TW201615938A - Method for producing briquettes and briquettes produced using the same - Google Patents

Abstract

Provided are a method for producing briquettes and briquettes produced thereby, the method for producing briquettes may include a process of obtaining a silicon-containing waste slurry, a primary oil cleaning process of separating a silicon-containing slurry and a water soluble oil from the silicon-containing waste slurry, and a forming process of forming briquettes by using a mixture which is prepared by mixing the silicon-containing slurry with a binder, and waste slurry which contains silicon that is generated during the production of semiconductor or solar cell wafers may be purified and used for increasing the heat and modifying the composition of molten steel in the steel making process.

Description

Method for making bricks and bricks made with the same background

The present invention relates to a method for making bricks and bricks produced by the method, and more particularly to a waste mash slurry produced by manufacturing a semiconductor or solar wafer by purification for use in a steelmaking process. One of the bricks in the process.

Typically, in a steelmaking process, impurities (including carbon) contained in the pig iron are oxidized in the molten steel at a temperature of about 1,500 ° C, and the oxides are removed as slag. In the steel making process, steel is introduced after introduction of oxygen and then a predetermined time. At this time, ferromanganese, ferroniobium or the like is added to the molten steel to adjust the composition and prevent deoxidation from occurring. Here, however, the production of bismuth iron added to molten steel requires a large amount of ruthenium, but since most of the ruthenium must be input and thus expensive, the total cost of the steelmaking process increases. Moreover, bismuth (Si) having a high calorific value is used as a heating agent for raising the temperature inside the blast furnace during an iron & steel making process (including a common steel making process). However, the steel industry requires a large amount of antimony, and since the use as a heating agent is expensive, the total cost of producing steel can be increased.

It is well known that ruthenium is used as a main material in the semiconductor industry, and when a semiconductor product is manufactured by various processes, a waste slurry containing a large amount of ruthenium is produced as a by-product. If Severe air and land contamination can occur if only the waste slurry is burned or buried underground. Accordingly, a method of solidifying a waste slurry into a treated cement slurry to store or bury the treated cement slurry waste slurry has been implemented.

One process for discharging a waste slurry containing a large amount of hydrazine will be described in detail below.

A germanium wafer for fabricating a semiconductor-integrated circuit or a solar cell is produced by a process of cutting a germanium ingot. The cut wafer is also planarized by a surface polishing process.

In the process of cutting the twin ingot (also known as a wire saw process), a tantalum carbide (SiC) mixed as a cutting agent and a coolant for cutting oil (for cutting water or oil-soluble oil) are used. Slurry. In the wire sawing process, the ruthenium wafer can be produced by cutting a ruthenium ingot using a cutting device called a wire saw while supplying the slurry. In addition to niobium carbide, alumina, diamond, yttria or the like may be used as the material of the dicing agent.

Since the wire saw used in the process of cutting the twin ingot has a predetermined thickness, a large number of twin ingots are generated as sawdust during the cutting process. The more the thickness of the wafer and wire saw increases, the more the amount of sawdust increases.

For example, when the tantalum wafer has a thickness of about 0.1 mm and the wire saw has a thickness of about 0.1 mm, about 50% of the twin ingots can be formed as sawdust. Therefore, after the cutting of the ingot or the polishing of the crucible wafer, the cutting agent, the cutting oil, the sawdust, the fine dust generated from the device, and the like can be contained in the waste slurry.

The waste slurry generated in this manner during the manufacture of the crucible wafer is classified as a special waste. Severe air and land contamination can occur when only the waste slurry is burned or buried. Therefore, the generated waste slurry is solidified into cement and then stored or buried.

However, even if the waste slurry is solidified into cement for its disposal, the storage or burial space of the waste slurry is limited. In addition, this disposal method can result in waste of natural resources. Therefore, there is an urgent need for a method for recycling and recycling waste slurry.

Specifically, since a large amount of dust is contained in the waste slurry during the cutting of the twin ingot, the effective separation and recycling of the dust has become an important issue in the field of resource recycling and industrial waste disposal.

The present disclosure provides a method for fabricating a brick for increasing the temperature of molten steel and adjusting the composition of molten steel in a steelmaking process by purifying the waste containing ruthenium generated during the manufacture of the semiconductor or solar wafer The slurry is applied; and the brick produced by the method.

The present disclosure also provides a method of fabricating a brick capable of increasing the temperature of molten steel and adjusting the composition of molten steel at a low cost and high efficiency in a steelmaking process, and a brick produced by the method.

The present disclosure also provides a method of fabricating bricks produced by this method which is capable of reducing the disposal cost of a waste slurry which causes environmental pollution.

The present disclosure also provides a method of fabricating a brick capable of preventing deterioration of quality due to oxidation of niobium and a brick produced by the method.

