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Lorenzo Decaul Phones & Addresses

  • 149 Oakridge Dr, Langhorne, PA 19047 (215) 504-9323 (215) 529-1047
  • 19 Westbrite Ct, Wilmington, DE 19810 (302) 529-7947
  • Chester, PA
  • Sellersville, PA
  • Philadelphia, PA
  • Prospect Park, PA
  • Buck, PA
  • 149 Oakridge Dr, Langhorne, PA 19047

Work

Position: Protective Service Occupations

Languages

English

Resumes

Resumes

Lorenzo Decaul Photo 1

Lorenzo Decaul

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Location:
149 Oakridge Dr, Langhorne, PA 19047
Languages:
English

Publications

Us Patents

Multi-Component Molecular Sieve Catalyst Compositions And Their Use In Aromatics Reactions

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US Patent:
7276638, Oct 2, 2007
Filed:
Mar 29, 2006
Appl. No.:
11/392804
Inventors:
Jihad M. Dakka - Whitehouse Station NJ, US
James C. Vartuli - Schwenksville PA, US
John S. Buchanan - Lambertville NJ, US
Jose G. Santiesteban - Baton Rouge LA, US
Doron Levin - Annandale NJ, US
Lorenzo C. DeCaul - Langhorne PA, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C07C 2/66
US Classification:
585467, 585469
Abstract:
The invention relates to a process for producing alkylated aromatic hydrocarbons, preferably with an oxygen or sulfur containing alkylating agent, in the presence of a multi-component molecular sieve catalyst composition that includes a molecular sieve and an active metal oxide. The invention is also directed to methods of making and formulating the multi-component molecular sieve catalyst composition useful in producing alkylated aromatics.

Process For Making Cyclohexylbenzene

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US Patent:
7579511, Aug 25, 2009
Filed:
Oct 10, 2008
Appl. No.:
12/287655
Inventors:
Jihad Mohammed Dakka - Whitehouse Station NJ, US
Lorenzo Cophard DeCaul - Langhorne PA, US
Teng Xu - Hampton NJ, US
Assignee:
Exxonmobil Research and Engineering Company - Annadale NJ
International Classification:
C07C 2/64
C07C 2/66
US Classification:
585316, 585314, 585318, 585319, 585320, 585323
Abstract:
Provided is a process for making cyclohexylbenzene. The process includes the following steps: (a) contacting benzene and hydrogen in the presence of a first catalyst under hydroalkylation conditions sufficient to form a first effluent stream having cyclohexylbenzene, cyclohexane, methyl cyclopentane, and unreacted benzene; (b) supplying at least part of said first effluent stream to a first separation system to divide said first effluent stream part into a cyclohexane/methylcyclopentane-rich stream, a cyclohexane-rich stream, a benzene-rich stream, and a dicyclohexyl benzene-rich stream; (c) recycling at least part of the benzene-rich stream to the contacting step (a); (d) contacting the cyclohexane/methylcyclopentane-rich stream with a second catalyst that catalyzes dehydrogenation and exhibits low acidity under conditions sufficient to convert at least a portion of the cyclohexane to benzene and at least a portion of the methylcyclopentane to linear and/or branched paraffins to form a second effluent stream; and (e) recycling at least part of the second effluent stream to the contacting step (a).

Process For Producing Phenol And/Or Cyclohexanone

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US Patent:
8247627, Aug 21, 2012
Filed:
Mar 16, 2009
Appl. No.:
12/933935
Inventors:
Jihad M. Dakka - Whitehouse Station NJ, US
J. Scott Buchanan - Lambertville NJ, US
Jane C. Cheng - Bridgewater NJ, US
Tan-Jen Chen - Kingwood TX, US
Lorenzo C. DeCaul - Langhorne PA, US
Terry E. Helton - Bethlehem PA, US
Jon E. Stanat - Westhampton Beach NY, US
Francisco M. Benitez - Houston TX, US
Assignee:
ExxonMobil Chemical Patents Inc. - Houston TX
International Classification:
C06C 2/68
C07C 5/327
C07C 45/27
C07C 27/08
US Classification:
585323, 585446, 585467, 585440, 568361, 568798
Abstract:
In a process for producing phenol and/or cyclohexanone, benzene and hydrogen are contacted with a first catalyst in a hydroalkylation step to produce a first effluent stream comprising cyclohexylbenzene, cyclohexane, and unreacted benzene. At least part of the first effluent stream is supplied to a first separation system to divide the first effluent stream part into a cyclohexylbenzene-rich stream and a C6 product stream comprising unreacted benzene and cyclohexane.

