Solvent recovery process for processing of hydrocarbons

Claim 2

In a process for refining a petroleum hydrocarbon fraction selected from the group consisting of a vacuum gas oil, a deasphalted residual oil, and an asphalt-containing residual oil comprising undesirable components of cyclic, naphthenic, olefinic, aromatic, nitrogenous, and sulfurous compounds, or mixtures of any of such compounds wherein undesirable components are separated from said petroleum hydrocarbon fraction by a selective solvent selected from the group consisting of furfural, phenol, N-methyl pyrollidone, nitrobenezene and mixtures thereof and wherein said selective solvent is recovered by evaporation techniques from a solvent-enriched extract phase including said extracted undesirable components, an improved process for recovering said selective solvent from said solvent-enriched phase, which comprises: (a) heating said solvent-enriched phase and introducing the heated solvent-enriched phase into a first flash zone to effect flashing thereof to form a first vapor stream comprising solvent and a first bottom stream comprising substantially solvent and said undesirable components: (b) heating said first bottom stream and introducing the heated bottom stream into a second flash zone to effect flashing thereof to form a second vapor stream comprising solvent and a second bottom stream comprising substantially solvent and said undesirable components, said second flash zone being operated at above atmospheric pressure; (c) heating said second bottom stream; (d) introducing the heated second bottom stream into a third flash zone to effect flashing thereof to form a third vapor stream and a third bottom stream comprising said undesirable components, said first, second, and third flash zones being operated at incrementally increased ranges of temperatures and pressures whereby the vapor from any successive flash zone is used as a source of heat in the preceding flash zone to effect vaporization in said preceding flash zone; and (e) recovering said selective solvent from said vapor streams.

Claim 3

In a process for dewaxing a petroleum hydrocarbon fraction comprising, petroleum hydrocarbons, and dewaxed oil wherein said wax is extracted from the petroleum hydrocarbon fraction by a selective solvent selected from the group consisting of methyl ethyl ketone; mixtures of methyl ethyl ketone and benzene; mixtures of methyl ethyl ketone and toluene; mixtures of methyl ethyl ketone, benzene, and toluene; methyl isobutyl ketone; mixtures of methyl isobutyl ketone and benzene; mixtures of methyl isobutyl ketone and toluene; mixtures of methyl isobutyl ketone, benzene and toluene; dichloromethane; and methylene chloride and wherein said selective solvent is recovered by evaporative techniques from a solvent-enriched extract phase including said dewaxed oil, an improved process for recovering said solvent from said the solvent-enriched phase, which comprises: (a) heating said solvent-enriched phase and introducing the heated solvent-enriched phase into a first flash zone to effect flashing thereof to form a first vapor stream comprising solvent and a first bottom stream comprising substantially solvent and said dewaxed oil; (b) heating said first bottom stream and introducing the heated bottom stream into a second flash zone to effect flashing thereof to form a second vapor stream comprising solvent and a second bottom stream comprising substantially solvent and said dewaxed oil, said second flash zone being operated at above atmospheric pressure; (c) heating said second bottom stream; (d) introducing the heated second bottom stream into a third flash zone to effect flashing thereof to form a third vapor stream and a third bottom stream comprising said wax, said first, second, and third flash zones being operated at incrementally increased ranges of temperatures and pressures whereby the vapor from any successive flash zone is used as a source of heat in the preceding flash zone to effect vaporization in said preceding flash zone; and (e) recovering said selective solvent from said vapor streams.

Claim 4

In a process for dewaxing a petroleum hydrocarbon fraction comprising, petroleum hydrocarbons, and dewaxed oil wherein said wax is extracted from the petroleum hydrocarbon fraction by a selective solvent selected from the group consisting of methyl ethyl ketone; mixtures of methyl ethyl ketone and benzene; mixtures of methyl ethyl ketone and toluene; mixtures of methyl ethyl ketone, benzene, and toluene; methyl isobutyl ketone; mixtures of methyl isobutyl ketone and benzene; mixtures of methyl isobutyl ketone and toluene; mixtures of methyl isobutyl ketone, benzene and toluene; dichloromethane; and methylene chloride and wherein said selective solvent is recovered by evaporative techniques from a solvent-enriched extract phase including said dewaxed oil, an improved process for recovering said solvent from said the solvent-enriched phase, which comprises: (a) heating said solvent-enriched phase and introducing the heated solvent-enriched phase into a first flash zone to effect flashing thereof to form a first vapor stream comprising solvent and a first bottom stream comprising substantially solvent and said dewaxed oil; (b) heating said first bottom stream and introducing the heated bottom stream into a second flash zone to effect flashing thereof to form a second vapor stream comprising solvent and a second bottom stream comprising substantially solvent and said dewaxed oil, said second flash zone being operated at above atmospheric pressure; (c) heating said second bottom stream; (d) introducing the heated second bottom stream into a third flash zone to effect flashing thereof to form a third vapor stream and a third bottom stream comprising said wax, said first, second, and third flash zones being operated at incrementally increased ranges of temperatures and pressures whereby the vapor from any successive flash zone is used as a source of heat in the preceding flash zone to effect vaporization in said preceding flash zone; and (e) recovering said selective solvent from said vapor streams.

