METHOD FOR PURIFICATION OF 226RA-CONTAINING SOLUTION, METHOD FOR PRODUCING A 226RA TARGET AND METHOD FOR PRODUCING 225AC

Description

Technical Field

[0001] The present invention relates to a method for purifying a 226< Ra-containing solution, a method for producing a 226< Ra target, and a method for producing 225< Ac.Background Art

[0002] In the field of nuclear medicine, radionuclide therapy has been performed in which a drug containing a radioisotope (RI) is selectively taken into a lesion such as a tumor for treatment. Among radiations, an alpha-ray has a characteristic that the effect of unnecessary exposure on the surrounding normal cells is small because the range is short. 225< Ac being one of the alpha-ray emitting nuclides is a radionuclide with a half-life period of 10 days, and has been expected as a therapeutic nuclide in cancer treatment in recent years.

[0003] 225< Ac is produced by a nuclear reaction of (p, 2n), for example, by irradiating a 226< Ra target with a proton using an accelerator. Patent Literature 1 discloses a method for separation and purification of an 225< Ac component from a solution containing 226< Ra ions and 225< Ac ions, which is obtained by dissolving the 226< Ra target after irradiation.Citation ListPatent Literature

[0004] Patent Literature 1: JP 2009-527731 A

[0005] EP 2 528 063 A2 describes methods of purifying acidic metal solutions by removing at least a portion of alpha-particle emitting materials.

[0006] US 2009 / 101586 A1 describes a process for the adsorption of radionuclides from media, preferably waters or aqueous solutions, as arise, for example, in nuclear plants, preferably nuclear power plants, by contacting the medium to be treated, preferably water or aqueous solutions, with a mixed bed which is provided additionally with at least one covering layer of a monodisperse, macroporous ion exchanger having a median bead diameter smaller than the ion exchanger used in the mixed bed.

[0007] JP H11 262661 A describes a treating method of radium-containing waste water using a radium adsorbent consisting of a strong acidic cation exchange resin and moist oxides of titanium and zirconium, and the moist oxides of titanium and zirconium are chemically bonded to the strong acidic cation exchange resin.Summary of Invention

[0008] However, there has been a problem that the amount of the 225< Ac produced from a 226< Ra target is extremely small, and most of the 226< Ra remains unreacted.

[0009] Further, since 226< Ra is a precious nuclide and the disposal of 226< Ra is not easy, it has been demanded to establish a method for purifying efficiently and easily a solution containing 226< Ra ions after 225< Ac separation in order to reuse the unreacted 226< Ra. The technique disclosed in Patent Literature 1 has a problem in terms of efficiency and ease, such as the need for distillation and reflux.

[0010] The present invention has been made in view of the circumstances as described above, and an object of the present invention is to provide a method for purifying efficiently and easily a 226< Ra-containing solution obtained when 225< Ac is produced from a 226< Ra target, a method for producing a 226< Ra target by using the purified 226< Ra-containing solution obtained by the above purification method, and a method for producing 225< Ac including these above methods.

[0011] One embodiment of the present invention is a method for purifying a 226< Ra-containing solution as defined in claim 1.

[0012] Further, another embodiment of the present invention is a method for producing a 226< Ra target, comprising the steps: (R4) of preparing an electrodeposition liquid by using a purified 226< Ra-containing solution (b) obtained by the method for purifying a 226< Ra-containing solution described above; and (R5) of electrodepositing a 226< Ra-containing substance on a substrate by using the electrodeposition liquid.

[0013] Furthermore, another embodiment of the present invention is a method for producing 225< Ac, comprising a step (A1) of irradiating a 226< Ra target produced by the method for producing a 226< Ra target described above with at least one kind selected from a charged particle, a photon, and a neutron by using an accelerator to produce 225< Ac.

[0014] According to the method for purifying a 226< Ra-containing solution of the present invention, a 226< Ra-containing solution obtained when 225< Ac is produced from a 226< Ra target can be purified efficiently and easily. Further, a 226< Ra target can be produced efficiently by using the purified 226< Ra-containing solution obtained by the above purification method. Furthermore, 225< Ac can be obtained efficiently and stably by a method for producing 225< Ac including these above methods.Brief Description of Drawings

[0015] Fig. 1 is a flow chart showing an outline of the method for purifying a 226< Ra-containing solution, method for producing a 226< Ra target, and method for producing 225< Ac according to the present invention.Description of Embodiments

[0016] Hereinafter, the embodiments of the present invention will be described in detail. A flow chart showing an outline of the method for purifying a 226< Ra-containing solution, method for producing a 226< Ra target, and method for producing 225< Ac according to the present invention is shown in Fig. 1.Method for Purifying 226< Ra-Containing Solution

