TWI312334B - Method and apparatus for the pneumatic conveying of solids - Google Patents

Method and apparatus for the pneumatic conveying of solids Download PDF

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Publication number
TWI312334B
TWI312334B TW93136087A TW93136087A TWI312334B TW I312334 B TWI312334 B TW I312334B TW 93136087 A TW93136087 A TW 93136087A TW 93136087 A TW93136087 A TW 93136087A TW I312334 B TWI312334 B TW I312334B
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Taiwan
Prior art keywords
coal
solid
transport
flow
pulverized
Prior art date
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TW93136087A
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Chinese (zh)
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TW200526497A (en
Inventor
Holger Wulfert
Walter Hartig
Horst Zewe
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Loesche Gmb
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Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/001Injecting additional fuel or reducing agents
    • C21B5/003Injection of pulverulent coal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00Treating solid fuels to improve their combustion
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/02Making special pig-iron, e.g. by applying additives, e.g. oxides of other metals
    • C21B5/023Injection of the additives into the melting part
    • C21B5/026Injection of the additives into the melting part of plastic material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B1/00Shaft or like vertical or substantially vertical furnaces
    • F27B1/10Details, accessories, or equipment peculiar to furnaces of these types
    • F27B1/16Arrangements of tuyeres
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00Charging; Discharging; Manipulation of charge
    • F27D3/18Charging particulate material using a fluid carrier
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/005Separation by a physical processing technique only, e.g. by mechanical breaking
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/02Working-up flue dust
    • 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

Description

1312334 九、發明說明: 【發明所屬之技術領域】 〜本發明係有關一種依照申請專利範圍第^項前言之用 於固體之氣動運輸的方法,以 申請專利範於施行依照 不1 υ項刖5之方法的設備。 【先前技術】 在許多技術領域中,如何將固體運輸經過管路係 的重要。此結果容許輸送作用發生於密閉管路内,其中即 將被運輸的材料—開始是會 成细小如亦鹿,而且特別是會被粉碎 至於所/ 接著再與—運送介質或運輸介質相混合。 是礼氣運送介質,特別是由運輸氣體所組成,例如 一 口工轧’或是具有相當高濃度二氧化碳之煙道氣。 =輸作用的產生係藉由於運輸區段部位起點與終 來決定,亦^ 輸作用的效果好壞係由若干項參數 '、卩固體的精細度和顆粒尺寸分佈狀況, 載情形 '黏度和運送介質的溫度。 及衣 已知與在高爐中產生驻鐵有關之内容,藉由鼓風煤炭 :之作用而被$入的熱風係會被吹入至高爐内,上述之煤 仄灰則疋被用來作為替代還原劑/用於焦炭之替代燃料,亦 即是依照粉碎煤炭注入(pci)程序或其他加工程序,用以 =^爐操作H濟性’特別是減少焦炭的消耗量,同時, 行到相㈣的面爐操作穩定度和增加高爐的使用效率。 於疋例如疋在2002年5月出版之Paul furth S A 公司型錄粉碎煤炭注人系統”中,其中描述了依照粉碎煤 1312334 反注入裎岸夕田, 動佴岸焊户太 煤炭灰的粉碎用設備和具有用於氣 術和設傷種類亦被加設備,以及加工技 備是以壓'縮惰氣( :王性的要求’注入設 * 55 ^ . 疋鼠乱)來4呆作,至少是在圓筒倉 W今态内作動。投山七 為 ’、火火之氣動運輸作用幾乎是以一種被稱 僅合產生非=輪的方法來施行,特別是會造成於管路内 μ ^ ^ ^ . 磨耗以及相較於薄層運輸方法,厚 a動運如方法的氣體消耗量是非常低。 在一種粉碎乾燥設備中 適宜㈣機開始疋於一相對應的 汽入沾卜 碎和乾趣。接著,可能是來自一圓 二煤炭會進入至該注入設備内和進入至一個分配容器 =1配容器本身則是會受到氣體所施加的壓力。隨後, &動性的問題出現於該 配备°°之出口區域内和額外地出 現方;藉由增加一運輪备挪/ 々命 運輪氣體(例如是氮氣)所產生之後續管 煤厌灰€成可以被輸送。結果導致相 :::路’分配容器内具有過高的壓力,煤炭是 内被施=壓力和被輸送至後續的使用位置點。當煤炭灰被 /主入至兩爐内時,以上έ士婁沾— ^ 'π果的元成則是藉由高爐鼓風口之 作動。 心 a煤炭灰的計量或是使用(亦即是控制煤炭灰的流量) 疋二以藉由相對應改變在輸送區段部位上之壓力梯度或是 改變在該輸送區段部位内 一 U <硬翰虱體流量而得到。另外, 亦可以結合管路控制閥’這些管路控制閥的自由通道開口 是可以被調整。接著’一個控制間會被結合成具有流量測 1312334 里力%,—個控制迴路得以被成形。 已知問題會出現於煤炭灰( 之煤炭灰)的運輸作用上。此門題向爐注入設襟内 之型式出現於、、主入… 係例如是振動或堵塞 段部位内,㈣「:中。倘若控制閥被結合至該運輸區 振動,並且由=部:r夠以未受控制之方式而產生 即將被運道,该控制閥亦容易被阻塞。 粒尺寸分1?料的材料性質(特別是粒狀程度和顆 要。另外況)對於所發生之問題和後續問題是很重 亦有特定的材料性質是經常無法被完全評估。 之表現結實μ,可流動性和運輸與控制 苹此烊山巾的差異性。因此,相較於其他煤炭, 杲二塥厌的黏性較高。 在&路内氣動運輸煤炭灰有關的問題可以導致於後 程序和用錢續使用之位置點出現相當大的缺點。 因e知煤厌灰的注入速率和全部煤炭灰流量控制的精 雀:句s大幅影響到煤炭灰注入作用的效果,於是,影響 幻、盧操作的經濟性。在注入管線内的問題會對於整個高 爐的知作程序產生負面影響,進而造成链鐵的生產成本增 加和品質降低。 【發明内容】 I本發明之目的係在提供一種方法和一種設備,用以改 °在&線内之固體的氣動運輪狀況,並且後續的加工程序1312334 IX. Description of the invention: [Technical field to which the invention pertains] ~ The present invention relates to a method for pneumatic transportation of solids in accordance with the preamble of the scope of the patent application, in which the patent application is applied in accordance with paragraph 5 The method of the device. [Prior Art] In many technical fields, how to transport solids through a pipeline system is important. This result allows the transport to take place in the closed conduit, where the material to be transported - initially becomes as small as a deer, and in particular will be shredded as to/and then mixed with the transport medium or transport medium. It is a ritual transport medium, especially composed of transport gas, such as a factory or a flue gas with a relatively high concentration of carbon dioxide. = The production of the transmission is determined by the starting point and the end of the transportation section. The effect of the transmission is also determined by several parameters ', the fineness of the solid and the distribution of the particle size, the loading situation 'viscosity and transport The temperature of the medium. The hood is known to be related to the production of iron in the blast furnace. The hot air that is entangled by the action of blasting coal is blown into the blast furnace, and the above-mentioned coal ash is used as an alternative. Reducing agent / alternative fuel for coke, that is, according to the pulverized coal injection (pci) program or other processing procedures, used to control the consumption of coke, especially to reduce the consumption of coke, and at the same time, to the phase (4) The furnace operation stability and the efficiency of the blast furnace are increased. Yu Yu, for example, Paul Furth SA, published in May 2002, catalogue