Patent US4094921A successfully refreshed from Google Patents.
US4094921A
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Selective ethylation of mono alkyl benzenes
Assignee: Mobil Oil AS
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Filing: 1977-04-15
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Granted: 1978-06-13
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Expires: 1997-04-15
Abstract
Abstract A catalytic process is provided for the ethylation of a mono alkyl benzene wherein the alkyl substituent contains 1 or 2 carbon atoms, i.e. toluene or ethylbenzene, to selectively produce the para and meta derivatives of said mono alkyl benzene to the exclusion or substantial exclusion of the ortho derivative thereof by contacting said mono alkyl benzene, under conversion conditions, with an ethylating agent in the presence of a catalyst comprising a crystalline aluminosilicate zeolite, which zeolite is characterized by an activity, in terms of alpha value, of between about 2 and about 5000, and preferably between about 20 and about 500, a xylene sorption capacity greater than 1 gram/100 grams of zeolite and an ortho xylene sorption time for 30 percent of said capacity of greater than 10 minutes, said sorption capacity and sorption time being measured at 120 DEG C. and a xylene pressure of 4.5 +/- 0.8 mm. of mercury, said crystalline aluminosilicate zeolite being further characterized by having a silica to alumina ratio of at least about 12 and a constraint index, as hereinafter defined, within the approximate range of 1 to 12, said catalyst having been subjected to steam treatment at a temperature between about 250 and about 1000 DEG C. for a period of between about 0.5 and about 100 hours.
Inventors
- 👤 Warren W. Kaeding
- 👤 Lewis B. Young
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 03:56
CPC Classifications
C; C07; C07C; C07C2/00; C07C2/86; C07C2/862; C07C2/865; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/061; B01J29/40; C07C2/54; C07C2/64; C07C2/66; C07C2/861; C07C2/864; C07C2/868; B01J2229/00; B01J2229/10; B01J2229/26; B01J2229/30; B01J2229/36; B01J2229/42; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/40
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
192 words
Process for the ethylation of a mono alkyl benzene wherein the alkyl substituent contains 1 to 2 carbon atoms to selectively produce the para and meta derivatives of said mono alkyl benzene to the substantial exclusion of the ortho derivative thereof which comprises contacting said mono alkyl benzene under conversion conditions, with ethylene in the presence of a catalyst comprising a crystalline aluminosilicate zeolite, which zeolite is characterized by an activity, in terms of alpha value, of between about 2 and about 5000, a xylene sorption capacity greater than 1 gram/100 grams of zeolite and an ortho xylene sorption time for 30 percent of said capacity of greater than 10 minutes, said sorption capacity and sorption time being measured at 120° C. and a xylene pressure of 4.5 ± 0.8 mm. of mercury, said crystalline aluminosilicate zeolite further being characterized by a silica to alumina ratio of at least about 12, and a constraint index within the approximate range of 1 to 12, said catalyst having been subjected to steam treatment at a temperature between about 250° and about 1000° C. for a period of between about 0.5 and about 100 hours.
Claim 2
Dependent Claim
192 words
Process for the ethylation of a mono alkyl benzene wherein the alkyl substituent contains 1 to 2 carbon atoms to selectively produce the para and meta derivatives of said mono alkyl benzene to the substantial exclusion of the ortho derivative thereof which comprises contacting said mono alkyl benzene under conversion conditions, with ethylene in the presence of a catalyst comprising a crystalline aluminosilicate zeolite, which zeolite is characterized by an activity, in terms of alpha value, of between about 2 and about 5000, a xylene sorption capacity greater than 1 gram/100 grams of zeolite and an ortho xylene sorption time for 30 percent of said capacity of greater than 10 minutes, said sorption capacity and sorption time being measured at 120° C. and a xylene pressure of 4.5 ± 0.8 mm. of mercury, said crystalline aluminosilicate zeolite further being characterized by a silica to alumina ratio of at least about 12, and a constraint index within the approximate range of 1 to 12, said catalyst having been subjected to steam treatment at a temperature between about 250° and about 1000° C. for a period of between about 0.5 and about 100 hours.
Claim 3
Dependent Claim
54 words
The process of claim 1 wherein said conversion conditions include a temperature between about 250° and about 600° C., a pressure between about 0.1 and about 100 atmospheres utilizing a feed weight hourly space velocity between about 0.1 and about 100 and a molar feed ratio of toluene/ethylene between about 1 and about 10.
