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CHAPTER-3
OVERVIEW OF
BIOMASS
BASESD FUELS
AND THEIR
CONVERSION
TECHNOLOGIES
CHAPTER-3
OVERVIEW OF BIOMASS BASED FUELS AND THEIR CONVERSION
TECHNOLOGIES
3.1- Classification of biomass
The wood is the most common example of the biomass. When burned, it releases the
stored solar energy stored into it through photosynthesis by the tree. Still, the wood is not only
example of best known biomass. Different sources of biomass are agricultural residues like
bagasse from sugarcane, straw, hay, fiber and nutshells; wood wastes like bark, sawdust, mill
scrap and timber blocks and the trash paper and organic materials in municipal waste. Also
energy crops, in the form of fast growing trees and shrubs like poplars, willows, Jatropha and
several wild growing grasses like switchgrass, algae (in ponds, lakes or ocean and municipal
waste water treatment plants), the methane captured from landfills and manure from cattle or
poultry can also be used as viable biomass feedstock.
Biomass, after being processed for converting it into fuel is termed as feedstock. Biomass
can be classified in several groups based on a variety of criteria. They may be grouped on the
basis of their availability, physical properties, conversion processes or types of utilization.
Communally the biomass feedstock can be classified in two distinct ways. First they may be
categorized, depending on either their sources of supply or availability in nature. Another way of
classifying the biomass feedstock is to differentiate them as per their physical characteristics.
Different classes of feedstock depending on their route of sources are enlisted in the table
3.1 along with the representative examples.
3.1.1 - Classification of Biomass feedstock supply sector wise
Table 3.1
Classification of biomass feedstock supply sector wise
Supply Sector
Type of feedstock Example
Agriculture Dry residues
Stalk, straw, bagasse, husk, leaves and roots (tubers and bulbs)
Livestock wastes Solid and liquid manure
Energy crops
Dry woody crops Bamboo, willow, poplar, eucalyptus
Dry non-woody crops
Miscanthus, switch grass, common reed, giant reed
Oil crops Jatropha, Soybean, palm, cottonseed,
sunflower
Starch crops Wheat, potatoes, maize, barley, corn,
sugarcane, agave, cactus
Aquatic plants Hyacinth, algae
Forest
Byproducts Bark, leaves, wood chips, logs from
branches and natural thinning
Bio-energy plantation
Pine, eucalyptus, hybrid poplar, sweetgum, cottonwood
Industry
Wood industry Residues
Bark, wood chips, off-cuts, slabs, sawdust from sawmills/ timber mills
Fibrous waste from pulp and paper production units
Food industry Residues
Wet cellulosic waste parts of vegetable and grains, used cooking oils, oil cakes, tallow,
and slaughter-house waste
Industrial products Organic wastes (solvents and other
compounds) of chemical and pharmaceutical processes
Others Shells and husks from palm, coconut,
almond, olive, walnut
Municipal Parks and Gardens Twigs, leaves, bark from pruning and grass
Organic wastes Wood, landfill gas, sewage sludge, sewage
gas
Roadside wastes Wood, shrubs, grass and hay
The classification of feedstock, based on their physical properties is described in the
following subsection 3.1.2 with some representative examples.
3.1.2 - Classification of Biomass feedstock based on the physical characteristics:
Woody biomass: They include materials from trees, bushes and shrubs. Their characteristics are
high bulk density, high calorific value, low moisture content and low ash content. Woody
biomass is a preferred class of feedstock for biomass to energy conversion processes.
Non-woody biomass: They include grains and non-woody stalks/stems of the residues from
agricultural crop harvest, wastes from poultry and livestock farms, organic parts of municipal
solid wastes (MSW) and animal excreta and residues from the food processing industry. Their
characteristics are lower bulk density, higher moisture content, lower calorific value and higher
ash content,. Although, they are economical than woody biomass but, less preferred due to
various associated drawbacks. Typical energy potentials of some common agricultural crops are
summarized in table 3.2.
Table 3.2
Energy potential of some common non-woody agricultural crop residues
Agricultural Crop
Type of Residue
Calorific Value (Kcal/Kg)
Wheat Straw 3500
Paddy Straw 2400
Paddy Husk 3000
Bajra Stalk 3850
Maize Stalk 3450
Maize Cobs 3800
Groundnut Stalk 4150
Gram (Chana)
Cotton
A
Figure 3.1 A
B- Cowdung heap, C
Gram (Chana) Straw 3800
Stalk 4650
B
C
Figure 3.1 A- Cowdung (Calorific value: 3300 Kcal/Kg),
Cowdung heap, C- Cowdung cakes (Calorific value: 3100 Kcal/Kg)
Cowdung (Calorific value: 3300 Kcal/Kg),
Cowdung cakes (Calorific value: 3100 Kcal/Kg)
Dry lignocellulosic biomass feedstock is used for thermo-chemical conversion like
combustion, gasification and liquefaction processes. The wet lignocellulosic biomass feedstock
is used for biological conversion processes, mostly digestion or fermentation. Most important
technical specifications of solid biofuels developed between 2010 and 2012 are EN 14961 for
specification and classification and EN 15234 for quality assurance.
