Patent US3962128A successfully refreshed from Google Patents.
US3962128A
Expired / Lapsed
US
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Coal dust fuel distribution system and method of manufacturing activated carbon
Assignee: Westvaco Corp
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Filing: 1974-07-05
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Granted: 1976-06-08
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Expires: 1994-07-05
Abstract
Abstract Coal dust comprising coal particles of 40 mesh or less may be utilized as a fuel for stable combustion by aspirating the dust in fluidized suspension for delivery to a turbulent reservoir and aspirating the suspension from the reservoir for delivery to a combustion zone.
Inventors
- 👤 James D. Nelson
- 👤 Gert R. Winge
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 17:16
CPC Classifications
C; C10; C10B; C10B49/00; C10B49/02; C10B49/04; C10B23/00; C10L; C10L9/00; C10L9/02; C10L9/06; C21; C21B; C21B5/00; C21B5/001; C21B5/003
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
161 words
A method of manufacturing coal based activated carbon comprising the steps of: A. segregating coal dust particles of 40 mesh and less from a bulk coal supply; B. transporting coal particles larger than 40 mesh from said bulk supply through a multihearth activation furnace; C. aspirating said dust particles into a first fluidized mixture stream with a first air flow stream; D. delivering said first fluidized mixture stream to a mixing chamber; E. holding said dust particles in turbulent fluidized suspension within said mixing chamber; F. aspirating a second fluidized mixture stream from said mixing chamber to a combustion hearth of said multihearth activation furnace with a second air flow stream; G. conducting a third fluidized mixture stream from said mixing chamber to a particle reservoir; and H. controlling the relative flow rates of said first, second, and third fluidized mixture streams whereby the combined flow rates of said second and third mixture streams equal or exceed said first mixture stream.
Claim 2
Independent Claim
161 words
A method of manufacturing coal based activated carbon comprising the steps of: A. segregating coal dust particles of 40 mesh and less from a bulk coal supply; B. transporting coal particles larger than 40 mesh from said bulk supply through a multihearth activation furnace; C. aspirating said dust particles into a first fluidized mixture stream with a first air flow stream; D. delivering said first fluidized mixture stream to a mixing chamber; E. holding said dust particles in turbulent fluidized suspension within said mixing chamber; F. aspirating a second fluidized mixture stream from said mixing chamber to a combustion hearth of said multihearth activation furnace with a second air flow stream; G. conducting a third fluidized mixture stream from said mixing chamber to a particle reservoir; and H. controlling the relative flow rates of said first, second, and third fluidized mixture streams whereby the combined flow rates of said second and third mixture streams equal or exceed said first mixture stream.
Claim 3
Dependent Claim
39 words
A method as described by claim 1 wherein said coal particles of larger than 40 mesh are subjected to a precarbonization process step preceeding said multihearth activation furnace, said particle segregation step occurring before and after said precarbonization step.
Claim 4
Dependent Claim
204 words
In combination with a heat generating furnace, a fuel distribution system for delivering particulate coal dust to a combustion hearth of said furnace, said distribution system comprising: A. a bulk reservoir for said coal dust; B. a first aspirator having a chamber proximate of a low pressure induction zone of said first aspirator for receiving said coal dust from said reservoir; C. a first pressurized air supply source connected to said first aspirator for evacuating said coal dust from said chamber into a first fluidized flow stream; D. a mixing chamber having a first conduit connected therewith for receiving said first fluidized flow stream and holding a fluidized mixture of air and coal dust in turbulent suspension; E. a second aspirator having a receiving chamber and low pressure induction zone flow connected to said mixing chamber through a second conduit; F. a second pressurized air supply source connected to said second aspirator for evacuating said fluidized mixture from said second aspirator receiving chamber into a second fluidized flow stream for delivery to said furnace combustion hearth; and, G. a third conduit having flow control means therein connected to said mixing chamber for venting a select portion of fluidized mixture within said mixing chamber therefrom.
Claim 5
Dependent Claim
204 words
In combination with a heat generating furnace, a fuel distribution system for delivering particulate coal dust to a combustion hearth of said furnace, said distribution system comprising: A. a bulk reservoir for said coal dust; B. a first aspirator having a chamber proximate of a low pressure induction zone of said first aspirator for receiving said coal dust from said reservoir; C. a first pressurized air supply source connected to said first aspirator for evacuating said coal dust from said chamber into a first fluidized flow stream; D. a mixing chamber having a first conduit connected therewith for receiving said first fluidized flow stream and holding a fluidized mixture of air and coal dust in turbulent suspension; E. a second aspirator having a receiving chamber and low pressure induction zone flow connected to said mixing chamber through a second conduit; F. a second pressurized air supply source connected to said second aspirator for evacuating said fluidized mixture from said second aspirator receiving chamber into a second fluidized flow stream for delivery to said furnace combustion hearth; and, G. a third conduit having flow control means therein connected to said mixing chamber for venting a select portion of fluidized mixture within said mixing chamber therefrom.
Claim 6
Independent Claim
151 words
A method of firing a heat generating furnace combustion hearth with coal dust having a particle size of 40 mesh or less, said method comprising the steps of: A. providing a bulk reservoir for said coal dust; B. aspirating said dust from said reservoir into a first fluidized mixture stream with a first air flow stream; C. delivering said first fluidized mixture stream to a mixing chamber; D. holding said dust in turbulent fluidized suspension within said mixing chamber; E. aspirating a second fluidized mixture stream from said mixing chamber to a furnace combustion hearth with a second air flow stream; F. conducting a third fluidized mixture stream from said mixing chamber to a recirculation system; and G. controlling the relative flow rates of said first, second and third fluidized mixture streams whereby the combined flow rates of said second and third mixture streams equal or exceed said first mixture stream.
Claim 7
Independent Claim
151 words
A method of firing a heat generating furnace combustion hearth with coal dust having a particle size of 40 mesh or less, said method comprising the steps of: A. providing a bulk reservoir for said coal dust; B. aspirating said dust from said reservoir into a first fluidized mixture stream with a first air flow stream; C. delivering said first fluidized mixture stream to a mixing chamber; D. holding said dust in turbulent fluidized suspension within said mixing chamber; E. aspirating a second fluidized mixture stream from said mixing chamber to a furnace combustion hearth with a second air flow stream; F. conducting a third fluidized mixture stream from said mixing chamber to a recirculation system; and G. controlling the relative flow rates of said first, second and third fluidized mixture streams whereby the combined flow rates of said second and third mixture streams equal or exceed said first mixture stream.
References Cited (Backward Citations)
US327210A
Cited
US1042576A
Cited
FR784139A
Cited
GB546531A
Cited
US3033134A
Cited
US3204942A
Cited
US3843559A
Cited
US3876505A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-06-08 | 1979-12-08 | 1980-06-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-08 | 1983-12-08 | 1984-06-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-08 | 1987-12-08 | 1988-06-08 | $7700.00 | Window Closed / Lapsed |