| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 41 | Apparatus for charging inclined chamber coke oven | US808774 | 1977-06-21 | US4151045A | 1979-04-24 | Dietrich Wagener |
| An inclined chamber of a coke oven is defined by a heating side wall, a coke removal side, a horizontal chamber ceiling and a chamber floor inclined downwardly from the heating side wall to the coke removal side. Briquettes are charged into the chamber, through charging holes in the heating side wall arranged vertically one above the other and through charging holes in the chamber ceiling arranged one behind the other, in separate inclined fill layers. The charging operation is through separate charging holes, in a sequence from the lowermost charging hole in the heating side wall to the uppermost charging hole therein, and then from the chamber ceiling charging hole closest to the heating side wall to the chamber ceiling charging hole furthest therefrom. The vertical and horizontal spacing between adjacent charging holes is dimensioned to avoid breakage of the briquettes. | ||||||
| 42 | Discharge apparatus for inclined coke ovens | US818928 | 1977-07-25 | US4145257A | 1979-03-20 | Heinz-Gunther Grewe; Horst Seeberg; Horst Fach; Friedrich Isermann |
| A device for automatically detaching and/or loosening coke within a coke oven chamber, particularly such a chamber of the type having an inclined or obliquely extending floor, includes a track support adapted to be mounted at a position confronting the coke removal opening of the coke oven chamber. An elongated poking bar is supported by the track support and has at a first end thereof a stoking or broaching head for abutting or scraping coke within the chamber. A trolley is mounted on the track support for movement therealong, and the poking bar is pivoted to the trolley. A reversibly operable cable drive moves the trolley and thus the poking bar along the track support from an initial position whereat the poking bar is positioned outside of the chamber to an operative position wherein the broaching head of the poking bar is inserted into the chamber to abut against coke therein. The poking bar is guided during the movement thereof to follow a predetermined displacement path such that the poking bar will avoid obstructions such as a quencher car located outside the coke oven chamber, such that the broaching head will be passed through the coke removal opening of the chamber even when the chamber door is only partially opened, and such that the broaching head will be positioned on the floor of the chamber. Movement of the poking bar thereafter will be guided by sliding contact of the broaching head on the floor, and possibly on the side walls, of the chamber. | ||||||
| 43 | Method and inclined chamber furnace for carbonizing fluent carbon-containing material | US822318 | 1977-08-05 | US4126518A | 1978-11-21 | Julio C. S. da Silva Bento |
| A method of, and apparatus for, coking or carbonizing fluent or flowable carbon-containing material, such as wood, peat, residues, wastes or the like, by means of gases in an inclined treatment chamber through which the material moves from the top towards the bottom under the influence of gravity while utilizing the flow action of the material while exceeding the natural angle of repose of the material. Gas is conducted from the bottom towards the top in countercurrent flow to the material through the treatment chamber. The gases, constituting a mixture of an infed dosed supply of air and distillation gas escaping out of the material in gaseous state into the hot gas mixture, are exclusively conducted upwardly in the treatment chamber over the material in direct contact therewith owing to the natural rise or lift and the heat needed for coking or carbonizing the material is exclusively produced in the treatment chamber by combustion of the distillation gas with the infed air. | ||||||
| 44 | Inclined rotary furnace | US3461037D | 1965-07-06 | US3461037A | 1969-08-12 | KNAPPSTEIN JOHANNES; THIERSCH FRIEDRICH |
| 45 | Inclined coking-retort oven | US59437522 | 1922-10-13 | US1606140A | 1926-11-09 | JOSEPH BECKER |
| 46 | Carbonizing furnace retort | US22641018 | 1918-04-03 | US1409597A | 1922-03-14 | HOWARD SMITH CHARLES |
| 47 | HORIZONTAL ROTATING DRUM RETORT | PCT/US2019/039941 | 2019-06-28 | WO2020006487A1 | 2020-01-02 | SWAIN, Lloyd W. |
A retort including a drum, an electric induction coil, a motor, and first and second jacks. The drum includes an inlet port at an inlet end, an outlet port at an outlet end, and a cylindrical tube extending between the inlet end and the outlet end. The electric induction coil is proximate the cylindrical tube for heating the cylindrical tube. The motor is operably and rotatably coupled to the cylindrical tube of the drum. The first jack is coupled to the drum proximate the inlet end, and is configured to raise and lower the inlet end of the drum. And the second jack is coupled to the drum proximate the outlet end, and is configured to raise and lower the outlet end of the drum. |
