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Instruments 2018, 2(3), 15;

First Steps at the Cyclotron of Orléans in the Radiochemistry of Radiometals: 52Mn and 165Er
CEMHTI (Conditions Extrêmes et Matériaux: Haute Température et Irradiation), CNRS, UPR3079, University of Orléans, F-45071 Orléans, France
TRISKEM, 3, rue des champs Géons ZAC de l’Eperon 35170 Bruz, France
Correspondence: [email protected]; Tel.: +33-238-255-427
Current address: ISTO, UMR7327, CNRS, University of Orléans, F-45071 Orléans, France.
Received: 17 April 2018 / Accepted: 10 August 2018 / Published: 16 August 2018


This work describes the first real developments in radiochemistry around exotic radionuclides at the cyclotron of Orléans focusing on the radiochemistry of two radiometals 165Er and 52Mn. For these developments, targets were irradiated during 0.5–2 h at a maximum current of 2 µA. All activities have been determined by radiotracer method. The production of 165Er from a natural Ho target that was irradiated is described. Higher activities of 165Er were obtained via deuteron irradiation then proton with lower ratio 165Er/166Ho (400/1 to 8/1). By using LN2 resin, the separation of adjacent lanthanides was made on various concentrations of HNO3 (0.3 to 5 M). Weight coefficients (Dw) were defined in a batch test. Then, the first tests of separation on a semi-automated system were made: the ratio 166+natHo/165Er in an isolated fraction was significantly reduced (1294 ± 1183 (n = 3)) but the reliability and reproducibility of the system must be improved. Then, a new Cr powder-based target for 52Mn production was designed. Its physical aspects such as mechanics, thermal resistance and porosity have been studied. Dw for various compositions of eluent Ethanol/HCl were evaluated by reducing contact time (1 h) comparative to the literature. A first evaluation of semi-automated separation Cr/Mn has been made.
165Er; 52Mn; irradiation; separation; resin; radiometals; heavy Rare Earth Elements (hREE)

1. Introduction

The cyclotron of Orléans [1,2,3,4] is a research accelerator allowing production of many beam types such as the proton, deuteron and alpha at variable energy from 10 to 45 MeV (Figure 1). Most of the applied uses of the beams focuses on materials studies and characterization. However, its properties give access to numerous radionuclides with potential applications especially for medical imaging. For example, in the period 2005–2013, 211At was produced once a week (300 MBq) (irradiation of target only, no radiochemistry made at Orléans) until the cyclotron ARRONAX (Nantes) was built and became operational to produce regular batch of this radionuclide for alpha-immunotherapy [5,6,7,8]. In a general context of the development of radiometals, such possibilities appear to be very interesting for accessing exotic radionuclides. The production of a radionuclide needs not only to perform a nuclear reaction but also to separate the radionuclide of interest from a bulk target. For this purpose, the cyclotron of Orléans is of interest in producing radionuclides for analytical applications allowing for the validation of the separation by the radiotracer method [9] and a method as sensitive as Inductively Coupled Plasma–Mass Spectrometry (ICP–MS). In this context, it was necessary to initiate tools and methodology in radiochemistry to develop further the accelerator in the area of medical radionuclides. However, two constraints relative to the choice of radionuclides were met at the cyclotron of Orléans. The first constraint was to produce gamma emission and the second was that the half-life of the radionuclide produced must be below 100 days (due to nuclear waste management considerations). Hence for the following work, we used 165Er/Er, 166Ho/Ho, 51Cr/Cr and 52Mn/Mn. Other tools to improve radiochemical separation based on resins, methodology, and target design must be developed. Two cases hereafter illustrate the method’s development for the production and subsequent separation of 165Er and 52Mn.
A task of the radiochemist is to define the conditions of separation of two elements: including resin, eluent (simple and compatible with the radiolabeling process) and the methodology (radiotracer method, irradiation conditions). These aspects have been developed during the production of 165Er. Difficulties were the separation of two adjacent lanthanides in disproportionate quantities and a separation compatible with the radiolabeling of molecules. 165Er decays with electron capture without gamma-ray emission, producing only X-rays (47–55 keV with a cumulative intensity of 73.7%) [10]. It is an ideal radionuclide for Auger electron therapy [11] and can be used for bimodality Magnetic Resonance Imaging / Single Photon Emission Computed Tomography (MRI/SPECT) [12]. It is accessible by irradiation of a natural Ho target by a proton or deuteron beam [13,14]. Its half-life of T1/2 = 10.36 h is compatible with radiolabeling of small molecules. To access 165Er, irradiation with proton and deuteron beam has been used. The conditions of separation of Er/Ho have been defined by determination of weight coefficients (Dw). Tests on a small column (2 mL) have been performed to validated elution parameters. First tests on semi-automation of the separation have been made to allow manipulation of more than 100 MBq of 165Er. The ratio 166+natHo/165Er has been determined to evaluate the efficiency of separation.
The access to the desired radionuclide might in some cases be challenging due to the irradiation path rather than to the radiochemical separation. Design of the target then becomes the key point. This is the case for 52Mn. It has a low average energy in β + and its range in biological tissues (244.6 keV, 0.63 mm) [15] is comparable to 18F (250 keV, 0.62 mm) [16,17]. These values are better than those of 51Mn (970.2 kev, 4.275 mm) in terms of Positron Emission Tomography (PET) resolution (ratio of 6). In addition, the short half-life of 51Mn (T1/2 = 46.2 m.) requires working with high activities to optimize radiochemical separations. Finally, the need to use enriched targets in 50Cr or 54Fe in case of 51Mn is a real obstacle. In first approach, to the implementation of radiolabeling studies, 52Mn (T1/2 = 5.59 days) has been suggested for the diagnosis and treatment of blood diseases [18], as a cationic perfusion tracer [19], and for the study of the involvement of manganese in the pathophysiology of degenerative neurological diseases [20]. To perform the first irradiations to determine Dw, according to the literature, irradiation of a target of Cr is necessary. Foil of Cr does not exist with convenient dimensions allowing direct irradiation to obtain 52Mn. Therefore, we have designed a target of Cr using powder of chromium.

