WO2013086011A1 - Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices - Google Patents

Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices Download PDF

Info

Publication number
WO2013086011A1
WO2013086011A1 PCT/US2012/067971 US2012067971W WO2013086011A1 WO 2013086011 A1 WO2013086011 A1 WO 2013086011A1 US 2012067971 W US2012067971 W US 2012067971W WO 2013086011 A1 WO2013086011 A1 WO 2013086011A1
Authority
WO
WIPO (PCT)
Prior art keywords
flow channel
blood
blood flow
oxygen
implementations
Prior art date
Application number
PCT/US2012/067971
Other languages
French (fr)
Inventor
Jeffrey T. Borenstein
Joseph L. Charest
James C. Hsiao
Tatiana Kniazeva
Ernest Kim
Alla Epshteyn
Vijaya Kolachalama
Original Assignee
The Charles Stark Draper Laboratory, Inc.
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.)
Filing date
Publication date
Application filed by The Charles Stark Draper Laboratory, Inc. filed Critical The Charles Stark Draper Laboratory, Inc.
Priority to JP2014546025A priority Critical patent/JP6395608B2/en
Priority to AU2012347922A priority patent/AU2012347922B2/en
Priority to EP12799501.7A priority patent/EP2788042B1/en
Priority to CN201280059591.9A priority patent/CN104053461A/en
Priority to ES12799501T priority patent/ES2700249T3/en
Priority to CA2858080A priority patent/CA2858080C/en
Priority to IN4342CHN2014 priority patent/IN2014CN04342A/en
Publication of WO2013086011A1 publication Critical patent/WO2013086011A1/en

Links

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M1/00Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
    • A61M1/14Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis
    • A61M1/16Dialysis systems; Artificial kidneys; Blood oxygenators ; Reciprocating systems for treatment of body fluids, e.g. single needle systems for hemofiltration or pheresis with membranes
    • A61M1/1698Blood oxygenators with or without heat-exchangers
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M2206/00Characteristics of a physical parameter; associated device therefor
    • A61M2206/10Flow characteristics
    • A61M2206/20Flow characteristics having means for promoting or enhancing the flow, actively or passively

