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     Advances in BioethanolPratima Bajpai

    Published by 

    Pira International Ltd

    Cleeve Road, Leatherhead

    Surrey kt22 7ru

    UK 

     T   +44 (0) 1372 802080

    F  +44 (0) 1372 802079

    [email protected] W  www.intertechpira.com

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     The facts set out in this publication

    are obtained from sources which we

    believe to be reliable. However, we

    accept no legal liability of any kind

    for the publication contents, nor any

    information contained therein nor

    conclusions drawn by any party from it.

    No part of this publication may be

    reproduced, stored in a retrieval

    system, or transmitted, in any form or

    by any means, electronic, mechanical,

    photocopying, recording or otherwise

    without the prior permission of theCopyright owner.

    ISBN 1 85802 518 4

    © Copyright

    Pira International Ltd 2007

    Head of publications and events

    Philip Swinden

    [email protected]

    Publisher

    Rav Lally 

    [email protected]

    Head of editorial

     Adam Page

    [email protected]

    Global editor

    Nick Waite

    [email protected]

    Head of US publishing

    Charles E. Spear, [email protected]

     Assistant editor

    Claire Jones

    [email protected]

    Customer services manager

    Denise Davidson

    [email protected]

     T +44 (0)1372 802080

     Typeset in the UK by

     Jeff Porter, Deeping St James,Peterborough, Lincs

     [email protected]

    Pira International Ltd acknowledges product, service and company names referred to

    in this report, many of which are trade names, service marks, trademarks or registered

    trademarks.

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    Contents

    List of tables vList of figures vi

    Introduction 1

    Background 1

    Scope of the report 8

    Methodology 9

    Glossary 9

    Ethanol: an overview 13

    Key drivers 13

     Trends 14

    Chemistry 15

     Types of ethanol 16

    Sources 16

     The energy balance of ethanol 19Future of bioethanol 21

    Production of bioethanol 23

    Production of alcohol from corn 24

    Dry milling 27 

    Wet milling 28

    New technologies 28

    Co-products 28Production of ethanol from lignocellulosic

    biomass 29

    Pre-treatment 30

    Hemicellulose hydrolysis 31

    Cellulose hydrolysis 33

    Fermentation 37 

    Product recovery 39

    Recycling of process stream 40

    Promising developments in the

    production of ethanol from

    cellulose 41

    Estimates of production costs of bioethanol

    from different raw materials 47

    Markets for bioethanol 49

    Oxygenated and reformulated fuels 50

    E5 51

    E10 (gasohol) 51

    E15 52

    E20 52

    E85 52

    E95 54

    E100 54

    Niche markets 55

    Fuel cells 55

    E diesel 55

     Aviation 56 

     Snowmobiles 56 

    Boats/marine 56 

     Small-engine equipment 57 

    Characteristics of ethanol 59

    Using ethanol in engines 62

    Fuel economy 64

    Benefits of bioethanol 65

    Environmental benefits 67

    Carbon dioxide 67 

    Carbon monoxide 68

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    Nitrous oxide 68Other octane additives 68

    Ozone 68

    Particulate matter 69

    Lead 69

    Environmental behaviour 69

    Health effects 70

    Summary 71

    Problems with ethanol/ethanol

    blends 73

    Storage 73

     Transportation 73

    Corrosion 73

    Solvent effect 73

    Separation of layer 74

    Combustion 74

    Effect on other vehicle parts 74

    Scale of operation 74Environment 75

    Bioethanol worldwide 77

    EU 77

    France 80

    Germany 80

     Spain 80

     Sweden 81

    Poland 81

     Austria 82

    Italy 82

    UK 82

     Australia 83

    China 83

    US 84

    Brazil 88

    Canada 91

    India 91

     Thailand 92

     Japan 92References 95

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     Advances in BioethanolContents

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    Page v © Copyright Pira International Ltd 2007

    List of tables

    1.1 Biofuels summary 11.2 Pros and cons of ethanol fuel 3

    1.3 Reductions in per-mile GHG

    emissions by ethanol blend to

    displace an energy-equivalent

    amount of gasoline 5

    1.4 GHG emission reduction per

    gallon of ethanol to displace an

    energy-equivalent amount of

    gasoline 5

    1.5 World ethanol production in 2006 7

    1.6 Ethanol production in the US,1980–2006 7

    2.1 Properties of bioethanol 16

    2.2 Feedstocks for bioethanol

    production 17

    2.3 Typical composition of lignocellulosic

    biomass 18

    2.4 Ethanol’s net energy value:

    a summary of major studies,

    1995–2005 20

    3.1 First- and second-generation raw

    materials for ethanol production 23

    3.2 Composition of corn 27

    3.3 Comparison of various pre-treatment

    options 33

    3.4 Comparison of the different cellulosehydrolysis processes 37

    4.1 Companies developing biofuel

    technologies 44

    6.1 Properties of fuel ethanol 59

    6.2 Ethanol emissions compared to

    gasoline 60

    6.3 Comparison of fuel properties 60

    6.4 Volumetric energy density of ethanol

    compared to gasoline and other

    fuels 61

    9.1 EU bioethanol fuel production,2004–06 78

    9.2 EU: leading ethanol producers 79

    9.3 Ethanol industry expansion in the

    US, 2000–07 84

    9.4 US ethanol statistics, 2005–06 85

    9.5 Ethanol imports in the US, 2006 85

    9.6 Top ten ethanol producers by

    capacity in the US, 2006 85

    9.7 Flexi-fuel cars sold in Brazil,

    2003–06 89

    9.8 Ethanol production costs in different

    countries 89

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    Page vi © Copyright Pira International Ltd 2007

    List of figures

    1.1 The carbon cycle 31.2 World ethanol production,

    1980–2006 6

    3.1 Ethanol production from corn by the

    wet milling process 25

    3.2 Ethanol production from corn by the

    dry milling process 26

    3.3 Distillers grains from US ethanol

    refineries 29

    3.4 Biomass to ethanol process 30

    3.5 SHF with separate pentose andhexose sugars and combined sugar

    fermentation 35

    3.6 SSF with combined sugars (pentoses

    and hexoses) 35

    4.1 Iogen’s cellulose ethanol process 41

    4.2 Celunol process for production of

    ethanol from biomass 43

    9.1 EU: bioethanol fuel production,

    1993–2006 79

    9.2 Ethanol production in Brazil,

    1982–2006 88

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    1

    Page 1 © Copyright Pira International Ltd 2007

      Background  The 1970 energy crisis stimulated research into alternative fuels, with an objectiveto reduce the dependency on oil in the strategic sector of transport (Wyman and

    Hinman, 1990; Lynd and Wang, 2004; Herrera, 2004; Tanaka, 2006; Dien et al., 2006; Sun

    and Cheng, 2004; Yacobucci and Womach, 2003; Chandel et al., 2007; Gray et al., 2006;

    Kheshgi et al., 2000). At present, one of the main reasons for the interest in renewable

    biofuels is the possibility of obtaining a considerable reduction of noxious exhaust

    emissions from combustion, particularly as statutory limits are becoming more stringent

    and more exhaust components are regulated. Table 1.1 summarises the developments.

      Wider use of a chemically simple fuel such as bioethanol will mean that there are less

    harmful effects on life and ecosystems. In particular, people living in urban areas may

    in future appreciate the use of improved low-emission vehicles that do not smell, aresmokeless and are propelled either by reformulated bioethanol, by bioethanol blended

    with gasoline or by neat biofuels. How the air quality can be improved is something that

    is increasingly worth investigating for the sake of people and the environment.

    Large-scale, sustainable, worldwide production and use of bioethanol from biomass

    resources will produce tangible significant benefits for our growing and fast-evolving

    society and also for the earth’s climate. The following list summarises the factors

    favouring bioethanol.

        Bioethanol is a proven global transport fuel, presently supplying 1.2% of the world’s

    petrol.

      It can be produced from virtually any organic material which means that it is a secureform of energy and in the long run will be relatively cheap.

    Introduction

     TABLE 1.1 Biofuels summary 

     What are biofuels? Benefits of biofuelsGeneral definition: Biofuel is a generic term Reduced dependency on fossil fuel

    for any liquid fuel produced from sources other

    than mineral reserves such as oil, coal and

    gas. In general, biofuels can be used as a

    substitute for, or additive to, petrol and diesel

    in most transport and non-transport

    applications

    Biomass means any plant-derived organic Reductions in GHG (greenhouse gas) emissions

    matter available on a renewable basis (biofuels recycle carbon dioxide that is extracted

    from the atmosphere in producing biomass).

