CA2030155C - Circumferential flow heat exchanger - Google Patents
Circumferential flow heat exchangerInfo
- Publication number
- CA2030155C CA2030155C CA002030155A CA2030155A CA2030155C CA 2030155 C CA2030155 C CA 2030155C CA 002030155 A CA002030155 A CA 002030155A CA 2030155 A CA2030155 A CA 2030155A CA 2030155 C CA2030155 C CA 2030155C
- Authority
- CA
- Canada
- Prior art keywords
- valleys
- energy exchange
- hollow
- generally
- plates
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0012—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
- F28D9/0037—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each other
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
- F28F3/046—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being linear, e.g. corrugations
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S165/00—Heat exchange
- Y10S165/916—Oil cooler
Abstract
The invention relates to an improved energy exchange structure, comprising generally parallel plates, joined to define a hollow passageway for the generally circular flow of fluid between an inlet and an outlet, said plates undulating in cross-structure to define obliquely disposed crossing opposing valleys, and comprising multiple sets of generally parallel valleys and an involute disposition of said valleys.
Description
CIRCUMFERENTIAL FLOW HEAT EXC~L~NGER
This invention relates to an improved ripple plate heat exchanger, having particular applicatior. in automot ve engine oil co~ling utilities where high ratios of heat transfer to oil pressure drop are desired.
BACRGROUND OF THE I~ENTION
With the development of lighter, high revolution, high torque and more compact internal combustion engines there has been increased need for more efficient oil cooling means.
Many auto engine manufacturers have incorporated into their basic engine design the need for oil cooling means in addition to that which can be attained thro~gh traditional cooling fluid passages integrally molded into the engine block. Some 1~ manufactu-_rs ~.ave specified the use of non-in~egral oil coolers whic~ act to cool a flow of oil by means exterior to the engine block. One typical mounting means comprises mounting the oil cooling n.eans at an oil filtering means. To satisfy the demands of the automotive in~ustry, such cooling means must typically be compact, lightweight and capable of high heat transfer efficiency while not adversely reducing oil pressures. Thus, the continuing need to provide lighter and more efficient heat transfer devices, has occasioned the development of a multiplicity of new designs and `- 2030 1 55 confiqurations in the manufacture of heat transfer devices for use in automotive oil cooling systems.
Early externally mounted heat transfer devices generally used as oil coolers in automotive applications typically comprised a continuous serpentine configured tube, with and without fins, mounted exterior to the engine typically in the air stream in front of the radiator or within the cooling system radiator. Oil, such as tr~n~icsion or engine oil and the like, is routed to flow tnrough the tube to be cooled.
A cooling medium typically was passed over the tube, for example within a ccolant containing radiator or an air cooling separate unit, thus allowing enerqy exchange from the heated oil in the tube to the cooling medium.
With the need for compact efficiencies oil coolers were later introduced which were mounted on the engine, typically between the engine block and an externally mounted oil filter assembly, that cooled the oil going to or coming from the filter by utilizing fluid flow from the engine cooling system.
These filter mounted coolers generally use multiple hollow, generally parallel spaced plate structures between which oil and cooling fluid flows in parallel planes to maximize heat transfer. Such spaced plate structures may contain fins between the hollow plate structures or are of ripple plate configuration. In such devices oil flows to the cooler from 203~ 1 55 a port located at or about the filter mount and circulates between parallel plates of the cooler. Coolant from the engine cooling system circulates between and/or about the parallel plates confining the circulating oil and acts to S transfer heat energy from the oil to the coolant. Many variations of the system exist, with oil being filtered first then flowing to the cooling device or the reverse and typically with coolant flowing from the cooling sy~tem of the engine, usually from the radiator or the water pump, to the - 10 cooling device.
One typical characteristic of filter mounted oil coolers is that one or both of the two fluids flow in a generally circular direction about the center of the cooler and typically the heat transfer elements, that is the fins or lS ripples, are typically not aligned in more than one or two directions. We have found that such configuration of the fins or ripples results in areas of decreased heat transfer efficiency to pressure drop within the heat exchanger.
A problem thus continues to exist particularly in optimizing heat transfer ratios to oil pressure drop within the heat exchanger. With the increased average operating - revolutions of modern engines, coupled with the high tor~ue and decreased response times, the need for oil cooling devices which are highly efficient and have minimum effect upon the oil pressure of the engine oiling system, have become desirable.
It is an object of this invention to provide energy exchange structures having improved heat transfer.
It is a further object of the invention to provide energy exchange structures having reduced internal fluid pressure drop.
It is another object of the invention to provide an automotive oil cooler having reduced internal oil pressure drop.
- It is still another object of the invention to provide a method of manufacturing an energy ~xch~nge structure having efficient heat transfer and reduced internal fluid pressure drop.
1~ - These and other objects of the invention are achieved by the invention described as follows:
SU~ARY OF rHE INV~:N-1 IO~
The invention relates to an improved energy exchange structure, comprising generally parallel opposing plates, joined to define a hollow passageway for the generally :ircular flow of fluid between an inlet and an outlet, said opposing plates undulating in cross-structure to define a plurality of opposing valleys extending into the hollow 2030 ~ 5~
passageway and arranged to follow generally involute curves - obliquely disposed to a circular direction of fluid flow within the passageway. Valleys of a first plate ~re arranged to cross valleys of a second plate such that the area between opposing valleys defire crossing passages through which the fluid can flow.
Provision is also made for energy exchange structures comprising joined opposing undulating plates wherein the undulations are comprised in four or more sets of generally parallel valleys, with each set being arranged oblique angularly to a circular flow direction within the hollow passageway defined by the joined plates. Sets of valleys of a first plate are arranged to cross opposing sets of valleys of a second plate such that the area between opposing valleys of the opposing sets define crossing passages through which the fluid can flow.
