Background
The mineral wool has excellent performances of heat preservation, heat insulation, sound insulation and the like, and is widely applied to various fields of national economy. Both natural rock and metallurgical slag can produce mineral wool. Because of the large production of the metallurgical waste slag and the increase of the environmental protection pressure, the resource utilization of the metallurgical slag to produce the mineral wool attracts more and more attention, wherein the ferroalloy smelting waste slag becomes a high-quality raw material for producing the mineral wool due to the high yield and the good cotton forming performance.
The manufacturing processes for mineral wool are divided into centrifugal and blowing processes, depending on the way in which the fibres are formed. The centrifugal method has the advantages of high production efficiency, good product quality and the like, is generally applied to industrial production, and the blowing method is mainly used for experimental research and small-scale production. The specific production process of mineral wool can be simplified as follows: 1. tempering and melting raw materials; 2. centrifuging or blowing to form fiber; 3, collecting cellucotton; 4, subsequent process of product preparation. Regardless of the process and feedstock, complete melting of the slag is a necessary process. The raw materials are heated to a molten state, the energy consumption is huge, and the higher the temperature of the molten state is, the larger the energy consumption is, and the larger the loss of refractory materials and the like is.
At present, the quenching and tempering and melting of raw materials are mainly carried out by an electric arc furnace in the production of mineral wool. The heating principle of the electric furnace is that the graphite electrode and the consumed electric energy are utilized for electric arc heating, compared with the traditional shaft furnace for melting raw materials, the electric furnace has higher heating efficiency and less carbon dioxide emission. In the actual production process of mineral wool, the slag raw material is firstly put into an electric furnace for heating and tempering, and meanwhile, in order to ensure the smooth production process, the final heating temperature, namely the end point melting temperature of the slag raw material is generally much higher than the melting temperature and the melting point of slag. As to how much the end point melting temperature is higher than the melting temperature, there is no scientific and accurate method, and empirical values are generally obtained by industrial practice. The cost of the electric furnace molten raw materials mainly comes from electricity consumption, furnace body refractory material loss and graphite electrode material consumption. However, all costs are directly related to the end point melting temperature of the raw material, and the higher the end point melting temperature, the longer the melting time, the greater the power consumption, and the more severe the erosion of the refractory and the electrode by the slag.
Therefore, the invention of a method is urgently needed to scientifically and accurately determine the end point melting temperature of the slag raw material in the process of producing mineral wool from ferroalloy slag, so that the ferroalloy slag can be used for obtaining mineral wool products with high quality and high efficiency at the lowest possible end point melting temperature. The method has great practical significance for guiding the production, efficient manufacturing and green manufacturing of the mineral wool.
Disclosure of Invention
Aiming at the problems in the prior art, the invention provides a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool from ferroalloy smelting waste slag.
The method disclosed by the invention is adopted for determining the smelting end point temperature, so that the end point melting temperature of the ferroalloy slag material can be accurately controlled, the smelting efficiency is greatly improved, the smelting power consumption is saved, and the loss of refractory materials is saved. Meanwhile, the method provided by the invention has the advantages of common detection instruments, simplicity and convenience in operation, strong adaptability, and accurate and scientific obtained data.
In order to achieve the technical purpose of the end point melting temperature, the invention discloses a method for determining the melting end point temperature of slag wool produced by ferroalloy smelting waste slag, which uses the following instruments and equipment: 1, hot wire equipment, 2, a high-temperature melt viscosity tester and 3, an infrared temperature measuring probe; the hot wire equipment is used for measuring the melting temperature interval (melting start temperature T) of the ferroalloy slagiComplete melting temperature Ta) The viscometer is used for the melting temperature T of the ferroalloy slagbDetermination that the infrared temperature probe is used for the differential temperature TcMeasurement of (temperature T of molten slag of iron alloy slag in electric furnace)dAnd the fiber forming temperature T of the slag when the slag reaches a centrifugal roller or a blowing openingxA difference of (i.e. T)c=Td-Tx) (ii) a After the temperature data is obtained, the lowest end point melting temperature which can ensure that qualified products can be produced is finally obtained by considering the compensation temperature and matching the iteration of the compensation temperature and the experiment.
