US 4,839,022 AGranted

Method and apparatus for treating oil-water-solids sludges and refinery waste streams

AssigneeAtlantic Richfield Company

InventorJames L. Skinner

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Abstract

Heavy hydrocarbon containing sludges such as refinery waste streams, oil storage tank sludges and marine oil tanker ballast are treated by passing the sludges in a flow stream through an indirect dryer to vaporize liquids having a boiling point at atmospheric pressure of less than about 700.degree. F. and to provide substantially dried solid particles discharged from the dryer. The dried particles, containing heavy hydrocarbons as a coating or as a part of the solids, are conducted to a combustor/oxidizer and exposed to a high velocity flow stream of oxygen containing gas, typically low pressure forced air, to burn the residual hydrocarbons in the solids and to reduce heavy metals and the like to oxides thereof. A sludge handling system includes a rotary disk type indirect dryer connected to a lift pipe type combustor/oxidizer for thorough exposure of the dried solids to an oxygen containing atmosphere. A centrifigal or cyclone type gas-solids separator receives the flow stream discharged from the lift pipe and a portion of the dried solids may be diverted after discharge from the dryer back to the dryer inlet to reduce the moisture content of the sludge flow stream introduced to the dryer to minimize caking and clogging of the dryer itself.

Claims7

Dependent claims

A method for treating a sludge stream comprising a quantity of solids particles including particles of heavy metals and heavy hydrocarbon substances which are coated on said solids including said heavy metals, said method comprising the steps of:

providing a dryer apparatus for receiving said sludge stream and including means for discharging vapors of liquids boiled off in said dryer, means for discharging solids comprising particles dried in said dryer and heat exchange surface means operable to dry said sludge substantially only by contact with said sludge such that substantially only dried solids of said sludge are discharged by said means for discharging solids and substantially only vapors of said liquids are discharged through said means for discharging vapors;
providing oxidizer means for receiving dried solids and exposing said dried solids to an oxygen containing gas;
introducing said sludge stream into said dryer and heating said sludge stream to evaporate substances having a boiling point less than about 700.degree. F.;
discharging vapors generated in said dryer from heating said sludge stream in said dryer;
discharging dried solids from said dryer and introducing said dried solids to said oxidizer means;
subjecting all of said dried solids in said oxidizer means to an oxygen-containing gas by passing a gas flow stream through said oxidizer means at a sufficient flow rate to thoroughly mix said dried solids and oxidize hydrocarbons coated on said dried solids having a boiling temperature greater than about 500.degree. F. and to reduce the portion of said dried solids which comprise heavy metals selected from a group consisting of chromium, vanadium and nickel, to oxides of said heavy metals;
conducting gases from said oxidizer means;
and
conducting substantially hydrocarbon free, oxidized and dried solids from said oxidizer means for disposal.

6 more elements

providing a dryer apparatus for receiving said sludge stream and including means for discharging vapors of liquids boiled off in said dryer, means for discharging solids comprising particles dried in said dryer and heat exchange surface means operable to dry said sludge substantially only by contact with said sludge such that substantially only dried solids of said sludge are discharged by said means for discharging solids and substantially only vapors of said liquids are discharged through said means for discharges vapors;
providing a combustor/oxidizer apparatus for receiving dried solids and including means for discharging said dried solids from said combustor/oxidizer apparatus;
introducing said sludge stream into said dryer and heating said sludge stream to evaporate substances having a boiling point less than about 700.degree. F.;
discharging vapors generated in said dryer from heating said sludge stream in said dryer and condensing said vapors;
discharging dried solids from said dryer and introducing all of said dried solids to said combustor/oxidizer;
subjecting said dried solids in said combustor/oxidizer to an oxygen-containing gas flow stream by passing said gas flow stream through said combustor/oxidizer at a sufficient flow rate to lift said dried solids, thoroughly mix said dried solids and oxidize hydrocarbon substances coated on said dried solids and to reduce any of said dried solids which comprise heavy metals selected from a group consisting of chromium, vanadium, and nickel, to oxides of said heavy metals and wherein said dried solids are at a temperature in the range of about 700.degree. F. to 1100.degree. F. in said combustor/oxidizer;
conducting gases from said combustor/oxidizer;
and
conducting substantially hydrocarbon free, oxidized and dried solids away from said combustor/oxidizer for disposal.

6 more elements

Dependencies are inferred from the claim text.

Facts

Application: 06/796,349Filed 8 Nov 1985 · continuation in part
Priority: 3 Dec 1984
Granted: 13 Jun 1989
Term ends: Not estimatedThe source records don’t support an estimate.

Classification20 codes

F26B 17/20
With movement performed by rotating helical blades or other rotary conveyors which may be heated moving materials in stationary chambers , e.g.…:…
B01D 17/00
Separation of liquids, not provided for elsewhere
B01D 17/048
Breaking emulsions: by changing the state of aggregation
C02F 11/13
By de-watering, drying or thickening: by heating