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CN113332954B - A kind of sintering flue gas denitrification adsorbent and its preparation method and application - Google Patents

A kind of sintering flue gas denitrification adsorbent and its preparation method and application Download PDF

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CN113332954B
CN113332954B CN202110400815.9A CN202110400815A CN113332954B CN 113332954 B CN113332954 B CN 113332954B CN 202110400815 A CN202110400815 A CN 202110400815A CN 113332954 B CN113332954 B CN 113332954B
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adsorbent
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CN113332954A (en
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林国
张江
王炜
曾彪
陈绪亨
杨代伟
陈柏文
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Wuhan University of Science and Technology WHUST
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28002Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
    • B01J20/28011Other properties, e.g. density, crush strength
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28054Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
    • B01J20/28057Surface area, e.g. B.E.T specific surface area
    • B01J20/28064Surface area, e.g. B.E.T specific surface area being in the range 500-1000 m2/g
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/40Nitrogen compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases
    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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Abstract

本发明提供了一种烧结烟气脱硝吸附剂及其制备方法与应用。本发明通过将预定量的兰炭与硝酸铁加入蒸馏水中,充分搅拌后进行过滤、干燥,得到初产物;再将得到的初产物置于微波场中,在预定的微波功率及加热温度下反应预定时间,制备了烧结烟气脱硝吸附剂。通过上述方式,本发明能够以兰炭为载体,在其表面负载铁氧化物,从而制备稳定性好、强度高、脱硝率高且成本低廉的脱硝吸附剂;该脱硝吸附剂不仅能够用于烧结过程的烟气脱硝,吸附后的材料还可送入高炉替代部分喷吹煤料,实现了资源的多次利用;且本发明提供的制备方法工艺简单、易于调控、原材料廉价易得,具有较高的应用价值。The invention provides a sintering flue gas denitration adsorbent and a preparation method and application thereof. In the present invention, a predetermined amount of blue charcoal and ferric nitrate are added into distilled water, fully stirred, and then filtered and dried to obtain an initial product; and then the obtained initial product is placed in a microwave field to react at a predetermined microwave power and heating temperature. At a predetermined time, a sintered flue gas denitration adsorbent was prepared. Through the above method, the present invention can use blue carbon as a carrier and support iron oxide on its surface, thereby preparing a denitration adsorbent with good stability, high strength, high denitration rate and low cost; the denitration adsorbent can not only be used for sintering In the process of flue gas denitrification, the adsorbed material can also be sent to the blast furnace to replace part of the coal injection, thereby realizing the multiple utilization of resources; and the preparation method provided by the invention is simple in process, easy to control, cheap and easy to obtain raw materials, and has the advantages of relatively low cost and low cost. high application value.

Description

一种烧结烟气脱硝吸附剂及其制备方法与应用A kind of sintering flue gas denitrification adsorbent and its preparation method and application

技术领域technical field

本发明涉及气体吸附材料制备与应用技术领域,尤其涉及一种烧结烟气 脱硝吸附剂及其制备方法与应用。The invention relates to the technical field of preparation and application of gas adsorption materials, in particular to a sintered flue gas denitration adsorbent and a preparation method and application thereof.

背景技术Background technique

在钢铁行业中,烧结烟气的排放占整个钢铁工业烟气排放的40%左右, 烧结烟气中包含较多的细粉尘、硫氧化物、氮氧化物、二噁英等污染物,特 别是氮氧化物,给人们的生活环境带来严重影响,同时环保部出台修改了《钢 铁烧结、球团工业大气污染物排放标准》文件,对企业烟气排放提出了更加 严格的要求。如何降低烧结烟气氮氧化物的排放,是广大冶金工作者一直在 努力解决的问题。In the iron and steel industry, sintering flue gas emissions account for about 40% of the entire iron and steel industry flue gas emissions, and sintering flue gas contains a lot of fine dust, sulfur oxides, nitrogen oxides, dioxins and other pollutants, especially Nitrogen oxides have a serious impact on people's living environment. At the same time, the Ministry of Environmental Protection has issued and revised the document "Emission Standards for Air Pollutants in Iron and Steel Sintering and Pelletizing Industries", which has put forward more stringent requirements for enterprise flue gas emissions. How to reduce the emission of nitrogen oxides in sintering flue gas is a problem that the majority of metallurgical workers have been trying to solve.

