4.7 OCCURRENCE AND ISOLATION OF LANTHANIDE
ELEMENTS
Except promethium which is unstable and occurs only in traces, all the
lanthanides occur in nature to a considerable extent, cerium being the most abundant
of all the elements. There are more than hundred minerals known to contain
lanthanides but very few are of commercial importance. Monazite sand is the best
known and most important mineral of lanthanide elements which is essentially a
mixture of orthophosphates, LnPO4 containing upto 12% thorium, the element of 5f-
series, small amounts of Zr, Fe and Ti as silicates, lanthanum and about 3% yttrium.
Among lanthanides contained in monazite, the bulk is of Ce, Nd, Pr and others occur
in minute quantities.
Extraction of lanthanide metals
After conventional mineral dressing which gives minerals of more than 90
percent purity, the mineral is broken down by either acidic or alkaline attack. By
making use of different solubilites of double salts: Ln2(SO4)3.Na2SO4.xH2O for light
and heavy lanthanides and low solubility of hydrated oxide of thorium, the lanthanide
fractions and thorium containing portions are separated in acidic medium.
Monazite is treated with hot conc. H2SO4 when thorium, lanthanum and
lanthanons dissolve as sulphates and are separated from insoluble material
(impurities). On partial neutralisaion by NH4OH, thorium is precipitated as ThO2.
Then Na2SO4 is added to the solution. Lanthanum and light lanthanides are
precipitated as sulphates leaving behind the heavy lanthanides in solution. To the
precipitate obtained as above, is added hot conc. NaOH. The resulting hydroxides of
light lanthanides are dried in air at 1000C to convert the hydroxides to oxides. The
oxide mixture is treated with dil. HNO3. This brings CeO2 as precipitate and other
lanthanides in solution. From the solutions obtained as above for heavy and light
lanthanides, individual members of lanthanide series are isolated by the following
methods:
Isolation of Individual Lanthanide Elements:
All the lanthanides have the same size and charge (of +3 unit). The chemical
properties of these elements which depend on the size and charge are, therefore,
almost identical. Hence, their isolation from one another is quite difficult. However,
the following methods have been used to separate them from one another.
1. Fractional Crystallization Method:
This method is based on the difference in solubility of the salts such as
nitrates, sulphates, oxalates, bromates, perchlorates, carbonates and double salts
of lanthanide nitrates with magnesium nitrate which crystallize well and form
crystals. Since, the solubility of these simple and double salts decreases from La
to Lu, the salts of Lu will crystallize first followed by those of lighter members.
The separation can be achieved by repeating crystallization process a number of
times. A non-aqueous solvent, viz., diethyl ether has been used to separate
Nd(NO3)3 and Pr(NO3)3.
2. Fractional Precipitation Method:
This method is also based on the difference is solubility of the precipitate
formed, which is formed on addition of the precipitant, i.e. Precipitating agent.
If a little amount of precipitant is added, the salt with lowest solubility is
precipitated most readily and rapidly. For example, when NaOH is added to a
solution of Ln(NO3)3, Lu-hydroxide being the weakest base and having the
lowest solubility product is precipitated first while La-hydroxide which is the
strongest base and has the highest solubility product is precipitated last. By
dissolving the precipitate in HNO3 and reprecipitating the hydroxides a number
of times, it is possible to get the complete separation of lanthanide elements.
3. Valency change Method:
This method is based on the change of chemical properties by changing the
oxidation state of the lanthanide elements. The most important application of
this method is made in the separation of cerium and europium elements from
mixture of lanthanides.
(i) The mixture containing Ln3+ ions if treated with a strong oxidising agent
such as alkaline KMnO4, only Ce3+ ion is oxidized to Ce4+ while other
Ln3+ ions remain unaffected. To this solution alkali is added to
precipitate Ce(OH)4 only, which can be filtered off from the solution.
(ii) Eu2+ can be separated almost completely from Ln3+ ions from a solution
by reducing it with zinc-amalgam and then precipitating as EuSO4 on
adding H2SO4 which is insoluble in water and hence can be separated.
The sulphates of other Ln3+ ions are soluble and remain in solution.
4. Complex Formation Method:
This method is generally employed to separate heavier lanthanide elements
from the lighter ones by taking the advantage of stronger complexing tendency
of smaller cations with complexing agents. When EDTA is added to Ln3+ ion
solution, lanthanides form strong complexes. If oxalate ions are added to the
solution containing EDTA and Ln3+ ions, no precipitate of oxalates is obtained.
However, on adding small amount of acid, the least stable complexes of lighter
lanthanides are dissociated and precipitated as oxalates, but the heavier
lanthanides remain in solution as EDTA complexes.
5. Solvent Extraction Method:
This method is based on the difference in the values of partition coefficient of
lighter and heavier lanthanides between two solvents, e.g., water and tri-butyl
phosphate (TBP). Heavier lanthanides are more soluble in TBP than lighter
ones whereas reverse trend of solubility is found in water and other ionic
solvents. La(NO3)3 and Gd(NO3)3 have been separated by this method
because the partition coefficient of Gd-nitrate in water and TBP is different
from that of La-nitrate. Thus, Gd-nitrate can be separated from La-nitrate by
continuous extraction with water from a solution of these salts in TBP in
kerosene oil or by using a continuous counter-current apparatus which gives a
large number of partitions automatically.
6. Modern Ion-Exchange Method:
This is the most rapid and most effective method for the isolation of individual
lanthanide elements from the mixture. An aqueous solution of the mixture of
lanthanide ions (Ln3+aq) is introduced into a column containing a synthetic
cation exchange resin such as DOWAX-50 [abbreviated as HR (solid)]. The
resin is the sulphonated polystyrene containing-SO3H as the functional group.
As the solution of mixture moves through the column, Ln3+aq ions replace H+
ions of the resin and get themselves fixed on it:
Ln3+aq + 3H(resin) → Ln(resin)3 + 3H+
aq
The H+
aq ions are washed through the column. The Ln3+aq. ions are fixed at
different positions on the column. Since, Lu3+aq. is largest (Lu3+ anhyd. is
smallest and is hydrated to the maximum extent) and Ce3+aq. is the smallest,
Lu3+aq. ion is attached to the column with minimum firmness remaining at the
bottom and Ce3+aq. ion with maximum firmness remaining at the top of the
resin column. In order to move these Ln3+aq. ions down the column and recover
them, a solution of anionic ligand such as citrate or 2-hydroxy butyrate is
passed slowly through the column (called elution). The anionic ligands form
complexes with the lanthanides which possess lower positive charge than the
initial Ln3+aq ions. These ions are thus displaced from the resin and moved to
the surrounding solutions as eluant- Ln complexes.
For example, if the citrate solution (a mixture of citric acid and ammonium
citrate) is used as the eluant, during elution process, NH4
+
ions are attached to
the resins replacing Ln3+aq. ions which form Ln-citrate complexes:
Ln (resin)3 + 3NH4
+
→ 3NH4- resin + Ln3+aq
Ln3+aq + citrate ions → Ln-citrate complex
As the citrate solution (buffer) runs down the coloumn, the metal ions get
attached alternately with the resin and citrate ions (in solution) many times and
travel gradually down the column and finally pass out of the bottom of the
column as the citrate complex. The Ln3+aq cations with the largest size are,
eluted first (heavier Ln3+aq ions) because they are held with minimum firmness
and lie at the bottom of the column. The lighter Ln3+aq ions with smaller size
are held at the top of the column (with maximum firmness) and are eluted at
last. The process is repeated several times by careful control of concentration of
citrate buffer in actual practice