a result, the radiator having increased head size will have an improved heat transfer co-efficient as a result of the higher oil flow velocity. Along with the header 12 and 14 sizes, couplings or connections from the oil bath may be similarly sized so as not to create an undesired diminishment of flow to or from the headers 12 and 14.


The diameters 16 and 18 need not be identical in other exemplary embodiments but may be different from one another. Further, the diameters 16 and 18 need not be only five inches but can be variously sized in other arrangements. For example, the diameters 16 and 18 may each be from 3.5 to 5 inches, from 4 to 6 inches, or from 4.5 to 5.5 inches in accordance with various exemplary embodiments.


Oil may flow from the inlet header 12 into an inlet neck 22 of the plate 20. Oil then flows into a series of ducts defined in the plate 20. FIG. 2 illustrates a cross-sectional view of the plate 20 at a location located half-way between the center axes of the inlet header 12 and the outlet header 14. The plate 20 is formed by a first panel 26 and a second panel 28 that are attached to one another through welding. However, it is to be understood that the panels 26 and 28 may be attached to one another by use of various means in other embodiments. Further, the plate 20 need not include a pair of panels 26 and 28 but may include only one panel in other arrangements. Although formed as a unitary piece, the first panel 26 may be the portion of the plate 20 above the lateral centerline 30, and the second panel 28 may be the portion of the plate 20 below lateral centerline 30. The first panel 26 and second panel 28 define a plurality of ducts 32, 34, 36, 38, 40, and 42 through which oil may flow. The first duct 32 and the sixth duct 42 that are located on opposite ends of the plate 20 with respect to the longitudinal centerline 102 may be symmetrical to one another with respect to centerline 102. The first panel 26 defines a first duct first ridge 56 that has is convex and has a radius of 0.1377 inches. The first panel 26 also defines a first duct second ridge 58 that is likewise convex and has a radius of 0.1377 inches. A first duct first furrow 64 is located between the ridges 56 and 58 and is concave in shape with a radius of 0.0937 inches.


The second panel 28 defines a first duct third ridge 60 that is convex in shape and is located opposite from the first duct first ridge 56 with respect to the lateral centerline 30 of the plate 20. The first duct third ridge 60 may have a radius of 0.1378 inches. However, in another exemplary embodiment the first duct third ridge 60 has a radius that is 0.1377 inches. The second panel 28 additionally defines a first duct third ridge 62 that is located opposite from the first duct second ridge 58 and is convex in shape. The first duct third ridge 62 may have a radius of 0.1377 inches in accordance with one embodiment. A first duct second furrow 66 is disposed between the ridges 60 and 62 and is concave in shape with a radius of 0.0937 inches. The first duct second furrow 66 is located opposite from the first duct first furrow 64 with respect to the lateral centerline 30. The first duct 64 may have a first duct width 68 of 2.25 inches.


The sixth duct 42 can be arranged in a manner identical to the first duct 32. Here, the sixth duct 42 is symmetrical with respect to the first duct 32 about the longitudinal centerline 102. In this regard, the ridge of the sixth duct 42 formed by the first panel 26 that is farthest from the inlet header 12 along the lateral centerline 30 may be arranged in a manner identical to the first duct first ridge 56. Also, the ridge of the sixth duct 42 formed by the first panel 26 closest to the inlet header 12 along the direction of the lateral centerline 30 can be arranged in a manner similar to the first duct second ridge 58 as previously discussed. The furrow formed by the first panel 26 may be made in an identical manner to the first duct first furrow 64 as previously discussed. Additionally, the features of the sixth duct 42 formed by the second panel 28 may be identical and symmetrical to the features of the first duct 32 formed by the second panel 28.