According to an exemplary embodiment, a method includes preparing a ruthenium-containing waste slurry; performing a primary oil cleaning process for separating the mash-containing slurry and the water-soluble oil from the mash-containing waste slurry; and using one of the binders The mixture containing the mash slurry is mixed to form the brick.

The ruthenium-containing waste slurry may be formed when a ruthenium ingot is cut or polished on one surface of a wafer and contains the mash-containing slurry and the water-soluble oil.

The cerium-containing waste slurry contains at least cerium (Si) and cerium carbide (SiC).

The primary oil cleaning process may include mixing water and the cerium-containing waste slurry at a first mixing ratio; agitating the cerium-containing waste slurry and the water; and filtering the mash-containing slurry and the mixture of the water to include the mixture The mash waste slurry, the water-soluble oil, and the water are separated from each other.

The first mixing ratio of water to the volume of the mash-containing waste slurry may correspond to from about 0.2 times to about 8 times.

It may further comprise performing a secondary oil cleaning process for removing the water soluble oil from the mash containing slurry prior to forming the brick.

The secondary oil cleaning process may include mixing the water and the mash-containing slurry at a second mixing ratio; agitating the mash-containing slurry and the water; and filtering the mash-containing slurry and the mixture of the water to separate the mash-containing slurry The water-soluble oil and the water.

The second mixing ratio of water to the volume of the mash-containing waste slurry may correspond to from about 0.2 times to about 8 times.

It may further comprise performing fractionation on the water-soluble oil and water separated from each other in the primary oil cleaning process to separate the water-soluble oil from the water after the primary oil cleaning process.

The method further includes performing at least one of a mash-containing slurry drying process and a mash-containing slurry milling process prior to forming the brick.

In the formation of the brick, a source of Fe may be selectively added to the mixture of the slurry containing the binder and the binder during the formation of the brick.

The mixture may contain from about 35% to about 97% by weight of the cerium-containing slurry, from about 0% to about 50% by weight of the Fe source, and about 3, based on the total weight of the mixture. From about 1% by weight to about 15% by weight of the binder.

The binder may contain at least one of syrup, starch, bentonite, calcium hydroxide, and sodium citrate.

The binder may comprise the water and water-soluble oil separated in the primary oil cleaning process, the water and water-soluble oil separated in the secondary oil cleaning process, and the water-soluble oil separated in the separation process And at least one of the waters.

According to an exemplary embodiment, the brick may be made by means of a method of making a brick comprising tantalum, niobium carbide, and a binder.

The brick may further comprise a source of Fe.

10‧‧‧First stirrer

20‧‧‧First filtration system

30‧‧‧ fractionation system

40‧‧‧Second stirrer

50‧‧‧Second filtration system

60‧‧‧Dryer

70‧‧‧Milling machine

80‧‧‧Brick forming device

310‧‧‧Water/Oil Storage Tank

320‧‧‧ pump

330‧‧‧Distillation tower

340‧‧‧First collection unit

350‧‧‧Second collection unit

360‧‧‧First heat exchanger

370‧‧‧second heat exchanger

380‧‧‧Water storage tank

390‧‧‧oil storage tank

S10, S12, S14, S16, S20, S30, S32, S34, S36, S40, S50, S60, S62, S64, S66‧‧‧ steps

Exemplary embodiments of the present invention can be understood in more detail from the following description in conjunction with the accompanying drawings, in which: FIG. 1 is a diagram illustrating the purification of waste containing waste as a by-product in the manufacture of a semiconductor wafer or a solar wafer. A view of the process of the slurry.

2 is a flow chart illustrating a method of making a brick by purifying a slurry containing ruthenium according to an exemplary embodiment for raising temperature and changing composition in a steelmaking process.

Figure 3 is a flow chart illustrating one of the primary oil cleaning processes illustrated in Figure 2.

Figure 4 is a flow chart illustrating one of the secondary oil cleaning processes illustrated in Figure 2.

Figure 5 is a flow chart illustrating one of the brick forming processes illustrated in Figure 2.

Figure 6 is a view illustrating an example of an apparatus for carrying out an exemplary embodiment.

Fig. 7 is a view for explaining an example of the fractionation system of Fig. 6.

Hereinafter, specific embodiments will be described in detail with reference to the accompanying drawings.

Detailed descriptions of related functions or configurations that may unnecessarily obscure the essential features of the present invention will be omitted.

Fig. 1 is a view for explaining a process for purifying a ruthenium-containing waste slurry which is produced as a by-product in the production of a semiconductor wafer or a solar wafer.

Referring to Fig. 1, a cutting agent, sawdust, cutting oil, and a cutting agent or fine dust generated from a wire saw generated in other cutting processes are included in one of the cutting processes or the surface of a polished wafer. In the waste slurry generated in a process.

