Cleaner Fossil Fuel OPET
| WP4. | Promotion of the Low Temperature Carbonisation (LTC) Technology |
Summary
For sustainable and sound economic development there
is a strong demand for extended clean power production, which is affordable by
cost, utilising extended volumes of renewable biomass and continuously
increased waste streams as well, and also offering high level of process safety
with comprehensive long term management of residual process streams.
Among
various available technologies for clean energy production, the Low Temperature
Carbonisation (LTC) fuel pre-treatment technology is looking promising for
future project implementations. The Low Temperature Carbonisation (LTC)
technology is essentially a process for producing fuels – solid, liquid, and
gaseous – from coal and other carbonaceous material, such as biomass and organic
wastes. It is a value added technology, since it converts widely
available low-grade fuels to high-grade fuels, while removing hazardous air
pollutants, such as Sulphur, Chlorine and Mercury, which can be separately
treated or recycled. Thus, produced Clean Coal can be utilised in power
production, making LTC a complete and cost efficient revitalisation option. LTC
is a preventive environmental protection technology that may utilise available
domestic fuels and may contribute to compliance with environmental legislation
in energy production. It is therefore consistent with both demands of an energy
market operating under open market principles and sustainable environmental
protection.
In the framework of this work-package an overview of
Low Temperature Carbonisation (LTC) technology is attempted, including its
present status, properties, yields and utilisation of LTC chars, a survey of
competitive carbonisation methods, carbonisation conditions and their effect,
and short assessment of advantages, economic and technological development of
LTC.
Co-ordinator/partners
|
|
CENTRE
for RESEARCH and TECHNOLOGY HELLAS INSTITUTE
for SOLID FUELS TECHNOLOGY
and APPLICATIONS (CE.R.T.H. / I.S.F.T.A.) |
Objective
and Strategic Aspects
Socio-Economic Objectives
·
Improving
new employment prospects in the coal mining, coal utilisation and agricultural
industries, through utilisation of renewables and waste vegetable oils
·
Improved
boiler efficiecy, thus decreased cost for production of clean energy, resulting
in more affordable energy, which in turn supports the sustainable economic
development
·
Improving
the quality of life, health and safety, including working conditions
·
Improving
the use and development of skills in European dimension
·
Expanding
Trans-European cooperation between several countries
Contribution to EU Policies
·
Development
of this novel fuel preteratment technology may lead to the economic
exploitation of the coal/lignite and renewable biomass. This is directly
connected with the EU efforts to create new work positions and to open new
markets for clean energy for small and medium sized solid fuel power plants
·
Adoption
of the low temperature carbonisation technology fits well into the European
policies concerning the protection of the environment, as well as the
improvement of the quality of air, control and reuse of residuals, and offers
an improtant step toward full implementation of the Kyoto Protocol
·
Development
of a technology with good industrial export potential for the limitation of the
hazardous air pollutants in power generation. Implementations may promote the
application of the Clean Development Mechanism and allow developing countries
without reduction targets to benefit from emission reduction projects, while
developed countries may obtain emission reduction credits through such projects
Scientific/Technical Objectives and
Innovation
·
Delivering
a novel technology for the preventive pre-treatment and cleaning of coal and
renewable biomass streams, while utilizing waste vegetable oils
·
Reuse
of residuals and the opportunity to utilise wastes such as spent vegetable oils
in Europe, which are not yet sufficiently controlled for sewage treatment
exposure
·
Preventive
action for removal of multiple hazardous air pollutants and minimisation of
environmental impact through significant pollution abatement
·
Better
matching of the availability of the feed resource by offering the ability of
flexible multi-fuel application
·
Improvement
of boiler efficiency and reduction of operation and maintenance cost through
decreased boiler corrosion
Results – Deliverables
Studies/Reports
Overview of Low Temperature
Carbonisation
Present Status – Properties, Yields and
Utilisation of LTC chars – Survey of Various Methods – Pre-treatment Conditions
& Effects – Advantages, Economic & Technological Development
Prepared by CE.R.T.H./I.S.F.T.A.
Abstarct
Products from the various low
temperature processes vary in quantities and qualities depending on the coal
used and the nature of the treatments to which it has been exposed. The differences
can be of great significance in the selection of a process for a given
application, and careful study is necessary before a choice can be made.
