Selective olefin extraction

Patent metadata

Field	Value
Publication number	US-2016303489-A1
Application number	US-201615196297-A
Country	US
Kind code	A1
Filing date	Jun 29, 2016
Priority date	Nov 7, 2012
Publication date	Oct 20, 2016
Grant date	—

Abstract

A process and system for separating butenes and butanes by extractive distillation using a polar solvent is disclosed. The process may include: contacting a hydrocarbon mixture including butanes and butenes with a lean solvent mixture in an extractive distillation column to form an enriched solvent fraction comprising butenes; recovering an overheads fraction comprising butanes and a bottoms fraction from the extractive distillation column; feeding the bottoms fraction to a stripper including a stripping section and a wash section; recovering the lean solvent mixture as a bottoms fraction and a stripper overheads fraction comprising butenes and water from the stripper; condensing the overheads fraction to form a water fraction and a product butenes fraction; feeding water as reflux to a top of the stripper wash section; feeding at least a portion of the condensed water fraction intermediate the top and bottom of the stripper wash section as a second reflux.

First claim

What is claimed:

1 . A system for separating butenes and butanes by extractive distillation using a polar solvent, the system comprising:
an extractive distillation column for contacting a hydrocarbon mixture comprising butanes and butenes with a lean solvent mixture comprising water and one or more polar solvents and recovering an overheads fraction comprising butanes and an bottoms fraction comprising enriched solvent fraction comprising the butenes and solvent(s); a stripper comprising a stripping section and a was section for separating the butenes from the solvents in the bottoms fraction, recovering a lean solvent mixture as a stripper bottoms fractions and butenes and water as a stripper overheads fraction, wherein the bottoms fraction is fed to the stripper above the stripping section and below the wash section; a condenser for condensing the stripper overheads fraction to form a water fraction and a product butenes fraction; a first flow conduit for feeding water as a reflux to a top of the stripper wash section; and a second flow conduit for feeding at least a portion of the water fraction intermediate the top and bottom of the stripper wash section as a second reflux.

2 . The system of claim 1 , further comprising a butadiene recovery process for producing the hydrocarbon mixture as a vapor fraction.

3 . The system of claim 1 , further comprising a feed vaporization system for vaporizing the hydrocarbon mixture prior to the extractive distillation column.

4 . The system of claim 1 further comprising a two-stage condensation system for condensing the stripper overheads fraction producing the condensed water fraction and the product butene fraction.

5 . The system of claim 1 , further comprising:
a liquid side draw from the stripper; and a first heat exchanger for partially vaporizing the liquid side draw by indirect heat exchange with the stripper bottoms fraction.

6 . The system of claim 5 , further comprising a second heat exchanger for contacting via indirect heat exchange at least one of (a) the enriched solvent fraction from the extractive distillation column and (b) one or more liquid side draws from the extractive distillation column with a partially cooled stripper bottoms fraction from the first heat exchanger.

7 . The system of claim 6 , wherein at least one of the first heat exchanger and the second heat exchanger is a once-thru vaporization type exchanger.

8 . A system for separating butenes and butanes by extractive distillation using a polar solvent, the system comprising;
an extractive distillation column for contacting a hydrocarbon mixture comprising butanes and butenes with a lean solvent mixture comprising water and one or more polar solvents to recover an enriched solvent fraction comprising the butenes and solvent(s) as a bottoms fraction and to recover an overheads fraction comprising the butanes; a stripper comprising a lower stripping section and an upper wash section to separate the bottoms fraction and recover an overheads fraction comprising butenes and water and a bottoms fraction comprising the lean solvent mixture; a stripper overheads system for condensing the overheads fraction comprising butenes and water to form a water fraction and a product butenes fraction; a flow conduit for feeding water as a reflux to a top of the stripper wash section; a flow conduit for feeding at least a portion of the condensed water fraction intermediate the top and bottom of the stripper wash section as a second reflux.

9 . The system of claim 8 , further comprising a feed vaporization system for vaporizing the hydrocarbon mixture upstream of the extractive distillation column.

10 . The system of claim 8 , further comprising a flow conduit for feeding the bottoms fraction to the stripper at a location above the stripping section and below the wash section.

11 . The system of claim 8 , wherein the stripper overheads system comprises a two-stage condensation system comprising:
a first condenser for partially condensing the overheads fraction to condense and recover the water as the condensed water fraction and to recover a vapor fraction comprising the butenes; a second condenser for condensing the vapor fraction comprising the butenes to form the product butene fraction.

12 . The system of claim 8 , further comprising:
a flow conduit for withdrawing a liquid side draw from the stripper; a first heat exchanger for at least partially vaporizing the liquid side draw by indirect heat exchange with the lean solvent mixture recovered as a bottoms fraction from the stripper; a flow conduit for returning the at least partially vaporized side draw to the stripper.

13 . The system of claim 12 , further comprising:
a flow conduit for recovering a partially cooled lean solvent mixture from the first heat exchanger; one or more second heat exchangers for contacting at least one of (a) the enriched solvent fraction as a bottoms fraction from the extractive distillation column and (b) one or more liquid side draws from the extractive distillation column via indirect heat exchange with the partially cooled lean solvent mixture.

14 . The system of claim 13 , appropriately, wherein at least one of the first heat exchanger and the one or more second heat exchanger is a once-three vaporization type exchanger.

15 . The system of claim 13 , further comprising a third heat exchanger for contacting a partially cooled lean solvent mixture recovered from at least one of the first heat exchanger and the second heat exchanger via indirect heat exchange with the hydrocarbon mixture to at least partially vaporize the hydrocarbon mixture.

16 . A system for separating butenes and butanes by extractive distillation using a polar solvent, the system comprising:
a feed vaporization system for vaporizing a hydrocarbon mixture comprising butanes and butenes; an extractive distillation column for contacting the vaporized hydrocarbon mixture with a lean solvent mixture comprising water and one or more polar solvents to recover an enriched solvent fraction comprising the butenes and solvent(s) as a bottoms fraction and to recover an overheads fraction comprising the butanes; a stripper comprising a lower stripping section and an upper wash section to separate the bottoms fraction and recover an overheads fraction comprising butenes and water and a bottoms fraction comprising the lean solvent mixture; a stripper overheads system for condensing the overheads fraction comprising butenes and water to form a water fraction and a butenes fraction; a butene stripper product condenser for condensing the butenes fraction to form a product butene stream; a flow conduit for feeding water as a reflux to a top of the stripper wash section; a flow conduit for feeding at least a portion of the condensed water fraction intermediate the top and bottom of the stripper wash section as a second reflux.

17 . The system of claim 16 , further comprising a flow conduit for feeding the bottoms fraction to the stripper at a location above the stripping section and below the wash section.

18 . The system of claim 16 , further comprising:
a flow conduit for withdrawing a liquid side draw from the stripper; a first heat exchanger for at least partially vaporizing the liquid side draw by indirect heat exchange with the lean solvent mixture recovered as a bottoms fraction from the stripper; a flow conduit for returning the at least partially vaporized side draw to the stripper.

19 . The system of claim 16 , wher

Assignees

• Lummus Technology Inc

Inventors

• Schwint Kevin John
• Brummer Robert J

Classifications

• B01D3/34

  with one or more auxiliary substances · CPC title

• C10G7/08

  Azeotropic or extractive distillation (refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents C10G21/00) · CPC title

• B01D3/4205

  Reflux ratio control splitter · CPC title

• C07C7/005 Primary

  Processes comprising at least two steps in series · CPC title

• C07C7/08 Primary

  by extractive distillation · CPC title