The improved automotive oil coolers of the invention comprise multiple opposing plates, stacked to form a plurality of interconnected energy exchange structures for the generally circular flow of oil. Inlets of the energy exchange structures terminate at an inlet header where they are parallel interconnected with other inlets or are serially interconnected with outlets of a second structure. Outlets terminate at an outlet header and also are parallel or serially interconnected with outlets or inlets of a second structure.
The interconnected, stacked energy exchange structures provide passage for the flow of oil within the energy exchange structures and passage for the flow of cooling fluid exterior to the energy exchange structures. A preferred cooling fluid flow is generally at an oblique angular direction to the opposing valleys of the opposing plates of the energy exchange structures to enhance energy exchange.
lo The energy exchange structures may be ccnfined J.~ hin a tank like container whe.~in a liquid and/or gaseous coolant can be circulated over and between the opposing plates comprising the energy exchange structures, or may be exposed to allow the flow of air or the like thereover. The periphery of the stacked energy ~Yrh~nge structures may be joined to the tank walls to define separated coolant passages which also may be separately connected, parallel interconnected or serially interconnected to coolant inlets and/or outlets.
Tne improved automotive oil coolers of the invention a_e produced by a process wherein opposing plates, undulating in - cross-section to have a plurality of valleys arranged to follow involute curves obliquely disposed to the direction of flow of a fluid between said plates, are arranged such that apexes of valieys ~f a first plate cross apexes of opposing valleys of a second plate and the area between opposing valleys define crossing passages which are obliquely disposed preferably at from about 5 to about 75 degrees to the circumferential direction of the energy exchange structure.
Said first and second plates are joined to form a hollow passageway, comprising a fluid inlet and a fiuid outlet, the passageway being arranged to direct fluid entering the passageway from an inlet in a generally circular flow to an outlet. The multiple energy exchange structures can be assembled in series and/or parallel to form the cooler, with an inlet of a first energy exchange structure connected to an inlet or to an outlet from a second energy exchange structure.
Typically, it is preferred to assemble two or more groups of parallel connected energy exchange structures with each group in serial arrangement with inlet and outlet headers.
Typically the so assembled energy exchange structures are encased in a tank like container having a cooling fluid inlet and outlet means. Generally, the external joined borders oE
the opposing plates are extended in a joined flattened plate to provide additional energy exchange surface at the exterior borders of the exchange structure. Such extension allows the circulation of coolant around the exterior boundaries of the stacked structures for additional cooling and can also provide 2~3~ ~ 55 convenient means for inter- connecting the exchange structures to stabilize them within the encasing tank.
DESCRIPTION OF THE DRAWINGS
Fig. 1 is a top perspective view of an oil cooler made in accordance with the present invention.
Fig. 2 is a bottom perspective view of the oil cooler of Fig. 1.
Fig. 3 is a sectional view taken approximately on line 3-3 of Fig. 1.
Fig. 3a is an enlarged sectional view of a hollow energy rh~nge structure 23 of Fig. 3.
Fig. 4 is a sectional view taken approximately on line 4-4 of Fig. 1.
Fig. 5 is a perspective view of an energy exchange structure made in accordance with the present invention.
Fig. 6 is a plan view of the interior surface of the upper plate of Fig. 5.
Fig. 7 is a plan view of the interior surface of the lower 20plate of Fig. 5.
Fig. 8 is a schematic view of a further embodiment of a plate made in accordance with the present invention.
2030 1 ~5 DETAILED DESCRIPTION OF THE INVENTION
An exemplary embodiment of an automotive oil cooler made according to the invention is illustrated in Figs. 1 and 2.
It should however be understood that the present invention can be utilized in a plurality of other applications wherein an energy exchange structure is desired.
Referring now to Figs. 1 and 2, therein a typical automotive oil cooler 10 is illustrated which is generally installed between the automotive engine and the oil filter in a typical automotive application. Cooler 10 comprises canister 11 having motor attachment end 12, oil filter attachment end 20, exterior canister side 17 and interior canister slot 14. Motor attachment end 12 comprises oil inlet 13 and motor seal slot 16 which retains oil seal 15, J illustrated in Figs 3 and 4. Exterior canister side 17 of canister 11 comprises coolant inlet 18 and coolant outlet 19~
Oil filter attachment end 20 comprises oil outlet 21 and oil filter seal surface 22. Interior canister slot 14 extends from motor attachment end 12 through oil filter attachment end 20 ar.d provides a slot through which an oil filter can be removably attached to the motor in order to seal the oil cooler and the filter to the motor and provide passage back to the motor of cooled and filtered oil.
Oil cooler 10 comprises a~ plurality of hollow energy exchange structures, contained within canister 11, through which oil flows between oil inlet 13 and oil outlet 21.
Surrounding at least a portion of the energy exchange structures are hollow passages through which coolant can flow in energy ~xch~nge relationship with the hollow energy exchange structures from coolant inlet 18 to coolant outlet 19.
In a typical operation of the illustrated embodiment, a lo first, heat energized, fluid such as hot engine oil enters oil cooler 10 through oil inlet 13, flows between opposing plates through the generally circular passages of a plurality of hollow energy exchange stru~Lu~es and through cooler motor oil outlet 21 to the inlet of an oil filter(not illustrated).
The cooled oil flows through the oil filter, and is directed through a hollow, oil filter attachment shaft (not illustrated) which extends through interior canister slot li to the motor. The hollow, oil filter attachment shaft, engages the motor and is typically threaded to compressingly attach the oil cooler and filter assemblies to the motor. The shaft thus provides both a means of attachment of the filter and the cooler to the motor and a passageway for cooled and filtered oil flow back to the motor from the filter.
Alternately, it should be understood that the oil can flow in reverse direction from the motor through the attachment shaft, to the filter, through the cooler and back to the motor from the cooler.
The flow of oil through the exchange sLL~ures is directed by the !angularly disposed, involute curve arranged, valleys - which extend inwardly to-the hollow passageway of the opposing plates. The oil stream is passively separated and mixed by the crossing paths of valleys increasing oil stream contact with opposing plates of the energy exchange structure. Heat energy from the oil is dissipated to the opposing plates of the energy exchange structures and to any fin plates which may be in contact therewith.
