TW202014528A - Preparation method and system of combustion-supporting agent dehydrating converter sludge to generate a mud cake - Google Patents

Preparation method and system of combustion-supporting agent dehydrating converter sludge to generate a mud cake Download PDF

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TW202014528A
TW202014528A TW107134734A TW107134734A TW202014528A TW 202014528 A TW202014528 A TW 202014528A TW 107134734 A TW107134734 A TW 107134734A TW 107134734 A TW107134734 A TW 107134734A TW 202014528 A TW202014528 A TW 202014528A
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fuel
combustion
mud cake
oxide
converter
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TW107134734A
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TWI704233B (en
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孫文彬
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孫文彬
黃秀敏
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Priority to CN201910839469.7A priority patent/CN110982577A/en
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    • 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
    • C10L9/10Treating solid fuels to improve their combustion by using additives
    • 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • 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
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/22Function and purpose of a components of a fuel or the composition as a whole for improving fuel economy or fuel efficiency
    • 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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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

This invention relates to a preparation method and a system for combustion-supporting agent. The method includes: dehydrating converter sludge to generate a mud cake, wherein the mud cake contains 40wt%-70wt% of iron oxide, 10wt%-30wt% of calcium oxide and 20wt%-40wt% of water; adding 0.1wt%-0.0001wt% of the mud cake into a fuel according to the total weight of the fuel; and uniformly stirring the mud cake and the fuel, wherein the 0.1wt%-0.0001wt% of mud cake is used as a combustion-supporting agent in the fuel. The system includes a converter smoke recovery device for recovering converter smoke by using a wet recycle method to generate the converter sludge, a dehydrating equipment for dehydrating the converter sludge to generate the mud cake, a combustion device provided with the fuel and used for adding the 0.1wt%-0.0001wt% of the mud cake into the fuel according to the total weight of the fuel, and a stirring device for uniformly mixing and stirring the mud cake and the fuel. Accordingly, the present invention enables resources to be efficiently utilized and reduce pollution emission.

Description

助燃劑的製備方法及其系統 Method and system for preparing combustion aid

本發明係為一種助燃劑的製備方法及其系統,尤指一種應用回收轉爐塵泥之助燃劑的製備方法及其系統。 The invention is a preparation method and system of a combustion aid, in particular to a preparation method and system of a combustion aid using recovered converter dust and mud.

隨著我國經濟持續迅速發展,城市化進程加快,人口不斷增加,煤炭年消耗量逐年以大幅度增加。煤燃燒是煤炭利用的主要方式,我國能源結構主要以煤為主,對環境造成嚴重的污染。 As my country's economy continues to develop rapidly, the urbanization process accelerates, the population continues to increase, and the annual coal consumption has increased substantially year by year. Coal combustion is the main method of coal utilization. my country's energy structure is mainly dominated by coal, causing serious pollution to the environment.

其次,使用交通工具的人口越來越多,然而,人們必須為此付出非常大的代價。因為當汽機車數目一天天的增加,所製造的污染也隨著擴大,交通工具所產生的廢氣之溫室氣體和懸浮微粒對我們的健康和生活環境會有很大的影響。自2005年以來,許多國家已相繼公告並推動禁售燃油車政策,計畫將在未來數十年內禁止販售部分或所有以化石燃料(包括汽油、液化石油氣和柴油)為動力源的載具,進而達成改善空氣污染、減緩全球暖化等目的。 Secondly, more and more people use transportation, however, people must pay a very high price for this. Because the number of steam locomotives increases day by day, the pollution produced also expands, and the greenhouse gases and suspended particles of the exhaust gas generated by the transportation will have a great impact on our health and living environment. Since 2005, many countries have successively announced and promoted a ban on the sale of fuel-fueled vehicles. They plan to ban the sale of some or all fossil fuels (including gasoline, liquefied petroleum gas, and diesel) as power sources in the next few decades. Vehicles to achieve the goals of improving air pollution and slowing down global warming.

綜上所述,如何高效的利用資源並且最大限度的減少排放污染,成為擺在我們面前的一項迫切任務。因此,亟需開發一種強效燃煤助劑以達到燃燒完全,進而減少污染物的排放。 In summary, how to efficiently use resources and minimize emission pollution has become an urgent task before us. Therefore, there is an urgent need to develop a powerful coal-burning additive to achieve complete combustion, thereby reducing pollutant emissions.

有鑑於現今汽機車燃油不完全及工廠燃煤對環境造成嚴重污染,增加溫室氣體和懸浮微粒因而影響我們的健康和生活環境。本發明的目的在於提供一種助燃劑的製備方法及其系統,使汽機車或工廠中的燃燒完全以減少對環境的污染,可達到減少懸浮微粒、硫氧化物、氮氧化物及揮發性有機物的排放並增加燃燒效能的目的。 In view of the incomplete fuel consumption of automobiles and locomotives and the serious pollution of the environment caused by coal burning in factories, the increase of greenhouse gases and suspended particulates affects our health and living environment. The purpose of the present invention is to provide a method and system for preparing a combustion aid to complete combustion in a steam locomotive or factory to reduce environmental pollution and reduce suspended particulates, sulfur oxides, nitrogen oxides and volatile organic compounds The purpose of emitting and increasing combustion efficiency.

