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US3490523A - Transfer device - Google Patents

Transfer device
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US3490523A
US3490523AUS719594AUS3490523DAUS3490523AUS 3490523 AUS3490523 AUS 3490523AUS 719594 AUS719594 AUS 719594AUS 3490523D AUS3490523D AUS 3490523DAUS 3490523 AUS3490523 AUS 3490523A
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envelope
transfer device
channels
flow
sheets
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US719594A
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William G Esmond
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US Department of Health and Human Services
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US Department of Health and Human Services
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Jan. 20, 1970 w. G. ESMOND TRANSFERDEVICE Filed April 8, 1968 WQLLMM G. ESMOND ATTORNEY United States Patent U.S. Cl. 165-166 11 Claims ABSTRACT OF THE DISCLOSURE This disclosure relates to a transfer device which includes a centrally disposed envelope having secured to opposite sides thereof in sealed relation a pair of flow sheets. Each flow sheet has a plurality of longitudinal channels which open towards the respective face of the envelope throughout the lengths of the channels whereby a first fluid may flow through the envelope and a second fluid may flow through the channels of the flow sheet. The envelope is formed of a flexible material and when clamped by the flow sheets, a plurality of individual channels is formed within the envelope. The channels of the flow sheets are preferably of the sine-cosine configuration. The transfer device, depending upon the material from which the envelope is formed, may be utilized as a heat exchanger, an artificial kidney or an artificial lung or gill.
This invention relates in general to new and useful improvements in transfer devices, and more particularly to a novel transfer device which may be used as an exchanger of all types both in the industrial and medical fields. The transfer device includes a central envelope through which a first fluid flows and the material of which envelope is varied in accordance with the desired transfer. The envelope is clamped between two face sheets which have formed therein longitudinally extending channels. The envelope is of a flexible construction and when clamped between the face sheets, the channels of the face sheets automatically form channels within the envelope to provide for a controlled flow :path therethrough. n
A primary object of this invention is to provide a novel transfer device which is of a construction to provide an even flow resistance geometry so that even amounts of two fluids may be constantly and evenly distributed on the opposite sides of a mass transfer or heat exchange surface.
Another object of this invention is to provide a novel transfer device wherein two fluids are passed through an envelope and; on opposite surfaces of the envelope between the envelope and a pair of face sheets, and the face sheets and envelope having formed therein channels which are of the sine-cosine configuration and wherein there is a relative crossing of the channels of the two face sheets and a like crossing of the channels within the envelope whreby there is a constant intermixing of the fluid flowing through the envelope and a constantly changmg relationship between the fluid in the envelope and the fluid passing between the envelope and the face sheets.
Another object of this invention is to provide a novel transfer device which may be utilized as a heat transfer device when the envelope thereof is formed of an impermeable material and at the same time is of a construction whreein when the envelope is in the form of a membrane, the transfer device will have uses in the medical field depending upon the construction of the membrane 7 envelope and the particular fluids passed therethrough.
3,490,523 Patented Jan. 20, 1970 Still another object of this invention is to provide a novel light weight transfer device which can be very inexpensively mass produced.
A still further object of this invention is to provide a novel transfer device wherein the flow sheets are formed of a transparent material and the envelope is in the form of a membrane whereby the passage of bubbles through the membrane may be visually observed so as to visually determine the operation of the transfer device.
With the above and other objects in view that will hereinafter appear, the nature of the invention will be more clearly understood by reference to the following detailed description, the appended claims and the several views illustrated in the accompanying drawings.
In the drawings:
FIGURE 1 is an exploded perspective view of the transfer device and shows generally the details thereof.
FIGURE 2 is a schematic single line sectional view taken along theline 22 through one of the flow sheets.
FIGURES 3 and 4 are schematic single line sectional views similar to FIGURE 2 for taking along the lines 3-3 and 44, respectively.
FIGURE 5 is a schematic single line transverse sectional view taken through the entire transfer device along the line 55 of FIGURE 1.
FIGURE 6 is a fragmentary enlargement of FIGURE 5 and shows specifically the details of the transfer device.
Referring now to the drawings in detail, it will be seen that there is illustrated in FIGURE 1 the transfer device which is generally identified by thenumeral 10. Thetransfer device 10 includes a central envelope, which is generally identified by thenumeral 11, and through which a first fluid is intended to flow. On opposite sides of theenvelope 11 there is clamped a pair offlow sheets 12 and 13. It is intended that a second fluid flow between the flow sheets and the envelope.
