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US4097369A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for reclaiming used hydrocarbon oils

Assignee: Schmids Adolf Erben AG
•
Filing: 1976-02-27
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Granted: 1978-06-27
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Expires: 1996-02-27
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Abstract

Abstract A process for reclaiming used hydrocarbon oils through prepurification by means of coagulation, adsorption, filtration, distillation, and after-treatment, wherein said oils are prepurified and then dehalogenated, fractionally distilled and hydrogenated. It is preferred that for the prepurification, said coagulation and said adsorption are carried out by means of a hydroxide or hydroxide mixture, preferably aluminum and/or ferric hydroxide, in a proportion of 0.5 - 5.0% by weight, preferably 1-2% by weight, of hydroxide relative to said used oil at a reaction temperature of from 20° - 200° C, preferably from 50 to 150° C, said hydroxide or hydroxides being produced directly in said used oil in the presence of water or being introduced into said used oil in the form of an aqueous slurry. It is also preferred that the dehalogenation and accompanying desulfurization are carried out through treatment of said oil with an alkali metal, especially Na or K, an alkaline earth metal, especially Mg or Ca, an alkali, alkaline earth or aliminum alcoholate, an alkali hydride or amide, an organic base, especially pyridine or piperidine, or with metallic aluminum or anhydrous aluminum chloride, in a proportion of the respective treatment agent of from 1 to 2000 moles per metric ton of said oil in the absence of air and humidity at a reaction temperature of from 15° - 300° C.

Inventors

  • 👤 Eckhard Ebel
  • 👤 Hans-Rudolf Kobel
  • 👤 Ernst Widmer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 16:07
CPC Classifications
C; C10; C10M; C10M175/00; C10M175/0016

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 92 words
In a process of reclaiming used hydrocarbon oils from which water and light hydrocarbons have been removed by distillation and wherein the oils are prepurified either by coagulation, adsorption, a combination of coagulation and adsorption, by filtration, or by vacuum distillation, with subsequent fractional distillation and after-treatment, the improvement which comprises subjecting the prepurified product to dehalogenation, partial desulfurization, and removal of residual metal contents prior to the fractional distillation and after-treatment by contacting said prepurified oil with an agent selected from the group consisting of alkali metals and alkali metal hydrides.
Claim 2
Dependent Claim 44 words
The process of claim 1, wherein the prepurification is by coagulation with a solvent selected from the group consisting of low molecular weight esters, ethers, ketones, and mixtures thereof, in the ratio of used oil to solvent of from 3:1 to 1:10 by weight.
Claim 3
Dependent Claim 21 words
The process of claim 2, wherein the solvent is selected from the group consisting of ethyl acetate, acetone, and mixtures thereof.
Claim 4
Dependent Claim 17 words
The process of claim 2, wherein the ratio of used oil to solvent is 1:3 by weight.
Claim 5
Dependent Claim 58 words
The process of claim 1, wherein the adsorption step is carried out with an agent selected from the group consisting of an alkaline earth or heavy metal hydroxide or a mixture thereof in the proportion of from 0.5%-5.0% by weight of hydroxide relative to said used oil and at a temperature of from 20° C to 200° C.
Claim 6
Dependent Claim 22 words
The process of claim 5, wherein the proportion of hydroxide relative to the used oil is from 1% to 2% by weight.
Claim 7
Dependent Claim 22 words
The process of claim 5, wherein the adsorption step is carried out at a temperature of from 50° C to 150° C.
Claim 8
Dependent Claim 24 words
The process of claim 5, wherein the hydroxide is selected from the group consisting of calcium hydroxide, aluminum hydroxide, ferric hydroxide, and mixtures thereof.
Claim 9
Dependent Claim 55 words
The process of claim 1, wherein the step of dehalogenation, partial desulfurization, and removal of residual metal contents is carried out by contact with from 1 to 2000 moles of the treating agent per metric ton of oil, in the absence of air and humidity and at a temperature of from 15° to 300° C.
Claim 10
Dependent Claim 19 words
The process of claim 9, wherein the treating agent is selected from the group consisting of sodium and potassium.
Claim 11
Dependent Claim 14 words
The process of claim 10 wherein the temperature of treatment is about 250° C.
Claim 12
Dependent Claim 11 words
The process of claim 1, wherein the after-treatment is catalytic hydrogenation.
Claim 13
Dependent Claim 101 words
In a process of reclaiming used hydrocarbon oils from which water and light hydrocarbons have been removed by distillation and wherein the oils are prepurified either by coagulation, adsorption, a combination of coagulation and adsorption, by filtration, or by vacuum distillation, with subsequent fractional distillation and after-treatment, the improvement which comprises subjecting the prepurified product to dehalogenation prior to the fractional distillation and after-treatment by contacting said prepurified oil with an agent selected from the group consisting of alkaline earth metals, alkali metal alcoholates, alkaline earth metal alcoholates, aluminum alcoholates, alkali metal amides, pyridine, piperidine, metallic aluminum and anhydrous aluminum chloride.
Claim 14
Dependent Claim 46 words
The process of claim 13 wherein the dehalogenation step is carried out by contact with from 1 to 2000 moles of the treating agent per metric ton of oil, in the absence of air and humidity and at a temperature of from 15° to 300° C.
Claim 15
Dependent Claim 11 words
The process of claim 13, wherein the after-treatment is catalytic hydrogenation.
Claim 16
Dependent Claim 19 words
The process of claim 13, wherein the treating agent is selected from the group consisting of magnesium and calcium.
Claim 17
Dependent Claim 19 words
The process of claim 13, wherein the treating agent is selected from the group consisting of pyridine and piperidine.

References Cited (Backward Citations)

US1707671A Cited
US1869781A Cited
US1934068A Cited
US2328707A Cited
GB742909A Cited
GB1124260A Cited
US3773658A Cited
US3819508A Cited
US3919076A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-06-26 1981-12-26 1982-06-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-06-26 1985-12-26 1986-06-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-06-26 1989-12-26 1990-06-27 $7700.00 Window Closed / Lapsed

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