2.3 Lignocellulosic-based biofuels from synthesis gas
The book on Lignocellulosic-based biofuels from synthesis gas explores the conversion of lignocellulosic biomass into biofuels.
4. Bio-oil produced via pyrolysis
Bio-oil produced via pyrolysis
Pyrolysis is the chemical and physical separation of solid biomass into different molecules at high temperatures and in the absence of oxygen. Hemicelluloses, celluloses, and lignin in the biomass degrade at different temperatures, rates and by different pathways. Lignin is more termically stable and decomposes over a wider temperature range compared to cellulose and hemicellulose (Bridgewater et al. 1999). After decomposition of the chemical bonds the molecules recombine to new compounds. A part of the biomass is reduced to carbon, while other parts are oxidized and hydrolyzed to carbohydrates, alcohols, phenols, aldehydes, ketones, or carboxylic acids (Uddin 2018). The received products have different characteristics than the raw material. Pyrolysis produces three different fractions after cooling down the pyrolysis vapours:- Liquid phase (pyrolysis oil)
- Gasous phase (e.g hydrogen, methane, carbon monoxide, nitrogen)
- Solid phase (char)
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Types of pyrolysis
Two main process types of pyrolysis can be distinguished:Slow pyrolysis:
Slow pyrolysis takes place at around 400 to 500°C. Solids and vapour remain in the reactor for hours or days. Secondary reactions are promoted by the long residence times resulting in higher char contents and less bio-oil fractions. Already since centuries humans are using this process to produce charcoal (charcoal burning).edu sharing object
Fast pyrolysis:
Fast pyrolysis is used to produce liquid fuels and molecules for the chemical industry. Solids and vapor remain in the reactor only for some seconds at temperatures between 500 and 900°C. The high heating and heat transfer rates require finely ground biomass. Organic vapors, pyrolysis gases and charcoal are produced. After cooling and condensing the organic vapors bio-oil is received. The bio-oil share can be optimized to 60-70% when the fast pyrolysis takes place at around 500°C and with very short residence times (< 1 sec).Reactor designs
Different reactor designs are suitable for fast pyrolysis:Fluidized bed reactors
Fluidized bed reactors are a well-known technology, used on industrial scale but is also still further improved. They allow rapid heat transfer and distribution, have short vapor residence times and are easy to control. The fluidizing medium is sand. Bubbling fluidized bed and circulating fluidized bed reactors are available.edu sharing object
Rotating cone reactors
Rotating cone reactors provide a good contact between the bed material and the biomass with only little char formation. They enable good heat transfer through an internal rotating cone. So far there is no commercial application of a rotating cone reactor.edu sharing object
Ablative reactors
Here heat transfer works via the contact of the biomass to the hot wall of the reactor under pressure. Pyrolysis happens between the surface of the biomass and the reactor. The molten layer then vaporises and leaves the reactor in a gaseous state. It has to be cooled and condensated afterwards.
Here heat transfer works via the contact of the biomass to the hot wall of the reactor under pressure. Pyrolysis happens between the surface of the biomass and the reactor. The molten layer then vaporises and leaves the reactor in a gaseous state. It has to be cooled and condensated afterwards.
2.3.5.3 Pyrolysis bio-oil properties
Untreated
pyrolysis bio-oils consist of about 25% water, lignin fragments,
aldehyds, carboxylic acids, carbohydrates, phenols, fufural, alcohols
and kentones.
Due to its complex compositition they are not storable and not miscible with other fuels. Also, to use them as a motor fuel they have to be upgraded. Oxygen, nitrogen and sulfur have to be removed through hydrotreatment. Light fractions of the hydrotreated oil are distilled to remove butane and lighter components. The heavier fractions in the oil have to be sent to the hydrocracker to split them into gasoline and diesel components. In a last step gasoline, diesel and by-product gases have to be seperated by distillation.
Due to its complex compositition they are not storable and not miscible with other fuels. Also, to use them as a motor fuel they have to be upgraded. Oxygen, nitrogen and sulfur have to be removed through hydrotreatment. Light fractions of the hydrotreated oil are distilled to remove butane and lighter components. The heavier fractions in the oil have to be sent to the hydrocracker to split them into gasoline and diesel components. In a last step gasoline, diesel and by-product gases have to be seperated by distillation.
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There are several fast pyrolysis demonstration plants in operation, e.g. in The Netherlands (https://www.btgworld.com/en/rtd/technologies/fast-pyrolysis), UK, Spain, Canada, Germany (https://www.ikft.kit.edu/english/255.php), Finland, the U.S (https://bioenergy-concept.com/ablative-fast-pyrolysis/) and China (Uddin et al. 2018, Table 7).
Read more about pyrolysis technologies in general and fast pyrolysis in particular:
An Overview of Recent Developments in Biomass Pyrolysis Technologies: https://www.mdpi.com/1996-1073/11/11/3115/htm
Challenges and Opportunities in Fast Pyrolysis of Biomass: https://publications.aston.ac.uk/id/eprint/32132/
Lignocellulosic Biomass to Liquid Biofuels: https://publications.aston.ac.uk/id/eprint/32132/
Challenges and Opportunities in Fast Pyrolysis of Biomass: https://publications.aston.ac.uk/id/eprint/32132/
Lignocellulosic Biomass to Liquid Biofuels: https://publications.aston.ac.uk/id/eprint/32132/