The potential and challenges of “drop in” biofuels

The potential and challenges of
“drop in” biofuels
OH
OH
O H
H
OH
H
- O2
H
HO
OH
H
H
H
H
H
H
C
C
C
C
H
H
H
H
H
OH
Hydrocarbon
H
H
HO
OH
H
OH
Carbohydrate
O H
H
OH
“Petroleum-like” biofuel
Sergios Karatzos, Jim McMillan and Jack Saddler
International Energy Agency Bioenergy Task 39 (liquid biofuels)
Forest Products Biotechnology/Bioenergy (FPB/B)
Commissioned Task 39
‘drop in’ biofuel report
§  OVERVIEW
§  Definition
§  Role of Hydrogen in drop in biofuels
§  Role of Hydrogen in petroleum industry
§  TECHNOLOGIES
Forest Products Biotechnology/Bioenergy at UBC
Definition of a “drop-in” biofuel
§  Bioethanol: Biogenic ethyl alcohol
§  Biodiesel: Fatty acid methyl esters (FAME)
§  Drop-in biofuels are liquid hydrocarbons that are
functionally equivalent and as oxygen-free as petroleumderived transportation blendstocks (fuels)
§  Examples:
§  Hydrotreated Vegetable Oils (HVO)
§  Hydrotreated Pyrolysis Oils (HPO)
§  Fischer Tropsch Liquids (FT liquids)
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Properties of transportation fuels
Drop-in biofuels need
to have similar
properties to
petroleum fuels:
•  Fit the carbon
number range
•  Low to No oxygen
24
22
20
18
16
14
12
10
8
6
4
2
0
400
carbon number
350
boiling point
B10
?
300
250
200
Jet
150
100
50
E10
0
Ethanol Gasoline
Jet A
Diesel
Biodiesel
Unlike
conventional biofuels, “drop-in” biofuels should be
Forest Products Biotechnology/Bioenergy at UBC
indistinguishable from petroleum fuels for end uses!
Oxygen Challenge
§  Oxygen is present in biomass in the form of hydroxyls,
esters, and ethers
§  Can oxidize fuel components, reactors and pipeline
metallurgy to cause corrosion
§  Oxygen content reduces energy density
CH3
Ethanol
Biodiesel (fatty acid methyl ester)
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Oxygen content vs. energy density
Energy density (MJ/L)
Drop in biofuel
45
Crude oil (No O2)
40
Biodiesel(11% O2)
35
Butanol (21.5% O2)
30
25
Ethanol(35% O2)
20
15 R² = 0.99438
Biomass/
10
Sugar
(50% O2)
5
0
0
0.1
0.2
0.3
0.4
0.5
0.6
O/C molar ratio
Increasing Oxygen content reduces fuel energy density
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Deoxygenating biomass dilemma
…add H2 or lose yield?
-H2O
Insert Hydrogen
A Hydrocarbon
e.g. Butane
A Carbohydrate
e.g. Glucose
- O2
C6H12O6
High H/C ≈ 2
Oxidize Carbon
“sacrificing” feedstock
C4H10
-CO2
Objective is to deoxygenate and enrich H2 content of biomass
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Effective hydrogen to carbon ratio (Heff/C)
§  A high Effective Hydrogen to Carbon ratio is
desired for drop-in biofuels
§  Heff/C
=​𝑛(𝐻)−2𝑛(𝑂)/𝑛(𝐶) Heff/C = 0
Heff/C ≈ 2
OH
O H
H
OH
H
H
H
HO
OH
H
OH
Carbohydrate
Forest Products Biotechnology/Bioenergy at UBC
H
H
H
H
C
C
C
C
H
H
H
H
H
Hydrocarbon
(e.g. Butane, Diesel)
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The Effective H/C ratio staircase…
‘Drop-in’ biofuel
Oleochemical
Diesel 2.0
Lipids 1.8
1.6
1.4
1.2
1.0
0.8
Lignin 0.6
Ethanol 0.4
Wood
Sugar
0
Thermochemical
0.2
Biochemical
High O2 or low H/C feedstocks require more processing and H2 inputs
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The Hydrogen-Oxygen dilemma
§  “Drop-in biofuels” is a loose term referring to
liquid biofuels containing low or no oxygen content
§  Deoxygenation requires hydrogen inputs or
“oxidizing/burning” of feedstock carbon
§  High Heff/C ratio feedstocks such as lipids are well
suited for drop-in biofuel production
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What will determine the success of “drop in
biofuels”?
