EP0213589A2 - Generator of technecium-99m, its preparation and use - Google Patents

Generator of technecium-99m, its preparation and use Download PDF

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EP0213589A2
EP0213589A2 EP86111788A EP86111788A EP0213589A2 EP 0213589 A2 EP0213589 A2 EP 0213589A2 EP 86111788 A EP86111788 A EP 86111788A EP 86111788 A EP86111788 A EP 86111788A EP 0213589 A2 EP0213589 A2 EP 0213589A2
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copper
silica gel
aluminum oxide
generator
technetium
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EP0213589A3 (en
EP0213589B1 (en
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Ludwig Dr. Kuhlmann
Dietrich Pütter
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CIS Bio International SA
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Hoechst AG
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    • GPHYSICS
    • G21NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21GCONVERSION OF CHEMICAL ELEMENTS; RADIOACTIVE SOURCES
    • G21G4/00Radioactive sources

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  • the invention relates to an improved technetium-99m generator based on carrier-adsorbed molybdenum-99, a process 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.
  • containing only a small amount of aluminum oxide even if the minimum copper (II) concentrations mentioned are used, this is not sufficient 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 containing 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 such 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.
  • 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.
  • (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, that is, in a preferred embodiment, aluminum oxide as layer (2) and amino group-modified silica gel as layer (3).
  • FIG. 2 denotes 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 polysilicate, the latter with chain, ribbon or layer (sheet) ) Structure included. Such materials are used for example for chromatographic processes.
  • a 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.

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Abstract

Silica gels modified with amino groups or magnesium silicates are suitable carrier materials for technetium-99m generators since they retain copper(II) ions well and thus produce a copper-free eluate.

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, a process 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 eluting 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 activity and which in the eluate would lead to unnecessary radiation exposure 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.However, there arises the difficulty that the small amounts of aluminum oxide are not sufficient to prevent the copper from permeating 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 Prioritäts­ tag 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 that have priority were common on the day of the aforementioned German publication, containing only a small amount of aluminum oxide, even if the minimum copper (II) concentrations mentioned are used, this is not sufficient 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 containing 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 such 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) -loaded 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:1 and 2 show schematically and not necessarily to scale two embodiments of the invention:

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).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, that is, 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 denotes 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 polysilicate, 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.

Beispiel 1example 1

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.

Figure imgb0001
By elution under the same conditions, it was determined to what extent the carrier materials are capable. Capture copper (II) ions. Eluates No. 1-8 were copper-free in all cases. As Table 1 below shows, the silica gel can trap copper (II) much better than the aluminum oxide.
Figure imgb0001

Beispiel 2Example 2

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 x 2H₂O 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 every working day with physiological saline solution containing 20 µg CuCl₂ x 2H₂O per ml. Before the addition of the copper (II) chloride, the saline solution was sterilized together with the PVC film which 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, a 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.

Die Tabelle 2 zeigt:

  • 1. Durch Einsatz von Kieselgel wird der Mo-99-Gehalt im Eluat unter 1 ppm gesenkt.
  • 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.
  • 3. Durch Einsatz von Kieselgel kann der Kupfer(II)-Gehalt im Elutionsmittel über den minimalen Anteil von 20 ppm hinaus gesteigert werden.
Figure imgb0002
Table 2 shows:
  • 1. The use of silica gel lowers the Mo-99 content in the eluate below 1 ppm.
  • 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 copper (II) being detectable in the eluate in any significant amounts.
  • 3. By using silica gel, the copper (II) content in the eluent can be increased beyond the minimum proportion of 20 ppm.
Figure imgb0002

Beispiel 3Example 3

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.

Figure imgb0003
Generator columns were produced using the method of EP-B 0 014 957. However, some also contained silica gel as the bottom layer. These were loaded with Mo-99 and eluted daily with physiological saline. Table 3 shows the results.
Figure imgb0003

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)

1. Technetium-99m-Generator auf Basis von trägeradsorbier­tem Molybdän-99, der mit Kupfer(II) enthaltenden Lösun­gen eluiert wird, gekennzeichnet durch einen Gehalt an einem aminogruppenmodifizierten Kieselgel.1. Technetium-99m generator based on carrier-adsorbed molybdenum-99, which is eluted with solutions containing copper (II), characterized by a content of an amino group-modified silica gel. 2. Generator nach Anspruch 1, dadurch gekennzeichent, daß in einer Elutionssäule (1) der das Molybdän-99 enthal­tende Träger als obere Schicht (2) und das aminogruppen­modifizierte Kieselgel als untere Schicht (3) angeord­net ist.2. Generator according to claim 1, characterized in that in an elution column (1) the carrier containing the molybdenum-99 is arranged as the upper layer (2) and the amino group-modified silica gel as the lower layer (3). 3. Generator nach Anspruch 1 oder 2, durch gekennzeich­net, daß er zusätzlich ein Magnesiumsilikat enthält.3. Generator according to claim 1 or 2, characterized in that it additionally contains a magnesium silicate. 4. Generator nach Anspruch 1, 2 oder 3, dadurch gekenn­zeichnet, daß in einer Elutionssäule (1) als obere Schicht (4) Kupfer(II)-beladenes Aluminiumoxid, als mittlere Schicht (2) Aluminiumoxid und als untere Schicht (3) aminogruppenmodifiziertes Kieselgel ange­ordnet ist.4. Generator according to claim 1, 2 or 3, characterized in that in an elution column (1) as the upper layer (4) copper (II) -loaded aluminum oxide, as the middle layer (2) aluminum oxide and as the lower layer (3) modified amino groups Silica gel is arranged. 5. Verfahren zur Herstellung eines Generators nach An­spruch 1 bis 4, dadurch gekennzeichnet, daß man als Trägermaterial ein aminogruppenmodifiziertes Kieselgel einsetzt.5. A process for producing a generator according to claim 1 to 4, characterized in that an amino group-modified silica gel is used as the carrier material. 6. Verwendung eines Generators nach Anspruch 1 bis 4 zur Gewinnung eines Technetium-99m enthaltenden Eluats.6. Use of a generator according to claim 1 to 4 for the production of a technetium-99m containing eluate.
EP86111788A 1985-09-03 1986-08-26 Generator of technecium-99m, its preparation and use Expired - Lifetime EP0213589B1 (en)