A second fluid flow, typically a liquid coolant such as a lS water/antifreeze mixture, flows through coolant inlet 18 such that the coolant flows across the opposing pla,tes and any fin plates that may be in contact therewith, preferably counter current to the oil flow. Heat energy dissipates from the energy exchange structures to the coolant when the heat energy of the coolant is less than that of the energy exchange structures. The coolant flows through the canister containing the energy exchange structures through coolant outlet 19 for recycle through the cooling system.
2030 1 ~5 Referring now to Fig. 3, therein is illustrated a sectional view of the oil cooler of Fig. 1 taken approximately on line 3-3, which illustrates a stacked arrangement of hollow energy exchange structures 23, within canister 11. In Fig. 3a, an enersy exchange structure 23 is enlarged and illustrated to comprise upper opposing undulating plate 24 and lower opposing undulating plate 25, joined to form exterior joined border 26.
Apexes of inwardly extending valleys 27 of the upper opposing plate 24 cross opposing apexes of inwardly ext~n~ing valleys 28 of lower opposing plate 25, with the area between apexes of valleys of a plate comprising crests 29 in upper plate 24 and crests 30 in lower plate 25. The inwardly extending valleys direct oil flow within the ~Yrh~nge structures along the crests, with crossing valleys continuously effecting a passive separation, mixing and oblique, involute redirecting of the oil flow stream generally along a circumferential flow direction from energy exchange structure inlet to energy exchange structure outlet. The area between stac~ed energy exchange structures comprises passageways also resulting from the undulating plates. Coolant flowing through these passageways is directed along the invol~te arrangement of valleys 27 and 28. As with the flow of oil, the involute arrangement of the valleys continuously effects a passive .
separation, mixing a*d oblique involute redire_ting of the ccolant stream from coolant inlet to coolant outlet.
In the illustrated embodiment of Fig. 3, the interior central borders of upper plates 24 and lower plates 25 are conveniently joined through compression rings 31 to provide structural integrity of the hollow exchange structures and fluid separation from the cooling passages therebetween.
Interior canister slot surface 34, with upper lip 32 and lower lip 33 holds motor attachmen' end 12 and filter attachment er,d 2Q in compressing engagement to join upper~lates 24 and lower plates 2S, in alternating direct and interspaced relationship with compression rings 31, to each other.
Fig. 4 co~prises a sectional view of Fig. 1, particularly illustrating oil inlet header 35 an-~ o~l outlet header 3~.
Thereat, upper plates from a first stacked energy exchange structure are joined to lower plates of a second energy exchange structure, about the interior periphery of the headers, to provide sealed separation of the coolant flow from the oil flow of the exchange structures. It should be understood that though the embodiment illustrates common headers between all inlets and outlets of the energy exchange structure for a parallel oil flow between exchange structures, the invention specifically contenplates and includes separate -2 ~ 3 G ~ 5 ~
headers between outlets`and -inlets of the stac~ed exchange structures for series oil flow.
The plates of the exchange structures are joined by any appropriate means that provide a seal of sufficient structural integrity to withstand the pressures generated within the system. Typically braze weld bonding is a preferred embodiment when the materials of construction are stainless steel, copper, ~rass or aluminum. In the event polymeric or ceramic materials are the materials of choice, preferable joining may comprise solvent or adhesive bQn~ing, or heat or ultrasonic bonding.
FIG. 5 illustrates a preferred ~-~o~ L of the energy eYch~nge structures of the invention. Therein, energy ~xch~nge structure 23 comprises opposing undulating upper plate 24 and undulating lower plate 25. Upper plate 24 comprises inwardly ext~n~ing valleys 27 and lower plate 25 comprises opposing inwardly extending valleys 28(not shown).
The area between valleys of upper plate 24 comprising crests 29 and the area between valleys of lower plate 25 comprising crests 30(not shown) each of which comprise passages through which oil flows. The opposing plates are joined at their exterior border 26. In the preferred embodiment illustrated, the exterior border is brazed welded to insure structural integrity of the seal of the energy exchange structures. The 2~30 ~ 55 interior central border of the exchange structure comprises compression ring 31 to which the plates are joined.
The valleys of the opposing plates can be conveniently formed by stamping, embossing, or otherwise forming the desired shaped va~leys into the plates. The valleys can be shaped along involute curves or can be otherwise curved or generally straight shaped and be arranged generally along an involute curve. When the valleys are shaped along involute curves they may typically be of any length within the confines of the curve on the plate. When the valleys are shaped along involute curves but generally arranged along such, they are typically straight or slightly curved and it is preferred they comprise shortened segments to reduce the exter.t of valley generally varying from the involute curvature.
Though valleys need not be generally equidistant spaced from adjacent valleys throughout their length, such is preferred in many automotive applications. By equidistant spaced is meant that the distance between adjacent valleys should be generally the same throughout the valley's length.
It should be understood that preferred equidistant spacing also does not mean that the distance between adjacent valleys need be the same, though such is preferred for many applications.
.
2030 1 5~
The area between adjacent valleys comprise adjacent crests.
Neither adjacent crests nor àdiacent valleys need be of the same width. The crests can be in the same plane as the plate, or can be stamped, embossed, or otherwise formed to extend s above the plane of the plate. It should be understood that other means well known in the art are contemplated for use in the formation of the valleys and crests, including molding and - the li~e.
Generally the crests and valleys will be at an oblique o angle to the rcumferential direction of the plate.
Preferably, the oblique angle will be from about 5 to about 75 degrees from the circumferential direction of oil flow between the-plates and most preferably from about 15 to about 45 degrees.
lS opposing first and second elongated plates, having angularly disposed valleys, are assembled so that the valleys of the first plate cross opposing valleys of the second plate.
It is not essential for the valleys or crests of the first plate to be at the same oblique angle to the longitudinal direction as those of the second plate, though such is generally preferred.
