EP0213589B1 - Generator of technecium-99m, its preparation and use - Google Patents
Generator of technecium-99m, its preparation and use Download PDFInfo
- Publication number
- EP0213589B1 EP0213589B1 EP86111788A EP86111788A EP0213589B1 EP 0213589 B1 EP0213589 B1 EP 0213589B1 EP 86111788 A EP86111788 A EP 86111788A EP 86111788 A EP86111788 A EP 86111788A EP 0213589 B1 EP0213589 B1 EP 0213589B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- generator
- copper
- silica gel
- aluminum oxide
- technetium
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21G—CONVERSION OF CHEMICAL ELEMENTS; RADIOACTIVE SOURCES
- G21G4/00—Radioactive sources
Definitions
- the invention relates to an improved technetium-99m generator based on carrier-adsorbed molybdenum-99, processes for producing such generators and their use for obtaining eluates which contain technetium-99m in the form of pertechnetate.
- Technetium-99m is the most commonly used radioactive nuclide in nuclear medicine diagnostics. This is due to its core physical properties that are optimal for this application (short half-life of 6.0 hours, no corpuscular radiation, favorable ⁇ energy of 140 keV). It can be easily and easily obtained from a molybdenum 99 / technetium 99m generator.
- the molybdenum-99 from which the isotope technetium-99m is continuously formed by core decay, is adsorbed onto an aluminum oxide column as molybdenum-99-molybdate.
- Technetium-99m which is chemically pertechnetate, is separated from Molydbän-99 by washing with isotonic saline.
- the so-called split molybdenum-99 is used almost exclusively as molybdenum-99. It is isolated from the fission product mixture that occurs during the core decay of uranium-235 and has a very high specific activity. This makes it possible to get high technetium-99m activity in small volumes of saline from a generator.
- split molybdenum made it possible to use only small amounts (1-2 g) of aluminum oxide in the generators, whereby the minimum amount of saline solution required for the elution of the technetium-99m could be limited to a few milliliters (approx. 5 ml).
- German Offenlegungsschrift 1 929 067 describes adding copper (II) acetate to the eluent.
- this is not sufficient - even when using the minimum copper (II) concentrations mentioned - to prevent the aforementioned passage of copper into the eluate.
- silica gels modified with amino groups and, if appropriate, magnesium silicates are advantageous carrier materials for technetium-99m generators which are capable of firmly binding copper (II) ions.
- the invention thus relates to technetium-99m generators based on carrier-adsorbed molybdenum-99, which are characterized by a content of an amino group-modified silica gel and, if appropriate, magnesium silicates.
- the amino group-modified silica gel is able to adsorb radioactive molybdenum-99. This means that the Mo-99 content in the eluate can be reduced to less than 1 ⁇ Ci Mo-99 / Ci Tc-99m.
- a technetium-99m generator the carrier material of which consists of silica group modified with amino groups.
- preferred embodiments of this invention additionally contain aluminum oxide and, if appropriate, magnesium silicates.
- Generators according to the invention with a content of magnesium silicate expediently contain, in addition to the silica group-modified silica gel according to the invention, additionally aluminum oxide for the adsorption of Mo-99.
- For generators that contain more than one carrier material it is fundamentally possible to mix the carrier materials and to fill the usual equipment with the mixture. However, since the different materials generally have a different grain size, special precautions, for example joint grinding, must be used to ensure that no "channels" remain open in the filling. It is therefore generally more convenient to fill the different materials in layers in the generators. "Layer by layer” can mean that the different materials are introduced in several, alternating layers, but it is advisable to introduce each material in the form of a single layer.
- the amino group-modified silica gel is preferably introduced as the bottom layer in the generator column. A layer of aluminum oxide is then applied over this.
- FIG. 1 and 2 show schematically and not necessarily to scale two embodiments of the invention:
- (1) means the column into which the carrier material is filled, the direction of elution (from top to bottom) being indicated by the arrow.
- (2) and (3) mean the layers of different carrier materials, in a preferred embodiment aluminum oxide as layer (2) and amino group-modified silica gel as layer (3).
- FIG. 2 designates a corresponding arrangement with three layers, three different materials (2), (3) and (4) being used.
- (4) means a layer of copper (II) -loaded aluminum oxide, (2) aluminum oxide and (3) amino group-modified silica gel and optionally magnesium silicates.
- nuclide generators The technical design of nuclide generators is known and is described, for example, in German Patent Specification 1,614,486 (or the corresponding US Pat. No. 3,369,121) or GB Pat. No. 1,186,587. Details can therefore be dispensed with here.
- the amount of carrier material depends on the dimensioning of the generator and the load; it can be easily determined by simple preliminary tests.
- Amino group-modified silica gels are customary as support materials for chromatographic processes.
- a preferred form contains the amino groups in the form of 1,3-propylamine groups.
- carrier materials for example those with secondary or tertiary amino groups, such as those used as adsorbents for acidic compounds, are also possible.
- Suitable as magnesium silicate are naturally occurring products such as forsterite, entstatite, serpentine, serpentine asbestos, talc, antigorite or meerschaum as well as corresponding synthetic products, the magnesium ortho-, di- or polysilicates, the latter with chain, ribbon or layer (sheet) ) Structure included. Such materials are used for example for chromatographic processes.