As shown in Figure 1, an oil cleaning process is performed on the waste slurry to separate the recyclable crucible and the cutting agent from the waste slurry. The cutting agent is removed by means of an oil cleaning process. Here, the generated wastewater is transferred to a wastewater treatment system and then recycled. Next, a helium separation process is performed on the waste slurry subjected to the oil cleaning process to separate the effective helium and recycle the separated helium. Here, a centrifugation process can be used for separating the ruthenium. The separated helium is recycled by means of a drying process.

In the crucible separation process, only crucibles having a large particle size can be separated, and thus a large number of fine The cleavage agent and impurities and fine ruthenium may remain in the waste slurry after separation of the ruthenium having a large particle size.

Figure 2 is a flow chart illustrating a method of making a brick by purifying a slurry containing ruthenium according to an exemplary embodiment for raising temperature and changing composition in a steelmaking process, Figure 3 To illustrate a flow chart of a primary oil cleaning process illustrated in FIG. 2, FIG. 4 is a flow chart illustrating a secondary oil cleaning process illustrated in FIG. 2, and FIG. 5 is a description 2 is a flow chart illustrating one of the brick forming processes illustrated in the figure. Further, Fig. 6 is a view for explaining an example of a device for carrying out an exemplary embodiment, and Fig. 7 is a view for explaining an example of the fractionation system of Fig. 6.

Referring to Fig. 2, a primary oil cleaning process (S10), a separation process (S20), a primary oil cleaning process (S30), a drying process (S40), a milling process (S50), and a brick forming process (S60). It is one of the final products of the exemplary embodiment (ie, used to raise the temperature of the molten steel during the production of molten steel in a steelmaking process and adjust the composition of the molten steel) by means of the primary oil cleaning process (S10) And brick forming process (S60) to make. Here, the secondary oil cleaning process (S30), the drying process (S40), and the milling process (S50) may be selectively performed as needed. Therefore, at least one of the secondary oil cleaning process (S30), the drying process (S40), and the milling process (S50) may be one of the processes that can be selectively performed in the brick making process. Hereinafter, a method of fabricating a brick according to an exemplary embodiment will be described, which includes a primary oil cleaning process (S10), a separation process (S20), a secondary oil cleaning process (S30), a drying process (S40), and a milling process. (S50), and brick forming process (S60).

First, in the primary oil cleaning process (S10), the oil may be separated from a cerium-containing waste slurry (for example, an initial waste slurry) containing cerium (Si), cerium carbide (SiC), and a water-soluble oil.

The ruthenium-containing waste slurry (ie, the initial waste slurry) is used as a semiconductor Generated by by-products generated during wafer or solar wafer fabrication processes. Therefore, the initial waste slurry may contain niobium which is formed when the ingot is cut, and tantalum carbide (SiC) which is a cutting agent, and a water-soluble oil which is a cutting oil. In addition, it may contain about 5% iron (Fe) source and a small amount of copper (Cu). The process of separating one of the water-soluble oils contained in the initial waste slurry can be performed in the primary oil cleaning process (S10). Here, since the niobium carbide contained in the initial waste slurry has various particle diameters, one of the processes of separating the niobium carbide having a relatively large particle diameter by a centrifugal process can be performed before the primary oil cleaning process (S10).

The initial waste slurry is a by-product produced in a process such as a wire saw, and contains from about 10% to about 30% by weight of a water-soluble oil (for example, polyethylene glycol (PEG) + diethylene glycol (DEG)). Therefore, the water-soluble oil contained in the initial waste slurry must be removed to a predetermined amount to use the initial waste slurry in the steelmaking process. A combustion process at a high temperature and a cleaning process using water can be performed to remove the oil. However, when the water-soluble oil is burned at a high temperature, air pollution becomes more serious as the content of the water-soluble oil increases, and helium can be oxidized at a high temperature. Since the initial waste slurry contains a large amount of water-soluble oil, the initial waste slurry can be washed with water. However, in this case, the water-soluble oil is soluble in water to increase the cost of wastewater treatment.

In this example, the water soluble oil can be separated from the initial waste slurry and then reused by one of the processes set forth below. Moreover, the water-soluble oil may be additionally removed from the mash-containing slurry as needed, in which the water-soluble oil is removed to a predetermined amount. Therefore, there is an economic benefit in that air pollution and deuterium oxidation due to oil burning are prevented and water-soluble oil is reused. Further, as described below, since the water system is separated from the water-soluble oil by fractional distillation, there is almost no cost in processing the finally produced wastewater.

As described above, by-products (e.g., water-soluble oil or water) formed while separating the water-soluble oil from the initial waste slurry can be reused as one of the binders in the production of bricks.

To this end, the water-soluble oil and water are separated from the initial waste slurry by a pressing method using a filter press, in a state where water is mixed in the initial waste slurry to a predetermined amount sufficient for stirring and pumping. Next, the water-soluble oil is reused by evaporating water, and the slurry in which the water-soluble oil has been reduced to a predetermined amount (i.e., the mash-containing slurry) is subjected to a drying process and then milled to a suitable size. The milled slurry forms a brick for raising the temperature of the molten steel in the steelmaking process and adjusting the composition of the molten steel.

