# US 2014/0194659 A1 · Staged propylene production process

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- Number: US 2014/0194659 A1
- Document ID: US20140194659A1
- Status: Published application
- Kind: A1
- Application number: 13/738,631
- Filed: 2013-01-10
- Published: 2014-07-10
- Earliest claimed: 2013-01-10
- Assignees: Equistar Chemicals, LP; Lyondell Chemical Technology, L.P.
- Inventors: Allen David Hood, JR.; Robert S. Bridges
- Web page: https://patentgrep.com/patent/US20140194659A1

## CPC

- C07C 4/06: Catalytic processes {(C07C4/025 takes precedence)}
- C07C 6/04: at a carbon-to-carbon double bond
- C07C: ACYCLIC OR CARBOCYCLIC COMPOUNDS

## Abstract

Processes for forming propylene are described herein. The processes generally include reacting a metathesis feed stream including butene with ethylene in the presence of a first metathesis catalyst via a first metathesis reaction to form a first metathesis product stream including propylene, ethylene, butene, and C5+ olefins; separating at least a portion of the propylene and ethylene from the first metathesis product stream to form a first overhead stream and to form a first de-propenized bottoms stream including butene and C5+ olefins; reacting at least a portion of the first de-propenized bottoms stream with ethylene in the presence of a second metathesis catalyst via a second metathesis reaction to form a second metathesis product stream including propylene, ethylene, butene, and C5+ olefins; and separating at least a portion of the propylene and ethylene from the second metathesis product stream to form a second overhead stream; and recovering propylene from the first overhead stream, the second overhead stream or combinations thereof.

## Claims

### Claim 1

A process for forming propylene comprising:
reacting a metathesis feed stream comprising butene with ethylene in the presence of a first metathesis catalyst via a first metathesis reaction to form a first metathesis product stream comprising propylene, ethylene, butene, and C5+ olefins, wherein the first metathesis reaction takes place at an first ethylene:butene ratio of from 0.3:1 to 3:1;
separating at least a portion of the propylene and ethylene from the first metathesis product stream to form a first overhead stream and to form a first de-propenized bottoms stream comprising butene and C5+ olefins;
reacting at least a portion of the first de-propenized bottoms stream with ethylene in the presence of a second metathesis catalyst via a second metathesis reaction to form a second metathesis product stream comprising propylene, ethylene, butene, and C5+ olefins, wherein the second metathesis reaction takes place at an second ethylene:butene ratio of from 2.0:1 to 10:1; and
separating at least a portion of the propylene and ethylene from the second metathesis product stream to form a second overhead stream; and
recovering propylene from the first overhead stream, the second overhead stream or combinations thereof.

### Claim 2 (depends on 1)

The process of claim 1 further, wherein the first overhead stream comprises propylene and ethylene and the second overhead stream comprises propylene and ethylene.

### Claim 3 (depends on 1)

The process of claim 1 further comprising:
separating at least a portion of the first overhead stream to form an ethylene stream and a propylene stream.

### Claim 4 (depends on 1)

The process of claim 1 further comprising:
separating at least a portion of the second overhead stream to form an ethylene stream and a propylene stream.

### Claim 5 (depends on 1)

The process of claim 1 further comprising:
separating at least a portion of the first overhead stream and at least a portion of the second overhead stream to form an ethylene stream and a propylene stream.

### Claim 6 (depends on 5)

The process of claim 5 further comprising recycling at least a portion of the ethylene stream to the first metathesis reaction, the second metathesis reaction or a combination thereof.

### Claim 7 (depends on 1)

The process of claim 1, wherein the metathesis feed stream further comprises Raffinate-2.

### Claim 8 (depends on 1)

The process of claim 1, wherein the first metathesis reaction, the second metathesis reaction or a combination thereof further comprises reacting the corresponding metathesis feed stream with ethylene in the presence of an isomerization catalyst.

### Claim 9 (depends on 8)

The process of claim 8, wherein the isomerization catalyst comprises magnesium oxide.

### Claim 10 (depends on 1)

The process of claim 1, wherein ethylene is introduced to the first metathesis reaction and the second metathesis reaction at rates sufficient to provide a lower ethylene:butene ratio contacting the first metathesis catalyst than the ethylene:butene ratio contacting the second metathesis catalyst.

### Claim 11 (depends on 1)

The process of claim 1, wherein the first metathesis reaction takes place at an first ethylene:butene ratio of from 0.5:1 to 2.5:1.

### Claim 12 (depends on 11)

The process of claim 11, wherein the second metathesis reaction takes place at an second ethylene:butene ratio of from 3.75:1 to 6.75:1.

### Claim 13 (depends on 1)

The process of claim 1, wherein the process exhibits a total butene conversion of at least 85%.

### Claim 14 (depends on 1)

The process of claim 1, wherein the first metathesis catalyst and the second metathesis catalyst comprise a transition metal oxide.

### Claim 15 (depends on 1)

The process of claim 1, wherein the first metathesis catalyst and second metathesis catalyst comprise the same material.

### Claim 16 (depends on 1)

The process of claim 1, wherein separating at least a portion of the propylene and ethylene from the second metathesis product forms a second de-propenized bottoms stream comprising butene and C5+ olefins.

### Claim 17

(canceled)