- one glass column was filled with 1.2 g of aluminum oxide and another with 105 mg of silica gel and 1.0 g of aluminum oxide.
- These comparative generators were eluted with copper-free eluent contaminated with organic contaminants.
- the results are summarized in Table 2.
- the yield of Tc-99m is given in%, based on the Mo-99 activity, the molybdenum-99 content in ppm, based on the Tc-99m activity and the copper (II) content in ppm.
- Table 3 shows the reduction of the Mo-99 content in the eluate even when using the design according to EP-B 0 014 957. Cu (II) could not be found in any eluate.
Landscapes
- High Energy & Nuclear Physics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Medicinal Preparation (AREA)
- Steroid Compounds (AREA)
- Cosmetics (AREA)
Abstract
Description
Die Erfindung betrifft einen verbesserten Technetium-99m-Generator auf Basis von trägeradsorbiertem Molybdän-99, Verfahren zur Herstellung solcher Generatoren und ihre Verwendung zu Gewinnung von Eluaten, die Technetium-99m in Form von Pertechnetat enthalten.The invention relates to an improved technetium-99m generator based on carrier-adsorbed molybdenum-99, processes for producing such generators and their use for obtaining eluates which contain technetium-99m in the form of pertechnetate.
Technetium-99m ist das am häufigsten benutzte radioaktive Nuklid in der nuklearmedizinischen Diagnostik. Dies beruht auf seinen für diese Anwendung optimalen kernphysikalischen Eigenschften (kurze Halbwertszeit von 6,0 Stunden, keine Korpuskularstrahlung, günstige γ-Energie von 140 keV). Es kann aus einem Molybdän-99/Technetium-99m-Generator leicht und einfach gewonnen werden.Technetium-99m is the most commonly used radioactive nuclide in nuclear medicine diagnostics. This is due to its core physical properties that are optimal for this application (short half-life of 6.0 hours, no corpuscular radiation, favorable γ energy of 140 keV). It can be easily and easily obtained from a molybdenum 99 / technetium 99m generator.
Bei dem zur Zeit verbreitetsten Generatortyp wird das Molybdän-99, aus dem das Isotop Technetium-99m durch Kernzerfall ständig gebildet wird, als Molybdän-99-molybdat an eine Aluminiumoxidsäule adsorbiert. Das Technetium-99m, das chemisch als Pertechnetat vorliegt, wird durch Waschen mit isotonischer Kochsalzlösung vom Molydbän-99 abgetrennt. Als Molybdän-99 wird heute fast ausschließlich das sogenannte Spaltmolybdän-99 verwendet. Es wird aus der beim Kernzerfall von Uran-235 anfallenden Spaltproduktmischung isoliert und besitzt eine sehr hohe spezifische Aktivität. Durch wird es möglich, hohe Aktivitäten an Technetium-99m in kleinen Volumina Kochsalzlösung aus einem Generator zu erhalten.In the currently most widespread generator type, the molybdenum-99, from which the isotope technetium-99m is continuously formed by core decay, is adsorbed onto an aluminum oxide column as molybdenum-99-molybdate. Technetium-99m, which is chemically pertechnetate, is separated from Molydbän-99 by washing with isotonic saline. The so-called split molybdenum-99 is used almost exclusively as molybdenum-99. It is isolated from the fission product mixture that occurs during the core decay of uranium-235 and has a very high specific activity. This makes it possible to get high technetium-99m activity in small volumes of saline from a generator.
Die Einführung des Spaltmolybdäns erlaubte es, in den Generatoren nur noch geringe Mengen (1-2 g) Aluminiumoxid einzusetzen, wodurch die zur Elution des Technetium-99m notwendige minimale Menge Kochsalzlösung auf wenige Milliliter (ca. 5 ml) begrenzt werden konnte.The introduction of split molybdenum made it possible to use only small amounts (1-2 g) of aluminum oxide in the generators, whereby the minimum amount of saline solution required for the elution of the technetium-99m could be limited to a few milliliters (approx. 5 ml).
Die an einen gebrauchsfertigen Generator zu stellenden Mindestanforderungen sind in der DIN 6854 (Januar 1985) zusammengefaßt. Danach sollte die eluierbare Aktivität an Tc-99m bei einer Elution in 24 Stunden-Intervallen 70 % nicht unterschreiten. Die Qualität des Eluates unterliegt dabei bestimmten Anforderungen. Es ist natürlich wünschenswert, diese Grenzwerte so weit wie möglich zu unterschreiten. Dies gilt besonders für Molybdän-99, das in hohen Aktivitäten im Generator enthalten ist und im Eluat auf Grund der langen Halbwertszeit von 66,0 h zu einer unnötigen Strahlenbelastung bei der Anwendung am Menschen führen würde.The minimum requirements for a ready-to-use generator are summarized in DIN 6854 (January 1985). Thereafter, the elutable activity on Tc-99m should not be less than 70% when eluted at 24 hour intervals. The quality of the eluate is subject to certain requirements. It is of course desirable to fall below these limits as much as possible. This applies in particular to molybdenum-99, which is contained in the generator in high activities and which in the eluate would lead to unnecessary radiation exposure when used in humans due to the long half-life of 66.0 h.