Considering first the construction of theenvelope 11, it will be seen that it is formed of a pair ofsheets 14 and 15 of flexible material which has positioned in the opposite ends thereof flow tubes 16 and 17. Thesheets 14 and 15 are bonded together in any suitable manner about the peripheral edges thereof and to the flow tubes 16 and 17 to form a fluid tight seal therewith.
It is to be noted that one end of each of the flow tubes 16 and 17 is open to facilitate either the inlet or discharge of a fluid and the opposite end thereof is closed by means of a suitable plug. In addition, each of the flow tubes 16 and 17 is provided with anelongated slot 18 which opens longitudinally of theenvelope 11 so as to provide for the even distribution of fluid across the width of the envelope. For purposes of description, the flow tube 16 is an inlet tube and the flow tube 17 is a discharge tube.
Each of theflow sheets 12 and 13 is formed with a plurality of longitudinally extendingchannels 20 which open towards theenvelope 11 and together with theenvelope 11 form flow passages for a second fluid. These channels may vary in cross section, as is clearly shown in FIGURES 2, 3 and 4.
Adjacent the opposite ends of each of theflow sheets 12 and 13 there is provided a pair of transversely extending channels which are preferably of a half cylinder configuration. The channels at each end of eachflow sheet 12 and 13 includes aninner channel 21 and anouter channel 22. Thechannels 21 and 22 of the flow sheets combine to define transverse passages. It will be readily apparent that thechannels 21 snugly fit about the flow tubes 16 and 17 and the respective enlarged portions of theenvelope 11 while thechannels 22 combine to define inlet and discharge passages for the second fluid. At one end of the transfer device, the cooperating pair ofchannels 22 is provided with an inlet fitting 23 at one end and a plug 24 at the opposite end. The other of the passages defined by thechannels 22 is provided with a discharge fitting 25 at one end and aplug 26 at the opposite end.
It is to be noted that thechannels 20 extend across thechannels 21 and terminate in thechannels 22 so that there is fluid flow from onechannel 22 across thechannels 21 and to theother channel 22. It is also to be noted that the peripheral edges of theflow sheets 12 and 13 are planar whereby a suitable seal may be formed between theflow sheets 12 and 13 and theenvelope 11.
It is to be understood that theenvelope 11 is to be formed of a suitably flexible material whereby when theenvelope 11 is clamped between theflow sheets 12 and 13, not only will there be formed as separate fluid passages between the flow sheets and the envelope within therespective channels 20, but also the envelope will be collapsed between the contacting portions of the flow sheets to form a plurality of individual channels orpassages 27 within the envelope. Thus, there is a controlled flow of fluid both within the envelope and between the envelope and the flow sheets.
It has been found that the most efficient configuration of thechannels 20 is that of the sine-cosine curve. Furthermore, it has been found to be most effective if theflow sheets 12 and 13 are identical and when disposed in face-to-face relations, thechannels 20 thereof are 180 out of phase. With this particular type of construction, the twoflow sheets 12 and 13 reinforce one another with the ridges thereof defining thechannels 20 crossing one another at regular intervals and preventing relative collapse. In addition, the channels or passages formed in the envelope are disposed in constantly crossing relation with the result that there is produced within the fluid flowing through the envelope a shearing and mixing force which constantly changes the relationship of the fluid passing through the envelope with respect to the envelope and at the same time constantly changes the relationship of the fluid within the envelope relative to that passing around the envelope. This provides for a maximum efliciency in the transfer device.
At this time it is pointed out that although thechannels 20 are illustrated as being uniform, it is to be understood that certain of thechannels 20 may be of a greater volume than others. By so constructing theflow sheets 12' and 13, a greater priming volume may be provided. The priming volume of the transfer device may initially be accurately controlled.
