GB2067343A - Generation of radio-isotopes - Google Patents
Generation of radio-isotopes Download PDFInfo
- Publication number
- GB2067343A GB2067343A GB8100647A GB8100647A GB2067343A GB 2067343 A GB2067343 A GB 2067343A GB 8100647 A GB8100647 A GB 8100647A GB 8100647 A GB8100647 A GB 8100647A GB 2067343 A GB2067343 A GB 2067343A
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- United Kingdom
- Prior art keywords
- reservoir
- isotope
- adsorbent
- cation
- generator system
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- 239000003463 adsorbent Substances 0.000 claims abstract description 37
- 239000000463 material Substances 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 18
- 238000005341 cation exchange Methods 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 230000002285 radioactive effect Effects 0.000 claims abstract description 11
- 239000012217 radiopharmaceutical Substances 0.000 claims abstract description 10
- 229940121896 radiopharmaceutical Drugs 0.000 claims abstract description 10
- 230000002799 radiopharmaceutical effect Effects 0.000 claims abstract description 10
- 229950009740 molybdenum mo-99 Drugs 0.000 claims description 15
- ZOKXTWBITQBERF-AKLPVKDBSA-N Molybdenum Mo-99 Chemical compound [99Mo] ZOKXTWBITQBERF-AKLPVKDBSA-N 0.000 claims description 14
- 238000000926 separation method Methods 0.000 claims description 13
- 239000011347 resin Substances 0.000 claims description 12
- 229920005989 resin Polymers 0.000 claims description 12
- 239000011521 glass Substances 0.000 claims description 11
- 239000003729 cation exchange resin Substances 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 10
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 9
- -1 polyethylene Polymers 0.000 claims description 9
- 239000003480 eluent Substances 0.000 claims description 8
- 238000001179 sorption measurement Methods 0.000 claims description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 7
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims description 6
- 239000004698 Polyethylene Substances 0.000 claims description 5
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 229920000573 polyethylene Polymers 0.000 claims description 5
- 150000002500 ions Chemical class 0.000 claims description 4
- 239000003365 glass fiber Substances 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims 2
- 239000000126 substance Substances 0.000 abstract description 7
- 238000010828 elution Methods 0.000 description 21
- 239000000243 solution Substances 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 5
- 238000002372 labelling Methods 0.000 description 5
- 229910052750 molybdenum Inorganic materials 0.000 description 5
- 239000011733 molybdenum Substances 0.000 description 5
- 229920001467 poly(styrenesulfonates) Polymers 0.000 description 5
- 230000005855 radiation Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000004458 analytical method Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000004992 fission Effects 0.000 description 3
- 230000036512 infertility Effects 0.000 description 3
- 239000002504 physiological saline solution Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 2
- 229910017963 Sb2 S3 Inorganic materials 0.000 description 2
- 229910052768 actinide Inorganic materials 0.000 description 2
- 150000001255 actinides Chemical class 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000011491 glass wool Substances 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000011684 sodium molybdate Substances 0.000 description 2
- 235000015393 sodium molybdate Nutrition 0.000 description 2
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 description 2
- 125000006850 spacer group Chemical group 0.000 description 2
- 229910052959 stibnite Inorganic materials 0.000 description 2
- 229940055492 99 molybdenum Drugs 0.000 description 1
- DPYZUSDYVFKGKL-UHFFFAOYSA-N C=C.OOP(=O)OP(O)=O Chemical compound C=C.OOP(=O)OP(O)=O DPYZUSDYVFKGKL-UHFFFAOYSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 229910017974 NH40H Inorganic materials 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000005388 borosilicate glass Substances 0.000 description 1
- 229940023913 cation exchange resins Drugs 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical class [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000009828 non-uniform distribution Methods 0.000 description 1
- 239000008194 pharmaceutical composition Substances 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 238000011045 prefiltration Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- VBHKTXLEJZIDJF-UHFFFAOYSA-N quinalizarin Chemical compound C1=CC(O)=C2C(=O)C3=C(O)C(O)=CC=C3C(=O)C2=C1O VBHKTXLEJZIDJF-UHFFFAOYSA-N 0.000 description 1
- 230000005258 radioactive decay Effects 0.000 description 1
- 239000012857 radioactive material Substances 0.000 description 1
- 238000002798 spectrophotometry method Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21G—CONVERSION OF CHEMICAL ELEMENTS; RADIOACTIVE SOURCES
- G21G1/00—Arrangements for converting chemical elements by electromagnetic radiation, corpuscular radiation or particle bombardment, e.g. producing radioactive isotopes
- G21G1/0005—Isotope delivery systems
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21G—CONVERSION OF CHEMICAL ELEMENTS; RADIOACTIVE SOURCES
- G21G1/00—Arrangements for converting chemical elements by electromagnetic radiation, corpuscular radiation or particle bombardment, e.g. producing radioactive isotopes
- G21G1/04—Arrangements for converting chemical elements by electromagnetic radiation, corpuscular radiation or particle bombardment, e.g. producing radioactive isotopes outside nuclear reactors or particle accelerators
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21G—CONVERSION OF CHEMICAL ELEMENTS; RADIOACTIVE SOURCES
- G21G1/00—Arrangements for converting chemical elements by electromagnetic radiation, corpuscular radiation or particle bombardment, e.g. producing radioactive isotopes
- G21G1/001—Recovery of specific isotopes from irradiated targets
- G21G2001/0042—Technetium
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Medicines Containing Antibodies Or Antigens For Use As Internal Diagnostic Agents (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Investigating Or Analysing Biological Materials (AREA)
Abstract
A method of preparing a liquid containing radioisotope for radiopharmaceutical application comprises eluting a radioactive daughter isotope from a parent isotope which is adsorbed on an adsorbent by means of a physiological solution, wherein a fission- produced parent isotope is used and the eluate comprising a daughter isotope is purified with a cation-exchange material. The method produces a liquid containing a radioisotope having an exceptionally high chemical, radiochemical and radionuclidic purity in a high yield. An isotope generator system suitable for use of the said method and a reservoir for said generator system is also described and claimed.
