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David G Flanigan, 411100 Pine Pl UNIT 214, Miami, OK 74354

David Flanigan Phones & Addresses

Miami, OK   

Tulsa, OK   

203 N West Ave, Afton, OK 74331   

Bernice, OK   

Peggs, OK   

Locust Grove, OK   

2141 N Birmingham Pl, Tulsa, OK 74110   

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Career records & work history

Medicine Doctors

David C. Flanigan

Specialties:
Orthopedic Sports Medicine, Orthopaedic Surgery
Work:
OSU Sports Medicine
2050 Kenny Rd STE 3100, Columbus, OH 43221
614-2933600 (phone) 614-2934399 (fax)
Education:
Medical School
University of Iowa Carver College of Medicine
Graduated: 1998
Procedures:
Arthrocentesis, Hallux Valgus Repair, Hip/Femur Fractures and Dislocations, Joint Arthroscopy, Knee Arthroscopy, Lower Leg Amputation, Lower Leg/Ankle Fractures and Dislocations, Shoulder Arthroscopy, Wound Care
Conditions:
Appendicitis, Breast Disorders, Cholelethiasis or Cholecystitis, Fractures, Dislocations, Derangement, and Sprains, Inguinal Hernia, Internal Derangement of Knee, Internal Derangement of Knee Cartilage, Internal Derangement of Knee Ligaments, Intervertebral Disc Degeneration, Lateral Epicondylitis, Osteoarthritis, Overweight and Obesity, Plantar Fascitis, Rheumatoid Arthritis, Rotator Cuff Syndrome and Allied Disorders, Systemic Lupus Erythematosus, Ventral Hernia
Languages:
English, Spanish
Description:
Dr. Flanigan graduated from the University of Iowa Carver College of Medicine in 1998. He works in Columbus, OH and specializes in Orthopedic Sports Medicine and Orthopaedic Surgery. Dr. Flanigan is affiliated with Ohio State University Wexner Medical Center.

David Flanigan resumes & CV records

Resumes

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David Flanigan

Location:
United States

Publications & IP owners

Us Patents

Process For Cleaning Particulate Solids

US Patent:
5080721, Jan 14, 1992
Filed:
Feb 28, 1990
Appl. No.:
7/487350
Inventors:
David A. Flanigan - Cleveland OK
Robert E. Williams - Houston TX
Assignee:
Conoco Inc. - Ponca City OK
International Classification:
B08B 310
US Classification:
134 26
Abstract:
A system for cleaning solids contaminated with solvent-soluble contaminants. The system, which includes both process and apparatus, comprises the use of at least two successive cleaning zones, each of which includes a slurrying stage and a centrifuge separation stage, wherein the solids to be cleaned and the solvent used for cleaning flow in countercurrent relationship to each other between the successive zones.

Apparatus For Cleaning Particulate Solids

US Patent:
5107874, Apr 28, 1992
Filed:
Aug 29, 1991
Appl. No.:
7/751917
Inventors:
David A. Flanigan - Cleveland OK
Robert E. Williams - Houston TX
Assignee:
Conoco Inc. - Ponca City OK
International Classification:
E21B 2106
US Classification:
134 60
Abstract:
A system for cleaning solids contaminated with solvent-soluble contaminants. The system comprises the use of at least two successive cleaning zones, each of which includes a slurry stage and a centrifuge separation stage, wherein the solids to be cleaned and the solvent used for cleaning flow in countercurrent relationship to each other between the successive zones.

Process And Apparatus For Cleaning Particulate Solids

US Patent:
5053082, Oct 1, 1991
Filed:
Feb 28, 1991
Appl. No.:
7/487351
Inventors:
David A. Flanigan - Cleveland OK
Joe K. Heilhecker - Houston TX
Robert E. Williams - Houston TX
Assignee:
Conoco Inc. - Ponca City OK
International Classification:
B08B 308
B08B 1300
US Classification:
134 251
Abstract:
A system for cleaning solids contaminated with solvent-soluble contaminants. The system, which includes both process and apparatus, comprises slurrying of the solids with a solvent, feeding the slurry to a cyclone separation zone integrally connected to a countercurrent extraction zone, separating the slurry into an overflow stream which includes solvent and fine particles of solids and an underflow stream which includes mostly coarse particles of solids in the cyclone separation zone, processing the overflow stream in a cleaning zone with additional solvent, processing the underflow stream in countercurrent relationship with additional solvent through the countercurrent extraction zone, combining the cleaned coarse particles of solids withdrawn from the extraction zone with the cleaned fine particles of solids withdrawn from the cleaning zone and centrifuging the combined cleaned particles to remove residual solvent and recovering the combined solids having reduced contamination for disposal.

Low Pressure Hydrocyclone Separator

US Patent:
4900445, Feb 13, 1990
Filed:
Feb 22, 1989
Appl. No.:
7/314609
Inventors:
David A. Flanigan - Cleveland OK
Elwyn Shimoda - Ponca City OK
James E. Stolhand - Ponca City OK
Assignee:
Conoco Inc. - Ponca City OK
International Classification:
B01D 4512
US Classification:
2105121
Abstract:
A system is provided for the separation of oil from oily water, particularly where the oily water is available only at relatively low pressures insufficient ot drive a hydrocyclone separator. Particular combinations of pumps and hydrocyclones can be effective in these low pressure situations where the pressure boost required is not substantially greater than a differential pressure at which the pump begins to substantially degrade the volumetric mean size of droplets of oil in the oily water passing therethrough. This is achieved by operating the pump at relatively near its maximum flow rate capacity to substantially reduce on a percentage basis the effect of fluid slippage within the pump. Improved techniques for analysis of oil droplet size distribution are also disclosed.

Method And Apparatus For Reduction Of Particle Disintegration

US Patent:
5151079, Sep 29, 1992
Filed:
Sep 27, 1990
Appl. No.:
7/589720
Inventors:
David A. Flanigan - Cleveland OK
John D. Boadway - Kingston, CA
Assignee:
Conoco Specialty Products Inc. - Houston TX
International Classification:
B04B 1100
B04B 120
US Classification:
494 27
Abstract:
This invention relates to an improved particulate receiving chamber within a centrifugal separation device and more particularly within a decanter centrifuge. The improved receiving chamber reduces particle disintegration of the particulates which is particularly advantageous if the particulates are subjected to a further centrifugal separation step because particle disintegration compromises the clarification achievable by successive centrifugal separators. The preferred embodiment of the particulate receiving chamber includes a plurality of spray nozzles for spraying fluid in the chamber whereby the fluid absorbs the impact forces of the particulates which impact against surfaces within the chamber.

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