of crushed coal injection systems, which describes the crushing equipment for coal ash in accordance with the smashing coal 1312334 And the equipment used for gas and the type of injury is also added, and the processing technology is based on the pressure of the inertia (the requirements of the king's requirements, *55 ^. Mole), at least In the state of the cylinder warehouse W. The mountain is seven, 'the pneumatic transport of the fire is almost a method that is said to produce only non-wheels, especially in the pipeline μ ^ ^ ^ . Abrasion and the gas consumption of the thick a transport method is very low compared to the thin layer transport method. In a pulverizing and drying equipment, the appropriate (four) machine begins to smash a corresponding steam in the smashing and dry Then, it may be that from a round of two coal will enter the injection equipment and into a distribution container = 1 the container itself will be subjected to the pressure exerted by the gas. Subsequently, the problem of mobility occurs in the equipment ° ° within the exit area and extra The appearance of the tube; the subsequent tube coal ash can be transported by adding a wheel to prepare the gas/forward wheel gas (for example, nitrogen). The result is that the phase::: road 'distribution container is too high The pressure, the coal is applied internally = pressure and is transported to the subsequent use point. When the coal ash is/into the two furnaces, the above gentleman's dip - ^ 'π fruit is formed by the blast furnace The operation of the blaster. The measurement or use of the coal ash (that is, the flow rate of the coal ash) is controlled by changing the pressure gradient at the conveying section or changing the location of the conveying section. In the U-lt; hard 虱 body flow obtained. In addition, can also be combined with the pipeline control valve 'the free passage opening of these pipeline control valves can be adjusted. Then 'a control room will be combined to have flow measurement 1312334 Lili%, a control loop can be formed. Known problems will occur in the transportation of coal ash (the coal ash). This type of problem is injected into the furnace and the type appears in the main... Is vibration or blockage In the section, (4) ":. If the control valve is combined to vibrate in the transport area, and the = part: r is enough to be transported in an uncontrolled manner, the control valve is also easily blocked. The material properties of the material (especially the degree of graininess and the size of the particles) are very important for the problems and subsequent problems that occur, and the specific material properties are often not fully evaluated. The performance is strong, μ Mobility and transport and control are different from each other. Therefore, compared with other coals, the viscosity of the cockroaches is higher. The problems related to pneumatic transport of coal ash in the & road can lead to post-procedures. And the use of money to continue to use the location point has a considerable shortcomings. Because of the knowledge of the coal injection rate of gray ash and the control of the entire coal ash flow: sentence s greatly affect the effect of coal ash injection, so, the impact of magic, The economics of the operation of Lu. Problems in the injection line can have a negative impact on the know-how of the entire blast furnace, which in turn leads to increased production costs and reduced quality of the chain iron. SUMMARY OF THE INVENTION I. The object of the present invention is to provide a method and an apparatus for modifying the condition of a pneumatic carrier of a solid within a & line, and subsequent processing procedures

亦·ίΘ 5 I 户于到正面影響。特別是能夠將在高爐之注入設備内的煤 人運輸狀況予以最佳化和減少所可能出現的錯誤與問 1312334 題。 依照本發明’以上目的之得到係藉 項特點的方法,以B M i b τ明專利靶圍弟1 備。本㈣之二及藉由申請專利範圍第〗6項特點的設 利範圍中和隨附圖形之描述内容中。 於心後申,月專 本發明係依據藉由增加特定比例之至 而能夠顯著•盖y· & 種其他材料 ‘、 。在官路中固體之氣動運送過裎mi 制表現結果。以” 如的運輸和控 同具有黏性之固增加的添加劑以是連 另々f之固體或灰塵為特別有利。 已::倘若二種材料具有相當大的密度差異時 與添加劑混合在一起是 體 劑可以β一❹ 巾文善其可流動性。此添加 看,二二料或一種材料混合物。從此方法之觀點來 :该添力:劑疋能夠在粉碎固體之前、期間或之後㈣ 入至固體夕中亦I以將相對應之粉碎過型式添加劑額外地加 " 添加劑是被加人至運輸區段部位之前或是 部位内’而且以是被加入至運輸管線之起點= 於計量閥的上游處,用以控制住位於個 不同注入管線上的固體产吾 處的固體流量。 ”制W分佈機構之下游 有關於在管線内運輸煤炭灰,特別是在位於高爐鼓風 口内之注入煤炭灰上,已知經由包含鐵/氧化鐵之材料(特 別是輾麗碎片)之混合作用,是能夠大幅改善精細粉碎過 之煤炭的可流動性。 已知煤厌灰之改良過運輸特性會導致計量間或控制間 1312334 的操作得到大幅改進。此計量闕例如是被使用於具有單一 要素控制方法之煤炭灰注入設備中,其中是具有一種獨 立、連續式量測方法和控制住在注入管線内之煤炭灰流 量’用以將煤炭灰注入至一高爐鼓風口内。由於單一要素 控制方法之作動,煤炭是會被非常均勻地分佈於高爐周邊 部位之上。 此外’在具有單一要素控制方法之煤炭灰注入設備内 的氣氣或若干其他運輸氣體之特定消耗量是相當低,此結 果亦有助於南爐的作動程序得到最佳化。 在個別不同煤炭灰注入管線内之計量閥和控制迴路亦 可以被使用於注入設備内,其中全部煤炭灰之流動是以受 到控制之方式而被分佈至個別不同的注入管線上。在此種 設備中,一個流量測量機構和煤炭灰計量閥是會被安裝至 每一個位於一靜態分配器之下游處的注入管線内。 單一要素控制方法之優點,或是在氣動運輸系統中使 用計量與控制閥是能夠克服由於閥門和注入管線被堵塞所 可旎產生的操作問題,以及解決控制迴路產生振動和由於 無法控制之振動所帶來的缺失。 由於流動改良劑連同固體之新創混合作用,以上之缺 失均能夠被避免。此結果已經由煤炭灰與相混合之輾壓碎 片的測试作用而得到證實。藉由相混合之輾壓碎片的動 作,具有煤炭灰之運輸氣體能夠被更加均勻裝填,進'、 少控制閥與運輸區段部位之阻塞或是堵塞現象的產生而減 倘若被人入至注入设備内的煤炭灰是與輾壓碎片戋類 1312334 似材料相混合時,、、 將會被大幅減少。…主入設備之控制迴路產生故障的情形 除了輾壓碎Η # 能夠與其他的流勤 含鐵材料以彳,上述之煤炭灰亦 塵例如是煙道力卩良劑灰塵相混合’這些流動改良劑灰 特別有心=塔沈積物和缚造用隔室沈積物。 最終使用裝置或=用Τ良添加劑是能夠有效改善 良添㈣是可程序的作動情形,而且該流動改 如是在後續高^ 料用亦可以被應用至例 物之灰塵。…卫程序中的輾壓碎片和含有鐵/鐵氧化·· Θ 5 I have a positive impact. In particular, it is possible to optimize the transport situation of coal in the blast furnace injection equipment and to reduce the possible errors and problems. According to the present invention, the method for obtaining the characteristics of the above-mentioned objects is prepared by the B M i b τ 。 