2. Materials and Methods

2.1. Materials

All irradiations were made at the cyclotron of Orléans (a CGR-MeV 680 Type [21,22,23,24,25], (Figure 1) in a targetry named “hatch tip” (Figure 2) for the experiments presented in this work.
Ho and Cr elements were used to product various radionuclides. Commercial (Alfa Aesar) high purity foil of Ho (purity: 99.9%; thickness: 127 and 300 µm) was used. As commercial high purity chromium foil is not available with a thickness less than 500 µm without polymer support, chromium sample were made by sintering of high purity chromium powder (99%, 100 mesh metal basis density = 2.0–3.0 g/cm2). The chromium powder was pressed to obtain 13 mm (outer diameter) pellets.
Nitric acid (67–69%; SCP Science Plasma Pure; Fisher Scientific), hydrochloric acid (32–35%; SCP Science; Fisher Scientific), alcohol ethanolic (Fisher Chemical), AG1x8® resin anion exchange (200–400 mesh) (Bio-Rad Laboratories) and LN2 resin (Triskem). A small column in 2 mL polypropylene (PP) including frits (pore size = 20 µm) (PE: polyethylene) was used with internal diameter: 7 mm and a filling height of resin > 39 mm, reference AC-142-TK from Triskem. All water used for the dilutions had a resistivity of 18 MΩ and was prepared using Purelab (Veolia) (Ultrapure Water Purification System).
Activated samples were diluted and put in a tube in a determinated geometry. Activity measurements were assessed by ϒ-ray spectrometry with an HPGe (High-Purity Germanium) detector. The HPGe detector was calibrated in energy and efficiency for different geometries with certified standard radioactive sources (Cerca, France). For activity measurement, Υ-ray spectrum analysis software package, Genie 2000 (Canberra, France) was used. The concentrations of Er Ho, Cr and Mn were estimated following peaks centered at 53 keV for 165Er, 80 keV for 166Ho, 320 kev for 51Cr and 935 for 52Mn (744 and 1434 can be used too). All activities were determined at the end of beam (EOB).
For polishing the chromium target, Model ES 300GTL has been used. The magnetic putty (1, 3 and 6 µm) carpet for pre-polishing (graduation 120, 320, 600 and 1200) and carpet for polishing (1, 3 and 6 µm) came from ESCIL (France).

2.2. Methods for 165Er (an Emitter Auger Electron and Bimodality)

2.2.1. Irradiation

165Er has been the subject of some publications concerning various methods of production from a cyclotron or a neutron reactor. The neutron pathway leads to a very large range of activities but the result is “carrier added” (i.e., the presence of other isotopes of erbium). However, a ligand radiolabeling application has to be a “no carrier added” pathway. Therefore, irradiation with a cyclotron, starting from a different element, can be more interesting.
Irradiation of an erbium target (natural or enriched) by a proton beam will be according to the reactions: natEr (p, xn) 165Tm → (by decay) 165Er or natEr (d, xn) 165Tm → 165Er [25]. The irradiation of this natural target will lead to 165Tm (30.06 h) but also to 167Tm (T ½ = 9.25 days) and 168Tm (T ½ = 93.1 days). Indeed, the percentage (%) of every isotope on natural erbium is 0.139, 1.601, 33.503, 22.869, 26.978 and 14.910 respectively to isotope 162, 164, 166, 167, 168 and 170 of erbium.
To overcome this, the irradiation of a 166Er enriched target guarantees a single nuclear reaction such as: 166Er (p, 2n) 165Tm which is quite challenging as it is not an easy and cheap way to obtain 165Er for proof of concept.
The “easiest” way to access to 165Er is the irradiation of a natural holmium target by proton beam according to the nuclear reaction 165Ho (p, n) 165Er at 16 MeV or deuteron beam by 165Ho (d, 2n) 165Er at 17.5 MeV. The proton beam method can be exploited in a commercial cyclotron (less than 20 MeV). At the cyclotron of Orléans, two ways of production have been explored. All cross sections were known and obtained by irradiation or simulation from calculation codes (ALICE-IPPE) [12,13,26,27].
The ratio 165Er/166Ho produced by proton and deuteron beam is respectively of around 400/1 and 8/1. The origin of the production of 166Ho by proton irradiation is not clearly identified, but neutron activation seems to be the source.