Description
SPECIFICATION
Generation of radioisotopes
This invention relates to a method of preparing a liquid for radiopharmaceutical application comprising a radioisotope, and to an isotope generator suitable for preparing said liquid. More particularly the invention relates to a method of preparing a liquid for radiopharmaceutical application comprising a radioisotope by eluting from a parent isotope, which is adsorbed on an adsorbent, a radioactive daughter isotope by means of a physiological solution. The invention also relates to an isotope generator system suitable for conducting the above-described method, as well as to a reservoir for said generator system.
Radioisotopes having a half-life up to a few days are used for diagnostic purposes in medicine. In order to minimize damage to the tissues by radiation, it is recommendable to use radioisotopes which emit only gamma radiation. The radioisotope 99mTc is a pure gamma radiator and has a comparatively short half-life.
Therefore, this isotope is excellently suitable for use as a diagnostic, but also it may be used for radioactively labelling other substances such as proteins. The 99mTc isotope is generated by radioactive decay of the parent isotope 99Mo. It is known, for example from Netherlands Patent Application 7302304 (corresponding with U. S. patent 3,970,583) to adsorb the parent isotope in the form of a molybdate on a suitable adsorbent and then to elute the daughter isotope 99mTc by means of a physiological saline solution. An apparatus suitable for producing a 99mTc-containing liquid in this manner is an isotope generator as is also described in the above-mentioned Netherlands Patent Application No.7302304.
As a result of the fast development of radiodiagnostics in the past ten years, there has come a need for a liquid for radiopharmaceutical application comprising a radioisotope, which liquid has a higher concentration of radioactive material and a greater chemical purity than the radio-diagnostics heretofore used. The present 99mtechnetium eluate is produced in an isotope generator from natural or enriched molybdenum irradiated in a nuclear reactor. The radioactive isotope 99Mo is present in this product in a very small concentration; the bulk consists of non-radioactive molybdenum and serves as a carrier for 99Mo. The dimensions of the column containing the adsorbent for the parent isotope are restricted because a column that is too large can not be eluted efficiently.This applies in particular to the withdrawal of small elution volumes from the column, which are necessary for certain purposes in which a higher isotope concentration is required. Since restrictions are imposed jupon the dimensions of the column and upon the adsorption capacity of the adsorbent, only comparatively little parent isotope can be present in the generator, as a result of which the required high concentration of radioactivity in the eluate cannot be obtained with prior isotope generators.
Meanwhile, radioactive isotopes, for example, radioactive molybdenum and cerium, have been produced in a different manner, namely by a fission reaction. For example, 99molybdenum is produced by fission of 235U; 235U is irradiated in a nuclear reactor with neutrons, after which the other fission products can be removed from 99Mo by a chemical separation process. Afission-produced radioisotope is purified to an acceptable degree of radionuclidic purity, but still contains traces of contaminations such as 115Cd,136Cs, 140La, 156Eu, 89Sr, 90Sr, sZr, 140Ba and actinides. In addition to gamma radiation emitted by most of these radioisotopes, these contaminations also emit corpuscular radiation, namely alpha or beta radiation.These alpha or beta radiators are very undesirable in pharmaceutical compositions because they can seriously attack the tissues; the strontium isotopes and actinides are considered to be most toxic.
It has now been found that a liquid comprising a radioisotope suitable for radiopharmaceutical application can be produced in a high yield by elution of a fission-produced parent isotope adsorbed on a suitable adsorbent, when the eluate containing a daughter isotope is purified by means of a cation-exchange material, preferably a cation-exchange resin. Particularly suitable for this purpose are strongly-acidic cation-exchange resins which are neutralized, and have a particle size of, for example, 50-400 mesh, preferably 100-200 mesh. As an example of a resin suitable for this purpose may be mentioned Dowex or
Bio-Rad 50W-X8. These strongly-acidic resins are preferably neutralized by treating them with an alkali metal base, e.g., NaOH, KOH, or with NH40H, and then washing with water. In this manner the resins are converted into the Na+, K+ or NH4+ form.