patent target. This (4) bis and the scope of the application by the characteristics of the application of the scope of the sixth paragraph and the description of the drawings. In the case of the heart, the invention is based on the fact that by adding a certain proportion, it is possible to cover the y· & other materials ‘, . In the official road, the solid pneumatic transported the performance results of the 裎mi system. It is particularly advantageous to transport and control additives with viscous solids to add solid or dust to the other. It has been: If the two materials have considerable density differences, they are mixed with the additives. The body agent can be used for the flowability of β. The addition of the two materials or a mixture of materials. From the point of view of this method: the addition force: the agent can be added before, during or after the pulverization of the solid (four) In the case of a solid shovel, I add an additional additive to the pulverized type additive. The additive is added to the front or part of the transport section and is added to the starting point of the transport line. Upstream, used to control the solids flow of solids at different injection lines. "The downstream of the W distribution mechanism is about transporting coal ash in the pipeline, especially in the blast furnace blast inlet. In the above, it is known that the fluidity of the finely pulverized coal can be greatly improved by the mixing action of the material containing iron/iron oxide (especially the shards). It is known that the improved transport characteristics of coal ash can lead to significant improvements in the operation of the metering or control room 1312334. This metering is used, for example, in coal ash injection equipment with a single factor control method, which has an independent, continuous measurement method and control of coal ash flow in the injection line to inject coal ash into Inside a blast furnace blaster. Due to the single element control method, coal is distributed very evenly around the blast furnace. In addition, the specific consumption of gas or several other transport gases in coal ash injection equipment with a single factor control method is quite low, and this result also contributes to the optimization of the operation of the South Furnace. Metering valves and control loops in individual different coal ash injection lines can also be used in the injection equipment where all of the coal ash flow is distributed to individual injection lines in a controlled manner. In such an apparatus, a flow measuring mechanism and a coal ash metering valve are installed in each of the injection lines located downstream of a static distributor. The advantages of the single element control method, or the use of metering and control valves in pneumatic transport systems, are able to overcome operational problems due to blockage of valves and injection lines, as well as to address vibrations in control loops and vibrations due to uncontrollable vibrations. The lack of bringing. Due to the new combination of flow improvers and solids, the above defects can be avoided. This result has been confirmed by the test effect of coal ash and mixed crushed chips. By mixing the crushing debris, the transportation gas with coal ash can be more uniformly filled, and the control valve and the transportation section are blocked or blocked, and if it is injected into the injection When the coal ash in the equipment is mixed with the material of the smashed debris 1312334, it will be greatly reduced. ...the situation in which the control circuit of the main equipment is faulty except for the crushing Η# can be mixed with other ferrous materials such as ash, and the above-mentioned coal ash is also mixed with dust such as flue gas and good agent dust. The agent ash is particularly hearty = tower deposits and compartmental deposits. The final use of the device or the use of the good additive is an effective way to improve the improvement of the good (4), and the flow can be applied to the dust of the sample if it is used in subsequent high-level applications. ...the rolling debris in the program and the oxidation of iron/iron

對於固體可法知llL 運輸作用發生故二二方案的重要優點是減少 省輸送介質C輸氣體之裝填量,•而導致節 果' 。於注入設備内的煤炭灰計量或是控制結 . ^ .. 被加入至煤厌灰中,此結果亦有助於加 速在馬爐加工程序内的燃燒速度。 想严二外一優點係在輾軋加工操作中被製造出相當大量的 輾P片和類似材料是會被其本身與煤炭灰之混合作用合 理與有效地採用。 已知*動煤炭灰碎片混合物所具有之報壓碎片含量為 3到15 *量百分比、容積密度大約為〇·7公噸/立方公尺和 :狀程度為80到70百分比小於9。微米,以上這些特性於 氣力運輸操作日守疋無法產生分離現象。改良過之氣動運動 操作則能夠有效地增加煤炭灰的生產量。 對於氣動ϋ輪操作和控制煤炭灰之&良結果亦有助於 10 1312334 煤炭灰碎片混合物的加工程序 刷拭作用”,達而導致得到媒山〇工種序被稱為是,,鐵絲 在運輪管線和計量闕尹、::減主入作用的最佳化。已知 =降低煤炭灰伽合物㈣塞狀公=導:, 精確度的增加,並且結合全 t…致控制 另外,管路、計量閥等元件亦^口私序之相關優點。 ^ ’、不會因此而增加磨耗量。 外’亦可—物材料- ::。此:,此種礦物材料亦同時能夠= 用。生有瓜的作用。煤屑的品質亦會受到此種添加劑的作 特別是當使用振壓碎片時,拉則古本丨> 士二 y ^ ^ f特別有利之處為該輾壓碎 月月匕夠承受一整合式粉碎作用 外卞用特別疋—種粉碎、乾燥與 厌相結合之作用。此輾壓碎片亦可以被進給至一個從煤 炭分離或是採用特殊還原劑的輾粉機。然而,必須適宜地 :-混合用裝置(例如是一混合用床或—混合用鼓)内製 造出一粗煤炭碎片混合物,並且將該混合物進給至一輾粉 機内。 1 煤炭或一些其他還原劑或還原碳混合物與一碎片材料 或一些其他含有鐵/鐵氧化物材料的整合式粉碎作用是能 夠在所有適宜之粉碎系統和輾粉機内被施行。 —種在一 Loesche型滾子輾粉機内的整合式粉碎作用 是特別節省成本、合理與有效率。已知影響到一粉碎加工 長序之特定參數’例如是特定功率需求和輾粉機的功率因 1312334 子是=會受到由於將大約3%到15%輾壓碎片混合至—坑 2 2或此合至一坑煤與石油焦炭之混合物内所帶來的負面 影f。顆粒尺寸的分佈狀況幾乎是大致相同,亦即是僅有 非d的差異係產生於50%趵〇挪到〇 〇5% :用對於特定功率需求,介於-純梓的 作用贫連同碎片的粉碎作用之間。由於在混合物内之 比例:增加,甚至是輾粉機的功率需求亦可以被減少。 〜有輾壓碎片之煤炭灰的改良過運 現係有助於煤炭顆粒與碎片成份之間的緊 If 由於整合式粉碎加卫程序所帶來的連―特別是 入之方4 ^ 、、,°果,碎片顆粒是以注 附者至煤炭灰顆粒’使得分離加工程序益法 產生。上述之,,鐵絲刷拭作用,,亦有助於 : :度差異的材料。於是,煤炭的密度⑴到:二 方么为,同時,碎片的密度則是 .克立 輾㈣和—些其他的特別含::克/立方公分。 成-個介於…㈣之間的範=加:是可以被混合 〇/ ξι, ! ,0/ ^ „ y 耗㈤内’較佳地係介於3 /。到⑸之間。假設碎片材料所具 是30%到80% 。 