TWI697561B - Method for evaluating melting loss of bottom blowing hole of converter - Google Patents
Method for evaluating melting loss of bottom blowing hole of converter Download PDFInfo
- Publication number
- TWI697561B TWI697561B TW108119568A TW108119568A TWI697561B TW I697561 B TWI697561 B TW I697561B TW 108119568 A TW108119568 A TW 108119568A TW 108119568 A TW108119568 A TW 108119568A TW I697561 B TWI697561 B TW I697561B
- Authority
- TW
- Taiwan
- Prior art keywords
- converter
- temperature
- low temperature
- bottom blow
- blow hole
- Prior art date
Links
- 238000007664 blowing Methods 0.000 title claims abstract description 28
- 238000002844 melting Methods 0.000 title claims abstract description 27
- 230000008018 melting Effects 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims abstract description 26
- 230000036541 health Effects 0.000 claims abstract description 13
- 238000010079 rubber tapping Methods 0.000 claims description 9
- 238000004364 calculation method Methods 0.000 claims description 8
- 238000001931 thermography Methods 0.000 claims description 7
- 229910000831 Steel Inorganic materials 0.000 description 13
- 239000010959 steel Substances 0.000 description 13
- 238000010586 diagram Methods 0.000 description 10
- 230000000875 corresponding effect Effects 0.000 description 9
- 230000002159 abnormal effect Effects 0.000 description 5
- 230000008901 benefit Effects 0.000 description 3
- 239000011449 brick Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000002596 correlated effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000010223 real-time analysis Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Images
Landscapes
- Radiation Pyrometers (AREA)
Abstract
Description
本發明是有關於一種轉爐狀況之評估方法,且特別是有關於一種轉爐之底吹孔之熔損的評估方法。 The present invention relates to a method for evaluating the condition of a converter, and more particularly to a method for evaluating the melting loss of the bottom blow hole of the converter.
轉爐利用設置於其底部之底吹孔對爐內之鋼液進行吹氣攪拌處理,藉此可有效提高鋼液的均勻度。因此,透過底吹孔的吹氣攪拌處理在鋼液的精煉過程扮演非常重要的角色。然而,轉爐之底吹孔的狀況變化非常大,若底吹孔的凹陷過深或經由底吹孔所吹出之氣體流量異常,轉爐便隨時可能發生洩鋼的情況。 The converter utilizes the bottom blowing holes arranged at the bottom of the furnace to blow and stir the molten steel in the furnace, thereby effectively improving the uniformity of the molten steel. Therefore, the blowing and stirring process through the bottom blowing hole plays a very important role in the refining process of molten steel. However, the condition of the bottom blow hole of the converter changes greatly. If the bottom blow hole is too deep or the gas flow rate through the bottom blow hole is abnormal, the converter may leak steel at any time.
煉鋼廠一般使用雷射測厚儀來評估底吹殘厚。但雷射測厚儀之拍攝間隔太長,而無法即時分析底吹殘厚。舉例而言,一種轉爐爐襯與底吹孔熔損程度的評估技術係利用雷射測厚儀來量測轉爐之各位置之作業磚的殘厚。此技術係將裝載雷射裝置的台車移動至轉爐前方,雷射裝置再對轉爐內部逐一進行不同角度的掃描,並計算描繪出轉爐體各拍攝處的殘厚資料。當線上操作人員發現底吹孔周圍之作業磚 的最小厚度過小時,在隨後停爐時即可將此底吹孔予以封孔,使此底吹孔的熔損速率降至最低,以達到整個爐代結束時永久磚不外露的目標。 Steel mills generally use laser thickness gauges to assess bottom blown residual thickness. However, the shooting interval of the laser thickness gauge is too long to analyze the bottom blow residual thickness in real time. For example, a technique for evaluating the degree of melting loss of the converter lining and bottom blow holes is to use a laser thickness gauge to measure the residual thickness of the working bricks at each position of the converter. This technology moves the trolley loaded with the laser device to the front of the converter, and the laser device scans the interior of the converter one by one at different angles, and calculates and depicts the residual thickness data of each shooting location of the converter body. When the online operator found the work bricks around the bottom blow hole If the minimum thickness is too small, the bottom blow hole can be sealed when the furnace is subsequently shut down, so that the melt loss rate of the bottom blow hole can be minimized, so as to achieve the goal of not showing permanent bricks at the end of the entire furnace generation.
