Not Applicable
1. Field of Invention
This invention relates to a reagent delivery system for use in the production of radiopharmaceuticals for positron emission tomography (PET). More specifically, it relates to a method of multi-batch production of 18F-labeled glucose, known as fluorodeoxyglucose or “FDG.”
2. Description of the Related Art
Positron Emission Tomography is a powerful tool for diagnosing and treatment planning of many diseases wherein radiopharmaceuticals or radionuclides are injected into a patient to diagnose and assess the disease. For example, the radiopharmaceutical 18F-labeled glucose, known as fluorodeoxyglucose or “FDG”, can be used to determine where normal glucose would be used in the brain. FDG is a labeled compound in which a fluorine-18 ion (18F) is substituted for part of the glucose. FDG labeled in this manner is a desirable radiopharmaceutical because the fluorine-18 is a positron emission nuclide with a half-life period of 109.7 minutes.
The production of PET radiopharmaceuticals requires the use of various reagents and solutions to effect the necessary chemical conversions. The reagents and solutions must be delivered to a reaction vessel, where the conversions take place. The deliveries must be accurate, reproducible and, in addition, there must be minimal cross-contamination between the various reagents. A more detailed discussion of this type of delivery system is disclosed in the above-referenced patent application Ser. No. 09/569,780, filed on May 12, 2000.
Generally, the production of FDG includes the steps of bombarding a target material with a particle beam, mixing the target material with other materials, processing the resulting compound in a reaction vessel, and filtering the product. An accelerator produces radioisotopes by accelerating a particle beam and bombarding a target material, housed in a target system, with the particle beam. To produce FDG, the product of bombardment, fluorine-18 ions, is further processed to produce a substance suitable for injection into the human body. These ions are further processed to produce FDG (2-deoxy-2-fluoro-D-glucose) in a process typically referred to as radiosynthesis.
Well known in the art are various methods for producing FDG. For example, U.S. Pat. No. 4,794,178 issued to Coenen at al. on Dec. 27, 1988 discloses a process for labeling organic compounds with fluorine-18 through a nucleophilic substitution reaction. U.S. Pat. No. 5,169,942 issued to Johnson at al. on Dec. 8, 1992 discloses a method for making FDG that uses a phase-transfer reagent U.S. Pat. No. 5,932,178 issued to Yamazaki at al. on Aug. 3, 1999 discloses an FDG synthesizer that uses a labeling reaction resin column. Although these patents disclose various methods of FDG production, none of these patents teach a method that addresses the specific objects and advantages of the present invention.
Fluorine-18 is a radioactive material to which human exposure should be limited. Also, the particle beam striking the target material is a radioactive process, which should also have limited human exposure. Accordingly, the radiation exposure to persons producing the FDG is an important consideration. Toward this end, efforts have been made to automate the production of radioisotopes, in particular, FDG.
Automation of radionuclide and radiochemical syntheses is discussed in a paper entitled “Introduction: State of the Art in Automated Syntheses of Short-lived Radiopharmaceuticals” by Jeanne M. Link, John C. Clark, and Thomas J. Ruth, Targetry '91, pp 174-185. At page 174, the paper discusses the advantages and disadvantages of the various levels of automation, including manual and remote operation, remote automated operation, and robotic operation. Specifically, the paper identifies the advantages of automation as a reduction of radiation exposure and a reduction of time to perform radiosynthesis. Furthermore, at page 183, the paper describes self-cleaning automated FDG systems.
Many commercially available components can be used to automate the production of FDG. Valves, tubing, and fittings are well known in the art and are well suited to this application. So too are membrane filters. Other components are specially designed for the process. See, for example, the reaction vessel disclosed in the above-referenced patent application Ser. No. 09/569,780, filed on May 12, 2000, and the related patent application Ser. No. 09/795,744 filed on Feb. 28, 2001 by Zigler, et al.
Although the prior art systems have proven successful for the production of FDG, there exists a need for further automation, including the capability of producing multiple batches of FDG with minimum operator intervention. Furthermore, to minimize operator intervention, multi-batch capability requires that the apparatus be self-cleaning and include automated testing of components, such as the membrane filters.
Therefore, it is an object of the present invention to provide an apparatus for performing multiple FDG production runs with a single set up.
It is another object of the present invention is to minimize radiation exposure to the apparatus operators.
It is yet another object of the present invention to provide an apparatus that is easy to handle and economic to use.
Another object of the present invention is to provide an apparatus that is self-cleaning.
