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Josiane M Ginestra

age ~71

from Richmond, TX

Also known as:
  • Josiane C Ginestra
  • Jean C Ginestra
  • Jc Ginestra
  • Jennifer Ginestra
  • Ginestra Jean-Charles
  • Ginestra R Josiane
Phone and address:
5207 Mimosa Ln, Richmond, TX 77469
281-342-7046

Josiane Ginestra Phones & Addresses

  • 5207 Mimosa Ln, Richmond, TX 77469 • 281-342-7046
  • Houston, TX

Work

  • Position:
    Service Occupations

Education

  • Degree:
    High school graduate or higher

Us Patents

  • Alumina Having Bimodal Pore Structure, Catalysts Made Therefrom And Processes Using Same

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  • US Patent:
    6984310, Jan 10, 2006
  • Filed:
    Dec 17, 2002
  • Appl. No.:
    10/321810
  • Inventors:
    Josiane M. Ginestra - Richmond TX, US
    Russell C. Ackerman - Katy TX, US
    Christian G. Michel - Houston TX, US
  • Assignee:
    Shell Oil Company - Houston TX
  • International Classification:
    C01G 35/06
    C01G 47/02
    C01G 47/04
    C01G 11/02
    B01J 23/00
  • US Classification:
    208137, 208112, 208114, 208123, 208124, 208136, 208138, 208251 R, 208254 R, 502211, 502213, 502314, 502315, 502316, 502320, 502322, 502323, 502327, 502332, 502333, 502334, 502335, 502336, 502337, 502338, 502339, 502355, 502415, 502439
  • Abstract:
    Alumina having a pore structure characterized by the absence of macropores, no more than 5% of the total pore volume in pores greater than 350 Å, a high pore volume (greater than 0. 8 cc/g measured by mercury intrusion) and a bi-modal pore volume distribution character, where the two modes are separated by 10 to 200 Å, and the primary pore mode is larger than the median pore diameter (MPD), calculated either by volume or by surface area, the MPD by volume being itself larger than the MPD by surface area. Also provided are catalysts made from and processes using such alumina.
  • Method Of Restoring Catalytic Activity To A Spent Hydroprocessing Catalyst, A Spent Hydroprocessing Catalyst Having Restored Catalytic Activity, And A Hydroprocessing Process

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  • US Patent:
    7696120, Apr 13, 2010
  • Filed:
    Jan 19, 2005
  • Appl. No.:
    11/039677
  • Inventors:
    Josiane Marie-Rose Ginestra - Richmond TX, US
    James Dallas Seamans - The Woodlands TX, US
    Kenneth Scott Lee - The Woodlands TX, US
  • Assignee:
    Shell Oil Company - Houston TX
  • International Classification:
    B01J 38/02
    B01J 21/20
    B01J 38/48
    B01J 38/62
    B01J 38/50
    B01J 38/12
  • US Classification:
    502 56, 502 20, 502 22, 502 29, 502 38, 502514
  • Abstract:
    Disclosed is method for restoring catalytic activity to a hydroprocessing catalyst that has become spent due to its use or to the deposition of carbon thereon. The method includes a carbon reduction step whereby carbon is removed from the spent hydroprocessing catalyst in a controlled manner to within a specifically defined concentration range. Following the carbon removal step, the resulting catalyst, having a reduced concentration of carbon, is subjected to a chelation treatment whereby the resulting carbon-reduced catalyst is contacted with a chelating agent and aged for a time period necessary for realizing the benefit from the controlled carbon reduction step. In a preferred embodiment, the catalyst resulting from the chelation treatment is subjected to a sulfurization treatment involving the incorporation of elemental sulfur therein and contacting therewith an olefin.
  • Process And Catalyst For The Hydroconversion Of A Heavy Hydrocarbon Feedstock