The invention relates to a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool by using ferroalloy smelting waste residues; obtaining the complete melting temperature T of the ferroalloy smelting waste residueaObtaining the melting temperature T of the ferroalloy smelting waste residueb,
For the same batch of ferroalloy smelting waste slag raw materials, the temperature T of the molten slag in the electric furnace is carried out at least oncedAnd fiber forming temperature TeTest by Td-Te=TcCalculating to obtain Tc(ii) a When the same batch of ferroalloy smelting waste slag raw materials are tested for multiple times, TdAverage value of multiple tests, TeAlso the average of a number of tests, said TdGreater than or equal to Ta+200 ℃ and TdGreater than or equal to Tb+200 ℃; meanwhile, detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, and if the quality is qualified; the following steps are carried out; if not, adjusting TdUntil the quality of the obtained mineral wool is qualified, the method comprises the following steps:
definition of TBig (a)Is Ta、TbThe higher of the two;
the melting end point temperature T is calculated by the first theoryf1Is the melting temperature TBig (a)Plus a difference temperature TcIn addition to the compensation temperature Tg1I.e. Tf1=TBig (a)+Tc+Tg1(1) (ii) a At this time Tg1Any temperature greater than 0 degrees celsius; the operation then proceeds in two cases:
the first condition is as follows:
heating the same batch of ferroalloy smelting waste residue raw material to Tf1Producing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is qualified; further use of a value lower than Tg1Compensated temperature T ofg2Instead of Tg1Substituted into equation (1) to calculate and determine a temperature Tf2(ii) a Then heating the same batch of ferroalloy smelting waste residue raw material to Tf2Producing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is qualified; further use of a value lower than Tg2Compensated temperature T ofg3Instead of Tg2Substituted into equation (1) to calculate and determine a temperature Tf3(ii) a Repeating the operation until the compensation temperature is TgiWhen the quality of the obtained product is not qualified, then at TgiTo Tgi-1In the temperature interval of (3), selecting the experimental temperature from low to high; until a qualified product is obtained, the compensation temperature of the obtained qualified product is Tgi+nThe optimum compensation temperature is obtained; then at this time equation (1) becomes Tf=TBig (a)+Tc+Tgi+n(ii) a I is greater than or equal to 2, and n is greater than or equal to 1;
if at Tf2Producing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is unqualified; then at Tf1And Tf2Selecting the experimental temperature from low to high; until a qualified product is obtained, the compensation temperature of the obtained qualified product is Tg2+n(ii) a Namely the optimal compensation temperature; then at this time equation (1) becomes Tf=TBig (a)+Tc+Tg2+n(ii) a N is greater than or equal to 1;
case two:
heating the same batch of ferroalloy smelting waste residue raw material to Tf1Producing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is unqualified; further adopt a value higher than Tg1Compensated temperature T ofg2Instead of Tg1Substituted into equation (1) to calculate and determine a temperature Tf2(ii) a And at Tf2Producing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is qualified; then at Tf1And Tf2Selecting the experimental temperature from low to high; until a qualified product is obtained, the compensation temperature of the obtained qualified product is Tg2+n(ii) a Namely the optimal compensation temperature; then at this time equation (1) becomes Tf=TBig (a)+Tc+Tg2+n(ii) a N is greater than or equal to 1;
if at Tf2Producing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is unqualified; further adopt a value higher than Tg2Compensated temperature T ofg3Instead of Tg2Substituted into equation (1) to calculate and determine a temperature Tf3(ii) a And at Tf3Producing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is qualified; then at Tf2And Tf3From low to highSelecting an experiment temperature; until a qualified product is obtained, the compensation temperature of the obtained qualified product is Tg3+n(ii) a Namely the optimal compensation temperature; then at this time equation (1) becomes Tf=TBig (a)+Tc+Tg3+n(ii) a N is greater than or equal to 1; if T isfiProducing the mineral wool at the temperature, and detecting the quality of the obtained mineral wool according to the national standard GB/T11835-2016, if the quality is unqualified; continuing to increase the compensation temperature until the obtained product is qualified; at this time, the compensation temperature is Tgi(ii) a Then at Tgi andTgi-1in the formed interval, the experiment temperature is selected from low to high; until a qualified product is obtained, the compensation temperature of the obtained qualified product is Tgi+nThe optimum compensation temperature is obtained; then at this time equation (1) becomes Tf=TBig (a)+Tc+Tgi+n(ii) a I is not less than 3, and n is not less than 1.
