Post on 09-Feb-2022
transcript
Advanced Biorefinery Concepts Towards Certified Jet Fuel
Sandra Adelung, Ralph-Uwe Dietrich, Stefan Estelmann, Simon Maier,
Julia Weyand
ABC-Salt Summer School 2019
Birmingham, 14.08.2019
DLR.de • Chart 1 R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019
SUMMER SCHOOL 2019ABC-Salt project has received funding from the EU’s Horizon 2020
research and innovation Programme under Grant Agreement No 764089
SUMMER SCHOOL 2019
Agenda
A. Introduction
B. Biomass-to-Liquid: Routes and Unit Operations
→ Feedstock, conversion and conditioning, synthesis, refining
C. Methodology for assessing different routes
→ Technical, economic, ecologic
D. Take-home-messages
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 2
SUMMER SCHOOL 2019
Definition: Biorefinery
IEA Bioenergy Task 42:
“Biorefinery is the sustainable processing of biomass into a spectrum of
marketable products and energy. “
→ Biorefineries can be facilities, processes, plants or cluster of facilities
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 3
Biomass Biorefinery
Fuels
Chemicals
Power
Heat
…
Biorefinery
SUMMER SCHOOL 2019
Biorefineries- Classification (IEA Bioenergy Task 42)
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 4
Feedstocks
Energy cropsStarch crops, oil crops, sugar crops, …
Biomass residuesStraw, bark, cooking oils, …
Products
EnergyBio-ethanol, biodiesel, FT-fuels, …
ProductsChemicals, materials, …
Platforms / Intermediates
C5/C6, sugars, syngas, biogas, …
Conversion processes
Biochemical(fermentation, enzymatic conv., …)
Thermochemical(gasification, pyrolysis, …)
Chemical(acidic hydrolysis, esterification, …)
Mechanical(fractionation, milling, …)
Multiple process routes
possible
SUMMER SCHOOL 2019
Biomass-to-Fuels
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 5
SUMMER SCHOOL 2019DLR.de • Chart 6DLR.de • Chart 6
EU 28 bioenergy potential[1]
DLR.de • Chart 6 R.-U. Dietrich • Biorefineries concepts and design • ABC-Salt Summer School • 14.08.2019
Feedstock Biomass category Biomass type PJ (2020)
Agriculture
Energy crops1 Sugar, oil crops, starchy crops, lignocellulosic biomass, energy maize
3,184
Agricultural residues
Dry & liquid manure, straw, olive pits 2,312
Forestry
Stem wood production
Stem wood, woodchips 2,096
Forestry residuesLogging residues, landscape care, woodchips, saw dust, black liquor
3,166
Waste Residues Public greens, solid waste, sewage sludge 454
[1] Pablo Ruiz et al.. (2015): „The JRC-EU-TIMES model. Bioenergy potentials for EU and neighbouring countries.”, JRC Science for policy report
[2] Carolina Perpiña Castillo et al. (2015): An assessment of dedicated energy crops in Europe under the EU Energy Reference Scenario 2013, JRC Science for policy report
1Land use of energy crops in 2020: 4,733 kha (1.3 % of total available land , ~2.4 % of agricultural land)[2]
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019
SUMMER SCHOOL 2019
EU 28 bioenergy potential-2010[1] – regional distribution
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 7
[1] Pablo Ruiz et al.. (2015): „The JRC-EU-TIMES model. Bioenergy potentials for EU and neighbouring countries.”, JRC Science for policy report
Highest potential:
France, Germany,
Spain, Poland,
Sweden, Italy,
Romania
SUMMER SCHOOL 2019
Certified alternative jet fuels (ASTM D7566 – 14c [1])
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 8
Feedstock Synthesis technology Fuel
Coal, natural gas, biomass, CO2 & H2 Fischer-Tropsch (FT) synthesis Synthetic paraffinic kerosene
