Precursor compound of radioactive halogen-labeled organic compound
US-10010632-B2 · Jul 3, 2018 · US
US11077216B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11077216-B2 |
| Application number | US-201515318599-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 30, 2015 |
| Priority date | Jun 30, 2014 |
| Publication date | Aug 3, 2021 |
| Grant date | Aug 3, 2021 |
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The present invention provides a composition comprising anti-1-amino-3- 18 F-fluorocyclobutyl-1-carboxylic acid ( 18 F-FACBC) having an improved impurity profile compared with previous such compositions. Also provided is a method to obtain said composition.
Opening claim text (preview).
The invention claimed is: 1. A method of preparation of a PET tracer composition in a cassette system having an end of synthesis (EOS) radiochemical purity (RCP) of at least 95%, comprising (a) reacting in a reaction vessel of the cassette system a source of 18 F-fluoride with a precursor compound of Formula I: wherein: LG is a leaving group; PG 1 is a carboxy protecting group; and, PG 2 is an amine protecting group; wherein said reacting step is carried out in acetonitrile; to obtain a reaction mixture comprising a compound of Formula II: wherein PG 1 and PG 2 are as defined for Formula I; (b) transferring said reaction mixture comprising said compound of Formula II out of said reaction vessel onto a reversed phase solid phase cartridge of the cassette system and carrying out removal of PG 1 to obtain a reaction mixture comprising a compound of Formula III: wherein PG 1 is as defined for Formula I; (c) applying heat to said reaction vessel to remove residual solvent from the reaction vessel at the same time as carrying out removal of PG 1 on the reversed phase solid phase cartridge; (d) transferring said reaction mixture comprising said compound of Formula III from the reversed phase solid phase cartridge back into said reaction vessel and carrying out removal of PG 2 to obtain a reaction mixture comprising 18 F-FACBC; (e) purifying said reaction mixture comprising 18 F-FACBC by passing it through a hydrophilic lipophilic balanced (HLB) solid phase, wherein said purifying does not comprise passing the reaction mixture comprising 18 F-FACBC through an alumina solid phase, wherein the purified reaction mixture is obtained in steps (c) or (e) with citrate buffer, wherein said composition comprises no more than 5.0 μg/mL dissolved aluminium (Al) and no more than 25 μg/mL acetonitrile (MeCN). 2. The method as defined in claim 1 wherein LG is a linear or branched C 1-10 haloalkyl sulfonic acid substituent, a linear or branched C 1-10 alkyl sulfonic acid substituent, a fluorosulfonic acid substituent, or an aromatic sulfonic acid substituent. 3. The method as defined in claim 2 wherein LG is methanesulfonic acid, toluenesulfonic acid, nitrobenzenesulfonic acid, benzenesulfonic acid, trifluoromethanesulfonic acid, fluorosulfonic acid, or perfluoroalkylsulfonic acid. 4. The method as defined in claim 1 wherein LG is trifluoromethanesulfonic acid. 5. The method as defined in claim 1 wherein PG 1 is a linear or branched C 1-10 alkyl chain or an aryl substituent. 6. The method as defined in claim 5 wherein PG 1 is methyl, ethyl, t-butyl or phenyl. 7. The method as defined in claim 6 wherein PG 1 is methyl or ethyl. 8. The method as defined in claim 7 wherein PG 1 is ethyl. 9. The method as defined in claim 1 wherein PG 2 is a carbamate substituent, an amide substituent, an imide substituent or an amine substituent. 10. The method as defined in claim 9 wherein PG 2 is t-butoxycarbonyl, allyloxycarbonyl, phthalimide, or N-benzylideneamine. 11. The method as defined in claim 10 wherein PG 2 is t-butoxycarbonyl. 12. The method as defined claim 1 which is automated. 13. The method as defined in claim 1 wherein step (c) of applying heat to said reaction vessel is carried out at a temperature of 80° C.-140° C. 14. The method as defined in claim 1 wherein step (c) of applying heat to said reaction vessel is carried out at a temperature of 85° C.-130° C. 15. The method as defined in claim 1 , said composition comprises no more than 20 μg/mL acetonitrile (MeCN). 16. The method as defined in claim 1 , wherein step (c) comprises cooling the heated reaction vessel using nitrogen purging followed by application of vacuum.
Acyclic or carbocyclic compounds · CPC title
with a four-membered ring · CPC title
Organic compounds · CPC title
with the nitrogen atom of at least one of the carbamate groups bound to a carbon atom of a ring other than a six-membered aromatic ring · CPC title
by reactions not involving the formation of carbamate groups · CPC title
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