Resumes
Resumes
Edward Aitken Phones & Addresses
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61 Gingham St, Trabuco Canyon, CA 92679 (949) 766-9001
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Trabuco Cyn, CA
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La Quinta, CA
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Laguna Beach, CA
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Beaumont, TX
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Brea, CA
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Orange, CA
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61 Gingham St, Trabuco Canyon, CA 92679
Work
Position:
Professional/Technical
Business Records
Name / Title
Company / Classification
Phones & Addresses
The Process Group LLC
Services-Misc Engineering Services · Consulting
Services-Misc Engineering Services · Consulting
5405 Alton Pkwy, Irvine, CA 92604
27758 Santa Margarita Pkwy, San Juan Capistrano, CA 92691
26964 Safiro, San Juan Capistrano, CA 92691
27758 Santa Margarita Pkwy, San Juan Capistrano, CA 92691
26964 Safiro, San Juan Capistrano, CA 92691
President
AITKEN ENGINEERING, INC
54-829 Firestone, La Quinta, CA 92253
54-829 Firestone, La Quinta, CA 92253
54-829 Firestone, La Quinta, CA 92253
Publications
Wikipedia
Arthur Aitken
View pageMajor General Arthur Edward Aitken (1861 1924) was a British military commander. Born in Rochford in Essex by the time of the 1871 Census he was a 9-year ...
Isbn (Books And Publications)
Zoo in the Garden
View page
Author
Edward Hamilton Aitken
ISBN #
8178241218
Us Patents
Process For Cracking Nitrogen-Containing Feedstocks
View pageUS Patent:
47311746, Mar 15, 1988
Filed:
Jun 24, 1987
Appl. No.:
7/065889
Inventors:
Mario L. Occelli - Yorba Linda CA
Edward J. Aitken - Brea CA
Edward J. Aitken - Brea CA
Assignee:
Union Oil Company of California - Los Angeles CA
International Classification:
C10G 1105
C10G 17095
C10G 17095
US Classification:
208120
Abstract:
Hydrocarbon feedstocks containing relatively high levels of nitrogen contaminants are converted to products of lower average molecular weight by first mixing the feedstock with a dicarboxylic acid such as oxalic acid and then contacting the resultant mixture with a cracking catalyst in a cracking zone under cracking conditions in the substantial absence of added molecular hydrogen. The use of a dicarboxylic acid in lieu of a mineral acid such as sulfuric acid or nitric acid results in less corrosion to FCC unit internals and less emissions of sulfur and nitrogen oxides from the FCC unit regenerator.
Process For Reducing Sulfur Oxide Emissions From Catalytic Cracking Units
View pageUS Patent:
46421777, Feb 10, 1987
Filed:
Sep 30, 1985
Appl. No.:
6/781755
Inventors:
Zoltan C. Mester - Laguna Niguel CA
Edward J. Aitken - Brea CA
Edward J. Aitken - Brea CA
Assignee:
Union Oil Company of California - Los Angeles CA
International Classification:
C10G 1100
C01B 1760
C01B 1760
US Classification:
208113
Abstract:
A sulfur sorbent for use in reducing the emissions of sulfur oxides from regenerators of cyclic catalytic cracking units comprises a rare earth component or mixture of rare earth components in combination with a porous, inorganic refractory oxide component. The rare earth components used as a portion of the sorbent are preferably derived from the mineral bastnaesite by treating the bastnaesite to remove at least 50 weight percent of its fluorine, calculated as the element. The activity of the sulfur sorbent for removing sulfur oxides during catalytic cracking processes is increased to unexpectedly high levels by including in the composition cobalt or other transition metal component comprising an element selected from Group IB, Group IIB, Group IVA, Group VA, Group VIA, Group VIIA, and Group VIII of the Periodic Table of Elements.
Sorbent For Reducing Sulfur Oxide Emissions From Catalytic Cracking Units And Process For Producing The Sorbent
View pageUS Patent:
46862048, Aug 11, 1987
Filed:
Jul 31, 1986
Appl. No.:
6/891145
Inventors:
Zoltan C. Mester - Laguna Niguel CA
Edward J. Aitken - Brea CA
Edward J. Aitken - Brea CA
Assignee:
Union Oil Company of California - Los Angeles CA
International Classification:
B01J 2002
B01J 2008
B01J 2008
US Classification:
502406
Abstract:
A sulfur sorbent for use in reducing the emissions of sulfur oxides from regenerators of cyclic catalytic cracking units comprises a rare earth component or mixture of rare earth components in combination with a porous, inorganic refractory oxide component. The rare earth components used as a portion of the sorbent are preferably derived from the mineral bastnaesite by treating the bastnaesite to remove at least 50 weight percent of its fluorine, calculated as the element. The activity of the sulfur sorbent for removing sulfur oxides during catalytic cracking processes is increased to unexpectedly high levels by including in the composition cobalt or other transition metal component comprising an element selected from Group IB, Group IIB Group IVA, Group VA, Group VIA, Group VIIA, and Group VIII of the Periodic Table of Elements.