Definitions

  • Blood oxygenation systems are used for short term respiratory support, such as during coronary artery bypass graft surgeries or for acute respiratory distress syndrome patients.
  • blood is oxygenated by pumping oxygen through an inner, hollow fiber pumping blood though a larger, outer fiber that encapsulates the inner fiber.
  • the walls of the inner fiber are permeable to oxygen and allow for the oxygenation of blood near the inner fiber.
  • Current oxygenation systems maintain a laminar blood flow, only allowing the oxygenation of red blood cells within a close proximity of the permeable membrane.
  • a microfluidic oxygenation device includes a first polymer layer defining a first oxygen flow channel.
  • the device also includes a second polymer layer defining a first blood flow channel.
  • the first blood flow channel overlaps the first oxygen flow channel, and the two channels are separated by a permeable membrane that allows communication between the channels at overlapping portions.
  • first blood flow channel further includes at least one passive mixing element along at least one wall. The passive mixing element is configured to redistribute a fluid flowing through the first blood flow channel within the channel.
  • the passive mixing element is one of a straight ridge, an angled ridge, a chevron canal, a dome, a cone, a pit or a post.
  • a first fluid such as oxygen
  • a second fluid such as blood
  • the height or depth of the passive mixing element is less than about 30% of the height of the first blood flow channel, and the passive mixing elements are incorporated into the floor of the first blood flow channel.
  • the height of the first blood flow channel is between about 10 and 100 microns and the membrane thickness is between about 10 and about 50 microns.
  • the length of the first oxygen flow channel and the first blood flow channel is between about 1 mm and 50 mm and the width is between about 100 microns and 200 microns.
  • the membrane is permeable to oxygen and carbon dioxide.
  • the walls of the first blood flow channel are coated with an anticoagulant.
  • the device includes a second blood flow channel separated from the first oxygen flow channel by a second permeable membrane.
  • a method for oxygenating deoxygenate blood includes providing a microfluidic device comprising a first polymer layer defining a first oxygen flow channel and a second polymer layer defining a first blood flow channel.
  • the first blood flow channel also includes at least one passive mixing element.
  • a membrane separates the first oxygen flow channel and the first blood flow channel and allows communication between the first oxygen flow channel and the first blood flow channel.
  • the method also includes introducing partially deoxygenated blood into a proximal end of the microfluidic device, and flowing the partially deoxygenated blood through the device.
  • the method includes flowing oxygen through the first oxygen flow channel. Finally, oxygenated blood is received at a distal end of the microfluidic device.
  • the method also includes collecting partially deoxygenated blood from a patient, flowing the partially deoxygenated blood through the first blood flow channel to reoxygenate the blood, and returning the reoxygenated blood to the patient.
  • the method further includes removing carbon dioxide from the partially deoxygenated blood as the partially deoxygenated blood flows through the first blood flow channel.
  • the method also includes flowing oxygen through the first oxygen flow channel from a first direction, and flowing blood through the first blood flow channel in a second direction opposite to the first direction.
  • the blood is flowed through the first blood flow channel at 4-5 L/min and oxygen is transferred to the blood at a rate of about 150-200 mL/min.
  • Figure 1A is an isometric view of a device for oxygenating blood, according to one illustrative implementation of the present disclosure
  • Figure IB is a cut-away view of a device for oxygenating blood, according to one illustrative implementation of the present disclosure
  • Figure 1C is an end view of a device of oxygenating blood as depicted in Figure 1, according to one illustrative implementation of the present disclosure
  • Figure 2 is a cross-sectional view illustrating the flow patterns of blood in a blood oxygenation device without passive mixing elements, according to one illustrative implementation of the present disclosure
  • Figure 3 is a cross-sectional view illustrating the flow patterns of blood in a blood oxygenation device with passive mixing elements as depicted in Figures 1A-1C, according to one illustrative implementation of the present disclosure
  • FIGS. 4A-J are top and isometric view of exemplary passive mixing elements of a blood oxygenation device as depicted in Figure 1 , in accordance with an illustrative implementation of the present disclosure.
  • Figure 5 is a flow chart of a method for oxygenating deoxygenated blood with a blood oxygenation device as depicted in Figure 1 , in accordance with an illustrative implementation of the present disclosure.
  • the present system described herein generally relates to a system and method for oxygenating blood. Accordingly, in various implementations, the disclosure relates to oxygenating blood by passively mixing the blood as it flows through the blood oxygenation device. In certain implementations, the device includes a plurality of passive elements on one wall of the device to mix the flowing blood.
  • Figures 1A and IB show an isometric view of a blood oxygenation device 100 and a cutaway view thereof. Described in greater detail below, but briefly, the device 100 includes a first flow channel 101 separated from a second flow channel 102 by a gas permeable membrane 103. The floor 105 of the second flow channel 102 includes a passive mixing element 106. The flow channels 101 and 102 are fabricated within a polymer substrate 104.
  • device 100 includes a first flow channel 101 and second flow channel 102 fabricated within a polymer substrate 104.
  • the polymer substrate 104 is a thermoplastic, such as polystyrene or polyimide, biodegradable polyesters, such as polycaprolactone (PCL), or soft elastomers such as polyglycerol sebacate (PGS).
  • the substrate 104 is a thermoplastic, such as polystyrene or polyimide, biodegradable polyesters, such as polycaprolactone (PCL), or soft elastomers such as polyglycerol sebacate (PGS).
  • the substrate 104 is a thermoplastic, such as polystyrene or polyimide, biodegradable polyesters, such as polycaprolactone (PCL), or soft elastomers such as polyglycerol sebacate (PGS).
  • the substrate 104 is a thermoplastic, such as polystyrene or polyimide, biodegradable polyesters, such as
  • the substrate 104 includes non-polymer materials such as, but not limited to, ceramics;
  • metals glasses; nanotubes or nanowires formed from, for example, carbon or zinc oxide; or other non-polymer materials.
  • the device 100 and the passive mixing elements 106 are fabricated in the substrate 104 using, for example, photolithographic techniques, injection molding, direct micromachining, deep RIE etching, hot embossing, or any combinations thereof.
  • the first flow channel 101 communicates with the second flow channel 102 via the membrane 103.
  • the membrane 103 is permeable or semi-permeable to ions, molecules, cells or any combination thereof.
  • the membrane 103 may allow for oxygen to pass from the first flow channel 101 to the second flow channel 102 and carbon dioxide to pass from the second flow channel 102 to the first flow channel 101.
  • the membrane 103 is not permeable to red blood cells.
  • the membrane 103 is fabricated from a semi-porous or porous material, such as polyethersulfone or PDMS.
  • the membrane 103 is created by electrospinning a polymer to create a flexible, porous polymer mesh.
  • the first flow channel 101 and the second flow channel 102 of device 100 run substantially parallel to one another, and, as described above, are separated by the membrane 103 at overlapping portions.
  • the first flow channel 101 includes three smooth walls, with the fourth wall being the membrane 103.
  • the device 100 includes additional flow channels to the left, right, and/or above the first flow channel 101.
  • the first flow channel 101 is also separated from these additional flow channels by a permeable membrane 103.
  • the first flow channel is configured for the flow of a gas.
  • oxygen may be flowed through the first flow channel 101.
  • the first flow channel 101 is configured to flow a liquid.
  • the flow first flow channel may be configured to flow blood.
  • the second flow channel 102 includes at least one passive mixing element 106 along at least one wall of the channel.
  • the floor 105 includes passive mixing elements 106(1)-106(V).
  • any wall of the first or second flow channel can include a passive mixing element 106.
  • the floor, or other wall(s) that include a passive mixing element 106 is replaceable, such that different configurations of passive mixing elements can be used for different fluids.
  • the device 100, or components thereof, is disposable.
  • the passive mixing elements include a plurality of ridges, channels, protrusions, or any combination thereof.
  • the passive mixing elements 106(l)-106(n) span the entire length of a flow channel. In other implementations, the mixing elements 106 cover only a sub-portion of the total length of a flow channel 102. In yet other implementations, the passive mixing elements 106(1)-106(V) are grouped together.
  • the fluid flow channel 102 may contain a first type of passive mixing element 106 along a first portion of the flow channel 102 and then a second type of passive mixing element 106 along a second portion of the flow channel 102.
  • Figure 1C illustrates an end view of device 100.
  • the device 100 is fabricated as a top component 104(b) and a bottom component 104(b) that are fabricated separately and assembled to form device 100.
  • the components 104(a), 104(b), and the membrane 103 are attached to one another with an adhesive.
  • the components of device 100 can be bound together with a chemical adhesive, plasma bonding, and/or by clamping the components together.