2.2.2. Separation 165Er/166Ho

The major difficulty in the development of 165Er is its extraction from the holmium target. The selectivity factor for the couple Ho/Er (SF: Separation Factor around 1.5) is amongst the lowest in the lanthanides. In all publications relative to the irradiation of a Ho target, only one evokes a treatment of this target by a separation of the Ho/Er [11] pair. The complexing agent, α-HIBA (alpha-HydroxyIsoButyric Acid) is widely used in the separation of lanthanides [28]. However, these separations are often made at the analytical level with the use of an online chromatographic system (High-Performance Liquid Chromatography (HPLC)) on balanced mixtures or traces (some ng or pg) for each lanthanide. To separate a few ng of 165Er from of few mg of a target of about 200 mg of natural holmium becomes more complex. In addition, the separation conditions must allow the use of 165Er in radiolabeling of ligands aiming vectorised therapy with Auger electron or used in radiotracer for biomodality MRI/SPECT.
HDEHP (di(2-ethylhexyl) phosphoric acid), HEHEHP (mono-2-ethylhexyl ester of phosphonic acid) and (H[DTMPeP]) bis(2,4,4-trimethylpentyl) phosphinic acid are the main acidic organophosphorous extractants [29] used in Rare Earth Element (REE) separation processes and have also been commercialized (for Triskem commercial name: LN, LN2 and LN3). HDEHP has been widely used for primary separation because the distribution coefficients of the REEs as a group differ markedly from impurities in leach groups (e.g., in spent fuel actinides and REEs) [30]. For this project, LN2 resin (Triskem) based on (HEHEHP) was used. This reagent was chosen because REEs can be stripped at lower acidities than from HDEHP [31]. They were used for the separation of adjacent lanthanides including the separation of a microcomponent from a macrocomponent [32,33,34]. Weight coefficients Dw have been determined for various concentrations of HNO3. Additional evaluation of these coefficients on LN2 resin was performed with higher 166Ho activity using deuteron irradiation, which should allow more sensitivity. The results presented here are part of a more complete study about Ho/Er with comparison LN, LN2 and LN3 (in the case of LN3, it is necessary to use a low concentration of HNO3). The main drawbacks of HDEHP (LN) is a low adjacent separation factor, relatively low acidity for REE stripping, as well as low hydrolytic stability [35]. Phosphonic and phosphinic acids are more hydrolytically stable and effective extractants when compare with HDEHP. Moreover, they have demonstrated a high selectivity for the “heavy”REE (hREEs) compared to “light”REE (lREEs) [29].
For determination of distribution coefficient Dw, a target of natural Ho of 0.3 mm of thickness (196 mg) was irradiated during 2 h at 2 µA at 17.5 Mev deuterons (AEOB: Activity (EOB)): around 700 MBq of 165Er/90 MBq of 166Ho were produced then dissolved in 1 mL of 5 M HNO3 solution (no cut target for batch tests) and after that the complete dissolution of the target, adjusted to 5.5 mL with 18 MΩ water. This solution of 0.9 M HNO3 was the crude solution (concentration around 35 mg/mL of holmium and 13 MBq of 165Er/1.6 MBq of 166Ho). Around 100 mg of LN2 resin was weighed for each test, which was always done in triplicate. In every tube, LN2 resin was mixed with 100 µL of crude solution and volume was adjusted to 1.5 mL with different volumes of HNO3 and water 18 MΩ to obtain the final concentration of HNO3.
For example, at 0.5 M HNO3, 650 µL of 1 M HNO3 and 750 µL of 18 MΩ water were added to 100 µL of crude solution of 165Er/166Ho (initial concentration 0.9 M HNO3). Every tube was shaken for 30 min [36,37] then allowed to rest and centrifuged for 20 min. 500 µL of each solution were extracted and diluted to 2 mL by adding 1.5 mL 18 MΩ water (geometry called as “Tube 2G”). Then samples were measured at spectrometry γ in this defined geometry with acceptable dead time (<5%). For several tubes, it was necessary to allow for one to two days of decay to perform a measurement.
Capacity of LN2 resin adsorption is 0.16 mmol/mL: maximum of 26.4 mg of holmium can be used for 0.37 g of resin (1 mL). However, Triskem recommends a surety factor of 50% on the capacity of adsorption. For that, in all batch tests 100 µL of crude solution contained around 3.5 mg of natural Ho. In a concentration of 0.4 M HNO3, two tests (denote 0.4 100 and 0.4 200) with 100% and 200% capacity of resin had added, respectively with 200 and 400 µL of crude solution to evaluate this factor on values Dw and SF.
Weight distribution Dw (mL/g) and separation factor (SFEr/Ho) were calculated using the following equation:
D w = A 0 A e A e × V m
Here A0 and Ae are the liquid phase metal activities (Bq) before and after equilibrium, m is the weight of the LN2 resin in grams and V is the volume of liquid phase in mL.
S F E r / H o = D w ( E r ) D w ( H o )
Then tests on a 2 mL column with around 0.37 g of LN2 resin (1 mL) were made first by the gravimetry method then with variation of flow (1 mL/min and 3 mL/min) at atmospheric pressure using a peristaltic pump in the outlet of the column. A gradient of concentration on HNO3 was used: 0.4 M 0.8 M, 1 M and 2 M or/and 5 M if necessary. Tests at 1 bar of Nitrogen (maximum pressure of solenoid valves from Bio-Chem (used in semi-automated system) is 1.4 bars) were made. Around 4 g of LN2 (for a maximum of mass target of 140 mg, around 11 mL) 50–90 mg of the target were used in semi-automated tests. Four tests on a homemade automation system (drive with the homemade software ACCRA (Automatisme & Contrôle Commande Radiochimie)) were made using the remote control sketch below (Figure 3) from the dissolution step of the target until the final evaporation step of HNO3.
In a semi-automated system 50 µL of solution were collected manually to determine the extraction yield of radionuclide in each test after adding 2 mL of 0.3 M HNO3 in the reactor. The reactor was weighed before and after addition of 0.3 M HNO3 (no weighing for test n°3: no extraction yield). This was the activity reference for 165Er and 166Ho (Aref: deposited activity). With these values, the initial activity of 165Er and 166Ho in the cut target were determined. A relationship activity-weight was established by the ratio 165Ho/166Ho: activity of 166Ho in Bq by mg of 165Ho (cut target). the initial ratio Ho/165Er (for Ho, 165Ho was considered because the mass of 166Ho was insignificant) on the target (cut target mass) and the ratio in an isolated fraction of 165Er was calculated. A Ho decontamination factor was determined according to the following formula:
F H o   ( c o n t . ) = A 0 ( H o ) 166 / A c t f ( H o ) 166 A 0 ( E r ) 165 / A f ( E r ) 165
  • F H o   ( c o n t . ) : Contamination factor in Ho
  • A 0 ( H o ) 166 : Activity 166Ho in cut target
  • A f ( H o ) 166 : Activity 166Ho in isolated fraction of 165Er
  • A 0 ( E r ) 165 : Activity 165Er in cut target
  • A f ( E r ) 165 : Activity 165Er in isolated fraction of 165Er
All dilution factors were determined by weighing aliquots of fraction. A geometry “Tube 2G” was used to determine the activities of the samples. Extraction yield (%) was defined as:
Y   ( % ) = A c t i v i t i e s   a l l   t u b e s A r e f
  • A c t i v i t i e s   a l l   t u b e s : sum of all activities in fraction tubes for one radionuclide (166Ho or 165Er)
  • Aref: deposited activity on column.
The same column was used and between different tests (4), column is conditioned with 30 mL of 5 M HNO3 then 18 MΩ water until pH was neutral. Then, 30 mL of 0.3 M HNO3 was used to conditioning column. Manually target was cut and around 50% of target was dissolved (more than 90% of activity of target). All weights listed for the target were referenced to cut the target (not all the irradiated mass of the target). The height of the column (glass) was 14 cm and the inner diameter 1 cm. The LN2 resin was shaken for 30 min with 18 MΩ water then put on the column. It was conditioned with 20 mL of 18 MΩ water then 30 mL of 0.3 M HNO3 before depositing the sample. Then, the cut target was dissolved in 1 mL of 5 M HNO3 in a reactor of 3 mL. Nitric acid was evaporated until it was in a pink gel formation. Then 2 mL of 0.3 M HNO3 was added to dissolve the pink residue and transfer it to the column under flow of nitrogen (20 mL/min). The solution on top of column was adsorbed under the flow of nitrogen (100 mL/min). When the solution on top of the column was adsorbed, 0.4 M HNO3 (100–120 mL) was used to elute Ho at flow of 1–2 drops/s (1 mL/min) under 1 bar of Nitrogen (at flow of 100 mL/min). Then 1 M HNO3 was used (around 40 mL except for sample 3 (22 mL)) and finally, in some cases, 2 M (15 mL for sample 3) and 5 M HNO3 (sample 1 and 3) more to elute residue activity on the column. The radiotracer method was used for this separation using 166Ho for Ho and 165Er for Er.