Still another object of the present invention is to provide an apparatus which includes means for automating the pressure integrity test of the membrane filtration device used in final product sterilization.
According to a preferred embodiment of the present invention, a method for multi-batch production of FDG is disclosed. The method includes the steps of selecting the reagents necessary for producing FDG, transferring said reagents to a reaction chamber, producing FDG, filtering the produced FDG, delivering the FDG to a container, cleaning the production apparatus, and repeating the previous steps to produce multiple batches of FDG.
The above-mentioned features of the invention will become more clearly understood from the following detailed description of the invention read together with the drawings in which:
In the preferred embodiment, the rotary carousel 102 has two concentric rings of holes 202 in which the vials 104 are placed. Five vials 104i fit in the inside ring of holes 202i, and ten vials 104o fit in the outside ring of holes 202o. Vials with tight internal diameter tolerances are commercially available, such as those by Kimble Glass Inc. The vials 104 may be large volume (20 ml) or small volume (10 ml), and are securely mounted in the individual vial holes 202. Also in the inside ring are smaller holes or slots placed between the openings for the vials 104i. The purpose of these smaller holes or slots is to provide a place for the inside needles 112i, 132i to pass when the rotary carousel 102 is positioned so that only one outside vial 104 is being used. The reagent which is the target material is placed in the inside vials 104i.
As illustrated in
The needles 112, 132 provide a gas inlet to the septum-sealed reagent vials 104 and a liquid outlet from the vials 104. In the preferred embodiment, the needles 112, 132 are comprised of separate, concentric needles. In this embodiment, which is shown in
Both needle embodiments deliver liquids with the required accuracy and reproducibility, but the concentric needle embodiment offers several advantages over the parallel needle embodiment. First, the concentric design allows for the use of a smaller gauge needle 112 for liquid delivery. This reduces the effect of sudden pressure changes and thus provides more control during the liquid delivery. Second, the increased structural integrity provided by the larger gas needle 132 dramatically reduces the possibility of bending the liquid needle 112, even when the liquid needle 112 has a blunt tip (a blunt tip affords more accurate liquid deliveries than a slanted needle tip). The added strength eliminates the need for a needle guide or other means to prevent the bending of small gauge needles. Finally, a common problem encountered in repeated punctures of a septum 402 with a needle is “coring,” or the shredding of small pieces of the septum material with the needle annulus. The resulted pieces lodge in the needle and block the flow of gas or liquid. This problem especially holds for larger gauge needles. Since the smaller gauge needle forms a “pilot” hole for the larger gauge needle, the concentric needle design greatly reduces the incidence of septum coring. Thus, the concentric design simultaneously allows the use of a non-bending, small gauge liquid needle 112 (to better control liquid delivery) and a non-coring, large gauge gas needle 132 (to provide structural integrity). A more detailed discussion of the needle configuration is disclosed in a related patent application Ser. No. 09/795,214 filed on Feb. 28, 2001 by Zigler, et al.
The gas (for example, nitrogen, helium, argon, or other non-reactive gas) used to pressurize the reagent vials 104 is delivered to the needles 132 through electronic mass flow controllers 134. The mass flow controllers 134 are commercially available devices that are interfaced to the control system 160 to allow remote gas flow set points and feedback. The mass flow controllers 134 control the gas flow to within less than 1 standard cm3/minute.
The liquid outlet needle 112 is connected to small-bore flexible tubing (for example, 1/16″ outside diameter Teflon or polyethylene tubing) to route the liquid during the transfer process. To ensure the successful transfer of liquid, the reagent delivery system 10 employs liquid sensors 116 that detect the presence of liquid in the tubing and supply this data to the control system 160. The preferred embodiment uses a miniature ultrasonic transmitter and receiver affixed to the outside of the tubing, such as the commercially-available detectors manufactured by Introtek. When liquid is present in the tubing, the receiver generates a signal that is sent to the control system 160.
The liquid sensor 116 allows an operator to fill the reagent vials 104 in the rotary carousel 102 with any volume of liquid, and then perform an “auto-detect” sequence to determine the quantity of liquid in the vials. Thus, a key feature of the reagent delivery system 10 is that the operator does not have to measure the volume of liquid, thereby facilitating the set up process. An important feature of the liquid sensors 116 is that they do not directly contact the liquid, which eliminates the possibility of reagent contamination and detector corrosion.