為達上述目的,本發明係提供一種助燃劑的製備方法及其系統,該助燃劑的製備係應用回收煉鋼轉爐塵泥,該轉爐塵泥係為轉爐煉鋼過程中產生的副產物,具有鐵含量高、鈣含量高、水含量高,且其細微性細、黏度大、活性高、雜物多等特點,該轉爐塵泥係為寶貴的二次資源,如不進行回收利用,不僅浪費了礦物資源,同時也會佔用大量土地面積並污染環境。 In order to achieve the above object, the present invention provides a method for preparing a combustion aid and a system thereof. The preparation of the combustion aid uses recycling of steelmaking converter dust, which is a by-product produced during the steelmaking process of the converter. With high iron content, high calcium content, high water content, and its fineness, high viscosity, high activity, and many debris, the converter dust and sludge system is a valuable secondary resource. If it is not recycled, it is not only a waste In addition to mineral resources, it will also occupy a lot of land area and pollute the environment.

目前轉爐煙塵回收多以濕法為主,轉爐煙塵以塵泥形式產出。根據有關統計資料,我國鋼產量近幾年穩定在為8億多噸,每生產1噸鋼大約產生100kg以上的含鐵塵泥,我國含鐵塵泥年產生量在8000萬噸以上。鋼鐵生產包括燒結、球團、煉鐵等程序,各生產程序均設置了除塵裝備以確保排放達標。含鐵塵泥為除塵過程收集的顆粒物,鋼鐵生產過程中產生的粉塵或塵泥,如燒結粉塵、高爐煤氣灰、泥、轉爐塵泥及氧化鐵皮等。在一般情況下,含鐵粉塵和氧化鐵皮量約占鋼產量的6~10%。粉塵大部分顆粒很細且常含有鉛、鋅和鹼金屬氧化物等有害雜質應予回收利用。 At present, most of the converter dust recovery is based on the wet method, and the converter dust is produced in the form of dust sludge. According to relevant statistics, my country's steel output has stabilized at more than 800 million tons in recent years. For every ton of steel produced, more than 100 kg of iron-bearing dust and sludge are produced. my country's annual production of iron-bearing dust and sludge is more than 80 million tons. Steel production includes sintering, pelletizing, iron making and other procedures. Each production procedure is equipped with dust removal equipment to ensure that emissions are up to standard. Iron-containing dust and sludge are the particles collected in the dust removal process, and the dust or dust generated in the steel production process, such as sintered dust, blast furnace gas ash, mud, converter dust and oxide scale, etc. Under normal circumstances, the amount of iron-containing dust and iron scale accounts for about 6 to 10% of the steel output. Most of the dust particles are very fine and often contain harmful impurities such as lead, zinc and alkali metal oxides and should be recycled.

為達上述目的,本發明可提供一種助燃劑的製備方法,可包括:(a)將一轉爐塵泥脫水以產生一泥餅,該泥餅包括40wt%~70wt%的氧化鐵、10wt%~30wt%的氧化鈣及20wt%~40wt% 的水;(b)相對於一燃料的總重量,將0.1wt%至0.0001wt%的該泥餅加入該燃料中;以及(c)將該泥餅及該燃料混勻攪拌;其中,0.1wt%至0.0001wt%的該泥餅在該燃料中作為一助燃劑。 In order to achieve the above object, the present invention can provide a method for preparing a combustion aid, which can include: (a) dewatering a converter dust sludge to produce a mud cake, the mud cake including 40wt%~70wt% iron oxide, 10wt%~ 30wt% calcium oxide and 20wt%~40wt% Water; (b) add 0.1wt% to 0.0001wt% of the mud cake to the fuel relative to the total weight of a fuel; and (c) mix and mix the mud cake and the fuel; wherein, 0.1wt % To 0.0001wt% of the mud cake acts as a combustion aid in the fuel.

於前述本發明之助燃劑的製備方法中,在產生該泥餅的步驟之後可更包括一第一燃燒步驟,在該第一燃燒步驟中該燃料反應形成一氮氧化物、一硫氧化物、一碳氫化合物或一懸浮微粒。 In the aforementioned method for preparing a combustion aid of the present invention, after the step of generating the mud cake may further include a first combustion step, in which the fuel reacts to form a nitrogen oxide, a sulfur oxide, A hydrocarbon or a suspended particle.

於前述本發明之助燃劑的製備方法中,在將該泥餅及該燃料混勻攪拌之後可更包括一第二燃燒步驟,該第二燃燒步驟可包括溫度範圍在200℃~700℃之間的一反應溫度,在一實施例中,該反應溫度可為250℃~650℃之間;在另一實施例中,該反應溫度可為300℃~600℃之間。 In the foregoing preparation method of the combustion aid of the present invention, after the mud cake and the fuel are mixed and stirred, a second combustion step may be further included, and the second combustion step may include a temperature range between 200°C and 700°C In one embodiment, the reaction temperature may be between 250°C and 650°C; in another embodiment, the reaction temperature may be between 300°C and 600°C.

