Regeneration of selective solvents for extractive processes

Patent metadata

Field	Value
Publication number	US-9440947-B2
Application number	US-201213707554-A
Country	US
Kind code	B2
Filing date	Dec 6, 2012
Priority date	Feb 26, 2012
Publication date	Sep 13, 2016
Grant date	Sep 13, 2016

Abstract

Recovering a polar hydrocarbon (HC) selective solvent substantially free of hydrocarbons (HCs) and other impurities from a lean solvent stream containing the selective solvent, measurable amounts of heavy aromatic HCs, and polymeric materials that are generated in an extractive distillation (ED) or liquid-liquid extraction (LLE) process. At least a portion of the lean solvent stream is contact in a solvent clean-up zone with a slip stream from the HC feed stream of the ED or LLE process or an external stream. The HC feed stream, such as pyrolysis gasoline or reformate, contains significant amounts of benzene and at least 50% polar (aromatic) HCs and serves as a displacement agent to remove the heavy HCs and polymeric material from the lean solvent stream. A magnetic filter can be used to remove the paramagnetic contaminants from the lean solvent.

First claim

What is claimed is:

1. A method of recovering a polar hydrocarbon selective solvent substantially free of hydrocarbons and other impurities from a solvent-rich stream containing selective solvent, measurable amounts of heavy hydrocarbons, and polymeric materials, which method comprises the steps of:
(a) providing a feed stream containing polar and less polar hydrocarbons wherein the feed stream contains one or more petroleum products that is selected from reformate, pyrolysis gasoline, coke oven oil and coal tar;
(b) introducing the feed stream into an extraction zone, which includes an extractive distillation column or a liquid-liquid extraction column, to yield (i) a less polar hydrocarbon stream and a first water stream and (ii) a polar hydrocarbon stream, lean a solvent stream and a second water stream; and
(c) introducing a portion of the lean solvent stream into a solvent cleanup zone at a first location and introducing a slip stream from the feed stream into the solvent cleanup zone at a second location whereby aromatic hydrocarbons in the slip stream displace heavy hydrocarbons from the lean solvent stream thereby yielding a solvent phase that is introduced into the extraction zone and a hydrocarbon phase that contains the displaced heavy hydrocarbons.

2. The method of claim 1 , wherein the polar hydrocarbons are aromatic and the less polar hydrocarbons are paraffinic, naphthenic, and olefinic.

3. The method of claim 1 wherein the solvent is selected from the group consisting of sulfolane, alkyl-sulfolane, N-formyl morpholine, N-methyl pyrrolidone, tetraethylene glycol, triethylene glycol, diethylene glycol, and mixtures thereof.

4. The method of claim 1 wherein the solvent cleanup zone is an extraction column that is selected from the group consisting of (i) columns equipped with trays, packings or rotating discs, (ii) a multi-stage mixer/settler and (iii) pulse column.

5. The method of claim 1 wherein the solvent cleanup zone is a countercurrent extraction column.

6. The method of claim 1 wherein step (b) comprises the steps of:
(i) introducing the feed stream into a middle portion of the extractive distillation column (EDC) and introducing a solvent-rich stream into an upper portion of the EDC as a selective solvent feed;
(ii) recovering a water-containing, less polar hydrocarbon-rich stream from a top of the EDC and withdrawing a first solvent-rich stream containing solvent and polar hydrocarbons from a bottom of the EDC;
(iii) introducing the first solvent-rich stream into the middle portion of a solvent recovery column (SRC), recovering a polar hydrocarbon-rich stream, that is substantially free of solvent and less polar hydrocarbons, from a top of the SRC, and removing a second solvent-rich stream from a bottom of the SRC;
(iv) introducing a first portion of the second solvent-rich stream into the upper portion of the EDC in step (i) as the selective solvent feed; and
(v) cooling a second portion of the second solvent-rich stream in step (iii) and introducing the cooled second portion of the solvent-rich stream into an upper portion of the solvent cleanup zone to form the solvent phase; wherein step (c) comprises the steps of:
(vi) introducing the slip stream into a lower portion of the solvent cleanup zone, as a heavy hydrocarbon displacement agent, to squeeze out heavy hydrocarbons and polymeric materials from the solvent phase into a hydrocarbon phase; and
(vii) withdrawing an accumulated hydrocarbon phase containing heavy hydrocarbons and polymeric materials from an upper portion of the solvent cleanup zone, and recovering the solvent phase containing solvent and polar hydrocarbons and substantially reduced levels of heavy hydrocarbons and polymeric materials, from a lower portion of the solvent cleanup zone; and, the method further comprises the step of: (viii) introducing the solvent phase from the solvent cleanup zone into a middle portion of the EDC as part of a hydrocarbon feed to recycle purified solvent into a solvent loop.

