Process for the preparation of higher alcohols

Patent metadata

Field	Value
Publication number	US-9346725-B2
Application number	US-201214358377-A
Country	US
Kind code	B2
Filing date	Nov 7, 2012
Priority date	Nov 18, 2011
Publication date	May 24, 2016
Grant date	May 24, 2016

Abstract

Process for production of a higher alcohol product from an alcohol synthesis gas comprising hydrogen, carbon monoxide, carbon dioxide, and lower alcohols, comprising a carbon dioxide and optional alkane removal step. Use a stripper using synthesis gas as stripping gas to purify the liquid phase containing the lower and highers alcohols, in order to strip the lower alcohol from the alcohol stream. Synthesis gas used for stripping is used as recycle stream in the reactor.

First claim

The invention claimed is:

1. A process for production of a higher alcohol product, comprising the steps of:
(a) providing an alcohol synthesis gas comprising hydrogen, carbon monoxide and lower alcohols by mixing a fresh synthesis gas with a gaseous recycle stream comprising the lower alcohols;
(b) converting the alcohol synthesis gas into a crude alcohol product stream comprising higher alcohols and unconverted alcohol synthesis gas in presence of one or more catalysts active in conversion the alcohol synthesis gas;
(c) cooling and separating the crude alcohol product stream withdrawn from step (b) into a gas phase comprising hydrogen, carbon monoxide and carbon dioxide and optionally alkanes and into a liquid product comprising the lower alcohols from the unconverted alcohol synthesis gas and the higher alcohols formed in the conversion of the alcohol synthesis gas;
(d) subjecting the gas phase from step (c) to a carbon dioxide and optional alkane removal step and reducing content of carbon dioxide and optionally alkanes in the gas phase;
(e) recycling the liquid product obtained from step (c) to a stripping treatment and stripping the liquid product with the gas phase obtained in step (d) to form the recycle stream in step (a);
(f) subsequent the stripping treatment of the liquid phase in step (e) withdrawing the stripped liquid phase being depleted in the lower alcohols and subjecting the thus treated liquid phase to a separation; and
(g) recovering the higher alcohol product from the separation in step (f).

2. The process of claim 1 , wherein the one or more catalysts in step (b) comprise copper, zinc oxide and aluminium oxide and are optionally promoted with one or more metals selected from alkali metals, basic oxides of earth alkali metals and lanthanides.

3. The process of claim 1 , comprising the further step of introducing a stream of the lower alcohols being separated from the higher alcohol product in the separation of step (f) into the stripping treatment of step (e).

4. The process of claim 1 , comprising the further steps of:
cooling the crude alcohol product from step (b); and
contacting the cooled product with a hydrogenation catalyst in presence of a hydrogenation catalyst prior to introduction into step (c).

5. The process of claim 1 , wherein amounts of carbonyl compounds being present in the alcohol synthesis gas are reduced in the synthesis gas by contacting the gas with a sorbent comprising copper aluminium spinel being modified by reduction in a reducing atmosphere at a temperature of between 200° C. and 500° C. prior to being contacted with the synthesis gas.

6. The process of claim 5 , wherein the sorbent comprises copper in excess to the amount of copper contained in the copper aluminum spinel.

7. The process of claim 5 , wherein the sorbent is arranged on top of a fixed bed of catalyst in step (b).

8. The process of claim 1 , wherein the conversion of the alcohol synthesis gas is performed at a pressure of between 2 and 15 MPa and a temperature of above 220° C.

9. The process of claim 4 , wherein the hydrogenation catalyst comprises copper, zinc oxide and aluminium oxide.

10. The process of claim 4 , wherein the hydrogenation catalyst comprises platinum and/or palladium.

11. The process of claim 1 , wherein a further stream of lower alcohols is introduced into the alcohol synthesis gas upstream the step (b).

12. The process of claim 4 , wherein a further stream of ketones and/or aldehydes is introduced into the alcohol synthesis gas.

13. The process of claim 12 , wherein the further stream of ketones and/or aldehydes is introduced during the stripping treatment in step (e).

14. The process of claim 1 , wherein the carbon dioxide and alkane removal step is performed by a physical wash.

Assignees

• Haldor Topsoe As
• Haldor Topsoe As

Inventors

• Wix Christian

Classifications

• C07C29/1518

  one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis · CPC title

• C07C29/32 Primary

  increasing the number of carbon atoms by reactions without formation of -OH groups · CPC title

• C07C29/76

  by physical treatment · CPC title

• C07C29/34 Primary

  by condensation involving hydroxy groups or the mineral ester groups derived therefrom, e.g. Guerbet reaction · CPC title

• C07C29/132

  by reduction of an oxygen containing functional group · CPC title