於前述本發明之助燃劑的製備方法中,該反應溫度可在400℃~500℃之間時,經由一氧化碳將該氧化鐵表面的Fe3+還原為Fe2+,Fe2+再將氮氧化物還原為一氮氣,總反應式如下:C+1/2O2→1/2N2+CO2 (式1) In the aforementioned preparation method of the combustion aid of the present invention, when the reaction temperature can be between 400°C and 500°C, Fe 3+ on the surface of the iron oxide is reduced to Fe 2+ via carbon monoxide, and then Fe 2+ oxidizes the nitrogen The substance is reduced to a nitrogen gas. The total reaction formula is as follows: C+1/2O 2 →1/2N 2 +CO 2 (Equation 1)

於前述本發明之助燃劑的製備方法中,該燃料可為一固體燃料或一液體燃料;其中,該固體燃料可包括燃煤、一可燃的黑色或棕黑色沉積岩、一焦炭或一含碳物質,該液體燃料可包括一種或多種液體的碳氫化合物組成的物質,包括一漁船燃油、一汽車燃油、一機車燃油、一柴油、一原油或一燃煤鍋爐的燃油。 In the foregoing preparation method of the combustion aid of the present invention, the fuel may be a solid fuel or a liquid fuel; wherein, the solid fuel may include coal, a combustible black or brownish black sedimentary rock, a coke or a carbonaceous substance The liquid fuel may include one or more liquid hydrocarbons, including a fishing boat fuel, an automobile fuel, a locomotive fuel, a diesel, a crude oil, or a coal-fired boiler fuel.

為達上述另一目的,本發明可提供一種助燃劑的製備系統,可包括一轉爐煙塵回收裝置、一脫水設備、一燃燒裝置及一攪拌裝置。首先,該轉爐煙塵回收裝置可經由一濕法回收一轉爐煙塵以產生一轉爐塵泥。其次,該脫水設備可將該轉爐塵泥 進行脫水以產生一泥餅,該泥餅包括40wt%~70wt%的氧化鐵、10wt%~30wt%的氧化鈣及20wt%~40wt%的水。此外,該燃燒裝置可設置一燃料,相對於該燃料的總重量,將0.1wt%至0.0001wt%的該泥餅加入該燃料中。再者,該攪拌裝置可將該泥餅及該燃料混勻攪拌;其中,0.1wt%至0.0001wt%的該泥餅在該燃料中作為一助燃劑。 In order to achieve the other object mentioned above, the present invention can provide a preparation system for a combustion aid, which can include a converter soot recovery device, a dehydration device, a combustion device and a stirring device. First, the converter soot recovery device can recover a converter soot through a wet process to produce a converter dust. Secondly, the dewatering equipment can convert the converter dust and mud Dehydration is performed to produce a mud cake, which includes 40 wt% to 70 wt% iron oxide, 10 wt% to 30 wt% calcium oxide, and 20 wt% to 40 wt% water. In addition, the combustion device may be provided with a fuel, and 0.1% to 0.0001% by weight of the mud cake is added to the fuel relative to the total weight of the fuel. Furthermore, the stirring device can mix and stir the mud cake and the fuel; wherein, 0.1 wt% to 0.0001 wt% of the mud cake is used as a combustion aid in the fuel.

於前述本發明之助燃劑的製備系統中,在產生該泥餅之後,於該燃燒裝置中可進行一第一燃燒步驟,在該第一燃燒步驟中該燃料反應形成一氮氧化物、一硫氧化物、一碳氫化合物或一懸浮微粒。 In the aforementioned preparation system of the combustion aid of the present invention, after the mud cake is produced, a first combustion step may be performed in the combustion device, in which the fuel reacts to form a nitrogen oxide and a sulfur Oxide, a hydrocarbon or a suspended particulate.

於前述本發明之助燃劑的製備系統中,在將該泥餅及該燃料混勻攪拌之後,在該燃燒裝置中可進行一第二燃燒步驟,該燃燒步驟包括溫度範圍在200℃~700℃之間的一反應溫度。在一實施例中,該反應溫度可為250℃~650℃之間;在另一實施例中,該反應溫度可為300℃~600℃之間。 In the aforementioned preparation system of the combustion aid of the present invention, after the mud cake and the fuel are mixed and stirred, a second combustion step may be performed in the combustion device, and the combustion step includes a temperature range of 200°C to 700°C A reaction temperature between. In one embodiment, the reaction temperature may be between 250°C and 650°C; in another embodiment, the reaction temperature may be between 300°C and 600°C.