Process descriptions have shown that many methods for the
low-temperature carbonisation of coal are available for use, and from them
chars with a wide variety of characteristics can be obtained. One desirable
characteristic of char is its smokeless quality. This property, together with
suitable form characteristics, has won for the lump char produced by certain
processes important places in the domestic fuel market in Great Britain and in
other European countries. The second product, also of major importance, has
been the large volume of tar. During 1920s there was a common expectation that
the values of these products, especially the chemicals to be derived from the
tar, plus possible economies in the carbonisation processes as compared to
high-temperature coke ovens, would lead to attractive profits from a low
temperature plant. Engineers and inventors have proposed a great amount of work
and innumerable designs. Of all the processes worked on during that period,
only one-the present Disco process - survived.
There are five necessary conditions to be met if a low-temperature
carbonisation process is to be rendered technically and economically feasible:
(1) Universal
applicability to different types of high-volatile coals
(2) Production
of a firm, abrasion –resistant product
(3) Maintenance
of desirable temperature conditions through the system to produce a uniform tar
(4) Maintenance
of an output which is economically attractive, a condition dependent on
rabidity of heat transfer and involving oven design and the thickness of the
coal bed
(5) Smooth,
trouble-free oven operation
The two processes in regular commercial use are the Disco process of the
Consolidation Coal company, this plant being located near Pittsburgh,
Pennsylvania, and the stoker carbonisation process, operated by Shawinigan
Chemicals Ltd. in Canada. In addition to these plants, the Parry process has
been operated experimentally on lignite by the Texas Power and Light Company at
the power installation for the Aluminum Company of America at Rockdale, Texas.
The Lurgi-Spulgas process also has operated in North Dakota for some time on
the local lignite. A process for producing a metallurgical formed coke from
Wyoming subbituminous coal was announced, and production of a low-temperature
char is one of the first steps. This plant is operated by Food Machinery and
Chemical Company and the United States Steel Corporation at Kemmerer, Wyoming.
In Europe, Japan, and other parts of the world, the Kruoo-Lurgi, Lurgi-spulgas
and Rochdale gas re-circulation appear to be most widely in use, but work is
proceeding at a number of locations on smaller-scale units of other carbonisation
methods.
Although many processes have been realised, they have been operated on different coals, in different ways, and for widely different objectives. Little correlation between them is available. Each process has often functioned on pretty much an experimental scale, without reaching the more critical stage of successful commercial practice. The engineer entering the low-temperature field finds it almost a virgin one, which encompasses first the selection of a process for a given need, then the design and engineering with the identification and definition of the problems to be faced, and finally plant operation and meeting the unexpected developments. For these reasons commercial evaluations of processes are still very difficult
Low temperature chars differ markedly from high-temperature cokes in appearance and properties. Generally, pieces of low temperature chars are black to dull grey, with an open, porous structure. They are softer, more friable, and weigh less than high-temperature coke. Both the apparent and true densities are lower. The volatile content of the char usually lies in the range from about 20% down to 9 or 10%. When heated, a char gives off much hydrogen, and the gas burns with an almost non-luminous flame. Because of the high volatile content and the open structure, char ignites readily and burns freely. These qualities make a lump char an ideal fuel for the open domestic grade. The quality of a charcoal can be represented by a great many other properties including charcoal yield, fixed-carbon content, moisture content, calorific value, elemental composition, hardness (abrasion resistance), compressive strength, bulk and true densities, surface area, porosity and pore volume distribution, electrical resistivity, and reactivity. The high reactivity of chars necessitates their thorough quenching or cooling unless they are to be used very shortly. In general, the properties of chars are greatly affected by the coals from which they have been produced and by the conditions to which they have been exposed during carbonisation. Commercial utilisation of low temperature chars includes domestic or industrial fuel, blast furnace fuel, reducing agent, electrodes and other uses.