Referring to Fig. 3, the primary oil cleaning process (S10) may include processes (S12, S14, and S16).

First, in the process (S12), the initial waste slurry stored in a waste slurry storage tank is supplied to a first agitator 10, and the amount of water corresponding to a first mixing ratio is supplied to the first agitation. The vessel 10 mixes the initial waste slurry with water.

For example, the interior of the waste slurry storage tank can be maintained at a predetermined temperature to prevent the stored initial waste slurry from decreasing in viscosity. Moreover, the agitation can be performed in a predetermined cycle to prevent the stored initial waste slurry from solidifying due to precipitation which occurs over time. In this case, the waste slurry storage tank can support a stirring function.

The initial waste slurry can include by-products generated in the process of manufacturing a semiconductor wafer or a solar wafer. By-products may include bismuth (Si), tantalum carbide (SiC), water-soluble oil, iron (Fe), copper (Cu), and the like.

The first mixing ratio of the initial waste slurry to water can be set in the range of from about 1:0.2 to about 1:8 (by volume ratio). In other words, the initial slurry can be mixed with water such that the volume of water is from about 0.2 to about 8 times the initial waste slurry. As described above, the first mixing ratio is set in consideration of agitation and pumping of the initial waste slurry.

In the process (S14), a process of operating the first agitator 10 to agitate the mixture of the initial waste slurry and water is performed.

The primary oil cleaning process (S10) will be described in detail below.

First, in the process (S12), the initial waste slurry stored in a waste slurry storage tank is supplied to a first agitator 10, and the amount of water corresponding to a first mixing ratio is supplied to the first agitation. To mix the initial waste slurry with water.

For example, the interior of the waste slurry storage tank can be maintained at a predetermined temperature to prevent the stored initial waste slurry from decreasing in viscosity. Further, the agitation may be performed in a predetermined cycle to prevent the stored initial waste slurry from solidifying due to precipitation which occurs over time. In this case, the waste slurry tank can support a stirring function.

The initial waste slurry includes by-products generated in the process of manufacturing a semiconductor wafer or a solar wafer. The by-products may specifically include cerium (Si), cerium carbide (SiC), water-soluble oil, iron (Fe), copper (Cu), and the like.

The first mixing ratio of the initial waste slurry to water can be set in the range of from about 1:0.2 to about 1:8 by volume. In other words, the initial slurry is mixed with water such that the volume of water is from about 0.2 to about 8 times the initial waste slurry. As described above, the first mixing ratio is set in consideration of agitation and pumping of the initial waste slurry.

In the process (S14), a process of operating the first agitator 10 to agitate the mixture of the initial waste slurry and water is performed.

In the process (S16), after a predetermined stirring time, the agitated mixture of the initial waste slurry and water is supplied to the first filtration system 20, and the water and water-soluble are separated from the mixture of the initial waste slurry and water by filtration. One of the oil processes. As a specific filter Alternatively, a press process can be performed using a filter press to separate water from the water soluble oil. Alternatively, various known techniques can be used, such as centrifugation.

After undergoing the filtration process, the water-soluble oil contained in the initial waste slurry can be removed to a predetermined amount to obtain the mash-containing slurry.

As described below, when the mash-containing slurry which is an intermediate product produced according to an exemplary embodiment is dried and milled, a cerium-containing powder can be obtained. The cerium-containing powder contains a large amount of cerium and cerium carbide and thus has an extremely large heating value. Therefore, when the cerium-containing powder is inserted as it is into a converter or the like, there is a risk of fire. Therefore, the niobium-containing powder can be pressed and then processed to form a brick having a predetermined size and shape by means of a brick forming process (S60). Here, if the amount of the oil contained in the niobium-containing powder for making the intermediate product for raising the temperature and adjusting the composition is remarkably insufficient, it may be difficult to maintain the form of the compressed brick, and thus the brick may be easily broken. Therefore, when a predetermined amount of oil is contained in the niobium-containing powder, the oil can contribute to the formation of the brick. When the content of the water-soluble oil remaining in the mash-containing slurry obtained by the primary oil cleaning process (S10) is excessive, the water-soluble oil may be additionally removed by means of the secondary oil cleaning process (S30) which will be described later. the amount.

Next, in the separation process (S20), the separation process of the water-soluble oil and water is performed by fractional distillation of the water-soluble oil and water separated in the primary oil cleaning process (S10). The water soluble oil extracted by this process can be recycled in the brick forming process (S60) set forth below, and the water can be purified to the extent that no additional wastewater treatment process is required.

An example of a specific composition of one of the fractionation systems 30 in which the separation process (S20) is performed will be explained with reference to FIG.