(SPK)
Lipids from Biomass (e.g. algae, soya, jatropha) Hydroprocessed esters and fatty acids (HEFA) Synthetic paraffinic kerosene
Sugar from Biomass Direct Sugars to Hydrocarbons (DSHC) Synthetic iso-paraffins /
Farnesane
Bioethanol (-propanol, -butanol) dehydration+oligomerization+hydration
(Alcohol-to-Jet, AtJ)
AD-SPK
[1] ASTM International, „ASTM D7566 - 14C: Standard Specification for Aviation Turbine Fuel Containing Synthesized Hydrocarbons“, 2015
[2] Dietrich et al., “Challenges & opportunities for sustainable aviation”, 13th Concawe Symposium - Low Carbon Pathways and Refining Technologies, March 2019, Antwerp
European crop based kerosene? – from rapeseed & soya / sugar beet / wheat
All European rapeseed & soya to HEFA: 14.7 Mt/a (≈ 26 % of aviation demand) [2]
All European sugar beet to DSHC: 3.4 Mt/a (≈ 6 % of demand) [2]
All European wheat to AtJ: 31.9 Mt/a (≈ 56 % of demand) [2]
SUMMER SCHOOL 2019
Certified alternative jet fuels (ASTM D7566 – 14c [1])
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 9
Feedstock Synthesis technology Fuel
Coal, natural gas, biomass, CO2 & H2 Fischer-Tropsch (FT) synthesis Synthetic paraffinic kerosene
(SPK)
Lipids from Biomass (e.g. algae, soya, jatropha) Hydroprocessed esters and fatty acids (HEFA) Synthetic paraffinic kerosene
Sugar from Biomass Direct Sugars to Hydrocarbons (DSHC) Synthetic iso-paraffins /
Farnesane
Bioethanol (-propanol, -butanol) dehydration+oligomerization+hydration
(Alcohol-to-Jet, AtJ)
AD-SPK
[1] ASTM International, „ASTM D7566 - 14C: Standard Specification for Aviation Turbine Fuel Containing Synthesized Hydrocarbons“, 2015
[2] Pablo Ruiz, „The JRC-EU-TIMES model. Bioenergy potentials for EU and neighbouring countries”, Table 38-43, 2015
[3] Albrecht, “A standardized methodology for the techno-economic evaluation of alternaitve fuels – a case study”, 2016
European BtL Fischer-Tropsch kerosene? – from forestry and municipal waste:
Forest residues, municipal waste potential [2]: ≈ 8 EJLHV/a
Conversion to fuel[ 3]: 0.363 PLHV,Kerosene/PLHV,Biomass
European kerosene production based on BtL: 68.4 Mt/a (121 % of aviation demand)
SUMMER SCHOOL 2019
Biomass-to-Fuels
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 10
SUMMER SCHOOL 2019
Gasification - Types
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 11
Moving bed Fluidized bed Entrained flow
Fuel feeding Dry Dry Dry/Slurry
Typical process Lurgi, BGL Winkler, HTW, HRL, CFB, KBR, KRW, U-Gas
KT, Shell, Siemens, EAGLE, GEE, E-Gas, ICCT OMB
Fuel size limits 5 – 80 mm < 6 mm < 0.1 mm
Oper. Temperature ~ 1000 °C 800 – 1100 °C > 1200 °C
Oper. Pressure > 20 bar 1 – 35 bar 1 – 85 bar
Oxidant demand Low Moderate High
Product gas temperature 400 – 650 °C 900 – 1050 °C 1250 – 1600 °C
SUMMER SCHOOL 2019
Pyrolysis- Products[1]
Different operating conditions:
• Residence time
• Temperature
• Heating rate
→ varying product compositions
→ post-processing varies
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 13
[1] John A. Dutton e-Education Institute: “Alternative Fuels from Biomass sources”, https://www.e-education.psu.edu/egee439/node/537
SUMMER SCHOOL 2019
Pyrolysis- Products[1]
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 14
[1] John A. Dutton e-Education Institute: “Alternative Fuels from Biomass sources”, https://www.e-education.psu.edu/egee439/node/537
• Consists of about 400 types of organic
compounds (Acids, Esters, Alcohols,
Ketones, Aldehydes, Phenols,
Alkenes, Aromatics, …)
-> high value components?
