TWI341867B - - Google Patents

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TWI341867B
TWI341867B TW96144808A TW96144808A TWI341867B TW I341867 B TWI341867 B TW I341867B TW 96144808 A TW96144808 A TW 96144808A TW 96144808 A TW96144808 A TW 96144808A TW I341867 B TWI341867 B TW I341867B
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Taiwan
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dust
discharge
gas
patent application
blast furnace
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TW96144808A
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Chinese (zh)
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TW200923105A (en
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China Steel Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Blast Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

1341867 九、發明說明: 【發明所屬之技術領域】 本發明是有關於—種出料方法及其系統,特別是指- 種能完全防止爐氣外逸,且降低爐塵回收再利用成本之高 爐爐塵乾式出料方法及其系統。 【先前技術】 目前於各廠區所進行的高爐爐塵出料收集作業,一般 皆疋採用濕式出料方式,即,習知之高爐在進行其爐塵出 料作業時,是將原先乾燥之高爐爐塵喷水,以避免所產生 之1¾爐氣由出料管道逸出,而導致現場作業人員中毒和氣 爆之危害。 參閱圖1’習知之濕式爐塵出料系統包括一具有一輸料 811並可谷置由一尚爐(圖未示)送出之複數爐塵801及 爐氣802之集塵槽81、一設置於該集塵槽81下方且與該輸 料口 811相連通之下料管82、一設置於該下料管82下方, 且可承接來自該下料管82之爐塵801及爐氣802的攪拌機 83、及一可將水灑入該攪拌機83中之灑水裝置84 ;其中, 於該下料管82上間隔設有用來控制該等爐塵8〇1下料之一 上閘閥821與—下閘閥822,並於該上閘閥821與下閘閥 822之間的該下料管82上,再設有一可控制下料速度之擋 板823;另,該攪拌機83是具有二可轉動之螺桿(圖未示) ,並連設有—可將經該攪拌機83攪拌後之濕式爐塵8〇1送 出之出料管831。 當乾的該等爐塵801經由該下料管82落至該攪拌機83 5 1341867 時’該灑水裝置84噴灑適量的水於該攪拌機Μ内该等 爐塵8G1經由關拌機83内轉動之雙螺桿混拌並推進至咳 出料管83卜進而掉落至位於該出料管831下方之_承載卡 車85令,該承載卡車85是具有_開放式料槽851,用以裝 ^落入之濕式爐塵8G1。上述習知高爐爐塵於出料過程時,、 疋错由該㈣機83内的濕泥狀爐塵8〇1之阻撐以產生阻 擋爐氣802外狀氣阻效果,防止有害之該等爐&謝 洩。 然而,在出料作業時,於該集塵槽81内所累積之該等 爐塵8(H的典型溫度約15(rc左右’因此,當該等爐塵謝 於該搜拌機83内受水調濕時,水會因受高熱而產生蒸氣, 致使大量蒸氣瀰漫於現場;再者,若該等爐塵8〇 1之溼度 不均時,極易在掉落於該承載卡車85之開放式料槽851内 的過程中,發生仍為乾燥之該等爐塵8〇1四處飛揚之現象 ,以致有污染廠區環境的不良現象,同時,更因該承載卡 車85之料槽851是為開放式狀態,也會造成該承載卡車85 運載該等爐塵801至堆存區之路途中及進行卸料的過程, 沿途有大量水蒸氣逸散或爐塵8〇1飛揚的狀況,此皆會導 致廠區週遭環境受到污染與破壞。 此外,多數業者均有回收該等爐塵801並予以進行造 粒作業,俾再次作為高爐之進料,達到節省部分進料成本 之功效。但是,由於此造粒作業所處理之該等爐塵8〇丨須 為乾燥粉料’因此’當使用上述所提及之現有濕式爐塵時 ’將使所出料之該等爐塵801夾帶有約13%之水份,故於 61341867 IX. DESCRIPTION OF THE INVENTION: TECHNICAL FIELD OF THE INVENTION The present invention relates to a method and system for discharging the same, and particularly to a blast furnace capable of completely preventing furnace gas from escaping and reducing the cost of recycling and recycling of the dust. Dry dust discharging method and system thereof. [Prior Art] At present, the blast furnace dust discharge collection operations carried out in various factories generally adopt the wet discharge method, that is, the conventional blast furnace is the original blast furnace when performing the dust discharge operation. The dust is sprayed to prevent the 13⁄4 furnace gas generated from escaping from the discharge pipe, which may cause harm to the on-site workers poisoning and gas explosion. Referring to FIG. 1 'the conventional wet dust discharge system includes a dust collecting tank 81 having a feed 811 and a plurality of furnace dust 801 and furnace gas 802 sent from a furnace (not shown). The tube 82 is disposed under the dust collecting groove 81 and communicates with the feeding port 811, and is disposed below the cutting pipe 82, and can receive the dust 801 and the furnace gas 802 from the discharging pipe 82. a mixer 83, and a sprinkler device 84 for sprinkling water into the agitator 83; wherein the lowering pipe 82 is spaced apart from the gate valve 821 for controlling the discharge of the dust 8? a lower gate valve 822, and a lower baffle 82 between the upper gate valve 821 and the lower gate valve 822, and a baffle 823 capable of controlling