George Swan

In the United States, there are 470 individuals named George Swan spread across 46 states, with the largest populations residing in Florida, California, New Jersey.

Public information about George Swan

Resumes

Software Engineer

Location:

Orlando, FL

Industry:

Computer Software

Work:

Perceptive Technologies, Inc. Jan 2005 - Oct 2008
Manager of Software Solutions Comsys Jan 2005 - Oct 2008
Software Engineer

Education:

Florida Metropolitan University 2003 - 2004
Master of Business Administration, Masters, Management Florida State University - College of Business 1995 - 2000
Bachelors, Bachelor of Science, Management

Managing Director

Location:

Detroit, MI

Industry:

Non-Profit Organization Management

Work:

G W Swan Group
Managing Director

George Swan

Location:

San Francisco Bay Area

Industry:

Computer Software

George Swan

Work:

North Carolina A&T State University
Associate Professor

Sales Engineer

Location:

Charleston, SC

Work:

Bayliss Machine & Welding
Sales Engineer

Education:

Pennsylvania College of Technology

President

Location:

Santa Rosa, CA

Industry:

Construction

Work:

Swan Plumbing
President

Education:

Santa Rosa High School 1984 - 1986

George Swan

Location:

Riverside, CA

Industry:

Building Materials

Work:

Insideout Sales & Marketing
Retired

Owner

Location:

Lake George, MN

Industry:

Business Supplies And Equipment

Work:

Style
Owner

Background search with BeenVerified

Background Search for George Swan

Phone Address Email Family Social Criminal Property Bankruptcy Residence

Data provided by Veripages

Phones & Addresses

Name

Addresses

Phones

George Swan

Fort Worth, TX

817-427-1796

George Swan

Knoxville, TN

865-249-7836

George A. Swan

Biloxi, MS

228-392-3064

George Swan

Apex, NC

919-362-7900

George Swan

Little Chute, WI

920-687-9299

George Bud Swan

Blaine, WA

360-371-2952

George Swan

Danville, CA

925-362-0801

George Swan

Yuma, AZ

928-342-0985

George Swan

284 Hawley St, Pendleton, NY 14094

716-434-0795

George Swan

286 County Road 1241, Vinemont, AL 35179

256-385-5706

George Swan

1382 Cove Rd, Jackson, OH 45640

740-988-2252

George Swan

2912 Vallette St, Bellingham, WA 98225

360-734-7533

George Swan

292 Garfield Ave, Jersey City, NJ 07305

201-538-1020

George Swan

139 Waterford Dr, Jupiter, FL 33458

561-889-2946

George Swan

308 Labarre Rd, New Orleans, LA 70121

504-432-5513

George Swan

320 Smithburg Rd, Gillsburg, MS 39657

601-876-3211

Business Records

Name / Title

Company / Classification

Phones & Addresses

George Swan
Owner

American Waste Services DBA
Services-Misc

21978 Platteview Rd, Gretna, NE 68028
402-334-0964

George Swan
President

SWAN PLUMBING, INC
Plumbing/Heating/Air Cond Contractor · Plumbing

1821 Empire Industrial Ct #F, Santa Rosa, CA 95403
252 Somerville Rd, Santa Rosa, CA 95409
1821 Empire Industrial Ct Ste F, Santa Rosa, CA 95403
707-575-5541, 707-538-5045, 707-538-2784

Mr. George Swan
Owner

American Waste Services LLC
American Waste Service LLC
Waste Reduction. Recycle Service - Industrial

21978 Platteview Rd #100, Gretna, NE 68028
402-334-0964

George Swan
President

Glass House & Supplies, Inc
Glass Repair

804 N Alexander St, Gonzales, LA 70737
804 N Alexander Ave, Gonzales, LA 70737
225-644-3985, 225-647-3465

George Swan
Owner

Corner Collectibles
Gift Shops

201 S Main St, Galena, IL 61036
815-777-8210

George Swan
Owner

Corner Collectibles
Gift Shops

201 S Main St, Galena, IL 61036
815-777-8210

George Swan
President

Detroit Literacy Coalition
School/Educational Services

5057 Woodward Ave, Detroit, MI 48202
313-577-7683

George R. Swan
President

Swan Ranch Co
Beef Cattle-Except Feedlot

70 Silver Spg Rd, Sheridan, MT 59749
PO Box 956, Amsterdam, MT 59741
406-842-5929

Publications

Us Patents

Catalytic Reforming Process

US Patent:

