Higher severity HDT needed for low-sulfur diesel
Journal Article
·
· Oil Gas J.; (United States)
OSTI ID:6502925
Most existing mid-distillate hydroprocessing units will have to operate at higher temperatures, lower liquid hourly space velocities (LHSV), or a combination of both, to meet the Environmental Protection Agency's proposed rules to limit sulfur in diesel to 0.05 wt % and total aromatics content to 20 vol %. If current space velocities are maintained, much higher operating temperatures will be required to maintain current diesel output. Higher temperatures will result in much shorter cycle lengths and significantly higher operating costs. Some existing units may not be able to reach the higher temperatures. If space velocities are lowered, refiners may have to consider adding parallel hydroteating units to maintain current production quantities. This could be restricted by the availability of new capital for the additions. A study, that included pilot plant tests, was conducted to determine the ability of existing hydroprocessing units throughout the U.S. to produce diesel fuel at the proposed sulfur and aromatics limits.
- Research Organization:
- American Cyanamid Co., Wayne, NJ
- OSTI ID:
- 6502925
- Journal Information:
- Oil Gas J.; (United States), Journal Name: Oil Gas J.; (United States) Vol. 85:15; ISSN OIGJA
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
02 PETROLEUM
020400* -- Petroleum-- Processing
AROMATICS
CAPITAL
CHEMICAL PREPARATION
CHEMICAL REACTIONS
CHEMICAL REACTORS
COST
CRACKING
DECOMPOSITION
DIESEL FUELS
DISTILLATES
ENERGY SOURCES
FOSSIL FUELS
FUELS
FUNCTIONAL MODELS
HYDROCRACKING
HYDROGENATION
INDUSTRIAL PLANTS
NATIONAL ORGANIZATIONS
NORTH AMERICA
OPERATING COST
ORGANIC COMPOUNDS
PERFORMANCE TESTING
PETROLEUM
PETROLEUM DISTILLATES
PETROLEUM FRACTIONS
PETROLEUM PRODUCTS
PETROLEUM REFINERIES
PILOT PLANTS
PYROLYSIS
REGULATIONS
SULFUR CONTENT
SYNTHESIS
TEMPERATURE EFFECTS
TESTING
THERMOCHEMICAL PROCESSES
US EPA
US ORGANIZATIONS
USA
VELOCITY
020400* -- Petroleum-- Processing
AROMATICS
CAPITAL
CHEMICAL PREPARATION
CHEMICAL REACTIONS
CHEMICAL REACTORS
COST
CRACKING
DECOMPOSITION
DIESEL FUELS
DISTILLATES
ENERGY SOURCES
FOSSIL FUELS
FUELS
FUNCTIONAL MODELS
HYDROCRACKING
HYDROGENATION
INDUSTRIAL PLANTS
NATIONAL ORGANIZATIONS
NORTH AMERICA
OPERATING COST
ORGANIC COMPOUNDS
PERFORMANCE TESTING
PETROLEUM
PETROLEUM DISTILLATES
PETROLEUM FRACTIONS
PETROLEUM PRODUCTS
PETROLEUM REFINERIES
PILOT PLANTS
PYROLYSIS
REGULATIONS
SULFUR CONTENT
SYNTHESIS
TEMPERATURE EFFECTS
TESTING
THERMOCHEMICAL PROCESSES
US EPA
US ORGANIZATIONS
USA
VELOCITY