Process for high temperature removal of trace chloride contaminants in a catalytic dehydrogenation process

Patent metadata

Field	Value
Publication number	US-9718747-B2
Application number	US-201313922071-A
Country	US
Kind code	B2
Filing date	Jun 19, 2013
Priority date	Jun 19, 2013
Publication date	Aug 1, 2017
Grant date	Aug 1, 2017

Abstract

A process for removal of trace chloride contaminants from a reactor effluent in a catalytic dehydrogenation process is described. The reactor effluent is compressed in a compressor to provide a compressed effluent. The compressed effluent is introduced from the compressor into a chloride treater. In the chloride treater, trace chloride contaminants in the compressed effluent are adsorbed to provide a treated effluent. The treated effluent is cooled in a cooler.

First claim

What is claimed is:

1. A process for removal of trace chloride contaminants in a reactor effluent in a catalytic dehydrogenation process, the process comprising:
compressing the reactor effluent, comprising trace chloride contaminants, hydrocarbons having 3 to 5 carbon atoms and from about 5 to 500 wppm polynuclear aromatics, in a compressor to provide a compressed effluent;
cooling or heating the compressed effluent to a temperature above the dew point of the compressed effluent, but below polymerization temperatures of the compressed effluent, to produce a cooled or heated compressed effluent, wherein the temperature to which the compressed effluent is cooled or heated is between 93° C. and 300° C.;
introducing the cooled or heated compressed effluent into a chloride remover;
adsorbing trace chlorides contaminants present in the cooled or heated compressed effluent in the chloride remover, to provide a treated effluent; and
cooling the treated effluent in a cooler to produce a cooled treated effluent.

2. The process of claim 1 , wherein adsorbing the chlorides takes place at a temperature between about 121° C. and 177° C.

3. The process of claim 1 , wherein adsorbing the chlorides comprises:
contacting the cooled or heated compressed effluent with an adsorbent material.

4. The process of claim 3 , wherein adsorbing the chlorides comprises physical adsorption, chemisorption, or a combination thereof.

5. The process of claim 3 , wherein the adsorbent material comprises activated alumina, a promoted alumina product, metal oxides, molecular sieves, or a combination thereof.

6. The process of claim 3 , wherein the adsorbent material comprises a highly promoted alumina.

7. The process of claim 1 , further comprising:
introducing the cooled treated effluent to a drier;
wherein cooling the treated effluent takes place downstream of the chloride remover and upstream of the drier.

8. The process of claim 1 , wherein the pressure of the compressed effluent is between about 345 kPa and 2750 kPa.

9. A process for removal of trace chloride contaminants from a reactor effluent in a catalytic dehydrogenation process, the process comprising:
dehydrogenating a hydrocarbon, feed comprising hydrocarbons having 3 to 5 carbon atoms in a dehydrogenation reaction zone under dehydrogenation reaction conditions in the presence of a dehydrogenation catalyst to form a reactor effluent comprising trace chloride contaminants, hydrocarbons having 3 to 5 carbon atoms and from about 5 to 500 wppm polynuclear aromatics;
compressing the reactor effluent to provide a compressed effluent;
introducing the compressed effluent into a chloride remover at a temperature that is above the dew point of the compressed effluent, yet below polymerization reaction temperatures of the compressed effluent, wherein the temperature at which the compressed effluent is introduced into the chloride remover is between 93° C. and 300° C.;
adsorbing trace chloride contaminants present in the compressed effluent in the chloride remover with an adsorbent to provide a treated effluent; and
cooling the treated effluent to produce a cooled treated effluent.

10. The process of claim 9 , wherein the adsorbent comprises an activated alumina, a promoted alumina product, metal oxides, molecular sieves, or combinations thereof.

11. The process of claim 9 , wherein adsorbing the trace chloride contaminants takes place at a pressure between about 345 kPa to 2750 kPa.

12. The process of claim 9 , wherein adsorbing the trace chloride contaminants comprises physical adsorption, chemisorption, or a combination thereof.

13. The process of claim 9 , further comprising:
introducing the cooled treated effluent to a drier;
wherein cooling the treated effluent takes place downstream of the chloride remover and upstream of the drier.

14. The process of claim 13 , further comprising:
separating an olefin product, an unconverted paraffin, and a recycle hydrogen stream from an output stream of the drier;
recovering the olefin product; and
recycling the recycle hydrogen stream and the unconverted paraffin to the dehydrogenation reaction zone.

Assignees

• Uop Llc

Inventors

• Luebke Charles P
• Gorawara Jayant K
• Kanazirev Vladislav I

Classifications

• C07C7/12 Primary

  by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers · CPC title

• C07C5/327 Primary

  Formation of non-aromatic carbon-to-carbon double bonds only · CPC title

• C07C11/08

  with four carbon atoms · CPC title

• C07C11/06

  Propene · CPC title