The plate 20 also features a second duct 34 defined by the first panel 26 and the second panel 28. The first panel 26 defines a second duct first ridge 70 that is convex with a radius of 0.2003 inches. A second duct second ridge 72 is also defined by the first panel 26 and may be convex with a radius of 0.1378 inches. A second duct first furrow 86 is defined between the ridges 70 and 72 and is concave in shape and may have a radius of 0.0938 inches. Third and fourth second duct ridges 74 and 76 are likewise defined by the first panel 26 and are convex in shape. The ridge 74 may have a radius of 0.1377 inches in one embodiment, and ridge 76 may have a radius of 0.2002 inches in one embodiment. The first panel 28 defines a second duct second furrow 88 located between the ridges 72 and 74, and the first panel 28 defines a second duct third furrow 90 that is located between the ridges 74 and 76. The furrows 88 and 90 may be concave in shape and can each have a radius of 0.0938 inches in accordance with one embodiment.


The second panel 28 defines additional portions of the second duct 34 such as a second duct fifth ridge 78 that is convex in shape and is located opposite from ridge 70 with respect to the lateral centerline 30. Ridge 78 may have a radius of 0.2003 inches in certain embodiments. A second duct sixth ridge 80 is present and is convex in shape and located opposite to the ridge 72 with respect to the lateral centerline 30. Ridge 80 may have a radius of 0.1378 inches in accordance with certain embodiments. A second duct fourth furrow 92 is located between the ridges 78 and 80 and is located opposite from the furrow 86 with respect to the lateral centerline 30. The furrow 92 may have a radius of 0.0938 and can be concave in shape in accordance with certain exemplary embodiments. A second duct seventh ridge 82 and a second duct eighth ridge 84 may likewise be defined on the second panel 28 and can be located opposite from the ridge 74 and ridge 76 respectively. The ridges 82 and 84 may have a radius of 0.1377 inches and a radius of 0.2002 inches respectively and may both be convex in shape. A second duct fifth furrow 94 and a second duct sixth furrow 96 can be included and may be concave in shape with a radius of 0.0938 inches. The second duct fifth furrow 94 is located opposite from the furrow 88 with respect to the lateral centerline 30, and furrow 96 is located opposite from the furrow 90 with respect to the lateral centerline 30.


The second duct 34 may have a width 98 of 3.19 inches in accordance with certain exemplary embodiments. The second duct 34 thus features eight ridges 70, 72, 74, 76, 78, 80, 82, and 84 that are convex in shape and six furrows 86, 88, 90, 92, 94, and 96 that are concave in shape. The ridges 70, 72, 74, 76, 78, 80, 82, and 84 may be symmetrical about the lateral centerline 30 in certain embodiments. Further, the furrows 86, 88, 90, 92, 94, and 96 may be symmetrical to the opposite furrow 86, 88, 90, 92, 94, or 96 about the lateral centerline 30 in various embodiments.


The fifth duct 40 is provided with four convex ridges on the first panel 26 and four convex ridges oppositely disposed on the second panel 28. Concave furrows are also present on the first panel 26 that are located opposite from concave furrows on the second panel 28. The fifth duct 40 may be identically arranged with respect to the second duct 34 and symmetrical thereto with respect to the longitudinal centerline 102. However, it is to be understood that other embodiments may exist in which the second and fifth ducts 34 and 40 are not symmetrical about longitudinal centerline 102.


The third and fourth ducts 36 and 38 are located the closest to the longitudinal centerline 102 in the distance along the lateral centerline 30 than any of the other ducts. The third and fourth ducts 36 and 38 may each have eight ridges and six furrows that are located opposite to one another about the lateral centerline 30 as discussed above concerning the second duct 34. The third and fourth ducts 36 and 38 may be symmetrical with respect to one another about the longitudinal centerline 102. The ridges and furrows of the third and fourth ducts 36 and 38 may have radii that are different from or the same as the radii of the ridges and furrows of the second duct 34 and/or the fifth duct 40. In one embodiment, the third duct 36 may be constructed in a manner identically to that of the second duct 34, and the fourth duct 38 may be constructed in a manner identical to the fifth duct 40. In this regard, the second duct 34 and third duct 36 may be symmetrical to the fourth and fifth ducts 38 and 40 about the longitudinal centerline 102. Further, in another exemplary embodiment the first duct 56 and the sixth duct 42 may be symmetrical about the longitudinal centerline 102 so that all of the ducts of the plate 20 are symmetrical to another one of the ducts about the longitudinal centerline 102. However, it is to be understood that the ducts can be variously arranged in other exemplary embodiments so that all or none of the ducts of the plate 20 are symmetrical about the longitudinal centerline 102. Further, it is to be understood that each individual duct 32, 34, 36, 38, 40, and 42 may or may not be symmetrical about the lateral centerline 30 in accordance with various exemplary embodiments.


