Method and apparatus for cleaning fine waste material mixed with oil and water
OwnerLeonard A. Duvalinventor
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OwnerLeonard A. Duvalinventor
Estimating the term…
A mixture of solids, mostly finely divided, and oil, such as usually mixed with mill scale, and water is the feed material for this process. Most of the water is first drawn off. Then the material is fed through a plurality of mixers, and after each mixer the entire composition is passed through a separator, herein described as a dewetting apparatus, which separates the fine solids from the oil and returns the expended solvent upstream toward the feed point. The diminished volume of material then passes through a final dewetting screen where the solids are washed by a small stream of fresh solvent and the fine solids then pass through a dryer. All expended solvent is collected and passed through a fractionating still which separates the recovered oil, for storage, and the solvent vapors pass through a condenser to a regenerated solvent storage tank. All of the expended solvent is saved and used over and over.
An apparatus for cleaning fine solid waste material mixed with oil and water, comprising one integrated system having at least two primary mixers and two primary dewetting separators and one final dewetting separator and three coacting centifugal pumps acting both for mixing and transportation of a slurry containing fine solid waste material and solvent, together with a final dryer of fine solids, a reservoir for expended solvent, a reservoir for regenerated solvent, and an evaporating still connected between said reservoirs, and a condenser for solvent vapors from said still, and conduit from said condenser to said regenerated solvent reservoir, and a storage tank for oil recovered from said fine solid waste material;
A method of cleaning fine solid waste material mixed with oil and water, comprising one intergrated system including (a) first decanting most of the water at a feed point, then (b) mixing with solvent said solids-oil-water material thoroughly in a first mixer, (c) returning excess expended solvent from said first mixer to said feed point, (d) then pumping the slurry of solids and solvents to a first dewetter-separator device, (e) transferring expended solvent from said first dewetter-separator device back to said first mixer, (f) transferring solids from said first dewetter-separator device to a second mixer, (g) thoroughly mixing with solvent these latter solids in the second mixer, (h) pumping the slurry of solids-solvent-water from said second mixer to a second dewetting-separator device, (i) transferring expended solvent from said second dewetting-separator device to said second mixer, (j) transferring solids from said second dewetting-separator device to a dewetting screen, (k) washing said solids on said dewetting screen with a small amount of clean solvent, (l) transferring expended solvent from said dewetting screen to said second mixer, (m) transferring solids from said dewetting screen to a dryer, (n) drying said solids in said dryer for use, (o) collecting all said expended solvent and passing it through a fractioning still and collecting therefrom the recovered oil, and (p) passing the solvent vapor through a condenser and to a regenerated solvent storage.
Dependencies are inferred from the claim text.