CN111893424B - Plate blank surface iron scale heating control method based on hot-conveying and hot-charging process - Google Patents

Plate blank surface iron scale heating control method based on hot-conveying and hot-charging process Download PDF

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CN111893424B
CN111893424B CN202010616409.1A CN202010616409A CN111893424B CN 111893424 B CN111893424 B CN 111893424B CN 202010616409 A CN202010616409 A CN 202010616409A CN 111893424 B CN111893424 B CN 111893424B
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heating
section
oxidation
slab
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CN111893424A (en
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魏兵
尹云洋
张扬
梁文
张鹏武
谭佳梅
徐峰
王立新
王世森
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Wuhan Iron and Steel Co Ltd
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    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
    • C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
    • C23C8/10—Oxidising
    • C23C8/12—Oxidising using elemental oxygen or ozone
    • C23C8/14—Oxidising of ferrous surfaces
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
    • C23C8/08—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases only one element being applied
    • C23C8/10—Oxidising
    • C23C8/16—Oxidising using oxygen-containing compounds, e.g. water, carbon dioxide
    • C23C8/18—Oxidising of ferrous surfaces

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  • Engineering & Computer Science (AREA)
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  • Organic Chemistry (AREA)
  • Manufacturing Of Steel Electrode Plates (AREA)
  • Metal Rolling (AREA)

Abstract

A slab surface iron scale heating control method based on a hot-feeding and hot-charging process comprises the following steps: dividing the interior of the heating furnace into a preheating section, a heating section and a soaking section in sequence; acquiring a parabolic oxidation rule formula corresponding to the heating section and a linear oxidation rule formula corresponding to the soaking section; calculating the critical oxygen concentration according to the parabolic oxidation law formula and the linear oxidation law formula; introducing a first heating atmosphere into the preheating section, introducing a second heating atmosphere into the heating section, and introducing a third heating atmosphere into the soaking section; conveying the slabs into the preheating section to preheat the slabs; conveying the slab into the heating section for a first oxidation thereof; transporting the mat into the soaking section for a second oxidation thereof. The invention does not need to modify the existing production line, only needs to optimize the heating process parameters and control the heating temperature of the atmosphere in the furnace and the corresponding section, is simple and easy to implement and has general popularization significance.

Description

Plate blank surface iron scale heating control method based on hot-conveying and hot-charging process
Technical Field
The invention belongs to the technical field of steel manufacturing for hot rolled strips, and particularly relates to a slab surface iron scale heating control method based on a hot-feeding hot-charging process.
Background
The continuous casting billet hot-feeding hot charging and direct rolling are a new process and a new technology which are developed by integrating the latest technical achievements of steel making, continuous casting and steel rolling in recent years, promote the integrated process of the production management of steel making, continuous casting and steel rolling, can obtain the comprehensive benefits of energy conservation, consumption reduction, product quality and productivity improvement and the like, and are continuously improved in proportion of application in steel enterprises. According to the introduction of data, only the hot-feeding and hot-charging process is adopted, the fuel consumption can be reduced by 45%, and the production cost can be reduced by about 30-60 yuan/ton. In the continuous low-level steel market and the current situation that various large steel plants fight for survival, energy conservation, consumption reduction, cost reduction and efficiency improvement are particularly important, so that a plurality of steel enterprises carry out deep research and integrated innovation on heating furnace process technologies and equipment for hot charging and direct rolling. The heating furnace has the advantages that the heating furnace is flexible to operate and accurate to control, can be used for reheating high-temperature casting blanks and directly heating cold blanks by combining the characteristics of key factors such as continuous casting, steel-making plane arrangement, equipment configuration and the like, meets the requirements of direct rolling continuity and quick passing performance of slabs, and realizes energy conservation and consumption reduction.
The hot charging or direct charging process has higher requirements on the overall coordination capacity of steel enterprises, and manufacturing management departments, hot rolling plants, steel mills and sales centers are often required to be in seamless connection, but the process is difficult to achieve in the actual production organization process, and a large part of steel billets still enter a furnace in a cold charging mode. The hot history of the plate blank charged into the furnace by cold charging is completely different from that of hot charging, the heating requirements are different, meanwhile, the temperature of the cold charging plate blank is above 400 ℃, a layer of thicker iron oxide scale exists on the surface of the plate blank, and if the subsequent heating process is not proper, the serious quality problem of the final product can be caused. Therefore, a system research of a slab heating process needs to be carried out aiming at the hot-feeding hot-charging process, a proper heating process needs to be formulated, the problem of surface defects of the slab is solved, and the surface quality of the slab is improved.