  • the device 100 is fabricated as a single, continuous unit.
  • device 100 can be created by injection molding.
  • the top portion 104(b) and the bottom portion 104(a) are formed by injection molding.
  • the channels are coated with an anticoagulant.
  • the anticoagulant is embedded in the polymer substrate 104.
  • the height or depth of a passive mixing element 106 is between about 5% and about 10%, between about 10% and about 20%>, or between about 20% and 30% of the total height of the flow channel 102. In some implementations, each passive mixing element in a channel is the same height or depth. While in other words,
  • the height or depth of the passive mixing elements changes along the length of the flow channel 102.
  • the width, height, and length of the first flow channel 101 and second flow channel 102 are the same. In other implementations, one or all of the dimensions between different flow channels is different. In some implementations, the height of the flow channels is between about 10 microns and 25 microns, between about 25 microns and 50 microns, or between about 50 microns and 100 microns. In some implementations the thickness of the membrane 103 is between about 10 microns and 25 microns, between about 25 microns and 50 microns, or between about 50 microns and 100 microns.
  • the length of the flow channels is between about 1 mm and 10 mm, between about 10 mm and 50 mm, or between about 50 mm and 100 mm and the width is between about 100 microns and 200 microns, between 200 microns and 500 microns, or between about 500 microns and 1 cm.
  • Figure 2 illustrates how fluid may flow through a blood oxygenation device without passive mixing elements similar.
  • Figure 2 illustrates a blood oxygenation device 201 without passive mixing elements along the floor 105(b).
  • oxygen flows through the first flow channel 201 as deoxygenated blood (white circles) flows through the second flow channel 202.
  • the blood in the second flow channel 201 flows in a laminar pattern 203.
  • the blood cells become oxygenated (gray circles) as they flow substantially close to the membrane 204.
  • oxygen diffusion can only occur at distances substantially close to the membrane 204, the portion of blood flowing along the floor of the second flow channel 202 may never become oxygenated.
  • Figure 3 illustrates how blood flows through a blood oxygenation device 300 similar to the blood oxygenation device 100.
  • the floor 105 of device 300 includes a number of passive flow elements 106. These passive flow elements 106 create non-laminar flow 301 in the fluid of channel 102. In some implementations this creates chaotic flow in channel 102.
  • the passive mixing elements 106 drive fluid from the bottom of the fluid flow channel 102 towards the membrane 103.
  • the passive mixing elements 106 create a rotational flow within in the flow channel.
  • the passive mixing elements 106 may create a rifling effect that causes the fluid to swirl as it flows down the flow channel 102.
  • the device 100 induces mixing within a fluid without inducing mechanical trauma to the components of the fluid.
  • the passive mixing elements 106 of device 100 may drive blood towards the membrane 103 without causing the red blood cells to hemorrhage or clot.
  • the device 300 As illustrated in Figure 3, the device 300, with the passive mixing elements 106, is able to fully oxygenate the blood over a shorter span of the device's length when compared to device 200 that does not include a passive mixing element 106. This allows for a shorter channel, and therefore allows the device to be primed with less blood than a channel without such passive mixing elements.
  • Figures 4A-J show a top and isometric view of possible, non-limiting examples of passive mixing elements 106.
  • Figures 4 A and 4B illustrate an alternating herringbone pattern.
  • the design consists of a herringbone pattern wherein the center of the herringbone pattern shifts from one side of the flow channel to the other through the length of the flow channel 102.
  • the alternating herringbone pattern causes the fluid in the flow channel to enter the flow channel and begin rotating in a first direction. Then, when the flowing fluid encounters a shifted herringbone pattern, the fluid is forced to rotate in a direction opposite to the first rotational direction.
  • the fluid may enter the channel 102 flowing in a laminar fashion, and then alternatingly switch between clockwise and counter clockwise rotations as the fluid encounters consecutive, offset herringbone patterns.
  • the number of chevrons per herringbone pattern and/or the number of groupings is configured to create a specific level of mixing over a given length of the device 100.
  • the herringbone pattern does not alternate, but is constant along the duration of the flow channel.
  • the center of the herringbone patterns is in the center of the channel, while in other implementations the center of the pattern is off-center with respect to the channel.
  • the mixing of a fluid is created with slanted ridges. Similar to the herringbone patter described above, in some implementations the slanted ridge pattern also creates a swirling rotation of the fluid that drives fluid from the bottom of the fluid flow channel towards the permeable membrane 103.
  • the angle of the slanted ridge and the herringbone patter is between about 35 and about 55 degrees.
  • the spacing between the ridges is between about 50 microns and about 100 microns, between about 100 microns and 150 microns, or between about 150 and about 200 microns.
  • the spacing of the ridges is 2 ⁇ /( ⁇ width of the channel), such that the diameter of the induced rotation is less than the width or depth of the channel.
  • the ridges of the above implementations are rounded.
  • the passive mixing elements 106 are designed to create vortices and other high and low pressure areas which drive the fluid towards the membrane 103.
  • Figures 4E and 4F like the illustrative implementation of Figure 3, include a plurality of ridges.
  • the ridges are spaced between about 20 microns and about 50 microns, between about 50 microns and 100 microns or between about 100 microns and 500 microns.
  • the passive mixing elements can be, but are not limited to, posts, mounds, ramps, pits, cones or any combination thereof.
  • Figures 4G-4J illustrate a possible post and mound implementation. In the implementation illustrated in Figures 4G and 4H, each row of posts is off set from the previous row. This causes the fluid to mix laterally in addition to driving fluid upwards. In other implementations, as illustrated in Figure 41 and 4J, the passive mixing elements are aligned with the passive mixing elements in the previous row.
  • FIG. 5 is a flow chart of a method 500 for oxygenating blood with a microfluidic device.
  • a microfluidic device is provided (step 501).
  • partially deoxygenated blood is introduced into a proximal end of the microfluidic device (step 502).
  • the partially deoxygenated blood is flowed through a first channel of the microfluidic device (step 503), and oxygen is flowed through a second channel of the microfluidic device (step 504).
  • oxygenated blood is collected from a distal end of the microfluidic device (step 505).
  • the method 500 for oxygenating partially deoxygenated blood begins with providing a microfluidic device (step 501).
  • the microfluidic device is similar to device 100 described above.
  • the microfluidic device includes a plurality of oxygen channels and/or a plurality of blood flow channels.
  • the microfluidic device is a array of devices similar to device 100.
  • the device is configured to allow for about 500-1000 mL/min, about 1-4 L/min, or about 4-5 L/min of blood flow.
  • the device is configured to transfer oxygen into the blood at a rate of about 160 to about 200 mL/min.
  • the method 500 of oxygenating blood continues with the introduction of partially deoxygenated blood into a proximal end of the microfluidic device (step 502).
  • the blood is directly collected form a patient and introduced into the device.
  • the device may be part of a heart-lung bypass system that oxygenates blood during surgery.
  • the blood is collected, stored, and then oxygenated at a later time.
  • the blood may be collected during a blood drive and then oxygenated prior to being transfused into a patient.
  • the blood is actively pumped through the device by an external pump, and in other implementations the blood is pumped through the device by the patient's heart.
  • the method 500 continues by flowing the partially deoxygenated blood through a first blood flow channel (step 503).
  • the device includes at least one passive mixing element that inducing mixing within the channel as the blood travels the length of the device.
  • the blood is thinned with a blood thinning agent such as the drug Coumadin or Heparin.
  • the walls of the blood flow channels are coated with an anticoagulant.
  • the method 500 continues by flowing oxygen through a first oxygen flow channel (step 504).
  • a first oxygen flow channel Referring to Figure 1, the blood flow channel and oxygen flow channel are separated by a permeable membrane. Oxygen diffuses through the membrane, oxygenating the blood as it flows down the length of the channel.
  • the blood is continually mixed within the channel by the passive mixing elements similar to those described above.
  • the continual mixing allows a given volume of deoxygenated blood to be oxygenated more efficiently by continually exposing different red blood cells to the region near the membrane where oxygen diffusion can occur.
  • the membrane is also porous to carbon dioxide, and the carbon dioxide initially within the deoxygenated blood diffuses into the oxygen flow channel.
  • the oxygen and blood are flowed through the microfluidic device starting at different ends. For example, the blood may enter the device at a proximal end and the oxygen may enter the device at a distal end of the device.
  • the method 500 continues, with the collection of the oxygenated blood at a distal end of the microfluidic channel.
  • the oxygenated blood is transfused directly back into the patient from which it was collected.
  • the blood is collected and stored for later transfusion or experimentation.

