Anal. Chem. 1998, 70, 3880-3885
S e p a ra t io n o f Clo s e ly Bo ilin g Is o m e rs a n d
Id e n t ic a lly Bo ilin g Is o t o p o m e rs via
Ele c t ro n -Tra n s fe r-As s is t e d Ex t ra c t io n
Che ryl D. Ste ve ns on,* Da nie l J . Mc Elhe ny, Da vid E. Ka ge , J a m e s T. Cis ze w s ki, a nd Ric ha rd C. Re ite r
Department of Chemistry, Illinois State University, Normal, Illinois 61790-4160
Mixtures of isotopomers with identical molecular weights
ethyl-d -benzene + ethylbenzene-d and ter t-butyl-d
biphenyl + ter t-butylbiphenyl-d ) have been partially
method for separating ethylbenzene from m- and p-xylene); (ii)
fractional crystallization5 (this method employs differences in
-12
(
5
5
9
-
freezing points); (iii) fractional crystallization used in conjunction
9
with catalytic isomerization;1
3-16
(iv) membrane permeation;17,18
resolved by making use of their differing solution electron
affinities. EP R analysis of the anion radicals resulting
from the partial potassium reduction of mixtures of the
isotopomers (*R and R, respectively) in tetrahydrofuran
(v) adsorption19,20 (the Universal Oil Products (UOP) “Parex”
process for separating m- and p-xylenes), and the recently
reported electrochemically modulated chromatography,21 the UOP
“Ebex” process for separating ethylbenzene from m- and p-
xylenes;22 (vi) reactive distillation which makes use of chemical
differences (i.e., selectivity) between the isomers and a third
component, the reactive entrainer.3a
•-
+
show that the equilibrium constant for the reaction R ,M
•
-
+
+
*R ) R + *R ,M deviates from unity. These EP R
results predict that a separation of anion radical from
neutral molecule would effect a separation of the isoto-
pomers. Removal of the solvent leaves a solid mixture of
neutral and potassium anion radical salt forms of the
isotopomers. Subsequent dissolution of the neutral ma-
terials from the anion radical salts yields a mixture that
is enriched in the ring-deuterated isotopomer, and reoxi-
dation of the anion radical with iodine yields a mixture
that is enriched in the ring-protiated isotopomer. Analo-
gous experiments were also used to separate closely
boiling geometric isomers.
An example of the reactive distillation process is the separation
of m- and p-xylene isomers.3a Organosodium-exchange reactions
of this type (reaction 1) are reversible and fast and involve
-
2
+
-
1
+
R H + R ,Na h R H + R ,Na
(1)
1
2
organometallic compounds with very low vapor pressures. In
reaction 1, the sodium preferentially binds to the stronger acid
component. The key to attaining a rapid equilibrium is the
introduction of a chelating agent which will complex with the
organosodium compounds. The crown ether, 18-crown-6, was
chosen for this particular purpose. Also, a hydrocarbon solvent,
Due, in part, to industrial needs, the development of non-
destructive separation techniques for closely boiling isomeric
mixtures remains an ongoing challenge in separation science.
Examples of such mixtures include aromatics (i.e., o-xylene,
(
5) Meek, P. D. In Advances in Petroleum Chemistry and Refining; McKetta, J.
p-xylene, ethylbenzene), dichlorinated toluenes, and alkyl-
J., Ed.; Interscience: New York, 1961; Vol. 4.
(6) Wolfe, P. Commun. ACM 1 9 5 9 , 2, 12.
7) Chem. Eng. News 1 9 6 8 , 46, (40, Sept 16), 50.
8) Machall, E. F. U.S. Patent 3 798 282, 1972.
substituted biphenyls.1 Other examples are isotopic in nature,
(
(
2 2 2 2
such as H O/ D O and H
16O/ H 18O.2
One of the most attractive separation processes is extractive
distillation.3a Extractive distillation utilizes the addition of a third
(9) Oden, E. C. U.S. Patent 3 788 819, 1974.
(10) Benris, A. G. U.S. Patent 3 798 283, 1972.
(
(
11) Egan, C. J.; Luthy, R. V. Ind. Eng. Chem. 1 9 5 5 , 47, 250.
component to a mixture of two closely boiling components. This
process is most effective for two closely boiling components that
are different in chemical nature. However, this separation process
cannot be successfully applied to isomers because the entrainer
has about the same effect on each of the components and
therefore does not change their relative volatility.
12) Schaeffer, W. D.; Dorsey, W. S. In Advances in Petroleum Chemistry and
Refining; McKetta, J. J., Ed.; Interscience: New York, 1962; Vol. 6.
13) Hahn, A. The Petrochemical Industry; McGraw-Hill: New York, 1970.
14) Brownstein, A. U. S. Petrochemicals; Petroleum Publishing Co.: Tulsa, OK,
(
(
1972.
(15) Goldstein, R. F.; Waddams, A. L. The Petroleum Chemicals Industry, 3rd ed.;
F. N. Spon Ltd.: London, 1967.
(
16) Waddams, A. L. Chemicals from Petroleum; The Noyes Press: Pearl River,
Alternative techniques must therefore be investigated for the
NY, 1962.
separation of mixtures of isomers. Some alternatives include the
following: (i) mixed extractive entrainers3b,4 (this is an effective
(17) Choo, C. Y. In Advances in Petroleum Chemistry and Refining; McKetta, J.
J., Ed.; Interscience: New York, 1967; Vol. 6.
(
18) Kikic, I.; Alessi, P.; Visalberghi, M. O. Inst. Chem. Eng. Symp. Ser. 1 9 7 8 ,
No. 54, 139.
(
(
(
1) Tyreus, B. D.; Luben, W. L. Chem. Eng. Commun. 1 9 8 2 , 16, 91.
2) Huffman, J. R.; Urey, H. C. Ind. Eng. Chem. 1 9 3 7 , 29, 531.
3) (a) Doherty, M. F.; Sylvester, L. F.; Terrill, D. L. Ind. Eng. Chem. Processes
Des. Dev. 1 9 8 5 , 24, 1062. (b) Berg. L.; Kober, P. J. AICheE J. 1 9 8 0 , 26,
(19) Winnick, J. Chem. Eng. Processes 1 9 9 0 , 41.
(20) Rosset, A. J. U.S. Patent 3 665 046, 1972.
(21) Deinhammerf, R. S.; Ting E. Porter, M. D. Anal. Chem. 1 9 9 5 , 67, 237.
(22) de Rosset, A. J.; Neuzil, R. W.; Tajbl, D. G.; Braband, J. M. Sep. Sci. Technol.
1 9 8 0 , 15, 637.
8
62.
(
4) Berg, L. AIChE J. 1 9 8 3 , 29, 694.
3880 Analytical Chemistry, Vol. 70, No. 18, September 15, 1998
S0003-2700(98)00221-2 CCC: $15.00 © 1998 American Chemical Society
Published on Web 08/08/1998