It is known from Int J. Appl. Rad. Isotopes 1978, Viol.29, pp. 91-96, that the resin Dowex 50W-X8 in the Na+ form may be used for the separation of 90Y from 90Sr. In the reaction circumstances described in this article, namely in the presence of a small quantity of EDTA, the influence of the pH on the adsorption of 90Sr was determined. From the results it appears that 90Sr is adsorbed on Dowex 50 resin at a pH of 1.5-5.5, but not at a pH of 7.0. The concentration of EDTA had no influence on the adsorption of 90Sr. These results give rise to the supposition that Dowex 50 resin is not suitable to adsorb 90Sr from a solution suitable for pharmaceutical application, namely an approximately neutral physiological saline solution.However, quite contrary to expectations it has been found that a cation-exchange resin, in particular a strongly-acidic cation-exchange resin such as Dowex or Bio-Rad 50W-X8 converted into the Na+, K+ or NH4+ form is particularly suitable to purify 99mTc produced from fission-produced 99Mo, so that a solution containing 99mTc and suitable for radiopharmaceutical application is obtained with an exceptionaliy high chemical, radiochemical and radionuclidic purity.
From the above-mentioned Netherlands patent application 7302304 it is known that aluminium oxide which contains fully or partly hydrated manganese dioxide is an adsorption agent for the parent isotope 99Mo. It has been found that this material also is excellently suitable as an adsorbentforthe entirely, or substantially, molybdenum carrier-free, fission-produced 99Mo. This is not obvious as such, because the latter concerns extremely small quantities of adsorbed molybdenum which moreover contains undesired contaminants.The desired optimum elution yield strongly depends on the nature and quantity of the material to be eluted and the adsorbed material present, and it is generally known that small differences in these respects can easily disturb this subtle equilibrium, as a result of which either a less optimum yield, or an undesired elution pattern, could be obtained.
From the above it will be clearthatthe method according to the invention will preferably be used in an isotope generator system. An isotope generator system is to be understood to mean the actual isotope generator provided with a connection to a reservoir with eluent and with an eluate conduit, and enclosed by a generator housing. Such a system is sometimes termed "cow". The invention therefore also relates to a generator system the isotope generator of which comprises a reservoir having a supply facility for the eluent and an outlet facility for the eluate, and in which the adsorption agent for the parent isotope is present. Such a generator is known, for example, from the above-mentioned Netherlands Patent Application 7302304.
However, the generator according to the invention comprises a fission-produced radioisotope and a cation-exchange material. Because the fission-produced radioisotope is fully or substantially carrier-free, a small quantity of adsorbent for the parent isotope is amply sufficient. As a result of this the dimensions of the generator system can be greatly reduced, so that the apparatus is easier to handle, both in use (in hospital or clinical laboratory the generator system must regularly be changed), and upon assembly by the manufacturer. It is of great advantage that the cation-exchange material is also present in the generator system according to the invention.As a result of this, the eluate can be purified in the generator itself so that the liquid withdrawn from the generator and comprising radioactive daughter isotope has a high chemical and radionuclidic purity, hence is suitable for radiopharmaceutical application. Purification afterwards of the eluate, that is to say after it has left the generator is superfluous. Such a purification afterwards generally is even impossible or at least undesired, because the daughter isotope obtained usually has too short a half-life to be able to stand such an after-treatment, and also because an after-treatment in a hospital or clinical laboratory where auxiliary means suitable for the purpose are lacking, is out of the question for reasons of safety.
It is usual to enclose the adsorbent for the parent isotope in the reservoir of the generator system between two filters. In order to load the adsorbent with the radioactive parent isotope, a solution of this isotope is admitted to one side of the reservoir. Glasswool or glass beads are frequently used on this side as a filtering material. However, glass beads cause channeling in the adsorbent and hence inefficient loading and a non-uniform distribution of the parent isotope over the adsorbent. Glasswool often impedes the loading due to too large a resistance and in addition it tends, as also synthetic resins, for example, polyethylene, to adsorb a little parent isotope. This latter is very objectionable because upon elution of the generator, the quantity of parent isotope not adsorbed on the adsorption agent will contaminate the eluate.
As a particular aspect of the invention it has now been found that the above-mentioned disadvantages can be removed by the filter on that side of the generator reservoir where the solution of the parent isotope is admitted being made of sintered glass. It has been found that when such a filter is used which, of course, can also be used in the prior art isotope generators, an efficient and homogenous loading of the adsorbent can very easily be achieved, while no parent isotope is adsorbed by the filter.
The generator system according to the invention is preferably constructed so that both the cationexchange resin and the adsorbent for the parent isotope are present in the same reservoir. In this embodiment in which the dimensions of the generator can be minimized and an optimum purity of the radiopharmaceutical composition can be reached,the above-mentioned advantages stand out even better, while the cost of production can also be kept as low as possible.
In a further preferred embodiment the reservoir containing both the cation-exchange resin and the adsorbent for the parent isotope is divided into two compartments which are separated from each other by a filter the circumference of which adjoins the inner wall of the reservoir. One compartment of the reservoir comprises a supply facility for the eluent and the adsorbent for the parent isotope is present between supply facility and separation filter, the adsorbent being enclosed between the above-mentioned sintered glass filter and the separation filter. The other compartment of the reservoir comprises an outlet facility for the eluate. The cation-exchange material is present between separation filter and outlet facility, the space between the adsorbent particles and between the particles of the ion-exchanger being filled with a physiological solution.A separation filter suitable for this purpose consists of two filter disks covering each other entirely, or substantially entirely, the disk adjoining the adsorption agent consisting of glass fibre paper, for example, a millipore pre-filterAP 200, the disk adjoining the ion exchanger consisting of porous polyethylene.
