WO1998002594A1 - Selective separation of dissolved metal species with substituted 1,3,5 triazine extractants - Google Patents

Selective separation of dissolved metal species with substituted 1,3,5 triazine extractants Download PDF

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WO1998002594A1
WO1998002594A1 PCT/GB1996/001700 GB9601700W WO9802594A1 WO 1998002594 A1 WO1998002594 A1 WO 1998002594A1 GB 9601700 W GB9601700 W GB 9601700W WO 9802594 A1 WO9802594 A1 WO 9802594A1
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triazine
metal species
compound
heterocyclic
organic phase
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PCT/GB1996/001700
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French (fr)
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Michael James Hudson
Gabriel Yee Shun Chan
Pascal Baron
Charles Madic
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Commissariat A L'energie Atomique
The University Of Reading
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Application filed by Commissariat A L'energie Atomique, The University Of Reading filed Critical Commissariat A L'energie Atomique
Priority to PCT/GB1996/001700 priority patent/WO1998002594A1/en
Priority to JP50570098A priority patent/JP3901736B2/en
Priority to EP96924093A priority patent/EP0850322B1/en
Publication of WO1998002594A1 publication Critical patent/WO1998002594A1/en

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D401/00Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom
    • C07D401/14Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing three or more hetero rings
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/26Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
    • C22B3/36Heterocyclic compounds
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B60/00Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
    • C22B60/02Obtaining thorium, uranium, or other actinides
    • C22B60/0295Obtaining thorium, uranium, or other actinides obtaining other actinides except plutonium
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Definitions