Es ist bekannt, daß Mo-99/Tc-99m-Generatoren mit Spaltmolybdän, insbesondere bei höheren Mo-99-Aktivitäten, zu Ausbeuteverlusten oder manchmal sogar zu Ausbeutezusammenbrüchen neigen (EP-B 0 014 957). Dieser Effekt wird durch organische Verunreinigungen im Elutionsmittel, die z.B. aus Kunststoffelutionsmittelbehältern in die Kochsalzlösung gelangen können, noch verstärkt.It is known that Mo-99 / Tc-99m generators with split molybdenum, in particular in the case of higher Mo-99 activities, tend to lose yields or sometimes even breakdowns (EP-B 0 014 957). This effect is caused by organic impurities in the eluent, e.g. can get into the saline solution from plastic eluent containers.
Um diese Ausbeuteverluste zu vermeiden, werden Ausbeutestabilisatoren eingesetzt. Es ist bekannt, daß Kupfer(II)-Ionen diese stabilisierende Wirkung haben.In order to avoid these losses in yield, yield stabilizers are used. It is known that copper (II) ions have this stabilizing effect.
Hierbei tritt jedoch die Schwierigkeit auf, daß die geringen Mengen an Aluminiumoxid nicht ausreichen, den Durchtritt des Kupfers in das Eluat auf Dauer zu verhindern.Here, however, there arises the difficulty that the small amounts of aluminum oxide are not sufficient to prevent the passage of the copper into the eluate in the long term.
In der deutschen Offenlegungsschrift 1 929 067 wird beschrieben, dem Elutionsmittel Kupfer(II)-acetat zuzusetzen. Als minimale Menge werden 0,001 Volumenprozent gefordert, worunter wohl im Falle von Kupfer(II)-acetat 10 µg/ml = 3,5 µg Cu(II)/ml zu verstehen sind. Für moderne Generatoren, die im Gegensatz zu denen, die am Prioritätstag der genannten deutschen Offenlegungsschrift üblich waren, nur eine geringe Menge an Aluminiumoxid enthalten, reicht diese - selbst bei Einsatz der genannten minimalen Kupfer(II)-Konzentrationen - nicht aus, den erwähnten Durchtritt des Kupfers in das Eluat zu verhindern. Darüber hinaus hat sich gezeigt, daß 3,5 µg Cu(II)/ml Elutionsmittel nicht immer eine stabil hohe Ausbeute gewährleisten können.German Offenlegungsschrift 1 929 067 describes adding copper (II) acetate to the eluent. A minimum amount of 0.001 percent by volume is required, which in the case of copper (II) acetate means 10 µg / ml = 3.5 µg Cu (II) / ml. For modern generators, unlike those on the priority day of the aforementioned German published application, which only contain a small amount of aluminum oxide, this is not sufficient - even when using the minimum copper (II) concentrations mentioned - to prevent the aforementioned passage of copper into the eluate. In addition, it has been shown that 3.5 µg Cu (II) / ml eluent cannot always ensure a stable, high yield.
Zur Verhinderung des Durchtritts von Kupferionen in das Eluat wurde in der EP-B -0 014 957 ein Verfahren beschrieben, das die Fixierung von größeren Mengen Kupfer(II) auf dem Aluminiumoxid erlaubt. Diese Methode erfordert jedoch einen zusätzlichen Verfahrenschritt bei der Herstellung der Generatoren und ist somit aufwendig.In order to prevent the passage of copper ions into the eluate, a process was described in EP-B-0 014 957 which allows large amounts of copper (II) to be fixed on the aluminum oxide. However, this method requires an additional process step in the production of the generators and is therefore complex.
Es wurde nun gefunden, daß mit Aminogruppen modifizierte Kieselgele und gegebenenfalls Magnesiumsilikate vorteilhafte Trägermaterialien für Technetium-99m-Generatoren darstellen, die Kupfer(II)-ionen fest zu binden vermögen. Die Erfindung betrifft somit Technetium-99m-Generatoren auf Basis von trägeradsorbiertem Molybdän-99, die durch einen Gehalt an einem aminogruppenmodifizierten Kieselgel und gegebenenfalls Magnesiumsilikaten gekennzeichnet sind.It has now been found that silica gels modified with amino groups and, if appropriate, magnesium silicates are advantageous carrier materials for technetium-99m generators which are capable of firmly binding copper (II) ions. The invention thus relates to technetium-99m generators based on carrier-adsorbed molybdenum-99, which are characterized by a content of an amino group-modified silica gel and, if appropriate, magnesium silicates.