The invention relates to a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool by using ferroalloy smelting waste slag, which is characterized in that a hot wire device is used for measuring a ferroalloy slag melting temperature interval, wherein the ferroalloy slag melting temperature interval is from the ferroalloy slag melting starting temperature to the complete melting temperature; the hot wire utilizing device has the functions of real-time imaging and temperature measurement. The start melting temperature and the complete melting temperature of the ferroalloy slag are determined. The method is not restricted by the type of hot wire equipment.
The invention relates to a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool by using ferroalloy smelting waste slag.
The invention relates to a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool by using ferroalloy smelting waste slag, wherein a 135-degree tangent line is tangent to a temperature-viscosity curve on the temperature-viscosity curve of the obtained ferroalloy smelting waste slag, and the tangent point temperature is the corresponding melting temperature Tb。
The invention relates to a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool from ferroalloy smelting waste slag, wherein the ferroalloy smelting waste slag is selected from one of waste slag generated in a silicomanganese alloy smelting process, waste slag generated in a ferronickel alloy smelting process and blast furnace slag.
The invention relates to a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool by using ferroalloy smelting waste slagiComplete melting temperature Ta) The method comprises the following specific operations: onset of melting temperature TiThe temperature corresponding to the moment when the liquid phase of the ferroalloy slag in the hot wire begins to generate, the complete melting temperature TaThe temperature corresponding to the moment when the ferroalloy slag is completely in the liquid phase.
In the present invention Ta、TbCan be obtained by a small trial.
The invention relates to a method for obtaining the lowest melting end point temperature in the process of producing qualified slag wool by using ferroalloy smelting waste slag, wherein the difference temperature T iscThe specific operation of the determination is as follows: the difference between the melting heat preservation temperature of the ferroalloy slag and the temperature measured by the infrared probe. In the present invention, T is obtained by one measurementcAfter that, consider TcIs a constant value. Because the model and the relative position of the equipment are completely fixed when the equipment is applied to a factory, the temperature drop of the equipment is generally not changed greatly when the equipment is guided to a roller or a nozzle although the temperature of the equipment is different during the melting and heat preservation. In order to reduce the rapid attainment of the lowest melting end point temperature, it is considered to be a constant value in the present invention.
The invention firstly obtains the complete melting temperature TaObtaining the melting temperature T of the ferroalloy smelting waste residuebThen comparing the two, taking the larger value T of the twoBig (a)As a reference for the next operation, T is obtained through one experimentc(ii) a Then searching for the optimal compensation temperature through an experiment and iteration method; according to TBig (a)+TcCalculating the lowest melting end point temperature in the process of producing qualified mineral wool by using the optimal compensation temperature; then verifying whether the lowest melting end point temperature can produce qualified slag wool or not; if not, the optimal compensation temperature obtained in the previous step is increased again to carry out verification experiment until qualified mineral wool is obtainedAt this time, the corresponding compensation temperature is the optimal compensation temperature.
Principles and advantages
The invention principle is as follows:
the temperature of the iron alloy slag in the electric furnace is not as high as possible in view of power consumption, loss of refractory, and production efficiency. On the contrary, on the premise of ensuring the quality production of the mineral wool, the lower the end point melting temperature, the more the economical efficiency of the production process can be ensured. The invention scientifically and accurately measures the melting temperature, the melting property temperature and other data of the slag by utilizing hot wire equipment and viscosity equipment; meanwhile, the temperature difference between the slag temperature in the electric furnace and the fiber forming temperature of the centrifugal roller or the airflow jet outlet area is measured by utilizing a preliminary experiment; and finally, searching the optimal compensation temperature by using an iterative method, and obtaining a calculation method and a formula for calculating the minimum production slag wool melting temperature. The method can scientifically and accurately obtain the lowest melting end point temperature in the process of producing qualified mineral wool from the ferroalloy smelting waste slag, thereby ensuring the high-quality production of the mineral wool and reducing the energy consumption and the cost in the production process.
