公开(公告)号：US20220372374A1

公开(公告)日：2022-11-24

申请号：US17764577

申请日：2020-09-29

Applicant: REOIL SP. Z O.O.

Inventor： Michal Mikuskiewicz ,  Pawel Mikuskiewicz ,  Sebastian Zygmunt ,  Bronislaw Rolnik

IPC: C10B53/07 ,  C10B47/44 ,  B01D53/78 ,  B01D53/48 ,  C10G1/10 ,  C10G1/00 ,  C01B32/324

Abstract: An installation for the production of oil, gas and char for carbon black, from elastomers, characterized in that, it has a screw dispenser (3) with a shaft (1), which from the loading side is closed hydraulically with a lock (2) by a nitrogen, a reactor (4), which is divided into zones A, B, C, corresponding to the subsequent stages of the pyrolysis process: zone A—the beginning of depolymerization (350° C.), zone B—carbonization (350-400° C.) and zone C—aromatic compounds cracking (400-650° C.), while a bubbler (5) hydraulically closed with a siphon (6) and a separator (7) with a hydraulic closure (8) and an oil separator (9) equipped with a transport screw (10) and an afterburner chamber (20) are installed outside the reactor (4), wherein the oil separator (9) is closed at the outlet by an accumulation shaft (12) and from the side of receiving a solid product—with a shaft (13), which is connected by an U-shaped screw conveyor (14) with economizers (11) and (15). wherein the installation is provided with a scrubber (16).

公开(公告)号：US11807813B2

公开(公告)日：2023-11-07

申请号：US17764577

申请日：2020-09-29

Applicant: REOIL SP. Z O.O.

Inventor： Michal Mikuskiewicz ,  Pawel Mikuskiewicz ,  Sebastian Zygmunt ,  Bronislaw Rolnik

IPC: C10B53/07 ,  C10B47/44 ,  C10G1/00 ,  C10G1/10 ,  C01B32/324 ,  B01D53/48 ,  B01D53/78

CPC classification number: C10B53/07 ,  B01D53/48 ,  B01D53/78 ,  C01B32/324 ,  C10B47/44 ,  C10G1/002 ,  C10G1/10 ,  C10G2300/1003

Abstract: An installation for the production of oil, gas and char for carbon black, from elastomers, characterized in that, it has a screw dispenser (3) with a shaft (1), which from the loading side is closed hydraulically with a lock (2) by a nitrogen, a reactor (4), which is divided into zones A, B, C, corresponding to the subsequent stages of the pyrolysis process: zone A—the beginning of depolymerization (350° C.), zone B—carbonization (350-400° C.) and zone C—aromatic compounds cracking (400-650° C.), while a bubbler (5) hydraulically closed with a siphon (6) and a separator (7) with a hydraulic closure (8) and an oil separator (9) equipped with a transport screw (10) and an afterburner chamber (20) are installed outside the reactor (4), wherein the oil separator (9) is closed at the outlet by an accumulation shaft (12) and from the side of receiving a solid product—with a shaft (13), which is connected by an U-shaped screw conveyor (14) with economizers (11) and (15). wherein the installation is provided with a scrubber (16).