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> Bio-oil applications
> Introduction
> Properties
> Application
> Chemicals from bio-oil
> Status of the technology
> Projects
> Reference
> Links
> Contact
> Introduction
Bio-oil can be used as a substitute for fossil fuels to generate
heat, power and / or chemicals. Short-term applications are boilers
and furnaces (including power stations), whereas turbines and
diesel engines may become available on the somewhat longer term.
Upgrading of the bio-oil to a transportation fuel is technically
feasible, but needs further development. Transportation fuels such
as methanol and Fischer-Tropsch fuels can be derived from the
bio-oil through synthesis gas processes. Furthermore, there is a
wide range of chemicals that can be extracted or derived from the
bio-oil.
> Properties
Representative values for the pyrolysis oil properties are
listed in the Table below. It is typically a liquid, almost black
through dark red-brown, depending on its chemical composition and
the presence of micro-carbon. The density of the liquid is about
1200 kg/m3, which is higher than of fuel oil, and
significantly higher than of the original biomass The viscosity of
the oil varies from as low as 25 cP up to 1000 cP depending on the
water content, the amount of light ends, and the extent to which
the oil has aged.
Due to large amounts of oxygenated components present, the oil
has a polar nature and does not mix readily with hydrocarbons. It
contains less nitrogen than petroleum products, and almost no metal
and sulphur components
The degradation products from the biomass constituents include
organic acids (like formic and acetic acid), giving the oil its low
pH of about 2 to almost 4. The oil attacks mild steel, and storage
of the oils should be in acid proof materials like stainless steel
or poly-olefins. Neutralisation of the oil is not an interesting
option as it can cause polymerisation.
Water is an integral part of the single-phase chemical solution.
The (hydrophilic) bio-oils have water contents of typically 15 - 35
wt.%, which can not be removed by conventional methods like
distillation. Phase separation may occur above certain water
contents. It is reported that this phase separation does not occur
until the moisture content increases above about 30 to 45 %.
Beneficial effects of the high water contents have also been
reported, viz. in case of combustion. It causes a decrease in
viscosity of the oil (facilitating transport, pumping and
atomisation), it improves the stability, it lowers the combustion
temperature and, as a consequence, it may cause a reduction of the
NOx emission.
The heating values: the higher heating value (HHV) is below 19
MJ/kg (compared to 42 - 44 MJ/kg for conventional fuel oils).
| The range of the elemental composition and of the properties
for a wood derived bio-oil. |
| |
Physical property |
pyrolysis conditions |
|
water content (wt.%)
|
|
15-30
|
Temperature (K)
|
770
|
|
pH
|
|
2.8-3.8
|
Gas residence time (s)
|
0.46
|
|
Density (kg/m3)
|
|
1110-1250
|
particle size (m)
|
590
|
|
Elemental analysis
|
|
|
moisture (wt.%)
|
3.3
|
|
(wt.% moisture free)
|
|
|
cellulose (wt.%)
|
49.1
|
| |
C
|
55.3-63.5
|
Ash (wt.%)
|
0.46
|
| |
H
|
5.2-7.0
|
|
|
| |
N
|
0.07-0.39
|
Yields (wt.%)
|
|
| |
S
|
0.00-0.05
|
Organic liquid
|
65.8
|
| |
O
|
Balance
|
Water
|
12.2
|
| |
Ash
|
0.03-0.30
|
Char
|
7.7
|
| |
|
|
Gas
|
10.8
|
|
HHV (MJ/kg)
|
|
16-19
|
|
|
| |
|
|
|
|
|
Viscosity (315 K, cP)
|
|
25-1000
|
|
|
| |
|
|
|
|
|
ASTM vacuum
|
|
|
Pour point (K)
|
250
|
|
distillation (wt.%)
|
430 K
|
10
|
|
|
| |
466 K
|
20
|
Solubility (wt.%)
|
Hexane
|
1
|
| |
492 K
|
40
|
|
Toluene
|
16
|
| |
distillate
|
50
|
|
Acetone
|
> 99
|
| |
|
|
|
acetic acid
|
> 99
|
> Application
Many different applications have been developed or under developent
for the use of bio-oil.
Heat Production
The heating value of bio-oil is
lower than for fossil fuel, and a significant portion of the
bio-oil consists of water. Nevertheless, flame combustion tests
showed that fast pyrolysis oils can replace heavy and light fuel
oils in industrial boiler applications. In its combustion
characteristics, the oil is more similar to light fuel oil,
although significant differences in ignition, viscosity, energy
content, stability, pH and emission levels are observed. Problems
identified in flame combustion of bio-oil are related to these
deviating characteristics, but these can be overcome in practice.
Bio-oil combustion in a boiler and / or furnace is shown to be the
most straightforward approach for use of bio-oil. Meanwhile,
bio-oil has been used commercially to co-fire a coal utility boiler
for power generation.