[0017] The method for purifying a 226< Ra-containing solution (hereinafter, also referred to as "purification method (X)") according to the present invention is characterized by including: an adsorption step (R1) of allowing a 226< Ra ion to adsorb onto a carrier having a function of selectively adsorbing a divalent cation (hereinafter, also referred to as "carrier (i)") by bringing a 226< Ra-containing solution (a) into contact with the carrier (i) under an alkaline condition; and an elution step (R2) of eluting the 226< Ra ions from the carrier (i) under an acidic condition. In this way, 226< Ra ions are concentrated, and impurities can be reduced. The solution obtained by the purification method (X) is referred to as a purified 226< Ra-containing solution (b).

[0018] The 226< Ra-containing solution (a) is obtained by separating an 225Ac component from a solution in which a 226Ra target irradiated with at least one kind selected from a charged particle, a photon, and a neutron by using an accelerator has been dissolved, and is preferably an aqueous solution containing 226< Ra ions. In order to perform an adsorption step (R1) under an alkaline condition, the 226< Ra-containing solution (a) is preferably an alkaline aqueous solution, and has a pH of preferably 8 or more, and more preferably 9 or more. Examples of the alkaline aqueous solution include an aqueous ammonium solution, an aqueous sodium hydroxide solution, and an aqueous potassium hydroxide solution. In this way, 226< Ra ions can be adsorbed onto a carrier (i) efficiently.

[0019] As the 226< Ra-containing solution (a), a solution after an irradiation step (A1), a dissolution step (A2), and a separation step (A3) in the production method for producing 225< Ac to be described later, that is, a solution obtained by separating an 225< Ac component from a solution in which a 226< Ra target irradiated with at least one kind selected from a charged particle, a photon, and a neutron by using an accelerator has been dissolved is used.<Adsorption step (R1)>

[0020] In an adsorption step (R1), 226< Ra ions are adsorbed onto a carrier (i) by bringing a 226< Ra-containing solution (a) into contact with the carrier (i) under an alkaline condition.

[0021] The carrier (i) is not particularly limited as long as it can form a complex with a metal ion under an alkaline condition and elute the metal ion under an acidic condition. As the carrier (i), for example, a carrier having a divalent cation-exchange group can be mentioned. As the divalent cation-exchange group, specifically, an iminodiacetic acid group, a polyamine group, or a methyl glycan group can be mentioned. As the divalent cation-exchange group, an iminodiacetic acid group is preferable. The carrier having a divalent cation-exchange group is not particularly limited as long as the divalent cation-exchange group is retained on a solid-phase carrier such as a resin. A more preferable example of the carrier includes a styrene-divinylbenzene copolymer retaining an iminodiacetic acid group. Examples of the commercially available resin having an iminodiacetic acid group include the "Chelex" series manufactured by Bio-Rad Laboratories, Inc., "DIAION" series manufactured by Mitsubishi Chemical Corporation, and "Amberlite" series manufactured by The Dow Chemical Company, and more specifically include "Chelex 100" (particle diameter: 50 to 100 mesh, and ionic form: Na form, Fe form) manufactured by Bio-Rad Laboratories, Inc. The carrier (i) may be charged in a tube for use. The tube is not particularly limited as long as the carrier (i) can be charged in the tube and the tube has flexibility, and is preferably a flexible tube made of rubber, a resin, or the like, and more preferably a tube for medical use.

[0022] By using such a tube, a length longer than that of a common glass column can be obtained, that is, the number of theoretical plates can be increased, so that the adsorption efficiency of 226< Ra ions can be increased. Further, the carrier (i) through which a radioactive substance ( 226< Ra-containing solution) has been passed can be easily discarded while being charged in a tube without radioactively contaminating other instruments, devices, and the like.<Elution step (R2)>

[0023] In an elution step (R2), 226< Ra ions are eluted from a carrier (i) under an acidic condition. Specifically, by passing an inorganic acid through the carrier (i), the 226< Ra ions adsorbed onto the carrier (i) can be eluted.

[0024] The inorganic acid is not particularly limited as long as it can dissolve a 226< Ra component adsorbed onto the carrier (i) and generate ions, and examples of the inorganic acid include hydrochloric acid and nitric acid.

[0025] In this regard, from the viewpoints that 226< Ra ions can be efficiently eluted from the carrier and that anions derived from an inorganic acid can be efficiently removed in the later step, the concentration of the inorganic acid is preferably 0.1 to 12 mol / L, more preferably 0.3 to 5 mol / L, furthermore preferably 0.5 to 2 mol / L, and particularly preferably 0.7 to 1.5 mol / L.<Anion exchange step (R3)>

[0026] The purification method (X) according to the present invention may further include an anion exchange step (R3) in which a solution containing 226< Ra ions eluted in an elution step (R2) is passed through an anion exchange resin.

