CN116903276A - A powdery raw meal melting accelerator and its preparation method - Google Patents
A powdery raw meal melting accelerator and its preparation method Download PDFInfo
- Publication number
- CN116903276A CN116903276A CN202310916629.XA CN202310916629A CN116903276A CN 116903276 A CN116903276 A CN 116903276A CN 202310916629 A CN202310916629 A CN 202310916629A CN 116903276 A CN116903276 A CN 116903276A
- Authority
- CN
- China
- Prior art keywords
- electrolytic aluminum
- solid waste
- rare earth
- sodium
- aluminum solid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/38—Preparing or treating the raw materials individually or as batches, e.g. mixing with fuel
- C04B7/42—Active ingredients added before, or during, the burning process
- C04B7/428—Organic materials
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/38—Preparing or treating the raw materials individually or as batches, e.g. mixing with fuel
- C04B7/42—Active ingredients added before, or during, the burning process
- C04B7/421—Inorganic materials
- C04B7/424—Oxides, Hydroxides
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/36—Manufacture of hydraulic cements in general
- C04B7/38—Preparing or treating the raw materials individually or as batches, e.g. mixing with fuel
- C04B7/42—Active ingredients added before, or during, the burning process
- C04B7/421—Inorganic materials
- C04B7/425—Acids or salts thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
技术领域Technical field
本发明属于水泥熟料煅烧技术领域,具体涉及一种粉体生料熔解促进剂及其制备方法。The invention belongs to the technical field of cement clinker calcination, and specifically relates to a powdery raw meal melting accelerator and a preparation method thereof.
背景技术Background technique
据统计,典型水泥企业电力消耗占综合能源消耗量5.90%,原煤消耗占综合能源消耗量3.61%,燃料油消耗占综合能源消耗量0.49%。而对于燃煤在水泥能耗中,熟料能耗约占70%-80%。而在熟料煅烧过程中,碳酸盐的分解作为强吸热反应,所需热量约占悬浮预热窑或预分解窑生产总消耗的1/2,所需煤耗占比60-70%。在熟料烧成的过程中,液相的形成、固液反应等过程也需要消耗大量的能量,约占40%。因此促进碳酸钙的分解、改善煅烧过程中液相的生成条件及性质是促进熟料烧成、降低能耗的重要途径。According to statistics, typical cement enterprises’ electricity consumption accounts for 5.90% of comprehensive energy consumption, raw coal consumption accounts for 3.61% of comprehensive energy consumption, and fuel oil consumption accounts for 0.49% of comprehensive energy consumption. For coal-fired cement energy consumption, clinker energy consumption accounts for about 70%-80%. During the clinker calcination process, the decomposition of carbonate is a strong endothermic reaction, and the heat required accounts for about 1/2 of the total production consumption of the suspension preheating kiln or precalcining kiln, and the required coal consumption accounts for 60-70%. In the process of clinker firing, the formation of liquid phase, solid-liquid reaction and other processes also consume a large amount of energy, accounting for about 40%. Therefore, promoting the decomposition of calcium carbonate and improving the formation conditions and properties of the liquid phase during the calcination process are important ways to promote clinker sintering and reduce energy consumption.
铝冶炼行业蓬勃发展的同时,生产过程产生的炭渣、大修渣和铝灰等危险废物所带来的环境风险也日益凸显。目前电解铝过程中产生的固体危险废弃物,处置方法主要包括填埋法、焙烧法和资源综合利用等传统方法。填埋法流程简单,但易造成Al、F资源浪费,且会造成土壤和地下水污染。有价元素进行回收,有价金属回收方法目前大多仍大多停留在实验室阶段,还无法实现铝电解固废的高值化利用。水泥窑协同处置危险废物技术较为成熟,相关标准体系也较为完善。目前也有水泥窑协同处置技术,但普遍将其作为水泥生产的替代燃料,或替代原料,以实现固废的无害化处置。While the aluminum smelting industry is booming, the environmental risks posed by hazardous wastes such as carbon slag, overhaul slag and aluminum ash generated during the production process have become increasingly prominent. At present, the disposal methods of solid hazardous waste generated in the electrolytic aluminum process mainly include traditional methods such as landfill, roasting and comprehensive utilization of resources. The landfill method has a simple process, but it can easily cause waste of Al and F resources and cause soil and groundwater pollution. Valuable elements are recycled. Valuable metal recovery methods are still mostly in the laboratory stage, and it is not yet possible to achieve high-value utilization of aluminum electrolysis solid waste. The technology for collaborative disposal of hazardous waste in cement kilns is relatively mature, and the relevant standard system is also relatively complete. There is also cement kiln co-processing technology, but it is generally used as an alternative fuel or alternative raw material for cement production to achieve harmless disposal of solid waste.
经调研,电解铝固体废弃物中碱、氟含量较高,如电解铝大修渣中碱含量为14.23%,氟含量为11.503%,氟化物含量可达30%-40%,氟化物在高温过程中可生成新相,加速生料分解反应的发生,同时可与氧化钙、三氧化二铝形成氟铝酸钙固溶于熟料,是一种较优的改善生料的易烧性的材料,可提高熟料的产量,增强水泥强度。After investigation, the alkali and fluorine contents in electrolytic aluminum solid waste are relatively high. For example, the alkali content in electrolytic aluminum overhaul slag is 14.23%, the fluorine content is 11.503%, and the fluoride content can reach 30%-40%. Fluoride in high-temperature processes It can generate new phases in the clinker to accelerate the decomposition reaction of raw meal. At the same time, it can form calcium fluoroaluminate solid solution with calcium oxide and aluminum oxide and dissolve in the clinker. It is an excellent material for improving the burnability of raw meal. , can increase clinker production and enhance cement strength.
