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Process for recovering hydrocarbons from a diatomite-type ore

Assignee: Chevron USA Inc
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Filing: 1981-10-26
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Granted: 1983-02-15
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Expires: 2001-10-26
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Abstract

Abstract A process for recovering hydrocarbons from a diatomite-type ore which comprises contacting the diatomite ore with a C 4 -C 10 alcohol and thereafter contacting the diatomite ore-alcohol mixture with an aqueous alkaline solution to separate a hydrocarbon-alcohol phase and an alkaline aqueous phase containing the stripped diatomite ore. Thereafter, the alcohol is distilled off from the hydrocarbon phase and recycled back into the initial process.

Inventors

  • 👤 Bruce W. Davis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 17:17
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04

Claims Analysis

Total Claims: 22
Claim 1
Independent Claim 65 words
A process for recovering hydrocarbons from diatomite ore comprising: (a) contacting a diatomite ore containing hydrocarbons with an effective amount of a C 4 -C 10 alcohol or mixture of alcohols; (b) contacting the diatomite ore-alcohol mixture with an aqueous alkaline solution to separate the mixture into a hydrocarbon phase and an alkaline aqueous-diatomaceous ore fraction; and (c) recovering the alcohol-hydrocarbon phase from step (b).
Claim 2
Dependent Claim 65 words
A process for recovering hydrocarbons from diatomite ore comprising: (a) contacting a diatomite ore containing hydrocarbons with an effective amount of a C 4 -C 10 alcohol or mixture of alcohols; (b) contacting the diatomite ore-alcohol mixture with an aqueous alkaline solution to separate the mixture into a hydrocarbon phase and an alkaline aqueous-diatomaceous ore fraction; and (c) recovering the alcohol-hydrocarbon phase from step (b).
Claim 3
Dependent Claim 34 words
The process according to claim 1 wherein the C 4 -C 10 alcohol is a C 4 -C 10 straight- or branched-chain aliphatic, alicyclic, aromatic, substituted aromatic, substituted alicyclic, aromatic-alicyclic, olefinic, or mixtures thereof.
Claim 4
Dependent Claim 16 words
The process according to claim 1 wherein the alcohol is a straight-chain or a branched-chain alcohol.
Claim 5
Dependent Claim 17 words
The process according to claim 3 wherein the alcohol is a straight-chain C 4 -C 10 alcohol.
Claim 6
Dependent Claim 19 words
The process according to claim 1 wherein the aqueous alkaline solution has a pH greater than about pH 9.
Claim 7
Dependent Claim 23 words
The process according to claim 5 wherein the aqueous alkaline solution has a temperature of from about 20° C. to about 95° C.
Claim 8
Dependent Claim 32 words
The process according to claim 6 further comprising settling the mixture of step (b) for a sufficient time to separate said mixture into two phases prior to recovery of the alcohol-hydrocarbon phase.
Claim 9
Dependent Claim 32 words
The process according to claim 7 wherein the pH is obtained by adding a condensed silicate, a condensed phosphate, a hydroxide, an alkali metal silicate, or mixtures thereof, to an aqueous solution.
Claim 10
Dependent Claim 16 words
The process according to claim 8 wherein the aqueous alkaline solution contains 3 percent sodium metasilicate.
Claim 11
Dependent Claim 23 words
The process according to claim 6 further comprising: (d) separating the alcohol solvent from the hydrocarbon and recycling the alcohol into step (a).
Claim 12
Dependent Claim 16 words
The process according to claim 10 wherein the alcohol is separated from the hydrocarbons by distillation.
Claim 13
Dependent Claim 26 words
The process according to claim 6 wherein the ratio of alcohol to alkaline aqueous solution is from about 1 to 2 to about 1 to 16.
Claim 14
Dependent Claim 20 words
The process according to claim 12 wherein the ratio of alcohol to alkaline aqueous solution is about 1 to 4.
Claim 15
Dependent Claim 24 words
The process according to claim 12 wherein the alcohol to diatomaceous ore ratio is from about 1 to 1 to about 1 to 5.
Claim 16
Dependent Claim 18 words
The process according to claim 14 wherein the alcohol to diatomaceous ore ratio is about 4 to 5.
Claim 17
Dependent Claim 13 words
The process according to claim 15 wherein the alcohol is n-hexanol or n-heptanol.
Claim 18
Dependent Claim 21 words
The process according to claim 14 wherein the contacting of step (b) is from about 10 seconds to about 15 minutes.
Claim 19
Dependent Claim 21 words
The process according to claim 17 wherein the contacting is by mixing the diatomaceous ore-alcohol mixture with the aqueous alkaline solution.
Claim 20
Dependent Claim 12 words
The process according to claim 18 wherein the mixing is countercurrent mixing.
Claim 21
Dependent Claim 57 words
The process according to claim 19 wherein the alcohol is n-hexanol, the aqueous alkaline solution contains 3 percent by weight sodium meta-silicate, the mixing of step (b) is for about 30 seconds, the ratio of alcohol to ore is about 4 to 5, and the ratio of alcohol to aqueous alkaline solution is about 1 to 4.
Claim 22
Dependent Claim 35 words
The process according to claim 1, 5, 7, 10, 12, or 18 wherein the diatomaceous ore tailings are separated from the alkaline aqueous solution and said alkaline aqueous solution is recycled back into step (b).

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-02-14 1986-08-16 1987-02-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-02-14 1990-08-16 1991-02-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-02-14 1994-08-16 1995-02-15 $7700.00 Window Closed / Lapsed

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