    Examples: ethanol, methanol, Fischer-Tropsch Ethanol produced from corn can achieve moderate

    diesel, gaseous fuels such as hydrogen and reductions in GHG emissions whereas ethanolmethane produced from cellulosic plants can achieve much

    greater energy and GHG benefits

     The most popular biofuels are ethanol Reductions in air pollution

    and biodiesel

      No new logistics and infrastructure required

      Supportive of local agriculture

     Source: Pira International Ltd 

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     Advances in BioethanolIntroduction

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        Bioethanol contains more useful energy than is required to produce it.    Bioethanol reduces emissions of greenhouse gases, of carcinogens such as benzene and

    of other harmful emissions such as particulates. It is biodegradable in water and soil.

        Biofuel industries provide economic development and employment in rural areas. The

    World Bank reports that biofuel industries require about 100 times more workers per

    unit of energy produced than the fossil fuel industry.

        Bioethanol enhances competitiveness through the development of new and efficient

    technologies. Above all, it offers the prospect of converting lignocellulose into

    fuel. This will, at a stroke, further improve energy security, reduce greenhouse gas

    emissions and broaden economic development and employment opportunities.

        Even with subsidies, the economic savings with bioethanol from avoided oil imports

    are considerable.

        Bioethanol has the potential to be used in compression engines as well as spark

    ignition engines.

        Bioethanol is unique amongst today’s sustainable transport fuel options in that it

    can be used in internal combustion engines but is also a perfect fuel source for the

    hydrogen fuel cell. So its development now offers a seamless transition into the

    hydrogen energy system of the future.

      Important environmental benefits could be achieved in the socio-economic development

    of large rural populations and the diversification of energy supply, in particular for the

    strategically vital sector of transport (Turkenberg, 2000). A life-cycle analysis of ethanol

    production – from field to the car – by the US Department of Agriculture found that

    ethanol has a large and positive energy balance. Ethanol yields 134% of the energy used

    to grow and harvest the corn and process it into ethanol. By comparison gasoline yields

    only 80% of the energy used to produce it. Bioethanol does not add to global CO2 levels

    because it only recycles CO2 already present in the atmosphere. See Figure 1.1.

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     Advances in BioethanolIntroduction

      More specifically, CO2 is removed from the atmosphere through photosynthesis when

    crops intended for conversion to bioethanol are grown. CO2 is then released into the

    atmosphere during combustion. In contrast, burning a fossil fuel such as petrol adds

    to global CO2 because it releases new amounts of CO2 that were previously trapped

    underground for millions of years. Finally, unlike oil, bioethanol is a renewable fuel, which

    inherently helps the environment by allowing us to conserve other energy resources. The

    pros and cons of ethanol fuel are detailed in Table 1.2.

    FIGURE 1.1 The carbon cycle

     Source: Pira International Ltd 

     

     TABLE 1.2 Pros and cons of ethanol fuel

    Pros Cons

    Positive net energy balance Reduced fuel economy 

    Reduced air pollution Gas cost for consumer initially similar

    Carbon cycle maintains a balance of carbon Many modern cars cannot run ethanol

    dioxide in the atmosphere when ethanol is concentrations higher than E10 gasohol

    used as a fuel source under warranty 

    Reduced dependence on foreign oil Ethanol-powered vehicles will have trouble

    starting at low temperatures

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     Advances in BioethanolIntroduction

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      Ethanol is already commonly used in a 10% ethanol/90% gasoline blend. Adapted

    internal combustion engine vehicles (ICEVs) can use a blend of 85% ethanol/15%

    gasoline (E85) or even 95% ethanol (E95). Addition of ethanol increases octane and

    reduces CO, volatile organic compounds (VOCs) and particulate emissions of gasoline.

     And, via on-board reforming to hydrogen, ethanol is also suitable for use in future fuel

    cell vehicles (FCVs). Those vehicles are supposed to have about double the current ICEV

    fuel efficiency (Lynd, 1996). Beginning with the model year 1999, an increasing number of

     vehicles in the world are manufactured with engines which can run on any gasoline from

    0% ethanol up to 85% ethanol without modification. Many light trucks are designed to

    be dual fuel or flexible fuel vehicles, since they can automatically detect the type of fuel

    and change the engine’s behaviour, principally the air-to-fuel ratio and ignition timing, to

    compensate for the different octane levels of the fuel in the engine cylinders.

      Ethanol has three major uses: as a renewable fuel, as a beverage and for industrial

    purposes. Of the three grades of ethanol, fuel grade ethanol is driving record ethanol

    production in many countries. About 95% of all ethanol is derived from sugar or

    starch crops by fermentation; the rest is produced synthetically. The synthesis route

    involves dehydration of hydrocarbons (e.g. ethylene) or by reaction with sulphuric

    acid, to produce ethyl sulphate, followed by hydrolysis. The production routes from

    biomass are based on fermentation or hydrolysis. According to FO Licht (Berg 2004),

    synthetic alcohol production is concentrated in the hands of a few, mostly multinational,

    companies such as:

      Sasol, with operations in South Africa and Germany 

        SADAF of Saudi Arabia    A 50:50 joint venture between Shell of the UK and the Netherlands

        The Saudi Arabian Basic Industries Corporation

        BP of the UK 

        Equistar in the US.

    Fermentation ethanol is mainly produced for fuel, though a small share is used by

    the beverage industry and the industrial industry. The bulk of the production and

    consumption is located in Brazil and the US. Fermentation technologies for sugar and

    starch crops are very well developed but have certain limits – these crops have a high

     value for food application, and their sugar yield per hectare is very low compared with the

     TABLE 1.2 (Continued)Pros Cons

    Smooth transition from gasoline through Vehicles need alteration to run on ethanol

    alcohol mixtures

    Will slow global warming It is harder to transport 

    Greater production at refineries

     Source: Pira International Ltd 

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     Advances in BioethanolIntroduction

    most prevalent forms of sugar in nature (cellulose and hemicellulose). Suitable processesfor lignocellulosic biomass therefore have room for further development:

      A bigger crop variety can be employed

        A larger portion of these crops can be converted.

      Hence larger scales and lower costs are possible. There is a copious amount of

    lignocellulosic biomass worldwide that can be exploited for fuel ethanol production.

     According to the US Department of Energy, cellulosic ethanol reduces greenhouse gas

    emissions by 85% over reformulated gasoline.

     TABLE 1.4 GHG emission reduction per gallon of ethanol to displace an

    energy-equivalent amount of gasoline

    Ethanol blends Reduction (%)

    E10 GV: DM

    Corn ethanol –26

    E10 GV: WM

    Corn ethanol –18

    E10 GV:Cellulosic ethanol –85

    E85 FFV: DM

    Corn ethanol –29

    E85 FFV: WM

    Corn ethanol –21

    E85 FFV:

    Cellulosic ethanol –86

    Note: GV = gasoline vehicle; FFV = exible fuel vehicle; DM = dry milling; WM = wet milling

     Source: Based on data from Wang (2005)

     TABLE 1.3 Reductions in per-mile GHG emissions by ethanol blend to displace an

    energy-equivalent amount of gasolineEthanol blends Reduction (%)

    E10 GV: DM

    Corn ethanol –2

    E10 GV: WM

    Corn ethanol –2

    E10 GV:

    Cellulosic ethanol –6

    E85 FFV: DM

    Corn ethanol –23

    E85 FFV: WM

    Corn ethanol –17

    E85 FFV:Cellulosic ethanol –64

    Note: GV = gasoline vehicle; FFV = exible fuel vehicle; DM = dry milling; WM = wet milling

     Source: Based on data from Wang (2005)

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      By contrast, sugar-fermented ethanol reduces greenhouse gas emissions by 18–19%compared with gasoline. Dan Sperling, UCD professor and director of the Institute of

     Transportation Studies has commented that ethanol from cellulose is a great energy

    strategy because for every gallon of ethanol, a small amount of fossil material is used. It

    is much better from an energy perspective as a dramatic reduction in greenhouse gases is

    observed. Ethanol-blended fuels reduced CO2-equivalent GHG emissions by approximately

    7.8 million tonnes in 2005 which is equivalent to removing the annual GHG emissions

    of 1.18 million cars from the road (RFA, 2006a). Beyond added environmental benefits,

    cellulose-based ethanol could offer additional revenue streams to farmers for the

    collection and sale of currently unused corn stover (leaves, stalks and cobs) or straw, for

    example.

    Close analysis of the current production and future expansion of ethanol production

    in the US, Brazil and worldwide reveals that the generation of ethanol can hardly be

    identified as a trend anymore: it is a well-defined and planned expansion programme

    (Berg, 2004; Paszner, 2006). Most major oil-consuming or agricultural exporting countries

    either have or are considering public policies to introduce ethanol as a blend agent into

    their gasoline supplies. Many are encouraging ethanol production (BP, 2006). Total world

    ethanol production increased substantially in 2006 totalling 13.5 billion gallons, with 70%

    of this total produced by the US and Brazil. Other significant producers are China, India

    and the EU (RFA, 2007a).

