US2943845A - Heat exchanger for viscous fluids - Google Patents

Heat exchanger for viscous fluids Download PDF

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Publication number
US2943845A
US2943845A US692015A US69201557A US2943845A US 2943845 A US2943845 A US 2943845A US 692015 A US692015 A US 692015A US 69201557 A US69201557 A US 69201557A US 2943845 A US2943845 A US 2943845A
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core
oil
fluid
heat transfer
flow
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US692015A
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Jaklitsch Franz
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01MLUBRICATING OF MACHINES OR ENGINES IN GENERAL; LUBRICATING INTERNAL COMBUSTION ENGINES; CRANKCASE VENTILATING
    • F01M5/00Heating, cooling, or controlling temperature of lubricant; Lubrication means facilitating engine starting
    • F01M5/005Controlling temperature of lubricant
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01PCOOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
    • F01P11/00Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
    • F01P11/08Arrangements of lubricant coolers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/026Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled and formed by bent members, e.g. plates, the coils having a cylindrical configuration

Definitions

  • This invention relates to heat transfer devices and in particular to a device for controlling the temperature of viscous fluid systems such as oil systems, by heat exchange between the oil with a hotter or cooler fluid.
  • oil cooling systems including oil coolers and fans, have always been a critical part of power packages especially in combat or military vehicles where unusual restrictions to cooling air flow are imposed due to the requirement for ballistic protection.
  • Fig. l is a sectional elevational view of a heat transfer device.
  • Fig. 2 is a sectional view taken along line II-II of Fig. 1.
  • Fig. 3 is a sectional elevational view of a modification of the -heat transfer device.
  • a heat transfer device 4 utilizing air as a coolant comprises a hollow housing 6
  • the oil cooler systems in use are largely 2 Y having a plurality of longitudinal 8 on the internal surface.
  • Within the housing 6 is a series of cores of' tubes 10 having a plurality of longitudinal fins 12 which intermate with longitudinal fins 8 of housing 6.
  • Y The thickness of these cores from the inner diameter 11 to the roots 13 is sufficient to withstand the pressure eni countered in the hydraulic system of which inlet 24 and outlet 26 is a part. This thickness will vary'in acCbIflance with the pressures to be encountered and the materialU used for the core. 'Fig.
  • the space 14 between the pairs of intermating fins forms a passageway for the cooling air which enters through coll- ⁇ duit 16 of inlet manifold 18 and then flows axially through the longitudinal passage formed by space 14.
  • This space has a greater clearance at the roots -13 of the fins 12 than at the tips or peaks 15 resulting in a concentration 0f the maximum flow of coolant past the surfaces of highest temperatures, namely lthe root ofthe respective fins, thereby providing a most effective heat transfer.
  • This also results in keeping the amount of coolant at a minimum, since it is applied at the highest temperature zone thereby eliminating every cross section of flow of low efficiency.
  • the coolant then discharges through outlet v20 of exit manifold 22.
  • the fluid to be cooled enters the core 10 by intake pipe 24 and exits through outlet pipe 26, each of the pipes being attached to housing 6 in any conventional means.
  • core l0 is a free rotating helicoidal screw 32 on central shaft or bar 34 rotatably supported against axial movement by thrust bearing 33 and spider network 35 or any other thrust bearing device which forces the oil to flow along the walls ofthe core in spiral paths thereby increasing the time of contact of the oil with the core l0 ⁇ with a tendency toward turbulent flow.
  • Rotation of screw 32 is generally accomplished by the flow of the oil or other viscous fluid. As the oil is cooled by the'flow of coolant through the counterlins, layers of the oil tend to adhere to the walls of core 10. The rotation of the screw 32 meets with more resistance with decreasing temperature of the oil and by the rotation of screw 32 the layers are then sheared from the core allowing the higher temperature fluid lto come into immediate contact with the walls of the core lll.
  • the behavior of the screw 32 is self-controlling in that the flow of fluid is forced along the spiral in a ⁇ greater' number of helices at lower temperatures of the fluid and vice versa for higher temperatures of the fluid.
