The invention is related to a device for injection of a reducing gas into a shaft furnace.
In blast furnaces, the conversion of the iron-containing charge (sinter, pellets and iron ore) to cast iron, or hot metal, is conventionally carried out by reduction of the iron oxides by a reducing gas (in particular containing CO, H2 and N2), which is formed by combustion of coke at the tuyeres located in the bottom part of the blast furnace where air preheated to a temperature between 1000° C. and 1300° C., called hot blast, is injected.
In order to increase the productivity and reduce the costs, auxiliary fuels are also injected at the tuyeres, such as coal in pulverized form, fuel oil, natural gas or other fuels, combined with oxygen enrichment of the hot blast.
The gas recovered in the upper part of the blast furnace, called top gas, mainly consists of CO, CO2, H2 and N2 in respective proportions of 20-28% v, 17-25% v, 1-5% v and 48-55% v. Despite partial use of this gas as fuel in other plants, such as power plants, blast furnace remains a significant producer of CO2.
In view of the considerable increase in the concentration of CO2 in the atmosphere since the beginning of the last century and the subsequent greenhouse effect, it is essential to reduce emissions of CO2 where it is produced in a large quantity, and therefore in particular at blast furnaces.
For this purpose, during the last 50 years, the consumption of reducing agents in the blast furnace has been reduced by half so that, at present, in blast furnaces of conventional configuration, the consumption of carbon has reached a low limit linked to the laws of thermodynamics.
One known way of additionally reducing CO2 emissions is to reintroduce top gases that are purified of CO2 and that are rich in CO into the blast furnace, said blast furnaces are known as TGRBF (Top-Gas Recycling Blast Furnaces). The use of CO-rich gas as a reducing agent thus makes it possible to reduce the coke consumption and therefore the CO2 emissions. This injection may be done at two levels, at the classical tuyere level, in replacement of hot blast and in the reduction zone of the blast furnace, for example in the lower part of the stack ok the blast furnace.
Injection at the tuyere level may be performed at the location of the existing equipment. However, in current practice there is no injection at the reduction zone level and new equipment must thus be installed. This equipment will be in contact with the burden charged in the furnace and will thus be subjected to shocks and abrasion. Moreover, the burden may comprise some fines and volatiles matter which can clog or foul the injection outlet and thus request a change in the device.
There is so a need for a device allowing injection of reducing gas which has an improved lifetime. There is notably a need for a device with a limited risk of clogging by matters charged into the furnace. There is also a need for a device which is light and easy to implement.
The present invention provides a device which comprises an external casing having a rear and a front face, said front face being provided with an outlet for gas injection into the shaft furnace, an internal casing located inside the external casing wherein reducing gas is circulating, said internal casing having an opening matching the gas injection outlet of the front face of the external casing, wherein the front face comprises an upper and a lower part, the gas injection outlet being located in the lower part and the lower and upper parts being designed so that the injection outlet is located inwards from the upper part.
The device of the invention may also comprise the following optional characteristics considered separately or according to all possible technical combinations:
Other characteristics and advantages of the invention will emerge clearly from the description of it that is given below by way of an indication and which is in no way restrictive, with reference to the appended figures in which:
Elements in the figures are for illustration only and may not have been drawn to scale. Same references are used for same elements from one figure to another.
The injection is performed through several injection outlets 4 around the circumference of the furnace, as illustrated in
The front face 21 of the injection device 4 comprises at least two parts, an upper 21A and a lower part 21B comprising the gas injection outlet 23. These upper and lower parts are designed so that the gas injection outlet 23 is located inwards from the upper part 21A so that this upper part protects the gas injection outlet 23 from the burden falling inside the furnace. This allows to create a cavity without material around the gas injection outlet 23 when gas is injected and thus to avoid the injection outlet to become dirty and/or to be clogged. This improves the lifetime of the injection device 4.
The internal casing 24 is able to transport the reducing gas, having a temperature comprised between 800° C. and 1200° C., up to the gas injection outlet 23 so that said reducing gas is injected into the blast furnace 1. The internal casing 24 and the gas injection outlet 23 are designed so that the injection of the reducing gas inside the blast furnace stack is performed downwards, preferably at an angle α with the perpendicular to the internal wall comprised between 0 and 30°. The diameter of the internal casing 24 is chosen to fulfil required speed injection in the blast furnace. In a preferred embodiment this speed is comprised between 75 and 200 m/s. In another embodiment it is inferior to 60 m/s. The refractory layer 25 allows to mitigate the variation of temperature of the reducing gas circulating into the internal casing 12.
A refractory layer 25 may furthermore be provided between the external 20 and the internal casing 24.
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In all embodiments, the injection device 4 may be provided on its front face with a stone box structure which aims to locally reinforce the external casing 20 and protect it from the burden falling into the furnace and thus to improve the lifetime of the injection device 4.
The injection device according to anyone of the previous embodiments is attached to the shell of the blast furnace 1. It may be bolted or welded to this shell.
The injection device according to any of the previous embodiments may be preferentially used for injection of a reducing gas at shaft level in a blast furnace and more specifically in a Top Gas Recycling Blast furnace. This reducing gas contains preferentially between 65% v and 75% v of carbon monoxide CO, between 8% v and 15% v of hydrogen H2, between 1% v and 5% v of carbon dioxide CO2, remainder being mainly nitrogen N2. It is preferentially injected at a temperature comprised between 850 and 1200° C.
Filing Document | Filing Date | Country | Kind |
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PCT/IB2020/058565 | 9/15/2020 | WO |