Economic and Environmental Concerns

In current scenario to utilize the lignocellulosic material for green energy, the pre­treatment is an unavoidable step in biorefinery with the cost as high as 30 cents/gallon ethanol produced [10]. Approximately, pretreatment alone costs around 30 % to the

Table 16.4 Effect of different pretreatment methods on sugarcane residues for the sugars recovery after enzymatic hydrolysis

Pretreatment type

Enzymatic hydrolysis conditions

Sugars recovery (g/g or g/L)

References

Low alkali (NaOH)

Celluclast 1.5 L and

Novozyme188 at 3:1 ratio (v/v) in citrate buffer (50 mM pH 4.8) at 50 °C

98 % Cellulose conversion

[51]

Ethanol

organosolv

Celluclast 1.5 L (15 FPU/g substrate) and Novozym 188 (15 IU/g substrate) in citrate buffer (pH 4.8), SB 5 % (w/v), 150 rpm at 50 °C

20.9 g Glucose/100 g SB

[22]

H2O2 in alkaline media

Crude enzymatic extract from Thermoascus aurantiacusin citrate buffer (0.05 M, pH5.0) at 50 °C

39 % of Xylose, 59 % of xylobiose and 2 % of other

xylooligosaccharides

[21]

AFEX

Spezyme CP (33 mg/g glucan), Novozyme 188 (31 mg/g glucan), Multifect xylanase (15 mg/g glucan), sodium citrate buffer (50 mM, pH 4.8), 96 h, 250 rpm, 50 °C

Conversion of xylan to xylose was 10 % higher for cane leaf residue (72 %) when compared with SB (62 %)

[8]

Ethanol

organosolv

Celluclast 1.5 L (15 FPU/g substrate) and Novozym 188 (15 IU/g substrate) in citrate buffer (pH 4.8), SB 5 % (w/v), 150 rpm at 50 °C

18.1 g/L Glucose corresponding to 29.1 g glucose/100 g SB

[22]

IL

2 ml Of enzymatic mix containing Acremonium cellulase per gram of substrate (15 FPU/g substrate), OptimashTM (0.2 % v/v), BG P-xylosidase in sodium acetate buffer (50mM pH 5.0), 0.05 g of IL-treated substrates (2.5 % w/v), 48hat45 °C

Higher glucose (98.2 %) and xylose (60.7 %) saccharification yields in the presence of [Emim] [Ac]. Treatment with [Mmim] [DMP] resulted in glucose (61.9 %) and xylose (43.9 %)

[24]

total processing cost in the conversion oflignocellulosics into ethanol [29]. Perfor­mance of pretreatment methods and the incurred cost on bioconversion process was comprehensively analyzed by Eggeman and Elander [72]. The ideal pretreatment process needs to be highly efficient with imposing low operational and capital cost with less pollution [10, 16, 73]. Recovery of maximum sugars after pretreatment, less chemical load, usage of by-products, faster kinetics, and less process complexity are the important criteria to determine the overall impact of pretreatment methods [11, 16, 17]. All these features determine the cost on downstream processing steps and the trade-off with operational cost, capital cost, and biomass cost [10, 68, 73]. Table 16.5 analyzes the environment and economic impact of various pretreatment

Fig. 16.3 Scanning electron microscopic analysis of SB after various pretreatments: a Native SB: Lignin-cellulose-hemicellulose close network in highly organized manner, b dilute sulfuric acid pretreated SB: Removal of hemicelluloses, less organized structure, c sodium hydroxide pretreat­ment of acid pretreated SB: Removal of lignin from cellulignin leaving cellulose in disorganized manner, making it amenable for cellulase action, d cellulase mediated hydrolysed SB: Coordinated action of cellulase leads the breakdown of cellulose polymer into glucose as monomeric units

methods applied to SB/SL. Critical features like upstream and downstream process­ing cost, capital investment, chemical recycling, usage of by-products, and waste treatment systems makes the comparison and evaluation of pretreatment methods difficult [74]. Net impact of each pretreatment method concerning the economics and environmental impact shows that chemical-based pretreatment methods have strong impact on economics of overall biomass conversion along with considerable environmental pollution burden (Table 16.5).

