4525 E Overlook Dr, Buffalo, NY 14221 • 716 632-4295
Williamsville, NY
Houston, TX
Youngstown, NY
Lewiston, NY
Westfield, NY
4525 E Overlook Dr, Buffalo, NY 14221
Work
Position:
Food Preparation and Serving Related Occupations
Education
Degree:
Associate degree or higher
Name / Title
Company / Classification
Phones & Addresses
Charles E Swain Vice Presi, Vice President
PARSONS GOVERNMENT SERVICES INC 150 · Construction-General · Engineering And Construction · Engineering Services · Business Services · Business Consulting Services Whol Electronic Parts/Equipment · Whol Electronic Parts/Equipment Business Consulting Services · Direct Retail Sales
100 W Walnut St, Pasadena, CA 91124 16055 SPACE CENTER BLVD STE 725, Houston, TX 77062 100 W Walnut St , Pasadena, CA 91124 311 S Division Street , Carson City, NV 89703 626 440-2000, 202 469-6000, 703 481-6100
Charles E. Swain Director
Rcm Capital Management LLC
Isbn (Books And Publications)
Life Of Sir Walter Scott: With Remarks Upon His Writings
From Wikipedia, the free encyclopedia. Jump to: navigation, search. Charles Edward Swain (16 January 1885 9 February 1974) was an Australian athlete. ...
A process for the purification of difluoromethane comprising: (a) subjecting a mixture comprising at least difluoromethane (HFC-32) and dichlorodifluoromethane (CFC-12) to a first distillation step in which a majority of either CFC-12 or HFC-32 is concentrated in a first distillate and a majority of the other component is concentrated in a first bottoms; and (b) subjecting the first distillate in step (a) to at least one additional second distillation step conducted at a different pressure in which a majority of the component concentrated in said first distillate is concentrated in a second bottoms and in which the other component is concentrated in a second distillate; and (c) recovering purified HFC-32 from one of said first or second bottoms.
Kane David Cook - Eggertsville NY Charles Francis Swain - Williamsville NY Peter Brian Logsdon - Orchard Park NY
Assignee:
Honeywell International Inc. - Morristown NJ
International Classification:
B01D 1500
US Classification:
210690, 95142, 570179
Abstract:
A process for removing a chlorinated methane impurity from a stream comprising a halogenated compound other than the chlorinated methane impurity, the process comprising contacting the stream with a polymer adsorbent to produce a purified product stream, the polymer adsorbent having a pore size distribution characterized by a higher cumulative porosity as a function of the log of pore diameter than that of activated carbon.
Charles Swain - Williamsville NY, US Stephen Cottrell - Baton Rouge LA, US Clifford Riegel - Baton Rouge LA, US Curtis Brescher - Baton Rouge LA, US
International Classification:
C07C017/093
US Classification:
570/170000
Abstract:
A process for producing a fluorinated organic compound comprising: (a) reacting an organic starting material with a fluorination agent in the presence of a liquid fluorination catalyst under conditions which are effective to vaporize one or more chlorinated organic by-products and to produce a gaseous product stream containing said fluorinated organic compound and said one or more chlorinated organic by-products; and (b) recovering said fluorinated organic compound from said product stream, and a system for performing the aforementioned process and recovering the chlorinated by-product.
Extraction Of Hydrogen Fluoride From A Halocarbon/Hydrogen Fluoride Azeotropic Mixture
Hang T. Pham - Amherst NY Rajiv R. Singh - Getzille NY Charles F. Swain - Williamsville NY Michael Van Der Puy - Amherst NY
Assignee:
Honeywell International Inc. - Morristown NJ
International Classification:
C07C 1738
US Classification:
570177
Abstract:
A process for the separation of mixtures containing halocarbons and hydrogen fluoride. Either water alone or a blend comprising water and hydrogen fluoride is added to a mixture comprising a halocarbon and hydrogen fluoride to thereby form a first phase rich in the halocarbon and a second phase rich in hydrogen fluoride and water. The most preferred halocarbon is 1,1,1,3,3-pentafluoropropane. Preferably, the first and second phases are then separated. Optionally, the second phase rich in hydroger fluoride and water is also separated.
Gustavo Cerri - Boonton NJ Kin Ching Kong - Woodside NY Charles Francis Swain - Williamsville NY Rajat Subhra Basu - East Amherst NY
Assignee:
AlliedSignal Inc. - Morristown NJ
International Classification:
B01D 334
US Classification:
203 67
Abstract:
The present invention provides a method for separating dichlorodifluoromethane from difluoromethane. More specifically, a process is provided for separating dichlorodifluoromethane and difluoromethane using azeotropic distillation.
Liquid Phase Process For The Preparation Of 1,1-Difluoroethane
Alagappan Thenappan - Cheektowaga NY Charles F. Swain - Williamsville NY Matthew H. Luly - Lancaster NY
Assignee:
AlliedSignal Inc. - Morris Township NJ
International Classification:
C07C 17093 C07C 1720 C07C 1908
US Classification:
570168
Abstract:
1,1-difluoroethane is produced by the reaction of 1,2-dichloroethane with anhydrous hydrogen fluoride in a liquid phase and in the presence of a Lewis acid. Preferably the Lewis acid is tin, antimony, titanium, molybdenum, tungsten, niobium or tantalum halide or a mixture thereof.
Single Stage Process For Producing Hydrofluorocarbons From Perchloroethylene
Hsueh S. Tung - Getzville NY Addison M. Smith - Amherst NY Charles F. Swain - Williamsville NY
Assignee:
AlliedSignal Inc. - Morris County NJ
International Classification:
C07C 1738 C07C 1708
US Classification:
570178
Abstract:
A process for the preparation of one or more of CHClFCF. sub. 3 (HCFC-124), CHF. sub. 2 CClF. sub. 2 (HCFC-124a) and CHF. sub. 2 CF. sub. 3 (HFC-125) by reaction of perchloroethylene with hydrogen fluoride in a single stage reaction vessel in the presence of a fluorination catalyst. These compounds are useful in a variety of industrial applications including blowing agents, refrigerants, sterilant gases and solvent applications. Distilling the reaction product produces a distillate comprising HCl, CHClFCF. sub. 3, CHF. sub. 2 CClF. sub. 2 and CHF. sub. 2 CF. sub. 3 and a minor amount of HF which distillate is scrubbed to remove the acids. The bottoms product comprises perchloroethylene, hydrogen fluoride and organic by-products which is phase separated to sequester the hydrogen fluoride from the mixture of perchloroethylene and organic by-products. The hydrogen fluoride and mixture of perchloroethylene with organic by-products are then preferably re-mixed at a controlled rate and recycled to the reaction vessel.
Separation Of Hydrogen Fluoride From A Fluorocarbon/Hydrogen Fluoride Azeotropic Mixture By Sulfuric Acid
Charles Francis Swain - Williamsville NY Rajiv Ratna Singh - Getzville NY Hang Thanh Pham - Amherst NY
Assignee:
AlliedSignal Inc. - Morristown NJ
International Classification:
C01B 719 C07C 1738
US Classification:
423483
Abstract:
The invention provides a process for the separation of azeotropic mixtures of fluorocarbons from hydrogen fluoride. The most preferred fluorocarbon for this invention is 1,1,1,3,3-pentafluoropropane, which is also known as HFC-245fa. The separation in conducted by adding sulfuric acid to the mixture while the mixture is in either the liquid or gaseous states.
James A. Garfield Elementary School Long Beach CA 1964-1966, John Muir Elementary School Long Beach CA 1966-1971, William Stephens Junior High School Long Beach CA 1971-1974