然而,每次利用雷射測厚儀進行拍攝時,需先將雷射測厚儀的設備定位,設備定位再加上後續的拍攝總共約需耗費20分鐘至30分鐘。因此,對於轉爐之雷射測厚的拍攝作業需在繁忙的生產期間找空檔進行。在爐代前期通常是大約每吹煉500爐會進行一次轉爐的雷射測厚拍攝,而在風險較高的爐代中後期則約每吹煉200爐至300爐進行一次轉爐的雷射測厚拍攝。因此,雷射拍攝的間隔最短也約需要1星期至2星期。但轉爐之底吹狀況變化相當大,若底吹孔的凹陷過深或底吹孔所吹出的氣體流量異常,隨時都可能發生洩鋼。因此,雷射測厚儀因單次拍攝時間太長,而導致拍攝間隔過久進而無法頻繁進行拍攝作業的情況就成為很大的問題。 However, every time the laser thickness gauge is used for shooting, the device of the laser thickness gauge must be positioned first. The positioning of the device and the subsequent shooting will take about 20 to 30 minutes in total. Therefore, the laser thickness measurement of the converter needs to be carried out during the busy production period. In the early stage of the furnace generation, the laser thickness measurement of the converter is usually carried out about once every 500 furnaces, and in the middle and late stages of the furnace generation with higher risks, the laser measurement of the converter is carried out about every 200 to 300 furnaces. Thick shoot. Therefore, the shortest interval between laser shots is about 1 to 2 weeks. However, the bottom blowing conditions of the converter have changed considerably. If the bottom blowing hole is too deep or the gas flow rate blown by the bottom blowing hole is abnormal, steel leakage may occur at any time. Therefore, because the single shooting time of the laser thickness gauge is too long, the shooting interval is too long and the shooting operation cannot be performed frequently, which becomes a big problem.
因此,本發明之一目的就是在提供一種轉爐之底吹孔之熔損的評估方法,其利用紅外線熱像儀拍攝蒐集轉爐內部之爐底位置的溫度資訊,並分析各底吹區塊的低溫區域面積與高低溫差,藉此可有效量化底吹孔的健康度,進而可降低底吹孔熔穿洩鋼的風險。 Therefore, one object of the present invention is to provide a method for evaluating the melting loss of the bottom blow hole of the converter, which uses infrared thermal imaging camera to collect the temperature information of the bottom position inside the converter, and analyze the low temperature of each bottom blowing block The difference between the area area and the high and low temperature can effectively quantify the health of the bottom blow hole, thereby reducing the risk of the bottom blow hole melting through the steel.
本發明之另一目的是在提供一種轉爐之底吹孔之熔損的評估方法,其中由於紅外線熱像儀僅需在定點安裝 與進行拍攝,因此不需花費設備定位的時間,且紅外線熱像儀在拍攝與收集轉爐之爐底位置的溫度資訊所需的時間非常短,因此可增加對轉爐內部之爐底拍攝的頻率,進而可提供快速且即時的分析回饋,有效降低底吹孔熔穿的風險。 Another object of the present invention is to provide a method for evaluating the melt loss of the bottom blow hole of the converter, in which the infrared camera only needs to be installed at a fixed point Therefore, there is no need to spend the time of equipment positioning, and the time required for the infrared thermal imager to capture and collect the temperature information of the bottom of the converter is very short, so the frequency of shooting the bottom of the converter can be increased. In turn, it can provide fast and immediate analysis feedback, effectively reducing the risk of bottom blow hole melt-through.
根據本發明之上述目的,提出一種轉爐之底吹孔之熔損的評估方法。在此方法中,利用紅外線熱像儀對轉爐內部之爐底進行錄影操作,以取得轉爐內部之爐底的溫度資訊。轉爐具有複數個底吹孔設於爐底中。利用溫度資訊計算每個底吹孔之低溫區域面積、以及每個底吹孔之高低溫差。分別根據這些低溫區域面積及/或高低溫差判斷每個底吹孔之健康度。 According to the above object of the present invention, a method for evaluating the melting loss of the bottom blow hole of the converter is proposed. In this method, an infrared thermal imager is used to record the bottom of the furnace inside the converter to obtain the temperature information of the bottom of the converter. The converter has a plurality of bottom blowing holes arranged in the bottom of the furnace. Use the temperature information to calculate the area of the low temperature area of each bottom blow hole and the difference between the high and low temperature of each bottom blow hole. The health of each bottom blow hole is judged according to the area of these low temperature regions and/or the difference between high and low temperature.
