Pretreatment

The first step in lignocellulose conversion to bioethanol is size reduction and pre­treatment. Pretreatment of biomass is technically challenging and is a large part of the process cost and therefore will need to be optimized prior to commercialization.

Table 20.1 Composfficm of Carbohydrate composition

representative lignocellulosic (% dry wt)

feedstocks Feedstocks Cellulose Hemicellulose Lignin

Barley hull

34

36

19

Barley straw

36-43

24-33

6.3-9.8

Bamboo

49-50

18-20

23

Banana waste

13

15

14

Corn cob

32.3-45.6

39.8

6,7-13.9

Corn stover

35.1-39.5

20.7-24.6

11.0-19.1

Cotton

85-95

5.1-15

0

Cotton stalk

31

11

30

Coffee pulp

33.7-36.9

44.2-47.5

15.6-19.1

Dauglas fir

35-48

20-22

15-21

Eucalyptus

45-51

11.1-18

29

Hardwood stems

40-55

24-40

18-25

Rice straw

29.2-34.7

23-25.9

17-19

Rice husk

28.7-35.6

11.96-29.3

15.4-20

Wheat straw

35-39

22-30

13-16

Wheat brain

10.5-14.8

35.5-39.2

8.3-12.5

Grasses

25-40

25-50

10.2-30

News paper

40-45

24-39

18-30

Sugarcane bagasse

25-45

28-32

15-25

Sugarcane tops

35

32

14

Pine

42-49

13-25

23-29

Poplar wood

45-51

25-28

20-21

Olive tree biomass

25.2

15.8

19.1

Jute fibers

45-53

18-21

21-26

Switchgrass

35-40

25-30

15-20

Winter rye

29-30

22-26

16.1

Oilseed rape

27.3

20.5

14.2

Softwood stem

45-50

24-40

18-25

Oat straw

31-35

20-26

10.1-15

Nut shells

25-30

22-28

30-40

Sorghum straw

32-35

24-27

15-21

Tamarind kernel

11-15

55-56

Water hyacinth

18.2-22.1

48.7-50.1

3.5-5.4

Menon and Rao (2012)

The purpose of the pretreatment step is increasing the surface area and porosity, lignin removal, depolymerization of hemicellulose, hemicelluloses removal, and disruption of lignocelluloses structure. Thus the cellulose component is accessible to hydrolyzing agents and reduces the crystallinity of cellulose to further facilitate hydrolysis (Balat et al. 2008).

A successful pretreatment must meet the following requirements: (1) improve formation of sugars or the ability to subsequently form sugars by hydrolysis, (2) avoid degradation or loss of carbohydrate, (3) avoid formation of by-products inhibitory to subsequent hydrolysis and fermentation processes, and (4) minimize energy input

and be cost-effective. The pretreatment stage promotes the physical disruption of the lignocellulosic matrix in order to facilitate acid — or enzyme-catalyzed hydroly­sis. Pretreatments can have significant implications on the configuration and effi­ciency of the rest of the process and, ultimately, also the economics (Hamelinck et al. 2005) . The goal of pretreatment of lignocellulosic biomass to biofuel is depicted in Fig. 20.2.

The most pretreatments are done through physical or chemical means. In order to achieve higher efficiencies, both physical and chemical pretreatments are required. Physical pretreatment is often aimed to reduce size of the biomass. Chemical pretreatment is aimed at removing chemical barriers so that the enzyme can access cellulose for microbial destruction. Each type of feedstock requires a particular combination of pretreatment methods to optimize the yield of that feed­stock, minimize degradation of the substrate, and maximize the sugar yield.