A technological scheme used for the commercial synthesis of anesthesin (p-aminobenzoic acid ethyl ester) includes the stage of reduction of p-nitrobenzoic acid ethyl ester (I) by iron cuttings in the presence of acetic acid. The reduction of ester I leads to the formation of anesthesin acetate, which is treated with sodium carbonate to obtain the target compound. The product is purified by recrystallization from ethanol in the presence of activated charcoal and sodium hydrosulfite in order to reduce and decolorize the soluble impurities [1]. The impurities present in the anesthesin represent for the most part the products of incomplete reduction of the nitro group, including p-nitrobenzoic acid ethyl ether (II), p-hydroxyaminobenzoic acid ethyl ester (III), and diethyl esters of azoxybenzene- (IV), azobenzene- (V), and hydroazobenzene- (VI) 4,4-dicarboxylic acids. The formation of anesthesin and semiproducts II – VI from the initial nitro compound I can be described by the following scheme: The rate of formation and the amount of the products of incomplete reduction of nitro groups depend on the temperature, solvent type, and nature of the reducing agent. In order to increase the yield of anesthesin, we have studied the process of hydrogenation of p-nitrobenzoic acid ethyl ester and the products of its incomplete reduction. The hydrogenation of ester I to the target compound (p-aminobenzoic acid ethyl ester) was carried out in the presence of a heterogeneous palladium catalyst Pd/C and palladium-containing anion exchangers AN-1 and AV-17-8 (an advantage of using the latter system in hydrogenation reactions was pointed out in [2, 3]). The results of preliminary investigations showed that, under the conditions selected, the hydrogenation of compounds I – VI proceeds in the kinetic regime and is a first-order process with respect to catalyst and hydrogen. However, dependence of the reaction rate on the substrate concentration was variable: when the substrate concentration became comparable to the concentration of active centers on the catalyst surface, the reaction order changed from zeroth to first. The plots of the effective hydrogenation rate constant for the initial nitro compound I versus palladium content in the catalyst (Fig. 1) exhibits an extremal shape. The reaction rate constant increases in proportion to the palladium content in the range of metal concentrations below 4 wt.%. The further increase in the metal content is accompanied by a decrease in the reaction rate, probably, because of a decrease in the catalytic activity caused by the growth of microcrystals. Thus,