Disclosure of Invention
In view of the above problems, the present invention provides a method for controlling the heating of scale on the surface of a slab based on a hot-charging process, which overcomes or at least partially solves the above problems.
In order to solve the technical problem, the invention provides a slab surface iron scale heating control method based on a hot-delivery hot-charging process, which comprises the following steps:
dividing the interior of the heating furnace into a preheating section, a heating section and a soaking section in sequence;
acquiring a parabolic oxidation rule formula corresponding to the heating section and a linear oxidation rule formula corresponding to the soaking section;
calculating the critical oxygen concentration according to the parabolic oxidation law formula and the linear oxidation law formula;
introducing a first heating atmosphere into the preheating section, introducing a second heating atmosphere into the heating section, and introducing a third heating atmosphere into the soaking section;
conveying the slabs into the preheating section to preheat the slabs;
conveying the slab into the heating section for a first oxidation thereof;
transporting the mat into the soaking section for a second oxidation thereof.
Preferably, the formula of the parabolic oxidation law is as follows:
Figure BDA0002559128990000021
wherein, W represents the scale oxidation increment, Kp represents the speed constant of the parabolic oxidation law, and t represents time.
Preferably, the linear oxidation law formula is as follows:
W＝K1*Po2*t
where W represents the increase in scale, K1 represents the rate constant of the linear oxidation law, Po2 represents the oxygen concentration, and t represents time.
Preferably, the formula of the critical oxygen concentration is:
Po2lin＝7.519*Kp/(2*G*K1)
wherein, it represents critical oxygen concentration, Kp represents parabolic oxidation rate constant, G represents thickness of iron scale, and K1 represents linear oxidation rate constant.
Preferably, said conveying of slabs into said preheating section for preheating thereof comprises the steps of:
keeping the charging temperature of the plate blank to be more than or equal to 400 ℃;
the plate blank is heated by using the flue gas to recover the waste heat;
keeping the heating time of the preheating section at 40-60 min;
the temperature of the end section of the preheating section is maintained at 700-1000 ℃.
Preferably, before the step of maintaining the charging temperature of the slab to be more than or equal to 400 ℃, the method further comprises the following steps:
connecting the heating section and the soaking section with the preheating section respectively;
recovering the flue gas waste heat generated in the heating section and the soaking section into the preheating section;
and heating the plate blank in the preheating section by using the residual heat of the flue gas.
Preferably, said conveying of said slabs into said heating section for a first oxidation thereof comprises the steps of:
introducing the second heating atmosphere into the heating section;
keeping the heating time of the heating section at 65-80 min;
keeping the end temperature of the heating section at 1200-1300 ℃;
and keeping the temperature of the slab uniform, wherein the temperature gradient in the slab is less than or equal to 20 ℃.
Preferably, the second heating atmosphere comprises: the air-fuel ratio is 1.05-1.25, the oxygen content is more than or equal to the critical oxygen concentration, H2O content of 15% or more, CO2Content of not less than 8%, N2The content is 71-74%.
Preferably, said conveying of said slab into said soaking section for a second oxidation thereof comprises the steps of:
introducing the third heating atmosphere into the soaking section;
keeping the temperature gradient between the soaking section and the tail end of the heating section to be less than or equal to 20 ℃;
keeping the heating time of the soaking section at 25-40 min;
keeping the end temperature of the soaking section at 1200-1300 ℃;
and keeping the temperature of the slab uniform, wherein the temperature gradient in the slab is less than or equal to 20 ℃.
Preferably, the third heating atmosphere comprises: the air-fuel ratio is 0.90-1.0, the oxygen content is less than or equal to the critical oxygen concentration, H2O content of 10-15%, CO2Content of 6-8%, N2The content is 71-74%.
One or more technical solutions in the embodiments of the present invention have at least the following technical effects or advantages:
(1) according to the invention, the critical oxygen concentration in the heating furnace is determined according to the oxidation rule of the plate blank, the oxygen concentration of each section in the heating process is reasonably controlled, the plate blank is subjected to oxidation according to the designed oxidation rule, and finally, an iron scale structure mainly comprising FeO is realized;
(2) the invention does not need to modify the existing production line, only needs to optimize the heating process parameters and control the heating temperature of the atmosphere in the furnace and the corresponding section, is simple and easy to implement and has general popularization significance.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments are briefly introduced below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings based on the drawings without creative efforts.
