TWI776567B - Method and system for monitoring walls of a blast furnace - Google Patents
Method and system for monitoring walls of a blast furnace Download PDFInfo
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本發明是有關於一種高爐爐壁監測方法與系統。特別是有關於高爐爐壁結塊之監測方法與系統。The present invention relates to a method and system for monitoring a blast furnace wall. Especially about the monitoring method and system of blast furnace wall agglomeration.
一般而言,在高爐煉鐵的過程中,高爐爐壁上可能會有結塊產生。以學理上來講,爐壁結塊是爐內鹼金屬之循環與沉積所造成。鹼金屬通常以矽酸鹽複合物存於礦料以及焦炭灰份中。當爐料到達1500℃的高溫區時才會分解,而此時大部分的鹼金屬氧化物會融入渣中,少部分鹼金屬蒸氣隨著氣流上升,接觸到溫度低的爐壁而冷凝沉積,進而在爐壁上形成結塊。Generally speaking, in the process of blast furnace ironmaking, there may be agglomerates on the blast furnace wall. From a theoretical point of view, the agglomeration of the furnace wall is caused by the circulation and deposition of alkali metals in the furnace. Alkali metals are usually present in mineral aggregates and coke ash as silicate complexes. When the charge reaches the high temperature zone of 1500°C, it will decompose, and at this time, most of the alkali metal oxides will be integrated into the slag, and a small part of the alkali metal vapor will rise with the airflow and contact the low temperature furnace wall to condense and deposit, and then Formation of lumps on the furnace walls.
爐壁上的結塊可能會影響爐況,使得高爐產出不佳。更甚者,結塊可能會掉落而破壞高爐中的設備,例如鼓風嘴。因此,需要一種高爐爐壁監測方法與系統來監測高爐爐壁上的結塊。Agglomeration on the furnace walls can affect furnace conditions, resulting in poor blast furnace output. What's more, the agglomerates can fall and damage equipment in the blast furnace, such as blower nozzles. Therefore, there is a need for a blast furnace wall monitoring method and system to monitor agglomeration on the blast furnace wall.
本發明之實施例提出一種高爐爐壁監測方法與系統,其可監測高爐爐壁上的結塊,再者也可進一步調整高爐的入料來減少/縮小高爐爐壁上的結塊。Embodiments of the present invention provide a blast furnace wall monitoring method and system, which can monitor the agglomeration on the blast furnace wall, and further adjust the blast furnace feed to reduce/reduce the agglomeration on the blast furnace wall.
根據本發明之一態樣,上述之高爐爐壁監測方法包含提供複數筆爐壁溫度資料,其中這些爐壁溫度資料係一對一地對應至複數個高爐爐壁區段;根據這些爐壁溫度資料來計算出這些高爐爐壁區段所對應之複數個結塊厚度值;判斷這些結塊厚度值之一者是否大於一預設厚度閥值;當上述結塊厚度值之一者大於預設厚度閥值時,計算此結塊厚度值之大於預設厚度閥值之一持續時間,並判斷此持續時間是否大於一預設持續時間閥值;以及當此持續時間大於預設持續時間閥值時,發出警示訊息。According to an aspect of the present invention, the above-mentioned blast furnace wall monitoring method includes providing a plurality of pieces of furnace wall temperature data, wherein these furnace wall temperature data correspond to a plurality of blast furnace wall sections in a one-to-one manner; according to these furnace wall temperatures data to calculate a plurality of agglomeration thickness values corresponding to these blast furnace wall sections; determine whether one of these agglomeration thickness values is greater than a preset thickness threshold; when one of the agglomeration thickness values is greater than a preset thickness When the thickness threshold is used, calculate the duration of the cake thickness value greater than the preset thickness threshold, and determine whether the duration is greater than a preset duration threshold; and when the duration is greater than the preset duration threshold , a warning message is issued.
