2014 Gas/Electric Partnership
Strategies for Utilizing/Monetizing Wellhead Gas
Brian Cody – February 5
About us
• Unique innovative technology solution for smaller scale GTL
• World-class pedigree − 20 yrs of research and development— University of Oxford: top global research centre;
largest chemistry department in Western World— Battelle: world’s largest independent science and
technology organisation
• Global leader— World’s largest and strongest microchannel IP portfolio (>800 patents)— >$300 million invested, much by commercial partners
• Critical mass— ~100 employees focused on FT; backed by a strong balance sheet
• First class partners offering a complete GTL solution
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Leaders in smaller scale GTL
Many applications
• Shale gas: monetizing low prices in North America
• Stranded gas: estimated over 30% of world reserves are uneconomic to bring to market
• Associated gas: 5% of natural gas production is flared
• GTL allows valuable products to be created and shipped— Ultra low-sulfur diesel (70 cetane) & jet — Waxes, lubricants and solvents
• Not just gas: also biomass and coal
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From low-value gas to high-value fungible products
The gas-to-liquids (GTL) process
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Chemical conversion of gas to refined products
Reforming
LNG / CNG = physical compression Product remains natural gas
GTL = chemical conversion into refined products (petroleum equivalent)
Fischer-Tropsch (FT)
Nat
ural
Gas
Syncrude(syntheticcrude oil)
Hydro-processing
Syngas(carbon monoxide
+ hydrogen)
Clean syntheticfuels & chemicals
(diesel, jet fuel,lubricants etc.)
Smaller scale GTL: gas-based mini-refinery
Velocys microchannel technology
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Compact, robust, efficient and economic
• Principles of design and operation— Particulate catalyst in small channels— High catalyst volume fraction— Syngas downflow, products exit bottom— Cross-flow coolant water / steam generation— Heat removal by steam generation
• Strengths— High per pass conversion (75%+)— Isothermal behavior – thermally stable— Extremely robust to upsets— Strong economy of mass manufacturing — Accommodates high activity catalysts— Installed spares relatively cheap— High on-stream factor— Tail gas recycle only to achieve high conversion— Extremely high volumetric productivity— Ease of modularizationVelocys FT reactor
Microchannel scale up = numbering up
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Equivalent to conventional fixed bed reactors
Key dimensions do not change• Laboratory reactor
— Channel dimensions same as commercial reactor
• Pilot reactor — Full size repeating layer
• Demonstration reactor— >1 full size repeating layer
• Commercial reactor — Many full size repeating layers
• Micro-macro interface ensures consistent results in pilot and commercial installations
COMMERCIAL
DE
MO
NS
TR
AT
ION
PILOT
Gas flowL
AB
OR
AT
OR
Y
Number of channels increases, size does not
Super-active FT catalyst
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Velocys catalyst is 10x more active than conventional
(Shell) (Sasol)
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1600
Fixed Bed Slurry Bed Velocys
Cat
alys
t Pro
duct
ivity
(kg/
m3/
hr)
Exceptional FT catalyst stability
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Operated for 2 years without regeneration
CO conversion
CH4 selectivity
TemperatureCurrent operation approaching 3 yrs
High productivity (single stage with recycle)
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>90% overall conversion with minimal recycle
Equal to 91-92%overall conversion
Equal to 94.5%overall conversion
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0%
10%
20%
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100%
0 50 100 150 200 250 300 350
Tem
pera
ture
, oC
% C
onve
rsio
n, %
Sel
ectiv
ity
Time on Stream (days)
Regeneration
Loss of cooling system - high t.
CO conversion
Temperature
Methane selectivity
Reactor design
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Optimized for serviceability
Manways size and location designed with Mourik for optimum access for catalyst handling
Diameter ~4.5 ftLength ~12 ft (15 ft for a 4-core)
Bottom manways have elliptical heads to allow liquid phase product draining. Removable for catalyst change-out
Reactor size optimized for weight / crane limits
Weld locations optimized for mass manufacturing
Integrated modular GTL facility
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Site-specific client designs underway
Velocys enables winning economics
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Base case
$0
$25
$50
$75
$100
$125
$150
Costs of Velocys enabledGTL plant
Proceeds from production ofliquid fuels
Cos
ts &
pro
ceed
s ($
/bar
rel o
f liq
uid
prod
ucts
)
Premium from sale of dieselOil (WTI)OPEXDepreciationNatural gas
Key financial assumptions
• Facility producing 80% diesel & 20% naphtha
• Gas price = $4/mmbtu
• 9,500 scf gas per barrel
• Capital cost = $100k per bpd for 2,500 bpd stand-alone Gulf coast plant
• Operating cost = $15/bbl
• 20 year plant life
Pilot plant and training facility
• Integrated GTL pilot plant at the Velocys Ohio, USA site
• Provides— Performance data to support differing
client designs— Product for client studies— Permanent training facility for plant
operators
• Platform for— Developing our own field support staff— Demonstrating future product
generations
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Supporting sales and delivery
Add pilot plant photo
Pilot plant
Complete GTL solution
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Together with world-class partners
Modular GTL
Technology
Engineering
Fabrication
Catalyst
Field services
Resource holders