目前我国烧结烟气脱硝最重要的是NOX治理方法。但NOX的去除相当 困难,主要原因是烟道气中NOX的主要成分为相对稳定的NO。目前,净化 处理烟气中NO的方法按治理工艺可分为干法和湿法。其中,干法主要有: 吸附法、非催化还原法、等离子法、催化还原法等;湿法主要有:氧化吸收、 络合吸收、碱吸收、液相还原吸收、酸吸收、微生物法等。在上述方法中, 吸附法以其工艺简单、脱硝性能好等优点得到了广泛应用,而吸附法的实际 效果与相应的吸附材料密切相关。因此,如何研发出具有优异脱硝效果的吸 附材料已成为当前的研究重点。At present, the most important method for denitrification of sintering flue gas in China is the NO X treatment method. However, the removal of NO X is quite difficult, mainly because the main component of NO X in the flue gas is relatively stable NO. At present, the method of purifying and treating NO in flue gas can be divided into dry method and wet method according to the treatment process. Among them, dry methods mainly include: adsorption method, non-catalytic reduction method, plasma method, catalytic reduction method, etc.; wet methods mainly include: oxidation absorption, complex absorption, alkali absorption, liquid-phase reduction absorption, acid absorption, microbial method, etc. Among the above methods, the adsorption method has been widely used due to its advantages of simple process and good denitration performance, and the actual effect of the adsorption method is closely related to the corresponding adsorption material. Therefore, how to develop adsorption materials with excellent denitration effect has become the current research focus.

公开号为CN106563482A的专利提供了一种低温脱硝富氮多孔炭材料的 制备方法。该专利以原煤和兰炭颗粒为主体,以粘合剂和去离子水为客体, 经混合、成型、炭化和水蒸气活化,得到富含多孔的炭材料,最后经混酸氧 化和醋酸亚铁还原形成低温高脱硝效率的富氮多孔炭材料。然而,该方法不 仅工艺复杂,且制得的多孔炭材料在不同温度下的脱硝率仅能达到65%以上, 难以满足实际生产与应用的需求。Patent publication number CN106563482A provides a preparation method of low-temperature denitration nitrogen-enriched porous carbon material. The patent uses raw coal and blue carbon particles as the main body, binder and deionized water as the guest, and obtains a porous carbon material through mixing, molding, carbonization and steam activation. Finally, it is oxidized by mixed acid and reduced by ferrous acetate. A nitrogen-rich porous carbon material with high denitration efficiency at low temperature is formed. However, this method is not only complicated in process, but also the denitrification rate of the prepared porous carbon material at different temperatures can only reach more than 65%, which is difficult to meet the needs of actual production and application.

有鉴于此,有必要对现有的脱硝吸附剂及其制备方法进行改进,利用更 简单的工艺制备具有高脱硝率的烧结烟气脱硝吸附剂,以解决上述问题。In view of this, it is necessary to improve the existing denitration adsorbent and its preparation method, and use a simpler process to prepare a sintered flue gas denitration adsorbent with high denitration rate to solve the above problems.

