abstract naoh and its derivatives are used as pulping reagents, wherein the spent naoh is recovered...

1
Abstract NaOH and its derivatives are used as pulping reagents, wherein the spent NaOH is recovered in salt form and reused. In this study, low concentration of NaOH (approx. 1-5%) was used for pretreatment of corn stover and high lignin (HL) hybrid poplar. It was done with the understanding that NaOH can be recovered. In alkaline pretreatments, it is technically feasible to retain most of carbohydrates while removing large fraction of lignin in the biomass. The enhancement of digestibility is caused primarily by lignin removal. Retention of hemicellulose after pretreatment gives a significant economic benefit since it eliminates the need of detoxifying hemicellulose sugars. The main objective of this study is to see if NaOH treatment can achieve that goal. From the results, the optimum process conditions were identified for each of the feedstocks on the basis of carbohydrate retention and digestibility of treated solid. Among the noteworthy findings was that corn stover, after treated with NaOH under moderate conditions, attains near 100% glucan digestibility. On the other hand, hybrid poplar required treatment with much higher severity, in terms of temperature and NaOH concentration, in order to attain acceptable digestibility. It is found that hydrogen peroxide supplementation in pretreatment of hybrid poplar helps in retaining the sugar in solids and further enhances the delignification thus digestibility of solids. Xylanase supplementation during the enzymatic digestibility of treated hybrid poplar drastically improves the sugars yields. Corn Stover Untreated corn stover Treated with 15% ammonia Treated with 1.5% NaOH SEM Pictures of Untreated and treated Corn stover High Lignin Hybrid Poplar Effect of NaOH treatment on composition and Digestibility 35% 31% 30% 28% 22% 17% 16% 8% 18% 6% 5% 3% 0% 20% 40% 60% 80% U ntreated 1% 1.5% 5% NaO H C oncentration Com p o sit % Lignin Rem aining % Xylan Rem aining % G lucan Rem aining Treatment Conditions: Temperature ( 60°C); Time (24hrs); Solid:Liq.(1:10) NaOH treatment at very mild conditions Treatment Conditions: Concentration (1%); Temperature ( 60°C) Time (24hrs); Solid : Liquid (1:10) 0% 20% 40% 60% 80% 100% 0 20 40 60 80 100 Tim e(hrs) G lucan D igestibility 1% 1.5% 5% 0% 20% 40% 60% 80% 100% 0 20 40 60 80 100 Tim e(hrs) X ylan D igestibility 1% 1.5% 5% Glucan Digestibility Xylan Digestibility Enzyme Loading: C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) Enzyme Loading: C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) C+ β-G +X : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) + Xylanase (31.3mg protein/g glucan) 0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 0 10 20 30 40 50 60 70 80 Tim e(hrs) % G lucan Equivalent C +β-G C +β-G +X 0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 0 10 20 30 40 50 60 70 80 Time(hrs) % Xylan Digestibility C +β-G C+β-G +X Glucan Digestibility Xylan Digestibility 34.55% 32.91% 21.78% 17.84% 17.75% 10.41% 0% 10% 20% 30% 40% 50% 60% 70% 80% Untreated 25°C-1% NaO H TreatmentConditions Com position Lignin Xylan Glucan Composition Composition and Digestibility( With and Without Xylanase add.) of NaOH treated Corn stover Overall Sugar Yield 60°C-1.5% NaO H w /o xylanase w /o xylanase w xylanase Glucan 81.74% 62.22% 79.05% X ylan 47.69% 40.37% 62.44% TotalS ugarYiled 68.58% 53.77% 72.63% 25°C-1% NaO H Effect of NaOH treatment on composition and Digestibility Treatment Conditions: Temperature ( 80°C); Time (24hrs); Solid:Liq.