Air purification process

• US 6,238,460 B1
• Filed: 03/26/1999
• Issued: 05/29/2001
• Est. Priority Date: 09/26/1997
• Status: Expired due to Fees

• Current Assignee: BOC Group, Inc. (Messer Adolf Family)
• Original Assignee: BOC Group, Inc. (Messer Adolf Family)
• Inventors: Gittleman, Craig S., Ojo, Adeola Florence, Kumar, Ravi, Fitch, Frank R., Bulow, Martin, Deng, Shuguang
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US09/277,306
• Time in Patent Office: 795 Days
• Field of Search: 95/96-98, 95/100-105, 95/117-119, 95/121, 95/122, 95/139
• US Class Current: 95/98
• CPC Class Codes: B01D 2253/104 Alumina
• CPC Class Codes: B01D 2253/108 Zeolites
• CPC Class Codes: B01D 2253/1085 characterized by a silicon-aluminium ratio
• CPC Class Codes: B01D 2256/22 Carbon dioxide
• CPC Class Codes: B01D 2259/40052 Recycled product or process gas
• CPC Class Codes: B01D 2259/416 involving cryogenic temperature treatment
• CPC Class Codes: B01D 53/02 by adsorption, e.g. preparative gas chromatography solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: B01D 53/261 by adsorption
• CPC Class Codes: Y02C 20/40 of CO2

Abstract

Substantially all of the carbon dioxide is removed from a gas containing up to about 1% by volume carbon dioxide by subjecting the gas to a pressure swing adsorption process using a two layer adsorption system, wherein the first layer contains activated alumina and the second layer is a zeolite or a combination of zeolites having a silicon to aluminum atomic ratio of at least 1.5. The process is particularly suitable for removing substantially all carbon dioxide and water vapor contained in air prior to subjecting the air to cryogenic distillation.

Claims

1. A method of removing carbon dioxide from air containing up to 1000 ppm carbon dioxide by a pressure swing adsorption process having an adsorption step and an adsorbent regeneration step, the adsorption step of which comprises passing said gas through a two layer adsorption zone containing a first layer of activated alumina and a second layer comprising dealuminated type Y zeolite having a high capacity for carbon dioxide and a low capacity for nitrogen and oxygen and having a silicon/aluminum atomic ratio of at least about 1.5, thereby producing a substantially carbon dioxide-free gas stream.

2. The method of claim 1, wherein said silicon/aluminum atomic ratio is in the range of about 2.0 to about 150.

3. The method of claim 1, wherein said gas additionally contains water vapor and said water vapor is removed from said gas as it passes through said layer of activated alumina, thereby producing a substantially water vapor- and carbon dioxide-free gas.

4. The method of claim 3, wherein the air leaving said adsorption zone is subjected to a cryogenic distillation step.

5. The method of claim 4, wherein the adsorbents in said adsorption zone are purged with a waste stream produced during said cryogenic distillation step during at least part of said adsorbent regeneration step.

6. The method of claim 1 or claim 3, wherein said adsorption step is carried out at a temperature in the range of about 0 to about 50°

C.

7. The method of claim 6, wherein said adsorption step is carried out at a pressure in the range of about 0.9 to about 50 bara.

8. The method of claim 6, wherein said adsorbent regeneration step is carried out a pressure in the range of about 0.1 to about 2 bara.

9. The method of claim 1 or claim 3, wherein said adsorbent regeneration step is carried out at a temperature in the range of about 0 to about 100°

C.

10. The method of claim 1 or claim 3, wherein the adsorbents in said adsorption zone are purged with a substantially water vapor- and carbon dioxide-free gas stream during at least part of said adsorbent regeneration step.