Use of water/methanol mixtures as solvents for aromatics extraction

Claim 2

A process for the separation of aromatic and paraffinic hydrocarbon constituents of an aromatics-containing petroleum distillate selected from the group consisting of kerosene, naphtha, diesel fuel and mixtures thereof which comprises the steps of (1) introducing at a temperature of from about 150° to about 400° F. the petroleum distillate into an extraction zone containing a methanol/water solvent having at least 20 vol.% of water to obtain an aromatic-rich solvent phase and a paraffinic-rich raffinate phase, (2) passing the solvent phase to a cooling and settling zone where the temperature is lowered to below 150° F., thereby separating an aromatic-rich hydrocarbon stream and a solvent stream, (3) recycling the solvent stream to the extraction zone, and (4) recovering as products a paraffinic-rich hydrocarbon stream and an aromatic-rich hydrocarbon stream.

Claim 3

A process according to claim 1 wherein the petroleum distillate is a catalytic naphtha.

Claim 4

A process according to claim 1, in which, in step (1), the solvent to oil volume ratio is from about 0.5 to about 5.

Claim 5

A process according to claim 1 wherein, in step (1), the extraction temperature is between about 200° and about 350° F.

Claim 6

A process according to claim 1 in which the methanol/water solvent contains from about 22 to about 40 vol.% of water.

Claim 7

A process according to claim 5 in which the methanol/water solvent contains about 25 vol.% of water.

Claim 8

A process according to claim 6 in which, in step (2), the temperature is lowered to between about 65° and about 90° F.

Claim 9

A process according to claim 7 in which the temperature is lowered to about 75° F.

Claim 10

A process according to claim 1 in which the paraffinic hydrocarbon phase obtained in step (1) and the aromatic-rich hydrocarbon phase obtained in step (2) are separately passed to flashing zones where any residual methanol/water solvent is removed for recycling to the extraction zone.

Claim 11

A process for the separation of aromatic and paraffinic hydrocarbon constituents of a catalytic naphtha petroleum fraction which comprises the steps of (1) introducing at a temperature of about 300° F the petroleum fraction into an extraction zone containing a methanol/water solvent having about 25 vol.% water to obtain an aromatic-rich solvent phase and a paraffinic-rich raffinate phase, (2) passing the solvent phase to a cooling and settling zone where the temperature is lowered to about 75° F thereby separating an aromatic-rich hydrocarbon stream and a solvent stream, (3) recycling the solvent stream to the extraction zone, (4) separately passing the paraffinic-rich hydrocarbon phase obtained in step (1) and the aromatic-rich hydrocarbon stream obtained in step (2) to flashing zones where residual methanol/water solvent is removed for recycling to the extraction zone, and (5) recovering as products a paraffinic-rich hydrocarbon stream and an aromatic-rich hydrocarbon stream.

Claim 12

A process for the separation of aromatic and paraffinic hydrocarbon constituents of a catalytic naphtha petroleum fraction which comprises the steps of (1) introducing at a temperature of about 300° F the petroleum fraction into an extraction zone containing a methanol/water solvent having about 25 vol.% water to obtain an aromatic-rich solvent phase and a paraffinic-rich raffinate phase, (2) passing the solvent phase to a cooling and settling zone where the temperature is lowered to about 75° F thereby separating an aromatic-rich hydrocarbon stream and a solvent stream, (3) recycling the solvent stream to the extraction zone, (4) separately passing the paraffinic-rich hydrocarbon phase obtained in step (1) and the aromatic-rich hydrocarbon stream obtained in step (2) to flashing zones where residual methanol/water solvent is removed for recycling to the extraction zone, and (5) recovering as products a paraffinic-rich hydrocarbon stream and an aromatic-rich hydrocarbon stream.