It is to be understood that fluids are to be passed through the transfer device under pressure. As a result, it is necessary to tightly clamp theflow sheets 12 and 13 against the envelope in addition to sealing the peripheral edges of the flow, sheets to the envelope. Inasmuch as this clamping can be effected in many ways which in of itself is not a part of this invention, there has been no specific illustration of the clamping devices. However, it is desirable to set forth here several illustrative clamping methods. The simplest clamping method would be the 'clamping of the transfer device between a pair of rigid plates. In undersea work the pressure of the water alone has been found sufficient to hold the unit flat and retain its precise geometry. Theflow sheets 12 and 13 may be held in clamped relation to theenvelope 11 by submerging the transfer device in a pool of mercury. Another method of holding the transfer device together is to fix it between two air filter pressurized bladders which are held together by suitable supports such as two vacuum formed blisters clamped together with an air bladder in each and with the transfer unit clamped between the two air bladders. Further, if the expense of the transfer device Warrants it, theflow sheets 12 and 13 may be formed of a heavy rigid construction so that the flow sheets themselves. o ld resist distortion.
When thetransfer device 10 is utilized as a simple heat exchanger, thesheets 14 and 15 of theenvelope 11 must be formed of an impermeable material. It has been found that this material may be a thin Teflon film or a Mylar film. In addition, even very thin metal sheets, including silver and stainless steel, may be used to form the envelope. Normally, the fluid whose temperature is to be controlled is passed through the envelope while the heat exchanger fluid is passed between the envelope and the flow sheets.
When thetransfer device 10 is utilized as an artificial lung or gill, it is necessary that theenvelope 11 be formed of a membrane material which is permeable to the gases (oxygen and carbon dioxide) that must be transported. It has been found that the membrane material best suited for the formation of thesheets 14 and 15 includes a very thin Teflon film, silicon rubber and a newly developed siliconpolycarbonate which has additional strength. In the operation of the artificial lung, venous blood is pumped into theenvelope 11 while oxygen is led through the outer compartments between theflow sheets 12 and 13 in the envelope with the oxygen preferably flowing countercurrent to the flow of the blood.
The oxygen diffuses through or dissolves in the material of theenvelope 11 and finally is picked up in the blood and oxygenates through the hemoglobin in the red cells of the blood. At the same time, carbon dioxide diffuses out of the blood through the membrane envelope and is swept in a rapid stream of excess oxygen. The oxygenated blood is then returned to the patient into an artery.
When thetransfer device 10 is utilized as an artificial kidney, the material of thesheets 14 and 15 of the envelope must be that of a membrane which is selectively permeable to some specific toxin in the blood or be nonselective to diifusible ions and molecules of low molecular weight such as a thin cellulose cellophane member or cellulose member from hydrolized cellulose acetate. In the use of the transfer device as an artificial kidney, a bath solution or electrolyte is passed through the outer compartments defined between theflow sheets 12 and 13 and the envelope while the blood to be treated is pumped through the envelope. This electrolyte is preferably held at a normal temperature of 37.5" C. although the temperature may be slightly varied. The electrolyte is a bath solution containing NaCl, Na acetate, MgCI- KCl, CaCl and glucose in proper concentrations such as Na+ 132 meq./ l., CllOO meq./l., Ca++ 2.5 meq./l., Mg++ 1.5 meq./l, K+ 2 to 4 meq/l. and glucose to 200 mg. percent or more.
The electrolyte is pumped or siphoned by gravity through the outer compartments and recirculated or possibly pased directly down a drain in One pass at the rate of 500 ml./min. The blood is led through thecellulose membrane envelope 11 by arterial pressure or by a pump and after the loss of toxins (uremic or drugs) by dialysis, the blood is led back through the tubing into the patients veins.
At this time it is pointed out that although the preferred pattern of thechannels 20 of the flow sheets is preferably that of a sine-cosine cur-ve, it is to be understood that this pattern may be interrupted at intervals or may be slightly modified without varying the spirit and scope of the invention.
It is also pointed out here that while theflow sheets 12 and 1 3 may be formed in any desired manner, it has been found that the flow sheets may be most economically formed from plastic sheet material by a vacuum molding process. When the material of theflow sheets 12 and 13 is a transparent material, the operation of the transfer device, particularly when utilized as either an artificial kidney or an artificial lung, may be readily observed and the rate of bubbling of gases outwardly from theenvelope 11 may be visually detected,
Although the flow sheets may be secured to the envelope by any type of sealing medium, it has been found that in many instances where the envelope and the flow sheets are formed of plastic materials, a suitable waterproof cement manufactured by General Electric and identified as RTV118 has proved to be very satisfactory.
Although only a single embodiment of the transfer device has been specifically illustrated and described herein, it is to be understood that minor variations may be made in the transfer device without departing from the spirit and scope of the invention, as defined by the appended claims.