依據本發明之一實施例,進行上述之錄影操作時,轉爐處於出鋼狀態。 According to an embodiment of the present invention, the converter is in a tapping state during the aforementioned video recording operation.
依據本發明之一實施例,進行上述之錄影操作時,轉爐已完成出鋼與倒渣作業。 According to an embodiment of the present invention, when performing the above-mentioned video recording operation, the converter has completed the tapping and slag dumping operations.
依據本發明之一實施例,上述之錄影操作持續進行一分鐘以上。 According to an embodiment of the present invention, the aforementioned video recording operation lasts for more than one minute.
依據本發明之一實施例,上述計算每個底吹孔之每個低溫區域面積時包含:將紅外線熱像儀所取得之溫度資訊繪製成3D圖,其中3D圖之X軸與Y軸表示平面位置,3D圖之Z軸表示溫度,3D圖包含分別對應於底吹孔之複數個低溫區域。根據3D圖選擇背景溫度代表值。以背景溫度代表值減去預設溫度值而得到閥值。在3D圖之每個低溫區 域中,計算閥值所包圍之截面面積而得到此底吹孔之低溫區域之低溫區域面積。 According to an embodiment of the present invention, the calculation of the area of each low temperature region of each bottom blow hole includes: plotting the temperature information obtained by the infrared thermal imager into a 3D graph, wherein the X axis and Y axis of the 3D graph represent the plane For position, the Z axis of the 3D graph represents temperature, and the 3D graph contains a plurality of low temperature regions corresponding to bottom blow holes. Select the representative value of the background temperature according to the 3D graph. The threshold value is obtained by subtracting the preset temperature value from the representative value of the background temperature. In each low temperature zone of the 3D map In the domain, calculate the cross-sectional area enclosed by the threshold to obtain the low-temperature area of the bottom blow hole.
依據本發明之一實施例,上述計算每個底吹孔之高低溫差時包含:在3D圖之每個低溫區域中,以背景溫度代表值減去低溫區域之最低溫度值而獲得高低溫差。 According to an embodiment of the present invention, the calculation of the high and low temperature difference of each bottom blow hole includes: in each low temperature region of the 3D image, subtract the lowest temperature value of the low temperature region from the representative value of the background temperature to obtain the high and low temperature difference.
依據本發明之一實施例,上述之背景溫度代表值為3D圖中之一背景區之最高溫、此背景區之最低溫、或此背景區之平均溫度。 According to an embodiment of the present invention, the aforementioned representative value of the background temperature is the highest temperature in a background area in the 3D image, the lowest temperature in the background area, or the average temperature of the background area.
依據本發明之一實施例,上述之預設溫度值為約20℃至約200℃。 According to an embodiment of the present invention, the aforementioned preset temperature value is about 20°C to about 200°C.
依據本發明之一實施例,在上述判斷每個底吹孔之健康度中,當這些低溫區域面積之一者的尺寸變大時,代表這些低溫區域面積之該者所對應之底吹孔的尺寸變大。 According to an embodiment of the present invention, in the above-mentioned judging the health of each bottom blow hole, when the size of one of the low temperature area areas becomes larger, it represents the size of the bottom blow hole corresponding to the area of the low temperature area The size becomes larger.
依據本發明之一實施例,在上述判斷每個底吹孔之健康度中,當這些高低溫差之一者變大時,代表這些高低溫差之該者所對應之底吹孔的尺寸變大。 According to an embodiment of the present invention, in the above determination of the health of each bottom blow hole, when one of the high and low temperature differences becomes larger, the size of the bottom blow hole corresponding to the one representing the high and low temperature differences becomes larger.