§  Drop-in biofuel technologies complexity/
selectivity and hydrogen demand
§  Commercialization challenges such as capital,
yield and refinery insertion
§  Crude oil is becoming increasingly hydrogen
deficient (‘heavier’ and ‘sourer’)
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Crude oil quality declining…
90
Million barrels per day
80
70
an
”
y
v
“Hea
ing
s
a
e
r
inc
l
i
o
ur”
o
S
“
d
60
50
Heavy Sour
40
Light Sour
30
Light Sweet
20
“Sour” = High Sulfur
10
0
1990
2000
2010
2020
Purvin & Gertz forecast for world crude oil quality (Source: data from EIA)
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The H/C ratio staircase for petroleum…
Diesel 2.0
Light crude 1.8
1.6
Heavy crude 1.4
Oil sands 1.2
1.0
0.8
0.6
Coal 0.4
Lower quality fossil feedstocks = lower H/C ratio = higher H2 inputs
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Hydrotreating and Hydrocracking
§  Hydrotreating (Removes sulfur impurities as H2S)
§  Hydrocracking (breaks heavy oil to lighter molecules)
Heavy crude molecule
Gasoline range molecule
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Diesel range molecule
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US Hydrotreating capacity 1990-2030
million barrels per day
30
25
20
15
10
5
Rapid increase in H2 consumption in US refineries
0
1990
1995
2000 2004
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2010
2015
2020
2025
2030
15
Source EIA, Annual Energy Outlook 2006
Natural gas: Where H2 comes from
CO2
§  90 % of commercial H2 comes from steam
reforming natural gas
CH4
Steam reforming
H2
ENERGY INTENSIVE PROCESS!!
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Role of H2 in upgrading petroleum and
drop-in biofuels
Petroleum
!  Increasing
Drop-in Biofuels
Sulfur content
!  Increasing
heavy oil
needs cracking
§  No Sulfur
§  High Oxygen content of
feedstock needs
hydrogenation
Both require Hydrogen for upgrading to finished fuels
Hydrogen will likely come from Natural Gas
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Commissioned Task 39
‘drop in’ biofuel report
§  OVERVIEW
§  Definition
§  Role of Hydrogen in drop in biofuels
§  Role of Hydrogen in petroleum industry
§  TECHNOLOGIES
Forest Products Biotechnology/Bioenergy at UBC
The commercialization potential of Drop in
Biofuel platforms and their H2 dependence
§  Oleochemical (HVO, algae)
§  Thermochemical (Pyrolysis - HPO, Gasification
FT-liquids)
§  Biochemical (Advanced Fermentation)
§  Hybrid platforms (e.g. Virent, Zeachem, Lanzatech)
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Biomass fiber
hydrolysis
sugars
fermentation
gasification
syngas
catalytic
conversion
pyrolysis
biooil
upgrading
animal
digestion
oilseed crop
lipids
Autotrophic
algae
Oleo
Sun photons, water, CO2
and nutrients
sugar crop
FT liquids
(e.g. CHOREN)
HPO
(e.g. ENSYN)
Blending
LEGEND materials
processes
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Isoprenoids
(e.g. Amyris)
Hydroprocessing
Higher alcohols
(e.g. Gevo)
Thermo
CONVENTIONAL
INTERMEDIATES
Bio
Technology pathways to “drop-in”
drop-in
fuel
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Oleochemical Platform
Hydrotreated Vegetable Oils or HEFAs
Fatty acid feedstock
Challenges
§  Costly feedstock (approx. $500-1000/t)
§  Sustainability?
Forest Products Biotechnology/Bioenergy at UBC
Hydroprocessing
Major advantages
§  “Simple” technology, low risk (processes already commercial)
§  Bio SPK ASTM certification
§  High Hydrogen to carbon ratio (low Oxygen) of Feedstock
§  Palm oil
Gases
§  Tallow (rendered animal fat)
Gasoline
Jet
Diesel
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Commercial drop-in biofuel companies
Neste Oil facility, Rotterdam
§  All based on oleochemical
§  Neste Oil: 2,400,000,000 L diesel
from palm oil
§  Dynamic Fuels: 280,000,000 L diesel
animal fat
Forest Products Biotechnology/Bioenergy at UBC
fr
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Many examples of commercial biofuel flights
§  Virtually all based on oleochemical
§ 
§ 
§ 
§ 
§ 
§ 
US Navy: Sept 2011 Solazyme algae oil and palm oil
Continental Airlines: Nov 2011 Solazyme algae oil
Alaska Airlines: Jan 2012 tallow and algae
Lufthansa: July 2011 Jatropha, Camelina
Finnair: July 2011 Used Cooking Oils
Many more
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Thermochemical drop-in biofuel platforms
Pyrolysis oil
Gases
HPO
900°C
some O2
Gasification
Syngas
Fischer
Tropsch
Biomass
Forest Products Biotechnology/Bioenergy (FPB/B)
FT liquids
Hydrocracking
No O2
Hydro
treatment 2
500°C
CATALYTIC
UPGRADING
Hydro
treatment 1
INTERMEDIATES
Gasoline
Jet
Diesel
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Example of pyrolysis drop in facility:
KiOR
§  50,000,000 L per year in Mississippi (in operation)
H2
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Forest BtL Oy and Choren’s Carbo-V
§  130,000,000 L per year of Gasification FT liquids by 2016
(Finland)
Pretreat.