  • the present invention relates to certain 1,3,5- triazines having heterocyclic substituents at the 2,4 and 6-positions, some of which are novel compounds.
  • the heterocyclic groups may be nitrogen-containing heterocycles such as pyridyl or quinolyl.
  • the heterocyclic substituents are selected to give the species hydrophobic character. This may be effected by the presence of hydrophobic substituents (e.g. alkyl groups) on the heterocyclic rings.
  • the invention also relates to the synthesis of the triazines and their uses as solvent extraction reagents for the separation of metal-containing species.
  • metal-containing complexes formed by the interaction of the above triazines with the metal- containing complexes may have different chemical and/or physical properties from the original metal-containing species, and these properties may be exploited.
  • a metal species in aqueous solution or suspension may be extracted by reaction with one of the above triazines, followed by solvent extraction to take the species formed into a different, typically organic, phase.
  • selectivity of the combination of the metal-containing species with the above triazines followed by solvent extraction can give an improved process for selectively removing a particular metal or class of metals e.g. separation of actinides (An), from lanthanides ( n ) .
  • separation of trivalent americium [Am(III)] from trivalent europium [Eu(III)] by the above reagents is embodied in this invention.
  • TPTZ 5-triazine
  • the present invention is primarily concerned with the incorporation of substituents in triazines so as to improve their hydrophobic and selectivity properties.
  • the invention provides a 1,3,5 triazine having a heterocyclic substituent at each of the 2,4 and 6 positions (the three substituents being the same or different). At least 1 or 2 and preferably all of the heterocyclic substituents are selected to give the triazine external hydrophobic character ( facilitating extraction into an organic phase) while providing .( together with the triazine nitrogen atoms) a polar interior.
  • a generally polar heterocycle such as pyridine may have one or more hydrophobic substituents e.g. alkyl groups.
  • the invention is also concerned with compounds such as 2,4,6- tripyridyl-1,3, 5-triazines wherein one or more of the pyridine rings bears at least one hydrophobic substituent.
  • a pyridine-containing compound of this invention may have the general formula depicted in Figure 1 wherein the groups R, and R 2 and R 3 are the same or different and may alternatively or additionally be located in the 2, 3 or 5 positions of the pyridine rings.
  • the groups may be alkyl, aryl, substituted aryl, alkoxy or heterocyclic. (Some, but not all, may be hydrogen.)
  • substituents are heterocycles, then these may in turn have ( non-heterocyclic ) substituents of the types specified for R : , R 2 and R 3 .
  • a molecule tends to present a highly hydrophobic exterior, with an interior containing polar nitrogen atoms which may be suitably disposed for bonding directly through coordination, or indirectly through ion-pair formation, to metal ions.
  • Embodiments of this invention can.be used for extraction systems to produce compounds and wastes, the organic components of which are completely incineratable.
  • the organic component usually comprises compounds containing C,H, N and oxygen but other elements such as S and P are not specifically excluded.
  • the invention provides methods for preparing compounds according to the first aspect.
  • a method may employ a step of trimerising a cyano-substituted heterocycle to generate a triazine ring with three heterocyclic substituents.
  • a method may employ a step of introducing hydrophobic substituents into the heterocyclic rings of a tri-(2,4,6- heterocyclic)-l,2,5-triazine, e.g. by free-radical alkylation.
  • the invention provides a method for extracting a metal species from a mixture comprising adding a compound according to the first aspect to the mixture so that it forms a complex with the desired metal species; partitioning the system between organic and inorganic phases; and recovering the metal species from the organic phase .
  • Fig. 1 shows the formula of one class of compound embodying the invention
  • Fig. 2 shows a synthetic scheme for converting 4-t- butylpyridine to the 2-cyano-der ⁇ vat ⁇ ve
  • Fig. 3 is a scheme showing the trimerisation- cyclization of 2-cyano-4-t-butylpyr ⁇ d ⁇ ne.
  • Figs. 4 and 5 are graphs showing the effects of nitric acid concentration and extractant concentration on distribution coefficients.
  • the triazines may be prepared from the cyclisation of the corresponding cyano compound.
  • E.g. 2,4, 6-tri-(4-t-butyl)-l,3,4-tr ⁇ azme ( TtBPTZ ) may be synthesised by cyclisation of the 2-cyano-4- tertbutylpyridine compound.
  • TtBPTZ 6-tri-(4-t-butyl)-l,3,4-tr ⁇ azme
  • one stage in the preparation may be to prepare the corresponding alkyl cyano compound by alkylation of 2-cyanopyridine.
  • the substituted pyridine may be cyanidised through the N- oxide, as shown in Fig. 2.
  • M * for (4) has m/z equal to 161.
  • Trimerisation of 2-cvano-4-tert-butylpyrid ⁇ ne (4) to TtBPTZ A possible mechanism for the trimerisation/cyclisation of 2-cyano-4-terr-butylpyridine (4) is shown in Figure 3.
  • the trimerisation of (4) was carried out in a methanolic solution at 65 °C with a pressure of about 10 kbar for 6 days. Yields ranged from 5-60% depending on the presence of a suitable ammonium salt with an active hydrogen atom. This increased the rate of formation of TtBPTZ.
  • High pressure cyclisation of (4) to TtPTZ proceeded via the addition of methanol to form a pyridyliminoester (5).
  • di erised to (6) di erised to (6).
  • the dimer (6) then added on a further molecule of the ester ( 5 ) to form TtBPTZ.
  • TtBPTZ Thin layer chromatography using hexane/diethyl ether (1:1) revealed that four different components were present in the reaction mixture after trimerisation.
  • a flash chromatography column with silica gel as stationary phase was set up to separate the components. The first fraction was isolated by running 100% hexane; the second with hexane/diethyl ether (1:1); the third with 100% diethyl ether and finally the last fraction, of TtBPTZ, with methanol.
  • TtPBTZ was characterised by mass spectrometry; m.pt., FT-IR spectroscopy, elemental analysis and 400 Mhz NMR.
  • the FT-IR spectrum did not have any bands attributable to free CN groups. Found: C, 74.11;: H, 7.80; N, 17.24; C 30 H, 3 N 5 requires C, 74.96; H, 7.55; N 17.48%).
  • the 400MHz NMR in deuterochloroform showed ring protons at 2(3H,d):7.58 ppm; 3(3H,d):8.S3 ppprn; 5 . ( 3H,d) : 8.86 ppm; a-the butyl hydrogens- ( 27H, s ): 1.46 ppm.
  • Alkylation of TPTZ Substituents can also be introduced into the heterocyclic rings after formation of the triazine structure.
  • the pyridine rings of TPTZ can be alkylated by free radical alkylation.
  • Alkyl radicals e.g. .C-(CH 3 ) 3 or . C 5 H U
  • Each experiment used a 2- phase system containing trace amounts of Am ⁇ : ⁇ and Eu Ii: , at room temperature.
  • the aqueous phase contained nitric acid in varying amounts.
  • the organic phase contained ⁇ - bromocapric acid (1 molar) and varying amounts of TPTZ or TtBPTZ, in TPH (a mixture of branches hydrocarbons, average C 12 ) .
  • the results are presented in Table 1 and in Figs 4 and 5.
  • Figure 5 shows the variation of distribution coefficient ( D ) with the concentration of TP TZ or TtBPTZ , for systems using 0.05 molar nitric acid as the aqueous phase.
  • the separation of Am ( III ) and EU ( III ) is much b etter at low concentrations of

