Process for preparing linear butenes from methanol

Patent metadata

Field	Value
Publication number	US-9624143-B2
Application number	US-201314425976-A
Country	US
Kind code	B2
Filing date	Aug 28, 2013
Priority date	Sep 5, 2012
Publication date	Apr 18, 2017
Grant date	Apr 18, 2017

Abstract

The invention relates to a method for producing linear butenes from methanol. The problem addressed is that of specifying such a method in which the methanol used is converted, to the largest possible extent, into butenes. The problem is solved by combining a methanol-to-propylene process with a metathesis reaction by means of which the propene obtained from the methanol is converted into linear butenes.

First claim

The invention claimed is:

1. Process for preparing linear butenes from methanol, comprising:
a) reacting methanol in a first reaction stage to give a first reaction mixture containing dimethyl ether, water, and optionally unreacted methanol;
b) reacting dimethyl ether in a second reaction stage to give a second reaction mixture containing propene and further hydrocarbons having two, four, and five carbon atoms, where the second reaction stage is at least partly supplied with the first reaction mixture;
c) working-up the second reaction mixture to give a propene-rich fraction and at least one low-propene fraction, where the low-propene fraction is at least partly recirculated to the second reaction stage;
d) reacting propene in a third reaction stage to give a third reaction mixture containing ethene and linear butenes selected from the group consisting of 1-butene, cis-2-butene, trans-2-butene, where the third reaction stage is supplied at least partly with or from the propene-rich fraction;
e) working-up the third reaction mixture to give a target fraction rich in linear butenes and an ethene-rich fraction,
wherein the propene-rich fraction contains propane,
wherein the reaction in the third reaction stage occurs in the presence of propane, and
wherein a propane-rich fraction is isolated during the course of working-up the third reaction mixture.

2. Process according to claim 1 , wherein the ethene-rich fraction is at least partly recirculated to the second reaction stage.

3. Process according to claim 1 , further comprising:
f) converting ethene into a fourth reaction mixture comprising linear butenes selected from the group consisting of 1-butene, cis-2-butene, trans-2-butene in a fourth reaction stage, where the fourth reaction stage is supplied from the ethene-rich fraction.

4. Process according to claim 1 , wherein a fraction rich in hydrocarbons having two carbon atoms, a fraction rich in hydrocarbons having four carbon atoms, and a fraction rich in hydrocarbons having five carbon atoms are also isolated during the course of working-up the second reaction mixture, where the fraction rich in hydrocarbons having two carbon atoms and the fraction rich in hydrocarbons having five carbon atoms are at least partly recirculated to the second reaction stage.

5. Process according to claim 1 , wherein a high boiler fraction containing hydrocarbons having more than five carbon atoms is also isolated during the course of working-up the second reaction mixture.

6. Process according to claim 1 , wherein an aqueous fraction is also isolated during the course of of working-up the second reaction mixture.

7. Process according to claim 1 , wherein, prior to the reacting:
preparing a synthesis gas containing carbon monoxide and hydrogen from a water-containing or water-free carbon source, and optionally with addition of water or water vapour; and
in a fifth reaction stage, catalytically converting the synthesis gas into methanol for the reacting a).

8. Process according to claim 7 , wherein the carbon source is a fossil carbon source, a renewable carbon source, or a mixture thereof, and wherein the carbon source is selected from the group consisting of: hard coal, brown coal, petroleum fractions, peat, natural gas, oil sand, shale gas, wood, biogas, biomass, domestic waste, manure, and sewage sludge.

9. Process according to claim 1 , wherein the reaction in the first reaction stage occurs in the presence of a solid silica-alumina catalyst.

10. Process according to claim 1 , wherein the reaction in the second reaction stage occurs in the presence of a zeolite catalyst.

11. Process according to claim 1 , wherein the reaction in the third reaction stage occurs in the presence of a tungsten and/or molybdenum catalyst.

12. Process according to claim 11 , wherein propene which has not reacted in the third reaction stage is separated off from the third reaction mixture and recirculated to the third reaction stage.

13. Process according to claim 3 , wherein the reaction in the fourth reaction stage occurs in the presence of a catalytic system composed of trialkylaluminium and alkyl titanate in ethers.

Assignees

• Winterberg Markus
• Pettijohn Ted M
• Bowers Stephen
• Schallenberg Joerg
• Naeem Shahbaz
• Busch Oliver Markus
• Evonik Degussa Gmbh

Inventors

• Winterberg Markus
• Pettijohn Ted M
• Bowers Stephen
• Schallenberg Joerg
• Naeem Shahbaz
• Busch Oliver Markus

Classifications

• C07C43/043

  Dimethyl ether · CPC title

• C10J2300/0973

  Water · CPC title

• C07C11/06

  Propene · CPC title

• C07C11/08

  with four carbon atoms · CPC title

• C07C1/24

  by elimination of water · CPC title