100‧‧‧操作 100‧‧‧Operation
110‧‧‧操作 110‧‧‧Operation
120‧‧‧操作 120‧‧‧Operation
200‧‧‧轉爐 200‧‧‧Converter
200a‧‧‧爐口 200a‧‧‧stove mouth
210‧‧‧爐底 210‧‧‧Furnace bottom
220‧‧‧紅外線熱像儀 220‧‧‧Infrared Thermal Imager
300‧‧‧3D圖 300‧‧‧3D drawing
310‧‧‧低溫區域 310‧‧‧Low temperature area
320‧‧‧背景區 320‧‧‧Background area
330‧‧‧低溫區 330‧‧‧Low temperature zone
為讓本發明之上述和其他目的、特徵、優點與實施例能更明顯易懂,所附圖式之說明如下:〔圖1〕係繪示依照本發明之一實施方式的一種轉爐之底吹孔之熔損的評估方法的流程圖; 〔圖2A〕至〔圖2C〕係繪示依照本發明之一實施方式的一種轉爐之底吹孔之錄影操作的裝置流程示意圖;〔圖3〕係繪示依照本發明之一實施方式的一種轉爐之各底吹孔的高低溫差隨拍攝時間的變化曲線圖;以及〔圖4〕係繪示依照本發明之一實施方式的一種溫度資訊所繪製之3D圖的局部示意圖,其中3D圖之X軸與Y軸表示平面位置,3D圖之Z軸表示溫度。 In order to make the above and other objects, features, advantages and embodiments of the present invention more comprehensible, the description of the accompanying drawings is as follows: [FIG. 1] shows a bottom blowing of a converter according to an embodiment of the present invention Flow chart of the evaluation method of hole melting loss; [FIG. 2A] to [FIG. 2C] are schematic diagrams of the device flow diagram of the bottom blow hole recording operation of a converter according to an embodiment of the present invention; [FIG. 3] is a schematic diagram of an apparatus according to an embodiment of the present invention The graph of the variation curve of the difference between the high and low temperature of each bottom blow hole of the converter with the shooting time; and [Fig. 4] is a partial schematic diagram showing a 3D diagram drawn by a temperature information according to an embodiment of the present invention, where X of the 3D diagram The axis and Y axis represent the plane position, and the Z axis of the 3D graph represents temperature.
有鑑於習知利用雷射測厚儀來評估轉爐之底吹孔的健康度的技術有單次拍攝時間過長、以及拍攝間隔太長,而無法即時分析底吹殘厚的問題。因此,本發明在此提出一種轉爐之底吹孔之熔損的評估方法,利用紅外線熱像儀來蒐集轉爐內部之爐底的溫度資訊,並根據溫度資訊來分析轉爐之爐底之各底吹區塊的低溫區域面積與高低溫差,藉此可有效量化轉爐之各底吹孔的健康度,並可提供快速且即時之分析回饋。 In view of the fact that the conventional techniques for using a laser thickness gauge to assess the health of the bottom blow holes of the converter include too long a single shooting time and too long shooting intervals, it is impossible to analyze the bottom blow residual thickness in real time. Therefore, the present invention proposes a method for evaluating the melting loss of the bottom blow holes of the converter. The infrared thermal imager is used to collect the temperature information of the bottom of the converter, and the bottom blow of the bottom of the converter is analyzed based on the temperature information. The area of the low temperature area and the difference between the high and low temperature of the block can effectively quantify the health of the bottom blow holes of the converter and provide fast and real-time analysis feedback.
請參照圖1與圖2A至圖2C,其中圖1係繪示依照本發明之一實施方式的一種轉爐之底吹孔之熔損的評估方法的流程圖,圖2A至圖2C係繪示依照本發明之一實施方式的一種轉爐之底吹孔之錄影操作的評估的裝置流程示意圖。轉爐200具有多個底吹孔(未繪示)穿設於爐底210中。轉爐200之底吹孔的熔損評估可於轉爐200的吹煉結束後進行。如圖2A所示,在吹煉時,轉爐200呈站立狀,且轉爐
200的爐口200a朝上。在一些實施例中,如圖2B所示,於轉爐200完成吹煉後,傾轉轉爐200而開始出鋼,此時底吹孔維持吹氣狀態。轉爐200的傾轉角度可例如為約0度至90度。