[0027] If any anions (for example, chloride ions or the like) derived from an inorganic acid (for example, hydrochloric acid or the like) used in the elution step (R2) remain in the solution, such anions may affect the electrodeposition rate of 226< Ra ions in an electrodeposition step (R5) described later. For this reason, it is preferable to treat the solution containing the 226< Ra ions eluted in the elution step (R2), in the anion exchange step (R3) because the anions derived from an inorganic acid can be reduced by being exchanged for hydroxide ions, and the electrodeposition efficiency of 226< Ra ions in the electrodeposition step (R5) can be improved.

[0028] The anion exchange resin is not particularly limited as long as it can exchange anions (for example, chloride ions or the like) derived from an inorganic acid for hydroxide ions, and is preferably a strongly basic anion exchange resin, and more preferably a resin having a quaternary ammonium salt. Examples of the commercially available anion exchange resin include the "MONOSPHERE" series manufactured by The Dow Chemical Company, and the "AG" series manufactured by Bio-Rad Laboratories, Inc., and more specifically include "MONOSPHERE 550A" (particle diameter: 590 ± 50 mesh, ionic form: OH form).

[0029] In this regard, the anion exchange resin may be charged in a tube for use in a similar manner as in the case of a carrier (i). As the tube capable of being used for the charging, a tube similar to that in which the above-described carrier (i) is to be charged can be mentioned.<Other step>

[0030] A step of washing a carrier (i) may be included between the step (R1) and the step (R2) in a purification method (X). Specifically, a step can be mentioned in which water is passed through a carrier (i). In this way, the proportion of impurities contained in a purified 226< Ra-containing solution (b) can be reduced.Method for Producing 226< Ra Target

[0031] The method for producing a 226< Ra target according to the present invention is characterized by including an electrodeposition liquid preparation step (R4) of preparing an electrodeposition liquid by using a purified 226< Ra-containing solution (b) obtained by a purification method (X), and an electrodeposition step (R5) of electrodepositing a 226< Ra-containing substance on a substrate by using the electrodeposition liquid.

[0032] It is preferable that the method for producing a 226< Ra target according to the present invention further includes a purification method (hereinafter, also referred to as "purification method (Y)") including an adsorption step (R6) of allowing 226< Ra ions to adsorb onto a carrier having a function of selectively adsorbing divalent cations (hereinafter, also referred to as "carrier (ii)") by bringing a 226< Ra-containing solution (c) after the electrodeposition step (R5) into contact with the carrier (ii) under an alkaline condition, and an elution step (R7) of eluting the 226< Ra ions from the carrier (ii) under an acidic condition. The solution obtained by the purification method (Y) is referred to as a purified 226< Ra-containing solution (d).<Electrodeposition liquid preparation step (R4)>

[0033] In an electrodeposition liquid preparation step (R4), an electrodeposition liquid is prepared by using a purified 226< Ra-containing solution (b), and at this time, a purified 226< Ra-containing solution (d) obtained by a purification method (Y) may be mixed with the purified 226< Ra-containing solution (b) to prepare an electrodeposition liquid. In this way, the recovery rate of 226< Ra can be further increased, and 226< Ra can be recovered more efficiently.

[0034] By adding as needed a buffer agent, an acid, or the like to a purified 226< Ra-containing solution (b) or a mixture of a purified 226< Ra-containing solution (b) and a purified 226< Ra-containing solution (d), an electrodeposition liquid to be used in an electrodeposition step (R5) described later can be prepared.

[0035] Examples of the buffer agent include a chloride salt such as ammonium chloride; a carbonate such as ammonium carbonate, sodium carbonate, potassium carbonate, calcium carbonate, or magnesium carbonate; a hydrogen carbonate such as ammonium hydrogen carbonate, sodium hydrogen carbonate, or potassium hydrogen carbonate; an acetate such as ammonium acetate, sodium acetate, or potassium acetate; a succinate such as monosodium succinate, disodium succinate, monopotassium succinate, dipotassium succinate, monoammonium succinate, or diammonium succinate; and a benzoate such as sodium benzoate, potassium benzoate, or ammonium benzoate. Among them, ammonium acetate is preferable from the viewpoints, for example, of being easy to maintain the pH of an electrodeposition liquid within the desired range described later, and of electrodepositing 226< Ra ions on a substrate more efficiently.