发明内容Contents of the invention
针对上述问题,本发明提供了一种粉体生料熔解促进剂及其制备方法,该促进剂可有效促进碳酸盐分解,降低碳酸钙分解温度,多组分协同降低共熔点,促进水泥熟料的烧成。In view of the above problems, the present invention provides a powdery raw meal melting accelerator and a preparation method thereof. The accelerator can effectively promote the decomposition of carbonate, reduce the decomposition temperature of calcium carbonate, and has multiple components that synergistically reduce the eutectic point and promote cement ripening. The burning of materials.
粉体生料煅烧熔解促进剂,包括以下重量百分比的原料制备而成:活化电解铝固体废弃物40-70%、共掺杂纳米稀土组分5-20%、煅烧助熔组分10-35%、辅助促分解组分5-20%。The powdered raw meal calcined melting accelerator is prepared by including the following weight percentages of raw materials: 40-70% of activated electrolytic aluminum solid waste, 5-20% of co-doped nano-rare earth components, and 10-35% of calcined fluxing components. %, auxiliary decomposition component 5-20%.
所述活化电解铝固体废弃物为电解铝固体废弃物通过机械-化学耦合活化法制得;The activated electrolytic aluminum solid waste is obtained from electrolytic aluminum solid waste through a mechanical-chemical coupling activation method;
所述电解铝固体废弃物为电解铝废大修渣和电解铝碳渣的一种或一种以上;The electrolytic aluminum solid waste is one or more of electrolytic aluminum waste overhaul slag and electrolytic aluminum carbon slag;
所述电解铝固体废弃物为电解铝废大修渣;The electrolytic aluminum solid waste is electrolytic aluminum waste overhaul slag;
所述电解铝废大修渣含有氟化物33.4%重量,含碳材料38.6%,霞石8.4%,氧化铝3.8%,莫来石5.1%,钠长石2.6%,生石膏0.3%,其他材料5.9%,水1.9%;The electrolytic aluminum waste overhaul slag contains 33.4% by weight of fluoride, 38.6% of carbonaceous materials, 8.4% of nepheline, 3.8% of alumina, 5.1% of mullite, 2.6% of albite, 0.3% of gypsum, and 5.9% of other materials. , water 1.9%;
所述共掺杂纳米稀土组分为稀土元素化合物通过多元共沉淀法制得;The co-doped nano-rare earth component is a rare earth element compound prepared by a multi-element co-precipitation method;
所述稀土元素化合物为硝酸铈、硝酸镧、氯化铈、氯化镧、硝酸钇中的一种或几种;The rare earth element compound is one or more of cerium nitrate, lanthanum nitrate, cerium chloride, lanthanum chloride, and yttrium nitrate;
所述煅烧助熔组分为硫代硫酸钠、磷酸二氢钠、硫酸锌中的一种或几种;The calcining fluxing component is one or more of sodium thiosulfate, sodium dihydrogen phosphate, and zinc sulfate;
所述辅助促分解组分氟硅酸钠、柠檬酸钠、油酸钠中的一种或几种;One or more of the auxiliary decomposition-promoting components sodium fluorosilicate, sodium citrate, and sodium oleate;
所述机械-化学耦合活化法制备活化电解铝固体废弃物,具体步骤如下:The mechanical-chemical coupling activation method prepares activated electrolytic aluminum solid waste. The specific steps are as follows:
取适量电解铝固体废弃物,加入行星磨内,同时向磨内加入助磨组分以300r/min进行粉磨,粉磨时间40min,保证粉磨后颗粒的结晶度降至最低值,无序程度>40%,粉磨结束后,向磨内按化学耦合激发剂/废弃物为2%的比例,加入化学激发剂,随后继续以500r/min粉磨时间60min,即得活化电解铝固体废弃物。Take an appropriate amount of electrolytic aluminum solid waste and add it to the planetary mill. At the same time, add grinding aid components to the mill for grinding at 300r/min. The grinding time is 40min to ensure that the crystallinity of the particles after grinding is reduced to the minimum value and disordered. The degree is >40%. After the grinding is completed, add a chemical activator into the mill at a ratio of chemical coupling initiator/waste of 2%, and then continue grinding at 500r/min for 60 minutes to obtain activated electrolytic aluminum solid waste. things.