the cutting speed; and the agitator 83 has a rotatable screw (not shown), and connected to the discharge pipe 831 which can be sent out by the wet furnace dust 8〇1 which is stirred by the mixer 83. When the dry soot 801 falls to the mixer 83 5 1341867 via the lowering pipe 82, the sprinkling device 84 sprays an appropriate amount of water in the mixer to rotate the dust 8G1 through the mixer 83. The twin-screw is mixed and pushed to the coughing tube 83 and then dropped to the _ carrying truck 85 which is located below the discharging pipe 831. The carrying truck 85 has an open trough 851 for loading and falling into Wet dust 8G1. In the above-mentioned conventional blast furnace dust, during the discharge process, the fault is prevented by the wet mud-like dust 8 〇 1 in the (4) machine 83 to generate an external gas barrier effect of the barrier furnace gas 802, thereby preventing harmful effects. Furnace & However, during the discharge operation, the dust 8 accumulated in the dust collecting tank 81 (the typical temperature of H is about 15 (around rc). Therefore, when the furnace dust is thanked to the picker 83 When the water is conditioned, the water will be vaporized by the high heat, causing a large amount of steam to permeate the site; in addition, if the humidity of the dust 8 〇 1 is uneven, it is easy to fall on the openness of the load truck 85. During the process in the material tank 851, the phenomenon that the dust is still flying around 8〇1 is caused to be dry, so that there is a problem of polluting the environment of the plant area, and at the same time, the trough 851 of the carrying truck 85 is open. The state of the load will also cause the load carrying truck 85 to carry the dust 801 to the storage area and carry out the unloading process. A large amount of water vapor escapes or the dust of the furnace dust is flying along the way. The environment around the plant area is polluted and destroyed. In addition, most of the operators have recovered the furnace dust 801 and carried out the granulation operation, and once again used as the feed of the blast furnace to save part of the feed cost. The dust 8 processed by the grain operation is not required The dry powder 'supled' will use the existing wet dust mentioned above to cause the soot 801 to be discharged to have about 13% moisture, so that 6

Claims (1)

1341867 第_侧鮮物_充、紅後無割線、申請專利範圍·· 之說明書替換 1· 一種高爐爐塵乾式出粗 _ 出枓系統,適用於處理原物料噔一高 爐後所產生並儲置於— ^^同 該集塵裝置包括-且有Γ 多數爐塵及爐氣, 該集塵槽下方,且料:之集塵槽,及一設置於 高爐爐塵乾式出料系統包含: °玄 螺方疋运料機,位於該集塵裝置之第一下料管下方 且與之相連,並具有—將由該集塵裝置之S -下料管所 導入之該等爐塵排出之出料口,及一氮氣導入孔; -下料裝置,包括—第二下料管,該第二下料管具 有一與該螺旋送料機之Ψ # 很之出枓口相連,並能承接該等爐塵 之入a端 相反於該入口端之出口端,及-位於該入 口端與該出口端間之抽氣口; Μ 一密閉式槽體’包括—具有—顯現於外之入料口且 可容置該等爐塵之容室; 一抽氣單元,用以將該等爐氣柚離並防止逸散,且 該抽氣單元具有一與該第二下料管之抽氣口相連之抽吸 口; 一抽風官’該抽風管具有一與該第二下料管之抽氣 口緊密相連之第一端口,及一與該抽氣單元之抽吸口相 連之第二端口; 一調控裝置’裝設於該抽風管中,該調控裝置包括 皆分設於該抽風管上之—流孔板氣體流量計、—氣流量 調節閥、一管線關斷閥,及一氣體溫度計用以監督該抽 20 1341867 第〇%1448〇8號專利申請案補充、修正後無劃線之說明書替換阁年丨丨⑽日修⑷正替換頁 修正日期:99年11月 ' 風管於該等爐氣通過時之狀態,並隨之應對調控,以避 免溫升過高而燒毁;及 一尚壓氮氣導入裝置,其具有一與該氮氣導入孔相 接之官線,利用咼壓將氮氣經由該管線導入該螺旋送料 機中,以稀釋該螺旋送料機内之該等爐氣中的一氧化碳 濃度。 2·依據申請專利範圍第丨項所述之高爐爐塵乾式出料系統 ,其中,該下料裝置之第二下料管是為可伸縮管狀物。 3. 依據申請專利範圍第2項所述之高爐爐塵乾式出料系統 ,更包含一具有一與該集塵裝置之第一下料管相連通之 管線的高壓氮氣導入裝置,利用高壓將氮氣經由該管線 導入該第一下料管中,以稀釋該第一下料管内之該等燐 氣中的一氧化碳濃度。 Λ 4. 依據申請專利範圍第2項所述之高爐爐塵乾式出料系統 ,更包含一裝設在該螺旋送料機上之壓力指示計,以龄 控所導入氮氣之壓力。 5. 依據申請專利範圍第4項所述之高爐爐塵乾式出料系統 ,其中,該螺旋送料機更具有一螺桿驅動馬達二— 累杯驅動馬達之電流負載情況及該壓力指示計來, 該調控裝置之氣流量調節閥。 "控制 6. 依據申請專利範圍第5項所述之高爐爐塵乾式出 :其中,該槽體之容室更具有一排氣口,且該高爐爐2 乾式出料系統更包含一具有一儲氣空間之濾袋式指示件 ,該儲氣空間是與該槽體之容室連通,且該遽代曰一 〜衣·八指不 21 1341867 第嶋棚號專利申請案補充、修正後無劃線之說明書替換 件是顯現於外界。 