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| 48 | METHOD AND PLANT FOR DISPOSING OF WASTES COMPOSED OF PLASTIC MATERIALS AND BIOMASSES | PCT/IT2015/000015 | 2015-02-02 | WO2015125166A1 | 2015-08-27 | BENZI, Giuseppe |
The present invention deals with a method and a plant for disposing of solid wastes, composed of plastic materials and biomasses, and liquid wastes, particularly composed of spend vegetal oils and greases. The method provides a pyrolysis treatment of the solid and liquid wastes, from which a synthesis gas (syngas) and an inert residual are obtained. The pyrolysis plant comprises: a first section (100), which performs the pyrolysis of solid and liquid waste materials, the pyrolysis producing synthesis gas (syngas) and residual ashes; a second section (200) which performs the separation of a lighter fraction of ashes (pulverized coal or carbon black) from syngas, the lighter fraction being transported by the syngas; a third section (300), which performs the fractioned distillation of syngas, obtaining the separation of the volatile fraction of syngas from a bituminous residual (tar); a fourth section (400), which performs the recycle of the bituminous residual of the fractioned distillation, for a further treatment. |
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| 49 | FURNACE FOR PYROLYSIS | US17915089 | 2021-03-31 | US20230151277A1 | 2023-05-18 | Rory HUGHES |
| A rotary furnace (1) for pyrolyzing a feedstock, the furnace (1) comprises a rotating vessel (12) having an upstream end (12A) with an inlet (16) for receiving feedstock and a downstream end (12B) with an outlet (17A, 17B) for egress of pyrolysis products, and a gas extraction pipe (13) extending within and along the rotating vessel (12) from the downstream end (12B), the gas extraction pipe (13) having an opening (18) upstream of the downstream end (12B) to accept gaseous components generated in use. | ||||||
| 50 | PROCESS AND SYSTEM FOR WHOLE TYRES AND PLASTIC COMPOSITES PYROLYSIS TO FUEL CONVERSION AND COMPOUND RECOVERY | US14423531 | 2013-07-12 | US20150184079A1 | 2015-07-02 | Frank Riedewald |
| Disclosed is a process for treating waste plastic materials such as whole tyres, coarsely cut tyres, large plastic pieces, plastic composites such as hoses or combinations of above into gases, liquids and solids by direct heating in a pyrolysis liquid (1) such as molten salt or molten metal. The pyrolysis system is constructed such that the segregation of the light and heavy materials occurs within the pyrolysis chamber. The carbon black is segregated from the pyrolysis vapours via a cyclone and fractions of carbon black may be obtained by installing a number of cyclones in series so that different qualities of carbon black may be produced. Diesel or other oils, steel, carbon black, ZnO and synthesis gas are recovered; all of which can be feed streams to other processes. This process avoids the inefficient procedure of cutting the tyres or other plastic composites into small pieces before treatment by pyrolysis and also recovers valuable components. | ||||||
| 51 | Process and apparatus for charging inclined chamber coke oven | US751707 | 1976-12-17 | US4133719A | 1979-01-09 | Dietrich Wagener |
| An inclined chamber of a coke oven is defined by a heating side wall, a coke removal side, a horizontal chamber ceiling and a chamber floor inclined downwardly from the heating side wall to the coke removal side. Briquettes are charged into the chamber, through charging holes in the heating side wall arranged vertically one above the other and through charging holes in the chamber ceiling arranged one behind the other, in separate inclined fill layers. The charging operation is through separate charging holes, in a sequence from the lowermost charging hole in the heating side wall to the uppermost charging hole therein, and then from the chamber ceiling charging hole closest to the heating side wall to the chamber ceiling charging hole furthest therefrom. The vertical and horizontal spacing between adjacent charging holes is dimensioned to avoid breakage of the briquettes. | ||||||
| 52 | Inclined chamber coke oven | US751711 | 1976-12-17 | US4070251A | 1978-01-24 | Kurt Prange; Friedrich Isermann; Ernst Hasenacker; Manfred Blase |
| An inclined chamber has vertical heating flues on each side thereof. The floors of the heating flues are vertically staggered in an inclined manner. Pairs of heating flues are joined at the tops thereof by guide openings which are vertically staggered in an inclined manner. Central and upper air inlet openings extend into the heating flues and are vertically staggered in an inclined manner. | ||||||