所述助磨组分包含硬脂酸钠、油酸、乙醇的一种或多种;The grinding aid component includes one or more of sodium stearate, oleic acid, and ethanol;
所述化学激发剂为硫酸钠、硅酸钠和木质素磺酸钠中的一种或几种;The chemical activator is one or more of sodium sulfate, sodium silicate and sodium lignosulfonate;
所述的多元共沉淀法制备共掺杂纳米稀土组分,具体步骤如下:The described multi-element co-precipitation method prepares co-doped nano-rare earth components, and the specific steps are as follows:
以Ce(NO3)3·6H2O和La(NO3)3·6H2O为稀土组分原料,分别取适量Ce(NO3)3·6H2O和La(NO3)3·6H2O,按3:1的比例溶于去离子水中,配置为0.1mol/L的Ce3+、La3+共存稀土溶液,取适量共沉淀剂溶于去离子水,配置0.3mol/L的共沉淀剂溶液,在60℃以及搅拌速度400rpm的条件下,向共沉淀剂溶液中缓慢地加入共存稀土溶液。待反应完毕后,将溶液在室温静置2h。抽滤清洗后,烘干。将烘干后的材料置于行星式球磨机进行球磨,以500r/min,球磨时间为40min,即得共掺杂纳米稀土组分。Using Ce(NO 3 ) 3 ·6H 2 O and La(NO 3 ) 3 ·6H 2 O as rare earth component raw materials, take appropriate amounts of Ce(NO 3 ) 3 ·6H2O and La(NO 3 ) 3 ·6H 2 O respectively. , dissolve in deionized water at a ratio of 3:1, configure a 0.1mol/L Ce3+, La3+ rare earth solution, take an appropriate amount of coprecipitant and dissolve it in deionized water, configure a 0.3mol/L coprecipitant solution, and Under the conditions of 60° C. and a stirring speed of 400 rpm, the coexisting rare earth solution was slowly added to the coprecipitant solution. After the reaction is completed, let the solution stand at room temperature for 2 hours. After suction filtration and cleaning, dry it. Place the dried material into a planetary ball mill for ball milling at 500r/min and for 40min to obtain co-doped nano-rare earth components.
所述共沉淀剂为碳酸铵、碳酸氢铵、草酸、碳酸钠、氢氧化钠的一种或几种。The co-precipitating agent is one or more of ammonium carbonate, ammonium bicarbonate, oxalic acid, sodium carbonate, and sodium hydroxide.
所述的粉体生料熔解促进剂的制备方法,具体步骤如下:The preparation method of the powdery raw meal melting accelerator, the specific steps are as follows:
按比例取适量权利要求2所述的机械-化学耦合活化法制备的活化电解铝固体废弃物和权利要求3所述的多元共沉淀法制备的共掺杂纳米稀土组分,加入干粉搅拌机内,搅拌10min,随后向搅拌机内按比例加入权利要求1所述的煅烧助熔组分和生料促分解组分一起搅拌,搅拌时间20min,即得粉体熔解促进剂。Take an appropriate amount of the activated electrolytic aluminum solid waste prepared by the mechanical-chemical coupling activation method described in claim 2 and the co-doped nano rare earth component prepared by the multi-element co-precipitation method described in claim 3 in proportion, and add them into a dry powder mixer. Stir for 10 minutes, and then add the calcined fluxing component and the raw material decomposition promoting component described in claim 1 in proportion to the mixer and stir together for 20 minutes to obtain a powder melting accelerator.
所述粉体生料熔解促进剂采用如下方式中的至少一种加入到水泥生产过程中:The powdered raw meal melting accelerator is added to the cement production process in at least one of the following ways:
(1)将粉末状复合生料熔解促进剂在生料磨前皮带与水泥生料混合;(1) Mix the powdery composite raw meal melting accelerator with the cement raw meal on the belt before the raw meal mill;
(2)将粉末状复合生料熔解促进剂在进入预热器前与水泥生料混合;(2) Mix the powdery composite raw meal melting accelerator with the cement raw meal before entering the preheater;
本发明获得的有益效果:Beneficial effects obtained by the present invention:
(1)活化电解铝固体废弃物:机械活化后,电解铝固体废弃物颗粒尺寸变小显著变小,此时加入少量的化学激发剂可改变物料表面的物理化学等方面的性能,使粉料颗粒表面化学键的破坏加快,化学健力发生改变,粉料活性增加,具有更好的表面效应。在应用过程中,一是可在高温条件下生成新相,破坏晶体结构,使晶体结构趋向无定形化,促进碳酸盐分解反应的发生;二是可生成中间相,促使C3S的提前出现,提高烧成速度、达到降低水泥熟料烧成能耗的目的;三是含有微量多种金属元素,具有多元素协同降低共熔点的作用;四是废弃物中含有部分碳基组分,在高温时可放出部分热量,有助于降低熟料制备煤耗。(1) Activated electrolytic aluminum solid waste: After mechanical activation, the particle size of electrolytic aluminum solid waste becomes significantly smaller. At this time, adding a small amount of chemical activators can change the physical and chemical properties of the material surface, making the powder The destruction of chemical bonds on the particle surface is accelerated, the chemical strength is changed, the activity of the powder is increased, and it has a better surface effect. During the application process, first, it can generate new phases under high temperature conditions, destroy the crystal structure, make the crystal structure tend to be amorphous, and promote the occurrence of carbonate decomposition reactions; second, it can generate intermediate phases, promoting the early appearance of C3S, Increase the firing speed and reduce the energy consumption of cement clinker firing; third, it contains trace amounts of various metal elements, which have the effect of multiple elements synergistically lowering the eutectic point; fourth, the waste contains some carbon-based components, which at high temperatures Part of the heat can be released at this time, which helps to reduce coal consumption in clinker preparation.