Figure 3.2 - Aquatic weeds a promising biomass for energy
3.2 - Composition of Biomass
Although, the chemical composition of biomass material varies among species, however
plants consist of mainly carbohydrates or sugars and lignin. The carbohydrate part consists of
several sugar molecules linked together in long chains or as polymers. Cellulose and
hemicellulose are wo larger categories of carbohydrate having significant values. Long cellulose
polymers are used in nature to build the fibers that give strength to a plant. Further, lignin in the
biomass consists of non-sugar molecules and acts like a glue that binds the cellulose fibers
together. The carbon dioxide from the atmosphere is combined with the water in the process of
photosynthesis and produces carbohydrates, which form the bulk of the biomass. Thus, solar
energy is basically stored in the biomass in the form of chemical energy through the process of
photosynthesis. When biomass is burnt, the oxygen from the atmosphere reacts with the carbon
present in the biomass, to generate carbon dioxide and water. This process of extracting the
energy stored in the chemical bonds of the biomass material is cyclic in nature, as carbon dioxide
is again used for producing newer biomass material through the process of photosynthesis.
Wood (largely secondary cell walls) is made up of following major constituents which
also vary with type and age of a particular species:
• Cellulose (C6H10O5)n is major structural component and constitutes a major portion (35-
50%) of plant cell wall. It consists of long chains of polysaccharides.
• Hemicellulose is constituted by sugars which comprises of 20-35% of plant biomass on
dry weight basis. Xylans, a type of hemicellulose, are highly complex short chains of
polysaccharides made from units of xylose which is a pentose sugar. They are found in
cell walls of plants and some algae.
• Lignin (10-25%) complex and high molecular weight polymer. It is formed by de-
hydrogenation of p-hydroxy-cinnamyl alcohols. Lignin is a complex phenolic polymer
which fills the gaps or spaces in the cell wall. It strengthens the cell wall by driving out water.
• Water soluble constituents include sugars, amino acids and aliphatic acids.
• Ethers and alcohol-soluble constituents (e.g. fats, oils, waxes, resin and many pigments).
• Proteins of different chemical compositions (1-5%).
3.3 -Physical Biofuel types
Solid biomass based fuels
The utilization of solid biomass based fuels demands a lower effort for conditioning and
conversion of biomass feedstock. This results in total energy balance in consideration of the
complete utilization chain. Wood is considered to have better efficiency amongst the solid
biomass based energy sources. They are used in decentralized environment of households or
small industries for heat generation in the form of firewood, briquettes and pellets with fine
particulate air filters to reduce atmospheric pollu
biomass based fuels are utilized through cogeneration of heat and power. Cogeneration of heat
and power using Sterling engines at a very small scale are being developed, using wood pellets.
Wood from short-rotation plantations can achieve a high thermal energy yield per acre.
Straw and husks from short-rotation agriculture or plantations are reported with good energy
yield, but requires an expensive treatment
competition in the food production.
the near absence of oxygen. It is
This dual functionality of biochar, to
atmosphere, is very useful for mitigating climate change.
small industries for heat generation in the form of firewood, briquettes and pellets with fine
particulate air filters to reduce atmospheric pollution. In centralized larger facilities solid
biomass based fuels are utilized through cogeneration of heat and power. Cogeneration of heat
and power using Sterling engines at a very small scale are being developed, using wood pellets.
ation plantations can achieve a high thermal energy yield per acre.
rotation agriculture or plantations are reported with good energy
yield, but requires an expensive treatment and less efficient. However, they
competition in the food production. Biochar is obtained through burning biomass
is a carbon negative energy source and an important
dual functionality of biochar, to enhance soil fertility while holding carbon back from the
is very useful for mitigating climate change.
Figure 3.3 - Fuelwood
small industries for heat generation in the form of firewood, briquettes and pellets with fine
tion. In centralized larger facilities solid
biomass based fuels are utilized through cogeneration of heat and power. Cogeneration of heat
and power using Sterling engines at a very small scale are being developed, using wood pellets.
ation plantations can achieve a high thermal energy yield per acre.
rotation agriculture or plantations are reported with good energy
they can avoid the
burning biomass feedstock in
important soil builder.
carbon back from the
Liquid biomass based fuels
Liquid biomass based fuels belong to natural vegetable oils,
(BTL) fuels (produced by using
depolymerization) and biodiesel. However, the efficient and economical production of fuels is
feasible only in centralized large production f
economical production is good only when it is used locally, e.g., in tractors or agricultural
machines. The use of natural vegetable oils requires complex modifications in standard diesel.
However, biodiesel may be used
blended with the petroleum diesel. Bioethanol
and can be made from common sugar crops like sugar beet
starch through the microbial fermentation of sugar.
Figure 3.4 - Charcoal
Liquid biomass based fuels belong to natural vegetable oils, bioethanol, biomass to liquid
by using Fischer-Tropsch process, flash pyrolysis
and biodiesel. However, the efficient and economical production of fuels is
feasible only in centralized large production facilities. The decentralized efficient and
economical production is good only when it is used locally, e.g., in tractors or agricultural
machines. The use of natural vegetable oils requires complex modifications in standard diesel.
e used, in unmodified conventional diesel engines
petroleum diesel. Bioethanol and biobutonol are easy to manufacture
and can be made from common sugar crops like sugar beet and sugar cane or crops containing
through the microbial fermentation of sugar.
bioethanol, biomass to liquid
Tropsch process, flash pyrolysis or Catalytic
and biodiesel. However, the efficient and economical production of fuels is
acilities. The decentralized efficient and
economical production is good only when it is used locally, e.g., in tractors or agricultural
machines. The use of natural vegetable oils requires complex modifications in standard diesel.
diesel engines, standalone or
easy to manufacture/process
sugar cane or crops containing
Figure 3.5 - Bioethanol from Econol (UK)
Figure 3.6 - Biodiesel Fuel
Gaseous biomass based fuels
Gaseous biomass based fuels from organic waste are obtained through thermal
gasification or biological processes of fermentation and anaerobic digestion. These methods are
energy-efficient even at small scale in households and thus well suited for small plants in rural
and remote areas. These small biogas plants do not convert the gas directly into electricity but
condition the gas to be used locally. Biomethane and Syngas (a mixture of carbon monoxide and
hydrogen gases) are examples of biomass based gaseous fuels. Direct composting of organic
waste has negative impact on climate. Therefore, organic waste from different sources can be
separated and used to produce biofuels using multiple stages of fermentation and composting to
maximize yield along with environmental protection.