2.3. Methods for 52Mn (Radioimmunotherapy and Bimodality)

To obtain this radionuclide from a cyclotron, the irradiation of chromium by a proton beam is the most used route, by the reaction 52Cr (p,n)52Mn to 16–17 MeV [38], because it is also the most accessible by commercial cyclotrons. Then, the separation of 52Mn from a chromium target was carried out by liquid–liquid extraction [39], but the most interesting results concern the use of an ion exchange resin [40,41]. This route seems more suitable for subsequent automation of the separation step. The choice of the best way to access 52Mn must be focused in part on the simplicity of the separation process. Indeed, because of its three high gamma rays with an emission of more than 90%, the radiation safety for operators is a paramount criterion. Here, a target design (Cr pellet) is described in detail. Various studies have been made to validate the specifications of a pellet of chromium for irradiation.
As chromium is a compound that oxidizes very easily with air, the sintering of Cr powder has to be done in an inert or reducing atmosphere in an electrical furnace (Nabertherm with controller P 320). Therefore, we used an H2/N2 mixture (5% hydrogen). In addition, to ensure that the chromium does not react with the residual oxygen, we surrounded it with crushed graphite. We placed the whole in an alumina crucible (Figure 4):
Finally, we proceeded to the heat treatment with the following thermal cycle:
  • Temperature rise rate: 5 °C·min−1
  • Isothermal run time, 30 min
  • Cooling speed: 5 °C·min
The same program was used in vacuum conditions. The vacuum was 10−7 mBar and the furnace is a homemade system where the measurement of temperature is determined by pyrometry. The sample was put on a block next to a block of molybdenum. By measuring the emissivity of molybdenum, the temperature of the sample was determined.
After sintering, Cr pellets were tested in bending conditions (to determine stress resistance of pellet). The device used was unconventional and inspired by the “Ball on ring” test (Figure 5). A moving speed (0.5 mm/min) of a ball of alumina (9.32 mm diameter) was applied. The measurement stops when the target broke. To compare mechanical properties in bending conditions of each Cr pellet, we compared the load required to break the pellet.
Using a target of Cr designed (800 mg pressed at 8.3 tons and sintered 1 h at 800 °C), a first determination of Dw for separation Cr/Mn was done. The radiotracer method was used to follow two elements 51Cr for Cr and 52Mn for Mn. To obtain a significant activity of 51Cr, irradiation of the Cr pellet was performed at 23 MeV. In these experimental conditions, nuclear reactions natCr (p,n)52Mn and natCr(p,x)51Cr occurred.
For the resin exchange anions, the AG1x8® resin was used and different concentrations of HCl (1, 4, 8 and 12 M) and various percentages of Ethanol (0 and 93 to 98% by step of 1%) in eluted solution (ethanol/HCl) were tested. Contact time was 1 h instead of several hours reference studies [14,40].
Briefly, a Cr pellet of around 800 µm of thickness (800 mg) was irradiated during 0.5 h at 0.2 µA(EOI: around 2.9 MBq of 52Mn/1.45 MBq of 51Cr). The target was dissolved in 5 mL of 12 M HCl and evaporated to dryness. Then, we dissolved the residue with 2 mL 2 M HCl. This was the crude solution of 52Mn/51Cr. Around 80 mg of AG1x8® resin were weighed for each test (all tests were triplicated). In every tube, AG1x8® resin was mixed with 970 µL of elution solution. Then 30 µL of crude solution was added. Every tube was shaken for 1 h then allowed to rest, and finally centrifuged for 10 min. 500 µL of each solution were extracted and diluted to 2 mL by adding 1.5 mL 18 MΩ water. Then samples were measured at spectrometry γ in this geometry called “Tube 2G” with acceptable dead time. For several tubes, it was necessary to allow for one to two days of decay to perform a measurement. All calculations were made according to Equations (1) and (2) in Section 2.2.2. Separation 165Er/166Ho.
For a test of the semi-automation of Cr/Mn separation, a 1.2 mL of dissolved chromium solution (eluent 1: Ethanol/HCl 12 M (97/3)) was used. No calculations of a decontamination Cr factor were done. This aliquot which contained 35,000 Bq of 51Cr and 3100 Bq of 52Mn, was deposited on column 1. Three columns with 300, 200 and 100 mg of AG1x8® resin were used, respectively, as columns 1, 2 and 3. The sample was deposited on column (all have been conditioned with 10 mL of water 18 MΩ, then 10 mL ethanol and finally 10 mL of eluent 1). Column 1 was eluted first with 8 mL of eluent 1 then rinsed with 10 mL of eluent 1 divided into 3 fractions of 3 mL. Finally 1 mL of HCl 12 M was used to recover 52Mn. An aliquot of this fraction was used to quantify 51Cr and 52Mn. 30 mL of pure ethanol were added and mixture was shaken 10 min then deposited on column 2. After that, 3 mL of eluent was added and 1 mL of HCl 12 M desorbed 52Mn. After collecting the fraction for measurements, 30 mL of pure ethanol was added and the batch shaken for 10 min. The batch was adsorbed on column 3 and eluted with 3 mL of eluent 1. Finally, 52Mn was desorbed with 1.5 mL of 12 M HCl.
For optimizing this process and reducing the quantity of chromium, pre-polishing and polishing on the chromium target was made like this:
Pre-polishing is necessary to reduce dramatically thickness of pellet:
  • 30 min with carpet of 120 at 100 rpm;
  • 8–10 min with new carpet of 120 at 100 rpm.
Then, the thickness was checked because on following operations, every carpet decreased in thickness by about 100 µm around:
  • 5 min with carpet of 320 at 100 rpm;
  • 10 min with carpet of 600 at 100 rpm;
  • 20 min with carpet of 1200 at 100 rpm;
  • 30 min with carpet of 6 µm at 100 rpm;
  • 45 min with carpet of 3 µm at 100 rpm;
  • 45 min with carpet of 1 µm at 100 rpm.
When illustrations showed polished samples, only the polishing step was taken.
Irradiation tests and separations were performed on unpolished targets.