依據申請專利筋圚笛= 項所述之咼爐爐塵乾式出料 ,更包含一中央栌制势 π糸統 導入裝置、該壓力於氣氧 日不计、該抽氣單元、及該螺旋送料 機之螺桿驅動馬達皆鱼夕φ β & 梵送抖 ,硬自與之電連接,以監控其等 載狀態。 电机負 8. 一種高爐爐塵乾式出料方法,包含以下步驟: 一承載疋位步驟’開啟-密閉式槽體之-入料 並將該入料口定位於— ^ , 端之正下方; 下以置之-第一下料管的出口 -啟動預備步驟’確認該第二下料管之 槽體之入料口是否接合緊密,接著啟動該下料敦置Λ -出料作業步驟’依序啟動一螺旋送料機、―’ 裝置之一第一下料管的— 集塵 下開閥及一上閘閥,播其 載於該集塵裝置之—隹庙冰μ ’承 開始; 置之1塵槽内之複數爐塵及爐氣之出料 乍業’。束步驟’當該槽體滿載該等爐塵 關閉該集塵裝置之第_下虹其M u 依序 禾下枓官的上、下閘閥,及吁碑 送料機;及 ^螺旋 一出料完成步驟’關閉該下料裝置,再將 置之第二下料營接斗软仏 卜科裝 業。 …移離該槽體之入料口,完成出料作 9.依據t料㈣圍第8項所狀高爐㈣乾以 ’更包含在泫啟動預備步驟與該出料作業步驟之間的二 22 1341867 酌年11月24日修(要)正替換頁 冬正日期:99车丨丨q ' 第隱4侧號專利申請案補充、修正後無劃線之說明書替換 1峰正日期:99车1丨 爐氣抽吸步驟,啟動一抽氣單元,並開啟-抽風管之- 管線閥門,調整適當抽齑旦 *礼里’利用負壓抽吸原理將該等 爐氣抽離。 1 0 .依據申請專利範图笼Q ^ 粑圍第9項所述之高爐爐塵乾式出料方法 ’其中’在該出料作業舟明(士 乍蒹^驟中,於啟動該螺旋送料機鱼 啟動該集塵裝置之第一下+ 恂〇 弟 卜枓官的下閘閥之間,調整由— 南壓氮氣導入裝置、、乞人$ 置庄玄螺紅送料機内的氮氣流量,以 稀釋該等爐氣中之一氧化碳濃度。 1 1 .依據申請專利範筮Q β丄 祀圍第9項所述之高爐爐塵乾式出料方法 其中,在该出料作業步驟中,;@ 啟動該集塵裝置之第一下…於_螺%送料機與 Κ弟下枓官的下閘閥之間,調整ά 一 高壓氣氣導入裝置注入該集塵裝置之第一下料管的: -量以稀釋遠等爐氣中之一氧化碳濃度。 •依據申請專利範圍帛1〇項所述之高爐爐塵乾式出 八中#在及作業結束步驟中’於關閉該集塵裝置之筮 先讓系統再持續運轉數分鐘後, 再關閉遠⑽氮氣導人裝置,停止將氮氣注人該螺 枓機内,最後再依序關閉該集塵裝置之第一^ 閉閥、該螺旋送料機,及該抽氣單元。 S的下 13 ·依據申請專利筋囹楚 ,更包人h 爐爐塵乾式出料方法 3 °x出料完成步驟後之一爐塵運離步 該槽體之入料口,击立丨m t ^ ’關閉 再利用一拖車將該滿載爐麈 離。 〜僧體拖 14.依據申請專利筘囹曾1<3 = /丄 J钯圍第13項所述之高爐爐塵乾式出料方去 23 1341867 第0961448〇8號專利申 I ------ 。薄莱補充、修正後無劃線之說明書替換样9年11月24曰修(要)正替換 ,其卜“ 、 該螺旋送料機之::二:=達錯由-中央控制器監挪 集塵裝置… 電流負載,來判斷該 i Ί否已達卸清該槽内爐塵之狀態。 二中。:在圍第14項所述之高爐爐塵乾式出料方法 ’、甲 在5亥承載定位步明1由 m Ba 軌步驟中,同時將該槽體之-排氣 口開啟,並將—滅袋式指 ' 分从旅 件罩合於該排氣口上,並在 6玄作業結束步驟中,由e,目丨g a f错由監測罩合於該槽體之排氣口上 之慮為式指示件是否因内部 ^ ^ ^ P爐塵卸清,而呈鼓漲狀態, 來輔助判斷該集塵裝置集 塵之狀態。 帛塵槽义否已達却清該槽内爐 241341867 The first _ side fresh _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ ————^ The same dust collecting device includes - and has a majority of dust and furnace gas, the dust collecting tank below, and the material: the dust collecting tank, and a dry blasting system disposed in the blast furnace dust containing: The screw hopper conveyor is located below and connected to the first discharge pipe of the dust collecting device, and has a discharge port for discharging the dust introduced by the S-feed pipe of the dust collecting device And a nitrogen introduction hole; - a feeding device, comprising - a second discharge pipe, the second discharge pipe having a connection with the 送 很 of the screw feeder, and capable of receiving the dust The inlet end of the inlet end is opposite to the outlet end of the inlet end, and the suction port between the inlet end and the outlet end; Μ a closed tank body includes - has - the inlet port appears and can be accommodated a chamber of the dust; a pumping unit for separating and preventing the pomelo Stopping and dissipating, and the pumping unit has a suction port connected to the suction port of the second discharge pipe; a drafting unit having a first connection with the suction port of the second discharge pipe a port, and a second port connected to the suction port of the pumping unit; a regulating device 'installed in the air exhaust pipe, the regulating device includes a orifice plate gas respectively disposed on the air exhaust pipe A flow meter, a gas flow regulating valve, a line shut-off valve, and a gas thermometer are used to supervise the pumping of the patent application No. 20 1341867 No. 1448 No. 8 (10) Daily repair (4) Replacement page Correction date: November, 1999 'The state of the air duct in the passage of the furnace gas, and then coping with regulation to avoid excessive temperature rise and burned; and a pressurized nitrogen gas introduction device And having a line connected to the nitrogen introduction hole, and introducing nitrogen gas into the screw feeder through the line to dilute the concentration of carbon monoxide in the furnace gas in the screw feeder. 