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David Milks, 76440 Highway 332, Richwood, TX 77566

David Milks Phones & Addresses

440 Highway 332, Lake Jackson, TX 77566    979-2974020   

Richwood, TX   

1425 Virginia St, Charleston, WV 25301    304-3470017   

1216 Paula Rd, Charleston, WV 25314    304-3454716   

Brazoria, TX   

PO Box 3695, Lake Jackson, TX 77566   

Work

Position: Production Occupations

Mentions for David Milks

Publications & IP owners

Us Patents

Control Acr Product Yields By Adjustment Of Severity Variables

US Patent:
4952745, Aug 28, 1990
Filed:
May 4, 1988
Appl. No.:
7/190114
Inventors:
Cyril Tellis - Charleston WV
Saburo Hori - Iwaki, JP
David Milks - Charleston WV
Assignee:
Union Carbide Chemicals and Plastics Company Inc. - Danbury CT
International Classification:
C07C 404
US Classification:
585648
Abstract:
Improved operation of the ACR process is achieved by regulating the reactions within a small area in the combustion feedstock mixing zone, "Scorch Zone", by the addition of steam or other fluid such as ethane at the point of feed injection.

Process For The Thermal Cracking Of Hydrocarbons

US Patent:
4136015, Jan 23, 1979
Filed:
Jun 7, 1977
Appl. No.:
5/804227
Inventors:
Gerard R. Kamm - South Charleston WV
David Milks - Charleston WV
James D. Kearns - Charleston WV
Herbert I. Britt - Charleston WV
Cyrus R. Khavarian - South Charleston WV
Assignee:
Union Carbide Corporation - New York NY
International Classification:
C10G 938
US Classification:
208129
Abstract:
In a process for the thermal cracking of hydrocarbons by the introduction of liquid petroleum feedstock in atomized form into a stream of hot combustion products formed by the combustion of fuel and oxidant in successive burner and mixing zone, constricting throat zone, a velocity acceleration diffuser zone and secondary cracking and reaction zone along the path of hot combustion product stream flow, an improvement is disclosed which comprises: effecting initial mixing, vaporization and cracking of said atomized liquid petroleum feedstock in said stream of hot combustion products in said burner and mixing zone maintained at subsonic velocity flow; effecting substantially complete mixing and vaporization in said constricting throat zone wherein said stream is maintained, at exit, at sonic velocity flow; passing said stream through a velocity acceleration diffuser zone maintained at supersonic velocity flow; passing said stream through a shock region produced by cross-sectional expansion of a diffuser zone; and effecting a final thermal cracking conversion in said stream in a subsonic velocity additional cracking reaction zone before quenching of said stream.

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