US4276835A
Expired / Lapsed
US
⏱️ 0.0 years remaining
method for processing sewage sludge
Assignee: Von Roll AG
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Filing: 1979-10-04
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Granted: 1981-07-07
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Expires: 1999-10-04
Abstract
Abstract A method for drying sludge which may contain combustible vapors in a manner to positively prevent fires and explosions within the sludge dryer and the associated sludge-drying piping. The method provides for a substantial reduction of the oxygen content of the sludge-drying vapors by deviating a part of the sludge-drying vapor stream from the principal vapor circuit and passing it as secondary combustion air into the combustion chamber which generates hot gases for drying the sludge. Furthermore, a portion of the hot effluents from the combustion chamber is deviated from the sludge-drying circuit and is used to heat the sludge-drying vapors whereafter it is vented to the atmosphere. In a variant of the invention, an acid scrubber is provided to remove hydrochloric acid. A number of embodiments is presented.
Inventors
- 👤 Erich Zeltner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 05:14
CPC Classifications
F; F23; F23G; F23G7/00; F23G7/001; C; C02; C02F; C02F11/00; C02F11/12; C02F11/13; F26; F26B; F26B23/00; F26B23/001; F26B23/002; F26B23/02; F26B23/022; Y; Y02; Y02E; Y02E50/00; Y02E50/30; Y02P; Y02P70/00; Y02P70/10
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
399 words
A method of self-energized drying of sewage sludge while leaving essentially dust-free and odor-free effluent from an apparatus having a combustion chamber (60, 60a) having a solid particle or powder burner (90); a mixing or pulverizing-type dryer (1) receiving the sludge, in which the sludge is dried; a solid-particle separator (2) for removing solid particles upon drying of the sludge; a blower (4) generating an air stream; a heat exchanger (5); said combustion chamber, dryer, solid-particle separator, blower, and heat exchanger being connected in a closed loop circuit; and a controlled bypass connection (P2) between the downstream side of the heat exchanger (5) and the dryer, bypassing the combustion chamber, said method comprising the steps of generating, by means of the blower (4), a stream of air in the closed circuit; introducing sludge material into the dryer (1) where the sludge is dried and at least partly converted into volatile combustible dust components and gaseous components to form a gas; removing solid dust particles from the mixture of the air in the air stream and volatile combustible components from the dried sludge in the separator (2) to obtain a powder of combustible dust; passing the remaining gas of the stream through the heat exchanger (5) and removing heat therefrom; conveying the powder of combustible dust as a fuel to the powder burner (90); introducing a portion (P1) of the gas received from the heat exchanger to the combustion chamber (60, 60a) to provide combustion air thereto; circulating the remaining portion (P2) of the gas received from the heat exchanger (5) to the dryer (1); removing from the combustion chamber (60, 60a) (a) ash and non-combustible residue after burning of the combustible dust by the burner in the presence of the first portion (P1) of gas from the heat exchanger and (b) hot combustion gases; re-introducing a portion of said hot combustion gases from the combustion chamber to the dryer (1); mixing the hot combustion gases received from the combustion chamber with the gas received from the heat exchanger to provide to the dryer and the sludge introduced thereto drying air at a temperature which is below the temperature of the combustion chamber and which has an oxygen content insufficient for spontaneous combustion of the sludge introduced into the dryer; and filtering the remaining portion of hot gases removed from the combustion chamber and then venting them to the atmosphere.