Figure 3.7 - Pre-fabricated biogas plant for domestic use
3.4 - Classification of biofuels based on the sequence of development
Although biomass based fuels are produced in solid, liquid and gas physical forms.
However due to development in conversion techniques over the time they may be classified in
the following categories as per sequence of their advancement with time:
3.4.1 - First Generation Biofuels
First generation biomass based fuels are also termed as conventional biofuels. They may
be solid fuels available in nature in raw form like wood, grass, dried animal wastes and forest
residue. They can also be derived from domestic, agricultural or industrial wastes like household
refuse, sawdust, wood chips, charcoal and biochar. Liquid biofuels are extracted from sugars,
starch and vegetable oils of biomass feedstock and include like bioalcohals (Ethanol, methanol,
butanol), bioethers, biodiesel, green diesel and biofuel gasoline. Gaseous biofuels are produced
by anaerobic digestion or combustion of organic feedstock. Biogas (mostly methane) and Syngas
(mixture of carbon monoxide, hydrogen and hydrocarbons) are examples of these biofuels which
are non-polluting and sustainable.
These fuels are also derived from energy crops and biomass that is part of staple food in
several communities and grown on agricultural land thus endangering the food chain. The
growing demands of biofuels derived from these sources also have serious negative impact on
the sustenance of biodiversity of the region and efficient land use. Therefore first generation
biofuels have problem of continuous feedstock supply and so they cannot be considered as
sustainable.
3.4.2 - Second Generation Biofuels
To overcome the problem of sustainable supply of feedstock associated with first
generation biofuels, efforts have been done to use biomass obtained from inedible waste and
non-food crops and non-invasive grasses/shrubs grown on non-agricultural, marginal and no-
arable lands across the world. These avoid food vs. fuel conflict and proper land use without
disturbing ecology and biodiversity. This ensures the sustainability of feedstock to produce
biofuels with increasing demand. Second generation biofuels are obtained by the conversion of
lignocellulosic parts of biomass or woody material of the plants using advanced complex
chemical and biological conversion processes.
Fischer-Tropsch Diesel, wood diesel, cellulosic ethanol, biomethanol and biohydrogen
are examples of these fuels. Dimethyl ether (DME) and BioDME are produced from
lignocellulosic biomass feedstock and used in internal combustion engines as a substitute of
petroleum diesel and gasoline. They are also used as substitute of propane in liquefied petroleum
gas (LPG) in domestic and industrial applications. They are used in turbines for electricity
generation in place of natural gas. Lignocellulosic biomass based fuels has the capability of
reducing GHG emissions to >88% in comparison to 13% by cellulosic biomass based fuels.
3.4.3 - Third Generation Biofuels
Variety of biomass feedstock, including the first and second generation biofuels, may be
used for better yield with improved performance of the produced fuel at an affordable cost using
only limited area of land. Therefore, third generation biomass based fuels are derived from non-
food and otherwise waste biomass feedstock using complex conversion techniques involving
enzymatic and microbial activities and advanced genetic engineering. As an example, genetically
engineered varieties of Jatropha, grown in a small area of marginal land, are economically viable
source of feedstock to produce biodiesel at competitive cost. Work has been done to produce
myco-diesel from cellulose using Gliocladium roseum, a fungus. Lipids extracted from another
species of fungus Cunninghamella japonica have also been converted economically and
efficiently into biofuels. Bacteria like Clostridium have properties to convert lignocellulosic
biomass into useful biomass.
Several species of algae growing in ponds, lakes and oceans are being considered to
provide biofuels in large amounts at economical scale solving the energy problem. Algae
feedstock provides lipids, proteins and carbohydrates, which can be converted into biodiesel
fuels, methane and ethanol respectively. Algae need nutrients, CO2 and water to grow under
sunlight. So, if grown on commercial scale in ponds and bioreactors, algae can absorb huge
amounts of CO2 emitted from industries and thermal power plants and mitigate GHG problem up
to a large extent. Also non-fuel parts of the biomass can be used as nutrient to further grow more
algae. The yield can be measured in mass per unit of volume instead of mass per unit of area as
extremely large quantities of algal biomass can be cultivated in vertical columns requiring
reduced horizontal space.
Figure 3.8 - Algae as pond scum
Figure 3.9 - Close up view of algae as pond scum
3.4.4 - Fourth Generation Biofuels
In addition to replace fossil fuels, biomass based fuels need to reduce CO2 concentration
in atmosphere. Second and third generation biofuels are helpful in this regard by reaching up to a
level of being carbon-neutral. This is possible through absorbing atmospheric CO2 by
photosynthesis during biomass growing and improvements in the biomass to fuel conversion
processes. However, increasing levels of CO2 due to industrial growth require further steps in
this direction for sustainability. Forth generation biofuels are aimed to be produced using such
processes, which not only reduce the levels by replacing fossil fuels, but also capture large
amounts of CO2 from atmosphere and store into emptied underground gas and oil wells or use in
the industrial processes.
3.5 - Biomass to Fuel Conversion Technologies:
Biomass in general may not be used to get energy directly. It is required to be converted
into suitable types/forms of fuels for being used in real life applications in an efficient and
economical way. This function is achieved by converting biomass into fuel form through
appropriate technology. The important biomass to fuel conversion technologies in practice has
been described in this chapter.