  • the helical screw 32 can be actuated by a gear or hydraulic device. In such a case, rotation of screw 32 is independent of the flow of the fluid and is easily controlled in accordance with the cooling requirements.
  • the device 4 can also be utilized for facilitating start ing the engine under the low temperature conditions by merely shifting from a coolant to a heating medium (a heated coolant) in order to preheat and thereby liquefy the oil and provid'eran unrestricted circulation. Once the engine is operating cooling air can again be provided.
  • a heating medium a heated coolant
  • the shaft 34 is replaced by a central tube 4i).
  • a similar helicoidal screw 3l is rotatably supported against axialrnovement by thrust bearing 37 and spider network 39 on tube 40 or any other supporting device.
  • a valve 4l normally urged to a closed position by spring 42. This valve is utilized to controlvthe pressure within core 1l?.
  • the valve 41 opens and flow takes place through the central tube 46 rather than through the spiral path within core 10.
  • a 'heat transfer device ofthe' character described comprising a corehavingY anrinne'r uid flow passage and ppluralityjof peripheral ns thereon each extending parallelto therlongitudinal aXis thereof, a housing 'sur- Y Y rounding said core'and having a plurality of longitudinal llstherein vintermating with said core fins and defining ⁇ ha ;second 'uidr owpassage positioned in directY heat transferable relation to said core uid ow passage, a t :,shaftarrying a bladed helicoidal screw rotatably mounte'd in VYsaid core inner passage 'and adapted 4to be rotated .uponvow of uid in said core inner passage, said screw jin said core inner passage defining a spiral uid ow passage Vtherein, the blade of said screw during rotation thereof being adapted to prevent adherence of uid in said Y Y
  • a heat transfer device as set forth in Yclaim 1 Where- Y, in said fluid ovv control means comprises ak check valve positioned n said diverting fluid iow passage:Y and adapted t0 onenvillenflowY resistance nsaid Spiralpath reahes a predetermined value and to closewhen said ow resistancedecreases,N belowY said predetermined value.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

July 5, 1960 F. JAKLITSCH HEAT EXCHANGER Foa vrscous muros Filed oct. 23, 1957 IN V EN TOR.
@HA/Z Jn/Ef# BY WMLM,-fwm v im @im ,United States Patent ce This invention may be manufactured and used by or for the Government of the United States for -governmental purposes without the payment to me of any royalties thereon.
This invention relates to heat transfer devices and in particular to a device for controlling the temperature of viscous fluid systems such as oil systems, by heat exchange between the oil with a hotter or cooler fluid. v
The oil cooling systems, including oil coolers and fans, have always been a critical part of power packages especially in combat or military vehicles where unusual restrictions to cooling air flow are imposed due to the requirement for ballistic protection.
One of the primary reasons for failures in power packages of vehicles is the high heat transfer requirements ofthe power plant system necessitating the use of large oil coolers. based on a multitude of narrow'cross sections of flow and relatively thin thicknesses of walls assembled with brazed connections so that they are not adaptable to high pressures and which are therefore subject to leakage and vibration failures. While the hydraulic pipe system can withstand pressures of 1000 pounds per square inch, present oil coolers can withstand approximately 250 pounds per square inch and then only for short intervals of time.
The high demand of air coolant necessitates llarge fans of high horsepower vinput thereby providing favorable conditions for material and bearing failures yin the fans also.
Accordingly, it is an object of this invention to provide a heat transfer device which is capable of elcient heat exchange between a viscous fluid, such as oil, and
air.
It is also an object of this invention to provide a heat transfer device which prevents formation of a thick adherent layer of the viscous material on the walls of the zdevice as it is cooled.
It is a further object of this invention to provide a heat transfer device in which the coolant quantity is kept to a It is a further object of this invention to provide a heat transfer device having elements capable of withstanding pressures of the same level at the hydraulic pipe system to which the heat transfer device is connected.
It is another object of this invention to provide a heat transfer device in which it is possible to preheat efficiently the viscous uid so that circulation will occur in the low temperature range.