在一些實施例中,上述之預設厚度閥值為1000毫米(mm),預設持續時間閥值為6小時。In some embodiments, the above-mentioned predetermined thickness threshold is 1000 millimeters (mm), and the predetermined duration threshold is 6 hours.
在一些實施例中,上述之高爐爐壁監測方法除了上述之步驟外,更包含:根據高爐之一熱負荷值以及一熱負荷持續時間來決定一佈角參數;以及根據佈角參數來控制高爐之佈料操作。In some embodiments, in addition to the above-mentioned steps, the above-mentioned blast furnace wall monitoring method further includes: determining a layout angle parameter according to a heat load value and a heat load duration of the blast furnace; and controlling the blast furnace according to the layout angle parameter the cloth operation.
在一些實施例中,高爐之熱負荷值為高爐之爐腰(belly)的熱負荷值。In some embodiments, the heat load value of the blast furnace is the heat load value of the belly of the blast furnace.
在一些實施例中,上述之佈角參數包含焦炭和鐵礦之佈料參數。In some embodiments, the above-mentioned distribution angle parameters include distribution parameters of coke and iron ore.
根據本發明之另一態樣,上述之高爐爐壁監測系統包含複數個溫度感測器以及高爐程控系統。溫度感測器設置於高爐之複數個高爐爐壁區段中,以提供複數筆爐壁溫度資料,其中這些爐壁溫度資料係一對一地對應至高爐爐壁區段。高爐程控系統係用以:接收爐壁溫度資料;根據爐壁溫度資料來計算出高爐爐壁區段所對應之複數個結塊厚度值;判斷這些結塊厚度值之一者是否大於預設厚度閥值;當上述結塊厚度值之一者大於預設厚度閥值時,計算此結塊厚度值之大於預設厚度閥值之一持續時間,並判斷此持續時間是否大於一預設持續時間閥值;以及當此持續時間大於預設持續時間閥值時,發出警示訊息。According to another aspect of the present invention, the above-mentioned blast furnace wall monitoring system includes a plurality of temperature sensors and a blast furnace program control system. The temperature sensors are arranged in a plurality of blast furnace wall sections of the blast furnace to provide a plurality of furnace wall temperature data, wherein these furnace wall temperature data are corresponding to the blast furnace wall sections one-to-one. The blast furnace program control system is used to: receive the furnace wall temperature data; calculate a plurality of agglomerate thickness values corresponding to the blast furnace wall section according to the furnace wall temperature data; determine whether one of these agglomerate thickness values is greater than the preset thickness Threshold value; when one of the agglomeration thickness values is greater than the preset thickness threshold value, calculate a duration of the agglomeration thickness value greater than the preset thickness threshold value, and determine whether the duration time is greater than a preset duration time threshold; and when the duration is greater than the preset duration threshold, a warning message is issued.
在一些實施例中,上述之溫度感測器為熱電偶,預設厚度閥值為1000毫米,該預設持續時間閥值為6小時。In some embodiments, the above-mentioned temperature sensor is a thermocouple, the predetermined thickness threshold is 1000 mm, and the predetermined duration threshold is 6 hours.
在一些實施例中,除了上述之步驟外,上述之高爐程控系統更用以:根據高爐之一熱負荷值以及一熱負荷持續時間來決定佈角參數;以及根據佈角參數來控制高爐之佈料操作。In some embodiments, in addition to the above-mentioned steps, the above-mentioned blast furnace programming control system is further used to: determine the layout angle parameter according to a heat load value and a heat load duration of the blast furnace; and control the layout of the blast furnace according to the layout angle parameter material operation.
在一些實施例中,高爐之一熱負荷值為高爐之爐腰的熱負荷值。In some embodiments, one of the heat load values of the blast furnace is the heat load value of the hearth of the blast furnace.
在一些實施例中,上述之佈角參數包含焦炭和鐵礦之佈料參數。In some embodiments, the above-mentioned distribution angle parameters include distribution parameters of coke and iron ore.