Finally the invention relates to a reservoir for the above-mentioned generator, which reservoir contains both the cation-exchange material and the adsorbent for the parent isotope. It has been found that such a reservoir that is loaded and sterilized can be stored in an uncooled condition for more than 3 months and can be incorporated in a generator system at any desired moment during this period without any pre-treatment.
The reservoir can then be used to provide an eluate containing radioactive daughter isotope in a high yield.
this is of advantage because the reservoirs can be manufactured in stock and be shipped to the supplier of generator system who can at any desired moment use a reservoir for his generator system without any pretreatment; this means a considerable saving of costs.
The invention will be described in greater detail with reference to the following specific example.
The drawing is cross-sectional view of a favorable embodiment of the reservoir of the isotope generator according to the invention. A substantially cylindrical reservoir (4) of a suitable inert material, for example glass or a polymeric material, preferably borosilicate glass, is widened at each end and provided with a flange portion (10, 13). The openings at the two ends of the reservoir are closed by means of rubber stoppers (2, 14) comprising a flange portion (11, 15) and a jacket portion (12, 16); -the flange portion of the stopper engages the flange portion of the reservoir, the jacket portion fitting in the opening of the reservoir.The flange portions of stopper and reservoir are connected together by means of a metal cap, for example and aluminum folded cap (1, 17). The reservoir contains a slurry of the adsorbent (5) in a solution of 0.9% NaCI in water. This adsorbent consists of Al203 particles which are covered entirely or partly with a layer of fully or partially hydrated manganese dioxide. In the reservoir, the adsorbent is enclosed between a filter of sintered glass (3) of an average porosity and a filter disk of glass fibre paper (6), namely a millipore prefilter AP 200.
The reservoir furthermore contains a slurry of the resin Bio-Rad 50W-X8 in the Na+ form (8) in a solution of 0.9% NaCI in water. The resin has been converted into the Na+ form by a treatment with NaOH succeeded by a washing with water. This resin is enclosed between a filter disk (7) of porous polyethylene engaging filter disk (6) and a filter disk (18), likewise of porous polyethylene, supported by a polycarbonate spacer ring (9).
Example 1
Ten of the above-described reservoirs were stored for 3 months and then used for the following experiment.
Each reservoir was loaded with fission-produced molybdenum-carrier4ree 95Mo in the form of sodium molybdate (pH 1-5-10) by perforating the stoppers at the ends of the reservoir, so that an inlet and an outlet aperture were obtained, and then causing a solution of the radioactive sodium molybdate to flow into the reservoir through the inlet aperture (at A). After washing and sterilizing in an autociave at 121"C for 30 minutes, the isotope generator thus obtained was placed in a generator system. The radioactivity of the isotope generator was 1,000 mCi.
When using the generator, the eluent was supplied through the inlet aperture at one end of the reservoir (at A), while the eulate was drained through the outlet aperture at the opposite end of the reservoir. The generators were eluted with sterile isotonic saline solutions (0.9% wt/vol% NaCI in water) in quantities of 4.6 or 15 ml, the average elution yields recorded in the table below being obtained.
TABLE 1
Properties of 4.6 ml and 15 ml 99mTc-containing eluates
Elution voiume: 4.6 ml Elution Volume: 15 ml
Elution Average elution Elution Average elution
yield (%) yield (%)
1 89.4 1 90.8
2 89.9 2 94.1
3 89.1 3 93.9
4 88.6 4 92.4
5 89.6 5 93.3
6 89.6 6 94.2
7 87.2 7 90.9
8 89.3 8 93.1
9 89.6 9 92.7
10 88.5 10 91.9
fcontinuation Table)
Analyses: Analyses:
pH: 6 pH:6
radiochem. purity > 99% radiochem. purity > 99%
Mn++: < 0.3 0.31lg/ml Mn++: < 0.3 Rg/ml Al+++: < 0.5 g/ml Al+++:< 0.5 g/ml
labelling efficiency: labelling efficiency:
-EHDP 97.8% -EHDP 98.4%
-Sb2 S3 97.5% -Sb2 S3 97.0%
radionuclidic purity: radionuclidic purity: -99Mo < 1 nCi/mCi 99mTc -99Mo < 2 nCi/mCi 99mTc
-131| < 1 nCi/mCi 99mTc -131| < 1 nCi/mCi 99mTc -103Ru < 1 nCi/mCi 99mTc -103Ru < 1 nCi/mCi 99mTc sterility: sterile sterility: sterile
apyrogenicity: pyrogen-free apyrogenicity: pyrogen-free
The elution yields recorded in the above table denote the average percentage over the ten generators of the theoretically available 99mTc activity per elution, the generators being eluted ten times each on successive days.So a high elution yield was reached, namely on an average 89.06% + 2.15 and 92.17% + 1.64 of the theoretically available 99mTc activity upon elution with 4.6 and 15 ml of eluent, respectively.