These and other advantages will be apparent from the following description and drawings:
Fig. l is a sectional elevational view of a heat transfer device.
Fig. 2 is a sectional view taken along line II-II of Fig. 1.
Fig. 3 is a sectional elevational view of a modification of the -heat transfer device.
Referring to the drawings, a heat transfer device 4 utilizing air as a coolant comprises a hollow housing 6 The oil cooler systems in use are largely 2 Y having a plurality of longitudinal 8 on the internal surface. Within the housing 6 is a series of cores of' tubes 10 having a plurality of longitudinal fins 12 which intermate with longitudinal fins 8 of housing 6. YThe thickness of these cores from the inner diameter 11 to the roots 13 is sufficient to withstand the pressure eni countered in the hydraulic system of which inlet 24 and outlet 26 is a part. This thickness will vary'in acCbIflance with the pressures to be encountered and the materialU used for the core. 'Fig. 2 shows only two cores within the housing but any number may be used depend.- ent on the requirements of the individual system. The space 14 between the pairs of intermating fins forms a passageway for the cooling air which enters through coll- `duit 16 of inlet manifold 18 and then flows axially through the longitudinal passage formed by space 14. This space has a greater clearance at the roots -13 of the fins 12 than at the tips or peaks 15 resulting in a concentration 0f the maximum flow of coolant past the surfaces of highest temperatures, namely lthe root ofthe respective fins, thereby providing a most effective heat transfer. This also results in keeping the amount of coolant at a minimum, since it is applied at the highest temperature zone thereby eliminating every cross section of flow of low efficiency. The coolant then discharges through outlet v20 of exit manifold 22.
The fluid to be cooled enters the core 10 by intake pipe 24 and exits through outlet pipe 26, each of the pipes being attached to housing 6 in any conventional means. Within core l0 is a free rotating helicoidal screw 32 on central shaft or bar 34 rotatably supported against axial movement by thrust bearing 33 and spider network 35 or any other thrust bearing device which forces the oil to flow along the walls ofthe core in spiral paths thereby increasing the time of contact of the oil with the core l0 `with a tendency toward turbulent flow.
Rotation of screw 32 is generally accomplished by the flow of the oil or other viscous fluid. As the oil is cooled by the'flow of coolant through the counterlins, layers of the oil tend to adhere to the walls of core 10. The rotation of the screw 32 meets with more resistance with decreasing temperature of the oil and by the rotation of screw 32 the layers are then sheared from the core allowing the higher temperature fluid lto come into immediate contact with the walls of the core lll. The behavior of the screw 32 is self-controlling in that the flow of fluid is forced along the spiral in a `greater' number of helices at lower temperatures of the fluid and vice versa for higher temperatures of the fluid.
If desired, the helical screw 32 can be actuated by a gear or hydraulic device. In such a case, rotation of screw 32 is independent of the flow of the fluid and is easily controlled in accordance with the cooling requirements.