4425222, Jan 10, 1984

Filed:

Apr 6, 1983

Appl. No.:

6/482512

Inventors:

George A. Swan - Baton Rouge LA

Assignee:

Exxon Research and Engineering Co. - Florham Park NJ

International Classification:

C10G 3506

US Classification:

208 65

Abstract:

A process wherein, in a series of reforming zones, or onstream reactors, each of which contains a bed, or beds of catalyst, the catalyst in the leading reforming zones is constituted of supported platinum and a relatively low concentration of rhenium, and the catalyst in the last reforming zone, or reactor of the series, is constituted of platinum and a relatively high concentration of rhenium, and a swing reactor, also containing a supported platinum and rhenium catalyst, is manifolded so that it can be substituted for any one of the onstream reactors of the unit. The entry side, or upper portion of the swing reactor contains a catalyst constituted of platinum and a relatively low concentration of rhenium, and the exit side, or lower portion of the reactor contains a catalyst constituted of platinum and a relatively high concentration of rhenium. The amount of rhenium relative to the platinum on the catalyst in the last reactor and lower portion of the swing reactor is present in a weight ratio of rhenium:platinum of at least 1. 5:1; preferably at least about 2:1, and more preferably ranges from about 2:1 to about 3:1.

Multistage Reforming With Ultra-Low Pressure Cyclic Second Stage

US Patent:

5203988, Apr 20, 1993

Filed:

Aug 19, 1991

Appl. No.:

7/747897

Inventors:

George A. Swan - Baton Rouge LA
James P. Bailor - Kenvil NJ
David W. Staubs - Baton Rouge LA
Eduardo Mon - Baton Rouge LA

Assignee:

Exxon Research & Engineering Company - Florham Park NJ

International Classification:

C10G 3504

US Classification:

208 65

Abstract:

Disclosed is a process for catalytically reforming a gasoline boiling range hydrocarbonaceous feedstock. The reforming is conducted in multiple stages with heavy aromatics removal between the first and second stages.

Superheating Atomizing Steam With Hot Fcc Feed Oil

US Patent:

6352639, Mar 5, 2002

Filed:

Dec 13, 2000

Appl. No.:

09/735779

Inventors:

Jackson I. Ito - Sacramento CA
Leonard Schoenman - Citrus Heights CA
Dean C. Draemel - Kingwood TX
Teh C. Ho - Bridgewater NJ
George A. Swan - Baton Rouge LA

Assignee:

Exxon Research and Engineering Company - Annandale NJ

International Classification:

C10G 1100

US Classification:

208113, 208153, 208157, 239 8

Abstract:

An atomizing gas, such as steam, and a hot fluid comprising a hot liquid to be atomized, are passed under pressure, through separate fluid conduits in a heat exchange means, in which the hot liquid heats the steam to a superheat temperature, by indirect heat exchange. The superheated steam is then injected into the hot fluid, which comprises a two-phase fluid comprising steam and the hot liquid, subsequent to the superheated steam injection. The two-phase fluid is passed through an atomizing means, such as an orifice, into a lower pressure atomizing zone, which causes the steam to expand and atomize the liquid into a spray of liquid droplets. The two-phase fluid is formed before or as a consequence of the superheated steam injection and is preferably steam-continuous when passed through the atomizing means. This process is useful for atomizing a hot feed oil for a fluid cat cracking (FCC) process.

Process For Reforming At Low Severities With High-Activity, High-Yield, Tin Modified Platinum-Iridium Catalysts

US Patent:

5269907, Dec 14, 1993

Filed:

Mar 6, 1992

Appl. No.:

7/847541

Inventors:

William C. Baird - Baton Rouge LA
Joseph P. Boyle - Sarnia, CA
George A. Swan - Baton Rouge LA

Assignee:

Exxon Research and Engineering Co. - Florham Park NJ

International Classification:

C10G 35085

US Classification:

208 65

Abstract:

A process for reforming a naphtha feed at low severities with tin modified platinum-iridium catalysts. In particular, both high selectivity, and high activity are manifested by such catalysts in reforming a naphtha feed at low severities in the lead reactor, or reactors, of a series of reactors; i. e. , within the dehydrogenation and ring isomerization zone, or zones, of a reforming unit. The lead reactors of the series are charged with a tin-containing platinum-iridium catalyst, and the naphtha feed reformed to produce a low RON clear C. sub. 5 + liquid reformate. The low octane product of the lead reactors may be transferred to a mogas pool, into blending components, or all or some part of the product further reformed. Preferably, the product is further reformed in a tail reactor, and preferably the tail reactor is charged with a non-tin containing platinum, or platinum-iridium catalyst.

