KR100605524B1 - Direct pressure equalizing method of hopper using in blast furnace rising gas - Google Patents

Abstract

The present invention relates to a direct equalization method of a charge hopper using the rising gas in the furnace.

To this end, the present invention is provided with a direct pressure control valve and a direct pressure control valve that can properly control the blast-furnace gas generated during the charging of raw materials, raw materials, and open and close the fuel and raw materials at the same time when the pressure equalization command is issued. This is achieved by charging and closing the nitrogen purge valve and intake nitrogen valve for a certain period of time after charging and closing them.

Accordingly, the present invention prevents the pressure loss of the hopper at the time of filling the raw material, after the completion of the pressure equalization of the top hopper to improve the discharge rate of the charge to induce a smooth molten metal discharge and increase the production, as well as higher than necessary during the pressure equalization Since it does not require the use of nitrogen gas, it not only reduces the production cost but also contributes to the production of high-quality molten iron.

Description

DIRECT PRESSURE EQUALIZING METHOD OF HOPPER USING IN BLAST FURNACE RISING GAS}

1 is a schematic configuration diagram of a road equipment having a back pressure, a pressure equalizing, a charging valve according to the prior art,

2 is a schematic configuration diagram of a road equipment equipped with a direct equalization means using blast furnace gas according to the present invention;

3 is a block diagram of a control unit for controlling a direct equalization means according to the present invention;

4 is a flowchart illustrating a direct equalization method according to the present invention;

Figure 5 is a graph illustrating the difference in pressure loss of the hopper according to the present invention and the prior art.

Explanation of symbols on the main parts of the drawings

1: blast furnace, 2: ore detector,

7: secondary equalization valve, 10: primary equalization valve,

12: back pressure valve, 15: hopper,

16: blast furnace rising gas pipe, 16a: in-house reducing gas withdrawal pipe,

19-1,19-2: direct equalization valve, 20: direct equalization control valve

21-1: nitrogen purge valve, 21-2: suction nitrogen valve,

22: Atmospheric release valve.

The present invention relates to a method of directly equalizing pressure by using a gas generated when charging fuel and raw materials into a blast furnace, and more particularly, in an apparatus for equalizing pressure at a pressure equal to or higher than that of a top hopper in order to charge the blast furnace charge. The present invention relates to a direct equalization method of a charge hopper using a rising gas in a furnace to directly improve the charging speed by using a blast furnace gas.

Referring to the conventional blast furnace process with reference to Figure 1, the ore detector (2) is operated according to the charge rate of the charge inside the blast furnace is followed by the ore charging command.

Typically, the charge is operated to go through the back pressure step-raw material import step-equalization step-charging step, first to back up the pressure of the hopper 15 to atmospheric pressure to transfer the ore weighed from the raw material to the hopper 15 The back pressure valves 11 and 12 are operated.

The back pressure is operated by the ore transfer signal of the raw material, that is, the gate open signal. When the back pressure valves 11 and 12 are opened to atmospheric pressure, the seal valve 6 is opened to import the ore (SWEEP). Then it is closed.

When the back pressure is completed primarily and the ore is imported, the blast furnace (1) is subjected to a uniform pressure to the inside of the hopper 15 at the top pressure. This is because the top pressure is excessive (approximately 2600 g / ㎠). This is also to eliminate the phenomenon of hitting the hopper 15 at the instantaneous pressure to scatter the ore to the top.

This equalization control is when the closing of the back pressure valve and the charging valve is completed, the dust discharge valve (8) is opened and the first pressure regulator valve (10) is opened to equalize.

When a predetermined time has elapsed by the time setting, the primary pressure equalizing valve 10 is closed and the secondary pressure equalizing valve 7 is opened to control the pressure equal to +200 g / cm 2 relative to the top pressure.

The gas for equalization control used at this time is nitrogen.

When the equalization is completed, the charging level is set by the signal transmitted from the ore detector 2, and when the charging level is reached, the charging is performed.

In the charging process, precise control must be made to maintain the ore distribution in the blast furnace, and care should be taken when the ore distribution is disturbed, causing problems such as yellowing.

First, when the ore detector 2 rises to the standby position, the tilt turning chute 3 moves and rotates to be positioned at a predetermined angle, which may be set differently depending on the level of the ore or the type of the ore.

When the tilt turning chute 3 reaches a predetermined position, the seal valve 4 is opened and the flow regulating valve 5 is opened at a predetermined angle.

Subsequently, when the charge is charged, the charging operation is performed in the reverse order as described above, and the ore detector 2 is continuously operated.

In the above process, if the pressure of the hopper 15 increases more than the set value due to sudden changes in the furnace situation, the emergency back pressure valve 13 is opened to protect the equipment.

However, when the secondary pressure is completed after the first pressure, the ore is dropped by various factors, and the pressure is quickly moved from the high place to the low place by the pressure deviation inside the hopper 15. For example, from the inside of the furnace to the charge hopper side, even if the secondary pressure relief valve 7 is opened to replenish nitrogen momentarily, it cannot afford this.

