AU741088B2 - A centrifuge apparatus with temperature control means - Google Patents
A centrifuge apparatus with temperature control means Download PDFInfo
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- AU741088B2 AU741088B2 AU58169/98A AU5816998A AU741088B2 AU 741088 B2 AU741088 B2 AU 741088B2 AU 58169/98 A AU58169/98 A AU 58169/98A AU 5816998 A AU5816998 A AU 5816998A AU 741088 B2 AU741088 B2 AU 741088B2
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- Australia
- Prior art keywords
- container
- piston
- temperature
- heat
- emitting device
- Prior art date
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- 238000010438 heat treatment Methods 0.000 claims description 30
- BWGVNKXGVNDBDI-UHFFFAOYSA-N Fibrin monomer Chemical group CNC(=O)CNC(=O)CN BWGVNKXGVNDBDI-UHFFFAOYSA-N 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 16
- 229910052736 halogen Inorganic materials 0.000 claims description 11
- 150000002367 halogens Chemical class 0.000 claims description 11
- 108010073651 fibrinmonomer Proteins 0.000 claims description 10
- 230000003213 activating effect Effects 0.000 claims description 7
- 230000008569 process Effects 0.000 claims description 7
- 230000004044 response Effects 0.000 claims description 5
- 230000005855 radiation Effects 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 2
- 239000008280 blood Substances 0.000 description 33
- 210000004369 blood Anatomy 0.000 description 33
- 108010073385 Fibrin Proteins 0.000 description 8
- 102000009123 Fibrin Human genes 0.000 description 8
- 229950003499 fibrin Drugs 0.000 description 8
- 108010049003 Fibrinogen Proteins 0.000 description 6
- 102000008946 Fibrinogen Human genes 0.000 description 6
- 238000005119 centrifugation Methods 0.000 description 6
- 239000000306 component Substances 0.000 description 6
- 229940012952 fibrinogen Drugs 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 108090000790 Enzymes Proteins 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 4
- 229940088598 enzyme Drugs 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 101000772006 Bombus ignitus Venom serine protease Bi-VSP Proteins 0.000 description 3
- 108090000190 Thrombin Proteins 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 229960004072 thrombin Drugs 0.000 description 3
- 101800000974 Fibrinopeptide A Proteins 0.000 description 2
- 101800003778 Fibrinopeptide B Proteins 0.000 description 2
- 238000003776 cleavage reaction Methods 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- 229920000515 polycarbonate Polymers 0.000 description 2
- 230000007017 scission Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- JWICNZAGYSIBAR-LEEGLKINSA-N (4s)-4-[[2-[[(2s)-2-[[(2s)-2-[[(2s)-2-aminopropanoyl]amino]-3-carboxypropanoyl]amino]-3-hydroxypropanoyl]amino]acetyl]amino]-5-[[2-[[(2s)-3-carboxy-1-[[(2s)-1-[[1-[[(2s)-1-[[(2s)-4-carboxy-1-[[2-[[2-[[2-[[(2s)-1-[[(1s)-1-carboxy-4-(diaminomethylideneamino Chemical compound NC(N)=NCCC[C@@H](C(O)=O)NC(=O)[C@H](C(C)C)NC(=O)CNC(=O)CNC(=O)CNC(=O)[C@H](CCC(O)=O)NC(=O)[C@H](C)NC(=O)C(CC(C)C)NC(=O)[C@@H](NC(=O)[C@H](CC(O)=O)NC(=O)CNC(=O)[C@H](CCC(O)=O)NC(=O)CNC(=O)[C@H](CO)NC(=O)[C@H](CC(O)=O)NC(=O)[C@H](C)N)CC1=CC=CC=C1 JWICNZAGYSIBAR-LEEGLKINSA-N 0.000 description 1
- 108010080379 Fibrin Tissue Adhesive Proteins 0.000 description 1
- 102400000525 Fibrinopeptide A Human genes 0.000 description 1
- 102400001063 Fibrinopeptide B Human genes 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000012503 blood component Substances 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- MYRIFIVQGRMHRF-OECXYHNASA-N fibrinopeptide b Chemical compound N([C@@H](C(C)C)C(=O)N[C@@H](CC(N)=O)C(=O)N[C@@H](CC(O)=O)C(=O)N[C@@H](CC(N)=O)C(=O)N[C@@H](CCC(O)=O)C(=O)N[C@@H](CCC(O)=O)C(=O)NCC(=O)N[C@@H](CC=1C=CC=CC=1)C(=O)N[C@@H](CC=1C=CC=CC=1)C(=O)N[C@@H](CO)C(=O)N[C@@H](C)C(=O)N[C@@H](CCCNC(N)=N)C(O)=O)C(=O)CNC(=O)[C@@H]1CCC(=O)N1 MYRIFIVQGRMHRF-OECXYHNASA-N 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000006187 pill Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B15/00—Other accessories for centrifuges
- B04B15/02—Other accessories for centrifuges for cooling, heating, or heat insulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0217—Separation of non-miscible liquids by centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/042—Breaking emulsions by changing the temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
- B01D21/262—Separation of sediment aided by centrifugal force or centripetal force by using a centrifuge
