Methods for multi-dose synthesis of [F-18]FDDNP for clinical settings

Abstract

A method of manufacturing 2-(1-{6-[(2-[F-18]fluoroethyl)(methyl)amino]-2-naphthyl}ethylidene)-malononitrile ([F-18]FDDNP) utilizes a semi-automated module that is used to perform fluorination, pre-purification, separation, product extraction, and formulation. The method is able to produce [F-18]FDDNP with high yields and ready for human administration under existing FDA regulations, and without the need for hazardous organic solvents such as dichloromethane (DCM), methanol (MeOH), and tetrahydrofuran (THF). The method also improves the speed with which [F-18]FDDNP can be synthesized with the method being able to generate a final product within about 90 to 100 minutes. This synthesis method is easily adaptable to FDA registered and approved automated synthesis systems.

Claims

1. A method of manufacturing 2-(1-{6-[(2-[F-18]fluoroethyl)(methyl)amino]-2-naphthyl}ethylidene)-malononitrile ([F-18]FDDNP) comprising: trapping [F-18]fluoride ion in a resin cartridge; eluting the [F-18]fluoride ion into a reaction vessel having a cryptand solution contained therein by passing a potassium salt solution followed by water through the resin cartridge, wherein a [F-18]fluoride/cryptand complex is formed therein; subjecting the [F-18]fluoride/cryptand complex to multiple rounds of azeotropic evaporation with anhydrous acetonitrile to form dried [F-18]fluoride ion/cryptand complex residue in the reaction vessel; reacting the dried [F-18]fluoride ion/cryptand complex with tosyloxy precursor 2-{[6-(2,2-dicyano-1-methylvinyl)-2-naphthyl](methyl)amino}ethyl-4-methylbenzenesulfonate (DDNPTs) in anhydrous acetonitrile to form a reaction product; passing the reaction product through an alumina cartridge and into an injection vessel; injecting the reaction product contained in the injection vessel to an HPLC column; collecting a fraction containing [F-18]FDDNP from the HPLC column in a dilution vessel; diluting the collected [F-18]FDDNP contained in the dilution vessel with water; passing the diluted [F-18]FDDNP through a solid-phase extraction cartridge and eluting [F-18]FDDNP with ethanol; and diluting the [F-18]FDDNP contained in ethanol with saline and human serum albumin to form a final product.

2. The method of claim 1, further comprising transferring the final product into a sterile vial.

3. The method of claim 2, wherein the final product is filtered with a filter during transfer to the sterile vial.

4. The method of claim 3, further comprising rinsing final product residue through the filter with saline and human serum albumin into the sterile vial.

5. The method of claim 2, wherein the [F-18]FDDNP in the sterile vial has a radiochemical yield of greater than 35%.

6. The method of claim 2, wherein the [F-18]FDDNP in the sterile vial is produced in more than 400 mCi (corrected to EOB) amounts with a radiochemical yield of greater than 35% with one Ci of F-18 fluoride as starting cyclotron produced activity.

7. The method of claim 1, wherein passing the reaction product directly through the alumina cartridge and into an injection vessel further comprises rinsing the reaction vessel with anhydrous acetonitrile and flowing the rinse through the alumina cartridge.

8. The method of claim 1, further comprising adding chilled ammonium acetate (NH.sub.4OAc)/L-ascorbic acid to the injection vessel after passing the reaction product through an alumina cartridge and into an injection vessel.

9. The method of claim 1, wherein the HPLC column is prepared with MeCN/ammonium acetate (NH.sub.4OAc) and L-ascorbic acid.

10. The method of claim 1, wherein the final product is produced in less than 120 minutes.

11. The method of claim 1, wherein the final product is produced in about 100 minutes or less.

12. The method of claim 1, wherein the [F-18]FDDNP is produced using an automated synthesizer.

13. The method of claim 1, wherein the [F-18]FDDNP is produced using at least some manual operations.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 schematically illustrates the reaction that is used to produce [F-18]FDDNP.

(2) FIGS. 2A-2B illustrate a schematic diagram of the semi-automated synthesis module used for the synthesis of [F-18]FDDNP; including unit operations performed by various components of the module.

