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Andrew J Novotny

from Cassopolis, MI
Age ~39

Andrew Novotny Phones & Addresses

  • 23210 Kelsey Lake St, Cassopolis, MI 49031 (269) 362-7291
  • 23308 Kelsey Lake St, Cassopolis, MI 49031 (269) 782-3950
  • 56641 Glenwood Rd, Cassopolis, MI 49031 (269) 782-1799
  • Glen Ellyn, IL
  • Lombard, IL
  • Chicago, IL
  • Denver, CO

Work

Company: Wilton tent sale - Woodridge, IL May 2014 Position: Cashier

Education

School / High School: Downers Grove South Highschool- Downers Grove, IL 2010 Specialities: High School Diploma

Skills

Several years of Technical Computer and ... • attended a year of culinary classes • attended a year and a half of fitness an... • attended a half a year of graphic design • web design • and 3D design & animation classes • possesses knowledge of use of cash regis... • possesses high levels of both patience a... • quick to fully grasp new tasks • responsibilities • and technology.

Resumes

Resumes

Andrew Novotny Photo 1

Andrew Paul Novotny Woodridge, IL

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Work:
Wilton Tent Sale
Woodridge, IL
May 2014 to Jun 2014
Cashier

Wilton Tent Sale
Woodridge, IL
May 2013 to Jun 2013
Cashier

Education:
Downers Grove South Highschool
Downers Grove, IL
2010 to 2014
High School Diploma

Skills:
Several years of Technical Computer and Mobile Phone knowledge, attended a year of culinary classes, attended a year and a half of fitness and weight training classes, attended a half a year of graphic design, web design, and 3D design & animation classes, possesses knowledge of use of cash registers, possesses high levels of both patience and endurance, quick to fully grasp new tasks, responsibilities, and technology.

Publications

Us Patents

Methods For Reducing Flue Gas Emissions From Fluid Catalytic Cracking Unit Regenerators

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US Patent:
20170204338, Jul 20, 2017
Filed:
Mar 29, 2017
Appl. No.:
15/473162
Inventors:
- Des Plaines IL, US
Stanley Joseph Frey - Palatine IL, US
Patrick D. Walker - Park Ridge IL, US
Andrew R. Novotny - Chicago IL, US
International Classification:
C10G 11/18
Abstract:
Methods for reducing flue gas particulate emissions from fluid catalytic cracking unit regenerators are provided. In one embodiment, a method for reducing flue gas particulate emissions from an FCC unit regenerator includes the steps of combining biochar with a hydrocarbon feedstock to generate a biochar-containing feedstock and contacting the biochar-containing feedstock with an FCC catalyst. In another embodiment, a method for reducing flue gas particulate emissions from a FCC unit regenerator includes the steps of fluidizing catalyst fines and biochar particles in a fluidizing gas and adhering a portion of the catalyst fines to the biochar particles while in the fluidizing gas.

Processes For Minimizing Catalyst Fines In A Regenerator Flue Gas Stream

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US Patent:
20160312127, Oct 27, 2016
Filed:
Apr 22, 2015
Appl. No.:
14/693644
Inventors:
- Des Plaines IL, US
Derek Froehle - Wheeling IL, US
Andrew R. Novotny - Chicago IL, US
International Classification:
C10G 11/00
Abstract:
Process for minimizing the amount of catalyst fines in a flue gas from a catalyst regenerator. Pyrolysis oil is injected into the reaction zone, preferably downstream from the feedstream inlet. The catalyst fines will be passed along with the hydrocarbon effluent stream and can be removed with a filter or other similar device. The amount of pyrolysis oil can be controlled, for example, based upon the opacity of the flue gas from the catalyst regenerator, or based upon the amount of catalyst injected into the reaction zone.

Apparatuses And Methods For Fluid Catalytic Cracking With Limited Particulate Emissions

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US Patent:
20160090538, Mar 31, 2016
Filed:
Sep 29, 2014
Appl. No.:
14/499639
Inventors:
- Des Plaines IL, US
Patrick D. Walker - Park Ridge IL, US
Andrew R. Novotny - Chicago IL, US
Stanley Joseph Frey - Palatine IL, US
International Classification:
C10G 11/05
C10G 3/00
C10G 55/06
Abstract:
Methods and apparatuses are provided for cracking a hydrocarbon. The method includes contacting a first hydrocarbon stream with a cracking catalyst in a riser. The cracking catalyst is regenerated in a regenerator to produce a flue gas stream having a particulate concentration, where the flue gas stream is vented. A second stream is contacted with the cracking catalyst in the riser while the first hydrocarbon stream is contacted with the catalyst, where the second stream includes a natural oil. The particulate concentration is a second particulate concentration while the second stream contacts the cracking catalyst, and a first particulate concentration prior to the second stream contacting the cracking catalyst. The first particulate concentration is greater than the second particulate concentration.
Andrew J Novotny from Cassopolis, MI, age ~39 Get Report