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Steven Auvil Phones & Addresses

  • 4737 Pringle Rd, Snover, MI 48472
  • Macungie, PA
  • 4455 West St, Cass City, MI 48726
  • 6300 Adams Rd, Marlette, MI 48453
  • Fairgrove, MI
  • Essexville, MI
  • East Tawas, MI

Publications

Us Patents

Liquid Distributor Internal Baffling

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US Patent:
6758463, Jul 6, 2004
Filed:
Nov 21, 2001
Appl. No.:
09/990410
Inventors:
Ian Robert Zone - Woking, GB
Raymond Elliott Sacks - Upper Norwood, GB
Kenneth William Kovak - Macungie PA
Mohammad Ali Kalbassi - Walton-on-Thames, GB
Steven Ray Auvil - Macungie PA
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
B01F 304
US Classification:
261 97, 261110, 62121
Abstract:
An apparatus for distributing a liquid in an exchange column includes a plate and at least one elongated internal baffle. The plate has at least one elongated channel, which has a first longitudinal axis, a bottom, and at least one aperture in the bottom. At least a substantial portion of the internal baffle, which has a second longitudinal axis substantially parallel to the first longitudinal axis, is disposed in the channel.

Periodic High Temperature Regeneration Of Thermal Swing Adsorption Systems

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US Patent:
7128776, Oct 31, 2006
Filed:
Mar 10, 2004
Appl. No.:
10/797742
Inventors:
William Paul Schmidt - Wescosville PA, US
Steven Ray Auvil - Macungie PA, US
Mohammad Ali Kalbassi - Weybridge, GB
Timothy Christopher Golden - Allentown PA, US
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
B01D 53/04
B01D 53/26
US Classification:
95115, 95126, 95129, 95139
Abstract:
An improved thermal swing adsorption process is set forth which addresses the problem of water ingress into the adsorbent by periodically heating the adsorbent to a temperature greater than the temperature used in the normal regeneration cycle.

Removal Of Gaseous Contaminants From Argon

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US Patent:
7862645, Jan 4, 2011
Filed:
Feb 1, 2008
Appl. No.:
12/024168
Inventors:
Roger Dean Whitley - Allentown PA, US
Annemarie Ott Weist - Macungie PA, US
Steven Ray Auvil - Macungie PA, US
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
B01D 53/047
US Classification:
95 96, 95130, 95148, 96130, 422169
Abstract:
Method for argon recovery that comprises (a) providing a feed gas mixture comprising argon and nitrogen; (b) contacting at least a portion of the feed gas mixture with a nitrogen-selective adsorbent in a cyclic pressure swing adsorption process and adsorbing at least a portion of the nitrogen on the adsorbent in a first pressure range above 100 psia to provide a purified argon product and an adsorbent comprising adsorbed nitrogen; and (c) desorbing the adsorbed nitrogen in one or more regeneration steps effected in a second pressure range between atmospheric pressure and a super-atmospheric pressure below any pressure in the first pressure range, inclusive; wherein the cyclic pressure swing adsorption process is effected at an average operating temperature of at least about 0 C.

Alkylation Of Aromatic Amines With Olefins On Partially Dealuminated Zeolites

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US Patent:
48763772, Oct 24, 1989
Filed:
Mar 22, 1988
Appl. No.:
7/171602
Inventors:
Rakesh Agrawal - Allentown PA
Steven R. Auvil - Allentown PA
Michel Deeba - North Brunswick NJ
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
C07C 87452
US Classification:
558416
Abstract:
This invention pertains to an improved process for the alkylation of aromatic amines. The improvement resides in the use with particular aromatic amines and olefins a catalyst which is a highly acidic partially dealuminated zeolite having an increased silica to alumina molar ratio over the original zeolite and an acidity factor of at least 0. 3. The partially dealuminated zeolites are preferably exchanged with hydrogen or rare earth metal and are particularly effective for producing an alkylated aromatic amine where the alkyl group is ortho to the amine. The highly acidic partially dealuminated H-mordenite and partially dealuminated HY faujasite are very effective for the alkylation of aniline with propylene.

