Commercial Lignocellulose Processes

One of the problems of using enzymes to degrade lignocellulose is the cost of the enzymes. Recent reduction in the cost of cellulose enzymes (Greer, 2005) has allowed lignocellulose to be considered as a viable alternative to sugar and starch as a substrate

Table 6.10. Some of the pilot plants constructed for the production of ethanol from lignocellulose. (From Solomon et a/., 2007.)

Company

Location

Feedstock

Capacity 102 kg/day

Start date

Iogen

Ottawa, Canada

Wood chips

9.0

1985

Iogen

Ottawa, Canada

Wheat straw

9.0

1993

Masada/TVA

Muscle Shoals, USA

Wood

Na

1993

SunOpta

Norval, Canada

Various

4.5

1995

Arkenol

Orange, USA

Various

9.0

1995

NREL/DOE

Golden, USA

Maize stover

9.0

2001

Pearson Technologies

Aberdeen, USA

Wood, rice straw

0.27

2001

NEDO

Izumi, Japan

Wood chips

3.0

2002

Dedini

Pirassununga, Brazil

Bagasse

42.0

2002

Tsukishima Kikai Co.

Ichikawa, Japan

Wood residues

9.0

2003

Etek EtanolTeknik

Ornskoldvik, Sweden

Spruce sawdust

5.0

2004

PureVision

Ft Lupton, USA

Maize stover

9.0

2004

Universal Entech

Phoenix, USA

MSW

1.0

2004

Sicco A/S

Odense, Denmark

Wheat straw

1.0

2005

Abengoa Bioenergy

York, USA

Maize stover

52.0

2006

MSW, municipal solid waste.

for ethanol production. A number of countries have pilot plants in operation process­ing lignocellulose, although most are in the USA (Table 6.10) and larger commercial plants are being developed. Figure 6.13 shows the process developed by Iogen, a Canadian enzyme manufacturer, for the use of lignocellulose to produce ethanol. Wood chips or straw are treated with dilute acid steam explosion and the cellulose and hemi — cellulose hydrolysed with enzymes produced by Trichoderma sp. Initially the fermenta­tion used S. cerevisiae but later a recombinant Z. mobilis has been introduced which could ferment the pentoses produced from the hemicellulose. The lignin is separated and burnt in a combined heat and power unit to provide energy for the process.

Another process is that designed by the National Renewable Energy Laboratory (NREL) (Fig. 6.14). The biomass, maize stover, is pretreated with dilute acid followed by simultaneous saccharification and co-fermentation (SSCF) with a recombinant Z. mobilis capable of fermenting glucose, xylose and T. reesei. The cellulose hydroly­sis is carried out with T. reesei cellulases and the hemicellulase hydrolysate is detoxi­fied before adding to the fermenter.