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US1454053A - Oil cooler - Google Patents

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Publication number
US1454053A
US1454053A US359607A US35960720A US1454053A US 1454053 A US1454053 A US 1454053A US 359607 A US359607 A US 359607A US 35960720 A US35960720 A US 35960720A US 1454053 A US1454053 A US 1454053A
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US
United States
Prior art keywords
oil
tubes
shell
passage
inlet
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
Application number
US359607A
Inventor
Russell C Jones
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Griscom Russell Co
Original Assignee
Griscom Russell Co
Priority date (The priority date 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 date listed.)
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Publication date
Application filed by Griscom Russell Co filed Critical Griscom Russell Co
Priority to US359607A priority Critical patent/US1454053A/en
Application granted granted Critical
Publication of US1454053A publication Critical patent/US1454053A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/355Heat exchange having separate flow passage for two distinct fluids
    • Y10S165/40Shell enclosed conduit assembly
    • Y10S165/401Shell enclosed conduit assembly including tube support or shell-side flow director
    • Y10S165/405Extending in a longitudinal direction
    • Y10S165/406Helically or spirally shaped
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/916Oil cooler

Definitions

  • the object of the present invention is to provide a heat exchanger and particularly a cooler of the type above mentioned in which the surfaces of the heat transferring tubes are scoured throughout their len 11 so that there will beno' accumulation 0 congealed oil at any point along the length of the tube.
  • the scouring action takes lace continuously during the operation 0 the apparatus and serves to maintain the heat transferring surfaces of the tubes at all times in condition for the most advantageous heat transfer.
  • Oil coolers of the kind described in my copending application above referred to consist essentiall of a shell with inlet and outlet passages or the oil to be cooled, the shell containing a series of longitudinal tubes through which the cooling liquid is circulated.
  • Supported within the shell is a series of baflle'plates connected together to form a continuous helical passa efrom the inlet to the outlet passage 0 the shell, whereby in traversing the short length of 40 the shell the-oil is caused to pass again and again across the tubes containing the cooling liquid, thus providing in an apparatus of small dimensions a passage for the oil man times the length of the shell whereby an e fective cooling of the oil is obtained.
  • bafiie plates are of perforated for the passage of the tubes which are set close together in the shell.
  • the oil was found that there was a tendency of the oil to congeal in the corners at the intersection of the tubes and the bafiie plates, particularly on he'atfrom the oil to the liquid.
  • each shaped T to constitute a single turn of the screw and which rendered a considerable portion of the tubesurfa'ce in'efl'ective for the transfer- ⁇ of is thepurpose of the resent invention to prevent this accumulation of' congealed oil, which purpose is secured cssentia lyby providing a clearance between the battles and the, tubes sufficient to cause a slight shortcircuiting of a portion of'the oil along each tube from one section of the helical-bathe to the next, the flow of the oil under pressure through the narrow passage around-the I0 rapidl asit forms, whereby the tubes are he to can throughout their length n the accompanying drawings-1,1 have illustrated my improvement a plied tea cooler of the. character disclose in my said patent, and in said drawings,
  • Figure 1 is a longitudinal section of my Fig. 2 is a transverse section through the central portion of my improved cooler;
  • FIGs. 3 and 4 are enlarged details showingKthe improved b'afile construction.
  • he cooling liquid is circulated throu h tubes 4 supported at'one end in. the tu sheet 5 clamped against one end of the shell by a service header 6 and supported at the head or drum 7 which is mounted to sli e longitudinally of the shell in a packed bearing 8 with the expansion and contraction of the tubes.
  • the service header 6 is divided into' inlet and outletcompartments by a transverse partition, whereby the cooling liquid passes from the inlet 9 through the tubes at the upper half of the bundle, thence through the floating head 7 to the outlet 10.
  • the oil is caused to flow transversely of the tubes through the shell by a spiral 'bafie made up of separate plates 11, each bent to form a single helix of the spiral 'withthe edges of the adjacent helices aligned with *each other and in some cases attached toprovide a long narrow passage for the oil from the inlet to the outlet through which the oil may be forced with an appreciable velocity in order to prevent its congealmg on the tubes.
  • the separate bafiie plates 11 are preferably maintained in properly spaced relation by short sleeves or th mbles 12 mounted on rods 13 arranged around the periphery of the tube bundle and abuttlng at their opposite ends against the tube sheet 4 and floating head "7, respectively.
  • the baflie plates 11 are preferably cut out at the center to receive a rod 14: whose ends are supported in recesses in the tube sheet and header. 7
  • cross currents keep the tube surfaced scoured. clean on all sides, particularly at the intersection of the baflie plates where the main current of oil would otherwise be at low velocity.
  • Thecross currents also serve to keep the oil well agitated, thereby increasing the ethciency by constantly bringing fresh oil against the heat-absorbing surfaces of the tubes;
  • the agitation of the oil through the cross currents also counteracts the tendency of the oil to acquire a higher velocity at the surface of the shell through the effect of centrifugal force and prevents the formation of ockets at the middle of the shell.
  • baflies fitting closely on the center rod 14 and also on the peripheral rods '13.
  • These latter rods instead of abutting against the flat faces of the tube sheet and head 7, may be set in sockets formed in the faces of the sheet and head wall, whereby the baflles will be maintained in fixed relation to the tubes so that the tubes will be aeeaoaa my patent above mentioned, it is to be understood that the improvement may be applied with advantage to other forms of baflies, and
  • a shell for the circulating liquid means in said shell for causing a main current of said liquid to flow in acircuitous path, and means for causing sec fluid, baflies in said shell arranged to cause a main current of said liquid to be treated in a circuitous path across said tubes, 1 and means for causing auxiliary cross currents of said liquids along the tube surfaces.
  • baflies in said shell arranged to provide a circuitous passage from the inlet to the outlet opening, and passages through the said bafiles for producing cross currents in the fluid in directions different from the main current along the baffles.
  • baflies arranged in said shell forming a'con tinuous CH'CUllJOHS passage from inlet to outlet opening, tubes in said shell for the pasondary cross currents in said main current, Y

