Cleaning of liquid hydrocarbon streams by means of copper-containing sorbents

Patent metadata

Field	Value
Publication number	US-9963644-B2
Application number	US-201415103805-A
Country	US
Kind code	B2
Filing date	Nov 5, 2014
Priority date	Dec 12, 2013
Publication date	May 8, 2018
Grant date	May 8, 2018

Abstract

The invention relates to a method for cleaning hydrocarbon mixtures, in which a contaminated hydrocarbon mixture comprising hydrocarbons having three to eight carbon atoms is at least partly freed of impurities by contacting with a solid sorbent, wherein the hydrocarbon mixture is exclusively in the liquid state during contact with the sorbent. The object of the invention is to specify a process for cleaning liquid C 3 to C 8 hydrocarbon mixtures, which is based on a readily available but non-carcinogenic sorbent and which achieves better purities compared to traditional molecular sieves. This object is achieved by using, as sorbents, solid materials of the following composition:
copper oxide: 10% to 60% by weight (calculated as CuO); zinc oxide: 10% to 60% by weight (calculated as ZnO); aluminum oxide: 10% to 30% by weight (calculated as Al 2 O 3 ); other substances: 0% to 5% by weight.

Materials of this kind are otherwise used as catalysts in methanol synthesis.

First claim

What is claimed is:

1. Process for purifying hydrocarbon mixtures, in which a contaminated hydrocarbon mixture comprising hydrocarbons having three to eight carbon atoms is at least partly freed of contaminants by contacting it with a solid sorbent in the absence of hydrogen, the hydrocarbon mixture being exclusively in the liquid state during the contact with the sorbent, wherein the sorbent has the following composition that adds up to 100% by weight:
copper oxide: 10% to 60% by weight (calculated as CuO);
zinc oxide: 10% to 60% by weight (calculated as ZnO);
aluminium oxide: 10% to 30% by weight (calculated as Al 2 O 3 );
other substances: 0% to 5% by weight;
wherein the sorbent is supplied in an oxidized state without being activated by a reduction reaction; and
wherein the contact is effected under the following conditions:
temperature between 30° C. and 120° C.;
pressure between 0.5 and 3.5 MPa; and
weight hourly space velocity between 0.5 h −1 and 7 h −1 .

2. Process according to claim 1 , wherein the sorbent has the following composition that adds up to 100% by weight:
copper oxide: 30% to 45% by weight (calculated as CuO);
zinc oxide: 30% to 50% by weight (calculated as ZnO);
aluminium oxide: 10% to 15% by weight (calculated as Al 2 O 3 );
further metal oxides: 0% to 2% by weight;
graphite: 0% to 3% by weight;
other substances: 0% to 1% by weight.

3. Process according to claim 1 , wherein the contaminated hydrocarbon mixture contains at least one impurity from one of the following substance classes:
a) thiols having the general formula R—SH where R may be an alkyl, aryl, cycloalkyl or alkenyl radical;
b) disulphides having the general formula R—S—S—R′ where R and R′ may be identical or different alkyl, aryl, cycloalkyl or alkenyl radicals;
c) sulphides having the general formula R—S—R′ where R and R′ may be identical or different alkyl, aryl, cycloalkyl or alkenyl radicals;
d) substituted or unsubstituted sulphur-containing heterocycles.

4. Process according to claim 1 , wherein the proportion by weight of the contaminants in the contaminated hydrocarbon mixture, based on the total weight thereof, is less than 0.2% by weight.