Fractionation system 30 can include a water/oil storage tank 310, a pump 320, a distillation The tower 330, a first collecting unit 340, a second collecting unit 350, a first heat exchanger 360, a second heat exchanger 370, a water storage tank 380, and an oil storage tank 390.

The water-soluble oil and water separated from the mixture of the initial waste slurry and water by the primary oil washing process (S10) are supplied to the water/oil storage tank 310 and temporarily stored.

Hereinafter, the description is given by using an example in which the water-soluble oil system is composed of polyethylene glycol (PEG) and diethylene glycol (DEG). The values of temperature, pressure, flow rate, etc. disclosed in the following description are merely examples and may be modified according to specific needs.

In Figure 7, the temperatures, pressures, and flow rates for the specific locations F, F1, F2, B1, B2, B3, W1, W2, and W3 are given at which, for example, the system is constructed A valve is installed in one of the supply flow paths between the components. The water-soluble oil and water stored in the water/oil storage tank 310 have a mixing ratio of PEG:DEG:water of about 20:13:67 based on % by weight.

The pump 320 supplies the water-soluble oil and water to the distillation column 330 at a temperature of about 20 ° C, a pressure of about 760 mmHg, and a flow rate of about 300 kg / hour.

The distillation column 330 separates the water-soluble oil from the water by fractional distillation and can be roughly divided into a heating unit, a cooling unit, and a collecting unit according to functions.

For example, distillation column 330 can perform distillation in a plurality of trays (eg, in 10 trays). When the water-soluble oil and water are heated and distilled by using a reboiler whose boiler steam has a temperature of about 150 ° C or higher, the temperature is about 51.5 ° C, the pressure is about 100 mmHg, and the flow rate is about 200 kg / hour. Water may be collected in the first collection unit 340, and a water soluble oil (ie, PEG/DEG) having a temperature of about 137 ° C, a pressure of about 106 mm Hg, and a flow rate of about 99.5 kg / hour may be collected in the second collection unit 350 in.

The temperature supplied by the first collecting unit 340 is about 51.5 ° C, and the pressure is large. Water having a flow rate of about 200 kg/hr and having a flow rate of about 200 kg/hr may pass through the first heat exchanger 360 and then be supplied to the water storage tank at a temperature of about 30 ° C, a pressure of about 2967 mm Hg, and a flow rate of about 200 kg / hour. 380.

The water-soluble oil supplied by the second collecting unit 350 having a temperature of about 137 ° C, a pressure of about 106 mmHg, and a flow rate of about 99.5 kg / hr passes through the second heat exchanger 370 and then at a temperature of about 30 ° C, pressure. It is supplied to the oil storage tank 390 at a rate of about 2967 mmHg and a flow rate of about 99.5 kg/hr.

The water storage tank 380 is for storing one unit of water supplied after passing through the first heat exchanger 360. The stored water has a temperature of about 30 ° C, a pressure of about 760 mm Hg, and a chemical oxygen demand (COD) of only a few PPM (obtained from the simulation). Therefore, it seems that almost no wastewater treatment is required.

The oil storage tank 390 is for storing one unit of oil supplied after passing through the second heat exchanger 370. The stored oil was at a temperature of about 30 ° C and a pressure of about 760 mm Hg, and an oil containing about 0.5% by weight moisture, about 60.3 % by weight PEG, and about 39.2% by weight DEG (according to the simulation results) was collected.

Next, in the secondary oil cleaning process (S30), the slurry of the water-soluble oil and water is separated therefrom by means of the primary oil cleaning process (S10) (ie, by containing the mash slurry therein after stirring) The process of washing the water-soluble oil remaining in the mash-containing slurry is performed by mixing and filtering in a state where the second mixing ratio is mixed with water.

For example, the second mixing ratio may be set such that the volume of water contains about 0.2 to about 8 times the mash slurry, and the secondary oil cleaning process (S30) can be performed at a low temperature of about 50 ° C or below.

As described above, although a predetermined amount of the water-soluble oil contained in the initial waste slurry is removed by the primary oil cleaning process (S10), the remaining water-soluble oil may be additionally removed according to the process conditions. To this end, a secondary oil cleaning process (S30) can be performed.

The secondary oil cleaning process S30 will be described in detail below. Referring to Figure 4, the secondary oil cleaning process (S30) can be configured to include processes (S32, S34, and S36).

First, in the S32 process, the water-soluble oil from the primary oil cleaning process (S10) is removed to a predetermined amount of slurry (i.e., the mash containing slurry supplied to a second agitator 40) and a certain amount of water. The second agitator 40 is supplied to the second agitator 40 in accordance with the predetermined second mixing ratio to perform a process of mixing the slurry containing the slurry with water.

The second mixing ratio of the mash-containing slurry to water can be set in the range of from about 1:0.2 to about 1:8 (by volume ratio). In other words, the slurry containing the mixture can be mixed with water such that the volume of water is from about 0.2 times to about 8 times the volume of the mash containing slurry.

