Production of actinium-225 for alpha particle mediated radioimmunotherapy

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Abstract

The initial clinical trials for treatment of acute myeloid leukemia have demonstrated the effectiveness of the alpha emitter 213Bi in killing cancer cells. Bismuth-213 is obtained from a radionuclide generator system from decay of 10-days 225Ac parent. Recent pre-clinical studies have also shown the potential application of both 213Bi, and the 225Ac parent radionuclide in a variety of cancer systems and targeted radiotherapy. This paper describes our five years of experience in production of 225Ac in partial support of the on-going clinical trials. A four-step chemical process, consisting of both anion and cation exchange chromatography, is utilized for routine separation of carrier-free 225Ac from a mixture of 228Th, 229Th and 232Th. The separation of Ra and Ac from Th is achieved using the marcoporous anion exchange resin MP1 in 8 M HNO3 media. Two sequential MP1/NO3 columns provide a separation factor of ∼106 for Ra and Ac from Th. The separation of Ac from Ra is accomplished on a low cross-linking cation exchange resin AG50-X4 using 1.2 M HNO3 as eluant. Two sequential AG50/NO3 columns provide a separation factor of ∼102 for Ac from Ra. A 60-day processing schedule has been adopted in order to reduce the processing cost and to provide the highest levels of 225Ac possible. Over an 8-week campaign, a total of ∼100 mCi of 225Ac (∼80% of the theoretical yield) is shipped in 5–6 batches, with the first batch typically consisting of ∼50 mCi. After the initial separation and purification of Ac, the Ra pool is re-processed on a bi-weekly schedule or as needed to provide smaller batches of 225Ac. The averaged radioisotopic purity of the 225Ac was 99.6 ± 0.7% with a 225Ra content of ⩽0.6%, and an average 229Th content of (4−4+5)×10−5%.

Introduction

Radioisotopes which decay with the emission of alpha particles are rapidly becoming of greater interest for short range and site-specific therapy of cancers and micrometastic disease. Within the past five years, the investigation of targeted cancer therapy using alpha-emitters has considerably developed, and recent clinical trials have generated promising results and have attracted an increasing number of researchers and clinicians. The initial clinical trials in patients with acute myeloid leukemia have demonstrated the effectiveness of the alpha emitter 213Bi in killing cancer cells (Jurcic et al., 2002). The 8-MeV alpha particles from 213Bi can penetrate 6–10 nearby cell layers, killing everything in their short path (∼100 μm) including tumor cells. Recent preclinical studies have also demonstrated the potential application of both 213Bi, and the 225Ac parent radionuclide, in a variety of cancer systems and targeted radiotherapy (McDevitt et al., 1999, McDevitt et al., 2001; Behr et al., 1999a, Behr et al., 1999b; Davis et al., 1999; Kennel et al., 1999; Kennel and Mirzadeh, 1998; Deal et al., 1999; Nikula et al., 1999; Chen et al. 1998; Kock et al., 1998; Kaspersen et al., 1995; Geerlings et al., 1993). A comprehensive review of the applications of alpha emitters is beyond the scope of present work and potential readers are referred to two recent review articles (McDevitt et al., 1998; Hassfjell and Brechbiel, 2001). The latter provides a useful account of the development of the bi-functional chelating ligands for the attachments of bismuth and actinium radioisotopes to proteins. Beside 213Bi and 225Ac, the list of potential radionuclides for these applications includes only eight α-emitting radioisotopes, namely 149Tb, 211At, 212Bi, 212Pb, 223Ra, 224Ra, 225Ra, and 255Fm (See for examples, Henriksen et al., 2002; Mirzadeh 1998; Howell et al., 1997).

In addition to the in vitro and in vivo stability of the radiolabeled biomolecules, there are a number of other factors that must be considered for potential clinical use of any radioisotope. These factors include availability, cost, nuclear characteristics, and chemical properties. This paper focuses on the availability and describes our five years of experience in production of 225Ac in partial support of the on-going clinical trials at the Sloan Kettering Memorial Cancer Center (SKMCC), where 213Bi is generated in-house from the decay of 225Ac in a generator system (Ma et al., 2001; Bray et al., 2000; Mirzadeh, 1998; Wu et al., 1997; Boll et al., 1997a).