關於本文中所使用之『第一』、『第二』、…等,並非特別指次序或順位的意思,其僅為了區別以相同技術用語描述的元件或操作。The terms "first", "second", .
請參照圖1,其係繪示根據本發明實施例之高爐爐壁監測系統的示意圖。高爐爐壁監測系統包含複數個溫度感測器110以及高爐程控系統120。溫度感測器110係設置於高爐130的複數個爐壁區段中。在本實施例中,溫度感測器110為熱電偶,其係埋設於高爐之爐壁中,以感測相應爐壁區段的溫度值。然而本發明之實施例並不受限於此。Please refer to FIG. 1 , which is a schematic diagram of a blast furnace wall monitoring system according to an embodiment of the present invention. The blast furnace wall monitoring system includes a plurality of
高爐係依照高度將爐身分為複數個層S1~S8,而每個層又依照方向分為8個區段,例如東方區段、東南區段、南方區段等等。如此,整個高爐被分出8x8個區段,而溫度感測器110則設置於這64個區段中,以量測此64個區段的爐壁溫度值,並輸出相應的爐壁溫度資料至高爐程控系統120。然而,本發明之實施例並不受限於此。本發明實施例之高爐不受限於分為8層,也不受限於每層分出8個區段。本領域技術人員可根據實據需求來對高爐分層,以及對每個層分區,以量測這些區段的溫度值。The blast furnace is divided into multiple layers S1~S8 according to the height, and each layer is divided into 8 sections according to the direction, such as the east section, the southeast section, the south section and so on. In this way, the entire blast furnace is divided into 8×8 sections, and the
高爐程控系統120係用以接收溫度感測器110所傳送之爐壁溫度資料,並根據爐壁溫度資料來監測高爐爐壁的結塊狀況。The blast furnace
請參照圖2,其係繪示高爐程控系統120所進行之高爐爐壁監測方法200的流程示意圖。在高爐爐壁監測方法200中,首先進行步驟210,以接收溫度感測器110所傳送之複數筆爐壁溫度資料。每筆爐壁溫度資料包含相應之高爐爐壁區段的溫度值。然後,進行步驟220,以根據上述之爐壁溫度資料來計算出高爐爐壁區段所對應之複數個結塊厚度值。在本發明之一實施例中,高爐程控系統120可應用使用者介面來顯示高爐爐壁區段對應的結塊厚度值,如圖3所示。在圖3中,高爐爐壁區段係以方塊S101~S108、方塊S201~S208、方塊S301~S308、方塊S401~S408、方塊S501~S508、方塊S601~S608、方塊S701~S708、方塊S801~S808來表示。Please refer to FIG. 2 , which is a schematic flowchart of a blast furnace
方塊S101~S108係代表高爐第一層S1在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第一層S1之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S101 to S108 represent eight furnace wall sections in eight directions on the first floor S1 of the blast furnace. As mentioned above, the
方塊S201~S208係代表高爐第二層S2在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第二層S2之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S201 to S208 represent eight furnace wall sections in eight directions on the second floor S2 of the blast furnace. As mentioned above, the
方塊S301~S308係代表高爐第三層S3在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第三層S3之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S301 to S308 represent eight furnace wall sections in eight directions on the third floor S3 of the blast furnace. As mentioned above, the
方塊S401~S408係代表高爐第四層S4在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第四層S4之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S401 to S408 represent eight furnace wall sections in eight directions on the fourth floor S4 of the blast furnace. As mentioned above, the
方塊S501~S508係代表高爐第五層S5在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第五層S5之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S501 to S508 represent eight furnace wall sections in eight directions on the fifth floor S5 of the blast furnace. As mentioned above, the
方塊S601~S608係代表高爐第六層S6在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第六層S6之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S601 to S608 represent eight furnace wall sections in eight directions on the sixth floor S6 of the blast furnace. As mentioned above, the
