US4451184A
Expired / Lapsed
US
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Apparatus and method for feeding pulverized hydrocarbonaceous solids into a high pressure reactor
Assignee: Chevron USA Inc
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Filing: 1981-06-12
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Granted: 1984-05-29
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Expires: 2001-06-12
Abstract
Abstract The instant disclosure relates to the feeding of pulverized hydrocarbonaceous solids, such as coal, coke, tar sands, oil shale, etc., into a high pressure reactor for retorting or gasification of the solids. The pulverized hydrocarbonaceous solids are mixed with a motive fluid and pressurized in a jet ejector. The pulverized solid/motive fluid mixture is then separated by a cyclone separator. The operation may be repeated in successive stages to achieve the desired pressures. The pressurized solids from the cyclone separator are introduced into the reactor, and motive fluid from the separator is recirculated to the jet ejector.
Inventors
- 👤 David S. Mitchell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:23
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/46; C10J3/48; C10J3/485; C10J3/50; C10J3/503; C10J3/506; C10J3/72; C10J3/78; C21; C21B; C21B5/00; C21B5/001; C21B5/003; C10J2200/00; C10J2200/15; C10J2200/152; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/093; C10J2300/0943; C10J2300/0946; C10J2300/0953; C10J2300/0973; C10J2300/0976; C10J2300/0983; C10J2300/0993; Y; Y10; Y10S; Y10S48/00; Y10S48/04
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
286 words
An apparatus for primary feeding of entrained particulate materials into a high pressure section of a fluidized bed reactor, comprising: a first pressurization stage including: a first venturi tube; means for supplying the particulate material through an entry port of the first venturi tube; a first motive gas nozzle in the entry port of the first venturi tube; means for supplying pressurized motive gas to the first nozzle, the motive gas being mixed with the particulate material in the first venturi tube to form a first pressurized particulate material/motive gas mixture; and a first centrifugal means for separating a predetermined amount of the motive gas from the particulate material/motive gas mixture; and a second pressurization stage, for receiving and further pressurizing the separated particulate material/motive gas mixture from the first centrifugal means, including: a second venturi tube; means for supplying the particulate material/motive gas mixture through an entry port of the second venturi tube; a second motive gas nozzle in the entry port of the second venturi tube; means for supplying pressurized motive gas to the second nozzle, the motive gas being mixed with the particulate material in the second venturi tube to form a second pressurized particulate material/motive gas mixture; and second centrifugal means for separating a predetermined amount of the motive gas from the second particulate material/motive gas mixture to be introduced into the high pressure section of the reactor; and means for recirculating the motive gas from the first and second centrifugal means to the first and second motive gas nozzles; whereby the pressure of the particulate material introduced into the reactor is raised 50- 150 psi by the feeding apparatus to a pressure greater than the pressure within the high pressure reactor.
Claim 2
Independent Claim
286 words
An apparatus for primary feeding of entrained particulate materials into a high pressure section of a fluidized bed reactor, comprising: a first pressurization stage including: a first venturi tube; means for supplying the particulate material through an entry port of the first venturi tube; a first motive gas nozzle in the entry port of the first venturi tube; means for supplying pressurized motive gas to the first nozzle, the motive gas being mixed with the particulate material in the first venturi tube to form a first pressurized particulate material/motive gas mixture; and a first centrifugal means for separating a predetermined amount of the motive gas from the particulate material/motive gas mixture; and a second pressurization stage, for receiving and further pressurizing the separated particulate material/motive gas mixture from the first centrifugal means, including: a second venturi tube; means for supplying the particulate material/motive gas mixture through an entry port of the second venturi tube; a second motive gas nozzle in the entry port of the second venturi tube; means for supplying pressurized motive gas to the second nozzle, the motive gas being mixed with the particulate material in the second venturi tube to form a second pressurized particulate material/motive gas mixture; and second centrifugal means for separating a predetermined amount of the motive gas from the second particulate material/motive gas mixture to be introduced into the high pressure section of the reactor; and means for recirculating the motive gas from the first and second centrifugal means to the first and second motive gas nozzles; whereby the pressure of the particulate material introduced into the reactor is raised 50- 150 psi by the feeding apparatus to a pressure greater than the pressure within the high pressure reactor.
Claim 3
Dependent Claim
42 words
The apparatus of claim 1 wherein the particulate material is pulverized coal 50 mesh or less in size; wherein the motive gas is steam and wherein the pulverized coal constitutes approximately 10% by volume of a coal/steam mixture formed in the venturi.