於前述本發明之助燃劑的製備系統中,該反應溫度可在400℃~500℃之間時,經由一氧化碳將該氧化鐵表面的Fe3+還原為Fe2+,Fe2+再將氮氧化物還原為一氮氣。 In the aforementioned preparation system of the combustion aid of the present invention, when the reaction temperature is between 400°C and 500°C, Fe 3+ on the surface of the iron oxide is reduced to Fe 2+ via carbon monoxide, and then Fe 2+ oxidizes the nitrogen The material is reduced to nitrogen.

於前述本發明之助燃劑的製備系統中,該燃料可為一固體燃料或一液體燃料;其中,該固體燃料可包括燃煤、一可燃的黑色或棕黑色沉積岩、一焦炭或一含碳物質,該液體燃料可包括一種或多種液體的碳氫化合物組成的物質,包括一漁船燃油、一汽車燃油、一機車燃油、一柴油、一原油或一燃煤鍋爐的燃油。 In the foregoing preparation system of the combustion aid of the present invention, the fuel may be a solid fuel or a liquid fuel; wherein, the solid fuel may include coal-fired, a combustible black or brown-black sedimentary rock, a coke or a carbonaceous substance The liquid fuel may include one or more liquid hydrocarbons, including a fishing boat fuel, an automobile fuel, a locomotive fuel, a diesel, a crude oil, or a coal-fired boiler fuel.

根據上述諸多優點,並為使審查委員對本發明能進一步的瞭解,故揭露一較佳之實施方式如下,配合圖式、圖號, 將本發明之構成內容及其所達成的功效詳細說明如後。 Based on the above many advantages, and in order for the reviewing committee to further understand the present invention, a preferred embodiment is disclosed as follows, in conjunction with the drawings and drawing numbers, The detailed description of the composition of the present invention and the effect achieved by it are as follows.

1‧‧‧助燃劑的製備系統 1‧‧‧Combustion agent preparation system

10‧‧‧轉爐煙塵回收裝置 10‧‧‧Converter soot recovery device

11‧‧‧轉爐煙塵 11‧‧‧Converter soot

12‧‧‧轉爐塵泥 12‧‧‧Converter dust and mud

20‧‧‧脫水設備 20‧‧‧Dehydration equipment

21‧‧‧泥餅 21‧‧‧ Mud cake

21’‧‧‧助燃劑 21’‧‧‧combustion aid

30‧‧‧燃燒裝置 30‧‧‧Combustion device

301‧‧‧氮氧化物 301‧‧‧ Nitrogen oxide

302‧‧‧硫氧化物 302‧‧‧Sulfur oxide

303‧‧‧碳氫化合物 303‧‧‧Hydrocarbon

304‧‧‧懸浮微粒 304‧‧‧ suspended particles

31‧‧‧燃料 31‧‧‧ Fuel

40‧‧‧攪拌裝置 40‧‧‧Stirring device

圖1為本發明實施例1之助燃劑的製備方法之流程圖;圖2為本發明實施例1之助燃劑的製備方法之方塊圖;圖3為本發明實施例2之助燃劑的製備系統之示意圖;圖4為本發明實施例2之助燃劑的製備系統之示方塊圖。 1 is a flow chart of the preparation method of the combustion aid of Example 1 of the invention; FIG. 2 is a block diagram of the preparation method of the combustion aid of Example 1 of the invention; FIG. 3 is a preparation system of the combustion aid of Example 2 of the invention 4 is a block diagram of a preparation system for a combustion aid according to Embodiment 2 of the present invention.

以下係藉由具體實施例說明本發明之實施方式,熟習此技藝之人士可由本說明書所揭示之內容輕易地了解本發明之其他優點與功效。此外,本發明亦可藉由其他不同具體實施例加以施行或應用,在不悖離本發明之精神下進行各種修飾與變更。 The following describes the implementation of the present invention through specific examples. Those skilled in the art can easily understand other advantages and effects of the present invention from the content disclosed in this specification. In addition, the present invention can also be implemented or applied by other different specific embodiments, and various modifications and changes can be made without departing from the spirit of the present invention.

請參閱圖1至圖2所示,圖1為圖1為本發明實施例1之助燃劑的製備方法之流程圖;及圖2為本發明實施例1之助燃劑的製備方法之方塊圖。 Please refer to FIG. 1 to FIG. 2. FIG. 1 is a flowchart of the method for preparing the combustion aid of Embodiment 1 of the present invention; and FIG. 2 is a block diagram of the method of preparing the combustion aid of Embodiment 1 of the present invention.