3.5.1 - Mechanical Conversion Techniques:
Different varieties of biomass feedstock can be utilized, through direct combustion, to
generate energy, without converting it into any other fuel form. However, the biomass, as
available in the natural form is seldom useful and requires some kind of conditioning for proper
and efficient utilization. These biomass feedstocks can be converted into convenient forms as
highly useful and economical biofuels using following mechanical conversion processes:
(1) Cutting or chopping
Biomass available in nature is of varying in shape and size ranging from wheat and paddy
stalks of crop residue to branches and trunks from forest logging operations and timber industry.
The odd size or shape of these biomass feedstock pose practical problems in using them directly
into the kitchens stoves or furnaces of boilers in industries and power plants. For direct
combustion in domestic and commercial applications, these materials are required to be
converted into smaller pieces of appropriate shape and size (figure 3.1). This conversion is being
done by mechanical process of cutting or chopping/shredding of the available biomass feedstock
into appropriate size/shape. The sizing in small quantity can be done manually by breaking or
chopping through hand operated tools, by applying manual labor. However, cutting machines
like sawmills are used for sizing at large scale in production plants. Sizing of biomass material is
beneficial from storage and transportation points of view. The process, up to some extent, also
increases active surface area of the biomass feedstock and improves combustion with a reduction
in moisture content. Sizing can also be precursor of other biomass to fuel conversion processes
as a pre-treatment stage.
Figure 3.10 - Firewood blocks
(2) Pulverizing
Pulverizing is a type of downsizing of woody and non-woody biomass into fine granules
or powder. Pulverizing increases the active surface area of the biomass feedstock. This helps in
combustion of the biomass more efficiently generating more heat per unit mass of the fuel.
Finely powdered biomass material, as shown in figure x.x, can be used in stoves directly or
mixed with coal for co-firing in furnaces of the boilers at power plants. Pulverizing can also be
precursor of other biomass to fuel conversion processes as a pre-treatment stage of the main
process.
Figure 3.11 - Pulverized wood for co
(3) Briquetting
Briquetting is the process of compacting the loose strands or chips of biomass material.
It provides economic and compact high density fuel which can be stored in smaller space and
transported easily. Briquetted biomass is also low in GHG emission and is
industrial applications as an alternative to the fossil fuels. They are used in power plants alone
are co-fired with fossil coal for generating electricity. Biomass feedstock, from wastes and
residues of agriculture, forestry and wood
using as fuel.
The biomass feedstock is pulverized to a fine size of 3
to reduce its moisture content to 12
briquetting machines, of type and size, depending on the quantity and variety of the available
feedstock and capacity of the plant. No binders are required as high temperature of briquetting
plasticize the lignin present in the biomass to bind fine wood pa
Pulverized wood for co-firing with coal in a CHP plant
Briquetting is the process of compacting the loose strands or chips of biomass material.
It provides economic and compact high density fuel which can be stored in smaller space and
transported easily. Briquetted biomass is also low in GHG emission and is used in domestic and
industrial applications as an alternative to the fossil fuels. They are used in power plants alone
fired with fossil coal for generating electricity. Biomass feedstock, from wastes and
residues of agriculture, forestry and wood industry sectors, is compressed into briquettes for
The biomass feedstock is pulverized to a fine size of 3-5 mm and dried in a drying system
to reduce its moisture content to 12-15%. This pretreated feedstock is then briquetted using
briquetting machines, of type and size, depending on the quantity and variety of the available
feedstock and capacity of the plant. No binders are required as high temperature of briquetting
plasticize the lignin present in the biomass to bind fine wood particles into solid mass. High
firing with coal in a CHP plant
Briquetting is the process of compacting the loose strands or chips of biomass material.
It provides economic and compact high density fuel which can be stored in smaller space and
used in domestic and
industrial applications as an alternative to the fossil fuels. They are used in power plants alone
fired with fossil coal for generating electricity. Biomass feedstock, from wastes and
industry sectors, is compressed into briquettes for
5 mm and dried in a drying system
15%. This pretreated feedstock is then briquetted using
briquetting machines, of type and size, depending on the quantity and variety of the available
feedstock and capacity of the plant. No binders are required as high temperature of briquetting
rticles into solid mass. High
energy density and low moisture content (~4%) make biomass briquettes an ideal substitute of
coal and petroleum oil for use in furnaces of industries and power plants. They are also used as
feedstock to produce other biofuels like charcoal.
Source: http://www.cnpelletmachine.com/Related_Product/Biomass_Briquette_Machine.html
Figure 3.12 - Wheat straw (loose straw and briquettes)
(4) Pelletizing
Pelletizing is also a process of compacting of the biomass feedstock, into small
manageable sizes for direct use in stoves and furnaces to produce heat through combustion.
Pellets are basically smaller size briquettes (in the shape of rods or tablets) ranging from 5-12
mm and used as heating fuel in homes and industries. Due to their high energy density, they are
used in power plants for electricity generation. Wood pellets are manufactured from residues and
wastes of sawmills and other wood industries. The feedstock is first compressed into a hammer
mill and then passed through a press. High pressure of press increases the temperature of the
feedstock and makes the lignin as a bonding agent for the wood particles. The process is highly
energy efficient as total energy involved in conversion is <2% of the energy content of the
pellets. Most of the agricultural and forest residues like grass can also be converted into different
grades of pellets depending on their energy density. The energy content of approximately 4.7 –
5.2 MWh/tone for wood pellets have been reported. However, to reduce particulate matter
emission on combustion, filters and precipitators are required in industries and power plants.