、载或鐵氧化物含量For solids, it is known that llL transport occurs. The important advantage of the two-two scheme is to reduce the loading of the transport medium C transport gas, which leads to the result. The coal ash metering or control knot in the injection equipment is added to the coal ash, which also helps to accelerate the burning rate in the horse oven processing program. The advantage of being a stricter one is that a considerable amount of bismuth P sheets and similar materials are produced in the rolling processing operation and are rationally and effectively employed by their own mixing with coal ash. It is known that the mixture of moving coal ash debris has a content of reported fragments of 3 to 15 * percent, a bulk density of about 7 metric tons per cubic meter, and a degree of 80 to 70 percent less than 9. Micron, these characteristics can not be separated during the pneumatic transport operation. Improved aerodynamic motion operations can effectively increase the production of coal ash. For the pneumatic boring wheel operation and control of coal ash & good results also contribute to the processing of 10 1312334 coal ash debris mixture processing procedures, which led to the acquisition of the media mountain planting order is called,, the wire is in operation Wheel pipeline and metering 阙 Yin, :: reduction of the main input effect. Known = reduce coal ash gamma (four) plug-like public = guide:, increase in accuracy, and combined with full t... control The components such as roads and metering valves are also related to the private sequence. ^ ', will not increase the amount of wear. External 'can also material materials - ::. This:, this mineral material can also = use. The quality of coal chips is also affected by the use of such additives, especially when using vibrating debris, Laguna Guben > 士二 y ^ ^ f is particularly advantageous for the 辗 crushing month It can withstand an integrated pulverization effect. It is specially used for the combination of pulverization, drying and anaerobic. This smashed shard can also be fed to a pulverizer that is separated from coal or uses a special reducing agent. However, it must be appropriate to: - a mixing device (for example A mixture of coarse coal fragments is produced in a mixing bed or a mixing drum, and the mixture is fed to a powder mill. 1 Coal or some other reducing agent or reducing carbon mixture with a piece of material or some other containing The integrated comminution of iron/iron oxide materials can be carried out in all suitable comminution systems and powder mills. - The integrated comminution in a Loesche roller pulverizer is particularly cost effective and reasonable. Efficiency. Known specific parameters that affect the long order of a pulverization process 'for example, the specific power demand and the power of the pulverizer are 1312334 = will be affected by mixing about 3% to 15% of the smashing debris to the pit 2 2 Or the negative effect brought by the mixture of coal and petroleum coke. The distribution of particle size is almost the same, that is, only the difference of non-d is generated from 50%. 〇5%: used for specific power requirements, between the effect of pure 梓 and the comminution of the smash. Because of the ratio in the mixture: increase, even the power demand of the pulverizer To be reduced. ~The improved coal ash with rolling debris helps the tightness between the coal particles and the debris components. ^, ,, ° fruit, the debris particles are attached to the coal ash particles 'to make the separation process process profitable. The above, the wire brushing action, also helps:: the difference in the material. So, The density of coal (1) to: the two sides, at the same time, the density of the debris is. Keli (four) and some other special:: g / cubic centimeter. Cheng - a range between ... (four) = plus : It can be mixed 〇 / ξι, ! , 0 / ^ „ y consuming (five) within 'better' is better than 3 /. Between (5). Assume that the fragment material is 30% to 80%. , or iron oxide content

依照本發明之爭j隹 jK 乃之更進-步發展結果, 他還原劑或還原碳混合物是會混 —-$厌或一二其 料或-些其他含鐵/鐵氧化物的材;^’除了—碎片材 是一粉碎鬆軟團塊)是可以芦由、/卜’粉碎粗粒(例如 動之方式被進給至-高爐内錯由—庄入設備之作用而以氣 另外,必須適宜地於一適宜輾粉機内粉碎該粉碎粗粒 12 I312334 :挺煤炭和碎片材料’再將其進給至—注以備或一儲 I各器内。粉碎粗粒的密度通常是小於公克/立方公 二此密度值是不同於粗煤炭的密度,特別是不同於輾壓 τ片的密度。 因此,有利之處為能夠以氣動之方式來運輸—煤炭碎 Θ私碎粗粒的混合物。 在煤炭碎片混合物内之拾边h k 円之叔碎粗粒的比例以是相當低為 传T,例如是大約°·5到1重量比。此佔有比例基本上 粉碎粗粒或粗碎鬆軟團塊的成份來決定。此佔有比例 I別是會被加以選擇,使得在述鐵和鋼的製造過程中, ,、屯物的限度必須是無法被超過。 /、粉碎粗粒所具有的平均、較低熱值為32. 5百萬焦耳 :公斤、-灰燼含量是小於1。重量比和一殘留蒸氣含量是 9、於1重量比,連同一平均含碳量是73重量比、氫含量是 3. 〇重里比、氮含量是2· 2重量比和下列平均數值:氧化鈣: 二6重里比、氧化矽:3· 〇重量比、氧化錳·· 〇. 8重量比、 乳:鈦:〇. 7重量比、氧化鋁:°. 7重量比、氧化鐵:。· 3 重里比,以上這些成份的數值是適合用於具有粗煤炭、碎 ^材料之整合式粉碎作用,例如是在一垂直式輾粉機内, 亚且用於經由高爐鼓風口的隨後氣動運輸操作與計旦 作用。 〇 13里進給 與粉碎粗粒相關之優點是特別合理、有效使用,伴& 著符合相肖應之環保法規的要纟。 飞 在本發明之範圍内的内容為:於粉碎設備之下游處 13 1312334 混合碎片材料或—含鐵,鐵 至鼓風口内連同替抑物之添加劑,並且將其進給 白八的還原劑。& 且特別是呈灰雇刑々 接考被適宜加以粉碎,而 生主式之該添加劑是 替代還原劑(例如是煤户太 疋了以被加入至一個用於 被加入至該館存玄哭&厌火之儲存容器的上游處,或是 倘若該添加劑是會胃 歹1 D疋鼓風口的上游處)。 項接續著煤炭或— 彳彳產生不利的影響,一 二,、他替代還原杳丨 給動作則是特別適宜。 a碎作用以後的進 注入設備内或在注入容:至,主入设備之上游處或在該 劑所具有的有利作用將二實例 依照本發明之設備二後續的“閥内。 、…“ 疋具有至少-種採用該添加劑作為 —流動改良劑的進給裝置。 刀月Η乍馮 置β : : *叶里作用之煤炭灰注入設備中,此進q 置是可以被安晋热社、+ 适”·口衰 攸文罝於該〉主入設備之 内。在具有單一钭旦从 次疋在该注入設備 彳里作用之煤炭灰注入設備中,1 一個以氮氣作為運輸氣體 ;;/、有 4、古一伽,富认 > 询矾體令益或壓力容器,至 運輸軋體能夠被進給至其中 器,-個分配衮哭… ^之運輸谷益或分配容 ……或—個於出口側邊上具有可流動錐體的 口二/於不同注入管線的計量閥與一個高爐之鼓風 …上述二進給動作是可以發生於一個儲存容器或用於煤 /反/的上游處,和/或發生於運輸容器的上游處和 或分配容器或注入容器的上游處’使得在意欲得到之顆粒 尺寸分佈狀況中的流動改良劑能夠與煤炭灰相混合。 如同先前所描述之内容,結合煤炭灰一起作動和具有 14 1312334 有效作用的可流動性係發生於計量閥β,以及在 内和在高爐之加工程序中。 ^秦 在-較佳之設備型式中’藉由增加明確界定 (特別是輾壓碎片)比例而被用來改善㈣(特別是 幻之氣動運輸操作的設備包含有一概粉設備,= 炭碎片混合物係會被進給至—輾粉機(特別是—垂” Loeshe型滾子輾粉機)和承受到先前所提及之粉碎:直 工程序。接著於一例如是過據器内分離出煤炭灰碎二:二 物’該混合物是能夠被儲存於一儲存容器内,再二 容器内被進給至煤炭注人設備’此煤炭注人設備本子 具有運輸容器或分配容器和一儲# $器或注入$器,連: 具有流量測量機構和用於將煤炭灰個別注入至鼓風: 量閥的注入管線。 有利之處為輾粉設備可以採用低成本之方式而被安置 成能夠混合或增加粉碎粗粒’用以結合粗煤炭和碎 來完成整合式粉碎作用。 煤炭灰能夠破適宜地與一流動改良劑相混合,此流動 改良劑特別是-碎片材料和其部份比例為粉碎粗粒,:得 特別是在氣動運輸之過程中不致於發生分離的現象。 依照本發明,現有最佳的注入設備是具有單一計量作 用,亦即是具有用於控制個另『煤炭灰流入至個別注入=線 内的計量閥’藉由混合-流動改良劑,用以精確地控制住 煤炭灰的流動。由於其較窄通道所產生之問題,例如是在 注入管線内之振動或堵塞,或是在控制迴路中之益法^制 15 1312334 振動’連同被阻塞之計量閥亦可避免出現。 