[0036] Examples of the acid include an inorganic acid, and a carboxylic acid having 2 to 6 carbon atoms. Examples of the inorganic acid include nitric acid, hydrochloric acid, and boric acid. Further, examples of the carboxylic acid having 2 to 6 carbon atoms include acetic acid, succinic acid, and benzoic acid.

[0037] The acid is preferably a monovalent or divalent acid from the viewpoint of improving the yield of 225< Ac.

[0038] From the viewpoint that 226< Ra ions can be more efficiently electrodeposited on a substrate, the pH of an electrodeposition liquid is preferably 4 to 7, and more preferably 5 to 6. The pH of the electrodeposition liquid can be kept within the above range by appropriately adding a buffer agent or an acid.

[0039] The electrodeposition liquid may contain as needed a component that has been used in conventional electroplating or the like within a range that does not impair the effects of the present invention. As the other components, one kind may be used, or two or more kinds may be used.<Electrodeposition step (R5)>

[0040] In an electrodeposition step (R5), a 226< Ra-containing substance is electrodeposited on a substrate by using an electrodeposition liquid prepared in an electrodeposition liquid preparation step (R4).

[0041] Examples of the 226< Ra-containing substance include a 226< Ra metal, and a 226< Ra salt. The obtained 226< Ra target can be reused in an irradiation step (A1) in a method for producing 225< Ac described later.

[0042] Examples of the metal to be used for the substrate include aluminum, copper, titanium, silver, gold, iron, nickel, niobium, and alloys containing these metals (such as phosphor bronze, brass, nickel silver, beryllium copper, Corson alloy, and stainless steel).

[0043] Further, the substrate may be plated a conductive support with these metals.

[0044] As the substrate, a gold plate is preferable, for example, from the viewpoint of being less likely to cause adverse effects on an accelerator and the like even during irradiation with at least one kind selected from a charged particle, a photon, and a neutron by using the accelerator and of being capable of preventing contamination with a metal derived from the substrate during the irradiation or the dissolution of a target, and from the viewpoint of being capable of electrodepositing 226< Ra ions on a substrate more efficiently.

[0045] The electrodeposition step (R5) can be performed by a known method. Specifically, by energizing an electrodeposition liquid, a 226< Ra-containing substance is electrodeposited on a substrate.

[0046] As the power source for energization, it is not particularly limited, and a direct current (DC) power source, an alternating current (AC) power source, a pulse power source, a PR pulse power source, or the like can be used. Among them, a pulse power source or a PR pulse power source is preferably used, for example, from the viewpoints of being easy to improve the diffusion of 226< Ra ions and to uniformly electrodeposit a 226< Ra-containing substance, being capable of suppressing the generation of heat, and being capable of performing the electrodeposition with a small power source.

[0047] As the temperature (temperature of electrodeposition liquid) in the electrodeposition step (R5), it is not particularly limited, and a temperature of, for example, around 10 to 80°C can be employed.<Adsorption step (R6)>

[0048] In an adsorption step (R6), 226< Ra ions are allowed to adsorb onto a carrier (ii) by bringing a 226< Ra-containing solution (c) containing residual 226< Ra ions after an electrodeposition step (R5) into contact with the carrier (ii) under an alkaline condition.

[0049] As the carrier (ii), a carrier similar to the carrier (i) to be used in an adsorption step (R1) in a purification method (X) can be used, and the carrier (ii) may be charged in a tube for use in a similar manner as in the case of the purification method (X).<Elution step (R7)>

[0050] In an elution step (R7), 226< Ra ions are eluted from a carrier (ii) under an acidic condition. Specifically, by passing an inorganic acid through the carrier (ii), the 226< Ra ions adsorbed onto the carrier (ii) can be eluted.

[0051] As the inorganic acid to be used in the elution step (R7), an inorganic acid similar to that to be used in an elution step (R2) can be used, and the inorganic acid can also have a concentration similar to that of the inorganic acid to be used in the elution step (R2).<Anion exchange step (R8)>

[0052] A purification method (Y) may further include an anion exchange step (R8) in which a solution containing 226< Ra ions eluted in an elution step (R7) is passed through an anion exchange resin.