• Immiscible with transportation fuels
but emulsifying with Diesel possible
-> special surfactants
• Water content emulsified
-> separation problem
ABC-Salt
Approach
– Bio-Oil properties
SUMMER SCHOOL 2019
Pre-Treatment and hydrolysis
Pre-Treatment possibilities
• Milling
• Drying
• Acidic
• Alkaline
• Solvents
• Oxidants
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 16
Pre-treatment
(Physical, thermo-chemical)
Enzymatic Hydrolysis Acidic Hydrolysis
Sugars
Biomass
SUMMER SCHOOL 2019
Biomass-to-Fuels
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 17
SUMMER SCHOOL 2019
Synthesis from Syngas
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 18
Fischer-Tropsch MeOH EtOH
ProductMostly alkanes or alkenes
(product distribution α = 0.75-0.95)Methanol
Ethanol and higher
alcohols
TemperatureLTFT (190 – 250°C)
HTFT (300 – 350°C)200-300 °C 200-300 °C
Pressure 25-40 bar 40-150 bar 40-100 bar
Reactor
typesSlurry, Fixed-bed, micro-channel Fixed-bed Fixed-bed
Feed H2/CO = 2.0-2.2 H2/(2CO + 3CO2) = 1.05 H2/CO = 0.45-2.33
TRL 8-9 8-9 1-3
SUMMER SCHOOL 2019
Synthesis from Sugars
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 19
Fermentation Aqueous phase reforming
Product EthanolFarnesane
(kerosene blend)Alkanes, alkenes and oxygenates
Temperature 32 - 34 °C 180 – 370 °C
Pressure Ambient 10 - 90 bar
Environment Anaerobic Aerobic -
Feed Mono-saccharidesPolyhydric alcohols,
short-chain oxygenates
SUMMER SCHOOL 2019
Biomass-to-Fuels
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 20
SUMMER SCHOOL 2019
Refining unit operations
• Hydrocracking
• Decrease chain length
• Dehydrogenation/Hydrogenation
• Remove/add hydrogen from molecules →
increase alkene/alkane content
• Dehydration/ Hydration
• Decrease/increase alcohol content
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 21
+H2
→ 2
⇌+H2
-H2
OH+ H2O
+H2
-H2
⇌
SUMMER SCHOOL 2019
Refining unit operations – cont.
• Alkylation
• Merge aliphatic HCs/aromatics with alkenes
(increase octane number, RON)
• Oligomerization
• Increase chain length of alkenes
(increase boiling point, energy density)
• Isomerization (alkenes)/ Hydroisomerization (alkanes)
• Increase number of branches, RON
• De-/Aromatization
• De-/Increase number of aromatics
(Reduce soot formation / increase RON)
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 22
+ →
⇌
2 ⇌
⇌-H2
+H2
SUMMER SCHOOL 2019
Refining design objectives and design hierarchy
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 23
Feed Characterization
Product specification
Conversion processes
Separation processes
Heat integration
Utilities
• Primary Design Objectives
• Refinery type
• Products and markets
• Feed selection
• Location
• Secondary Design Objectives
• NPC ↓
• CAPEX ↓
• Efficicency ↑
• Environmental footprint ↓
• Flexibility ↑
• Complexity ↓
• …
SUMMER SCHOOL 2019
Biomass-to-Fuels
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 24
SUMMER SCHOOL 2019
Transportation fuels specifications - Gasoline and Diesel
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 25
RON
MON
AromaticsOlefines
SulfurBoiling Point
Vapour pressureDensity
C5+ ethers
C3+ alcohols
EthanolMethanol
Benzene
Cetane number
Flash point
Lubricity
Unwashed gums
Washed gums
Gasoline
Polycyclic aromatics
Water
Distillation points
Region specific: US, EU + Time dependent: Euro-5, Euro-6, …
Diesel
SUMMER SCHOOL 2019
Selected specifications for Jet A-1 from Fischer-Tropsch synthesis
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 26
Property Up to 50 % Blend [1]
Net heat of combustion
[MJ/kg]min. 42,8
Density at 15 °C [kg/m3] 775-840
Viscosity at -20 °C [mm2/s] max. 8000
Freezing point [°C] max. -47
Flash point [°C] min. 38
Aromatics [Vol. %] max. 25
Distillation:
T10-TFinal[°C] 205 - 300
[1] ASTM International, „ASTM D7566 - 14C: Standard Specification for Aviation Turbine Fuel Containing Synthesized Hydrocarbons“, 2015
Jet A-1 from FT-synthesis:
• Drop-in fuel
(ASTM D7566 – 14c [1])
• Fully synthetic (100 %) certified
by Royal Airforce (U.K.)