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

Description

May 8, 1923 R. C. JONES OIL COOLER Filed Feb. 18 1920 Patented May 8,1923.
Russian. c. Jorms'or imoimvrnmi, Nnw Yonx, s'ssreno'a rro an emseoi-nussnri f j comrnmz, or new YORK,
A. conrona'rron, orgnmwsnn.
'oincoonnnf Application medIebi-uary 1s, oz'c. s mi in}. 355,60
To whom it may concern}- the 'far side of the in the of 36.
p B ait known that I, Russnrn Jonas, a the flow of the oil, the congealed oil gradu citizen. of the United States, residing at. ally accumulating in the shape of afillet Bronxville in the county of Westchester, a State of ew' York, have invented, certain new and useful Improvements in Oil Coolers' and-I do hereby declare. the following .to be a full, clear, and exact description of g the invention, such as will enable others lo skilled in the artto which it appertains to make and use the same. This invention relates to improvements in oil coolers, particularly of the t pe disclosed in the atent to R. C.-Jones, 0. 1,335,506, issued arch 30, 1920. f
The object of the present invention is to provide a heat exchanger and particularly a cooler of the type above mentioned in which the surfaces of the heat transferring tubes are scoured throughout their len 11 so that there will beno' accumulation 0 congealed oil at any point along the length of the tube. The scouring action takes lace continuously during the operation 0 the apparatus and serves to maintain the heat transferring surfaces of the tubes at all times in condition for the most advantageous heat transfer.
Oil coolers of the kind described in my copending application above referred to consist essentiall of a shell with inlet and outlet passages or the oil to be cooled, the shell containing a series of longitudinal tubes through which the cooling liquid is circulated. Supported within the shell is a series of baflle'plates connected together to form a continuous helical passa efrom the inlet to the outlet passage 0 the shell, whereby in traversing the short length of 40 the shell the-oil is caused to pass again and again across the tubes containing the cooling liquid, thus providing in an apparatus of small dimensions a passage for the oil man times the length of the shell whereby an e fective cooling of the oil is obtained. As v constructed for actual commercial use the bafiie plates are of perforated for the passage of the tubes which are set close together in the shell. As originally constructed it was found that there was a tendency of the oil to congeal in the corners at the intersection of the tubes and the bafiie plates, particularly on he'atfrom the oil to the liquid.
tubes acting to scour the congealed oil 01f as improved oil cooler;
from the inlet passage other end by a floatin sheet iron, each shaped T to constitute a single turn of the screw and which rendered a considerable portion of the tubesurfa'ce in'efl'ective for the transfer-{of is thepurpose of the resent invention to prevent this accumulation of' congealed oil, which purpose is secured cssentia lyby providing a clearance between the battles and the, tubes sufficient to cause a slight shortcircuiting of a portion of'the oil along each tube from one section of the helical-bathe to the next, the flow of the oil under pressure through the narrow passage around-the I0 rapidl asit forms, whereby the tubes are he to can throughout their length n the accompanying drawings-1,1 have illustrated my improvement a plied tea cooler of the. character disclose in my said patent, and in said drawings,
Figure 1 is a longitudinal section of my Fig. 2 is a transverse section through the central portion of my improved cooler; and
Figs. 3 and 4 are enlarged details showingKthe improved b'afile construction.
eferring'to the drawings, 1 i dicates the shell. through which the oil is circulated 2 to the outlet passage 3. p a
, he cooling liquid is circulated throu h tubes 4 supported at'one end in. the tu sheet 5 clamped against one end of the shell by a service header 6 and supported at the head or drum 7 which is mounted to sli e longitudinally of the shell in a packed bearing 8 with the expansion and contraction of the tubes. The service header 6 is divided into' inlet and outletcompartments by a transverse partition, whereby the cooling liquid passes from the inlet 9 through the tubes at the upper half of the bundle, thence through the floating head 7 to the outlet 10.
The oil is caused to flow transversely of the tubes through the shell by a spiral 'bafie made up of separate plates 11, each bent to form a single helix of the spiral 'withthe edges of the adjacent helices aligned with *each other and in some cases attached toprovide a long narrow passage for the oil from the inlet to the outlet through which the oil may be forced with an appreciable velocity in order to prevent its congealmg on the tubes. The separate bafiie plates 11 are preferably maintained in properly spaced relation by short sleeves or th mbles 12 mounted on rods 13 arranged around the periphery of the tube bundle and abuttlng at their opposite ends against the tube sheet 4 and floating head "7, respectively. The baflie plates 11 are preferably cut out at the center to receive a rod 14: whose ends are supported in recesses in the tube sheet and header. 7