依照本發明之設備能夠導致在運輸區段部位和計量 内的磨耗快速減少,並且改善計量和控制表現結果,對於 後續加工程序(例如是高爐加工程序)產生有利的作用。 【實施方式】 ° +圖1言兒明依照本發明《方法與設#,此方法與設備係 藉由一用於含碳流體混合物之粉碎和注入設備的作用,此 含碳流體混合物並且是連同埶風一 《u…、凤起被進給至尚爐鼓風口 内。 上述之含碳流體混合物包含有一流動改良劑33, 進入至-氣掃式滚子輾粉機2内而被加以粉碎之前… 動改良劑是會與固體30 (亦即是粗煤炭6)相混合。在: 項實施例中,用於流動改良齊"3 (例如是輾塵碎 材料7)之進給裝置是一個煤倉17 ’並且該碎片材料 錯由一碎片分配器14 <作用而被進給至—混合用裝 内。在該混合用裝置5内,辟g敁杻7 β人t 4 碎片材枓7疋會與即將被粉碎 之煤厌6相混合,並且從一煤炭堆8而進入至一粗煤 16 ’經由-煤厌分配器15而到達該混合用裝置同時, 該混合物是藉由-運輸用裝£ 4之作用而被進 式滚子輾粉機2内。 & # 在此氣掃式滾子輾粉機2内,其中係藉由_ 之協:力而能夠完成粉碎乾燥作用,在此項實施例中,、二 性氣❹產生於—熱氣產以1被進給至該氣掃式^ 操粉機2内之粗煤炭碎片混合物是包含有預先設定比例的 16 1312334 ::::7,該預先設定比例以是3%物為較適宜。隹 ::力物是採用與將粗煤炭粉碎成煤炭灰之相同方 式而被加以粉碎和篩選。煤 ^方 遽'器12内的惰性氣體”被分離片二物疋從位於-過 流入至-儲存容器2◦。出未’並且經由-吊桶輪 藉由一運輸管線或連結管線 是合被逑紝s 、 篆仏之作用,该儲存容器20 θ —2中僅表不出—個運輸容器22)是會被來 -屋力容器21之作為運輸氣體的氮氣施加壓力。此煤炭 :碎片混t物是於分配容器或運輸容器22、23内流動,另 亦可名員外地伴隨著加入其他的輪送用氣體,並且該煤 厌人碎片混合物是經由運輸管線25而進人至-注人容器24 内。 圖2表示出具有單一要素控制方法之煤炭灰注入設傷 的概略配置圖形,1 Λ lL w^ —其中此煤厌灰碎片混合物是藉由一分配 容器 '之作用而被進給至-注入容器24内,此分配容器 22—本身疋破配置有—#重用裝置39,接$,再藉由被提供 每個7主入管線26内的計量閥36之作用,該煤炭灰碎 片:合物是广被進給至-高爐28的鼓風口 27内,其中注 ^ 疋位於被安置在注入容器2 4之出口側邊處的流 動用錐體28之下游處。(參考圖1)。 在每個例子中’該個別的注入管線26係會被連結至高 的S支風口 27 (參考圖1 ),在此實施例中,此高爐28 的鼓風口 27係代表著使用裝置。 17 1312334 在流動用錐體38的附近(參考圖 體(例如是作為流體或運輸氣體之氮 :由一惰性氣 灰/碎片混合物會產生更進一步流動助’該煤炭 額外地從壓力容器21内被進給出來。生氣體則是 用來作為-個加壓該運輸容 力容器是被 每一項應用實例中的流動氣體均衝容器。在 圖2亦表示出用於控制住煤炭灰」:進給。 別不同注入管線26内之數量的控制迴路3; ^入至個 汽體二片混合物能夠_當多的優點。在 /一合物中疋代表著流動改良劑33 在 運輸氣體連同煤炭顆粒-起被均勻裝填,減少:二 Μ内和於注人管'線26 W且塞或堵塞的現象:此項= 則可顯著改善計量闕或控制間”的操作狀況(袁考圖『果 導致產生—個被稱為是”鐵絲刷拭作用,,之結果,用以改蓋在 禮产有助於輸與控制情形。所增加的控制精 確度有助於k升向爐加工程序之穩定性和柱鐵之品質。欽 而,不致於增加在運輪瞢綠9 g …、 【圖式簡單說明】線25和注入管線26内的… 出·· 蒼考下列之示意圖’本發明將被詳加描述,其中表示 置圖 圖1為具有—粉碎設備和一煤炭灰注入設備之 〇 廠 圖2為具有計量閥和控制迴路之依照圖1之煤炭灰 入設備的注入容器。 18 1312334 【主要元件符號說明】 2.氣掃式滾子輾粉機 5.混合用裝置 7.碎片材料 9.惰性氣體 1 2.過濾器 1 5.煤炭分配器 17.煤倉 20.儲存容器 22.分配容器/運輸容器 24.注入容器 2 6.注入管線 28.高爐/使用裝置 30.固體 3 6.計量閥 38.流動用錐體 4.運輸用裝置 6.粗煤炭/固體 8.煤炭堆 11.熱氣產生器 14.碎片分配器 16.粗煤炭倉 1 8.吊桶輪 21.壓力容器 23.分配容器/運輸容器 25.運輸管線/連結管線 27.鼓風口 /使用裝置 29.管線 3 3.流動改良劑 3 7.計量閥/控制閥/控制迴路 39.稱重用裝置According to the competition of the present invention, j还原jK is a further development step, and the reducing agent or the reduced carbon mixture is mixed--$ 厌 or one or two other materials containing iron/iron oxide; 'In addition to - the debris material is a crushed soft mass" can be reed, / Bu 'smash coarse particles (for example, the way to be fed to the blast furnace is wrong - the role of the machine into the gas and the gas must be appropriate The pulverized coarse granules 12 I312334 are pulverized in a suitable pulverizing machine: the coal and the shard material are fed to the inside of the vessel. The density of the pulverized coarse granules is usually less than gram per cubic centimeter. This density value is different from the density of coarse coal, especially the density of the rolling τ piece. Therefore, it is advantageous to be able to transport it in a pneumatic manner - a mixture of coal crushed smashed coarse granules. The proportion of the undisturbed coarse particles of the picking edge hk 円 in the mixture of fragments is relatively low, such as a weight ratio of about 0.5 to 1. This proportion substantially comminutes the coarse or coarse crushed mass. To decide. This proportion of possession I will be chosen to make In the manufacturing process of iron and steel, the limits of the sputum must not be exceeded. /, the average calorific value of pulverized coarse particles is 32. 5 million joules: kg, - ash content is Less than 1. The weight ratio and a residual vapor content are 9, in the weight ratio of 1, the same average carbon content is 73 weight ratio, the hydrogen content is 3. The weight ratio is 2, the nitrogen content is 2.6 weight ratio and the following average values : Calcium oxide: 6% by weight, yttrium oxide: 3 · 〇 weight ratio, manganese oxide · · 〇. 8 weight ratio, milk: titanium: 〇. 7 weight ratio, alumina: °. 7 weight ratio, iron oxide: 3. The ratio of these components is suitable for integrated pulverization with coarse coal and crushed materials, for example, in a vertical powder mill, and for subsequent pneumatic transport through the blast furnace blaster. Operation and counting effect. The advantages of feeding in 〇13 and crushing coarse granules are particularly reasonable and effective, and the requirements of complying with environmental regulations are in accordance with the scope of the present invention. : at the downstream of the crushing equipment 13 1312334 mixed crushed Sheet material or - iron, iron to the blaster with the additive of the stiletto, and it is fed to the white eight of the reducing agent. & and especially the gray shackles are suitable for crushing, and the owner The additive is an alternative to the reducing agent (for example, the coal is too embarrassed to be added to the upstream of a storage container for being added to the library, or if the additive is stomach歹1 D疋 upstream of the tuyere.) The item continues to coal or - 彳彳 has an adverse effect, one or two, he is particularly suitable for the action of replacing the 杳丨. In the injection capacity: to the upstream of the main equipment or in the agent has the advantageous effect of the second example in accordance with the device of the present invention in the subsequent "valve. ,..." 