SUMMER SCHOOL 2019
Techno-Economic and ecological assessment (TEEA)
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 27
Alternative jet fuel
Technical evaluation
Ecological evaluation
Economic assessment
DLR’s Techno economic
process evaluation tool
Efficiencies (X-to-Liquid, Overall)
Carbon conversion
Specific feedstock demand
Exergy analysis
CAPEX, OPEX, NPC
Sensitivity analysis
Identification of most economic
feasible process design GHG-footprint
GHG-abatement costs
SUMMER SCHOOL 2019
Techno-economic assessment
DLR Methodology
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 28
Literature
survey
1. Step
Identification of best
suited process design
Energy and material
balance
3. Step 4. Step
Identifying
crucial
process
parameters
Feedback to
project
partners
5. Step
Exchange
with project
partners
2. Step
Detailed
process
simulation
Stationary flowsheet
model
Technical
optimization (Process
control,
Heat integration, …)
Techno-
economic
evaluation
TEPET-
ASPEN Link
Exchange of process
parameters
Automatic sequencing
and economic
optimization
Calculation of NPC
(CAPEX, OPEX, etc.)
Sensitivity analysis &
upscaling
Iteration
Aspen Plus®
Simulation
SUMMER SCHOOL 2019
Process scheme (block flow diagram)
Example: EU-Project COMSYN
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 30
COMSYN project has received funding
from the European Union’s Horizon 2020
research and innovation programme
under grant agreement No 727476
SUMMER SCHOOL 2019
Second step: AspenPlus flowsheet model
Example: EU-Project COMSYN
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 31
Drying and
Gasification sectionReforming and
gas cleaning section
FT-Synthesis
sectionCentralized product
upgrading section
COMSYN project has received funding
from the European Union’s Horizon 2020
research and innovation programme
under grant agreement No 727476
Design data of each unit required
SUMMER SCHOOL 2019
AspenPlus – Heat integration
Process flowsheet – Heat integration
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 32
COMSYN project has received funding
from the European Union’s Horizon 2020
research and innovation programme
under grant agreement No 727476
SUMMER SCHOOL 2019
0
100
200
300
400
500
600
700
800
900
1000
0 20 40 60 80 100 120
Tem
pera
ture
/ °
C
Energy / MW
Warm Stream Cold Stream
AspenPlus – Technical assessment
Example – Heat integration – Composite curves
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 33
High amount of
excess heat > 400 °C
cooling demand
(< 90 °C)
SUMMER SCHOOL 2019
Techno-Economic and ecological assessment (TEEA)
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 35
Alternative jet fuel
Technical evaluation
Ecological evaluation
Economic assessment
DLR’s Techno economic
process evaluation tool
CAPEX, OPEX, NPC
Sensitivity analysis
Identification of most economic
feasible process design
SUMMER SCHOOL 2019
TEPET – Economic assessment
Methodology
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 36
Plant and unit sizes
Capital costs
• Equipment costs
• Piping & installation
• Factory buildings
• Engineering services …
Process simulation
results
SUMMER SCHOOL 2019
TEPET – Economic assessment
Methodology
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 37
Plant and unit sizes
Process simulation
results
Equipment costs:
• Standard equipment (compressors, pumps, heat exchangers):Chemical engineering data for industrial plants [1]
• Non-standard equipment (reactors, electrolyzers):Literature survey/Exchange with project partnersABC-Salt: project partners best guess?
[1] Peters M., Timmerhaus K., West R., Plant design and economics for chemical engineers, 2004
Capital costs
• Equipment costs
• Piping & installation
• Factory buildings
• Engineering services …
SUMMER SCHOOL 2019
TEPET – Economic assessment
Methodology
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 38
Plant and unit sizes
Material and energy balance
Operational costs
• Raw materials
• Operating materials
• Maintenance
• Labor costs …
Process simulation
results
Capital costs
• Equipment costs
• Piping & installation
• Factory buildings
• Engineering services …
SUMMER SCHOOL 2019
TEPET – Economic assessment
Methodology
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 39
Capital costs
• Equipment costs
• Piping & installation
• Factory buildings
• Engineering services …
Material and energy balance
Plant and unit sizes
Material and energy balance
Operational costs
• Raw materials
• Operating materials
• Maintenance
• Wages …
Process simulation
results
• Raw material prices and by-product revenues are year-specific (2017) introduced for Germany (stock market, market surveys)ABC-Salt: Different markets?