Also recorded in the above table are the average results of the analysis of the eluates. The radiochemical purity was determined by means of a paper chromatographic method; the concentration of Mn++ and Al+++ was determined by means of a spectrophotometric method and a colorimetric (as quinalizarine complex) method, respectively. The labelling efficiency of ethylene hydroxy diphosphonate (EHDP) and Sb2S3 proves that the resulting 99mTc is excellently suitable for preparing 99mTc-labelled compounds and may hence be used for all desired applications. The radionuclidity purity was determined by means of a gamma analyzer.
At most, traces of the radioisotopes 99Mo, 1311 and 103Ru could be detected; other radionuclidic contaminations were not found in the eluate.
It will be obvious from the results shown that the long storage of the filled reservoirs had had no detrimental influence whatsoever on the elution yield and on the purity of the eluate.
In another experiment the same isotope generator could be eluted 15 times with 20 ml of a physiological saline solution without the elution yield changing or the resulting 99mtechnetium eluate being contaminated with cationic contaminants.
Example 2
Ten additional columns substantially similar to those employed in Example 1 but with less dead volume were used to generate 99mTc. The reduced dead volume is achieved by dispensing with the spacer ring and utilizing a cylindrical, non-flanged reservoir in constructing the column. The results are shown in the following tables: Table II
Elution yield
Elution yields (% of available 99mTc activity) gen. mCi 99Mo elution 1st 2nd 3rd 4th 5th 6th 7th 8th 9th 10th no. loaded volume el. el. el. el. el. el. el. el. el. el.
1 768 15 ml 92.36 92.03 92.41 94.25 93.41 89.66 87.48 92.61 90.54 89.52 3 1161 4.6ml 90.45 91.09 89.82 89.61 91.14 88.14 87.17 90.70 89.32 88.96 4 1103 4.6ml 90.25 91.15 89.65 89.09 91.30 88.45 85.69 94.15 88.62 88.59 5 1833 4.6ml 92.02 91.03 90.19 89.76 88.99 90.74 86.24 91.93 89.06 87.12 6 1089 15 ml 92.50 93.27 91.82 92.10 91.47 89.41 88.05 94.18 90.46 89.40 7 1826 4.6ml 90.44 89.91 90.21 90.15 89.91 91.69 86.36 93.22 89.21 87.49 9 1810 15 ml 92.24 93.50 91.95 92.41 91.93 92.34 88.81 93.68 91.42 88.86 10 1815 4.6ml 91.52 90.89 90.45 89.91 91.40 89.80 86.63 92.01 89.98 88.01 TABLE Ill
Chemical purity of eluate
1st eluates 10th eluates
gen. no.
pH yg Mn/ml yg Al/ml pH g Mn/ml Cig Al/ml
1 5.8 < 0.3 < 1 5.8 0.55 < 1
3 5.9 5.9 < 0.30
4 5.8 5.8 < 0.30
5 5.9 6.0 < 0.30
6 5.8 5.9 0.35
7 5.8 5.8 < 0.30
9 6.0 5.9 0.78
10 5.8 5.8 < 0.30
Radiochemical purity - 1st eluates > 99% Labelling properties - 1st eluates Sb2S3 colloid
labelled with 2 ml from 4.6 ml eluate 96.0%
4 ml from 4.6 ml eluate 93.9%
2mlfrom15 mleluate 100.0%
4mlfrom15 ml eluate 99.8%
TABLE IV 99Mo4n eluate
Preliminary test detector: Nal/single channel analyzer
99Mo-breakthrough (nCi 99Mo/mCi 99mTc)
gen. no. 1st 2nd 3rd 4th 5th 6th 7th 8th 9th 10th
el. el. el. el. el. el. el. el. el. el.
1 1.78 1.47 1.72 0.91 1.47 0.78 0.31 1.24 0.90 1.88
3 1.80 1.70 2.00 1.52 1.23 1.41 2.01 2.01 0.34 1.76
4 3.21 2.83 2.31 2.19 2.43 1.86 2.37 3.35 1.03 2.35
5 1.05 1.26 1.19 0.87 1.00 0.92 1.06 0.62 0.89 0.63
6 5.40 3.91 3.47 3.01 3.08 2.37 2.68 1.53 2.66 1.73
7 2.90 2.37 3.09 2.12 2.30 1.47 1.74 1.89 1.31 0.99
9 2.50 2.32 1.84 1.59 1.51 1.60 1.81 1.42 0.94 2.18
10 1.82 1.42 1.61 1.33 1.15 1.25 1.66 1.35 1.03 1.53 TABLE V
Radionuclidic purity of eluate
Definitive test detector: Ge(Li)/Nuclear Data System 4410 analyzer and ND 812 minicomputer 1st eluates 10th eluates gen. no 131 InCi/mCi Tc 103Ru nCi/mCi Tc 99Mo nCi/mCi Tc 131InCi/mCi Tc 103Ru nCi/mCi Tc 99Mo nCi/mCi Tc 1 not detectable not detectable not detectable 3 " " " 4 " " " 5 not detectable not detectable 0.29 " " " 6 " " 3.70 " " " 7 " " 1.71 " " " 9 0.005 " 1.27 " " " 10 0.004 " not detectable " " "
Sterility - sterile
Apyrogenicity - pyrogen-free
Claims (20)
1. A method of preparing a liquid for a radiopharmaceutical application comprising a radioisotope, by eluting from a parent isotope, which is adsorbed on an adsorbent, a radioactive daughter isotope by means of a physiological solution, wherein a fission-produced parent isotope is used and the eluate containing a daughter isotope is purified with a cation-exchange material.