Claim 5

In a process for deasphalting a petroleum hydrocarbon fraction comprising asphalt wherein deasphalted oil is extracted from the petroleum hydrocarbon fraction by a selective solvent selected from the group consisting of at least one C 3 -C 5 alkane and mixtures of at least one C 3 -C 5 alkane with ethane, propylene, or butylene and wherein said solvent is recovered by evaporative techniques from a solvent-enriched extract phase including said extracted deasphalted oil, an improved process for recovering said solvent from said solvent-enriched phase, which comprises: (a) heating said solvent-enriched phase and introducing the heated solvent-enriched phase into a first flash zone to effect flashing thereof to form a first vapor stream comprising solvent and a first bottom stream comprising substantially solvent and said deasphalted oil; (b) heating said first bottom stream and introducing the heated bottom stream into a second flash zone to effect flashing thereof to form a second vapor stream comprising solvent and a second bottom stream comprising substantially solvent and said asphalt, said second flash zone being operated at above atmospheric pressure; (c) heating said second bottom stream; (d) introducing the heated second bottom strem into a third flash zone to effect flashing thereof to form a third vapor stream and a third bottom stream comprising said deasphalted oil, said first, second, and third flash zones being operated at incrementally increased ranges of temperatures and pressures whereby the vapor from any successive flash zone is used as a source of heat in the preceding flash zone to effect vaporization in said preceding flash zone; and (e) recovering said selective solvent from said vapor streams.

Claim 6

In a process for deasphalting a petroleum hydrocarbon fraction comprising asphalt wherein deasphalted oil is extracted from the petroleum hydrocarbon fraction by a selective solvent selected from the group consisting of at least one C 3 -C 5 alkane and mixtures of at least one C 3 -C 5 alkane with ethane, propylene, or butylene and wherein said solvent is recovered by evaporative techniques from a solvent-enriched extract phase including said extracted deasphalted oil, an improved process for recovering said solvent from said solvent-enriched phase, which comprises: (a) heating said solvent-enriched phase and introducing the heated solvent-enriched phase into a first flash zone to effect flashing thereof to form a first vapor stream comprising solvent and a first bottom stream comprising substantially solvent and said deasphalted oil; (b) heating said first bottom stream and introducing the heated bottom stream into a second flash zone to effect flashing thereof to form a second vapor stream comprising solvent and a second bottom stream comprising substantially solvent and said asphalt, said second flash zone being operated at above atmospheric pressure; (c) heating said second bottom stream; (d) introducing the heated second bottom strem into a third flash zone to effect flashing thereof to form a third vapor stream and a third bottom stream comprising said deasphalted oil, said first, second, and third flash zones being operated at incrementally increased ranges of temperatures and pressures whereby the vapor from any successive flash zone is used as a source of heat in the preceding flash zone to effect vaporization in said preceding flash zone; and (e) recovering said selective solvent from said vapor streams.

Claim 7

The process as defined in claim 1 wherein the heating of said second bottom stream is effected by a fired heater.

Claim 8

The process as defined in claim 2 wherein the heating of said second bottom stream is effected by a fired heater.

Claim 9

The process as defined in claim 3 wherein the heating of said second bottom stream is effected by a fired heater.

Claim 10

The process as defined in claim 4 wherein said solvent is furfural.

Claim 11

The process as defined in claim 5 wherein said solvent is a solvent selected from the group consisting of methyl ethyl ketone and methyl isobutyl ketone.

Claim 12

The process as defined in claim 1 further comprising at least one additional flash zone.

Claim 13

The process as defined in claim 2 further comprising at least one additional flash zone.

Claim 14

The process as defined in claim 3, further comprising at least one additional flash zone.

Claim 15

The process as defined in any one of claims 1 to 3 wherein liquid solvent is introduced into the upper portion of each of said flash zones.

Claim 16

The process as defined in any one of claims 1 to 3 wherein the second and third vapor streams are condensed and introduced into a column in contact with said first vapor stream and wherein a vapor stream is withdrawn therefrom and passed in indirect heat transfer relationship to a water stream to reproduce steam.