The device 4 can also be utilized for facilitating start ing the engine under the low temperature conditions by merely shifting from a coolant to a heating medium (a heated coolant) in order to preheat and thereby liquefy the oil and provid'eran unrestricted circulation. Once the engine is operating cooling air can again be provided. Y
In the modification shown in Fig. 3, the shaft 34 is replaced by a central tube 4i). A similar helicoidal screw 3l is rotatably supported against axialrnovement by thrust bearing 37 and spider network 39 on tube 40 or any other supporting device. At the exit end of tube 40 is a valve 4l normally urged to a closed position by spring 42. This valve is utilized to controlvthe pressure within core 1l?. When the pressure of flow from the intake 24 reaches a given point the valve 41 opens and flow takes place through the central tube 46 rather than through the spiral path within core 10. Under the in- A 2,943,845A Patented July 5,
fflfo spring `42tfhe` Y pressure allowing the` o'ilY tomagain owinrthe mnner valve 41V closesY on t decreasing previouslyl described. Y
" i; If desiredthe-valve 41Vcou1d be operatedby a remote Qontrol '^systei'n`} H(not shown) Ai111 Such Va -a'sevv automatic Yfonti-holslcould-be-used Whichl could be activated bythe ktemperatn'e of the enteringV fluid or the temperature of the discharging uid as Well as the regulation'by the pres.- Y
A 'heat transfer device ofthe' character described comprising a corehavingY anrinne'r uid flow passage and ppluralityjof peripheral ns thereon each extending parallelto therlongitudinal aXis thereof, a housing 'sur- Y Y rounding said core'and having a plurality of longitudinal llstherein vintermating with said core fins and defining `ha ;second 'uidr owpassage positioned in directY heat transferable relation to said core uid ow passage, a t :,shaftarrying a bladed helicoidal screw rotatably mounte'd in VYsaid core inner passage 'and adapted 4to be rotated .uponvow of uid in said core inner passage, said screw jin said core inner passage defining a spiral uid ow passage Vtherein, the blade of said screw during rotation thereof being adapted to prevent adherence of uid in said Y Ycore inner pass-age,V said shaft having inner passage f therethrough'deiining '"a"divertingy fluid ow'passagega'nd .Y uid ow control means regulating fluid ow in saidV divert ing uid ow passage.
2. A heat transfer device as set forth in Yclaim 1 Where- Y, in said fluid ovv control means comprises ak check valve positioned n said diverting fluid iow passage:Y and adapted t0 onenvillenflowY resistance nsaid Spiralpath reahes a predetermined value and to closewhen said ow resistancedecreases,N belowY said predetermined value. Y
References Cited in the le'of thislpatent UNIKTEDYSTATES PATENTS France Mar. 14, 1957
US692015A 1957-10-23 1957-10-23 Heat exchanger for viscous fluids Expired - Lifetime US2943845A (en)

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Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3213930A (en) * 1964-06-01 1965-10-26 Robinson Robert Clayton Oil temperature regulators for internal combustion engines
US3521458A (en) * 1967-07-19 1970-07-21 Air Reduction Apparatus for making hydrogen slush using helium refrigerant
US3780801A (en) * 1973-01-29 1973-12-25 Egan Machinery Co Material feeding apparatus
US3877514A (en) * 1972-06-19 1975-04-15 Hayden Trans Cooler Inc Heat exchanger valve system
US3973623A (en) * 1974-07-02 1976-08-10 Mobil Oil Corporation Heat exchange apparatus
US4151090A (en) * 1974-05-30 1979-04-24 Brigante Miguel F Unitary package for water treatment for attachment to home hot water heater
US4174750A (en) * 1978-04-18 1979-11-20 Nichols Billy M Tube cleaner having anchored rotatable spiral member
US4548776A (en) * 1983-11-23 1985-10-22 Techplastics, Inc. Method and apparatus for molding structural foam articles
US4564066A (en) * 1981-07-29 1986-01-14 Gorman Jeremy W Perforate bearing plate for turbulators in heat exchangers