[0053] If any anions (for example, chloride ions or the like) derived from an inorganic acid (for example, hydrochloric acid or the like) used in the elution step (R7) remain in the solution, such anions may affect the electrodeposition efficiency of 226< Ra ions when an electrodeposition liquid is prepared in an electrodeposition liquid preparation step (R4) and then an electrodeposition step (R4) is performed. For this reason, it is preferable to treat a solution containing the 226< Ra ions eluted in the elution step (R7), in an anion exchange step (R8) because the anions derived from an inorganic acid can be reduced by being exchanged for hydroxide ions, and the electrodeposition rate of the 226< Ra ions can be improved in a case where the solution is used again as an electrodeposition liquid in the electrodeposition step (R4).<Other step>

[0054] A step of washing a carrier (ii) may be included between the step (R6) and the step (R7) in a purification method (Y). Specifically, a step can be mentioned in which water is passed through a carrier (ii). In this way, the proportion of impurities contained in a purified 226< Ra-containing solution (d) is reduced.Method for Producing 225< Ac

[0055] The method for producing 225< Ac according to the present invention is characterized by including an irradiation step (A1) of irradiating a 226< Ra target produced by the above-described method for producing a 226< Ra target according to the present invention with at least one kind selected from a charged particle, a photon, and a neutron by using an accelerator. It is preferable that the method for producing 225< Ac according to the present invention further includes a dissolution step (A2) of dissolving the 226< Ra target irradiated in the irradiation step (A1), and a separation step (A3) of separating a colloidal 225< Ac component by alkalizing the solution obtained in the dissolution step (A2).<Irradiation step (A1)>

[0056] In an irradiation step (A1), a 226< Ra target produced by the above-described method for producing a 226< Ra target according to the present invention is irradiated with at least one kind selected from a charged particle, a photon, and a neutron by using an accelerator, and 225< Ac is allowed to generate by a nuclear reaction. As the particle, a proton, a deuteron, an a particle, or a γ particleis preferable, and a proton is more preferable.

[0057] In this regard, as for the irradiation method and the irradiation condition, a known method and a known condition can be adopted.<Dissolution step (A2)>

[0058] In a dissolution step (A2), a 226< Ra target irradiated in an irradiation step (A1) is dissolved in an acid solution. As a result, a solution containing 226< Ra ions and 225< Ac ions is obtained.

[0059] As the acid solution, an acid solution that can dissolve 225< Ac and 226< Ra as ions is mentioned, and specifically an aqueous solution of an inorganic acid such as hydrochloric acid, or nitric acid, preferably an aqueous solution of hydrochloric acid is mentioned.<Separation step (A3)>

[0060] In a separation step (A3), a colloidal 225< Ac component by alkalizing a solution obtained in a dissolution step (A2) is separated.

[0061] The 225< Ac dissolved in water as 225< Ac ions under an acidic condition becomes actinium hydroxide ( 225< Ac(OH) 3 ) under an alkaline condition, and forms colloids in an aqueous solution. The colloidal actinium hydroxide is collected on a filter by filtering with a membrane filter or the like, and can be separated from the solution.

[0062] In addition, a 226< Ra component exists as ions in a solution to which an alkaline solution has been added, and is separated from an 225< Ac component by a separation step (A3), and a 226< Ra-containing solution (a) is obtained. The obtained 226< Ra-containing solution (a) is supplied to an adsorption step (R1) in a purification method (X).<Recovery step (A4)>

[0063] By dissolving 225< Ac separated in a separation step (A3) with an acid solution, an 225< Ac-containing solution is obtained. The obtained 225< Ac-containing solution may be further purified by a known method, as needed.<<Dissolution>>

[0064] Actinium hydroxide separated in a separation step (A3) can be dissolved by using an acid solution. The acid solution to be used for dissolution is not particularly limited as long as it can dissolve actinium hydroxide as ions, and for example, the same acid solution as that used in a dissolution step (A2) can be used. Further, it is preferable that the concentration is 1 to 6 mol / L, and more preferably 2 to 5 mol / L, from the viewpoints that actinium hydroxide is easily dissolved as ions and that a carrier easily adsorbs 226< Ra.<<Purification>>

[0065] A solution containing 225< Ac ions dissolved with an acid solution can be purified, for example, by a solid-phase extraction method. A solid-phase extraction agent to be used in the solid-phase extraction method is not particularly limited as long as it can capture 225< Ac ions and then elute the 225< Ac ions under a predetermined condition, and examples of the solid-phase extraction agent include ones containing a compound represented by the formula (1).

[0066] In the formula (1), m and n are independently 0 or 1, and preferably 1; and R 1< , R 2< , R 3< , and R 4< are independently a straight or branched chain alkyl group having 8 or more and 12 or less carbon atoms, and preferably independently an octyl group or 2-ethylhexyl. Such a solid-phase extraction agent is commercially available, for example, as "DGA Resin" manufactured by Eichrom Technologies Inc.