Figs. 6 and 7 comprise plan views of the interior facing surfaces of the upper plate 24 and lower plate 25 of Fig. 5.
~ig. 6 illustrates valleys 27 of upper plate 24, arranged to follow involute curves, being essentially equidistant to adjacent valleys throughout their length on the plate.
Crests illustrated in this preferred embodiment are of essentially equal width, but it should be understood that the invention contemplates and includes configurations wherein crests or valleys of a plate are not equal in width to adjacent crests or valleys.
Fig. 7, illustrates the interior surface of lower plate 25 that faces the interior surface of upper plate 24.
Therein, valleys 28 are arranged to follow involute curves, being essentially equidistant to adjacent valleys throughout their length and comprising on assembly a reverse mirror image of upper plate 24. When upper and lower plates are assembled, facing each other, to form the energy exchange structure of the invention, the valleys following involute curves of the upper plate cross the valleys following involute curves of the lower plate.
Fig. 8, comprises a schematic of a configuration of valleys on internal facing surfaces of joined undulating plates wherein the undulations are comprised in four or more sets of generally parallel valleys, with each set being arranged oblique angularly to a circular flow direction within the hollow passageway defined by joined opposing plates. When upper and lower plates having such configuration are assembled, facing each other, to form the energy exchange ;
. ;
~0 1 ~5 -structure of the invention, the valleys following the schematic direction in the upper plate cross the valleys following the schematic direction in the lower plate. Sets of valleys of the first plate cross opposinq sets of valleys of the second plate such that the area between opposing valleys of the opposing sets define crossing passages through which the fluid can flow.
Typically, the oil coolers of the invention can be manufactured from any convenient material that will withstand the corroding effects and internal fluid pressures of the system. Typical materials include the malleable metals, such as aluminum, copper, steel, stainless steel or alloys thereof and could even include plastics and/or ceramics.
The materials may be internally or externally coated, lS treated or the like. Typically, ~t is desirable to use as thin a material as possible to gain ~Yi efficiency in the energy exchange process. Generally, each of the components of a cooler are desirably formed from the same materials when they are to be joined together. ~or example, the plates used to manufacture the energy exchange structures would be typically formed from the same material. It should be understood however that it is within the contemplation of the invention to use diverse materials in the assembly, for example the use o~ steel or plastic~ in the canisters or 2030 1 5~
surfaces of the ends of the canister while using other metals, plastics or ceramics in the energy exchange structures.
It should be understood that though the illustrated invention comprises an automotive oil cooler, it is seen as being applicable to multiple heat ~Ych~nger utilities.
This invention relates to an improved ripple plate heat exchanger, having particular applicatior. in automot ve engine oil co~ling utilities where high ratios of heat transfer to oil pressure drop are desired.
BACRGROUND OF THE I~ENTION
With the development of lighter, high revolution, high torque and more compact internal combustion engines there has been increased need for more efficient oil cooling means.
Many auto engine manufacturers have incorporated into their basic engine design the need for oil cooling means in addition to that which can be attained thro~gh traditional cooling fluid passages integrally molded into the engine block. Some 1~ manufactu-_rs ~.ave specified the use of non-in~egral oil coolers whic~ act to cool a flow of oil by means exterior to the engine block. One typical mounting means comprises mounting the oil cooling n.eans at an oil filtering means. To satisfy the demands of the automotive in~ustry, such cooling means must typically be compact, lightweight and capable of high heat transfer efficiency while not adversely reducing oil pressures. Thus, the continuing need to provide lighter and more efficient heat transfer devices, has occasioned the development of a multiplicity of new designs and `- 2030 1 55 confiqurations in the manufacture of heat transfer devices for use in automotive oil cooling systems.
Early externally mounted heat transfer devices generally used as oil coolers in automotive applications typically comprised a continuous serpentine configured tube, with and without fins, mounted exterior to the engine typically in the air stream in front of the radiator or within the cooling system radiator. Oil, such as tr~n~icsion or engine oil and the like, is routed to flow tnrough the tube to be cooled.
A cooling medium typically was passed over the tube, for example within a ccolant containing radiator or an air cooling separate unit, thus allowing enerqy exchange from the heated oil in the tube to the cooling medium.
With the need for compact efficiencies oil coolers were later introduced which were mounted on the engine, typically between the engine block and an externally mounted oil filter assembly, that cooled the oil going to or coming from the filter by utilizing fluid flow from the engine cooling system.
These filter mounted coolers generally use multiple hollow, generally parallel spaced plate structures between which oil and cooling fluid flows in parallel planes to maximize heat transfer. Such spaced plate structures may contain fins between the hollow plate structures or are of ripple plate configuration. In such devices oil flows to the cooler from 203~ 1 55 a port located at or about the filter mount and circulates between parallel plates of the cooler. Coolant from the engine cooling system circulates between and/or about the parallel plates confining the circulating oil and acts to S transfer heat energy from the oil to the coolant. Many variations of the system exist, with oil being filtered first then flowing to the cooling device or the reverse and typically with coolant flowing from the cooling sy~tem of the engine, usually from the radiator or the water pump, to the - 10 cooling device.
One typical characteristic of filter mounted oil coolers is that one or both of the two fluids flow in a generally circular direction about the center of the cooler and typically the heat transfer elements, that is the fins or lS ripples, are typically not aligned in more than one or two directions. We have found that such configuration of the fins or ripples results in areas of decreased heat transfer efficiency to pressure drop within the heat exchanger.
A problem thus continues to exist particularly in optimizing heat transfer ratios to oil pressure drop within the heat exchanger. With the increased average operating - revolutions of modern engines, coupled with the high tor~ue and decreased response times, the need for oil cooling devices which are highly efficient and have minimum effect upon the oil pressure of the engine oiling system, have become desirable.
It is an object of this invention to provide energy exchange structures having improved heat transfer.
It is a further object of the invention to provide energy exchange structures having reduced internal fluid pressure drop.
It is another object of the invention to provide an automotive oil cooler having reduced internal oil pressure drop.