I claim:
1. A transfer device for fluids comprising an envelope having first fluid inlet and discharge fittings at the opposite ends thereof, and a pair of flow sheets disposed on opposite sides of said envelope and being sealed thereto at least along peripheral edge portions of said envelope, each of said flow sheets having formed therein longitudinally extending channels opening substantially throughout the length thereof to face surfaces of said envelope wherein said channels are of the sine-cosine configuration and the two flow sheets are so positioned that said channels are arranged in crossing relation, and second fluid inlet and discharge fittings at the opposite ends thereof.
2. The transfer device of claim 1 wherein said envelope is flexible with said envelope being clamped between said flow sheet intermediate said channels with intermediate portions of said envelope projecting into said channels and forming longitudinal flow passages in said envelope.
3. The transfer device of claim 1 wherein said channels of the two flow sheets are 180 out of phase.
4. The transfer device of claim 1 wherein said flow sheets define at each end thereof two transverse assages, inner ones of said transverse passages receiving said first fluid inlet and discharge fittings, and outer ones of said transverse passages forming parts of said second fluid inlet and discharge means, and said longitudinal channels extending across said inner transverse passages and terminating in said outer transverse passages.
5. The transfer device of claim 1 wherein said envelope is in the form of a membrane capable of limited predetermined fluid flow therethrough.
6. The transfer device of claim 1 wherein said transfer device is an artificial kidney and wherein said envelope is in the form of a membrane capable of having passed therethrough by diffusion waste products from blood flowing through said envelope. i
7. The artificial kidney of claim 6 wherein said membrane envelope is formed of a cellulose material selected from a group including cellulose cellophane and hydrolized cellulose acetate.
8. The artificial kidney of claim 6 wherein an electrolyte is passed through said channels.
9. The transfer device of claim 1 wherein said transfer device is an artificial lung with said envelope being formed of a membrane capable of passing gases from blood running through said envelope and delivering oxygen from said channels to blood within said envelope.
10. The artificial lung of claim 9 wherein said membrane is formed of a material from a group including Teflon, silicon rubber and silicon-polycarbonate;
11. The transfer device of claim 1 wherein said transfer device is a heat exchanger and said envelope is formed of an impermeable material.
References Cited UNITED STATES PATENTS 2,735,812 2/1956 Van Hoek 210-321 X 3,216,492 11/ 1965 Weaver -166 X 3,332,746 7/1967 Claff et al 23-2585 3,362,540 1/1968 Bluemle 210-321 3,398,091 8/1968 Greatorex 210-321 X 3,412,865 11/1968 Lantz et a1. 210-321 3,435,893 4/1969 Withers 165-180 X MEYER PERLIN, Primary Examiner T. W. STREULE, Assistant Examiner US. Cl. X.R. 23-2585; 165-46; 210-321
US719594A1968-04-081968-04-08Transfer deviceExpired - LifetimeUS3490523A (en)

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Cited By (32)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US3567028A (en)*1968-12-261971-03-02Research CorpMembrane envelope assembly
US3602298A (en)*1969-04-251971-08-31Mecislaus Joseph CiesielskiHeat exchanger
US3667612A (en)*1969-09-041972-06-06Joe H LeonardArtificial kidney system
US3709367A (en)*1970-04-081973-01-09Baxter Laboratories IncSupport structure for membrane diffusion devices
US3729098A (en)*1971-02-081973-04-24J SerurTreating blood
US3743097A (en)*1968-12-161973-07-03Rhone Poulenc SaDialyzer
US3839204A (en)*1972-04-271974-10-01Gen ElectricIntegral blood heat and component exchange device and two flow path membrane blood gas exchanger