Source: http://www.pellet-press.com/News/bamboo-pelletizing-mill.html
Figure 3.13 - Bamboo stalk pellets
3.5.2 - Thermo-chemical Conversion Techniques:
(1) Thermal Decomposition Processes
(a) Carbonization or Charcoal Making
The main objective of carbonization is to increase the calorific value of the biomass
feedstock by converting it into solid product charcoal (figure 3.x). Carbonization is the process
of dry distillation of biomass feedstock such as wood, bark, bamboo, rice husks, etc. by heating
at 400-600°C in the partial or complete absence of air or oxygen. The biomass feedstock is
arranged in a pile (figure 3.x) and burnt after covering it from all sides to prevent air/oxygen.
Charcoal is produced as the main product which is used as a solid fuel for food-cooking and
space-heating purpose.
Source: http://en.wikipedia.org/wiki/Charcoal
Figure 3.14 - Charcoal
The process is very easy to operate using inexpensive equipments producing efficient
biofuels at reasonable cost. The process also produces tar, pyroligneous acid (used as deodorant),
and combustible gases as by-products. The process of carbonization helps in reducing
environmental degradation by utilizing wastes from several sources. This is very useful process
for producing biomass based fuels and solving waste disposal problem simultaneously.
Source: http://en.wikipedia.org/wiki/Charcoal
Figure 3.15 - Wood pile for charcoal making
(b) Gasification
Direct combustion of biomass, in certain cases, produces slagging residues and corrosive
substances, hindering the operation of the furnaces and boilers during the process. Therefore,
direct combustion or co-firing of biomass is not always a techno-economically feasible option
for producing heat. However, biomass may be converted into a clean gaseous fuel form which
can be easily and efficiently burnt into the furnace to generate heat and electricity. The gaseous
fuel thus produced may be transported to the point of utilization. The process of gasification, as
shown in equation 3.1, is a thermo-chemical process of partial combustion and reduction, which
converts solid biomass feedstock into useful clean gaseous fuels.
C6H10O5 + ½ O2 → 6CO + 5H2 + Energy (3.1)
This is an environment friendly (very low GHG and particulate emissions) and well
proven technology in practice for several decades. There are several types of gasifiers used
depending on the type of feedstock and plant capacity. Producer gas and Syngas are produced
from the biodegradable waste material, solving waste disposal problem. Syngas can be used
without any further processing or modifications, directly in gas engines and turbines. Syngas
may also used for producing hydrogen and methanol or can be converted into synthetic biofuel
through the Fischer–Tropsch process.
Source: https://www.ecn.nl/fileadmin/ecn/units/bio/Overig/pdf/Biomassa_voordelen.pdf
Figure 3.16 - Block diagrams of direct gasification reactors
Gasification of biomass is done by using gasifiers of different configurations. Selection
of a gasifier type depends on the characteristics of biomass feedstock and end products. Block
diagrams four basic fixed bed reactor types for gasification are shown in figure 3.16.
Source: N.L. Panwar et al. (2012)
Figure 3.17 - Fixed bed downdraft biomass gasifier
Updraft gasifiers are very efficient with high conversion rates of gasification. The exit
gas temperatures are in the range of 100-300 0C and consist of mainly product gas. Fixed bed
downdraft gasifiers are less efficient with lower rates of conversion. Conversion rate of
downdraft gasifiers can be increased by supplying oxygen to increase the temperature. But this
increases the cost of conversion. Fluidized bed reactors are used for large scale gasification
operations. Fluidized bed gasifiers are designed as circulating fluidized bed (CFB), bubbling
fluidized bed (BFB) and coupled fluidized bed types.
Conversion efficiency of fluidized bed gasifiers is in the range of 90-98%. The output is
in the form of product gas (N2-free) and flue gases. Entrained bed or flow reactor type gasifier is
used to produce Syngas. The biomass feedstock is required to be pulverized to 1mm size in order
to be used. The operation is accomplished at high temperature and pressure than other three types
of gasifiers.
Source: https://www.ecn.nl/fileadmin/ecn/units/bio/Overig/pdf/Biomassa_voordelen.pdf
Figure 3.18 - Block diagram of an advanced two-step gasification process
(c) Pyrolysis
Pyrolysis is the thermal decomposition of biomass, which occurs in the absence of air or
oxygen. The organic material is heated in a non-reactive atmosphere. This process is composed
of both simultaneous and successive reactions. Thermal decomposition of organic components in
biomass starts at 350 - 550 °C and goes up to 700 - 800 °C in the process. The long chains of
carbon, hydrogen and oxygen compounds in the biomass break down into the molecules, with
smaller chains of carbon, in the form of gases, condensable vapors and solid charcoal. The rate
and extent of decomposition of various components depend on the process parameters of the
reactor. They consists of temperature, biomass heating rate, pressure, reactor configuration and
characteristics of the biomass feedstock. Biomass pyrolysis yields mainly biochar, bio-oil and
gases, which include carbon dioxide, hydrogen, methane and carbon monoxide. Carbonization as
described in the section (a) is also a type of low temperature pyrolysis for producing charcoal, a
solid biofuel. The typical pyrolysis process reaction is shown in equation 3.2.
HEAT C6H12O6 ====� (H2 + CO + CH4 + C2H6 + …..+ C5H12) + (CH3OH + CH3COOH) + H2O + C + Tar
(3.2) Biomass Gas Liquid Water Char
Pyrolysis processes has been broadly classified into three basic types:
Slow pyrolysis process is characterized by the low temperature and pressure process of
very long duration (ranging from few hours to several days). Carbonization as described earlier
to produce charcoal is an example of the slow pyrolysis. Ashes and other residue may have some
commercial value, depending on the species of the biomass used in the process.