The reason why the mash-containing slurry and water are mixed at the above mixing ratio is as follows.

When the viscosity of the mash-containing slurry is taken into consideration, in the case of a mixing ratio of about 0.2 times or less, it is difficult to carry out the subsequent stirring process and the pumping process. In the case of a mixing ratio of about 8 or more, the removal ratio of the water-soluble oil sharply increases to deteriorate the formability of the subsequent brick forming process (S60).

In other words, the water mixed with the mash-containing slurry is subjected to agitation and a filtration process as will be described later and then mixed with a water-soluble oil, thereby being discharged as waste water. Waste water can be one of the causes of environmental pollution, and thus an additional wastewater treatment process must be performed. Therefore, it is advantageous to increase the amount of water to facilitate the execution of the wastewater treatment process. Further, as the amount of water increases, the degree of cleanliness of the oil may increase, and thus the amount of oil removed from the mash-containing slurry may also increase.

As described above, when the cerium-containing slurry which is one of the intermediate products produced according to an exemplary embodiment is dried and milled, a cerium-containing powder can be obtained. Since the niobium-containing powder has an extremely large calorific value, if the niobium-containing powder is inserted into a converter or the like as it is, a risk of fire may occur. Therefore, the niobium-containing powder can be pressed and then processed to form a brick having a predetermined size and shape by means of a brick forming process (S60). Here, if the amount of the oil contained in the niobium-containing powder for making the intermediate product for raising the temperature and adjusting the composition is remarkably insufficient, it may be difficult to maintain the form of the compressed brick, and thus the brick may be easily broken. Therefore, the cerium-containing powder may contain a predetermined amount of oil.

Therefore, the mixing ratio of the cerium-containing powder and water can be set as described above to increase the efficiency of the wastewater treatment process and brick production.

Next, in the process (S34), the second stirrer 40 is operated to drive the dissolution of the water-soluble oil remaining in the mash-containing slurry, thereby performing the stirring of the mash-containing slurry mixed with water.

Next, in the process (S36), after a predetermined stirring time, the mash-containing slurry which is stirred with water is supplied to a second filtration system 50 to filter water and water-soluble oil dissolved therein. One of the processes for removing water and water-soluble oil from the slurry. Various known techniques can be implemented as specific filtration methods.

In the process of washing the mash containing slurry by using water, if the water temperature is too low, the oil cleaning ability may be slightly deteriorated. On the other hand, if the water temperature is too high, the antimony can be deteriorated by the reaction of hydrazine with water to produce cerium oxide (SiO ₂ ). Therefore, to prevent this limitation, according to an exemplary embodiment, the entire or a portion of the secondary oil cleaning process (S30) can be performed at a low temperature of 50 ° C or below.

Next, in the drying process (S40), the mash-containing slurry in which the water-soluble oil is washed by the secondary oil cleaning process (S30) is supplied to a dryer 60 to dry the mash-containing slurry at a predetermined drying temperature. Process. The drying process (S40) can be selectively performed as needed. For example, the drying process (S40) can be performed as a natural drying process or at an air or nitrogen atmosphere at a temperature of 200 ° C or below.

The drying process S40 will be explained in detail below.

The drying process S40 may be a process of drying the mash-containing slurry prior to milling, and the water-soluble oil has been removed to a predetermined amount in the mash-containing slurry.

Here, when the niobium contained in the niobium-containing slurry is exposed to the air state for a predetermined time or longer, the niobium is oxidized by oxygen in the air to generate cerium oxide. Therefore, the exothermic property of the heating agent or the composition adjustment efficiency of the molten steel can be deteriorated.

Therefore, to prevent this limitation, the drying process of the mash-containing slurry is carried out at a temperature of 200 ° C or below, or more specifically at a temperature of about 110 ° C to about 130 ° C under an air or nitrogen atmosphere. When the mash-containing slurry is dried under a nitrogen atmosphere, the drying temperature can be increased to a high temperature without ruthenium oxide, and thus the drying rate can be faster, and the drying rate can be increased.

In the milling process (S50), the mash-containing slurry formed in the form of a block formed by the drying process (S40) is supplied to a mill 70 and then milled. The milling process (S50) can be selectively performed as needed.

For example, in the milling process (S50), the dried mash-containing slurry can be ground into particles having a diameter of about 5 cm or less. After the milling process (S50), a cerium-containing powder which is one of the intermediate products was obtained. Here, the powder may have a regular or irregular form.

Next, in the brick forming process (S60), a binder is added to the aid The cerium-containing powder obtained by the milling process (S50) is stirred to agitate the mixture. Next, a process of forming the mixture into a brick by using a brick forming device 80 is performed. Here, although a process of forming a brick by drying and milling the mash-containing slurry and using the cerium-containing powder is described, the brick can be formed by using a mash-containing slurry when the drying and milling process is not performed.