疋 has at least one kind of feed device using this additive as a flow improver. Knife Η乍 Η乍 置 β : : * The coal ash injected into the device in the leaf, this can be set by An Jin The hot society, + 适"· 口 攸 攸 罝 该 该 该 该 该 该 该 主 主 主 主 主 主 主In a coal ash injection device having a single 钭 从 从 疋 该 该 该 该 该 该 1 1 1 1 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭 煤炭The pressure vessel, to the transport rolling body, can be fed to the vessel, a distribution crying... ^Transportation or distribution capacity... or a port 2 with a flowable cone on the outlet side The metering valve of the injection line and the blast of a blast furnace... the above two feed action can occur at a storage container or upstream of the coal/reverse/, and/or at the upstream of the transport container and or the dispensing container or Injection into the upstream of the vessel ' enables the flow improver in the desired particle size distribution to be mixed with the coal ash. As previously described, the flowability in conjunction with coal ash and having an effective effect on 14 1312334 occurs in the metering valve β, as well as in the processing of the blast furnace. ^Qin in the preferred device type 'is improved by increasing the proportion of well-defined (especially rolling debris) (4) (especially the equipment for the pneumatic transport operation of the phantom contains a powdering device, = charcoal debris mixture Will be fed to - powder machine (especially - vertical) Loeshe type roller powder machine) and with the previously mentioned crushing: direct processing. Then, for example, the coal ash is separated in the instrument Broken two: two things' the mixture can be stored in a storage container, and then the two containers are fed to the coal injection equipment. The coal injection equipment has a shipping container or a distribution container and a storage device or Injecting $, with: Flow measuring mechanism and injection line for injecting coal ash into the blast: quantity valve. The advantage is that the powdering equipment can be placed in a low cost manner to be able to mix or increase the crushing. The coarse granules are used to combine the coarse coal and the crush to complete the integrated pulverization. The coal ash can be suitably mixed with a flow improver, and the flow improver, especially the shard material and a part thereof, is pulverized. Coarse grain: the phenomenon that separation does not occur especially during pneumatic transportation. According to the present invention, the existing optimal injection device has a single metering effect, that is, it has a function for controlling the flow of coal ash to Individual injection = in-line metering valve 'by mixing-flow modifiers to precisely control the flow of coal ash. Due to problems caused by its narrower channels, such as vibration or blockage in the injection line, or It is the benefit of the control loop 15 1312334 Vibration 'with the blocked metering valve can also be avoided. The device according to the invention can lead to a rapid reduction in wear in the transport section and metering, and improve metering and control The performance result has an advantageous effect on the subsequent processing program (for example, the blast furnace processing program). [Embodiment] FIG. 1 is a method and device according to the present invention. The action of the pulverizing and injecting device of the carbon fluid mixture, the carbon-containing fluid mixture and being fed to the furnace blaster together with the hurricane The above-mentioned carbon-containing fluid mixture comprises a flow improver 33, which is introduced into the air-sweeping roller powder mill 2 and is pulverized before... The dynamic modifier is combined with the solid 30 (that is, coarse coal 6). In the embodiment: the feed device for the flow improvement of the "3 (for example, the dusty material 7) is a coal bunker 17 ' and the debris material is wrongly divided by a debris distributor 14 < The action is fed to the mixing device. In the mixing device 5, the g敁杻7 β human t 4 fragment material 枓7疋 is mixed with the coal rot 6 which is about to be pulverized, and from a coal The pile 8 enters a coarse coal 16' to the mixing device via the coal-disintegrating distributor 15 while the mixture is introduced into the roller-roller 2 by the action of the transporting device. &# In this air-sweeping roller powder machine 2, in which the pulverization drying effect can be accomplished by the force of _, in this embodiment, the two-dimensional gas sputum is produced in the hot gas production 1 The coarse coal debris mixture fed into the air-sweeping machine 2 is 16 1312334 containing a predetermined ratio: :::7, the pre-set ratio is preferably 3%.隹 :: The force is pulverized and screened in the same manner as the coarse coal is pulverized into coal ash. The inert gas in the coal separator 12 is separated from the separator by the inflow into the storage container 2◦. The outlet is not and is connected to the vial by a transport line or a connecting line.纴s, 篆仏, the storage container 20 θ 2 only shows that a transport container 22) is the pressure applied by the nitrogen gas as the transport gas of the house-house container 21. This coal: debris mixed t The material flows in the dispensing container or the transport container 22, 23, and may also be accompanied by other polling gases in the field, and the coal-agricultural debris mixture is introduced into the container via the transport line 25. Figure 24. Figure 2 shows a schematic configuration of a coal ash injection set with a single element control method, 1 Λ lL w^ - where the coal anesthetic debris mixture is fed by a distribution container' - Injecting into the container 24, the dispensing container 22 - itself being smashed with a -# reuse device 39, connected to $, and by the action of a metering valve 36 provided in each of the 7 main inlet lines 26, the coal ash fragments: The compound is widely fed into the blast opening 27 of the blast furnace 28 Wherein the injection is located downstream of the flow cone 28 disposed at the outlet side of the injection container 24 (refer to Figure 1). In each of the examples, the individual injection line 26 is linked. The upper S tuyere 27 (refer to Fig. 1), in this embodiment, the tuyere 27 of the blast furnace 28 represents the use device. 