公开(公告)号：US20240300838A1

公开(公告)日：2024-09-12

申请号：US18578225

申请日：2022-07-15

Applicant: Georgia Tech Research Corporation

Inventor： Shannon YEE ,  David HASLER ,  Roland LEHMANN ,  Christian SEILER ,  Christian FORRER ,  Christoph FARRÉR ,  Andreas STAUB ,  Marco CADUFF ,  Janine GLATTHARD ,  Mathias SCHLAURI ,  Adrian GEMPERLI ,  Florian FISCHER ,  Daniel RÜDISÜLI ,  Valdinei FRASSON

IPC: C02F11/123 ,  C02F1/00 ,  C02F103/00

CPC classification number: C02F11/123 ,  C02F1/00 ,  C02F2001/007 ,  C02F2103/005 ,  C02F2201/008

Abstract: System and method for buffer tank separation and homogenization are described. The system can include a belt separator (104), a liquids collection tank (106), a solids collection tank (108), and a homogenizer (110). The belt separator comprising a perforated belt looped between two rollers, the belt separator positioned to receive an input comprising at least one of: solids and liquids, the input received via the at least one inlet onto the belt of the belt separator, the belt separator configured to deliver a solids portion of the input to the solids collection tanks and to deliver the liquids portion of the input to the liquids collection tank; and a homogenizer connected to the solids outlet, the homogenizer configured to receive a collected solids portion output and form a uniform and homogenized slurry.

公开(公告)号：US20240308897A1

公开(公告)日：2024-09-19

申请号：US18578243

申请日：2022-07-15

Applicant: Georgia Tech Research Corporation

Inventor： Shannon YEE ,  David HASLER ,  Roland LEHMANN ,  Christian SEILER ,  Christian FORRER ,  Christoph FARRÉR ,  Andreas STAUB ,  Marco CADUFF ,  Janine GLATTHARD ,  Adrian GEMPRELI ,  Florian FISCHER ,  Daniel RÜDISÜLI ,  Valdinei FRASSON ,  Josef FISCHER ,  Tobias BLEIKER

IPC: C02F11/08 ,  C02F11/13 ,  C02F103/00

CPC classification number: C02F11/086 ,  C02F11/13 ,  C02F2103/005 ,  C02F2201/007 ,  C02F2301/066 ,  C02F2303/04

Abstract: System and method for micro-Super Critical Water Oxidation solids treatment of fecal waste are described. The system includes an injector vessel (112) and a reactor (114). The reactor can receive an injection of a slurry batch and an input of compressed air that is heated over time to a temperature at or above the critical point of water into the super critical fluid phase. A combined concentrator and phase separator (150)) can receive a treated output from the reactor and separate solid ash from liquid and gaseous effluent. A drying tunnel (170) can receive and dry the solid ash. The treatment process includes heating the slurry batch, within the reactor, to a temperature of at or above the critical point of water into the super critical fluid phase and maintaining the slurry batch a minimum temperature, within the reactor, for a predetermined treatment time to produce a treated output.