(2)共掺杂纳米稀土组分:在使用过程中,会进一步发生分解生成尺寸更小的多元纳米稀土组分,同时生成气体,扰动生料,有助于均匀分散;同时,纳米颗粒比表面积进一步增大,表面配位不足的原子占比更高,表面能进一步提升,表现出高活性的特点,更易与原材料发生反应,嵌入原料晶格内部,增加原料中的结构空位,促进质点扩散过程,降低反应势能,加速反应的发生。(2) Co-doped nano-rare earth components: During use, further decomposition will occur to generate smaller multi-element nano-rare earth components. At the same time, gas will be generated, disturbing the raw material, and helping to disperse evenly; at the same time, the nanoparticle ratio The surface area is further increased, the proportion of atoms with insufficient surface coordination is higher, the surface energy is further improved, showing high activity characteristics, and is easier to react with raw materials, embedded inside the raw material lattice, increasing structural vacancies in the raw materials, and promoting particle diffusion process, reducing the reaction potential energy and accelerating the occurrence of the reaction.
(3)煅烧助熔组分:碱金属、过渡金属等组分的引入,进一步增强多元素协同作用,降低体系最低共融温度,使液相可在在较低反应温度生成,液相提前出现,有助于增加液相量,造成局部电价不平,改变液相的性质,降低液相粘度,以促进C3S的生成,加速熟料烧成;同时可发生固溶反应,促使熟料矿物发生晶格畸变,向强度较好的晶型转变,提高水化活性。(3) Calcination fluxing components: The introduction of alkali metals, transition metals and other components further enhances the synergy of multi-elements and lowers the minimum eutectic temperature of the system, so that the liquid phase can be generated at a lower reaction temperature and the liquid phase appears in advance , helps to increase the amount of liquid phase, cause uneven local electricity prices, change the properties of the liquid phase, reduce the viscosity of the liquid phase, promote the generation of C3S, and accelerate the firing of clinker; at the same time, solid solution reaction can occur, prompting the crystallization of clinker minerals. Lattice distortion, transformation to a crystal form with better strength, and improved hydration activity.
(4)辅助促分解组分:部分组分可与生料反应,在表面生成新相,新相在加热过程中可发生热解,释放出热量,使得局部温度升高,有利于碳酸盐的的分解。或与生料反应,改变生料结构状态,在材料表面形成大量缺陷,有助于碳酸盐分解过程中的传质传热,加速碳酸盐分解过程。(4) Auxiliary decomposition-promoting components: Some components can react with raw materials to generate new phases on the surface. The new phases can pyrolyze during the heating process and release heat, causing the local temperature to increase, which is beneficial to carbonate of decomposition. Or it reacts with the raw material, changes the structural state of the raw material, and forms a large number of defects on the surface of the material, which contributes to mass and heat transfer during the carbonate decomposition process and accelerates the carbonate decomposition process.
本发明添加剂掺量为0.06-0.2%,可显著促进生料中碳酸盐的分解,降低碳酸盐的分解温度,促进水泥熟料的烧成,改善水泥熟料质量,节约熟料生产煤耗,具有广阔的经济效益和社会效益。The additive dosage of the present invention is 0.06-0.2%, which can significantly promote the decomposition of carbonates in raw materials, reduce the decomposition temperature of carbonates, promote the burning of cement clinker, improve the quality of cement clinker, and save coal consumption in clinker production. , has broad economic and social benefits.
具体实施方式Detailed ways
下面通过对实施例的描述,对本发明的具体实施方式作进一步详细的说明,以帮助本领域的技术人员对本发明的发明构思、技术方案有更完整、准确和深入的理解。The specific implementation modes of the present invention will be further described in detail through the description of the examples below to help those skilled in the art have a more complete, accurate and in-depth understanding of the inventive concepts and technical solutions of the present invention.
实施例1Example 1
本发明公开了一种粉体生料熔解促进剂的制备方法,包括如下具体步骤:The invention discloses a method for preparing a powdery raw meal melting accelerator, which includes the following specific steps:
(1)取适量电解铝固体废弃物,加入行星磨内,同时向磨内加入0.5%的硬脂酸钠和0.1%的油酸,以300r/min进行粉磨,粉磨时间40min,保证磨后颗粒的结晶度降至最低值,无序程度>40%,结束后,向磨内按化学耦合激发剂/废弃物为2%的比例,加入化学激发剂,化学激发剂为硅酸钠:木质素磺酸钠5:1,随后继续以500r/min粉磨时间60min,即得活化电解铝固体废弃物;(1) Take an appropriate amount of electrolytic aluminum solid waste and add it to the planetary mill. At the same time, add 0.5% sodium stearate and 0.1% oleic acid into the mill and grind at 300r/min. The grinding time is 40min to ensure that the The crystallinity of the final particles drops to the lowest value, and the degree of disorder is >40%. After completion, a chemical activator is added into the mill at a ratio of chemical coupling activator/waste of 2%. The chemical activator is sodium silicate: Sodium lignosulfonate 5:1, and then continue grinding at 500r/min for 60min to obtain activated electrolytic aluminum solid waste;