Process For Preparing Poly Alpha Olefins And Lubricant Basestocks From Fischer-Tropsch Liquids

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US Patent:
8440872, May 14, 2013
Filed:
Oct 5, 2007
Appl. No.:
11/973281
Inventors:
John S. Buchanan - Lambertville NJ, US
Margaret M. Wu - Skillman NJ, US
Lorenzo DeCaul - Langhorne PA, US
Assignee:
Exxonmobil Research and Engineering Company - Annandale NJ
International Classification:
C07C 2/22
US Classification:
585532, 585324, 585329, 585330, 585502, 585518, 585519, 585520, 585530
Abstract:
A process for preparing poly alpha olefins from a Fisher-Tropsch product. The process comprising the steps of contacting a C-Cfraction of an alpha-olefinic hydrocarbon mixture produced from thermal cracking a C-CFisher-Tropsch product with an oligomerization catalyst under conditions to produce an oligomerized product; and fractionating the oligomerized product to obtain a fractionated product having an average carbon number greater than 30. A process for preparing lubricant base stocks from a Fisher-Tropsch product is also provided.

Regeneration Of Metal-Containing Catalysts

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US Patent:
20120083637, Apr 5, 2012
Filed:
Aug 26, 2011
Appl. No.:
13/218520
Inventors:
Kenneth R. Clem - Humble TX, US
Larry L. Iaccino - Seabrook TX, US
Mobae Afeworki - Phillipsburg NJ, US
Juan D. Henao - Lebanon NJ, US
Neeraj Sangar - League City TX, US
Xiaobo Zheng - Houston TX, US
Lorenzo C. DeCaul - Langhorne PA, US
International Classification:
C07C 2/76
B01J 38/02
US Classification:
585415, 502 34
Abstract:
In a process for the regeneration of a coked metal-containing catalyst, the coked catalyst is contacted in a regeneration zone with an atmosphere which contains carbon dioxide and carbon monoxide at a temperature of at least 400 C.

Dehydrogenation Process

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US Patent:
20120302798, Nov 29, 2012
Filed:
Dec 17, 2010
Appl. No.:
13/515104
Inventors:
Jihad M. Dakka - Whitehouse Station NJ, US
Lorenzo C. Decaul - Langhorne PA, US
Sabato Miseo - Pittstown NJ, US
James R. Lattner - Laporte TX, US
Tan-Jen Chen - Kingwood TX, US
Terry E. Helton - Bethlehem PA, US
Teng Xu - Houston TX, US
International Classification:
C07C 37/08
C07C 5/32
US Classification:
568798, 585379
Abstract:
A dehydrogenation process for the dehydrogenation of at least one dehydrogenatable hydrocarbon, the process comprising contacting a feed comprising the at least one dehydrogenatable hydrocarbon under dehydrogenation conditions with a catalyst composition comprising a support and at least one dehydrogenation component wherein said conditions include a temperature of from 400 C. to 750 C. and a pressure of at least 50 psig (345 kPag).

Dehydrogenation Catalyst And Process

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US Patent:
20120302799, Nov 29, 2012
Filed:
Dec 17, 2010
Appl. No.:
13/515142
Inventors:
Jihad M. Dakka - Whitehouse Station NJ, US
Lorenzo C. Decaul - Langhorne PA, US
Terry E. Helton - Bethlehem PA, US
Teng Xu - Houston TX, US
Jenna L. Wallace - Bethlehem PA, US
International Classification:
C07C 37/07
C07C 37/08
B01J 23/04
B01J 37/08
B01J 23/58
US Classification:
568798, 502184, 502243, 502330, 502344, 568799
Abstract:
A catalyst composition comprises (i) a support; (ii) a dehydrogenation component comprising at least one metal or compound thereof selected from Groups 6 to 10 of the Periodic Table of Elements; and (iii) potassium or a potassium compound present in an amount of about 0.15 to about 0.6 wt % of potassium based upon the total weight of the catalyst composition, wherein the catalyst composition has an oxygen chemisorption of greater than 50%.

Cyclohexanone Dehydrogenation Catalyst And Process

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US Patent:
20130090499, Apr 11, 2013
Filed:
Dec 17, 2010
Appl. No.:
13/520467
Inventors:
Teng Xu - Houston TX, US
Terry E. Helton - Bethlehem PA, US
Jihad M. Bakka - Whitehouse Station NJ, US
Tan-Jen Chen - Kingwood TX, US
Sabato Miseo - Pittstown NJ, US
Lorenzo C. Decaul - Langhorne PA, US
International Classification:
B01J 23/58
C07C 37/07
C07C 37/08
US Classification:
568798, 585430, 568799
Abstract:
A catalyst composition comprising: (i) a support; (ii) a first component comprising at least one metal component selected from Group 1 and Group 2 of the Periodic Table of Elements; and (iii) a second component comprising at least one metal component selected from Groups 6 to 10 of the Periodic Table of Elements, wherein the catalyst composition exhibits an oxygen chemisorption of greater than 50%.
Lorenzo C Decaul from Langhorne, PA, age ~74 Get Report