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US4583470A Expired / Lapsed US ⏱️ 0.0 years remaining

Ash disposer for system to recover resources from sludge

Assignee: NIPPON FURNACE KOGYO CO Ltd
•
Filing: 1985-01-07
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Granted: 1986-04-22
•
Expires: 2005-01-07
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Abstract

Abstract A system for recovering resources from sludge in which sludge containing water in the amount of 90 to 70 percent is first supplied to a sludge concentrator through a forced supply equipment where the sludge is concentrated to contain a water content of a maximum of about 60 percent; then is sent to a drying furnace having a fluidized sand bed. The product obtained in the drying furnace is separated to gas and solid. After the separated gas is pressurized by a fan and is heated by a heat exchanger through a circulator passage, a portion thereof is supplied to the drying furnace as gas for drying and the remainder is sent to the sludge concentrator. The water content is then removed from the concentrated gas and the gas obtained from the sludge concentrator is used in the system as gaseous fuel. Further, the separated solid is dried and distilled through a special gasifying apparatus to recover gaseous fuel, and in addition, the separated solid is fed into ash disposal equipment; the ash generated from the gasifying apparatus is also supplied to the ash disposal equipment to allow the ash to be melted and then to allow the ash to be solidified in the ash disposal equipment and to take out the solidified massive ashes; the exhaust gases from the gasifying apparatus and ash disposal equipment are supplied to the said heat exchanger.

Inventors

  • 👤 Yasuo Hirose

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 22:54
CPC Classifications
F; F23; F23G; F23G7/00; F23G7/001; C; C02; C02F; C02F11/00; C02F11/008; C02F11/10; C02F11/12; C02F11/13; C10; C10B; C10B53/00; Y; Y02; Y02W; Y02W10/00; Y02W10/40

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 86 words
Ash disposer for recovering resources from sludge comprising: a cyclone combustion chamber having a cylindrical inner circumferential wall, a solid sludge feeder connected to said cyclone combustion chamber, a primary air feed pipe supplying air tangentially along said inner circumferential wall, a throttled section below said combustion chamber and a water tank just below said throttled section, a flame tube connected to the side of said apparatus between said combustion chamber and said water tank, and a second stage combustion chamber downstream of said flame tube.
Claim 2
Dependent Claim 86 words
Ash disposer for recovering resources from sludge comprising: a cyclone combustion chamber having a cylindrical inner circumferential wall, a solid sludge feeder connected to said cyclone combustion chamber, a primary air feed pipe supplying air tangentially along said inner circumferential wall, a throttled section below said combustion chamber and a water tank just below said throttled section, a flame tube connected to the side of said apparatus between said combustion chamber and said water tank, and a second stage combustion chamber downstream of said flame tube.
Claim 3
Dependent Claim 96 words
Ash dispenser for recovering resources from sludge comprising: a cyclone combustion chamber having a cylindrical inner circumferential wall, a solid sludge feeder connected to said cyclone combustion chamber, a primary air feed pipe supplying air tangentially along said inner circumferential wall, a throttled section below said combustion chamber and a water tank just below said throttle section, a flame tube connected to the side of said apparatus between said combustion chamber and said water tank, and a second stage combustion chamber downstream of said flame tube, and ash supply means connected to said cyclone combustion chamber.
Claim 4
Dependent Claim 96 words
Ash dispenser for recovering resources from sludge comprising: a cyclone combustion chamber having a cylindrical inner circumferential wall, a solid sludge feeder connected to said cyclone combustion chamber, a primary air feed pipe supplying air tangentially along said inner circumferential wall, a throttled section below said combustion chamber and a water tank just below said throttle section, a flame tube connected to the side of said apparatus between said combustion chamber and said water tank, and a second stage combustion chamber downstream of said flame tube, and ash supply means connected to said cyclone combustion chamber.
Claim 5
Dependent Claim 20 words
The ash disposer apparatus of claim 1 further comprising secondary air feed means connected to said second stage combustion chamber.
Claim 6
Dependent Claim 23 words
The ash disposer apparatus of claim 1 further comprising said flame tube being connected midway between said combustion chamber and said water tank.
Claim 7
Independent Claim 63 words
A method for recovering the ash of sludge comprising: feeding dried sludge to a combustion zone, subjecting said dried sludge to cyclonic action in the presence of hot combustion gases, melting at least a portion of said sludge, permitting the melted sludge to flow in a downward direction, plunging the melted sludge with quenching means, solidifying said sludge into a finely divided form.
Claim 8
Independent Claim 63 words
A method for recovering the ash of sludge comprising: feeding dried sludge to a combustion zone, subjecting said dried sludge to cyclonic action in the presence of hot combustion gases, melting at least a portion of said sludge, permitting the melted sludge to flow in a downward direction, plunging the melted sludge with quenching means, solidifying said sludge into a finely divided form.
Claim 9
Dependent Claim 30 words
The method according to claim 5 further comprising subjecting the dried sludge to the action of a flame in the combustion zone at a temperature of at least 1200° C.
Claim 10
Dependent Claim 17 words
The method according to claim 5 further comprising subjecting the melted sludge to a quench in water.
Claim 11
Dependent Claim 15 words
The method according to claim 5 further comprising solidifying said sludge into pebble sized particles.

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) 1989-04-21 1989-10-21 1990-04-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-04-21 1993-10-21 1994-04-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-04-21 1997-10-21 1998-04-22 $7700.00 Window Closed / Lapsed

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