3. Results

3.1. 165Er

Concentrations of 0.3 M, 0.4 M, 0.5 M, 0.8 M, 1 M, 2 M and 5 M HNO3 were evaluated for the separation at 50% of capacity adsorption of resin. They were also evaluated for concentration 0.4 M 100% (point 0.4 100) and 200% (0.4 200) of capacity (Figure 6).
Weight distribution Dw (mL/g) and separation factor SFEr/Ho was determined (Table 1):
There was no difference between SFEr/Ho at 0.3 and 0.4 M HNO3 but Dw were high in the case of 0.3 M HNO3: concentration for dissolution of target. Then, to start elution 0.4 M HNO3 can considered a better choice than 0.3 M HNO3. The separation factor was influenced by % of capacity resin involved in separation: at 200% of capacity, this factor SF decreased significantly and Dw was weaker. At this ratio, selectivity was low and a significant part of the erbium could be eluted with holmium. That is why some tests of elution on a 2 mL column were done with the following conditions: target dissolved in 0.3 M HNO3, starting elution of batch with 100–120 mL 0.4 M or gradient with 0.4 M/0.8 M HNO3 before desorbing holmium with 1 M HNO3 and then erbium. If 1 M HNO3 was used directly, no separation was done, but using 0.4 M HNO3 generated a difference of elution between Ho and Er more important than the other eluent.
On a 2 mL column, by gravimetry, time elution was more than 1 h with 370 mg of resin LN2. There was no influence of flow between 1 mL/min and 3 mL/min in separation only in separation time. At 1 bar of nitrogen, the flow was too quick and was reduced to 1 mL/min in setting pressure of nitrogen to 0.7 bars.
With these previous tests, a semi-automated system of separation of Ho/Er was evaluated on a column of 4 g of LN2 resin (Table 2).
The isolated fraction in all samples (Table 3) contained more than 60% (72.3 ± 5.1 % (n = 4)) of 165Er activity.
The separation profile is illustrated in Figure 7 with the sample 3.
The extraction yields of erbium and holmium were higher than 90% (except sample 4). A Ho decontamination factor was calculated on sample 1, 2 and 4 (not possible for 3 because no reference activity Aref (deposited activity on top of column)). The semi-automated separation system was significantly reduced quantity of holmium on isolated fraction of 165Er by more than a factor 1294 ± 1183 (n = 3) (Table 4).

3.2. 52Mn

3.2.1. Design Target Conception

In order to obtain 52Mn, a natural chromium target was irradiated by a proton beam. Once irradiated, the target was then chemically treated to isolate 52Mn from Cr. However, the preparation of this target requires special attention. No commercial Cr foil exists with a thickness less than 500 µm without polymer support. However, this element is commercially available in the form of powder. Because of the risks of cyclotron contamination, powdery targets are difficult to irradiate. A Cr pellet was therefore designed taking into account the following criteria: the risks of contamination during irradiation, dissolution of the target, limitation of the amount of chromium not activated in radiochemical separation (possibly through lower thickness). For these purposes, the physical aspects of the target such as mechanics, thermal resistance and porosity (closed and opened porosity) were studied.

3.2.2. Compaction

A study about optimization of parameters (force, mass and time of compaction of pellets) was made to obtain a pellet of 13 mm diameter with good visual mechanical resistance. First, a force of 8.3 tons was applied on the powder during 5 min. Several quantities of powder were tested from 200 to 1200 mg (Table 5). The aim was to obtain a complete pellet with a lower mass.
Tests were carried out to reduce this mass (therefore the thickness) by varying time and compaction force. Results obtained are presented on the following Table 6.
Eleven pellets were made with better conditions of compaction, of 650 mg 30 min at 8.3 tons (300 bars) with a good visual aspect and these were added to 4 obtained in first tests (Table 6). Thus a variability, was made among 15 pellets:
  • weight average 649.6 ± 0.6 mg (15),
  • thickness = 0.87 ± 0.02 mm (13) (2 broken pellets by manipulating).

3.2.3. Sintering

Despite compaction, the pellets remained fragile. This was a problem for the irradiation as it means that in contact with a beam of high intensity, the pellet was likely to crumble or break. In order to improve the mechanical strength of the pellets, a study of sintering heat treatment was carried out on the pellet at various temperatures and different specific conditions of sintering (in air, vacuum and inert atmosphere).
The first tests were operated under atmosphere controls in oxygen (500 °C to 1400 °C) (Figure 8). A bending test has been performed to check the flexural strength of the pellet. A load was applied, via a ball, to the center of the sample that would be biased in bending [42,43]. The force applied was recorded as a function of the vertical displacement of the ball. The tests were carried out on pellets of 800 mg of compaction at 8.3 tons during 5 min, sintered at 500 °C, 800 °C and 1000 °C for 1 h. Each test was repeated three times. Recording was stopped when the ball was cracked.
Subsequently, the average maximum stress resistance was determined (Figure 9).
We could observe that stress resistance increases with sintering temperature; however, above 800 °C no differences appeared. This higher stress resistance could be explained by a decrease of porosity as the temperature of sintering increases. An optimization of conditions of sintering was made at 600 and 800 °C with 650 mg and 800 mg pellets (Table 7).
According to these results, a temperature of 800 °C was necessary to obtain a good resistance structure. The presence of oxygen or a H2/N2 atmosphere during the sintering have no influence on the mechanical properties. It only influences the chemical composition of the pellet: in the presence of oxygen, a high amount of chromium oxide appears during the heat treatment.