Fast pyrolysis (shown in figure 3.9), in contrast to the slow pyrolysis process, occurs at
higher temperatures of 577-977 °C and takes <2 seconds of vapor residence time. This is
characterized by the use of otherwise waste lignocellulosic or hard parts of woody biomass
residue to produce environment friendly biofuels. Pyrolysis plants are best located near the
source of the feedstock to for economic reasons. The transportation costs are reduced to only the
costs of transporting produced fuels. Also, the feedstock needs to be finely grinded for fast
reactions.
Source: N.L. Panwar et al. (2012)
Figure 3.19 - Block diagram of fast pyrolysis process
Flash pyrolysis, as the name suggests, have much shorter vapor residence time than the
fast pyrolysis process. The process is used to produce bio-crude oil from organic waste material.
The conversion takes place at higher temperatures in the range of 750-1000 °C and typical vapor
residence time is 5-10 seconds. The yields have been reported to be up to 70%. Therefore, this
process is considered to be very efficient conversion process for producing high quality and
clean biofuels with very low ash content (Shurong Wang et al. 2005). However, the presence of
pyrolytic water in the bio-crude oil is a problem needed to be solved along with techno-economic
feasibility of using particular biomass feedstock for conversion using flash pyrolysis (Z.W.
Zhong et al. 2010).
Source: Shurong Wang et al. (2005)
Figure 3.20 - Schematic of fluidized bed reactor for flash pyrolysis
Plasma pyrolysis is an emerging technology and uses high energy plasma arc to break
down the biomass feedstock into gases at atomic level and solid residue. Plasma is the 4th state of
matter and the conversion takes place at very high temperature (about 12000 °C) and slightly
negative pressure to remove the produced gas. The vapor residence time is very short (5-10
seconds). High energy arc is produced by applying high voltage across a pair of electrodes inside
the reactor. The high temperatures convert biomass into Syngas as a biofuel product and solid
slag as residue. In case of using organic MSW, the cleanup of produced gas is required to
remove trace contaminating metal elements (H. Huang and L. Tang, 2007). The process has
advantages of converting of large quantities of waste material into useful fuel and solving landfill
problem. However, energy efficiency of the system along with technological challenges of
design and fabrication of appropriate reactor for high temperature and chemically corrosive
environment are the key issues of using this technique. The process has been reported to be
economically viable and energy efficient for pyrolysis of rubber waste materials and is to be
investigated for wet biological wastes (Christopher J. Lupa et al. 2012).
Characteristics of the products depend on the parameters like temperature, pressure,
residence time and rate of heating during the conversion process. The liquid fuels referred as bio-
crude or bio-oil may need further up gradation or refinement to be used as advanced biofuel. The
process of pyrolysis has significance of converting lignocellulosic biomass feedstock, obtained
from residue and waste materials, into useful fuels. This helps in reducing the use of edible
varieties of biomass feedstock for producing biofuels and thus avoiding food conflict in a large
number of communities.
(d) Hydrothermal Liquefaction
In the biomass liquefaction macro-molecule compounds in the feedstock, in the presence
of a suitable catalyst, are decomposed into fragments of light molecules. These fragments, which
are unstable and reactive, at the same time, re-polymerize into oily compounds of proper
molecular weights. In this process, the resulting product is liquid oil or bio-crude oil which can
be stored, transferred through pumping systems and used either in direct combustion furnaces or
as feedstock for treatment leading to specific biofuels (Saqib Sohail Toor et al. 2011).
Source: Kruse A et al. (2007)
Figure 3.21 - Hydrothermal biomass degradation
Hydrothermal liquefaction is used to produce bio-crude oil with higher heating value than
the one produced through pyrolysis. The bio-crude oil can be refined, by the process of
hydrogenation, to get fuels comparable to the ones obtained from fossil crude oil. In this process
wet untreated biomass feedstock is injected into a preheated reactor at ~400 °C under high
pressure (<150 bar). The reaction takes about 15 minutes and then it is cooled down very quickly
to ~70°C. The process is highly efficient (~85-90%) and environment friendly as it does not
require drying of feedstock or any contaminating solvents and heat is recycled between heating
and cooling phases of the process. The product bio-crude oil can directly be used in heavy oil
engines. It can further be refined to get diesel, gasoline and jet fuels for transportation systems. It
can be stored, pumped or transported to remote locations of use.
Some drawbacks of the process are high cost of high pressure reactors and feeding
mechanism of slurry and pre-treatment processes of the feedstock. Therefore, the process needs
to be made economically attractive through research and development work as an appropriate
alternative to polluting and uneconomical petroleum and other fossil fuels.
(e) Hydrothermal Gasification
Hydrothermal gasification of biomass is efficient and environment friendly process to
convert wet biomass such as sewage sludge, manure and other high-moisture containing biomass
and wet organic residues into useful gaseous fuel. The biomass feedstock is fed into a gasifier at
supercritical conditions of higher temperature and pressure (>374 0C and >221 bar). The water in
the reactor at supercritical state acts as non-polar organic solvent and converts organic
compounds of feedstock including lignin parts into gases. The reaction can be described as in the
equation 3.3, shown below.
2C6H12O6 + 7H2O → CO + 15H2 + 2CH4 + 9CO2 (3.3) Biomass Water Synthetic natural gas
Overall efficiency of 70% for synthetic natural gas (SNG) has been reported. SNG or
Bio-methane (mixture of H2, CO2 and CH4) is tar free gas. Short residence time of 30 seconds to
2 minutes with complete transformation of the biomass organic material are benefits over
conventional thermochemical gasification of the biomass as described earlier in section (b) of
this chapter. Produced CO2 is dissolved in water and can be concentrated to be used for carbon
sequestration through agricultural and industrial processes.