Actinium-225 is currently obtained from the decay of 7340-years 229Th, through one intermediate radionuclide, 15-days 225Ra (Fig. 1) (Apostolidis et al., 2001; Boll et al., 1997a, Boll et al., 1997b; Khalkin et al., 1997). After the initial separation of 225Ra and 225Ac from 229Th, a stock of purified 225Ra further provides a continuous but, of course, declining (with a 15 day half life) supply of 225Ac over a 45-day period. While the bulk of 225Ac, freshly separated from 229Th (up to 50 mCi), have been typically provided to SKMCC, smaller batches of 225Ac (20 mCi and less) from the decay of 225Ra has been supplied to a number of research institutes and universities throughout the US, as well as Europe and Australia.

Thorium-229 originates from 233U as the first alpha decay daughter, and both nuclides are members of the extinct Neptunium series (Fig. 1, Friedlander et al., 1981). Uranium-233, which has a fission characteristic similar to that of 235U, was produced as part of the US molten salt breeder reactor research program and is currently stored at ORNL. Irradiation of a natural thorium target in a nuclear reactor simply transmutes a non-fissile target to a fissile product; the neutron capture product of 232Th is short-lived 233Th, which beta decays quickly to 233Pa, then to 233U by the 232Th[n,γ]233Th(β-, t1/2=22.3min)233Pa(β-, t1/2=27days)233U reaction. Although 233U is presently the only viable source for high purity 229Th, the anticipated growth in demand for 225Ac may soon exceed the levels of 229Th present in the aged 233U stockpile. It is estimated that only ∼37 g or ∼8 Ci of 229Th (the theoretical specific activity of 229Th is 0.213 Ci/g based on a 7340 years half life) can be extracted from the entire ORNL 233U stockpile. This is about 50 times the current recovered ORNL 229Th stock. Considering the rather low annual in-growth production rate of 229Th from 233U and the increasing difficulties associated with 233U safeguards, routine processing of 233U is not presently feasible. Other means of production are being considered in order to meet the future demand for 225Ac and 213Bi (Garland and Mirzadeh, 2003; Apostolidis et al., 2001; Mirzadeh, 1998).

The current ORNL 229Th supply is about 150 mCi. During the 1995–1996 period, ∼90 mCi of 229Th (batch “Th–W”) was extracted from the pre-existing waste material which was stored at ORNL for about 35 years. In the past three years, ∼60 mCi of 229Th (batch “Th–U”) has also been recovered from chemical separation of stored 233U oxides. In the 1960s, after recovery of 233U, the processed Th target (which now includes 229Th) was stored in stainless steel waste tanks. The initial purification of the 229Th from the waste material began at ORNL in 1995 and was solely supported by internal ORNL funding. In 1994, about 30% of the sludge from the waste tank was purchased by PharmActinium, Inc. (Alphamedical Holding BV, Amsterdam, The Netherlands) and was sent to the Institute for Transuranium Elements (ITU, Karlsruhe, Germany) where the Th was purified. Since then, the 225Ac from ITU has been routinely sent to MSKCC also in partial support of the clinical trials (Jurcic et al., 2002; Apostolidis et al., 2001).

This paper describes a sequence of chemical steps consisting of both anion and cation exchange chromatography for routine separation of carrier-free Ra radioisotopes and carrier-free 225Ac from macro amounts of Th (a mixture of 228Th, 229Th and 232Th). The paper further outlines the separation of 225Ac from a mixture of 224Ra and 225Ra.