- It is still another object of the invention to provide a method of manufacturing an energy ~xch~nge structure having efficient heat transfer and reduced internal fluid pressure drop.
1~ - These and other objects of the invention are achieved by the invention described as follows:
SU~ARY OF rHE INV~:N-1 IO~
The invention relates to an improved energy exchange structure, comprising generally parallel opposing plates, joined to define a hollow passageway for the generally :ircular flow of fluid between an inlet and an outlet, said opposing plates undulating in cross-structure to define a plurality of opposing valleys extending into the hollow 2030 ~ 5~
passageway and arranged to follow generally involute curves - obliquely disposed to a circular direction of fluid flow within the passageway. Valleys of a first plate ~re arranged to cross valleys of a second plate such that the area between opposing valleys defire crossing passages through which the fluid can flow.
Provision is also made for energy exchange structures comprising joined opposing undulating plates wherein the undulations are comprised in four or more sets of generally parallel valleys, with each set being arranged oblique angularly to a circular flow direction within the hollow passageway defined by the joined plates. Sets of valleys of a first plate are arranged to cross opposing sets of valleys of a second plate such that the area between opposing valleys of the opposing sets define crossing passages through which the fluid can flow.
The improved automotive oil coolers of the invention comprise multiple opposing plates, stacked to form a plurality of interconnected energy exchange structures for the generally circular flow of oil. Inlets of the energy exchange structures terminate at an inlet header where they are parallel interconnected with other inlets or are serially interconnected with outlets of a second structure. Outlets terminate at an outlet header and also are parallel or serially interconnected with outlets or inlets of a second structure.
The interconnected, stacked energy exchange structures provide passage for the flow of oil within the energy exchange structures and passage for the flow of cooling fluid exterior to the energy exchange structures. A preferred cooling fluid flow is generally at an oblique angular direction to the opposing valleys of the opposing plates of the energy exchange structures to enhance energy exchange.
lo The energy exchange structures may be ccnfined J.~ hin a tank like container whe.~in a liquid and/or gaseous coolant can be circulated over and between the opposing plates comprising the energy exchange structures, or may be exposed to allow the flow of air or the like thereover. The periphery of the stacked energy ~Yrh~nge structures may be joined to the tank walls to define separated coolant passages which also may be separately connected, parallel interconnected or serially interconnected to coolant inlets and/or outlets.
Tne improved automotive oil coolers of the invention a_e produced by a process wherein opposing plates, undulating in - cross-section to have a plurality of valleys arranged to follow involute curves obliquely disposed to the direction of flow of a fluid between said plates, are arranged such that apexes of valieys ~f a first plate cross apexes of opposing valleys of a second plate and the area between opposing valleys define crossing passages which are obliquely disposed preferably at from about 5 to about 75 degrees to the circumferential direction of the energy exchange structure.
Said first and second plates are joined to form a hollow passageway, comprising a fluid inlet and a fiuid outlet, the passageway being arranged to direct fluid entering the passageway from an inlet in a generally circular flow to an outlet. The multiple energy exchange structures can be assembled in series and/or parallel to form the cooler, with an inlet of a first energy exchange structure connected to an inlet or to an outlet from a second energy exchange structure.
Typically, it is preferred to assemble two or more groups of parallel connected energy exchange structures with each group in serial arrangement with inlet and outlet headers.
Typically the so assembled energy exchange structures are encased in a tank like container having a cooling fluid inlet and outlet means. Generally, the external joined borders oE
the opposing plates are extended in a joined flattened plate to provide additional energy exchange surface at the exterior borders of the exchange structure. Such extension allows the circulation of coolant around the exterior boundaries of the stacked structures for additional cooling and can also provide 2~3~ ~ 55 convenient means for inter- connecting the exchange structures to stabilize them within the encasing tank.
DESCRIPTION OF THE DRAWINGS
Fig. 1 is a top perspective view of an oil cooler made in accordance with the present invention.
Fig. 2 is a bottom perspective view of the oil cooler of Fig. 1.
Fig. 3 is a sectional view taken approximately on line 3-3 of Fig. 1.
Fig. 3a is an enlarged sectional view of a hollow energy rh~nge structure 23 of Fig. 3.
Fig. 4 is a sectional view taken approximately on line 4-4 of Fig. 1.
Fig. 5 is a perspective view of an energy exchange structure made in accordance with the present invention.
Fig. 6 is a plan view of the interior surface of the upper plate of Fig. 5.
Fig. 7 is a plan view of the interior surface of the lower 20plate of Fig. 5.
Fig. 8 is a schematic view of a further embodiment of a plate made in accordance with the present invention.
2030 1 ~5 DETAILED DESCRIPTION OF THE INVENTION
An exemplary embodiment of an automotive oil cooler made according to the invention is illustrated in Figs. 1 and 2.
It should however be understood that the present invention can be utilized in a plurality of other applications wherein an energy exchange structure is desired.
Referring now to Figs. 1 and 2, therein a typical automotive oil cooler 10 is illustrated which is generally installed between the automotive engine and the oil filter in a typical automotive application. Cooler 10 comprises canister 11 having motor attachment end 12, oil filter attachment end 20, exterior canister side 17 and interior canister slot 14. Motor attachment end 12 comprises oil inlet 13 and motor seal slot 16 which retains oil seal 15, J illustrated in Figs 3 and 4. Exterior canister side 17 of canister 11 comprises coolant inlet 18 and coolant outlet 19~
Oil filter attachment end 20 comprises oil outlet 21 and oil filter seal surface 22. Interior canister slot 14 extends from motor attachment end 12 through oil filter attachment end 20 ar.d provides a slot through which an oil filter can be removably attached to the motor in order to seal the oil cooler and the filter to the motor and provide passage back to the motor of cooled and filtered oil.
Oil cooler 10 comprises a~ plurality of hollow energy exchange structures, contained within canister 11, through which oil flows between oil inlet 13 and oil outlet 21.
