High temperature dry desulfurization system and method using multi regeneration reactor

Patent metadata

Field	Value
Publication number	US-10046968-B2
Application number	US-201615232987-A
Country	US
Kind code	B2
Filing date	Aug 10, 2016
Priority date	Aug 11, 2015
Publication date	Aug 14, 2018
Grant date	Aug 14, 2018

Abstract

A desulfurization system removes sulfur ingredients included in synthetic gas generated from gasification of coal in a high temperature dry state. The system includes a desulfurization reactor, a desulfurization cyclone, and first and second regeneration reactors branched with the desulfurization cyclone. A first oxidizing agent is injected to a first oxidizing agent inlet of the first regeneration reactor, and a second oxidizing agent is injected to a second oxidizing agent inlet of the second regeneration reactor. A controller operates one of the first and second regeneration reactors in a regeneration mode, controlling the other to operate in a desulfurization mode.

First claim

What is claimed is:

1. A desulfurization system for removing sulfur included in a synthetic gas in a high temperature dry state, comprising:
a desulfurization reactor for removing sulfur from the synthetic gas using a desulfurizing agent;
a desulfurization cyclone for separating the synthetic gas and the desulfurizing agent discharged from the desulfurization reactor;
a first regeneration reactor to be coupled to the desulfurization cyclone for regenerating the desulfurizing agent;
a second regeneration reactor to be coupled to the desulfurization cyclone for regenerating the desulfurizing agent;
a first oxidizing agent supply for injecting oxidizing agent into the first regeneration reactor, and a second oxidizing agent supply for injecting oxidizing agent into the second regeneration reactor;
a first inlet valve coupled between the desulfurization cyclone and a first inlet of the first regeneration reactor, a first outlet valve at a first outlet of the first regeneration reactor, a second inlet valve coupled between the desulfurization cyclone and a second inlet of the second regeneration reactor, and a second outlet valve at a second outlet of the second regeneration reactor;
a controller for operating one of the first regeneration reactor and the second regeneration reactor in a regeneration mode, and for operating the other regeneration reactor in a desulfurization mode by circulating the desulfurizing agent with the desulfurization reactor, when operating the first regeneration reactor in the regeneration mode, closing the first inlet valve and the first outlet valve, and operating the first oxidizing agent supply, when operating the second regeneration reactor in the regeneration mode, closing the second inlet valve and the second outlet valve, and operating the second oxidizing agent supply;
a first regeneration cyclone for separating gas and solid discharged through a first recirculation outlet of the first regeneration reactor and recirculating the solid through a first recirculation inlet of the first regeneration reactor when the first regeneration reactor operates in the regeneration mode;
a second regeneration cyclone for separating gas and solid discharged through a second recirculation outlet of the second regeneration reactor and recirculating the solid through a second recirculation inlet of the second regeneration reactor when the second regeneration reactor operates in the regeneration mode;
a first measuring sensor for measuring whether oxygen is discharged by the first regeneration reactor when the first regeneration reactor operates in the regeneration mode; and
a second measuring sensor for measuring whether oxygen is discharged by the second regeneration reactor when the second regeneration reactor operates in the regeneration mode;
the controller for
determining whether the regeneration mode of the first regeneration reactor has ended based on the first measuring sensor, and determining whether the regeneration mode of the second regeneration reactor has ended based on the second measuring sensor, and
when the first regeneration reactor operates in the regeneration mode, gas including the desulfurizing agent is discharged by the first regeneration reactor and sulfur is flowed into the first regeneration cyclone, the desulfurization agent is discharged from the first outlet of the first regeneration cyclone and recirculates to the first regeneration reactor, and the gas including sulfur is flowed into a sulfur recovery reactor, when the second regeneration reactor operates in the regeneration mode, gas including the desulfurizing agent is discharged by the second regeneration reactor and sulfur is flowed into the second regeneration cyclone, the desulfurization agent is discharged from the second outlet of the second regeneration cyclone and recirculates to the second regeneration reactor, and the gas including sulfur is flowed into the sulfur recovery reactor.

