• What data is available from the Research Report – Operational Problems, Trace Emissions and By-Product Management for Industrial Biomass Co-Combustion?

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      espadmin

1. Sources

The present Combustion File is part of the cluster of CFs produced within the literature survey phase of the industrial sponsored research and development project PowerFlam1 and is confidential to the participants registered for that project.

This CF is specifically concerned with the research project:

Spliethoff, H., Hein, K.R.G., Hendriksen, N., Skrifvars, B. and Dugwell, D. (1999): Operational Problems, Trace Emissions and By-Product Management for Industrial Biomass Co-Combustion, which is published within 4th International Conference on Technologies and Combustion for a Clean Environment, 5-9 July, Lisboa, Portugal.

2. Background

·         This combustion file is concerned with the provision of combustion related data to the sponsors.

·         In this html file the source of the data is summarised in section 4 below, in order to give the reader a general overview of the way the experiment was carried out.

·         The research project in which this CF is based, does not present fuel and related data, therefore, they are not presented in individual Microsoft Excel Worksheets.

·         All credits and sources, and where necessary, instructions/advice for data use, are presented in this html file.

3. Abstract

In comparison to other renewable energy sources, thermal utilisation of biomass or waste is a cheap and technically feasible option to contribute to reducing the net CO2 emissions. Co-combustion of biomass or waste together with coal in existing large-scale firing systems offers several advantages, e.g. the possibility to utilise a large quantity of biomass or lower investment costs compared with systems exclusively fired with biomass. Utilisation of biomass or wastes, however, may have consequences on combustion behaviour, emissions, corrosion, and residual matter.

Based on the experience of the APAS programme, the objective of this project was to concentrate the research effort on the problem areas like slagging, fouling, corrosion, ash utilisation and trace emissions for different co-combustion systems and carefully investigate technical options to avoid these negative effects. The solution of these technical problems is essential for a technically and economically feasible and environmentally advantageous co-combustion and will promote a widespread utilisation of existing biomass resources.

Based on the work of the different partners, the final goal was to compare the different methods of co-combustion (PF, FB, pre-treatment) with regard to technical, economical, and environmental issues.

The objectives of the project have been in detail:

          to find out the optimum co-combustion technique with regard to operation, by-product management and trace emissions,

          to point out measures for eliminating operational problems and reducing environmental impacts or to show the restrictions of co-combustion in dependence on the biomass fuel,

          to promote utilisation of by-products from co-combustion¨,

          to evaluate the effect of co-combustion on trace emissions,

          to demonstrate the technical and economical feasibility of biomass co-combustion,

          to techno-economically compare direct co-combustion and pre-treatment by pyrolysis and gasification.

 

The article is also available in German language, see Source.

4. Synopsis

Style:

Experimental

Original report

Scale: laboratory – [industrial

Semi-industrial]

Semi-industrial

 

 

 

 

 

 

 

 

 

 

 

 

full scale

500kW thermal power coal dust combustion facility (IVD)

400kW thermal power coal dust combustion facility (IVD)

150kW thermal power coal dust combustion facility (ICME)

100kW thermal power FBC (NTUA)

1MW thermal power FBC (Cerchar)

2.5MW thermal power FBC (TPS)

50kW thermal power BFB (TPS)

200MW thermal power BFB (TPS)

5MW thermal power PF/LCV-gas (TPS)

2MW CFB gasifier (TPS)

50kW thermal flow pyr./gas. (IVD)

50kW thermal comb. (IVD)

30kW slag tap furnace

100MW thermal PFC (SEAB)

80MW thermal CFB (Elsam)

30MW thermal CFB (VAB)

100MW thermal BFB (VAB)

43MW thermal CFB (CRE)

Data on combustor

Schematic fig.

0.3MW slag tap furnace (IVD)

Company/Institute

Consortium (IVD, ICME, NTUA, Cerchar, TPS, SEAB, Elsam, VAB, CRE

Combustion type

Co-firing

Pulverised fuel combustion PFC

Fluidised bed combustion FBC (bubbling BFB, circulating CFB)

Pre-treatment facilities

Slagging combustor

Main fuel

Coal, oil

Substitute fuel

Wood, wood pulp, bark, straw, wood matter from pressed olive stones, sewage sludge

Fuel data

None

Experiments

Extensive experiments in various units

Results

Describing/solving problems: slagging, fouling, corrosion, ash utilization, trace organic compounds emissions (dioxins, furans, PCBs, VOCs), impact of biomass co-combustion

Comments

International co-operation 3-year Joule III programme of the EU: “Operation Problems, Trace emissions and By-Product Management for Industrial Biomass Co-combustion

Overview the project facilities, topics, Results

Good summary of biomass co-combustion in FBC, PFC, pretreatment facilities

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