Please refer to Figure 1 and Figures 2A to 2C, in which Figure 1 shows a flow chart of a method for evaluating the melting loss of the bottom blow hole of a converter according to an embodiment of the present invention, and Figures 2A to 2C show a flow chart according to A schematic flow diagram of an apparatus for evaluating the recording operation of bottom blow holes in a converter according to an embodiment of the present invention. The
在一些例子中,於轉爐200傾轉出鋼的期間,可進行操作100,以利用紅外線熱像儀220對轉爐200之內部的爐底210進行錄影操作,而連續拍攝爐底210一段時間,藉此可取得轉爐200之內部之爐底210的溫度資訊。即,進行爐底210的錄影操作時,轉爐200係處於出鋼狀態。爐底210的溫度資訊包含爐底210各位置的溫度。請一併參照圖3,其係繪示依照本發明之一實施方式的一種轉爐之各底吹孔的高低溫差隨拍攝時間的變化曲線圖。轉爐200之各底吹孔的高低溫差在拍攝開始大約一分鐘後即維持在一相對穩定數值。這也表示,紅外線熱像儀220開始拍攝錄影約一分鐘後即可達到穩定狀態。因此,在一些示範例子中,錄影操作可持續進行約一分鐘以上。紅外線熱像儀220完成拍攝後,即可將轉爐200予以轉回歸位,如圖2C所示。
In some examples, during the period when the
由於每次紅外線熱像儀220對轉爐200的爐底210所進行的錄影操作僅需約一分鐘,相當短的時間即可完成,因此可大大地提升對轉爐200之爐底210的拍攝頻率,藉此可有效降低轉爐200之底吹孔熔穿洩鋼的風險。
Since the recording operation of the infrared
在上述實施例中,利用紅外線熱像儀220對轉爐200之爐底210進行錄影操作係在轉爐200傾轉出鋼的期間進行。在另一些實施例中,可在轉爐200吹煉結束,並完
成出鋼與倒渣作業後,再將空的轉爐200傾轉約0度至約90度,接著才利用紅外線熱像儀220對轉爐200之爐底210進行錄影操作,而連續拍攝爐底210約一分鐘以上,藉以取得轉爐200之內部之爐底210的溫度資訊。也就是說,進行爐底210之錄影操作時,轉爐200已完成出鋼與倒渣作業而處於空爐狀態。在這些實施例中,轉爐200在出鋼與倒渣時,轉爐200之底吹孔維持吹氣狀態。上述兩種實施態樣的選用可根據生產時的條件與需求來決定。
In the above embodiment, the recording operation of the bottom 210 of the
請再次參照圖1,完成轉爐200之爐底210的錄影操作後,可進行操作110,以利用所蒐集到之轉爐200內部之爐底210的溫度資訊,來計算轉爐200之每個底吹孔的低溫區域面積、以及每個底吹孔的高低溫差。在一些例子中,可先將溫度資訊繪製成3D圖,再利用此3D圖的輔助來計算轉爐200之每個底吹孔的低溫區域面積與高低溫差。
Please refer to Figure 1 again. After the recording operation of the bottom 210 of the
請一併參照圖4,其係繪示依照本發明之一實施方式的一種溫度資訊所繪製之3D圖的局部示意圖,其中3D圖之X軸與Y軸表示平面位置,3D圖之Z軸表示溫度。即,3D圖300之X軸與Y軸為爐底各位置投影到一平面上的位置,而3D圖300之Z軸表示爐底各位置之溫度分布。此3D圖300包含數個低溫區域310,這些低溫區域310分別對應於轉爐200之底吹孔。低溫區域310的產生是因為底吹孔在無鋼液覆蓋的情況下,底吹孔吹氣造成局部冷卻所引起的現象。利用所蒐集到之爐底210的溫度資訊建立出此3D圖300後,可根據3D圖300選擇背景溫度代表值。由3D圖300之
圖形的溫度轉折,可將3D圖300之圖形粗略分成背景區320與低溫區330,其中低溫區330為大致對應底吹孔的區域,而背景區320大致為底吹孔區域外的區域,例如轉爐之內部空間。背景溫度代表值即是選自背景區320的溫度。舉例而言,背景溫度代表值可為3D圖300之背景區320的最高溫、背景區320的最低溫、或背景區320的平均溫度。在一些示範例子中,背景溫度代表值選擇背景區320的最高溫。
Please refer to FIG. 4 together, which is a partial schematic diagram of a 3D graph drawn by a temperature information according to an embodiment of the present invention, where the X axis and Y axis of the 3D graph represent the plane position, and the Z axis of the 3D graph represents temperature. That is, the X-axis and Y-axis of the 3D diagram 300 are the positions where each position of the furnace bottom is projected onto a plane, and the Z-axis of the 3D diagram 300 represents the temperature distribution of each position of the furnace bottom. The
背景溫度代表值主要在提供一計算閥值的參考基準,因此不管是背景區320的最高溫、最低溫、平均溫度、或其他有助於分析的溫度數值,只要轉爐之所有底吹孔的計算均使用同一類型選定值來計算閥值即可,在標準一致的情況下可使各底吹孔透過閥值所計算出的截面積具比較性。由於每爐次的爐溫會有變化,因此背景溫度代表值會隨著不同爐次而變動。甚至,因爐底溫度分布並非均一,所以同一爐次的每個底吹孔之間也可能會不同,但在一些示範例子中可視現場需求而統一訂定。
The representative value of the background temperature is mainly to provide a reference for calculating the threshold. Therefore, whether it is the highest temperature, lowest temperature, average temperature, or other temperature values helpful for analysis in the