Es wurde weiterhin gefunden, daß das aminogruppenmodifizierte Kieselgel in der Lage ist, radioaktives Molybdän-99 zu adsorbieren. Damit können die Mo-99-Gehalte im Eluat auf weniger als 1 µCi Mo-99/Ci Tc-99m gesenkt werden. Eine Ausgestaltung der Erfindung betrifft somit einen Technetium-99m-Generator, dessen Trägermaterial aus aminogruppenmodifiziertem Kieselgel besteht. Bevorzugte Ausgestaltungen dieser Erfindung enthalten jedoch zusätzlich Aluminiumoxid und gegebenenfalls Magnesiumsilikate.It was also found that the amino group-modified silica gel is able to adsorb radioactive molybdenum-99. This means that the Mo-99 content in the eluate can be reduced to less than 1 µCi Mo-99 / Ci Tc-99m. One embodiment of the invention thus relates to a technetium-99m generator, the carrier material of which consists of silica group modified with amino groups. However, preferred embodiments of this invention additionally contain aluminum oxide and, if appropriate, magnesium silicates.
Erfindungsgemäße Generatoren mit einem Gehalt an Magnesiumsilikat enthalten neben dem erfindungsgemäßen aminogruppenmodifizierten Kieselgel zweckmäßig zusätzlich Aluminiumoxid zur Adsorption des Mo-99. Für solche Generatoren, die mehr als ein Trägermaterial enthalten, ist es grundsätzlich möglich, die Trägermaterialien zu mischen und mit der Mischung die üblichen Apparaturen zu füllen. Da jedoch die unterschiedlichen Materialien im allgemeinen eine unterschiedliche Korngröße aufweisen, muß durch besondere Vorkehrungen, beispielweise gemeinsames Vermahlen, darauf geachtet werden, daß in der Füllung keine "Kanäle" offenbleiben. Es ist deshalb im allgemeinen zweckmäßiger, die unterschiedlichen Materialien schichtweise in die Generatoren einzufüllen. "Schichtweise" kann hierbei bedeuten, daß die unterschiedlichen Materialien in mehreren, abwechselnd aufeinander folgenden Schichten eingebracht werden, zweckmäßig ist jedoch, jedes Material in Form einer einzigen Schicht einzubringen.Generators according to the invention with a content of magnesium silicate expediently contain, in addition to the silica group-modified silica gel according to the invention, additionally aluminum oxide for the adsorption of Mo-99. For generators that contain more than one carrier material, it is fundamentally possible to mix the carrier materials and to fill the usual equipment with the mixture. However, since the different materials generally have a different grain size, special precautions, for example joint grinding, must be used to ensure that no "channels" remain open in the filling. It is therefore generally more convenient to fill the different materials in layers in the generators. "Layer by layer" can mean that the different materials are introduced in several, alternating layers, but it is advisable to introduce each material in the form of a single layer.
Vorzugsweise wird das aminogruppenmodifizierte Kieselgel als unterste Schicht in die Generatorsäule eingebracht. Darüber wird dann eine Schicht aus Aluminiumoxid aufgetragen.The amino group-modified silica gel is preferably introduced as the bottom layer in the generator column. A layer of aluminum oxide is then applied over this.
Es kann auch von der in der EP-B 0 014 957 beschriebenen Erfindung Gebrauch gemacht werden, indem man einen Generator herstellt, bei dem in der obersten Schicht das Kupfer(II)-beladene Aluminiumoxid eingebracht ist, darunter eine Schicht von Aluminiumoxid und hierunter eine Schicht des erfindungsgemäßen Trägermaterials folgt.Use can also be made of the invention described in EP-B 0 014 957 by producing a generator in which the copper (II)-laden aluminum oxide is introduced in the top layer, including a layer of aluminum oxide and one below Layer of the carrier material according to the invention follows.
In den Figuren 1 und 2 sind schematisch und nicht notwendigerweise maßstabsgerecht zwei Ausgestaltungen der Erfindung dargestellt:
In Figur 1 bedeutet (1) die Säule, in welche das Trägermaterial eingefüllt wird, wobei durch den Pfeil die Elutionsrichtung (von oben nach unten) angedeutet ist. (2) und (3) bedeuten die Schichten unterschiedlicher Trägermaterialien, in einer bevorzugten Ausgestaltung also Aluminiumoxid als Schicht (2) und aminogruppenmodifiziertes Kieselgel als Schicht (3).1 and 2 show schematically and not necessarily to scale two embodiments of the invention:
In FIG. 1, (1) means the column into which the carrier material is filled, the direction of elution (from top to bottom) being indicated by the arrow. (2) and (3) mean the layers of different carrier materials, in a preferred embodiment aluminum oxide as layer (2) and amino group-modified silica gel as layer (3).
Die Figur 2 bezeichnet eine entsprechende Anordnung mit drei Schichten, wobei drei unterschiedliche Materialien (2), (3) und (4) Verwendung finden. In einer bevorzugten Ausgestaltung dieses Aspektes der Erfindung bedeutet (4) eine Schicht aus Kupfer(II)-beladenem Aluminiumoxid, (2) Aluminiumoxid und (3) aminogruppenmodifiziertes Kieselgel und gegebenenfalls Magnesiumsilikate.FIG. 2 designates a corresponding arrangement with three layers, three different materials (2), (3) and (4) being used. In a preferred embodiment of this aspect of the invention, (4) means a layer of copper (II) -loaded aluminum oxide, (2) aluminum oxide and (3) amino group-modified silica gel and optionally magnesium silicates.
