Process for neutralization of petroleum acids (LAW810)
AssigneeExxon Research & Engineering Co.
InventorsRamesh Varadaraj, David William Savage
Life of this patent
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Abstract
The present invention describes a process for decreasing the acidity of a starting calcium containing, non-acid treated acidic crude oil by adding such an acidic crude oil to an effective amount of an aqueous base solution at conditions of pH and temperature sufficient to form an unstable emulsion of the acidic crude oil in the aqueous base solution; and breaking the emulsion to form a phase containing treated crude oil having a decreased acidity and aqueous phase residual containing base and neutralized acids. The invention has utility in crude oil processing.
Claims9
A process for decreasing the acidity and calcium content of an acidic, calcium-containing non-acid pretreated starting acidic crude oil, comprising:
- (a) contacting an acidic, calcium containing non-acid pretreated crude with an effective wherein the ratio of starting acidic crude to aqueous base solution is amount of aqueous base at least 1:3 to 1:15 based on the weight of acidic crude to weight of aqueous base solution at conditions of pH and temperature sufficient to forming an unstable emulsion of the non-acid treated starting acidic, calcium containing crude oil in an aqueous base solution;
- (b) breaking the unstable oil in aqueous base emulsion to produce a first phase containing treated crude oil having a decreased acidity and calcium content, a second aqueous phase containing residual base and neutralized acids, and a third intermediate phase containing an insoluble calcium containing compounds.
A process for decreasing the acidity and calcium content of an acidic, calcium containing, non-acid pretreated starting acidic crude oil, comprising:
- (a) separating a starting whole acidic, calcium containing, non-acid pretreated starting crude oil feedstream into a first stream containing primarily water and trace amounts of the starting crude oil and a second stream containing primarily the starting crude oil and trace amounts of water;
- (b) combining the first stream with aqueous base;
- (c) countercurrently contacting the first and second stream to produce an unstable oil in aqueous base emulsion of from 1:3 to 1:5 ratio of crude:aqueous phase;
- (d) recovering from step (c), a lower phase containing primarily aqueous base and residual treated oil and an upper phase containing primarily treated oil and residual aqueous base;
- (e) separating the upper phase from step (d) into a treated oil stream containing residual water and an aqueous base stream containing residual treated oil;
- (f) passing the lower phase of step (d) and the aqueous base stream of step (e) to a separator to recover an aqueous base stream and treated oil stream;
- (g) passing the treated oil stream from step (e) and the treated oil stream from step (f) to a stabilizer tower;
- (h) degassing and recovering the treated oil stream.
Dependencies are inferred from the claim text.