    FIGURE 1.2 World ethanol production, 1980–2006 (million gallons)

     Source: Based on data from RFA (2006a, 2007a); www.earth-policy.org/Updates/2005/Update49_data.htm

                                       

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

                

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     Advances in BioethanolIntroduction

      Fuel ethanol production has been on the rise in the US since 1980, though production has

    increased dramatically since 2001. US ethanol production is expected to grow from 4.9 

    billion gallons/yr in 2006 to 7.5 billion gallons/yr by 2013 (Jessel, 2006). The production

    and use of nearly 5 billion gallons of domestic ethanol in the US reduced CO2-equivalent

    GHG emissions by approximately 8 million tonnes in 2006. That would be the equivalent

    of removing 1.21 million cars from US roads.

      In Europe and other parts of the world, high gasoline prices and an urgency to find

    cleaner fuel additives has increased the interest in ethanol production as well. However,

     TABLE 1.5 World ethanol production in 2006 (%)US 39.1

    Brazil 33.3

    China 7.5

    India 3.7

    Others 16.4

     Source: Based on data from RFA, 2007a

     TABLE 1.6 Ethanol production in the US, 1980–2006

     Year Million gallons

    1980 175

    1981 215

    1982 350

    1983 375

    1984 430

    1985 610

    1986 710

    1987 830

    1988 845

    1989 870

    1990 900

    1991 950

    1992 1,100

    1993 1,200

    1994 1,3501995 1,400

    1996 1,100

    1997 1,300

    1998 1,400

    1999 1,470

    2000 1,630

    2001 1,770

    2002 2,130

    2003 2,810

    2004 3,410

    2005 3,900

    2006 4,900

     Source: Based on data from RFA, 2006c, 2007a

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    the quantity of production still lags far behind Brazil and the US. The primary reasonfor this is said to be a lack of a single biomass source that would help standardise the

    industry, although other economic hurdles also still exist. Asia’s three main countries

    involved in the development of ethanol production are China, Thailand and India. China

    has built the world’s biggest ethanol plant and is planning another just as big.

     The technology on the whole has risen ever since the modest inception of a sizeable

    ethanol industry, thus developing lower-cost methods of producing greater quantities of

    fuel ethanol which are simultaneously more efficient in their use of fossil fuel inputs. These

    combined effects have helped the production of ethanol fuel to increase in the US by more

    than 225% between 2001 and 2005 (RFA, 2006a). Ethanol has also been used outside the

    US, most notably in Brazil which started a programme of government-mandated ethanol

    production in 1975 and has since encouraged production of flex-fuel vehicles (FFVs)

    and cars fuelled entirely by ethanol (Luhnow and Samor, 2006). Due to its geographic

    advantage in growing sugar cane (an ideal ethanol feedstock), Brazil is one of the biggest

    producers of ethanol. Brazil is so efficient that it can produce a gallon of ethanol for

    about €0.73 (Luhnow and Samor, 2006). The Brazilian ethanol market, which was once

    dependent on governmental regulation and subsidies, has blossomed into a system that

    thrives even without regulation. Fuel ethanol production in the US caught up with that

    in Brazil for the first time, growing by 15% in 2005, as both remained the dominant

    producers (REN21, 2006). Although there are cultural and institutional differences between

    the US and Brazil , the general pattern of ethanol production and consumption under a

    regulatory environment in the US could closely mirror what has happened in Brazil. Their

    policy effectiveness can be used as a benchmark for the US market.

      Scope of the report  This report covers bioethanol that is predominantly produced from biomass, including

    living organisms or their metabolic by-products. Bioethanol produced from traditional

    biomass, for example fuel wood and charcoal, etc. as used in developing countries, falls

    outside the scope of this report. This report provides a general background and looks at

    the key drivers and the recent trends, chemistry, types of ethanol, sources and production

    of the first- and second-generation bioethanol. For first-generation bioethanol, theproduction technologies have already been developed and can be implemented directly.

    For second-generation bioethanol, the production technologies need to be developed

    further before their production is possible on a large scale.

     This report also discusses the advantages, biotechnology breakthroughs and

    promising developments in the production of cellulosic ethanol. Furthermore, it addresses

    the end-use application of bioethanol as a transportation fuel and the smaller niche

    markets such as fuel-cell applications, E diesel, aviation, etc. where ethanol can be

    utilised. It also presents information about the benefits, problems, environmental effects

    and characteristics of fuel ethanol. Finally, the report provides detailed information about

    the use of ethanol in different parts of the world and also highlights the challenges andfuture of ethanol.

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     Advances in BioethanolIntroduction

      Methodology Information has been collected from scientific literature, reports from internationaland national agencies, websites, conference presentations, patent literature, statistics

    databases, small and medium-sized biotechnology companies and university research

    groups.

      Glossary  Alcohol : The family name of a group of organic chemical compounds composed of carbon,

    hydrogen and oxygen. The molecules in the series vary in chain length and are composed

    of a hydrocarbon plus a hydroxyl group. Examples are methanol, ethanol, etc.

       Anhydrous ethanol : This is water free or ‘absolute’. The 95% pure product is dehydrated

    using a molecular sieve or azeotropic processes to remove the water, resulting in 99%

    pure ethanol. Anhydrous ethanol is normally blended with 10–25% petrol for use in most

    unmodified or slightly modified engines or as a  3% blend in diesel.

      Bacteria: Single-celled micro-organisms which can exist either as independent organisms

    or as parasites that break down the wastes and bodies of dead organisms, making their

    components available for reuse by other organisms.

      Bagasse: The fibrous material left after the extraction of juice from the sugar cane. It is

    often burned by sugar mills as a source of energy.

      Biodiesel : Biodiesel is a general name for methyl esters from organic feedstock. Biodiesel

    can be made from a wide range of vegetable oils, including rapeseed, and competitor

    oils such as sunflower, palm oil and soy. It can also be derived from animal fats, grease

    and tallow. Rapeseed is one of the main oil-seed crops grown in Europe and is the most

    common feedstock used for biodiesel production. The oil undergoes a chemical process

    (esterification) to make a methyl ester which has similar fuel specifications to fossil diesel.

      Bioenergy : Energy (fuel, electricity, heat) produced from biomass.

      Bioethanol : Ethanol produced from biomass feedstocks. This includes ethanol produced

    from the fermentation of crops such as corn, as well as cellulosic ethanol produced from

    woody plants or grasses. E5 contains 5% ethanol and 95% gasoline; E10 contains 10%

    ethanol and 90% gasoline; E15 contains 15% ethanol and 85% gasoline; E20 contains

    20% ethanol and 80% gasoline; E25 contains 25% ethanol and 75% gasoline; E85 

    contains 85% ethanol and 15% gasoline; E95 contains only 5% gasoline and 95% ethanol

    and E100 is straight ethanol, which is most widely used in Brazil and Argentina.

      Biofuel : Liquid or gaseous fuel for transport, produced from biomass.

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      Biomass: Organic matter available on a renewable basis. Biomass includes forest and millresidues, agricultural crops and waste, wood and wood waste, animal waste, livestock

    operation residues, aquatic plants, fast-growing trees and plants, municipal and industrial

    waste, etc.

    Biorefinery : A facility that processes and converts biomass into value-added products.

     These products can range from biomaterials to fuels such as ethanol or important

    feedstocks for the production of chemicals and other materials. Biorefineries can be

    based on a number of processing platforms using mechanical, thermal, chemical and

    biochemical processes.

      Cellulase: Cellulase is an enzyme that hydrolyses cellulose to its constituent

    monosaccharide (glucose) and disaccharide (cellobiose) units.

      Cellulosic biomass: Biomass composed primarily of inedible plant fibres having cellulose

    as a prominent component. These fibres may be hydrolysed to yield a variety of sugars

    that can subsequently be fermented by micro-organisms. Examples of cellulosic biomass

    include grass, wood and cellulose-rich residues resulting from agriculture of forest

    products.

      E diesel : Blends containing up to 15% ethanol, blended with standard diesel and a

    proprietary additive, are called E diesel.

      Emissions: Waste substances released into the air or water.

    Energy crops: Crops grown specifically for their fuel value. These include food crops

    such as corn and sugar cane, and non-food crops such as poplar trees and switchgrass.

    Currently, two energy crops are under development: short-rotation woody crops, which are

    fast-growing hardwood trees harvested in 5–8 years, and herbaceous energy crops, such

    as perennial grasses, which are harvested annually after taking 2– 3 years to reach fullproductivity.

      Enzyme: Protein that acts as a catalyst, or biocatalyst, in living organisms.

      Ethyl tertiary butyl ether (ETBE): This is produced from bioethanol. This is used as a fuel

    additive to increase the octane rating and reduce knocking.

    Ethanol : Also known as ethyl alcohol, alcohol or grain-spirit. This is a clear, colourless,

    flammable oxygenated hydrocarbon with a boiling point of 78.5°C in the anhydrous state.