发明内容SUMMARY OF THE INVENTION

针对上述现有技术的缺陷,本发明的目的在于提供一种烧结烟气脱硝吸 附剂及其制备方法与应用。通过以兰炭为载体,在其表面负载铁氧化物,制 备稳定性好、强度高、脱硝率高且成本低廉的脱硝吸附剂;该脱硝吸附剂不 仅能够用于烧结过程的烟气脱硝,吸附后的材料还可送入高炉替代部分喷吹 煤料,实现资源的多次利用。In view of the above-mentioned defects of the prior art, the object of the present invention is to provide a sintering flue gas denitration adsorbent and its preparation method and application. By using blue carbon as a carrier and supporting iron oxides on its surface, a denitration adsorbent with good stability, high strength, high denitration rate and low cost is prepared; the denitration adsorbent can not only be used for flue gas denitrification in the sintering process, The resulting material can also be sent to the blast furnace to replace part of the coal injection to realize the multiple utilization of resources.

为实现上述目的,本发明提供了一种烧结烟气脱硝吸附剂的制备方法, 包括如下步骤:In order to achieve the above purpose, the present invention provides a preparation method of a sintered flue gas denitration adsorbent, comprising the following steps:

S1、将预定量的兰炭与硝酸铁加入蒸馏水中,充分搅拌后进行过滤,再 干燥一定时间使兰炭含水量在10%~20%之间,得到初产物;S1, a predetermined amount of blue charcoal and ferric nitrate are added to distilled water, filter after fully stirring, and then dry for a certain time to make the blue charcoal water content between 10%~20%, obtain initial product;

S2、将步骤S1得到的所述初产物置于微波场中,在预定的微波功率及 加热温度下反应预定时间,得到烧结烟气脱硝吸附剂。S2. The initial product obtained in step S1 is placed in a microwave field, and reacted for a predetermined time under a predetermined microwave power and a heating temperature to obtain a sintered flue gas denitration adsorbent.

作为本发明的进一步改进,在步骤S1中,所述蒸馏水与所述兰炭的液 固比为(5~15):1mL/g。As a further improvement of the present invention, in step S1, the liquid-solid ratio of the distilled water and the blue charcoal is (5~15): 1mL/g.

作为本发明的进一步改进,在步骤S1中,所述蒸馏水与所述硝酸铁的 液固比为(25~35):1mL/g。As a further improvement of the present invention, in step S1, the liquid-solid ratio of the distilled water and the ferric nitrate is (25~35): 1mL/g.

作为本发明的进一步改进,在步骤S1中,所述搅拌过程在室温条件下 进行,搅拌时间为1~3h。As a further improvement of the present invention, in step S1, the stirring process is carried out at room temperature, and the stirring time is 1-3 hours.

作为本发明的进一步改进,在步骤S2中,所述微波功率为600~800W, 所述加热温度为600~800℃。As a further improvement of the present invention, in step S2, the microwave power is 600-800W, and the heating temperature is 600-800°C.

作为本发明的进一步改进,在步骤S2中,所述反应预定时间为反应 15~35min。As a further improvement of the present invention, in step S2, the predetermined reaction time is 15-35 minutes.

为实现上述目的,本发明还提供了一种烧结烟气脱硝吸附剂,该烧结烟 气脱硝吸附剂根据上述技术方案中任一技术方案制备得到。In order to achieve the above object, the present invention also provides a sintered flue gas denitration adsorbent prepared according to any one of the above technical solutions.

作为本发明的进一步改进,所述烧结烟气脱硝吸附剂的比表面积为 790~820m2/g,抗压强度为380~430N/cm2,NOX转化率大于90%。As a further improvement of the present invention, the specific surface area of the sintered flue gas denitration adsorbent is 790-820 m 2 /g, the compressive strength is 380-430 N/cm 2 , and the NO X conversion rate is greater than 90%.

为实现上述目的,本发明还提供了所述烧结烟气脱硝吸附剂在烧结烟气 脱硝领域的应用。To achieve the above object, the present invention also provides the application of the sintering flue gas denitrification adsorbent in the field of sintering flue gas denitrification.

作为本发明的进一步改进,所述烧结烟气脱硝吸附剂在吸附所述烧结烟 气后用于替代高炉喷吹煤粉。As a further improvement of the present invention, the sintering flue gas denitration adsorbent is used to replace the blast furnace injection of pulverized coal after adsorbing the sintering flue gas.

