Method for the simultaneous production of iron and a crude syngas containing CO and H
The invention relates to a method for simultaneously producing iron and a crude syngas containing CO and H 2 by means of a blast furnace that is charged with iron ore and carbon-containing reducing agents. The amount of carbon-containing reducing agents fed to the blast furnace is greater than the amount of fuel required for producing the iron. Technically pure oxygen is fed into the blast furnace for the blast furnace process and for producing the crude syngas. In addition, CO 2 and/or steam are fed to the blast furnace in order to control the ratio between CO and H 2 in the crude syngas discharged from the blast furnace as top gas and/or moderate the temperature at which the oxygen is injected.
1. Method for the simultaneous production of iron and a crude synthesis gas that contains CO and H 2 , using a blast furnace that is charged with iron ores and coke,
wherein an amount of coke supplied to the blast furnace is greater than an amount of fuel required for iron production in order to maximize the production of the crude synthesis gas amount,
wherein technically pure oxygen is supplied to the blast furnace, for a blast furnace process and for production of the crude synthesis gas, an amount of the oxygen being adapted to the fuel amount and also being greater than an amount required for pure iron production,
wherein in addition, CO 2 and/or steam is/are supplied to the blast furnace, in order to control a CO/H 2 ratio of crude synthesis gas that leaves the blast furnace as furnace gas.
2. Method according to claim 1 , wherein substances for reducing sulfur content in the crude synthesis gas are supplied to the blast furnace.
3. Method according to claim 1 , wherein part of the furnace gas is recirculated back into the blast furnace.
4. Method according to claim 1 , wherein dust is removed from the crude synthesis gas that leaves the blast furnace as furnace gas.
5. Method according to claim 1 , wherein the CO 2 supplied to the blast furnace is obtained from the crude synthesis gas that leaves the blast furnace.
6. Method according to claim 1 , wherein at least part of the crude synthesis gas is reacted by CO conversion, with addition of steam, to produce H 2 and CO 2 , and hydrogen is obtained in a subsequent pressure change adsorption system, and
wherein an exhaust gas stream rich in CO 2 is recirculated back into the blast furnace for temperature modification, from the pressure change adsorption system, so that the CO 2 supplied to the blast furnace is obtained from the crude synthesis gas that was reacted by CO conversion.