Kinetics of Citraconic Anhydride Formation via Condensation of Formaldehyde
and Succinates
Dushyant Shekhawat, Kirthivasan Nagarajan,
²
James E. Jackson,
²
and Dennis J. Miller*
Department of Chemical Engineering, Michigan State UniVersity, East Lansing, Michigan 48824, U.S.A.
Abstract:
Formation of citraconic anhydride via condensation of succinic
acid and its derivatives with formaldehyde is carried out over
γ-alumina catalyst in a continuous fixed-bed reactor. Dimethyl
succinate and Formalin (37 wt % formaldehyde, 10 wt %
methanol in water) are the preferred feed materials for the
reaction; catalyst activity is sustained with Formalin relative
to that with other formaldehyde sources such as trioxane or
Formcel, because the water in Formalin inhibits coke formation.
With this feed combination, a total citraconate yield of 31% of
theoretical with 72% selectivity is achieved at a weight hour
space velocity of 0.9 kg of succinate/kg of catalyst/h, a succinate
to formaldehyde molar feed ratio of 1:2, and a temperature of
380 °C. The reaction is free from mass transfer limitations at
these conditions. A kinetic model is presented that describes
product distributions and reactant conversion as a function of
space velocity and temperature. The reaction system is part of
an overall process to produce itaconic acid from renewable
resource-based succinic acid.
I. Introduction
Succinic acid (1,4-butanedioic acid) and its alkyl esters
are reactive species that find applications in industrial and
consumer products and as intermediates for specialty and
fine chemicals production.
1,2
Recent advances in fermentation
technologies for succinic acid production,
3-6
arising both
from genetic modification of the microorganism and im-
proved separations, have led to yields of succinic acid as
high as 1.1 kg of succinic acid/kg of glucose (with CO
2
incorporation) and have nearly eliminated acetic acid as a
coproduct.
6
A significant decrease in the price of the acid
as a raw material is thus expected as the manufacturing
technology matures, making it attractive as a feedstock for
biomass-based chemical production.
The Stobbe condensation,
7
discovered in 1894, offers a
potentially efficient route for the production of substituted
succinates via condensation of esters of succinic acid with
aldehydes and ketones. The reaction is essentially unique to
succinic acid esters and generally takes place in alcohol
solution in the presence of a strong base (alkoxide or sodium
hydride) to give the half-ester as a product.
8
The classic Stobbe condensation does not occur to any
practical extent when formaldehyde is used as the aldehyde.
However, the vapor-phase catalytic (heterogeneous) con-
densation of succinic acid, succinic anhydride, or alkyl
succinate esters with formaldehyde does take place to give
citraconic anhydride (CAN), an isomer of itaconic anhydride
(Scheme 1). Several patents describe catalytic routes to CAN
formation from succinates,
9-12
with transient yields as high
as 70% of theoretical claimed.
9
The motivation for CAN
formation is to produce itaconic acid via hydrolysis of CAN
to citraconic acid and isomerization to itaconic acid. Itaconic
acid is a carboxylated analogue of the important monomer
methacrylic acid and as such is able to take part in addition
polymerization, giving polymers with many free carboxylic
acid groups that confer advantageous wettability and ion-
exchange properties.
13
Itaconic acid is currently produced commercially (8 ×
10
6
kg/yr) by the fermentation of glucose using Aspergillus
terreus.
13
This fungal fermentation is carried out in batch
processes requiring dilute solutions (∼10 wt % glucose) and
extended processing times (6-10 days per batch). Itaconic
acid yields are on the order of 50-60% of theoretical; this
process results in an itaconic acid selling price of ∼$2/lb
* To whom correspondence should be addressed. Department of Chemical
Engineering, 2527 Engineering Building, Michigan State University, East
Lansing, MI 48824. Telephone: (517) 353-3928. Fax: (517) 432-1105. E-mail:
millerd@egr.msu.edu.
²
Department of Chemistry, Michigan State University, East Lansing, MI
48824.
(1) Fumagalli, C.; Spa, L. In Kirk-Othmer Encyclopedia of Chemical Technol-
ogy, 4th ed; Kroschwitz, J. I., Howe-Grant, M., Eds.; John Wiley and
Sons: New York, 1997; 22, 1074-1102.
(2) Szmant, H. H. Organic Building Blocks of the Chemical Industry; John
Wiley and Sons: New York, 1989.
(3) Guettler, M. V.; Jain, M. K.; Soni, B. K. (Michigan Biotechnology Institute)-
. U.S. Patent 5,504,004, 1994.
(4) Datta, R.; Glassner, D. A.; Jain, M. K.; Vick Roy, J. R. (Michigan
Biotechnology Institute). U.S. Patent 5,168,055, 1992.
(5) Tsao, G. T.; Cao, N. J.; Gong, C. S. AdV. Biochem. Eng. Biotechnol. 1999,
65, 243-280.
(6) Nghiem, N. P.; Donnelly, M.; Millard, C. S.; Stols, L. (Lockheed Martin
Energy Research Corporation). U.S. Patent 5,869,301, 1999.
(7) Stobbe, H. Ber. Dtsch. Chem. Ges. 1893, 26, 2312.
(8) Johnson, W. S.; Daub, D. B. In Organic Reactions; Adams, R., Ed.; John
Wiley and Sons: New York, 1951; VI, 2-73.
(9) Tate, B.; Berg. R. (Pfizer). U.S. Patent 3,835,162, 1974.
(10) Fujii, C.; Kibayashi, I.; Hasegawa, Y. (denki Kagaku Kogyo K. K.). Japanese
Patent 50-049223, 1975.
(11) Fujii, C.; Shimizui, T. (denki Kagaku Kogyo K. K.). Japanese Patent 49-
101326, 1974.
(12) Fujii, C.; Shimizui, T. (denki Kagaku Kogyo K. K.). Japanese Patent 49-
101327, 1974.
(13) Luskin, L. S. In Functional Monomers; Yocum, R. H., Nyquist, E. B., Eds.;
Marcel Dekker: New York, 1974; Vol. 2, pp 465-500.
Scheme 1
Organic Process Research & Development 2002, 6, 611-617
10.1021/op020210r CCC: $22.00 © 2002 American Chemical Society Vol. 6, No. 5, 2002 / Organic Process Research & Development • 611
Published on Web 06/08/2002