    In transportation, ethanol is used as a vehicle fuel by itself (E 100 – 100% ethanol by

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     Advances in BioethanolIntroduction

     volume), blended with gasoline (E85 – 85% ethanol by volume), or as a gasoline octaneenhancer and oxygenater (10% by volume). It is produced by fermenting biomass high

    in carbohydrates. Most ethanol is made using sugars and starches, but researchers are

    working to more efficiently make alcohol from cellulose and other polymers in plants.

    Ethanol made from cellulosic biomass is called cellulosic ethanol.

      Feedstock : The source of carbon for production of organic fuels and chemicals via

    industrial processes.

    Fermentation: Conversion of carbon-containing compounds by micro-organisms for

    production of fuels and chemicals such as alcohols, acids or energy-rich gases.

      Flexible fuel vehicle (FFV): Vehicles whose engines can be operated with petrol as well as

    with E85 or any interim products.

    Fossil fuel : Solid, liquid or gaseous fuels formed in the ground after millions of years by

    chemical and physical changes in plant and animal residues under high temperature and

    pressure. Oil, natural gas and coal are fossil fuels.

    Fuel cell : A device that converts the energy of a fuel directly to electricity and heat

    without combustion.

      Fuel ethanol : A liquid transportation fuel, which accounts for roughly two-thirds of world

    ethyl alcohol. Most fuel ethanol is made from sugar cane, corn and other starch crops.

      Fungi : Superficially this resembles a plant, but it does not have leaves and roots, and it

    lacks chlorophyll, so that it must obtain its nutrients from other organisms by living either

    as a parasite on living organisms or as a saprophyte on dead organic matter.

    Gasoline: A liquid fuel for use in internal combustion engines where the fuel–air mixtureis ignited by a spark. It consists of a mixture of volatile hydrocarbon derived from the

    distillation and cracking of petroleum. It normally contains additives such as lead

    compounds or benzene to improve performance (the prevention of premature ignition) or

    rust inhibitors. It is also called gas (in the US) or petrol.

      Greenhouse effect : The effect of certain gases in the Earth’s atmosphere that traps heat

    from the sun.

      Greenhouse gases: Gases that trap the heat of the sun in the Earth’s atmosphere,

    producing the greenhouse effect. The two major greenhouse gases are water vapour and

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    Page 12 © Copyright Pira International Ltd 2007

    carbon dioxide. Other greenhouse gases include methane, ozone, chlorofluorocarbons andnitrous oxide.

      Hemicellulase: An enzyme that breaks down hemicellulose, which is not as complex as

    cellulose and is easier to break down.

      Hemicellulose: A type of polysaccharide found in plant cell walls, which is broken down

    more easily than cellulose, the main component of the cell walls.

      Hydrous ethanol : This can be used as a pure form of fuel in specially modified vehicles. It

    has a purity of about 95% plus 5% water. Brazil is the only country that produces vehicles

    that run on this form of ethanol.

      Lignin: The structural constituent of wood and (to a lesser extent) other plant tissues,

    which encrusts the cell walls and cements the cells together. It is not fermentable.

      Mannanase: This is an enzyme that breaks down mannans. Mannans are mannose-

    containing polysaccharides found in plants as storage material, in association with

    cellulose (as hemicellulose).

      Methyl tertiary butyl ether (MTBE): This is methyl tertiary butyl ether produced from

    methanol and it is used as a fuel additive to increase the octane rating and reduce

    knocking. It does not biodegrade and can contaminate groundwater.

       Starch: Starch is a polymer made from thousands of glucose units.

       Sustainable: An ecosystem condition in which biodiversity, renewability and resource

    productivity are maintained over time.

       Synthetic ethanol : Ethanol produced from ethylene, a petroleum by-product.

       Xylanase: An enzyme that digests xylans and xylose, components of the plant cell wall.

     These are used in animal feed and added to cereal-based diets to aid the efficiency of

    carbohydrate breakdown. It is also used in the pulp and paper industry to cut and remove

    hemicelluloses from fibres.

      Yeast : A general term including single-celled, usually rounded fungi that produce

    by budding. Some yeasts transform to a mycelial stage under certain environmental

    conditions, while others remain single celled. They ferment carbohydrates.

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      This chapter considers the key drivers, trends, chemistry, types, sources, energy balanceand future of bioethanol.

      Key drivers  The forces pushing for ethanol fuel vary considerably, but there are some common

    features (Rosillo-Calle and Walter, 2006; FAO, 2006; Hazell and Pachauri, 2006;

    Bergstrom, 2007):

        Environmental: around the world concern with clean air is a social and political

    priority. For example, the necessity to reduce pollutant emissions and achieve targets

    defined by the Kyoto Protocol.

        Energy security: increasing dependency on imported energy supply, especially in a

    context of rising oil prices, is also a general concern, particularly in the US and EU.

      Social and economic pressures: for example, the desire to support rural development

    and to generate jobs.

    In recent years, there has been growing interest regarding the use of renewable biofuels

    in the transport sector, ethanol and biodiesel being the best short-term alternatives. More

    than 30 countries have introduced or are interested in introducing programmes for fuel

    ethanol (Rosillo-Calle and Walter, 2006). Other countries have done the same regarding

    biodiesel, but to a lesser extent. Thus, the ethanol experience is so far much more

    important than with biodiesel, excluding Europe where the prospects for biodiesel use are

    much better than fuel ethanol due to the availability of feedstock.

      Developing countries have a reasonably good potential for biofuels production due to

    the availability of land, better weather conditions and the availability of a cheaper labour

    force. Another important issue to be taken into account is that it is imperative for these

    countries to strengthen their rural economies. Obviously each country is different, and a

    careful analysis is required to assess the pros and cons of large-scale biofuels production,

    particularly with regard to competition for land and water for food production and

    potential pressures on food prices (Hazell and von Braun, 2006).

      Another important driving force for ethanol production is the generation of a huge

    amount of new employment. The ethanol industry in Brazil is responsible for about one

    million direct jobs, approximately 50% of them being in sugar cane production. Indirect jobs are estimated at 2.5– 3 million. However, it should be mentioned that this high

    employment is partly due to the low level of mechanisation of agricultural activities, as

    well as poor automation at the industrial site.

      From an environmental perspective, first the benefits of phasing out lead from

    gasoline should be highlighted, as lead has adverse neurological effects. Hydrated ethanol

    has a higher level of octanes than regular gasoline (Joseph, 2005), and its use in blends

    allows the phasing out of lead at a low cost. This would be a very important advantage of

    ethanol use in countries where lead is still in use, as is the case of many African and some

     Asian and Latin American countries.

    In order to protect the environment, developing countries need to change over toclean and renewable fuel from crude oil-based fuels. Large-scale use of biofuels is one

    Ethanol: an overview 2

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    of the main strategies for the reduction of GHG emissions (IPCC, 2001). Despite the factthat developing countries currently do not have binding GHG reduction targets under the

    Kyoto Protocol, two main aspects should be considered:

    Under the clean development mechanism (CDM), developing countries can sell credits

    to those with reduction commitments. Considering a typical Brazilian figure of 2.7kg

    of CO2 equivalent avoided per litre of anhydrous ethanol, biofuels use could represent

    additional income of $0.02–$0.05 (€0.0146–€0.0365) per litre (on credits in the

    range $7–$20 per tonne of CO2 equivalent), value that should be compared with

    production costs in the $0.23–$0.28 per litre range (Nastari; Nastari et al., 2005).

    Climate change effects are supposed to be worst in developing countries so it is

    important to take action.

      Trends  The international market in fuel ethanol is in its initial stage and its full development will

    require:

     The diversification of production in terms of both feedstocks and the number of

    producing countries;

       Technological development in the manufacturing field;

      Favourable policies to induce market competitiveness;

    Sustainable development.

    (Rosillo-Calle F and Walter A, 2006).

    Bioethanol production based on lignocellulosic biomass is the technology of the

    future. Lignocellulosic ethanol is made from a wide variety of plant materials, including

    wood wastes, crop residues and grasses, some of which can be grown on marginal lands

    not suitable for food production (Ghosh and Ghose, 2003). Lignocellulosic raw materials

    minimise the potential conflict between land use for food and feed production and energy

    feedstock production. The raw material is less expensive than conventional agricultural

    feedstock and can be produced with lower input of fertilisers, pesticides and energy.

    Biofuels from lignocellulose generate low net GHG emissions, reducing environmental

    impacts, particularly climate change (Hahn et. al, 2006).