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  • US Patent:
    7790652, Sep 7, 2010
  • Filed:
    Sep 15, 2004
  • Appl. No.:
    10/941462
  • Inventors:
    Russell Craig Ackerman - Houston TX, US
    Josiane Marie-Rose Ginestra - Richmond TX, US
    Christian Gabriel Michel - Ossining NY, US
  • Assignee:
    Shell Oil Company - Houston TX
  • International Classification:
    B01J 23/24
    B01J 23/40
    B01J 23/74
    C01F 7/02
  • US Classification:
    502313, 502315, 502316, 423625, 423628
  • Abstract:
    A method of hydroprocessing a heavy hydrocarbon feedstock using a hydroprocessing catalyst having specific properties making it effective in the hydroconversion of at least a portion of the heavy hydrocarbon feedstock to lighter hydrocarbons. The hydroprocessing catalyst comprises a Group VIB metal component (e. g. , Cr, Mo, and W), a Group VIII metal component (e. g. , Ni and Co) and, optionally, a potassium metal component that are supported on a support material comprising alumina. The alumina has novel physical properties that, in combination with the catalytic components, provide for the hydroprocessing catalyst. The hydroprocessing catalyst is particularly effective in the conversion of the heavy hydrocarbon feedstock. The alumina is characterized as having a high pore volume and a high surface area with a large proportion of the pore volume being present in the pores within a narrow pore diameter distribution about a narrowly defined range of median pore diameters. The support material preferably does not contain more than a small concentration of silica.
  • Method Of Restoring Catalytic Activity To A Spent Hydrotreating Catalyst, The Resulting Restored Catalyst, And A Method Of Hydroprocessing

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  • US Patent:
    7820579, Oct 26, 2010
  • Filed:
    Jan 19, 2005
  • Appl. No.:
    11/038291
  • Inventors:
    Josiane Marie-Rose Ginestra - Richmond TX, US
    James Dallas Seamans - The Woodlands TX, US
    Kenneth Scott Lee - The Woodlands TX, US
  • Assignee:
    Shell Oil Company - Houston TX
  • International Classification:
    B01J 38/50
    B01J 38/62
    B01J 38/12
  • US Classification:
    502 29, 502 28, 502 38
  • Abstract:
    A method of restoring catalytic activity to a spent hydroprocessing catalyst that has a first carbon concentration. The concentration of carbon on the spent hydroprocessing catalyst is reduced to provide a carbon-reduced catalyst having a second carbon concentration that is less than the first carbon concentration. The carbon-reduced catalyst is exposed to a solution, comprising a chelating agent and a solvent, for an aging time period sufficient to provide for a restored catalytic activity thereby resulting in an aged catalyst having incorporated therein the chelating agent and the solvent. The aged catalyst is exposed to conditions, including a drying temperature, so as to remove from the aged catalyst a portion of the solvent without removing a significant portion of the chelating agent from the aged catalyst thereby resulting in a dried aged catalyst. The dried aged catalyst is then sulfur treated to thereby provide a restored catalyst. The restored catalyst and those catalysts made by the treatment method can be used in a hydroprocessing process comprising contacting the restored catalyst with a hydrocarbon feedstock under hydroprocessing conditions.
  • Method Of Restoring Catalytic Activity To A Spent Hydrotreating Catalyst, The Resulting Restored Catalyst, And A Method Of Hydroprocessing

