Co-feeding of reduced poly-aromatics to the catalytic
pyrolysis of biomass: Improved yields of BioBTX
André Heeres, PhD
• BioBTX, Zernikelaan 17, 9747 AA Groningen, The Netherlands
• University of Groningen, Nijenborgh 4 9747 AG Groningen, The Netherlands
• Hanze University of Applied Sciences, Zernikeplein 7, 9747 AS Groningen
Content
• “Drivers for bio-aromatics”
• Catalytic pyrolysis towards aromatics/BTX
• H/Ceff ratio of feedstocks used in catalytic pyrolysis, influence on yield of BTX
• Valorization of the higher aromatic fraction (co-feeding)
• Downstream to polyesters
20
thCentury: The great acceleration
• Growth of population by a factor 3.7• Annual extraction growth
- construction materials a factor of 34 - ores and minerals by a factor of 27 - fossil fuels by a factor of 12
- biomass by a factor of 3.6
• Total material extraction grew by a factor of 8 • GHG emissions grew by a factor of 13
21
thCentury: Population
• Population growth (2050 – 9.7 billion)• Per capita consumption growth (up to 3 billion consumers moving from low to middle class consumption till 2030)
• Increased need materials
Plastics from biomass
• Sustainable Consumption and Production, utilization of natural resources: an attractive alternative?
• About 40% of plastics contain aromatics.
(Bio)aromatics: applications
Prices BTX strongly dependent on oil price (benzene $900/ton, toluene $800/ton, p-xylene $1050/ton (oil about $60 barrel))
7
Catalytic pyrolysis towards aromatics/BTX
In situ catalytic pyrolysis
• Efficient one-step process
• Sustainable, low carbon footprint
• Non food and cheap biomass
• Conventional zeolite catalysts
• Moderate yields of BTX (5-25%, depending on biomass/conditions)
• …….. but the “life time” of the catalyst??
Ex situ aromatization
• Extended life time of the catalyst
• Ability to use highly contaminated/wet biomass streams
• More “tools” for optimization
1. Thermal cracking 2. Catalytic conversion 3. Liquids collection
Ex situ catalytic pyrolysis Black Liquor
• Tandem Micro reactor (T1 = 500°C, T2 = 600°C)
André Heeres, Niels Schenk, Inouk Muizebelt, Ricardo Blees, Bart De Waele, Arend-Jan Zeeuw, Nathalie Meyer, Rob Carr, Erwin Wilbers, Hero Jan Heeres,
ACS Sustainable Chem. Eng., 2018, 6 (3), pp 3472–3480
Integrated Cascading Catalytic Pyrolysis (ICCP)
Hypothesis: A (cracking) catalyst could influence both the composition and amount of the gaseous phase.
Schenk, N.J., Biesbroek, A., Heeres, A., Heeres, H.J., Process for the preparation of aromatic compounds, WO2015047085
1. Thermal cracking 2. Catalytic conversion 3. Liquids collection
Significant effects “cracking” catalyst on yields BTX
High H/C
effincrease yields BTX
• Definition: H/Ceff = (H-2O)/C• Glucose, sorbitol, glycerol, tetrahydrofuran, methanol, several bio-oils (fixed bed, H-ZSM-5 catalyst)
H. Zhang, Y-T Cheng, T.P. Vispute, R. Xiao, G.W. Huber, Energy Environ. Sci, 2011, 2297.
• An example (glycerol, C3H8O3)
• H/Ceff= (8-2*3)/3 = 2/3 = 0,667
• Increasing H/Ceff results in higher BTX yields and lower coke yields.
Ex situ pyrolysis: product distribution
source BTX yield (%) bio-oil (%) ratio
glycerol 15.48 33.46 2.16 sucrose 3.82 13.71 3.59 cellulose 4.48 13.95 3.11 jatropha oil 23.71 53.34 2.25 lignin 2.14 12.19 5.70 wood 3.02 16.03 5.30 Gram scale unit, H-ZSM-5 (23), T = 550 ⁰C
S. He, I. Muizebelt, A. Heeres, N.J. Schenk, R. Blees, H.J. Heeres, Appl. Cat. B: Environmental, 2018, 45-55.
“Reduced polyaromatic hydrocarbons”
• Distillation (isolation BTX)
• (Partial) hydrogenation of higher aromatics obtained
“Reduced polyaromatic hydrocarbons”
• Utilization as a hydrogen rich additive in co-pyrolysis of biomass feedstocks.
• Additional formation of BTX from biomass.
•
%C = 88,45%, %H = 11,55%
•
“C
7,36H
11,55”
Co-feeding with biomass:
additional formation of BTX
• Ex situ pyrolysis of several biomass feedstocks co-fed with reduced PAH (i.e., PCA) at
1:1 wt. ratio using H-ZSM-5 zeolite