发明名称 |
Blast furnace top gas recycling process and corresponding recycling equipment |
摘要 |
A process for recycling blast furnace gas is provided. At least one portion of the gases resulting from the blast furnace undergo a CO2 purification step to create a CO-rich gas which is reinjected at a first top injection point at a temperature between 700° C. and 1000° C. through a top injection line, and at a second bottom injection point at a temperature between 1000° C. and 1300° C. through a bottom injection line. The gases from the bottom and top injection lines are heated at a temperature between 1000° C. and 1300° C. A portion of the CO-rich gas exiting the purification step is directly introduced into the top injection line via a cold gas injection line to obtain a temperature between 700° C. and 1000° C. at the first top injection point. The gas that flows through the bottom and top injection points controlled upstream of the system of the heaters. A device is also provided. |
申请公布号 |
US8992664(B2) |
申请公布日期 |
2015.03.31 |
申请号 |
US200913257146 |
申请日期 |
2009.03.17 |
申请人 |
Arcelormittal Investigación y Desarrollo, S.L. |
发明人 |
Didelon Fernand;Rachenne Yves;Gillion Christian;Borlee Jean;Sert Dominique |
分类号 |
F23N5/02;C21B5/06;C21B5/00;C21B7/00;C21B9/00 |
主分类号 |
F23N5/02 |
代理机构 |
Davidson, Davidson & Kappel, LLC |
代理人 |
Davidson, Davidson & Kappel, LLC |
主权项 |
1. A process for recycling blast furnace gas, the processing comprising:
subjecting at least one portion of gases resulting from the blast furnace to a CO2 purification so as to create a CO-rich gas which is reinjected at a first top injection point located above a base of the blast furnace at a temperature between 700° C. and 1000° C. through a top injection line, and at a second bottom injection point at the base of the blast furnace at a temperature between 1000° C. and 1300° C. through a bottom injection line, in which the gases from the bottom and top injection lines are heated with at least one heater from which the gases emerge at a temperature between 1000° C. and 1300° C.; directly introducing a portion of the CO-rich gas exiting the purification into the top injection line via a cold gas injection line in order to obtain a temperature between 700° C. and 1000° C. at the first top injection point; and controlling at least one gas flow through the bottom injection point and top injection point upstream of a system of heaters. |
地址 |
Sestao Bizkaia ES |