US4001144A
Expired / Lapsed
US
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Process for modifying the pore volume distribution of alumina base catalyst supports
Assignee: CIT Group Business Credit Inc
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Filing: 1975-12-19
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Granted: 1977-01-04
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Expires: 1995-12-19
Abstract
Abstract Modification of the pore volume distribution of an alumina base catalyst support is accomplished by treating an alumina precursor of chi-rho-eta structure with an aqueous ammonium carbonate or bicarbonate solution under pressure at about 100 DEG -160 DEG C for 10-24 hours, followed by drying and thermal activation at a temperature of at least about 500 DEG C. The resulting support will possess more than about 70% of its total pore volume in the 45-300 angstrom unit pore diameter range. This pore volume distribution renders it particularly suitable for use as a catalyst carrier for hydrodesulfurization purposes.
Inventors
- 👤 Michael J. Pearson
- 👤 Ronald J. Rigge
- 👤 Stephen C. Carniglia
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 14:50
CPC Classifications
B; B01; B01J; B01J21/00; B01J21/02; B01J21/04; B01J35/00; B01J35/60; B01J37/00; B01J37/0009; B01J37/0018; C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08; B01J35/61; B01J35/615; B01J35/63; B01J35/635; B01J35/64; B01J35/647; B01J35/66; B01J35/67
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
160 words
A process for modifying the pore volume distribution of an alumina base catalyst support precursor which comprises the steps of: a. treating an alumina precursor of chi-rho-eta structure with an aqueous solution of an ammonium salt selected from the group consisting essentially of ammonium carbonate, ammonium bicarbonate and mixtures thereof; b. subjecting the treated alumina to a pressure treatment at a temperature in the range of about 100° and 160° C for a time period of about 10 hours to 24 hours; c. drying of the pressure-treated alumina at a temperature in excess of about 100° and up to about 200° C for about 1-24 hours followed by thermal activation at a temperature of at least about 500° and not in excess of about 700° C; and d. recovering an eta-free, alumina base catalyst support of modified pore volume distribution characterized by having at least about 70% of its total pore volume in the 45-300 angstrom unit pore diameter range.
Claim 2
Dependent Claim
160 words
A process for modifying the pore volume distribution of an alumina base catalyst support precursor which comprises the steps of: a. treating an alumina precursor of chi-rho-eta structure with an aqueous solution of an ammonium salt selected from the group consisting essentially of ammonium carbonate, ammonium bicarbonate and mixtures thereof; b. subjecting the treated alumina to a pressure treatment at a temperature in the range of about 100° and 160° C for a time period of about 10 hours to 24 hours; c. drying of the pressure-treated alumina at a temperature in excess of about 100° and up to about 200° C for about 1-24 hours followed by thermal activation at a temperature of at least about 500° and not in excess of about 700° C; and d. recovering an eta-free, alumina base catalyst support of modified pore volume distribution characterized by having at least about 70% of its total pore volume in the 45-300 angstrom unit pore diameter range.
Claim 3
Dependent Claim
20 words
Process according to claim 1 wherein the treatment with the aqueous ammonium salt and the pressure treatment are accomplished simultaneously.
Claim 4
Dependent Claim
12 words
Process according to claim 1, wherein the ammonium salt is ammonium carbonate.
Claim 5
Dependent Claim
12 words
Process according to claim 1, wherein the ammonium salt is a bicarbonate.
Claim 6
Dependent Claim
198 words
A process for modifying the pore volume distribution of an alumina base catalyst support precursor which comprises the steps of: a. admixing an alumina base precursor of chi-rho-eta structure with a cellulose followed by preparing agglomerates from the admixture; b. calcining the admixture in the range of about 400° and 700° C to combust substantially all of the cellulosic material; c. treating the calcined agglomerates with an aqueous solution of an ammonium salt selected from the group consisting essentially of ammonium carbonate, ammonium bicarbonate and mixtures thereof; d. subjecting the treated agglomerates to a pressure treatment at a temperature in the range of about 100° and 160° C for a time period of about 10 hours to about 24 hours; e. drying of the pressure-treated agglomerates at a temperature in excess of about 100° and up to about 200° C for about 1-24 hours followed by thermal activation at a temperature of at least about 500° and not in excess of about 700° C; and f. recovering an eta-free alumina base catalyst support of modified pore volume distribution characterized by having at least about 70% of its total pore volume in the 45-300 angstrom unit pore diameter range.
Claim 7
Dependent Claim
198 words
A process for modifying the pore volume distribution of an alumina base catalyst support precursor which comprises the steps of: a. admixing an alumina base precursor of chi-rho-eta structure with a cellulose followed by preparing agglomerates from the admixture; b. calcining the admixture in the range of about 400° and 700° C to combust substantially all of the cellulosic material; c. treating the calcined agglomerates with an aqueous solution of an ammonium salt selected from the group consisting essentially of ammonium carbonate, ammonium bicarbonate and mixtures thereof; d. subjecting the treated agglomerates to a pressure treatment at a temperature in the range of about 100° and 160° C for a time period of about 10 hours to about 24 hours; e. drying of the pressure-treated agglomerates at a temperature in excess of about 100° and up to about 200° C for about 1-24 hours followed by thermal activation at a temperature of at least about 500° and not in excess of about 700° C; and f. recovering an eta-free alumina base catalyst support of modified pore volume distribution characterized by having at least about 70% of its total pore volume in the 45-300 angstrom unit pore diameter range.
Claim 8
Dependent Claim
19 words
Process of claim 5, wherein the treatment with the aqueous ammonium salt and the pressure treatment are accomplished simultaneously.
Claim 9
Dependent Claim
12 words
Process according to claim 5, wherein the ammonium salt is ammonium carbonate.
Claim 10
Dependent Claim
12 words
Process according to claim 5, wherein the ammonium salt is ammonium bicarbonate.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-01-04 | 1980-07-05 | 1981-01-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-01-04 | 1984-07-05 | 1985-01-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-01-04 | 1988-07-05 | 1989-01-04 | $7700.00 | Window Closed / Lapsed |