The advantages of the invention are as follows:
1. accurate slag base temperature data is obtained. The slag temperature data based on the melting temperature, the solubility temperature, the difference temperature existing in the process and the like of the slag are obtained by utilizing equipment and methods such as hot wire equipment, viscosity equipment, pre-experiments and the like.
2. A calculation method and a formula of the minimum production slag wool melting temperature are established. The optimal compensation temperature is scientifically found out by utilizing an iterative method, and a calculation method and a formula for calculating the minimum production slag wool melting temperature are obtained through comprehensive analysis.
3. The power consumption is saved, and the refractory material and the electrode loss are reduced. The power consumption, the wear of the refractory and the wear of the electrode mainly depend on the temperature of the ferroalloy slag and the running time of the electric furnace, the accurate end point melting temperature can ensure that the temperature is as low as possible, the melting time is reduced, and the corrosion of the refractory caused by high-temperature slag is reduced.
Detailed Description
Ferronickel smelting waste residue and silicomanganese smelting waste residue are used as raw materials, and a spraying method and a centrifugal method are respectively used for carrying out experiments and production practices for producing mineral wool. The main components of the ferronickel slag and the silicomanganese slag are shown in tables 1 and 2. The invention is further illustrated by the following schematic and specific examples.
TABLE 1 main Components of ferronickel slag
FeO
|
SiO2 |
CaO
|
MgO
|
Al2O3 |
Cr2O3 |
6.71
|
48.41
|
5.45
|
30.07
|
4.21
|
1.54 |
TABLE 2 main composition of silicomanganese slag
SiO2 |
Al2O3 |
CaO
|
MnO
|
MgO
|
FeO
|
39.83
|
18.65
|
19.97
|
8.84
|
6.51
|
1.28 |
Example 1 (corresponding to case 1-1)
The implementation refers to the situation of producing mineral wool by using ferronickel slag as a raw material and utilizing an injection process, and takes part in figure 1. Measuring basic temperature: taking ferronickel smelting waste residues as raw materials, and respectively carrying out ferronickel slag melting temperature interval and melting temperature by utilizing hot wire equipment and a high-temperature melt viscometerThe measurement of (1) shows that the melting start temperature of the ferronickel slag is Ti1346 ℃ and a complete melting temperature Ta1509 deg.C, melting temperature Tb1431 ℃, see fig. 2 and 3. Measuring the differential temperature in a preliminary experiment: melting the nickel-iron slag in an electric furnace to 1709 deg.C, maintaining the temperature for 3min, reversing the furnace to remove slag, blowing to form cotton at 0.55Mpa, detecting the fiber forming temperature of the blowing port with infrared probe of 1628 deg.C, and calculating to obtain difference temperature TcThe detected slag wool quality is qualified when the temperature is 81 ℃, so that the difference temperature of the batch and the equipment under the process condition is determined as Tc81 ℃. Determining the optimal compensation temperature: setting Tg1=40℃,Tf1=TBig (a)+Tc+Tg1The temperature is 1509+81+40 ═ 1630 ℃, and the quality of the mineral wool is qualified; let Tg2=30℃,Tf2=TBig (a)+Tc+Tg2The quality of the slag wool is qualified when the temperature is 1509+81+ 20-1620 ℃; t isg3=10℃,Tf3=TBig (a)+Tc+Tg3The slag wool quality is unqualified when the temperature is 1509+81+ 10-1600 ℃; at Tf2And Tf3Selecting the temperature from low to high for re-testing; let Tg3+1=15℃,Tf=TBig (a)+Tc+Tg2+11605 deg.C, unqualified quality of mineral wool; let Tg3+2=20℃,Tf=TBig (a)+Tc+Tg2+2The quality of the slag wool is qualified when the temperature is 1610 ℃; t isg3+2At 20 deg.C, T is the optimum compensation temperaturef=TBig (a)+Tc+Tg3+21610 ℃. EXAMPLE Mass production: and (3) calculating the melting end point temperature of the same batch of ferronickel slag raw materials according to a formula to be 1610 ℃, and performing mineral wool production by using other process parameters and processes, wherein the product is qualified after detection. The quality detection standard and requirement of the mineral wool conform to the national standard GB/T11835-2016.