如圖2所示,在轉爐煉鋼過程中會產生鋼液及轉爐塵泥12之副產物,如圖1所示,本發明實施例係為一種助燃劑的製備方法,包括S101步驟:將一轉爐塵泥12脫水以產生一泥餅21,該泥餅21包括40wt%~70wt%的氧化鐵、10wt%~30wt%的氧化鈣及20wt%~40wt%的水;S102步驟:相對於一燃料31的總重量,將0.1wt%至0.0001wt%的該泥餅21加入該燃料31中;以及S103步驟:將該泥餅21及該燃料31混勻攪拌;其中,0.1wt%至0.0001wt%的該泥餅21在該燃料31中作為一助燃劑21’。 As shown in FIG. 2, by-products of molten steel and converter dust 12 are produced in the steelmaking process of the converter. As shown in FIG. 1, an embodiment of the present invention is a method for preparing a combustion aid, including step S101: The converter dust 12 is dehydrated to produce a mud cake 21, which includes 40wt%~70wt% iron oxide, 10wt%~30wt% calcium oxide and 20wt%~40wt% water; Step S102: relative to a fuel The total weight of 31, add 0.1wt% to 0.0001wt% of the mud cake 21 to the fuel 31; and step S103: the mud cake 21 and the fuel 31 are mixed and stirred; wherein, 0.1wt% to 0.0001wt% The mud cake 21 is used as a combustion aid 21' in the fuel 31.

如圖1所示,在產生該泥餅的步驟之後更包括一第一 燃燒步驟(S1011步驟),在該第一燃燒步驟中該燃料反應形成一氮氧化物、一硫氧化物、一碳氫化合物或一懸浮微粒。在將該泥餅及該燃料混勻攪拌之後更包括一第二燃燒步驟(S104步驟),該燃燒步驟包括溫度範圍在200℃~700℃之間的一反應溫度;其中,該反應溫度在400℃~500℃之間時,經由一氧化碳將該氧化鐵表面的Fe3+還原為Fe2+,Fe2+再將氮氧化物還原為一氮氣,總反應式如下:C+1/2O2→1/2N2+CO2 (式1) As shown in FIG. 1, after the step of producing the mud cake, a first combustion step (step S1011) is further included, in which the fuel reacts to form a nitrogen oxide, a sulfur oxide, and a hydrocarbon in the first combustion step Compound or a suspended particle. After the mud cake and the fuel are mixed and stirred, a second combustion step (step S104) is further included. The combustion step includes a reaction temperature ranging from 200°C to 700°C; wherein the reaction temperature is 400 Between ℃ and 500℃, the Fe 3+ on the surface of the iron oxide is reduced to Fe 2+ through carbon monoxide, and the Fe 2+ reduces the nitrogen oxide to nitrogen, the total reaction formula is as follows: C+1/2O 2 → 1/2N 2 +CO 2 (Formula 1)

其次,該轉爐塵泥12中包括具有脫硫功能的該氧化鈣,可以減少燃燒氧化硫的排放。 Secondly, the converter dust 12 includes the calcium oxide having a desulfurization function, which can reduce the combustion of sulfur oxide emissions.

該燃料係為一固體燃料或一液體燃料;其中,該固體燃料包括燃煤,該液體燃料包括一漁船燃油、一汽車燃油、一機車燃油、一柴油或一燃煤鍋爐的燃油。在一般燃煤電廠中,煤炭通常會變成細粉狀,在空氣中燃燒後產生蒸汽驅動渦輪機來發電。整個過程都處於高溫狀態,生成的污染物氧化氮和二氧化碳很難被隔離。煤與空氣並沒有發生化學反應,而與含氧材料(如氧化鐵)直接反應。 The fuel is a solid fuel or a liquid fuel; wherein the solid fuel includes coal-fired fuel, and the liquid fuel includes a fishing boat fuel oil, an automobile fuel oil, a locomotive fuel oil, a diesel fuel, or a coal-fired boiler fuel oil. In general coal-fired power plants, coal usually turns into a fine powder, which is burned in the air to generate steam to drive turbines to generate electricity. The entire process is at a high temperature, and the generated pollutants nitric oxide and carbon dioxide are difficult to isolate. Coal does not chemically react with air, but directly reacts with oxygen-containing materials (such as iron oxide).

在溫度400℃、450℃及500℃之該反應溫度,該反應溫度越高該氧化鐵的活性提升,能增加對該氮氧化物及該硫氧化物的去除效率及操作時間,因而,該氮氧化物及該硫氧化物除量就越多。而隨進流濃度、流通量的提高,無論是該氮氧化物或該硫氧化物與鐵粉接觸反應時,因參與反應之鐵粉較快消耗,使得去除率效果降低。本發明所使用的該助燃劑21’在該第二燃燒步驟中,可使該燃料31燃燒提高15%~20%,以及能有效去除該燃料31在該第一燃燒過程中產生的該硫氧化物25%~35%,去除氮氧化物20%~60%,去除一氧化碳及該碳氫化合物50%~70%,去除一煙塵50%~70%。 At the reaction temperature of 400°C, 450°C and 500°C, the higher the reaction temperature is, the higher the activity of the iron oxide is, which can increase the removal efficiency and operation time of the nitrogen oxide and the sulfur oxide. Therefore, the nitrogen The more oxides and sulfur oxides are removed. With the increase of the inflow concentration and the flow rate, whether the nitrogen oxide or the sulfur oxide is in contact with the iron powder, the iron powder participating in the reaction is consumed faster, which reduces the effect of the removal rate. The combustion aid 21' used in the present invention can increase the combustion of the fuel 31 by 15% to 20% in the second combustion step, and can effectively remove the sulfur oxidation generated by the fuel 31 in the first combustion process Matter 25%~35%, removal of nitrogen oxides 20%~60%, removal of carbon monoxide and the hydrocarbon 50%~70%, removal of soot 50%~70%.