Landscapes

  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Urology & Nephrology (AREA)
  • Heart & Thoracic Surgery (AREA)
  • Vascular Medicine (AREA)
  • Engineering & Computer Science (AREA)
  • Anesthesiology (AREA)
  • Biomedical Technology (AREA)
  • Hematology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • External Artificial Organs (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A device and method for oxygenating blood is disclosed herein. The device includes a plurality of passive mixing elements that causes a fluid to mix as it flows through the device. The passive mixing elements continually expose new red blood cells to the portion of the flow channel where oxygenation can occur. Accordingly, in some implementations, the device and method uses less blood to prime the device and allows for the oxygenation of blood with a substantial shorter flow channel when compared to conventional oxygenation methods and devices.

Description

METHOD FOR REDUCING THE BLOOD PRIMING VOLUME AND MEMBRANE
SURFACE AREA IN MICROFLUIDIC LUNG ASSIST DEVICES
CROSS-REFERENCE TO RELATED PATENT APPLICATIONS
[0001] This application claims priority from Provisional U.S. Patent Application 61/567,104, filed December 5, 2011, incorporated herein by reference in its entirety.
BACKGROUND OF THE DISCLOSURE
[0002] Blood oxygenation systems are used for short term respiratory support, such as during coronary artery bypass graft surgeries or for acute respiratory distress syndrome patients. In current systems, blood is oxygenated by pumping oxygen through an inner, hollow fiber pumping blood though a larger, outer fiber that encapsulates the inner fiber. The walls of the inner fiber are permeable to oxygen and allow for the oxygenation of blood near the inner fiber. Current oxygenation systems maintain a laminar blood flow, only allowing the oxygenation of red blood cells within a close proximity of the permeable membrane.
SUMMARY OF THE DISCLOSURE
[0003] According to one aspect of the disclosure, a microfluidic oxygenation device includes a first polymer layer defining a first oxygen flow channel. The device also includes a second polymer layer defining a first blood flow channel. The first blood flow channel overlaps the first oxygen flow channel, and the two channels are separated by a permeable membrane that allows communication between the channels at overlapping portions. Additionally, first blood flow channel further includes at least one passive mixing element along at least one wall. The passive mixing element is configured to redistribute a fluid flowing through the first blood flow channel within the channel.
[0004] In some implementations, the passive mixing element is one of a straight ridge, an angled ridge, a chevron canal, a dome, a cone, a pit or a post. In some implementations, a first fluid, such as oxygen, flows through the first oxygen flow channel and a second fluid, such as blood, flows through the first blood flow channel.
[0005] In some implementations, the height or depth of the passive mixing element is less than about 30% of the height of the first blood flow channel, and the passive mixing elements are incorporated into the floor of the first blood flow channel. In other implementations, the height of the first blood flow channel is between about 10 and 100 microns and the membrane thickness is between about 10 and about 50 microns. In yet other implementations, the length of the first oxygen flow channel and the first blood flow channel is between about 1 mm and 50 mm and the width is between about 100 microns and 200 microns.
[0006] In other implementations, the membrane is permeable to oxygen and carbon dioxide. In yet other implementations, the walls of the first blood flow channel are coated with an anticoagulant. In yet other implementations, the device includes a second blood flow channel separated from the first oxygen flow channel by a second permeable membrane.
[0007] According to another aspect of the disclosure, a method for oxygenating deoxygenate blood includes providing a microfluidic device comprising a first polymer layer defining a first oxygen flow channel and a second polymer layer defining a first blood flow channel. The first blood flow channel also includes at least one passive mixing element. A membrane separates the first oxygen flow channel and the first blood flow channel and allows communication between the first oxygen flow channel and the first blood flow channel. The method also includes introducing partially deoxygenated blood into a proximal end of the microfluidic device, and flowing the partially deoxygenated blood through the device.
Additionally, the method includes flowing oxygen through the first oxygen flow channel. Finally, oxygenated blood is received at a distal end of the microfluidic device.
[0008] In some implementations, the method also includes collecting partially deoxygenated blood from a patient, flowing the partially deoxygenated blood through the first blood flow channel to reoxygenate the blood, and returning the reoxygenated blood to the patient. In other implementations, the method further includes removing carbon dioxide from the partially deoxygenated blood as the partially deoxygenated blood flows through the first blood flow channel.
[0009] In yet other implementations, the method also includes flowing oxygen through the first oxygen flow channel from a first direction, and flowing blood through the first blood flow channel in a second direction opposite to the first direction. In some implementations, the blood is flowed through the first blood flow channel at 4-5 L/min and oxygen is transferred to the blood at a rate of about 150-200 mL/min. BRIEF DESCRIPTION OF THE DRAWINGS
[0010] The skilled artisan will understand that the figures, described herein, are for illustration purposes only. It is to be understood that in some instances various aspects of the described implementations may be shown exaggerated or enlarged to facilitate an
understanding of the described implementations. In the drawings, like reference characters generally refer to like features, functionally similar and/or structurally similar elements throughout the various drawings. The drawings are not necessarily to scale, emphasis instead being placed upon illustrating the principles of the teachings. The drawings are not intended to limit the scope of the present teachings in any way. The system and method may be better understood from the following illustrative description with reference to the following drawings in which:
[0011] Figure 1A is an isometric view of a device for oxygenating blood, according to one illustrative implementation of the present disclosure;
[0012] Figure IB is a cut-away view of a device for oxygenating blood, according to one illustrative implementation of the present disclosure;
[0013] Figure 1C is an end view of a device of oxygenating blood as depicted in Figure 1, according to one illustrative implementation of the present disclosure;
[0014] Figure 2 is a cross-sectional view illustrating the flow patterns of blood in a blood oxygenation device without passive mixing elements, according to one illustrative implementation of the present disclosure;
[0015] Figure 3 is a cross-sectional view illustrating the flow patterns of blood in a blood oxygenation device with passive mixing elements as depicted in Figures 1A-1C, according to one illustrative implementation of the present disclosure;
[0016] FIGS. 4A-J are top and isometric view of exemplary passive mixing elements of a blood oxygenation device as depicted in Figure 1 , in accordance with an illustrative implementation of the present disclosure; and
[0017] Figure 5 is a flow chart of a method for oxygenating deoxygenated blood with a blood oxygenation device as depicted in Figure 1 , in accordance with an illustrative implementation of the present disclosure. DETAILED DESCRIPTION
[0018] The various concepts introduced above and discussed in greater detail below may be implemented in any of numerous ways, as the described concepts are not limited to any particular manner of implementation. Examples of specific implementations and applications are provided primarily for illustrative purposes.
[0019] The present system described herein generally relates to a system and method for oxygenating blood. Accordingly, in various implementations, the disclosure relates to oxygenating blood by passively mixing the blood as it flows through the blood oxygenation device. In certain implementations, the device includes a plurality of passive elements on one wall of the device to mix the flowing blood.
[0020] Figures 1A and IB show an isometric view of a blood oxygenation device 100 and a cutaway view thereof. Described in greater detail below, but briefly, the device 100 includes a first flow channel 101 separated from a second flow channel 102 by a gas permeable membrane 103. The floor 105 of the second flow channel 102 includes a passive mixing element 106. The flow channels 101 and 102 are fabricated within a polymer substrate 104.
[0021] As illustrated in Figures 1A and IB and discussed above, device 100 includes a first flow channel 101 and second flow channel 102 fabricated within a polymer substrate 104. In some implementations, the polymer substrate 104 is a thermoplastic, such as polystyrene or polyimide, biodegradable polyesters, such as polycaprolactone (PCL), or soft elastomers such as polyglycerol sebacate (PGS). In other implementations, the substrate 104 is
polydimethylsiloxane (PDMS), poly(N-isopropylacrylamide). In yet other implementations, the substrate 104 includes non-polymer materials such as, but not limited to, ceramics;
metals; glasses; nanotubes or nanowires formed from, for example, carbon or zinc oxide; or other non-polymer materials.
[0022] In some implementations, the device 100 and the passive mixing elements 106 are fabricated in the substrate 104 using, for example, photolithographic techniques, injection molding, direct micromachining, deep RIE etching, hot embossing, or any combinations thereof.
[0023] The first flow channel 101 communicates with the second flow channel 102 via the membrane 103. In some implementations, the membrane 103 is permeable or semi-permeable to ions, molecules, cells or any combination thereof. For example, the membrane 103 may allow for oxygen to pass from the first flow channel 101 to the second flow channel 102 and carbon dioxide to pass from the second flow channel 102 to the first flow channel 101.
However, in some implementations, the membrane 103 is not permeable to red blood cells. In some implementations, the membrane 103 is fabricated from a semi-porous or porous material, such as polyethersulfone or PDMS. In other implementations, the membrane 103 is created by electrospinning a polymer to create a flexible, porous polymer mesh.
[0024] The first flow channel 101 and the second flow channel 102 of device 100 run substantially parallel to one another, and, as described above, are separated by the membrane 103 at overlapping portions. In some implementations, the first flow channel 101 includes three smooth walls, with the fourth wall being the membrane 103. In other implementations, the device 100 includes additional flow channels to the left, right, and/or above the first flow channel 101. In some of these implementations the first flow channel 101 is also separated from these additional flow channels by a permeable membrane 103. In other
implementations, the first flow channel is configured for the flow of a gas. For example, oxygen may be flowed through the first flow channel 101. In other implementations, the first flow channel 101 is configured to flow a liquid. For example, the flow first flow channel may be configured to flow blood.
[0025] The second flow channel 102 includes at least one passive mixing element 106 along at least one wall of the channel. In the implementation of device 100, the floor 105 includes passive mixing elements 106(1)-106(V). In other implementations, any wall of the first or second flow channel can include a passive mixing element 106. In some implementations, the floor, or other wall(s) that include a passive mixing element 106, is replaceable, such that different configurations of passive mixing elements can be used for different fluids. In yet other implementations the device 100, or components thereof, is disposable.
[0026] As described below, in some implementations, the passive mixing elements include a plurality of ridges, channels, protrusions, or any combination thereof. In some
