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Heat & electricity bio-energyAuthor(s): Evans, H.
Published: 2016
Publisher: ETI
Author(s): Pritchard, D.
Published: 2005
Publisher: Department of Trade and Industry
The aim of this project was to further develop micro turbine indirect firing and to develop this into a biomass generator, building on the success of the previous project. The system was redesigned and rebuilt using the experience gained and the recommendations reported in our last project. The efficiency, maintenance and safety of the system was improved through this development project.
The Specific aims were:
The main achievements of these projects are:
Author(s): The TESBiC consortium
Published: 2012
Publisher: ETI
Author(s): ETI
Published: 2012
Publisher: ETI
Author(s): ETI
Published: 2012
Publisher: ETI
Author(s): The TESBiC consortium
Published: 2011
Publisher: ETI
Author(s): The TESBiC consortium
Published: 2011
Publisher: ETI
Author(s): ETI
Published: 2012
Publisher: ETI
Author(s): The TESBiC consortium
Published: 2011
Publisher: ETI
Author(s): The TESBiC consortium
Published: 2012
Publisher: ETI
Author(s): Bhave, A. and Livingston, B.
Published: 2012
Publisher: ETI
Author(s): The TESBiC consortium
Published: 2012
Publisher: ETI
Author(s): The TESBiC consortium
Published: 2012
Publisher: ETI
Author(s): ETI
Published: 2010
Publisher: ETI
Author(s): Davis, CJ & Pinder, LW
Published: 2004
Publisher: Department of Trade and Industry
In order to examine the corrosive effects of co-firing biomass with coal in existing subcritical and possible future (ultra) supercritical boilers, typical and potential boiler tube alloys have been exposed to simulated furnace wall and superheater/reheater environments in the 1MWTH pulverised coal fired Combustion Test Facility (CTF) at Power Technology. A total of four CTF runs have been completed, each of which were nominally of 50 hours duration. Up to 15 furnace wall and 16 superheater/reheater steel alloy specimens were exposed to a range of metal temperatures, with differing heat fluxes and gaseous environments, representative of pulverised coal combustion under low NOx conditions with biomass additions. The biomass fuels were co-fired with Daw Mill coal, furnace wall corrosion specimens having previously been tested without biomass additions in this environment, providing base line corrosion data for comparison. Numerous previous tests with coals provided baseline data for superheater/reheater corrosion rates. Biomass was fired at both 20% and 10% on a thermal basis, representing proportions significantly above and close to the maximum proportions expected to be utilised in actual plant, enabling examination of concentration effects. The specimens were exposed to the combustion environment on air-cooled, precision metrology, corrosion probes.
When co-firing with wood at both 20% and 10% on a thermal basis, there was no discernable worsening of either furnace wall or superheater/reheater corrosion when compared with firing coal alone. Whilst there was no comparable data for TP316 austenitic stainless steel superheater/reheater specimens, the measured corrosion rates were substantially reduced when compared to the ferritic T22 specimens exposed at the same location.
This report is divided into the following sections:Author(s): Newton-Cross, G. and Evans, H.
Published: 2015
Publisher: ETI
Author(s): DTI
Published: 2005
Publisher: Department of Trade and Industry
The objectives of this project were:
Typical and potential boiler tube alloys have been exposed to simulated furnace wall and superheater/reheater environments in the 1MWTh Combustion Test Facility (CTF) at Power Technology.
A total of four nominally 50 hour duration exposures have been completed. Specimens were exposed to a range of metal temperatures, heat fluxes and gaseous environments, representative of pulverised coal combustion under low NOx conditions with biomass additions. Biomass was co-fired with Daw Mill coal on 20% and 10% thermal or heat input basis (approx 35% and 17% by mass). Specimens were exposed to the combustion environment on air-cooled, precision metrology, corrosion probes.
This summary provides information on:Author(s): DTI
Published: 2005
Publisher: Department of Trade and Industry
The project aims to provide boiler operators with greater confidence in using higher levels of biofuel replacement (50% thermal or more). The specific objectives of the project are:
The increased use of biomass, a fuel that is seen as largely CO2 neutral, in power generation is one of the few ways in which the power industry could make a significant step to reducing CO2 emissions. Co-fired boiler trials have been encouraging and have shown that small amounts of coal can be replaced by biofuels without undue impact on boiler performance. However, in order to make a real impact towards reaching Government targets, the amount of biomass for co-combustion would have to be greatly increased.
This profile provides information on:Author(s): Robson, D.