Fixed-Bed/Moving-Bed Two Stage Catalytic Reforming With Interstage Aromatics Removal

US Patent:

5211838, May 18, 1993

Filed:

Dec 9, 1991

Appl. No.:

7/805334

Inventors:

Stuart S. Goldstein - Ewell, GB2
Paul W. Kamienski - Basking Ridge NJ
Gerrit S. Swart - Westfield NJ
George A. Swan - Baton Rouge LA
Kenneth R. Clem - Humble TX

Assignee:

Exxon Research & Engineering Company - Florham Park NJ

International Classification:

C10G 3504

US Classification:

208 65

Abstract:

A two stage process for catalytically reforming a gasoline boiling range hydrocarbonaceous feedstock. The reforming is conducted in two stages wherein the first stage is operated in a fixed bed mode, and the second stage is operated in a moving bed continual catalyst regeneration mode. A gaseous stream comprised of hydrogen and predominantly C. sub. 4. sup. - and a C. sub. 5. sup. + liquid stream are produced between stages. A portion of the hydrogen-rich stream is recycled and the and the remaining portion and an aromatics-lean stream, which is obtained during aromatics separation between stages, is sent to second stage reforming.

Fluid Cat Cracking With High Olefins Prouduction

US Patent:

2002000, Jan 10, 2002

Filed:

Dec 30, 1998

Appl. No.:

09/222864

Inventors:

B. ERIK HENRY - BATON ROUGE LA, US
WILLIAM A. WACHTER - BATON ROUGE LA, US
GEORGE A. SWAN - BATON ROUGE LA, US

International Classification:

C10G009/00
C10G011/00
C10G011/02
C10G011/04

US Classification:

208/106000, 208/113000, 208/114000, 208/119000

Abstract:

The propylene production of a fluid catalytic cracking unit employing a large pore zeolite cracking catalyst, produces more propylene by adding a naphtha cracking riser and a medium pore zeolite catalytic component to the unit, and recycling at least a portion of the naphtha crackate to the naphtha riser. The large pore size zeolite preferably comprises a USY zeolite and the medium pore size is preferably ZSM-5. Propylene production per unit of naphtha feed to the naphtha riser is maximized, by using the 60-300 F. naphtha crackate as the feed.

Process For Suppression Of Catalyst Deactivation And C.sub.5 + Liquid Yield Loss In A Cyclic Reforming Unit

US Patent:

4125454, Nov 14, 1978

Filed:

Nov 14, 1977

Appl. No.:

5/851060

Inventors:

Kenneth R. Clem - Baton Rouge LA
George A. Swan - Baton Rouge LA
Louis Dauber - Cranford NJ

Assignee:

Exxon Research & Engineering Co. - Linden NJ

International Classification:

C10G 3508

US Classification:

208 65

Abstract:

A process for reforming with hydrogen, or hydroforming, a naphtha in a cyclic reforming unit which contains a plurality of catalyst-containing on stream reactors in series, and a catalyst-containing swing reactor manifolded therewith which can be periodically placed in series and substituted for an on stream reactor while the latter is removed from series for regeneration and reactivation of the catalyst contained therein. In the process, a reactor which is next scheduled for regeneration and reactivation of its near deactivated catalyst is located immediately downstream next in series with a reactor which contains freshly regenerated, reactivated catalyst at the time the latter is initially put on stream so that sulfur released by the freshly regenerated, reactivated catalyst which occurs a short time after the upstream reactor has been returned to service, is adsorbed by the near deactivated catalyst of the reactor next requiring removal from the series for catalyst regeneration and reactivation. Subsequent to this time, and prior to any desorption and release of major concentrations of sulfur from the deactivated catalyst, the reactor used for scavenging the sulfur is then swung out of series for regeneration and reactivation of the sulfided catalyst, and replaced in the series by the swing reactor.