implementations the passive mixing elements 106(l)-106(n) span the entire length of a flow channel. In other implementations, the mixing elements 106 cover only a sub-portion of the total length of a flow channel 102. In yet other implementations, the passive mixing elements 106(1)-106(V) are grouped together. For example, the fluid flow channel 102 may contain a first type of passive mixing element 106 along a first portion of the flow channel 102 and then a second type of passive mixing element 106 along a second portion of the flow channel 102.
[0027] Figure 1C illustrates an end view of device 100. In some implementations, the device 100 is fabricated as a top component 104(b) and a bottom component 104(b) that are fabricated separately and assembled to form device 100. In some implementations, the components 104(a), 104(b), and the membrane 103 are attached to one another with an adhesive. For example, the components of device 100 can be bound together with a chemical adhesive, plasma bonding, and/or by clamping the components together. In other
implementations, the device 100 is fabricated as a single, continuous unit. For example, device 100 can be created by injection molding. In yet other implementations, the top portion 104(b) and the bottom portion 104(a) are formed by injection molding. In some
implementations, after the device 100 is fabricated the channels are coated with an anticoagulant. In other implementations, the anticoagulant is embedded in the polymer substrate 104.
[0028] In some implementations the height or depth of a passive mixing element 106 is between about 5% and about 10%, between about 10% and about 20%>, or between about 20% and 30% of the total height of the flow channel 102. In some implementations, each passive mixing element in a channel is the same height or depth. While in other
implementations, the height or depth of the passive mixing elements changes along the length of the flow channel 102.
[0029] In some implementations, the width, height, and length of the first flow channel 101 and second flow channel 102 are the same. In other implementations, one or all of the dimensions between different flow channels is different. In some implementations, the height of the flow channels is between about 10 microns and 25 microns, between about 25 microns and 50 microns, or between about 50 microns and 100 microns. In some implementations the thickness of the membrane 103 is between about 10 microns and 25 microns, between about 25 microns and 50 microns, or between about 50 microns and 100 microns. In some implementations, the length of the flow channels is between about 1 mm and 10 mm, between about 10 mm and 50 mm, or between about 50 mm and 100 mm and the width is between about 100 microns and 200 microns, between 200 microns and 500 microns, or between about 500 microns and 1 cm. [0030] Figure 2 illustrates how fluid may flow through a blood oxygenation device without passive mixing elements similar. Figure 2 illustrates a blood oxygenation device 201 without passive mixing elements along the floor 105(b). In this example, oxygen flows through the first flow channel 201 as deoxygenated blood (white circles) flows through the second flow channel 202. The blood in the second flow channel 201 flows in a laminar pattern 203. The blood cells become oxygenated (gray circles) as they flow substantially close to the membrane 204. In some implementations, because oxygen diffusion can only occur at distances substantially close to the membrane 204, the portion of blood flowing along the floor of the second flow channel 202 may never become oxygenated.
[0031] In contrast, Figure 3 illustrates how blood flows through a blood oxygenation device 300 similar to the blood oxygenation device 100. The floor 105 of device 300 includes a number of passive flow elements 106. These passive flow elements 106 create non-laminar flow 301 in the fluid of channel 102. In some implementations this creates chaotic flow in channel 102. For example, in some implementations, the passive mixing elements 106 drive fluid from the bottom of the fluid flow channel 102 towards the membrane 103. In some implementations, the passive mixing elements 106 create a rotational flow within in the flow channel. For example, the passive mixing elements 106 may create a rifling effect that causes the fluid to swirl as it flows down the flow channel 102. In some implementations, the device 100 induces mixing within a fluid without inducing mechanical trauma to the components of the fluid. For example, the passive mixing elements 106 of device 100 may drive blood towards the membrane 103 without causing the red blood cells to hemorrhage or clot.
[0032] As illustrated in Figure 3, the device 300, with the passive mixing elements 106, is able to fully oxygenate the blood over a shorter span of the device's length when compared to device 200 that does not include a passive mixing element 106. This allows for a shorter channel, and therefore allows the device to be primed with less blood than a channel without such passive mixing elements.
[0033] Figures 4A-J show a top and isometric view of possible, non-limiting examples of passive mixing elements 106. Figures 4 A and 4B illustrate an alternating herringbone pattern. The design consists of a herringbone pattern wherein the center of the herringbone pattern shifts from one side of the flow channel to the other through the length of the flow channel 102. In some implementations, the alternating herringbone pattern causes the fluid in the flow channel to enter the flow channel and begin rotating in a first direction. Then, when the flowing fluid encounters a shifted herringbone pattern, the fluid is forced to rotate in a direction opposite to the first rotational direction. For example, the fluid may enter the channel 102 flowing in a laminar fashion, and then alternatingly switch between clockwise and counter clockwise rotations as the fluid encounters consecutive, offset herringbone patterns. In some implementations, the number of chevrons per herringbone pattern and/or the number of groupings is configured to create a specific level of mixing over a given length of the device 100. In some implementations, the herringbone pattern does not alternate, but is constant along the duration of the flow channel. In some of these implementations the center of the herringbone patterns is in the center of the channel, while in other implementations the center of the pattern is off-center with respect to the channel.
[0034] As illustrated in Figures 4C and D, in some implementations, the mixing of a fluid is created with slanted ridges. Similar to the herringbone patter described above, in some implementations the slanted ridge pattern also creates a swirling rotation of the fluid that drives fluid from the bottom of the fluid flow channel towards the permeable membrane 103. In some implementations, the angle of the slanted ridge and the herringbone patter is between about 35 and about 55 degrees. In some implementations, the spacing between the ridges is between about 50 microns and about 100 microns, between about 100 microns and 150 microns, or between about 150 and about 200 microns. In some implementations, the spacing of the ridges is 2π/(ώε width of the channel), such that the diameter of the induced rotation is less than the width or depth of the channel. In some implementations, the ridges of the above implementations are rounded.
[0035] In yet other implementations, the passive mixing elements 106 are designed to create vortices and other high and low pressure areas which drive the fluid towards the membrane 103. For example, Figures 4E and 4F, like the illustrative implementation of Figure 3, include a plurality of ridges. In some implementations, the ridges are spaced between about 20 microns and about 50 microns, between about 50 microns and 100 microns or between about 100 microns and 500 microns.
[0036] In some implementations, the passive mixing elements can be, but are not limited to, posts, mounds, ramps, pits, cones or any combination thereof. Figures 4G-4J illustrate a possible post and mound implementation. In the implementation illustrated in Figures 4G and 4H, each row of posts is off set from the previous row. This causes the fluid to mix laterally in addition to driving fluid upwards. In other implementations, as illustrated in Figure 41 and 4J, the passive mixing elements are aligned with the passive mixing elements in the previous row.
[0037] Figure 5 is a flow chart of a method 500 for oxygenating blood with a microfluidic device. First, a microfluidic device is provided (step 501). Then, partially deoxygenated blood is introduced into a proximal end of the microfluidic device (step 502). The partially deoxygenated blood is flowed through a first channel of the microfluidic device (step 503), and oxygen is flowed through a second channel of the microfluidic device (step 504). Finally, oxygenated blood is collected from a distal end of the microfluidic device (step 505).
[0038] As set forth above, and referring to Figure 1, the method 500 for oxygenating partially deoxygenated blood begins with providing a microfluidic device (step 501). In some implementations, the microfluidic device is similar to device 100 described above. In other implementations, the microfluidic device includes a plurality of oxygen channels and/or a plurality of blood flow channels. In yet other implementations, the microfluidic device is a array of devices similar to device 100. In some implementations, the device is configured to allow for about 500-1000 mL/min, about 1-4 L/min, or about 4-5 L/min of blood flow. In some implementations, the device is configured to transfer oxygen into the blood at a rate of about 160 to about 200 mL/min.
[0039] Next, the method 500 of oxygenating blood continues with the introduction of partially deoxygenated blood into a proximal end of the microfluidic device (step 502). In some implementations, the blood is directly collected form a patient and introduced into the device. For example, the device may be part of a heart-lung bypass system that oxygenates blood during surgery. In other implementations, the blood is collected, stored, and then oxygenated at a later time. For example, the blood may be collected during a blood drive and then oxygenated prior to being transfused into a patient. In some implementation, the blood is actively pumped through the device by an external pump, and in other implementations the blood is pumped through the device by the patient's heart.
[0040] The method 500 continues by flowing the partially deoxygenated blood through a first blood flow channel (step 503). As described above, the device includes at least one passive mixing element that inducing mixing within the channel as the blood travels the length of the device. In some implementations, the blood is thinned with a blood thinning agent such as the drug Coumadin or Heparin. In some implementations, the walls of the blood flow channels are coated with an anticoagulant.
[0041] Responsive to flowing blood through the first blood flow channel, the method 500 continues by flowing oxygen through a first oxygen flow channel (step 504). Referring to Figure 1, the blood flow channel and oxygen flow channel are separated by a permeable membrane. Oxygen diffuses through the membrane, oxygenating the blood as it flows down the length of the channel. In some implementations, the blood is continually mixed within the channel by the passive mixing elements similar to those described above. In some
implementations, the continual mixing allows a given volume of deoxygenated blood to be oxygenated more efficiently by continually exposing different red blood cells to the region near the membrane where oxygen diffusion can occur. In other implementations, the membrane is also porous to carbon dioxide, and the carbon dioxide initially within the deoxygenated blood diffuses into the oxygen flow channel. In yet other implementations, the oxygen and blood are flowed through the microfluidic device starting at different ends. For example, the blood may enter the device at a proximal end and the oxygen may enter the device at a distal end of the device.
[0042] The method 500 continues, with the collection of the oxygenated blood at a distal end of the microfluidic channel. In some implementations, the oxygenated blood is transfused directly back into the patient from which it was collected. In other implementations, the blood is collected and stored for later transfusion or experimentation.