3.2.4. Dissolution of Target

Tests of dissolution were then made on various pellets (variation of temperature of sintering) with 12 M HCl and heating at 200 °C on a block. These results were obtained with a pellet of 800 mg 5 min of compaction at 8.3 tons.
Dissolution tests have been shown to have difficulties solving the target sintered up to 1000 °C, but it was not necessary to complete the dissolution of pellet to extract all the 52Mn [41]. However, the results reported in Table 8 would be very useful for optimizing target dissolution.
Although sintering at 600 °C could be suitable for the dissolution of the pellet, the breaking strength remains an essential criterion in the choice of the preparation. The sintering at 800 °C was selected for the design of this target. For the development of the separation method, this target was used (however, the thickness was still substantial at 900 μm for a weight of 650 mg).
The dissolution of the Cr pellet by hydrochloric acid solution starts at the grain boundaries and increases the porosity. Scanning Electron Microscope (SEM) observations confirm that grain boundaries are attacked and material becomes more porous after the dissolution step (Figure 10).
For temperature higher than 600 °C, the densification is very high. The residual porosity is too low, the reactive surface is, therefore, too small and the acid cannot penetrate the core of the material.
Chromium is a compound that oxidizes very easily: a small amount of chromium oxide crystallizes during the sintering step or during dissolution when in contact with the acid. Chromium oxide is a stable compound that is impossible to dissolve. During dissolution, the acid solution is charged with chromium ions. At 600 °C, if 10 mL of hydrochloric acid is set from the beginning, and the pellet does not dissolve. In contrast, an initial addition of 20 mL allows complete dissolution.
During sintering, the pellet is in the presence of carbon to avoid oxidation. It is possible that chromium carbide is formed and can then limit the dissolution (Figure 11) [44].
Nevertheless, it should be noted that the higher the density, the more difficult it is to attack with the acid during dissolution because the grains are very close. Indeed, a pellet sintered at 650 or 800 °C does not dissolve completely while a sintering at 600 °C dissolves completely.

3.2.5. Porosity of Target

To validate these explications, more investigations were undertaken. First, average density of the Cr pellet was determined at different conditions of sintering (by weighing pellets and measurement of thickness and diameter) (Table 9):
As the sintering temperature increases, the density increases. Before sintering, the density of the 800 mg pellet was 73%. After sintering, the density increased. A heat treatment was used to densify the material (Figure 12). It is clear that the porosity decreased. Grains were close together or even welded.
The porosity of the pellets was then defined: this was opened and closed porosity. The closed porosity corresponds to a pore which is isolated from the others and which does not communicate with the outside. On the contrary, we observed opened porosity when the pores communicated with the outside. The results obtained are summarized in the following Figure 13.
These results show that the non-sintered chromium pellets is very porous. The higher the sintering temperature, the lower the porosity obtained. Therefore, when the porosity was very low, the attack of the acid for dissolution was difficult because the acid could not penetrate the core of the pellet and attack grain boundaries and grains. This may also explain why a pellet sintered at 600 °C dissolved easily while sintering at 800 °C did not completely dissolve.
To understand the ability to dissolve as a function of the sintering temperature, the evolution of the microstructure as a function of temperature was followed. For this, observations in optical microscopy and SEM were performed. Some micrographs are presented in the following Figure 14 and Figure 15.
The heat treatment of the Cr pellet in N2/H2 atmosphere and in a crucible containing graphite powder induced the formation of small areas of chromium oxide (because of residual oxygen adsorbed in the porosity) and the formation of a chromium carbide, when the temperature was higher, for example 1400 °C: chromium carbide was formed from the chromium of the pellet and the carbon powder. During the dissolution step, these two compounds will not facilitate the attack of the pellet with hydrochloric acid.
X-ray diffraction (XRD) analysis was performed on a pellet sintered at 800 °C (Figure 16). These results highlights the presence of chromium metal in the majority phase and the presence of traces of eskolaïte Cr2O3. This result is consistent with observations and analysis made by SEM.

3.2.6. Dw in Separation of Cr/Mn

Figure 17 presents these results. With an eluent without ethanol, no separation between Cr and Mn was observed. An ethanolic eluent (93 to 98%) modified impressively this separation. Cr was not retained on AG1x8® resin whereas Mn was and Dw was bigger as HCl concentration of the eluent solution increased.
These results were in agreement with literature [40] but, in our case, less activity was undertaken for nuclear safety considerations and less contact time (1 h). Agreements of Dw with published results have led us to make a first test of the semi-automation of the Cr/Mn separation.

3.2.7. Semi-Automated Separation of Cr/Mn

It is necessary to modify the remote-control sketch of 165Er for use in the extraction of 52Mn, and this requires three columns at least to obtain a suitable separation (Figure 18).
Results for the first test, with weak activity, on a semi-automation of separation Mn/Cr are listed in Table 10.

3.2.8. Reduction of Pellet Thickness

To optimize the target design of a Cr pellet, a reduction of the target thickness and, by this way, a limitation of non-irradiated Cr mass, polishing is a useful solution.
This operation reduced the amount of chromium handled during the extraction process. Thickness was reduced by one third (from 900 µm to 350 µm) and the oxide layer on surface of target was removed.