Gasification
conditioning
Sundrop biofuels 190 MLPY
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H2
H2
CO2
FT
Hydrocracking
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USD/ Gallon Gasoiline Equivalent Feedstock and Capital cost of drop-in Biofuels
18 16 14 12 10 8 6 4 2 0 Feedstock cost Capital (installed capacity) Oleochemical
HVO Pyrolysis Gasifica6on Feedstock
intensive vs Capital intensive platforms
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Source: Kazi et al. 2010, Pearlson et al. 2011, Jones et al. 2009
USD/ Gallon Gasoiline Equivalent “Over the fence” Hydrogen inputs can reduce
capital and feedstock costs
18 16 14 12 10 8 6 4 2 0 H2
3% H2
7% H2
Feedstock cost Capital (installed capacity) Oleochemical
HVO Pyrolysis Gasifica6on Pyrolysis
is highly
dependent
on access to cheap Hydrogen
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Biotechnology/Bioenergy
at UBC
Source: Kazi et al. 2010, Pearlson et al. 2011, Jones et al. 2009
Drop in biofuels leveraging on Oil refineries
OLEOCHEMICAL
OIL REFINERY
Lipids
HPO
Gasification
Syngas
Fischer
Tropsch
Biomass
Forest Products Biotechnology/Bioenergy (FPB/B)
FT liquids
Hydrocracking
Pyrolysis oil
Hydro
treatment 2
THERMOCHEMICAL
Hydro
treatment 1
Gases
Gasoline
Jet
Diesel
over the fence H2
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Drop in biofuels leveraging on Oil refineries
DISTILLATION
(CATALYTIC) UPGRADING
Lipids FT liquids
HPO
Light ends
Reformer
Hydrotreatment
Fluid
catalytic
cracking
Vacuum
unit
Coker
Jet
Diesel, Jet
Diesel, Jet
Gasoline
Hydrocracker
Heavy ends
Gasoline
Hydrotreatment
Gasoline
Diesel, Jet
Product blending
Distillation
tower
Crude
oil
BLENDING
Coke
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Challenges of hydroprocessing biofeed:
The Haldor Topsoe experience
§  Higher Hydrogen consumption
§  requirements more than doubled when just 5% of feed
was replaced with biofeed!
§  Presence of oxygenated gases such as CO and H2O
§  Heterogeneity of feedstock (Catalyst design challenges)
Forest Products Biotechnology/Bioenergy at UBC
Source: Haldor Topsoe, 2009
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Major scale up challenges for each platform
§  Pyrolysis
§  Hydrogen
§  Hydrotreating catalyst
§  Gasification
§  Capital / scale
§  Feedstock /yields
§  HVO oleochemical
§  Feedstock
§  Refinery insertion challenges
Forest Products Biotechnology/Bioenergy at UBC
Sources: Jones et al. 2009; Swanson
et al. 2010; Pearlson et al. 2011
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Biochemical: Sugar fermentation to drop-in
SUGAR
FERMENTATION
Target molecule
Modified algae,
bacteria or yeast
Long alcohols
Aliphatic chains
§  Major advantages
§  Pure and “functionalized” product streams suitable for
value added markets
§  Major challenges
§  Volumetric productivity about 10x lower than ethanol
§  Recovery challenges: e.g. recovery from fermentation
broth and intracellular expression
§  Sugar feedstock highly oxidized (H/C = 0)
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Fermentation pathways for deoxygenating
Carbohydrates
Glucose
(C6)
x
•  High requirement for
reducing power
(derived from NADPH
or Hydrogen)
Pyruvate
(C3)
PPP cycle
Elongation
cycles:
7
Repeat
•  Energy intensive
CO2
Compared to
ethanologenic yeast:
Example:
acid
LanzatechFatty
CO2 +
H2
biosynthesis
example
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Acetyl-ACP
(C2)
HCO3 Malonyl-ACP
(C3)
Acetoacetyl-ACP
ACP +
2x
NADPH HCO3
ButyrylACP (C4)
ACP
Palmitate
(C18)
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Climbing fewer steps on the Heff /C staircase
…
‘Drop-in’ biofuels
Diesel 2.0
Lipids 1.8
1.6
1.4
1.2
1.0
0.8
0.6
Value-added
biorenewables
0.4
Wood
Sugar
0
0.2
Biochemical feedstock
Value Forest
added
chemicals
have
Products
Biotechnology/Bioenergy
at UBClower Heff /C ratios than fuels
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Summary
§  Oleochemical: commercial now and less H2-dependent with
considerable potential for growth (feedstock challenges?)
§  Thermochemical well suited for long term drop-in biofuels
§  H2 and catalyst challenges (Pyrolysis), Scale challenges (Gasification)
§  Leveraging on oil refineries: more challenging than expected
§  Biochemical “drop-in” products more valuable in rapidly
growing chemicals markets
§  Accessing cheap/renewable Hydrogen will be a key
challenge for both drop-in biofuels and crude oil of decreasing
quality
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ACKNOWLEDGEMENTS
International Energy Agency Bioenergy Task 39 colleagues
www.Task39.org
Forest Products Biotechnology/Bioenergy (FPB/B)
Future competition for Hydrogen inputs…
§  Heavy oil processing
e.g.
Venezuela and Alberta
§  Ammonia industry
§  Drop-in biofuels?
Forest Products Biotechnology/Bioenergy at UBC
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