Robert S Nebergall from Overland Park, KS, age 60

Resumes

General Sales Manager

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Location:

14742 Outlook St, Overland Park, KS 66223

Industry:

Chemicals

Work:

Clarimex
General Sales Manager
Power Utilities Chemical Petro-Chemical 1988 - 2018
Sales and Marketing Manager | Business Development
Babcock & Wilcox 2016 - 2017
Business Development Manager, Industrial
Babcock & Wilcox Nov 2014 - 2016
General Sales Manager, Central Region
Cabot Corporation 2013 - 2014
Application Support and New Business Development Manager, South America

Education:

Lewis University 1992 - 1995
Master of Business Administration, Masters, Marketing Drake University 1980 - 1985
Bachelors, Bachelor of Arts, Chemistry Valley High School

Skills:

Global Business Development
Business Development
Contract Negotiation
Sales Management
International Sales
Spanish
Utility Industry
Marketing Strategy
Direct Sales
Mercury
Chemistry
Chemical Industry
Food Industry
Edible Oil
Product Development
Mergers and Acquisitions
Process Engineering
Chemical Engineering
Water Treatment
R&D
Polymers
Manufacturing
Energy
Wastewater Treatment
Process Optimization
Engineering
Project Management
New Business Development
Strategic Planning
Research and Development

Languages:

Spanish
English

Publications

Us Patents

Process For Regenerating Spent Acid-Activated Bentonite Clays And Smectite Catalysts

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US Patent:

53589157, Oct 25, 1994

Filed:

Feb 12, 1993

Appl. No.:

8/017382

Inventors:

Robert S. Nebergall - Lombard IL
Dennis R. Taylor - Palatine IL
Carolyn J. Kucharz - Chicago IL

Assignee:

American Colloid Company - Arlington Heights IL

International Classification:

B01J 2034
B01J 3860
B01J 3864
C11B 310

US Classification:

502 27

Abstract:

A three step process for regenerating spent bleaching clays and acid-activated smectite catalyst granules includes: (1) an extraction step to remove a majority of entrained oil, preferably about 75% to about 95% by weight of the entrained oil, when regenerating bleaching clays; (2) an oxidation step to remove the majority of remaining carbonaceous adsorbates which are not removed by the preceding extraction step, and (3) an acid wash step to restore the acidity normally associated with fresh acid-activated bleaching clays. The features of steps 2 and 3 may be combined into a single step by using an appropriate oxidant, for example, a source of acidic protons, such as peracetic acid.