US3847211A (en)*1969-01-281974-11-12Sub Marine Syst IncProperty interchange system for fluids
US3910841A (en)*1974-04-021975-10-07William G EsmondStacked exchange device
FR2340758A1 (en)*1976-02-161977-09-09Gambro Ag DEVICE FOR THE DIFFUSION OF SUBSTANCES BETWEEN TWO FLUIDS THROUGH SEMI-PERMEABLE MEMBRANES
US4054527A (en)*1976-06-251977-10-18Esmond William GCountercurrent capillary transfer device
US4173537A (en)*1977-05-231979-11-06Newhart Earle EIntegral artificial kidney unit
WO1980002806A1 (en)*1979-06-201980-12-24Newhart RBlood perfusion units
WO1981001247A1 (en)*1979-11-011981-05-14Newhart RIntegral artificial kidney unit
US4282099A (en)*1979-12-101981-08-04Jones John LIntegral partitioned hemodialysis unit
US4304669A (en)*1979-07-211981-12-08Sartorius GmbhDevice for the mass transfer between fluids
EP0048943A1 (en)*1980-09-251982-04-07Terumo CorporationOxygenator
WO1986004255A1 (en)*1985-01-251986-07-31James William WalshMembrane processing system and method
US4804469A (en)*1985-01-251989-02-14Walsh James WFlexible jacket membrane processing apparatus
US4892662A (en)*1985-01-251990-01-09Walsh James WMembrane processing method
US5823252A (en)*1994-07-281998-10-20Daimler-Benz AktiengesellschaftTwo-stage evaporator unit
US6551347B1 (en)*1988-09-282003-04-22Life Enhancement Technologies, Inc.Cooling/heating system
US20090178393A1 (en)*2008-01-102009-07-16Jesper NorskMethod and system for purification of exhaust gas from diesel engines
US20100314088A1 (en)*2009-06-112010-12-16Agency For Defense DevelopmentHeat exchanger having micro-channels
US20120305217A1 (en)*2011-06-012012-12-06Alstom Technology LtdHeating element undulation patterns
US10094626B2 (en)2015-10-072018-10-09Arvos Ljungstrom LlcAlternating notch configuration for spacing heat transfer sheets
US10175006B2 (en)2013-11-252019-01-08Arvos Ljungstrom LlcHeat transfer elements for a closed channel rotary regenerative air preheater
US10197337B2 (en)2009-05-082019-02-05Arvos Ljungstrom LlcHeat transfer sheet for rotary regenerative heat exchanger
US10378829B2 (en)2012-08-232019-08-13Arvos Ljungstrom LlcHeat transfer assembly for rotary regenerative preheater
US20190302178A1 (en)*2018-04-032019-10-03Advantest CorporationHeat exchanger and electronic device handling apparatus including the same
CN111928688A (en)*2020-07-222020-11-13武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所)Fluid channel structure of printed circuit board heat exchanger and printed circuit board heat exchanger
US10914527B2 (en)2006-01-232021-02-09Arvos GmbhTube bundle heat exchanger

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Publication numberPriority datePublication dateAssigneeTitle
US2735812A (en)*1952-03-131956-02-21Van hoek
US3216492A (en)*1961-07-031965-11-09John M WeaverExchange unit
US3332746A (en)*1963-03-291967-07-25Single Cell Res Foundation IncPulsatile membrane oxygenator apparatus
US3362540A (en)*1966-08-241968-01-09Research CorpDisc-shaped, multiple cone type dialyzer having a tapered flow path
US3398091A (en)*1966-08-091968-08-20IonicsMembrane separation apparatus and process
US3412865A (en)*1964-11-161968-11-26John F. LontzArtificial kidney
US3435893A (en)*1967-07-311969-04-01Du PontHeat exchanger component formed with flexible plastic tubes

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2735812A (en)*1952-03-131956-02-21Van hoek
US3216492A (en)*1961-07-031965-11-09John M WeaverExchange unit
US3332746A (en)*1963-03-291967-07-25Single Cell Res Foundation IncPulsatile membrane oxygenator apparatus
US3412865A (en)*1964-11-161968-11-26John F. LontzArtificial kidney
US3398091A (en)*1966-08-091968-08-20IonicsMembrane separation apparatus and process
US3362540A (en)*1966-08-241968-01-09Research CorpDisc-shaped, multiple cone type dialyzer having a tapered flow path
US3435893A (en)*1967-07-311969-04-01Du PontHeat exchanger component formed with flexible plastic tubes

Cited By (40)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US3743097A (en)*1968-12-161973-07-03Rhone Poulenc SaDialyzer
