KR19990048923A - Pickling method of ferritic stainless steel - Google Patents

Abstract

The present invention relates to a method for pickling ferritic stainless steel, the purpose of which is to maintain the acid concentration in the sulfuric acid bath solution than the conventional conditions and lower the acid concentration of the acid solution in the sulfuric acid bath solution without lowering The metal concentration is kept low, thereby providing a pickling method of ferritic stainless steel that can improve the productivity of acid solution and shorten the pickling time of the mixed acid bath and prevent the pipe from clogging.

In the present invention for achieving the above object, in the method of pickling ferritic stainless steel, a part of the scale is removed by grinding the steel sheet passed through annealing and shot blaster, and the sulfuric acid bath temperature is 90-100 ℃, concentration 120-160 g / l, pickling conditions of mixed acid bath temperature 40-50 ° C., nitric acid concentration 100-150 g / l, hydrofluoric acid concentration 1-5 g / l and line speed 30-35 mpm. The gist of the ferritic stainless steel is to be pickled.

Description

Pickling method of ferritic stainless steel

The present invention relates to a method for pickling ferritic stainless steel, and more particularly, to a method for washing a ferritic stainless steel sheet to remove scale and to prevent clogging of a pipe between an acid tank and a heat exchanger.

The working process of the continuous annealing pickling line currently being used is briefly described with reference to FIG. 1 as follows. The dense scale of the surface of heat-treated hot-rolled annealed steel sheet takes a long time to be removed when using only chemical method, so it gives a mechanical impact with a shot ball of about 0.4mm in diameter from the shot blaster. In addition to removing a part of the scale, micro-crack is applied to the remaining scale so that the acid solution penetrates well in the subsequent process. The role of the sulfuric acid tank 4 not only activates the base and scale interface to facilitate the removal of the scale in the mixed acid tank 6 but also removes part of the scale.

In addition, the mixed acid tank 6 is composed of two # 1, # 2, the role of the mixed acid tank to completely remove the residual scale not removed in the sulfuric acid tank as well as to form a protective film on the surface of the stainless steel.

Steel grade Sulfuric acid tank Mixed acid tank Temperature (℃) Concentration (g / l) Metal amount (g / l) Temperature (℃ HNO ₃ concentration (g / l) HF concentration (g / l) Metal amount (g / l) 430 70 180-200 ≤50 45 150 10 ≤60 409L 40 100 5

The steel sheet passed through the mixing tank passes through the brush roll 8 and the washing machine 9 and then completely removes water from the surface of the dryer 10 and evenly winds up the skin in the skin pass roll 11. After winding in (13), the product is shipped as a hot rolled coil or sent to a cold rolling mill for cold rolling.

However, the conventional method as described above places more weight on the pickling conditions of the mixed acid tank than the sulfuric acid tank, so that the HF concentration is 5 to 10 g / l in the mixed acid tank, and the metal ion in the pickling liquid is controlled to a maximum of 60 g / l. As the concentration increases rapidly in a short time, the activity of the acid decreases, which not only shortens the acid life, but also sludge (mainly FeF ₃ precipitate) is deposited in the pipe 14 between the acid tank and the heat exchanger, causing the pipe to clog the acid tank ( By interrupting the circulation of acid between 6) and the heat exchanger 15, the cooling capacity of the acid solution is drastically reduced, and ultimately, the pipe is completely blocked, which is a problem. Here, the sludge generating mechanism can be seen that the HF concentration and the metal ion concentration affects as shown in Equation 1 below.

3F + Me ³ = MeF ₃ ↓ (sludge)

Therefore, in order to suppress sludge generation that causes clogging of pipes, the concentration of hydrofluoric acid and metal ions should be controlled below the MeF ₃ precipitation point in the mixed acid tank.

In order to solve the above problems, the present inventors have repeatedly studied and experimented and proposed the present invention based on the results, and the present invention suggests that the temperature of the sulfuric acid bath is higher than the conventional condition and the acid concentration is lower than the conventional condition. By keeping the acid concentration of acid solution low while maintaining the acid pickling capacity of sulfuric acid tank, ferrite system can improve the productivity of acid solution and shorten the pickling time of mixed acid tank and prevent the pipe blockage. To provide a pickling method of stainless steel, the object is to.

