Smelting and Working
ZHANG Weiguo1,ZHANG Zongwang1,XU Runsheng1,ZHANG Jianliang1,YE Lian1,ZHU Jinfeng2
Abstract: In order to study the effect of blast furnace injection of hydrogenrich gas on the lipflow condition, the energy and mass balance model of blast furnace injection of hydrogenrich gas was established, and the influences of the injection amount of natural gas, coke oven gas and top circulating gas on fuel ratio, direct reduction degree, belly gas amount, hydrogen utilization rate, belly gas amount and CO2 emission were studied. Taking into account factors such as the heat absorption of raw fuel ash, the heat absorption of unburned coal powder, and the heat absorption of methane decomposition, the calculation method for the theoretical combustion temperature of the tuyere has been revised to obtain more accurate results. Hydrogenrich gas injection can reduce the degree of direct reduction, develop indirect reduction and reduce fuel consumption. When the oxygen enrichment rate and coke ratio remain unchanged, natural gas has the greatest influence on the degree of direct reduction, the quality of coke in tuyere and the theoretical combustion temperature, followed by coke oven gas and circulating gas. The direct reduction degree of natural gas, coke oven gas and circulating gas decreases by 0.014, 0.009 and 0.0024, respectively, when the injection volume increases by 10m3, tuyere burning coke volume increased by 3.22, 2.01 and 0.55kg, respectively, theoretical combustion temperature increases by 20℃, 14.33℃ and 10.17℃, respectively. After injecting hydrogen rich gas into the blast furnace, the production and emission of CO2 in the blast furnace decreased. The CO2 emission reduction effect of natural gas injection is the most significant. Compared with the base period, the CO2 emission of 60m3 natural gas injection is reduced by 9.46%.