Ionic liquid-water mixtures enhance pretreatment and anaerobic digestion of agave bagasse

被引:11
|
作者
Perez-Pimienta, Jose A. [1 ]
Garcia-Lopez, Rocio M. [2 ]
Mendez-Acosta, Hugo O. [2 ]
Gonzalez-Alvarez, Victor [2 ]
Simmons, Blake A. [3 ]
Mendoza-Perez, Jorge A. [4 ]
Arreola-Vargas, Jorge [5 ]
机构
[1] Univ Autonoma Nayarit, Dept Chem Engn, Tepic, Mexico
[2] Univ Guadalajara, CUCEI, Dept Ingn Quim, Guadalajara, Jalisco, Mexico
[3] Lawrence Berkeley Natl Lab, Biol Syst & Engn Div, Joint BioEnergy Inst, Emeryville, CA USA
[4] Inst Politecn Nacl, Dept Engn Environm Syst, Mexico City, DF, Mexico
[5] Texas A&M Univ, Dept Plant Pathol & Microbiol, College Stn, TX 77843 USA
关键词
Agave bagasse; Bionic liquid; Biogas; Methane; Saccharification; METHANE PRODUCTION; BIOGAS PRODUCTION; LIGNOCELLULOSIC BIOMASS; TEQUILANA BAGASSE; ETHANOL; ACID; RECALCITRANCE; FRACTIONATION; WASTE; BATCH;
D O I
10.1016/j.indcrop.2021.113924
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Agave bagasse (AB), a byproduct of tequila production, is a waste generated in large quantities and an emerging alternative for biofuels production. Nevertheless, the use of lignocellulosic biomass for this purpose requires a pretreatment that maximizes its degradation and utilization. Although there are several pretreatment types, using ionic liquids (IL) has become attractive due to its ability to dissolve the lignocellulosic biomass under mild conditions of time and temperature. As a drawback are the high cost of IL's and their high viscosity; thus mixing them with water is a way to overcome these hindrances. This work aimed to evaluate the effect of pretreatment with three diluted ILs on the A. tequilana bagasse structure and sugars production, as well as the potential of the enzymatic hydrolysate to produce methane in batch mode. The evaluated ILs were: 1-ethyl-3-methylimidazolium acetate [Emim][OAc], choline lysinate [Ch][Lys] and ethanolamine acetate [EOA][OAc]. The results showed that the IL with the best performance was [Ch][Lys], which not only offered the highest yields of sugar production (0.57 +/- 0.03 g total sugars / g bagasse) but also, it is possible to use it at 30 % in a mix with water obtaining similar yields as with pure IL. Enzymatic hydrolysis of IL pretreated AB achieved 50.7 kg sugars and 49.3 kg of sugars for 90 %-[Ch][Lys] and 30 %-[Ch][Lys], respectively per 100 kg of untreated biomass. The enzymatic hydrolysate from the 30 %-[Ch][Lys] pretreated AB was able to achieve 0.28 L CH4/g CODfed, demonstrating that both sugar and methane yields are maintained when pure or 30 %-[Ch][Lys] are used for pretreatment, representing a step forward towards process feasibility.
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页数:10
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