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Pyrolysis: Difference between revisions
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Fast pyrolysis provides conditions to maximise the production of the liquid fraction of the products that are bio-oils (e.g. pyrolysis oil and biocrude). The primary goal is producing a renewable fuel intermediate in the pathway to finished hydrocarbon fuels from [[Biomass|biomass]] feedstock<ref>[https://www.sciencedirect.com/science/article/pii/B9780128182130000011 Pyrolysis of Biomass for Fuels and Chemicals]</ref>. The typical fast pyrolysis conditions are: moderate pyrolysis treatment temperatures (600-1000°C), rapid heating rates of biomass particles (>100°C/min), combined with short residence times of the biomass particles and pyrolysis vapours (0.5-2s) at high temperatures. Combination of medium pyrolysis temperature with short vapour residence time ensures high yield of good quality pyrolysis liquids while keeping the char and gas yields to a minimum. Due to the low thermal conductivity of [[Biomass|biomass]], small particle sizes are required to achieve the high heating rate needed<ref>[https://www.sciencedirect.com/science/article/pii/B9780081004555000217 Handbook of Biofuels Production]</ref>. Fluidised bed reactors are best suited for this type of pyrolysis due to offering high heating rates, rapid devolatilization and are easy to operate<ref name="ref1" />. | Fast pyrolysis provides conditions to maximise the production of the liquid fraction of the products that are bio-oils (e.g. pyrolysis oil and biocrude). The primary goal is producing a renewable fuel intermediate in the pathway to finished hydrocarbon fuels from [[Biomass|biomass]] feedstock<ref>[https://www.sciencedirect.com/science/article/pii/B9780128182130000011 Pyrolysis of Biomass for Fuels and Chemicals]</ref>. The typical fast pyrolysis conditions are: moderate pyrolysis treatment temperatures (600-1000°C), rapid heating rates of biomass particles (>100°C/min), combined with short residence times of the biomass particles and pyrolysis vapours (0.5-2s) at high temperatures. Combination of medium pyrolysis temperature with short vapour residence time ensures high yield of good quality pyrolysis liquids while keeping the char and gas yields to a minimum. Due to the low thermal conductivity of [[Biomass|biomass]], small particle sizes are required to achieve the high heating rate needed<ref>[https://www.sciencedirect.com/science/article/pii/B9780081004555000217 Handbook of Biofuels Production]</ref>. Fluidised bed reactors are best suited for this type of pyrolysis due to offering high heating rates, rapid devolatilization and are easy to operate<ref name="ref1" />. | ||
=== Flash === | === Flash === | ||
Flash pyrolysis (sometimes referred to as very fast pyrolysis) is characterised by rapid heating rates (>1000°C/s) and high reaction temperatures (900-1300°C), producing high yields of bio-oil with low resulting water content and conversion efficiencies of up to 70%. The residence time is shorter than fast pyrolysis at less than 0.5 seconds. The [[Biomass|biomass]] feedstock must go through vigorous pre-treatment to reduce particle size as much as possible (around 105-250 μm) which is required to achieve such high heating and heat transfer rates<ref>[https://www.sciencedirect.com/science/article/pii/B9780444538789000096 New and Future Developments in Catalysis]</ref>. Entrained flow or fluidised bed reactors are considered the best pyrolyzers for this purpose<ref name="ref1" />. | Flash pyrolysis (sometimes referred to as very fast pyrolysis) is characterised by rapid heating rates (>1000°C/s) and high reaction temperatures (900-1300°C), producing high yields of bio-oil with low resulting water content and conversion efficiencies of up to 70%. The residence time is shorter than fast pyrolysis at less than 0.5 seconds. The [[Biomass|biomass]] feedstock must go through vigorous pre-treatment to reduce particle size as much as possible (around 105-250 μm) which is required to achieve such high heating and heat transfer rates<ref>[https://www.sciencedirect.com/science/article/pii/B9780444538789000096 New and Future Developments in Catalysis]</ref>. Entrained flow or fluidised bed reactors are considered the best pyrolyzers for this purpose<ref name="ref1" />. | ||
== Pyrolysis Reactors == | |||
=== Fixed Bed Reactor === | |||
[[File:Schematic diagram of a fixed bed pyrolysis reactor.png|250px|right|Schematic diagram of a fixed bed pyrolysis reactor. All rights reserved.]] | |||
Fixed bed reactors were traditionally used to produce charcoal due to slow and poor heat transfer resulting in very low liquid charcoal yields. The technology is simple and reliable and utilises relatively uniform particle size. This type of gasifier is divided into downdraft and updraft. | |||
In a downdraft fixed bed reactor, the solid moves slowly down a vertical shaft and reacts with the air introduced at the throat that supports the gasifying feedstock. The solid and product gas move downward in a co-current mode which produces a relatively clean gas with low tar and high carbon conversion rate. In an updraft fixed bed reactor, the feedstock also moves down a vertical shaft but in a counter-current mode. This results in a dirty product gas with high levels of tars which can be alleviated using tar crackers. However, due to the feedstock not moving during the process, it is difficult to obtain heating of large quantities of feedstock material on an industrial scale. This could be solved if the reactor used methods that enable better heat transfer such as heat pipes. | |||
<ref>[https://www.sciencedirect.com/journal/thermal-science-and-engineering-progress/vol/3/suppl/C Potential of Pyrolysis Processes in the Waste Management Sector]</ref> | |||
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=== Fluidised Bed Reactor === | |||
Fluidised bed reactors are typically used for fast pyrolysis and are characterised by a high heating rate and small particle size. This type of reactor can be split into bubbling and circulating fluidised bed. | |||
==== Bubbling ==== | |||
[[File:Bubbling Fluidised Bed Reactor with an Electrostatic Precipitator.png|250px|right|Bubbling fluidised bed reactor with an electrostatic precipitator. All rights reserved.]] | |||
In bubbling fluidised beds, biomass particles are entered into a bed of hot sand fluidised by a recirculated product gas. The high heat transfer rates from the fluidised sand cause rapid heating of biomass particles and some ablation with the sand particles occurs. This type of reactor is characterised by good temperature control, limited turn down capacity and efficient heat transfer to biomass particles due to high solid density. <ref>[https://www.researchgate.net/publication/318678876_Review_of_Synthetic_Fuels_and_New_Materials_Production_Based_on_Pyrolysis_Technologies Review of Synthetic Fuels and New Materials Production Based on Pyrolysis Technologies]</ref> | |||
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==== Circulating ==== | |||
[[File:Circulating Fluidised Bed Reactor.png|250px|right|Circulating fluidised bed reactor. All rights reserved.]] | |||
In circulating fluidised beds, biomass particles are introduced into a circulating bed of hot sand. The recirculated product gas, sand and biomass move together in the reactor. The high heat transfer rates from the sand ensure rapid heating of the biomass and ablation is more prevalent than bubbling fluidised beds. This reactor is characterised by good temperature control and high heating rates. The residence time for the tar produced is around the same for the vapour and gas and can be separated by cyclone. | |||
<ref name="ref2">[https://www.researchgate.net/publication/330335978_Design_of_A_Fluidized_Bed_Reactor_For_Biomass_Pyrolysis Design of A Fluidized Bed Reactor For Biomass Pyrolysis]</ref> | |||
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==References== | ==References== | ||
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