Process for treating oil sludge

• US 4,985,131 A
• Filed: 11/21/1989
• Issued: 01/15/1991
• Est. Priority Date: 06/30/1988
• Status: Expired due to Fees

• Current Assignee: The Thermal Waste Management
• Original Assignee: The Thermal Waste Management
• Inventors: Lane, George M.
• Primary Examiner(s): MCFARLANE, ANTHONY R
• Application Number:
  US07/440,471
• Time in Patent Office: 420 Days
• Field of Search: 208/13, 208/179, 208/184, 208/186, 44/24, 201/25, 201/44, 201/3, 210/609, 585/240
• US Class Current: 208/13
• 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: C10B 55/00 Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material cracking oils C10G

Abstract

A process for treating pretroleum refinery sludge to produce a coke-like residue product wherein an oily petroleum refinery sludge containing organic solid material boiling above 1000° F. and water is heated to a temperature above the boiling point of water and below the thermal cracking temperature of hydrocarbons and water in the sludge forms steam used to steam strip any light hydrocarbons from the organic solid material which is recovered as a solid coke-like residue product.

Claims

1. A process for treating petroleum refinery sludge to produce a solid residue product which process comprises:

(a) forming a feed-stream of an oily petroleum refinery sludge containing organic solid material boiling about 1000°

F. and water;

(b) pretreating said feed-stream to adjust the water content thereof to between about 5% and about 25%, based upon the total weight of the resulting pre-treated feed-stream;

(c) introducing the resulting pre-treated feed-stream into a thermal sludge drier wherein said pre-treated feed-stream is indirectly heated by a heat transfer medium;

(d) heating said pretreated feed-stream in said drier to a temperature above the boiling point of water and below the temperature at which thermal cracking of said feed-stream occurs;

(e) maintaining the heated feed-stream in a nonoxidative atmosphere in said sludge drier for a time sufficient for said water in said feed-stream to form steam and for said steam to strip any light hydrocarbons from the solid material in said feed-stream to form a solid residue;

(f) separating a hydrocarbon-water vapor stream from said solid material; and

(g) recovering said solid material as a solid residue product having a BTU content between about 3000 and 10,000 BTU/lb.

2. The process of claim 1, wherein said feed-stream is API separator sludge, heat exchange bundle cleaning sludge, tank bottoms sludge, slop oil emulsion solids, dissolved air flotation float or any mixture thereof.

3. The process of claim 1 wherein said pre-treated feed-stream is introduced into and heated in a hollow-screw, jacketed-trough sludge drier.

4. The process of claim 1, wherein the solid material content of said pretreated feed-stream is from about 20% to about 75%, based upon the total weight of the pretreated feed stream.

5. The process of claim 1, wherein said pretreatment comprises passing said feed stream through a centrifuge, filter press or chemical treatment step effective to dewater said feed stream.

6. The process of claim 1, wherein said heat transfer medium is heated by the combustion of a hydrocarbon fuel, said feed stream is dewatered to adjust the water content thereof, the dewatered feed-stream is preheated in a hollow-screw, jacketed-trough thermal preheater, and hot flue gas generated by combustion of said hydrocarbon fuel is used to indirectly heat said dewatered feed-stream in said preheater.

7. The process of claim 1, further comprising preheating said pre-treated feed stream prior to introducing said pre-treated feed stream into said sludge drier.

8. The process of claim 5, wherein said pre-treatment comprises passing said feed stream through a centrifuge.

9. The process of claim 7, wherein said pre-treated feed stream is preheated with a heat medium heated with hot flue gas generated in the combustion of fuel used to heat said heat transfer medium, prior to introducing said pre-treated feed-stream into said sludge drier.