方塊S701~S708係代表高爐第七層S7在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第七層S7之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S701 to S708 represent eight furnace wall sections in eight directions on the seventh floor S7 of the blast furnace. As mentioned above, the
方塊S801~S808係代表高爐第八層S8在八個方向的八個爐壁區段。如之前所述,此八個爐壁區段中埋設有溫度感測器110,以感測第八層S8之八個爐壁區段的溫度值,並將其回傳至高爐程控系統120,以便高爐程控系統120計算出相應的結塊厚度值。Blocks S801 to S808 represent eight furnace wall sections in eight directions on the eighth floor S8 of the blast furnace. As mentioned above, the
在圖3中,高爐程控系統120係以不同的顏色漸層變化來表示不同的結塊厚度值。例如,當結塊厚度值在400毫米(mm)以下時,以較深的顏色,例如深綠色表示。又例如,當結塊厚度超過400毫米,但在460毫米以下時,以稍微淺一點的顏色,例如稍微淺一點的綠色表示。再例如,當結塊厚度超過460毫米,但在520毫米以下時,以更淺一點的顏色,例如更淺一點的綠色表示。在本實施例中,顏色漸層的變化係以60毫米為單位來進行,但本發明之實施例並不受限於此。In FIG. 3 , the blast furnace
在一些實施例中,方塊S101~S808也可顯示相應高爐區段的結塊厚度值。本發明之實施例並不受限於此。In some embodiments, blocks S101 to S808 may also display the agglomerate thickness values of the corresponding blast furnace sections. Embodiments of the present invention are not so limited.
請回到圖2,在步驟230中,判斷上述結塊厚度值之一者是否大於一預設厚度閥值。當結塊厚度值之一者大於預設厚度閥值時,進行步驟240,以計算此結塊厚度值之一者大於預設厚度閥值之一持續時間。例如,當一結塊厚度值於一時間點開始大於預設厚度閥值時,便會開始進行時間累計,以計算出此結塊厚度值大於預設厚度閥值之持續時間。Referring back to FIG. 2 , in
然後,進行步驟250,以判斷此結塊厚度值大於預設厚度閥值之持續時間是否大於一預設持續時間閥值。當結塊厚度值大於預設厚度閥值之持續時間大於預設持續時間閥值時,進行步驟260,以發出警示訊息。Then, step 250 is performed to determine whether the duration of the cake thickness value greater than the predetermined thickness threshold value is greater than a predetermined duration time threshold value. When the duration of the agglomerate thickness value greater than the preset thickness threshold value is greater than the preset duration time threshold value,
在本實施例中,此預設厚度閥值為1000毫米,預設持續時間閥值為6小時。當高爐區段的結塊厚度值超過1000毫米,且滿足6小時的持續時間條件時,高爐程控系統120便會發出警示訊息,例如文字訊息、燈光訊息或是顏色訊息。如圖3所示,當方塊S202、S203以及S303所對應之高爐區段的結塊厚度值超過1000毫米,且滿足6小時的持續時間條件時,高爐程控系統120可以閃光或者在方塊邊框上加上特定色彩的方式來顯示方塊S202、S203以及S303,以提出警示。如此,當高爐程控人員觀察到有方塊開始閃光或是有特定色彩邊框時,可清楚地了解到高爐中有部分區段具有超過標準的結塊厚度值。然而,本發明之實施例並不受限此。In this embodiment, the preset thickness threshold is 1000 mm, and the preset duration threshold is 6 hours. When the agglomeration thickness value of the blast furnace section exceeds 1000 mm and the duration condition of 6 hours is satisfied, the blast furnace
在一些實施例中,亦可針對超過結塊預設厚度閥值的高爐區段進行相應的處理,例如調整高爐的入料,以減少/縮小高爐爐壁上的結塊。例如,計算高爐之一熱負荷值,並根據熱負荷值以及熱負荷持續時間來提供不同的佈角參數,以控制高爐的佈料操作來消除結塊。In some embodiments, corresponding treatment can also be performed for the blast furnace section exceeding the preset thickness threshold of agglomeration, for example, adjusting the feed of the blast furnace to reduce/reduce the agglomeration on the blast furnace wall. For example, a heat load value of one of the blast furnaces is calculated, and different distribution angle parameters are provided according to the heat load value and the heat load duration to control the distribution operation of the blast furnace to eliminate agglomeration.