[0067] As the specific purification method, first, an 225< Ac-containing solution is passed through a solid-phase extraction agent to capture 225< Ac ions and the like in the solid-phase extraction agent. Next, the captured unnecessary 226< Ra is eluted by passing the solution through a solid-phase extraction agent with an inorganic acid such as hydrochloric acid. At this time, the concentration of the inorganic acid is set to a relatively high concentration so that 225< Ac does not elute. After that, 225< Ac ions can be eluted from the solid-phase extraction agent by passing through an inorganic acid having a relatively low concentration.Examples

[0068] Hereinafter, the present invention is further specifically described on the basis of Examples, however, the present invention is in no way limited to these Examples.Examples 1 and 2<Evaluation item 1: Mass balance of 226< Ra in purification method (X)>

[0069] An irradiated 226< Ra target (size: Φ10 mm, thickness: 2 to 3 mm, and 226< Ra mass: 0.3 to 1 mg) was dissolved in 5 mL of 1 mol / L hydrochloric acid, and then the obtained solution was filtered with a membrane filter to remove insoluble matters. To the filtrate, 1 mL of 28% by mass ammonia water (product name: Ammonia solution (25.0 to 27.9%) for atomic absorption spectrometry, manufactured by KANTO CHEMICAL CO., INC.) was added to adjust the pH to 10 to 12, and colloid of actinium hydroxide was generated. Next, the generated actinium hydroxide was filtered by using a membrane filter at a flow rate of 1 to 2 mL / min to recover a 226< Ra-containing solution (a-1). The radioactivity of the obtained 226< Ra-containing solution (a-1) was measured by a germanium semiconductor detector manufactured by EURISYS MESURES.

[0070] Next, in order to prevent contamination by Na in a purified 226< Ra-containing solution (b-1) described later, one that had been obtained by converting Chelex 100 (particle diameter: 50 to 100 mesh, ionic form: Na form, and use amount: 3 mL, manufactured by Bio-Rad Laboratories, Inc.) to a NH 4 +< form was charged in a medical tube having an inner diameter of 3.2 mm, an outer diameter of 4.4 mm, and a length of 50 cm (extension tube, 3.2 × 4.4 × 500 mm (4 mL), MS-FL, manufactured by HAKKO CO., LTD.), 50 to 80 mL of the obtained 226< Ra-containing solution (a-1) (pH > 9) was passed through the medical tube at a flow rate of 1 to 2 mL / min, and the eluate was taken as a waste liquid (W1). Next, 10 mL of water was passed through Chelex 100 at a flow rate of 1 to 2 mL / min, and the eluate was merged with the waste liquid (W1).

[0071] Next, MONOSPHERE 550A (particle diameter: 590 ± 50 mesh, ionic form: OH form, and use amount: 20 mL, manufactured by The Dow Chemical Company) was washed with hydrochloric acid, water, sodium hydroxide, and water in this order, and then the washed MONOSPHERE 550A was charged in a medical tube having an inner diameter of 3.2 mm, an outer diameter of 4.4 mm, and a length of 200 cm (extension tube, 3.2 × 4.4 × 500 mm (4 mL), MS-FL, manufactured by HAKKO CO., LTD.), and the medical tube was connected to a tube filled with Chelex 100. 10 mL of 1 mol / L hydrochloric acid was passed through Chelex 100 and MONOSPHERE 550A in this order at a flow rate of 1 to 2 mL / min, and then 8 mL of water was further passed through the resultant Chelex 100 and MONOSPHERE 550A at a flow rate of 1 to 2 mL / min, and 18 mL of a purified 226< Ra-containing solution (b-1) was obtained.

[0072] The radioactivity of the obtained purified 226< Ra-containing solution (b-1) was measured by a germanium semiconductor detector. Further, the radioactivity of each of the waste liquid (W1) and the materials of Chelex and MONOSPHERE 550A was measured in order to examine the distribution of residual 226< Ra.

[0073] The same operation was performed twice in total (Examples 1 and 2), and the mass balance of each 226< Ra was calculated. The results are shown in Table 1. Table 1Example 1Example 2Numerical valuePercentageNumerical valuePercentage 226< Ra-Containing solution (a-1) (calculated value)9.13 MBq100%2.97 MBq100%Waste liquid (W1)N. D< 0.2%* 1< N. D< 0.7%* 1< Residual in materialChelex after elutionN.D< 0.2%* 1< N. D< 0.7%* 1< MONOSPHERE 550A after elutionN.D< 0.2%* 1< N. D< 0.7%* 1< Purified 226< Ra-containing solution (b-1)9.13 MBq> 99.3%2.97 MBq> 98.0%

[0074] In Table 1, the 226< Ra-containing solution (a-1) was calculated from the following formula (1).

[0075] In this regard, for the purified 226< Ra-containing solution (b-1) of Example 2, a value calculated from the difference in radioactivity between the Ra-adsorbed Chelex and the Ra-eluted Chelex was used.

