Delignification 
BY SREEREMYA.S,M.PHIL 
LECTURER 
MERCY COLLEGE,PALAKKAD
Introduction 
 Lignocellulose is a generic term for describing the 
main constituents in most plants, namely 
cellulose,hemicelluloses, and lignin. Lignocellulose is 
a complex matrix, comprising many different 
polysaccharides, phenolic polymers and proteins.
 Rice straw has the potential to serve as a relatively 
inexpensive feedstock for biofuel production because 
of its abundance and low value for other applications 
[2]. In 2007, worldwide rice production was 157 
million hectare (651 million tons) [3] with estimated 
rice straw generation of 5.6 to 6.7 t/ha (628–785 
million dry tons)[4, 5]. This amount of rice straw can 
theoretically produce 69 to 86 billion gallons of 
ethanol, which has 21% to 26% of the energy 
equivalence of the gasoline consumed worldwide in 
2005
 Like other sources of lignocellulosic biomass, rice 
straw requires pretreatment to improve the 
efficiency of enzymatic hydrolysis. Several 
pretreatment methods have been developed to 
increase the enzymatic hydrolysis sugar yields from 
lignocellulosic biomass
PRETREATEMENTS 
 Alkaline pretreatment is one approach that has 
several potential advantages compared to other 
pretreatment processes including low operation cost, 
reduced degradation of holocellulose, and 
subsequent formation of inhibitors for downstream 
processing
 The main mechanisms of alkaline pretreatment are 
the degradation of ester bonds and cleavage of 
glycosidic linkages in the lignocellulosic cell wall 
matrix, which lead to the alteration of the structure 
of lignin, the reduction of the lignin–hemicellulose 
complex, cellulose swelling, and the partial 
decrystallization of cellulose
 When compared to other sources of alkali, Ca(OH)2 is a 
relatively inexpensive reagent and easily handled. In 2005, 
the price was ∼$70/ton for hydrated lime, ∼$325/ton for 
sodium hydroxide (NaOH, 50% liquid), ∼$322/ton for 
potassium hydroxide (KOH, 45% liquid), ∼$270/ton for 
ammonia (fertilizer grade, anhydrate), and ∼$1,110/ton for 
hydrogen peroxide (50%, as is basis) [7]. However, 
Ca(OH)2 has very limited solubility in water: 1.6 g/L at 20°C 
and 0.71 g/L at 100°C [19]. This property requires longer 
times and higher quantities of water for pretreatment. In 
contrast to Ca(OH)2, NaOH is a strong alkali and requires 
much less water to dissolve and a lower reaction temperature 
[20]. NaOH pretreatment studies have been published for 
wheat straw, Miscanthus, and cotton stalk, showing the 
effects on delignification and enzymatic hydrolysis
 During alkaline pretreatment, some portions of the 
cellulose and hemicellulose are degraded and 
removed from the biomass by the action of 
hydroxide ions in addition to delignification
CONCLUSION 
 In the present study, bioethanol production process from 
lignocellulosic biomass i.e, Rice husk was developed. In 
order to fraction the lignin and hemicellulose from the 
lignocellulosic substrate, alkali and sodium chlorite 
pretreatment was adopted, which offers the possibility of 
producing cellulosic material that eventually will be 
highly amenable for microbial enzymatic hydrolysis. A 
detoxification strategy was also developed to eliminate 
the fermentation inhibitors from the hydrolysates. The 
delignified substrate was then hydrolyzed by commercial 
enzymes and microorganism. The results obtained with 
direct treatment with enzymes had faster and higher 
results than with microorganisms, but was not cost 
effective.
 THANK YOU
Delignification

Delignification

  • 1.
    Delignification BY SREEREMYA.S,M.PHIL LECTURER MERCY COLLEGE,PALAKKAD
  • 2.
    Introduction  Lignocelluloseis a generic term for describing the main constituents in most plants, namely cellulose,hemicelluloses, and lignin. Lignocellulose is a complex matrix, comprising many different polysaccharides, phenolic polymers and proteins.
  • 3.
     Rice strawhas the potential to serve as a relatively inexpensive feedstock for biofuel production because of its abundance and low value for other applications [2]. In 2007, worldwide rice production was 157 million hectare (651 million tons) [3] with estimated rice straw generation of 5.6 to 6.7 t/ha (628–785 million dry tons)[4, 5]. This amount of rice straw can theoretically produce 69 to 86 billion gallons of ethanol, which has 21% to 26% of the energy equivalence of the gasoline consumed worldwide in 2005
  • 4.
     Like othersources of lignocellulosic biomass, rice straw requires pretreatment to improve the efficiency of enzymatic hydrolysis. Several pretreatment methods have been developed to increase the enzymatic hydrolysis sugar yields from lignocellulosic biomass
  • 5.
    PRETREATEMENTS  Alkalinepretreatment is one approach that has several potential advantages compared to other pretreatment processes including low operation cost, reduced degradation of holocellulose, and subsequent formation of inhibitors for downstream processing
  • 6.
     The mainmechanisms of alkaline pretreatment are the degradation of ester bonds and cleavage of glycosidic linkages in the lignocellulosic cell wall matrix, which lead to the alteration of the structure of lignin, the reduction of the lignin–hemicellulose complex, cellulose swelling, and the partial decrystallization of cellulose
  • 7.
     When comparedto other sources of alkali, Ca(OH)2 is a relatively inexpensive reagent and easily handled. In 2005, the price was ∼$70/ton for hydrated lime, ∼$325/ton for sodium hydroxide (NaOH, 50% liquid), ∼$322/ton for potassium hydroxide (KOH, 45% liquid), ∼$270/ton for ammonia (fertilizer grade, anhydrate), and ∼$1,110/ton for hydrogen peroxide (50%, as is basis) [7]. However, Ca(OH)2 has very limited solubility in water: 1.6 g/L at 20°C and 0.71 g/L at 100°C [19]. This property requires longer times and higher quantities of water for pretreatment. In contrast to Ca(OH)2, NaOH is a strong alkali and requires much less water to dissolve and a lower reaction temperature [20]. NaOH pretreatment studies have been published for wheat straw, Miscanthus, and cotton stalk, showing the effects on delignification and enzymatic hydrolysis
  • 8.
     During alkalinepretreatment, some portions of the cellulose and hemicellulose are degraded and removed from the biomass by the action of hydroxide ions in addition to delignification
  • 9.
    CONCLUSION  Inthe present study, bioethanol production process from lignocellulosic biomass i.e, Rice husk was developed. In order to fraction the lignin and hemicellulose from the lignocellulosic substrate, alkali and sodium chlorite pretreatment was adopted, which offers the possibility of producing cellulosic material that eventually will be highly amenable for microbial enzymatic hydrolysis. A detoxification strategy was also developed to eliminate the fermentation inhibitors from the hydrolysates. The delignified substrate was then hydrolyzed by commercial enzymes and microorganism. The results obtained with direct treatment with enzymes had faster and higher results than with microorganisms, but was not cost effective.
  • 10.
  • 23.