Fig. 1 is a schematic diagram of surface scale on a discharged plate blank obtained by using a plate blank surface scale heating control method based on a hot charging process provided by an embodiment of the invention;
FIG. 2 is a schematic diagram of the surface scale of a discharged slab obtained by a conventional heating process in the prior art.
Detailed Description
The present invention will be described in detail below with reference to specific embodiments and examples, and the advantages and various effects of the present invention will be more clearly apparent therefrom. It will be understood by those skilled in the art that these specific embodiments and examples are for the purpose of illustrating the invention and are not to be construed as limiting the invention.
Throughout the specification, unless otherwise specifically noted, terms used herein should be understood as having meanings as commonly used in the art. Accordingly, unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. If there is a conflict, the present specification will control.
Unless otherwise specifically stated, various raw materials, reagents, instruments, equipment and the like used in the present invention are commercially available or can be prepared by existing methods.
In the embodiment of the application, the application provides a slab surface iron scale heating control method based on a hot-delivery hot-charging process, and the method comprises the following steps:
dividing the interior of the heating furnace into a preheating section, a heating section and a soaking section in sequence;
acquiring a parabolic oxidation rule formula corresponding to the heating section and a linear oxidation rule formula corresponding to the soaking section;
calculating the critical oxygen concentration according to the parabolic oxidation law formula and the linear oxidation law formula;
introducing a first heating atmosphere into the preheating section, introducing a second heating atmosphere into the heating section, and introducing a third heating atmosphere into the soaking section;
conveying the slabs into the preheating section to preheat the slabs;
conveying the slab into the heating section for a first oxidation thereof;
transporting the mat into the soaking section for a second oxidation thereof.
When the plate blank is in the heating section, sufficient oxygen required by oxidation reaction is contained in the atmosphere gas in the furnace, the oxidation speed of the plate blank is determined by the diffusion of iron ions at high temperature, the oxidation speed is high at the moment, and the oxidation is carried out according to a parabolic oxidation rule formula, wherein the parabolic oxidation rule formula is as follows:
Figure BDA0002559128990000041
wherein, W represents the scale oxidation increment, Kp represents the speed constant of the parabolic oxidation law, and t represents time.
Further, Kp can be calculated by the following formula:
Figure BDA0002559128990000042
where Kpo is 0.60g2/(cm2 · s), E represents activation energy, R represents a gas constant, and T represents temperature.
Under the condition of high oxygen concentration, the surface of the slab can obtain a typical three-layer iron scale structure (the outermost layer Fe)2O3Middle layer Fe3O4And the innermost layer FeO).
When the slab is in the soaking section, along with the continuous oxidation of slab, its surface scale thickness is more and more thick, can't supply sufficient oxygen from outermost scale to the innermost scale (being close to the base member), and high temperature scale is under the low oxygen concentration condition, and the oxidation rate mainly is supplied with the decision by the oxygen in the iron sheet, and the oxidation rate is slower, and the oxidation law goes on with mild straight line oxidation law formula, straight line oxidation law formula is:
W＝K1*Po2*t
wherein W represents the scale increase, K1 represents the linear oxidation rate constant (9.6 x 10-6 g/(cm-2. cndot. s)), Po2 represents the oxygen concentration, and t represents time.
In the process, the high-valence oxides continuously lose oxygen, and finally, an iron scale structure mainly containing FeO is obtained, and little Fe304 and Fe203 or no Fe304 and Fe203 exist in the iron scale.
The transition from high oxygen concentration to low oxygen concentration is critical and requires accurate calculation of the critical oxygen concentration. The oxygen concentration critical point is calculated by equalizing the high oxygen concentration atmosphere condition in which oxidation is performed according to the parabolic oxidation law formula and the low oxygen concentration atmosphere condition in which oxidation is performed according to the linear oxidation law formula, as shown below,
Figure BDA0002559128990000051
the following relationship exists between the thickness of the iron scale and the oxidation increment:
W＝G/7.519，
wherein G represents the thickness (um) of the scale.