1 is a schematic diagram of a pickling line commonly used

* Description of the symbols for the main parts of the drawings *

1 Shot Blaster 2 Brid Roll

3 washer 4 sulfate bath

5 Washer 6 Mixed Tank

7 Sunspray Nozzle 8 Brush Roll

9 Washer 10 Dryers

11 Skin Pass Mill 12 roofer

13 winder 14 piping

15 heat exchanger

In the present invention for achieving the above object, in the method of pickling ferritic stainless steel, a part of the scale is removed by grinding the steel sheet passed through annealing and shot blaster, and the sulfuric acid bath temperature is 90-100 ℃, concentration 120-160 g / l, pickling conditions of mixed acid bath temperature 40-50 ° C., nitric acid concentration 100-150 g / l, hydrofluoric acid concentration 1-5 g / l and line speed 30-35 mpm. It relates to a pickling method of ferritic stainless steel.

Hereinafter, the present invention will be described in detail.

In the present invention, a part of the scale is physically removed from the steel sheet subjected to the annealing and shot blaster using a machine such as a grinding brush.

In addition, in this invention, the conditions of a sulfuric acid tank are made into 90-100 degreeC, and concentration is 120-160 g / l.

Maintaining the temperature of the sulfuric acid tank to 90 ℃ or more to enhance the pickling conditions of the sulfuric acid tank compared to the prior art. However, when the temperature exceeds 100 ° C, it is difficult to control due to boiling of the solution.

If the concentration of the sulfuric acid tank is less than 120g / l is required a lot of time to obtain the pickling effect, if it exceeds 160g / l has little effect on the concentration increase.

In the present invention, the conditions of the mixed acid bath are 40 to 50 ° C., nitric acid concentration is 100 to 150 g / l, and hydrofluoric acid concentration is 1 to 5 g / l.

If the temperature of the sulfuric acid tank is less than 40 ℃, pickling is not good, if it exceeds 50 ℃ there is a problem that NO _X occurs.

If the nitric acid concentration is less than 100g / l is not pickling well, if it exceeds 150g / l metal melts to increase the metal concentration.

If the hydrofluoric acid concentration is less than 1g / l, pickling is not good, and if it exceeds 5g / l, there is a problem in that the metal melts a lot and metal ions increase.

When pickling ferritic stainless steel under sulfuric acid and mixed acid conditions as described above, the line speed can be maintained at 30 to 35 mpm.

The present invention having the configuration as described above changes the conditions of the present invention in the conventional pickling method, so that the pickling capacity of the sulfuric acid bath and the mixed acid bath in the conventional method is about 50:50. It is characterized by maximum reinforcement. Therefore, even if the conditions of the mixed acid tank were weaker than the existing pickling conditions, it was possible to maintain the conventional line speed (LINE SPEED) or more, and it was possible to lower the HF concentration and the metal ion concentration causing the pipe blockage. In addition, by reducing the scale to be removed from the mixed acid tank it is possible to extend the life of the mixed acid tank than the conventional method.

Hereinafter, the present invention will be described in more detail with reference to Examples.

Example

The 430 stainless steel sheet and 409L stainless steel sheet which were hot-rolled and annealed by the conventional method were prepared. The steel sheets were treated with a shot blaster and a grinding brush, and then pickled under the conditions of Tables 2 and 3 below. After pickling, the line speed was evaluated, and whether sludge was generated was evaluated by production (O) and unproduced (X). The results are shown in Table 2 for 430 stainless steel sheet and Table 3 for 409L stainless steel sheet, respectively. It was.