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/34—Controlling the feed distribution; Controlling the liquid level ; Control of process parameters
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01K—MEASURING TEMPERATURE; MEASURING QUANTITY OF HEAT; THERMALLY-SENSITIVE ELEMENTS NOT OTHERWISE PROVIDED FOR
- G01K7/00—Measuring temperature based on the use of electric or magnetic elements directly sensitive to heat ; Power supply therefor, e.g. using thermoelectric elements
- G01K7/42—Circuits effecting compensation of thermal inertia; Circuits for predicting the stationary value of a temperature
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/48—Biological material, e.g. blood, urine; Haemocytometers
- G01N33/483—Physical analysis of biological material
- G01N33/487—Physical analysis of biological material of liquid biological material
- G01N33/49—Blood
- G01N33/491—Blood by separating the blood components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2221/00—Applications of separation devices
- B01D2221/10—Separation devices for use in medical, pharmaceutical or laboratory applications, e.g. separating amalgam from dental treatment residues
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/04—Radial chamber apparatus for separating predominantly liquid mixtures, e.g. butyrometers
- B04B5/0442—Radial chamber apparatus for separating predominantly liquid mixtures, e.g. butyrometers with means for adding or withdrawing liquid substances during the centrifugation, e.g. continuous centrifugation
- B04B2005/0485—Radial chamber apparatus for separating predominantly liquid mixtures, e.g. butyrometers with means for adding or withdrawing liquid substances during the centrifugation, e.g. continuous centrifugation with a displaceable piston in the centrifuge chamber
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Thermal Sciences (AREA)
- Biomedical Technology (AREA)
- General Physics & Mathematics (AREA)
- Hematology (AREA)
- Ecology (AREA)
- General Health & Medical Sciences (AREA)
- Urology & Nephrology (AREA)
- Food Science & Technology (AREA)
- Medicinal Chemistry (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- Molecular Biology (AREA)
- Biophysics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Centrifugal Separators (AREA)
- Investigating Or Analysing Biological Materials (AREA)
- Automatic Analysis And Handling Materials Therefor (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Description
WO 98/30304 PCT/US98/00251 1 A Centrifuge Apparatus with Temperature Control Means Technical Field The invention relates to methods and apparatus for centrifuging and monitoring/controlling the temperature of a liquid, blood, within a rotating centrifuge container.
Background Art U.S. 5,603,845, WO 96/16713, WO 96/16714 and WO 96/16715 disclose a method and a container for separating a component, such as fibrin monomer, from blood or plasma by centrifugation, whereby blood is fed to a first annular chamber in a device, where the annular chamber is defined by a cylindrical outer wall and a cylindrical inner wall, both walls extending coaxially about a common axis, as well as by a top wall and a bottom wall. The top wall is formed by a piston body displaceable within the first chamber. This method involves a centrifugation of the device about the said common axis to substantially separate blood into a cell fraction and a plasma fraction followed by the resulting plasma fraction being transferred while influenced by the piston body to a second chamber defined by an outer cylindrical wall. The outer cylindrical wall extends coaxially with the said common axis, whereby a fraction with fibrin monomer is caused to be separated in the second chamber while a suitable enzyme is being added. The separation of fibrin monomer from the plasma fraction in the second chamber is carried out during continued centrifugation whereby a polymerized fibrin is deposited on the cylindrical outer wall of said second chamber, whereafter the fluid fraction collected at the bottom of the second chamber is transferred while influenced by the piston body to the first chamber. The fraction with polymerized fibrin deposited on the cylindrical wall in the second chamber is caused to be dissolved by addition of a solvent and by centrifugation, whereafter it is WO 98/30304 PCT/US98/00251 2 transferred to a receiving container placed within the piston rod by passing after enzyme capture and filtration, whereby a fibrin monomer-containing solution is provided.