Surrounding at least a portion of the energy exchange structures are hollow passages through which coolant can flow in energy ~xch~nge relationship with the hollow energy exchange structures from coolant inlet 18 to coolant outlet 19.
In a typical operation of the illustrated embodiment, a lo first, heat energized, fluid such as hot engine oil enters oil cooler 10 through oil inlet 13, flows between opposing plates through the generally circular passages of a plurality of hollow energy exchange stru~Lu~es and through cooler motor oil outlet 21 to the inlet of an oil filter(not illustrated).
The cooled oil flows through the oil filter, and is directed through a hollow, oil filter attachment shaft (not illustrated) which extends through interior canister slot li to the motor. The hollow, oil filter attachment shaft, engages the motor and is typically threaded to compressingly attach the oil cooler and filter assemblies to the motor. The shaft thus provides both a means of attachment of the filter and the cooler to the motor and a passageway for cooled and filtered oil flow back to the motor from the filter.
Alternately, it should be understood that the oil can flow in reverse direction from the motor through the attachment shaft, to the filter, through the cooler and back to the motor from the cooler.
The flow of oil through the exchange sLL~ures is directed by the !angularly disposed, involute curve arranged, valleys - which extend inwardly to-the hollow passageway of the opposing plates. The oil stream is passively separated and mixed by the crossing paths of valleys increasing oil stream contact with opposing plates of the energy exchange structure. Heat energy from the oil is dissipated to the opposing plates of the energy exchange structures and to any fin plates which may be in contact therewith.
A second fluid flow, typically a liquid coolant such as a lS water/antifreeze mixture, flows through coolant inlet 18 such that the coolant flows across the opposing pla,tes and any fin plates that may be in contact therewith, preferably counter current to the oil flow. Heat energy dissipates from the energy exchange structures to the coolant when the heat energy of the coolant is less than that of the energy exchange structures. The coolant flows through the canister containing the energy exchange structures through coolant outlet 19 for recycle through the cooling system.
2030 1 ~5 Referring now to Fig. 3, therein is illustrated a sectional view of the oil cooler of Fig. 1 taken approximately on line 3-3, which illustrates a stacked arrangement of hollow energy exchange structures 23, within canister 11. In Fig. 3a, an enersy exchange structure 23 is enlarged and illustrated to comprise upper opposing undulating plate 24 and lower opposing undulating plate 25, joined to form exterior joined border 26.
Apexes of inwardly extending valleys 27 of the upper opposing plate 24 cross opposing apexes of inwardly ext~n~ing valleys 28 of lower opposing plate 25, with the area between apexes of valleys of a plate comprising crests 29 in upper plate 24 and crests 30 in lower plate 25. The inwardly extending valleys direct oil flow within the ~Yrh~nge structures along the crests, with crossing valleys continuously effecting a passive separation, mixing and oblique, involute redirecting of the oil flow stream generally along a circumferential flow direction from energy exchange structure inlet to energy exchange structure outlet. The area between stac~ed energy exchange structures comprises passageways also resulting from the undulating plates. Coolant flowing through these passageways is directed along the invol~te arrangement of valleys 27 and 28. As with the flow of oil, the involute arrangement of the valleys continuously effects a passive .
separation, mixing a*d oblique involute redire_ting of the ccolant stream from coolant inlet to coolant outlet.
In the illustrated embodiment of Fig. 3, the interior central borders of upper plates 24 and lower plates 25 are conveniently joined through compression rings 31 to provide structural integrity of the hollow exchange structures and fluid separation from the cooling passages therebetween.
Interior canister slot surface 34, with upper lip 32 and lower lip 33 holds motor attachmen' end 12 and filter attachment er,d 2Q in compressing engagement to join upper~lates 24 and lower plates 2S, in alternating direct and interspaced relationship with compression rings 31, to each other.
Fig. 4 co~prises a sectional view of Fig. 1, particularly illustrating oil inlet header 35 an-~ o~l outlet header 3~.
Thereat, upper plates from a first stacked energy exchange structure are joined to lower plates of a second energy exchange structure, about the interior periphery of the headers, to provide sealed separation of the coolant flow from the oil flow of the exchange structures. It should be understood that though the embodiment illustrates common headers between all inlets and outlets of the energy exchange structure for a parallel oil flow between exchange structures, the invention specifically contenplates and includes separate -2 ~ 3 G ~ 5 ~
headers between outlets`and -inlets of the stac~ed exchange structures for series oil flow.
The plates of the exchange structures are joined by any appropriate means that provide a seal of sufficient structural integrity to withstand the pressures generated within the system. Typically braze weld bonding is a preferred embodiment when the materials of construction are stainless steel, copper, ~rass or aluminum. In the event polymeric or ceramic materials are the materials of choice, preferable joining may comprise solvent or adhesive bQn~ing, or heat or ultrasonic bonding.
FIG. 5 illustrates a preferred ~-~o~ L of the energy eYch~nge structures of the invention. Therein, energy ~xch~nge structure 23 comprises opposing undulating upper plate 24 and undulating lower plate 25. Upper plate 24 comprises inwardly ext~n~ing valleys 27 and lower plate 25 comprises opposing inwardly extending valleys 28(not shown).
The area between valleys of upper plate 24 comprising crests 29 and the area between valleys of lower plate 25 comprising crests 30(not shown) each of which comprise passages through which oil flows. The opposing plates are joined at their exterior border 26. In the preferred embodiment illustrated, the exterior border is brazed welded to insure structural integrity of the seal of the energy exchange structures. The 2~30 ~ 55 interior central border of the exchange structure comprises compression ring 31 to which the plates are joined.
The valleys of the opposing plates can be conveniently formed by stamping, embossing, or otherwise forming the desired shaped va~leys into the plates. The valleys can be shaped along involute curves or can be otherwise curved or generally straight shaped and be arranged generally along an involute curve. When the valleys are shaped along involute curves they may typically be of any length within the confines of the curve on the plate. When the valleys are shaped along involute curves but generally arranged along such, they are typically straight or slightly curved and it is preferred they comprise shortened segments to reduce the exter.t of valley generally varying from the involute curvature.