Therefore, the critical oxygen concentration at the intersection of the high oxygen concentration and the low oxygen concentration atmosphere can be calculated by the above formula:
Po2lin＝7.519*Kp/(2*G*K1)
wherein, it represents critical oxygen concentration, Kp represents parabolic oxidation rate constant, G represents thickness of iron scale, and K1 represents linear oxidation rate constant.
This formula shows that the critical oxygen concentration is not only dependent on the oxygen supply in the furnace, but also closely related to the thickness of the scale and the temperature of the furnace. Therefore, during the actual rolling process of the slab, the heating process parameters are established according to the principle, and a thin and single iron oxide scale structure is generated on the surface of the slab.
Firstly, calculating the critical oxygen concentration in the heating furnace according to the formula so that the oxygen concentration of the heating section and the soaking section meets certain requirements: in the heating section, the oxygen content is required to be not more than equal, and in the soaking section, the oxygen content is required to be not more than equal. And then, according to the specific requirements of each section such as temperature, time and the like, reasonably setting the process parameters of each heating stage to meet the final requirements. Meanwhile, certain water vapor is generated in the heating oxidation process, the oxygen concentration of the water vapor can affect the surface of the plate blank, and the concentration of the water vapor in the furnace also needs to be strictly controlled.
In an embodiment of the application, said conveying the slabs into said preheating section for preheating thereof comprises the steps of:
keeping the charging temperature of the plate blank to be more than or equal to 400 ℃;
the plate blank is heated by using the flue gas to recover the waste heat;
keeping the heating time of the preheating section at 40-60 min;
the temperature of the end section of the preheating section is maintained at 700-1000 ℃.
In the embodiment of the application, before the step of maintaining the charging temperature of the slab to be more than or equal to 400 ℃, the method further comprises the following steps:
connecting the heating section and the soaking section with the preheating section respectively;
recovering the flue gas waste heat generated in the heating section and the soaking section into the preheating section;
and heating the plate blank in the preheating section by using the residual heat of the flue gas.
In the embodiment of the application, the slab in the preheating section can be preheated by using the waste heat of the tail gas generated by heating in the heating section and the soaking section, so that on one hand, the waste heat of the tail gas can be utilized to improve the utilization efficiency of energy; on the other hand, resources such as heating gas can be saved.
In an embodiment of the present application, said conveying said slab into said heating section for a first oxidation thereof comprises the steps of:
introducing the second heating atmosphere into the heating section; wherein the air-fuel ratio of the second heating atmosphere is 1.05-1.25, the oxygen content is greater than or equal to the critical oxygen concentration, and H2O content of 15% or more, CO2Content of not less than 8%, N2The content is 71% -74%;
keeping the heating time of the heating section at 65-80 min;
keeping the end temperature of the heating section at 1200-1300 ℃;
and keeping the temperature of the slab uniform, wherein the temperature gradient in the slab is less than or equal to 20 ℃.
In the embodiment of the application, the conveying the slab into the soaking section to carry out the second oxidation comprises the following steps:
introducing the third heating atmosphere into the soaking section; wherein the air-fuel ratio of the third heating atmosphere is 0.90-1.0, the oxygen content is less than or equal to the critical oxygen concentration, and H2O content of 10-15%, CO2Content of 6-8%, N2The content is 71% -74%;
keeping the temperature gradient between the soaking section and the tail end of the heating section to be less than or equal to 20 ℃;
keeping the heating time of the soaking section at 25-40 min;
keeping the end temperature of the soaking section at 1200-1300 ℃;
and keeping the temperature of the slab uniform, wherein the temperature gradient in the slab is less than or equal to 20 ℃.
The present application is described in detail below with specific examples.
Example 1:
in the actual production process of hot rolling, the critical oxygen concentration in the heating furnace is calculated according to the above formula. The critical oxygen concentration is 5 percent, and the oxygen content in the heating section is not less than Po2linIn the soaking zone, the oxygen content is required to be less than or equal to Po2lin. And (4) calculating according to the specific temperature and time of each section, and reasonably formulating the process parameters of each heating stage.
Combining the specific parameters of the heating furnace of the hot rolling 2250 production line, the process key points and the furnace atmosphere requirements of each section are as follows:
(1) preheating section
The feeding temperature of the plate blank is 400 ℃, a burner is not arranged in the preheating section of the heating furnace, the high-temperature plate blank is preheated by utilizing the recovered flue gas waste heat, the temperature of the plate blank is mainly improved through heat radiation, no fuel gas is supplied in the stage, the oxidation weight gain is not obvious, the heating time of the preheating section is 60min, and the temperature of the preheating tail section is 850 ℃.