Claim 4
Dependent Claim
34 words
The process of claim 1 wherein the catalyst is subjected to steam treatment at a temperature between about 400° and about 700° C. for a period of between about 1 and about 24 hours.
Claim 5
Dependent Claim
11 words
The process of claim 1 wherein said crystalline aluminosilicate is ZSM-5.
Claim 6
Dependent Claim
22 words
The process of claim 1 wherein the steamed catalyst has deposited thereon between about 2 and about 75 weight percent of coke.
Claim 7
Dependent Claim
16 words
The process of claim 1 wherein said crystalline aluminosilicate zeolite is admixed with a binder therefor.
Claim 8
Dependent Claim
14 words
The process of claim 4 wherein said ZSM-5 is admixed with a binder therefor.
Claim 9
Dependent Claim
24 words
The process of claim 1 wherein the crystal size of the crystalline aluminosilicate zeolite is within the approximate range of 0.01 to 0.10 micron.
Claim 10
Dependent Claim
20 words
The process of claim 1 wherein the crystal size of the crystalline aluminosilicate zeolite is greater than about 1 micron.
Claim 11
Dependent Claim
24 words
The process of claim 1 wherein the crystal size of the crystalline aluminosilicate zeolite is within the approximate range of 1 to 40 microns.
Claim 12
Dependent Claim
19 words
The process of claim 1 wherein the crystal size of the crystalline aluminosilicate zeolite is 1 to 6 microns.
Claim 13
Dependent Claim
12 words
The process of claim 1 wherein said mono alkyl benzene is toluene.
Claim 14
Dependent Claim
12 words
The process of claim 1 wherein said mono alkyl benzene is ethylbenzene.
Claim 15
Dependent Claim
142 words
A process for the ethylation of a mono alkyl benzene wherein the alkyl substituent contains 1 or 2 carbon atoms to selectively produce the para and meta derivatives of said mono alkyl benzene to the substantial exclusion of the ortho derivative thereof which comprises contacting said mono alkyl benzene, under conversion conditions, with ethylene in the presence of a catalyst comprising a crystalline aluminosilicate zeolite characterized by a silica to alumina ratio of at least about 12, a constraint index within the approximate range of 1 to 12 and an alkali metal content of less than about 1.5 weight percent, said catalyst having been treated, prior to use, with an atmosphere containing from about 5 to about 100 percent steam at a temperature of from about 250° to about 1000° C for a period of between about 0.5 and about 100 hours.
Claim 16
Dependent Claim
142 words
A process for the ethylation of a mono alkyl benzene wherein the alkyl substituent contains 1 or 2 carbon atoms to selectively produce the para and meta derivatives of said mono alkyl benzene to the substantial exclusion of the ortho derivative thereof which comprises contacting said mono alkyl benzene, under conversion conditions, with ethylene in the presence of a catalyst comprising a crystalline aluminosilicate zeolite characterized by a silica to alumina ratio of at least about 12, a constraint index within the approximate range of 1 to 12 and an alkali metal content of less than about 1.5 weight percent, said catalyst having been treated, prior to use, with an atmosphere containing from about 5 to about 100 percent steam at a temperature of from about 250° to about 1000° C for a period of between about 0.5 and about 100 hours.
Claim 17
Dependent Claim
54 words
The process of claim 14 wherein said conversion conditions include a temperature between about 250° and about 600° C, a pressure between about 0.1 and about 100 atmospheres utilizing a feed weight hourly space velocity between about 0.1 and about 100 and a molar feed ratio of toluene/ethylene between about 1 and about 10.
Claim 18
Dependent Claim
34 words
The process of claim 14 wherein the catalyst is subjected to steam treatment at a temperature between about 400° and about 700° C for a period of between about 1 and about 24 hours.
Claim 19
Dependent Claim
11 words
The process of claim 14 wherein said crystalline aluminosilicate is ZSM-5.
Claim 20
Dependent Claim
20 words
The process of claim 14 wherein the crystal size of the crystalline aluminosilicate zeolite is greater than about 1 micron.
Claim 21
Dependent Claim
12 words
The process of claim 14 wherein said mono alkyl benzene is toluene.
Claim 22
Dependent Claim
12 words
The process of claim 14 wherein said mono alkyl benzene is ethylbenzene.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-06-12 | 1981-12-12 | 1982-06-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-06-12 | 1985-12-12 | 1986-06-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-06-12 | 1989-12-12 | 1990-06-13 | $7700.00 | Window Closed / Lapsed |