2. A high temperature dry desulfurization method comprising:
performing a first stage putting a desulfurizing agent into a desulfurization reactor by opening a first inlet valve of a first regeneration reactor and opening a first outlet valve of the first regeneration reactor, and opening a second inlet valve of a second regeneration valve reactor and opening a second outlet valve of the second regeneration reactor;
performing a second stage by operating the first regeneration reactor in a regeneration mode by putting an oxidizing agent into the first regeneration reactor by closing the first inlet valve and the first outlet valve, and performing a desulfurization reaction by circulating the desulfurizing agent with the desulfurization reactor;
performing a third stage by operating the second regeneration reactor in the regeneration mode by putting an oxidizing agent into the second regeneration reactor by closing the second inlet valve and the second outlet valve when regeneration of the first regeneration reactor is ended, and performing the desulfurization by circulating the desulfurizing agent with the desulfurization reactor; and
performing a fourth stage by repeating the second stage and the third stage.

3. The method of claim 2 , wherein performing the first stage comprises using a controller to close the first inlet valve, the first outlet valve, the second inlet valve, and the second outlet valve, and charging the desulfurizing agent in the first regeneration reactor and in the second regeneration reactor;
circulating the desulfurizing agent in the first regeneration reactor with the desulfurization reactor by using the controller to open the first inlet valve and the first outlet valve; and
circulating the desulfurizing agent in the second regeneration reactor with the desulfurization reactor by using the controller to open the second inlet valve and the second outlet valve.

4. The method of claim 3 , wherein operating the first regeneration reactor in the regeneration mode comprises regenerating the desulfurizing agent by injecting oxidizing agent into the first regeneration reactor; flowing gas including the desulfurizing agent and sulfur into a first regeneration cyclone through a first recirculation outlet of the first regeneration reactor; regenerating the desulfurizing agent by circulating the first regeneration reactor through the first regeneration cyclone; and recovering sulfur by flowing the gas including sulfur through a gas outlet of the first regeneration cyclone; and
wherein operating the second regeneration reactor in the desulfurization mode comprises controlling sulfur of a synthetic gas in the desulfurization reactor by flowing the desulfurizing agent within the second regeneration reactor into the desulfurization reactor, flowing the desulfurizing agent and the synthetic gas from the desulfurization reactor into a desulfurization cyclone, emitting the synthetic gas from the desulfurization cyclone and circulating the desulfurizing agent into the second regeneration reactor.

5. The method of claim 4 , comprising using a first measuring sensor to measure whether the first regeneration reactor discharges oxygen, and determining, by using the controller, whether regeneration of the first regeneration reactor is terminated based on the first measuring sensor.

6. The method of claim 5 , wherein operating the second regeneration reactor in the regeneration mode in the third stage comprises regenerating the desulfurizing agent by injecting the oxidizing agent into the second regeneration reactor; flowing gas including the desulfurizing agent and sulfur into a second regeneration cyclone through a second recirculation outlet of the second regeneration reactor; regenerating the desulfurizing agent by circulating the second regeneration reactor through the second regeneration cyclone; an

Assignees

• Korea Inst Energy Res

Inventors

• Ryu Ho-Jung
• Lee Dong-Ho
• Jin Gyoung-Tae
• Shun Do-Won
• Yi Chang-Keun
• Park Jae-Hyeon
• Bae Dal-Hee
• Jo Sung-Ho
• Lee Seung-Yong
• Park Young Cheol
• Moon Jong-Ho
• Lee Hyo Jin
• Baek Jeom In

Classifications

• C10J2300/093

  Coal · CPC title

• C01B17/0491

  with hydrogen or hydrogen-containing mixtures, e.g. synthesis gas · CPC title

• Y02E20/16

  Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT] · CPC title

• C01B3/56 Primary

  by contacting with solids; Regeneration of used solids · CPC title

• B01D2256/16

  Hydrogen · CPC title