Electricity production
Several hundreds of hours has been achieved in the last years
on various diesel engines from laboratory test units to
large size modified dual fuel engines. Test results mention
positive results of engine performance in terms of smooth running.
Nevertheless some problems still need to be resolved to use bio-oil
to replace diesel, especially if the acidic nature of the oil (pH
3) and its tendency for soot formation and
re-polymerisation is considered. The use of a bio-oil requires
modification of various parts of the engine, amongst which the most
important ones are the fuel pump, the linings and the injection
system. Slight modifications of both the bio-oil and the diesel
engine can render bio-oils a quite acceptable substitute for diesel
fuel in stationary engines (CHP applications)
Experience with bio-oil combustion in gas turbines is
limited. R&D projects known are those carried out by a Canadian
company (Orenda), and Italian and German Research institutes. The
potential is high, but there are technical limitations such as the
fuel thermal stability, contaminants, and acidity.
Non-conventional atomisers are required to account for the special
properties of the oil. Ignition difficulties and significant
carbonaceous deposits of unburned material inside the combustion
chamber have been noticed. Nevertheless, commercially available gas
turbines are said to be available within several years.
Synthesis gas
For the production of "green" hydrocarbons, only
biomass can play a major role, because it is impossible to produce
these from the other renewable sources. A comparison between the
use of the solid biomass and the use of the liquid bio-oil as
feedstock for synthesis gas production encourages considering
gasification of bio-oil in large-scale syngas generation. In that
case a conventional entrained flow gasifier can be used, which is
proven technology. Apart from the scale-related considerations,
another problem of solid biomass gasification is that the
gasification conditions usually do not match properly with
synthesis gas requirements:
-
Direct biomass gasification is carried out at relatively low
temperatures with air or with steam / oxygen mixtures, to avoid ash
melting. The syngas produced therefore contains large amounts of
nitrogen (when air is used), and high "tar" and methane
concentrations. These "inert" compounds reduce the
selectivity and reactivity of catalysts applied in further
processing. Operation of a direct biomass gasification on pure
oxygen requires steam to decrease the gasification temperature.
- Pressurization of biomass is expensive, and biomass gasifiers
are yet developed for atmospheric conditions only. High-pressure
syngas processing requires expensive syngas compression to 60
bar.
-
The design of biomass gasifiers is different, due to the special
requirements for the biomass-solids handling
Gasification of bio-oil with pure oxygen and further processing
of the crude synthesis gas in Fischer-Tropsch processes may become
technical and economic feasible. Experimental tests are carried
out, gasifying bio-oil gasification with (enriched) air and pure
oxygen.
> Chemicals from bio-oil
Chemical components
More than 300 compounds have been identified as fragments of the basic
compounds of biomass, viz. the lignin (amongst others phenols,
eugenols and guaiacols), cellulose and hemi-cellulose derivatives
(sugars, acetaldehyde and formic acids). Large fractions of acetic
acid, acetol, and hydroxyacetaldehyde are reported in the analysis
results. Until now, only 40 to 50 % of the oil identity
(excluding the water) is revealed, but especially the large, less
severely cracked molecules are not yet identified. All types of
functional groups are present: acids, sugars, alcohols, ketones,
aldehydes, phenols and their derivatives, furanes and other mixed
oxygenates. Phenols are present in high concentrations (up to 50 wt.%).
The important chemicals identified in the oil are summarised in
Table below. Pre-treatment of wood can result in an increase of one
particular component at the expense of the other. In wood-derived
pyrolysis oil, specific oxygenated compounds are present in
relatively large amounts. Basically, the recovery of pure compounds
from the complex bio-oil is technically feasible but probably
economically unattractive because of the high costs for the
recovery of the chemical and its low concentration in the oil.
A large fraction of the oil is the phenolic fraction,
consisting of relatively small amounts of phenol, eugenol, cresols,
and xylenols, and much larger quantities of alkylated (poly-)
phenols (the so-called water insoluble pyrolytic lignin). It showed
good performance as adhesive for waterproof plywood.
Levoglucosan is a sugar derivative. Existing and potential
applications and markets for biomass-derived LG are due to the
possible self-polymerisation of LG, giving low molecular weight
oligo- or poly-saccharides. Another anhydrosugar identified in the
oil is the doubly dehydrated anhydrosugar Levoglucosenone..
Yields of LGS from cellulose can amount up to 24 wt.%. Another
sugar derivate, hydroxy-acetaldehyde can be present in
relatively large amounts in the bio-oil. It represents the smallest
sugar, and can be used for the browning of foods.
Components that can also be derived from bio-oil are
carboxylic acids. In the aqueous fraction of the bio-oil
these acids are present in small amounts. Finally, furfural and
furfurylalcohol are present in amounts up to 30 wt.% and 12 to 30
wt.%, respectively were produced.
