US3490523A - Transfer device - Google Patents

Transfer device Download PDF

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US3490523A
US3490523A US719594A US3490523DA US3490523A US 3490523 A US3490523 A US 3490523A US 719594 A US719594 A US 719594A US 3490523D A US3490523D A US 3490523DA US 3490523 A US3490523 A US 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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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/06Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material
    • F28F21/065Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material the heat-exchange apparatus employing plate-like or laminated conduits
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/24Dialysis ; Membrane extraction
    • B01D61/28Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D63/00Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08Flat membrane modules
    • B01D63/089Modules where the membrane is in the form of a bag, membrane cushion or pad
    • 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
    • F28D9/00Heat-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
    • F28D9/0031Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04Elements 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
    • F28F3/042Elements 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
    • F28F3/046Elements 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/12Elements constructed in the shape of a hollow panel, e.g. with channels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2313/00Details relating to membrane modules or apparatus
    • B01D2313/08Flow guidance means within the module or the apparatus
    • 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
    • Y10S165/356Plural plates forming a stack providing flow passages therein
    • Y10S165/373Adjacent heat exchange plates having joined bent edge flanges for forming flow channels therebetween
    • Y10S165/384Thermally bonded side edges

Definitions

  • 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.
  • 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.
  • 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.
  • 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.
  • 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 the line 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.
  • FIGURE 1 the transfer device which is generally identified by the numeral 10.
  • the transfer device 10 includes a central envelope, which is generally identified by the numeral 11, and through which a first fluid is intended to flow. On opposite sides of the envelope 11 there is clamped a pair of flow sheets 12 and 13. It is intended that a second fluid flow between the flow sheets and the envelope.
  • the envelope 11 is formed of a pair of sheets 14 and 15 of flexible material which has positioned in the opposite ends thereof flow tubes 16 and 17.
  • the sheets 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.
  • 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.
  • each of the flow tubes 16 and 17 is provided with an elongated slot 18 which opens longitudinally of the envelope 11 so as to provide for the even distribution of fluid across the width of the envelope.
  • the flow tube 16 is an inlet tube and the flow tube 17 is a discharge tube.
  • Each of the flow sheets 12 and 13 is formed with a plurality of longitudinally extending channels 20 which open towards the envelope 11 and together with the envelope 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.
  • each of the flow sheets 12 and 13 Adjacent the opposite ends of each of the flow 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 each flow sheet 12 and 13 includes an inner channel 21 and an outer channel 22.
  • the channels 21 and 22 of the flow sheets combine to define transverse passages. It will be readily apparent that the channels 21 snugly fit about the flow tubes 16 and 17 and the respective enlarged portions of the envelope 11 while the channels 22 combine to define inlet and discharge passages for the second fluid.
  • the cooperating pair of channels 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 the channels 22 is provided with a discharge fitting 25 at one end and a plug 26 at the opposite end.
  • the channels 20 extend across the channels 21 and terminate in the channels 22 so that there is fluid flow from one channel 22 across the channels 21 and to the other channel 22. It is also to be noted that the peripheral edges of the flow sheets 12 and 13 are planar whereby a suitable seal may be formed between the flow sheets 12 and 13 and the envelope 11.
  • the envelope 11 is to be formed of a suitably flexible material whereby when the envelope 11 is clamped between the flow sheets 12 and 13, not only will there be formed as separate fluid passages between the flow sheets and the envelope within the respective channels 20, but also the envelope will be collapsed between the contacting portions of the flow sheets to form a plurality of individual channels or passages 27 within the envelope. Thus, there is a controlled flow of fluid both within the envelope and between the envelope and the flow sheets.
  • the most efficient configuration of the channels 20 is that of the sine-cosine curve. Furthermore, it has been found to be most effective if the flow sheets 12 and 13 are identical and when disposed in face-to-face relations, the channels 20 thereof are 180 out of phase. With this particular type of construction, the two flow sheets 12 and 13 reinforce one another with the ridges thereof defining the channels 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.
  • the channels 20 are illustrated as being uniform, it is to be understood that certain of the channels 20 may be of a greater volume than others.
  • a greater priming volume may be provided.
  • the priming volume of the transfer device may initially be accurately controlled.
  • the flow sheets 12 and 13 may be held in clamped relation to the envelope 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, the flow sheets 12 and 13 may be formed of a heavy rigid construction so that the flow sheets themselves. o ld resist distortion.
  • the sheets 14 and 15 of the envelope 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.
  • the envelope 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 the sheets 14 and 15 includes a very thin Teflon film, silicon rubber and a newly developed siliconpolycarbonate which has additional strength.
  • venous blood is pumped into the envelope 11 while oxygen is led through the outer compartments between the flow 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 the envelope 11 and finally is picked up in the blood and oxygenates through the hemoglobin in the red cells of the blood.
  • 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.
  • the material of the sheets 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.
  • a bath solution or electrolyte is passed through the outer compartments defined between the flow 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 the cellulose 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.
  • the preferred pattern of the channels 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.
  • the flow 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.
  • the material of the flow 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 the envelope 11 may be visually detected,
  • 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.
  • 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.
  • 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.
  • said membrane envelope is formed of a cellulose material selected from a group including cellulose cellophane and hydrolized cellulose acetate.
  • 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.
  • said membrane is formed of a material from a group including Teflon, silicon rubber and silicon-polycarbonate;

