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.

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

IPC: B01J3/00 ,  B01J3/02 ,  C02F11/08 ,  B01J19/24

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.