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公开(公告)号:US11187465B2
公开(公告)日:2021-11-30
申请号:US16073118
申请日:2017-01-27
Applicant: ARCHIMEDE S.R.L.
Inventor: Alberto Brucato , Giuseppe Caputo , Gianluca Tumminelli , Gaetano Tuzzolino , Calogero Gattuso , Roberto Rizzo
Abstract: A heat exchanger (1; 1*; 100) includes a bundle of tubes (8), each extending in a respective elongation direction (X1) and defining a flow path for a working fluid that extends in the elongation direction, wherein each tube (8) of the bundle of tubes can be supplied with a working fluid; a matrix (6) of thermally conductive material that houses the tubes (8) of the bundle and that is configured, in use, for promoting heat exchange between working fluids that run through corresponding tubes (8) of the bundle; and a shell (4) made of thermally insulating material arranged around the matrix (6), wherein: the matrix (6) is made up of a plurality of sections (10; 10*) arranged aligned in the elongation direction (X1) and alternated by thermal interruptions (12) that extending transversely to the elongation direction (X1).
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公开(公告)号:US20240343984A1
公开(公告)日:2024-10-17
申请号:US18682150
申请日:2022-08-04
Applicant: Archimede S.r.l.
Inventor: Gianluca TUMMINELLI , Gaetano TUZZOLINO , Fabio SANTORO , Francesco DE PATRIZIO , Eleonora Maria FLORIA , Claudio SCARANTINO
IPC: C10J3/62 , C01B3/34 , C10G2/00 , C10G45/00 , C10J3/78 , C10K1/00 , C10K3/04 , C10K3/06 , C10L3/08 , C10L3/12
CPC classification number: C10J3/62 , C01B3/34 , C10G2/32 , C10G45/00 , C10J3/78 , C10K1/003 , C10K3/04 , C10K3/06 , C10L3/08 , C10L3/12 , C01B2203/0233 , C01B2203/025 , C01B2203/061 , C01B2203/062 , C01B2203/065 , C01B2203/1258 , C10G2300/42 , C10G2400/04 , C10J2300/0906 , C10J2300/0916 , C10J2300/0959 , C10J2300/0973 , C10J2300/0979 , C10J2300/1662 , C10J2300/1684 , C10J2300/169 , C10J2300/1807 , C10J2300/1846
Abstract: A method for the conversion of organic waste and/or biological waste into combustible products includes: feeding a first flow having organic waste and/or biological waste: performing a pyrolysis of the first flow to obtain one or more liquid pyrolysis products, one or more gaseous pyrolysis products, and one or more solid pyrolysis products; mixing the one or more solid pyrolysis products with a first aqueous flow, and subjecting the mixture to oxidation to obtain oxidation products; taking a first gaseous flow from the oxidation products; subjecting the one or more gaseous pyrolysis products to reforming, thereby obtaining one or more reforming products, taking a second gaseous flow from the reforming products, and subjecting the first gaseous flow and the second gaseous flow to catalytic hydrogenation, to obtain at least one first combustible.
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公开(公告)号:US10086346B2
公开(公告)日:2018-10-02
申请号:US15565336
申请日:2016-04-11
Applicant: Archimede S.r.l.
Inventor: Alberto Brucato , Giuseppe Caputo , Franco Grisafi , Francesca Scargiali , Gianluca Tumminelli , Gaetano Tuzzolino , Roberto D'Agostino , Roberto Rizzo
IPC: B01J3/00 , C10J3/78 , C02F11/00 , A61L11/00 , B09B3/00 , C02F11/08 , C10J3/00 , B01D19/00 , B01J19/00 , C10J3/86 , F28D1/02 , C02F101/20 , C02F101/30 , C02F101/32 , C02F103/00 , C02F103/06 , C02F103/10 , C02F103/24 , C02F103/28 , C02F101/10
Abstract: A plant for the disposal of wastes includes a supercritical water oxidation reactor, a supercritical water gasification reactor, and a feeding system configured for feeding at least two organic currents of wastes to the supercritical water oxidation reactor and supercritical water gasification reactor and configured for feeding at least one aqueous flow within said plant. The feeding system is configured for feeding the at least one aqueous current with a series flow through the supercritical water oxidation reactor and supercritical water gasification reactor. The feeding system is configured for feeding the at least two organic currents of wastes with a parallel flow through the supercritical water oxidation reactor and supercritical water gasification reactor and so as to selectively feed each of the organic currents of wastes to the supercritical water oxidation reactor or to the supercritical water gasification reactor.
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公开(公告)号:US20180117561A1
公开(公告)日:2018-05-03
申请号:US15565336
申请日:2016-04-11
Applicant: Archimede S.r.l.