Production Of Lactone In Molten Salt Electrolysis

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US Patent:
45607753, Dec 24, 1985
Filed:
Jun 13, 1983
Appl. No.:
6/503980
Inventors:
James P. Coleman - Maryland Heights MO
Richard C. Hallcher - Maryland Heights MO
Dudley E. McMackins - St. Charles MO
Charles R. Penquite - Ballwin MO
Steven R. Auvil - Macungie PA
Assignee:
Monsanto Company - St. Louis MO
International Classification:
C07D30732
C07C 6705
US Classification:
549326
Abstract:
Butadiene and acetic acid are reacted with a metal salt oxidant in molten salt medium to form. gamma. -vinyl-. gamma. -butyrolactone. The process includes electrolytic regeneration of the oxidant and provides a simple reaction system which permits product recovery and reactant recycle without extensive solvent handling. A high surface area reactor can be employed.

Purification Of Nitrogen Trifluoride By Continuous Cryogenic Distillation

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US Patent:
62761684, Aug 21, 2001
Filed:
May 8, 2000
Appl. No.:
9/566075
Inventors:
Zbigniew Tadeusz Fidkowski - Macungie PA
John Frederick Cirucci - Schnecksville PA
Rakesh Agrawal - Emmaus PA
Shyam Ramchand Suchdeo - Wescosville PA
Steven Ray Auvil - Macungie PA
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
F25J 100
US Classification:
62625
Abstract:
The process recovers NF3 from a multicomponent fluid containing NF3, one or more components less volatile than NF3, and one or more components more volatile than NF3. The process uses a first distillation column and a second distillation column, each distillation column having a top and a bottom. The process includes the following steps: feeding the multicomponent fluid to the first distillation column at a first feed location below the top of the first distillation column; feeding a cryogenic liquid to the first or second distillation column adjacent the top of the first or second distillation column; withdrawing a mixture containing NF3 from the first distillation column; feeding the mixture to the second distillation column at a second feed location; separating NF3 from the mixture in the second distillation column; and removing a stream of NF3 from the second distillation column.

Alkylation Of Aromatic Amines Over Thermally Pretreated Zeolites

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US Patent:
50269127, Jun 25, 1991
Filed:
Mar 27, 1990
Appl. No.:
7/499925
Inventors:
Rakesh Agrawal - Allentown PA
Steven R. Auvil - Macungie PA
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
C07C20968
US Classification:
564409
Abstract:
A process for selectively producing ortho-alkylated aromatic amines in high selectivity relative to N-alkylated aromatic amines. The process comprises reacting an aromatic amine, having at least one hydrogen atom in a position ortho to the amine functionality, and an olefin under conditions sufficient to effect an alkylation reaction, in the presence of a zeolite catalyst which has been thermally pretreated by heating the catalyst to a temperature greater than about 500. degree. C. for a period ranging from 0. 5 to about 10 hours while sweeping an inert gas over the heated catalyst to remove water and ammonia formed during the thermal treatment, and subsequently recovering the alkylated aromatic amine.

Air Separation By Pressure Swing Adsorption With A High Capacity Carbon Molecular Sieve

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US Patent:
52404749, Aug 31, 1993
Filed:
Jan 30, 1992
Appl. No.:
7/828264
Inventors:
Steven R. Auvil - Macungie PA
Joan M. Schork - Allentown PA
Rajagopalan Srinivasan - Allentown PA
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
B01D 5304
US Classification:
95 96
Abstract:
Nitrogen is produced by separating air in a pressure swing adsorption process using a high capacity kinetically O. sub. 2 selective material as the adsorbent. An example of such an adsorbent is a carbon molecular sieve made from coconut shell char. Such a coconut shell char having a high oxygen volumetric capacity is provided by crushing and sizing coconut shells to form granules which are then heated in flowing inert gas at a temperature ramp rate of about 2 to 12. degree. C. per minute to a peak temperature of 775 to 900. degree. C. which is then held so that the total heating time is up to 8 hours and thereafter the granular char is cooled in an inert gas atmosphere. The granular char thus produced is kinetically selective for O. sub. 2 over N. sub. 2 without further modification to narrow the openings of its micropores and has an oxygen volumetric capacity in excess of 8. 0 cc/cc at 1 atm.
Steven R Auvil from Snover, MI, age ~59 Get Report