US4123462A
Expired / Lapsed
US
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Amination process using nickel-rhenium catalysts
Assignee: Union Carbide Corp
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Filing: 1976-01-07
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Granted: 1978-10-31
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Expires: 1996-01-07
Abstract
Abstract The present invention concerns a new nickel-rhenium catalyst and method of preparing said catalyst. The invention also relates to the catalytic amination of lower aliphatic alkane derivatives such as alkanemono-ols, alkanediols and alcoholamines utilizing the new nickel-rhenium catalyst.
Inventors
- 👤 Donald C. Best
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 13:35
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/76; B01J23/84; B01J23/889; B01J23/8896; C; C07; C07C; C07C209/00; C07C209/04; C07C209/14; C07C209/16; C07C209/24; C07C209/28
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
152 words
In the process for aminating a lower aliphatic alkane derivative with ammonia in the presence of a solid catalyst wherein the products comprise both economically desirable alkylamines and undesirable by-products of lesser economic significance, the improvement in selectivity and increased conversion, evidenced by the production of a substantially greater amount of said valuable alkylamines together with concomitant reduction in the yield of undesirable by-products from a given alkane charge, which comprises reacting under amination conditions said alkane charge with ammonia in the presence of hydrogen and a nickel-rhenium catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths and silica-titanias, wherein said catalyst has a total nickel and rhenium metal content of 3-30% by weight of the support and the atom ratio of the nickel to the rehnium present is in the range from about 2:1 to about 30:1.
Claim 2
Dependent Claim
152 words
In the process for aminating a lower aliphatic alkane derivative with ammonia in the presence of a solid catalyst wherein the products comprise both economically desirable alkylamines and undesirable by-products of lesser economic significance, the improvement in selectivity and increased conversion, evidenced by the production of a substantially greater amount of said valuable alkylamines together with concomitant reduction in the yield of undesirable by-products from a given alkane charge, which comprises reacting under amination conditions said alkane charge with ammonia in the presence of hydrogen and a nickel-rhenium catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths and silica-titanias, wherein said catalyst has a total nickel and rhenium metal content of 3-30% by weight of the support and the atom ratio of the nickel to the rehnium present is in the range from about 2:1 to about 30:1.
Claim 3
Dependent Claim
35 words
The process of claim 1 wherein said alkane derivative contains from one to six carbon atoms and at least one functional group capable of being replaced by an amino group by the catalytic amination process.
Claim 4
Dependent Claim
23 words
The process of claim 1 wherein said alkane derivative contains from one to six carbon atoms and at least one hydroxy functional group.
Claim 5
Dependent Claim
29 words
The process of claim 1 wherein the desirable alkylamine product is ethylenediamine and the alkane derivative is selected from the group consisting of ethylene glycol, monoethanolamine, and mixtures thereof.
Claim 6
Dependent Claim
18 words
The process of claim 1 wherein said catalyst is comprised of boron in addition to nickel and rhenium.
Claim 7
Dependent Claim
20 words
The process of claim 1 wherein said catalyst is comprised of boron and cobalt in addition to nickel and rhenium.
Claim 8
Dependent Claim
12 words
The process of claim 1 wherein said support material is an α-alumina.
Claim 9
Dependent Claim
12 words
The process of claim 1 wherein said support material is a silica-alumina.
Claim 10
Dependent Claim
27 words
The process of claim 4 wherein the ammonia is present in an amount greater than the stochiometric amount required by the alkane derivative coreactant that is present.
Claim 11
Dependent Claim
27 words
The process of claim 9 wherein the ammonia is present in an amount in the range 2-15 times the stochiometric amount required by the alkane derivative coreactant.
Claim 12
Dependent Claim
134 words
A process for producing lower aminoalkanes by the catalytic amination of lower aliphatic alkane derivatives selected from lower alkanemono-ols, lower alkanediols, lower alkanolamines, and mixtures thereof, said process comprising the step of reacting said alkane derivatives with ammonia under pressure, at a temperature of from 125° C to 350° C, and in the presence of hydrogen and an active nickel-rhenium catalyst, said catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths, and silicatitanias, wherein the nickel and rhenium metal content is from 3-30% by weight of the support material and the atom ratio of the nickel to the rhenium present is in the range from about 2:1 to about 30:1, and wherein said catalyst is present in a catalytic amount.
Claim 13
Dependent Claim
134 words
A process for producing lower aminoalkanes by the catalytic amination of lower aliphatic alkane derivatives selected from lower alkanemono-ols, lower alkanediols, lower alkanolamines, and mixtures thereof, said process comprising the step of reacting said alkane derivatives with ammonia under pressure, at a temperature of from 125° C to 350° C, and in the presence of hydrogen and an active nickel-rhenium catalyst, said catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths, and silicatitanias, wherein the nickel and rhenium metal content is from 3-30% by weight of the support material and the atom ratio of the nickel to the rhenium present is in the range from about 2:1 to about 30:1, and wherein said catalyst is present in a catalytic amount.
Claim 14
Dependent Claim
24 words
The process of claim 11 wherein the catalyst is activated by heating it in the presence of hydrogen in the temperature range 200°-600° C.
Claim 15
Dependent Claim
20 words
The process of claim 11 wherein the pressure during the reaction is in the range of 500 to 5,000 psig.
Claim 16
Dependent Claim
12 words
The process of claim 11 wherein the lower aliphatic alcohol is 1,3-propanediol.
Claim 17
Dependent Claim
16 words
The process of claim 11 wherein the lower aliphatic alcohol is selected from ethanol and 2-propanol.
Claim 18
Dependent Claim
152 words
A process for producing ethylenediamine by the catalytic amination of a compound selected from the group consisting of ethylene glycol, monoethanolamine, ethyleneoxide, ethyleneimine, and mixtures thereof, said process comprising reacting said compound with ammonia in the presence of hydrogen and a Ni-Re catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths, and silica-titanias, said catalyst having a total nickel and rhenium metal content of 3-30% by weight of the support and a nickel to rhenium atom ratio in the range from about 2:1 to about 30:1 and wherein said catalyst is activated in the presence of hydrogen at elevated temperature, and wherein the temperature of the amination reaction is in the range 125°-350° C, the pressure is 500-5000 psig and the amount of ammonia present is in excess of 2 times the stochiometric amount required by the compound.
Claim 19
Dependent Claim
152 words
A process for producing ethylenediamine by the catalytic amination of a compound selected from the group consisting of ethylene glycol, monoethanolamine, ethyleneoxide, ethyleneimine, and mixtures thereof, said process comprising reacting said compound with ammonia in the presence of hydrogen and a Ni-Re catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths, and silica-titanias, said catalyst having a total nickel and rhenium metal content of 3-30% by weight of the support and a nickel to rhenium atom ratio in the range from about 2:1 to about 30:1 and wherein said catalyst is activated in the presence of hydrogen at elevated temperature, and wherein the temperature of the amination reaction is in the range 125°-350° C, the pressure is 500-5000 psig and the amount of ammonia present is in excess of 2 times the stochiometric amount required by the compound.
References Cited (Backward Citations)
US3223735A
Cited
US3022349A
Cited
US3152185A
Cited
US3270059A
Cited
US3387032A
Cited
US3520933A
Cited
US3666412A
Cited
JPS4734181U
Cited
US3739029A
Cited
US4036883A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-10-30 | 1982-05-01 | 1982-10-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-10-30 | 1986-05-01 | 1986-10-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-10-30 | 1990-05-01 | 1990-10-31 | $7700.00 | Window Closed / Lapsed |