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Louis J Nordrum

from American Canyon, CA
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Related to:
Ernest I Blake, 99Josephine Nordrum, 29Susanna Nordrum, 35Christina A Nordrum, 27Kerry L Nordrum, 66Susann Blake Nordrum, 60Thomas O Nordrum, 64
Connected to:
Michael J Nordseth, 38Gerald Nordsiek, 46Sylvie Nordson, 65Maria E Nordstedt, 90Agneta K Nordstrom, 93Alberta R Nordstrom, 79Anna N Nordstrom, 92Blaine A Nordstrom, 72Darlene C Nordstrom, 58Eric W Nordstrom, 74

Louis Nordrum Phones & Addresses

  • American Canyon, CA
  • Belgrade, MT
  • 100 Grove Ave, Corte Madera, CA 94925 (415) 924-7841
  • 100 Grove Ave, Corte Madera, CA 94925

Work

Company: Chevron Position: Program manager

Education

Degree: High school graduate or higher

Skills

Petroleum • Energy • Gas • Process Engineering • Upstream • Petrochemical • Engineering • Chemical Engineering • Oil/Gas • Project Engineering • Oil and Gas • Process Simulation • Natural Gas • Project Planning • Project Management • Energy Industry • Commissioning • Downstream Processing • Process Optimization • Epc

Emails

b***[email protected]

Industries

Oil & Energy

Resumes

Resumes

Louis Nordrum Photo 1

Program Manager

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Location:
514 Americas Way, Box Elder, SD 57719
Industry:
Oil & Energy
Work:
Chevron
Program Manager
Skills:
Petroleum
Energy
Gas
Process Engineering
Upstream
Petrochemical
Engineering
Chemical Engineering
Oil/Gas
Project Engineering
Oil and Gas
Process Simulation
Natural Gas
Project Planning
Project Management
Energy Industry
Commissioning
Downstream Processing
Process Optimization
Epc

Publications

Us Patents

Process For Separating And Recovering Metals

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US Patent:
20120039777, Feb 16, 2012
Filed:
Jun 9, 2011
Appl. No.:
13/156589
Inventors:
Rahul Shankar Bhaduri - Moraga CA, US
Louis Joseph Nordrum - Corte Madera CA, US
Alexander E. Kuperman - Orinda CA, US
Assignee:
c/o Chevron Corporation - San Ramon CA
International Classification:
C22B 34/30
US Classification:
423 58
Abstract:
A process for treating spent catalyst containing heavy metals, e.g., Group VIB metals and Group VIII metals is provided. In one embodiment after deoiling, the spent catalyst is treated with an ammonia leach solution under conditions sufficient to dissolve the group VIB metal and the Group VIII metal into the leaching solution, forming a leach slurry. After solid-liquid separation to recover a leach solution, chemical precipitation and solids repulping is carried out to obtain an effluent stream containing ammonium sulfate (Amsul), ammonium sulfamate, Group VB, Group VIB and Group VIII metals. Following sulfidation, the Group VIII metal is fully removed and Group VB and Group VI metals are partially removed from the Amsul stream. In the additional steps of oxydrolysis and iron precipitation, an effective amount of ferric ion at a pre-select pH is added to form insoluble complexes with the Group VB and Group VIB metals, which upon liquid-solid separation produces an effluent ammonium sulfate stream containing less than 10 ppm each of the Group VB and Group VIB metals.

Process For Separating And Recovering Metals

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US Patent:
20140348729, Nov 27, 2014
Filed:
Aug 6, 2014
Appl. No.:
14/452843
Inventors:
Rahul Shankar BHADURI - Moraga CA, US
Louis Joseph NORDRUM - Corte Madera CA, US
Alexander E. KUPERMAN - Orinda CA, US
Assignee:
CHEVRON U.S.A. INC. - San Ramon CA
International Classification:
C22B 34/34
C22B 3/00
C22B 34/22
US Classification:
423 55
Abstract:
A process for treating spent catalyst containing heavy metals, e.g., Group VIB metals and Group VIII metals is provided. In one embodiment after deoiling, the spent catalyst is treated with an ammonia leach solution under conditions sufficient to dissolve the group VIB metal and the Group VIII metal into the leaching solution, forming a leach slurry. After solid-liquid separation to recover a leach solution, chemical precipitation and solids repulping is carried out to obtain an effluent stream containing ammonium sulfate (Amsul), ammonium sulfamate, Group VB, Group VIB and Group VIII metals. Following sulfidation, the Group VIII metal is fully removed and Group VB and Group VI metals are partially removed from the Amsul stream. In the additional steps of oxydrolysis and iron precipitation, an effective amount of ferric ion at a pre-select pH is added to form insoluble complexes with the Group VB and Group VIB metals, which upon liquid-solid separation produces an effluent ammonium sulfate stream containing less than 10 ppm each of the Group VB and Group VIB metals.
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Louis J Nordrum from American Canyon, CA Get Report