Device to inject a reducing gas into a shaft furnace
20230366049 · 2023-11-16
Inventors
- Edouard IZARD (Saint Julien Les Metz, FR)
- Dominique SERT (Montoy Flanville, FR)
- Jérôme DAULMERIE (Dunkerque, FR)
Cpc classification
F27D1/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
C21B5/001
CHEMISTRY; METALLURGY
F27B1/12
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F27B1/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F27B1/16
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A device to inject a reducing gas into a shaft furnace includes an external casing whose front face is provided with an outlet for gas injection into the shaft furnace, an internal casing located inside the external casing wherein reducing gas is circulating. The internal casing has an opening matching the gas injection outlet of the front face of the external casing. The front face of the external casing includes an upper and a lower part and the gas injection outlet is in the lower part and inwards from the upper part.
Claims
1-12. (canceled)
13: A device to inject a reducing gas into a shaft furnace, the device comprising: an external casing having a rear and a front face, the front face being provided with an outlet for gas injection into the shaft furnace; an internal casing located inside the external casing, the reducing gas passing through the internal casing, the internal casing having an opening matching a gas injection outlet of the front face of the external casing; the front face including 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 gas injection outlet is located inwards from the upper part.
14: The device as recited in claim 13 further comprising a refractory layer located between the external casing and the internal casing.
15: The device as recited in claim 13 wherein the internal casing is made of steel having a resistance to temperature up to 1200° C.
16: The device as recited in claim 13 wherein no cooling system is present.
17: The device as recited in claim 13 wherein the shaft furnace is a blast furnace.
18: The device as recited in claim 13 wherein the device is bolted to the shaft furnace.
19: The device as recited in claim 13 further comprising reinforcing plates to support the internal casing.
20: The device as recited in claim 13 wherein the internal casing is designed so that injection of the reducing gas inside the shaft furnace is performed at an angle perpendicular to the shaft furnace internal wall, the angle being between 0 and 30°.
21: The device as recited in claim 13 further comprising a stone box in the upper part of the front face.
22: The device as recited in claim 13 wherein the front face of the external casing has a triangular shape.
23: The device as recited in claim 13 wherein the lower part is recessed from the upper part.
24: The device as recited in claim 13 wherein the lower part is chamfered from the upper part.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0024] 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:
[0025]
[0026]
[0027]
[0028]
[0029]
DETAILED DESCRIPTION
[0030] 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.
[0031]
[0032] The injection is performed through several injection outlets 4 around the circumference of the furnace, as illustrated in
[0033]
[0034] 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.
[0035] 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.
[0036] A refractory layer 25 may furthermore be provided between the external 20 and the internal casing 24.
[0037] In the embodiment of
[0038] In the embodiment of
[0039] In the embodiment of
[0040] 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.
[0041] 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.
[0042] 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.