US4621501A (en) * 1981-08-12 1986-11-11 Mitsubishi Denki Kabushiki Kaisha Refrigeration system having auxiliary cooling for control of coolant flow
US4641705A (en) * 1983-08-09 1987-02-10 Gorman Jeremy W Modification for heat exchangers incorporating a helically shaped blade and pin shaped support member
US4702695A (en) * 1983-12-30 1987-10-27 Blach Josef A Housing section for a twin screw shaft machine
US4813480A (en) * 1985-12-13 1989-03-21 O&K Orenstein & Koppel Aktiengesellschaft Apparatus for cooling dust or finely granular bulk material
US4960167A (en) * 1987-02-24 1990-10-02 Hypeco Ab Heat exchanger
US4991643A (en) * 1989-08-23 1991-02-12 Hayden, Inc. Heat exchanger with internal bypass valve
US5013368A (en) * 1988-11-18 1991-05-07 Compagnie De Raffinage Et De Distribution Total France Method and device for cleaning a tube in which a fluid-circulates, and their use in heat-exchanger tubes
US5228503A (en) * 1991-05-17 1993-07-20 Smith Douglas W P High viscous fluid heat exchanger
US5802961A (en) * 1994-04-15 1998-09-08 Fmc Corporation Methods and apparatus for particulate heat exchange and transfer
FR2790545A1 (en) * 1999-03-05 2000-09-08 Saint Gobain Isover Unit for extraction of heat from dust-containing hot gas, such as glass melting furnace combustion gas, includes device for creating helicoidally rotating gas current in a heat exchanger
US7192469B1 (en) * 2004-07-02 2007-03-20 Joann Rumell, legal representative Exhaust treatment device, system and methods for internal combustion engines
US20090000777A1 (en) * 2007-06-28 2009-01-01 Wanni Amar S Plate heat exchanger port insert and method for alleviating vibrations in a heat exchanger
US7530552B1 (en) 2006-06-06 2009-05-12 Enviropure Industries, Inc. Exhaust gas treatment device and method
WO2013007842A1 (en) 2011-07-14 2013-01-17 Antonio Moreno Garcia Improved heat-exchanging device for treating liquids and others
US20140284038A1 (en) * 2013-03-21 2014-09-25 Hamilton Sundstrand Corporation Heat exchanger design and fabrication
US20160018170A1 (en) * 2012-12-05 2016-01-21 Tojo KAMINO, Scrape-off type heat exchanger
US20190107341A1 (en) * 2016-03-14 2019-04-11 Calsonic Kansei Corporation Double pipe
US11191279B2 (en) * 2015-10-27 2021-12-07 Feltrim Pastoral Company Pty Ltd Apparatus for storing organic material

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1132420A (en) * 1913-12-02 1915-03-16 Joseph Engelbert Anderau Heater for gaseous fluids.
GB279446A (en) * 1926-10-20 1929-01-03 Precision Moderne Oil cooling radiator for engine lubricating systems
GB310157A (en) * 1928-03-21 1929-04-25 Serck Radiators Ltd Improvements relating to oil and other liquid coolers and heaters and similar heat exchanging apparatus
GB347904A (en) * 1930-05-17 1931-05-07 Vilhelm Mickelsen Improvements in heat interchangers for fluids
US2313705A (en) * 1941-05-28 1943-03-09 J M Lehmann Company Inc Chocolate tempering apparatus
US2549687A (en) * 1947-11-21 1951-04-17 Duriron Co Heat exchanger
DE807939C (en) * 1949-12-24 1951-07-09 Gutehoffnungshuette Oberhausen Heat exchanger
FR1132667A (en) * 1955-10-04 1957-03-14 Co-axial tubes for heat exchangers

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1132420A (en) * 1913-12-02 1915-03-16 Joseph Engelbert Anderau Heater for gaseous fluids.
GB279446A (en) * 1926-10-20 1929-01-03 Precision Moderne Oil cooling radiator for engine lubricating systems
GB310157A (en) * 1928-03-21 1929-04-25 Serck Radiators Ltd Improvements relating to oil and other liquid coolers and heaters and similar heat exchanging apparatus
GB347904A (en) * 1930-05-17 1931-05-07 Vilhelm Mickelsen Improvements in heat interchangers for fluids
US2313705A (en) * 1941-05-28 1943-03-09 J M Lehmann Company Inc Chocolate tempering apparatus
US2549687A (en) * 1947-11-21 1951-04-17 Duriron Co Heat exchanger
DE807939C (en) * 1949-12-24 1951-07-09 Gutehoffnungshuette Oberhausen Heat exchanger