(3) FIG. 3A illustrates the radiation trace illustrating the elution of [F-18]FDDNP from a separate analytical HPLC column. Note that the elution of [F-18]FDDNP is done using a quality control setup that utilizes a different HPLC column as well as different mobile phase conditions which causes the elution at around 9.5 minutes which is much sooner than the elution time through the semi-preparative HPLC column.

(4) FIG. 3B illustrates the ultra-violet (UV) light absorption trace illustrating the elution of [F-18]FDDNP from the HPLC column of FIG. 3A.

DETAILED DESCRIPTION OF ILLUSTRATED EMBODIMENTS

(5) FIG. 1 illustrates the radiochemical reaction that leads to the production of the biomarker or PET tracer 2-(1-{6-[(2-[F-18]Fluoroethyl)(methyl)amino]-2-naphthyl)}ethylidene)malononitrile ([F-18]FDDNP) from the tosyloxy precursor 2-{[6-(2,2-dicyano-1-methylvinyl)-2-naphthyl](methyl)amino}ethyl-4-methylbenzenesulfonate (DDNPTs). Subsequent to preparation or synthesis, the PET tracer [F-18]FDDNP is purified by semi-preparative High Performance Liquid Chromatography (HPLC). FIGS. 2A-2B illustrate a schematic diagram of the semi-automated module 10 used for the preparation of [F-18]FDDNP. The semi-automated module 10 is setup in a hot cell that is found in a cyclotron or other radiochemistry laboratory. The hot cell is a dedicated enclosure that is used for the handling of radioactive materials. The hot cell is exhausted and radiation shielded enclosures that prevent the technician or operator from exposure to radiation from gamma ray emitters. Various types of concrete, lead, lead glass, steel, and depleted uranium can be used for shielding materials.

(6) As explained herein, some components of the semi-automated module 10 may be located outside the hot cell. These may include the dose calibrator readout 12, heater controller 14, HPLC pump 18, HPLC solvent reservoir 19, and strip chart recorder or plotter 20, as well as input lines or tubing that are used to delivery various reagents and solvents to the module 10. The heating bath 22, valves (V1-V5), HPLC injector 24, detectors 26, 28, stirring machine 30 are remotely controlled via power switches (not illustrated) located outside the hot cell.

(7) As seen in FIGS. 2A-2B, the semi-automated module 10 has five (5) functional units (i.e., identified as UNITS 1-5), with each unit performing one of the five steps of the radiosynthesis (fluorination, pre-purification, separation, product extraction, formulation). It should be appreciated that UNITS 1-5 are not physically separate units; a single semi-automated module 10 is used for the synthesis. The UNITS 1-5 that are described herein are referred to as individual units that each performs different operations or processes in the synthesis and final formulation yet are part of a single overall module 10. The individual components of the units are connected to one another via tubing or lines (e.g., Polytetrafluoroethylene (PTFE) or Teflon tubing) and the terminals of the tubing may be fitted with male or female Luer tips for connection with stopcocks/syringes. During the operation, reagents and solvents are added to the system remotely via tubing or lines (e.g., Line 1-Line 10 as seen in FIGS. 2A and 2B) by application of either vacuum or positive pressure from outside of the hot cell, using a 60 mL syringe, nitrogen gas (for applying positive pressure), or other source of vacuum.

(8) Described below are the individual units and their construction and function.

(9) UNIT-1 Fluorination unit: This unit includes an automated pinch valve (V1) with a loop or flow path that is used for delivering [F-18]fluoride ion to a resin cartridge 42 for subsequent elution. In one embodiment, the resin cartridge 42 is an anion exchange resin cartridge that is prepared to isolate [F-18]fluoride ion from proton irradiated [O-18]water in order to conserve the [O-18]water and reduce the amount of water that needs to be evaporated during the synthesis. In one embodiment the resin cartridge 42 is custom made by loading 0.125 inch (inner diameter), 0.160 inch (outer diameter) PTFE tubing with BioRad MP-1 resin (catalog #1411851 available from BioRad, Hercules, Calif.). The BioRad MP-1 resin is a macroporous strong anion exchange resin that uses a matrix of styrene divinylbenzene. The functional group is RCH.sub.2N.sup.+(CH.sub.3).sub.3. The BioRad MP-1 resin is packed into the tubing using either gravity settling or pulling the resin in the tube with vacuum. The resin is retained in the tubing using a pair of frits (made from 70 m pore polyethylene frit material) that are formed with a inch hole punch. The frits secure the resin material inside the tube and permit the passage of fluid through the resin material. The ends of the tubing may be fitted with Luer fittings to finalize the formation of the resin cartridge 42.