[0076] The values with *1 shown in Table 1 were calculated assuming that a maximum of 0.02 MBq was detected because it is unclear whether the measurement of less than 0.02 MBq is possible although the measured value was N.D.

[0077] As in Examples 1 and 2, by passing the 226< Ra-containing solution (a-1) through Chelex 100, impurities (ammonium chloride (hydrochloric acid + ammonia), ammonia, and the like) other than 226< Ra can be removed. Further, most of the chloride ions can be removed by these adsorption step (R1), elution step (R2), and anion exchange step (R3).Examples 3 to 8<Evaluation item 2: Mass balance of 226< Ra after dissolution step (A2) and separation step (A3)>

[0078] An irradiated 226< Ra target (size: Φ10 mm, thickness: 2 to 3 mm, and 226< Ra mass: 0.3 to 1 mg) was dissolved in 5 mL of 1 mol / L hydrochloric acid, and then the obtained solution was filtered with a membrane filter to remove insoluble matters. To the filtrate, 1 mL of 28% by mass ammonia water (product name: Ammonia solution (25.0 to 27.9%) for atomic absorption spectrometry, manufactured by KANTO CHEMICAL CO., INC.) was added to adjust the pH to 10 to 12, and colloid of actinium hydroxide was generated. Next, the generated actinium hydroxide was filtered by using a membrane filter at a flow rate of 1 to 2 mL / min to obtain a 226< Ra-containing solution (a-2).

[0079] Next, DGA Resin (DGA Normal Resin, 1-mL cartridge, manufactured by Eichrom Technologies Inc.) was connected to a membrane filter. 6 mL of 4 mol / L nitric acid was passed through the membrane filter and the DGA Resin in this order at a flow rate of 1 to 2 mL / min, and the eluate was taken as a waste liquid (W2).

[0080] The radioactivity of the solution after the dissolution step (A2) was measured by a germanium semiconductor detector. Further, the radioactivity of each of the waste liquid (W2) and the materials of membrane filter and DGA Resin was measured by a germanium semiconductor detector in order to examine the distribution of residual 226< Ra. The same operation was performed three times in total (Examples 3 to 5), and the mass balance of each 226< Ra was calculated. The results are shown in Table 2.<Evaluation item 3: Mass balance of 225< Ac>

[0081] Next, the DGA Resin was removed from the membrane filter, 6 mL of 8 mol / L hydrochloric acid was passed through the DGA Resin at a flow rate of 1 to 2 mL / min, and the eluate was taken as a waste liquid (W3). After that, 10 mL of 0.01 mol / L hydrochloric acid was passed through the DGA Resin at a flow rate of 1 to 2 mL / min, and an 225< Ac-containing solution was obtained.

[0082] The radioactivity of the obtained 225< Ac-containing solution was measured by a germanium semiconductor detector. Further, the radioactivity of each of the waste liquid (W3) and the materials of membrane filter and DGA Resin was measured by a germanium semiconductor detector in order to examine the distribution of residual 225< Ac. The same operation was performed three times in total (Examples 6 to 8), and the results are shown in Table 3. Table 2Example 3Example 4Example 5Numerical valuePercentageNumerical valuePercentageNumerical valuePercentageSolution after dissolution step (A2)11.70 MBq100%17.03 MBq100%35.90 MBq100%Residual in materialMembrane filterN. D< 0.2a* 1< N.D< 0.1%* 1< 0.02 MBq0.1%DGA ResinN.D< 0.2%* 1< N.D< 0.1%* 1< N. D< 0.1%* 1< Waste liquid (W2)0.18 MBq1. 5%0.03 MBq0.2%0.46 MBq1. 3%Recovered amount 226< Ra-Containing solution (a-2) not containing waste liquid (W2) (calculated value)11.52 MBq> 98.1%17.00 MBq> 99.6%35.43 MBq> 98.6% 226< Ra-Containing solution (a-2) containing waste liquid (W2) (calculated value)11.70 MBq> 98.7%17.03 MBq> 99.8%35.88 MBq> 99.9% Table 3 Example 6Example 7Example 8Numerical valuePercentageNumerical valuePercentageNumerical valuePercentageMembrane filter-collected amount (calculated value)49.30 kBq100%47.55 kBq100%73.45 kBq100%Residual in materialMembrane filter* 2< N. D< 1.2%* 1< N. D< 1.2%* 1< 0.93 kBq1.27%DGA Resin* 2< N. D< 1.2%* 1< N. D< 1.2%* 1< N. D< 0.8%* 1< Waste liquid (W3) after passed through DGA Resin* 2< N. D< 1.2%* 1< 1.67 kBq3.50%N. D< 0.8%* 1< Recovered amountAfter membrane collection* 2< 49.30 kBq> 96.5%* 3< 45.88 kBq> 94.1%* 3< 72.51 kBq> 97.1%* 3<

[0083] The values with *1 shown in Table 2 were calculated assuming that a maximum of 0.02 MBq was detected because it is unclear whether the measurement of less than 0.02 MBq is possible although the measured value was N.D.