The height of the apexes of the various ridges to the lateral centerline 30 can be different or the same with respect to all of the ridges of the ducts 32, 34, 36, 38, 40 and 42. In one embodiment, the height 100 of the ridge of the fourth duct 38 farthest from the longitudinal centerline 102 may be 0.23 inches as measured from the apex of the ridge to the lateral centerline 30. Any other one or ones of the ridges of ducts 32, 34, 36, 38, 40 and 42 may have a similar height 100. Further, all of the furrows of the ducts 32, 34, 36, 38, 40 and 42 may have the same near point to the lateral center line 30 or may have varying near points to the lateral center line 30 in accordance with various exemplary embodiments.


The plate 20 includes a first section 44 that is located between the first duct 32 and the second duct 34. The first section 44 features engagement between the first panel 26 and the second panel 28 so that oil will not flow through the first section 44. In addition, a second section 46, third section 48, fourth section 50, and fifth section 52 are provided between the ducts 34, 36, 38, 40, and 42. The various sections 46, 48, 50 and 52 are arranged so that the first panel 26 engages the second panel 28 to prevent oil from flowing therethrough. The third section 54 is located at the longitudinal centerline 102 of the plate 20 and has a width 54 of 0.5 inches in accordance with one exemplary embodiment. The various sections 44, 46, 48, 50 and 52 may all have the same width or may have different widths from one another in accordance with different exemplary embodiments.



FIGS. 3 and 4 illustrate a radiator section 10 of a known design in which the diameters 16 and 18 are 3.5 inches. Five ducts 32, 34, 36, 38, 40, and 42 are present in which the first duct 32 and the sixth duct 42 each have a design with 6 ridges and 4 furrows. Ducts 34, 36, 38, and 40 each have 10 ridges and 8 furrows. The radiator section 10 has a second plate 104 with a plate spacing 106 between the plate 20 and the second plate 104. The plate spacing 106 may be the distance between the lateral centerline 30 of plate 20 and the lateral centerline 108 of the second plate 104. In the embodiment shown, the plate spacing 106 is 1.77 inches. The radiator section 10 of the exemplary embodiment of FIGS. 1 and 2 may have a plurality of additional plates as is known in the art. However, the plate 20 may have a plate spacing 106 of 2.25 inches so that the distance from the lateral centerline 30 of plate 20 to the lateral centerline of an adjacent plate is 2.25 inches. Each one of the plates of the plurality of plates may have a plate spacing of 2.25 inches in accordance with one exemplary embodiment of the radiator. The increase in plate spacing in the embodiment of FIGS. 1 and 2 provides for a better air flow between the plates and reduces interference between the inherent boundary layers that occur adjacent to the plates. The plate spacing may be from 2 to 3 inches, from 2.1 to 2.8 inches, from 2.2 to 2.75 inches, or from 2.25 to 2.5 inches in accordance with various exemplary embodiments.


Since the plate spacing in the embodiment in FIGS. 1 and 2 is increased, it is also desirable to increase the heat transfer area by providing an enhanced ripple pattern to the plates 20. The enhanced ripple pattern was previously shown and described with respect to the ridges and furrows and other features of the ducts 32, 34, 36, 38, 40, and 42. In the arrangement illustrated in FIGS. 1 and 2, fewer plates 20 may be used within the same footprint of a previous radiator to bring about comparable performance even though fewer plates 20 are utilized. As seen in reference to FIGS. 1 and 2, the ripple pattern defines a ripple having a longer length in which the defining angles are sharper. The combination of length and angles provides an increase to the hydraulic diameter of the plate 20 which offers less resistance to oil flow. As the oil flow increases, the amount of heat transferred to the ambient air increases, enhancing the overall heat dissipation by the system.