Though valleys need not be generally equidistant spaced from adjacent valleys throughout their length, such is preferred in many automotive applications. By equidistant spaced is meant that the distance between adjacent valleys should be generally the same throughout the valley's length.
It should be understood that preferred equidistant spacing also does not mean that the distance between adjacent valleys need be the same, though such is preferred for many applications.
.
2030 1 5~
The area between adjacent valleys comprise adjacent crests.
Neither adjacent crests nor àdiacent valleys need be of the same width. The crests can be in the same plane as the plate, or can be stamped, embossed, or otherwise formed to extend s above the plane of the plate. It should be understood that other means well known in the art are contemplated for use in the formation of the valleys and crests, including molding and - the li~e.
Generally the crests and valleys will be at an oblique o angle to the rcumferential direction of the plate.
Preferably, the oblique angle will be from about 5 to about 75 degrees from the circumferential direction of oil flow between the-plates and most preferably from about 15 to about 45 degrees.
lS opposing first and second elongated plates, having angularly disposed valleys, are assembled so that the valleys of the first plate cross opposing valleys of the second plate.
It is not essential for the valleys or crests of the first plate to be at the same oblique angle to the longitudinal direction as those of the second plate, though such is generally preferred.
Figs. 6 and 7 comprise plan views of the interior facing surfaces of the upper plate 24 and lower plate 25 of Fig. 5.
~ig. 6 illustrates valleys 27 of upper plate 24, arranged to follow involute curves, being essentially equidistant to adjacent valleys throughout their length on the plate.
Crests illustrated in this preferred embodiment are of essentially equal width, but it should be understood that the invention contemplates and includes configurations wherein crests or valleys of a plate are not equal in width to adjacent crests or valleys.
Fig. 7, illustrates the interior surface of lower plate 25 that faces the interior surface of upper plate 24.
Therein, valleys 28 are arranged to follow involute curves, being essentially equidistant to adjacent valleys throughout their length and comprising on assembly a reverse mirror image of upper plate 24. When upper and lower plates are assembled, facing each other, to form the energy exchange structure of the invention, the valleys following involute curves of the upper plate cross the valleys following involute curves of the lower plate.
Fig. 8, comprises a schematic of a configuration of valleys on internal facing surfaces of joined undulating plates wherein the undulations are comprised in four or more sets of generally parallel valleys, with each set being arranged oblique angularly to a circular flow direction within the hollow passageway defined by joined opposing plates. When upper and lower plates having such configuration are assembled, facing each other, to form the energy exchange ;
. ;
~0 1 ~5 -structure of the invention, the valleys following the schematic direction in the upper plate cross the valleys following the schematic direction in the lower plate. Sets of valleys of the first plate cross opposinq sets of valleys of the second plate such that the area between opposing valleys of the opposing sets define crossing passages through which the fluid can flow.
Typically, the oil coolers of the invention can be manufactured from any convenient material that will withstand the corroding effects and internal fluid pressures of the system. Typical materials include the malleable metals, such as aluminum, copper, steel, stainless steel or alloys thereof and could even include plastics and/or ceramics.
The materials may be internally or externally coated, lS treated or the like. Typically, ~t is desirable to use as thin a material as possible to gain ~Yi efficiency in the energy exchange process. Generally, each of the components of a cooler are desirably formed from the same materials when they are to be joined together. ~or example, the plates used to manufacture the energy exchange structures would be typically formed from the same material. It should be understood however that it is within the contemplation of the invention to use diverse materials in the assembly, for example the use o~ steel or plastic~ in the canisters or 2030 1 5~
surfaces of the ends of the canister while using other metals, plastics or ceramics in the energy exchange structures.
It should be understood that though the illustrated invention comprises an automotive oil cooler, it is seen as being applicable to multiple heat ~Ych~nger utilities.
Claims
WE CLAIM:
An improved energy exchange structure, comprising first and second generally parallel opposing plates joined to define a hollow passageway for the generally circular flow of fluid between an inlet and an outlet, said opposing plates undulating in cross-structure to define a plurality of opposing valleys extending into the hollow passageway and arranged to follow generally involute curves, with valleys of the first plate arranged to cross valleys of the second plate such that the area between opposing valleys define crossing passages.
The structure of claim 1 wherein said valleys are formed along involute curves.
The structure of claim 1 wherein said valleys are arranged generally along involute curves.
The structure of claim 3 wherein generally straight valleys are arranged generally along involute curves.
The structure of claim 3 wherein generally curved valleys are arranged generally along involute curves.
The structure of claim 1 wherein the valleys are obliquely disposed at from about 5 to about 75 degrees to the direction of fluid flow within the passageway.
The structure of claim 1 wherein valleys of a plate are generally equidistant spaced from adjacent valleys through-out their length.
The structure of claim 7 comprising valleys of generally equal width.
The structure of claim 1 wherein the exterior borders of the plates are joined to form a flat joined plate.
An improved automotive oil cooler, comprising an energy exchange structure of claim 1.
The cooler of claim 10 wherein an inlet of a hollow energy exchange structure is connected to a header and an outlet of a hollow energy exchange structure is connected to a header.
The cooler of claim 10 wherein an inlet of one hollow energy exchange structure is connected to an outlet of another hollow energy exchange structure.
The cooler of claim 10 wherein at least one of said hollow structures comprises energy dissipating plates extending from an end of said hollow structures.
The cooler of claim 10 wherein the stacked arrangement of hollow energy exchange structures is assembled within a hollow structure configured to allow flow of a second fluid about surfaces of the stacked energy exchange structures.
A process for forming an improved oil cooler of claim 10 comprising forming plates, undulating in cross-section and having a plurality of valleys arranged to follow generally involute curves; arranging said plates such that apexes of valleys of a first plate are arranged to cross apexes of valleys of a second plate: joining said first and second plates centrally and along elongated edges to form an energy exchange structure having a hollow passage extending in a generally circular direction with inlet and outlet means therein and wherein said valleys of said plates are oblique angularly disposed to the circular direction of said passage;
and assembling a plurality of energy exchange structures in stacked arrangement.