Source: H. Schmieder et al. (2000)
Figure 3.22 – Schematic of a Hydrothermal Gasification plant
(g) Thermal Catalytic Cracking
Cracking is a thermal process that breaks the heavier and higher boiling-point
hydrocarbon fractions into lighter liquid hydrocarbons. The process provides a range of valuable
products such as petroleum gasoline, gas oils and fuel oil, which can be used in different
convenient ways. Two basic types of cracking processes, thermal cracking and catalytic
cracking, are in practice. Thermal cracking is a technique that uses high temperatures and
pressure to break down the hydrocarbons. Catalytic cracking use catalysts to crack the heavy
hydrocarbons into light molecules. The catalytic cracking of hydrocarbons is not restricted to a
single reaction. In fact, several reactions take place and result in to a variety of products with
different compositions.
(h) Torrefaction
Woody biomass feedstock suffers from some serious inherent drawbacks high levels of
moisture content and lower calorific value (low energy density) in comparison to the herbaceous
biomass. They are hygroscopic in nature and absorb moisture from atmosphere during storage.
They are difficult to pulverize and have serious problem of slagging due to presence of elements
like Si, Ca and K in them, resulting fouling of the furnaces, Also, they have high mass with wide
variations in important parameters related to combustion properties. These characteristics make
woody biomass economically less attractive due to high costs involved in their handling and
transportation. They are difficult to pulverize. All these problems are solved upto a large extent
by the process of torrefaction of woody biomass.
Torrefaction is a low temperature (250-300 °C) thermo-chemical process similar to the
roasting of biomass feedstock in absence of air or oxygen. The process occurs at atmospheric
pressure and the duration varies from 30-120 minutes. Predominant moisture in feedstock, during
the process, evaporates and generates steam. The hemicellulose and some other volatile organic
compounds in the biomass are decomposed and produce H2O, CO and CO2 gases after reaction
with this steam.
Source: M.J.C. van der Stelt et al. (2011)
Figure 3.23 - Schematic of wood torrefaction
Torrefaction is basically a form of mild pyrolysis (Maillard reactions) and a precursor to
many other biomass to fuel conversion processes. Torrefaction alone in general decreases energy
density but allows mechanical densification easier and thus results in increased volumetric
energy density. After torrefaction, due to proportional increase in the binding lignin content,
pelletizing of biomass becomes easier. It reduces transportation costs 40-50% in comparison to
raw biomass. Bio-coal is produced through densification (pelletisation and briquetting) of
torrefied biomass. Yields of 66-75% are reported and depend on the variety of the biomass
feedstock.
The resulting fuel is hydrophobic in nature and can be stored in open air without danger
of wetting by rain and rotting by biological decomposition. Another significant advantage is that
a variety of lignocellulosic biomass feedstock (mostly inedible woody biomass consisting of
cellulose, hemicellulose and lignin polymeric structures) can be converted into a homogenous
fuel compositions. Thus, the process enables the conversion of otherwise useless sources of
biomass like wood chips and a wide variety of forest residues into useful biofuels.
Lignocellulosic biomass conversion also reduces competition with edible or food crops.
Torrefied biomass can be utilized as feedstock to produce transportation liquid fuels by using
Fischer–Tropsch process. Finely ground torrefied wood powder can be compressed and used like
liquefied petroleum gas (LPG). Torrefied biomass fuels can easily be ground and mixed with
fossil fuels for co-firing in power plants. The co-firing of fuels results in the reduced levels of
emissions and helps in prevention of atmospheric pollution.
(i) Transesterification
Vegetable oil as fuel for using in internal combustion engines was demonstrated by Rudolf
Diesel (1858-1913) in 1900 in Paris. His idea was to substitute fossil fuels by biomass fuels and
so he invented ‘Diesel Engine’. He wanted the formers to use the fuel produced by them at
farms.
Source: en.wikipedia.org/wiki/Rudolf
Figure 3.24 – Prototype of Diesel Engine invented by Rudolf Diesel (inset) for using biomass
Rudolf_Diesel
of Diesel Engine invented by Rudolf Diesel (inset) for using biomass
based liquid fuels
of Diesel Engine invented by Rudolf Diesel (inset) for using biomass
Edible and non-edible vegetable oils including used/waste oils from food processing
industry are a very good source of valuable biomass based fuel. A variety of non-edible oil
species can be cultivated on marginal land to get large quantities of liquid fuel. Vegetable oils
are obtained by pressing and extraction technologies. They can be used as fuel in compression
ignition (CI) type internal combustion engines (ICE) to produce mechanical power for industrial
and transportation applications and electricity in distributed generation (DG) plants. Petroleum
diesel fuel is traditionally used in these types of engines and so they are termed as diesel engines.
However, due to their inherent natural chemical composition, vegetable oils can be used directly
in the conventional diesel engines only with certain modifications in the engine mechanism.
These modifications limit use of the vegetable oils in the conventional diesel engines as they
require money and engines can run on only one type of fuel at a time. This problem is solved by
converting vegetable oils into a fuel, having petroleum diesel like characteristics, the biodiesel.
Biodiesel, alone or blends with petroleum diesel can be used directly in diesel engines without
any modifications.
Transesterification is the chemical process used for converting vegetable oils into
biodiesel fuel. Vegetable oils are esters of glycol with three fatty acid chains (triglycerides) and
thus have higher viscosity than petroleum diesel fuel. Therefore, vegetable oil, after filtration, is
converted into an ester with single fatty acid chain by reacting with ethyl or methyl alcohols in
presence of catalyst. The monoesters obtained after conversion are termed as biodiesel having
the characteristics very similar to the characteristics of petroleum diesel fuel.
