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VIEIRA, Rodrigo de Oliveira. Flow chemistry as an alternative to the batch process in the reaction of 2,4-thiazolidinedione with p-methoxybenzaldehyde. 2018. 150 f. Dissertação (Mestrado em Tecnologia Bioquímico-Farmacêutica). – Faculdade de Ciências Farmacêuticas, Universidade de São Paulo, São Paulo, 2018. The use of microreactors in the chemical-pharmaceutical industries offers several advantages due to their reduced size compared to batch reactors. In this work, the reaction of the 2,4-thiazolidinedione with p-methoxybenzaldehyde from the batch was transposed to the flow process in a capillary microreactor. In addition, solvent studies are presented with methanol, ethanol and n-propanol, which are most used by these industries. Ethanol had the best results in terms of reaction yield. In the batch process a yield of 100% in 480 min was obtained using piperidine (0.053 M) as base and equimolar concentration of the reactants (0.066 M), while for the reaction with pyrrolidine the yield was 100% in 50 min. With the transposition to the flow process, ethanol was also the best solvent, achieving 100% yield (T = 140°C, mean residence time: 12 min, pyrrolidine base). A base study was also carried out to promote the reaction, being morpholine, phenylethylamine, propargylamine, piperidine, diaminoethane, piperazine and pyrrolidine. In the flow-through process, pyrrolidine (0.033 M) had the best results in terms of conversion, yield and initial velocity at all temperatures (65, 78, 98, 120, 140 and 160°C) and average residence times (2 , 4, 8, 16, 20, 30, 50 and 70 min) studied in the three solvents mentioned. The same was observed in the batch process, with which conversion and maximum yields were obtained for each solvent at times shorter than in the reaction with piperidine. It was also estimated how many microreactors associated in parallel are required to match the production in the batch process and it was found that a single micro-reactor produces more than 1 batch reactor operating for 8h with the same reaction medium, when using ethanol (mean residence time 2 min, T = 140°C) thus showing that the micro-reactor can be used as a process alternative for this synthesis and that Microreactor Technology (TMR) may be better disseminated in the industry.

Química em fluxo como alternativa ao processo batelada na reação da 2,4-Tiazolidinadiona com <i>p</i>-Metoxibenzaldeído