Search

Theodore J Jenczewski

age ~81

from Midlothian, VA

Also known as:
  • Theo J Jenczewski
  • Judith Jenczewski
  • Theodore I
Phone and address:
2500 Chimney House Ct, Midlothian, VA 23112
(804)7634659

Theodore Jenczewski Phones & Addresses

  • 2500 Chimney House Ct, Midlothian, VA 23112 • (804)7634659
  • 2431 Viburg Ct, Midlothian, VA 23113
  • 3016 Three Bridges Rd, Midlothian, VA 23112 • (804)7634659
  • Richmond, VA
  • Sherrill, NY
  • 2500 Chimney House Ct, Midlothian, VA 23112 • (804)8159820

Work

  • Position:
    Professional/Technical

Education

  • Degree:
    Graduate or professional degree

Emails

Us Patents

  • Electrodialytic Methods For Removal Of Sulfur Oxides From Waste Gases

    view source
  • US Patent:
    45526354, Nov 12, 1985
  • Filed:
    Aug 9, 1984
  • Appl. No.:
    6/639528
  • Inventors:
    Theodore J. Jenczewski - Sherrill NY
    William H. Skinner - Budd Lake NJ
  • Assignee:
    Allied Corporation - Morris Township, Morris County NJ
  • International Classification:
    B01D 1302
  • US Classification:
    2041824
  • Abstract:
    Methods for removal of sulfur oxides, e. g. , SO. sub. 2 and SO. sub. 3, from sulfuric acid tail gases by alkaline solution scrubbing, acidification of the alkaline scrubbing solution containing absorbed sulfur valves, liberation of concentrated SO. sub. 2 from the acidified solution and regeneration of the alkaline scrubbing solution by means of two- or three-compartment electrodialytic water splitters are disclosed. A completely closed loop method suitable for continuous removal of sulfur oxides from sulfuric acid tail gas, recovery of concentrated SO. sub. 2 for use in sulfuric acid plants, regeneration of alkaline scrubbing process solution and improvement in the water balance in sulfuric acid plant by use of two- and three-compartment electrodialytic water splitters is also disclosed.
  • Manufacture Of High Purity Low Arsenic Anhydrous Hydrogen Fluoride

    view source
  • US Patent:
    47568992, Jul 12, 1988
  • Filed:
    Feb 12, 1987
  • Appl. No.:
    7/014422
  • Inventors:
    Theodore J. Jenczewski - Sherrill NY
    Robert L. Sturtevant - Hamburg NY
    Thomas R. Morgan - Jordan NY
    Barry J. Boghean - St. Clair Beach, CA
    Donald C. Butt - Brampton, CA
  • Assignee:
    Allied-Signal Inc. - Morris Township, Morris County NJ
  • International Classification:
    C01B 719
  • US Classification:
    423483
  • Abstract:
    A process for manufacturing high purity anhydrous hydrogen fluoride (HF) having low levels of arsenic impurity by contacting anhydrous hydrogen fluoride product, or an intermediate product obtained during the manufacture of HF, with hydrogen peroxide in the presence of a catalyst which comprises effective amounts of molybdenum or an inorganic molybdenum compound and a phosphate compound. The volatile trivalent arsenic impurity in the anhydrous hydrogen fluoride is oxidized to a non-volatile pentavalent arsenic compound and the resultant mixture is distilled to recover high purity anhydrous hydrogen fluoride with reduced levels of arsenic impurity. In one embodiment, an oxidizing agent such as nitric acid or a nitrate salt is added to the reaction mixture to oxidize organic contaminants.
  • Furnace Gas - Sulfuric Acid Contact Process For Hf Manufacture

    view source
  • US Patent:
    52719189, Dec 21, 1993
  • Filed:
    Mar 11, 1991
  • Appl. No.:
    7/666957
  • Inventors:
    Audie J. Patterson - Atlanta GA
    Robert A. Smith - Kinnelon NJ
    Theodore J. Jenczewski - Sherrill NY
  • Assignee:
    AlliedSignal Inc. - Morristown NJ
  • International Classification:
    C01B 719
  • US Classification:
    423485
  • Abstract:
    A method is provided wherein the equilibrium HF concentration in the mixture of HF, sulfuric acid and water fed to an HF reaction furnace is greatly reduced by injecting a controlled amount of steam into an HF-removal process wherein the sulfuric acid mixture is also contacted with the hot HF gas leaving the HF reaction furnace. Reducing the HF concentration in this manner significantly improves furnace performance. The purpose of injecting steam is to adjust the water content of the mixture to the optimum value (about 12. 5 weight percent) for HF removal, as well as to supply the heat required for HF removal without the need for an indirect heat exchanger. An additional advantage to this method is that since direct steam injection adds water to the process, in order to keep the furnace feed acid water concentration at the desirable level of less than 1%, oleum or SO. sub. 3 must be added to react with the excess water. Since the reaction of water and SO. sub.
  • Process For The Purification Of Caprolactam Obtained From The Depolymerization Of Polyamide-Containing Carpet