The apparatus so far described is the same as that disclosed in my patent referred to above. In the improve construction shown in the drawings, the baffle plates, in-
stead of closely fitting the tubes at the points a of intersection of the tubes and plates, have the holes for the passage of the tubes of larger diameter than the tubes, as shown particularly in Fig. '3 of the drawings, whereby there is provided an annular passage 15 through the baflies around each tube forming, as it were, a short-circuit from one turn of the helix to the adjacent turn. These short-circuiting passages serve several useful functions. In the first place, the most important, they prevent the accumulation of congealed oil at any point on the tube surface. The annular passage, while wide enough not to be stopped with sediment or oil film, is narrow enough to insure a rapid velocity of the oil through the passage forming, as it were, large numbers of cross currents of oil which extend well into.
the main current of oil, following the spiral path between the baflies. These cross currents keep the tube surfaced scoured. clean on all sides, particularly at the intersection of the baflie plates where the main current of oil would otherwise be at low velocity. Thecross currents also serve to keep the oil well agitated, thereby increasing the ethciency by constantly bringing fresh oil against the heat-absorbing surfaces of the tubes; The agitation of the oil through the cross currents also counteracts the tendency of the oil to acquire a higher velocity at the surface of the shell through the effect of centrifugal force and prevents the formation of ockets at the middle of the shell.
It wil be understood that it is only the holes in the bafile plates for the passage of the tubes which are of enlarged diameter, the baflies fitting closely on the center rod 14 and also on the peripheral rods '13. These latter rods, instead of abutting against the flat faces of the tube sheet and head 7, may be set in sockets formed in the faces of the sheet and head wall, whereby the baflles will be maintained in fixed relation to the tubes so that the tubes will be aeeaoaa my patent above mentioned, it is to be understood that the improvement may be applied with advantage to other forms of baflies, and
the invention is not to be understood as limited to my prior structure, except in so far as recited in the appended claims.
I have described my invention as particularly applicable to a heat exchan r in which both heat transferring 1i ui s are oils. It is evident, however, that t e appw r-atus is equally applicable for efiecting heat transfer between any two liquids either one of which is a liquid whose vlscosity changes with temperature. The apparatus may be advantageously employed in effecting heat transfer between non-viscous liquids in cases where it is desired to scour the tubes'clean of impurities or other substances which may be contained in the liquid.
I 'claim: 1 v
1. In an apparatus of the class described, the combination of a shell for the circulating liquid, means in said shell for causing a main current of said liquid to flow in acircuitous path, and means for causing sec fluid, baflies in said shell arranged to cause a main current of said liquid to be treated in a circuitous path across said tubes, 1 and means for causing auxiliary cross currents of said liquids along the tube surfaces.
4. In an apparatus of the class described,
the combination of a shell for the fluid to be treated, tubes extending through said shell for a second fluid, said shell having inlet and outlet openings, baflies in said shell arranged to provide a circuitous passage from the inlet to the outlet opening, and passages through the said bafiles for producing cross currents in the fluid in directions different from the main current along the baffles.
. 5. In an apparatus of the class described, the combination of a shell having inlet and outlet passages for the fluid to be treated,
baflies arranged in said shell forming a'con tinuous CH'CUllJOHS passage from inlet to outlet opening, tubes in said shell for the pasondary cross currents in said main current, Y
sage of the second fluid, said tubes projectpassa e from the inlet to the outlet opening through said bafiles and passages ing, tubes extending longitudinally of said through said bafiies around said tubes for shell and passing through said baflie in reducing cross currents in the fluid flowparallelism with the axis of the spiral and 5 mg through said passage from the inlet to annular passages in said baflles at the inthe outlet of the shell. tersection of the tubes and the baffles as and 6. In an apparatus of the class described, for the purpose set forth. the combination of ashell, inlet and outlet In testimony whereof I aflix my signaopenings for the fluid to be treated, a bafile ture. 10 in said shell forming a continuous spiral RUSSELL C. JONES.
US359607A 1920-02-18 1920-02-18 Oil cooler Expired - Lifetime US1454053A (en)