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Description

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 the line 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 the numeral 10. The transfer device 10 includes a central envelope, which is generally identified by the numeral 11, and through which a first fluid is intended to flow. On opposite sides of the envelope 11 there is clamped a pair of flow sheets 12 and 13. It is intended that a second fluid flow between the flow sheets and the envelope.
Considering first the construction of the envelope 11, it will be seen that it is formed of a pair of sheets 14 and 15 of flexible material which has positioned in the opposite ends thereof flow tubes 16 and 17. The sheets 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 an elongated slot 18 which opens longitudinally of the envelope 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 the flow sheets 12 and 13 is formed with a plurality of longitudinally extending channels 20 which open towards the envelope 11 and together with the envelope 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 the flow 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 each flow sheet 12 and 13 includes an inner channel 21 and an outer channel 22. The channels 21 and 22 of the flow sheets combine to define transverse passages. It will be readily apparent that the channels 21 snugly fit about the flow tubes 16 and 17 and the respective enlarged portions of the envelope 11 while the channels 22 combine to define inlet and discharge passages for the second fluid. At one end of the transfer device, the cooperating pair of channels 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 the channels 22 is provided with a discharge fitting 25 at one end and a plug 26 at the opposite end.
It is to be noted that the channels 20 extend across the channels 21 and terminate in the channels 22 so that there is fluid flow from one channel 22 across the channels 21 and to the other channel 22. It is also to be noted that the peripheral edges of the flow sheets 12 and 13 are planar whereby a suitable seal may be formed between the flow sheets 12 and 13 and the envelope 11.
It is to be understood that the envelope 11 is to be formed of a suitably flexible material whereby when the envelope 11 is clamped between the flow sheets 12 and 13, not only will there be formed as separate fluid passages between the flow sheets and the envelope within the respective channels 20, but also the envelope will be collapsed between the contacting portions of the flow sheets to form a plurality of individual channels or passages 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 the channels 20 is that of the sine-cosine curve. Furthermore, it has been found to be most effective if the flow sheets 12 and 13 are identical and when disposed in face-to-face relations, the channels 20 thereof are 180 out of phase. With this particular type of construction, the two flow sheets 12 and 13 reinforce one another with the ridges thereof defining the channels 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 the channels 20 are illustrated as being uniform, it is to be understood that certain of the channels 20 may be of a greater volume than others. By so constructing the flow 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 the flow 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. The flow sheets 12 and 13 may be held in clamped relation to the envelope 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, the flow sheets 12 and 13 may be formed of a heavy rigid construction so that the flow sheets themselves. o ld resist distortion.
When the transfer device 10 is utilized as a simple heat exchanger, the sheets 14 and 15 of the envelope 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 the transfer device 10 is utilized as an artificial lung or gill, it is necessary that the envelope 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 the sheets 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 the envelope 11 while oxygen is led through the outer compartments between the flow 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 the envelope 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 the transfer device 10 is utilized as an artificial kidney, the material of the sheets 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 the flow 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 the cellulose 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 the channels 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 the flow 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 the flow 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 the envelope 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
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Cited By (32)