    view source
  • US Patent:
    61879177, Feb 13, 2001
  • Filed:
    Oct 29, 1999
  • Appl. No.:
    9/429269
  • Inventors:
    Richard Eugene Mayer - Richmond VA
    Lamberto Crescentini - Chester VA
    Theodore John Jenczewski - Midlothian VA
  • Assignee:
    AlliedSignal Inc. - Morristownship NJ
  • International Classification:
    C07D20116
  • US Classification:
    540540
  • Abstract:
    The present invention provides a process for the preparation of purified caprolactam comprising the steps of: (a) depolymerizing polyamide-containing carpet in the presence of steam to obtain crude caprolactam and steam; (b) condensing or distilling said crude caprolactam and steam to form aqueous crude caprolactam comprising at least ten percent by weight water; (c) removing substantially all floating oil from the aqueous crude caprolactam so as to form a substantially floating oil-free aqueous crude caprolactam; (d) removing substantially all of said water from said substantially floating oil-free aqueous crude caprolactam; (e) distilling the resulting concentrated crude caprolactam at a pressure of less than about 8 mmHg and a temperature from about 110. degree. C. to about 145. degree. C. so as to form overheads and bottoms of the caprolactam; and (f) crystallizing the caprolactam overheads to obtain caprolactam crystals and mother liquor.
  • Phenol With Low Levels Of Methylbenzofuran

    view source
  • US Patent:
    54141540, May 9, 1995
  • Filed:
    Jun 6, 1994
  • Appl. No.:
    8/254729
  • Inventors:
    Theodore J. Jenczewski - Midlothian VA
    Lamberto Crescentini - Chester VA
    James A. Kweeder - Chester VA
  • Assignee:
    AlliedSignal Inc. - Morris Township, Morris County NJ
  • International Classification:
    C07C 3768
    C07C 3770
  • US Classification:
    568754
  • Abstract:
    A process for the reduction of methylbenzofuran (MBF) impurities in phenol obtained from the decomposition product of cumene hydroperoxide requires treating the phenol to reduce the level of acetol, contacting the phenol containing a low level of acetol with an acid resin at sufficient temperature and residence time to reduce the level of MBF by conversion to higher boiling compounds, then distilling the phenol to separate phenol from higher boiling compounds. The phenol may be treated in known ways, such as by treatment with an amine, to reduce the level of acetol. The phenol containing a low level of acetol is contacted with a strong acid resin to reduce the level MBF.
  • Process For The Purification Of Caprolactam Obtained From The Depolymerization Of Polyamide-Containing Carpet

    view source
  • US Patent:
    59903066, Nov 23, 1999
  • Filed:
    Sep 3, 1997
  • Appl. No.:
    8/922853
  • Inventors:
    Richard Eugene Mayer - Richmond VA
    Lamberto Crescentini - Chester VA
    Theodore John Jenczewski - Midlothian VA
  • Assignee:
    AlliedSignal Inc. - Morristown NJ
  • International Classification:
    C07D20112
  • US Classification:
    540540
  • Abstract:
    The present invention provides a process for the preparation of purified caprolactam comprising the steps of: (a) depolymerizing polyamide-containing carpet in the presence of steam to obtain crude caprolactam and steam; (b) removing substantially all of said water from said crude caprolactam and steam (c) distilling the resulting concentrated crude caprolactam at a pressure of less than about 8 mmHg and a temperature from about 110. degree. C. to about 145. degree. C. so as to form overheads and bottoms of the caprolactam; and (d) crystallizing the caprolactam overheads to obtain caprolactam crystals and mother liquor. The resulting purified caprolactam may then be used to make polycaprolactam which may then be used in engineered materials or spun into fiber.
  • Monomer Recovery From Multi-Component Materials

    view source
  • US Patent:
    56567570, Aug 12, 1997
  • Filed:
    Aug 10, 1995
  • Appl. No.:
    8/511334
  • Inventors:
    Theodore John Jenczewski - Midlothian VA
    Lamberto Crescentini - Chester VA
    Richard Eugene Mayer - Richmond VA
  • Assignee:
    AlliedSignal Inc. - Morristown NJ
  • International Classification:
    C07D20112
  • US Classification:
    540540
  • Abstract:
    A process for recovering monomer from multi-component waste material that includes a hydrolyzable polymer, includes contacting the multi-component waste material with water and subjecting the resulting mixture to heat and pressure to form a liquid aqueous portion and a water insoluble portion. The liquid aqueous portion mainly includes depolymerization products of the hydrolyzable polymer, and the water insoluble portion mainly includes components other than the depolymerization products. This mixture is cooled and the liquid aqueous portion and the water insoluble portion are separated. Monomer that formed the hydrolyzable polymer is recovered from the liquid aqueous solution.
  • Electrodialytic Process

    view source
  • US Patent:
    42193966, Aug 26, 1980
  • Filed:
    Aug 3, 1979
  • Appl. No.:
    6/063229
  • Inventors:
    Alan B. Gancy - Syracuse NY
    Theodore J. Jenczewski - Sherrill NY
  • Assignee:
    Allied Chemical Corporation - Morris Township, Morris County NJ
  • International Classification:
    B01D 1302
  • US Classification:
    204180P
  • Abstract:
    An improved process for the electrodialysis of aqueous NaCl which operates at high current efficiency and low unit cell voltage drop to produce high strength, high purity Na. sub. 2 CO. sub. 3 and either high purity HCl or CaCl. sub. 2 by utilizing cation permselective, anion permselective and bipolar membranes wherein the solutions on both sides of the anion permselective membrane are acidic.

Mylife

Theodore Jenczewski Photo 1

Theodore Jenczewski Midl...

view source
Lost touch with Theodore Jenczewski? Find old friends, classmates, and colleagues with the people search tool at mylife.

Facebook

Theodore Jenczewski Photo 2

Theodore Jenczewski

view source

Get Report for Theodore J Jenczewski from Midlothian, VA, age ~81
Control profile