David Leason - Chappaqua NY Edward J. Ellis - New York NY Eugene J. Lattuga - Bonita Springs FL
Assignee:
Elysee Beauty Products, Ltd. - Kwai Chung
International Classification:
A45D 702
US Classification:
132212, 132271, 57 13, 242593, 242594
Abstract:
An apparatus for wrapping hair with a cord is provided and according to one embodiment includes a housing; a main spindle operatively coupled to the housing and one or more cartridges with one cartridge being operatively coupled to the main spindle and the other cartridges being operatively coupled to one another. Each cartridge contains a cord that is dispensed and wrapped around hair as a result of the rotation of the main spindle.
David Leason - Chappaqua NY Edward J. Ellis - New York NY Eugene J. Lattuga - Bonita Springs FL
Assignee:
Elysee Beauty Products, Ltd. - Kwai Chung
International Classification:
A45D 702
US Classification:
132212, 132271, 57 13, 2425973, 242594, 242442
Abstract:
An apparatus for wrapping hair with a cord is provided and includes a housing; a main spindle operatively coupled to the housing and defining a main spindle bore for receiving cord and hair; a rotatable spool carrier and at least one spool. The spool carrier has a platform and a drive spindle operatively coupled to the main spindle so that rotation of the main spindle is translated into rotation of the platform. The drive spindle has guides for receiving cord and permitting the cord to be disposed through a bore extending through the drive spindle. The rotation of the main spindle causes cord to be dispensed through the one guide and the drive spindle bore and the main spindle bore, hair is disposed through the drive spindle bore and the main spindle bore, and the main spindle is rotated to wrap the hair with cord.
Apparatus For Combined Application Of Massage, Accupressure And Biomagnetic Therapy With Improved Steel Ball Supports
Patrick Bousfield - Middlesex, GB David Leason - Chappaqua NY, US Edward Ellis - New York NY, US Frank Leparik - Greenlawn NY, US
International Classification:
A61H015/00
US Classification:
601113000, 601129000, 601131000
Abstract:
An apparatus for applying massage, accupressure and biomagnetic therapy to a subject is provided and the apparatus includes a housing having a proximal end and a distal end; a motor disposed within the housing and having a shaft; and a magnet disposed within the housing about the shaft. The apparatus further includes a rotor rotatably supported by the shaft at the distal end of the housing. The rotor has an exterior face which is remote from the magnet and which defines a plurality of entrances, an opposing interior face proximate to the magnet, and a seat more proximate to the magnet than the interior face which is in communication with each of the entrances. Each seat is affixed relative to the rotor at one or more locations proximal to the exterior face. A plurality of metal balls are provided and which are seatable against the seat and retained within the entrances of the rotor by a magnetic field emanating from the magnet. Each ball has a center and is universally rotatable about its center. The seat is constructed and positioned so that it precludes contact of the metal balls with the magnet and counters forces applied to the balls when the apparatus applies therapy to the subject.
Combination Cocurrent And Countercurrent Staged Hydroprocessing With A Vapor Stage
Ramesh Gupta - Berkeley Heights NJ Henry Jung - Chatham Borough NJ Edward S. Ellis - Fairfax VA James J. Schorfheide - Baton Rouge LA Larry L. Iaccino - Friendwoods TX
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C10G 6500
US Classification:
208 59
Abstract:
A hydroprocessing process includes a cocurrent flow liquid reaction stage, a countercurrent flow liquid reaction stage and a vapor reaction stage in which feed components are catalytically hydroprocessed by reacting with hydrogen. Both liquid stages both produce a liquid and a vapor effluent, with the cocurrent stage liquid effluent the feed for the countercurrent stage and the countercurrent stage liquid effluent the hydroprocessed product liquid. Both liquid stage vapor effluents are combined and catalytically reacted with hydrogen in a vapor reaction stage, to form a hydroprocessed vapor. This vapor is cooled to condense and recover a portion of the hydroprocessed hydrocarbonaceous vapor components as additional product liquid. The uncondensed vapor is rich in hydrogen and is cleaned up if necessary, to remove contaminants, and then recycled back into the cocurrent stage as hydrogen-containing treat gas. Fresh hydrogen is introduced into the countercurrent stage and the countercurrent stage effluent contains sufficient, and preferably all of the hydrogen for the vapor stage reaction.