The process of claim 15 wherein said inlet means are connected to a first header and said outlet means are connected to second header.
The process of claim 15 wherein the stacked arrangement of hollow energy exchange structures is assembled within a hollow structure configured to allow flow of a second fluid about surfaces of the stacked energy exchange structures.
An improved energy exchange structure, comprising first and second generally parallel opposing plates joined to define a hollow passageway with a generally circular fluid flow direction between an inlet and an outlet, said opposing plates undulating in cross-structure to define a plurality of opposing valieys extending into the hollow passageway and arranged in multiple sets of generally parallel valleys, each set being oblique angled to adjacent sets and to the generally circular fluid flow direction, with valleys of the first plate arranged to cross valleys of the second plate such that the area between opposing valleys define crossing passages.
An improved energy exchange structure, comprising first and second generally parallel opposing plates joined to define a hollow passageway for the generally circular flow of fluid between an inlet and an outlet, said opposing plates undulating in cross-structure to define a plurality of opposing valleys extending into the hollow passageway and arranged to follow generally involute curves, with valleys of the first plate arranged to cross valleys of the second plate such that the area between opposing valleys define crossing passages.
The structure of claim 1 wherein said valleys are formed along involute curves.
The structure of claim 1 wherein said valleys are arranged generally along involute curves.
The structure of claim 3 wherein generally straight valleys are arranged generally along involute curves.
The structure of claim 3 wherein generally curved valleys are arranged generally along involute curves.
The structure of claim 1 wherein the valleys are obliquely disposed at from about 5 to about 75 degrees to the direction of fluid flow within the passageway.
The structure of claim 1 wherein valleys of a plate are generally equidistant spaced from adjacent valleys through-out their length.
The structure of claim 7 comprising valleys of generally equal width.
The structure of claim 1 wherein the exterior borders of the plates are joined to form a flat joined plate.
An improved automotive oil cooler, comprising an energy exchange structure of claim 1.
The cooler of claim 10 wherein an inlet of a hollow energy exchange structure is connected to a header and an outlet of a hollow energy exchange structure is connected to a header.
The cooler of claim 10 wherein an inlet of one hollow energy exchange structure is connected to an outlet of another hollow energy exchange structure.
The cooler of claim 10 wherein at least one of said hollow structures comprises energy dissipating plates extending from an end of said hollow structures.
The cooler of claim 10 wherein the stacked arrangement of hollow energy exchange structures is assembled within a hollow structure configured to allow flow of a second fluid about surfaces of the stacked energy exchange structures.
A process for forming an improved oil cooler of claim 10 comprising forming plates, undulating in cross-section and having a plurality of valleys arranged to follow generally involute curves; arranging said plates such that apexes of valleys of a first plate are arranged to cross apexes of valleys of a second plate: joining said first and second plates centrally and along elongated edges to form an energy exchange structure having a hollow passage extending in a generally circular direction with inlet and outlet means therein and wherein said valleys of said plates are oblique angularly disposed to the circular direction of said passage;
and assembling a plurality of energy exchange structures in stacked arrangement.
The process of claim 15 wherein said inlet means are connected to a first header and said outlet means are connected to second header.
The process of claim 15 wherein the stacked arrangement of hollow energy exchange structures is assembled within a hollow structure configured to allow flow of a second fluid about surfaces of the stacked energy exchange structures.
An improved energy exchange structure, comprising first and second generally parallel opposing plates joined to define a hollow passageway with a generally circular fluid flow direction between an inlet and an outlet, said opposing plates undulating in cross-structure to define a plurality of opposing valieys extending into the hollow passageway and arranged in multiple sets of generally parallel valleys, each set being oblique angled to adjacent sets and to the generally circular fluid flow direction, with valleys of the first plate arranged to cross valleys of the second plate such that the area between opposing valleys define crossing passages.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/437,680 | 1989-11-17 | ||
| US07/437,680 US5203832A (en) | 1989-11-17 | 1989-11-17 | Circumferential flow heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2030155A1 CA2030155A1 (en) | 1991-05-18 |
| CA2030155C true CA2030155C (en) | 1995-08-15 |
Family
ID=23737444
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002030155A Expired - Lifetime CA2030155C (en) | 1989-11-17 | 1990-11-16 | Circumferential flow heat exchanger |
Country Status (6)
| Country | Link |
|---|---|
| US (2) | US5203832A (en) |
| EP (1) | EP0430752B1 (en) |
| JP (1) | JPH0648150B2 (en) |
| BR (1) | BR9005827A (en) |
| CA (1) | CA2030155C (en) |
| DE (1) | DE69004220T2 (en) |
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- 1990-11-16 EP EP90403244A patent/EP0430752B1/en not_active Expired - Lifetime
- 1990-11-16 BR BR909005827A patent/BR9005827A/en not_active IP Right Cessation
- 1990-11-16 CA CA002030155A patent/CA2030155C/en not_active Expired - Lifetime
- 1990-11-16 DE DE90403244T patent/DE69004220T2/en not_active Expired - Lifetime
- 1990-11-16 JP JP2309013A patent/JPH0648150B2/en not_active Expired - Lifetime
-
1992
- 1992-11-24 US US07/980,871 patent/US5343936A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0648150B2 (en) | 1994-06-22 |
| JPH03213996A (en) | 1991-09-19 |
| US5343936A (en) | 1994-09-06 |
| CA2030155A1 (en) | 1991-05-18 |
| DE69004220T2 (en) | 1994-03-10 |
| EP0430752A1 (en) | 1991-06-05 |
| DE69004220D1 (en) | 1993-12-02 |
| BR9005827A (en) | 1991-09-24 |
| US5203832A (en) | 1993-04-20 |
| EP0430752B1 (en) | 1993-10-27 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKEX | Expiry |