(2) Heating section
The slab is required to be oxidized by a parabolic oxidation law formula, and the structure of the obtained iron scale is a typical three-layer structure (the outermost layer Fe203, the middle layer Fe304 and the innermost layer FeO). The atmosphere in the furnace needs to be under the condition of high oxygen concentration, and the specific parameters to be met are as follows: the air-fuel ratio of the atmosphere in the furnace was 1.25, the oxygen content was 5.5%, and H2O content 15%, CO2Content 8%, N2The content is 71%, the heating time is 70min, the temperature of the tail end of the heating section is 1280 ℃, the temperature of the plate blank is uniform, and the temperature gradient in the plate blank is 10 ℃.
(1) Soaking section
The slab is required to be oxidized by a relatively gentle linear oxidation law formula to obtain an iron scale structure mainly comprising FeO, the furnace atmosphere needs to be in a low oxygen concentration condition, and the specific parameters needed to be met are as follows: air-fuel ratio of furnace atmosphere was 0.90, oxygen content was 3%, H2O content 12%, CO2Content 8%, N2The content is 74 percent, the temperature gradient between the tail ends of the soaking section and the heating section is 10 ℃, the heating time of the soaking section is 30min, the temperature is uniform, the temperature gradient in the plate blank is less than or equal to 15 ℃, and the tapping temperature is 1280 ℃.
By adopting the heating process, the oxidation rate of the surface of the plate blank is low, the thickness of the obtained iron scale is small and is about 1.5cm, and meanwhile, the iron scale structure is mainly FeO, so that the iron scale with the thickness and the structure is beneficial to being completely removed in descaling before rough rolling.
Example 2:
in the actual production process of hot rolling, the critical oxygen concentration in the heating furnace is calculated according to the above formula. The critical oxygen concentration is 3 percent, and the oxygen content in the heating section is not less than Po2linIn the soaking zone, the oxygen content is required to be less than or equal to Po2lin. And (4) reasonably formulating the process parameters of each heating stage according to the specific temperature and time calculation of each stage.
Combining the specific parameters of the heating furnace of the hot rolling 2250 production line, the process key points and the furnace atmosphere requirements of each section are as follows:
(1) preheating section
The feeding temperature of the plate blank is 600 ℃, a burner is not arranged in the preheating section of the heating furnace, the high-temperature plate blank is preheated by utilizing the recovered flue gas waste heat, the temperature of the plate blank is mainly improved through heat radiation, no fuel gas is supplied in the stage, the oxidation weight gain is not obvious, the heating time of the preheating section is 50min, and the temperature of the preheating tail section is 900 ℃.
(2) Heating section
The slab is required to be oxidized by a parabolic oxidation law formula, and the structure of the obtained iron scale is a typical three-layer structure (the outermost layer Fe203, the middle layer Fe304 and the innermost layer FeO). The atmosphere in the furnace needs to be under the condition of high oxygen concentration, and the specific parameters to be met are as follows: the air-fuel ratio of the atmosphere in the furnace was 1.20, the oxygen content was 4.0%, and H was2O content 16%, CO2Content 8%, N2The content is 72%, the heating time is 80min, the temperature at the tail end of the heating section is 1230 ℃, the temperature of the plate blank is uniform, and the temperature gradient in the plate blank is 10 ℃.
(3) Soaking section
The slab is required to be oxidized by a relatively gentle linear oxidation law formula to obtain an iron scale structure mainly comprising FeO, the furnace atmosphere needs to be in a low oxygen concentration condition, and the specific parameters needed to be met are as follows: the air-fuel ratio of the furnace atmosphere is 0.90, the oxygen content is 2 percent, and H2O content 12%, CO2Content 7% N2The content is 74 percent, the temperature gradient between the tail ends of the soaking section and the heating section is 10 ℃, the heating time of the soaking section is 35min, the temperature is uniform, the temperature gradient in the plate blank is 5 ℃, and the tapping temperature is 1250 ℃.