Hydroprocessing Of Petroleum Fractions With A Dual Catalyst System
Ramesh Gupta - Berkeley Heights NJ Edward S. Ellis - Basking Ridge NJ William Ernest Lewis - Baton Rouge LA
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C10G 4500
US Classification:
208 89
Abstract:
Hydrocarbonaceous feedstocks admixed with a flow-through catalyst and hydrogen are hydroprocessed in a hydroprocessing reactor containing a captive hydroprocessing catalyst. The flow-through catalyst is continually withdrawn with the hydroprocessed feed from the hydroprocessing reactor. The flow-through catalyst may be an FCC, hydrocracking, isomerization or ring-opening catalyst. In a preferred embodiment, the captive hydroprocessing catalyst contains Co, Ni and/or Mo on an alumina base and the flow-through catalyst is an FCC zeolitic catalyst which is withdrawn with the hydroprocessed feed from the hydroprocessing reactor and then sent to an FCC unit.
Integrated Staged Catalytic Cracking And Staged Hydroprocessing Process
Ramesh Gupta - Berkeley Heights NJ Edward S. Ellis - Basking Ridge NJ
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
C10G 6902 C10G 6904
US Classification:
208 76
Abstract:
Disclosed is a catalytic cracking process that includes more than one catalytic cracking reaction step. The process integrates catalytic cracking steps with hydroprocessing in order to maximize olefins production, distillate quality and octane level of the overall cracked product. Preferably, one hydroprocessing step is included between the cat cracking reaction steps, and a portion of the hydroprocessed products, i. e. , a naphtha and mid distillate fraction, is combined with cracked product for further separation and hydroprocessing. It is also preferred that the first catalytic cracking reaction step be a short contact time reaction step.
Ramesh Gupta - Berkeley Heights NJ David C. Dankworth - Whitehouse Station NJ Dennis D. Fleming - East Horsley, GB Edward S. Ellis - Basking Ridge NJ James J. Schorfheide - Baton Rouge LA
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
B01J 804
US Classification:
422191
Abstract:
A reaction vessel for processing liquid petroleum or chemical streams wherein the stream flows countercurrent to the flow of a treat gas, such as a hydrogen-containing gas, in at least one interaction zone. The reaction vessel contains vapor, and optionally liquid, passageways to bypass one or more packed beds, preferably catalyst beds. This permits more stable and efficient vessel operation.
Two Stage Hydroprocessing With Vapor-Liquid Interstage Contacting For Vapor Heteroatom Removal
Henry Jung - Chatham Borough NJ Ramesh Gupta - Berkeley Heights NJ Edward S. Ellis - Basking Ridge NJ William E. Lewis - Baton Rouge LA
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
C10G 4502
US Classification:
208210
Abstract:
A hydroprocessing process includes two hydroprocessing reaction stages, both of which produce a liquid and a vapor effluent, and a liquid-vapor contacting stage. The first stage vapor effluent contains impurities, such as heteroatom compounds, which are removed from the vapor by contact with processed liquid effluent derived from one or both reaction stages and, optionally, also liquid recovered from processed vapor. The first and contact stage liquid effluents are passed into the second stage to finish the hydoprocessing. The contact and second stage vapor effluents are cooled to recover additional hydroprocessed product liquid.
Tekpro Services Dinwiddie, VA Nov 2012 to Dec 2014 Mailroom ClerkNYC Board of Elections Queens, NY Jun 2010 to Oct 2012 Mailroom ClerkWalgreens Brooklyn, NY Jun 2008 to Oct 2010 Head Of StockRGIS Queens, NY Dec 2007 to Mar 2010 Inventory SpecialistLaborerQueens, NY Jul 2007 to Nov 2007
Aug 2011 to 2000 Management traineeLittler Mendelson P.C. Washington, DC Jun 2011 to Aug 2011 Data InputInternal Revenue Service Crystal City, VA Jun 2010 to Aug 2010 Volunteer Intern
Education:
Morehouse College Atlanta, GA May 2011 Bachelor of Arts in Business Administration
Skills:
Personnel management, Microsoft office, Sales advise, interpersonal communication
MMC Healthworks 988 Oak Rdg Tpke STE L50, Oak Ridge, TN 37830 8658354320 (phone), 8658354328 (fax)
Education:
Medical School University of Tennessee College of Medicine at Memphis Graduated: 1979
Languages:
English
Description:
Dr. Ellis graduated from the University of Tennessee College of Medicine at Memphis in 1979. He works in Oak Ridge, TN and specializes in Occupational Medicine and Internal Medicine. Dr. Ellis is affiliated with Methodist Medical Center.
Darby & Darby, Professional Corporation 805 Third Avenue, New York, NY 10022 2125277704 (Office)
Licenses:
New York - Currently registered 1995
Education:
Franklin Pierce Law Center Degree - JD - Juris Doctor - Law Graduated - 1996 Bates College Degree - BS - Bachelor of Science - Chemistry Graduated - 1993
Specialties:
Intellectual Property - 80% Life Sciences / Biotechnology - 20%
Associations:
Connecticut Bar Association - Member Massachusetts Bar Association - Member