(10) When V1 is off (normally open), the valve V1 pinches or closes the flow path on the right side of the valve V1 in FIG. 2A and allows the target water to flow through resin cartridge 42 (also referred to as cartridge MP-1) where the [F-18]fluoride ion is loaded onto the resin contained in the resin cartridge 42 while the [O-18]water proceeds to the collection vial 34. When V1 is on, the valve V1 pinches or closes the flow path on the left side of the valve V1, whereby a potassium carbonate (or other potassium salt) solution can be flowed through the resin cartridge 42 to elute the [F-18]fluoride ion to the reaction vessel 44.

(11) The anion exchange resin cartridge 42 (e.g., MP-1 cartridge) that is located in the flow loop associated with valve V1 is for trapping [F-18]fluoride ion from the cyclotron irradiated target water. The cartridge 42 traps [F-18]fluoride ion and lets the [O-18]water pass through in order to be recovered in a 30 mL glass vial 34. A dose calibrator 45 (Model CRC-15R, Capintec, Inc., Florham, N.J.) is used for measuring the radioactivity trapped in the resin cartridge 42. The dose calibrator 45 is a well that is located in the hot cell and holds the valve V1 and the resin cartridge 42. The radioactivity is read by pressing the F-18 key on the instrument readout unit 12 that is coupled the dose calibrator sensor 45. The [F-18]fluoride ion that is trapped on the resin cartridge 42 is released by the addition of 0.4 mL of 0.25% potassium carbonate solution in water (other potassium salts may also be used), which is added via line 1 (made from PTFE), and collected in the fluorination reaction vessel 44 via the delivery line 46 (also made from PTFE). A heating oil bath 22 sits on a motorized jack platform (not shown) that permits the bath to selectively contact with reaction vessel 44. The glass fluorination reaction vessel 44 is positioned above the bath 22 with a silicon stopper 48 carrying three PTFE tubes (tube 46, line 2, and tube 50) to the reaction vessel 44. Line 2 is used for the addition of acetonitrile for the azeotropic drying of the aqueous [F-18]fluoride ion. Line 2 is also used to add the cryptand solution (e.g., Kryptofix/MeCN solution) as well as the precursor reagent that contains DDNPTs to the reaction vessel 44 that contains the dried [F-18]fluoride ion/cryptand complex residue. During the evaporation of acetonitrile from the fluorination reaction vessel 44, a gentle gas bubbling is enabled by connecting a source of nitrogen to the PTFE line 3 in UNIT 2 which transfers nitrogen via tube 50.

(12) UNIT-2 Alumina Sep-Pak pre-purification unit: The fluorination reaction mixture from UNIT-1 is transferred to a glass syringe barrel 52 (3 mL) coupled to an alumina-containing cartridge 54 (Sep-Pak Alumina N Plus Light Cartridge, product number WAT023561 Waters Corporation, Milford Mass.) by applying vacuum through line 3 which draws the reaction mixture from reaction vessel 44 to the glass syringe barrel 52 via PTFE tube 50. The alumina cartridge 54 is connected to the HPLC injection vessel 56 via PTFE tubing 58. Fluid passage through the alumina cartridge 54 is achieved by application of positive pressure (e.g., of nitrogen) through line 3 into glass syringe barrel 52.

(13) UNIT-3 Semi-preparative HPLC unit: The crude product mixture in the injection vessel 56 is then transferred to an electrically actuated HPLC injector valve 24 via line or tubing 60 that has a 3 mL loop volume by applying vacuum through a connected PTFE line (e.g., line 5). PTFE Line 4 is used for adding aqueous solution to the HPLC injection vessel 56 as seen in UNIT-2. Upon injection of the crude reaction mixture into the HPLC column 62 (Waters Symmetry PrepC18, 7, 7.8300 mm) using HPLC valve 24, the column effluent passes through an UV detector 26 followed by a gamma radioactivity detector 28. The detector signals are recorded with a strip chart recorder 20. The three-way solenoid valve V2 permits one to divert HPLC eluent to either waste 64 or to a collect position whereby the eluent enters tubing 66 for transfer to UNIT-4 (seen in FIG. 2B). Note that for valves V2, V3, and V4, NO stands for normally open. NC stands for normally closed.

