Dr. Jacobson graduated from the Northwestern University Feinberg School of Medicine in 1964. He works in Fort Lauderdale, FL and specializes in Endocrinology, Diabetes & Metabolism. Dr. Jacobson is affiliated with Memorial Regional Hospital.
Renin Associates 6 Essex Ctr Dr STE 306, Peabody, MA 01960 (978)5310677 (phone), (978)5315676 (fax)
Education:
Medical School SUNY Upstate Medical University Graduated: 1991
Procedures:
Dialysis Procedures
Conditions:
Acute Renal Failure Chronic Renal Disease Kidney Cancer Nephrotic Syndrome
Languages:
English
Description:
Dr. Jacobson graduated from the SUNY Upstate Medical University in 1991. He works in Peabody, MA and specializes in Nephrology.
Name / Title
Company / Classification
Phones & Addresses
Mitchell L. Jacobson President
Category-5 Entertainment, Inc
310 W 55 St, New York, NY 10019
Mitchell Jacobson Principal
Atlanta Mitchmar Properties Inc Nonresidential Building Operator
152 W 57 St, New York, NY 10019
Mitchell Jacobson Trustee
Nyu College/University
120 Sullivan St, New York, NY 10012
Mitchell L. Jacobson Dermatology, Medical Doctor
Michael Jacobs MD Dermatologist
407 E 70 St, New York, NY 10021 (212)7727190
Mitchell Jacobson
BSJ, LLC
152 W 57 St, New York, NY 10019 C/O Jfi - 152 West 57 St, New York, NY 10019
Mitchell Jacobson PRESIDENT
BERLIN TOOL SUPPLY PROPERTIES CO., INC
C/O Jfi, New York, NY 10019 75 Maxess Rd, Melville, NY 11747 1885 Muttontown Rd, Syosset, NY 11791
Mitchell Jacobson Director, President
MITCHMAR HOUSTON PROPERTIES INC
152 W 57 St FL 56 C/O JFI, New York, NY 10019 Attn: Lisa Salvaggio, Austin, TX 78701 C/O Jfi 152 W 57 St 56, New York, NY 10019 75 Maxess Rd, Melville, NY 11747
Mitchell Jacobson PRES
MILFORD INDUSTRIAL TOOL SUPPLY CO., INC
C/O Jfi, New York, NY 10019 75 Maxess Rd, Melville, NY 11747 67 Feeks Ln, Locust Valley, NY 11560
Us Patents
Two-Stage Process For Converting Residua To Gasoline Blendstocks And Light Olefins
A two-stage process for converting petroleum residua and other low value oils to high valued gasoline blendstocks and light olefins. The first stage is comprised of a thermal process unit containing a reaction zone comprised of a horizontal moving bed of fluidized hot particles operated at temperatures from about 500 to 600Â C. and having a short vapor residence time, and the second stage is comprised of a catalytic conversion zone operated at a temperature of about 525Â C. to about 650Â C. , and also having a short vapor residence time, preferably shorter than that of the first stage reaction zone.
Process For Deasphalting Residua By Reactive Recycle Of High Boiling Material
Mitchell Jacobson - Fairfax VA Willibald Serrand - Buxheim, DE Norman H. Sweed - Berkeley Heights NJ Hans J. M. Weiss - Oberursel, DE Ingo W. Dreher - Oberursel, DE Udo Zentner - Griesheim, DE Jorg H. Schmalfeld - Bad Homburg, DE
Assignee:
ExxonMobil Research and Engineering Company - Annandale NJ
International Classification:
C10C 302
US Classification:
208309, 208 39, 208 40
Abstract:
An improved process for deasphalting a residua feedstock by use of a short vapor residence time process unit comprised of a horizontal moving bed of fluidized and/or stirred hot particles. The vapor phase product stream from said process unit is passed to a soaker drum where a high boiling fraction is separated and recycled to the process unit after undergoing reactions causing molecular weight growth. This reactive recycle using the soaker drum results in substantially improved qualities of the liquid products compared with what is achieved by once-through residua deasphalting process alternatives.