These phenomena slow down the discharge rate of the charges, causing disruption to normal operation and ultimately lowering the amount of molten iron production.

In addition, by using more nitrogen than necessary for equalization of the charge hopper, the quality of the blast furnace gas (BFG: carbon dioxide, carbon monoxide, hydrogen, nitrogen, etc.) generated by the reduction process inside the furnace is degraded. It will reduce the combustibility of the gas.

The present invention has been made in view of the above-described problems of the prior art, and it is created to solve this problem. In the process of loading ore into the blast furnace, it is necessary to delay the charging time according to the pressure loss of the hopper and to use nitrogen gas more than necessary. It provides a direct equalization method of the charge hopper using the rising gas in the furnace to minimize the pressure hopper and the internal pressure of the charge hopper by suppressing and directly equalizing the gas in the furnace. The purpose is.

The purpose of the present invention described above is to determine whether there is an abnormality of the raw materials, such as the basis weight and the raw material, the feedstock, and the transfer equipment when the blast furnace load discharge instruction is issued, and to discharge the lead and raw materials, and to issue a pressure equalization command after completion of back pressure and import. Step 1; A second step of selecting one of the equalization modes among the first equalization mode, the first and second equalization modes, and the direct equalization mode after the first step; A third step of starting the charging of raw materials when the first pressure equalization mode is selected in the second step, after opening the first pressure equalization valve and pressure equalizing for a predetermined time, when the pressure equalization is completed; When the first and second pressure equalization modes are selected in the second step, the first pressure equalization valve is opened to close the primary pressure equalization valve after a predetermined time, and then the second pressure equalization valve is opened to perform equalization and the equalization is completed. A fourth step of initiating charging if it is; A fifth step of, when the direct equalization mode is selected in the second step, opening the direct equalization valve and then opening the direct equalization control valve and proceeding the equalization to complete charging when the equalization is completed; A sixth step of circulating to the first step after closing one of the valves opened in the corresponding step after the charging is completed after performing any one of the third and fourth steps; When the charging is completed after the step 5, after confirming that the valves are closed, the nitrogen purge valve and the suction nitrogen valve are opened, and when more than 5 seconds, the nitrogen purge valve and the suction nitrogen valve are closed and circulated to the first step. Achievement is achieved by including steps.

Hereinafter, a preferred embodiment according to the present invention will be described in more detail on the basis of the accompanying drawings.

Figure 2 is a block diagram of a road equipment equipped with a direct equalization means using the gas in the furnace according to the present invention, Figure 3 is a block diagram showing a control process of the direct equalization means according to the present invention.

According to the drawings, the in-house reducing gas withdrawal pipe 16a is installed on the side of the gas rise pipe 16 installed on both sides of the blast furnace 1.

The reducing gas withdrawal pipe (16a) is provided with two direct pressure equalizing valve (19-1) (19-2).

The direct pressure equalizing valves 19-1 and 19-2 are connected to the hopper 15 to connect the gas outlet pipe inside the furnace at the top of the blast furnace 1 to open, close and seal the flow of gas in the pipe. It is provided for the purpose, and the direct equalization control valve 20 is installed between the direct equalization valves 19-1 and 19-2 to precisely control the equalization.

Further, nitrogen purge valves 21-1 are installed at the inlet and outlet sides of the direct pressure control valve 20, respectively.

The nitrogen purge valve 21-1 is for cleaning that the dust is stuck between the valve and the inner pipe due to the dust contained in the gas in the blast furnace 1 and the sealing is poor and the smooth operation of the valve is hindered. In order to discharge the removed dust, a discharge purge valve 21-2 connected to the outlet side of the direct pressure control valve 20 is installed.

In addition, an atmospheric discharge valve 22 is provided adjacent to the discharge purge valve 21-2 side to replace the internal gas at the time of regular repair, emergency repair, or valve maintenance.

In order to control the above-mentioned valves, the raw material pellet (hereinafter referred to as 'PLC: PROGRAM LOGIC CONTROLLER') 34 controlling the soft and raw material processing plant and the charges supplied from the soft and raw material processing plant are charged into the furnace. The route PLC 35, which controls each valve of the hazard import (SWEEP), back pressure, equal pressure, and charging system, communicates with each other, exchanging signals of the gate position 32 and the gate drive 33, and the signal and the hopper in the furnace. Pressure, valve position (36-1) (36-2) and (36-3) signals are input to the business computer (40) via each PLC and the driver's input signal, i.e. the equalization mode control signal (38), is imported. In accordance with the instruction 39 and the back pressure instruction 41, an electrical signal system is provided to determine the operation and execute control.

4 is a flowchart illustrating a control flow according to the present invention, with reference to FIG. 4 to explain the equalizing method of the present invention.

 When the blast furnace charge discharge command is issued, it is determined whether there is an abnormality in the basis weight of raw materials and raw materials, which are transfer facilities (S1).