U.S. Patent 5,603,845 discloses an apparatus for initiating such a centrifuging. This apparatus comprises a housing which is basically divided into three compartments, viz. an upper compartment, a central compartment, and a lower compartment. The container with the fluid to be separated is placed in the central compartment. It is placed on a rotatable supporting turntable which is rotatably journalled on a journalling shaft, said shaft constituting an output shaft of a motor which is housed in the lower compartment. Accordingly, this motor constitutes a means for generating the high rotational speed at which the container is to be rotated about its central axis at a number of process steps. The latter process steps correspond to the separating process which the fluid is to be subjected to in order to be separated into the desired fluid components. The container is retained on the supporting turntable by means of gripping means engaging openings shaped along the lower rim of the container.
A
motor is arranged in the upper compartment. The said motor co-operates with a gripping means which is rotatably journalled and adapted to be vertically displaced so as to engage and co-operate with the piston rod of the container. This centrifuge apparatus corresponds to the apparatus described in the introduction to the specification.
EP 592242 describes a novel fibrin sealant method which prepares and utilizes fibrin monomer which is understood to refer to fibrin I, fibrin II or des BB fibrin. The monomer can be prepared using apparatus and methods as described in the aforementioned U.S. 5,603,845,
WO
96/16713, WO 96/16714 and WO 96/16715. Essentially, plasma fibrinogen is subjected to an enzyme which catalyzes the cleavage of fibrinopeptide A and/or B from fibrinogen, thrombin or a thrombin-like enzyme which converts fibrinogen to fibrin. Nondynamic fibrin monomer WO 98/30304 PCT/US98/00251 3 compositions can thereafter be obtained, for example, by solubilizing the resulting non-crosslinked fibrin polymer in a low Ph, about pH-4, buffer where the fibrin monomer is prevented from polymerizing until the pH is raised.
Summary of the Invention It has now been found that processes for producing and utilizing fibrin monomer are enhanced when the blood or plasma is heated to about 370 C during the processing cycle. Accordingly, the present invention involves methods of preparing fibrin monomer solutions and compositions from blood or plasma wherein the blood or plasma is heated to about 370 C prior to and during processing with the thrombin or thrombin-like enzyme. In preferred embodiments, the blood is preheated at low rotational speeds, 500-2000 RPM, with a heat source which radiates energy in the visible light range and the temperature of the blood is sensed indirectly using the formula T blood A T air B T surface where T blood the temperature of the blood T air the temperature of the surrounding air T surface the temperature of the surface of the blood container A a coefficient for the air B a coefficient for the surface of the container.
Using this formula and measuring T air and T surface, the temperature of the blood can be determined. Further, this can be fed into a control unit which controls the heat source.
Brief Description of the Drawing The invention is explained in greater detail below with reference to the accompanying drawing, in which WO 98/30304 PCT/US98/00251 4 FIG. 1 is a diagrammatic front view of parts of the apparatus according to the invention and with a container arranged therein for the separation of components of a liquid.
Detailed Description of Preferred Embodiments In accordance with the present invention an enhanced centrifuge system with capabilities of monitoring and controlling the temperature of a liquid, blood, during centrifugation is provided. It has been found that subjecting plasma fibrinogen to an enzyme which catalyzes the cleavage of fibrinopeptides A and/or B from fibrinogen, a thrombin or thrombinlike enzyme which converts fibrinogen to fibrin, proceeds more efficiently when the blood or plasma is at about 37' C. Careful temperature control is important since temperatures too low will not provide the enhanced effect and temperatures exceeding 40' C can damage the blood component and cells.
According to the invention it is particularly advantageous that the heatemitting device comprises a first heating source for emission of visible light substantially being directed towards the blood-containing portion, or first chamber, of the centrifuge container. Correspondingly, the wall of the centrifuge container is chosen to be of a visible light transmissive material so that the heat is transferred effectively to the blood with minimal excess heat absorption by the container itself. Medical grade plastics such as polycarbonate are preferred. The resulting utilization of the energy release from the heat-emitting device through the wall to the blood is thus optimal.
