Patent US4374092A successfully refreshed from Google Patents.
US4374092A
Expired / Lapsed
US
⏱️ 0.0 years remaining
System for electrically heating and regenerating spent activated carbon
Assignee: Individual
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Filing: 1981-07-09
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Granted: 1983-02-15
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Expires: 2001-07-09
Abstract
Abstract A system and method of reactivating wet spent activated carbon comprising a batch operated solid-liquid separator, a continuous feed electrically heated furnace and surge bin therebetween. Heat exchangers recover sensible heat of the exhaust gases and/or hot carbon leaving the furnace to heat the air used by the solid-liquid separator. A portion of the furnace exhaust along with added air is recirculated through the furnace to provide the appropriate atmosphere for regeneration of the carbon.
Inventors
- 👤 Gerald E. Marquess
- 👤 David J. Nell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 19:23
CPC Classifications
F; F26; F26B; F26B20/00; C; C01; C01B; C01B32/00; C01B32/30; C01B32/39; F26B3/00; F26B3/32; F26B3/34; F26B3/343; Y; Y02; Y02P; Y02P70/00; Y02P70/10
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
196 words
A system for reactivating a spent activated carbon material and the like comprising solid-liquid separator, a surge bin for receiving the output of the separator, a continuous feed electrically heated furnace for receiving material from the surge bin, said solid-liquid separator comprising means for passing fluids and retaining solid materials, means for gating the material to said surge bin, said surge bin arranged to receive the output of said solid-liquid separator and to continuously feed it to the electrically heated furnace, said electrically heated furnace being an elongate column with baffles therein for channeling the flow of carbon material centrally of the column through which the material flows, electrical resistance heating elements outside the flow of carbon material and positioned near the walls and inside of the furnace for radiation and convection heating of said material, controllable means for discharging materials at the bottom of the furnace, said furnace having an exhaust outlet near its upper end and a treatment gas inlet near its lower end, whereby the amount of energy required for reactivation of the spent activated carbon material is reduced and the amount of loss due to abrasion and excessive oxidation is also reduced.
Claim 2
Independent Claim
196 words
A system for reactivating a spent activated carbon material and the like comprising solid-liquid separator, a surge bin for receiving the output of the separator, a continuous feed electrically heated furnace for receiving material from the surge bin, said solid-liquid separator comprising means for passing fluids and retaining solid materials, means for gating the material to said surge bin, said surge bin arranged to receive the output of said solid-liquid separator and to continuously feed it to the electrically heated furnace, said electrically heated furnace being an elongate column with baffles therein for channeling the flow of carbon material centrally of the column through which the material flows, electrical resistance heating elements outside the flow of carbon material and positioned near the walls and inside of the furnace for radiation and convection heating of said material, controllable means for discharging materials at the bottom of the furnace, said furnace having an exhaust outlet near its upper end and a treatment gas inlet near its lower end, whereby the amount of energy required for reactivation of the spent activated carbon material is reduced and the amount of loss due to abrasion and excessive oxidation is also reduced.
Claim 3
Independent Claim
276 words
A system for reactivating a spent activated carbon material and the like comprising a batch operated solid-liquid separator, a surge bin for receiving the intermittent output of the separator, a continuous feed electrically heated furnace for receiving material from the surge bin, a heat exchanger and a recirculation system, said solid-liquid separator comprising means for passing fluids and retaining solid materials, and means for blowing air through the material accumulated on said retaining means to drive water from the material, means for gating the material to said surge bin, said surge bin arranged to receive the intermittent output of said solid-liquid separator and to continuously feed it to the electrically heated furnace, said electrically heated furnace being an elongate column with baffles therein for channeling the flow of carbon material centrally of the column through which the material flows, electrical resistance heating elements outside the flow of carbon material and positioned near the walls and inside of the furnace for radiation and convection heating of said material, controllable means for discharging materials at the bottom of the furnace, said furnace having an exhaust outlet near its upper end and a treatment gas inlet near its lower end, said heat exchanger for transferring sensible heat from the exhaust from the electrical furnace to the air being supplied to the solid-liquid separator, said recirculation system for mixing a portion of the exhaust gases with air and introducing the mixture at the lower end of the electrically heated furnace whereby the amount of energy required for reactivation of the spent activated carbon material is reduced and the amount of loss due to abrasion and excessive oxidation is also reduced.
Claim 4
Independent Claim
276 words
A system for reactivating a spent activated carbon material and the like comprising a batch operated solid-liquid separator, a surge bin for receiving the intermittent output of the separator, a continuous feed electrically heated furnace for receiving material from the surge bin, a heat exchanger and a recirculation system, said solid-liquid separator comprising means for passing fluids and retaining solid materials, and means for blowing air through the material accumulated on said retaining means to drive water from the material, means for gating the material to said surge bin, said surge bin arranged to receive the intermittent output of said solid-liquid separator and to continuously feed it to the electrically heated furnace, said electrically heated furnace being an elongate column with baffles therein for channeling the flow of carbon material centrally of the column through which the material flows, electrical resistance heating elements outside the flow of carbon material and positioned near the walls and inside of the furnace for radiation and convection heating of said material, controllable means for discharging materials at the bottom of the furnace, said furnace having an exhaust outlet near its upper end and a treatment gas inlet near its lower end, said heat exchanger for transferring sensible heat from the exhaust from the electrical furnace to the air being supplied to the solid-liquid separator, said recirculation system for mixing a portion of the exhaust gases with air and introducing the mixture at the lower end of the electrically heated furnace whereby the amount of energy required for reactivation of the spent activated carbon material is reduced and the amount of loss due to abrasion and excessive oxidation is also reduced.
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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) | 1986-02-14 | 1986-08-16 | 1987-02-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-02-14 | 1990-08-16 | 1991-02-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-02-14 | 1994-08-16 | 1995-02-15 | $7700.00 | Window Closed / Lapsed |