Research Article

Steam Explosion Pretreatment with Different Concentrations of Hydrogen Peroxide along with Citric Acid: A Former Step towards Bioethanol Production

Table 4

Recent analysis on steam explosion pretreatment of various lignocellulosic biomass.

Pretreatment techniquesBiomassRequired conditionDegradation in cellulose & hemicelluloseMajor findingsRef.

Steam explosionDefatted soyabean meal1.5 Mpa/193.1°C for 5 minCellulose-50.7%
Hemicellulose-71.1%
At high pressure, biomass saturated with water vapour, the fiber network gets relaxed and lignin content migrates[16]
Steam explosion +1%, , dil. H2SO4Rice straw (10 mm particle size)200°C for 10 minGlucan conversion to 89.6%Large particle size consumes less energy & low production cost[34]
Steam explosionMiscanthus200°C, 15 bar, 10 minXylo-oligosaccharide yield 55%, Larger biomass (10-30 mm) particles led to higher XOS yield (55%, )[35]
Steam explosion +0.8% NaOH +1.2% w/v CaOCorn stalk2.4 gm NaOH, 3.60 gm CaO in 5 : 1 ratio (), 130 kPa pressure for 1 hr54.7% reducing sugar yieldCrI has increased little due to an increase in the order of amorphous cellulose and degree of freedom[42]
Steam explosion +0.5% H2SO4Rice straw200°C/100 bar/10 minIncrease sugar concentration to 12.4 g/lMax. Sugar yield 86%[47]
Steam explosion & catalysed with H3PO4 & H2SO4Sugarcane bagasse195°C for 7.5 min69.4% of free sugar released after pretreatmentMaximum mass recovery in presence of acid catalysts and higher xylan content up to 6.6 wt.%[48]
Steam explosion + sulphonation (Na2SO3,12%,  + NaHCO3, 4%, )Woody Eucalyptus210°C for 5 minGlucan hydrolysis increased to 57.89% from 12.23%Solubilization of hemicellulose
Hydrolysis yield was higher at 210°C as compared to 200°C steam
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