Die technische Ausgestaltung von Nuklidgeneratoren ist bekannt und beispielsweise in der deutschen Auslegeschrift 1 614 486 (bzw. der entsprechenden US-PS 3 369 121) oder der GB-PS 1 186 587 beschrieben. Es kann deshalb hier auf Details verzichtet werden.The technical design of nuclide generators is known and is described, for example, in German Patent Specification 1,614,486 (or the corresponding US Pat. No. 3,369,121) or GB Pat. No. 1,186,587. Details can therefore be dispensed with here.
Die Menge des Trägermaterials richtet sich nach der Dimensionierung des Generators und der Beladung; sie ist durch einfache Vorversuche leicht zu ermitteln.The amount of carrier material depends on the dimensioning of the generator and the load; it can be easily determined by simple preliminary tests.
Aminogruppenmodifizierte Kieselgele sind als Trägermaterialien für chromatographische Prozesse üblich. Eine bevorzugte Form enthält die Aminogruppen in Form von 1,3-Propylamingruppen. Es sind jedoch auch andere Trägermaterialien, beispielsweise solche mit sekundären oder tertiären Aminogruppen, wie sie als Adsorbentien für saure Verbindungen dienen, möglich.Amino group-modified silica gels are customary as support materials for chromatographic processes. A preferred form contains the amino groups in the form of 1,3-propylamine groups. However, other carrier materials, for example those with secondary or tertiary amino groups, such as those used as adsorbents for acidic compounds, are also possible.
Als Magnesiumsilikat eignen sich natürlich vorkommende Produkte wie Forsterit, Enstatit, Serpentin, Serpentinasbest, Talk, Antigorit oder Meerschaum sowie entsprechende synthetische Produkte, die Magnesiumortho-, -di-oder -polysilikate, letztere mit Ketten-, Band- oder Schicht- (Blatt-)-Struktur enthalten. Solche Materialien werden beispielsweise für chromatographische Verfahren eingesetzt.Suitable as magnesium silicate are naturally occurring products such as forsterite, entstatite, serpentine, serpentine asbestos, talc, antigorite or meerschaum as well as corresponding synthetic products, the magnesium ortho-, di- or polysilicates, the latter with chain, ribbon or layer (sheet) ) Structure included. Such materials are used for example for chromatographic processes.
In den folgenden Beispielen wird die Erfindung näher erläutert.The invention is explained in more detail in the following examples.
Für die Herstellung von Generatorsäulen wurden folgende Trägermaterialien verwendet: Aluminiumoxid S, sauer, superaktiv; Fa. Riedel de Haen; (R)LiChroprep NH₂ für die Flüssigkeitschromatographie, Fa. Merck, im folgenden "Kieselgel". Als Elutionsmittel wurde physiologische Kochsalzlösung verwendet, die unterschiedliche Mengen an Kupfer(II)-chlorid, Dihydrat enthielt. Die Kupfer(II)-Bestimmung erfolgte kolorimetrisch, wobei die untere Nachweisgrenze 0,1 ppm betrug.The following carrier materials were used for the production of generator columns: aluminum oxide S, acidic, superactive; Riedel de Haen; (R) LiChroprep NH₂ for liquid chromatography, Merck, hereinafter "silica gel". Physiological saline containing different amounts of copper (II) chloride and dihydrate was used as the eluent. The copper (II) determination was carried out colorimetrically, the lower detection limit being 0.1 ppm.
Durch Elution unter gleichen Bedingungen wurde festgestellt, in welchem Maße die Trägermaterialien befähigt sind. Kupfer(II)-Ionen festzuhalten. Die Eluate Nr. 1-8 waren in allen Fällen kupferfrei. Wie die folgende Tabelle 1 zeigt, kann das Kieselgel Kupfer(II) sehr viel besser abfangen als das Aluminiumoxid.
In eine Glassäule werden 105 mg Kieselgel gepackt und darüber 1,0 g Aluminiumoxid geschichtet. Die Säule wird mit Mo-99 beladen und arbeitstäglich mit physiologischer Kochsalzlösung eluiert, die 20 µg CuCl₂ 2R₂0 pro ml enthält. Vor Zugabe des Kupfer(II)-chlorids wurde die Kochsalzlösung zusammen mit der üblicherweise zur Verpackung dienenden PVC-Folie im Autoklav sterilisiert. Es ist bekannt, daß dabei organische Verunreinigungen in das Elutionsmittel gelangen, die zu starken Ausbeuteverminderungen führen können.105 mg of silica gel are packed in a glass column and 1.0 g of aluminum oxide are layered on top. The column is loaded with Mo-99 and eluted daily with physiological saline containing 20 µg CuCl₂ 2R₂0 per ml. Before the addition of the copper (II) chloride, the saline solution was sterilized together with the PVC film that is usually used for packaging in an autoclave. It is known that organic impurities get into the eluent, which can lead to severe reductions in yield.
Zum Vergleich wurde eine Glassäule mit 1,2 g Aluminiumoxid und eine weitere mit 105 mg Kieselgel und 1,0 g Aluminiumoxid gefüllt. Diese Vergleichsgeneratoren eluierte man mit kupferfreiem, mit organischen Verunreinigungen belastetem Elutionsmittel.For comparison, one glass column was filled with 1.2 g of aluminum oxide and another with 105 mg of silica gel and 1.0 g of aluminum oxide. These comparative generators were eluted with copper-free eluent contaminated with organic contaminants.