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Abstract

A metal species (particularly an actinide, e.g. Am(III)) is extracted from a mixture (particularly one including lanthanide species e.g. Eu(III)) by adding a triazine compound to the mixture so that it forms a complex with the desired metal species; partitioning the system between organic and inorganic phases; and recovering the metal species from the organic phase. The triazine compound is a 1,3,5 triazine having heterocyclic substitutents at positons 2, 4, and 6, at least one of the heterocyclic substituents bearing at least one hydrophobic substituent such that the extractability of the compound from an aqueous phase into an organic phase is enhanced. It may be of formula (I) where R1, R2 and R3 are alkyl groups e.g. t-butyl.

Description

SELECTIVE SEPARATION OF DISSOLVED METAL SPECIES WITH SUBSTITUTED 1,3,5 TRIAZINE EXTRACTANTS
The present invention relates to certain 1,3,5- triazines having heterocyclic substituents at the 2,4 and 6-positions, some of which are novel compounds. Typically, the heterocyclic groups may be nitrogen-containing heterocycles such as pyridyl or quinolyl. Generally at least some of the heterocyclic substituents are selected to give the species hydrophobic character. This may be effected by the presence of hydrophobic substituents (e.g. alkyl groups) on the heterocyclic rings. The invention also relates to the synthesis of the triazines and their uses as solvent extraction reagents for the separation of metal-containing species. Use can be made of their hydrophobic nature and their ability to bind directly or through the formation of ion-pairs to metal-containing species. The resulting metal-containing complexes formed by the interaction of the above triazines with the metal- containing complexes may have different chemical and/or physical properties from the original metal-containing species, and these properties may be exploited. Thus a metal species in aqueous solution or suspension may be extracted by reaction with one of the above triazines, followed by solvent extraction to take the species formed into a different, typically organic, phase. With a mixture of metal species in aqueous solution, selectivity of the combination of the metal-containing species with the above triazines followed by solvent extraction can give an improved process for selectively removing a particular metal or class of metals e.g. separation of actinides (An), from lanthanides ( n ) . In particular, the separation of trivalent americium [Am(III)] from trivalent europium [Eu(III)] by the above reagents is embodied in this invention.
2, 4, 6-Tripyridyl-l, 3, 5-triazine (TPTZ) has previously been suggested for use in separating actinides from lanthanides ( FR-A-2509282 ; EP-A-70266 ) . TPTZ is soluble in water and is not efficiently extractable into an organic phase.
The present invention is primarily concerned with the incorporation of substituents in triazines so as to improve their hydrophobic and selectivity properties.
Thus in a first aspect the invention provides a 1,3,5 triazine having a heterocyclic substituent at each of the 2,4 and 6 positions (the three substituents being the same or different). At least 1 or 2 and preferably all of the heterocyclic substituents are selected to give the triazine external hydrophobic character ( facilitating extraction into an organic phase) while providing .( together with the triazine nitrogen atoms) a polar interior. Thus a generally polar heterocycle such as pyridine may have one or more hydrophobic substituents e.g. alkyl groups. The invention is also concerned with compounds such as 2,4,6- tripyridyl-1,3, 5-triazines wherein one or more of the pyridine rings bears at least one hydrophobic substituent. Other compounds such as (optionally substituted) 2,4,6- triquinoline-1, 3, 5-triazines are also included. The incorporation of substituents enhances the hydrophobic nature of the above triazines thus improving the solubilities in organic solvents of the triazines themselves and their metal-containing complexes with respect to TPTZ and its metal-containing complexes.