Furthermore, the heat-emitting device may according to the invention optionally comprise a second heating source for emission of infrared radiation substantially directed towards a second chamber in the container into which a fraction of the blood will be subsequently transferred for WO 98/30304 PCT/US98/00251 further processing at the desired temperature. In this manner it is possible to keep the container wall absorbing the infrared radiation at a desired temperature.
According to the invention it is Particularly preferred that the heat-emitting device is associated with a first temperature sensor for detecting the temperature of the air in the area around the container to be handled, as well as with a second temperature sensor for detecting the temperature of the container surface, and furthermore that a control unit is provided for controlling the heat-emitting device in response to the detected temperatures. Thus it is ensured in a particularly simple manner that the desired temperatures are maintained.
Furthermore, the control unit may according to the invention be adapted to successively activate the first and the second heating source in response to the part of the container running the separating process. In this manner the desired temperatures are ensured in the most advantageous manner.
According to the invention the first heating source may particularly advantageously be a halogen bulb, and the second heating source a heating plate of metal.
The apparatus shown in FIG. 1 comprises a supporting turntable 1 which is rotatably journalled in a housing not shown in greater detail by means of a ball bearing 2, cf. FIG. 2. The supporting turntable is formed integral with a vertical driving shaft 3. The driving shaft is connected through a coupling 4 to a motor 5 causing the supporting turntable to follow a rotating movement about a vertical axis of rotation. An activating bar 6 is rotatably journalled coaxially with the axis of rotation inside the driving shaft 3 of the supporting turntable 1, said activating bar 6 being connected through a coupling 7 with a spindle motor 8 with a spindle 9 in WO 98/30304 PCT/US98/00251 6 such a manner that when the spindle motor 8 is activated the activating bar 6 can be displaced vertically upwardly or downwardly for a releasable retaining of a container 10 on the supporting turntable 1.
The container 10 is arranged on top of the supporting turntable, said container being of the type described in U.S. Patent 5,603,845 or WO 96/16713, comprising a cylindrical member 11 and a piston 25 shown by means of dotted lines. The piston 25 is driven by means of a tubular piston rod 12 projecting upwardly from the upper end of the container The piston rod 12 is activated by means of a gripping means 13, which in turn is activated by means of a spindle motor 15 through a spindle 16 and a activating bar 17 connected thereto. The gripping means 13 is furthermore rotatably journalled in a housing 18 through a ball bearing 19. The housing 18 and the spindle motor 15 are secured to a common carrier indicated by means of dotted lines at the reference numeral 19. This carrier 19 is displaceably mounted on a rail 20 and caused to be vertically displaced thereon by means of a motor 21. The motor 21 co-operates through a ball spindle with a ball nut 23 stationarily secured in the apparatus in such a manner that a rotation of the ball spindle 22 by means of the motor 21 causes a movement of the carrier 19 and consequently of the gripping means 13 along the slide The apparatus of FIG. 1 is used in such a manner that the container with its content is subjected to centrifugation heat source, which is preferably described herein as a halogen bulb 26 is arranged substantially opposite the area above the piston 26, cf. the diagrammatic view of FIG. 1, said halogen bulb being adapted to subject this portion of the container 10 to a visible light. In a similar manner a heating plate 27 is arranged substantially opposite the area below the piston 25, cf. the diagrammatic view of FIG. 1 as well, said heating plate 27 subjecting this portion of the container 10 to an infrared radiation. The heating plate 27 can optionally be curved in such a manner that it substantially presents a curvature WO 98/30304 PCT/US98/00251 7 mating the outer periphery of the container. Both the halogen bulb 26 and the heating plate 27 are connected to a control unit 28 through respective conduits 29 and 30, respectively. The control unit 28 is also connected to temperature sensor 31 and optional sensor 32, respectively, through conduits 33 and 34, respectively. The temperature sensor 31 is adapted to measure the temperature on the surface of the portion of the container above the piston 25 while the temperature sensor 32 is adapted to measure the temperature on the surface of the portion of the container below the piston 25 and these sensors 31, 32 can be, infrared sensors. In addition, a sensor 35 is provided for measuring the temperature of the air around the container 10. The latter temperature sensor 35 is connected to the control unit 28 through a conduit 36. Both the halogen bulb 26 and the heating plate 27 are controlled by means of the control unit 28 in such a manner that as far as it is possible the blood and the components thereof contained in the container 10 are kept at a temperature of 370C during the stay inside the apparatus.