本发明的有益效果是:The beneficial effects of the present invention are:

(1)本发明以兰炭为载体,通过将其与硝酸铁共混,并进行微波加热, 从而以简便高效的工艺在兰炭表面均匀负载铁氧化物,并将其作为烧结烟气 脱硝吸附剂。基于上述制备工艺,本发明制备的负载有铁氧化物的兰炭具有 较高的比表面积、抗压强度和NOX转化率,能够作为吸附剂用于烧结烟气脱 硝,且具有稳定性好、强度高、脱硝率高、成本低廉等优点。同时,本发明 制备的脱硝吸附剂不仅能够用于烧结过程的烟气脱硝,吸附后的材料还可送 入高炉替代部分喷吹煤料,实现资源的多次利用,具有较好的应用前景。(1) The present invention uses blue carbon as a carrier, and by blending it with ferric nitrate and heating it by microwave, so as to uniformly load iron oxides on the surface of blue carbon with a simple and efficient process, and use it as sintering flue gas denitrification adsorption. agent. Based on the above preparation process, the iron oxide-loaded blue carbon prepared by the present invention has high specific surface area, compressive strength and NO X conversion rate, can be used as an adsorbent for sintering flue gas denitrification, and has good stability, It has the advantages of high strength, high denitrification rate and low cost. At the same time, the denitration adsorbent prepared by the invention can not only be used for flue gas denitrification in the sintering process, but the adsorbed material can also be sent to the blast furnace to replace part of the coal injection, so as to realize the multiple utilization of resources and have a good application prospect.

(2)兰炭作为煤在较低温度下热解的产物,其尚未热解完全,比表面积 比活性炭小,由于未得到有效利用而被废弃,造成资源的严重浪费。本发明 通过将兰炭作为载体,相对于活性炭来说,既可以有效降低成本,又能够提 高资源的利用率。在此基础上,本发明通过在兰炭表面负载铁氧化物,不仅 能够利用未完全热解的兰炭内部较多的氢、氧及其丰富的孔隙和表面结构保 证铁氧化物在兰炭中的均匀、牢固负载,还能够利用负载的铁氧化物有效提 高兰炭的强度及其吸附性能,从而实现对烧结烟气中氮氧化物的高效吸附, 达到优异的脱硝效果。并且,本发明通过在兰炭上负载铁氧化物制备的脱硝 吸附剂在完成吸附后还能够送入高炉替代部分喷吹煤料,既实现了资源的多 次利用,还完成了对吸附剂的无害化处理,具有较好的经济效益和环境效益。(2) Blue charcoal is the product of coal pyrolysis at lower temperature, but it has not been pyrolyzed completely, and its specific surface area is smaller than that of activated carbon, and it is discarded because it is not effectively utilized, resulting in a serious waste of resources. Compared with activated carbon, the present invention can effectively reduce the cost and improve the utilization rate of resources by using the blue carbon as the carrier. On this basis, by loading iron oxides on the surface of blue carbon, the present invention can not only utilize more hydrogen and oxygen inside the blue carbon that is not completely pyrolyzed and its rich pores and surface structure to ensure that iron oxides are in the blue carbon It can also effectively improve the strength and adsorption performance of blue carbon by using the supported iron oxides, so as to achieve efficient adsorption of nitrogen oxides in sintering flue gas and achieve excellent denitration effect. In addition, the denitration adsorbent prepared by loading iron oxides on blue carbon in the present invention can also be sent to the blast furnace to replace part of the coal injection after the adsorption is completed, which not only realizes the multiple utilization of resources, but also completes the adsorption of the adsorbent. Harmless treatment has good economic and environmental benefits.