2. A method as claimed in claim 1, wherein molybdenum-99 is used as a parent isotope.
3. A method as claimed in claim 1 or 2, wherein aluminium oxide which contains fully or partly hydrated
manganese dioxide is used as an adsorbent for the parent isotope.
4. A method as claimed in any one of the preceding claims, wherein a cation-exchange resin is used as a cation-exchange material.
5. A method as claimed in claim 4, wherein a strongly acid cation-exchange resin which has been
neutralised is used as a resin.
6. A method as claimed in claim 5, wherein a strongly acid cation-exchange resin which has been converted into a Na+, K+ or NH4+ form is used as a resin.
7. A method as claimed in any one of the claims 4 to 6, wherein a cation-exchange resin is used having a
particle size of 50-400 mesh.
8. A method as claimed in claim 7, wherein the resin particle size is 100 -200 mesh.
9. An isotope generator system suitable for use of the method as claimed in any one of the preceding claims, which generator system comprises a reservoir which has a supply facility for the eluent and an outlet facility for the eluate, and in which the adsorption agent for the parent isotope is present, and wherein the parent isotope is a fission-produced isotope which is fully or substantially carrier-free and that a cation-exchange material is present in the generator system.
10. A generator system as claimed in claim 9, in which the adsorbent for the parent isotope in the reservoir is enclosed between two filters and on that side of the reservoir where during the loading of the adsorbent the solution of the parent isotope is admitted, the filter consists of sintered glass.
11. A generator system as claimed in claim 9 or 10, wherein the cation-exchange material is present in the same reservoir as the eluent for the parent isotope.
12. A generator system as claimed in claim 11, wherein the reservoir is divided into two compartments which are separated from each other by a filter the circumference of which adjoins the inner wall of the reservoir, in which in one compartment which comprises a supply facility for the eluentthe adsorbent for the parent isotope is present between supply facility and separation filter, the adsorbent being enclosed between a sintered glass filter and the separation filter, and in which in the other compartment, which comprises an outlet facility for the eluate, the cation-exchange material is present between separation filter and outlet facility, the space between the adsorbent particles and between the particles of the ion exchanger being filled with a physiological solution.
13. A generator system as claimed in claim 12, wherein the separation filter consists of two disks covering each other entirely or substantially entirely, the disk adjoining the adsorbent consisting of glass fibre paper and the disk adjoining the ion exchanger consisting of porous polyethylene.
14. A reservoir for a generator system as claimed in claim 10, which reservoir comprises two filters between which the adsorbent for the parent isotope is enclosed, and wherein, on that side of the reservoir where during the loading of the adsorbent the solution of the parent isotope is admitted, the filter consists of sintered glass.
15. A reservoir for a generator system as claimed in claim 11, wherein the reservoir comprises both an adsorbent for the parent isotope and a cation-exchange material.
16. A reservoir for a generator system as claimed in claim 12 or 13, wherein the reservoir is divided into two compartments which are separated from each other by a filter the circumference of which adjoins the inner wall of the reservoir, in which in one compartment which comprises a supply facility for the eluent, the adsorbent for the parent isotope is present between supply facility and separation filter, the adsorbent being enclosed between a sintered glass filter and the separation filter, and in which in the other compartment, which comprises an outlet facility for the eluate, the cation-exchange material is present between separation filter and outlet facility, the space between the adsorbent particles and between the particles of the ion exchanger being filled with a physiological solution.
17. A reservoir for a radio isotope generator, which reservoir comprises two filters between which the adsorbent for the parent isotope is enclosed, and wherein on that side of the reservoir where during the loading of the adsorbent the solution of the parent isotope is admitted, the filter consists of sintered glass.
18. A method of preparing a liquid for a radiopharmaceutical application according to claim 1 substantially as described herein with reference to the examples.
