Process for purifying propylene

• US 6,406,521 B1
• Filed: 11/30/1999
• Issued: 06/18/2002
• Est. Priority Date: 11/30/1999
• Status: Expired due to Fees

• Current Assignee: UOP Llc (Honeywell International Inc.)
• Original Assignee: UOP Llc (Honeywell International Inc.)
• Inventors: Wilson, Stephen T., Yang, Ralph T., Padin, Joel, Rege, Salil U., Cheng, Linda S.
• Primary Examiner(s): Spitzer, Robert H.
• Application Number:
  US09/451,645
• Time in Patent Office: 931 Days
• Field of Search: 95/96--07, 951/10, 951/11, 951/44, 959/00, 959/02
• US Class Current: 95/98
• CPC Class Codes: B01D 2251/61 Phosphates
• CPC Class Codes: B01D 2253/116 Molecular sieves other than zeolites
• CPC Class Codes: B01D 2253/311 Porosity, e.g. pore volume
• CPC Class Codes: B01D 2256/24 Hydrocarbons
• CPC Class Codes: B01D 2257/7022 Aliphatic hydrocarbons
• CPC Class Codes: B01D 2259/4003 with two sub-steps
• CPC Class Codes: B01D 2259/40052 Recycled product or process gas
• CPC Class Codes: B01D 2259/40064 Five
• CPC Class Codes: B01D 2259/40079 Co-current
• CPC Class Codes: B01D 2259/40081 Counter-current
• CPC Class Codes: B01D 2259/402 using two beds
• CPC Class Codes: B01D 2259/404 using four beds
• CPC Class Codes: B01D 53/0476 Vacuum pressure swing adsorption
• CPC Class Codes: Y10S 95/902 Molecular sieve

Abstract

A process is provided for the concentration and recovery of propylene from propane by a pressure swing adsorption (PSA) process using an adsorbent comprising AlPO-14. A PSA process is used to remove propylene from a C₃ hydrocarbon stream comprising propylene and propane. The PSA process of the present invention can be employed in petroleum refining and petrochemical processes to purify and separate propylene from mixtures of propylene and propane without fractionation.

Claims

1. A process for the production of a high purity propylene stream from a mixture comprising propane and propylene, said process comprising:

a) contacting the mixture with a selective adsorbent comprising AlPO-14 at a temperature between 120°

C. and below a temperature of incipient reaction at an adsorption pressure in an adsorption step to provide an adsorption effluent stream comprising propane; and

b) desorbing propylene in desorption step at a desorption pressure lower than the adsorption pressure to provide a propylene product stream.

2. The process of claim 1 wherein the contacting of the mixture with the absorbent is carried out in a pressure swing adsorption process.

3. The process of claim 1 wherein the product stream comprises from about 95 to about 99.9 percent propylene.

4. A pressure swing adsorption process comprising:

a) admixing a feed stream comprising propylene and propane, and a recycle stream comprising propylene to provide a feed admixture and passing the feed admixture at an adsorption temperature between 120°

C. and below a temperature of incipient reaction and at an adsorption pressure to a first absorption bed in an adsorption zone comprising at least two adsorption beds, each of the adsorption beds containing an AlPO-14 adsorbent for the selective adsorption of propylene, and withdrawing an adsorption effluent comprising propane;

b) terminating the passing of the feed admixture to the first adsorption bed prior to breakthrough of propylene, and co-currently purging in a co-purge step with a purge gas stream at a purge pressure essentially equal to the adsorption pressure and withdrawing a purge effluent stream from the first adsorption bed;

c) terminating the co-purge step and desorbing the first adsorption bed at a desorption pressure lower than the adsorption pressure in a counter-current blowdown step to provide a high purity product stream comprising propylene;

d) compressing at least a portion of the high purity product stream to provide the purge gas stream and recycling the purge effluent stream to the adsorption step to provide the recycle stream;

e) co-currently repressurizing the first adsorption bed with the feed stream; and

f) repeating steps (a)-(e) to provide a continuous process.