US4338187A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Solids feeding device and system
Assignee: Stone and Webster Engineering Corp
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Filing: 1979-10-22
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Granted: 1982-07-06
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Expires: 1999-10-22
Abstract
Abstract An apparatus and process for delivering fluidization gas to a bed of particulate solids to selectively locally fluidize the solids above a delivery conduit in communication with a reaction chamber. Also an apparatus and process for intimately mixing hydrocarbon feed with the particulate solids at the end of the delivery conduit in the reaction chamber.
Inventors
- 👤 Robert J. Gartside
- 👤 Herman N. Woebcke
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 19:28
CPC Classifications
C; C10; C10G; C10G9/00; C10G9/28; C10G9/32; B; B01; B01J; B01J8/00; B01J8/0015; B01J8/003; C10G2400/00; C10G2400/20
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
101 words
A process for continually feeding particulate solids to a reaction chamber comprising the steps of: a. providing a bed of solids in a non-fluidized state; b. delivering aeration gas under pressure to a localized section of the bed of solids immediately above a conduit extending from the bed of solids to a reaction zone, said aeration gas having a flow rate less than a rate necessary for incipient fluidization of the bed of solids such that only the solids proximate to said conduit are fluidized; and c. passing the fluidized solids downwardly by gravity through the conduit to the reaction chamber.
Claim 2
Dependent Claim
101 words
A process for continually feeding particulate solids to a reaction chamber comprising the steps of: a. providing a bed of solids in a non-fluidized state; b. delivering aeration gas under pressure to a localized section of the bed of solids immediately above a conduit extending from the bed of solids to a reaction zone, said aeration gas having a flow rate less than a rate necessary for incipient fluidization of the bed of solids such that only the solids proximate to said conduit are fluidized; and c. passing the fluidized solids downwardly by gravity through the conduit to the reaction chamber.
Claim 3
Dependent Claim
42 words
A process as in claim 1 wherein the solids bed has a bed height of about 10 feet, a bed density of about 43 pounds per cu. ft. and wherein the aeration gas is delivered at the rate of about 47.2 ACFM.
Claim 4
Dependent Claim
61 words
A process as in claim 1 wherein solids are rapidly and intimately admixed with a fluid feed in the reaction chamber comprising the further step of: introducing said fluid feed into the downwardly flowing solids at the outlet end of said conduit in the reaction chamber from an orifice located peripherally around the opening of the conduit facing the reaction chamber.
Claim 5
Dependent Claim
30 words
A process as recited in claim 3 further comprising the step of delivering the fluid feed into the downwardly flowing solids from an orifice located peripherally around the reaction chamber.
Claim 6
Dependent Claim
35 words
A process as in claim 4 further comprising a step of delivering a second flow of fluid feed at an angle to the downwardly flowing solids, from a location peripherally around the first fluid feed.
Claim 7
Dependent Claim
22 words
A process as recited in claim 3 wherein the fluid feed is a hydrocarbon to be thermally cracked in the reaction chamber.
References Cited (Backward Citations)
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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) | 1985-07-05 | 1986-01-04 | 1986-07-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-07-05 | 1990-01-04 | 1990-07-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-07-05 | 1994-01-04 | 1994-07-06 | $7700.00 | Window Closed / Lapsed |