By adopting the heating process, the oxidation rate of the surface of the plate blank is low, the thickness of the obtained iron scale is small and is about 1.45cm, and meanwhile, the iron scale structure is mainly FeO, so that the iron scale with the thickness and the structure is beneficial to being completely removed in descaling before rough rolling.
Example 3:
in the actual production process of hot rolling, the critical oxygen concentration in the heating furnace is calculated according to the above formula. The critical oxygen concentration is 2 percent, and the oxygen content in the heating section is not less than Po2linIn the soaking zone, the oxygen content is required to be less than or equal to Po2lin. And (4) reasonably formulating the process parameters of each heating stage according to the specific temperature and time calculation of each stage.
Combining the specific parameters of the heating furnace of the hot rolling 2250 production line, the process key points and the furnace atmosphere requirements of each section are as follows:
(1) preheating section
The feeding temperature of the plate blank is 700 ℃, a burner is not arranged in the preheating section of the heating furnace, the high-temperature plate blank is preheated by utilizing the recovered flue gas waste heat, the temperature of the plate blank is mainly improved through heat radiation, no fuel gas is supplied in the stage, the oxidation weight gain is not obvious, the heating time of the preheating section is 40min, and the temperature of the preheating tail section is 1000 ℃.
(2) Heating section
The slab is required to be oxidized by a parabolic oxidation law formula, and the structure of the obtained iron scale is a typical three-layer structure (the outermost layer Fe203, the middle layer Fe304 and the innermost layer FeO). The atmosphere in the furnace needs to be under the condition of high oxygen concentration, and the specific parameters to be met are as follows: the air-fuel ratio of the furnace atmosphere was 1.15, the oxygen content was 3%, H2O content 12%, CO2Content 9%, N2The content is 73%, the heating time is 75min, the temperature at the tail end of the heating section is 1280 ℃, the temperature of the plate blank is uniform, and the temperature gradient in the plate blank is 10 ℃.
(3) Soaking section
The slab is required to be oxidized by a relatively gentle linear oxidation rule formula to obtain an iron scale structure mainly comprising FeO, the furnace atmosphere needs to be in a low oxygen concentration condition, and the specific parameters to be met are as follows: air-fuel ratio of furnace atmosphere was 0.90, oxygen content was 2%, H2O content 11%, CO2Content 8%, N2The content is 74%, the temperature gradient between the tail ends of the soaking section and the heating section is 10 ℃, the heating time of the soaking section is 35min, the temperature is uniform, the temperature gradient in the plate blank is 10 ℃, and the tapping temperature is 1230 ℃.
By adopting the heating process, the oxidation rate of the surface of the plate blank is low, the thickness of the obtained iron scale is small and is about 1.4cm, and meanwhile, the iron scale structure is mainly FeO, so that the iron scale with the thickness and the structure is beneficial to being completely removed in descaling before rough rolling.
Detailed description of the drawings 1-2:
as can be seen from figure 1, the surface scale of the discharged plate blank has a single structure, the thickness of the scale is 710-810 um, the thickness of the scale is thinner than that of the surface scale of the plate blank in the conventional process, and the interface between the scale and a matrix is complete, so that phosphorus removal is facilitated.
As can be seen from FIG. 2, in the conventional process, the iron scale on the surface of the discharged plate blank is partially broken, the thickness of the iron scale is 900-960 um, and the interface between the iron scale and the substrate is not flat, so that the removal of phosphorus is not facilitated.
The application provides a slab surface iron scale heating control method based on hot-delivery hot-charging process has the following advantages:
(1) according to the invention, the critical oxygen concentration in the heating furnace is determined according to the oxidation rule of the plate blank, the oxygen concentration of each section in the heating process is reasonably controlled, the plate blank is subjected to oxidation according to the designed oxidation rule, and finally, an iron scale structure mainly comprising FeO is realized;
(2) the invention does not need to modify the existing production line, only needs to optimize the heating process parameters and control the heating temperature of the atmosphere in the furnace and the corresponding section, is simple and easy to implement and has general popularization significance.
Finally, it should also be noted that the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. The terms "first", "second", etc. in the present invention can be understood as nouns.
While preferred embodiments of the present invention have been described, additional variations and modifications in those embodiments may occur to those skilled in the art once they learn of the basic inventive concepts. Therefore, it is intended that the appended claims be interpreted as including preferred embodiments and all such alterations and modifications as fall within the scope of the invention.