(3)本发明通过将干燥后兰炭的含水量控制在10%~20%,再将其置于 微波场中,不仅能够利用微波本身的催化造孔丰富兰炭的孔隙结构,还能够 使负载有硝酸铁的兰炭中含有的水分在微波场下迅速吸波升温并产生水蒸气, 进一步促进兰炭中大孔的形成,起到微波活化与水蒸气活化协同作用的双重 活化效果,从而使本发明制备的吸附剂具有优于常规吸附剂的高比表面积, 以实现对烧结烟气中氮氧化物的高效吸附。(3) In the present invention, by controlling the water content of the dried blue carbon to be 10% to 20%, and then placing it in a microwave field, not only can the pore structure of the blue carbon be enriched by the catalytic pore formation of the microwave itself, but also the pore structure of the blue carbon can be enriched. The water contained in the blue charcoal loaded with ferric nitrate rapidly absorbs waves and heats up under the microwave field and generates water vapor, which further promotes the formation of macropores in the blue charcoal, and plays a dual activation effect of the synergistic effect of microwave activation and water vapor activation, thereby The adsorbent prepared by the present invention has a higher specific surface area than the conventional adsorbent, so as to realize the efficient adsorption of nitrogen oxides in the sintering flue gas.

(4)本发明通过对蒸馏水与兰炭、硝酸铁的液固比进行控制,并进一步 对微波加热过程的参数进行控制,能够对铁氧化物的负载量及形成的吸附剂 的孔隙结构进行有效调控,从而使制备的烧结烟气脱硝吸附剂具有较高的强 度、较好的稳定性和优异的吸附性。且本发明提供的制备方法工艺简单、易 于调控、原材料廉价易得,制备过程中不需要进行常规的酸洗等处理方式, 不会造成二次污染,且制得的产品在烧结烟气脱硝和高炉替代部分喷吹煤粉 方面均具有很大的潜力,具有较高的应用价值。(4) The present invention can effectively control the loading of iron oxides and the pore structure of the adsorbent by controlling the liquid-solid ratio of distilled water, blue carbon and ferric nitrate, and further controlling the parameters of the microwave heating process. Therefore, the prepared sintered flue gas denitrification adsorbent has high strength, good stability and excellent adsorption. In addition, the preparation method provided by the present invention is simple in process, easy to control, cheap and easy to obtain raw materials, does not require conventional pickling and other treatment methods in the preparation process, and will not cause secondary pollution, and the prepared product is used in sintering flue gas denitrification and sintering. Blast furnaces have great potential in replacing part of pulverized coal injection, and have high application value.

具体实施方式Detailed ways

为了使本发明的目的、技术方案和优点更加清楚,下面结合具体实施例 对本发明进行详细描述。In order to make the objects, technical solutions and advantages of the present invention clearer, the present invention will be described in detail below with reference to specific embodiments.

另外,还需要说明的是,术语“包括”、“包含”或者其任何其他变体意在 涵盖非排他性的包含,从而使得包括一系列要素的过程、方法、物品或者设 备不仅包括那些要素,而且还包括没有明确列出的其他要素,或者是还包括 为这种过程、方法、物品或者设备所固有的要素。In addition, it should be noted that the terms "comprising", "comprising" or any other variation thereof are intended to encompass a non-exclusive inclusion such that a process, method, article or apparatus comprising a series of elements includes not only those elements, but also Also included are other elements not expressly listed or inherent to such a process, method, article or apparatus.

本发明提供了一种烧结烟气脱硝吸附剂的制备方法,包括如下步骤:The invention provides a preparation method of a sintered flue gas denitration adsorbent, comprising the following steps:

S1、将预定量的兰炭与硝酸铁加入蒸馏水中,充分搅拌后进行过滤,再 干燥一定时间使兰炭含水量在10%~20%之间,得到初产物;S1, a predetermined amount of blue charcoal and ferric nitrate are added to distilled water, filter after fully stirring, and then dry for a certain time to make the blue charcoal water content between 10%~20%, obtain initial product;

S2、将步骤S1得到的所述初产物置于微波场中,在预定的微波功率及 加热温度下反应预定时间,得到烧结烟气脱硝吸附剂。S2. The initial product obtained in step S1 is placed in a microwave field, and reacted for a predetermined time under a predetermined microwave power and a heating temperature to obtain a sintered flue gas denitration adsorbent.