Thus a pyridine-containing compound of this invention may have the general formula depicted in Figure 1 wherein the groups R, and R2 and R3 are the same or different and may alternatively or additionally be located in the 2, 3 or 5 positions of the pyridine rings. The groups may be alkyl, aryl, substituted aryl, alkoxy or heterocyclic. (Some, but not all, may be hydrogen.)
If the substituents are heterocycles, then these may in turn have ( non-heterocyclic ) substituents of the types specified for R:, R2 and R3. Thus a molecule tends to present a highly hydrophobic exterior, with an interior containing polar nitrogen atoms which may be suitably disposed for bonding directly through coordination, or indirectly through ion-pair formation, to metal ions. Embodiments of this invention can.be used for extraction systems to produce compounds and wastes, the organic components of which are completely incineratable. Thus the organic component usually comprises compounds containing C,H, N and oxygen but other elements such as S and P are not specifically excluded.
In a second aspect the invention provides methods for preparing compounds according to the first aspect. A method may employ a step of trimerising a cyano-substituted heterocycle to generate a triazine ring with three heterocyclic substituents. Alternatively or additionally a method may employ a step of introducing hydrophobic substituents into the heterocyclic rings of a tri-(2,4,6- heterocyclic)-l,2,5-triazine, e.g. by free-radical alkylation.
In a third aspect the invention provides a method for extracting a metal species from a mixture comprising adding a compound according to the first aspect to the mixture so that it forms a complex with the desired metal species; partitioning the system between organic and inorganic phases; and recovering the metal species from the organic phase .
Some embodiments of the invention will now be described in more detail with reference to the accompanying drawings, m which:
Fig. 1 shows the formula of one class of compound embodying the invention;
Fig. 2 shows a synthetic scheme for converting 4-t- butylpyridine to the 2-cyano-derιvatιve;
Fig. 3 is a scheme showing the trimerisation- cyclization of 2-cyano-4-t-butylpyrιdιne; and
Figs. 4 and 5 are graphs showing the effects of nitric acid concentration and extractant concentration on distribution coefficients.
Typically the triazines may be prepared from the cyclisation of the corresponding cyano compound. E.g. 2,4, 6-tri-(4-t-butyl)-l,3,4-trιazme ( TtBPTZ ) may be synthesised by cyclisation of the 2-cyano-4- tertbutylpyridine compound. Thus one stage in the preparation may be to prepare the corresponding alkyl cyano compound by alkylation of 2-cyanopyridine. Alternatively, the substituted pyridine may be cyanidised through the N- oxide, as shown in Fig. 2.
Synthesis of 4-tert-butyl pyridine N-oxide (Compound 2) (See Fig. 2 ) .
Hydrogen peroxide (30%; 2 mol, 250 mL) was carefully added to 4-tert-butyl pyridine (1.48 mol in 320 mL acetic acid). The solution was stirred at 80-90°C for 24h. Additional quantities of hydrogen peroxide (0.7 mol) were added after 6 and 12 h respectively. The cooled mixture was reduced to half its original volume; diluted with water; rendered slightly alkaline with solid NaOH, and extracted with dichloro ethane. The organic layer was evaporated to dryness to give compound (2) in 68% yield. It was recrystallised from cyclohexane. M.P. 100 °C (lit. value 101 βC: Greci et al, J.C.S. Perkin Trans, II (1984) 2013.
Synthesis of Compound ( 3 )
Equimolar amounts of (2) and dimethylsulphate (1.1 mol) were heated at 86 °C for 4h. Compound (3) was isolated by washing with acetone and obtained as a dark brown oil in 98% yield.
Synthesis of Compound (4)
A cooled ethanolic solution of (3) (1.6 mol in 1 L) was added slowly to a stirred aqueous solution of KCN (4.8 mol) keeping the reaction temperature at -5°C. Cooled water (200 mL ) was then added to the mixture and stirred for 4h. The reaction mixture was then extracted with dichloro ethane (4x200 mL ) . The collected extracts were washed with water. The organic layer was separated, dried (Na2S04) and evaporated to dryness by using a steam bath. Compound (4) was obtained in a 65% yield. B.P. 135°C at 1.5 mm Hg. (Found; C, 74.96; H, 7.55; N, 17.48%). M* for (4) has m/z equal to 161. Trimerisation of 2-cvano-4-tert-butylpyridιne (4) to TtBPTZ A possible mechanism for the trimerisation/cyclisation of 2-cyano-4-terr-butylpyridine (4) is shown in Figure 3.