Example 2 (corresponding to cases 1-2)
The implementation refers to the situation of producing mineral wool by using ferronickel slag as a raw material and utilizing an injection process, and takes part in figure 1. Measuring basic temperature: hot wire equipment utilizing ferronickel smelting waste residues as raw materialsAnd a high-temperature melt viscosity meter is used for respectively measuring the melting temperature interval and the melting temperature of the ferronickel slag, and the measured result shows that the melting temperature of the ferronickel slag is Ti1346 ℃ and a complete melting temperature Ta1509 deg.C, melting temperature Tb1431 ℃, see fig. 2 and 3. Measuring the differential temperature in a preliminary experiment: melting the nickel-iron slag in an electric furnace to 1709 deg.C, maintaining the temperature for 3min, reversing the furnace to remove slag, blowing to form cotton at 0.55Mpa, detecting the fiber forming temperature of the blowing port with infrared probe of 1628 deg.C, and calculating to obtain difference temperature TcThe detected slag wool quality is qualified when the temperature is 81 ℃, so that the difference temperature under the conditions of the batch, the equipment and the process is determined as Tc81 ℃. Determining the optimal compensation temperature: setting Tg1=40℃,Tf1=TBig (a)+Tc+Tg1The temperature is 1509+81+40 ═ 1630 ℃, and the quality of the mineral wool is qualified; let Tg2=10℃,Tf2=TBig (a)+Tc+Tg2The slag wool quality is unqualified when the temperature is 1509+81+ 10-1600 ℃; at Tf1And Tf2Selecting the temperature from low to high for re-testing; let Tg2+1=15℃,Tf=TBig (a)+Tc+Tg2+11605 deg.C, unqualified quality of mineral wool; let Tg2+2=20℃,Tf=TBig (a)+Tc+Tg2+2The quality of the slag wool is qualified when the temperature is 1610 ℃; t isg2+2At 20 deg.C, T is the optimum compensation temperaturef=TBig (a)+Tc+Tg2+21610 ℃. EXAMPLE Mass production: and (3) calculating the melting end point temperature of the same batch of ferronickel slag raw materials according to a formula to be 1610 ℃, and performing mineral wool production by using other process parameters and processes, wherein the product is qualified after detection. The quality detection standard and requirement of the mineral wool conform to the national standard GB/T11835-2016.