The hydraulic diameter is calculated as Dh=4*A/P where Dh is the hydraulic diameter, A is the area normal to the fluid flow, and P is the perimeter of the flow. The inlet and outlet headers 12 and 14 have a hydraulic diameter (Dh) of 5 inches in the exemplary embodiment of FIGS. 1 and 2 due to the fact that the diameters 16 and 18 may be 5 inches. This Dh is contrasted to a Dh of 3.5 inches of the inlet header 12 and the outlet header 14 of the embodiment in FIGS. 3 and 4 in which the diameters 16 and 18 are each 3.5 inches. Increasing the diameters 16 and 18 causes the hydraulic diameter on the inlet and exit side to be increased to result in a reduction of the fluid friction factor and thus an increase in oil flow. Within the interior of the plate 20, the actual values of area and perimeter are used to calculate the Dh as 0.529 inches in the FIGS. 1 and 2 embodiment as contrasted to a Dh of 0.457 inches in the FIGS. 3 and 4 embodiment. The modifications to the plate 20 may result in a 15.9% increase in the hydraulic diameter over the previous design illustrated in FIGS. 3 and 4. The hydraulic diameter is increased while the perimeter is reduced in addition to a reduction in the fluid flow friction factor of the oil. The ripple pattern disclosed in the exemplary embodiment of FIGS. 1 and 2 causes an increased hydraulic diameter to be associated with this portion of the radiator section 10. By increasing the hydraulic diameter, the fluid flow friction is reduced to result in an increased oil flow rate. Increasing the hydraulic diameter while minimizing a corresponding increase in materials utilized may allow a more efficient radiator to be achieved. The heat transfer coefficient (U) previously mentioned is calculated to be 10.1 W/° C./ft2 in the radiator of FIGS. 3 and 4, and the heat transfer coefficient U is calculated to be 12.4 W/° C./ft2 in the embodiment of FIGS. 1 and 2.


The increase of the diameters 16 and 18 may allow a larger slot or opening to be present between the headers 12 and 18 and the inlet neck 22 and outlet neck 24. The inlet neck 22 and outlet neck 24 may thus be larger in the embodiment in FIGS. 1 and 2 as compared to the embodiment of FIGS. 3 and 4. Increasing the cross-section of the necks 22 and 24 allows for an increase in oil flow that can improve the heat dissipation capacity of the radiator.


EXPERIMENTS CARRIED OUT IN ACCORDANCE WITH CERTAIN EXEMPLARY EMBODIMENTS

Applicant conducted various experiments regarding radiator sections 10 discussed herein. Table 1 below illustrates a test that compared a regular radiator built in a manner similar to the FIGS. 3 and 4 embodiment to a prototype radiator build along the lines discussed with reference to the FIGS. 1 and 2 embodiment. The testing was conducted in a lab.












TABLE 1







Regular
Prototype


Parameter
Units
Radiator
Radiator


















OA Test
1300 mm




Heat Dissipated,
[W]
7277
8759


Q


Hot Oil Temp Rise
[° C.]
65
65


No. of Panels, n
[—]
15
15


Heat Transfer
[W · ft2 · ° C.−1]
1.02
1.23


Coefficient, U


% Improvement In
[%]

20.37


U









Another experiment was carried out in accordance with a different exemplary embodiment at the original equipment manufacturer for radiators for transformers. The test was conducted between a regular radiator and an enhanced prototype and results thereof are illustrated below in Table 2. The regular radiator was a radiator bank with one radiator having 18 plates 20 and 4 radiators having 23 plates 20 each, and the enhanced prototype radiator was a radiator bank having 1 radiator with 15 plates 20 and 4 radiators with 18 plates 20 each.