4. Discussion

The cyclotron of Orléans is a multipurpose research accelerator (proton, deuteron and alpha at various energy from 10 to 45 MeV). With these specifications, more radionuclides can be accessed than in a commercial cyclotron. In this work, we demonstrate its capabilities for development of exotic radionuclides like 165Er and 52Mn. It is a wonderful tool for a radiochemist to product radionuclides aimed at imaging as well as analytical applications too (radiotracer method). But, with energy of 30 MeV, most of SPECT isotopes are produced by reactions (p, 2n) or (p, 3n) [45]. Even when one has the choice between (p, n) and (p, 2n), e.g., for 67Ga one favors (p, 2n) reaction for the yield (thicker targets, less warming by µA). For these two radionuclides produced at the cyclotron of Orléans, the first tool developments for separative radiochemistry have been made.
In the case of 165Er, separation Er/Ho needed to be better understood and a real improvement could also be made to facilitate semi-automation.
For a limited volume of isolated 165Er fraction with elution of 1 M HNO3, a NaI detector with two windows at 53 keV and 80 keV could be a solution. On the other hand, more detailed developments on geometric parameters on the elution curve are necessary because LN2 resin has a limited capacity for adsorption.
Semi-automation proved necessary with increased activity of 165Er by the deuteron method. A more sensitive evaluation of the quality of a 165Er batch and its ratio 166+165(nat)Ho/Er must be performed more carefully regarding the quality of the irradiated target and the by-products generated. Additional analysis by ICP–MS is necessary to complete these validations. At least, this protocol of separation Ho/Er can already be adapted as it answers issues of radiolanthanides extraction where the separation of micro- from macrocomponents is crucial.
This work made it possible to obtain a Cr target for the production of 52Mn for irradiation and method development tests: 650 mg of powder sintered at 800 °C for 1 h (thickness 900 µm).
In a detailed analysis of results of compaction, a test at 4 tons on 650 mg pellet gave a bad visual aspect and greater thickness of 1000 µm than those made at 8.3 tons (900 µm): density must be lower which is not interesting for an irradiation (mechanical firmness). A surprising result is compaction of 60 min at 8.3 tons on 650 mg pellet that gave a bad visual aspect. This can be explained by the fact that its time in pressed state can generated micro crack. Then, when the pellet is relieved of stress, the pellet cracked.
Regarding the conditions of sintering, at vacuum no difference with a pellet not-sintered has seen. This can be perhaps explain by system of sintering: temperature has defined by emissivity of molybdenum where pellets are put. A second explanation might be that more vacuum is, less tension surface on grain is. With a reduction of tension surface, grain boundaries are more difficult to form.
Between 600 °C and 800 °C, resistance rupture is twice as big. There is no relation between weight and resistance rupture. The optimum temperature of state transition is between 600 °C and 800 °C. Resistance rupture is less altered by the weight of the pellet than the temperature.
Breaking measurements must be carried out on the polished targets of 300–400 μm thickness as well as dissolution tests.

5. Conclusions

The production of 165Er from a natural Ho target was obtained via deuteron irradiation. This form of irradiation generated more activity than the proton method, with much activity of 166Ho (a radiotracer for Ho). LN2 resin (from Triskem) was used to separate Er and Ho with nitric acid solution. Selectivity between two radiolanthanides was weak (SF Er/Ho = 2.75 at 0.4 M HNO3) but an isolated fraction with 72.3 ± 5.1% (n = 4) of initial 165Er activity can be achieved by an appropriate gradient of elution with 0.4 M (120 mL) and 1 M HNO3 (40 mL). In this fraction, the mass of holmium was reduced by a factor 1294 ± 1183 (n = 3). Regarding 52Mn production, a design of the target has been established: a Cr pellet of 800 mg compressed at 8.3 tons (300 bars) and sintered at 800 °C. Elution on AG1x8® resin with a mixture of ethanol/HCl (12 M) (97/3 (v/v) gave good results for the separation of 51Cr from 52Mn. A test of semi-automation separation using three columns was made with a diluted solution of 51Cr and 52Mn. A global extraction of 47% on 52Mn was obtained.
For these two radiometals, 165Er and 52Mn, results were encouraging for the following experiments: some improvements are underway concerning the irradiation and the targeting. For the separation, a methodology about more detailed developments on geometric parameters on the elution curve must have been set. The first results of the Er/Ho and Mn/Cr separation on a semi-automated system demonstrated the versatility of the homemade system. However, these tests have been shown to require more reliability and reproducibility in the separation step with a better follow-up on line using adapted sensors.

Author Contributions

E.D. and F.D. worked on production of radionuclides for the ratiotracer method (definition of beam) and developed the simple tool to predict a nuclear reaction for a radiochemist; J.V. and M.G. worked on the design of the Cr-target and performed experiences on chemical and physical specifications of Cr-pellet; M-L.B. contributed to the design of the Cr-target through knowledge in materials and methods of analysis; G.A. (spectrometry γ), E.S. (52Mn) and C.R. (165Er) performed the experiments for determination of Dw and tests of resin; L.F. designed the automation of the process and analyzed the data by spectrometry γ; A.B. contributed reagents/materials/analysis tools and the definition of Er/Ho separation by using resin LN2 (Triskem); I.D.S. conceived the radiotracer methods, defined conditions of experiments and participated in all steps of these various works, and wrote the paper; I.D.S. would like to thank G. Junot (64Cu), K. Blanchard (64Cu), D. Barré (11C), A. Fournier (64Cu), L. Colas (11C), L. Léost (64Cu), A. Sabourin (11C), C. Dupressoir (64Cu) and N. Mialon (11C) for their work contributing to the setup of radiochemistry at the cyclotron of Orléans and, indirectly, to this article.


This research had financial support of Triskem Society and AAP—Défi 2017 “Instrumentation aux limites “project “CiSCoTe”: Cible Solide irradiée Contrôlée en Température”. It funded too by the French National Research Agency (grant ANR-13-JS07-0007).

Conflicts of Interest

The authors declare no conflict of interest.


