DRY DUST REMOVAL FROM FURNACE GAS

Abstract

A process and a plant for cleaning furnace gas includes utilizing one or more sensors to continuously monitor one or more parameters indicative for an expected temperature peak in the blast furnace gas flow. The gas flow is then passed through a conditioning tower. In case the measured parameter exceeds a predefined limit value, a coolant, such as water, is sprayed into the blast furnace gas flow in the conditioning tower. Subsequently the flow of blast furnace gas passes one or more filter stations.

Claims

1. A process for cleaning furnace gas, comprising the following steps: one or more sensors are used to continuously monitor one or more parameters indicative for an expected temperature peak in the furnace gas flow; the furnace gas flow is then passed through a conditioning tower; in case the measured parameter exceeds a predefined limit value, a coolant, e.g., water, is sprayed into the furnace gas flow in the conditioning tower; subsequently the flow of furnace gas passes one or more filter stations.

2. The process of claim 1, wherein the coolant is sprayed co-currently with the furnace gas flow.

3. The process of claim 1, wherein the parameter includes a temperature of the furnace gas flow measured at an off-take of a blast furnace.

4. The process of claim 1, wherein the mean residence time of the furnace gas in the conditioning tower is at least 3 seconds.

5. The process of claim 1, wherein the furnace gas flows downwards through the conditioning tower.

6. A plant for metal production, such as the production of steel or iron, the plant comprising a furnace with an off take for furnace gas and a downstream conditioning tower comprising nozzles connected to a coolant supply line.

7. The plant of claim 6, wherein at least a part of the nozzles are directed in a flow direction.

8. The plant of claim 6, wherein nozzles are positioned at an upstream end of a conical section of the conditioning tower, which conical section widens in flow direction.

9. The plant of claim 8, the conical section having a cone angle of 3-9 degrees.

10. The plant of claim 6, wherein the conditioning tower comprises a furnace gas inlet at its top section and a furnace gas outlet at its bottom section.

11. The plant of claim 10, wherein the furnace gas outlet comprises a side exit and a pipe section having a downwardly directed inlet and an outlet connected to the side exit.

12. The plant of claim 11, wherein the downwardly directed inlet is an upwardly pointing cone-shaped mouth piece with an open bottom side.

13. The plant of claim 6, wherein the conditioning tower has a bottom section tapering down to a dust outlet, wherein the cone-shaped mouth piece is positioned centrally above the tapering bottom section.

14. The plant of claim 6, comprising a lock hopper connected to a bottom of the conditioning tower by a discharge line.

15. The plant of claim 6, comprising a first dust removing device, such as a cyclone or dust catcher, between the off-take of the blast furnace and the conditioning tower and/or comprising one or more further dust removal devices, such as filter bag stations and/or electrostatic precipitators, downstream of the conditioning tower.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0031] Aspects of the invention will be explained with reference to the accompanying drawings, showing an exemplary embodiment.

[0032] FIG. 1: shows an exemplary embodiment of a blast furnace plant in side view;

[0033] FIG. 2: shows the plant of FIG. 1 schematically in side view;

[0034] FIG. 3: shows the nozzles within the conditioning tower of the plant of FIG. 1;

[0035] FIG. 4: shows a bottom section of the conditioning tower.

DETAILED DESCRIPTION

[0036] FIG. 1 shows a blast furnace plant 1, shown schematically in FIG. 2. The plant 1 comprises a blast furnace 2 with a gas take-off 3 connected to a line 4 leading to a cyclone 6, where larger dust particles are separated from the gas flow. The cyclone 6 has a gas outlet at its top end connected to a gas discharge line 7, and a dust outlet 8 at its bottom connected to a dust discharge line for collecting and discharging dust.

[0037] The gas discharge line 7 leads the gas flow to an inlet 9 at the top end of a conditioning tower 11. The conditioning tower 11 has a tapering bottom section 12 (see FIG. 2; in FIG. 1 this is surrounded by a cylindrical wall 13), tapering down to a dust discharge outlet 14. At a distance above the dust outlet 14 the conditioning tower 11 comprises a side exit 16 for gas with a flow deflector 17 deflecting the downward gas flow upwardly, as will be explained hereinafter with reference to FIG. 4.

[0038] FIG. 3 shows a middle section of the conditioning tower 11 in cross section. The interior of the conditioning tower 11 comprises a series of radially extending spray lances 15 crossing the wall of the conditioning tower 11. The spray lances 15 have downwardly directed nozzles 18 close to a vertical centerline of the condition tower 11. In an alternative embodiment the nozzles may be upwardly directed. The nozzles 18 are two-phase nozzles with a supply line 15a for pressurized nitrogen and a supply line 15b for water. The nitrogen serves as an atomizing gas for the water. Instead of nitrogen alternative inert atomizing gases can be used, such as steam.

[0039] The conditioning tower 11 has a cylindrical top section 11a connected to a conical middle section 11b which widens in downward direction. The spray lances 15 are positioned at a top end of the conical section 11b, close the transition to the cylindrical top section 11a of the conditioning tower 11. This position of the lances 15 promotes a good distribution of the cooling water.

[0040] A gas discharge line 19 (see FIG. 2) runs from the side exit 16 to a number of bag filter stations 21. The gas is distributed over the gas filter stations 21 and subsequently the cleaned gas is recollected. The clean gas can be used as a fuel for hot blast stoves or gas turbines.

[0041] At the gas off-take 3 the temperature of the passing blast furnace gas is continuously measured using one or more sensors 22. If the gas temperature passes a limit, e.g. 180 C., the one or more sensors 22 send a warning signal to a control unit 23. The control unit 23 is configured to activate the spray nozzles 18 in the conditioning tower 11. If the gas temperature in the off-take 3 drops below the limit, the sensors 22 send a second signal to the control unit 23. In response to the second signal the control unit 23 deactivates the spray nozzles 18.

[0042] In this exemplary embodiment, the length and the diameter of the conditioning tower 11 is such that the mean residence time of the blast furnace gas is at least 5 seconds.

[0043] A temperature peak in the blast furnace gas flow typically occurs for about 2-10 minutes. During that time water is sprayed to reduce the temperature peak.

[0044] FIGS. 3 and 4 show the nozzles 18 in more detail. After topping off the temperature peaks the blast furnace gas can be transferred to the bag filters 21 without damaging the filter material. In the line 19 from the conditioning tower 11 to the filter stations 21 basic compounds and/or adsorbents can be injected into the gas flow at an injection station 24 to remove contaminants. For instance, a mixture may be injected comprising hydrated lime and active coal. To maintain the moisture content as low as possible these compounds can be added as a dry powder.

[0045] In the conditioning tower 11 the separated dust and injected absorbents are collected and discharged at the bottom section 12. To this end the conditioning tower 11 comprises a pipe section 26 having a downwardly directed inlet 27 and an outlet 28 connected to the side exit 16. The downwardly directed inlet 27 is an upwardly pointing cone-shaped mouth piece 29 with an open bottom side 31. The cone-shaped mouth piece 29 is positioned centrally above the tapering bottom section 12. The downward flow direction of the blast furnace gas is deflected by the cone-shaped mouth piece 29 to an upward direction towards the side exit 16. Larger particles will not follow this deflection of the flow direction and will be separated from the gas flow and collected in the tapering bottom section 12 of the conditioning tower 11.