請參照圖4,其係繪示高爐程控系統120在不同熱負荷狀況下,對高爐進行不同的佈料操作。例如,高爐程控系統120會計算高爐爐腰(belly)的熱負荷值,根據所設定之熱負荷區間及持續時間,系統會依滿足之條件自動指引所設定之佈角參數。高爐爐腰的熱負荷值可透過,例如高爐冷卻水的資訊(水溫、流量等)來計算獲得。如圖4所示,在本實施例中,提供1~6號共6個不同的佈角參數組來控制高爐的佈料操作,其中不同的佈角參數組包含不同的焦炭/鐵礦之佈料參數。具體而言,每組佈料參數包含係焦炭/鐵礦的佈料圈數,其係對應至1~12種佈料位置(根據佈料槽角度決定)。例如,在第1號佈料參數組中,對應至第2種佈料位置之焦炭佈料圈數為4圈,而對應至第2種佈料位置之鐵礦佈料圈數為3圈。又例如,在第1號佈料參數組中,對應至第5種佈料位置之焦炭佈料圈數為2圈,而對應至第5種佈料位置之鐵礦佈料圈數為2圈。第1~6號佈角參數組可對應至不同的高爐通風性。具體而言,通風性由高至低排列為:第6號、第5號、第4號、第3號、第2號以及第1號。其中,第6號佈角參數組具有較高的周邊通風性(較強的周邊氣流),有利於消除爐壁上的結塊。此係因為焦炭被佈置在外邊的位置,焦炭具有較大的粒徑及結構強度較高。Please refer to FIG. 4 , which shows that the blast furnace
如圖4所示,當高爐爐腰的熱負荷值小於600百萬卡/小時(MCal/h)時,且持續時間超過2或4小時以上,高爐程控系統120設定第6號佈料參數組來控制高爐的佈料操作。當高爐爐腰的熱負荷值介於600MCal/h至700MCal/h之間時,且持續時間超過2或8小時以上,高爐程控系統120設定第5號佈料參數組來控制高爐的佈料操作。當高爐爐腰的熱負荷值介於700MCal/h至1200MCal/h之間時,且持續時間超過4或8小時以上,高爐程控系統120設定第4號佈料參數組來控制高爐的佈料操作。當高爐爐腰的熱負荷值介於1200MCal/h至1700MCal/h之間時,且持續時間超過6或8小時以上,高爐程控系統120設定第3號佈料參數組來控制高爐的佈料操作。當高爐爐腰的熱負荷值介於1700MCal/h至2200MCal/h之間時,且持續時間超過4或8小時以上,高爐程控系統120設定第2號佈料參數組來控制高爐的佈料操作。As shown in FIG. 4 , when the heat load value of the blast furnace waist is less than 600 million cal/h (MCal/h), and the duration exceeds 2 or 4 hours, the blast furnace
值得一提的是,當高爐爐腰的熱負荷值大於 2200MCal/h,且持續時間超過2小時(但未超過4小時)之時,高爐程控系統120設定第2號佈料參數組來控制高爐的佈料操作。當持續時間超過4小時之時,高爐程控系統120設定第1號佈料參數組來控制高爐的佈料操作。It is worth mentioning that when the heat load value of the blast furnace waist is greater than 2200MCal/h, and the duration exceeds 2 hours (but not more than 4 hours), the blast furnace
由上述說明可知,本發明實施例之高爐爐壁監測方法與系統係透過量測高爐爐壁的溫度來監控高爐爐壁結塊的狀況並及時提供警示給高爐操作人員。再者,本發明實施例之高爐爐壁監測方法與系統也可設定不同的佈料參數來控制高爐的佈料操作,以不同的焦炭/鐵礦配置來調整高爐內的通風性,以控制高爐爐壁的結塊大小,以避免爐壁上的結塊影響爐高爐產出不佳或破壞高爐中的設備。As can be seen from the above description, the blast furnace wall monitoring method and system according to the embodiments of the present invention monitor the agglomeration condition of the blast furnace wall by measuring the temperature of the blast furnace wall and provide warnings to blast furnace operators in time. Furthermore, in the blast furnace wall monitoring method and system according to the embodiment of the present invention, different distribution parameters can be set to control the distribution operation of the blast furnace, and the ventilation in the blast furnace can be adjusted with different coke/iron ore configurations to control the blast furnace. The size of the agglomeration on the furnace wall to avoid the agglomeration on the furnace wall affecting the poor output of the blast furnace or damaging the equipment in the blast furnace.
