Michael Mcgaugh resumes & CV records
Resumes
Michael Mcgaugh
Location:
3006 Toboggan Run, Midland, MI 48642
Industry:
Chemicals
Michael Calvin Mcgaugh, 85811 Shady Ln, Angleton, TX 77515
Michael Mcgaugh Phones & Addresses
811 Shady Ln, Angleton, TX 77515 979-8498719
215 Bronco Bend St, Angleton, TX 77515 979-8494879
1229 Walcik St, Angleton, TX 77515 979-8498719
San Marcos, TX
Midland, MI
Sanford, MI
Brazoria, TX
Roswell, GA
PO Box 1965, Midland, MI 48641 989-8371514
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Michael Calvin Mcgaugh
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Chemicals
Mentions for Michael Calvin Mcgaugh
Publications & IP owners
Us Patents
Continuous Process For The Removal Of Hydrogen Sulfide From A Gaseous Stream
US Patent:
4765873, Aug 23, 1988
Filed:
Dec 6, 1985
Appl. No.:
6/805671
Inventors:
Dane Chang - Houston TX
Michael C. McGaugh - Angleton TX
Michael C. McGaugh - Angleton TX
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
C01B 1716
C01B 1702
C25B 100
C25B 102
C01B 1702
C25B 100
C25B 102
US Classification:
204101
Abstract:
A process for removing hydrogen sulfide from a gaseous stream containing hydrogen sulfide by contacting said stream with an aqueous solution of ammonium hydroxide to produce ammonium sulfide; converting said ammonium sulfide to an ammonium polysulfide intermediate in an electrolytic cell at ambient temperature and pressure; and oxidizing said ammonium polysulfide to sulfur in a heating zone utilizing an oxygen containing gas sparge.
Continuous Process For Scrubbing Hydrogen Sulfide To Produce Elemental Sulfur
US Patent:
4765969, Aug 23, 1988
Filed:
Jan 15, 1987
Appl. No.:
7/003884
Inventors:
Dane Chang - Houston TX
Michael C. McGaugh - Angleton TX
Michael C. McGaugh - Angleton TX
Assignee:
The Dow Chemical Company - Midland MI
International Classification:
B01D 5334
C01B 1705
C01B 1705
US Classification:
423573R
Abstract:
A continuous process for removing hydrogen sulfide from a gas stream by contacting the gas stream with a solution of ammonium hydroxide to produce an effluent liquid stream comprising ammonium sulfide which is fed to a heating zone maintained at least at the boiling temperature of said solution and supplied with an oxygen containing gas sparge wherein ammonia and hydrogen sulfide are removed from said zone as vapor and sulfur is removed from said zone as an aqueous dispersion, the sulfur being separated in a filtration zone from the residual aqueous liquid which is recycled back to a contact zone together with said ammonia and said hydrogen sulfide vapor.
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