(14) UNIT-4 Product extraction unit: The HPLC fraction from UNIT-3 is received in a glass dilution vessel 68 via tubing 66 and is capped with a septum 70 carrying multiple lines. PTFE line 6 is used for dilution of the HPLC fraction with water, a transfer line 72 is used to siphon the content of the vessel 68 through a three-way solenoid valve V3, and line 7 acts as a vent line. The contents of the dilution vessel 68 are magnetically stirred with stirring device 30 and a magnetic stir-bar 74. The stir-bar 74 is placed in the dilution vessel 68 in advance of the preparation to homogenize the liquids contained therein. A cartridge 76 containing a silica-based bonded phase with strong hydrophobicity (Sep-Pak tC18 lcc Vac Cartridge, product number WAT0549 Waters Corporation, Milford Mass.) is connected to an output of solenoid valve V3. The contents of dilution vessel 68 are flushed through the cartridge 76 by applying pressure through line 6 (while line 7 is capped) to trap the drug substance on the cartridge 76 while solvents end up in a waste vial 64 through a three-way solenoid valve V4 via line 78. When the cartridge 76 is rinsed with water via a PTFE tubing line 8, the rinsing also ends up in the waste vial 64. When the radioactive product trapped in the cartridge 76 is released with the addition of ethanol (also input from PTFE tubing line 8), the product passes through the solenoid valve V4 and is collected in a mixing vessel 80 via tubing or line 82. The product in ethanol in the mixing vessel 80 is then diluted with normal saline (total 5.5 mL) and human serum albumin (HSA) (total 4.0 mL) added via PTFE line 9.

(15) UNIT-5 Final drug sterilization unit: The final drug product vial 84 is coupled to a 25 mm sterile filter 86 (for sterilization of the product solution) and a 4 mm sterile filter 88 (for vent) and a sterile needle/sterile syringe 90 is assembled in advance under aseptic conditions in a laminar flow hood. The contents of the mixing vessel 80 from UNIT-4 are transferred through a two-way solenoid valve V5 via line 92 to a glass syringe barrel 96 (10 mL) by applying vacuum through a connected PTFE line 10. After transfer, application of positive pressure through line 10 pushes the product through a check valve 98 and the sterilizing filter 86 into the sterile final drug product vial 84.

(16) In order to setup the semi-automated reaction module the following operations are performed: A) All the vessels, glassware, tubing parts, and valves are cleaned and dried before assembly. B) Regenerate the semi-preparative HPLC column 62 by eluting the column inversely with 180 mL of 80% methanol aqueous solution. C) The hot cell surface area is cleaned with 70% alcohol. D) Turn on the power for the module 10 and other equipment. E) Turn on and set the heater controller 14 for the oil bath 22 (front panel; 40 volt input) for 115 C.; check the oil bath temperature with a digital thermometer. F) After re-equilibrating the HPLC column 62 with 200 mL of the mobile phase, check the semi-prep HPLC system. Measure the pump flow rate by collecting mobile phase via the collection line in a 10 mL gradual cylinder at 5 mL/min for 2 min. Note the pressure at that flow rate, then lower the flow rate to 1 mL/min and switch V2 to waste. G) Rinse the alumina cartridge 54 with 6 mL of anhydrous MeCN with a 6 mL syringe. H) Cool the 0.1 M NH.sub.4OAc/0.02 M L-ascorbic acid solution in refrigerator. I) Activate the MP-1 anion resin cartridge 42 by washing with 12 mL of 1M KHCO.sub.3 solution followed by 212 mL of 18M water. J) Insert the activated MP-1 resin cartridge 42 in the pinch valve (V1) loop and place the fluoride trap into the Capintec well 45. K) Add Kryptofix/MeCN solution (1 mL, plastic syringe) to the reaction vessel 44. L) The product vial 84 with two sterile filters (one for filtration 86 and one for venting 88) is ordered from Cyclotron and assembled by Cyclotron staff in sterile environment. M) Label pre-assembled 30 mL sterile product vial 84 with label 18FDDNP HSA/saline/EtOH and batch number MM-DD-YY. N) Add stirring bar 74 and 9 mL 18 M water into the HPLC fraction dilution vessel 68. O) Assemble the module 10, leaving the ten (10) PTFE tubing terminals hanging out on the door of the hot cell. P) Add 2.5 mL of saline to the open mixing vessel 80 with a 6 mL plastic syringe. Q) Fill the HPLC injection loop 24 with HPLC mobile phase via line 5.