In den Eluaten wird der Gehalt an Technetium-99m, Molybdän-99 und soweit das Elutionsmittel Kupfer(II) enthält, der Anteil an Kupfer(II) gemessen. In der Tabelle 2 sind die Ergebnisse zusammengefaßt. Die Ausbeute an Tc-99m ist in %, bezogen auf die Mo-99-Aktivität, der Molybdän-99-Gehalt in ppm, bezogen auf die Tc-99m-Aktivität und der Kupfer(II)-Gehalt in ppm angegeben.The content of technetium-99m, molybdenum-99 and, to the extent that the eluent contains copper (II), the proportion of copper (II) is measured in the eluates. The results are summarized in Table 2. The yield of Tc-99m is given in%, based on the Mo-99 activity, the molybdenum-99 content in ppm, based on the Tc-99m activity and the copper (II) content in ppm.
- 1. Durch Einsatz von Kieselgel wird der Mo-99-Gehalt im Eluat unter 1 ppm gesenkt.1. The use of silica gel lowers the Mo-99 content in the eluate below 1 ppm.
- 2. Durch Einsatz von Kieselgel kann dem Elutionsmittel Kupfer(II) zugesetzt werden, wodurch die Ausbeute an Tc-99m gleichmäßig hoch bleibt, ohne daß Kupfer(II) in nennenswerten Mengen im Eluat nachgewiesen werden kann.2. By using silica gel, copper (II) can be added to the eluent, as a result of which the yield of Tc-99m remains uniformly high without any significant amounts of copper (II) being detectable in the eluate.
- 3. Durch Einsatz von Kieselgel kann der Kupfer(II)-Gehalt im Elutionsmittel über den minimalen Anteil von 20 ppm hinaus gesteigert werden.3. By using silica gel, the copper (II) content in the eluent can be increased beyond the minimum proportion of 20 ppm.
Es wurden Generatorsäulen nach dem Verfahren der EP-B 0 014 957 hergestellt. Einige enthielten jedoch als unterste Schicht zusätzlich Kieselgel. Diese wurden mit Mo-99 beladen und arbeitstäglich mit physiologischer Kochsalzlösung eluiert. Die Tabelle 3 zeit die Ergebnisse.
Die Tabelle 3 belegt die Herabsetzung des Mo-99-Gehaltes im Eluat auch bei Anwendung der Ausgestaltung nach EP-B 0 014 957. In keinem Eluat konnte Cu(II) festgestellt werden.Table 3 shows the reduction of the Mo-99 content in the eluate even when using the design according to EP-B 0 014 957. Cu (II) could not be found in any eluate.
Claims (6)
- A technetium-99m generator which is based on molybdenum-99 adsorbed on a carrier and is eluted with solutions containing copper(II), which contains a silica gel modified with amino groups.
- A generator as claimed in claim 1, wherein, in an elution column (1), the carrier containing the molybdenum-99 is arranged as the upper layer (2) and the silica gel modified with amino groups is arranged as the lower layers (3).
- A generator as claimed in claim 1 or 2, which additionally contains a magnesium silicate.
- A generator as claimed in claim 1, 2 or 3 wherein, in an elution column (1), aluminum oxide charged with copper(II) is arranged as the upper layer (4), aluminum oxide is arranged as the middle layer (2) and silica gel modified with amino groups is arranged as the lower layer (3).
- A process for the preparation of a generator as claimed in any one of claims 1 to 4, which comprises using a silica gel modified with amino groups as carrier.
