Oil C

NourEddine Fakhri

CEO chez MYRSA D&C LLC

*******@****.**

Expérience

President /Chief Executive Officer (CEO) at MYRSA D&C LP

juin 2010 - Poste actuel (3 ans 9 mois)

Philadelphia Waste petroleum refinery

Chief executive officer ( CEO) at GIF

janvier 1992 - Poste actuel (22 ans 2 mois)

Waste petroleum re refinery

Petroleum Products

1 recommandation disponible sur demande

Secretaire General at Groupe Petromax

février 1988 - septembre 1992 (4 ans 8 mois)

Brevets

process for the treatment of waste oil

Brevet - États-Unis US 7208079 B2 Publication 24 avril 2007

Inventeurs : NourEddine Fakhri

A process for the treatment of waste oil comprises the steps of (a) supplying a stream of the waste oil to a

dehydrator to dehydrate the waste oil and obtain a stream of dehydrated waste oil; (b) supplying the stream of

dehydrated waste oil to a fractionated distillation column having a lower tray, an upper tray and a middle tray

therebetween, wherein the lower tray is operated at a temperature of 370 to 390 C. under a sub-atmospheric

pressure of 50 to 100 mmHg, the middle tray is operated at a temperature of 265 to 280 C. under a

sub-atmospheric pressure of 35 to 45 mmHg and the upper tray is operated at a temperature of 100 to 110 C.

under a sub-atmospheric pressure of 30 to 40 mmHg; (c) withdrawing from the distillation column a bottom

product comprising a bituminous material; (d) withdrawing a first side stream from the distillation column

between the first and second trays, the first side stream comprising a heavy oil having a viscosity of 130 to

180 cSt at 40 C.; (e) withdrawing a second side stream from the distillation column between the second and

third trays, the second side stream comprising a light base oil having a viscosity of 38 to 43 cSt at 40 C.; (f)

withdrawing a third side stream from the distillation column above the third tray, the third side stream

comprising diesel having a viscosity of 4 to 7 cSt at 40 C.; (g) withdrawing from the distillation column an

overhead product comprising naphtha; and (h) recovering the bituminous material, heavy oil, light base oil,

diesel and naphtha. The process according to the invention enables one to produce refined oil which is

substantially free of heavy metal contaminants.

Page1

Publications

Process for the treatment of waste oils

24 avril 2007

Auteur(s) : NourEddine Fakhri

A process for the treatment of waste oil comprises the steps of (a) supplying a stream of the waste oil to a

dehydrator to dehydrate the waste oil and obtain a stream of dehydrated waste oil; (b) supplying the stream of

dehydrated waste oil to a fractionated distillation column having a lower tray, an upper tray and a middle tray

therebetween, wherein the lower tray is operated at a temperature of 370 to 390 C. under a sub-atmospheric

pressure of 50 to 100 mmHg, the middle tray is operated at a temperature of 265 to 280 C. under a

sub-atmospheric pressure of 35 to 45 mmHg and the upper tray is operated at a temperature of 100 to 110 C.

under a sub-atmospheric pressure of 30 to 40 mmHg; (c) withdrawing from the distillation column a bottom

product comprising a bituminous material; (d) withdrawing a first side stream from the distillation column

between the first and second trays, the first side stream comprising a heavy oil having a viscosity of 130 to

180 cSt at 40 C.; (e) withdrawing a second side stream from the distillation column between the second and

third trays, the second side stream comprising a light base oil having a viscosity of 38 to 43 cSt at 40 C.; (f)

withdrawing a third side stream from the distillation column above the third tray, the third side stream

comprising diesel having a viscosity of 4 to 7 cSt at 40 C.; (g) withdrawing from the distillation column an

overhead product comprising naphtha; and (h) recovering the bituminous material, heavy oil, light base oil,

diesel and naphtha. The process according to the invention enables one to produce refined oil which is

substantially free of heavy metal contaminants.

Formation

Université de Montréal

Can PHD, Macro economie, 1984 - 1987

Université Laval

Page2

NourEddine Fakhri

CEO chez MYRSA D&C LLC

*******@****.**

1 personne a recommandé NourEddine

""

Philip Lewis, a été client de NourEddine

Prenez contact avec NourEddine sur LinkedIn

Page3

Contact this candidate