Published: 2009
Publisher: Joule Centre
This document is a summary for the project titled 'Optimising the location of bioenergy sources: where should we grow bioenergy crops?'.
In order for the UK to meet its ambitious targets for energy production from renewable sources (10% of electricity by 2010, 15% by 2020) it needs to expand its capacity to generate all forms of renewable energy and marine energy is a big part of this. These internationally agreed targets are born out of the need to reduce CO2 emissions, to minimize the impacts of climate change, and to come up with a renewable alternative to dwindling fossil fuel supplies. Generating energy from biomass, which is biological material derived from living or recently living organisms, is a solution which meets both these objectives. The term biomass can apply to both animal and vegetable derived materials but this project is focused on the growth of high yield crops. These crops can then be converted into energy using one of the numerous forms of either thermal or chemical conversion technologies. Biomass is low carbon, the crops take carbon out of the air as they grow, and can be re-grown relatively quickly.
This project has two main objectives: to gauge the willingness of land-owners to plant bioenergy / biomass crops and to develop a GIS (Geographical Information System) enabled 'land use potential and stakeholder analysis' for bioenergy in Cumbria. GIS is a computer system for capturing, storing, checking, integrating, manipulating, analysing and displaying data related to geographic position. The GIS enabled 'land use potential and stakeholder analysis' will take the form of a pilot study for this project and extended later on. The willingness of land owners to grow bioenergy / biomass crops will be gauged by conducting semi-structured interviews or group meetings with stakeholders and experts, looking at existing research and developing a best practice for biomass crop management in partnership with land owners.
Author(s): Biomass Engineering Ltd
Published: 2006
Publisher: Department of Trade and Industry
Biomass Engineering Ltd. have demonstrated that their downdraft gasification technology is capable of producing very low tar levels in the producer gas, as independently measured, and have four gasifiers in operation. Developments in the gasifier configuration have led to a very low tar gas, allowing a simplified hot has filtration system to be used. Recent independent analysis of the "tars" from the Mossborough Hall farm gasifier at Rainford, NW England has shown that over 80wt% of the condensable organics in the gas are benzene, toluene, xylene and naphthalene and that problematic tar components in the gas were less than 20 mg/Nm3 under prolonged operation. The gasification technology of Biomass Engineering Ltd. is therefore close to a warrantable commercial reality.
Biomass Engineering Limited has succeeded in developing a downdraft gasifier capable of producing a very low tar, low particulate gas of consistent high calorific value (> 5 MJ/Nm3 for wood feedstocks). However, with the development of a technology capable of handling a well-defined wood, there is a requirement to assess the possibility of using other non-standard fuels, especially as these are more readily available in some locations and where other disposal and transportation options are not economical. To this end this work was concerned with testing a variety of fuels in an existing 80 kg/h (80 kWe) gasification system and measuring a range of process emissions and assess whether they could possibly be used in a downdraft gasifier for gas production for use in a boiler or engine. The fuels used were: dried papermill sludge (briquetted), Dried leather wastes (briquetted), palletwood wastes (and some demolition wood), medium density fibreboard (MDF), panel board (and other chipped pallets), pine/bark mixed waste strippings and renewable biomass fuel (RBF) produced form the organic fraction of MSW.
The Biomass Engineering Ltd. technology is a throated downdraft gasifier and it can be operated using different gas cleaning systems, including cyclones for dust removal, hot gas filter for very high dust capture efficiencies (>99wt%) on low tar gases and a wet scrubbing system for contaminated (volatile metals) and high tar gases. Wastes with high ash contents are more prone to high levels of tar formation. Tests of over 60 hours on each fuel were carried out, except for the RBF, of which there was only a limited quantity and of highly variable quality, which caused various processing difficulties.
Tests on the fuels showed that the high ash feedstocks (>15wt%, RBF and papermill sludge) were problematical in gasifier operation and not unexpectedly gave a producer gas with low heating values in the range of 1-3 MJ/Nm3. The buffings dust, pine/bark mix and the palletwood could be satisfactorily gasified to give a has with a good lower heating value of 4-5 MJ/Nm3. This is the expected value for low ash feedstocks and low tar levels in the gas. Extensive analyses of the feedstocks, the by-products chars and ashes, the producer gas and some of the condensates were made. The RBF fuel was prone to clinker formation on the grate possibly by the formation of low melting eutectic of SiO2 and CaO (or a derivative). The chars exhibited high carbon conversions of typically over 85wt%.
This report contains an executive summary, and is divided into the following sections:Author(s): Evans, H., Thirkill, A. and Hussain, B.
Published: 2018
Publisher: ETI
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