作为本发明的进一步改进,在步骤S1中,所述蒸馏水与所述兰炭的液 固比为(5~15):1mL/g;所述蒸馏水与所述硝酸铁的液固比为(25~35):1mL/g; 所述搅拌过程在室温条件下进行,搅拌时间为1~3h。As a further improvement of the present invention, in step S1, the liquid-solid ratio of the distilled water and the blue charcoal is (5~15): 1 mL/g; the liquid-solid ratio of the distilled water and the ferric nitrate is (25 ~35): 1 mL/g; The stirring process is carried out at room temperature, and the stirring time is 1 to 3 h.

在步骤S2中,所述微波功率为600~800W,所述加热温度为600~800℃; 所述反应预定时间为反应15~35min。In step S2, the microwave power is 600-800W, the heating temperature is 600-800°C; and the predetermined reaction time is 15-35 minutes.

本发明还提供了一种烧结烟气脱硝吸附剂,该烧结烟气脱硝吸附剂根据 上述技术方案中任一技术方案制备得到。The present invention also provides a sintering flue gas denitration adsorbent prepared according to any one of the above technical solutions.

所述烧结烟气脱硝吸附剂的比表面积为790~820m2/g,抗压强度为 380~430N/cm2,NOX转化率大于90%。The specific surface area of the sintered flue gas denitration adsorbent is 790-820 m 2 /g, the compressive strength is 380-430 N/cm 2 , and the NO X conversion rate is greater than 90%.

本发明还提供了所述烧结烟气脱硝吸附剂在烧结烟气脱硝领域的应用。The invention also provides the application of the sintering flue gas denitration adsorbent in the field of sintering flue gas denitration.

所述烧结烟气脱硝吸附剂在吸附所述烧结烟气后用于替代高炉喷吹煤 粉。The sintering flue gas denitration adsorbent is used to replace the blast furnace blowing pulverized coal after adsorbing the sintering flue gas.

下面结合具体的实施例对本发明提供的烧结烟气脱硝吸附剂及其制备 方法与应用进行说明。The sintered flue gas denitrification adsorbent provided by the present invention and its preparation method and application will be described below with reference to specific embodiments.

实施例1Example 1

本实施例提供了一种烧结烟气脱硝吸附剂的制备方法,包括如下步骤:The present embodiment provides a preparation method of a sintered flue gas denitration adsorbent, comprising the following steps:

S1、将兰炭与硝酸铁加入蒸馏水中,控制蒸馏水与兰炭的液固比为5:1 mL/g,蒸馏水与硝酸铁的液固比为25:1mL/g。在室温条件下搅拌1h后,将 产物过滤分离后置于恒温干燥箱中烘干,得到初产物;S1. Add blue charcoal and ferric nitrate into distilled water, control the liquid-solid ratio of distilled water and blue charcoal to be 5:1 mL/g, and the liquid-solid ratio of distilled water to ferric nitrate to be 25:1 mL/g. After stirring for 1 h at room temperature, the product was filtered and separated and then dried in a constant temperature drying oven to obtain the initial product;

S2、将步骤S1得到的所述初产物置于微波场中,在微波功率600W、加 热温度600℃的条件下反应15min,得到负载铁氧化物的兰炭,并将其作为烧 结烟气脱硝吸附剂。S2. The initial product obtained in step S1 is placed in a microwave field, and reacted for 15 min under the conditions of microwave power 600W and heating temperature 600°C to obtain iron oxide-loaded blue carbon, which is used as sintering flue gas for denitration adsorption agent.