    Global ethanol production more than doubled between 2000 and 2005, whileproduction of biodiesel, starting from a much smaller base, expanded nearly fourfold. In

    contrast, oil production increased by only 7% over this period. In 2005, ethanol comprised

    about 1.2% of the world’s gasoline supply by volume and about 0.8% by transport distance

    travelled (due to its lower energy content). From 2002 to 2004, world oil demand increased

    by 5. 3%. China’s consumption alone increased by 26.4%, while consumption in the US

    increased by 4.9%; Canada 10.2%; and the UK 6. 3%. Demand in Germany and Japan,

    meanwhile, reduced by 1% and 2.6% respectively. The World Bank reports that biofuel

    industries require about 100 times more workers per unit of energy produced than the fossil

    fuel industry. The ethanol industry is credited with providing more than 200,000 jobs

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     Advances in BioethanolEthanol: an overview

    in the US and half a million direct jobs in Brazil. Transportation, including emissions fromthe production of transport fuels, is responsible for about one-quarter of energy-related

    greenhouse gas (GHG) emissions, and that share is rising.

     The GHG balance of biofuels varies dramatically depending on such factors as

    feedstock choice, associated land use changes, feedstock production systems and the type

    of processing energy used. In general, most currently produced biofuels have a solidly

    positive GHG balance. The greatest GHG benefits will be achieved with cellulosic inputs as

    mentioned above. Energy crops have the potential to reduce GHG emissions by more than

    100% (relative to petroleum fuels) because such crops can also sequester carbon in the

    soil as they grow. The estimated GHG reductions for different feedstock are:

    Fibres (switchgrass, poplar): 70–110%

    Wastes (waste oil, harvest residues, sewage): 65–100%

    Sugars (sugar cane, sugar beet): 40–90%

       Vegetable oils (rapeseed, sunflower seed, soya beans): 45–75%

      Starches (corn, wheat): 15–40%.

      Major research challenges in the field of bioethanol production based on lignocellulosic

    biomass are:

    Improving the enzymatic hydrolysis with efficient enzymes.

      Reduced enzyme production cost and novel technology for high solids handling.

      Developing robust fermenting organisms which are more tolerant of inhibitors

    and ferment all sugars in the raw material in concentrated hydrolysates at high

    productivity and with high concentration of ethanol.

      Extending process integration to reduce the number of process steps and the energy

    demand and to reuse process streams for eliminating the use of fresh water and to

    reduce the amount of waste streams.

      (Hahn et al., 2006).

      Chemistry Ethanol is a clear, colourless, volatile, flammable liquid that is the intoxicating agent in

    liquors and is also used as a fuel or solvent. Ethanol is also called ethyl alcohol or grain

    alcohol. Ethanol is the most important member of a large group of organic compoundsthat are called alcohol. It may be shown as:

      In its pure form, ethanol is a colourless clear liquid with a mild characteristic odour.

    Ethanol melts at –114.1°C, boils at 78.5°C and has a density of 0.789g/ml at 20°C.

    2

      H H

    H–|C|

    –|C|

    –O–H or CH3CH2OH

      H H

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      Ethanol’s low freezing point has made it useful as the fluid in thermometers for

    temperatures below –40°C, the freezing point of mercury, and for other low-temperature

    purposes, such as for antifreeze in automobile radiators. The molecular weight is 46.07.

    One gallon of 190 proof ethanol weighs 6.8lb. Ethanol has no basic or acidic properties.

    When burned, ethanol produces a pale blue flame with no residue and considerable

    energy, making it an ideal fuel. Ethanol mixes readily with water and with most organic

    solvents. It is also useful as a solvent and as an ingredient when making many other

    substances including perfumes, paints, lacquer and explosives.

     Types of ethanol Ethanol can be produced in two forms:

    Hydrous ethanol: it can be used as a pure form of fuel in specially modified vehicles.

    It has a purity of about 95% plus 5% water. Brazil is the only country that produces vehicles that run on this form of ethanol.

       Anhydrous ethanol: it is water free or ‘absolute’. A second-stage process is required

    to produce high purity ethanol for use in petrol blends. The 95% pure product is

    dehydrated using a molecular sieve or azeotropic processes to remove the water,

    resulting in 99% pure ethanol. Anhydrous ethanol is normally blended with 10–25%

     volume in petrol for use in most unmodified or slightly modified engines or as a  3%

    blend in diesel.

      Sources Ethanol can be produced from a variety of organic materials. These can be classified in to

    three groups (see Table 2.2).

     TABLE 2.1 Properties of bioethanolPhysical properties

    Specific gravity 0.79g/cm3 

     Vapour pressure (38°C) 50mmHg

    Boiling temperature 78.5°C

    Dielectric constant 24.3

    Solubility in water ∞

    Chemical properties

    Formula C2H5OH

    Molecular weight 46.1

    Carbon (wt) 52.1%

    Hydrogen (wt) 13.1%

    Oxygen (wt) 34.7%

    C/H ratio 4

    Stechiometric ratio (AIR/ETOH) 9.0

     Thermal properties

    Lower heating value 6,400Kcal/kg

    Ignition temperature 35°C

    Specific heat (Kcal/Kg °C) 0.60

    Melting point –115°C

     Source: Based on data from EUBIA (2006)

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     Advances in BioethanolEthanol: an overview

      Agricultural waste available for ethanol conversion includes crop residues such as wheat

    straw, corn stover (leaves, stalks and cobs), rice straw, and bagasse (sugar cane waste).

    Forestry waste includes underutilised wood and logging residues; rough, rotten and

    salvable dead wood; and excess saplings and small trees. Municiple solid waste contains

    some cellulosic materials such as paper. Energy crops, developed and grown specifically

    for fuel, include fast-growing trees, shrubs and grasses such as hybrid poplars, willows and

    switchgrass (US DOE, 1996a). Switchgrass is one source likely to be tapped for ethanol

    production because of its potential for high fuel yields, hardiness and the ability to be

    grown in diverse areas. Trials show current average yields to be about five dry tonnes

    per acre. However, crop experts say that progressively applied breeding techniques could

    more than double that yield. Switchgrass’s long root system – actually a fifty-fifty split

    above ground and below – helps to keep carbon in the ground, improving soil quality. It is

    drought tolerant, grows well even on marginal land and does not require heavy fertilising.

    Other varieties including big blue stem and Indian grass are also possible cellulose sources

    for ethanol production. Researchers estimate that ethanol yield from switchgrass is in the

    range of 60–140 gallons per tonne; some say 80–90 gallons per tonne is a typical figure.

    It is estimated that the energy output/energy input ratio for fuel ethanol made from

    switchgrass is about 4.4 (Iowa State University, 2006). The US Department of Agriculture

    estimates that by 2030 approximately 129 million acres of excess cropland could be used

    for energy crops. If 40 million of these acres were utilised for energy crops for biofuels

    such as ethanol, it would provide a transportation fuel equivalent to 550 million barrels

    of oil per year (US DOE, 1996b). Sugar cane bagasse, the residue generated during the

    milling process, is another potential feedstock for cellulosic ethanol. Research shows that

    one tonne of sugar cane bagasse can generate 112 gallons of ethanol.

    Lignocellulosic feedstock is composed of cellulose, hemicellulose, lignin and extractivesand ash. The cellulose and hemicellulose, which typically comprise two-thirds of the dry

    mass, are polysaccharides that can be hydrolysed to sugars and eventually fermented to

    ethanol. The combination of hemicellulose and lignin provides a protective sheath around

    the cellulose, which must be modified or removed before efficient hydrolysis of cellulose

    can occur, and the crystalline structure of cellulose makes it highly insoluble and resistant

    to attack. Therefore, to hydrolyse hemicellulose and cellulose economically, more advanced

    pre-treatment technologies are required than those used in processing sugar or starch

    crops (Eggeman and Elander, 2005). After the cellulose and hemicellulose have been

    saccharified, the remainder of the ethanol production process is similar to grain ethanol.

    However, the different sugars require different enzymes for fermentation.

     TABLE 2.2 Feedstocks for bioethanol productionSugar-based: Sugar cane, molasses, sugar beet, sweet sorghum, fruits

    Starch-based: Cereal grains, potato, sweet potato, corn, cassava

    Cellulose-based: Agricultural plant waste, forest residue, municipal solid waste, energy crops

     Source: Based on data from Kim and Dale, 2004b; US DOE (2006a)

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      Lignocellulosic crops are promising feedstock for ethanol production because of highyields, low costs, good suitability for low-quality land and low environmental impact. Most

    ethanol conversion systems that are written about are based on a single feedstock. But

    considering the hydrolysis fermentation process, it is possible to use multiple feedstock types.

     Table 2. 3 presents biochemical compositions for several suitable feedstock. Pine has the

    highest combined sugar content, implying the highest potential ethanol production. The

    lignin content for most feedstock is about 27%, but grasses contain significantly less and

    will probably co-produce less electricity.

    Cellulosic resources are in general very widespread and abundant. For example, forests

    comprise about 80% of the world’s biomass. Being abundant and outside the human food

    chain makes cellulosic materials relatively inexpensive feedstocks for ethanol production.

