Michael Whittier resumes & CV records
Resumes
Michael Whittier
Skills:
Microsoft Office, Management
Michael C Whittier, 51W300S10418 Lakeside Dr, Mukwonago, WI 53149
Michael Whittier Phones & Addresses
W300S10418 Lakeside Dr, Mukwonago, WI 53149
S73W26260 Sierra Madre Ct, Waukesha, WI 53189 262-6624239
Vernon, WI
17604 70Th St, Shawnee, KS 66217 913-2686728
1764 70Th St, Lake Quivira, KS 66217 913-2686725
Milwaukee, WI
S73W26260 Sierra Madre Ct, Waukesha, WI 53189 262-6624239
Education
Degree:
Associate degree or higher
Mentions for Michael C Whittier
Publications & IP owners
Us Patents
Moving Bed Biofilm Reactor Media
US Patent:
D645116, Sep 13, 2011
Filed:
Sep 28, 2010
Appl. No.:
29/375844
Inventors:
Colin McKean - Wauwatosa WI, US
Todd Schwingle - Mukwonago WI, US
Michael Casey Whittier - Waukesha WI, US
Todd Schwingle - Mukwonago WI, US
Michael Casey Whittier - Waukesha WI, US
Assignee:
Siemens Industry, Inc. - Alpharetta GA
International Classification:
2301
US Classification:
D23207
Moving Bed Biofilm Reactor Media
US Patent:
D648821, Nov 15, 2011
Filed:
Sep 28, 2010
Appl. No.:
29/375846
Inventors:
Colin McKean - Wauwatosa WI, US
Todd Schwingle - Mukwonago WI, US
Michael Casey Whittier - Waukesha WI, US
Todd Schwingle - Mukwonago WI, US
Michael Casey Whittier - Waukesha WI, US
Assignee:
Siemens Industry, Inc. - Alpharetta GA
International Classification:
2301
US Classification:
D23207
Ballasted Solids Treatment System And Method
US Patent:
2019019, Jun 27, 2019
Filed:
Jun 7, 2017
Appl. No.:
16/307671
Inventors:
- Pittsburgh PA, US
Michael Casey Whittier - Vernon WI, US
Michael Casey Whittier - Vernon WI, US
International Classification:
C02F 9/00
Abstract:
Disclosed are apparatus and methods for treating wastewater. In one example a system for treating wastewater treatment is provided. The system comprises a biological reactor having an inlet in fluid communication with a source of wastewater and an outlet, the biological reactor configured to treat wastewater from the source of wastewater and output a biologically treated wastewater from the outlet, a solids-liquid separation system having an inlet in fluid communication with the outlet of the biological reactor and configured to separate the biologically treated wastewater into a solids-lean effluent and a solids-rich waste activated sludge (WAS), a treatment subsystem comprising a digester, an inlet in fluid communication with a WAS outlet of the solids-liquid separation system, and an outlet for providing ballasted and digested WAS, and a ballast feed system configured to deliver ballast to one of the biological reactor and the treatment subsystem.
Treatment Using Fixed Film Processes And Ballasted Settling
US Patent:
2015021, Jul 30, 2015
Filed:
Mar 15, 2013
Appl. No.:
14/405175
Inventors:
Todd SCHWINGLE - , US
Timothy LINDEMANN - Jefferson WI, US
Michael Casey WHITTIER - Waukesha WI, US
Steven E. WOODARD - Cumberland ME, US
Nathan ANTONNEAU - Wauwatosa WI, US
Andrew G. BISHOP - Windham ME, US
Robert BACKMAN - Wayland MA, US
- Warrendale PA, US
Timothy LINDEMANN - Jefferson WI, US
Michael Casey WHITTIER - Waukesha WI, US
Steven E. WOODARD - Cumberland ME, US
Nathan ANTONNEAU - Wauwatosa WI, US
Andrew G. BISHOP - Windham ME, US
Robert BACKMAN - Wayland MA, US
- Warrendale PA, US
International Classification:
C02F 3/04
B01D 21/01
B01D 21/01
Abstract:
A system and method is provided for water and wastewater treatment. The system comprises a fixed film biological process and a ballasted flocculation process.
Using Continuous Nitrate Measurement To Control Aeration In An Aerated-Anoxic Process
US Patent:
2014031, Oct 30, 2014
Filed:
Nov 16, 2012
Appl. No.:
14/357595
Inventors:
- Alpharetta GA, US
Michael Casey Whittier - Waukesha WI, US
Michael Casey Whittier - Waukesha WI, US
International Classification:
C02F 3/30
US Classification:
210614, 210 961
Abstract:
A method and system for treating wastewater is disclosed. In one embodiment the method includes introducing the wastewater into an aerated anoxic treatment unit, flowing an oxygen containing gas into the wastewater in the aerated anoxic treatment unit at a first flow rate, measuring a concentration of a nitrogen species in the wastewater in the aerated anoxic treatment unit, comparing the measured concentration of the nitrogen species to a target nitrogen species concentration, adjusting the flow of the oxygen containing gas into the wastewater in the aerated anoxic treatment unit to a second flow rate in response to a difference in the nitrogen species and the target nitrogen species concentrations, and maintaining the second flow rate for a time period sufficient for the wastewater to be treated in the aerated anoxic treatment unit and form an anoxically treated liquid having a reduced concentration of the nitrogen species.
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