Hydrogen donor cracking with donor soaking of pitch

• US 4,430,197 A
• Filed: 04/05/1982
• Issued: 02/07/1984
• Est. Priority Date: 04/05/1982
• Status: Expired due to Fees

• Current Assignee: Conoco Incorporated (ConocoPhillips)
• Original Assignee: Conoco Incorporated (ConocoPhillips)
• Inventors: Romine, Hugh E., Poynor, Paul C.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): Maull, Helane E.
• Application Number:
  US06/365,721
• Time in Patent Office: 673 Days
• Field of Search: 208/131, 208/56, 208/67
• US Class Current: 208/56
• CPC Class Codes: C10G 47/34 Organic compounds, e.g. hydrogenated hydrocarbons
• CPC Class Codes: C10G 51/023 only thermal cracking steps

Abstract

A hydrogen donor diluent cracking process in which the pitch fraction from the cracking step is heat soaked in the presence of hydrogen donor solvent and then returned to the cracking coil.

Claims

1. In a hydrogen donor diluent cracking process in which a heavy hydrocarbonaceous material is thermally cracked in a cracking coil in the presence of hydrogen donor solvent, and in which spent donor is separated from cracked products, rehydrogenated and recycled to the cracking step, the improvement wherein at least part of the pitch fraction from the cracked products is heat soaked in a soaking tank separate from said cracking coil in the presence of hydrogenated donor solvent for a time and at a temperature sufficient to substantially reduce the amount of material in said pitch which is insoluble in pentane and said heat-soaked pitch is returned to said cracking coil.

2. The process of claim 1 wherein the entire pitch fraction from said cracked products is heat soaked.

3. The process of claim 1 wherein said part of said pitch fraction is heat soaked at a temperature of from 500°

to 850°

F.

4. The process of claim 3 wherein said part of said pitch fraction is heat soaked for a period of from 1 to 3 hours at a temperature of from 600 to 700°

F.

5. The process of claim 3 wherein said part of said pitch fraction is heat soaked until the amount of pentane insolubles in said pitch fraction is reduced by more than 50 percent.

6. The process of claim 3 wherein said part of said pitch fraction is heat soaked in the presence of from 0.5 to 2.0 volumes of hydrogen donor solvent per volume of pitch treated.