Upgrading of heavy hydrocarbons

• US 4,347,120 A
• Filed: 12/22/1980
• Issued: 08/31/1982
• Est. Priority Date: 12/22/1980
• Status: Expired due to Term

• Current Assignee: Conoco Incorporated (ConocoPhillips)
• Original Assignee: Conoco Incorporated (ConocoPhillips)
• Inventors: McConaghy, James R., Anderson, Ardis L.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): Chaudhuri, Olik
• Application Number:
  US06/219,006
• Time in Patent Office: 617 Days
• Field of Search: 208/50, 208/56, 208/107, 208/108, 423/655, 252/375, 252/377, 252/373
• US Class Current: 208/50
• CPC Class Codes: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G
• CPC Class Codes: C10G 47/34 Organic compounds, e.g. hydrogenated hydrocarbons
• CPC Class Codes: C10G 69/02 plural serial stages only

Abstract

Heavy hydrocarbonaceous materials are converted to distillate products and pitch in a hydrogen donor diluent cracking process, and the pitch is utilized as feed to a delayed coker. Green coke is calcined in a vertical shaft kiln, and steam is injected into the bottom of the kiln to produce hydrogen by reaction of steam with coke. The hydrogen is drawn from the kiln and used to hydrogenate recycle donor solvent for the cracking step. High sulfur coke can be desulfurized in the kiln, and distillate products in addition to donor solvent can be hydrotreated using hydrogen from the kiln.

Claims

1. A process for upgrading a heavy liquid hydrocarbonaceous material comprising:

(a) subjecting said heavy liquid hydrocarbonaceous material to a hydrogen donor diluent cracking step;

(b) fractionating the products from said cracking step and subjecting the bottoms stream from the fractionation to delayed coking;

(c) passing delayed coke to a top fed internally fired moving bed vertical shaft kiln;

(d) introducing combustion air into said kiln to provide a combustion zone;

(e) maintaining upward gas flow in said kiln and recovering flue gas including nitrogen from the top of the kiln;

(f) introducing steam to the lower portion of said shaft kiln whereby hydrogen is produced by reaction of steam with descending hot coke;

(g) recovering a substantially nitrogen-free hydrogen-rich gas stream from said shaft kiln from a level above the steam injection level and below the combustion air injection level; and

(h) utilizing hydrogen from said hydrogen-rich gas stream to hydrogenate hydrogen-depleted recycle donor solvent for use in said donor cracking step.

2. The process of claim 1 wherein said hydrogen-depleted recycle donor solvent is a product of said fractionating step.

3. The process of claim 2 wherein said heavy hydrocarbonaceous material is a high sulfur material, and said shaft kiln is operated at desulfurizing conditions.

4. The process of claim 3 wherein a portion of said hydrogen is utilized to hydrotreat both recycle donor solvent and other distilled liquids from said fractionating step.

5. The process of claim 4 wherein carbon oxides are removed from said hydrogen-rich gas stream prior to utilizing said hydrogen.