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Figure 1. The cyclotron of Orléans.
Figure 1. The cyclotron of Orléans.
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Figure 2. Targetry “hatch tip” low current (<2 µA) for development.
Figure 2. Targetry “hatch tip” low current (<2 µA) for development.
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Figure 3. Remote control of Er/Ho separation.
Figure 3. Remote control of Er/Ho separation.
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Figure 4. Set-up of sintering.
Figure 4. Set-up of sintering.
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Figure 5. Bending test.
Figure 5. Bending test.
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Figure 6. Dw de Er/Ho with LN2.
Figure 6. Dw de Er/Ho with LN2.
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Figure 7. Profile of elution 165Er/166Ho of sample 3.
Figure 7. Profile of elution 165Er/166Ho of sample 3.
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Figure 8. Micrography of polished samples before and after sintering at (800 °C).
Figure 8. Micrography of polished samples before and after sintering at (800 °C).
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Figure 9. Comparison of maximum stress of various sintered target.
Figure 9. Comparison of maximum stress of various sintered target.
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Figure 10. Scanning electron microscope (SEM) micrograph (mode BSE (back-scatter electron). of sintered pellet at 800 °C, before and after dissolution.
Figure 10. Scanning electron microscope (SEM) micrograph (mode BSE (back-scatter electron). of sintered pellet at 800 °C, before and after dissolution.
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Figure 11. Cr-C phase diagram.
Figure 11. Cr-C phase diagram.
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Figure 12. Micrograph of non-sintered pellet at left and sintered pellet at 1300 °C at right.
Figure 12. Micrograph of non-sintered pellet at left and sintered pellet at 1300 °C at right.
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Figure 13. Evolution of the porosity of the Cr pellet with the sintering temperature.
Figure 13. Evolution of the porosity of the Cr pellet with the sintering temperature.
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Figure 14. Micrography of a 800 mg Cr pellet before sintering (optical microscope).
Figure 14. Micrography of a 800 mg Cr pellet before sintering (optical microscope).
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Figure 15. Micrography of a 800 mg Cr pellet after sintering and polished (SEM).
Figure 15. Micrography of a 800 mg Cr pellet after sintering and polished (SEM).
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Figure 16. XRD diffractograms of pellet before and after sintering at 800 °C.
Figure 16. XRD diffractograms of pellet before and after sintering at 800 °C.
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Figure 17. Dw of Mn and Cr.
Figure 17. Dw of Mn and Cr.
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Figure 18. Remote control of Mn/Cr separation.
Figure 18. Remote control of Mn/Cr separation.
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Table 1. Dw and SF of Er and Ho in HNO3.
Table 1. Dw and SF of Er and Ho in HNO3.
HNO3Dw (Er)Dw (Ho)SF Er/Ho
0.3 M45.7 ± 1.316.7 ± 0.42.74
0.4 M30.8 ± 2.011.2 ± 0.52.75
0.4 M 10015.4 ± 1.25.8 ± 0.42.70
0.4 M 20010.5 ± 1.14.7 ± 0.22.25
0.5 M23.4 ± 1.58.6 ± 0.42.71
0.8 M10.4 ± 0.23.9 ± 0.12.65
1 M5.4 ± 0.22.6 ± 0.12.11
2 M3.0 ± 1.01.8 ± 0.41.67
5 M0.1 ± 0.4−0.4 ± 0.3−0.21
Table 2. Elution of 4 samples on semi-automated system separation of Er/Ho.
Table 2. Elution of 4 samples on semi-automated system separation of Er/Ho.
Volume of Eluent (mL)Repartition of Ho (%)Repartition of Er (%)
HNO3 0.4 M10210412311087.982.490.989.
HNO3 1 M4538223812.
HNO3 2 MN.u.N.u.15N.u.--0.1- 75.7
HNO3 5 M45N.u.5N.u.0.0 0.0 0.0 0.0
N.u.: Not used.
Table 3. % of 165Er and 166Ho in isolated fraction against all fractions.
Table 3. % of 165Er and 166Ho in isolated fraction against all fractions.
SampleHNO3Isolated Fraction of 165Er
VolumeConcentration% of Rn
mean 0.1372.3
σ 0.145.1
% of Rn: percentage of radionuclide in isolated fraction against all fractions.
Table 4. Analysis of isolated fraction from 4 tests on semi-automated separation system.
Table 4. Analysis of isolated fraction from 4 tests on semi-automated separation system.
TestExtraction YieldCut TargetIsolated Fraction of 165ErF Ho (cont.)
Y (%)Mass (mg)Activity (Bq)Ratio 165Er/166HoActivity (Bq)Ratio 165Er/166Ho
1929888.49.5 × 1068.0 × 1078.45.7 × 1035.4 × 10793971123
2959857.46.3 × 1065.2 × 1078.31.4 × 1033.0 × 10721,0702553
3NDND53.8NDNDND3.1 × 1032.6 × 1078356ND
4868674.78.3 × 1067.2 × 1078.61.7 × 1033.0 × 1071773206
Mean9194 8.4 10,1491294
σ (n = 3)57 0.2 6950 *1183
* (n = 4).
Table 5. Various mass of pellet of Cr.
Table 5. Various mass of pellet of Cr.
Powder (mg)PelletDescription
200 Instruments 02 00015 i001pellet incomplete
400 Instruments 02 00015 i002pellet incomplete
600 Instruments 02 00015 i003pellet incomplete
800 Instruments 02 00015 i004pellet perfect
1200 Instruments 02 00015 i005pellet complete but too thick
Table 6. different masses and thicknesses of the pellets.
Table 6. different masses and thicknesses of the pellets.
Force Tons (Bars)Mass Powder (mg)Time Compaction (min)Thickness (mm)Visual Aspect
4 (150)649.651.08Bad
8.3 (300)599.7 (3) *50.89 (3)Bad
650.6 (3) *20.88Good (2) **
650.8 (2) *50.93Good
650.2 (4) *300.9Good
650 (2) *600.89Bad
699.6 (3) *20.96Good (2) **
699.4 (3) *50.95Good
* () number of tests; ** () number of tests with described visual aspect.
Table 7. Mechanical resistance for different masses and thicknesses of the pellets.
Table 7. Mechanical resistance for different masses and thicknesses of the pellets.
Mass (mg)Time Compaction (min)Sintering ConditionsT (°C)Resistance Rupture (MPa)Standard Deviation (MPa)
65030No sintering/122
V.: vacuum/C. A.: Controlled Atmosphere/C. A.N.: Not Controlled Atmosphere.
Table 8. Dissolution of target.
Table 8. Dissolution of target.
Sintering T (°C)130012001000800650600600550500
Volume 12 M HCl (mL)5 + 55 + 510101010201010
T(°C) heating100200200200200200200200200
DissolutionP.P.P.P.P.P.C. (20 min)C. (10 min)C. (10 min)
% Weigh dissolved in 30 min657576808080100100100
P.: Partial/C.: Complete.
Table 9. Evolution of pellet density relative to sintering temperature.
Table 9. Evolution of pellet density relative to sintering temperature.
Temperature (°C)500550600650800
Density (%)7680757782
(% of theoretical density of Cr for the same volume).
Table 10. Extraction yield in semi-automation separation of Mn/Cr.
Table 10. Extraction yield in semi-automation separation of Mn/Cr.
VolumeY (%)
Column 1Sample8.291.20.0
Eluent F13.72.80.0
Eluent F23.40.60.0
Eluent F33.30.30.0
HCl 12 M1.30.076.5
Column 2Sample29.60.00.0
Eluent F13.40.00.0
HCl 12 M1.00.081.7
Column 3Sample21.80.00.0
Eluent F13.50.00.0
HCl 12 M1.50.083.8
Global Yield (%) 94.946.7 *
Chromium was recovered in the first batch: it was not so much adsorbed on column 1 as was 52Mn. Global recovery of 52Mn was less than 50% (* calculated on the final batch of 52Mn: initial activity/final activity in batch).

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