Vegetable oil → Biodiesel + Glycerin (3.4)
The added advantage is that use of biodiesel significantly lowers SO2 emissions in the
atmosphere and lowers air pollution levels. However, transesterification requires handling of
toxic and dangerous chemicals during the conversion process. Therefore, it is done only at large
scale production facilities and not locally at small scale level.
3.5.3 - Biological Conversion Techniques:
(1) Enzymatic Breakdown
The hydrolysis of lignocelluloses to glucose is an important step in the production
processes of cellulosic biofuel like ethanol from abundant cost effective biomass feedstock. In
nature, some types of microorganisms, especially fungi, have ability to decompose the plant cell
wall using some synergistically active enzymes. Work has been done to genetically improve the
microorganisms which can be utilized to degrade the biomass, efficiently by decomposition of
different cell wall constituents like polysaccharides and cellulose, hemicelluloses, pectin and
lignin (James G Elkins et al. 2010). For making the conversion process to be economically
viable, microorganism should possess suitable characteristics. Genetically engineered microbial
systems like bacteria and fungi can be used for direct and efficient conversion of lignocellulosic
biomass feedstock into valuable biofuels. Pre-treatment of biomass feedstock is done before
enzymatic hydrolysis for efficient and economical conversion of biomass into fuel (Seung-Hwan
Lee et al. 2010).
(2) Fermentation
The process of fermentation has been in practice for long time to produce wine, beer,
yogurt and several other products. However, the process can also be used to convert organic
waste materials into useful liquid and gas biofuels. The fuels, produced by using the process
helps in saving environment by reducing atmospheric GHG concentration and solving problem
of landfills for MSW disposal. Fermentation is the metabolic process in which a microorganism
(typically bacteria) converts a carbohydrate, such as starch or a sugar, into an alcohol. The
specific products resulting from the fermentation are decided by the type of microorganism
involved in the process. As an example, yeast (a fungus) performs fermentation to obtain energy
by converting sugar into alcohol. The chemical formula of the process is shown in equation 3.5.
C6H12O6 → 2 C2H5OH + 2 CO2 (3.5) Glucose Ethanol
Fermentation process is of two basic types as described below depending on the process
being performed in presence or absence of air or oxygen.
(i) Aerobic Fermentation
In the aerobic fermentation, glucose, in presence of oxygen, is converted into ethanol
(Merico et al. 2007). During the process, a microorganism in presence of controlled air or
oxygen converts lignocellulosic biomass feedstock by biological degradation into the important
biofuels. During its own growth the microorganisms utilize, part of the produced ethanol as
carbon and energy source, as part of their metabolism (Zhenguo Lin and Wen-Hsiung Li, 2010).
This process is also a precursor to the anaerobic fermentation for the larger scale fuel production
process. Aerobic fermentation or ‘primary fermentation’ is about 70% of the total fermentation
process, before anaerobic or ‘secondary fermentation’ as described in next section.
(ii) Anaerobic Fermentation
Anaerobic fermentation or digestion is biodegradation of biomass feedstock in near
absence of the air or oxygen by microorganisms. Anaerobic fermentation is used to produce
bioethanol as a substitute or for blending of gasoline fuel. Methane, a useful fuel for generating
heat and electricity, is produced by anaerobic fermentation of organic domestic and municipal
waste materials.
Typical chemical reaction, as shown in equation 3.6, in the process produces biogas
(carbon dioxide + methane) by the digestion of carbohydrates.
C6H10O5 + H2O → 3 (CO2 + CH4) (3.6) Carbohydrates Moisture Biogas
In anaerobic fermentation reaction, typically 30-60% of the solid organic feedstock is
converted into biogas. It is an environment friendly process using a wide range of organic
feedstock, both in solid and liquid forms including MSW and agricultural wastes, converted into
useful fuels by methanogenic bacteria. Anaerobic digestion provides means for potential energy
savings. This is also very stable process for converting medium to high strength organic
effluents into useful fuels.
Source: http://en.wikipedia.org/wiki/Biogas
Figure 3.25 - Block diagram of a typical household biogas plant
Schematic of a typical household biogas generation plant, as shown in figure x.x, is used
for converting waste material into methane rich biogas. Waste-to-Energy (WTE) power plants
are highly efficient in harnessing the untapped renewable energy potential of organic wastes.
They are based on anaerobic digestion of biomass and convert the biodegradable fraction of the
waste into high calorific gaseous fuels, which in turn are used to generate heat and electricity. In
addition to the wastewater treatment, the fuel produced by these biogas plants is used for
domestic and industrial heating and electricity generation.
A combination of one or more conversion techniques can be used for producing different
biofuels. This increases the overall efficiency. This is very advantageous from environmental and
economical and point of view also. Because reduced amounts of residue are generated. For
example, acetic acid is formed by the biological conversion of sugars, the non-lignin cellulosic
part of the biomass feedstock. Lignin, as shown in equation 3.7, is converted into hydrogen by
gasification, which can be used to convert acetic acid into ethanol by hydrogenation.
C6H12O6 + 6H2 → 3CH3CH2OH + 3H2O (3.7)
From from ethanol Cellulose lignin
Challenge are to develop the economically viable and environment friendly conversion
technologies, for producing biogasoline and green diesel from the lignocellulosic, algal biomass
feedstock including organic material from waste-water. The development of these fuels can help
in reducing the consumption of fossil fuels in transportation and electricity generation sectors.