Exxon Mobil - Global Technology Forum
Exxon Mobil - Global Technology Forum
Exxon Mobil - Global Technology Forum
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Gasoline Benzene Reduction Through Reformate<br />
Alkylation Catalytic <strong>Technology</strong>: BenzOUT TM<br />
Dr. El-Mekki El-Malki<br />
Dr. Tim Hilbert<br />
<strong>Exxon</strong><strong>Mobil</strong> Research & Engineering Company<br />
(EMRE)<br />
Mr. Ronald Birkhoff<br />
Badger Licensing LLC<br />
ERTC 16 th Annual Meeting<br />
2011 Barcelona
The Refiner’s Challenge<br />
Properties<br />
Required for<br />
Engine<br />
Performance<br />
• Examples<br />
• Octane<br />
• Reid vapor pressure<br />
• Driveability Index<br />
Properties<br />
required under<br />
Government<br />
Regulations<br />
• Examples<br />
• Benzene<br />
• Oxygenates<br />
• Sulfur<br />
• Reid vapor pressure
Reducing Benzene in Gasoline Pool<br />
1.0 vol%<br />
1.0 vol%<br />
0.62 vol %<br />
MSATII<br />
1-4 vol%<br />
range<br />
1-5 vol%<br />
range<br />
1-3 vol%<br />
range<br />
1.0 vol%<br />
pending<br />
1.0 vol%
Typical Gasoline Pool Benzene<br />
Components<br />
Average<br />
Volume in<br />
Gasoline %<br />
Typical<br />
Benzene<br />
Level %<br />
Benzene<br />
Contribution %<br />
Reformate ~ 30 3-11 ~ 75<br />
FCC Gasoline ~ 36 0.5-2 ~ 16<br />
Hydrocrackate ~ 3 1-5 ~ 3<br />
Others ~ 31 0-3 ~ 6
Refiner’s Options<br />
Octane<br />
Gasoline<br />
Volume<br />
Gasoline<br />
Pool<br />
Hydrogen<br />
Balance<br />
Light<br />
Olefin<br />
Reformer Feed<br />
Tailoring<br />
Benzene Extraction<br />
Reduced<br />
Production<br />
No<br />
change<br />
Benzene Saturation<br />
BenzOUT<br />
High<br />
consumption<br />
No<br />
consumption<br />
Upgrade<br />
to<br />
Mogas
BenzOUT Process Configuration<br />
Benzene<br />
Concentrate<br />
Pretreatment<br />
Light Olefins<br />
Light end<br />
Full Reformate<br />
Splitter<br />
BenzOUT<br />
Reactor<br />
Stabilizer<br />
Products<br />
• Fixed Bed Reactor Configuration<br />
• Commercially Demonstrated<br />
• First Licensed Unit in Construction
Example of BenzOUT Boosting Product Volume<br />
Benzene<br />
Concentrate<br />
Pretreatment<br />
C 3= /C 3<br />
Light end<br />
Full Reformate<br />
40 KB/D<br />
Splitter<br />
BenzOUT<br />
Reactor<br />
Stabilizer<br />
42.3 KB/D<br />
• Approx. 5% Volume Increase Based on Full Reformate
Example of BenzOUT Product Properties<br />
Temperature ( o F)<br />
Typical Gasoline End Point<br />
Product<br />
Feed<br />
% Evaporated<br />
• Final Product Properties are a Function of Feed Composition and<br />
Benzene Conversion<br />
− Approx. (R+M)/2 increase of 2-5<br />
− Approx. RVP reduction of 0.5 PSI
Process Demonstrated in a North American Refinery<br />
C 3= /C 3<br />
Reformate<br />
BenzOUT<br />
Catalyst<br />
Mogas Blending<br />
• BenzOUT Catalyst Drop-in Application<br />
• BenzOUT Demonstration Conducted in One of the 3 Tubular Reactors<br />
• BenzOUT and Polygas Products Combined for Mogas Blending
Commercial Demonstration Results<br />
100<br />
Benzene Conversion (%)<br />
Olefin/Aromatic ratio<br />
0<br />
0 10 20 30 40 50 60<br />
Days on Stream<br />
• High Benzene Conversion Demonstrated<br />
• Commercial Results Confirm Pilot Plant Data
BenzOUT <strong>Technology</strong> Delivery<br />
• <strong>Exxon</strong><strong>Mobil</strong> Research & Engineering Company (EMRE)<br />
and Badger Licensing LLC formed an alliance:<br />
− BenzOUT offered exclusively by Badger Licensing LLC<br />
− Badger is the contracting party responsible for the process<br />
license, proposals and basic design packages.<br />
− EMRE supplies the BenzOUT Catalyst<br />
• <strong>Exxon</strong><strong>Mobil</strong> and Badger have a continuing 30 year<br />
history of licensing Petrochemical Processes
BenzOUT Value Proposition<br />
‐ Upgrade Olefins to High Octane Gasoline<br />
- Increase Gasoline Volume<br />
- Reduce RVP<br />
- Avoid Hydrogen Loss<br />
- Regain Reformer Flexibility e.g. Yield, Octane, H 2<br />
‐ Reduce Benzene Content in Gasoline
THANK YOU