Product distribution and how it is influenced by coal pyrolysis conditions have been studied. Lignite and bituminous coal are exhibiting quite different behaviour. Lignite products up to 700K are mainly water. Subsequently the evolution of CO2 and tar starts. At slightly higher temperatures CO, hydrocarbons and H2 are observed due to defunctionalisation. The hydrocarbons mainly consist of methane and ethylene. Based on char and gaseous products analyses, it is clear that the lignite char becomes relatively enriched in C, since even at the highest temperature only about 20% of the original carbon is lost. In the case of bituminous coal product distribution is dominated by tar. H2O is formed at relatively low temperature, below 700K. Carbon content profile is fundamentally different than that of lignite and it continuously decreases over the whole temperature range. Up to 50% of the originally present carbon is volatilised eventually. The hydrogen profile shows an analogous pattern that is in good agreement with the predominant evolution of tar. Apart from coal type, pyrolysis conditions that affect product distribution are the temperature, retention time, heating rate, pressure and particle size distribution.
Economic
and market prospects of LTC technologies are quite promising, since such fuel
pre-reatment technology fits into the European, North American and global
market developments, fulfils technical and cost efficiency demands, and meets
International Protocols and Agreements. Among key-points of LTC development is the
market tendency for expansion of small- and medium-sized power generation
plants. Traditional plants can easily be retrofitted by LTC add-on module,
whereas old plants can cost efficiently upgraded and still meet the new
environmental norms and regulations.
Potential LTC project development offers economical
benefits, such as decreased total cost of the end-product Clean Coal,
environmental control cost savings, increased profits due to efficiency
improvement, and reduced raw material cost, since domestic renewable sources
and agricultural wastes utilisation is feasible.
Major technical and scientific benefits of LTC
technologies employment include (a) preventive environmental protection, (b)
improved boiler efficiency, (c) total cost savings that may exceed 10%, (d)
reuse of industrial residuals, since flexible multi fuel operation is possible,
(e) enhancement of fuel diversity and security, (f) elimination of
environmental and health care risks, and (g) reduced boiler corrosion,
resulting in maintenance cost savings. One
of the major LTC advantages is fuel availability, since it offers potential
utilisation of alternative biomass and food industry wastes, whose disposal may
present today high cost and technical deficiency, such as (a) waste vegetable
oils (co-combustion), (b) non usable – non recyclable residuals from bio-diesel
production, (c) biomass residues, such as straw pellets and husk, (d) energy crops, such as short rotation wood and
sawdust, (e) biomass waste, i.e. demolition wood, and (f) meat meals
from animal by-product processing industry.
Among known
limitations that LTC technologies present are (a) reduced efficiency in
treatment of feed streams with very high moisture content and (b) removal of
all heavy metals from low grade fuels.
Development of R&D projects and future
implementations may be beneficial for most countries, including EU Members,
Accession Countries, East European and Asian Countries. In general, adoption of
LTC technologies offers significant advantages, among which are:
(6) It is a
preventive option that compared to “end-of-pipe” solutions results in:
a. Guaranteed and competitive long-term clean energy supply
b. Providing compatibility between development of open – liberalised energy
market and the objectives of the sustainable environmental protection
c. Providing overall cost savings for sustainable clean energy production
(7) Improved
overall safety and recycle-reuse of industrial material streams
(8) Flexible
feed choice application from regionally available feed supply by converting
trash (low grade fuels) into cash (clean energy)
(9) Improving
overall cost efficiency for sustainable green energy production
(10) Supporting schemes
for reduction of greenhouse gases as per Kyoto Protocol and European Commission
commitments
Articles
· Skodras, G. and Someus, Ed., “Clean Solid Fuels Production by Low Temperature Carbonisation for Sustainable Energy Generation”, submitted to Technika Chronika, Scientific Journal of the Greek Technical Chamber
·
Skodras,
G., Sofialidis, D., Faltsi, O, Skevis, G., Kaldis, S. and Sakellaropoulos, G.P.,
“Modelling Low Temperature Carbonisation of Solid Fuels in a Heated Rotary Kiln
for Clean Solid Fuel Production”, under preparation for submission to Fuel
·
Karlopoulos,
Ev., Skodras, G., Koukouzas, N. and Kakaras, E., “The Flexible
Mechanisms of Kyoto Protocol and the Implementation of a Potential Clean
Development Mechanism Project”, submitted to the Bulletin of the Hellenic
Association of Mechanical Engineers