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Andrew Patrylak Phones & Addresses

  • 5155 Hanover Dr, Allentown, PA 18106 (610) 395-4838
  • 5155 Hanover Ave, Wescosville, PA 18106 (610) 395-4838
  • Harmony, PA
  • Staten Island, NY
  • Macungie, PA
  • Butler, PA
  • 5155 Hanover Dr, Allentown, PA 18106 (484) 695-8484

Work

Position: Professional/Technical

Education

Degree: High school graduate or higher

Emails

Publications

Us Patents

Suitable Distillation Column Packing For The Cryogenic Separation Of Air

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US Patent:
48139882, Mar 21, 1989
Filed:
May 23, 1988
Appl. No.:
7/197555
Inventors:
Douglas L. Bennett - Allentown PA
Keith A. Ludwig - Emmaus PA
Andrew J. Patrylak - Wescosville PA
John Zabrenski - Allentown PA
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
F25J 300
US Classification:
62 18
Abstract:
This invention relates to a process for the cryogenic separation of oxygen-containing mixtures to produce an enriched product whereby oxygen concentrations greater than 21% by volume are achieved in the process via passing streams of liquid and vapor countercurrently through a mass transfer zone which contains packing elements fabricated from a material having a thickness of less than about 1 millimeter, having a copper concentration of at least about 30% by weight and a heat of combustion of less than 1. 0 Kcal/g, thereby avoiding the risk of flammability.

Process For Oxidation Of Black Liquor

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US Patent:
42395895, Dec 16, 1980
Filed:
Oct 2, 1978
Appl. No.:
5/947802
Inventors:
Edward F. Elton - Bethlehem PA
Andrew J. Patrylak - Wescosville PA
Joseph G. Santangelo - Allentown PA
Assignee:
Air Products and Chemicals, Inc. - Allentown PA
International Classification:
D21C 1110
D21C 1114
US Classification:
162 31
Abstract:
High recovery of useful energy from the heat of reaction in the oxidation of black liquor is obtained by integrating the oxidation into the multiple effect evaporation system of the pulp mill recovery sequence. The heat of reaction is thereby recovered as flash steam, which when combined with the vapors from an appropriate evaporator body enables recovery of its energy through further evaporation. The oxidation reaction may be carried out on the liquor leaving the second effect of the evaporation sequence for maximum energy recovery, or in accordance with an alternative embodiment, the reaction is carried out between the first effect and the flash tank with preferable addition of a second flash tank in series with the first.
Andrew J Patrylak from Wescosville, PA, age ~71 Get Report