ISSN 0023-1584, Kinetics and Catalysis, 2017, Vol. 58, No. 1, pp. 24–27. © Pleiades Publishing, Ltd., 2017.
Original Russian Text © S.A. Dzhumadullaeva, A.B. Baeshov, 2017, published in Kinetika i Kataliz, 2017, Vol. 58, No. 1, pp. 26–29.
Ion-Exchange Resin Catalysts in the Liquid-Phase Hydrazinolysis
of Cinnamic Acid
S. A. Dzhumadullaeva* and A. B. Baeshov
Kh. A. Yassawi International Kazakh–Turkish University, Turkestan, 161200 Kazakhstan
*e-mail: sveta.jumadullayeva@ayu.edu.kz
Received February 17, 2016
Abstracts—The catalytic activity of a synthetic ion-exchange resins has been studied in the reaction of cin-
namic acid with hydrazine (aqueous medium, 363 K, 1.0–2.5 h) yielding the corresponding hydrazide. Effi-
cient catalysts for the process are the anion-exchange resins AV-17-8 and AN-31. The modifying effect of the
substrate—hydrazine hydrate—on the catalytic properties of the ion-exchange systems has been demon-
strated. On the basis of IR spectroscopic studies, a plausible process mechanism was suggested. It involves
polymer-bound quaternary ammonium ions of the anion exchanger.
Keywords: ion-exchange resin catalysts, liquid-phase hydrazinolysis, cinnamic acid
DOI: 10.1134/S0023158417010025
Interest in synthetic derivatives of cinnamic acid is centration, and enable one to avoid high water
caused by the possibility of synthesizing, on their consumption and equipment corrosion.
basis, antituberculosis and hepatoprotective drugs and
antioxidants. [1]. For example, cinnamic acid hydra-
zide is active against Mycobacterium tuberculosis. It
provides a basis for the synthesis of a number of other
physiologically active substances [2]. For this reason,
methods for the synthesis of cinnamic acid derivatives
have been extensively studied, particularly the hydraz-
inolysis reaction of carboxylic acids and their esters.
Cinnamic acid hydrazide was synthesized [3] by cin-
namic acid esterification followed by the hydrazinoly-
sis of the ester in absolute ethanol. However, disad-
vantages of this method are the low yield of cinnamic
acid hydrazide (55%) and the necessity of employing
solvents that can impair the organoleptic properties of
the product. Because of the latter circumstance, the
product needs to be additionally purified.
The aim of this work was to study the catalytic
activity of a number of synthetic ion-exchange resins
in the reaction between cinnamic acid and aqueous
hydrazine and to optimize the reaction conditions.
EXPERIMENTAL
The following commercial synthetic ion exchange
resins were used as catalysts: highly basic anion
exchanger AV-17-8 (grain size 0.4–0.6 mm), weakly
basic anion exchangers AN-31 (0.4–2.0 mm) and
AN-1 (0.45–0.50 mm), strongly acidic sulfonic acid
cation-exchange resin KU-2-8 (0.40–0.55 mm), and
phosphoric acid cation exchanger KRF-10P (0.5–
1.0 mm). They were conditioned and converted into
Н+/ОН–-form by a standard method [6]. The
exchange capacity of the ion exchangers was measured
under static conditions by a standard method [7].
Cinnamic acid hydrazide was synthesized from
cinnamic acid by reacting it with hydrazine hydrate in
the presence of an ion-exchange resin catalyst. Exper-
iments were carried out in a static system in a tempera-
ture-controlled 250-cm3 glass reactor equipped with a
mechanical stirrer, thermometer, and reflux con-
denser using commercial hydrazine hydrate (99.9%)
The hydrazinolysis of carboxylic acids in an aque-
ous medium by the action of a basic catalyst is more
promising, for it allows obtaining hydrazides of aro-
matic and heterocyclic carboxylic acids in a single
step. We have demonstrated the possibility of using ion
exchange resins and synthetic zeolites as catalysts for
hydrazinolysis of 4-cyanopyridine and benzoic acid in
the synthesis of the corresponding hydrazides [4, 5].
Ion-exchange resin catalysts based on styrene– and cinnamic acid (reagent grade). The reaction mix-
divinylbenzene copolymers have several advantages: ture, which consisted of cinnamic acid, hydrazine
they are very selective, allow the reaction to be con- hydrate, water and an air-dry ion exchanger, was
ducted under relatively mild conditions, are easily sep- heated in a water bath at 363 K for 1–2.5 h. Next, the
arable from the reaction mixture (which allows a con- mixture was cooled and the ion exchanger was filtered
tinuous process,) do not require neutralization or con- out. The aqueous phase was evaporated to dryness at
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