Fuel making process

• US 4,014,661 A
• Filed: 03/17/1975
• Issued: 03/29/1977
• Est. Priority Date: 03/17/1975
• Status: Expired due to Term

• Current Assignee: Texaco Incorporated (Chevron Corp.)
• Original Assignee: Texaco Incorporated (Chevron Corp.)
• Inventors: Cole, Edward L., Franz, William F., Hess, Howard V.
• Primary Examiner(s): Wyman, Daniel E.
• Assistant Examiner(s): Harris-Smith, Mrs. Y.
• Application Number:
  US05/558,870
• Time in Patent Office: 743 Days
• Field of Search: 201/2.5, 201/25, 201/63, 44/51, 208/8
• US Class Current: 44/282
• CPC Class Codes: C10B 49/14 with hot liquids, e.g. molten metals
• CPC Class Codes: C10B 53/00 Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form wet carbonising of peat C10F
• CPC Class Codes: C10L 1/324 Dispersions containing coal, oil and water

Abstract

Disclosed is a process for making a hydrocarbon coke slurry fuel by coking carbonaceous materials in the liquid phase under autogenous pressure to form coke which is then extracted with a combustible hydrocarbon at high temperatures and pressures to produce a dense slurry of coke in the hydrocarbon suitable for use as a fuel.

Claims

1. A process for producing a coke-containing fuel, comprising coking a carbonaceous material in the liquid phase under a pressure of 300 to 3200 psig at a temperature of 400°

to 700°

F for 0.5 minutes to 3 hours to form gases, hot liquid and liquid-containing coke;

separating said coke from said liquid and gases;

drying said coke by extraction with a combustible hydrocarbon under a pressure of between 300 and 3200 psig at a temperature of between 400° and

700°

F to remove said liquid from said coke and form a hydrocarbon solution of water and a dense slurry of dry coke in said hydrocarbon suitable for burning.

2. The process as in claim 1, including the further steps of cooling said hydrocarbon solution by heat exchange with cooled liquid from said coking to form a water phase and a hydrocarbon phase and recycling said hydrocarbon phase for reuse as an extractant.

3. The process as in claim 1, including the further step of preheating said carbonaceous material with said hot liquid.

4. The process of claim 1, wherein said hydrocarbon has an API gravity of 18 to 40.

5. The process of claim 1 wherein said hydrocarbon is selected from the group of cracked distillates, vacuum gas oils, light and intermediate cycle oils, raffinates from the extraction of reformed naphthas and aromatic extracts.