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  • US Patent:
    8168557, May 1, 2012
  • Filed:
    Sep 9, 2010
  • Appl. No.:
    12/878825
  • Inventors:
    Josiane Marie-Rose Ginestra - Richmond TX, US
    James Dallas Seamans - The Woodlands TX, US
    Kenneth Scott Lee - The Woodlands TX, US
  • Assignee:
    Shell Oil Company - Houston TX
  • International Classification:
    B01J 27/02
    B01J 27/047
    B01J 27/043
    B01J 23/00
    B01J 23/10
    C10G 17/00
    C10G 19/00
    C10G 21/00
    C10G 25/00
    C10G 27/00
    C10G 29/00
    C10G 31/00
  • US Classification:
    502216, 502219, 502222, 502300, 502305, 502325, 208177
  • Abstract:
    A method of restoring catalytic activity to a spent hydroprocessing catalyst that has a first carbon concentration. The concentration of carbon on the spent hydroprocessing catalyst is reduced to provide a carbon-reduced catalyst having a second carbon concentration that is less than the first carbon concentration. The carbon-reduced catalyst is exposed to a solution, comprising a chelating agent and a solvent, for an aging time period sufficient to provide for a restored catalytic activity thereby resulting in an aged catalyst having incorporated therein the chelating agent and the solvent. The aged catalyst is exposed to conditions, including a drying temperature, so as to remove from the aged catalyst a portion of the solvent without removing a significant portion of the chelating agent from the aged catalyst thereby resulting in a dried aged catalyst. The dried aged catalyst is then sulfur treated to thereby provide a restored catalyst. The restored catalyst and those catalysts made by the treatment method can be used in a hydroprocessing process comprising contacting the restored catalyst with a hydrocarbon feedstock under hydroprocessing conditions.
  • High Surface Area Composition For Use In The Catalytic Hydroconversion Of A Heavy Hydrocarbon Feedstock, A Method Making Such Composition And Its Use

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  • US Patent:
    8372268, Feb 12, 2013
  • Filed:
    Oct 1, 2009
  • Appl. No.:
    12/572097
  • Inventors:
    Josiane Marie-Rose Ginestra - Richmond TX, US
    John G. Kester - The Woodlands TX, US
    David Andrew Komar - Magnolia TX, US
  • Assignee:
    Shell Oil Company - Houston TX
  • International Classification:
    C10G 47/04
  • US Classification:
    208112, 502313, 502314, 502315
  • Abstract:
    A catalyst composition that is especially useful in the hydroconversion of pitch, micro carbon residue and sulfur contents of a heavy hydrocarbon feedstock without the excessive formation of sediment. The catalyst composition is a reasonably high surface area composition containing alumina and a low molybdenum content with a high ratio of nickel-to-molybdenum. The catalyst composition further has a unique pore distribution that in combination with the special metals loading provide for good conversion of pitch and micro carbon residue without an excessive yield of sediment.
  • Metathesis Catalyst And Process

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  • US Patent:
    20060116542, Jun 1, 2006
  • Filed:
    Nov 28, 2005
  • Appl. No.:
    11/287604
  • Inventors:
    David Brown - Hercules CA, US
    Josiane Ginestra - Richmond TX, US
  • International Classification:
    C07C 6/00
  • US Classification:
    585643000
  • Abstract:
    An olefin metathesis process and a catalyst composition suitable for such process comprising (a) rhenium, (b) one or more metal(s) from Columns 5 and 6 of the Periodic Table, and (c) a support made from an alumina; wherein surface area of the catalyst is at least 200 m/g as determined by ASTM D-3663-03.
  • Catalyst Composition And A Process That Uses The Catalyst Composition For The Hydroconversion Of A Heavy Hydrocarbon Feedstock

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  • US Patent:
    20100006475, Jan 14, 2010
  • Filed:
    Jul 2, 2009
  • Appl. No.:
    12/496848
  • Inventors:
    Josiane Marie-Rose GINESTRA - Richmond TX, US
  • International Classification:
    C10G 47/04
    B01J 23/88
  • US Classification:
    208112, 502315
  • Abstract:
    A catalyst composition that provides for a high percentage conversion of the pitch component of a heavy hydrocarbon feedstock and a process of using the catalyst composition. The catalyst composition comprises a nickel component, a molybdenum component in an amount less than 12 wt % of the catalyst composition, and it may also include an alumina support material having special properties. The weight ratio of the nickel component-to-molybdenum component exceeds 0.25, and the support material preferably has a median pore diameter of from 100-140 Å. The catalyst composition has a characteristically unique Raman spectrum that distinguishes it over other compositions.

Resumes

Josiane Ginestra Photo 1

Josiane Ginestra

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Youtube

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