Pyrolysis

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Technology
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Technology details
Name:
Category:
Feedstock: Garden Waste, wood, leaves
Product: Coal, pyrolysis oil, pyrolysis gas

Pyrolysis (from greek pyr, "fire" and lysis, "loosing/unbind") is a conversion technology that utilises a thermochemical process to convert organic compounds in presence of heat and absence of oxygen into valuable products which can be solid, liquid or gaseous. The chemical transformations of substances are generally accompanied by the breaking of chemical bonds which leads to the conversion of more complex molecules into simpler molecules which may also combine with each other to build up larger molecules again. The products of pyrolysis are usually not the actual building blocks of the decomposed substance, but are structurally modified (e.g. by cyclization and aromatisation or rearrangement).

Feedstock

Origin and composition

Since all kind of biowaste contains hydrocarbonaceous material it can also be processed via pyrolysis. However, the composition of the feedstock has an impact on the pyrolysis process and therewith on the products which can be obtained. Usually wood and herbaceous feedstocks are processed which are composed differently[1] which qualifies garden waste as suitable feedstock.

Typical composition of typical pyrolysis feedstocks[1]
Feedstock: Corn stover Switchgrass Wood
Proximate analysis wt [%]
Moisture 8.0 9.8 42.0
Ash 6.9 8.1 2.3
Volatile matter 69.7 69.1 47.8
Fixed carbon 15.4 12.9 7.9
Elemental analysis [%]
Carbon 49.7 50.7 51.5
Hydrogen 5.91 6.32 4.71
Oxygen 42.6 41.0 40.9
Nitrogen 0.97 0.83 1.06
Sulphur 0.11 0.21 0.12
Chlorine 0.28 0.22 0.02
Structural organics wt [%]
Cellulose 36.3 44.8 38.3
Hemicellulose 23.5 35.3 33.4
Lignin 17.5 11.9 25.2

Pre-treatment

The pre-treatment of the feedstock has an impact on the pyrolysis process, its efficiency, and the yield of certain products. The following pre-treatments may be considered [2]:

Process

The pyrolysis is an endothermal process which requires the input of energy in form of heat which can either be directly (direct pyrolysis) applied via hot gases or indirectly (indirect pyrolysis) via external heating of the reactor. Compared to gasification, the process takes place in an atmosphere without oxygen or at least under a limitation of oxygen.

In general, pyrolysis can be divided into different steps which includes:

  1. Evaporation and vapourisation of water and other volatile molecules which is induced at temperatures > 100 °C
  2. Thermal excitation and dissociation of the molecules induced at temperatures between 100-600 °C, which also may involve the production of free radicals as intermediate stage
  3. Reaction and recombination of the molecules, and triggering of chain reactions through free radicals

The pyrolysis process and the formation of products can be controlled to a certain extend via different temperature ranges and reaction times as well as by utilising reactive gases, liquids, catalysts, alternative forms of heat application (e.g. via microwaves or plasma), and a variety of reactor designs. Depending on the residence time and temperature as well as different technical reaction environments the pyrolysis can be categorised under diffferent terms as follows.

Categorisation according residence time and temperature

  • Fast pyrolysis
  • Intermediate pyrolysis
  • Slow pyrolysis (charring, torrefaction)

Categorisation according technical reaction environment

Depending on these factors the pyrolysis technology can be divided into different categories as follows:

  • Catalytic cracking
    • One-step process
    • Two-step process
  • Hydrocracking
  • Thermal cracking
  • Thermal depolymerisation?

Reactions

A range of different reactions occur during the process such as dehydration, depolymerisation, isomerisation, aromatisation, decarboxylation, and charring[2].

Product

A range of solid, liquid, and gaseous products can be obtained from the pyrolysis process including char, pyrolysis oil, and pyrolysis gas. Depending on the feedstock origin and composition as well as the pre-treatment and process the yield as well as the chemical and physical properties of the products can vary.