Electronically controlled valves are used in the reagent delivery system 10 to route the flow of reagents and solvents throughout the automated apparatus for multi-batch production of FDG. Critical valves provide positional feedback to the control system 160 to ensure proper operation. The materials of construction for all the valves, tubing, and fittings are selected to minimize cross-contamination and dead space. These components are commercially available, for example, the valves are readily available through the Hamilton Company.
In the illustrated embodiment, an automatic pressure integrity test, based on the pressure retention method, reduces manual manipulation of the filter assembly 142, thereby reducing radiation exposure to the operator. Referring to
In the preferred embodiment, the control system 160 includes a personal computer communicating with a microcontroller which interfaces with the various components of the reagent delivery system 10. The personal computer is running automation software by Intellution, Inc. Those skilled in the art will recognize that other means for controlling the reagent delivery system may be used without interfering with the objects and advantages of the present invention. For example, a dedicated controller with appropriate software may be used instead of the personal computer and microcontroller.
Referring to
The reagent delivery system 10 uses a simple method to accurately and reproducibly dispense small quantities of reagents from the septum-sealed vials 104. The volume of reagent in the vial 104 may be calculated 812 from the diameter of the vial and the height of the liquid within the vial. For example, if the diameter of a vial 104 is 2 cm and the height of the liquid is 1 cm, then the volume of the liquid is (πr2×h), or 3.14 cm3. Different volumes may be dispensed from the vial 104 by changing the depth of the needle 112 used to remove the liquid.
With this method of liquid dispensing, only two sources of error contribute to variation in the volume of delivered reagent: error in the diameter of the vial 104 and error in the vertical position of the needle 112. The design of the reagent delivery system 10 minimizes the first source of error by specifying commercially-available vials with tight internal diameter tolerances, such as those sold by Kimble Glass Inc. The second source of error is minimized by accurately controlling the needle position with a linear actuator 114.
After the processing equipment 120 has produced a batch of FDG 708, the reagent delivery system 10 uses gas pressure to push the product 710 through the filter assembly 142 and into the final product vial 320. The next step 712 is to verify the integrity of the filter assembly 142. Referring to
Referring to
While a preferred embodiment has been shown and described, it will be understood that it is not intended to limit the disclosure, but rather it is intended to cover all modifications and alternate methods falling within the spirit and the scope of the invention as defined in the appended claims.
This Application is a Divisional of U.S. application Ser. No. 09/795,744, filed Feb. 28, 2001, now abandoned, which is a Continuation-In-Part of U.S. application Ser. No. 09/569,780, filed on May 12, 2000, now U.S. Pat. No. 6,599,484.
Number | Name | Date | Kind |
---|---|---|---|
4736638 | Okawa et al. | Apr 1988 | A |
4794178 | Coenen et al. | Dec 1988 | A |
4872974 | Hirayama et al. | Oct 1989 | A |
5012845 | Averette | May 1991 | A |
5037602 | Dabiri et al. | Aug 1991 | A |
5064529 | Hirayama et al. | Nov 1991 | A |
5169942 | Johnson et al. | Dec 1992 | A |
5280505 | Hughey et al. | Jan 1994 | A |
5282380 | DiLeo et al. | Feb 1994 | A |
5417101 | Weich | May 1995 | A |
5468355 | Shefer et al. | Nov 1995 | A |
5554811 | Rokugawa et al. | Sep 1996 | A |
5573747 | Lacy | Nov 1996 | A |
5594161 | Randhahn et al. | Jan 1997 | A |
5855851 | Matsubara et al. | Jan 1999 | A |
5932178 | Yamazaki et al. | Aug 1999 | A |
6011825 | Welch et al. | Jan 2000 | A |
6143573 | Rao et al. | Nov 2000 | A |
6172207 | Damhaut et al. | Jan 2001 | B1 |
6190617 | Clark et al. | Feb 2001 | B1 |
6241947 | Komatsu et al. | Jun 2001 | B1 |
6372183 | Akong et al. | Apr 2002 | B1 |
6567492 | Kiselev et al. | May 2003 | B2 |
6845137 | Ruth et al. | Jan 2005 | B2 |
Number | Date | Country | |
---|---|---|---|
20040022696 A1 | Feb 2004 | US |
Number | Date | Country | |
---|---|---|---|
Parent | 09795744 | Feb 2001 | US |
Child | 10421324 | US |
Number | Date | Country | |
---|---|---|---|
Parent | 09569780 | May 2000 | US |
Child | 09795744 | US |