(1:10) (Sugar yield from pretreatment liquor is not included here) 43.80% 39.33% 38.94% 14.85% 12.87% 7.81% 29.12% 20.75% 21.18% 0% 20% 40% 60% 80% 100% U ntreated 1.50% 5.00% N aO H C oncentration Com positio Lignin X ylose G lucose 43.80% 41.68% 38.96% 14.85% 12.01% 9.59% 29.12% 17.69% 11.97% 0% 20% 40% 60% 80% 100% U ntreated 1.50% 5.00% N aO H C oncentration C om positio Lignin X ylose G lucose 0% 20% 40% 60% 80% 100% 0 20 40 60 80 Tim e(hrs) G lucan D ig estib il 1.5% 5% 0% 20% 40% 60% 80% 100% 0 20 40 60 80 Tim e(hrs) G lucan D ig estib il 1.5% 5% 0% 20% 40% 60% 80% 100% 0 20 40 60 80 Tim e(hrs) X ylan D ig estib il 1.5% 5% 0% 20% 40% 60% 80% 100% 0 20 40 60 80 Tim e(hrs) X ylan D ig estib il 1.5% 5% Without Hydrogen Peroxide With Hydrogen Peroxide (5% conc. In Liquid) Glucan Digestibility Xylan Digestibility Effect of Xylanase supplementation Enzyme Loading: C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) Treatment Conditions: Temperature ( 80°C); NaOH Conc. (5%) H2O2 Conc. (5%); Time (24hrs); Solid:Liq. 0% 20% 40% 60% 80% 100% 0 20 40 60 80 Tim e(hrs) G lu can D igestibi C +β-G C +β-G +X 0% 20% 40% 60% 80% 100% 0 20 40 60 80 Tim e(hrs) X ylan D igestib i C+β-G C+β-G +X Glucan Digestibility Xylan Digestibility Enzyme Loading: C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) C+ β-G +X : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) + Xylanase (31.3mg protein/g glucan) Overall Sugar Yield 120°C-5% NaO H w /o Xylanase w /o Xylanase w Xylanase Glucan 84.92% 81.15% 88.96% Xylan 37.26% 36.83% 64.38% Total Sugar 72.85% 69.93% 82.73% H igh Lignin Poplar 80°C -5% N aO H-5% H 2O 2 (Sugar yield from pretreatment liquor is not included here) Enzymes Used: ellulase : GC220 (Supplied by Genencor Int.) ellobiase: Novo 188 ( Sigma; cat: C-6150) ylanase: Multifect Xylanase (Supplied by Genencor Int.) ary is very effective in delignification of corn stover. Treated under rate conditions of 60°C temp. and 1.5% concentration, the glucan stibility above 90% is obtained. ted at 25°C and 1%NaOH, corn stover retains more carbohydrates olids, and still gives 73% of overall sugar yield if enzymatic hydrolysis one with xylanase addition. Summary (Contd.) • HL hybrid poplar is more difficult to delignify, thus requires treatment conditions with high severity. • Addition of 5% hydrogen peroxide in NaOH treatment increases the delignification, helps retaining the carbohydrates, and significantly improves the glucan digestibility. • Hydrogen peroxide addition also reduces the Na + conc. in pretreatment liquor. It appears that hydrogen peroxide promotes NaOH induced lignin degradation. • As an oxidizing agent, hydrogen peroxide helps in stabilizing the reducing end in polysaccharide thus lowering the sugar degradation. Summary (Contd.) • The effect of hydrogen peroxide is higher with higher conc. of NaOH. The overall sugar yield in enzymatic digestion of NaOH/H 2 O 2 treated poplar drastically improved by xylanase supplementation. Acknowledgement • US Department of Energy for funding the project (US/DOE No. DE-PS36-00GO10482) • Members of CAFI-II team • Genencor International Inc. for supplying enzyme