(2)分别取适量Ce(NO3)3·6H2O和La(NO3)3·6H2O,按3:1的比例溶于去离子水中,配置为0.1mol/L的Ce3+、La3+共存稀土溶液,取适量碳酸铵溶于去离子水,配置0.3mol/L的碳酸铵溶液,在60℃以及搅拌速度400rpm的条件下,向碳酸铵溶液中缓慢地加入共存稀土溶液。待反应完毕后,将溶液在室温静置2h。抽滤清洗后,烘干。将烘干后的材料置于行星式球磨机进行球磨,以500r/min,球磨时间为40min,即得共掺杂纳米稀土组分;(2) Take appropriate amounts of Ce(NO 3 ) 3 ·6H 2 O and La(NO 3 ) 3 ·6H 2 O respectively, dissolve them in deionized water at a ratio of 3:1, and configure it to 0.1mol/L Ce 3+ , La 3+ coexisting rare earth solution, dissolve an appropriate amount of ammonium carbonate in deionized water, prepare a 0.3mol/L ammonium carbonate solution, and slowly add the coexisting rare earth solution to the ammonium carbonate solution at 60°C and a stirring speed of 400rpm. . After the reaction is completed, let the solution stand at room temperature for 2 hours. After suction filtration and cleaning, dry it. Place the dried material into a planetary ball mill for ball milling at 500r/min and a milling time of 40min to obtain co-doped nano-rare earth components;
(3)按比例取步骤(1)制备的活化电解铝固体废弃物和步骤(2)制备的共掺杂纳米稀土组分,加入干粉搅拌机内,搅拌10min,随后向搅拌机内按比例加入质量比为1:1的硫酸锌和磷酸二氢钠,搅拌10min,搅拌结束后继续按比例加入质量比为3:1的氟硅酸钠和柠檬酸钠一起搅拌,搅拌时间30min,即得粉体熔解促进剂。(3) Take the activated electrolytic aluminum solid waste prepared in step (1) and the co-doped nano-rare earth component prepared in step (2) in proportion, add them into a dry powder mixer, stir for 10 minutes, and then add the mass ratio into the mixer in proportion Zinc sulfate and sodium dihydrogen phosphate of 1:1, stir for 10 minutes. After stirring, continue to add sodium fluorosilicate and sodium citrate with a mass ratio of 3:1 in proportion and stir together. The stirring time is 30 minutes, and the powder is melted. accelerator.
其中,活化电解铝固体废弃物50%、共掺杂纳米稀土组分15%、煅烧助熔组分20%、辅助促分解组分15%,添加剂掺量为0.12%。Among them, 50% of activated electrolytic aluminum solid waste, 15% of co-doped nano-rare earth components, 20% of calcined fluxing components, 15% of auxiliary decomposition-promoting components, and the additive content is 0.12%.
实施例2Example 2
本发明公开了一种粉体生料熔解促进剂的制备方法,包括如下具体步骤:The invention discloses a method for preparing a powdery raw meal melting accelerator, which includes the following specific steps:
(1)取适量电解铝固体废弃物,加入行星磨内,先粉磨40min,间歇30min后,粉磨60min,即得电解铝固体废弃物;(1) Take an appropriate amount of electrolytic aluminum solid waste, add it to the planetary mill, grind it for 40 minutes, then grind for 60 minutes after an interval of 30 minutes, to obtain the electrolytic aluminum solid waste;
(2)按3:1的比例适量mamiCe2(CO3)3和La2(CO3)3粉体,置于搅拌机内搅拌混合,得纳米稀土组分;(2) Add an appropriate amount of mamiCe 2 (CO 3 ) 3 and La 2 (CO 3 ) 3 powder in a ratio of 3:1, stir and mix in a mixer to obtain nano-rare earth components;
(3)按比例取步骤(1)制备的活化电解铝固体废弃物和步骤(2)制备的纳米稀土组分,加入干粉搅拌机内,搅拌10min,随后向搅拌机内按比例加入质量比为1:1的硫酸锌和磷酸二氢钠,搅拌10min,搅拌结束后继续按比例加入质量比为3:1的氟硅酸钠和柠檬酸钠一起搅拌,搅拌时间30min,即得粉体熔解促进剂。(3) Take the activated electrolytic aluminum solid waste prepared in step (1) and the nano-rare earth component prepared in step (2) in proportion, add them to a dry powder mixer, stir for 10 minutes, and then add proportionally to the mixer with a mass ratio of 1: 1 zinc sulfate and sodium dihydrogen phosphate, stir for 10 minutes. After the stirring is completed, continue to add sodium fluorosilicate and sodium citrate with a mass ratio of 3:1 and stir together. The stirring time is 30 minutes to obtain a powder melting accelerator.
其中,活化电解铝固体废弃物50%、共掺杂纳米稀土组分15%、煅烧助熔组分20%、辅助促分解组分15%,添加剂掺量为0.12%。Among them, 50% of activated electrolytic aluminum solid waste, 15% of co-doped nano-rare earth components, 20% of calcined fluxing components, 15% of auxiliary decomposition-promoting components, and the additive content is 0.12%.
