Tequila Still Distillation Fractioned Residual Streams for Use in Biorefinery
Edgardo Martinez-Orozco,
Pablo Gortares-Moroyoqui,
Norberto Santiago-Olivares,
Juan Napoles-Armenta,
Ruth Gabriela Ulloa-Mercado,
Celia De la Mora-Orozco,
Luis Alonso Leyva-Soto,
Luis Humberto Alvarez-Valencia,
Edna Rosalba Meza-Escalante
Affiliations
Edgardo Martinez-Orozco
Dirección de Recursos Naturales, Instituto Tecnológico de Sonora, Ciudad Obregón, Sonora C.P. 85000, Mexico
Pablo Gortares-Moroyoqui
Dirección de Recursos Naturales, Instituto Tecnológico de Sonora, Ciudad Obregón, Sonora C.P. 85000, Mexico
Norberto Santiago-Olivares
Departamento de Ingeniería Ambiental, Unidad Académica Arandas, Instituto Tecnológico José Mario Molina Pasquel y Henríquez, Tecnológico Nacional de México, Arandas, Jalisco C.P. 47180, Mexico
Juan Napoles-Armenta
Cátedra CONACYT–Facultad de Agronomía, Universidad Autónoma de Nuevo León, General Escobedo, Nuevo Leon C.P. 66050, Mexico
Ruth Gabriela Ulloa-Mercado
Dirección de Recursos Naturales, Instituto Tecnológico de Sonora, Ciudad Obregón, Sonora C.P. 85000, Mexico
Celia De la Mora-Orozco
Departamento de Ingeniería Ambiental, Unidad Académica Arandas, Instituto Tecnológico José Mario Molina Pasquel y Henríquez, Tecnológico Nacional de México, Arandas, Jalisco C.P. 47180, Mexico
Luis Alonso Leyva-Soto
Cátedra CONACYT–Instituto Tecnológico de Sonora, Dirección de Recursos Naturales, 5 de Febrero 818 Sur, Ciudad Obregón, Sonora C.P. 85000, Mexico
Luis Humberto Alvarez-Valencia
Dirección de Recursos Naturales, Instituto Tecnológico de Sonora, Ciudad Obregón, Sonora C.P. 85000, Mexico
Edna Rosalba Meza-Escalante
Dirección de Recursos Naturales, Instituto Tecnológico de Sonora, Ciudad Obregón, Sonora C.P. 85000, Mexico
Tequila vinasses is a mixture made from up to six still distillation two-stage process residual effluents. First stage fractions: residual must (60%), heads (0.9%) and tails (20.0%); second stage fractions: non-evaporated (8.0%), heads (0.1%) and tails (1.0%); the result is a more complex effluent for its treatment or biorefining. The objectives of this study were to: (a) characterize the five still distillation volatile streams in the Tequila 100% Agave processing; compounds: methanol, ethanol, acetaldehyde, ethyl acetate, sec-butanol, n-propanol, iso-butanol, n-butanol, iso-amyl, n-amyl, and ethyl lactate were detected by gas chromatography; calculated chemical oxygen demand from chemical composition had very high values (53,760–1,239,220 mg/L); measurement of pH (3.24–4.80), color (38.6 UC Pt-Co max), turbidity (46.1 max), electrical conductivity (3.30–172.20 μS/cm), and solid content (0 mg/L) was also made; (b) report an energy analysis (2.02 × 109 KWh) and CO2 production (429 × 106 kg) in the Tequila industry during 2019; (c) up to date residues (365.2 × 106 kg agave bagasse, 1146.1 × 106 kg agave leaves and 3300.0 × 106 L agave vinasse) in 2019; (d) economic analysis, current tequila vinasses treatment price is 16.00 USD/m3 but could reach a considerable fraction value if is bio-refined, a break down component analysis reach for five volatile streams $51.23–$140.00 USD/m3.