There are several difficulties in accomplishing this. First, the heating element, the bulb 26, is not in direct contact with the blood to be heated and neither are any of the temperature sensors. Also, the blood is contained within a plastic container which must be taken into account.
Further, in many processes using such apparatus, the container with blood is spinning, being rotated. All of these factors need to be considered since in such a rotating container it is extremely difficult to position temperature probes directly into the blood.
It has been found that the temperature of the blood can be arrived at by indirectly measuring the temperature of the surface of the container and the temperature of the surrounding air using the formula.
Tblood ATi BTsurface WO 98/30304 PCT/US98/00251 8 where Tblood is the temperature of the blood, Tsuface is the temperature on the surface of the container wall 37, and Tair is the temperature of the surrounding air.
A and B are coefficients which are functions of the heat transfer coefficient of the air at the surface of the container, respectively, and depend partially on the rate of rotation of the container Coefficients A and B can be obtained experimentally with a series of trial runs for a given process by experimentally measuring the value of Tblood, Tair and Tsurface. Tbtood can be measured experimentally by stopping the process and taking direct temperature readings or by using a commercially available "heat pill", a small temperature sensitive capsule which can be placed into the blood during heating for remote readings. These coefficients can also be obtained theoretically using known equations by taking into account the energy flowing from the container to the air, the energy flowing from the inside of the wall of the container to the outside surface of the wall, and the energy flowing from the liquid (blood) to the container wall, assuming a steady state where all energy is transferred by the container wall and the air. In theoretical calculations, the heat transfer coefficient of the air depends of the rotational speed of the container in a directly proportioned manner.
In practice the rotational speed increases the coefficients A and B with higher rotational speeds. Higher coefficients are believed to make the above formula less sensitive and less accurate therefore lower rotational speeds, for example, 500-2500 RPM, have been found useful for preheating blood (about 100-150 ml) in a cylindrical centrifuge contained for processing. Preferably the speed during initial heating and temperature stabilization is about 1000 RPM. These speeds are useful in that they keep the coefficient values for A and B lower and yet providing a gently mixing of the blood and movement of the outside air for more uniform WO 98/30304 PCT/US98/00251 9 heating.
As mentioned above, the halogen bulb has been chosen because it emits an essentially visible light, the energy of which passes substantially freely through the container wall 37 and directly into the blood portion 38 without having undue amounts of heat energy absorbed by the material of the container wall.
An optional heating plate 27 emitting an infrared light has been chosen for heating the portion of the container below the piston 25 because the energy of infrared light is absorbed in the material of the container wall 37.
Such a choice of light is the most advantageous choice for this portion of the container 10 because nothing but a relatively small amount of liquid is present inside the container wall 37 in this portion. Therefore the heating plate 27 is solely controlled by a measuring of the surface temperature of the container wall on this portion of the container. This temperature is, as mentioned, measured by means of the temperature sensor 32.
When the described apparatus is used, the halogen bulb 26 is initially activated, and this activation continues as long as the blood portion positioned above the piston 25 is subjected to a centrifuging, and the desired separated component is transferred from this position to the area below the piston 25 by way of an actuation of the piston 25 through the piston rod 12. Subsequently, the halogen bulb 26 is turned off and actuates thereby the heating plate 27 so as to heat the lowermost portion of the container 10 during the continued step of the separation procedure.
The invention has been described with reference to a preferred embodiment. Many modifications can be carried out without thereby deviating from the scope of the invention. It is for instance possible to use other heating sources emitting the desired light beams instead of the above heating sources, viz. the halogen bulb 26 and the heating plate 27. Only one heating source can, if desired, be used for covering the entire container provided said heating source emits light beams of both types. The above constants A and B have been calculated in consideration of the visible light from the halogen bulb passing almost freely through the container wall 37, which is the case when said container wall is made of polycarbonate, which it often is. When the container is made of another plastic material, it can be necessary to adjust the coefficients in question in response thereto, said coefficients being found by way of practical tests as described herein.