Claim 2
Independent Claim
399 words
A method of self-energized drying of sewage sludge while leaving essentially dust-free and odor-free effluent from an apparatus having a combustion chamber (60, 60a) having a solid particle or powder burner (90); a mixing or pulverizing-type dryer (1) receiving the sludge, in which the sludge is dried; a solid-particle separator (2) for removing solid particles upon drying of the sludge; a blower (4) generating an air stream; a heat exchanger (5); said combustion chamber, dryer, solid-particle separator, blower, and heat exchanger being connected in a closed loop circuit; and a controlled bypass connection (P2) between the downstream side of the heat exchanger (5) and the dryer, bypassing the combustion chamber, said method comprising the steps of generating, by means of the blower (4), a stream of air in the closed circuit; introducing sludge material into the dryer (1) where the sludge is dried and at least partly converted into volatile combustible dust components and gaseous components to form a gas; removing solid dust particles from the mixture of the air in the air stream and volatile combustible components from the dried sludge in the separator (2) to obtain a powder of combustible dust; passing the remaining gas of the stream through the heat exchanger (5) and removing heat therefrom; conveying the powder of combustible dust as a fuel to the powder burner (90); introducing a portion (P1) of the gas received from the heat exchanger to the combustion chamber (60, 60a) to provide combustion air thereto; circulating the remaining portion (P2) of the gas received from the heat exchanger (5) to the dryer (1); removing from the combustion chamber (60, 60a) (a) ash and non-combustible residue after burning of the combustible dust by the burner in the presence of the first portion (P1) of gas from the heat exchanger and (b) hot combustion gases; re-introducing a portion of said hot combustion gases from the combustion chamber to the dryer (1); mixing the hot combustion gases received from the combustion chamber with the gas received from the heat exchanger to provide to the dryer and the sludge introduced thereto drying air at a temperature which is below the temperature of the combustion chamber and which has an oxygen content insufficient for spontaneous combustion of the sludge introduced into the dryer; and filtering the remaining portion of hot gases removed from the combustion chamber and then venting them to the atmosphere.
Claim 3
Dependent Claim
40 words
Method according to claim 1, including the step of generating an air flow to transport the powder of combustible dust to the powder burner (90) to thereby effect said step of conveying the dust from the separator to the burner.
Claim 4
Dependent Claim
18 words
Method according to claim 2, including the step of preheating the transport air in the heat exchanger (5).
Claim 5
Dependent Claim
46 words
Method according to claim 1, including the step of removing heat from the circumference of the combustion chamber whereby the combustion chamber will operate as an additional heat exchanger or boiler by circulation a fluid in heat exchange relation to the contents of the combustion chamber.
Claim 6
Dependent Claim
89 words
Method according to claim 1, further comprising the step of maintaining a constant volume of sludge vapors or gaseous components in the closed-loop vapor circuit (C) including the steps of monitoring the temperature in the closed circuit between the dryer (1) and the solid-particle separator (2); controlling the volume of sludge admitted to the grinding dryer as a function of said temperature; sensing the temperature in the combustion chamber (60, 60a); and controlling the rate of admission of combustible components into said chamber as a function of said temperature.
Claim 7
Dependent Claim
48 words
Method according to claim 5, wherein the step of controlling the admission of combustible components to the combustion chamber includes the step of controlling the admission of powder of combustible dust being conveyed to said powder burner (90) as a function of the temperature within the combustion chamber.
Claim 8
Dependent Claim
51 words
Method according to claim 1, wherein the step of mixing the hot combustion gases received from the combustion chamber (60, 60a) and the gases received from the heat exchanger comprises mixing said gases to establish, within the dryer, an atmosphere having an oxygen content of between about 5 to 7% maximum.
Claim 9
Dependent Claim
52 words
Method according to claim 1, wherein the step of mixing the hot combustion gases received from the combustion chamber (60, 60a) and the gases received from the heat exchanger comprises mixing said gases to establish, within the dryer, an atmosphere having a temperature in the order of between 800° to 900° C.
Claim 10
Dependent Claim
52 words
Method according to claim 7, wherein the step of mixing the hot combustion gases received from the combustion chamber (60, 60a) and the gases received from the heat exchanger comprises mixing said gases to establish, within the dryer, an atmosphere having a temperature in the order of between 800° to 900° C.
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) | 1984-07-06 | 1985-01-05 | 1985-07-07 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-07-06 | 1989-01-05 | 1989-07-07 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-07-06 | 1993-01-05 | 1993-07-07 | $7700.00 | Window Closed / Lapsed |