实施例3Example 3
本发明公开了一种粉体生料熔解促进剂的制备方法,包括如下具体步骤:The invention discloses a method for preparing a powdery raw meal melting accelerator, which includes the following specific steps:
(1)取适量电解铝固体废弃物,加入行星磨内,先粉磨40min,间歇30min后,粉磨60min,即得电解铝固体废弃物;(1) Take an appropriate amount of electrolytic aluminum solid waste, add it to the planetary mill, grind it for 40 minutes, then grind for 60 minutes after an interval of 30 minutes, to obtain the electrolytic aluminum solid waste;
(2)分别取适量Ce(NO3)3·6H2O和La(NO3)3·6H2O,按3:1的比例溶于去离子水中,配置为0.1mol/L的Ce3+、La3+共存稀土溶液,取适量碳酸铵溶于去离子水,配置0.3mol/L的碳酸铵溶液,在60℃以及搅拌速度400rpm的条件下,向碳酸铵溶液中缓慢地加入共存稀土溶液。待反应完毕后,将溶液在室温静置2h。抽滤清洗后,烘干。将烘干后的材料置于行星式球磨机进行球磨,以500r/min,球磨时间为40min,即得共掺杂纳米稀土组分;(2) Take appropriate amounts of Ce(NO 3 ) 3 ·6H 2 O and La(NO 3 ) 3 ·6H 2 O respectively, dissolve them in deionized water at a ratio of 3:1, and configure it to 0.1mol/L Ce 3+ , La 3+ coexisting rare earth solution, dissolve an appropriate amount of ammonium carbonate in deionized water, prepare a 0.3mol/L ammonium carbonate solution, and slowly add the coexisting rare earth solution to the ammonium carbonate solution at 60°C and a stirring speed of 400rpm. . After the reaction is completed, let the solution stand at room temperature for 2 hours. After suction filtration and cleaning, dry it. Place the dried material into a planetary ball mill for ball milling at 500r/min and a milling time of 40min to obtain co-doped nano-rare earth components;
(3)按比例取步骤(1)制备的活化电解铝固体废弃物和步骤(2)制备的共掺杂纳米稀土组分,加入干粉搅拌机内,搅拌10min,随后向搅拌机内按比例加入质量比为1:1的硫酸锌和磷酸二氢钠,搅拌10min,搅拌结束后继续按比例加入质量比为3:1的氟硅酸钠和柠檬酸钠一起搅拌,搅拌时间30min,即得粉体熔解促进剂。(3) Take the activated electrolytic aluminum solid waste prepared in step (1) and the co-doped nano-rare earth component prepared in step (2) in proportion, add them into a dry powder mixer, stir for 10 minutes, and then add the mass ratio into the mixer in proportion Zinc sulfate and sodium dihydrogen phosphate of 1:1, stir for 10 minutes. After stirring, continue to add sodium fluorosilicate and sodium citrate with a mass ratio of 3:1 in proportion and stir together. The stirring time is 30 minutes, and the powder is melted. accelerator.
其中,活化电解铝固体废弃物50%、共掺杂纳米稀土组分15%、煅烧助熔组分20%、辅助促分解组分15%,添加剂掺量为0.12%。Among them, 50% of activated electrolytic aluminum solid waste, 15% of co-doped nano-rare earth components, 20% of calcined fluxing components, 15% of auxiliary decomposition-promoting components, and the additive content is 0.12%.
实施例4Example 4
本发明公开了一种粉体生料熔解促进剂的制备方法,包括如下具体步骤:The invention discloses a method for preparing a powdery raw meal melting accelerator, which includes the following specific steps:
(1)取适量电解铝固体废弃物,加入行星磨内,同时向磨内加入0.5%的硬脂酸钠和0.1%的油酸,以300r/min进行粉磨,粉磨时间40min,保证磨后颗粒的结晶度降至最低值,无序程度>40%,结束后,向磨内按化学耦合激发剂/废弃物为2%的比例,加入化学激发剂,化学激发剂为硅酸钠:木质素磺酸钠5:1,随后继续以500r/min粉磨时间60min,即得活化电解铝固体废弃物;(1) Take an appropriate amount of electrolytic aluminum solid waste and add it to the planetary mill. At the same time, add 0.5% sodium stearate and 0.1% oleic acid into the mill and grind at 300r/min. The grinding time is 40min to ensure that the The crystallinity of the final particles drops to the lowest value, and the degree of disorder is >40%. After completion, a chemical activator is added into the mill at a ratio of chemical coupling activator/waste of 2%. The chemical activator is sodium silicate: Sodium lignosulfonate 5:1, and then continue grinding at 500r/min for 60min to obtain activated electrolytic aluminum solid waste;
(2)按3:1的比例适量mamiCe2(CO3)3和La2(CO3)3粉体,置于搅拌机内搅拌混合,得纳米稀土组分;(2) Add an appropriate amount of mamiCe 2 (CO 3 ) 3 and La 2 (CO 3 ) 3 powder in a ratio of 3:1, stir and mix in a mixer to obtain nano-rare earth components;
(3)按比例取步骤(1)制备的活化电解铝固体废弃物和步骤(2)制备的纳米稀土组分,加入干粉搅拌机内,搅拌10min,随后向搅拌机内按比例加入质量比为1:1的硫酸锌和磷酸二氢钠,搅拌10min,搅拌结束后继续按比例加入质量比为3:1的氟硅酸钠和柠檬酸钠一起搅拌,搅拌时间30min,即得粉体熔解促进剂。(3) Take the activated electrolytic aluminum solid waste prepared in step (1) and the nano-rare earth component prepared in step (2) in proportion, add them to a dry powder mixer, stir for 10 minutes, and then add proportionally to the mixer with a mass ratio of 1: 1 zinc sulfate and sodium dihydrogen phosphate, stir for 10 minutes. After the stirring is completed, continue to add sodium fluorosilicate and sodium citrate with a mass ratio of 3:1 and stir together. The stirring time is 30 minutes to obtain a powder melting accelerator.
其中,活化电解铝固体废弃物50%、共掺杂纳米稀土组分15%、煅烧助熔组分20%、辅助促分解组分15%,添加剂掺量为0.12%。Among them, 50% of activated electrolytic aluminum solid waste, 15% of co-doped nano-rare earth components, 20% of calcined fluxing components, 15% of auxiliary decomposition-promoting components, and the additive content is 0.12%.