2. The blast furnace dust dry discharge system according to the scope of the application of the patent application, wherein the second discharge pipe of the unloading device is a retractable tubular. 3. The blast furnace dust dry discharge system according to item 2 of the patent application scope further comprises a high pressure nitrogen gas introduction device having a pipeline connected to the first discharge pipe of the dust collection device, and nitrogen gas is used by high pressure. The first discharge pipe is introduced into the first discharge pipe to dilute the concentration of carbon monoxide in the helium gas in the first discharge pipe. Λ 4. The blast furnace dust dry discharge system according to item 2 of the patent application scope further comprises a pressure indicator installed on the screw feeder, and the pressure of the nitrogen introduced by the age control. 5. The blast furnace dust dry discharge system according to item 4 of the patent application scope, wherein the screw feeder further has a screw drive motor 2 - a current load condition of the tired cup drive motor and the pressure indicator, The air flow regulating valve of the regulating device. "Control 6. The blast furnace dust dry type according to item 5 of the patent application scope: wherein the tank body has a venting port, and the blast furnace 2 dry discharging system further comprises one a filter bag type indicating member of the gas storage space, the gas storage space is connected with the chamber of the tank body, and the 遽代曰一衣衣八指不 21 1341867 嶋 嶋 专利 patent application supplementary, no correction The replacement of the lined instructions is presented to the outside world. According to the application of the patented glutinous flute = the dry discharge of the furnace dust, further comprising a central 栌 势 导入 system introduction device, the pressure is not counted on the gas and oxygen day, the pumping unit, and the screw feeder The screw drive motor is yue φ β & Vatican shakes, hard to connect with it to monitor its load state. Motor negative 8. A blast furnace dust dry discharge method, comprising the following steps: a load carrying step 'opening - closed tank body - feeding and positioning the inlet port - ^, directly below the end; In order to determine whether the inlet of the tank of the second discharge pipe is tightly joined, the start of the first discharge pipe is initiated, and then the start of the discharge is completed. Start a screw feeder, one of the first unloading tubes of the device, a valve for dust collection and an upper gate valve, and broadcast it to the dust collector. The multiple dust and the discharge of the furnace gas in the tank are in use. The bundle step 'When the tank is full of the dust, the dust collector is turned off, the lower part of the dust collecting device, the upper and lower gate valves, and the arrow feeder; and the spiral one discharge is completed. In the step of 'closing the unloading device, the second unloading battalion will be connected to the soft bun. ...moving away from the inlet of the tank, and completing the discharge. 9. According to the t (four) circumference, the blast furnace (4) is dried to be included in the second step between the start preparation step and the discharge operation step. 1341867 On November 24th, the discretion of the year of the revision, the page is being replaced. The date of the winter is: 99 car 丨丨 q ' The second application of the patent application for the second hidden number is added, and the instruction without the line is replaced after the correction. 