請參閱圖3至圖4所示,圖3為本發明實施例2之助燃劑的製備系統之示意圖;及圖4為本發明實施例2之助燃劑的製備系統之方塊圖。 Please refer to FIG. 3 to FIG. 4. FIG. 3 is a schematic diagram of the combustion aid preparation system according to Embodiment 2 of the present invention; and FIG. 4 is a block diagram of the combustion aid preparation system according to Embodiment 2 of the present invention.

如圖3及圖4所示,本發明實施例2係為一種助燃劑的製備系統1,可包括一轉爐煙塵回收裝置10、一脫水設備20、一燃燒裝置30及一攪拌裝置40。首先,該轉爐煙塵回收裝置10可經由一濕法回收一轉爐煙塵11以產生一轉爐塵泥12。其次,該脫水設備20可將該轉爐塵泥12進行脫水以產生一泥餅21,該泥餅21包括40wt%~70wt%的氧化鐵、10wt%~30wt%的氧化鈣及20wt%~40wt%的水。此外,該燃燒裝置30可設置一燃料31,相對於該燃料31的總重量,將0.1wt%至0.0001wt%的該泥餅21加入該燃料31中。再者,該攪拌裝置40可將該泥餅21及該燃料31混勻攪拌;其中,0.1wt%至0.0001wt%的該泥餅21在該燃料31中作為一助燃劑21’。 As shown in FIGS. 3 and 4, Embodiment 2 of the present invention is a combustion aid preparation system 1, which may include a converter dust recovery device 10, a dehydration device 20, a combustion device 30 and a stirring device 40. First, the converter soot recovery device 10 can recover a converter soot 11 through a wet process to produce a converter dust 12. Secondly, the dewatering equipment 20 can dehydrate the converter dust 12 to produce a mud cake 21, the mud cake 21 includes 40wt%~70wt% iron oxide, 10wt%~30wt% calcium oxide and 20wt%~40wt% Water. In addition, the combustion device 30 may be provided with a fuel 31, and 0.1% to 0.0001% by weight of the mud cake 21 is added to the fuel 31 relative to the total weight of the fuel 31. Furthermore, the stirring device 40 can mix and stir the mud cake 21 and the fuel 31; wherein, 0.1 wt% to 0.0001 wt% of the mud cake 21 is used as a combustion aid 21' in the fuel 31.

如圖3及圖4所示,在產生該泥餅21之後,於該燃燒裝置30中可進行一第一燃燒步驟,在該第一燃燒步驟中該燃料31反應形成一氮氧化物301、一硫氧化物302、一碳氫化合物303或一懸浮微粒304。如圖4所示,在將該泥餅21及該燃料31混勻攪拌之後,在該燃燒裝置30中可進行一第二燃燒步驟,該燃燒步驟包括溫度範圍在200℃~700℃之間的一反應溫度。當該反應溫度在400℃~500℃之間時,經由一氧化碳將該氧化鐵表面的Fe3+還原為Fe2+,Fe2+再將氮氧化物301還原為一氮氣,以降低該氮氧化物301的排放量。其次,該泥餅21中的該氧化鐵,能還原該氮氧化物301而生成氮氣能有效抑制戴奧辛。 As shown in FIGS. 3 and 4, after the mud cake 21 is produced, a first combustion step may be performed in the combustion device 30, in which the fuel 31 reacts to form a nitrogen oxide 301, a Sulfur oxide 302, a hydrocarbon 303 or a suspended particulate 304. As shown in FIG. 4, after the mud cake 21 and the fuel 31 are mixed and stirred, a second combustion step may be performed in the combustion device 30. The combustion step includes a temperature range between 200°C and 700°C. One reaction temperature. When the reaction temperature is between 400°C and 500°C, the Fe 3+ on the surface of the iron oxide is reduced to Fe 2+ via carbon monoxide, and the Fe 2+ reduces the nitrogen oxide 301 to nitrogen to reduce the nitrogen oxidation The amount of 301 emissions. Secondly, the iron oxide in the mud cake 21 can reduce the nitrogen oxide 301 to generate nitrogen gas, which can effectively suppress dioxin.