实施例5Example 5
其余均与实施例1相同,不同之处在于:辅助促分解组分5%。The rest are the same as Example 1, except that the auxiliary decomposition-promoting component is 5%.
实施例6Example 6
其余均与实施例1相同,不同之处在于:煅烧助熔组分10%。The rest are the same as in Example 1, except that the calcined fluxing component is 10%.
实施例7Example 7
其余均与实施例1相同,不同之处在于:共掺杂纳米稀土组分5%。The rest are the same as in Example 1, except that 5% of nano-rare earth components are co-doped.
实施例8Example 8
其余均与实施例1相同,不同之处在于:活化电解铝固体废弃物60%。The rest are the same as in Example 1, except that 60% of the electrolytic aluminum solid waste is activated.
实施例9Example 9
其余均与实施例1相同,不同之处在于:添加剂掺量为0.06%。The rest are the same as Example 1, except that the additive content is 0.06%.
生料性能测试:取芜湖海螺水泥有限责任公司生料原料作为实验样品,掺入0%、0.06%和0.12%的熔解促进剂,不同之处在于,熔解促进剂制备方法及各组分比例不同,分别如实施例1-8所示,具体测试如下:Raw meal performance test: Take raw meal raw materials from Wuhu Conch Cement Co., Ltd. as experimental samples, and add 0%, 0.06% and 0.12% melting accelerators. The difference is that the preparation method of the melting accelerator and the proportion of each component are different. , as shown in Examples 1-8 respectively. The specific tests are as follows:
取芜湖海螺水泥水泥有限公司入窑生料粉,将水泥生料熔解煅烧促进剂剂按不同掺量与生料粉混合均匀,并在105℃温度下烘干2h;取制备好的混合生料1g,均匀平摊在坩埚内,以两两交叉的摆放方式,在820℃下煅烧30min,测其烧失量,分解率测试结果如表1所示:Take the raw meal powder from Wuhu Conch Cement Co., Ltd. and put it into the kiln, melt the cement raw meal and calcine the accelerator and mix it evenly with the raw meal powder in different amounts, and dry it at 105°C for 2 hours; take the prepared mixed raw meal 1g, spread evenly in the crucible, place them in a crosswise manner, calcine at 820°C for 30 minutes, measure the loss on ignition, and the decomposition rate test results are shown in Table 1:
表1分解率测试结果Table 1 Decomposition rate test results
水泥熟料煅烧性能:取芜湖海螺水泥水泥有限公司入窑生料粉,将水泥生料熔解煅烧促进剂剂按掺量与生料粉混合均匀后依据水泥生料易烧性试验方法制成试体,将试体在105℃烘干3h后,移入950℃煅烧30min,然后快速移入高温炉中在1350/1400℃中煅烧30min,急冷后,研磨成粉料,并在3d内测定其游离氧化钙。f-CaO测试结果如表2所示Calcining performance of cement clinker: Take the raw meal powder from Wuhu Conch Cement Co., Ltd. and melt it into the kiln. The cement raw meal is melted and calcined. The accelerator agent is evenly mixed with the raw meal powder according to the dosage, and the test is made according to the cement raw meal easiness test method. After drying the sample at 105°C for 3 hours, move it to 950°C for calcination for 30 minutes, then quickly move it into a high-temperature furnace and calcine for 30 minutes at 1350/1400°C. After rapid cooling, grind it into powder, and measure its free oxidation within 3 days. calcium. The f-CaO test results are shown in Table 2
表2 1350℃/1400℃f-CaO测试结果Table 2 1350℃/1400℃ f-CaO test results
上述结果表明,熔解促进剂能有效促进生料中碳酸盐的分解,改善水泥生料易烧性。具体表现为:(1)加入熔解促进剂后,水泥生料烧失量和分解率明显提升;(2)加入熔解促进剂后,制备的熟料中游离氧化钙含量明显降低;(3)活化后的熔解促进组分的性能明显优于未活化的熔解促进组分;(4)共掺纳米稀土组分的性能明显优于普通混合稀土组分。The above results show that the melting accelerator can effectively promote the decomposition of carbonates in the raw meal and improve the burnability of the cement raw meal. The specific performance is as follows: (1) After adding the melting accelerator, the loss on ignition and decomposition rate of cement raw materials are significantly increased; (2) After adding the melting accelerator, the free calcium oxide content in the prepared clinker is significantly reduced; (3) Activation The performance of the final melt-promoting component is significantly better than that of the unactivated melt-promoting component; (4) The performance of the co-doped nano-rare earth component is significantly better than that of the ordinary mixed rare earth component.
以上实施例仅为说明本发明的技术思想,不能以此限定本发明的保护范围,凡是按照本发明提出的技术思想,在技术方案基础上所做的任何改动,均落入本发明保护范围之内;本发明未涉及的技术均可通过现有技术加以实现。The above embodiments are only for illustrating the technical ideas of the present invention and cannot limit the protection scope of the present invention. Any changes made based on the technical solutions based on the technical ideas proposed by the present invention will fall within the protection scope of the present invention. Within; technologies not involved in the present invention can be implemented through existing technologies.