Claim 4
Dependent Claim
33 words
The apparatus of claim 2 wherein the ratio of the volumetric flow rate of the steam, Q R , to the volumetric flow rate of the pulverized coal, Q, is one or greater.
Claim 5
Dependent Claim
131 words
A process for feeding pulverized hydrocarbonaceous solids into a high pressure reactor comprising the steps of: (a) passing the pulverized hydrocarbonaceous solids through an entry port of a venturi tube having a motive fluid nozzle therein; (b) supplying pressurized motive fluid to the nozzle; (c) mixing the pressurized motive fluid and the pulverized hydrocarbonaceous solids in a constricted portion of the venturi tube; (d) centrifuging the pressurized motive fluid/pulverized solids mixture to at least partially separate the pressurized solids; (e) recirculating motive fluid separated from the pressurized motive fluid/pulverized solid mixture to the motive fluid nozzle; (f) repeating steps (a) through (e) on the separated, pressurized solids to increase the pressurization thereof; and (g) introducing the separated, pressurized solids into the high pressure reactor at a pressure greater than 50 psi.
Claim 6
Dependent Claim
131 words
A process for feeding pulverized hydrocarbonaceous solids into a high pressure reactor comprising the steps of: (a) passing the pulverized hydrocarbonaceous solids through an entry port of a venturi tube having a motive fluid nozzle therein; (b) supplying pressurized motive fluid to the nozzle; (c) mixing the pressurized motive fluid and the pulverized hydrocarbonaceous solids in a constricted portion of the venturi tube; (d) centrifuging the pressurized motive fluid/pulverized solids mixture to at least partially separate the pressurized solids; (e) recirculating motive fluid separated from the pressurized motive fluid/pulverized solid mixture to the motive fluid nozzle; (f) repeating steps (a) through (e) on the separated, pressurized solids to increase the pressurization thereof; and (g) introducing the separated, pressurized solids into the high pressure reactor at a pressure greater than 50 psi.
Claim 7
Independent Claim
230 words
An apparatus having at least two pressurization stages for feeding entrained particulate material into a high pressure reactor, said apparatus comprising: a first pressurization stage itself comprising: a first venturi tube; means for supplying the particulate material through an entry port of the first venturi tube; a first motive gas nozzle in the entry port of the venturi tube, through which a pressurized motive gas passes, which motive gas is mixed with the particulate material in the first venturi tube to form a pressurized particulate material/motive gas mixture; first centrifugal means for separating a predetermined amount of the motive gas from the particulate material/motive gas mixture; and first means for recirculating the motive fluid separated by the first centrifugal means to the first motive gas nozzle; and a second pressurizing stage, comprising: a second venturi tube to which the output mixture from the first centrifugal means is supplied; a second motive gas nozzle in the entry port of the venturi tube, through which a pressurized motive gas passes, which motive gas is mixed in the second venturi tube with the output mixture of the first centrifugal means; second centrifugal means for separating a predetermined amount of the motive gas from the particulate material/motive gas mixture produced in the second venturi; and second means for recirculating the motive fluid separated by the second centrifugal means to the second motive gas nozzle.
Claim 8
Independent Claim
230 words
An apparatus having at least two pressurization stages for feeding entrained particulate material into a high pressure reactor, said apparatus comprising: a first pressurization stage itself comprising: a first venturi tube; means for supplying the particulate material through an entry port of the first venturi tube; a first motive gas nozzle in the entry port of the venturi tube, through which a pressurized motive gas passes, which motive gas is mixed with the particulate material in the first venturi tube to form a pressurized particulate material/motive gas mixture; first centrifugal means for separating a predetermined amount of the motive gas from the particulate material/motive gas mixture; and first means for recirculating the motive fluid separated by the first centrifugal means to the first motive gas nozzle; and a second pressurizing stage, comprising: a second venturi tube to which the output mixture from the first centrifugal means is supplied; a second motive gas nozzle in the entry port of the venturi tube, through which a pressurized motive gas passes, which motive gas is mixed in the second venturi tube with the output mixture of the first centrifugal means; second centrifugal means for separating a predetermined amount of the motive gas from the particulate material/motive gas mixture produced in the second venturi; and second means for recirculating the motive fluid separated by the second centrifugal means to the second motive gas nozzle.
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) | 1987-05-29 | 1987-11-28 | 1988-05-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-05-29 | 1991-11-28 | 1992-05-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-05-29 | 1995-11-28 | 1996-05-29 | $7700.00 | Window Closed / Lapsed |