19. An isotope generator system according to claim 9 substantially as described herein.
20. A reservoir for a radio isotope generator substantially as described herein with reference to the accompanying drawing.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL8000125A NL8000125A (en) | 1980-01-09 | 1980-01-09 | PROCESS FOR PREPARING A RADIOISOTOPIC LIQUID FOR RADIOPHARMACEUTICAL USE AND ISOTOPE GENERATOR SUITABLE FOR PREPARING THIS LIQUID |
Publications (2)
Publication Number | Publication Date |
---|---|
GB2067343A true GB2067343A (en) | 1981-07-22 |
GB2067343B GB2067343B (en) | 1984-09-19 |
Family
ID=19834646
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8100647A Expired GB2067343B (en) | 1980-01-09 | 1981-01-09 | Generation of radio-isotopes |
Country Status (16)
Country | Link |
---|---|
JP (1) | JPS56104250A (en) |
AT (1) | AT374035B (en) |
AU (1) | AU535382B2 (en) |
BE (1) | BE887034A (en) |
BR (1) | BR8100111A (en) |
CA (1) | CA1185898A (en) |
CH (1) | CH661215A5 (en) |
DE (1) | DE3100365A1 (en) |
DK (1) | DK154370C (en) |
ES (1) | ES498419A0 (en) |
FR (1) | FR2473722B1 (en) |
GB (1) | GB2067343B (en) |
IT (1) | IT1143258B (en) |
NL (1) | NL8000125A (en) |
SE (2) | SE8100108L (en) |
YU (2) | YU41756B (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2155914A (en) * | 1984-02-24 | 1985-10-02 | Atomic Energy Of Australia | Treatment of technetium containing solns |
WO1994007247A1 (en) * | 1992-09-24 | 1994-03-31 | Kernforschungszentrum Karlsruhe Gmbh | Method of separating fission molybdenum |
WO2004000462A2 (en) * | 2002-06-19 | 2003-12-31 | Lynntech, Inc. | Generator for 188re |
WO2006056395A2 (en) * | 2004-11-26 | 2006-06-01 | Johannes Gutenberg-Universität Mainz | Method and device for isolating a chemically and radiochemically cleaned 68ga-radio nuclide and for marking a marking precursor with the 68ga-radio nuclide |
EP1786478A2 (en) * | 2004-08-30 | 2007-05-23 | Bracco Diagnostic Inc. | Improved containers for pharmaceuticals, particularly for use in radioisotope generators |
US7329400B2 (en) | 2002-06-19 | 2008-02-12 | Lynntech, Inc. | Generator for rhenium-188 |
DE102006058542A1 (en) * | 2006-12-12 | 2008-06-19 | Isotopen Technologien München AG | Column system for producing a solution with high specific activity |
EP2375421A3 (en) * | 2010-04-07 | 2012-06-20 | GE-Hitachi Nuclear Energy Americas LLC | Column geometry to maximize elution efficiencies for molybdenum-99 |
RU2525127C1 (en) * | 2012-12-27 | 2014-08-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Московский государственный машиностроительный университет (МАМИ)" | Method for sorption extraction of molybdenum |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT505410B1 (en) | 2007-08-07 | 2009-01-15 | Frauscher Josef | PISTON MACHINE |
US8699651B2 (en) * | 2009-04-15 | 2014-04-15 | Ge-Hitachi Nuclear Energy Americas Llc | Method and system for simultaneous irradiation and elution capsule |
DE102009049108B4 (en) * | 2009-10-12 | 2016-12-08 | Johannes Gutenberg-Universität Mainz | Method and apparatus for obtaining a radionuclide |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL7008953A (en) * | 1969-06-20 | 1970-12-22 | ||
US3749556A (en) * | 1971-08-19 | 1973-07-31 | Medi Physics Inc | Radiopharmaceutical generator kit |
US3902849A (en) * | 1971-08-19 | 1975-09-02 | Medi Physics Inc | Radioisotope and radiopharmaceutical generators |
NL165872C (en) * | 1973-02-20 | 1981-05-15 | Byk Mallinckrodt Cil Bv | ISOTOPE GENERATOR FOR THE PRODUCTION OF LIQUIDS CONTAINING 99M TC. |
US4001387A (en) * | 1973-07-30 | 1977-01-04 | Medi-Physics, Inc. | Process for preparing radiopharmaceuticals |
GB1531985A (en) * | 1975-03-06 | 1978-11-15 | Radiochemical Centre Ltd | Technetium-99m |
US4280053A (en) * | 1977-06-10 | 1981-07-21 | Australian Atomic Energy Commission | Technetium-99m generators |
US4401646A (en) * | 1981-05-08 | 1983-08-30 | University Patents Inc. | Method and apparatus for purifying materials radiolabeled with technetium-99m |
-
1980
- 1980-01-09 NL NL8000125A patent/NL8000125A/en not_active Application Discontinuation
-
1981
- 1981-01-08 BR BR8100111A patent/BR8100111A/en unknown
- 1981-01-08 DE DE19813100365 patent/DE3100365A1/en active Granted
- 1981-01-09 YU YU34/81A patent/YU41756B/en unknown
- 1981-01-09 CA CA000368191A patent/CA1185898A/en not_active Expired
- 1981-01-09 AT AT0005581A patent/AT374035B/en not_active IP Right Cessation
- 1981-01-09 GB GB8100647A patent/GB2067343B/en not_active Expired
- 1981-01-09 DK DK009781A patent/DK154370C/en not_active IP Right Cessation