TABLE 2








Enhanced




Regular
Prototype


Parameter
Units
Radiator
Radiator


















Heat Dissipation
[W]
38760
38760


Ambient Temp
[° C.]
21.7
20.2


Top Oil
[° C.]
70.8
69.9


Top Radiator
[° C.]
67.2
66.5


Bottom Radiator
[° C.]
45.6
49.8


Hot Spot Rise, HV
[° C.]
55.9
57.3


Hot Spot Rise, LV
[° C.]
57.0
57.3


Top Oil Rise
[° C.]
49.1
49.7


Heat Transfer
[ft2]
1108
877


Area


Overall Heat
[W · ft2 · ° C.−1]
0.712
0.890


Transfer


Coefficient, Based


on Top Oil Rise









The heat transfer area was reduced about 21% in the enhanced prototype radiator, and the heat transfer coefficient was improved about 22%. The difference between the top radiator oil temperature and the bottom radiator oil temperature showed an increase in oil flow of about 22%.


Additional testing was conducted in order to compare the heat dissipation capacity of 4 radiators with 36 plates 20 each and of 3200 mm in length (regular radiator) to 4 radiators with 29 plates 20 each and of 3200 mm in length (prototype radiator). Table 3 below is data of the test run at the original equipment manufacturer with an OA rating, and the results in Table 4 are from the original equipment manufacturer with an FA rating.












TABLE 3







Regular
Prototype


Parameter
Units
Radiator
Radiator


















OA Test
3200 mm




Heat Dissipated,
[W]
58246
58246


Q


Hot Oil Temp
[° C.]
57.2
62.2


Amb Temp
[° C.]
19.1
22.1


No. of Panels, n
[—]
102
87


Heat Transfer
[W · ft2 · ° C.−1]
0.84
0.93


Coefficient, U


% Improvement In
[%]

11.39


U



















TABLE 4







Regular
Prototype


Parameter
Units
Radiator
Radiator


















FA Test
3200 mm




Heat Dissipated,
[W]
171226
171226


Q


Hot Oil Temp
[° C.]
78.1
83.8


Amb Temp
[° C.]
19.9
23


No. of Panels, n
[—]
102
87


Heat Transfer
[W · ft2 · ° C.−1]
1.61
1.80


Coefficient, U


% Improvement In
[%]

12.23


U









Additional tests were conducted in regards to the radiator design set forth in FIGS. 1 and 2 which overall showed an improvement in the heat transfer coefficient by approximately 18% while maintaining the use of a reduced number of valves and other connections. Economic advantages of the enhanced heat transfer capability may be realized by a reduced number of plates 20 in each radiator or through a reduction in the total number of radiators used on a transformer for the same heat dissipation at the same specified hot oil temperature rise. Various test results are illustrated below in Tables 5-9. The tests were conducted at the original equipment manufacturer with the exception of the test of Table 7 that was instead conducted in a lab.












TABLE 5







Regular
Prototype


Parameter
Units
Radiator
Radiator


















OA Test
96 inches




Heat Dissipated,
[W]
57680
57440


Q


Hot Oil Temp
[° C.]
61.9
65.6


Amb Temp
[° C.]
19.27
22.07


No. of Panels, n
[—]
108
93


Heat Transfer
[W · ft2 · ° C.−1]
0.92
1.04


Coefficient, U


% Improvement In
[%]

13.25


U



















TABLE 6







Regular
Prototype


Parameter
Units
Radiator
Radiator


















FA Test
96 inches




Heat Dissipated,
[W]
83291
83680


Q


Hot Oil Temp
[° C.]
64.6
66.7


Amb Temp
[° C.]
25.9
26.8


No. of Panels, n
[—]
108
93


Heat Transfer
[W · ft2 · ° C.−1]
1.46
1.65


Coefficient, U


% Improvement In
[%]

13.16


U



















TABLE 7







Regular
Prototype


Parameter
Units
Radiator
Radiator


















OA Test
40 inches
model



Heat Dissipated,
[W]
5916
6461


Q


Hot Oil Temp
[° C.]
65
65


No. of Panels, n
[—]
14
14


Heat Transfer
[W · ft2 · ° C.−1]
0.48
0.52


Coefficient, U


% Improvement In
[%]