17 1312334 in the vicinity of the flow cone 38 (refer to the figure (for example, as a fluid) Or transporting the nitrogen of the gas: an inert gas ash/fragment mixture will produce further flow aids. The coal is additionally supplied from the pressure vessel 21. The raw gas is used as a pressure to transport the capacity. The container is flushed by the flowing gas in each application example. Also shown in Figure 2 is used to control the coal ash: feed. The number of control loops 3 in the injection line 26 is different; The two-powder mixture can have the advantage of being more. In the compound, 疋 represents the flow improver 33. The transport gas together with the coal particles is uniformly filled, and the reduction: the inside and the injection tube line 26 W and plugging or blocking phenomenon: this = then Can significantly improve the operation of the metering or control room (Yuan Kaitu "fruit causes a - is called" wire brushing effect, the result, used to change the gift in the gift production to help the transmission and control situation The added control accuracy helps to improve the stability of the k-to-furnace processing program and the quality of the column iron. It is not necessary to increase the green 9 g in the transport wheel, [Simple Description] Line 25 and Injection In the pipeline 26... The following is a schematic diagram of the present invention. The present invention will be described in detail, wherein the drawing is shown in Fig. 1 as a factory with a pulverizing device and a coal ash injecting device. Fig. 2 shows a metering valve and control The coal ash according to Figure 1 is injected into the injection container of the equipment. 18 1312334 [Explanation of main component symbols] 2. Air-sweeping roller powder machine 5. Mixing device 7. Fragment material 9. Inert gas 1 2. Filter 1 5. Coal distributor 17. Coal bin 20. Storage container 22. Dispensing container/transport container 24. Injecting container 2 6. Injection line 28. Blast furnace/use device 30. Solid 3 6. Metering valve 38. Flow cone 4. Transport device 6. Crude coal/solid 8. Coal Pile 11. Hot gas generator 14. Debris distributor 16. Crude coal bin 1 8. Bucket wheel 21. Pressure vessel 23. Dispensing container/transport container 25. Transport line/connection line 27. Blasting port/use device 29. Pipeline 3 3. Flow improver 3 7. Metering valve / control valve / control circuit 39. Weighing device

1919

Claims (1)

1312334 十、申請專利範圍: ^一 ~—一~ 1. 一種用於固體之氣動運輸的方法,其中被粉碎成灰 塵的固體係會與一運輸氣體相混合,並且該固體係以在一 運輸管線内保持一固體流體混合物之方式而被進給至一最 終使用裝置内, 其特徵為, 二、要9加可流動性,3亥固體係會與一流動改良劑相 此合,並且採用該流動改良劑之結果係能夠改善該固體流 體混合物的運輸和控制表現; 該流動改良劑係由一添加劑或具有不同於固體之密度 的材料混合物所組成; 一流動改良劑係以連續或非連續之方式而以精確界定 的比例與固體相混合; ㈣ϋ二作用係會取代一流動改良劑,用以協助在最終使 用裝置内該固體流體混合物的使用; 一個固體添加劑係會被混合成 取砀具有固體之流動改良 以對應於該固體 該固體添加劑係 被混合; 之顆粒尺寸分佈狀況 動改良劑是於其被粉碎之前 於被運輸和被注入至一使用m _間或之後,和/或 合,並且伟藉* w 、置内期間而與該固體相混 流動; 拗助而此夠連同該固體一起 和/或礦物材料 至於4固體煤炭灰,—含鐵/鐵氧化物 20 1312334 ^或—有機材料可以作為該流動改良劑,以及例如 或煙道乳的惰性氣體可以作為疋礼 煤炭灰、流動故㈣知w 勒氣體以上雙些固體 火机動改良劑和運輸氣體係相混合,在 内流動,並B在丨、;&祕庄丨 > 丄 王入§又備 …數量而經由鼓風口被進仏至-南爐内; 文、.,〇主~ 作為礦物添加劑和流叙 炭灰相混合,並劑的二氧化欽係會與該煤 汾響到在两爐内之煤屑的成形; 例如是煙道灰的灰塵'洗滌 積物係會與㈣卢亡4、e人 ㈣3心用隔室沈 )、'^煤厌灰相混合成為流動改良劑; 該碎片材料與該煤炭相混 片混合物内之碎片比例係為3% ;且^使付在煤… 粒狀程度為8Q到^百分比小於90微米。 2_如申請專利範圍第1項之方法, 其特徵為, 作二於該固體流體混合物之該煤炭灰係在-粉碎乾焊掻 作中而從煤炭、煤炭混合物、焦炭或煤炭隹炭, 造出來,並且钤人烛 &斥厌焦厌成〇物中製 被粉碎和以一:广氧化物之流動改良劑碎片材料係會 風口内。、厌犬/碎片流體之方式被進給至該高爐鼓 3·如申請專利範U第2項之方法, 其特徵為, Μ且22=氧化物成份W、含水量❹到 公厘的碎片材2 〇%與5%之間’連同顆粒尺寸高達50 材枓係與該煤炭一起承受粉碎乾燥作用。 21 I312334 4·如申請專利範圍第2項之方法, 其特徵為, 3亥煤炭灰和碎片材料係於一個垂 粉碎乾悔从:m ,ι, j. ^輾粉機内承受到 吁乾刼作用,後續的篩選和分離 又J 和額外之圓衿各枝、丨疋從一運送氣體 作為運輪备挪★ #斤 A犬/碎片混合物係連同 輸乳體之虱氣一起被氣動進給一 H . 主一注入容器内,此 ’、進m動作係經由運輸容器和一運輪I @ 量閥之谈α 連翰管線,並且藉由計 阀之協助而以可調整流量之方式 yk a ^ ^ 、俽進給經過注入管線而 机入3亥向爐鼓風口内。 5.如申請專利範圍第丨項之方法, 其特徵為, 作為有機材㈣粉碎粗粒係會連同㈣炭和/或一含 鐵鐵乳化物材料(特別是碎片材料)—起被粉碎,並且以 乳動之方式被運輸和進給經過鼓風口而到達—高爐内。 6·-種用於固體之氣動運輸的設備,其具有一個用於 粉碎固體⑷之粉碎用設備、—㈣於中間儲存精細粉碎 固體(30)之儲存容器(2〇)、_個介於儲存容器(2〇) 與至少-運輸容H ( 22、23 )之間的運輸管線(25 )和一 注入容器(24),該注入容器係可被來自—壓力容器(21) 之運輸氣體施加壓力,並且經由注入管線(26),其中所 流動之固體運輸氣體混合物能夠藉由一計量閥(36)之作 用而以流量受到控制之方式被進給至一使用裝置(27、28) 内,特別是被用來施行依照申請專利範圍第丨項到第5項 中任何一項之方法, 22 1312334 其特徵為, 至乂有一個進給裝置是被用來 該固體(6、+、 /風動改良劑(7)與 相渴•合,並且該該進认护署 粉碎用設備内和/或紗★ — d …裝置係被女置於該 容器(22、23)之子今器(2〇)之上游處和/或該運輸 上游處和/或該注入容 7.如申嗜直丨一 合器(24)之上游處。 〇月專利砣圍第6項之設備, 其特徵為, 在一個具有罝_ ^ ^ ^ ^ 要素控制方法和被安置於一粉碎用1 備之上游處的煤炭 物砰用》又 將粗焊炭te , s又備中,該粉碎用設備是被用來 壓力之而且具有一個以運輸氣體來施加 ==器(24)和流動用錐體(38)、計量閥⑻, 之計旦和的注入管線(26)連結至鼓風口(27) 〇十里和控制迴路(^ 7、 合一含鐵/鐵& 一個進給農置係被提供用來混 鐵/鐵乳化物材料(特別是一碎片材料⑺)。 •如申請專利範圍第6項或第7項之設備, 其特徵為, 備的附近?碎片材料(7 )之進給裝置係被安置於粉碎用設 、’特別係被安置於該輾粉機(2 )的上游處。 9.如申請專利範圍第8項之設備, 其特徵為, 二:3亥碎片材料⑺之進給裝置(Μ)係被提供有一 具有碎片分配器(14)的碎 θ 月煤倉(17),以及一個用於 -口碎片材料⑺的裝置(5)係具有粗煤炭⑷。 1 0.如申请專利範圍第6項或第7項之設備, 23 1312334 其特徵為, 一個用於將粉碎粗粒混合至即將被粉碎之固體(特別 是粗煤炭)的裝置,和/或具有即將被粉碎之流動改良劑, 或是一個用於將粉碎粗粒計量和進給至輾粉機内的裝置。 