Displacement desorption process for light olefin separation

Patent metadata

Field	Value
Publication number	US-9376354-B2
Application number	US-201113819007-A
Country	US
Kind code	B2
Filing date	Aug 26, 2011
Priority date	Aug 26, 2010
Publication date	Jun 28, 2016
Grant date	Jun 28, 2016

Abstract

A process and apparatus for separating an olefin from mixed gases containing light olefins is provided. The process includes adsorbing the olefin of an olefin-containing mixed gas in an adsorption column packed with an adsorbent selectively adsorbing the olefin; discharging gases other than the olefin through the outlet of the adsorption column; desorbing the adsorbed olefin by displacement using a desorbent, and separating the olefin from the desorbent, thereby producing a high-purity olefin. The apparatus includes adsorption columns packed with an adsorbent selectively adsorbing an olefin, and at least two distillation columns for separating an olefin/desorbent mixture and an olefin poor stream/desorbent into their components. If the olefin concentration of the off-gas from an olefin rinse step is higher than that of a raw material gas, recovering the olefin from the off-gas is carried out before or after the adsorption step.

First claim

The invention claimed is:

1. A method for separating an olefin from an olefin-containing mixed gas using at least one adsorption column and at least two distillation columns including a distillation column that separates an olefin rich stream and a desorbent and a distillation column that separates an olefin poor stream and a desorbent, the method comprising:
i) adsorption step: introducing the olefin-containing mixed gas into an adsorption column packed with an olefin selective adsorbent to adsorb an olefin from the mixed gas, and discharging unadsorbed components and a desorbent retained in the adsorption column at a desorption step to the outlet of the adsorption column and then discharging them to the distillation column that separates an olefin poor stream and a desorbent;
ii) rinse step: introducing a high-concentration olefin, obtained from the distillation column that separates an olefin rich stream and a desorbent, into the adsorption column, thereby removing paraffin and other gases from the adsorption, column to increase the purity of the olefin in the adsorption column;
iii) desorption step: introducing the desorbent, which was separated from the distillation columns in the steps i) and ii), or another desorbent, which is introduced independently of the desorbent separated in the steps i) and ii), into the adsorption column having been subjected to the step ii), to desorb the olefin from the adsorption column so as to form an olefin/desorbent mixture, and then sending the olefin/desorbent mixture to the distillation column that separates an olefin rich stream and a desorbent, thereby producing a high-purity olefin; and
before or after the step i), iv) recovery step: introducing an olefin-containing gas discharged from the rinse step into the adsorption column, thereby recovering an olefin from the olefin-containing gas.

2. The process of claim 1 , wherein the steps i) to iv) are repeatedly carried out in a plurality of adsorption columns.

3. The method of claim 1 , wherein, if the pressure of step i) is higher than atmospheric pressure, the process further comprises, before step ii), a step of discharging components other than olefin from the adsorption column by cocurrent pressurization.

4. The method of claim 1 , wherein the olefin selective adsorbent is a π-complex adsorbent selectively forming a π-complex with ethylene, a zeolite X adsorbent, a zeolite Y adsorbent or a zeolite A adsorbent.

5. The method of claim 1 , wherein the desorbent is a C3-C6 hydrocarbon.

6. The method of claim 1 , wherein step i) or iii) is carried out under conditions of a pressure of 1-30 atm and a temperature of 20˜150° C.

7. The method of claim 1 , wherein the desorbent separated in the distillation column for separating the olefin-poor stream/desorbent mixture and in the distillation column for separating the olefin rich stream/desorbent mixture is recycled to the adsorption column.

Assignees

• Kim Jong Nam
• Park Jong Ho
• Beum Hee Tae
• Lee Seong Jun
• Lee Jang Jae
• Kim Dong Wook
• Ko Chang Hyun
• Han Sang Sup
• Cho Soon Haeng
• Korea Energy Research Inst
• Sk Innovation Co Ltd

Inventors

• Kim Jong Nam
• Park Jong Ho
• Beum Hee Tae
• Lee Seong Jun
• Lee Jang Jae
• Kim Dong Wook
• Ko Chang Hyun
• Han Sang Sup
• Cho Soon Haeng

Classifications

• B01D53/04 Primary

  with stationary adsorbents {(B01D53/025 takes precedence)} · CPC title

• B01D2259/404

  using four beds · CPC title

• C07C11/04

  Ethene · CPC title

• B01D2257/7022

  Aliphatic hydrocarbons · CPC title

• B01D2256/24

  Hydrocarbons · CPC title