Solvent recovery process for N-methyl-2-pyrrolidone in hydrocarbon extraction
AssigneeExxon Research & Engineering Co.
InventorsJames D. Bushnell, Milton D. Leighton, Thomas M. McDonald
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Abstract
N-methyl-2-pyrrolidone is recovered from the raffinate and extract phases produced by its use in hydrocarbon extraction processes, particularly lube oil extraction, through the use of flash evaporation and/or distillation followed by gas stripping. Water buildup in the recovered solvent is prevented by employing solvent dehydration means in the solvent recovery line after gas stripping. Proper control of process parameters enables the dehydration means to remove excess water without requiring additional heat input to the process.
Claims8
An improved process for removing minor amounts of water extraneously introduced into a lube oil extraction solvent comprising NMP and minor amounts of water, said process comprising removing most of said solvent from a lube oil extract, as a first solvent vapor, by flash evaporation, simple distillation, rectification or combination thereof and stripping residual solvent from said extract with a non-aqueous stripping gas to form a mixture of solvent vapor and stripping gas, separating said solvent from said gas and recovering said solvent, wherein the improvement comprises the steps of:
- a. combining said first solvent vapor with said mixture;
- b. passing said combined mixture which contains extraneous and non-extraneous water through a first condensing zone wherein most of the solvent in said mixture is condensed to a liquid to form a mixture of condensed solvent, stripping gas and vapor and wherein said vapor contains NMP and said extraneous water;
- c. passing said second mixture to a separating zone to separate said condensed solvent from said vapor and stripping gas;
- d. passing at least a portion of the separated vapor and stripping gas from said separating zone to a rectifying zone wherein said NMP in said vapor is condensed and separated from said extraneous water and stripping gas;
- e. passing said extraneous water vapor and stripping gas from said rectifying zone to a second condensing zone to condense the extraneous water and separate same from the stripping gas;
- and
- f. returning a portion of said condensed water from the second condensing zone back to said rectifying zone to act as reflux therein.
Dependencies are inferred from the claim text.