WILLIAM MARTIN CAMPBELL
Engineers in Houston, TX
License number
Pennsylvania PE011713E
Category
Engineers
Type
Professional Engineer
Address
Address
2
Houston, TX 77210
Pennsylvania
Pennsylvania
Personal information
See more information about WILLIAM MARTIN CAMPBELL at radaris.comName
Address
Phone
50 Oak Villa Rd, Canyon Lake, TX 78133
506 S Austin St APT 96, Webster, TX 77598
5100 Lebanon Ave APT 1103, Philadelphia, PA 19131
506 Forest Edge Ln, Red Oak, TX 75154
5025 Raleigh Dr, Beaumont, TX 77706
Professional information
William Campbell - Houston, TX
Work:
St. Hope Foundation, Inc
Leader and team member in this St. Hope Foundation, Inc
Prevention Development Director The Warren Corporation - Houston, TX
Program Administrator Donald R. Watkins Memorial Foundation - Houston, TX
Program Coordinator
Leader and team member in this St. Hope Foundation, Inc
Prevention Development Director The Warren Corporation - Houston, TX
Program Administrator Donald R. Watkins Memorial Foundation - Houston, TX
Program Coordinator
Education:
Texas State University
BBA in Accounting
BBA in Accounting
President At Action Engineering And Inspection Services, Llc
Position:
President at Action Engineering And inspection Services, LLC
Location:
Houston, Texas Area
Industry:
Civil Engineering
Work:
Action Engineering And inspection Services, LLC
-
President
William Clay Campbell, Houston TX - Lawyer
Address:
The Structure Group
1655 Castle Ct, Houston 77006
(713) 854-8765
1655 Castle Ct, Houston 77006
(713) 854-8765
Licenses:
Texas - Eligible To Practice In Texas 2001
Education:
Pepperdine School of LawDegree Doctor of Jurisprudence/Juris Doctor (J.D.)Graduated 2001
Fluid Bed Desulfurization
US Patent:
5447702, Sep 5, 1995
Filed:
Mar 4, 1994
Appl. No.:
8/206569
Inventors:
William M. Campbell - Houston TX
Gunnar B. Henningsen - Sugar Land TX
Gunnar B. Henningsen - Sugar Land TX
Assignee:
The M. W. Kellogg Company - Houston TX
International Classification:
C10K 126, B01D 5352
US Classification:
423230
Abstract:
A method and apparatus for desulfurizing a gas and regenerating a sorbent is disclosed. The sulfur-containing feed gas which can be an effluent gas from a coal gasification reactor, for example, is desulfurized with a particulated metallic oxide sorbent in a transport riser. The sulfided sorbent is than separated from a desulfurized effluent gas and regenerated by contact with an oxygen-containing gas in a transport riser. The regenerated sorbent is separated from an SO. sub. 2 containing offgas and recycled to the desulfurization step. The degree of sorbent conversion in the desulfurization step is held at a low level and the sorbent regeneration rate is increased to avoid excessive temperature rise in the regeneration step. In such manner, sorbent cooling can be substantially eliminated. The regeneration riser preferably comprises a once-through lift riser to minimize the riser transport gas requirements to just oxidant gas or oxidant gas mixed with a reduced amount of diluent gas.
Fluid Bed Desulfurization
US Patent:
5578093, Nov 26, 1996
Filed:
Jun 5, 1995
Appl. No.:
8/463442
Inventors:
William M. Campbell - Houston TX
Gunnar B. Henningsen - Sugar Land TX
Gunnar B. Henningsen - Sugar Land TX
Assignee:
The M. W. Kellogg Company - Houston TX
International Classification:
C10K 126, B01D 5352
US Classification:
48128
Abstract:
A method and apparatus for desulfurizing a gas and regenerating a sorbent is disclosed. The sulfur-containing feed gas which can be an effluent gas from a coal gasification reactor, for example, is desulfurized with a particulated metallic oxide sorbent in a transport riser. The sulfided sorbent is than separated from a desulfurized effluent gas and regenerated by contact with an oxygen-containing gas in a transport riser. The regenerated sorbent is separated from an SO. sub. 2 containing offgas and recycled to the desulfurization step. The degree of sorbent conversion in the desulfurization step is held at a low level and the sorbent regeneration rate is increased to avoid excessive temperature rise in the regeneration step. In such manner, sorbent cooling can be substantially eliminated. The regeneration riser preferably comprises a once-through lift riser to minimize the riser transport gas requirements to just oxidant gas or oxidant gas mixed with a reduced amount of diluent gas.