Sulfuric acid tank Mixed acid tank result Temperature (℃) Concentration (g / l) Metal amount (g / l) Temperature (℃) HNO ₃ concentration (g / l) HF concentration (g / l) Metal amount (g / l) LINESPEED Weight loss (mg / cm ² ) Sludge Conventional Example 1 70 180 50 45 150 3 30 18 5.0 X Conventional Example 2 70 200 50 45 150 5 45 20 5.5 ○ Conventional Example 3 70 200 50 45 150 10 30 22 7.5 X Comparative Example 1 90 100 50 45 150 5 40 25 4.0 X Comparative Example 2 90 100 50 45 150 5 45 23 3.8 ○ Inventive Example 1 90 120 50 45 150 3 40 30 2.5 X Inventive Example 2 100 120 50 45 150 5 40 32 2.2 X Inventive Example 3 100 160 50 45 150 3 40 35 1.5 X Comparative Example 3 100 160 50 45 150 One 40 23 2.8 X

turn Sulfuric acid tank Mixed acid tank result Temperature (℃) Concentration (g / l) Metal amount (g / l) Temperature (℃) HNO ₃ concentration (g / l) HF concentration (g / l) Metal amount (g / l) LINESPEED Weight loss (mg / cm ² ) Sludge Conventional Example a 70 180 50 40 100 5 50 30 5.3 ○ Comparative Example a 90 180 50 40 100 3 45 33 5.7 ○ Comparative Example b 100 0 50 40 100 4 35 28 2.6 X Inventive Example b 100 120 50 40 100 One 35 33 2.5 X Inventive Example c 90 160 50 40 100 3 40 35 2.1 X Inventive Example c 100 160 50 40 100 One 40 32 1.7 X Comparative Example c 100 160 50 40 100 5 40 38 5.8 X

As shown in Table 2, the pickling method in which the sulfuric acid condition of the conventional example (1, 2, 3) is a low temperature (70 ° C.) and a high concentration (180-200 g / l) is used in a mixed acid tank to completely remove the scale. The longer the pickling time, the greater the weight loss per unit area. In addition, when the sulfuric acid concentration is 120 g / l or less as in Comparative Example (1), it can be seen that the activity of the conversion tank is reduced, so that the pickling time in the mixing tank is long, and the weight loss in the mixing tank is increased. In Comparative Example (2), the metal ion concentration was 40 g / l or more and sludge was generated. In Comparative Example (3), the weight loss was reduced by half compared to the conventional method, but the life of the acid was extended, but the line speed was not different from the conventional method. On the other hand, the invention examples (1, 2, 3) to which the conditions of the present invention are applied are all completely descaled even when working at the line speed steel of 30mpm or more, and the weight loss of the mixed acid tank is lower than 2.5mg / cm ^2, and the solution life is low. Could extend.

As shown in Table 3, in the conventional example (a) and the comparative example (a), sludge was generated because the amount of metal ions in the mixed acid bath was high. In Comparative Example (b), sludge did not occur at a conversion concentration of 100 g / l, but there is a disadvantage in that the line speed is slow. The condition of Comparative Example (c) is not good because the weight loss is large because the activity of sulfuric acid is increased and the concentration of hydrofluoric acid is high.

On the contrary, the invention examples (a, b, c) to which the conditions of the present invention are applied are all completely descaled even when the line speed is more than 30mpm, and the weight loss of the mixed acid tank is 2.5mg / cm ^2.

It was low below and the solution life was extended.

As described above, according to the present invention, a portion of the scale of the stainless steel sheet is removed, and the solution condition of the sulfuric acid bath is controlled at a temperature higher than the conventional condition, and the acid concentration is lower than the conventional condition, so that the acid pickling ability of the sulfuric acid bath is not reduced. By keeping the concentration low, the acid solution not only extends the life of the acid solution, but also the grinding brush and sulfuric acid bath descaling effect, which increases the descaling capacity of the sulfuric acid bath compared to the conventional pickling method. In addition to reducing the hydrofluoric acid concentration, the 430 steel can reduce the productivity to 5g / l or less and 409L steel to less than 3g / l, thus improving productivity and preventing pipe blockage.

Claims (2)

In the method of pickling ferritic stainless steel, A part of the scale is removed by grinding brush on the steel sheet which has undergone annealing and shot blasting. Pickling method of ferritic stainless steel, characterized in that pickling is performed at 100-150g / l, hydrofluoric acid concentration at 1-5g / l and line speed at 30-35mpm. The method of claim 1, The mixed acid tank is managed with a metal ion concentration of 40g / l or less, and the descaling amount is controlled to 2.5mg / cm ² or less pickling method of ferritic stainless steel