9.21


U



















TABLE 8







Regular
Prototype


Parameter
Units
Radiator
Radiator


















OA Test
3000 mm




Heat Dissipated,
[W]
67084
67943


Q


Hot Oil Temp
[° C.]
70.1
66.8


Amb Temp
[° C.]
31.5
28.4


No. of Panels, n
[—]
144
124


Heat Transfer
[W · ft2 · ° C.−1]
0.72
0.85


Coefficient, U


% Improvement In
[%]

18.23


U



















TABLE 9







Regular
Prototype


Parameter
Units
Radiator
Radiator


















FA Test
3000 mm




Heat Dissipated,
[W]
248701
245911


Q


Hot Oil Temp
[° C.]
83.1
84.9


Amb Temp
[° C.]
32.9
31.6


No. of Panels, n
[—]
144
124


Heat Transfer
[W · ft2 · ° C.−1]
2.05
2.21


Coefficient, U


% Improvement In
[%]

8.15


U









Although preferred embodiments of the invention have been described using specific terms, devices, and methods, such description is for illustrative purposes only. The words used are words of description rather than of limitation. It is to be understood that changes and variations may be made by those of ordinary skill in the art without departing from the spirit or the scope of the present invention as described. In addition, it should be understood that aspects of the various embodiments may be interchanged both in whole or in part. Therefore, the spirit and scope of the invention should not be limited to the description of the preferred versions contained therein.