    Brazil uses sugar cane as primary feedstock whereas in the US more than 90% of the

    ethanol produced comes from corn. Other feedstocks such as beverage waste, brewerywaste and cheese whey are also being utilised. In the EU, most of the ethanol is produced

    from sugar beet and wheat. Crops with higher yields of energy, such as switchgrass

    and sugar cane, are more effective in producing ethanol than corn. Ethanol can also be

    produced from sweet sorghum, a dry-land crop that uses much less water than sugar cane,

    does not require a tropical climate and produces food and fodder in addition to fuel. In

    terms of gallons of fuel per acre, the best farm crop for ethanol production is sugar beet,

    with the lowest water requirements to grow the crop. The beet plant drives a central tap

    root deep into the soil and the entire beet is underground, minimimising evaporation.

    One result of increased use of ethanol is increased demand for the feedstocks.

    Large-scale production of agricultural alcohol may require substantial amounts of

     TABLE 2.3 Typical composition of lignocellulosic biomass (%, dry basis)

    Feedstock Hardwood Softwood Grass

      Black Hybrid Eucalyptus Pine Switchgrasslocust poplar

    Cellulose 41.61 44.70 49.50 44.55 31.98

      Glucan 6C 41.61 44.70 49.50 44.55 31.98

    Hemicellulose 17.66 18.55 13.07 21.90 25.19  Xylan 5C 13.86 14.56 10.73 6.30 21.09

      Arbinan 5C 0.94 0.82 0.31 1.60 2.84

      Glactan 6C 0.93 0.97 0.76 2.56 0.95

      Mannan 6C 1.92 2.20 1.27 11.43 0.30

    Lignin 26.70 26.44 27.71 27.67 18.13

     Ash 2.15 1.71 1.26 0.32 5.95

     Acids 4.57 1.48 4.19 2.67 1.21

    Extractives 7.31 7.12 4.27 2.88 17.54

    Heating values 19.50 19.60 19.50 19.60 18.60 

    (GJHHV /tonnedry )

    Note: totals may not add up due to rounding

     Source: Based on data from Hamelinck (2003)

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     Advances in BioethanolEthanol: an overview

    cultivable land with fertile soils and water. This may lead to environmental damage suchas deforestation or decline of soil fertility due to reduction of organic matter.

    In 2003, about 5% of the ethanol produced in the world was actually a petroleum

    product. It is made by the catalytic hydration of ethylene with sulphuric acid as the

    catalyst. It can also be obtained via ethylene or acetylene, from calcium carbide, coal,

    oil, gas and other sources. Two million tonnes of petroleum-derived ethanol are produced

    annually. The principal suppliers are plants in the US, Europe and South Africa. Petroleum-

    derived ethanol (synthetic ethanol) is chemically identical to bioethanol and can be

    differentiated only by radiocarbon dating.

      The energy balance One of the most controversial issues relating to ethanol is the question of net energy of

    of ethanol ethanol production. The definition of net energy value (NEV) is the difference between the

    energy in the fuel product (output energy) and the energy needed to produce the product

    (input energy). While the topic has been hotly debated for years, the current prevailing

    opinion is that ethanol has a net positive energy balance. It takes less than 35,000BTU of

    energy to turn corn into ethanol, while the ethanol offers at least 77,000BTU of energy,

    which shows that ethanol’s energy balance is clearly positive (Shapouri et al., 1995, 2002,

    2003; Lorenz and Morris, 1995; Wang et al., 1999; Kim and Dale, 2004a; Farrell et al.,

    2006) and an extremely high petroleum/fossil energy displacement ratio.

    Since 1979, David Pimentel, of Cornell University has consistently argued – in more

    than 20 published articles – that the amount of fossil fuel energy needed to produce

    ethanol is greater than the energy contained in the ethanol. According to Pimentel and

    his colleague Tad Patzek of the University of California, Berkeley, there is just no energy

    benefit in using plant biomass for liquid fuel (Pimentel, 2003; Patzek, 2003; Ferguson,

    2003). Their research used fundamentally flawed, decades old data that is not valid

    considering today’s efficiencies in agriculture and in ethanol production. Now the advances

    in the farming community as well as technological advances in the production of ethanol

    have led to positive returns in the energy balance of ethanol. Studies have shown that

    the ethanol energy balance is improving by the year (Wang, 2005b; Shapouri et al., 1995,

    2002, 2003; Lorenz and Morris, 1995; Wang et al., 1999; Morris, 1995). These studies showthat the energy output to energy input ratio for converting irrigated corn to ethanol is now

    1.67:1. In a July 1995 US Department of Agriculture (USDA) Economic Research Service

    report entitled ‘Estimating the Net Energy Balance of Corn Ethanol’, it was concluded that

    the ethanol energy balance had a gain of 24%. That same report was revisited the next

    year, in a presentation entitled ‘Energy Balance of Corn Ethanol Revisited’ – the authors

    concluded that the ratio had risen to 34%. This number is reinforced by a 2002 report, ‘The

    Energy Balance of Corn Ethanol: An Update’ published by the USDA’s Office of the Chief

    Economist and Office of Energy Policy and New Uses. The report concluded that ethanol

    production is energy efficient because it yields 34% more energy than is used. In June

    2004, the USDA looked at this issue again and determined that ethanol continues to bemore efficient and now provides the aforementioned 1.67:1 gain in energy.

    2

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      Many advances have led to the surge in ethanol production efficiency. One key issueis the ability to produce more gallons of ethanol per bushel of corn. In the early 1990s,

    plants were able to produce about 2.5 gallons of ethanol per bushel. That number has

    since increased to between 2.7 and 2.8 gallons per bushel.

    Crops with a higher sugar content than corn, such as sugar beet, would result in

    production with a much higher positive net energy balance. If corn farmers use

    state-of-the-art, energy-efficient farming techniques, and ethanol plants use state-of-the-art

    production processes, then the amount of energy contained in a gallon of ethanol and the

    other co-products is more than twice the energy used to grow the corn and convert it into

    ethanol. Studies indicated an industry average net energy gain of 1. 38:1. The industry-best

    existing production net energy ratio was 2.09:1. If farmers and industry were to use all of

    the best technologies and practices, the net energy ratio would be 2.51:1. In other words,

    the production of ethanol would result in more than two-and-a-half times the available

    energy than it took to produce it.

     A 1999 study by Argonne National Laboratory found the energy balance of cellulosic

    ethanol to be in excess of 60,000BTU per gallon (Wang, 1999). Given that feedstocks

    for cellulosic ethanol are essentially waste products like corn stover, rice bagasse, forest

    thinnings or even municipal waste, there are relatively few chemical and energy inputs

    that go into the farming of feedstocks for cellulosic ethanol. A secondary factor, although

    to a much lesser extent, is the fact that cellulosic ethanol plants will presumably produce

    extra energy that can be fed into the power grid. Doing so will effectively displace the use

    of electricity produced in power plants, which for the most part rely upon fossil fuels.

     Table 2.4 shows ethanol’s net energy value as published by different researchers.

     TABLE 2.4 Ethanol’s net energy value: a summary of major studies, 1995–2005

     Authors and date NEV (BTU)

    Shapouri et al. (1995) – USDA +20,436 (HHV)

    Lorenz and Morris (1995) – Institute for Local Self-Reliance +30,589 (HHV)

     Agri. and Agri-Food, Canada (1999) +29,826 (LHV)

    Wang et al. (1999) – Argonne National Laboratory +22,500 (LHV)

    Pimentel (2002) – Cornell University –33,562 (LHV)

    Shapouri et al., update (2002) – USDA +21,105 (HHV)

    Kim and Dale (2002) – Michigan State University +23,866 to +35,463 (LHV)

    Graboski (2002) – Colorado School of Mines +17,508

    Pimentel (2003) – Cornell University –22,300

    Shapouri et al. (2003) – Argonne National Laboratory/USDA +21,105

    Shapouri et al., update (2004) – USDA +30,258 (LHV)

    Pimentel and Patzek (2005) – Cornell/UC-Berkeley –22,300

    Note: HHV = higher heating value; LHV = lower heating value

    ‘The energy balance of corn ethanol revisited’ (2003) by Shapouri et al. included a new energy credit for

    the co-product distillers dried grains with solubles (DDGS)

    ‘The 2001 net energy balance of corn-ethanol’ (2004) by Shapouri et al. included a revised energy credit

    for DDGS 

     Source: Based on data from White (2006)

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     Advances in BioethanolEthanol: an overview

     Future of bioethanol  The future of bioethanol appears to be bright as the need for renewable energy sourcesto replace dependence on foreign oil is growing. With many nations seeking to reduce

    petroleum imports, boost rural economies and improve air quality, world ethanol

    production rose to 13.5 billion gallons in 2006. The success of domestic ethanol industries

    in the US and Brazil has sparked tremendous interest in countries around the globe

    where nations have created ethanol programmes seeking to reduce their dependence

    on imported energy, provide economic boosts to their rural economies and improve the

    environment. As concerns over greenhouse gas emissions grow and supplies of world oil

    are depleted, Europe and countries like China, India, Australia and some south-east Asian

    nations are rapidly expanding their production and use of biofuels.