The brick forming process (S60) will be described in detail below.

Referring to Fig. 5, the brick forming process (S60) may include processes (S62, S64, and S66).

In the process (S62), a process of adding a Fe source and a binder to the ruthenium-containing binder obtained by the milling process (S50) is performed.

The addition of the Fe source is optional, and one of the reasons for adding the Fe source is to adjust the specific gravity of the last fabricated brick. During the steel making process of the steelmaking process, the bricks used to raise the temperature and adjust the composition of the final product made according to an exemplary embodiment are placed in a converter. When the specific gravity of the brick is too low, the brick cannot penetrate into the molten steel and thus float on the surface of the molten steel to deteriorate the temperature increase efficiency and composition adjustment efficiency.

Therefore, a Fe source is added to the cerium-containing powder. Here, the Fe source can be selectively added, and the Fe source can be sorted from the steel slag by means of a sorting process (eg, magnetic separation).

For example, in the brick forming process (S60), the bricks may be set to have from about 35% by weight to about 97% by weight, based on the total weight of the cerium-containing powder, Fe source, and binder, of cerium-containing powder, about 0% by weight to 50% by weight of the Fe source, and from about 3% by weight to about 15% by weight of the binder. Here, about 0% by weight of the Fe source indicates that the Fe source is not added.

The binder added in the process (S62) is used to form bricks by imparting viscosity to the cerium-containing powder or the powder containing cerium and Fe sources and may include syrup, starch, bentonite and hydroxide. At least one of calcium, and sodium citrate.

Moreover, the binder may further comprise at least one of water and water-soluble oil separated in the primary or secondary oil cleaning process or water-soluble oil and water separated in the separation process.

The mixing ratio between the materials forming the binder may vary depending on the circumstances, and water, a water-soluble oil, or both of the water and the water-soluble oil may be mixed with the binder.

For example, when water and a water-soluble oil are mixed and used in a binder, water and water-soluble oil separated from the initial waste slurry by the primary oil cleaning process (S10) can be reused as a material contained in the binder. .

In another example, when the binder is used by mixing with water, the water separated from the water-soluble oil by the separation process (S20) can be reused as a material contained in the binder. In this case, a part of Si may be oxidized to become SiO ₂ , thereby deteriorating the efficiency of the brick for raising the temperature and adjusting the composition in the final process. When a binder is used by mixing with water, a minimum amount of water can be mixed with the binder to form a brick, thereby preventing oxidation of Si.

In another example, when the binder is used by mixing with a water-soluble oil, the water-soluble oil separated from the water by the separation process (S20) can be reused as a material contained in the binder. As described above, when the binder is mixed with a water-soluble oil other than water, Si oxidation can be prevented.

In the process (S64), a process of stirring and sufficiently mixing one of the binder-containing cerium-containing powder or the composition containing the cerium and Fe source powder is performed. Of course, for agitation, the brick forming device 80 may have a self-stirring function, or a separate agitator may be used as the brick forming device 80.

In the process (S66), by using the brick forming device 80, the cerium-containing powder to which the binder is added and stirred, or the powder containing cerium and Fe source is formed to have one of the specific forms. One of the bricks.

According to one embodiment described above, the ruthenium-containing waste slurry produced during the manufacture of the semiconductor or solar wafer can be purified to form a powder, and then a binder can be added to the powder to form the brick by means of a compact. Here, the brick for raising the temperature of the molten steel and adjusting the composition in the steel making process can be produced at low cost and high efficiency.

In addition, the waste slurry for environmental pollution can be recycled and used in steelmaking plants in steel mills to raise the temperature of the molten steel and adjust the composition without burning or burying. Therefore, the disposal cost of waste products can be reduced, and the price competitiveness can be improved by cost reduction. In addition, environmental pollution that can occur during the steelmaking process can be minimized.

Waste water containing water-soluble oil and water formed in the pulverization process of the mash waste slurry can be used as an additive for making bricks. Therefore, it is not necessary to treat the discharged wastewater again, or the wastewater can be discharged after being purified to an amount that does not require further treatment. Thus, an environmentally friendly and economical method of making bricks for raising the temperature of the molten steel and adjusting the composition in the steelmaking process can be provided.

The water soluble oil can be reused by adding a water soluble oil rather than water to the binder used to maintain the viscosity of the cerium containing powder during the brick making process. Therefore, it is possible to provide a method of fabricating a brick for raising the temperature and adjusting the composition, which prevents deterioration of quality due to oxidation of ruthenium.

The mash waste slurry can be pulverized and then formed into the brick. Therefore, the brick can be easily placed in a converter in a steelmaking process and removes the risk of fire or explosion caused by the powder.

Moreover, the tantalum powder regarded as waste can be formed into a brick product for raising the temperature of the molten steel in the steel making process and adjusting the composition. Therefore, there is a role of being free from regulations (for example, regarding the operation of waste products in various places, etc.).

