US4541345A
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US
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Apparatus for recovering energy from pyrolyzable, carbonaceous waste materials of varying composition
Assignee: C DEILMANN AG A WEST-GERMAN CORP
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Filing: 1984-03-20
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Granted: 1985-09-17
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Expires: 2004-03-20
Abstract
Abstract An apparatus for recovering energy from pyrolyzable, carbonaceous waste materials, for example household refuse, comprising a rotary tube reactor (4) adapted to be charged with the waste materials and producing, as products, a (low temperature) carbonization gas and a pyrolytic coke at a reaction temperature of above 200° C.; a fluidized bed or swirling layer gasifier adapted to be supplied with an oxygen-containing gasifying agent, the pyrolytic coke and, optionally, waste materials and from which exit a hot gas having a temperature of between 400° and 1000° C. and an inert ash. Further, the system includes cleaning stages (8, 20) for the carbonization gas, connected subsequent to the rotary tube reactor and the gasifier (14), and further a combustion device (24) for the cleaned gases, as a part of a boiler system.
Inventors
- 👤 Heinrich Grumpelt
- 👤 Johannes Jaroch
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 14:10
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/58; C10J3/60; C10J3/64; C10J3/66; C10J3/46; C10J3/48; C10J3/52; C10J3/523; C10J3/54; C10G; C10G2300/00; C10G2300/10; C10G2300/1003; C10J2300/00; C10J2300/09; C10J2300/0913; C10J2300/0916; C10J2300/092; C10J2300/0946; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/0973; C10J2300/0976; C10J2300/12; C10J2300/1253; C10J2300/18; C10J2300/1861; C10J2300/1869; C10J2300/1884; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/129
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
163 words
Apparatus for recovering energy from pyrolyzable, carbonaceous waste materials of varying composition, comprising: at least one rotary tube reactor having means to receive the waste materials and means for producing as products, a low temperature carbonization gas and a pyrolytic coke at a reaction temperature of above 200° C., said reactor further including means to discharge said carbonization gas and means to discharge said coke; means to clean the carbonization gas, said means being connected subsequent to the rotary tube reactor; combustion means to combust the cleaned carbonization gas exiting from said cleaning means; a fluidized bed or swirling layer gasifier which has supplied thereto an oxygen-containing gasifying agent, the pyrolytic coke, and, optionally, waste materials, and from which exit a hot gas, having a temperature of between 400° and 1000° to be used for combustion in said combustion means, and an inert ash; and a separate cleaning or purification stage for the hot gas from the fluidized bed or swirling layer gasifier.
Claim 2
Dependent Claim
163 words
Apparatus for recovering energy from pyrolyzable, carbonaceous waste materials of varying composition, comprising: at least one rotary tube reactor having means to receive the waste materials and means for producing as products, a low temperature carbonization gas and a pyrolytic coke at a reaction temperature of above 200° C., said reactor further including means to discharge said carbonization gas and means to discharge said coke; means to clean the carbonization gas, said means being connected subsequent to the rotary tube reactor; combustion means to combust the cleaned carbonization gas exiting from said cleaning means; a fluidized bed or swirling layer gasifier which has supplied thereto an oxygen-containing gasifying agent, the pyrolytic coke, and, optionally, waste materials, and from which exit a hot gas, having a temperature of between 400° and 1000° to be used for combustion in said combustion means, and an inert ash; and a separate cleaning or purification stage for the hot gas from the fluidized bed or swirling layer gasifier.
Claim 3
Dependent Claim
26 words
The apparatus according to claim 1 further comprising gas conduits from the cleaning means and purification stage to carry the carbonization gas and hot gas respectively.
Claim 4
Dependent Claim
23 words
The apparatus according to claim 2, wherein the fluidized bed or swirling layer gasifier is adapted for use without employing a secondary medium.
Claim 5
Dependent Claim
17 words
The apparatus according to claim 1, wherein one or both cleaning or purification stages are solids-gas separators.
Claim 6
Dependent Claim
26 words
The apparatus according to claim 4 further comprisng gas conduits from the cleaning means and purification stage to carry the carbonization gas and hot gas respectively.
Claim 7
Dependent Claim
38 words
The apparatus according to claim 2, wherein one or both of the gas conduits carrying the carbonization gas or the hot gas, include heating means so as to maintain the temperature of the respective gas above 200° C.
Claim 8
Dependent Claim
18 words
The apparatus according to claim 2, wherein the gas conduits are joined together into a mixed gas conduit.
Claim 9
Dependent Claim
27 words
The apparatus according to claim 3, wherein the respective gas conduits for the carbonization gas or the hot gas are joined together into a mixed gas conduit.
Claim 10
Dependent Claim
27 words
The apparatus according to claim 5, wherein the respective gas conduits for the carbonization gas or the hot gas are joined together into a mixed gas conduit.
Claim 11
Dependent Claim
27 words
The apparatus according to claim 6, wherein the gas conduits for the carbonization gas or the hot gas, respectively, are joined together into a mixed gas conduit.
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) | 1988-09-16 | 1989-03-18 | 1989-09-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-09-16 | 1993-03-18 | 1993-09-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-09-16 | 1997-03-18 | 1997-09-17 | $7700.00 | Window Closed / Lapsed |