实施例2~3及对比例1~4Examples 2-3 and Comparative Examples 1-4

实施例2~3及对比例1~4分别提供了一种烧结烟气脱硝吸附剂的制备方 法,与实施例1相比,不同之处在于改变了步骤S1、S2中的工艺参数。实施 例2~3及对比例1~4的相应工艺参数如表1所示,其余步骤均与实施例1一 致,在此不再赘述。Embodiments 2 to 3 and comparative examples 1 to 4 respectively provide a preparation method of a sintered flue gas denitration adsorbent. Compared with embodiment 1, the difference is that the process parameters in steps S1 and S2 are changed. The corresponding process parameters of Examples 2 to 3 and Comparative Examples 1 to 4 are shown in Table 1, and the remaining steps are the same as those of Example 1, and will not be repeated here.

表1实施例2~3及对比例1~4的工艺参数Table 1 Process parameters of Examples 2-3 and Comparative Examples 1-4

Figure BDA0003020313800000061
Figure BDA0003020313800000061

为比较不同工艺参数下制备的烧结烟气脱硝吸附剂的性能,对实施例 1~3及对比例1~4制备的烧结烟气脱硝吸附剂的比表面积、抗压强度和NOX转化率进行检测,结果如表2所示。In order to compare the performance of the sintered flue gas denitrification adsorbents prepared under different process parameters, the specific surface area, compressive strength and NO X conversion rate of the sintered flue gas denitration adsorbents prepared in Examples 1 to 3 and Comparative Examples 1 to 4 were tested. The results are shown in Table 2.

表2实施例1~3及对比例1~4制备的烧结烟气脱硝吸附剂的检测数据Table 2 Detection data of the sintered flue gas denitration adsorbents prepared in Examples 1-3 and Comparative Examples 1-4

Figure BDA0003020313800000062
Figure BDA0003020313800000062

由表2可以看出,微波功率大、微波加热时间长的时候所制备的吸附材 料内孔结构会坍塌,虽然其抗压强度较高,但是氮氧化物转化率较低;当微 波功率低且微波加热时间短的时候所获得的吸附材料比表面积较低,脱硝能 力低。只有当兰炭和硝酸铁配加比例适当且微波功率和加热时间合适的情况 下,所制备得到的吸附材料才具有较好的脱硝能力。It can be seen from Table 2 that when the microwave power is high and the microwave heating time is long, the inner pore structure of the adsorbent material will collapse. Although its compressive strength is high, the nitrogen oxide conversion rate is low; when the microwave power is low and the When the microwave heating time is short, the adsorption material obtained has a lower specific surface area and lower denitrification capacity. Only when the proportion of blue carbon and ferric nitrate is appropriate and the microwave power and heating time are appropriate, the prepared adsorbent has a good denitration ability.

基于上述分析,本发明通过对蒸馏水与兰炭、硝酸铁的液固比进行控制, 并进一步对微波加热过程的参数进行控制,能够对铁氧化物的负载量及其与 兰炭的结合程度进行有效调控,从而使制备的烧结烟气脱硝吸附剂具有较大 的比表面积、较高的强度和优异的吸附性,达到较高的脱硝率,以满足实际 应用的需求。同时,本发明各实施例制备的烧结烟气脱硝吸附剂不仅能够用 于对烧结烟气进行高效脱硝,在吸附氮氧化物后,还能够作为高炉喷吹煤料 的替代品送入高炉,在完成对吸附剂的无害化处理的同时实现了资源的多次 利用,具有较好的应用前景。Based on the above analysis, the present invention controls the liquid-solid ratio of distilled water, blue charcoal, and ferric nitrate, and further controls the parameters of the microwave heating process, so that the loading of iron oxides and the degree of combination thereof with blue charcoal can be controlled. Effective regulation, so that the prepared sintered flue gas denitrification adsorbent has a large specific surface area, high strength and excellent adsorption, and achieves a high denitrification rate to meet the needs of practical applications. At the same time, the sintering flue gas denitrification adsorbent prepared in each embodiment of the present invention can not only be used for efficient denitrification of sintering flue gas, but also can be sent to the blast furnace as a substitute for blast furnace injection coal after adsorbing nitrogen oxides. The harmless treatment of the adsorbent is completed and the resources are reused many times, which has a good application prospect.

