Coal passivation process

• US 3,985,517 A
• Filed: 08/20/1975
• Issued: 10/12/1976
• Est. Priority Date: 08/20/1975
• Status: Expired due to Term

• Current Assignee: HRI, Inc. (Japan) (Canon Inc.)
• Original Assignee: Hydrocarbon Research Incorporated
• Inventors: Johnson, Clarence A.
• Primary Examiner(s): Dees, Carl F.
• Application Number:
  US05/606,258
• Time in Patent Office: 419 Days
• Field of Search: 44/1 R, 44/1 G, 44/6, 201/23, 201/31, 34/10
• US Class Current: 44/501
• CPC Class Codes: C10L 9/00 Treating solid fuels to improve their combustion
• CPC Class Codes: C10L 9/10 by using additives

Abstract

Low rank coals such as subbituminous or lignites containing more than about 10 weight percent moisture are dried and passivated against reabsorption of moisture in a fluidized bed by heating the particulate coal with a warm inert gas passing upwardly through the bed and simultaneously coating the warm particulate coal with a heavy liquid hydrocarbon material. Such coating aids in the removal of the moisture and prevents the reabsorption of moisture by the coal and thereby prevents consequential heating and possibly spontaneous ignition of the coal during its subsequent transportation or storage.

Claims

1. A process for passivating particulate pyrophoric low rank coals, in a fluidized treating vessel, wherein the material is simultaneously dried and coated with a hydrocarbon liquid, thereby rendering the material substantially resistant to reabsorption of moisture and adaptable for storage and shipment at ambient temperatures, comprising the steps of:

a. feeding the material to the treating vessel;

b. drying the material with a hot inert gas, maintained at a temperature sufficient to vaporize the moisture without devolatilizing the particulate material, said inert gas being introduced below the material in the treating zone and maintained at sufficient velocity to form a fluidized bed;

c. introducing a heavy liquid hydrocarbon into the treating vessel;

d. substantially uniformly coating the material with between about 0.5 to 2.5 weight percent of a heavy hydrocarbon liquid;

e. removing an effluent gas stream consisting essentially of water and hydrocarbons from the vessel;

f. withdrawing the hydrocarbon coated particulate material from the treating vessel.

2. The process of claim 1 wherein the fluidized bed temperature is maintained between 200°

and 500°

F and the pressure is maintained between 0 psig and 10 psig.

3. The process of claim 1 wherein a light condensed oil stream is withdrawn from the phase separation step (e) and at least a portion of the condensed oil is mixed with the heavy liquid hydrocarbon material as a carrier oil before being introduced into the fluidized bed.

4. The process of claim 1 wherein the gas stream withdrawn from the upper end of the treating zone is passed through a solids separation step before the cooling step, and the particulate fines removed therefrom are returned to the fluidized bed.

5. The process of claim 1 wherein the inert recycled gas is heated by a combustion type heater fired by a portion of the solid carbonaceous material and a portion of the flue gas produced therefrom is used as make-up for the inert fluidizing and heating gas.

6. The process of claim 1 wherein sufficient hydrocarbon liquid is introduced into the treating zone to coat the particulate solid material with 1.0 to 5.0 weight percent oil.

7. The process of claim 1 wherein a portion of the heavy liquid hydrocarbon material is introduced into the reaction zone in the upper portion of the fluidized bed.

8. The process of claim 1 wherein the pyrophoric particulate material is crushed to smaller than about 1/2-inch particle size.

9. The process of claim 1 wherein the water stream removed at step (e) is used to preheat the heavy liquid hydrocarbon material introduced into the fluidized bed.

10. The process of claim 9 wherein the cooled water from the liquid hydrocarbon preheating step is further used to partially cool the reactor effluent gas upstream of the phase separation step.

11. The process of claim 1 wherein the pyrophoric carbonaceous material is sized to between 1/8-inch and 3/8-inch, the pressure of the inert gas is 0.5 to 5.0 psig, the drying period is from 3 to 15 minutes, the temperature is between 200°

and 500°

F, the heavy hydrocarbon is a residual hydrocarbon having a boiling range above 650°

F which is sprayed on the carbonaceous material and the passivated material is recovered with from 1.0 to 2.0 weight percent of oil coating and a residual moisture of less than 5.0 weight percent.