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Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2442180A (en) * 1945-10-01 1948-05-25 Young Radiator Co Oil cooler construction
US2496301A (en) * 1944-02-16 1950-02-07 Howard Iron Works Inc Tube bundle assembly for heat exchangers and the like
US2560245A (en) * 1946-11-15 1951-07-10 Garrett Corp Two-port cooler
US2591658A (en) * 1948-01-09 1952-04-01 Directie Staatsmijnen Nl Process and apparatus for the separation of coke-oven gas
US2995343A (en) * 1957-07-29 1961-08-08 Griscom Russell Co Heat exchanger construction
US3610328A (en) * 1969-09-25 1971-10-05 Sun Oil Co Prevention of crevice coking in heat exchangers
US4120350A (en) * 1975-03-19 1978-10-17 The Babcock & Wilcox Company Tube support structure
US4836276A (en) * 1987-03-09 1989-06-06 Nippondenso Co., Ltd. Heat exchanger for engine oil
US5454429A (en) * 1992-05-23 1995-10-03 Neurauter; Peter Rods and mandrel turbulators for heat exchanger
US5832991A (en) * 1995-12-29 1998-11-10 Cesaroni; Joseph Anthony Tube and shell heat exchanger with baffle
US6092589A (en) * 1997-12-16 2000-07-25 York International Corporation Counterflow evaporator for refrigerants
US6681764B1 (en) * 1997-06-16 2004-01-27 Sequal Technologies, Inc. Methods and apparatus to generate liquid ambulatory oxygen from an oxygen concentrator
US20040173341A1 (en) * 2002-04-25 2004-09-09 George Moser Oil cooler and production method
US20040194932A1 (en) * 2003-02-25 2004-10-07 Honeywell International Inc. Solid buffer rods in high temperature heat exchanger
US20080190593A1 (en) * 2007-02-09 2008-08-14 Xi'an Jiaotong University Single shell-pass or multiple shell-pass shell-and-tube heat exchanger with helical baffles
WO2017213949A1 (en) * 2016-06-06 2017-12-14 Aerco International, Inc. Fibonacci optimized radial heat exchanger
US20180112925A1 (en) * 2015-04-24 2018-04-26 Hexsol Italy Srl Tube-nest heat exchanger with improved structure
US10559389B2 (en) 2017-02-06 2020-02-11 Battell Energy Alliance, LLC Modular nuclear reactors including fuel elements and heat pipes extending through grid plates, and methods of forming the modular nuclear reactors
US10910116B2 (en) 2017-03-16 2021-02-02 Battelle Energy Alliance, Llc Nuclear reactors including heat exchangers and heat pipes extending from a core of the nuclear reactor into the heat exchanger and related methods
US20220299270A1 (en) * 2019-08-22 2022-09-22 Commonwealth Scientific And Industrial Research Organisation Moving-bed particle heat exchanger
WO2025101511A1 (en) * 2023-11-06 2025-05-15 Lummus Technology Llc Heat exchanger with helical baffles