FR1132667A (en) * 1955-10-04 1957-03-14 Co-axial tubes for heat exchangers

Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3213930A (en) * 1964-06-01 1965-10-26 Robinson Robert Clayton Oil temperature regulators for internal combustion engines
US3521458A (en) * 1967-07-19 1970-07-21 Air Reduction Apparatus for making hydrogen slush using helium refrigerant
US3877514A (en) * 1972-06-19 1975-04-15 Hayden Trans Cooler Inc Heat exchanger valve system
US3780801A (en) * 1973-01-29 1973-12-25 Egan Machinery Co Material feeding apparatus
US4151090A (en) * 1974-05-30 1979-04-24 Brigante Miguel F Unitary package for water treatment for attachment to home hot water heater
US3973623A (en) * 1974-07-02 1976-08-10 Mobil Oil Corporation Heat exchange apparatus
US4174750A (en) * 1978-04-18 1979-11-20 Nichols Billy M Tube cleaner having anchored rotatable spiral member
US4564066A (en) * 1981-07-29 1986-01-14 Gorman Jeremy W Perforate bearing plate for turbulators in heat exchangers
US4621501A (en) * 1981-08-12 1986-11-11 Mitsubishi Denki Kabushiki Kaisha Refrigeration system having auxiliary cooling for control of coolant flow
US4641705A (en) * 1983-08-09 1987-02-10 Gorman Jeremy W Modification for heat exchangers incorporating a helically shaped blade and pin shaped support member
US4548776A (en) * 1983-11-23 1985-10-22 Techplastics, Inc. Method and apparatus for molding structural foam articles
US4702695A (en) * 1983-12-30 1987-10-27 Blach Josef A Housing section for a twin screw shaft machine
US4813480A (en) * 1985-12-13 1989-03-21 O&K Orenstein & Koppel Aktiengesellschaft Apparatus for cooling dust or finely granular bulk material
US4960167A (en) * 1987-02-24 1990-10-02 Hypeco Ab Heat exchanger
US5013368A (en) * 1988-11-18 1991-05-07 Compagnie De Raffinage Et De Distribution Total France Method and device for cleaning a tube in which a fluid-circulates, and their use in heat-exchanger tubes
US4991643A (en) * 1989-08-23 1991-02-12 Hayden, Inc. Heat exchanger with internal bypass valve
WO1991002936A1 (en) * 1989-08-23 1991-03-07 Hayden, Inc. Heat exchanger with internal bypass valve
US5228503A (en) * 1991-05-17 1993-07-20 Smith Douglas W P High viscous fluid heat exchanger
US5802961A (en) * 1994-04-15 1998-09-08 Fmc Corporation Methods and apparatus for particulate heat exchange and transfer
FR2790545A1 (en) * 1999-03-05 2000-09-08 Saint Gobain Isover Unit for extraction of heat from dust-containing hot gas, such as glass melting furnace combustion gas, includes device for creating helicoidally rotating gas current in a heat exchanger
US7192469B1 (en) * 2004-07-02 2007-03-20 Joann Rumell, legal representative Exhaust treatment device, system and methods for internal combustion engines
US7530552B1 (en) 2006-06-06 2009-05-12 Enviropure Industries, Inc. Exhaust gas treatment device and method
US20090000777A1 (en) * 2007-06-28 2009-01-01 Wanni Amar S Plate heat exchanger port insert and method for alleviating vibrations in a heat exchanger
US8240367B2 (en) 2007-06-28 2012-08-14 Exxonmobil Research And Engineering Company Plate heat exchanger port insert and method for alleviating vibrations in a heat exchanger
WO2013007842A1 (en) 2011-07-14 2013-01-17 Antonio Moreno Garcia Improved heat-exchanging device for treating liquids and others
US20160018170A1 (en) * 2012-12-05 2016-01-21 Tojo KAMINO, Scrape-off type heat exchanger
US9939214B2 (en) * 2012-12-05 2018-04-10 Noa Co., Ltd. Scrape-off type heat exchanger
US20140284038A1 (en) * 2013-03-21 2014-09-25 Hamilton Sundstrand Corporation Heat exchanger design and fabrication
US11191279B2 (en) * 2015-10-27 2021-12-07 Feltrim Pastoral Company Pty Ltd Apparatus for storing organic material
US20190107341A1 (en) * 2016-03-14 2019-04-11 Calsonic Kansei Corporation Double pipe
US11506459B2 (en) * 2016-03-14 2022-11-22 Marelli Cabin Comfort Japan Corporation Double pipe

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