Example 3 (corresponding case 2-1)
The implementation is directed to the case of producing mineral wool by using silicomanganese alloy slag as a raw material and utilizing a centrifugal process, and is shown in figure 4. Measuring basic temperature: the melting temperature of the silicomanganese slag is respectively carried out by taking silicomanganese smelting waste slag as raw materials and utilizing hot wire equipment and a high-temperature melt viscometerThe interval and the melting temperature are measured, and the measured result shows that the initial melting temperature of the silicomanganese slag is Ti1220 ℃ and a complete melting temperature Ta1345 ℃ and a melting temperature Tb1370 ℃, see fig. 5 and 6. Measuring the differential temperature in a preliminary experiment: heating and melting silicomanganese slag in an electric furnace to 1570 ℃, preserving heat for 3min, performing inverted furnace deslagging and centrifugal cotton forming operation, wherein the rotating speeds of four rollers are 1#2200r/min, 2#3300r/min, 3#4400r/min and 4#5800r/min respectively, the fiber forming temperature of the 1# centrifugal roller measured by an infrared probe is 1506 ℃, and calculating to obtain a difference temperature TcThe detected slag wool quality is qualified at 64 ℃, so that the difference temperature under the conditions of the batch, the equipment and the process is determined as TcAt 64 ℃. Determining the optimal compensation temperature: setting Tg1=10℃,Tf1=TBig (a)+Tc+Tg1The slag wool quality is unqualified when the temperature is 1370+64+ 10-1444 ℃; let Tg2=50℃,Tf2=TBig (a)+Tc+Tg2When the temperature is 1370+64+50, 1484 ℃, the quality of the mineral wool is qualified; at Tf1And Tf2Selecting the temperature from low to high for re-testing; let Tg2+1=15℃,Tf=TBig (a)+Tc+Tg2+11449 ℃, and the quality of the mineral wool is unqualified; let Tg2+2=20℃,Tf=TBig (a)+Tc+Tg2+2The quality of the mineral wool is unqualified at 1454 ℃; let Tg2+3=25℃,Tf=TBig (a)+Tc+Tg2+3The quality of the mineral wool is qualified at 1459 ℃; t isg2+5At 25 deg.C, T is the optimum compensation temperaturef=TBig (a)+Tc+T2+31459 ℃. EXAMPLE Mass production: and (3) calculating the melting end point temperature of 1459 ℃ according to a formula aiming at the same batch of silicomanganese slag raw materials, and carrying out mineral wool production by using other process parameters and processes as above, wherein the product is qualified after detection. The quality detection standard and requirement of the mineral wool conform to the national standard GB/T11835-2016.
Example 4 (corresponding to case 2-2)
The implementation is directed to the case of producing mineral wool by using silicomanganese alloy slag as a raw material and utilizing a centrifugal process, and is shown in figure 4.Measuring basic temperature: the melting temperature interval and the melting property temperature of the silicomanganese slag are respectively measured by using silicomanganese smelting waste slag as a raw material by using hot wire equipment and a high-temperature melt viscometer, and the measurement result shows that the melting starting temperature of the silicomanganese slag is Ti1220 ℃ and a complete melting temperature Ta1345 ℃ and a melting temperature Tb1370 ℃, see fig. 5 and 6. Measuring the differential temperature in a preliminary experiment: heating and melting silicomanganese slag in an electric furnace to 1570 ℃, preserving heat for 3min, performing inverted furnace deslagging and centrifugal cotton forming operation, wherein the rotating speeds of four rollers are 1#2200r/min, 2#3300r/min, 3#4400r/min and 4#5800r/min respectively, the fiber forming temperature of the 1# centrifugal roller measured by an infrared probe is 1506 ℃, and calculating to obtain a difference temperature TcThe detected slag wool quality is qualified at 64 ℃, so that the difference temperature under the conditions of the batch, the equipment and the process is determined as TcAt 64 ℃. Determining the optimal compensation temperature: setting Tg1=10℃,Tf1=TBig (a)+Tc+Tg1The slag wool quality is unqualified when the temperature is 1370+64+ 10-1444 ℃; let Tg2=20℃,Tf2=TBig (a)+Tc+Tg2The quality of the slag wool is unqualified when the temperature is 1370+64+ 20-1454 ℃; let Tg3=30℃,Tf3=TBig (a)+Tc+Tg3The temperature is 1464 ℃ when the temperature is 1370+64+30, and the quality of the mineral wool is qualified; at Tf2And Tf3Selecting the temperature from low to high for re-testing; let Tg3+1=25℃,Tf=TBig (a)+Tc+Tg3+1The quality of the mineral wool is qualified at 1459 ℃; t isg3+1At 25 deg.C, T is the optimum compensation temperaturef=TBig (a)+Tc+T3+11459 ℃. EXAMPLE Mass production: and (3) calculating the melting end point temperature of 1459 ℃ according to a formula aiming at the same batch of silicomanganese slag raw materials, and carrying out mineral wool production by using other process parameters and processes as above, wherein the product is qualified after detection. The quality detection standard and requirement of the mineral wool conform to the national standard GB/T11835-2016.