• Labor costs based on German labor market
Operational costs
• Raw materials
• Operating materials
• Maintenance
• Labor costs …
SUMMER SCHOOL 2019
TEPET – Economic assessment
Methodology
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 40
Plant and unit sizes
Material and energy balance
Net production costs
(NPC) [€/l; €/kg; €/MJ]
Capital costs
• Equipment costs
• Piping & installation
• Factory buildings
• Engineering services …
Process simulation
results
Operational costs
• Raw materials
• Operating materials
• Maintenance
• Labor costs …
SUMMER SCHOOL 2019
-0.5
0
0.5
1
1.5
2
2.5
3
3.5
Pro
du
ctio
n c
ost
s in
€/l
Electrolyzer
Fischer-Tropsch synthesis
Gasifier
Rest (CAPEX)
Biomass
Electricity
Oxygen
Remaining (Raw materials & Utilities)
Revenue from by-products
Maintenance
Labor costs
Rest (OPEX)
Example: TEEA of sustainable Jet fuel production
Base year: 2017
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 41
• 100 MWth biomass feed
• Annual production: 24.2 kt/a
• 2.86 €/liter FT-product
• Investment costs: 510 m€
• 100 MWth biomass feed
• + 164 MWe electrical power
• Annual production: 91.3 kt/a
• 2.51 €/liter FT-product
• Investment costs: 990 m€
SUMMER SCHOOL 2019
Techno-Economic and ecological assessment (TEEA)
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 42
Alternative jet fuel
Technical evaluation
Ecological evaluation
Economic assessment
DLR’s Techno economic
process evaluation tool
GHG-footprint
GHG-abatement costs
SUMMER SCHOOL 2019
GHG abatement costs
Example: Fischer-Tropsch jet fuel GHG Footprint
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 43
Electricity GHG
Footprint
GHG Footprint of
products
𝐆𝐇𝐆 𝐚𝐛𝐚𝐭𝐞𝐦𝐞𝐧𝐭 𝐜𝐨𝐬𝐭𝐬€
𝐭𝐂𝐎𝟐𝐞𝐪.=
𝐃𝐢𝐟𝐟𝐞𝐫𝐞𝐧𝐜𝐞 𝐢𝐧 𝐩𝐫𝐨𝐝𝐮𝐜𝐭𝐢𝐨𝐧 𝐜𝐨𝐬𝐭𝐬
𝐆𝐇𝐆 𝐚𝐛𝐚𝐭𝐞𝐦𝐞𝐧𝐭
Biorefinery
• System integration
• Efficiency
• Plant emissions
• Crediting of by-products
(steam, electricity, …)
Biomass GHG
footprint
Application
efficiency
SUMMER SCHOOL 2019
Take-home-messages
• Biomass residues could (theoretically) cover the foreseen European kerosene demand
→ Utilization competition
• No “Silver Bullet” Biomass-to-Liquid process route
→ Biochemical, thermochemical, chemical, mechanical conversion processes have to be adapted to
varying feedstock and product compositions
→ Refining and upgrading requires multiple unit operations to meet different product specifications
• Assessment requires transparency, reliability, accuracy → and collaboration
→ Techno-economic and ecologic evaluation methodology available for biorefinery concept comparison
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 44
Thank you for your attention!
Sandra Adelung, Ralph-Uwe Dietrich,
Felx Habermeyer, Simon Maier,
Moritz Raab, Julia Weyand
R.-U. Dietrich • Advanced Biorefinery concepts Towards Certified Jet Fuel • Aston, UK • 14.08.2019DLR.de • Chart 45
ABC-Salt project has received funding from the EU’s Horizon 2020
research and innovation Programme under Grant Agreement No 764089
SUMMER SCHOOL 2019