5. Process according to claim 1 , wherein the sorbent is used irreversibly.

6. Process according to claim 1 , wherein the contaminated hydrocarbon mixture fulfils one of the following specifications A, B, C and D, each of which adds up to 100% by weight, the stated proportions by weight each being based on the total weight of the contaminated hydrocarbon mixture:
Specification A:
isobutane 20% to 40% by weight;
n-butane 5% to 18% by weight;
1-butene 5% to 15% by weight;
isobutene 12% to 25% by weight;
2-butenes 9% to 40% by weight;
1,3-butadiene 0% to 3% by weight;
water 0% to 1% by weight;
contaminants less than 0.5% by weight;

Specification B:
isobutane 0.6% to 8% by weight;
n-butane 0.5% to 8% by weight;
1-butene 9% to 25% by weight;
isobutene 10% to 35% by weight;
2-butenes 3% to 15% by weight;
1,3-butadiene 25% to 70% by weight;
water 0% to 1% by weight;
contaminants less than 0.5% by weight;

Specification C:
isobutane 0.6% to 8% by weight;
n-butane 0.5% to 15% by weight;
1-butene 9% to 40% by weight;
isobutene 10% to 55% by weight;
2-butenes 3% to 25% by weight;
1,3-butadiene 0% to 1% by weight;
water 0% to 1% by weight;
contaminants less than 0.5% by weight;

Specification D:
n-butane 10% to 30% by weight;
1-butene 0.2% to 45% by weight;
2-butenes 35% to 85% by weight;
water 0% to 1% by weight;
contaminants less than 0.5% by weight.

7. Process according to claim 1 , further comprising one or more of the following steps:
a) extracting 1,3-butadiene from the hydrocarbon mixture which has been at least partly freed of contaminants;
b) selectively hydrogenating diolefins, acetylenes, or diolefins and acetylenes in the hydrocarbon mixture which has been at least partly freed of contaminants to form olefins;
c) oligomerizing olefins present in the hydrocarbon mixture which has been at least partly freed of contaminants to form oligomers;
d) distilling the hydrocarbon mixture which has been at least partly freed of contaminants to remove 1-butene, isobutene or both 1-butene and isobutene from the hydrocarbon mixture which has been at least partly freed of contaminants;
e) removing isobutene from the hydrocarbon mixture which has been at least partly freed of contaminants by converting the isobutene to tert-butanol with water or by converting the isobutene to methyl tert-butyl ether with methanol;
f) dehydrogenating butanes present in the hydrocarbon mixture which has been at least partly freed of contaminants to form butenes;
g) oxidatively dehydrogenating butenes present in the hydrocarbon mixture which has been at least partly freed of contaminants to form butadiene;
h) alkylating n-butene present in the hydrocarbon mixture which has been at least partly freed of contaminants with isobutane present in the hydrocarbon mixture which has been at least partly freed of contaminants;
i) oxidizing hydrocarbons having four carbon atoms present in the hydrocarbon mixture in the hydrocarbon mixture which has been at least partly freed of contaminants.

8. Process according to claim 3 , where R and R′ are each independently selected from a methyl, an ethyl, a propyl, a butyl, a phenyl, a cyclohexyl or a butenyl radical.

9. Process according to claim 3 , where the substituted or unsubstituted sulphur-containing heterocycles comprise thiophenes, thiolanes or both thiophenes and thiolanes.

10. Process according to claim 1 , wherein the proportion by weight of the contaminants in the contaminated hydrocarbon mixture, based on the total weight thereof, is less than 100 ppm by weight.

11. Process according to claim 1 , wherein the proportion by weight of the contaminants in the contaminated hydrocarbon mixture, based on the total weight thereof, is less than 10 ppm by weight.

Assignees

• Evonik Degussa Gmbh

Inventors

• Geilen Frank
• Peitz Stephan
• Stochniol Guido
• Winterberg Markus
• Maschmeyer Dietrich
• Rix Armin
• Vogt Mathias

Classifications

• C10G25/003 Primary

  Specific sorbent material, not covered by C10G25/02 or C10G25/03 · CPC title

• B01J2220/42

  Materials comprising a mixture of inorganic materials (materials coated or impregnated on a carrier B01J20/32) · CPC title

• C10G55/04

  including at least one thermal cracking step · CPC title

• C07C7/13

  by molecular-sieve technique · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title