Claims

CLAIMS What is claimed:
1. A micro fluidic oxygenation device comprising:
a first polymer layer defining a first oxygen flow channel therein;
a second polymer layer defining a first blood flow channel therein, the first blood flow channel overlapping the first oxygen flow channel, and the first blood flow channel further comprising at least one passive mixing element formed on or within a first wall of the first blood flow channel, the passive mixing element configured to redistribute a fluid flowing through the first blood flow channel within the channel; and
a membrane separating the first oxygen flow channel and the first blood flow channel at the overlapping portions of the channels, the membrane allowing communication between the first oxygen flow channel and the first blood flow channel.
2. The device of claim 1, wherein the passive mixing element is one of a straight ridge, an angled ridge, a chevron canal, a dome, a cone, a pit or a post.
3. The device of claim 1, wherein a first fluid flows through the first oxygen flow
channel and a second fluid flows through the first blood flow channel.
4. The device of claim 3, wherein the first fluid is oxygen and the second fluid is
deoxygenated blood.
5. The device of claim 1, wherein the height or depth of the passive mixing element is less than about 30% of the height of the first blood flow channel.
6. The device of claim 1, wherein the first wall of the first blood flow channel is the floor of the first blood flow channel.
7. The device of claim 1, wherein the height of the first blood flow channel is between about 10 and 100 microns.
8. The device of claim 1, wherein the membrane thickness is between about 10 and about 50 microns.
9. The device of claim 1, wherein the length of the first oxygen flow channel and the first blood flow channel is between about 1 mm and about 50 mm.
10. The device of claim 1, where the width of the first blood flow channel is between about 100 microns and 200 microns.
11. The device of claim 1 , wherein the membrane is permeable to oxygen and carbon dioxide.
12. The device of claim 1, wherein the walls of the first blood flow channel are coated with an anticoagulant.
13. The device of claim 1, wherein the device includes a second blood flow channel
separated from the first oxygen flow channel by a second permeable membrane.
14. A method for oxygenating deoxygenate blood, the method comprising:
providing a microfluidic device comprising a first polymer layer defining a first oxygen flow channel; a second polymer layer defining a first blood flow channel, the first blood flow channel further comprising at least one passive mixing element formed in or on a surface of the first blood flow channel; and a membrane separating the first oxygen flow channel and the first blood flow channel, the membrane allowing communication between the first oxygen flow channel and the first blood flow channel;
introducing partially deoxygenated blood into a proximal end of the microfluidic device;
flowing oxygen through the first oxygen flow channel;
flowing the partially deoxygenated blood through the first blood flow channel; and
receiving oxygenated blood at a distal end of the microfluidic device.
15. The method of claim 14, further comprising:
collecting partially deoxygenated blood from a patient;
flowing the partially deoxygenated blood through the first blood flow channel to reoxygenate the blood; and
returning the reoxygenated blood to the patient.
16. The method of claim 15, further comprising removing carbon dioxide from the partially deoxygenated blood as the partially deoxygenated blood flows through the first blood flow channel.
17. The method of claim 14, further comprising flowing oxygen through the first oxygen flow channel from a first direction.
18. The method of claim 14, further comprising flowing blood through the first blood flow channel in a second direction opposite to the first direction.
19. The method of claim 14, further comprising flowing the blood through the first blood flow channel at 4-5 L/min.
20. The method of claim 14, further comprising transferring oxygen into the blood at a rate of about 150-200 mL/min.
PCT/US2012/067971 2011-12-05 2012-12-05 Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices WO2013086011A1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP2014546025A JP6395608B2 (en) 2011-12-05 2012-12-05 Method for reducing blood injection volume and membrane surface area in a microfluidic lung assist device
AU2012347922A AU2012347922B2 (en) 2011-12-05 2012-12-05 Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices
EP12799501.7A EP2788042B1 (en) 2011-12-05 2012-12-05 Device for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices
CN201280059591.9A CN104053461A (en) 2011-12-05 2012-12-05 Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices
ES12799501T ES2700249T3 (en) 2011-12-05 2012-12-05 Procedure to reduce the priming volume and the surface area of the membrane in the microfluidic pulmonary assist devices
CA2858080A CA2858080C (en) 2011-12-05 2012-12-05 Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices
IN4342CHN2014 IN2014CN04342A (en) 2011-12-05 2012-12-05