(17) A number of solutions are prepared prior to the reaction process. This includes: (1) Kryptofix/MeCN solution (10 mg/mL); (2) KHCO.sub.3 solution (1M); (3) K.sub.2CO.sub.3 solution (0.25% weight: volume basis); (4) NH.sub.4OAc/L-ascorbic acid solution (0.1 M/0.02 M); (5) HPLC mobile phase (MeCN/0.1 M NH.sub.4OAc+0.02 M L-ascorbic acid).

(18) [F-18]Fluorination Reaction:

(19) (1) Delivery of [F-18]fluoride ion solution (typically 1 to 5 Ci based on cyclotron production capabilities) to the reaction vessel 44: a. Note down the radioactivity (& time) of [F-18]fluoride ion trapped on anion resin cartridge 42 using readout 12. b. Turn on valve V1 (depress the electrical switch on the hot cell panel). c. Release the [F-18]fluoride ion to the reaction vessel 44, pre-loaded with 1 mL of Kryptofix solution, by passing 0.4 mL of 0.25% K.sub.2CO.sub.3 solution followed by 0.1 mL 18 M water through the resin cartridge via Line 1. d. Turn off V1 (elevate the electrical switch on the hot cell panel). e. Note down the radioactivity (& time) of [F-18]fluoride ion residue in using readout 12. f. Open the side door of the hot cell and quickly remove the F-18 delivery line from the reaction vessel.

(20) (2) Drying [F-18]fluoride/Kryptofix complex: a. Introduce a gentle stream of nitrogen to the [F-18]fluoride ion solution via line 3 by adjusting the nitrogen flow rate with a metering valve. b. Raise the jack that holds to oil bath 22 to immerse the reaction vessel 44 in the oil bath 22 heated to 115 C. c. When the ground glass joint at the top of the reaction vessel 44 appears partially dry (5-6 min), add 0.5 mL of anhydrous acetonitrile via line 2 to the reaction vessel 44 and continue with nitrogen bubbling. d. Repeat twice more the azeotropic evaporation with anhydrous acetonitrile with 0.5 mL each time. At this point, the ground glass joint of the reaction vessel 44 should appear completely dry (15 min in total). e. Decrease the temperature of the oil bath 22 from 115 C. to 93 C. during the last two evaporations of acetonitrile.

(21) (3) [F-18]Fluorination reaction: a. Lower the oil bath 22 and add precursor DDNPTs (2.2-2.5 mg) in anhydrous acetonitrile (0.7 mL) with a 1 mL glass syringe via line 2 to the dried [F-18]fluoride ion/Kryptofix complex residue in reaction vessel. Details regarding the synthesis of DDNPTs may be found in Liu et al., High-Yield, Automated Radiosynthesis of 2-(1-{6-[(2-[18F]Fluoroethyl)(methyl)amino]-2-naphthyl}ethylidene)malononitrile ([18F]FDDNP) Ready for Animal or Human Administration, Molecular Imaging and Biology, Vol. 9, pp. 6-16 (2007), which is incorporated by reference herein.

(22) Mix the contents of reaction vessel by gentle bubbling of nitrogen for a few seconds. b. Elevate the oil bath 22 to heat the reaction mixture at 90-95 C. c. Stop heating of the reaction vessel 44 at fifteen (15) minutes time point by lowering the oil bath 22. d. Cool the reaction mixture by bubbling nitrogen stream for 2 minutes.

(23) Pre-Purification:

(24) (1) Transfer the cooled reaction mixture from the reaction vessel 44 to the syringe barrel 52 by pulling vacuum with a 60 mL plastic syringe via line 3.

(25) (2) Push with air pressure via line 3 the liquid through the alumina Sep-Pak cartridge 54 and into the injection vessel 56.

(26) (3) Add 0.5 mL of anhydrous MeCN to the reaction vessel 44 and repeat steps 1 and 2.