十一、圖式: 如次頁 241312334 X. Patent application scope: ^一~—一~ 1. A method for pneumatic transportation of solids, in which solids pulverized into dust are mixed with a transport gas, and the solids are in a transport pipeline. Feeding into a final use device in a manner that maintains a solid fluid mixture, characterized in that, 2, 9 fluidity is required, 3 sea solids will be combined with a flow modifier, and the flow is employed The result of the modifier is to improve the transport and control performance of the solid fluid mixture; the flow modifier consists of an additive or a mixture of materials having a density different from the solid; a flow modifier is in a continuous or discontinuous manner And mixing with the solid in a precisely defined ratio; (iv) the second action system replaces a flow improver to assist in the use of the solid fluid mixture in the end use device; a solid additive is mixed to obtain a solid Flow improvement to correspond to the solid, the solid additive is mixed; the particle size distribution is changed The agent is transported and injected into the use of m_ or after, and/or combined, and is mixed with the solid during the period of being pulverized, and is mixed with the solid; The solid together and / or mineral material to 4 solid coal ash, - iron / iron oxide 20 1312334 ^ or - organic materials can be used as the flow improver, and inert gas such as or flue milk can be used as a ash coal ash (4) know that the gas above the gas is mixed with the solid gas motor improver and the transport gas system, and the flow is in the inside, and B is in the 丨,; & 秘 秘 丨 丨 丄 入 入The blaster is plunged into the south furnace; Wen,., 〇主~ as a mineral additive and a mixture of ash and charcoal, the oxidizing agent of the sulphur will react with the coal slag to the coal swarf in the two furnaces. Forming; for example, the dust of the flue ash's washings will be mixed with (4) Lushen 4, e (4) 3 core compartments, and '^ coal ash as a flow improver; the debris material and the coal The proportion of fragments in the mixed mixture is 3%; and ^ Pay for the particulate coal ... extent to 8Q ^ percentage is less than 90 microns. 2_ The method of claim 1, wherein the coal ash is produced in a solid fluid mixture and is produced from coal, coal mixture, coke or coal. It comes out, and the swearing candle & swears that the smashing of the smashed material is smashed and the smashing material of the flow modifier of the wide oxide is contained in the vent. a method of feeding a canine/fragment fluid to the blast furnace drum 3, as in the method of claim 2, characterized in that, 22, an oxide component W, a moisture content of ❹ to a fraction of a metre 2 〇% and 5%' together with the particle size up to 50 枓 与 与 与 与 与 与 与 与 与 与 与 与 与 与 与 与 与21 I312334 4· The method of claim 2, characterized in that 3 hai coal ash and debris materials are in a smashing and smashing from: m, ι, j. Subsequent screening and separation, and J and extra round rafts, rafts from a transport gas as a transport wheel to prepare for the move. #斤 A dog/fragment mixture is pneumatically fed together with the sputum of the lactating body. When the main injection into the container, the 'm' movement is via the transport container and a transport wheel I @ quantity valve to the α 连 翰 line, and with the aid of the meter valve, the flow can be adjusted yk a ^ ^ The enthalpy is fed into the air vent of the furnace through the injection pipeline. 5. The method of claim 2, characterized in that, as an organic material (4), the pulverized coarse granules are pulverized together with (iv) carbon and/or a ferrous iron-containing emulsifier material (particularly a shard material), and It is transported and fed in a milky manner through the blast opening to reach the blast furnace. 6·-A device for pneumatic transportation of solids, which has a pulverizing device for pulverizing solids (4), (4) a storage container (2 〇) for storing fine pulverized solids (30) in the middle, and _ between storage a transport line (25) between the container (2〇) and at least the transport volume H (22, 23) and an injection container (24) which can be pressurized by the transport gas from the pressure vessel (21) And via an injection line (26), wherein the solid transport gas mixture flowing can be fed into a use device (27, 28) by a metering valve (36) in a controlled flow rate, in particular Is used to perform any of the methods of claim 5 to 12, which is characterized in that a feed device is used for the solid (6, +, / pneumatic) The modifier (7) is combined with the thirst, and the device is immersed in the equipment and/or the yarn is placed in the container (22, 23). Upstream and/or upstream of the transport and/or the injection volume 7. The upstream of the 丨 丨 丨 ( 。 。 。 。 。 。 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣 砣The coal material in the upstream is further used for the coarse welding of the carbon te, s, which is used for pressure and has a transport gas to apply the == device (24) and the flow cone (38). ), the metering valve (8), the metering line and the injection line (26) are connected to the blast port (27) 〇10 mile and the control circuit (^ 7, united with iron/iron & a feed farm is provided To mix iron/iron emulsion materials (especially a fragment material (7)). • Equipment as claimed in item 6 or 7 of the patent application, characterized in that the feeding device of the nearby fragment material (7) is prepared. It is placed in the smashing device, and the 'special system is placed upstream of the smashing machine (2). 9. The device of claim 8 is characterized in that: 2: 3 hai debris material (7) feed The device (Μ) is provided with a broken θ month coal bunker (17) having a debris distributor (14), and The device (5) for the --shard material (7) has coarse coal (4). 10. The device of claim 6 or 7, 23 1312334, characterized in that one is used for mixing the pulverized coarse particles A device to the solid to be pulverized (especially coarse coal), and/or a flow improver to be pulverized, or a device for metering and feeding the pulverized coarse particles into the pulverizer. Schema: as the next page 24
TW93136087A 2003-12-03 2004-11-24 Method and apparatus for the pneumatic conveying of solids TWI312334B (en)

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