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AT86111788T ATE63013T1 (en) 1985-09-03 1986-08-26 TECHNETIUM-99M GENERATOR, ITS MANUFACTURE AND USE.

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DE3531355 1985-09-03
DE19853531355 DE3531355A1 (en) 1985-09-03 1985-09-03 TECHNETIUM 99M GENERATOR, ITS PRODUCTION AND USE

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EP0213589A2 true EP0213589A2 (en) 1987-03-11
EP0213589A3 EP0213589A3 (en) 1988-03-16
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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)
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2761057C2 (en) * 2017-07-12 2021-12-02 Арланксео Дойчланд Гмбх Reactor and continuous polymerization method

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* Cited by examiner, † Cited by third party
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
CA2553957A1 (en) * 2004-01-27 2005-09-09 Arcana International, Inc. 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
US20080187489A1 (en) * 2004-10-12 2008-08-07 Mcmaster University Generator and Method for Production of Technetium-99m
ES2677024T3 (en) 2007-01-01 2018-07-27 Bayer Healthcare Llc Systems for generation, preparation, transport and administration of integrated radiopharmaceutical products
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
BR112012031359A2 (en) 2010-06-04 2016-10-25 Medrad Inc system and method of planning and monitoring the use of multiple dose radiopharmaceuticals in radiopharmaceutical injectors

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1929067A1 (en) * 1968-07-03 1970-01-15 Squibb & Sons Inc Eluent for radioisotope generators
FR2080451A5 (en) * 1970-02-05 1971-11-12 Osaka Soda Co Ltd
FR2304578A1 (en) * 1975-03-19 1976-10-15 Leuven Res & Dev Vzw METHOD FOR REMOVING METALS FROM SOLUTIONS CONTAINING IT
EP0014957A1 (en) * 1979-02-20 1980-09-03 Hoechst Aktiengesellschaft Process for separating technetium-99m from molybdenum-99
DE8533473U1 (en) * 1985-11-28 1986-02-06 Hoechst Ag, 6230 Frankfurt Technetium 99m generator

Family Cites Families (7)

* Cited by examiner, † Cited by third party
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
US3755161A (en) * 1970-02-05 1973-08-28 Osaka Soda Co Ltd 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
US4158700A (en) * 1976-03-08 1979-06-19 Karageozian Hampar L Method of producing radioactive technetium-99M
CA1169773A (en) * 1979-04-17 1984-06-26 Karel J. Panek Preparation and use of a su195m xxau-containing liquid

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1929067A1 (en) * 1968-07-03 1970-01-15 Squibb & Sons Inc Eluent for radioisotope generators
FR2080451A5 (en) * 1970-02-05 1971-11-12 Osaka Soda Co Ltd
FR2304578A1 (en) * 1975-03-19 1976-10-15 Leuven Res & Dev Vzw METHOD FOR REMOVING METALS FROM SOLUTIONS CONTAINING IT
EP0014957A1 (en) * 1979-02-20 1980-09-03 Hoechst Aktiengesellschaft Process for separating technetium-99m from molybdenum-99
DE8533473U1 (en) * 1985-11-28 1986-02-06 Hoechst Ag, 6230 Frankfurt Technetium 99m generator

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2761057C2 (en) * 2017-07-12 2021-12-02 Арланксео Дойчланд Гмбх Reactor and continuous polymerization method

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EP0213589A3 (en) 1988-03-16
BE905368A (en) 1987-03-02
JPS6271900A (en) 1987-04-02
PT83290A (en) 1986-10-01
US4837110A (en) 1989-06-06
PT83290B (en) 1993-04-30
ATE63013T1 (en) 1991-05-15
CA1276448C (en) 1990-11-20
DE3531355C2 (en) 1992-06-11
DE3678880D1 (en) 1991-05-29
DK417786D0 (en) 1986-09-02
IE59192B1 (en) 1994-01-26
GR862237B (en) 1986-12-31
ES2003343A6 (en) 1988-11-01
DK417786A (en) 1987-03-04
SU1471959A3 (en) 1989-04-07
IE862345L (en) 1987-03-03
EP0213589B1 (en) 1991-04-24
DE3531355A1 (en) 1987-03-12
ZA866644B (en) 1987-04-29

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