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(Referência obtida automaticamente do Web of Science, por meio da informação sobre o financiamento pela FAPESP e o número do processo correspondente, incluída na publicação pelos autores.)

Techno-Economic Analysis of Alternative Designs for Low-pH Lactic Acid Production

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Autor(es):
Marchesan, Andressa Neves [1] ; Leal Silva, Jean Felipe [1] ; Maciel Filho, Rubens [1] ; Wolf Maciel, Maria Regina [1]
Número total de Autores: 4
Afiliação do(s) autor(es):
[1] Univ Estadual Campinas, Sch Chem Engn, BR-13083852 Campinas, SP - Brazil
Número total de Afiliações: 1
Tipo de documento: Artigo Científico
Fonte: ACS SUSTAINABLE CHEMISTRY & ENGINEERING; v. 9, n. 36, p. 12120-12131, SEP 13 2021.
Citações Web of Science: 0
Resumo

Lactic acid production is highly affected by the fermentation pH. The need for neutralizing agents and the salts produced during fermentation have a significant impact on the overall process performance. Changing the neutralizing agent and allowing lower pH fermentation can improve the process profitability. This work investigates the impact of fermentation parameters and evaluates the process economics of alternative downstream processing designs to produce lactic acid. The results show that low-pH fermentation (pH = 3.86) was profitable (internal rate of return, IRR > 10%) at a fermentation yield of 0.97 g/g sucrose. Decomposing the salt subproduct to reduce the environmental burden associated with gypsum disposal has a significant impact on the economic performance, resulting in a lower IRR than the other designs. Although the salt decomposition process has a high energy demand, it is compensated by the savings obtained in the downstream processing, thus resulting in a similar overall energy demand when compared to conventional reactive distillation. A novel process configuration with ammonium sulfate subproduct shows potential for 3 p.p. higher IRR and up to 30% lower fuel demand in comparison with the conventional process. Therefore, alternative downstream processes could drive low-pH fermentation to outperform the conventional process without any neutralizing agent. (AU)

Processo FAPESP: 16/10450-1 - Desenvolvimento do processo de conversão de cana-de-açúcar a levulinato de etila: uma rota para um aditivo de biodiesel viável
Beneficiário:Jean Felipe Leal Silva
Modalidade de apoio: Bolsas no Brasil - Mestrado
Processo FAPESP: 15/20630-4 - Desenvolvimento integrado de biorrefinaria e planta de bioetanol de cana-de-açúcar com emissão zero de CO2: rotas para converter recursos renováveis em bioprodutos e bioeletricidade
Beneficiário:Rubens Maciel Filho
Modalidade de apoio: Auxílio à Pesquisa - Temático