- The use of a generator as claimed in any one of claims 1 to 4 for obtaining an eluate containing technetium-99m.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT86111788T ATE63013T1 (en) | 1985-09-03 | 1986-08-26 | TECHNETIUM-99M GENERATOR, ITS MANUFACTURE AND USE. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3531355 | 1985-09-03 | ||
DE19853531355 DE3531355A1 (en) | 1985-09-03 | 1985-09-03 | TECHNETIUM 99M GENERATOR, ITS PRODUCTION AND USE |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0213589A2 EP0213589A2 (en) | 1987-03-11 |
EP0213589A3 EP0213589A3 (en) | 1988-03-16 |
EP0213589B1 true EP0213589B1 (en) | 1991-04-24 |
Family
ID=6279972
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP86111788A Expired - Lifetime EP0213589B1 (en) | 1985-09-03 | 1986-08-26 | Generator of technecium-99m, its preparation and use |
Country Status (14)
Country | Link |
---|---|
US (1) | US4837110A (en) |
EP (1) | EP0213589B1 (en) |
JP (1) | JPS6271900A (en) |
AT (1) | ATE63013T1 (en) |
BE (1) | BE905368A (en) |
CA (1) | CA1276448C (en) |
DE (2) | DE3531355A1 (en) |
DK (1) | DK417786A (en) |
ES (1) | ES2003343A6 (en) |
GR (1) | GR862237B (en) |
IE (1) | IE59192B1 (en) |
PT (1) | PT83290B (en) |
SU (1) | SU1471959A3 (en) |
ZA (1) | ZA866644B (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5110474A (en) * | 1990-04-09 | 1992-05-05 | Arch Development Corporation | Method for liquid chromatographic extraction of strontium from acid solutions |
WO2002042990A1 (en) | 2000-11-27 | 2002-05-30 | Kabushiki Kaisha Sankyo Seiki Seisakusho | Card gate mechanism in card reader |
US7737415B2 (en) * | 2004-01-27 | 2010-06-15 | Laboratorios Bacon, S.A. | System for the control, verification and recording of the performance of a radioisotope generator's operations |
US20060023829A1 (en) * | 2004-08-02 | 2006-02-02 | Battelle Memorial Institute | Medical radioisotopes and methods for producing the same |
WO2006039787A1 (en) * | 2004-10-12 | 2006-04-20 | Mcmaster University | GENERATOR AND METHOD FOR PRODUCTION OF TECHNETIUM-99m |
EP2139541B1 (en) | 2007-01-01 | 2018-04-11 | Bayer Healthcare LLC | Systems for integrated radiopharmaceutical generation, preparation, transportation, and administration |
RU2443030C2 (en) * | 2010-02-03 | 2012-02-20 | Федеральное государственное унитарное предприятие "Ордена Трудового Красного Знамени научно-исследовательский физико-химический институт им. Л.Я. Карпова" (ФГУП "НИФХИ им. Л.Я. Карпова") | TECHNETIUM-99m GENERATOR WITH SULFO-CARBOXYLATED CATION-EXCHANGING PROTECTIVE LAYER AND THE METHOD OF ITS PRODUCTION |
WO2011153457A1 (en) | 2010-06-04 | 2011-12-08 | Medrad, Inc. | System and method for planning and monitoring multi-dose radiopharmaceutical usage on radiopharmaceutical injectors |
KR102612251B1 (en) * | 2017-07-12 | 2023-12-08 | 아란세오 도이치란드 게엠베하 | Reactor and method for continuous polymerization |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3369121A (en) * | 1966-04-06 | 1968-02-13 | Squibb & Sons Inc | Radioactive package and container therefor |
NL6607699A (en) * | 1966-06-03 | 1967-12-04 | ||
US3664964A (en) * | 1968-07-03 | 1972-05-23 | Squibb & Sons Inc | Eluent for radioisotopes |
US3755161A (en) * | 1970-02-05 | 1973-08-28 | Osaka Soda Co Ltd | Treatment process for removal of metals and treating agent therefor |
CA955035A (en) * | 1970-02-05 | 1974-09-24 | Osaka Soda Co. | Treatment process for removal of metals and treating agent therefor |
US3740558A (en) * | 1971-02-17 | 1973-06-19 | Dainabot Radioisotope Labor Lt | Radioactive isotope generator of short-lived nuclides |
US4167481A (en) * | 1975-03-19 | 1979-09-11 | Leuven Research & Development Vzw | Process for the removal of metals from solution |
NL7503293A (en) * | 1975-03-19 | 1976-09-21 | Leuven Res & Dev Vzw | METHOD OF REMOVING METALS FROM SOLUTION. |
US4158700A (en) * | 1976-03-08 | 1979-06-19 | Karageozian Hampar L | Method of producing radioactive technetium-99M |
DE2906439A1 (en) * | 1979-02-20 | 1980-09-04 | Hoechst Ag | METHOD FOR SEPARATING TECHNETIUM-99M FROM MOLYBAEN-99 |
CA1169773A (en) * | 1979-04-17 | 1984-06-26 | Karel J. Panek | Preparation and use of a su195m xxau-containing liquid |
DE8533473U1 (en) * | 1985-11-28 | 1986-02-06 | Hoechst Ag, 6230 Frankfurt | Technetium 99m generator |
-
1985
- 1985-09-03 DE DE19853531355 patent/DE3531355A1/en active Granted
-
1986
- 1986-08-26 EP EP86111788A patent/EP0213589B1/en not_active Expired - Lifetime
- 1986-08-26 DE DE8686111788T patent/DE3678880D1/en not_active Expired - Fee Related
- 1986-08-26 AT AT86111788T patent/ATE63013T1/en not_active IP Right Cessation
- 1986-08-29 CA CA000517245A patent/CA1276448C/en not_active Expired - Fee Related
- 1986-09-01 SU SU864028062A patent/SU1471959A3/en active
- 1986-09-01 ES ES8601541A patent/ES2003343A6/en not_active Expired
- 1986-09-01 GR GR862237A patent/GR862237B/en unknown
- 1986-09-02 ZA ZA866644A patent/ZA866644B/en unknown
- 1986-09-02 DK DK417786A patent/DK417786A/en not_active Application Discontinuation
- 1986-09-02 PT PT83290A patent/PT83290B/en not_active IP Right Cessation
- 1986-09-02 JP JP61205256A patent/JPS6271900A/en active Pending
- 1986-09-02 BE BE0/217116A patent/BE905368A/en not_active IP Right Cessation
- 1986-09-02 IE IE234586A patent/IE59192B1/en not_active IP Right Cessation
-
1988
- 1988-06-29 US US07/214,889 patent/US4837110A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
