Search

Steven George Calderone

from Santa Barbara, CA
Age ~64
Get Report
Also known as:
Steven G Calderone, Steve George Calderone, Steve G Calderone, Steve Caldera
Related to:
Jody Joe Thompson, 53Nicholas Calderone, 34Susan C Calderone, 64James D Calderone, 58Casey M Gorman, 41Kenneth M Calderone, 35Arlene M Calderone, 59Magda S Calderone, 66Kenneth Calderone, 81Casey D Craig, 48Philip A Calderone, 60
Connected to:
Adam Calderon, 73Adelaida Calderon, 75Alexandria Calderon, 31Alison Calderon, 47Alonzo M Calderon, 61Amelia Calderon, 102Anastasio R Calderon, 48Andrew R Calderon, 46Andrey Calderon, 36Angelique Calderon, 32

Steven Calderone Phones & Addresses

  • Santa Barbara, CA
  • Lombard, IL
  • Novi, MI
  • Crystal Lake, IL
  • Campbell, CA
  • Oak Park, IL
  • Felch, MI
  • Chicago, IL
  • Palatine, IL
  • Elk Grove Village, IL
  • Mount Prospect, IL
  • Rolling Meadows, IL
  • Marquette, MI

Resumes

Resumes

Steven Calderone Photo 1

Steven Calderone

View page
Location:
United States

Publications

Us Patents

Oil Recovery From Dry Corn Milling Ethanol Production Processes

View page
US Patent:
20080176298, Jul 24, 2008
Filed:
Nov 13, 2007
Appl. No.:
11/939191
Inventors:
Sarabjit S. Randhava - Evanston IL, US
Richard L. Kao - Northbrook IL, US
Steven G. Calderone - Oak Park IL, US
Ajaib S. Randhava - Streamwood IL, US
International Classification:
C12P 7/64
C12M 1/00
US Classification:
435134, 4352911
Abstract:
A corn oil extraction process is disclosed. The process includes the recovery of corn oil and other co-products, including but not limited to steam, electric power and chemicals, from an ethanol production process and in particular, a process that involves dry corn milling methods. The process involves extraction of oil from milled corn and residues from the fermentation step, including thick stillage, distillers wet grain, distillers dry grain and distillers dry grains with solubles, by the application of an alkyl acetate, phase separation and recovery of the separated matter. A process of drying wet co-product using ethanol and carbon dioxide from the production facility is also disclosed.

Dynamic Fuel Processor With Controlled Declining Temperatures

View page
US Patent:
20030188475, Oct 9, 2003
Filed:
Mar 29, 2002
Appl. No.:
10/112684
Inventors:
Shabbir Ahmed - Naperville IL, US
Sheldon Lee - Willowbrook IL, US
Steven Calderone - Arlington Heights IL, US
Richard Kao - Northbrook IL, US
Elias Camara - Clarendon Hills IL, US
Steven Lottes - Naperville IL, US
Michael Krumpelt - Naperville IL, US
Todd Harvey - Arlington Heights IL, US
International Classification:
B01J008/04
US Classification:
044/639000
Abstract:
A dynamic, compact, lightweight fuel processor that is capable of converting carbonaceous fuels to hydrogen rich gases suitable for all types of fuel cells or chemical processing applications. The fuel processor and process are based on the autothermal hydrodesulfurizing reforming reaction, followed by clean up of byproduct sulfur-containing gases and carbon monoxide that poison the fuel cell electrocatalyst. The fuel processor uses proprietary catalysts and hardware designs that enable the conversion in an energy efficient manner while maintaining desirable performance characteristics such as rapid start-stop and fast response to load change capabilities.

Processes And Control Systems For High Efficiency Anaerobic Conversion Of Hydrogren And Carobon Oxides To Alcohols

View page
US Patent:
20170088864, Mar 30, 2017
Filed:
Dec 13, 2016
Appl. No.:
15/377654
Inventors:
- Warrenville IL, US
STEVEN G. CALDERONE - CHICAGO IL, US
JIANXIN DU - NAPERVILLE IL, US
ROBERT HICKEY - OKEMOS MI, US
RICHARD E. TOBEY - ST. CHARLES IL, US
International Classification:
C12P 7/16
C12P 7/04
C12P 7/06
Abstract:
High conversion efficiency processes are disclosed for the anaerobic bioconversion of syngas to alcohol. The processes use bioreactors that have a non-uniform gas composition and a substantially uniform liquid composition such as deep tank bioreactors. By maintaining certain electron to carbon mole ratios in the syngas feed to the bioreactors and certain partial pressures of carbon dioxide in the off gas from the bioreactors, at least about 80 percent of the hydrogen and at least about 95 percent of the carbon monoxide in the feed can be consumed.

Integrated Processes For Anaerobic Conversion Of Hydrogen And Carbon Oxides To Alcohol

View page
US Patent:
20140227751, Aug 14, 2014
Filed:
Feb 7, 2014
Appl. No.:
14/175905
Inventors:
Rathin Datta - Chicago IL, US
Steven G. Calderone - Chicago IL, US
Jianxin Du - Naperville IL, US
Robert Hickey - Okemos MI, US
International Classification:
C12P 7/04
US Classification:
435157
Abstract:
Integrated processes are disclosed for the anaerobic bioconversion of syngas to alcohol.

Processes And Control Systems For High Efficiency Anaerobic Conversion Of Hydrogen And Carbon Oxides To Alcohols

View page
US Patent:
20140227752, Aug 14, 2014
Filed:
Feb 7, 2014
Appl. No.:
14/175928
Inventors:
Rathin Datta - Chicago IL, US
Steven G. Calderone - Chicago IL, US
Jianxin Du - Naperville IL, US
Robert Hickey - Okemos MI, US
Richard E. Tobey - St. Charles IL, US
International Classification:
C12P 7/16
C12P 7/04
C12P 7/06
US Classification:
435160, 435161, 435157
Abstract:
High conversion efficiency processes are disclosed for the anaerobic bioconversion of syngas to alcohol. The processes use bioreactors that have a non-uniform gas composition and a substantially uniform liquid composition such as deep tank bioreactors. By maintaining certain electron to carbon mole ratios in the syngas feed to the bioreactors and certain partial pressures of carbon dioxide in the off gas from the bioreactors, at least about 80 percent of the hydrogen and at least about 95 percent of the carbon monoxide in the feed can be consumed.

Integrated Processes For Anaerobic Conversion Of Hydrogen And Carbon Oxides To Alcohol

View page
US Patent:
20140227753, Aug 14, 2014
Filed:
Feb 7, 2014
Appl. No.:
14/176035
Inventors:
Rathin Datta - Chicago IL, US
Steven G. Calderone - Chicago IL, US
Jianxin Du - Naperville IL, US
Robert Hickey - Okemos MI, US
International Classification:
C12P 7/08
C12P 7/04
C12P 7/16
US Classification:
435160, 435163, 435157
Abstract:
Integrated processes are disclosed for the anaerobic bioconversion of syngas to alcohol wherein a gas substrate of carbon monoxide, hydrogen and carbon dioxide is in contact with an aqueous menstruum that continuously contacts the gas substrate with said aqueous menstruum to produce alcohol and a depleted gas phase that is continuously withdrawn from the aqueous menstruum; continuously or intermittently and the gas substrate is made up of at least two gases having different compositions to provide an overall gas substrate having a ratio of electrons to carbon atoms in the range of about 5.2:1 to 6.8:1.
Control profile
Steven George Calderone from Santa Barbara, CA, age ~64 Get Report