      A lot of research is being done including turning biomass (materials from plants) into

    ethanol using special biotechnological methods. Biomass ethanol is the future of ethanol

    production because biomass feedstocks, like wheat straw or switchgrass, require less fossil

    fuels to grow, harvest and produce. It also allows more marginal land, such as grasslands,

    to be utilised rather than precious acreage devoted to food crops like corn or soya beans.

    In this way, ethanol production from biomass does not negatively affect the livestock

    and food industry. The biorefinery, analogous to today’s oil refineries, could economically

    convert lignocellulose to an array of fuels and chemicals – not just ethanol – by

    integrating bio- and thermo-chemical conversion (Fernando, 2006). Fundamental research

    and partnerships with the emerging bioenergy industry are critical for the success.

     There has been continued research to improve the energy output of ethanol and

    improvements should continue. Currently, E85 stations are popping up everywhere and

    more products, from generators to power tools and lawnmowers, will all start to use

    alternative fuels. There are already engines that can run on 100% pure ethanol, and

    improvements will help migrate these engines to other areas. Big auto manufacturers like

    Nissan, Ford and Honda have all invested money into E85 models. Portable generators,

    stand-by and emergency generators should all start using ethanol as a fuel source.

     The emergence of carbon trading programmes in response to many countries’

    ratification of the Kyoto Protocol will also enhance the affordability of ethanol fuels in

    comparison to gasoline and diesel. Because ethanol fuels offer a substantial reductionin carbon dioxide emissions, users can obtain carbon credits that can be sold to heavy

    polluters, again reducing ethanol costs while increasing that of fossil fuels. The EU

    recently developed a carbon trading programme. Japan has conducted several scenario

    simulations and hopes to initiate its own nationwide trading system. As Russia considers

    ratification of the Kyoto Protocol, which would bring the agreement into effect, it seems

    likely that similar carbon trading schemes will continue to emerge around the world.

     A combination of well-reasoned government policies and technological advancements

    in ethanol fuels could guide a smooth transition away from fossil fuels in the

    2

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    transportation sector. As environmental factors continue to be incorporated into policyand the fledgling industry emerges, ethanol fuels are likely to become an increasingly

    attractive fuel alternative in the foreseeable future. Looking into the future, the ethanol

    industry envisions a time when ethanol may be used as a fuel to produce hydrogen for

    fuel-cell vehicle applications.

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      Production of bioethanol requires fermentation of the sugar (mono- and polysaccharides)in nearly all kinds of biomass (Olsson et al., 2005). Today there are primarily two types

    of process technology called first- and second-generation technology. First generation

    produces bioethanol from sugars (a dimer of the monosaccharides glucose and fructose)

    and starch-rich (polysaccharides of glucose) crops such as grain and corn.

      Sugars can be converted to ethanol directly, but starches must first be hydrolysed to

    fermentable sugars by the action of enzymes from malt or moulds. The technology is well

    known, but high prices of the raw material and the ethics about using food products for

    fuel are two major problems. This is not an issue with the second-generation production of

    bioethanol – instead a new technology is required. The raw material in second-generation

    process technology is lignocellulosic material such as straw, wood and agricultural residue,

    which is often available as waste.

      These kinds of materials are cheap but the process technology is more advanced than

    converting sugar and starch. The major cause is the lignin which binds together pectin,

    protein and the two types of polysaccharides, cellulose and hemicellulose, in lignocellulosic

    biomass. Lignin resists microbial attack and adds strength to the plant. Pre-treatment

    is therefore used to open the biomass by degrading the lignocellulosic structure and

    releasing the polysaccharides. Pre-treatment is followed by treatment with enzymes which

    hydrolyse cellulose and hemicellulose respectively. The cellulose fraction releases glucose

    (C6 monosaccharide – sugar with six carbon atoms) and the hemicellulose fraction

    releases pentoses (C5 monosaccharide – sugar with five carbon atoms) such as xylose. Out

    of carbohydrate monomers in lignocellulosic materials, xylose is the second most abundant

    Production of bioethanol

     TABLE 3.1 First- and second-generation raw materials for ethanol production

    First generation

    Sugar cane

    Corn

    Wheat 

    Rye

    Sorghum

    Cassava

    Second generation Agricultural waste

      Leftover crop material, such as stalks, leaves and husks of corn plants

    Forestry waste

      Wood chips and sawdust from lumber mills, dead trees and tree branches

    Energy crops

      Fast-growing trees and grasses such as switchgrass

    Municipal solid waste

      Household garbage and paper products

    Food processing and other industrial waste

      Black liquor, a paper manufacturing by-product 

     Source: Based on data from Hamelinck (2003); US DOE (2006a)

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    after glucose. Glucose is easily fermented into ethanol, but another fermentation process isrequired for xylose – for example using special micro-organisms.

     The second-generation technology holds great advantages for the fermentation of

    biomass in the form of agricultural waste materials. The first-generation technology is

    based on much more costly raw material and there are some ethical questions. This is not

    an issue with the second-generation technology – instead there are some challenges such

    as efficient pre-treatment and fermentation technologies together with environmentally

    friendly process technology (for example the reuse of the process water).

      Production of Ethanol is produced from corn by using one of two standard processes: wet milling or dry

    alcohol from corn milling (Yacobucci and Womach, 2003).

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     Advances in BioethanolProduction of bioethanol

    FIGURE 3.1 Ethanol production from corn by the wet milling process

     Source: Source: Based on RFA (2007d)

      

     

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      The main difference between the two processes is in the initial treatment of the grain.

    Dry milling plants cost less to build and produce higher yields of ethanol (2.7 gallons per

    bushel of corn), but the value of the co-products is less. The value of corn as a feedstock

    for ethanol production is due to the large amount of carbohydrates, specifically starch,

    present in corn.

    FIGURE 3.2 Ethanol production from corn by the dry milling process

     Source: Based on RFA (2007d)

     

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     Advances in BioethanolProduction of bioethanol

      Dry milling  In the US, most of the ethanol plants utilise a dry milling process. The major steps of dry

    milling are outlined below:

      1  Milling: after the corn (or other grain or biomass) is cleaned, it passes first through

    hammer mills which grind it into a fine powder.

    2 Liquefaction: the meal is then mixed with water and an enzyme (alpha amylase), and

    passes through cookers where the starch is liquefied. A pH of 7 is maintained by adding

    sulphuric acid or sodium hydroxide. Heat is applied to enable liquefaction. Cookers with

    a high temperature stage (120–150°C) and a lower temperature holding period (95°C)

    are used. The high temperatures reduce bacteria levels in the mash.

      3  Saccharification: the mash from the cookers is cooled and the enzyme glucoamylase is

    added to convert starch molecules to fermentable sugars (dextrose).

      4 Fermentation: yeast is added to the mash to ferment the sugars to ethanol and

    carbon dioxide. Using a continuous process, the fermenting mash flows through

    several fermenters until the mash is fully fermented and leaves the tank. In a batch

    fermentation process, the mash stays in one fermenter for about 48 hours.

      5 Distillation: the fermented mash, now called ‘beer,’ contains about 10% alcohol, as well

    as all of the non-fermentable solids from the corn and the yeast cells. The mash is then

    pumped to the continuous flow, multi-column distillation system where the alcohol

    is removed from the solids and water. The alcohol leaves the top of the final column

    at about 96% strength, and the residue mash, called stillage, is transferred from thebase of the column to the co-product processing area. The stillage is sent through a

    centrifuge that separates the coarse grain from the solubles. The solubles are then

    concentrated to about 30% solids by evaporation, resulting in Condensed Distillers

    Solubles (CDS) or syrup. The coarse grain and the syrup are then dried together

    to produce dried distillers grains with solubles (DDGS), a high-quality, nutritious

    livestock feed. The CO2 released during fermentation is captured and sold for use in

    carbonating soft drinks and beverages and the manufacture of dry ice. Drying the

    distillers grain accounts for about one-third of the plant’s energy usage (Bryan and

    Bryan Inc., 2001).

     TABLE 3.2 Composition of cornComponent Dry matter (%)

    Carbohydrates (total) 84.1

      Starch 72.0

      Fibre (NDF) 9.5

      Simple sugars 2.6

    Protein 9.5

    Oil 4.3

    Minerals 1.4

    Other 0.7

     Source: Pira International Ltd 

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      6 Dehydration: the alcohol then passes through a dehydration system where theremaining water is removed. Most plants use a molecular sieve to capture the last bit of

    water in the ethanol. The alcohol at this stage is called anhydrous (pure, without water)

    ethanol and is approximately 200 proof.

