US4064036A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Pressure testing of catalyst loaded reactors
Assignee: Union Oil Company of California
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Filing: 1976-10-14
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Granted: 1977-12-20
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Expires: 1996-10-14
Abstract
Abstract In the pressure testing of catalyst-loaded reactors with nitrogen gas at elevated temperatures, it is found that certain types of zeolite catalysts are substantially degraded in activity. The catalysts concerned comprises a Group VIII noble metal in an oxidized state, dispersed on a crystalline hydrogen zeolite, e.g., Y zeolite. It has now been discovered however that if such catalysts are first prereduced with a dilute, non-combustible mixture of nitrogen and hydrogen, damage on subsequent pressure testing with nitrogen is prevented or drastically reduced. Following pressure testing, the catalyst is activated by dehydration in a stream of hydrogen at elevated temperatures and pressures.
Inventors
- 👤 Danford E. Clark
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 08:31
CPC Classifications
C; C10; C10G; C10G49/00; C10G49/24
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
136 words
In the startup of a hydrocarbon conversion process employing high-pressure hydrogen, wherein said process is carried out in a pressure-retaining system including a ferrous reactor initially charged with a catalyst comprising a Group VIII noble metal in an oxidized state supported on an at least partially hydrated crystalline aluminosilicate zeolite, the improved method for pressure-testing said system and activating said catalyst which comprises: 1. reducing said catalyst in said reactor by contacting the same with a sufficient amount of a non-combustible reducing gas comprising a mixture of nitrogen and hydrogen to provide at least one mole of hydrogen per mole of noble metal in said catalyst, at least the initial portion of said contacting being carried out at between about 50° and 300° F, said contacting being terminated prior to complete dehydration of said catalyst; 2.
Claim 2
Dependent Claim
136 words
In the startup of a hydrocarbon conversion process employing high-pressure hydrogen, wherein said process is carried out in a pressure-retaining system including a ferrous reactor initially charged with a catalyst comprising a Group VIII noble metal in an oxidized state supported on an at least partially hydrated crystalline aluminosilicate zeolite, the improved method for pressure-testing said system and activating said catalyst which comprises: 1. reducing said catalyst in said reactor by contacting the same with a sufficient amount of a non-combustible reducing gas comprising a mixture of nitrogen and hydrogen to provide at least one mole of hydrogen per mole of noble metal in said catalyst, at least the initial portion of said contacting being carried out at between about 50° and 300° F, said contacting being terminated prior to complete dehydration of said catalyst; 2.
Claim 3
Dependent Claim
116 words
pressuring said system and catalyst with a non-combustible gas made up primarily of nitrogen to a static pressure above about 700 psig and above the contemplated operating pressure of said conversion process, and maintaining said static pressure at a temperature above about 200° F for a sufficient time to detect gas leakage from the system; and then 3. contacting said catalyst with a stream of substantially dry hydrogen-rich gas containing at least about 50 volume-percent hydrogen at a pressure above about 800 psig, a flow rate of at least about 100 GHSV and at temperatures gradually increasing to a maximum of at least about 450° F over a period of at least about 3 hours, thereby
Claim 4
Dependent Claim
116 words
pressuring said system and catalyst with a non-combustible gas made up primarily of nitrogen to a static pressure above about 700 psig and above the contemplated operating pressure of said conversion process, and maintaining said static pressure at a temperature above about 200° F for a sufficient time to detect gas leakage from the system; and then 3. contacting said catalyst with a stream of substantially dry hydrogen-rich gas containing at least about 50 volume-percent hydrogen at a pressure above about 800 psig, a flow rate of at least about 100 GHSV and at temperatures gradually increasing to a maximum of at least about 450° F over a period of at least about 3 hours, thereby
Claim 5
Dependent Claim
26 words
substantially dehydrating and activating said catalyst. 2. A method as defined in claim 1 wherein said noble metal is palladium and said zeolite is Y zeolite.
Claim 6
Dependent Claim
34 words
A method as defined in claim 2 wherein said Y zeolite is a steam stabilized hydrogen Y zeolite wherein less than about 25% of its original ion exchange capacity is satisfied by metal cations.
Claim 7
Dependent Claim
19 words
A method as defined in claim 1 wherein said reducing gas comprises about 0.1 - 5 vol. % hydrogen.
Claim 8
Dependent Claim
28 words
A method as defined in claim 1 wherein at least the initial portion of said reduction in step (1) is carried out at temperatures below about 200° F.
Claim 9
Dependent Claim
29 words
A method as defined in claim 1 wherein step (2) is carried out at a pressure between about 1200 and 2500 psig and a temperature above about 300° F.
Claim 10
Dependent Claim
19 words
A method as defined in claim 6 wherein said noble metal is palladium and said zeolite is Y zeolite.
Claim 11
Dependent Claim
34 words
A method as defined in claim 7 wherein said Y zeolite is a steam stabilized hydrogen Y zeolite wherein less than about 25% of its original ion exchange capacity is satisfied by metal cations.
Claim 12
Dependent Claim
28 words
A method as defined in claim 8 wherein at least the initial portion of said reduction in step (1) is carried out at temperatures below about 200° F.
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) | 1980-12-19 | 1981-06-20 | 1981-12-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-12-19 | 1985-06-20 | 1985-12-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-12-19 | 1989-06-20 | 1989-12-20 | $7700.00 | Window Closed / Lapsed |