The trimerisation of (4) was carried out in a methanolic solution at 65 °C with a pressure of about 10 kbar for 6 days. Yields ranged from 5-60% depending on the presence of a suitable ammonium salt with an active hydrogen atom. This increased the rate of formation of TtBPTZ. High pressure cyclisation of (4) to TtPTZ proceeded via the addition of methanol to form a pyridyliminoester (5). Subsequently, in the rate- determining step, (5) di erised to (6). The dimer (6) then added on a further molecule of the ester ( 5 ) to form TtBPTZ.
Isolation and Characterisation of TtBPTZ Thin layer chromatography using hexane/diethyl ether (1:1) revealed that four different components were present in the reaction mixture after trimerisation. A flash chromatography column with silica gel as stationary phase was set up to separate the components. The first fraction was isolated by running 100% hexane; the second with hexane/diethyl ether (1:1); the third with 100% diethyl ether and finally the last fraction, of TtBPTZ, with methanol. TtPBTZ was characterised by mass spectrometry; m.pt., FT-IR spectroscopy, elemental analysis and 400 Mhz NMR. M* has m/z = 481 and an accurately measured mass of 480.3002, m.pt. = 85-88°C. The FT-IR spectrum did not have any bands attributable to free CN groups. Found: C, 74.11;: H, 7.80; N, 17.24; C30H,3N5 requires C, 74.96; H, 7.55; N 17.48%). The 400MHz NMR in deuterochloroform showed ring protons at 2(3H,d):7.58 ppm; 3(3H,d):8.S3 ppprn; 5.( 3H,d) : 8.86 ppm; a-the butyl hydrogens- ( 27H, s ): 1.46 ppm. Alkylation of TPTZ Substituents can also be introduced into the heterocyclic rings after formation of the triazine structure. For example, the pyridine rings of TPTZ can be alkylated by free radical alkylation. Alkyl radicals (e.g. .C-(CH3)3 or . C5HU ) can be generated by silver-catalysed oxidative decarboxylation of the corresponding carboxylic acid, using peroxydisulphate .
In actual preparations, an aqueous solution of ammonium persulphate (0.04 mole) was added over 10m to a stirred solution of TPTZ (0.008 mole) and silver nitrate (4 X 10'4 mole) in 10% nitric acid (0.04 mole) at 85 °C. After evolution of carbon dioxide had ceased, stirring at 85° was continued for 30m. The solution was poured into an excess of sodium hydroxide solution, and extracted with dichloromethane. The extract was washed and dried. Removal of the solvent afforded an oil which was resolved into its components by thin layer chromatography. Separation of Actinides and Lanthanides The effectiveness of TPTZ and TtBPTZ for separating Am::ι from EuIι: was investigated. Each experiment used a 2- phase system containing trace amounts of Amι:ι and EuIi:, at room temperature. The aqueous phase contained nitric acid in varying amounts. The organic phase contained α- bromocapric acid (1 molar) and varying amounts of TPTZ or TtBPTZ, in TPH (a mixture of branches hydrocarbons, average C12 ) . The results are presented in Table 1 and in Figs 4 and 5.
TABLE 1
Nitric TPTZ or Distribution Distribution Ratio of
Acid TtBPTZ Coefficient Coefficient Distribution in Aqueous (mol/L) of Am111 of Eu111 Coefficients
Phase Am:EU
(mol/L)
TPTZ TtBPTZ TPTZ TtBPTZ TPTZ TtBPTZ
0,025 0,02 NM 11,6 NM 0,76 NM 15,2
0,05 0,01 NM 2,4 NM 0,085 NM 28,2
0,2 1,2 4,5 0,13 0,28 9,2 16,1
0,05 0,92 13,1 0,1 1,0 9,2 13,1
0,075 | 0,02 0,48 4,8 0,042 0.14 11, 4 34,3
0,10 0,02 NM 1, 5 NM 0,068 NM 22,6
0,15 0,05 NM 1,7 NM 0,062 j NM 27,4
NM: Not Measured
From Table 1, t can clearly be seen that the selectivities for Am(III) are greater w th TtBPTZ than TPTZ.
Figure 4 shows the variation of d str nution coefficient (D) witn nitric acid concentration, for systems using 0.02 molar TPTZ or TtBPTZ. The selectivity for Am(III) compared with Eu(III) is noticeably greater at higher acid concentrations for TtBPTZ than TPTZ.
10 Figure 5 shows the variation of distribution coefficient (D) with the concentration of TPTZ or TtBPTZ, for systems using 0.05 molar nitric acid as the aqueous phase. The separation of Am(III) and EU(III) is much better at low concentrations of
15 TtBPTZ than TPTZ. This implies that the reagent costs may be greatly reduced when TtBPZ is used.