選定背景溫度代表值後,再利用背景溫度代表值來計算閥值。首先根據所選擇之背景溫度代表值來決定預設溫度值。預設溫度值主要是用在閥值的計算上。閥值係以背景溫度代表值扣除無效的溫度區間,而預設溫度值即意欲表現此無效的溫度區間。預設溫度值與背景溫度代表值的選用有關。選用不同的背景溫度代表值就須調整預設溫度值,藉以使所計算出的閥值可較佳地解析底吹孔的大小。預設溫度值的數值越小越能提供較佳的解析能力,但若小至無法有
效濾除背景,則反而不利;而預設溫度值的數值越大則越可確保有效濾除背景,但解析能力也會相對變差。在一些例子中,預設溫度值可為約20℃至約200℃。在一些示範例子中,根據發明人於之前測試爐代的數據,背景溫度代表值係選用背景區320之最高溫,而預設溫度值則可選用約100℃。以所選擇之背景溫度代表值減去預設溫度值,來濾除背景區320後,即可得到閥值。
After the representative value of the background temperature is selected, the representative value of the background temperature is used to calculate the threshold. First, determine the preset temperature value according to the selected representative value of the background temperature. The preset temperature value is mainly used in the calculation of the threshold. The threshold is to deduct the invalid temperature interval from the representative value of the background temperature, and the preset temperature value is intended to represent the invalid temperature interval. The preset temperature value is related to the selection of the representative value of the background temperature. Choosing different representative values of the background temperature requires adjusting the preset temperature value so that the calculated threshold can better analyze the size of the bottom blow hole. The smaller the value of the preset temperature, the better the resolution, but if it is too small,
Effectively filter out the background, but it is not good; the larger the value of the preset temperature value, the more effective the background filter can be ensured, but the resolution ability will be relatively poor. In some examples, the preset temperature value may be about 20°C to about 200°C. In some exemplary examples, according to the data of the inventors in the previous test generations, the representative value of the background temperature is the highest temperature of the
完成閥值的計算後,在3D圖300的每個低溫區域310中,計算此閥值所包圍之截面面積,而可得到此低溫區域310所對應之底吹孔的低溫區域面積。此外,可利用背景溫度代表值來計算每個底吹孔之高低溫差。在3D圖300的每個低溫區域310中,以背景溫度代表值減去低溫區域310之最低溫度值即可獲得高低溫差。底吹孔之低溫區域310的低溫區域面積與高低溫差兩者的變化呈正相關。底吹孔之低溫區域面積與高低溫差兩者的數值太大,表示底吹孔可能有異常熔損的疑慮;若低溫區域面積與高低溫差兩者的數值太小甚至為0,則表示底吹孔可能有堵塞的現象、或殘厚不足。
After the calculation of the threshold is completed, in each
請繼續參照圖1,完成底吹孔之低溫區域310的低溫區域面積與高低溫差的計算後,可進行操作120,以根據每個底吹孔之低溫區域310的低溫區域面積、高低溫差、或同時根據低溫區域面積與高低溫差,來分別判斷每個底吹孔的健康度。在一些例子中,判斷每個底吹孔的健康度時,當一低溫區域310的低溫區域面積的尺寸變大時,代表此低
溫區域310之低溫區域面積所對應之底吹孔的尺寸變大,若低溫區域面積的尺寸變小,則可能代表此低溫區域310之低溫區域面積所對應之底吹孔的尺寸變小。此外,當一低溫區域310的高低溫差變大時,代表此高低溫差所對應之底吹孔的尺寸變大,若高低溫差變小,則可能代表此高低溫差所對應之底吹孔的尺寸變小。低溫區域310的低溫區域面積與高低溫差雖然呈正相關,但低溫區域面積與高低溫差兩者的最大值不一定會同時出現,現場工作人員可同時參考低溫區域面積與高低溫差的數值來評估轉爐之底吹孔的適當維護時機。
Please continue to refer to FIG. 1, after completing the calculation of the low temperature area of the
另外,一般而言,因為每個底吹孔為圓形,因此底吹孔的低溫區域310在正常狀態下呈近圓形。故,底吹孔的低溫區域310所呈現的形狀異常時,可能代表此底吹孔有異常剝離發生,需特別進行追蹤。
In addition, generally speaking, because each bottom blow hole is circular, the