综上所述,本发明提供了一种烧结烟气脱硝吸附剂及其制备方法与应用。 本发明通过将预定量的兰炭与硝酸铁加入蒸馏水中,充分搅拌后进行过滤、 干燥,得到初产物;再将得到的初产物置于微波场中,在预定的微波功率及 加热温度下反应预定时间,制备了烧结烟气脱硝吸附剂。通过上述方式,本 发明能够以兰炭为载体,在其表面负载铁氧化物,从而制备稳定性好、强度 高、脱硝率高且成本低廉的脱硝吸附剂;该脱硝吸附剂不仅能够用于烧结过 程的烟气脱硝,吸附后的材料还可送入高炉替代部分喷吹煤料,实现了资源 的多次利用;且本发明提供的制备方法工艺简单、易于调控、原材料廉价易 得,具有较高的应用价值。In summary, the present invention provides a sintered flue gas denitration adsorbent and a preparation method and application thereof. In the present invention, a predetermined amount of blue charcoal and ferric nitrate are added into distilled water, and the initial product is obtained by filtration and drying after full stirring; and then the obtained initial product is placed in a microwave field to react under a predetermined microwave power and heating temperature. At a predetermined time, a sintered flue gas denitration adsorbent was prepared. Through the above method, the present invention can use blue carbon as a carrier and support iron oxide on its surface, thereby preparing a denitration adsorbent with good stability, high strength, high denitration rate and low cost; the denitration adsorbent can not only be used for sintering In the process of flue gas denitrification, the adsorbed material can also be sent to the blast furnace to replace part of the coal injection, thereby realizing the multiple utilization of resources; and the preparation method provided by the invention is simple in process, easy to control, cheap and easy to obtain raw materials, and has the advantages of relatively low cost and low cost. high application value.

以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施 例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发 明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范 围。The above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be modified or equivalently replaced. Without departing from the spirit and scope of the technical solutions of the present invention.

Claims (6)

1. A preparation method of a sintering flue gas denitration adsorbent is characterized by comprising the following steps:
s1, adding a predetermined amount of semi-coke and ferric nitrate into distilled water, fully stirring, filtering, and drying for a certain time to ensure that the water content of the semi-coke is between 10 and 20 percent to obtain a primary product; the liquid-solid ratio of the distilled water to the semi-coke is (5-15) to 1 mL/g; the liquid-solid ratio of the distilled water to the ferric nitrate is (25-35) to 1 mL/g;
s2, placing the primary product obtained in the step S1 in a microwave field, and reacting for a preset time under a preset microwave power and heating temperature to obtain a sintered flue gas denitration adsorbent; the microwave power is 600-800W, and the heating temperature is 600-800 ℃;
the specific surface area of the sintering flue gas denitration adsorbent is 790-820 m2(g) the compressive strength is 380-430N/cm2,NOXThe conversion is greater than 90%.
2. The preparation method of the sintered flue gas denitration adsorbent according to claim 1, characterized by comprising the following steps: in step S1, the stirring process is performed at room temperature for 1-3 hours.
3. The preparation method of the sintered flue gas denitration adsorbent according to claim 1, characterized by comprising the following steps: in step S2, the reaction time is 15-35 min.
4. The sintered flue gas denitration adsorbent is characterized in that: the sintered flue gas denitration adsorbent is prepared by the preparation method of any one of claims 1 to 3.
5. The application of the sintered flue gas denitration adsorbent prepared by the preparation method of any one of claims 1 to 3 or the sintered flue gas denitration adsorbent of claim 4 is characterized in that: the sintering flue gas denitration adsorbent is applied to the field of sintering flue gas denitration.
6. The application of the sintered flue gas denitration adsorbent according to claim 5, wherein: the sintering flue gas denitration adsorbent is used for replacing blast furnace injection coal powder after adsorbing the sintering flue gas.
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