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Page 1: Abstract NaOH and its derivatives are used as pulping reagents, wherein the spent NaOH is recovered in salt form and reused. In this study, low concentration

Abstract NaOH and its derivatives are used as pulping reagents, wherein the spent NaOH is recovered in salt form and reused. In this study, low concentration of NaOH (approx. 1-5%) was used for pretreatment of corn stover and high lignin (HL) hybrid poplar. It was done with the understanding that NaOH can be recovered. In alkaline pretreatments, it is technically feasible to retain most of carbohydrates while removing large fraction of lignin in the biomass. The enhancement of digestibility is caused primarily by lignin removal. Retention of hemicellulose after pretreatment gives a significant economic benefit since it eliminates the need of detoxifying hemicellulose sugars. The main objective of this study is to see if NaOH treatment can achieve that goal. From the results, the optimum process conditions were identified for each of the feedstocks on the basis of carbohydrate retention and digestibility of treated solid. Among the noteworthy findings was that corn stover, after treated with NaOH under moderate conditions, attains near 100% glucan digestibility. On the other hand, hybrid poplar required treatment with much higher severity, in terms of temperature and NaOH concentration, in order to attain acceptable digestibility. It is found that hydrogen peroxide supplementation in pretreatment of hybrid poplar helps in retaining the sugar in solids and further enhances the delignification thus digestibility of solids. Xylanase supplementation during the enzymatic digestibility of treated hybrid poplar drastically improves the sugars yields.

Corn Stover

Untreated corn stover Treated with 15% ammonia Treated with 1.5% NaOH

SEM Pictures of Untreated and treated Corn stover

High Lignin Hybrid Poplar

Effect of NaOH treatment on composition and Digestibility

35% 31% 30% 28%

22%17% 16%

8%

18%

6% 5%

3%

0%

20%

40%

60%

80%

Untreated 1% 1.5% 5%NaOH Concentration

Co

mp

osit

ion

% Lignin Remaining

% Xylan Remaining

%Glucan Remaining

Treatment Conditions: Temperature ( 60°C); Time (24hrs); Solid:Liq.(1:10)

NaOH treatment at very mild conditionsTreatment Conditions: Concentration (1%); Temperature ( 60°C) Time (24hrs); Solid : Liquid (1:10)

0%

20%

40%

60%

80%

100%

0 20 40 60 80 100Time(hrs)

Glu

ca

n D

ige

sti

bili

ty

1%

1.5%

5%

0%

20%

40%

60%

80%

100%

0 20 40 60 80 100Time(hrs)

Xy

lan

Dig

es

tib

ility

1%

1.5%

5%

Glucan Digestibility Xylan Digestibility

Enzyme Loading:C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan)

Enzyme Loading:C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan)C+ β-G +X : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) + Xylanase (31.3mg protein/g glucan)

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

0 10 20 30 40 50 60 70 80Time(hrs)

% G

luca

n E

qu

ival

ent

C+β-G C+β-G+X

0%

10%

20%

30%

40%

50%

60%

70%

80%

90%

0 10 20 30 40 50 60 70 80Time(hrs)

% X

ylan

Dig

estib

ility

C+β-G C+β-G+X

Glucan Digestibility Xylan Digestibility

34.55% 32.91%

21.78%17.84%

17.75%

10.41%

0%

10%

20%

30%

40%

50%

60%

70%

80%

Untreated 25°C-1%NaOH

Treatment Conditions

Co

mp

osi

tion

Lignin

Xylan

Glucan

Composition

Composition and Digestibility( With and Without Xylanase add.)of NaOH treated Corn stover

Overall Sugar Yield60°C-1.5%NaOH

w/o xylanase w/o xylanase w xylanase

Glucan 81.74% 62.22% 79.05%Xylan 47.69% 40.37% 62.44%

Total Sugar Yiled 68.58% 53.77% 72.63%

25°C-1%NaOH

Effect of NaOH treatment on composition and Digestibility

Treatment Conditions: Temperature ( 80°C); Time (24hrs); Solid:Liq.(1:10)

(Sugar yield from pretreatment liquor is not included here)