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201161567104P 2011-12-05 2011-12-05
US61/567,104 2011-12-05

Publications (1)

Publication Number Publication Date
WO2013086011A1 true WO2013086011A1 (en) 2013-06-13

Family

ID=47352068

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2012/067971 WO2013086011A1 (en) 2011-12-05 2012-12-05 Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices

Country Status (9)

Country Link
US (1) US9180239B2 (en)
EP (1) EP2788042B1 (en)
JP (1) JP6395608B2 (en)
CN (1) CN104053461A (en)
AU (1) AU2012347922B2 (en)
CA (1) CA2858080C (en)
ES (1) ES2700249T3 (en)
IN (1) IN2014CN04342A (en)
WO (1) WO2013086011A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105682700A (en) * 2013-09-16 2016-06-15 强生创新有限责任公司 Microfluidic organ assist device incorporating boundary layer disrupters
WO2017205818A1 (en) * 2016-05-27 2017-11-30 The Charles Stark Draper Laboratory Inc. Biomimetic microfluidic device for high efficiency carbon dioxide removal from patients at low blood flow rates
EP3967143A1 (en) * 2013-02-28 2022-03-16 Hemanext Inc. Gas addition device for blood treatment and corresponding method

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9199016B2 (en) 2009-10-12 2015-12-01 New Health Sciences, Inc. System for extended storage of red blood cells and methods of use
US11284616B2 (en) 2010-05-05 2022-03-29 Hemanext Inc. Irradiation of red blood cells and anaerobic storage
AU2011258203A1 (en) * 2010-05-26 2013-01-10 The Charles Stark Draper Laboratory, Inc. Microfabricated artificial lung assist device, and methods of use and manufacture thereof
JP2017513625A (en) 2014-04-23 2017-06-01 ザ チャールズ スターク ドレイパー ラボラトリー インク Blood oxygenator
MX2017011595A (en) 2015-03-10 2018-06-15 New Health Sciences Inc Oxygen reduction disposable kits, devices and methods of use thereof.
JP7175611B2 (en) 2015-04-23 2022-11-21 ヘマネクスト インコーポレイテッド Anaerobic blood storage container
BR112017024091B1 (en) 2015-05-18 2022-09-20 Hemanext Inc METHOD TO REDUCE CYTOKINES IN A STORED WHOLE BLOOD PRODUCT, STORED WHOLE BLOOD COMPOSITION AND USE OF A STORED WHOLE BLOOD PRODUCT
JP7148499B2 (en) 2016-05-27 2022-10-05 ヘマネクスト インコーポレイテッド Anaerobic blood storage and pathogen inactivation methods
US11988471B2 (en) * 2021-03-27 2024-05-21 Massachusetts Institute Of Technology Devices and methods for fabrication of components of a multiscale porous high-temperature heat exchanger

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002076529A1 (en) * 2001-03-12 2002-10-03 Stichting Hogeschool Van Utrecht Blood processing device
US20110158847A1 (en) * 2009-12-31 2011-06-30 Charest Joseph L Microfluidic Device Facilitating Gas Exchange, and Methods of Use and Manufacture Thereof
US20110226686A1 (en) * 2008-09-03 2011-09-22 Novalung Gmbh Gas transfer device and use of a structured membrane
WO2011150216A1 (en) * 2010-05-26 2011-12-01 The Charles Stark Draper Laboratory, Inc. Microfabricated artificial lung assist device, and methods of use and manufacture thereof