[0084] The 226< Ra-containing solution (a-2) not containing the waste liquid (W2) after the separation step (A3) in Table 2 was calculated from the following formula (2).

[0085] The amount of 226< Ra contained in the solution after the dissolution step (A2) was calculated by collecting a part of the solution, measuring the amount of the part, and converting the measured amount of the part to an amount for the entire solution.

[0086] The values with *1 shown in Table 3 were calculated assuming that a maximum of 0.58 kBq was detected because it is unclear whether the measurement of less than 0.58 kBq is possible although the measured value was N.D.

[0087] The values with *2 shown in Table 3 were used to calculate the 225< Ac membrane filter-collected amount after the separation step (A3).

[0088] The values of the membrane filter-collected amount shown in Table 3 were calculated from the following calculation formula (3).

[0089] In this regard, as the 225< Ac recovered amount in the purified 225< Ac-containing solution of Example 6, a value calculated from the difference in radioactivity between the Ac adsorbed-DGA and the Ac-eluted DGA was used.

[0090] The values with *3 shown in Table 3 are each the mass balance after collection by a membrane filter, and the uncollected matters by the membrane filter are not taken into consideration. Further, since the radioactivity of 225< Ac in the 226< Ra solutions before and after being passed through a membrane filter cannot be measured due to the influence of 226< Ra, the recovery rate was calculated by assuming the denominator as "the membrane filter-collected amount after separation step (A3) (calculation value)".

Claims

1. A method for purifying a 226Ra-containing solution, comprising the steps: (R1) of allowing a 226Ra ion to adsorb onto a carrier having a function of selectively adsorbing a divalent cation by bringing a 226Ra-containing solution (a) into contact with the carrier under an alkaline condition; and (R2) of eluting the 226Ra ion from the carrier under an acidic condition, characterized in that the 226Ra-containing solution (a) is obtained by separating an 225Ac component from a solution in which a 226Ra target irradiated with at least one kind selected from a charged particle, a photon, and a neutron by using an accelerator has been dissolved.

2. The method for purifying a 226Ra-containing solution according to claim 1, wherein the carrier has a divalent cation-exchange group.

3. The method for purifying a 226Ra-containing solution according to claim 1 or 2, wherein the carrier has an iminodiacetic acid group.

4. The method for purifying a 226Ra-containing solution according to any one of claims 1 to 3, further comprising a step (R3) of performing anion exchange by passing a solution containing a 226Ra ion eluted in the elution step (R2) through an anion exchange resin.

5. The method for purifying a 226Ra-containing solution according to any one of claims 1 to 4, wherein the carrier is charged in a tube.

6. A method for producing a 226Ra target, comprising the steps: (R4) of preparing an electrodeposition liquid by using a purified 226Ra-containing solution (b) obtained by the purification method according to any one of claims 1 to 5; and (R5) of electrodepositing a 226Ra-containing substance on a substrate by using the electrodeposition liquid.

7. The method for producing a 226Ra target according to claim 6, further comprising a purification method comprising the steps: (R6) of allowing a 226Ra ion to adsorb onto a carrier having a function of selectively adsorbing a divalent cation by bringing a 226Ra-containing solution (c) after the electrodeposition step (R5) into contact with the carrier under an alkaline condition; and (R7) of eluting the 226Ra ion from the carrier under an acidic condition, wherein a purified 226Ra-containing solution (d) obtained by the purification method is mixed with the purified 226Ra-containing solution (b), and an electrodeposition liquid is prepared in the electrodeposition liquid preparation step (R4).

8. The method for producing a 226Ra target according to claim 7, further comprising a step (R8) of performing anion exchange by passing a solution containing a 226Ra ion eluted in the elution step (R7) through an anion exchange resin.

9. A method for producing 225Ac, comprising a step (A1) of irradiating a 226Ra target produced by the production method according to any one of claims 6 to 8 with at least one kind selected from a charged particle, a photon, and a neutron by using an accelerator to produce 225Ac.

10. The method for producing 225Ac according to claim 9, further comprising the steps: (A2) of dissolving the 226Ra target irradiated in the irradiation step (A1); and (A3) of separating a colloidal 225Ac component by alkalizing the solution obtained in the dissolution step (A2).