在本發明之實施例中,紅外線熱像儀在開始拍攝約一分鐘後,底吹孔之低溫區域的低溫區域面積與高低溫差即維持相對穩定的數值,因此底吹孔之低溫區域的低溫區域面積與高低溫差的判定已具參考性。故,對轉爐爐底的拍攝錄影僅需短時間即可取得轉爐內部之爐底的溫度資訊,而可大幅增加對轉爐內部之爐底的拍攝錄影頻率,進而可有效降低底吹孔熔穿洩鋼的風險。 In the embodiment of the present invention, the low temperature area of the low temperature area of the bottom blow hole and the difference between the high and low temperature maintain a relatively stable value after the infrared thermal imager starts shooting for about one minute, so the low temperature area of the low temperature area of the bottom blow hole The area and the difference between high and low temperature have been determined for reference. Therefore, it takes only a short time to capture and record the bottom of the converter to obtain the temperature information of the bottom of the converter, which can greatly increase the frequency of shooting and video recording of the bottom of the converter, thereby effectively reducing bottom blow hole melting and leakage Risk of steel.
由上述之實施方式可知,本發明之一優點就是因為本發明之轉爐之底吹孔之熔損的評估方法利用紅外線熱像儀拍攝蒐集轉爐內部之爐底位置的溫度資訊,並分析各 底吹區塊的低溫區域面積與高低溫差,藉此可有效量化底吹孔的健康度,進而可降低底吹孔熔穿洩鋼的風險。 It can be seen from the above-mentioned embodiments that one of the advantages of the present invention is that the method for evaluating the melting loss of the bottom blow hole of the converter of the present invention uses infrared thermal imaging camera to collect the temperature information of the bottom position inside the converter and analyze each The area of the low temperature area of the bottom blow block and the difference between the high and low temperature can effectively quantify the health of the bottom blow hole, thereby reducing the risk of the bottom blow hole melting through the steel.
由上述之實施方式可知,本發明之另一優點就是因為在本發明之轉爐之底吹孔之熔損的評估方法中,由於紅外線熱像儀僅需在定點安裝與進行拍攝,因此不需花費設備定位的時間,且紅外線熱像儀在拍攝與收集轉爐之爐底位置的溫度資訊所需的時間非常短,因此可增加對轉爐內部之爐底拍攝的頻率,進而可提供快速且即時的分析回饋,有效降低底吹孔熔穿的風險。 As can be seen from the above-mentioned embodiments, another advantage of the present invention is that in the method for evaluating the melting loss of the bottom blow hole of the converter of the present invention, since the infrared thermal imager only needs to be installed and photographed at a fixed point, it does not cost The time required for equipment positioning, and the time required for the infrared thermal imaging camera to capture and collect the temperature information of the furnace bottom of the converter is very short, so it can increase the frequency of shooting the furnace bottom inside the converter, thereby providing fast and real-time analysis Feedback, effectively reducing the risk of bottom blow hole melt-through.
雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何在此技術領域中具有通常知識者,在不脫離本發明之精神和範圍內,當可作各種之更動與潤飾,因此本發明之保護範圍當視後附之申請專利範圍所界定者為準。 Although the present invention has been disclosed in the above embodiments, it is not intended to limit the present invention. Anyone with ordinary knowledge in this technical field can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the protection scope of the present invention shall be subject to those defined by the attached patent application scope.