If there is an abnormality of the result of the judgment, it is decided to re-evaluate after the action, and if there is no abnormality, the hopper gate of the ore selected from the lead and raw materials is opened and the ore is discharged and the discharged ore is imported (S3).

Before the discharged ore is imported, a back pressure command is generated to prepare for import of the ore, the back pressure system valve is operated, and it is determined whether the back pressure is completed to proceed with the import process when completed (S2).

After the above process, if the import is completed by determining whether it is completed, issuing a pressure equalization command, and if not completed, the process of continuously determining until the import is completed (S4) (S5).

When the pressure equalization command is issued, the pressure equalization type is selected. It is possible to select any one of the first and second pressure equalization mode and direct pressure equalization mode (S6).

If the first equalization pressure is selected, the first pressure equalization valve is opened while the dust discharge valve is opened while the back pressure and the charging valve are closed (S7).

When the 1st and 2nd pressure equalization mode is selected in the process of selecting the equalization mode, the dust discharge valve is opened while the back pressure and the charge valve are closed, and the first pressure equalization valve is opened for a predetermined time and then closed, and the second pressure equalization valve is opened. Nitrogen gas is used for the second pressure, which is also one of the existing pressure equalization methods (S8).

If the direct equalization mode (to prevent pressure loss of the hopper) is selected in the equalization mode selection process, the direct equalization valve is opened first, and then the direct equalization control valve is also opened (S9). .

After the equalization is carried out for a certain period of time through the above-described process, the pressure of the hopper is detected by the equalization control valve to determine whether the equalization is appropriate. If the equalization is not appropriate, it is judged until the proper equalization and the equalization is appropriate. If the charging level is reached according to the signal transmitted from the ore detector, charging is started (S10) (S11).

After the charging is started, it is determined whether the valve is completed and the closing of each valve according to the selected mode in the equal pressure selection mode at the completion of charging (S12).

That is, when the first pressure equalization mode is selected, the first pressure equalization valve is closed and then cycled to a process of determining whether the initial raw material facility is normal (S13).

If the first and second pressure equalization modes are selected, the second pressure balance is closed and then cycled to a process of determining whether the first raw material facility is normal (S14).

In case of selecting direct equalization mode, close the direct equalization valve and then close the direct equalization control valve. Then, check if both valves are closed and if both valves are closed, open the nitrogen purge valve and intake nitrogen at the same time. After opening the valve, it is determined whether both valves are opened for at least 5 seconds (S15), S16, S17, and S18.

In this process, dust generated from the process of charging fuel and raw materials into the furnace is removed.

When the determination process is satisfied, the nitrogen purge valve and the suction nitrogen valve are all closed, and then the step of detecting an abnormality of the initial raw material facility is circulated (S19).

By controlling in this way, it is possible to prevent the pressure loss of the hopper generated when the raw material and the charging of the raw material after completion of the pressure equalization of the top hopper.

Figure 5 is a graph showing the pressure change at the time of charging the raw material before, after the present invention, as shown in the prior art as shown in the pressure fluctuations were severely maintained without variation in the same pressure in the case of the present invention. .

As described in detail above, the direct equalization method of the charge hopper using the rising gas in the furnace according to the present invention is smooth by improving the discharge rate of the charge by preventing the pressure loss of the hopper during the charging of raw materials after the completion of the equalization of the top hopper. It provides the effect of inducing molten iron and increasing its yield.

In addition, since it does not have to use expensive nitrogen gas more than necessary during the pressure equalization, it not only reduces the production cost but also contributes to the production of high-quality molten iron.

Claims (1)

 The first step of determining whether there is an abnormality of lead, raw material basis weight, and raw material facility, which is a transfer facility, and issuing lead, raw material, and issuing a pressure equalization command after completion of back pressure and import; A second step of selecting one of the equalization modes among the first equalization mode, the first and second equalization modes, and the direct equalization mode after the first step; A third step of starting the charging of raw materials when the first pressure equalization mode is selected in the second step, after opening the first pressure equalization valve and pressure equalizing for a predetermined time, when the pressure equalization is completed; When the first and second pressure equalization modes are selected in the second step, the first pressure equalization valve is opened to close the primary pressure equalization valve after a predetermined time, and then the second pressure equalization valve is opened to perform equalization and the equalization is completed. A fourth step of initiating charging if it is; A fifth step of, when the direct equalization mode is selected in the second step, opening the direct equalization valve and then opening the direct equalization control valve and proceeding the equalization to complete charging when the equalization is completed; A sixth step of circulating to the first step after closing one of the valves opened in the corresponding step after the charging is completed after performing any one of the third and fourth steps; When the charging is completed after the step 5, after confirming that the valves are closed, the nitrogen purge valve and the suction nitrogen valve are opened, and when more than 5 seconds, the nitrogen purge valve and the suction nitrogen valve are closed and circulated to the first step. Direct equalization method of the charge hopper using the rising gas in the furnace, characterized in that comprising a step.

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