(27) (4) Add another 0.5 mL of anhydrous MeCN to the reaction vessel 44 and repeat steps 1 and 2 again.

(28) HPLC Purification:

(29) (1) Set the HPLC pump 18 flow rate to 5 mL/min during the cooling, e.g. operation in [0046-47] to pump MeCN/0.1M NH.sub.4OAc+0.02M L-ascorbic acid (1:1) as prep HPLC mobile phase.

(30) (2) Add 1.5 mL of ice-cooled/chilled NH.sub.4OAc/L-ascorbic acid (0.1 M/0.02M) solution (use 3 mL plastic syringe) via line 4 to the HPLC injection vessel 56.

(31) (3) Transfer the mixture in the HPLC injection vessel 56 to the loop of HPLC injector 24 via line 60 by applying vacuum through line 5 (withdraw the syringe attached which is also used to fill the injection loop 24 with HPLC mobile phase).

(32) (4) Inject by switching the control box outside the hot cell to injection.

(33) (5) Start the strip chart recorder or plotter 20 and a stopwatch.

(34) (6) Monitor HPLC pump 18 back pressure for potential clogging.

(35) (7) Turn on the stirring device 30 for the dilution vessel 68 containing 9 mL of 18 M water.

(36) (8) Monitor the UV and radioactive traces on the strip chart recorder/plotter 20 and collect the radioactive peak into the dilution vessel 68 (by turning on V2) at 21 min retention time as observed on the strip chart recorder/plotter 20. Stop the collection after 1 minute and 15 second (by turning off V2).

(37) Extraction of Drug Substance from HPLC Fraction:

(38) (1) Continue to stir for another 1 min.

(39) (2) Pass the mixed liquid in the dilution vessel 68 through the cartridge 76 and let the effluent go into the HPLC waste flask 64 by applying pressure via line 6. Plug the vent tubing line 7 with a stopcock, if higher pressure is needed to pass the solution through the cartridge 76.

(40) (3) Turn on V3 and pass 12+8 mL of sterile water (use 12 mL plastic syringe) via line 8 to wash the cartridge 76. Let the eluent go into the waste 64.

(41) (4) Dry the cartridge 76 with a nitrogen stream.

(42) Drug Dose Preparation and Sampling for QC:

(43) (1) Turn on product 3-way valve V4 to collection.

(44) (2) Elute the cartridge 76 with 0.5 mL of EtOH (use 1 mL sterile syringe) via line 8 slowly into the mixing vessel 80 containing 2.5 mL of sterile normal saline.

(45) (3) Gently bubble nitrogen into mixing vessel 80 via line 8.

(46) (4) Stop the bubbling.

(47) (5) Take 100 L of the 16.7% EtOH/saline solution (Sample-1) from vessel 80 for QC.

(48) (6) Add 3 mL of 25% human serum albumin (HSA) via line 9 to the mixing vessel 80 with very gentle bubbling of nitrogen.

(49) (7) Stop nitrogen bubbling, turn on V5 and transfer the HSA/EtOH/saline solution by applying vacuum via line 10 to the HSA Syringe barrel 96.

(50) (8) Turn off V5 and apply pressure via line 10 to push the product through the sterile filter 86 into the sterile product vial 84.

(51) (9) Add another 1 mL of 25% human serum albumin and 3 mL of sterile normal saline via line 9 to the residue in mixing vessel 80.

(52) (10) Turn on V5 and transfer the rinsing HSA by applying vacuum via line 10 to the syringe barrel 96.

(53) (11) Turn off V5 and apply pressure via line 10 to transfer HSA through the sterile filter 86 into the product vial 84.

(54) (12) Check filter integrity.

(55) (13) Take 0.3 mL sample of the drug product (Sample-2) for bacterial endotoxin and sterility QC tests

(56) Power Down

(57) (1) Turn off the power for the whole module 10 inside the hot cell. Turn off the HPLC pump 18 around 25 min time point. Turn off the power strip 20 for the instruments outside of the hot cell.

(58) The radiochemical yield (%) that is produced using this method is high; generally above 35% as seen below in Table 1. The radiochemical yield is calculated from the radioactivity of the product corrected to EOBRadioactivity delivered to the reaction vessel 44 corrected to EOB100.