Inventor: Alberto BRUCATO , Giuseppe CAPUTO , Franco GRISAFI , Francesca SCARGIALI , Gianluca TUMMINELLI , Gaetano TUZZOLINO , Roberto D'AGOSTINO , Roberto RIZZO
IPC: B01J19/00 , B01J3/00 , B01D19/00 , C02F11/08 , C10J3/78 , C10J3/86 , F28D1/02 , B09B3/00 , A61L11/00
CPC classification number: B01J3/008 , A61L11/00 , B01D19/0073 , B01J19/0053 , B09B3/00 , C02F11/086 , C02F2101/101 , C02F2101/20 , C02F2101/301 , C02F2101/306 , C02F2101/32 , C02F2103/002 , C02F2103/008 , C02F2103/06 , C02F2103/10 , C02F2103/24 , C02F2103/28 , C02F2303/10 , C10J3/00 , C10J3/78 , C10J3/86 , C10J2300/0979 , F28D1/0226 , Y02W10/30
Abstract: A plant for the disposal of wastes includes a supercritical water oxidation reactor, a supercritical water gasification reactor, and a feeding system configured for feeding at least two organic currents of wastes to the supercritical water oxidation reactor and supercritical water gasification reactor and configured for feeding at least one aqueous flow within said plant. The feeding system is configured for feeding the at least one aqueous current with a series flow through the supercritical water oxidation reactor and supercritical water gasification reactor. The feeding system is configured for feeding the at least two organic currents of wastes with a parallel flow through the supercritical water oxidation reactor and supercritical water gasification reactor and so as to selectively feed each of the organic currents of wastes to the supercritical water oxidation reactor or to the supercritical water gasification reactor.
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公开(公告)号:US20190039036A1
公开(公告)日:2019-02-07
申请号:US16073919
申请日:2017-01-27
Applicant: ARCHIMEDE S.R.L.
Inventor: ALBERTO BRUCATO , GIUSEPPE CAPUTO , FRANCO GRISAFI , FRANCESCA SCARGIALI , GIANLUCA MINELLI , GAETANO TUZZOLINO , CALOGERO GATTUSO , ROBERTO RIZZO , MARIALAURA ALESSI , FABIO SANTORO
Abstract: Described herein is a reactor (1) includes: a first reaction volume (V1), a second reaction volume (V2), wherein: the first reaction volume (V1) is in fluid communication with an inlet port for an oxidizer agent (OX_IN), an inlet port for at least one first reactant (R1_IN) and an outlet port for at least one reaction product (P1_OUT), said second reaction volume (V2) is in fluid communication with an inlet port for at least one second reactant (R2_IN), an outlet port for at least one second reaction product (P2_OUT) and is furthermore in thermal exchange relationship with said first reaction volume (V1), wherein, during operation, in said first reaction volume (V1) an oxidation reaction occurs between said at least one first reactant and said oxidizer agent with the formation of said at least one first reaction product, and in said second reaction volume (V2) a gasification reaction occurs of said second reactant with the contribution of a thermal energy flow exchanged between the first and the second reaction volumes (V1, V2) with formation of said at least one second reaction product.
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公开(公告)号:US11266962B2
公开(公告)日:2022-03-08
申请号:US16073919
申请日:2017-01-27
Applicant: ARCHIMEDE S.R.L.
Inventor: Alberto Brucato , Giuseppe Caputo , Franco Grisafi , Francesca Scargiali , Gianluca Minelli , Gaetano Tuzzolino , Calogero Gattuso , Roberto Rizzo , Marialaura Alessi , Fabio Santoro
Abstract: Described herein is a reactor (1) includes: a first reaction volume (V1), a second reaction volume (V2), wherein: the first reaction volume (V1) is in fluid communication with an inlet port for an oxidizer agent (OX_IN), an inlet port for at least one first reactant (R1_IN) and an outlet port for at least one reaction product (P1_OUT), said second reaction volume (V2) is in fluid communication with an inlet port for at least one second reactant (R2_IN), an outlet port for at least one second reaction product (P2_OUT) and is furthermore in thermal exchange relationship with said first reaction volume (V1), wherein, during operation, in said first reaction volume (V1) an oxidation reaction occurs between said at least one first reactant and said oxidizer agent with the formation of said at least one first reaction product, and in said second reaction volume (V2) a gasification reaction occurs of said second reactant with the contribution of a thermal energy flow exchanged between the first and the second reaction volumes (V1, V2) with formation of said at least one second reaction product.
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公开(公告)号:US20190041136A1
公开(公告)日:2019-02-07
申请号:US16073118
申请日:2017-01-27
Applicant: ARCHIMEDE S.R.L.
Inventor: ALBERTO BRUCATO , GIUSEPPE CAPUTO , GIANLUCA TUMMINELLI , GAETANO TUZZOLINO , CALOGERO GATTUSO , ROBERTO RIZZO
Abstract: A heat exchanger (1; 1*; 100) includes a bundle of tubes (8), each extending in a respective elongation direction (X1) and defining a flow path for a working fluid that extends in the elongation direction, wherein each tube (8) of the bundle of tubes can be supplied with a working fluid; a matrix (6) of thermally conductive material that houses the tubes (8) of the bundle and that is configured, in use, for promoting heat exchange between working fluids that run through corresponding tubes (8) of the bundle; and a shell (4) made of thermally insulating material arranged around the matrix (6), wherein: the matrix (6) is made up of a plurality of sections (10; 10*) arranged aligned in the elongation direction (X1) and alternated by thermal interruptions (12) that extending transversely to the elongation direction (X1).
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