43.80% 39.33% 38.94%

14.85%12.87%

7.81%

29.12%

20.75%21.18%

0%

20%

40%

60%

80%

100%

Untreated 1.50% 5.00%NaOH Concentration

Co

mp

osit

ion

Lignin

Xylose

Glucose

43.80% 41.68% 38.96%

14.85%12.01%

9.59%

29.12%

17.69%

11.97%

0%

20%

40%

60%

80%

100%

Untreated 1.50% 5.00%NaOH Concentration

Co

mp

os

itio

n

Lignin

Xylose

Glucose

0%

20%

40%

60%

80%

100%

0 20 40 60 80Time(hrs)

Glu

can

Dig

esti

bil

ity 1.5%

5%

0%

20%

40%

60%

80%

100%

0 20 40 60 80Time(hrs)

Glu

can

Dig

esti

bil

ity

1.5%

5%

0%

20%

40%

60%

80%

100%

0 20 40 60 80Time(hrs)

Xyla

n D

igesti

bil

ity

1.5%

5%

0%

20%

40%

60%

80%

100%

0 20 40 60 80Time(hrs)

Xyla

n D

igesti

bil

ity

1.5%

5%

Without Hydrogen PeroxideWith Hydrogen Peroxide

(5% conc. In Liquid)

Glucan Digestibility

Xylan Digestibility

Effect of Xylanase supplementation

Enzyme Loading:C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan)

Treatment Conditions: Temperature ( 80°C); NaOH Conc. (5%) H2O2 Conc. (5%); Time (24hrs); Solid:Liq.(1:10)

0%

20%

40%

60%

80%

100%

0 20 40 60 80Time(hrs)

Glu

can

Dig

esti

bil

ity

C+β-G

C+β-G+X

0%

20%

40%

60%

80%

100%

0 20 40 60 80Time(hrs)

Xyla

n D

igesti

bil

ity

C+β-G

C+β-G+X

Glucan Digestibility Xylan Digestibility

Enzyme Loading:C+β-G : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan)C+ β-G +X : Cellulase (15FPU/g glucan) + Cellobiase (30CBU/g glucan) + Xylanase (31.3mg protein/g glucan)

Overall Sugar Yield120°C-5%NaOH

w/o Xylanase w/o Xylanase w Xylanase

Glucan 84.92% 81.15% 88.96%Xylan 37.26% 36.83% 64.38%

Total Sugar 72.85% 69.93% 82.73%High Lignin Poplar

80°C-5%NaOH-5% H2O2

(Sugar yield from pretreatment liquor is not included here)

Enzymes Used:Cellulase : GC220 (Supplied by Genencor Int.)Cellobiase: Novo 188 ( Sigma; cat: C-6150)Xylanase: Multifect Xylanase (Supplied by Genencor Int.)

Summary

• NaOH is very effective in delignification of corn stover. Treated under moderate conditions of 60°C temp. and 1.5% concentration, the glucan digestibility above 90% is obtained.

• Treated at 25°C and 1%NaOH, corn stover retains more carbohydrates in solids, and still gives 73% of overall sugar yield if enzymatic hydrolysis is done with xylanase addition.

Summary (Contd.)

• HL hybrid poplar is more difficult to delignify, thus requires treatment conditions with high severity.

• Addition of 5% hydrogen peroxide in NaOH treatment increases the delignification, helps retaining the carbohydrates, and significantly improves the glucan digestibility.

• Hydrogen peroxide addition also reduces the Na+ conc. in pretreatment liquor. It appears that hydrogen peroxide promotes NaOH induced lignin degradation.

• As an oxidizing agent, hydrogen peroxide helps in stabilizing the reducing end in polysaccharide thus lowering the sugar degradation.

Summary (Contd.)

• The effect of hydrogen peroxide is higher with higher conc. of NaOH.

• The overall sugar yield in enzymatic digestion of NaOH/H2O2 treated poplar is drastically improved by xylanase supplementation.

Acknowledgement

• US Department of Energy for funding the project (US/DOE No. DE-PS36-00GO10482)• Members of CAFI-II team• Genencor International Inc. for supplying enzyme