AU765827B2 - A method for monitoring/controlling the temperature of a liquid and for producing fibrin - Google Patents

A method for monitoring/controlling the temperature of a liquid and for producing fibrin Download PDF

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Publication number
AU765827B2
AU765827B2 AU15596/02A AU1559602A AU765827B2 AU 765827 B2 AU765827 B2 AU 765827B2 AU 15596/02 A AU15596/02 A AU 15596/02A AU 1559602 A AU1559602 A AU 1559602A AU 765827 B2 AU765827 B2 AU 765827B2
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Prior art keywords
container
temperature
blood
plasma
fibrin
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AU15596/02A
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AU1559602A (en
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Niels Erik Holm
Niels Hvid
Glenn A. Jorgensen
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VIVOLUTION AS
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Bristol Myers Squibb Co
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Priority claimed from AU58169/98A external-priority patent/AU741088B2/en
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Description

AUSTRALIA
Patents Act COMPLETE SPECIFICATION
(ORIGINAL)
Class Int. Class Application Number: Lodged: Complete Specification Lodged: Accepted: Published: Priority Related Art: Name of Applicant: Bristol-Myers Squibb Company Actual Inventor(s): Niels Hvid, Glenn A Jorgensen, Niels Erik Holm Address for Service: PHILLIPS ORMONDE FITZPATRICK Patent and Trade Mark Attorneys 367 Collins Street Melbourne 3000 AUSTRALIA Invention Title: A METHOD FOR MONITORING/CONTROLLING THE TEMPERATURE OF A LIQUID AND FOR PRODUCING FIBRIN Our Ref: 662565 POF Code: 232049/232049 The following statement is a full description of this invention, including the best method of performing it known to applicant(s): -1- 6006q 1A A -Method for Monitoring/Controlling the Temperature of a Liquid and for Producing Fibrin The present application is a divisional application of Australian patent application 58169/98 (the "Patent Application"), the entire contents of which are herein incorporated by reference.
Technical Field The invention relates to methods for converting fibrinogen to fibrin and monitoring/controlling the temperature of a liquid, eg, blood, within a rotating centrifuge container.
Background Art S" 15 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 o* 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 20 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 o••oo fraction and a plasma fraction followed by the resulting plasma fraction 25 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 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 10 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 rotaled 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 anO 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 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.
The discussion of the background to the invention herein is included to explain the context of the invention. This is not to be taken as an admission that any of the material referred to was published, known or part of the common general knowledge in Australia as at the priority date of any of the claims.
Summary of the Invention It has now been found that processes for producing and utilising fibrin monomer are enhanced when the blood or plasma is heated to about 37°C during the processing cycle.
Accordingly, in one aspect the present invention provides a method for converting fibrinogen to fibrin which comprises: a) heating a sample of blood or plasma to about 370°C; and b) subjecting said sample to an enzyme which catalyses the cleavage of fibrinopeptides A and/or B from fibrinogen in said blood or plasma.
The method can be used to prepare fibrin monomer solutions and compositions from blood or plasma wherein the blood or plasma is heated to about 37°C prior to and during processing with the thrombin or thrombin-like enzyme.
In preferred embodiments, the method step is carried out under centrifugation.
In a further preferred embodiment, the blood is centrifugally separated into a blood cell fraction and a plasma fraction prior to step W:\KATHRYN\Misc\Temp. 17.01.02.doc The blood may be heated at low rotational speeds, eg, 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. Thus, in another embodiment the present invention is directed to a method of indirectly determining the temperature of a blood sample in a container which comprises: a) measuring the temperature of the outside surface of the container; b) measuring the temperature of the air surrounding the container; and c) utilising the formula Tblood ATair BTsurface where Tblood is the temperature of the blood; Tsuface is the temperature of the outside surface of the container; Tair is the temperature of the air surrounding the container; A is a heat transfer coefficient for the surrounding air; B is a heat transfer coefficient for the surface of the container; to solve for the temperature of the blood.
Further, this method of determination can be fed into a control unit which controls a heat source. Thus, in another embodiment the present invention is directed to a method of controlling the temperature of blood in a container which comprises utilising an apparatus comprising a container with blood therein, a W:\KATHRYN\Misc\Temp. 17.01.02.doc heat source and a control unit for said heat source which control unit is responsive to an indirect determination as stated above.
Brief Description of the Drawing The invention is explained in greater detail below with reference to the accompanying drawing, in which FIG.1 is a diagrammatic front view of parts of the apparatus used in the invention and with a container arranged therein for the separation of components of a liquid.
.*e .e *i Detailed Description of Preferred Embodiments An enhanced centrifuge system with capabilities of monitoring and controlling the temperature of a liquid, eg, blood, during centrifugation is provided. It has been found that subjecting plasma fibrinogen to an enzyme which catalyses the cleavage of fibrinopeptides A and/or B from fibrinogen, ie, a thrombin or thrombin-like enzyme which converts fibrinogen to fibrin, proceeds more efficiently when the blood or plasma is at about 370C. Careful temperature control is important since temperatures too low will not provide the enhanced effect and temperatures exceeding 400C can damage the blood component and cells.
o• It is particularly advantageous that the heat-emitting 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 .i 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 utilisation of the 2. 20 energy release from the heat-emitting device through the wall to the blood is thus optimal.
°oO** S"Furthermore, the heat-emitting device may 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 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.
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 W:\KATHRYN\Misc\Tenp 1.17.01.02.doc detected temperatures. Thus it is ensured in a particularly simple manner that the desired temperatures are maintained.
Furthermore, the control unit may 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.
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 rotat- S. ing movement about a vertical axis of rotation. An activating bar 6 is S°o 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 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 i 2 projecting upwardly from the upper end of the container The piston rod 12 is activated by means of a gripping means 13, which in 10 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. "Phe o:oo 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 Sdisplaced 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 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 3II oI Liandhse sensors 31, 32 can be, infrared 10 sensors. In addition, a sensor 35 is provided for measuring the oo temperature of the air around the container 10. The latter temperature o 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 ATai BTsurtace where Tblood is the temperature of the blood, T,,ace is the temperature on the surface of the container wall 37, and Ta, 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 Tbood Tait and Tsurface. Tblood 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 oo" 15 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 o• o. ~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 20 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 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.
o a 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.
10 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 cbhtainer 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 15 mentioned, measured by means of the temperature sensor 32.
o o.
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 o- separated component is transferred from this position to the area below 20 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 the specification the word "comprise" and variations of the word, such as "comprising" and "comprises", is not o intended to exclude other additives, components, integers or steps.
a W:\KATHRYN\Misc\Temp. 17.01.02.doc

