Synergistic Inhibition of Xylose Fermentation by AFEX-CS Hydrolysate
To simplify this study, all characterized AFEX pretreatment-derived biomass decomposition products were divided into five groups (Table 4): 1) nitrogenous compounds, 2) furans, 3) aliphatic acids, 4) aromatic compounds, and 5) carbohydrates.
Plant cell wall-derived decomposition products and water-soluble extractives present in AFEX-CS hydrolysate (ACH)
Category
Compound
Concentration (mg/L)
Nitrogenous compounds¶
Feruloyl amide
1065
p-Coumaroyl amide
886
Acetamide
5674
2-Methylpyrazine
10
2,5-Dimethylpyrazine
1
2,6-Dimethylpyrazine
4
2,4-Dimethyl-1 H-imidazole
24
4-Methyl-1 H-imidazole
95
Furan¶
5-Hydroxymethyl furfural
145
Aliphatic acids
Malonic acid
33
Lactic acid
181
cis-Aconitic acid
111
Succinic acid
60
Fumaric acid
30
trans-Aconitic acid
329
Levulinic acid
2.5
Itaconic acid
8.2
Acetic acid
1958
Formic acid
517
Aromatic compounds
Vanillic acid
15
Syringic acid
15
Benzoic acid
59
p-Coumaric acid
345
Ferulic acid
137
Cinnamic acid
14
Caffeic acid
2
Vanillin
20
Syringaldehyde
29.5
4-Hydroxybenzaldehyde
24
4-Hydroxyacetophenone
3.4
Carbohydrates
Glucose
60 g/L
Xylose
26 g/L
Arabinose
5 g/L
Gluco-oligomers
12 g/L
Xylo-oligomers
18 g/L
¶The concentration of nitrogenous compounds and furan were calculated from the content of the analyte in dry pretreated biomass [15 (link)] based on 18% solids loading (w/v) assuming 100% solubilization into the liquid phase.
The effect of these five groups of compounds on xylose fermentation was tested individually and in combination (five groups in combination) in order to investigate their synergistic inhibitory effect. The fermentations were conducted in SM supplemented with 60 g/L glucose and 26 g/L xylose. The decomposition products in each group and their concentrations are given in Table 2, and matched their absolute abundance as found in 6% glucan loading-based ACHs. To make stock solutions of decomposition products, all compounds were dissolved in water according to the categories of aliphatic acids, aromatic acids, aromatic aldehyde/ketones, furans, imidazoles, and pyrazines at 50-fold higher concentrations and the stock solutions were sterile filtered prior to their addition into the SM. Ferulic acid, p-coumaric acid, amides, and carbohydrates were directly added to the fermentation media at the desired concentrations (Table 2) due to their lower solubility in water. Fermentations of SM without any decomposition products (blank) and ACHs were used as negative and positive controls, respectively. The ACH was adjusted to pH 5.5 before inoculum addition.
Tang X., da Costa Sousa L., Jin M., Chundawat S.P., Chambliss C.K., Lau M.W., Xiao Z., Dale B.E, & Balan V. (2015). Designer synthetic media for studying microbial-catalyzed biofuel production. Biotechnology for Biofuels, 8, 1.
Other organizations :
Biogas Institute of Ministry of Agriculture, Michigan State University, Great Lakes Bioenergy Research Center, Rutgers, The State University of New Jersey, Baylor University, Sichuan University
Addition of five groups of decomposition products (nitrogenous compounds, furans, aliphatic acids, aromatic compounds, and carbohydrates) individually and in combination
dependent variables
Effect on xylose fermentation
control variables
Fermentation medium (SM) supplemented with 60 g/L glucose and 26 g/L xylose
PH of ACH adjusted to 5.5 before inoculum addition
controls
Positive control: Fermentation of ACH
Negative control: Fermentation of SM without any decomposition products (blank)
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