US3567028A (en)*1968-12-261971-03-02Research CorpMembrane envelope assembly
US3847211A (en)*1969-01-281974-11-12Sub Marine Syst IncProperty interchange system for fluids
US3602298A (en)*1969-04-251971-08-31Mecislaus Joseph CiesielskiHeat exchanger
US3667612A (en)*1969-09-041972-06-06Joe H LeonardArtificial kidney system
US3709367A (en)*1970-04-081973-01-09Baxter Laboratories IncSupport structure for membrane diffusion devices
US3729098A (en)*1971-02-081973-04-24J SerurTreating blood
US3839204A (en)*1972-04-271974-10-01Gen ElectricIntegral blood heat and component exchange device and two flow path membrane blood gas exchanger
US3910841A (en)*1974-04-021975-10-07William G EsmondStacked exchange device
FR2340758A1 (en)*1976-02-161977-09-09Gambro Ag DEVICE FOR THE DIFFUSION OF SUBSTANCES BETWEEN TWO FLUIDS THROUGH SEMI-PERMEABLE MEMBRANES
US4054527A (en)*1976-06-251977-10-18Esmond William GCountercurrent capillary transfer device
US4173537A (en)*1977-05-231979-11-06Newhart Earle EIntegral artificial kidney unit
WO1980002806A1 (en)*1979-06-201980-12-24Newhart RBlood perfusion units
US4304669A (en)*1979-07-211981-12-08Sartorius GmbhDevice for the mass transfer between fluids
WO1981001247A1 (en)*1979-11-011981-05-14Newhart RIntegral artificial kidney unit
US4282099A (en)*1979-12-101981-08-04Jones John LIntegral partitioned hemodialysis unit
EP0048943A1 (en)*1980-09-251982-04-07Terumo CorporationOxygenator
US4374802A (en)*1980-09-251983-02-22Terumo CorporationOxygenator
US4892662A (en)*1985-01-251990-01-09Walsh James WMembrane processing method
WO1986004255A1 (en)*1985-01-251986-07-31James William WalshMembrane processing system and method
US4804469A (en)*1985-01-251989-02-14Walsh James WFlexible jacket membrane processing apparatus
US6551347B1 (en)*1988-09-282003-04-22Life Enhancement Technologies, Inc.Cooling/heating system
US20030229385A1 (en)*1988-09-282003-12-11Life Enhancement Technologies, Inc.Cooling/heating system
US7001417B2 (en)1988-09-282006-02-21Life Ehancement Technologies, Inc.Cooling/heating system
US5823252A (en)*1994-07-281998-10-20Daimler-Benz AktiengesellschaftTwo-stage evaporator unit
US10914527B2 (en)2006-01-232021-02-09Arvos GmbhTube bundle heat exchanger
US20090178393A1 (en)*2008-01-102009-07-16Jesper NorskMethod and system for purification of exhaust gas from diesel engines
US8127535B2 (en)*2008-01-102012-03-06Haldor Topsøe A/SMethod and system for purification of exhaust gas from diesel engines
US10197337B2 (en)2009-05-082019-02-05Arvos Ljungstrom LlcHeat transfer sheet for rotary regenerative heat exchanger
US10982908B2 (en)2009-05-082021-04-20Arvos Ljungstrom LlcHeat transfer sheet for rotary regenerative heat exchanger
US20100314088A1 (en)*2009-06-112010-12-16Agency For Defense DevelopmentHeat exchanger having micro-channels
US9644899B2 (en)*2011-06-012017-05-09Arvos, Inc.Heating element undulation patterns
US20120305217A1 (en)*2011-06-012012-12-06Alstom Technology LtdHeating element undulation patterns
US10378829B2 (en)2012-08-232019-08-13Arvos Ljungstrom LlcHeat transfer assembly for rotary regenerative preheater
US11092387B2 (en)2012-08-232021-08-17Arvos Ljungstrom LlcHeat transfer assembly for rotary regenerative preheater
US10175006B2 (en)2013-11-252019-01-08Arvos Ljungstrom LlcHeat transfer elements for a closed channel rotary regenerative air preheater
US10094626B2 (en)2015-10-072018-10-09Arvos Ljungstrom LlcAlternating notch configuration for spacing heat transfer sheets
US20190302178A1 (en)*2018-04-032019-10-03Advantest CorporationHeat exchanger and electronic device handling apparatus including the same
US10753971B2 (en)*2018-04-032020-08-25Advantest CorporationHeat exchanger and electronic device handling apparatus including the same
CN111928688A (en)*2020-07-222020-11-13武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所)Fluid channel structure of printed circuit board heat exchanger and printed circuit board heat exchanger

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