本發明將採用三種方式作測試,首先,將該助燃劑加入汽車燃油、機車燃油、柴油或漁船油箱中與該燃料混合後,測試汽車、機車、柴油車或漁船尾排,添加前後尾排中該氮氧化 物、該硫氧化物、該懸浮微粒及該碳氫化合物之排放。其次,小型工廠燃油鍋爐燃油添加該助燃劑前後之燃油用量,以及該氮氧化物、該硫氧化物、該懸浮微粒及該碳氫化合物排放量。再者,醫療廢棄物焚化爐添加該助燃劑前後之燃油用量,以及該氮氧化物、該硫氧化物、該懸浮微粒、該碳氫化合物及戴奧辛排放量比較。 The present invention will be tested in three ways. First, add the oxidizer to the fuel tank of automobile, locomotive fuel, diesel or fishing boat and mix it with the fuel, then test the tail row of automobile, locomotive, diesel vehicle or fishing boat, and add the front and rear tail row The nitrogen oxide Emissions of substances, the sulfur oxides, the suspended particulates and the hydrocarbons. Secondly, the fuel consumption of the fuel oil of small-scale factory fuel boilers before and after the addition of the oxidant, and the emissions of the nitrogen oxides, the sulfur oxides, the suspended particulates and the hydrocarbons. Furthermore, the amount of fuel used before and after adding the oxidant to the medical waste incinerator, and the emissions of the nitrogen oxides, the sulfur oxides, the suspended particulates, the hydrocarbons, and dioxin.

本發明的該助燃劑可應用範圍包括:1.汽柴機車燃油添加使用;2.漁船燃油(柴油)添加使用;3.內、外燃油、燃煤鍋爐添加使用;4.焚化爐、醫療廢棄物處理場燃燒添加使用;5.動物屍體焚化添加使用;以及6.火力發電廠、發電機燃油、燃煤發電添加使用。 The application range of the combustion aid of the present invention includes: 1. Use of fuel oil for steam and diesel locomotives; 2. Use of fuel oil (diesel) for fishing boats; 3. Use of internal and external fuel oil and coal-fired boilers; 4. Incinerator, medical waste Adding to the burning of the material treatment site; 5. Adding to the use of animal carcasses incineration; and 6. Adding to the use of thermal power plants, generator fuel, and coal-fired power generation.

藉由本發明的助燃劑的製備方法及其系統,所產生的該助燃劑可以作為小型燃油鍋爐的燃油添加劑,可以增加燃燒效能、減少燃油量、燃煤量,以及減少懸浮微粒(PM2.5、PM10及CH)、氮氧化物及硫氧化物的排放。其次,該助燃劑亦可作為柴、氣、機車燃油添加劑,可以減少燃油量、提升馬力以及可以減少懸浮微粒(PM2.5、PM10及CH)、氮氧化物及硫氧化物的排放。 With the preparation method and system of the combustion aid of the present invention, the produced combustion aid can be used as a fuel additive for small fuel boilers, which can increase the combustion efficiency, reduce the amount of fuel, coal, and reduce suspended particulates (PM2.5, PM10 and CH), nitrogen oxides and sulfur oxides emissions. Secondly, the combustion aid can also be used as a fuel additive for diesel, gas, and locomotives, which can reduce fuel consumption, increase horsepower, and reduce emissions of suspended particulates (PM2.5, PM10, and CH), nitrogen oxides, and sulfur oxides.

上述實施例僅係為了方便說明而舉例而已,本發明所主張之權利範圍自應以申請專利範圍所述為準,而非僅限於上述實施例。 The above embodiments are only examples for the convenience of description, and the scope of rights claimed by the present invention should be subject to the scope of the patent application, and not limited to the above embodiments.

1‧‧‧助燃劑的製備系統 1‧‧‧Combustion agent preparation system

10‧‧‧轉爐煙塵回收裝置 10‧‧‧Converter soot recovery device

11‧‧‧轉爐煙塵 11‧‧‧Converter soot

20‧‧‧脫水設備 20‧‧‧Dehydration equipment

21‧‧‧泥餅 21‧‧‧ Mud cake

30‧‧‧燃燒裝置 30‧‧‧Combustion device

31‧‧‧燃料 31‧‧‧ Fuel

40‧‧‧攪拌裝置 40‧‧‧Stirring device

Claims (10)