      7  Denaturing: ethanol that is used for fuel is then denatured with a small amount (2–5%)

    of some product, like gasoline, to make it unfit for human consumption.

    Wet milling  The wet milling operation is more elaborate because the grain must be separated into its

    components. After milling, the corn is heated in a solution of water and sulphur dioxide

    for 24–48 hours to loosen the germ and the hull fibre. The germ is then removed from the

    kernel, and corn oil is extracted from the germ. The remaining germ meal is added to the

    hulls and fibre to form corn gluten feed. A high-protein portion of the kernel called gluten

    is separated and becomes corn gluten meal which is used for animal feed. In wet milling,

    only the starch is fermented, unlike dry milling, when the entire mash is fermented.

      New technologies  The production of ethanol is an example of how science, technology, agriculture, and

    allied industries must work in harmony to change a farm product into a fuel. Ethanol

    plants receive the large quantities of corn that they need by lorry, rail or barge. The corn

    is cleaned, ground and blown into large tanks where it is mixed into a slurry of corn meal

    and water. Enzymes are added and exact acidity levels and temperatures are maintained,

    causing the starch in the corn to break down – first into complex sugars and then into

    simple sugars.

    New technologies have changed the fermentation process. In the beginning it took

    several days for the yeast to work in each batch. A new, faster and less costly method of

    continuous fermentation has been developed. Plant scientists and geneticists are also

    involved. They have been successful in developing strains of yeast that can convert greater

    percentages of starch to ethanol. Scientists are also developing enzymes that will convert

    the complex sugars in biomass materials to ethanol. Cornstalks, wheat and rice straw,

    forestry wastes and switchgrass all show promise as future sources of ethanol.

      Co-products  Each bushel of corn can produce 2.5–2.7 gallons of ethanol, depending on which milling

    process is used. Only the starch from the corn is used to make ethanol. Most of the

    substance of the corn kernel remains, leaving the protein and valuable co-products to

    be used in the production of food for people, livestock feed and various chemicals. The

     volume of co-products has increased dramatically with the growth in ethanol production.

    In the US in 2006, ethanol dry mills produced a record 12 million tonnes of distillers grains.

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     Advances in BioethanolProduction of bioethanol

      Of this, approximately 75–80% is fed to ruminants (dairy and cattle), 18–20% to swine

    and 3–5% to poultry. Some estimate that production of distillers grains will reach more

    than 20 million metric tonnes by the time the renewable fuel standard (RFS) is fully

    implemented in 2012. This level of output will make it necessary to find new markets and

    uses for co-products. New uses being considered include food, fertiliser and cat litter.

    While the majority of feed is dried and sold as distillers dried grains with solubles (DDGS),

    approximately 20–25% is fed wet locally, reducing energy costs associated with drying as

    well as transportation costs. Ethanol wet mills produced approximately 430,000 tonnes of

    corn gluten meal, 2.4 million tonnes of corn gluten feed and germ meal, and 565 million

    pounds of corn oil.

    Production of   Lignocellulosic biomass can be converted to ethanol by hydrolysis and subsequent

    ethanol from fermentation (Fan et al. 1987; Badger, 2002). Also thermo-chemical processes can be used

    lignocellulosic to produce ethanol: gasification followed either by fermentation or by a catalysed reaction.

      biomass Hydrolysis fermentation of lignocellulose is much more complicated than just fermentation

    of sugar. In hydrolysis, the cellulosic part of the biomass is converted to sugars, and

    fermentation converts these sugars to ethanol. To increase the yield of hydrolysis, a

    pre-treatment step is needed that softens the biomass and breaks down cell structures

    to a large extent. The pre-treatment and hydrolysis sections allow for many process

    configurations. Present pre-treatment processes are primarily chemically catalysed, but both

    FIGURE 3.3 Distillers grains from US ethanol refineries, 1999–2006

     Source: Based on data from RFA, 2007a

                                          

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    economic and environmental arguments drive the development of physical pre-treatments. The pre-treatment technology chosen affects the yield of both pre-treatment and

    subsequent process steps. Acid hydrolysis processes have been used for many decades, but

    have environmental consequences. Enzymatic processes under development are supposed

    to have roughly equal costs to conventional processes today, but are more environmentally

    sound, and these costs can be reduced further. Therefore, most studies focus on enzymatic

    hydrolysis (Lynd, 1996; Ogier et al., 1999; Yu and Zhang, 2004; Sheehan, 2001). The

    fermentation step, on its turn, does not yet convert all sugars with equal success. Future

    overall performance depends strongly on development of cheaper and more efficient

    micro-organisms and enzymes for fermentation. Newer micro-organisms may also allow for

    combining more process steps in one vessel, such as fermentation of different sugars and

    enzyme production (Lynd, 1996). Lastly, the biomass composition in hemicellulose, cellulose

    and sugar influences the ethanol yield.

      A simplified generic configuration of the hydrolysis fermentation process is shown in

    Figure 3.4.

      Pre-treatment   Pre-treatment is required to alter the biomass macroscopic and microscopic size and

    structure as well as its submicroscopic chemical composition and structure so that

    hydrolysis of carbohydrate fraction to monomeric sugars can be achieved more rapidly

    and with greater yields (Sun and Cheng, 2004; Mosier et al., 2005; Wyman et al., 2005a).

    FIGURE 3.4 Biomass to ethanol process

     Source: Based on RFA (2007d); Ladisch (2003); Wyman et al. (2005)

     

     

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     Advances in BioethanolProduction of bioethanol

    Pre-treatment affects the structure of biomass by solubilising hemicellulose, reducingcrystallinity and increasing the available surface area and pore volume of the substrate.

    Pre-treatment has been considered as one of the most expensive processing steps in

    biomass to fermentable sugar conversion (Mosier et al., 2005).

    Each type of feedstock requires a particular pre-treatment method to minimise the

    degradation of the substrate and to maximise the sugar yield. There is huge scope in

    lowering the cost of pre-treatment processes through extensive R&D approaches.

    Pre-treatment of cellulosic biomass in a cost-effective manner is a major challenge of

    cellulose to ethanol technology research and development.

    Native lignocellulosic biomass is extremely recalcitrant to enzymatic digestion.

     Therefore, a number of thermochemical pre-treatment methods have been developed

    to improve digestibility (Wyman et al., 2005a). Recent studies have clearly proved that

    there is a direct correlation between the removal of lignin and hemicellulose on cellulose

    digestibility (Kim and Holtzapple, 2006). Thermochemical processing options appear

    more promising than biological options for the conversion of lignin fraction of cellulosic

    biomass, which can have a detrimental effect on enzyme hydrolysis. It can also serve as

    a source of process energy and potential co-products that have important benefits in a

    life-cycle context (Sheehan et al., 2003). Pre-treatment can be carried out in different ways

    such as mechanical combination (Cadoche and Lopez, 1989), steam explosion (Gregg and

    Saddler, 1996), ammonia fibre explosion (Kim et al., 2003), acid or alkaline pre-treatment

    (Damaso et al., 2004; Kuhad et al., 1997) and biological treatment (Keller et al., 2003).

    Each technology has advantages and disadvantages in terms of costs, yields, material

    degradation, downstream processing and generation of process wastes.

      Hemicellulose In order to make the cellulose feedstock more digestible by enzymes, the surrounding

    hydrolysis hemicellulose and/or lignin is removed, and the cellulose microfibre structure is modified.

    Chemical, physical or biological treatment are employed to solubilise the lignin and

    hemicellulose. Subsequently, when water or steam is added, the free hemicellulose polymer

    is hydrolysed to monomeric and oligomeric sugars. During hydrolysis, hemicellulose

    sugars may be degraded to weak acids, furan derivates and phenolics. These compoundsinhibit the later fermentation, leading to reduced ethanol yields. The production of these

    inhibitors increases when hydrolysis takes place at higher temperatures and higher acid

    concentrations. In order to remove the inhibitors and increase the hydrolysate fermentability,

    several chemicals and biological methods have been used (Martinez et al., 2000; Nilvebrant,

    2001; Martin et al., 2002; Lopez et al., 2004). The detoxification of acid hydrolysates has

    been shown to improve their fermentability. However, the cost is often greater than the

    benefits achieved (Palmqvist and Hahn-Hagerdal, 2000; von Sivers et al., 1994).

      Common chemical pre-treatment methods use dilute acid, alkaline, ammonia, organic

    solvent, sulphur dioxide, carbon dioxide or other chemicals. The most important methods

    are the use of acid and alkali. Acid catalysed hydrolysis uses dilute sulphuric, hydrochloric

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    or nitric acids. Of all chemical pre-treatments, dilute sulphuric acid (0.5–1.5%, temperatureabove 160°C) has been most favoured for industrial application because it achieves

    reasonably high sugar yields from hemicellulose: xylose yields of at least 75–90% (Sun