Claims (4)

1. A method for converting fibrinogen to fibrin which comprises a) heating a sample of blood or plasma to about 370 C; and subjecting said sample to an enzyme which catalyzes the cleavage of fibrinopeptides A and/or B from fibrinogen in said blood or plasma.
2. The method of claim 1 wherein said method step is carried out under centrifugation.
3. The method of claims 1 or 2 wherein blood is centrifugally separated into a blood cell fraction and a plasma fraction prior to step
4. A method of indirectly determining the temperature of a blood sample ina container which comprises a) measuring the temperature of the outside surface of the container; b) measuring the temperature of the air surrounding the container; and c) utilising the formula Tblood ATair BTsurice 20 where Tblood is the temperature of the blood; Tsurace is the temperature of the outside surface of the container; Tair is the temperature of the air surrounding the container; A is a heat transfer coefficient for the surrounding air; B is a heat transfer coefficient for the surface of the container; to solve for the temperature of the blood. A method of controlling the temperature of blood in a container which comprises utilizing an apparatus comprising a container with blood ;therein, a heat source and a control unit for said heat source which contr-ol unit is responsive to an indirect determination as in claim 4. 30 DATED: 6 August 2003 PHILLIPS ORMONDE FITZPATRICK Attorneys for: Bristol-Myers Squibb Company
AU15596/02A 1997-01-08 2002-02-13 A method for monitoring/controlling the temperature of a liquid and for producing fibrin Ceased AU765827B2 (en)

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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
US60/034056 1997-01-08
AU58169/98A AU741088B2 (en) 1997-01-08 1998-01-08 A centrifuge apparatus with temperature control means
AU15596/02A AU765827B2 (en) 1997-01-08 2002-02-13 A method for monitoring/controlling the temperature of a liquid and for producing fibrin

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5733446A (en) * 1994-12-02 1998-03-31 Bristol-Myers Squibb Company Centrifuge with annular filter
US5750658A (en) * 1993-01-19 1998-05-12 Thermogenesis Corp. Fibrinogen processing apparatus, method and container

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5750658A (en) * 1993-01-19 1998-05-12 Thermogenesis Corp. Fibrinogen processing apparatus, method and container
US5733446A (en) * 1994-12-02 1998-03-31 Bristol-Myers Squibb Company Centrifuge with annular filter

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