Martin L. Gorbaty - Westfield NJ, US Michael Siskin - Randolph NJ, US Mitchell Jacobson - Fairfax VA, US
Assignee:
ExxonMobil Research and Engineering Company - Annandale NJ
International Classification:
C10G 11/14
US Classification:
208113, 208106, 208127, 585648
Abstract:
The present invention relates to a process for increasing the capacity for processing residua and obtaining higher yields of liquids having an average boiling point equal to or less than about 510 C. A residual feedstock is introduced with recycled product asphaltenes into a short vapor contact time thermal process unit wherein the vaporized product is sent to a fractionator zone to produce a 510 C. fraction and a 510 C. fraction. The 510 C. fraction is sent to a solvent extraction zone to produce an asphaltene-rich fraction that is recycled to the short vapor contact time thermal process unit.
Two-Stage Process For Obtaining Significant Olefin Yields From Residua Feedstocks
Willibald Serrand - Buxheim, DE Mitchell Jacobson - West Orange NJ
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C10G 928
US Classification:
208126
Abstract:
A two-stage process for obtaining a substantial amount of olefinic product from a residua feedstock. The first stage is comprised of a thermal process unit containing a reaction zone comprised of a horizontal moving bed of fluidized hot particles operated at temperatures from about 500. degree. to 600. degree. C. and having a short vapor residence time, and the second stage thermal conversion zone operated at a temperature of about 700. degree. C. to about 1100. degree. C. , and also having a short vapor residence time.
Integrated Residua Upgrading And Fluid Catalytic Cracking
Willibald Serrand - Buxheim, DE David G. Hammond - Madison NJ Mitchell Jacobson - West Orange NJ John F. Pagel - Cedar Knolls NJ Martin C. Poole - League City TX
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
C10G 5506
US Classification:
208 91
Abstract:
A process wherein a residuum feedstock is upgraded in a short vapor contact time thermal process unit comprised of a horizontal moving bed of fluidized hot particles, then fed to a fluid catalytic cracking process unit. Hot flue gases from the fluid catalytic cracking unit is used to circulate solid particles and to provide process heat to the thermal process unit.
Noel M. Seimandi - Brussels, BE Tony T. Cheng - Seabrook TX Willibald Serrand - Buxheim, DE Mitchell Jacobson - West Orange NJ Paul K. Ladwig - Randolph NJ John F. Pagel - Morris Plains NJ Michael R. Parrish - Morristown NJ Hans A. Weisenberger - Tervuren, BE
Assignee:
Exxon Chemical Patents Inc. - Houston TX
International Classification:
C07C 402 C10G 1100 C10G 926 C10B 5702
US Classification:
585648
Abstract:
A process for producing normally gaseous olefins from two different process units sharing common downstream quench and fractionation facilities, wherein one of the process units is a short contact time mechanically fluidized vaporization unit for processing petroleum residual feedstocks and the other is a conventional steam cracking unit.
David G. Hammond - Madison NJ Mitchell Jacobson - West Orange NJ John F. Pagel - Cedar Knolls NJ Martin C. Poole - Baton Rouge LA Willibald Serrand - Buxheim, DE
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C10G 928 C10G 1102 C10G 3510 C10C 300
US Classification:
208127
Abstract:
A process for deasphalting a residua feedstock by use of a short vapor contact time thermal process unit comprised of a horizontal moving bed of fluidized hot particles. It is preferred that a mechanical means be used to fluidize a bed of hot particles.
David G. Hammond - Madison NJ Mitchell Jacobson - West Orange NJ John F. Pagel - Cedar Knolls NJ Martin C. Poole - Baton Rouge LA Robert C. Green - Berkley Heights NJ Willibald Serrand - Buxheim, DE
Assignee:
Exxon Research & Engineering Company - Florham Park NJ
International Classification:
C10G 928 C10G 5104 C10B 5702
US Classification:
208127
Abstract:
An improved fluidized bed coking process wherein a residuum feedstock is introduced into a first stage comprised of a short vapor contact time reactor containing a horizontal moving bed of fluidized hot particles. Carbonaceous material is deposited onto the hot particles on contact with the hot particles, and a vapor product is produced. The hot particles, containing the carbonaceous deposits, are fed to a second stage fluidized bed coking process.
Jana, an investment advisory firm, is Agrium Inc.'s biggest shareholder. The company said Monday that its board nominees include David Bullock, Stephen Clark, Mitchell Jacobson, and Lyle Vanclief. It also includes Jana managing partner Barry Rosenstein.