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,任何所屬技術領域中具有通常知識者,在不脫離本發明的精神和範圍內,當可作些許的更動與潤飾,故本發明的保護範圍當視後附的申請專利範圍所界定者為準。Although the present invention has been disclosed above by the embodiments, it is not intended to limit the present invention. Anyone with ordinary knowledge in the technical field can make some changes and modifications without departing from the spirit and scope of the present invention. Therefore, The protection scope of the present invention shall be determined by the scope of the appended patent application.
110:溫度感測器
120:高爐程控系統
130:高爐
200:高爐爐壁監測方法
210~260:步驟
S1~S8:層
S101~S808:方塊
110: temperature sensor
120: Blast Furnace Program Control System
130: Blast Furnace
200: Blast Furnace
圖1係繪示根據本發明實施例之高爐爐壁監測系統的示意圖。 圖2係繪示根據本發明實施例之高爐程控系統所進行之高爐爐壁監測方法的流程示意圖。 圖3係繪示根據本發明實施例之顯示結塊厚度的方塊示意圖。 圖4係繪示根據本發明實施例之高爐佈角參數的示意圖。 FIG. 1 is a schematic diagram illustrating a blast furnace wall monitoring system according to an embodiment of the present invention. FIG. 2 is a schematic flow chart illustrating a method for monitoring a blast furnace wall performed by a blast furnace program control system according to an embodiment of the present invention. FIG. 3 is a block diagram showing the thickness of agglomerates according to an embodiment of the present invention. FIG. 4 is a schematic diagram illustrating a blast furnace layout angle parameter according to an embodiment of the present invention.
無none
200:高爐爐壁監測方法 200: Blast Furnace Wall Monitoring Method
210~260:步驟 210~260: Steps
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WO2020139325A1 (en) * | 2018-12-26 | 2020-07-02 | Hewlett-Packard Development Company, L.P. | Tracer gas endpoint-monitored sinter systems |
US20210018469A1 (en) * | 2018-03-30 | 2021-01-21 | Tata Steel Limited | Method of detecting crack propagation in wall of a metallurgical furnace and a detection unit |
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CN103614498A (en) * | 2013-12-18 | 2014-03-05 | 中南大学 | Method for reconstructing three-dimensional temperature field positioned on blast furnace wall and computer monitoring system |
TW201636431A (en) * | 2015-02-10 | 2016-10-16 | 保爾伍斯股份有限公司 | Optical monitoring system for observing internal conditions in the tuyere zone of a blast furnace |
US20210018469A1 (en) * | 2018-03-30 | 2021-01-21 | Tata Steel Limited | Method of detecting crack propagation in wall of a metallurgical furnace and a detection unit |
WO2020139325A1 (en) * | 2018-12-26 | 2020-07-02 | Hewlett-Packard Development Company, L.P. | Tracer gas endpoint-monitored sinter systems |
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