Pure chemical based pretreatment methods require significant amount of chemi­cals for biomass destruction with the significant amount of by-products generation [14, 17]. However, these methods are highly effective toward either lignin re­moval or hemicellulose degradation from lignocelluloses in short reaction times. Physico-chemical methods (dilute acid hydrolysis, AFEX, steam explosion, etc) have considerable effect on economics and environmental concerns [14, 17]. These methods are more specific toward hemicellulose or lignin degradation leaving cel — lulignin and holocellulose together but in disorganized manner amenable for better cellulases action. In comparison to alkaline methods, physic-chemical methods need less chemical load for the hemicellulose degradation. Biological, physical and LHW pretreatment methods do not require chemicals and are generally considered as mod­erate. Biological methods are generally safe but take longer time periods for lignin removal from the substrates.

Table 16.5 Economic and environmental aspects of different pretreatment methods applied to sugarcane residues

Pretreatment

Types

Factors governing

Factors governing

Net impact[13]

economic impact

environmental impact

Physical

Milling

Energy and capital

Minimal

+

intensive

Irradiation

Energy intensive

Radiations

+

Physico-

Hot water

Electricity

+

chemical

consumption

Partial

By-products

hemicellulose

breakdown

generation

Autohydrolysis

Electricity

consumption

Partial

By-products

+

hemicellulose

breakdown

generation

Steam explosion

Electricity

consumption

Partial

By-products

++

hemicellulose

breakdown

generation

Capital intensive

Ammonia fiber

Ammonia

High chemical load

++

expansion

consumption Capital intensive Lignin recovery

Ammonia recovery

Chemical

Acid pretreatment

Acid consumption

Acid load

++

Capital intensive

By-products

generation

By-products

generation

Alkaline

Capital intensive

High chemical load

+ + +

Sugars loss

By-products

generation

Lignin recovery

IL

Capital intensive

High chemical load

+ + +

Cost of chemicals

By-products

used

generation

Lignin recovery

Organosolv

Capital intensive

High chemical load

+ + +

Lignin recovery

By-products

generation

Oxidative

Capital intensive

High chemical load

+ + +

delignification

Lignin recovery

By-products

generation

Biological

ISMD

Longer incubation

Negligible

+

time

environment

pollution

Lignin recovery Sugars loss

Green technology

Application of lignin generated during alkaline pretreatment has been found im­portant in many products of commercial significance such as resins, adhesives and coatings. Many industries are aiming forward to commercialize the lignin derived products [73]. Pretreatment like dilute acid hydrolysis, auto-hydrolysis and LHW degrade hemicellulose fraction of cell wall into varieties of sugars (xylose, arabi- nose, glucose, mannose and galactose) are used for the production of value-added products like D-xylitol, ethanol, lactic acid, single cell protein etc [2].

A detail economic analysis of each pretreatment strategy considering all the in­volving factors will help to direct research and development efforts in the success of commercialization of bioconversion processes [72, 73]. The renewed interest in sus­tainable development and environment friendly based practices, biotransformation processes are generally preferred over the conventional chemical conversion process. Unfortunately, most pretreatment protocols involve either strong chemicals or harsh physical conditions except bio-delignification. Pretreatment methods autohydrolysis, LHW, steam explosion do not deal with corrosive chemicals however strong physical parameters (high temperature and pressure) are the matter of concern [10]. Biolog­ical pretreatment are the least environmental pollution causing methods but their slow reaction time and loss of significant amount of carbohydrates are the important concerns while selecting them as pretreatment method of choice [13,16]. Biological pretreatment methods have important benefits in a life cycle context also [68].