Throughout the description and claims of this specification, the word "comprise" and variations of the word, such as "comprising" and "comprises", is not intended S0* to exclude other additives, components, integers or steps.
•0 00
S@*
C:%WINWORDVALISON\SPECM8169SPE.DOC
Claims (7)
1. An apparatus for centrifuging and furthermore automatically handling a container for separating a component, such as fibrin monomer, from plasma, where said container comprises a cylindrical member and a piston displaceable therein and comprising a tubular piston rod, which extends through a top wall, and where said piston divides the cylindrical member into a first chamber positioned above said piston between said piston and said top wall and a second chamber positioned below said piston,.and where said apparatus comprises a supporting turntable with means for releasably retaining the cylindrical member, O said supporting turntable being connected to a first activating means for rotating the supporting turntable with the container about the central axis thereof, and where said apparatus further comprises a rotatably journalled piston activating mechanism adapted to activate the piston by means of a second activating 15 means, wherein a heat-emitting device is provided opposite the position of the cylindrical member in the apparatus and the heat- emitting device is associated with a first temperature sensor for detecting the temperature of the air in the area around the container to be handled, as well as with a second temperature 2 sensor for detecting the temperature of the container surface, and that a control lol unit is provided for controlling the heat-emitting device in response to the detected temperatures.
2. An apparatus as claimed in claim 1, wherein the heat-emitting device comprises a firft-heating source for emitting visible light substantially directed towards the position of the first chamber in the container to be handled.
3. An apparatus as claimed in claim 2, wherein the heat-emitting device comprises a second heating source emission of infrared radiation substantially directed towards the position of the second chamber in the container to be handled. 12
4. An apparatus as claimed in claim 3, wherein the control unit is adapted to successively activate the first and the second heating source in response to the part of the container running the separating process.
An apparatus as claimed in claim 2, wherein the first heating source is a halogen bulb.
6. An apparatus as claimed in claim 3, wherein the second heating source is a heating plate of metal.
7 7 An apparatus substantially as hereinbefore described as illustrated in figure I. 20 DATED: 10 September 2001 PHILLIPS ORMONDE FITZPATRICK Attorneys for: BRISTOL-MYERS SQUIBB COMPANY
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU15596/02A AU765827B2 (en) | 1997-01-08 | 2002-02-13 | A method for monitoring/controlling the temperature of a liquid and for producing fibrin |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US3405697P | 1997-01-08 | 1997-01-08 | |
| US60/034056 | 1997-01-08 | ||
| PCT/US1998/000251 WO1998030304A1 (en) | 1997-01-08 | 1998-01-08 | A centrifuge apparatus with temperature control means |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU15596/02A Division AU765827B2 (en) | 1997-01-08 | 2002-02-13 | A method for monitoring/controlling the temperature of a liquid and for producing fibrin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU5816998A AU5816998A (en) | 1998-08-03 |
| AU741088B2 true AU741088B2 (en) | 2001-11-22 |
Family
ID=21874032
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU58169/98A Ceased AU741088B2 (en) | 1997-01-08 | 1998-01-08 | A centrifuge apparatus with temperature control means |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP0975429A1 (en) |
| JP (1) | JP2001508447A (en) |
| AU (1) | AU741088B2 (en) |
| BR (1) | BR9806736A (en) |
| CA (1) | CA2277858A1 (en) |
| IL (1) | IL130728A (en) |
| NZ (1) | NZ336398A (en) |
| WO (1) | WO1998030304A1 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2366732C (en) * | 1999-03-25 | 2008-11-18 | Alphahelix Ab | Homogenising of small-volume mixtures by centrifugation and heating |