It will be apparent to those skilled in the art that various changes and modifications may be made in the present invention without departing from the spirit and scope of the invention. Thus, if such modifications and variations of the present invention fall within the scope of the claims of the present invention and their equivalents, the present invention is also intended to include such modifications and variations.

Claims (7)

1. A slab surface iron scale heating control method based on a hot-feeding and hot-charging process is characterized by comprising the following steps:
dividing the interior of the heating furnace into a preheating section, a heating section and a soaking section in sequence;
acquiring a parabolic oxidation rule formula corresponding to the heating section and a linear oxidation rule formula corresponding to the soaking section;
calculating the critical oxygen concentration according to the parabolic oxidation law formula and the linear oxidation law formula;
introducing a first heating atmosphere into the preheating section, introducing a second heating atmosphere into the heating section, and introducing a third heating atmosphere into the soaking section;
conveying the slabs into the preheating section to preheat the slabs;
conveying the slab into the heating section for a first oxidation thereof;
conveying the slab into the soaking section for a second oxidation thereof;
the formula of the parabola oxidation law is as follows:
Figure FDA0003638499050000011
wherein W represents the scale oxidation increment, Kp represents the speed constant of the parabolic oxidation law, and t represents time;
the formula of the linear oxidation rule is as follows:
W＝K1*Po2*t
wherein W represents the scale oxidation increment, K1 represents the linear oxidation rate constant, Po2Represents the oxygen concentration, t represents time;
the formula of the critical oxygen concentration is as follows:
Po2lin＝7.519*Kp/(2*G*K1)
wherein, it represents critical oxygen concentration, Kp represents parabolic oxidation rate constant, G represents thickness of iron scale, and K1 represents linear oxidation rate constant.
2. The method for controlling the heating of the scale on the surface of the slab based on the hot-feeding hot-charging process as claimed in claim 1, wherein the step of conveying the slab into the preheating section for preheating the slab comprises the steps of:
keeping the charging temperature of the plate blank to be more than or equal to 400 ℃;
the plate blank is heated by using the waste heat recovered by the flue gas;
keeping the heating time of the preheating section at 40-60 min;
the temperature of the end section of the preheating section is maintained at 700-1000 ℃.
3. The method for controlling the heating of the scale on the surface of the slab based on the hot charging process as claimed in claim 2, wherein the method further comprises the following steps before the step of keeping the charging temperature of the slab to be more than or equal to 400 ℃:
connecting the heating section and the soaking section with the preheating section respectively;
recovering the flue gas waste heat generated in the heating section and the soaking section into the preheating section;
and heating the plate blank in the preheating section by using the residual heat of the flue gas.
4. The method for controlling the heating of the scale on the surface of the slab based on the hot-charging process as claimed in claim 1, wherein the step of conveying the slab into the heating section for carrying out the first oxidation comprises the steps of:
introducing the second heating atmosphere into the heating section;
keeping the heating time of the heating section at 65-80 min;
keeping the end temperature of the heating section at 1200-1300 ℃;
and keeping the temperature of the slab uniform, wherein the temperature gradient in the slab is less than or equal to 20 ℃.
5. The slab surface scale heating control method based on the hot-delivery hot-charging process as claimed in claim 4, wherein the second heating atmosphere comprises: the air-fuel ratio is 1.05-1.25, the oxygen content is more than or equal to the critical oxygen concentration, H2O content of 15% or more, CO2Content of not less than 8%, N2The content is 71-74%.
6. The method for controlling the heating of the scale on the surface of the slab based on the hot charging process as claimed in claim 1, wherein the step of conveying the slab into the soaking section to carry out the second oxidation comprises the steps of:
introducing the third heating atmosphere into the soaking section;
keeping the temperature gradient between the soaking section and the tail end of the heating section to be less than or equal to 20 ℃;
keeping the heating time of the soaking section at 25-40 min;
keeping the end temperature of the soaking section at 1200-1300 ℃;
and keeping the temperature of the slab uniform, wherein the temperature gradient in the slab is less than or equal to 20 ℃.
7. The slab surface scale heating control method based on the hot-delivery hot-charging process as claimed in claim 1, wherein the third heating atmosphere comprises: the air-fuel ratio is 0.90-1.0, the oxygen content is less than or equal to the critical oxygen concentration, H2O content of 10-15%, CO2Content of 6-8%, N2The content is 71-74%.
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