公开(公告)号：US11781081B1

公开(公告)日：2023-10-10

申请号：US17318533

申请日：2021-05-12

Applicant: Streamline Innovations, Inc.

Inventor： Peter J Photos ,  Franklin Hailey Brown, II ,  David Sisk ,  Benjamin Isaac Tyler ,  Michael A Pue

IPC: C10L3/10 ,  B01D19/00 ,  B01J19/00

CPC classification number: C10L3/103 ,  B01D19/0042 ,  B01D19/0063 ,  B01D19/0068 ,  B01J19/0053 ,  B01J2204/005 ,  B01J2219/00182 ,  B01J2219/00243 ,  B01J2219/185 ,  C10L2290/54

Abstract: An oxidation-reduction desulfurization system includes a reactor vessel with sour gas inlet at the bottom and a gas outlet at the top. A primary stage phase separator includes a vertically-oriented pipe with an inlet located inside the reactor vessel. The ratio of the reactor vessel diameter to the pipe inlet diameter is in a range of 2:1 to 5:1. Surface foam and non-gaseous multi-phase mixture including emulsion flow into a partially gas-filled upper section of the vertically-oriented pipe and freefall to a lower level, thereby facilitating mechanical breaking of the foam and the emulsion. A secondary stage phase separator connected to the gas outlet separates non-gaseous surge from sweet gas. Valves and a controller automatically maintain target levels of the non-gaseous multi-phase mixture and non-gaseous surge.

公开(公告)号：US11795409B1

公开(公告)日：2023-10-24

申请号：US17574823

申请日：2022-01-13

Applicant: STREAMLINE INNOVATIONS, INC.

Inventor： Peter J Photos ,  Franklin Hailey Brown, II ,  David Sisk ,  Benjamin Isaac Tyler ,  Michael A Pue

IPC: B01J19/00 ,  B01D19/00 ,  C10L3/10

CPC classification number: C10L3/103 ,  B01D19/0042 ,  B01D19/0063 ,  B01D19/0068 ,  B01J19/0053 ,  B01J2204/005 ,  B01J2219/00182 ,  B01J2219/00243 ,  B01J2219/185 ,  C10L2290/54

Abstract: An oxidation-reduction desulfurization system includes a reactor vessel with sour gas inlet at the bottom and a gas outlet at the top. A primary stage phase separator includes a vertically-oriented pipe with an inlet located inside the reactor vessel. The ratio of the reactor vessel diameter to the pipe inlet diameter is in a range of 2:1 to 5:1. Surface foam and non-gaseous multi-phase mixture including emulsion flow into a partially gas-filled upper section of the vertically-oriented pipe and freefall to a lower level, thereby facilitating mechanical breaking of the foam and the emulsion. A secondary stage phase separator connected to the gas outlet separates non-gaseous surge from sweet gas. Valves and a controller automatically maintain target levels of the non-gaseous multi-phase mixture and non-gaseous surge.