一種助燃劑的製備方法,包括:(a)將一轉爐塵泥脫水以產生一泥餅,該泥餅包括40wt%~70wt%的氧化鐵、10wt%~30wt%的氧化鈣及20wt%~40wt%的水;(b)相對於一燃料的總重量,將0.1wt%至0.0001wt%的該泥餅加入該燃料中;以及(c)將該泥餅及該燃料混勻攪拌;其中,0.1wt%至0.0001wt%的該泥餅在該燃料中作為一助燃劑。 A method for preparing a combustion aid includes: (a) dewatering a converter dust sludge to produce a mud cake, the mud cake including 40 wt% to 70 wt% iron oxide, 10 wt% to 30 wt% calcium oxide and 20 wt% to 40 wt % Water; (b) add 0.1wt% to 0.0001wt% of the mud cake to the fuel relative to the total weight of a fuel; and (c) mix and mix the mud cake and the fuel; wherein, 0.1 The wt% to 0.0001 wt% of the mud cake acts as a combustion aid in the fuel. 如申請專利範圍第1項所述之助燃劑的製備方法,其中,在產生該泥餅的步驟之後更包括一第一燃燒步驟,在該第一燃燒步驟中該燃料反應形成一氮氧化物、一硫氧化物、一碳氫化合物或一懸浮微粒。 The method for preparing a combustion aid as described in item 1 of the patent application scope, wherein after the step of generating the mud cake, a first combustion step is further included, in which the fuel reacts to form a nitrogen oxide, A sulfur oxide, a hydrocarbon or a suspended particulate. 如申請專利範圍第1項所述之助燃劑的製備方法,其中,在將該泥餅及該燃料混勻攪拌之後更包括一第二燃燒步驟,該第二燃燒步驟包括溫度範圍在200℃~700℃之間的一反應溫度。 The method for preparing a combustion aid as described in item 1 of the patent application scope, wherein after the mud cake and the fuel are mixed and stirred, a second combustion step is further included. The second combustion step includes a temperature range of 200°C~ A reaction temperature between 700 °C. 如申請專利範圍第3項所述之助燃劑的製備方法,其中,該反應溫度在400℃~500℃之間時,經由一氧化碳將該氧化鐵表面的Fe3+還原為Fe2+,Fe2+再將氮氧化物還原為一氮氣。 The method for preparing a combustion aid as described in item 3 of the patent application scope, wherein, when the reaction temperature is between 400°C and 500°C, Fe 3+ on the surface of the iron oxide is reduced to Fe 2+ , Fe 2 via carbon monoxide + Then reduce the nitrogen oxide to nitrogen. 如申請專利範圍第1項所述之助燃劑的製備方法,其中,該燃料係為一固體燃料或一液體燃料。 The method for preparing a combustion aid as described in item 1 of the patent application scope, wherein the fuel is a solid fuel or a liquid fuel. 一種助燃劑的製備系統,包括:一轉爐煙塵回收裝置,經由一濕法回收一轉爐煙塵以產生一轉爐塵泥;一脫水設備,將該轉爐塵泥進行脫水以產生一泥餅,該泥餅包 括40wt%~70wt%的氧化鐵、10wt%~30wt%的氧化鈣及20wt%~40wt%的水;一燃燒裝置,設置一燃料,相對於該燃料的總重量,將0.1wt%至0.0001wt%的該泥餅加入該燃料中;以及一攪拌裝置,將該泥餅及該燃料混勻攪拌;其中,0.1wt%至0.0001wt%的該泥餅在該燃料中作為一助燃劑。 A combustion aid preparation system includes: a converter soot recovery device that recovers a converter soot through a wet process to produce a converter dust and sludge; and a dehydration device that dehydrates the converter soot to produce a mud cake, the mud cake package Including 40wt% ~ 70wt% iron oxide, 10wt% ~ 30wt% calcium oxide and 20wt% ~ 40wt% water; a combustion device, set a fuel, relative to the total weight of the fuel, 0.1wt% to 0.0001wt % Of the mud cake is added to the fuel; and a stirring device, the mud cake and the fuel are mixed and stirred; wherein, 0.1 wt% to 0.0001 wt% of the mud cake is used as a combustion aid in the fuel. 如申請專利範圍第6項所述之助燃劑的製備系統,其中,在產生該泥餅之後,於該燃燒裝置中進行一第一燃燒步驟,在該第一燃燒步驟中該燃料反應形成一氮氧化物、一硫氧化物、一碳氫化合物或一懸浮微粒。 The preparation system for a combustion adjuvant as described in item 6 of the patent application scope, wherein, after the mud cake is produced, a first combustion step is performed in the combustion device, and the fuel reacts to form a nitrogen in the first combustion step Oxide, a sulfur oxide, a hydrocarbon or a suspended particulate. 如申請專利範圍第6項所述之助燃劑的製備系統,其中,在將該泥餅及該燃料混勻攪拌之後,在該燃燒裝置中進行一第二燃燒步驟,第二燃燒步驟包括溫度範圍在200℃~700℃之間的一反應溫度。 A preparation system for a combustion aid as described in item 6 of the patent application scope, wherein after the mud cake and the fuel are mixed and stirred, a second combustion step is performed in the combustion device, and the second combustion step includes a temperature range A reaction temperature between 200 ℃ ~ 700 ℃. 申請專利範圍第8項所述之助燃劑的製備系統,其中,該反應溫度在400℃~500℃之間時,經由一氧化碳將該氧化鐵表面的Fe3+還原為Fe2+,Fe2+再將氮氧化物還原為一氮氣。 The system for preparing a combustion aid described in item 8 of the patent application scope, wherein, when the reaction temperature is between 400°C and 500°C, Fe 3+ on the surface of the iron oxide is reduced to Fe 2+ , Fe 2+ via carbon monoxide Then reduce the nitrogen oxide to nitrogen. 如申請專利範圍第6項所述之助燃劑的製備系統,其中,該燃料係為一固體燃料或一液體燃料。 The system for preparing a combustion aid as described in item 6 of the patent application scope, wherein the fuel is a solid fuel or a liquid fuel.
TW107134734A 2018-10-02 2018-10-02 Preparation method and system of combustion-supporting agent TWI704233B (en)

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CN201910839469.7A CN110982577A (en) 2018-10-02 2019-09-06 Application of converter dust and mud as combustion improver in fuel combustion

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