| US7033501B1 (en) * | 1999-09-24 | 2006-04-25 | Bristol-Myers Squibb Company | Centrifuge apparatus and method with improved temperature control |
| DE60032918T2 (en) * | 1999-10-12 | 2007-10-18 | Pneumatic Scale Corp., Cuyahoga Falls | CONTROL OF DISTRIBUTION IN A CENTRIFUGE |
| CN110882854B (en) * | 2019-12-10 | 2023-12-19 | 张家港市蓝鸟机械有限公司 | An oil-heated centrifugal device |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3604769A (en) * | 1968-09-23 | 1971-09-14 | Cryogenic Technology Inc | Temperature-controlled spindle for centrifuges and similar apparatus |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3073517A (en) * | 1959-04-07 | 1963-01-15 | Beckman Instruments Inc | Continuous flow centrifuge apparatus and rotor therefor |
| US3600900A (en) * | 1969-11-03 | 1971-08-24 | North American Rockwell | Temperature controlled centrifuge |
| CH586233A5 (en) * | 1971-01-18 | 1977-03-31 | Pentapharm Ag | |
| US3706412A (en) * | 1971-07-28 | 1972-12-19 | Haemonetics Corp | Pressure-actuated centrifuge chuck and centrifuge incorporating the same |
| US3856470A (en) * | 1973-01-10 | 1974-12-24 | Baxter Laboratories Inc | Rotor apparatus |
| CH626917A5 (en) * | 1976-08-17 | 1981-12-15 | Pentapharm Ag | |
| US4300717A (en) * | 1979-04-02 | 1981-11-17 | Haemonetics Corporation | Rotary centrifuge seal |
| US4442655A (en) * | 1981-06-25 | 1984-04-17 | Serapharm Michael Stroetmann | Fibrinogen-containing dry preparation, manufacture and use thereof |
| US5223420A (en) * | 1985-03-01 | 1993-06-29 | Institut National De La Sante Et De La Recherche Medicale | Elastin-based product, a procedure for its preparation and its biological applications; in particular as biomaterials and artificial supports |
| US5260420A (en) * | 1987-07-30 | 1993-11-09 | Centre Regional De Transfusion Sanguine De Lille | Concentrate of thrombin coagulable proteins, the method of obtaining same and therapeutical use thereof |
| FR2619619B1 (en) * | 1987-08-18 | 1990-01-12 | Jouan | SENSOR FOR MEASURING THE INTERNAL TEMPERATURE OF A REFRIGERATED OR THERMOSTAT CENTRIFUGAL TANK |
| US5100372A (en) * | 1990-03-02 | 1992-03-31 | Haemonetics Corporation | Core for blood processing apparatus |
| US5395923A (en) * | 1993-02-23 | 1995-03-07 | Haemacure-Biotech, Inc. | Process for the obtention of a biological adhesive made of concentrated coagulation factors by "salting-out" |
| US5389335A (en) * | 1993-06-18 | 1995-02-14 | Charm Sciences, Inc. | High temperature, short time microwave heating system and method of heating heat-sensitive material |
| ZA948564B (en) * | 1993-11-19 | 1995-07-26 | Bristol Myers Squibb Co | Liquid separation apparatus and method |
-
1998
- 1998-01-08 WO PCT/US1998/000251 patent/WO1998030304A1/en not_active Ceased
- 1998-01-08 IL IL13072898A patent/IL130728A/en not_active IP Right Cessation
- 1998-01-08 CA CA002277858A patent/CA2277858A1/en not_active Abandoned
- 1998-01-08 NZ NZ336398A patent/NZ336398A/en unknown
- 1998-01-08 BR BR9806736-2A patent/BR9806736A/en not_active IP Right Cessation
- 1998-01-08 JP JP53105898A patent/JP2001508447A/en not_active Ceased
- 1998-01-08 AU AU58169/98A patent/AU741088B2/en not_active Ceased
- 1998-01-08 EP EP98901714A patent/EP0975429A1/en not_active Withdrawn
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3604769A (en) * | 1968-09-23 | 1971-09-14 | Cryogenic Technology Inc | Temperature-controlled spindle for centrifuges and similar apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2277858A1 (en) | 1998-07-16 |
| IL130728A (en) | 2002-11-10 |
| BR9806736A (en) | 2000-02-29 |
| AU5816998A (en) | 1998-08-03 |
| WO1998030304A1 (en) | 1998-07-16 |
| NZ336398A (en) | 2000-12-22 |
| IL130728A0 (en) | 2000-06-01 |
| EP0975429A4 (en) | 2000-02-02 |
| JP2001508447A (en) | 2001-06-26 |
| EP0975429A1 (en) | 2000-02-02 |
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| Date | Code | Title | Description |
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| FGA | Letters patent sealed or granted (standard patent) |