Patent US4259294A successfully refreshed from Google Patents.
US4259294A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Apparatus for the hydrogenation of heavy hydrocarbon oils
Assignee: Shell USA Inc
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Filing: 1979-08-30
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Granted: 1981-03-31
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Expires: 1999-08-30
Abstract
Abstract A hydroconversion process for heavy hydrocarbon oil and reactor system having a series of closed reactor vessels containing substantially fixed catalyst beds in flow communication with each of one catalyst-supply conduit system and one catalyst-removal conduit system, both of said conduit systems communicating with each reactor in said series of reactor vessels, via separate valve means, whereby each reactor can be separately connected or disconnected to flow communication with each of said conduit systems and whereby process-deactivated catalyst present in each reactor is continuously or periodically replaced by fresh catalyst as a slurry in oil via said conduit systems.
Inventors
- 👤 Wouter C. Van Zijll Langhout
- 👤 Abraham A. Pegels
- 👤 Joannes B. Wijffels
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 19:49
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G65/00; C10G65/02; C10G65/04
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
291 words
An apparatus for catalytic treatment of hydrocarbons comprising: a plurality of closed reactors in series arrangement suitable for containing a substantially fixed bed of particulate catalyst, each said reactor having two inlets comprising a reactor inlet for admitting reactants to an upstream side of said catalyst bed and a catalyst inlet for admitting fresh catalyst; each said reactor having two outlets comprising a reaction effluent outlet for passing reaction effluent from each said reactor and a catalyst outlet for passing deactivated catalyst from each said reactor; a reactant source conduit means communicating with a source of reactants and with the inlet of each said reactor, a reaction effluent conduit means communicating with the outlet of each said reactor, for withdrawing reaction effluent therefrom, and ultimate withdrawing of reaction effluent from the apparatus; a plurality of reactant flow valve means disposed on each of said reactant source conduit means and said reaction effluent conduit means for isolating any of said reactors from flow of reactants through the remaining reactors serially; one catalyst supply conduit, communicating with a source of particulate catalyst as a slurry and with the catalyst inlet of each reactor for supplying fresh catalyst to each said reactor, and communication with a source of pressure for pressuring said catalyst supply conduit to substantially reactor pressure; one catalyst removal conduit, communicating with the catalyst outlet of each said reactor for removal of deactivated catalyst from said apparatus, and communicating with a source of pressure for pressuring said catalyst removal conduit to substantially reactor pressure, and a plurality of catalyst flow valve means disposed on each of said catalyst supply conduit and said catalyst removal conduit for isolating any of said reactors for removing deactivated catalyst therefrom and supplying fresh catalyst thereto.
Claim 2
Independent Claim
291 words
An apparatus for catalytic treatment of hydrocarbons comprising: a plurality of closed reactors in series arrangement suitable for containing a substantially fixed bed of particulate catalyst, each said reactor having two inlets comprising a reactor inlet for admitting reactants to an upstream side of said catalyst bed and a catalyst inlet for admitting fresh catalyst; each said reactor having two outlets comprising a reaction effluent outlet for passing reaction effluent from each said reactor and a catalyst outlet for passing deactivated catalyst from each said reactor; a reactant source conduit means communicating with a source of reactants and with the inlet of each said reactor, a reaction effluent conduit means communicating with the outlet of each said reactor, for withdrawing reaction effluent therefrom, and ultimate withdrawing of reaction effluent from the apparatus; a plurality of reactant flow valve means disposed on each of said reactant source conduit means and said reaction effluent conduit means for isolating any of said reactors from flow of reactants through the remaining reactors serially; one catalyst supply conduit, communicating with a source of particulate catalyst as a slurry and with the catalyst inlet of each reactor for supplying fresh catalyst to each said reactor, and communication with a source of pressure for pressuring said catalyst supply conduit to substantially reactor pressure; one catalyst removal conduit, communicating with the catalyst outlet of each said reactor for removal of deactivated catalyst from said apparatus, and communicating with a source of pressure for pressuring said catalyst removal conduit to substantially reactor pressure, and a plurality of catalyst flow valve means disposed on each of said catalyst supply conduit and said catalyst removal conduit for isolating any of said reactors for removing deactivated catalyst therefrom and supplying fresh catalyst thereto.
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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) | 1984-03-30 | 1984-09-29 | 1985-03-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-03-30 | 1988-09-29 | 1989-03-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-03-30 | 1992-09-29 | 1993-03-31 | $7700.00 | Window Closed / Lapsed |