According to an exemplary embodiment, generated during the manufacture of a semiconductor or solar wafer The cerium-containing waste slurry can be purified to form a powder, and then the binder can be added to the powder to form a brick in the steelmaking process for raising the temperature of the molten steel and adjusting the composition by means of the compact, thereby reducing the steelmaking cost.

Moreover, the mash slurry for environmental pollution can be recycled and used in steelmaking plants in steel mills to raise the temperature of the molten steel and adjust the composition without burning or burying. Therefore, the disposal cost of waste products can be reduced, and the price competitiveness can be improved by cost reduction. In addition, environmental pollution that can occur during the steelmaking process can be minimized.

Waste water containing water-soluble oil and water formed in the pulverization process of the mash waste slurry can be used as an additive for making bricks. Therefore, it is not necessary to treat the discharged wastewater again, or the wastewater can be discharged after being purified to an amount that does not require further treatment. Therefore, bricks used to raise the temperature of the molten steel and adjust the composition in the steel making process can be produced environmentally friendly and economically.

The water-soluble oil can be reused by adding a water-soluble oil instead of water to the binder used to maintain the viscosity of the cerium-containing powder during the brick making process to prevent deterioration of product quality.

The mash slurry can be pulverized and then formed into bricks. Therefore, the brick can be easily placed in a converter in a steelmaking process and removes the risk of fire or explosion caused by the powder.

Moreover, the tantalum powder regarded as waste can be formed into a brick product for raising the temperature of the molten steel in the steel making process and adjusting the composition. Therefore, there is a role of being free from regulations (for example, regarding the operation of waste products in various places, etc.).

Although the essential features of the invention have been described with reference to the drawings, they are merely exemplary embodiments and are not intended to limit the invention. In addition, it should be readily understood that various modifications and changes can be made by those skilled in the art without departing from the spirit and scope of the invention.

S10, S20, S30, S40, S50‧‧ steps

Claims (16)

A method for producing a brick, the method comprising: preparing a mash-containing waste slurry; performing a primary oil cleaning process for separating the mash-containing slurry and the water-soluble oil from the mash-containing waste slurry; The brick is formed by using a mixture of one of the binder and the mash-containing slurry. The method of claim 1, wherein the ruthenium-containing waste slurry is formed when the ruthenium ingot is cut or polished on one of the surfaces of the wafer, and the mash-containing slurry and the water-soluble oil are contained. The method of claim 2, wherein the cerium-containing waste slurry contains at least cerium (Si) and cerium carbide (SiC). The method of claim 2, wherein the primary oil cleaning process comprises: mixing water and the cerium-containing waste slurry at a first mixing ratio; agitating the cerium-containing waste slurry and the water; and filtering the cerium-containing slurry And the mixture of the water to separate the cerium-containing waste slurry, the water-soluble oil, and the water from each other. The method of claim 4, wherein the first mixing ratio of the water to the volume of the cerium-containing waste slurry corresponds to from about 0.2 times to about 8 times. The method of claim 1, further comprising performing a secondary oil cleaning process for removing the water-soluble oil from the mash-containing slurry prior to forming the brick. The method of claim 6, wherein the secondary oil cleaning process comprises: mixing the water with the mash-containing slurry at a second mixing ratio; agitating the mash-containing slurry and the water; The mash-containing slurry and the mixture of the water are filtered to separate the mash-containing slurry, the water-soluble oil, and the water. The method of claim 7, wherein the second mixing ratio of the water to the volume of the cerium-containing waste slurry corresponds to from about 0.2 times to about 8 times. The method of claim 1, further comprising performing fractionation on the water-soluble oil and the water separated from each other in the primary oil cleaning process to separate the water-soluble oil from the water after the primary oil cleaning process. The method of claim 1, further comprising performing at least one of a mash-containing slurry drying process and a mash-containing slurry milling process prior to forming the brick. The method of claim 5, wherein in the forming of the brick, a source of Fe is selectively added to the mixture of the mash-containing slurry and the binder during the formation of the brick. The method of claim 11, wherein the mixture contains from about 35% by weight to about 97% by weight of the cerium-containing slurry, from about 0% by weight to about 50% by weight of the Fe source, based on the total weight of the mixture, and From about 3% by weight to about 15% by weight of the binder. The method of claim 12, wherein the binder comprises at least one of syrup, starch, bentonite, calcium hydroxide, and sodium citrate. The method of claim 13, wherein the binder comprises the water and water-soluble oil separated in the primary oil cleaning process, the water and water-soluble oil separated in the secondary oil cleaning process, and And separating at least one of the water-soluble oil and water separated in the process. A brick produced by the production method according to any one of claims 1 to 14, which comprises niobium, tantalum carbide, and a binder. The brick of claim 15 further comprises a source of Fe.