Claims
  • 1. A radiator section of a radiator, comprising: a plate that defines a plurality of ducts for the flow of a fluid therethrough, wherein a first one of the ducts has only four convex ridges and only two concave furrows, wherein a second one of the ducts located closer to a longitudinal centerline of the plate than the first duct has only eight convex ridges and only six concave furrows.
  • 2. The radiator section as set forth in claim 1, wherein a third duct, a fourth duct, and a fifth duct are defined by the plate and each have only eight convex ridges and only six concave furrows.
  • 3. The radiator section as set forth in claim 2, wherein a sixth duct is defined by the plate and has only four convex ridges and only two concave furrows, wherein the first duct and the sixth duct are located farther from a longitudinal centerline of the plate than the second duct, the third duct, the fourth duct, and the fifth duct.
  • 4. The radiator section as set forth in claim 3, wherein the first duct and the sixth duct are symmetric to one another about the longitudinal centerline of the plate, wherein the second duct and the fifth duct are symmetric to one another about the longitudinal centerline of the plate, and wherein the third duct and the fourth duct are symmetric to one another about the longitudinal centerline of the plate, and wherein only six ducts are present.
  • 5. The radiator section as set forth in claim 1, further comprising an inlet header that is a tube that defines an internal conduit that has a circular cross-sectional shape, wherein the diameter of the internal conduit of the inlet header is 5 inches, wherein the inlet header is in communication with the plurality of ducts such that fluid from the inlet header is capable of flowing into an inlet neck of the plate and subsequently into the ducts.
  • 6. The radiator section as set forth in claim 5, further comprising an outlet header that is a tube that defines an internal conduit that has a circular cross-sectional shape, wherein the diameter of the internal conduit of the outlet header is 5 inches, wherein the outlet header is in communication with the plurality of ducts such that fluid from the ducts is capable of flowing into an outlet neck of the plate and subsequently into the outlet header.
  • 7. The radiator as set forth in claim 1, further comprising a second plate that defines a plurality of ducts for the flow of a fluid therethrough, wherein a first one of the ducts of the second plate has only four convex ridges and only two concave furrows, wherein a second one of the ducts of the second plate located closer to a longitudinal centerline of the second plate than the first duct of the second plate has only eight convex ridges and only six concave furrows, wherein the second plate is spaced a distance from 2.1 inches to 2.8 inches from the plate.
  • 8. The radiator as set forth in claim 7, wherein a lateral centerline of the plate is spaced a distance of 2.25 inches from a lateral centerline of the second plate.
  • 9. A radiator section of a radiator, comprising: an inlet header having a diameter that is at least 5 inches; anda plate with an inlet neck in communication with the inlet header such that fluid is capable of flowing from the inlet header into the inlet neck, wherein the plate has a plurality of ducts in communication with the inlet neck such that fluid is capable of flowing from the inlet neck into the ducts.
  • 10. The radiator section as set forth in claim 9, wherein the plate has an outlet neck in communication with the ducts such that fluid is capable of flowing from the ducts into the outlet neck, and further comprising an outlet header in communication with the outlet neck such that fluid is capable of flowing from the outlet neck into the outlet header, wherein the outlet header has a diameter that is at least 5 inches.
  • 11. The radiator section as set forth in claim 10, wherein the inlet header is a tube defining an internal conduit that has a circular cross-sectional shape, wherein the diameter of the internal conduit of the inlet header is 5 inches, and wherein the outlet header is a tube defining an internal conduit that has a circular cross-sectional shape, wherein the diameter of the internal conduit of the outlet header is 5 inches.
  • 12. The radiator section as set forth in claim 9, further comprising a second plate in communication with the inlet header such that fluid is capable of flowing from the inlet header into the second plate, wherein the plate is spaced a distance of 2.25 inches from the second plate.
  • 13. The radiator section as set forth in claim 12, wherein a lateral centerline of the plate is spaced a distance of 2.25 inches from a lateral centerline of the second plate.
  • 14. The radiator section as set forth in claim 9, wherein two of the ducts that are each located farthest from a longitudinal centerline of the plate each have only four convex ridges and only two concave furrows.
  • 15. The radiator section as set forth in claim 14, wherein only four additional ducts are present, wherein each one of the four additional ducts has only eight convex ridges and only six concave furrows.
  • 16. The radiator section as set forth in claim 15, wherein the two ducts that are farthest from the longitudinal centerline of the plate are symmetrical to one another with respect to the longitudinal centerline of the plate, wherein the two ducts that are closest to the longitudinal centerline of the plate are symmetrical to one another with respect to the longitudinal centerline of the plate, and wherein the two remaining ducts are symmetrical to one another with respect to the longitudinal centerline of the plate.
  • 17. A radiator section of a radiator, comprising: an inlet header configured for having a fluid flow therethrough;a plate in communication with the inlet header such that fluid is capable of flowing from the inlet header into the plate, wherein the plate has a plurality of ducts capable of having fluid flow therethrough, wherein the plate has a lateral centerline; anda second plate in communication with the inlet header such that fluid is capable of flowing from the inlet header into the second plate, wherein the second plate has a plurality of ducts capable of having fluid flow therethrough, wherein the second plate has a lateral centerline, and wherein the lateral centerline of the plate is located from 2.1 inches to 2.8 inches from the lateral centerline of the second plate.
  • 18. The radiator as set forth in claim 17, wherein the lateral centerline of the plate is located 2.25 inches from the lateral centerline of the second plate.
  • 19. The radiator as set forth in claim 17, wherein the inlet header is a tube that defines an internal conduit that has a circular cross-sectional shape, wherein the diameter of the internal conduit of the inlet header is 5 inches, and further comprising an outlet header in communication with the plate and the second plate such that fluid from the plate and the second plate is capable of flowing into the outlet header, wherein the outlet header is a tube that defines an internal conduit that has a circular cross-sectional shape, wherein the diameter of the internal conduit of the outlet header is 5 inches.
  • 20. The radiator as set forth in claim 17, wherein a first one of the ducts of the plate has only four convex ridges and only two concave furrows, wherein a second one of the ducts of the plate located closer to a longitudinal centerline of the plate than the first duct of the plate has only eight convex ridges and only six concave furrows.
CROSS REFERENCE TO RELATED APPLICATION

This application claims the benefit of U.S. Application Ser. No. 61/124,989 filed on Apr. 21, 2008 and entitled, “Air-Cooled Radiator Assembly for Oil-Filled Electrical Equipment.” U.S. Application Ser. No. 61/124,989, including all incorporated appendices, is incorporated by reference herein in its entirety for all purposes.

Provisional Applications (1)
Number Date Country
61124989 Apr 2008 US