Char

Wood-based char

As mentioned the functional properties of char may vary which includes carbon content, functional groups, heating value, surface area, and pore-size distribution. The application possibilities are versatile, the char can be used as soil amendment for carbon sequestration, soil fertility improvement, and pollution remediation. Furthermore the char can be used for catalytic purposes, energy storage, or sorbent for pollutant removal from water or flue-gas.

Pyrolysis oil

Pyrolysis oil from corn stover pyrolysis

Produced pyrolysis oil is a multiphase emulsion composed of water and and hundrets of organic molecules such as acids, alcohols, ketones, furans, phenols, ethers, esters, sugars, aldehydes, alkenes, nitrogen- and oxygen- containing molecules. A longer storage or exposure to higher temperature increases the viscosity due to possible chemical reactions of the compounds in the oil which leads to the formation of larger molecules[3]. The presence of oligomeric species with a molecular weight >5000 decreases the stability of the oil[2], furthermore the formation of aerosols from volatile substances accelerates the aging process in which the water content and phase separation increases. The application as fuel in standard equipment for petroleum fuels (e.g. boilers, engines, turbines) may be limited due to poor volatility, high viscosity, coking, and corrosiveness of the oil[3]. To overcome these problems the pyrolysis oil has to be upgraded in a post-treatment to be used as fuel and/or the equipment for the end-application has to be adapted.

Pyrolysis gas

Syngas can be obtained from the pyrolysis gas which is composed of different gases such as carbon dioxide, carbon monoxide, hydrogen, methane, ethane, ethylene, propane, suphur oxides, nitrogen oxides, and ammonia[2]. The different gases can be fractionated from each other in the post-treatment to utilise them for different applications such as the production of chemicals, cosmetics, food, polymers or the utilisation as fuel or technical gas.

Post-treatment

Technology providers

BioBTX (ICCP technology)

Pyrolysis provider
General information
Company: Bio-BTX B.V. 21-04-27 Tech4Biowaste rect-p.png
Country:
Contact:
Webpage: https://biobtx.com/
Technology and process details
Technology name: Technology category: Conversion (Thermochemical processes and technologies)
TRL: 5-6 Capacity: 40 kg·h-1
Atmosphere: Inert Catalyst: Zeolite
Heating: Fluidised sand bed Pressure: 1-4 bar
Reactor: Fluidised sand bed, fixed bed Temperature: 450-650 °C
Other: Unknown
Feedstock and product details
Feedstock: Biomass (liquid, solid), wood pulp lignin residues, used cooking oil Product: Benzene, toluene, xylene, aromatics, light gases

BioBTX was founded in 2012 by KNN and Syncom, in collaboration with the university of Groningen, Netherlands. The company is a technology provider developing chemical recycling technologies for different feedstocks including non-food bio- and plastics waste. In 2018 a pilot plant with the capability to process biomass and plastic waste was set up at the Zernike Advanced Processing (ZAP) Facility. The company is now focused on setting up their first commercial plant with a capacity of 20,000 to 30,000 tonnes. The investing phase B was recently completed, with the last investment phase in 2019 the financial requirements are fulfilled to complete the commercialisation activities to build the plant which is expected for 2023.

The technology is based on an Integrated Cascading Catalytic Pyrolysis (ICCP) process, being able to produce aromatics including benzene, toluene, and xylene (BTX) as well as light olefins from low grade biomass and plastics waste. This technology utilises catalytic cracking in a two-step process at temperatures between 450- 850 °C. In the first step the feedstock material is vaporised via thermal cracking. The pyrolysis vapours are then directly passed into a second reactor in which they are converted into aromatics by utilising a zeolite catalyst which can be continuously regenerated. Finally, the products are separated from the gas via condensation. An ex situ approach of catalytic conversion has several advantages such as the protection of the catalyst from deactivation/degradation expanding its lifetime, a greater variety of feedstock, and a precise adjustment of process conditions (e.g. temperature, catalyst design, and Weight Hourly Space Velocity (WHSV) in each step for improved yields. In current pilot plant with 10 kg h-1 feed capacity for either waste plastics or biomass, final design details are established, which will be include in the running engineering activities for the commercial plant.