Family Cites Families (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2876769A (en) 1955-10-11 1959-03-10 Cordova Jose Juan Apparatus for oxygenating, centrifuging and changing the temperature of blood
US3489647A (en) 1964-05-06 1970-01-13 Dow Corning Artificial organ for membrane dialysis of biological fluids
US3847211A (en) 1969-01-28 1974-11-12 Sub Marine Syst Inc Property interchange system for fluids
US3738813A (en) 1971-06-04 1973-06-12 W Esmond Mass transfer device and method of making same
GB1408562A (en) 1971-07-26 1975-10-01 Atomic Energy Authority Uk Apparatus for use in dialysis
GB1442754A (en) * 1972-06-28 1976-07-14 Nat Res Dev Apparatus for and method of effecting heat or mass transfer berween fluids
JPS5570149U (en) * 1978-11-06 1980-05-14
JPS573652A (en) 1980-06-06 1982-01-09 Kanegafuchi Chemical Ind Artificial lung using minute hole diameter film
FR2504392A1 (en) * 1981-04-24 1982-10-29 Hospal Sodip MEMBRANE APPARATUS WITH OFFSET ACTION SUPPORTS
US4620965A (en) 1982-09-22 1986-11-04 Terumo Corporation Hollow fiber-type artificial lung
JPS6264372A (en) 1985-09-13 1987-03-23 テルモ株式会社 Membrane type artificial lung
US4997565A (en) * 1986-06-16 1991-03-05 Niesen Lawrence J Laboratory scale ultrafiltration apparatus
US4756835A (en) 1986-08-29 1988-07-12 Advanced Polymer Technology, Inc. Permeable membranes having high flux-density and low fouling-propensity
GB8817793D0 (en) * 1988-07-26 1988-09-01 British Petroleum Co Plc Mixing apparatus
US5254259A (en) * 1989-08-17 1993-10-19 Bellhouse Brian John Method and apparatus for effecting the transfer of heat or mass through a membrane involving the use of vortices
US5207639A (en) 1991-02-21 1993-05-04 Cooper William I Fetal lung apparatus
US6514412B1 (en) * 1998-06-18 2003-02-04 3M Innovative Properties Company Microstructured separation device
US6241945B1 (en) 1998-03-16 2001-06-05 Life Science Holdings, Inc. Modular combined pump, filtration, oxygenation and/or debubbler apparatus
US7759113B2 (en) 1999-04-30 2010-07-20 The General Hospital Corporation Fabrication of tissue lamina using microfabricated two-dimensional molds
US7371400B2 (en) 2001-01-02 2008-05-13 The General Hospital Corporation Multilayer device for tissue engineering
US6759008B1 (en) 1999-09-30 2004-07-06 Therox, Inc. Apparatus and method for blood oxygenation
US7776021B2 (en) 2000-04-28 2010-08-17 The Charles Stark Draper Laboratory Micromachined bilayer unit for filtration of small molecules
JP2004512062A (en) 2000-07-28 2004-04-22 エモリー ユニバーシテイ Biological components consisting of artificial membranes
DE10139830A1 (en) 2001-08-14 2003-02-27 Roche Diagnostics Gmbh Flat sheet membrane, for filtration, has channel apertures five times larger than membrane nominal pore size
US20030175149A1 (en) 2002-03-18 2003-09-18 Bruce Searles Renewable, modifiable, membrane gas exchanger
US8147562B2 (en) 2002-09-23 2012-04-03 The General Hospital Corporation Three dimensional construct for the design and fabrication of physiological fluidic networks
AU2005294236A1 (en) 2004-10-06 2006-04-20 Home Dialysis Plus, Ltd. Mecs dialyzer
US7955504B1 (en) * 2004-10-06 2011-06-07 State Of Oregon Acting By And Through The State Board Of Higher Education On Behalf Of Oregon State University Microfluidic devices, particularly filtration devices comprising polymeric membranes, and method for their manufacture and use
US8663625B2 (en) 2004-10-15 2014-03-04 Cornell Research Foundation Diffusively permeable monolithic biomaterial with embedded microfluidic channels
US7794593B2 (en) 2005-11-30 2010-09-14 3M Innovative Properties Company Cross-flow membrane module
GB2437254B (en) * 2006-04-13 2010-11-17 Haemair Ltd Blood/air mass exchange apparatus
EP2200931B1 (en) 2007-09-19 2017-06-07 The Charles Stark Draper Laboratory, Inc. Microfluidic structures with circular cross-section
US20090234332A1 (en) 2008-03-17 2009-09-17 The Charles Stark Draper Laboratory, Inc Artificial microvascular device and methods for manufacturing and using the same
US8292492B2 (en) * 2008-11-11 2012-10-23 Sandia Corporation Airfoil-shaped micro-mixers for reducing fouling on membrane surfaces
US20110186165A1 (en) 2009-10-05 2011-08-04 Borenstein Jeffrey T Three-dimensional microfluidic platforms and methods of use and manufacture thereof
US9844779B2 (en) 2011-01-14 2017-12-19 The Charles Stark Draper Laboratory, Inc. Membrane-integrated microfluidic device for imaging cells

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002076529A1 (en) * 2001-03-12 2002-10-03 Stichting Hogeschool Van Utrecht Blood processing device
US20110226686A1 (en) * 2008-09-03 2011-09-22 Novalung Gmbh Gas transfer device and use of a structured membrane
US20110158847A1 (en) * 2009-12-31 2011-06-30 Charest Joseph L Microfluidic Device Facilitating Gas Exchange, and Methods of Use and Manufacture Thereof
WO2011150216A1 (en) * 2010-05-26 2011-12-01 The Charles Stark Draper Laboratory, Inc. Microfabricated artificial lung assist device, and methods of use and manufacture thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3967143A1 (en) * 2013-02-28 2022-03-16 Hemanext Inc. Gas addition device for blood treatment and corresponding method
CN105682700A (en) * 2013-09-16 2016-06-15 强生创新有限责任公司 Microfluidic organ assist device incorporating boundary layer disrupters
WO2017205818A1 (en) * 2016-05-27 2017-11-30 The Charles Stark Draper Laboratory Inc. Biomimetic microfluidic device for high efficiency carbon dioxide removal from patients at low blood flow rates
US11673094B2 (en) 2016-05-27 2023-06-13 The Charles Stark Draper Laboratory, Inc. Biomimetic microfluidic device for high efficiency carbon dioxide removal from patients at low blood flow rates

Also Published As

Publication number Publication date
AU2012347922B2 (en) 2017-12-21
IN2014CN04342A (en) 2015-09-04
CA2858080C (en) 2020-12-01
CA2858080A1 (en) 2013-06-13
US9180239B2 (en) 2015-11-10
JP6395608B2 (en) 2018-09-26
EP2788042B1 (en) 2018-10-31
US20130144266A1 (en) 2013-06-06
CN104053461A (en) 2014-09-17
JP2015500699A (en) 2015-01-08
ES2700249T3 (en) 2019-02-14
AU2012347922A1 (en) 2014-06-12
EP2788042A1 (en) 2014-10-15

Similar Documents

Publication Publication Date Title
AU2012347922B2 (en) Method for reducing the blood priming volume and membrane surface area in microfluidic lung assist devices
US8647410B2 (en) Microfabricated artificial lung assist device, and methods of use and manufacture thereof
Su et al. A water-powered micro drug delivery system
JP5669737B2 (en) Use of gas transport equipment and structured membranes
EP2943281B1 (en) Microfluidic device for increasing convective clearance of undesired particles
AU763508B2 (en) Membrane apparatus with enhanced mass transfer, heat transfer and pumping capabilities via active mixing
Thompson et al. Design analysis and optimization of a single-layer PDMS microfluidic artificial lung
US9597441B2 (en) Microfluidic organ assist device incorporating boundary layer disrupters
US6723284B1 (en) Membrane apparatus with enhanced mass transfer, heat transfer and pumping capabilities via active mixing
CN106794295B (en) Systems and methods for increasing convective clearance of undesired particles in a microfluidic device
JP2015500699A5 (en)
TW202123985A (en) Blood treatment systems
US10342909B2 (en) Systems and methods for increasing convective clearance of undesired particles in a microfluidic device
TW202128235A (en) Blood treatment systems

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12799501

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2858080

Country of ref document: CA

ENP Entry into the national phase

Ref document number: 2014546025

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2012347922

Country of ref document: AU

Date of ref document: 20121205

Kind code of ref document: A