DK417786D0 (en) | 1986-09-02 |
EP0213589A2 (en) | 1987-03-11 |
ZA866644B (en) | 1987-04-29 |
JPS6271900A (en) | 1987-04-02 |
US4837110A (en) | 1989-06-06 |
ATE63013T1 (en) | 1991-05-15 |
CA1276448C (en) | 1990-11-20 |
DE3531355A1 (en) | 1987-03-12 |
SU1471959A3 (en) | 1989-04-07 |
ES2003343A6 (en) | 1988-11-01 |
IE59192B1 (en) | 1994-01-26 |
PT83290B (en) | 1993-04-30 |
DK417786A (en) | 1987-03-04 |
GR862237B (en) | 1986-12-31 |
EP0213589A3 (en) | 1988-03-16 |
DE3678880D1 (en) | 1991-05-29 |
PT83290A (en) | 1986-10-01 |
DE3531355C2 (en) | 1992-06-11 |
BE905368A (en) | 1987-03-02 |
IE862345L (en) | 1987-03-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE60209818T2 (en) | METHOD AND DEVICE FOR SEPARATING IONES OF METALLIC ELEMENTS IN AQUEOUS SOLUTION | |
EP0443479A1 (en) | Process for producing Actinium-225 and Bismuth-213 | |
WO1999046779A1 (en) | Adsorption means for radionuclides | |
EP0213589B1 (en) | Generator of technecium-99m, its preparation and use | |
DE2542415A1 (en) | HIGH 82 SR HIGH 82 RB RADIO ISOTOP GENERATOR | |
DE3100365C2 (en) | ||
DE2536713A1 (en) | METHOD FOR DETERMINATION OF VITAMIN B-12 WITH RADIO ISOTOPES | |
DE102009049108B4 (en) | Method and apparatus for obtaining a radionuclide | |
DE102008064682B4 (en) | Anionic borane polymer, as well as its use and preparation | |
DE1210416B (en) | Process for separating metal ions | |
DE8533473U1 (en) | Technetium 99m generator | |
DE2909648A1 (en) | METHOD OF MANUFACTURING RADIOACTIVE TECHNETIUM-99M | |
DE202006020604U1 (en) | Column system for producing a solution with high specific activity | |
EP0014957B1 (en) | Process for separating technetium-99m from molybdenum-99 | |
DE2511712C3 (en) | Manufacture of a technetium 99m generator | |
DE2213137A1 (en) | Procedure for recharging a technetium-99m generator | |
DE2057543B2 (en) | Process for the recovery of aqueous solutions containing small amounts of radioactive yttrium-90 and of a high degree of purity | |
DE2030102A1 (en) | ||
DE2030102C3 (en) | Process for the production of technet! Um-99m from an aqueous solution of an inorganic salt of molybdenum-99 | |
DE2338366C3 (en) | Method of making a technetium-99m generator | |
DE112021003173T5 (en) | CHITOSAN/TITANIUM COMPOSITE AND METHOD OF MANUFACTURE AND USE THEREOF | |
DE2009492C3 (en) | Process for the separation of pyrogens from preparations of L-asparaginase | |
DE2511712B2 (en) | MANUFACTURING OF A TECHNETIUM-99M GENERATOR | |
DE2806849A1 (en) | Rechargeable radio-technetium generator - using column of activated chromatographic alumina and molybdate charging soln. | |
CH636724A5 (en) | PROCESS FOR THE PRODUCTION OF (52)MANGANE. |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AT CH DE FR GB IT LI LU NL SE |
|
PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): AT CH DE FR GB IT LI LU NL SE |
|
17P | Request for examination filed |
Effective date: 19880823 |
|
17Q | First examination report despatched |
Effective date: 19900926 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT CH DE FR GB IT LI LU NL SE |
|
REF | Corresponds to: |
Ref document number: 63013 Country of ref document: AT Date of ref document: 19910515 Kind code of ref document: T |
|
ITF | It: translation for a ep patent filed |
Owner name: ING. C. GREGORJ S.P.A. |
|
REF | Corresponds to: |
Ref document number: 3678880 Country of ref document: DE Date of ref document: 19910529 |
|
ET | Fr: translation filed | ||
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
EPTA | Lu: last paid annual fee | ||
EAL | Se: european patent in force in sweden |
Ref document number: 86111788.5 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PUE Owner name: HOECHST AKTIENGESELLSCHAFT TRANSFER- CIS BIO INTER Ref country code: CH Ref legal event code: NV Representative=s name: SCHAAD, BALASS & PARTNER AG |
|
NLS | Nl: assignments of ep-patents |
Owner name: CIS BIO INTERNATIONAL |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 19960731 Year of fee payment: 11 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 19960801 Year of fee payment: 11 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: TP |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19970826 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19970827 |
|
EUG | Se: european patent has lapsed |
Ref document number: 86111788.5 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19980831 Year of fee payment: 13 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20000301 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20000301 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: IF02 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 20020704 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20020708 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20020712 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20020724 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 20020726 Year of fee payment: 17 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030826 Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030826 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030831 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030831 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040302 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee | ||
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040430 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20050826 |