Reforming Using Novel Platinum-Tin Alumina Catalysts

US Patent:

4963249, Oct 16, 1990

Filed:

Jul 3, 1989

Appl. No.:

7/375570

Inventors:

William C. Baird - Baton Rouge LA
Kenneth L. Riley - Baton Rouge LA
George A. Swan - Baton Rouge LA

Assignee:

Exxon Research & Engineering Company - Florham Park NJ

International Classification:

C10G 35085

US Classification:

208139

Abstract:

A process for reforming gasoline boiling range naphthas which process comprises use of catalysts comprised of Pt and Sn on alumina and a modifier comprised of at least about 100 wppm Si and at least 10 wppm of one or more alkaline earth metals selected from Ca, Mg, Ba, and Sr wherein the total amount of modifier does not exceed about 5000 wppm.

Videos & Images

FAQ: Learn more about George Swan

What are the previous addresses of George Swan?

Previous addresses associated with George Swan include: 79 Martin Dr, Newport, PA 17074; 187 Hampstead Way, Marshfield, MA 02050; 282 Pudding Hill Ln, Marshfield, MA 02050; 255 Cascade Ave, Redmond, OR 97756; 26548 Harper Creek, Mount Vernon, OR 97865. Remember that this information might not be complete or up-to-date.

Where does George Swan live?

Asbury, IA is the place where George Swan currently lives.

How old is George Swan?

George Swan is 70 years old.

What is George Swan date of birth?

George Swan was born on 1954.

What is George Swan's email?

George Swan has such email addresses: choch***@thepla.net, de***@aol.com, georges***@netzero.net, george.s***@bellsouth.net, crystlyzedde***@aol.com, george.s***@cs.com. Note that the accuracy of these emails may vary and they are subject to privacy laws and restrictions.

What is George Swan's telephone number?

George Swan's known telephone numbers are: 228-392-3064, 360-371-2952, 518-483-8730, 407-737-7718, 225-272-9129, 509-924-6359. However, these numbers are subject to change and privacy restrictions.

How is George Swan also known?

George Swan is also known as: George A Swan. This name can be alias, nickname, or other name they have used.

Who is George Swan related to?

Known relatives of George Swan are: David Lincoln, Cynthia Swan, Judith Swan, Lincoln Swan, Lucas Swan, Showcase Swan, Joy Grutz. This information is based on available public records.

What are George Swan's alternative names?

Known alternative names for George Swan are: David Lincoln, Cynthia Swan, Judith Swan, Lincoln Swan, Lucas Swan, Showcase Swan, Joy Grutz. These can be aliases, maiden names, or nicknames.

What is George Swan's current residential address?

George Swan's current known residential address is: 1675 Fox Dr, Dubuque, IA 52003. Please note this is subject to privacy laws and may not be current.

Name Variants	Georgie Swan
Ages	53 to 96
Phones	228-392-3064	360-371-2952	518-483-8730
Addresses	79 Main, Nanticoke, PA 18634	79 Martin Dr, Newport, PA 17074	187 Hampstead Way, Marshfield, MA 02050
Business records	Receiving Specialist / Better Health	Healthy Community Engagement and Hospital Consultant / Jhealth Unlimited	Field Reviewer, Title Iii Strengthening Institutio... / Department of Education

George Swan

What do we know about George Swan

Public information about George Swan

Resumes

Resumes

Software Engineer

Managing Director

George Swan

George Swan

Sales Engineer

President

George Swan

Owner

Phones & Addresses

Business Records

Publications

Us Patents

Catalytic Reforming Process

Multistage Reforming With Ultra-Low Pressure Cyclic Second Stage

Superheating Atomizing Steam With Hot Fcc Feed Oil

Process For Reforming At Low Severities With High-Activity, High-Yield, Tin Modified Platinum-Iridium Catalysts

Fixed-Bed/Moving-Bed Two Stage Catalytic Reforming With Interstage Aromatics Removal

Fluid Cat Cracking With High Olefins Prouduction

Process For Suppression Of Catalyst Deactivation And C.sub.5 + Liquid Yield Loss In A Cyclic Reforming Unit

Reforming Using Novel Platinum-Tin Alumina Catalysts

FAQ: Learn more about George Swan

Possible Relatives