Cited By (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2496301A (en) * 1944-02-16 1950-02-07 Howard Iron Works Inc Tube bundle assembly for heat exchangers and the like
US2442180A (en) * 1945-10-01 1948-05-25 Young Radiator Co Oil cooler construction
US2560245A (en) * 1946-11-15 1951-07-10 Garrett Corp Two-port cooler
US2591658A (en) * 1948-01-09 1952-04-01 Directie Staatsmijnen Nl Process and apparatus for the separation of coke-oven gas
US2995343A (en) * 1957-07-29 1961-08-08 Griscom Russell Co Heat exchanger construction
US3610328A (en) * 1969-09-25 1971-10-05 Sun Oil Co Prevention of crevice coking in heat exchangers
US4120350A (en) * 1975-03-19 1978-10-17 The Babcock & Wilcox Company Tube support structure
US4836276A (en) * 1987-03-09 1989-06-06 Nippondenso Co., Ltd. Heat exchanger for engine oil
US5454429A (en) * 1992-05-23 1995-10-03 Neurauter; Peter Rods and mandrel turbulators for heat exchanger
US5832991A (en) * 1995-12-29 1998-11-10 Cesaroni; Joseph Anthony Tube and shell heat exchanger with baffle
US6681764B1 (en) * 1997-06-16 2004-01-27 Sequal Technologies, Inc. Methods and apparatus to generate liquid ambulatory oxygen from an oxygen concentrator
US6698423B1 (en) * 1997-06-16 2004-03-02 Sequal Technologies, Inc. Methods and apparatus to generate liquid ambulatory oxygen from an oxygen concentrator
USRE43398E1 (en) * 1997-06-16 2012-05-22 Respironics, Inc. Methods and apparatus to generate liquid ambulatory oxygen from an oxygen concentrator
US6092589A (en) * 1997-12-16 2000-07-25 York International Corporation Counterflow evaporator for refrigerants
US6530421B1 (en) 1997-12-16 2003-03-11 York International Corporation Counterflow evaporator for refrigerants
US20040173341A1 (en) * 2002-04-25 2004-09-09 George Moser Oil cooler and production method
US6988540B2 (en) * 2003-02-25 2006-01-24 Honeywell International Inc. Solid buffer rods in high temperature heat exchanger
US20040194932A1 (en) * 2003-02-25 2004-10-07 Honeywell International Inc. Solid buffer rods in high temperature heat exchanger
US20080190593A1 (en) * 2007-02-09 2008-08-14 Xi'an Jiaotong University Single shell-pass or multiple shell-pass shell-and-tube heat exchanger with helical baffles
US7740057B2 (en) * 2007-02-09 2010-06-22 Xi'an Jiaotong University Single shell-pass or multiple shell-pass shell-and-tube heat exchanger with helical baffles
US20110094720A1 (en) * 2007-02-09 2011-04-28 Xi'an Jiaotong University Shell-and-tube heat exchanger with helical baffles
US8540011B2 (en) 2007-02-09 2013-09-24 Xi'an Jiaotong University Shell-and-tube heat exchanger with helical baffles
US20180112925A1 (en) * 2015-04-24 2018-04-26 Hexsol Italy Srl Tube-nest heat exchanger with improved structure
US10684077B2 (en) * 2015-04-24 2020-06-16 Hexsol Italy Srl Tube-nest heat exchanger with improved structure
WO2017213949A1 (en) * 2016-06-06 2017-12-14 Aerco International, Inc. Fibonacci optimized radial heat exchanger
CN109716054A (en) * 2016-06-06 2019-05-03 热高国际公司 Fibonacci optimization of radial heat exchangers
US10627170B2 (en) 2016-06-06 2020-04-21 Aerco International, Inc. Fibonacci optimized radial heat transfer
US10559389B2 (en) 2017-02-06 2020-02-11 Battell Energy Alliance, LLC Modular nuclear reactors including fuel elements and heat pipes extending through grid plates, and methods of forming the modular nuclear reactors
US10910116B2 (en) 2017-03-16 2021-02-02 Battelle Energy Alliance, Llc Nuclear reactors including heat exchangers and heat pipes extending from a core of the nuclear reactor into the heat exchanger and related methods
US20220299270A1 (en) * 2019-08-22 2022-09-22 Commonwealth Scientific And Industrial Research Organisation Moving-bed particle heat exchanger
US12196495B2 (en) * 2019-08-22 2025-01-14 Commonwealth Scientific And Industrial Research Organisation Moving-bed particle heat exchanger
WO2025101511A1 (en) * 2023-11-06 2025-05-15 Lummus Technology Llc Heat exchanger with helical baffles

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