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Energy Consumption
Energy Consumption by Fuel | Fuel Consumption by End Use |
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Energy Intensity

Energy consumption in refineries is dominated by a few processes that, while not the most energy-intensive, have the greatest throughput. Atmospheric and vacuum distillation, for example, account for 35-40% of total process energy consumption. The reason is that every barrel of crude oil entering the refinery must be subjected to an initial separation by distillation. [DOE 1998]

1997 Estimated Energy Consumption by Refining Processa
Process Average Useb
(103 Btu/bbl)
Capacity
(106 bbl/cday)c
Annual Energy Consumption
(1012 Btu/year)
Atmospheric Distillationd 113.8 15.45 641.6
Vacuum Distillation 91.5 7.15 238.8
Visbreakinge
     - Coil
     - Soaker
 
136
63
 
0.0215
0.0436
 
1.07
1.00
Delayed Coking 166 1.671 114.6
Fluid Coking (net) 258 0.075 7.1
Flexicoking (net) 167 0.112 6.7
Fluid Catalytic Cracking 100 5.2 190.6
Catalytic Hydrocracking 240 1.3 109.7
Catalytic Hydrotreating 120 10.7 468.3
Catalytic Reforming 284 3.6 376.3
Alkylation
     - Sulfuric Acid
     - Hydrofluoric Acid
 
335
401
 
0.44
0.66
 
53.3
95.5
Ethers Production 403 0.18 33.4
Isomerization
     - Isoburane
     - Isopentane/Isohexane
     - Isobutylene
 
359
175
476
 
0.098
0.42
n/a
 
13.0
27
n/a
Lube Oil Manufacture 1506 0.20 109.5
TOTALf -- -- 2487.5

Source: DOE 1998

a Gross energy sue, which includes losses incurred during the generation and transmission of electricity (electricity conversion factor of 10,500 Btu/kWh). Does not include hydrogen or oxygen consumption.
b Average energy use based on estimated utility requirements for a range of technologies.
c bbls/cday = barrels per calendar day (365 days per year).
d Includes energy consumed for desalting of crude.
e Assumes 33% of capacity is coil type and 67% is soaker type visbreakers.
f Does not include hydrogen production processes, sulfur recovery and management processes, operation of cooling towers, and other supporting processes.
n/a indicates data is not available.




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