| 53 | Methods and apparatus for the continuous treatment of non-caking coal and other discrete materials | US3470068D | 1966-10-12 | US3470068A | 1969-09-30 | KEMMERER JOHN L JR; BUSCHOW EDWARD G |
| 54 | Gas retort | US49736321 | 1921-08-31 | US1663847A | 1928-03-27 | HEINRICH KOPPERS |
| 55 | METHOD AND PLANT FOR DISPOSING OF WASTES COMPOSED OF PLASTIC MATERIALS AND BIOMASSES | EP15714666.3 | 2015-02-02 | EP3107979B1 | 2018-03-28 | Benzi, Giuseppe |
| The present invention deals with a method and a plant for disposing of solid wastes, composed of plastic materials and biomasses, and liquid wastes, particularly composed of spend vegetal oils and greases. The method provides a pyrolysis treatment of the solid and liquid wastes, from which a synthesis gas (syngas) and an inert residual are obtained. The pyrolysis plant comprises: a first section (100), which performs the pyrolysis of solid and liquid waste materials, the pyrolysis producing synthesis gas (syngas) and residual ashes; a second section (200) which performs the separation of a lighter fraction of ashes (pulverized coal or carbon black) from syngas, the lighter fraction being transported by the syngas; a third section (300), which performs the fractioned distillation of syngas, obtaining the separation of the volatile fraction of syngas from a bituminous residual (tar); a fourth section (400), which performs the recycle of the bituminous residual of the fractioned distillation, for a further treatment. | ||||||
| 56 | METHOD AND PLANT FOR DISPOSING OF WASTES COMPOSED OF PLASTIC MATERIALS AND BIOMASSES | EP15714666.3 | 2015-02-02 | EP3107979A1 | 2016-12-28 | Benzi, Giuseppe |
| The present invention deals with a method and a plant for disposing of solid wastes, composed of plastic materials and biomasses, and liquid wastes, particularly composed of spend vegetal oils and greases. The method provides a pyrolysis treatment of the solid and liquid wastes, from which a synthesis gas (syngas) and an inert residual are obtained. The pyrolysis plant comprises: a first section (100), which performs the pyrolysis of solid and liquid waste materials, the pyrolysis producing synthesis gas (syngas) and residual ashes; a second section (200) which performs the separation of a lighter fraction of ashes (pulverized coal or carbon black) from syngas, the lighter fraction being transported by the syngas; a third section (300), which performs the fractioned distillation of syngas, obtaining the separation of the volatile fraction of syngas from a bituminous residual (tar); a fourth section (400), which performs the recycle of the bituminous residual of the fractioned distillation, for a further treatment. | ||||||
| 57 | CONTINUOUS COKING REFINERY METHODS AND APPARATUS | EP00980646.4 | 2000-11-21 | EP1246888A1 | 2002-10-09 | BRECHER, Lee, E.; JOHNSON, Lyle, A.; SEITHI, Vijay, K. |
| A system for refining hydrocarbon containing materials in a continuous coking mode may provide a pyrolyzer (1) which may be inclined to effect a liquid seal between a liquid conduction environment (6) and a gaseous conduction environment (7). A heat source (9) may heat the material past the coking point and the system may include a screw or auger (10) which can continuously remove the coke while simultaneously outputting refined products. | ||||||
| 58 | GASIFICATION APPARATUS | EP18799866.1 | 2018-10-26 | EP3720929B1 | 2023-08-30 | BELLOLI, Stefano |
| 59 | FURNACE FOR PYROLYSIS | EP21717175.0 | 2021-03-31 | EP4127099A1 | 2023-02-08 | HUGHES, Rory |
| 60 | GASIFICATION APPARATUS | PCT/IB2018/058358 | 2018-10-26 | WO2019111073A1 | 2019-06-13 | BELLOLI, Stefano |
The present invention concerns a gasification apparatus (1) for the separation of an inert material from mixtures comprising said material and one or more polymeric/organic materials, said apparatus (1) comprising: a) a casing body (2), which extends in a tubular manner along a longitudinal axis (L) between a proximal portion (2') and a distal portion (2"); b) a treatment body (4), contained at least in part in the casing body (2) and which delimits a primary chamber (6) to gasify - in the absence of oxygen - the polymeric/organic material in synthetic gas; the treatment body (4) being rotatable around an axis of rotation (Rl) and comprising first auger means (8) protruding into the primary chamber (6) to move a first mixture and the inert material in the distal direction (S1); c) a burner (10), arranged close to the casing body (2), in thermal contact with the primary chamber (6); d) a flame propagation body (12), which extends distally from the burner (10), inside the treatment body (4) to isolate the flame from the primary chamber (6); e) conveyance means, fluidically connected to draw (S2) the synthesis gas from the primary chamber (6) and to feed the burner flame (10) with said gas. |
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