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US3567028A (en) * 1968-12-26 1971-03-02 Research Corp Membrane envelope assembly
US3602298A (en) * 1969-04-25 1971-08-31 Mecislaus Joseph Ciesielski Heat exchanger
US3667612A (en) * 1969-09-04 1972-06-06 Joe H Leonard Artificial kidney system
US3709367A (en) * 1970-04-08 1973-01-09 Baxter Laboratories Inc Support structure for membrane diffusion devices
US3729098A (en) * 1971-02-08 1973-04-24 J Serur Treating blood
US3743097A (en) * 1968-12-16 1973-07-03 Rhone Poulenc Sa Dialyzer
US3839204A (en) * 1972-04-27 1974-10-01 Gen Electric Integral blood heat and component exchange device and two flow path membrane blood gas exchanger
US3847211A (en) * 1969-01-28 1974-11-12 Sub Marine Syst Inc Property interchange system for fluids
US3910841A (en) * 1974-04-02 1975-10-07 William G Esmond Stacked exchange device
FR2340758A1 (en) * 1976-02-16 1977-09-09 Gambro Ag DEVICE FOR THE DIFFUSION OF SUBSTANCES BETWEEN TWO FLUIDS THROUGH SEMI-PERMEABLE MEMBRANES
US4054527A (en) * 1976-06-25 1977-10-18 Esmond William G Countercurrent capillary transfer device
US4173537A (en) * 1977-05-23 1979-11-06 Newhart Earle E Integral artificial kidney unit
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WO1981001247A1 (en) * 1979-11-01 1981-05-14 Newhart R Integral artificial kidney unit
US4282099A (en) * 1979-12-10 1981-08-04 Jones John L Integral partitioned hemodialysis unit
US4304669A (en) * 1979-07-21 1981-12-08 Sartorius Gmbh Device for the mass transfer between fluids
EP0048943A1 (en) * 1980-09-25 1982-04-07 Terumo Corporation Oxygenator
WO1986004255A1 (en) * 1985-01-25 1986-07-31 James William Walsh Membrane processing system and method
US4804469A (en) * 1985-01-25 1989-02-14 Walsh James W Flexible jacket membrane processing apparatus
US4892662A (en) * 1985-01-25 1990-01-09 Walsh James W Membrane processing method
US5823252A (en) * 1994-07-28 1998-10-20 Daimler-Benz Aktiengesellschaft Two-stage evaporator unit
US6551347B1 (en) * 1988-09-28 2003-04-22 Life Enhancement Technologies, Inc. Cooling/heating system
US20090178393A1 (en) * 2008-01-10 2009-07-16 Jesper Norsk Method and system for purification of exhaust gas from diesel engines
US20100314088A1 (en) * 2009-06-11 2010-12-16 Agency For Defense Development Heat exchanger having micro-channels
US20120305217A1 (en) * 2011-06-01 2012-12-06 Alstom Technology Ltd Heating element undulation patterns
US10094626B2 (en) 2015-10-07 2018-10-09 Arvos Ljungstrom Llc Alternating notch configuration for spacing heat transfer sheets
US10175006B2 (en) 2013-11-25 2019-01-08 Arvos Ljungstrom Llc Heat transfer elements for a closed channel rotary regenerative air preheater
US10197337B2 (en) 2009-05-08 2019-02-05 Arvos Ljungstrom Llc Heat transfer sheet for rotary regenerative heat exchanger
US10378829B2 (en) 2012-08-23 2019-08-13 Arvos Ljungstrom Llc Heat transfer assembly for rotary regenerative preheater
US20190302178A1 (en) * 2018-04-03 2019-10-03 Advantest Corporation Heat exchanger and electronic device handling apparatus including the same
CN111928688A (en) * 2020-07-22 2020-11-13 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) 2006-01-23 2021-02-09 Arvos Gmbh Tube bundle heat exchanger

