Offgas stream direct contact condenser

Patent metadata

Field	Value
Publication number	US-10252957-B2
Application number	US-201715486043-A
Country	US
Kind code	B2
Filing date	Apr 12, 2017
Priority date	Sep 22, 2009
Publication date	Apr 9, 2019
Grant date	Apr 9, 2019

Abstract

Methods and systems for the dehydrogenation of hydrocarbons include a direct contact condenser to remove compounds from an offgas process stream. The reduction of compounds can decrease duty on the offgas compressor by removing steam and aromatics from the offgas. The dehydrogenation reaction system can be applicable for reactions such as the dehydrogenation of ethylbenzene to produce styrene, the dehydrogenation of isoamiline to produce isoprene, or the dehydrogenation of n-pentene to produce piperylene.

First claim

What is claimed is:

1. A method for removing aromatics and steam from a dehydrogenation reactor offgas, comprising:
feeding a dehydrogenation offgas stream comprising styrene and steam from an ethylbenzene reaction system for production of styrene into a direct contact condenser;
contacting the offgas stream with a cooling medium comprising chilled water and ethylbenzene;
condensing organic compounds including styrene and steam from the offgas stream to form condensed organic compounds and water;
removing the condensed organic compounds and water from the direct contact condenser;
removing noncondensable vapors from the direct contact condenser; and
sending the noncondensable vapors to an offgas compressor to compress the noncondensable vapors.

2. The method of claim 1 , wherein the condensed organic compounds comprise one or more of styrene, ethylbenzene, toluene, and benzene.

3. The method of claim 1 , further comprising sending the condensed organic compounds to a main process separator.

4. The method of claim 1 , wherein quench packing is located within an interior top section of the direct contact condenser.

5. The method of claim 4 , wherein the direct contact condenser is located downstream of a styrene offgas feed line and is in fluid contact with the styrene offgas feed line, wherein the styrene offgas feed line is downstream of a dehydrogenation reactor;
wherein a cooling medium inlet line is in fluid contact with the interior top section of the direct contact condenser; and
wherein a collector baffle is located within an interior bottom section of the direct contact condenser, and wherein a decanted aromatics outlet line is in fluid connection with the interior bottom section of the direct contact condenser.

6. The method of claim 1 , wherein a noncondensable vapors outlet line is in fluid connection with an interior top section of the direct contact condenser, and wherein a vacuum compressor is in fluid connection with the noncondensable vapors outlet line.

7. The method of claim 6 , wherein the direct contact condenser is in fluid contact with and downstream of a styrene offgas feed line, wherein the styrene offgas feed line is downstream of a dehydrogenation reactor;
wherein a cooling medium inlet line is in fluid contact with the interior top section of the direct contact condenser;
wherein a collector baffle is located within an interior bottom section of the direct contact condenser, and wherein a decanted aromatics outlet line is in fluid connection with the interior bottom section of the direct contact condenser.

8. The method of claim 1 , wherein the direct contact condenser has an interior top section and an interior bottom section, wherein the direct contact condenser is in fluid contact with a styrene offgas feed line, wherein a noncondensable vapors outlet line is in fluid connection with the interior top section of the direct contact condenser, wherein a vacuum compressor is in fluid connection with the noncondensable vapors outlet line, and wherein the direct contact condenser is located between the vacuum compressor and a dehydrogenation reactor.

9. The method of claim 8 , wherein the direct contact condenser comprises:
a cooling medium inlet line in fluid contact with the interior top section of the direct contact condenser;
a collector baffle located within the interior bottom section of the direct contact condenser;
a decanted aromatics outlet line in fluid connection with the interior bottom section of the direct contact condenser;
an overflow pipe adapted to conduct liquids from the collector baffle to the decanted aromatics outlet line;
quench packing, wherein the quench packing is located within the interior top section of the direct contact condenser;
a cooling medium outlet line in fluid connection with the bottom section of the direct contact condenser;
a refrigeration unit in fluid connection with the cooling medium outlet line and the cooling medium inlet line; and
an ethylbenzene line adapted to inject ethylbenzene into the cooling medium outlet line.

10. The method of claim 1 , wherein the direct contact condenser is located between a vacuum compressor and a dehydrogenation reactor.

Assignees

• Fina Technology

Inventors

• Welch Vincent A
• Butler James R

Classifications

• C07C7/09 Primary

  by fractional condensation · CPC title

• C07C5/333

  Catalytic processes · CPC title

• C01B3/50

  Separation of hydrogen or hydrogen-containing gases from gaseous mixtures, e.g. purification · CPC title

• C01B3/24

  of hydrocarbons · CPC title

• F28B9/06

  with provision for re-cooling the cooling water or other cooling liquid · CPC title