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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.)

Hydraulic and organic rates applied to pilot scale UASB reactor for sugar cane vinasse degradation and biogas generation

Texto completo
Autor(es):
Del Nery, Valeria [1] ; Alves, Inae [1] ; Rissato Zamariolli Damianovic, Marcia Helena [1] ; Pires, Eduardo Cleto [1]
Número total de Autores: 4
Afiliação do(s) autor(es):
[1] Univ Sao Paulo, EESC, Dept Hydraul & Sanitat, Av Trabalhador Sao Carlense 400, BR-13566590 Sao Carlos, SP - Brazil
Número total de Afiliações: 1
Tipo de documento: Artigo Científico
Fonte: BIOMASS & BIOENERGY; v. 119, p. 411-417, DEC 2018.
Citações Web of Science: 4
Resumo

A pilot-scale upflow anaerobic sludge blanket (UASB) reactor (120 L) was operated for biogas production by vinasse degradation. The reactor was operated for 700 days using a recirculation rate of 1:3 with organic loading rates (OLR) ranging from 0.5 to 32.4 kgCOD.m(-3).d(-1), upflow velocities ranged from 0.008 to 0.292 m h(-1) (feed added with recirculation) and the hydraulic retention time ranged from 33.33 to 0.86 days. The reactor demonstrated a stable performance at OLR at all applied loads. The COD removal efficiencies throughout the experiment were 87.5 +/- 5.3 and 90.5 +/- 3.6% for raw and soluble COD, respectively. Total volatile acids ranged from 59 mg L-1 to 585 mg L-1. The concentration of acetic and propionic acids at the reactor effluent reached 28 mg L-1 on OLR 20 kgCOD.m(-3).d(-1). The methane content in the biogas was 68.8 +/- 7.14%.The methane yield of 0.299 +/- 0.066 LCH4.g(-1)COD corresponds to about 76.4% of the theoretical methane yield. The methane productivity reached the highest value of 8.059 LCH4.L-1.d(-1) at 32.27 kgCOD.m(-3).d(-1)., corresponding to 83.9% of the theoretical value (9.611 LCH4.L-1.d(-1)). This result is very promising for power generation in the sugar and ethanol industry, complementing the energy balance of sugarcane, as shown by an energy balance evaluation. (AU)

Processo FAPESP: 13/17591-1 - Produção de biogás por degradação anaeróbia da vinhaça de cana-de-açúcar: investigação de taxas hidráulicas e de cargas orgânicas aplicadas em reator anaeróbio de fluxo ascendente com manta de lodo para otimização do processo
Beneficiário:Eduardo Cleto Pires
Modalidade de apoio: Auxílio à Pesquisa - Programa BIOEN - Regular