7. The method of claim 6 further comprising filtering the first portion of the second solvent-rich stream with an in-line filter that is enhanced with a magnetic field before the first portion of the second solvent-rich stream enters the upper portion of the EDC.

8. The method of claim 6 wherein the EDC is operated under such conditions so as to keep substantially all C 9 + hydrocarbons in the first solvent-rich stream in order to maximize benzene recovery.

9. The method of claim 6 wherein the SRC is operated under such conditions as to strip only C 8 and lighter hydrocarbons from the first solvent-rich stream and keep substantially all C 9 and heavier hydrocarbons in the second solvent-rich stream.

10. The method of claim 6 wherein step (iv) comprises:
introducing a greater portion of the second solvent-rich stream into an upper portion of the EDC and introducing a first minor portion of the second solvent-rich stream into an upper portion of a thermal solvent regeneration zone, recovering a third solvent-rich stream containing solvent, water, and hydrocarbons and other compounds having boiling points that are below that of the solvent, from a top of the solvent regeneration zone, and removing heavy sludge from a lower portion of the solvent regeneration zone; and wherein step (v) comprises:
cooling a mixture that comprises the third solvent-rich stream in step (iv) and a second minor portion of the second solvent-rich stream in step (iii) and introducing the mixture into an upper portion of the solvent cleanup zone to form the solvent phase.

11. The method of claim 6 wherein the solvent is sulfolane.

12. The method of claim 6 wherein the solvent is N-formyl morpholine.

13. The method of claim 1 wherein step (b) comprises the steps of:
(i) introducing the feed stream into a middle portion of a liquid-liquid extraction (LLE) column and introducing a solvent-rich stream into an upper portion of the LLE column as a selective solvent feed;
(ii) recovering a water-containing, less polar hydrocarbon-rich stream from a top of the LLE column and withdrawing the first solvent-rich stream containing solvent, polar hydrocarbons and minor amounts of less polar hydrocarbons from a bottom of the LLE column;
(iii) introducing a mixture comprising the first solvent-rich stream and a minor portion of a third solvent-rich stream from a bottom of a solvent recovery column (SRC) into an upper portion of an extractive stripping column (ESC), recovering a hydrocarbon-rich vapor, which contains less polar hydrocarbons and a significant amount of benzene and heavier aromatics, and which is condensed and recycled to a lower portion of LLE column as reflux, and withdrawing a second solvent-rich stream containing solvent and polar hydrocarbons, which is substantially free of less polar hydrocarbons, from a bottom of the ESC;
(iv) introducing the second solvent-rich stream in step (iii) into a middle portion of the SRC, withdrawing a polar hydrocarbon-rich stream, which is substantially free of solvent and less polar hydrocarbons, from a top of the SRC, and removing a third solvent-rich stream from the bottom of the SRC;
(v) introducing a major portion of the third solvent-rich stream into the upper portion of the LLE column in step (i) as the selective solvent feed; and
(vi) cooling a minor portion of the third solvent-rich stream in step (iv) and introducing the cooled minor portion of the third solvent-rich stream into an upper portion of a solvent cleanup zone to form the solvent phase; wherein step (c) comprises:
(vii) introducing the slip stream into a lower portion of the solvent cleanup zone, as a heavy hy

Assignees

• Amt Int Inc
• Cpc Corp Taiwan

Inventors

• Lee Fu-Ming
• Lin Tzong-Bin
• Wu Kuang-Yeu
• Hwang Jyh-Haur
• Chiu Jeffrey Tsung-Min
• Lee Jeng-Cheng
• Wu Yu-Ming
• Jan Han-Tjen

Classifications

• B01D11/0484

  Controlling means · CPC title

• B01D3/40 Primary

  Extractive distillation · CPC title

• C10G21/28

  Recovery of used solvent · CPC title

• C07C7/10

  by extraction, i.e. purification or separation of liquid hydrocarbons with the aid of liquids · CPC title

• C10G21/16

  Oxygen-containing compounds · CPC title