Claims

1. A method for extracting a metal species from a mixture comprising adding a triazine compound to the mixture so that it forms a complex with the desired metal species; partitioning the system between organic and inorganic phases- and recovering the metal species from the organic phase; wherein said triazine compound is a 1, 3, 5 triazine having heterocyclic substituents at positions 2, 4, and 6, at least one of the heterocyclic substituents bearing at least one hydrophobic substituent such that the extractability of the compound from an aqueous phase into an organic phase is enhanced.
2. A method according to claim 1 wherein the mixture contains actinide and lanthanide metal species, and the actiniae species is/are selectively taken nto the organic phase .
3. A method according to claim 2 wherein said metal species are trivalent.
4. A method according to claim 2 wherein said metal species comprise Am(III) and Eu(III) .
5. A method according to any preceding claim wherein said heterocyclic substituents are pyridyl groups .
6. A method according to any of claims 1-4 wherein said heterocyclic substituents are provided by quinoline groups, optionally substituted.
7. A method according to any preceding claim wherein said hydrophilic substituent (s) is/are selected from alkyl , aryl , substituted aryl , alkoxy , heterocyclic and substituted heterocyclic groups .
8 . A method according to any of claims 1 -4 wherein said triazine cotmoound is of formula ( I ) :
Figure imgf000013_0001
wherein R-_, R2 and R3 are alkyl groups.
9. A method according to any preceding claim wherein the triazine compound contains only elements selected from H_ N and O.
10. A method according to claim 9 wherein said compound is finally destroyed by incineration.
11. A method for extracting a metal species substantially as herein described and exemplified.
12. A 1, 3, 5 triazine having heterocyclic substituents at positions 2, 4 and 6, at least one of the heterocyclic substituents having at least one hydrophobic substituent such that the extractability of the compound from an aqueous phase into an organic phase is enhanced.
13. A triazine compound according to claim 12 as further defined in any of claims 5-9.
PCT/GB1996/001700 1994-12-21 1996-07-16 Selective separation of dissolved metal species with substituted 1,3,5 triazine extractants WO1998002594A1 (en)

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Application Number Priority Date Filing Date Title
GB9425776A GB2296917B (en) 1994-12-21 1994-12-21 Separation of actinides from lanthanides using 1,3,5-triazine derivatives
PCT/GB1996/001700 WO1998002594A1 (en) 1994-12-21 1996-07-16 Selective separation of dissolved metal species with substituted 1,3,5 triazine extractants
JP50570098A JP3901736B2 (en) 1996-07-16 1996-07-16 Selective separation of dissolved metal species using substituted 1,3,5 triazine extractants
EP96924093A EP0850322B1 (en) 1996-07-16 1996-07-16 Selective separation of dissolved metal species with substituted 1,3,5 triazine extractants

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GB9425776A GB2296917B (en) 1994-12-21 1994-12-21 Separation of actinides from lanthanides using 1,3,5-triazine derivatives
PCT/GB1996/001700 WO1998002594A1 (en) 1994-12-21 1996-07-16 Selective separation of dissolved metal species with substituted 1,3,5 triazine extractants

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GB2296917B (en) * 1994-12-21 1998-08-26 Univ Reading Separation of actinides from lanthanides using 1,3,5-triazine derivatives

Citations (4)

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Publication number Priority date Publication date Assignee Title
EP0070226A1 (en) * 1981-07-09 1983-01-19 COMMISSARIAT A L'ENERGIE ATOMIQUE Etablissement de Caractère Scientifique Technique et Industriel Process for separating trivalent actinides from trivalent lanthanides in an acidic aqueous solution
FR2607021A1 (en) * 1986-11-21 1988-05-27 Commissariat Energie Atomique Process for selective extraction of transition metals from acidic solutions using polydentate nitrogenous ligand systems and cation exchangers
US5510091A (en) * 1993-01-05 1996-04-23 Japan Atomic Energy Research Institute Method of separating transplutonium elements from lanthanides in acidic solutions by solvent extraction
GB2296917A (en) * 1994-12-21 1996-07-17 Univ Reading 1,3,5-Triazines useful for extracting metal species

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0070226A1 (en) * 1981-07-09 1983-01-19 COMMISSARIAT A L'ENERGIE ATOMIQUE Etablissement de Caractère Scientifique Technique et Industriel Process for separating trivalent actinides from trivalent lanthanides in an acidic aqueous solution
FR2607021A1 (en) * 1986-11-21 1988-05-27 Commissariat Energie Atomique Process for selective extraction of transition metals from acidic solutions using polydentate nitrogenous ligand systems and cation exchangers
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