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US4018671A Expired / Lapsed US ⏱️ 0.0 years remaining

Intermittent catalyst addition system

Assignee: Marathon Oil Co
•
Filing: 1975-01-14
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Granted: 1977-04-19
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Expires: 1995-01-14
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Abstract

Abstract Catalyst, e.g., for a fluid catalytic cracker, is added automatically by a system consisting of an addition hopper which is periodically fed by gravity from a storage hopper, sealed off from the supply, and then pressurized with air to discharge its contents to the carrier gas line feeding the hydrocarbon conversion unit, e.g., the regenerator section of a Fluid Catalytic Cracking Unit. Sequencing can be by electronic timer-solenoid (or pneumatic) valve system.

Inventors

  • 👤 Nicholaki A. Andon
  • 👤 Robert I. Fleece

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 22:05
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/0015; B01J8/0035; C; C10; C10G; C10G11/00; C10G11/14; C10G11/18; C10G11/187; B01J2208/00; B01J2208/00743; B01J2208/00752

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 264 words
In the catalytic conversion of feed materials by contacting said feed materials in a converter system with catalyst in a fluidized state, some of which catalyst is lost from said catalytic cracking process through reduced activity and/or entrainment in the effluent from said process, the improvement comprising: a. storing said catalyst in a storage tank maintained at a first internal pressure and having a conduit communicating through a storage valve with an addition hopper; b. maintaining said addition hopper at a pressure corresponding substantially to said first pressure of said storage tank by operation of a venting means and opening said storage valve to admit said catalyst to a predetermined level in said addition hopper, said addition hopper communicating through an addition valve to a carrier gas line leading to said converter; c. closing said venting means and pressurizing said addition hopper to a second addition pressure; d. thereafter opening said addition valve and permitting said addition hopper to empty into said carrier gas line; e. after emptying of said addition hopper, closing said addition valve, opening said venting means to reduce the pressure in said addition hopper to said first pressure, and opening said storage valve to admit additional catalyst to fill said addition hopper to a predetermined level determined by the volume of said addition hopper; f. thereafter closing said venting means, closing said storage valve and admitting additional gases to raise the pressure of said addition hopper to said addition pressure; g. thereafter opening said addition valve to admit additional catalyst to said carrier gas line and repeating the above cycle.
Claim 2
Dependent Claim 264 words
In the catalytic conversion of feed materials by contacting said feed materials in a converter system with catalyst in a fluidized state, some of which catalyst is lost from said catalytic cracking process through reduced activity and/or entrainment in the effluent from said process, the improvement comprising: a. storing said catalyst in a storage tank maintained at a first internal pressure and having a conduit communicating through a storage valve with an addition hopper; b. maintaining said addition hopper at a pressure corresponding substantially to said first pressure of said storage tank by operation of a venting means and opening said storage valve to admit said catalyst to a predetermined level in said addition hopper, said addition hopper communicating through an addition valve to a carrier gas line leading to said converter; c. closing said venting means and pressurizing said addition hopper to a second addition pressure; d. thereafter opening said addition valve and permitting said addition hopper to empty into said carrier gas line; e. after emptying of said addition hopper, closing said addition valve, opening said venting means to reduce the pressure in said addition hopper to said first pressure, and opening said storage valve to admit additional catalyst to fill said addition hopper to a predetermined level determined by the volume of said addition hopper; f. thereafter closing said venting means, closing said storage valve and admitting additional gases to raise the pressure of said addition hopper to said addition pressure; g. thereafter opening said addition valve to admit additional catalyst to said carrier gas line and repeating the above cycle.
Claim 3
Dependent Claim 21 words
A process according to claim 1 wherein the duration of opening of each of said valves is controlled by timing means.
Claim 4
Dependent Claim 21 words
A process according to claim 2 wherein the position of each of said valves is controlled by a sequencing control center.
Claim 5
Dependent Claim 59 words
A process according to claim 1 wherein said addition valve is closed substantially whenever said storage valve is open and wherein said storage valve is closed substantially whenever said addition valve is open, and wherein said venting means is open whenever said storage valve is open and wherein said storage valve is closed whenever said venting means is closed.
Claim 6
Dependent Claim 20 words
A process according to claim 4 wherein said venting means communicates with an upper portion of said catalyst storage tank.
Claim 7
Dependent Claim 18 words
A process according to claim 1 wherein said storage tank has a first pressure of approximately atmospheric pressure.

References Cited (Backward Citations)

US1535991A Cited
US2786800A Cited
US2892773A Cited
US3090593A Cited
US3156537A Cited
US3479093A Cited
US3850582A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-04-18 1980-10-18 1981-04-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-04-18 1984-10-18 1985-04-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-04-18 1988-10-18 1989-04-19 $7700.00 Window Closed / Lapsed

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