100‧‧‧操作 100‧‧‧Operation
110‧‧‧操作 110‧‧‧Operation
120‧‧‧操作 120‧‧‧Operation
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW108119568A TWI697561B (en) | 2019-06-05 | 2019-06-05 | Method for evaluating melting loss of bottom blowing hole of converter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW108119568A TWI697561B (en) | 2019-06-05 | 2019-06-05 | Method for evaluating melting loss of bottom blowing hole of converter |
Publications (2)
Publication Number | Publication Date |
---|---|
TWI697561B true TWI697561B (en) | 2020-07-01 |
TW202045735A TW202045735A (en) | 2020-12-16 |
Family
ID=72602244
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW108119568A TWI697561B (en) | 2019-06-05 | 2019-06-05 | Method for evaluating melting loss of bottom blowing hole of converter |
Country Status (1)
Country | Link |
---|---|
TW (1) | TWI697561B (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20180043407A1 (en) * | 2015-03-26 | 2018-02-15 | Toshiba Mitsubishi-Electric Industrial Systems Corporation | Temperature calculation method, temperature calculation apparatus, heating control method, and heating control apparatus |
CN109295277A (en) * | 2018-11-14 | 2019-02-01 | 钢铁研究总院 | A kind of on-line monitoring method and device of converter bottom blowing gas-feeding element air permeability effect |
-
2019
- 2019-06-05 TW TW108119568A patent/TWI697561B/en not_active IP Right Cessation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20180043407A1 (en) * | 2015-03-26 | 2018-02-15 | Toshiba Mitsubishi-Electric Industrial Systems Corporation | Temperature calculation method, temperature calculation apparatus, heating control method, and heating control apparatus |
CN109295277A (en) * | 2018-11-14 | 2019-02-01 | 钢铁研究总院 | A kind of on-line monitoring method and device of converter bottom blowing gas-feeding element air permeability effect |
Also Published As
Publication number | Publication date |
---|---|
TW202045735A (en) | 2020-12-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US9279773B2 (en) | Crack detection and measurement in a metallurgical vessels | |
JP2016519751A (en) | Method for determining the state of refractory lining of metallurgical vessels, especially for molten metal | |
JP6414102B2 (en) | Refining furnace discharge flow determination apparatus, refining furnace discharge flow determination method, and molten metal refining method | |
JP2015052148A (en) | Method for controlling blast furnace by determining operational situation thereof | |
TWI661052B (en) | Diagnosis support apparatus, diagnosis support method, diagnosis method, and repair method of vacuum degassing vessel | |
TWI697561B (en) | Method for evaluating melting loss of bottom blowing hole of converter | |
CA2078522A1 (en) | Ceramic welding method and apparatus | |
JP4873788B2 (en) | Detection method of furnace conditions | |
JP6477751B2 (en) | Evaluation method of bottom bottom tuyere integrity of bottom blown converter, method of extending life of bottom tuyere, and operation method of bottom blown converter | |
JP6010972B2 (en) | Metal adhesion measurement method and metal adhesion measurement device | |
JPH0972852A (en) | Detection method for crack of lining refractory in molten-metal receiver container and repair method for crack | |
JP6515342B2 (en) | Blast furnace tuyere closure removal device and blast furnace tuyere closure removal method | |
WO2021149490A1 (en) | Lance tip, converter internal temperature measuring equipment, and converter internal temperature measuring method | |
US20230358475A1 (en) | System and method for monitoring and controlling furnaces | |
CN110669896B (en) | Converter body multipoint temperature measurement method | |
JP4954688B2 (en) | Coke oven carbonization chamber furnace wall displacement measurement system, and coke oven carbonization chamber furnace wall displacement measurement method | |
JP5920267B2 (en) | Mushroom detection method for converter bottom tuyeres and anomaly detection method for bottom tuyeres using it | |
RU2811810C1 (en) | System and method for determining three-dimensional information about metallurgical vessel and its modification | |
JP6135998B2 (en) | Method for determining spheroidizing reaction of molten metal for spheroidal graphite cast iron | |
JPS62288503A (en) | Coke oven wall crack measurement method | |
TW201821785A (en) | Status monitoring system for fire-resistant material in furnace and monitoring method thereof | |
KR20220093224A (en) | Lance chip, in-converter temperature measurement equipment and in-converter temperature measurement method | |
JP2022144010A (en) | Method, device and program for evaluating tuyere landscape of blast furnace | |
WO2024128181A1 (en) | Oven-wall temperature distribution measurement system, oven-wall abnormality diagnosis system, coke-oven operating method, and coke-oven repairing method | |
JPH03180420A (en) | Method for deciding slopping of converter |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Annulment or lapse of patent due to non-payment of fees |