Olefin production utilizing whole crude oil/condensate feedstock and hydrotreating

• US 20080277314A1
• Filed: 05/08/2007
• Published: 11/13/2008
• Est. Priority Date: 05/08/2007
• Status: Abandoned Application

• Current Assignee: Equistar Chemicals LP (Lyondellbasell Industries NV)
• Original Assignee: Equistar Chemicals LP (Lyondellbasell Industries NV)
• Inventors: Halsey, Richard B.
• Application Number:
  US11/800,824
• Publication Number:
  US 20080277314A1
• Time in Patent Office: Days
• US Class Current: 208/108
• CPC Class Codes: C10G 45/02 to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
• CPC Class Codes: C10G 69/06 including at least one step of thermal cracking in the absence of hydrogen
• CPC Class Codes: C10G 9/005 Coking (in order to produce liquid products mainly)

Abstract

A method for thermally cracking a feed composed of whole crude oil and/or natural gas condensate using a vaporizer to vaporize the feed before cracking same, recovering pyrolysis gas oil from the cracked feed, subjecting the recovered pyrolysis gas oil to hydrotreating to form a hydrotreated product, and passing the hydrotreated product to the vaporizer as additional thermal cracking feed.

Claims

1. In a method for operating an olefin production plant that employs a pyrolysis furnace to severely thermally crack hydrocarbon containing material for subsequent processing of the thus cracked product in said plant which method of plant operation includes 1) providing at least one of whole crude oil and natural gas condensate as said hydrocarbon containing material, 2) submitting said whole crude/condensate feed to a vaporization step wherein said feed is substantially vaporized, and 3) feeding said substantially vaporized feed to said pyrolysis furnace, said plant further employing an oil quench step on said cracked material product to form a pyrolysis gas oil stream, the improvement comprising passing at least part of said pyrolysis gas oil stream to a hydrotreating step, hydrotreating said pyrolysis gas oil to form a hydrotreated product, and returning at least part of said hydrotreated product as feed to said vaporization step.

2. The method of claim 1 wherein a liquid stream is removed from said vaporization step and passed as feed to said hydrotreating step.

3. The method of claim 1 wherein said pyrolysis gas oil stream boils in the range of from about 380 to about 700 F

4. The method of claim 1 wherein said hydrotreating step is carried out at a temperature of from about 640 to about 840 F, pressure of from about 1,200 to about 5,000 psig, weight hourly space velocity of from about 0.1 to about 5, and hydrogen flow of from about 100 to about 200 cubic meters per ton of hydrocarbon feed.