Section snippets

Materials and methods

High purity concentrated HNO3 (65%) and HCl (30%) were purchased from EM Science (Suprapur). The anion exchange resin MP1 (Cl form), and the cation exchange resins AG50×4 (Na+ form) and MP50 (Na+ form) were purchased from Bio-Rad Laboratories. There resins were in two sizes, 100–200 and 200–400 mesh, and were stored in deionized water. When needed, the MP1 resin was converted to the nitrate form by washing the resin with several bed volumes of 8 M HNO3, until all Cl ions were removed (AgCl

Process description

The 229Th from waste (Th–W) is kept in three batches (A, B and C) each containing ∼35 g of 232Th and ∼30 mCi of 229Th. These batches are stored in three 1 L Teflon bottles which are replaced annually (the 228Th activity contents of these batches are only a few percent, Table 2). The freshly isolated 229Th from 233U (Th–U), containing significant levels of 228Th, is stored in a 500 mL poly carbonate bottle which is replaced in each campaign (about every 60 days). The processing of the 229Th stock is

Results

Thorium-229 stock. The current ORNL 229Th supply is ∼150 mCi. During the 1995–1996 period, ∼90 mCi of 229Th was extracted from the pre-existing waste material which was stored at ORNL for about 35 years (thorium batch (Th-W)). During the 1999–2002 period, ∼60 mCi of 229Th has been recovered from chemical separation of stored 233U (thorium batch (Th-U)). These batches are maintained separately because of the vast differences in their mass composition. The mass composition of Th–W batch is 99.6% 232

Discussion

The chemistry of U and Th has been studied extensively over the past 70 years, whereas the chemistry of Ac and Ra are less understood, mainly due to lack of long-lived isotopes of these elements in nature. Some recent examples of the sequential separation of U, Th, Ac, and Ra are given by Wlodzimirska et al. (2003), Apostolidis et al. (2001), Boll et al. (1997a), Khalkin et al. (1997), El Samad et al. (1993), and Reddy et al. (1981). Our contributions elaborated in this paper, have been to

Conclusion

A four-step chemical process has been described for routine separation of carrier-free 225Ac from a mixture of 228Th, 229Th and 232Th. The separation of Ra and Ac from Th is achieved using a macro-porous anion exchange resin MP50 in 8 M HNO3 media. Two sequential MP1/NO3 columns provide a separation factor of ∼106 for Ra and Ac from Th. A small MP1/Cl column was used for removal of Fe from a mixture of Ra and Ac. The separation of Ac from Ra is accomplished on a low cross-linking cation

Acknowledgements

The authors acknowledge the technical assistance of Greg Groover and Linda Farr for routine hot cell and glove box operations. The velocity separation of resins was conducted by Joseph Guy, and mass and elemental analysis was conducted by Joe Giaquinto and John Keller. Authors are grateful to Dr. Russ Knapp and Scott Aaron for their critical reviews of the manuscript. The authors further acknowledge the continuous support and interest of Dr. Jim Rushton, Emory Collins, Brad Patton and Dr. Jerry

References (36)

  • R.A. Boll et al.

    Bi-213 for alpha-particle-mediated radioimmunotherapy. Proceedings of XII International Symposium on Radiopharmaceutical Chemistry, Uppsala, Sweden, June 15–19, 1997

    J. Labelled Comp. XL

    (1997)
  • L.A. Bray et al.

    Development of a unique bismuth, (Bi-213) automated generator for use in cancer therapy

    Ind. Eng. Chem. Res.

    (2000)
  • X. Chen et al.

    Carboxylate-derived calixerines with high selectivity for actinium-225

    Chem. Cummun.

    (1998)
  • K.A. Deal et al.

    Improved in vivo stability of actinium-225 macrocyclic complexes

    J. Med. Chem.

    (1999)
  • Du, M., Peretz, F., Boll, R.A., Mirzadeh, S., 2003. Thorium-229 for medical applications. in: Laue, C.A, Nash, K.L....
  • O. El Samad et al.

    Fast radiochemical separation and γ spectroscopy of short-lived thallium isotopes

    Radiochim. Acta

    (1993)
  • M.A. Garland et al.

    Reactor production of thorium-229, Proceedings of National Meeting of American Nuclear Society, San Diego, CA, September 27, 2003

    Trans. Am. Nucl. Soc.

    (2003)
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