BTG Bioliquids

Pyrolysis technology provider
General information
Company: BTG Bioliquids Webpage: https://www.btg-bioliquids.com/
Location: The Netherlands Business-Model:
TRL: 8-9 Patent:
Technology: Rotating Cone Reactor Category: Fast pyrolysis
Feedstock: Woody biomass Product: Fast Pyrolysis Bio-Oil (FPBO)
Technology details
EMPYRO factory
The EMPYRO pyrolysis factory in Hengelo, the Netherlands.


BTG Bioliquids, a spin-off company from BTG Biomass Technology Group, was founded in 2007 in Enschede, the Netherlands. BTG Bioliquids aims for commercial implementation of their fast pyrolysis technology, which focuses on wood residues. Since 2015, the first successful production plant EMPYRO is in operation in Hengelo, the Netherlands, producing 24,000 tonnes pyrolysis oil per year. In 2018 EMPYRO was sold to Twence. Several new plants with Green Fuel Nordic in Finland and with Pyrocell in Sweden are announced, with currently one plant operational in Sweden.

Fortum (Combined Heat and Power plant, CHP; LignoCat?)

Fraunhofer UMSICHT (TCR-Process --> Susteen Technologies GmbH?)

Green Fuel Nordic

KIT (bioliq-Project)

Preem (Biozin; RenFuel)

Pyrocell

Statkraft (Silva Green Fuel)

VTT Technical Research Centre of Finland

Further providers

Pilots4U Database

Patents

References

Al Arni, S. 2018: Comparison of slow and fast pyrolysis for converting biomass into fuel. Renewable Energy, Vol. 124 197-201.  doi:https://doi.org/10.1016/j.renene.2017.04.060

Czajczyńska, D., Anguilano, L., Ghazal, H., Krzyżyńska, R., Reynolds, A. J., Spencer, N. and Jouhara, H. 2017: Potential of pyrolysis processes in the waste management sector. Thermal Science and Engineering Progress, Vol. 3 171-197.  doi:https://doi.org/10.1016/j.tsep.2017.06.003

Speight, J. 2019: Handbook of Industrial Hydrocarbon Processes. Gulf Professional Publishing, Oxford, United Kingdom.

Tan, H., Lee, C. T., Ong, P. Y., Wong, K. Y., Bong, C. P. C., Li, C. and Gao, Y. 2021: A Review On The Comparison Between Slow Pyrolysis And Fast Pyrolysis On The Quality Of Lignocellulosic And Lignin-Based Biochar. IOP Conference Series: Materials Science and Engineering, Vol. 1051  doi:10.1088/1757-899X/1051/1/012075

Waheed, Q. M. K., Nahil, M. A. and Williams, P. T. 2013: Pyrolysis of waste biomass: investigation of fast pyrolysis and slow pyrolysis process conditions on product yield and gas composition. Journal of the Energy Institute, Vol. 86 (4), 233-241.  doi:10.1179/1743967113Z.00000000067

Zaman, C. Z., Pal, K., Yehye, W. A., Sagadevan, S., Shah, S. T., Adebisi, G. A., Marliana, E., Rafique, R. F. and Johan, R. B. 2017: Pyrolysis: A Sustainable Way to Generate Energy from Waste. IntechOpen

  1. a b Carpenter, D., Westover, T. L., Czernik, S. and Jablonski, W., 2014: Biomass feedstocks for renewable fuel production: a review of the impacts of feedstock and pretreatment on the yield and product distribution of fast pyrolysis bio-oils and vapors. Green Chemistry, Vol. 16, (2), 384-406. doi: https://doi.org/10.1039/C3GC41631C
  2. a b c d Hu, X. and Gholizadeh, M., 2019: Biomass pyrolysis: A review of the process development and challenges from initial researches up to the commercialisation stage. Journal of Energy Chemistry, Vol. 39, 109-143. doi: https://doi.org/doi:https://doi.org/10.1016/j.jechem.2019.01.024
  3. a b Czernik, S. and Bridgwater, 2004: Overview of Applications of Biomass Fast Pyrolysis Oil. Energy & Fuels, Vol. 18, (2), 590-598. doi: https://doi.org/10.1021/ef034067u