Offgas stream direct contact condenser

Patent metadata

Field	Value
Publication number	US-9650317-B2
Application number	US-201514635041-A
Country	US
Kind code	B2
Filing date	Mar 2, 2015
Priority date	Sep 22, 2009
Publication date	May 16, 2017
Grant date	May 16, 2017

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 the dehydrogenation of hydrocarbons comprising:
contacting a hydrocarbon feedstock with a dehydrogenation catalyst within a reactor under reaction conditions effective to dehydrogenate at least a portion of said hydrocarbon feedstock in a dehydrogenation reaction;
removing an offgas stream that comprises hydrogen from the reactor;
providing a direct contact condenser, wherein the direct contact condenser circulates a cooling medium and contacts the offgas stream with the cooling medium;
cooling the offgas stream in the direct contact condenser to enable the condensation of compounds from the offgas stream;
removing from the direct contact condenser a cooled offgas stream having a reduced content of condensable compounds as compared to the offgas stream prior to contact with the cooling medium; and
compressing the cooled offgas stream in an offgas compressor, wherein the offgas compressor maintains the pressure within the reactor.

2. The method of claim 1 , further comprising:
supplying steam to the dehydrogenation reaction in a steam to hydrocarbon molar ratio of at least 4:1; and
operating the reactor at a temperature of at least 300° C.

3. The method of claim 1 , further comprising:
operating the reactor at vacuum conditions wherein substantially all of the hydrocarbons are in a vapor phase; and
recovering a vapor product from the reactor comprising dehydrogenated product.

4. The method of claim 1 , wherein the offgas stream comprises styrene offgas from an ethylbenzene reaction system.

5. The method of claim 1 , wherein the cooling medium comprises chilled water.

6. The method of claim 5 , wherein the cooling medium further comprises ethylbenzene.

7. The method of claim 1 , wherein the condensation of compounds from the offgas stream forms condensed compounds that comprise one or more of styrene, ethylbenzene, toluene, and benzene.

8. The method of claim 7 , further comprising blending the condensed compounds into the hydrocarbon feedstock.

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

10. The method of claim 9 , 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 an interior bottom section of the direct contact condenser; and
a decanted aromatics outlet line in fluid connection with the interior bottom section of the direct contact condenser.

11. The method of claim 1 , wherein a cooled offgas stream 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 cooled offgas stream outlet line.

12. The method of claim 11 , 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.

13. The method of claim 1 , wherein the direct contact condenser has an interior top section and an interior bottom section, wherein a cooled offgas stream 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 cooled offgas stream outlet line, and wherein the direct contact condenser is located between the vacuum compressor and the reactor.

14. The method of claim 13 , 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.

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

16. The method of claim 15 , wherein the vacuum compressor is in fluid connection with a cooled offgas stream outlet line, wherein the cooled offgas stream outlet line is in fluid connection with an interior top section of the direct contact condenser.

17. The method of claim 16 , wherein the direct contact condenser is installed in a suction knock out drum, has an interior top section and an interior bottom section, and 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; and
a decanted aromatics outlet line in fluid connection with the interior bottom section of the direct contact condenser.

Assignees

• Fina Technology

Inventors

• Welch Vincent A
• Butler James R

Classifications

• C01B2203/0495

  the impurity being water · CPC title

• C01B2203/048

  the impurity being an organic compound · CPC title

• C01B3/24

  of hydrocarbons · CPC title

• Y10S585/921

  using recited apparatus structure · CPC title

• F28B9/06

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