1 peak date: 99 car 1 In the furnace gas suction step, a pumping unit is started, and the - exhaust pipe - the pipeline valve is adjusted, and the appropriate pumping time is adjusted. 1 0. According to the patent application model cage Q ^ 粑 第 第 第 第 第 第 第 第 第 第 第 ' ' ' 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高 高The fish starts between the first lower part of the dust collecting device and the lower gate valve of the younger brother, and adjusts the nitrogen flow rate in the south-pressure nitrogen gas introducing device and the 乞人$Zhuangzhuang snail red feeder to dilute the nitrogen flow. The concentration of carbon monoxide in the furnace gas. 1 1. According to the dry method of the blast furnace dust according to Item 9 of the patent application, in the step of discharging, @Start the dust collection The first of the device is... between the _ screw % feeder and the lower gate valve of the younger brother, the first high-pressure gas introduction device is injected into the first discharge pipe of the dust collecting device: - the amount is diluted The concentration of carbon monoxide in the furnace gas. • According to the scope of the patent application 帛1〇, the blast furnace dust dry type is out of the middle eight. In the end of the operation step, the system continues to run after the dust collector is turned off. After a minute, turn off the far (10) nitrogen guide device and stop. Nitrogen gas is injected into the screw machine, and finally the first closing valve, the screw feeder, and the pumping unit of the dust collecting device are sequentially closed. The lower 13 of the S is based on the patent application, and further includes Man h furnace dust dry discharge method 3 °x discharge completion step one of the furnace dust transport away from the inlet of the tank, hit the 丨 mt ^ 'close and reuse a trailer to separate the full load furnace. ~僧体拖14. According to the patent application 筘囹曾1<3 = /丄J Palladium around the 13th item of the blast furnace dust dry discharge party to 23 1341867 No. 0961448〇8 Patent Application I ----- - The replacement of the thinlai, the revised no-line instructions to replace the sample 9 years November 24 曰 repair (to) is being replaced, its "", the screw feeder:: two: = wrong by - central controller The dust collecting device... The current load is used to determine whether the i Ί has reached the state of removing the dust in the tank. II.: The dry blast furnace dust discharge method described in Item 14 The sea bearing positioning step 1 is performed by the m Ba rail step, and the air outlet of the tank is opened at the same time, and the - bag type finger is divided into the travel pieces. Cooperating with the exhaust port, and in the 6-end operation end step, by e, the gag is wrongly monitored by the monitoring cover on the exhaust port of the trough, whether the type indicator is due to the internal ^ ^ ^ P furnace dust Unloading, and in a drum-up state, to assist in judging the state of dust collection by the dust collecting device.
TW96144808A 2007-11-26 2007-11-26 Exit system of dried furnace duct of blast furnace and process thereof TW200923105A (en)

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Application Number Priority Date Filing Date Title
TW96144808A TW200923105A (en) 2007-11-26 2007-11-26 Exit system of dried furnace duct of blast furnace and process thereof

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TWI341867B true TWI341867B (en) 2011-05-11

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