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Cited By (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3743097A (en) * 1968-12-16 1973-07-03 Rhone Poulenc Sa Dialyzer
US3567028A (en) * 1968-12-26 1971-03-02 Research Corp Membrane envelope assembly
US3847211A (en) * 1969-01-28 1974-11-12 Sub Marine Syst Inc Property interchange system for fluids
US3602298A (en) * 1969-04-25 1971-08-31 Mecislaus Joseph Ciesielski Heat exchanger
US3667612A (en) * 1969-09-04 1972-06-06 Joe H Leonard Artificial kidney system
US3709367A (en) * 1970-04-08 1973-01-09 Baxter Laboratories Inc Support structure for membrane diffusion devices
US3729098A (en) * 1971-02-08 1973-04-24 J Serur Treating blood
US3839204A (en) * 1972-04-27 1974-10-01 Gen Electric Integral blood heat and component exchange device and two flow path membrane blood gas exchanger
US3910841A (en) * 1974-04-02 1975-10-07 William G Esmond Stacked exchange device
FR2340758A1 (en) * 1976-02-16 1977-09-09 Gambro Ag DEVICE FOR THE DIFFUSION OF SUBSTANCES BETWEEN TWO FLUIDS THROUGH SEMI-PERMEABLE MEMBRANES
US4054527A (en) * 1976-06-25 1977-10-18 Esmond William G Countercurrent capillary transfer device
US4173537A (en) * 1977-05-23 1979-11-06 Newhart Earle E Integral artificial kidney unit
WO1980002806A1 (en) * 1979-06-20 1980-12-24 Newhart R Blood perfusion units
US4304669A (en) * 1979-07-21 1981-12-08 Sartorius Gmbh Device for the mass transfer between fluids
WO1981001247A1 (en) * 1979-11-01 1981-05-14 Newhart R Integral artificial kidney unit
US4282099A (en) * 1979-12-10 1981-08-04 Jones John L Integral partitioned hemodialysis unit
EP0048943A1 (en) * 1980-09-25 1982-04-07 Terumo Corporation Oxygenator
US4374802A (en) * 1980-09-25 1983-02-22 Terumo Corporation Oxygenator
US4892662A (en) * 1985-01-25 1990-01-09 Walsh James W Membrane processing method
WO1986004255A1 (en) * 1985-01-25 1986-07-31 James William Walsh Membrane processing system and method
US4804469A (en) * 1985-01-25 1989-02-14 Walsh James W Flexible jacket membrane processing apparatus
US6551347B1 (en) * 1988-09-28 2003-04-22 Life Enhancement Technologies, Inc. Cooling/heating system
US20030229385A1 (en) * 1988-09-28 2003-12-11 Life Enhancement Technologies, Inc. Cooling/heating system
US7001417B2 (en) 1988-09-28 2006-02-21 Life Ehancement Technologies, Inc. Cooling/heating system
US5823252A (en) * 1994-07-28 1998-10-20 Daimler-Benz Aktiengesellschaft Two-stage evaporator unit
US10914527B2 (en) 2006-01-23 2021-02-09 Arvos Gmbh Tube bundle heat exchanger
US20090178393A1 (en) * 2008-01-10 2009-07-16 Jesper Norsk Method and system for purification of exhaust gas from diesel engines
US8127535B2 (en) * 2008-01-10 2012-03-06 Haldor Topsøe A/S Method and system for purification of exhaust gas from diesel engines
US10197337B2 (en) 2009-05-08 2019-02-05 Arvos Ljungstrom Llc Heat transfer sheet for rotary regenerative heat exchanger
US10982908B2 (en) 2009-05-08 2021-04-20 Arvos Ljungstrom Llc Heat transfer sheet for rotary regenerative heat exchanger
US20100314088A1 (en) * 2009-06-11 2010-12-16 Agency For Defense Development Heat exchanger having micro-channels
US9644899B2 (en) * 2011-06-01 2017-05-09 Arvos, Inc. Heating element undulation patterns
US20120305217A1 (en) * 2011-06-01 2012-12-06 Alstom Technology Ltd Heating element undulation patterns
US10378829B2 (en) 2012-08-23 2019-08-13 Arvos Ljungstrom Llc Heat transfer assembly for rotary regenerative preheater
US11092387B2 (en) 2012-08-23 2021-08-17 Arvos Ljungstrom Llc Heat transfer assembly for rotary regenerative preheater
US10175006B2 (en) 2013-11-25 2019-01-08 Arvos Ljungstrom Llc Heat transfer elements for a closed channel rotary regenerative air preheater
US10094626B2 (en) 2015-10-07 2018-10-09 Arvos Ljungstrom Llc Alternating notch configuration for spacing heat transfer sheets
US20190302178A1 (en) * 2018-04-03 2019-10-03 Advantest Corporation Heat exchanger and electronic device handling apparatus including the same
US10753971B2 (en) * 2018-04-03 2020-08-25 Advantest Corporation Heat exchanger and electronic device handling apparatus including the same
CN111928688A (en) * 2020-07-22 2020-11-13 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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