Main Title |
Demetalization of heavy residual oils, phase III / |
Author |
Chervenak, M. C.,
|
Other Authors |
|
CORP Author |
Hydrocarbon Research, Inc., Trenton, N.J.;Industrial Environmental Research Lab., Research Triangle Park, N.C. |
Publisher |
U.S. Environmental Protection Agency, Office of Research and Development ; For sale by the National Technical Information Service, |
Year Published |
1976 |
Report Number |
EPA-600-2-76-165; EPA-68-02-0293; EPA-ROAP-21ADD-050 |
Stock Number |
PB-255 983 |
OCLC Number |
02504476 |
ISBN |
pbk. |
Subjects |
Petroleum--Refining--Desulfurization ;
Petroleum--Vanadium content ;
Petroleum--Refining--Desulphurization
|
Additional Subjects |
Residual oils ;
Catalysts ;
Fuel oil ;
Petroleum industry ;
Performance evaluation ;
Reaction kinetics ;
Desulfurization ;
Air pollution ;
Cost estimates ;
Operating costs ;
Tables(Data) ;
Thermodynamic properties ;
Demetallization ;
Air pollution abatement ;
Low sulfur fuels
|
Internet Access |
|
Holdings |
Library |
Call Number |
Additional Info |
Location |
Last Modified |
Checkout Status |
EKBD |
EPA-600/2-76-165 |
|
Research Triangle Park Library/RTP, NC |
06/27/2003 |
ELBD ARCHIVE |
EPA 600-2-76-165 |
Received from HQ |
AWBERC Library/Cincinnati,OH |
10/04/2023 |
ESAD |
EPA 600-2-76-165 |
|
Region 10 Library/Seattle,WA |
03/23/2010 |
NTIS |
PB-255 983 |
Some EPA libraries have a fiche copy filed under the call number shown. |
|
07/26/2022 |
|
Collation |
xv, 112 pages : illustrations, diagram, graphs ; 28 cm. |
Abstract |
The report gives results of Phase III work to optimize operating conditions in the demetallization step for overall desulfurization of heavy petroleum residual oils. Bachaquero and Lloydminster vacuum residue were demetallized to different levels of vanadium removal, the products desulfurized over commercial hydrodesulfurization catalyst at various operating conditions, and minimum operating costs were calculated to produce low sulfur fuel oil. The report describes test units, operating conditions, and procedures, and includes run summaries and tables of feedstock, product, and catalyst inspections. Graphs and tables depicting operating costs for producing 0.3, 0.5, and 1.0 wt % sulfur fuel oil are given, along with various correlations between demetallization levels, catalyst deactivation, demetallization rate constant, and contaminant metals deposited on catalyst. |
Notes |
Prepared by Hydrocarbon Research, Inc., Trenton, New Jersey, under contract no. 68-02-0293, ROAP no. 21ADD-050, program element no. 1AB013. Includes appendices. |