CA2352887A1 - Production de distillats a faible teneur en soufre et en aromatiques - Google Patents

Production de distillats a faible teneur en soufre et en aromatiques Download PDF

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Publication number
CA2352887A1
CA2352887A1 CA002352887A CA2352887A CA2352887A1 CA 2352887 A1 CA2352887 A1 CA 2352887A1 CA 002352887 A CA002352887 A CA 002352887A CA 2352887 A CA2352887 A CA 2352887A CA 2352887 A1 CA2352887 A1 CA 2352887A1
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CA
Canada
Prior art keywords
liquid
stream
reaction
reaction stage
vapor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CA002352887A
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English (en)
Other versions
CA2352887C (fr
Inventor
Edward Stanley Ellis
Henry Jung
William Ernest Lewis
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ExxonMobil Technology and Engineering Co
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority claimed from PCT/US1999/028790 external-priority patent/WO2000034416A1/fr
Publication of CA2352887A1 publication Critical patent/CA2352887A1/fr
Application granted granted Critical
Publication of CA2352887C publication Critical patent/CA2352887C/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

L'invention concerne un procédé d'hydrotraitement d'un distillat liquide hydrotraité, consistant à introduire le flux d'alimentation dans une cuve (R1) de réaction via le conduit (10), ainsi qu'un gaz de traitement renfermant de l'hydrogène via le conduit (12). Le flux produit à phases liquide et vapeur combinées sort de la cuve (R1) de réaction via le conduit (16). Le flux produit en phase vapeur est collecté en tête de distillation via le conduit (20). Le produit de réaction liquide traverse la cuve (R2) de réaction via le conduit (20) puis, s'écoule vers le bas, à travers les zones de réaction (22a) et (22b) ou la zone de réaction (R2).
CA2352887A 1998-12-08 1999-12-07 Production de distillats a faible teneur en soufre et en aromatiques Expired - Lifetime CA2352887C (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US11134698P 1998-12-08 1998-12-08
US60/111,346 1998-12-08
PCT/US1999/028790 WO2000034416A1 (fr) 1998-12-08 1999-12-07 Production de distillats a faible teneur en soufre et en aromatiques

Publications (2)

Publication Number Publication Date
CA2352887A1 true CA2352887A1 (fr) 2000-06-15
CA2352887C CA2352887C (fr) 2010-07-27

Family

ID=22337992

Family Applications (1)

Application Number Title Priority Date Filing Date
CA2352887A Expired - Lifetime CA2352887C (fr) 1998-12-08 1999-12-07 Production de distillats a faible teneur en soufre et en aromatiques

Country Status (1)

Country Link
CA (1) CA2352887C (fr)

Also Published As

Publication number Publication date
CA2352887C (fr) 2010-07-27

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Effective date: 20191209