Unfractionated bio-oil
The only commercial application of bio-oil is that of wood
flavour or liquid smoke. A number of companies produce these
liquids by adding water to the bio-oil. A red coloured product is
then obtained that can be used as such to brown and flavour
sausages, bacon, fish, etc.
The use of bio-oil or its water-soluble aldehyde fraction is
investigated for the replacement of formaldehyde in
urea-formaldehyde resins for particleboards. Due to the higher
cross-linking of the lignin derived compounds in the bio-oil, a
polymer with an improved strength can be obtained when mixed with
conventional urea-formaldehyde resins.
Pure bio-oil can be mixed with lime to form
BioLime . Injection of the mixture into flue-gas
tunnels results in almost complete removal of sulphur oxides and a
significant reduction of nitrogen oxides.
Reaction of bio-oil with ammonia, urea or other amino
compounds produces stable amides, amines, etc. They are non-toxic
to plants and can be used as slow release organic
fertilisers.
| Important chemicals identified in bio-oil. |
| Chemical |
concentration (wt.%) |
| Hydroxy-acetaldehyde |
up to 17 (from cellulose) |
| Levoglucosan |
up to 47 (from cellulose) |
| Levoglucosene |
up to 24 (from cellulose) |
| Phenolic compounds |
30-100 |
| Wood Preservatives |
|
| MethylArylether |
|
| Calcium Carboxylate salts |
|
| Furfural, Furfuryl alcohol |
up to 30 (from cellulose) |
| Steroids |
detected in vacuum pyrolysis oil |
| Nicotine/taxol precurors |
|
| Heavy metal recovery |
|
| polymeric carbon adsorbents |
|
| BioLime™ |
|
| Blended fuels |
|
| Slow release fertilizer |
|
> Status of technology
The current status of the processing of bio-oil is summarised in the Table
below. Indicated in bold are the most promising options on a short time scale.
|
The status of primary, secondary and tertiary
processing of bio-oil. Indices: 1=conceptual, 2=laboratory,
3=pilot, 4=demonstration and 5=commercial. Indicated in bold are
the most promising options on a short time scale.
|
| secondary processing |
secondary product |
tertiary processing |
final product |
| transport5 |
fuel |
combustion5 |
heat/steam/electricity |
| Boiler / furnace2 |
heat/steam |
steam turbine5 |
electricity |
| engine/turbine1 |
electricity |
|
|
| Stabilisation1 |
stabilised oil |
engine/turbine1 |
electricity |
| Upgrading2 |
hydrocarbons |
Refining5 |
diesel/gasoline |
| extraction1,5 |
chemicals |
refining1,5 |
chemicals |
| conversion5 |
chemicals |
refining1,2 |
chemicals |
| conversion2,3 |
(syn)gas2 |
fuel cell1 gas engine1 processing5 |
electricity electricity5 |
> Projects
- Diesel engine on bio-oil: a review
- Gasification of bio-oil for the production of green transportation fuels
- Toxicity and Health novem project
> Reference
- Venderbosch R.H., van Helden, 2001, Diesel engine on bio-oil: a review, SDE
- Venderbosch R.H., Vos J., Prins, 2000, Flash Pyrolysis
technologies for Biomass Usage in Small Decentralised Co-generation
Units, in: Proceedings van het Symposium Biomassa, Verbranden,
Vergassen, Vergisten, Pyrolyse (edited by W.L. Prins W.L. and J.
van Ham), Utrecht
- Venderbosch R.H., Wagenaar B.M., Gansekoele E., Sotirchos S.,
Moss H.D.T. 2000, Co-firing of bio-oil with simultaneous
SOx and NOx reduction. Paper presented at the
Conference on Thermochemical Biomass Conversion Technologies,
Tyrol, Austria, 17-22 September 2000
- Venderbosch R.H., Wagenaar B.M., Vos J., Prins W., 2001,
Combined Heat and Power (CHP) Production on basis of bio-oil
produced from agricultural waste streams, paper to be presented at
Sustain 2001, May 2001
- Van de Beld B., Venderbosch R.H., 2001, Production of
Transportation Fuels from Biomass, CTI-report (confidential)
- Prins W., Vos J., Venderbosch R.H., Wagenaar B.M., Van den Berg,
Van Haren P., 1998, Market Study for Applications of Flash
Pyrolysis Oil, EWAB Report 355297/6040
- >R.H. Venderbosch, B.M. Wagenaar, W. Prins, H.E.M. Stassen, 2002,
Hout-olie in bestaande ketels, NDEC hellip;..
> Links
Pyne
EET-pagina
> Contact
Dr. Ir. R.H. Venderbosch
Tel +31 53 486 2281
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