IP Library › Granted Patent US 9,079,168
Granted Patent B2
US 9,079,168 · App. 12/676,118 · Granted Jul 14, 2015

Process for producing propylene

Inventors: Haruyuki Minoura (Tokyo, JP); Yoshikazu Takamatsu (Tokyo, JP)
Assignee: ASAHI KASEI CHEMICALS CORPORATION
B01J35/002B01J29/40B01J29/44B01J37/0009B01J37/10B01J37/30C07C6/04B01J2229/36
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Quick Facts
Patent No.
US 9,079,168
App. No.
12/676,118
Granted
Jul 14, 2015
Kind
B2
Abstract

An object of the present invention is to provide a process for producing efficiently and stably propylene from a hydrocarbon raw material containing a high concentration of ethylene. The present invention discloses a process for producing propylene, comprising catalytically converting a hydrocarbon raw material containing ethylene in an amount exceeding 50% by mass with a zeolite-containing catalyst satisfying the following (1) to (3): (1) containing of a medium pore diameter zeolite having a pore size of from 5 to 6.5 Å; (2) a SiO 2 /Al 2 O 3 molar ratio in the medium pore diameter zeolite being from 20 to 300; and (3) an acid amount (TPD acid amount), determined by a high-temperature desorption amount in an ammonia temperature-programmed desorption spectrum, being from 20 to 350 μmol/g-zeolite.

Claims (10)

1. A process for producing propylene, comprising catalytically converting at a temperature within a range of 400 to 600° C. a hydrocarbon raw material containing ethylene in an amount exceeding 50% by mass to a propylene-containing gas with a zeolite-containing catalyst satisfying the following (1) through (4):

(1) containing of a medium pore diameter zeolite having a pore size of from 5 to 6.5 Å;

(2) a SiO 2 /Al 2 O 3 molar ratio in the medium pore diameter zeolite being from 20 to 300;

(3) an acid amount (TPD acid amount), determined by a high-temperature desorption amount in an ammonia temperature-programmed desorption spectrum, being from 20 to 350 μmol/g-zeolite, and

(4) wherein the zeolite-containing catalyst is heat-treated at 300° C. or higher in the presence of water vapor,

wherein the conversion rate of ethylene is within the range from 50 -85% and wherein the yield of propylene is greater than 20.6 weight %.

2. The process for producing propylene according to claim 1 , wherein the zeolite-containing catalyst is heat-treated at 550° C. or higher.

3. The process for producing propylene according to claim 1 or 2 , wherein the zeolite-containing catalyst comprises at least one element selected from the group consisting of the elements belonging to the group IB in the periodic table.

4. The process for producing propylene according to claim 1 or 2 , comprising a step in which the hydrocarbon raw material and 10% by mass or more of water based on the hydrocarbon raw material are brought into contact with the zeolite-containing catalyst.

5. The process for producing propylene according to claim 1 or 2 , comprising a step in which propylene is separated from the propylene-containing gas produced by the contact of the hydrocarbon raw material with the zeolite-containing catalyst, and at least part of the remaining gas is added to the hydrocarbon raw material.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 4, 2010
From: MINOURA, HARUYUKI; TAKAMATSU, YOSHIKAZU
To: ASAHI KASEI CHEMICALS CORPORATION
Reel/Frame 024030/0621 →
Priority Claims (1)
JP 2007-231400 · Sep 6, 2007 · national
Continuity (1)
Related Publication 20100204532A1 · Aug 12, 2010