(59) TABLE-US-00001 TABLE 1 Typical radiochemical yields of finally formulated [F-18]FDDNP with the method described herein Radiochemical Starting [F-18].sup. activity [F-18]FDDNP Yield Yield (mCi corrected to EOB) (mCi corrected to EOB) (%) 1138.5 440.9 38.7 1125.3 480.8 42.7 1242.6 457.0 36.8 1078.7 426.6 39.5 1133.4 529.1 46.7 1016.6 440.4 43.3 1160.6 486.3 41.2 EOB = End of bombardment for the cyclotron production of [F-18]fluoride ion.

(60) FIG. 3A illustrates the radiation trace illustrating the elution of [F-18]FDDNP from a separate analytical HPLC column. Note that the elution of [F-18]FDDNP is done using a quality control setup using a different HPLC column (i.e., an analytical column) as well as different mobile phase conditions which causes the elution at around 9.5 minutes. FIG. 3B illustrates the ultra-violet (UV) light absorption trace illustrating the elution of [F-18]FDDNP from the HPLC column of FIG. 3A. For quality control purposes, radio thin layer chromatography (TLC) and gas chromatography tests may also be performed.

(61) There are several important advantages of the method of manufacturing [F-18]FDDNP disclosed herein. First, the method does not incorporate a combination of hazardous organic solvents. Prior methods of synthesis required the use of dichloromethane (DCM), methanol (MeOH), and tetrahydrofuran (THF). See e.g., Liu et al. (2007), discussed supra. These organic solvents are classified as FDA Class 2 solvents and, under current FDA regulations and guidance, should be limited in pharmaceutical products because of their inherent toxicity. For example, the FDA has issued guidance for industry Q3C Impurities: Residual Solvents, which makes recommendations as to what amounts of residual solvent are considered safe in pharmaceuticals. See Q3C Tables and List Guidance for Industry, U.S. Department of Health and Human Services, Food and Drug Administration, Revision 3, June 2017, which is incorporated by reference herein. Solvents such as DCM and THF are not desirable to include in pharmaceutical products. For example, DCM is a known carcinogen. THF is a peroxide forming compound that is a known irritant to body tissues. Thus, in one embodiment, the manufacturing process is substantially free of organic solvents such as DCM, MeOH, or THF. The final product as described is ready for human administration under existing FDA regulations and guidance since the final product contains only a trace amount of acetonitrile (0-50 ppm) which is well below FDA established guideline limits (410 ppm). While the final product may contain some ethanol, the amount of ethanol is diluted for human administration to bring the concentration well below FDA guideline limits. Another benefit of the current method of manufacturing is the final product can be produced in less elapsed time (e.g., 100 minutes total as compared to 120 minutes). This is enabled by using a single alumina cartridge (i.e., Sep-Pak) to substitute for the prior synthesis method that used 1% HCl aqueous solution to quench the reaction followed by C-18 Sep-Pak extraction with an organic solvent and subsequent evaporation of the eluent. See e.g., Liu et al. (2007), discussed supra. Importantly, this is a non-aqueous workup that uses a single alumina cartridge directly after the fluorination reaction for pre-purification. This plays a significant role in reducing the autoradiolysis of [F-18]FDDNP in addition to shortening synthesis time. Thus, the method can produce a final product in less than 120 minutes in some embodiments and, more preferably, produce a final product in 100 minutes or less. For example, in one embodiment, the final product may be produced in about 90 to 100 minutes. This is significant because rapid radioactive decay that begins to occur as soon as the radioactive fluorine isotope is created (the half-life of fluorine-18 is 110 minutes). Another advantage is the high yields that are achieved using the method described herein. Generally, final product yields (when measured at the final, formulated product) range between about 30% to about 40%. However, yields higher than this have been obtained with the highest yields being around 45-46%. The method described herein is highly reliable and can produce up to one hundred (100) 10 mCi batch doses of pure, high specific activity (typically from 1 to 5 Ci/micromole) [F-18]FDDNP biomarker ready for human injection using available biomedical cyclotrons routinely producing up to 5-10 Ci of [F-18]fluoride ion.

(62) While embodiments of the present invention have been shown and described, various modifications may be made without departing from the scope of the present invention. The invention, therefore, should not be limited, except to the following claims, and their equivalents.