- 1981-01-09 SE SE8100108A patent/SE8100108L/en not_active Application Discontinuation
- 1981-01-09 IT IT67014/81A patent/IT1143258B/en active
- 1981-01-09 BE BE0/203455A patent/BE887034A/en not_active IP Right Cessation
- 1981-01-09 JP JP254681A patent/JPS56104250A/en active Granted
- 1981-01-09 ES ES498419A patent/ES498419A0/en active Granted
- 1981-01-09 FR FR8100335A patent/FR2473722B1/en not_active Expired
- 1981-01-09 CH CH137/81A patent/CH661215A5/en not_active IP Right Cessation
- 1981-01-09 AU AU66116/81A patent/AU535382B2/en not_active Ceased
-
1983
- 1983-05-30 YU YU01196/83A patent/YU119683A/en unknown
-
1988
- 1988-01-18 SE SE8800142A patent/SE8800142D0/en not_active Application Discontinuation
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2155914A (en) * | 1984-02-24 | 1985-10-02 | Atomic Energy Of Australia | Treatment of technetium containing solns |
US4738834A (en) * | 1984-02-24 | 1988-04-19 | Australia Nuclear Science & Technology Organization | Treatment of technetium containing solutions |
WO1994007247A1 (en) * | 1992-09-24 | 1994-03-31 | Kernforschungszentrum Karlsruhe Gmbh | Method of separating fission molybdenum |
US5508010A (en) * | 1992-09-24 | 1996-04-16 | Forschungszenlrum Karlsruhe Gmbh | Method of separating fission molybdenum |
WO2004000462A2 (en) * | 2002-06-19 | 2003-12-31 | Lynntech, Inc. | Generator for 188re |
WO2004000462A3 (en) * | 2002-06-19 | 2004-03-04 | Lynntech Inc | Generator for 188re |
US7329400B2 (en) | 2002-06-19 | 2008-02-12 | Lynntech, Inc. | Generator for rhenium-188 |
EP1786478A2 (en) * | 2004-08-30 | 2007-05-23 | Bracco Diagnostic Inc. | Improved containers for pharmaceuticals, particularly for use in radioisotope generators |
EP1786478A4 (en) * | 2004-08-30 | 2009-03-11 | Bracco Diagnostics Inc | Improved containers for pharmaceuticals, particularly for use in radioisotope generators |
EP2295143A3 (en) * | 2004-08-30 | 2011-06-29 | Bracco Diagnostic Inc. | Improved Containers for Pharmaceuticals, Particularly for Use in Radioisotope Generators |
US8058632B2 (en) | 2004-08-30 | 2011-11-15 | Bracco Diagnostics, Inc. | Containers for pharmaceuticals, particularly for use in radioisotope generators |
US9562640B2 (en) | 2004-08-30 | 2017-02-07 | Bracco Diagnostics Inc. | Containers for pharmaceuticals, particularly for use in radioisotope generators |
WO2006056395A3 (en) * | 2004-11-26 | 2007-01-25 | Univ Mainz Johannes Gutenberg | Method and device for isolating a chemically and radiochemically cleaned 68ga-radio nuclide and for marking a marking precursor with the 68ga-radio nuclide |
WO2006056395A2 (en) * | 2004-11-26 | 2006-06-01 | Johannes Gutenberg-Universität Mainz | Method and device for isolating a chemically and radiochemically cleaned 68ga-radio nuclide and for marking a marking precursor with the 68ga-radio nuclide |
US8147804B2 (en) | 2004-11-26 | 2012-04-03 | Johannes Gutenberg-Universität Mainz | Method and device for isolating a chemically and radiochemically cleaned 68Ga-radionuclide and for marking a marking precursor with the 68Ga-radionuclide |
DE102006058542A1 (en) * | 2006-12-12 | 2008-06-19 | Isotopen Technologien München AG | Column system for producing a solution with high specific activity |
EP2375421A3 (en) * | 2010-04-07 | 2012-06-20 | GE-Hitachi Nuclear Energy Americas LLC | Column geometry to maximize elution efficiencies for molybdenum-99 |
RU2525127C1 (en) * | 2012-12-27 | 2014-08-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Московский государственный машиностроительный университет (МАМИ)" | Method for sorption extraction of molybdenum |
Also Published As
Publication number | Publication date |
---|---|
YU41756B (en) | 1987-12-31 |
AT374035B (en) | 1984-03-12 |
FR2473722B1 (en) | 1985-08-16 |
JPS56104250A (en) | 1981-08-19 |
DK154370B (en) | 1988-11-07 |
SE8800142L (en) | 1988-01-18 |
YU3481A (en) | 1983-10-31 |
AU535382B2 (en) | 1984-03-15 |
DK9781A (en) | 1981-07-10 |
AU6611681A (en) | 1982-07-15 |
ES8204212A1 (en) | 1982-04-16 |
BE887034A (en) | 1981-05-04 |
ES498419A0 (en) | 1982-04-16 |
ATA5581A (en) | 1983-07-15 |
JPH0119102B2 (en) | 1989-04-10 |
SE8100108L (en) | 1981-07-10 |
BR8100111A (en) | 1981-07-21 |
YU119683A (en) | 1985-04-30 |
DE3100365A1 (en) | 1981-12-17 |
DK154370C (en) | 1989-04-10 |
DE3100365C2 (en) | 1990-10-31 |
CA1185898A (en) | 1985-04-23 |
FR2473722A1 (en) | 1981-07-17 |
SE8800142D0 (en) | 1988-01-18 |
GB2067343B (en) | 1984-09-19 |
IT1143258B (en) | 1986-10-22 |
IT8167014A0 (en) | 1981-01-09 |
CH661215A5 (en) | 1987-07-15 |
NL8000125A (en) | 1981-08-03 |
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