Claims (4)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310916629.XA CN116903276A (en) | 2023-07-25 | 2023-07-25 | A powdery raw meal melting accelerator and its preparation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310916629.XA CN116903276A (en) | 2023-07-25 | 2023-07-25 | A powdery raw meal melting accelerator and its preparation method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN116903276A true CN116903276A (en) | 2023-10-20 |
Family
ID=88364506
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202310916629.XA Pending CN116903276A (en) | 2023-07-25 | 2023-07-25 | A powdery raw meal melting accelerator and its preparation method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN116903276A (en) |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1837122A (en) * | 2005-03-25 | 2006-09-27 | 尹小林 | Raw materials combustion adjuvant |
| CN103058644A (en) * | 2012-12-19 | 2013-04-24 | 中国科学院合肥物质科学研究院 | A method for preparing rare earth-doped yttrium aluminum garnet transparent ceramics by synthesizing rare earth-doped Y2O3 nanopowder |
| RU2577871C1 (en) * | 2015-03-30 | 2016-03-20 | Общество с ограниченной ответственностью "Безотходные и малоотходные технологии" (ООО "БМТ") | Method for producing portland cement |
| CN109354425A (en) * | 2018-11-01 | 2019-02-19 | 济南大学 | A composite mineralizer suitable for calcining white sulfoaluminate cement clinker and preparation method thereof |
| CN110106312A (en) * | 2019-03-19 | 2019-08-09 | 新疆中合大正冶金科技有限公司 | A kind of technique using electrolytic aluminium carbon slag production LF slagging agent |
| CN112028509A (en) * | 2020-09-21 | 2020-12-04 | 临沂德艺科技发展有限公司 | Additive for dry-process cement pit clinker production |
| CN112939614A (en) * | 2021-03-24 | 2021-06-11 | 湖南国发控股有限公司 | Electrolytic aluminum overhaul slag synergistic ceramic treatment method |
| CN114524630A (en) * | 2022-01-25 | 2022-05-24 | 长沙紫宸科技开发有限公司 | Method for using aluminium ash as fuel, correcting material and sintering aid for dry cement production |
| CN115557720A (en) * | 2022-10-28 | 2023-01-03 | 安徽海螺制剂工程技术有限公司 | Cement clinker mineralization reinforcing agent |
| CN116119952A (en) * | 2023-01-13 | 2023-05-16 | 安徽海鑫矿化材料科技有限公司 | Composite raw material calcination melting accelerant and preparation method thereof |
| CN116354629A (en) * | 2023-04-21 | 2023-06-30 | 安徽海螺制剂工程技术有限公司 | A kind of composite raw meal melting accelerator and its application |
-
2023
- 2023-07-25 CN CN202310916629.XA patent/CN116903276A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1837122A (en) * | 2005-03-25 | 2006-09-27 | 尹小林 | Raw materials combustion adjuvant |
| CN103058644A (en) * | 2012-12-19 | 2013-04-24 | 中国科学院合肥物质科学研究院 | A method for preparing rare earth-doped yttrium aluminum garnet transparent ceramics by synthesizing rare earth-doped Y2O3 nanopowder |
| RU2577871C1 (en) * | 2015-03-30 | 2016-03-20 | Общество с ограниченной ответственностью "Безотходные и малоотходные технологии" (ООО "БМТ") | Method for producing portland cement |
| CN109354425A (en) * | 2018-11-01 | 2019-02-19 | 济南大学 | A composite mineralizer suitable for calcining white sulfoaluminate cement clinker and preparation method thereof |
| CN110106312A (en) * | 2019-03-19 | 2019-08-09 | 新疆中合大正冶金科技有限公司 | A kind of technique using electrolytic aluminium carbon slag production LF slagging agent |
| CN112028509A (en) * | 2020-09-21 | 2020-12-04 | 临沂德艺科技发展有限公司 | Additive for dry-process cement pit clinker production |
| CN112939614A (en) * | 2021-03-24 | 2021-06-11 | 湖南国发控股有限公司 | Electrolytic aluminum overhaul slag synergistic ceramic treatment method |
| CN114524630A (en) * | 2022-01-25 | 2022-05-24 | 长沙紫宸科技开发有限公司 | Method for using aluminium ash as fuel, correcting material and sintering aid for dry cement production |
| CN115557720A (en) * | 2022-10-28 | 2023-01-03 | 安徽海螺制剂工程技术有限公司 | Cement clinker mineralization reinforcing agent |
| CN116119952A (en) * | 2023-01-13 | 2023-05-16 | 安徽海鑫矿化材料科技有限公司 | Composite raw material calcination melting accelerant and preparation method thereof |
| CN116354629A (en) * | 2023-04-21 | 2023-06-30 | 安徽海螺制剂工程技术有限公司 | A kind of composite raw meal melting accelerator and its application |
Non-Patent Citations (3)
| Title |
|---|
| 和春梅;周惠群;罗玉银;: "稀土尾矿对水泥生料碳酸盐分解的影响", 中国水泥, no. 12, 1 December 2013 (2013-12-01) * |
| 杨立宏;赵涛;程秋林;: "铝工业生态产业链的设计及其利益关系分析", 科学管理研究, no. 02, 20 April 2009 (2009-04-20) * |
| 石志平;姜澜;杨洪亮;张靖宙;付高峰;: "铝灰的回收处理及资源化利用研究现状", 无机盐工业, no. 09, 10 September 2020 (2020-09-10) * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105541143B (en) | A method of utilizing dry-process rotory kiln system production high strength low-carbon clinker | |
| CN107879366B (en) | Activation method for extracting aluminum oxide from fly ash | |
| CN108821621B (en) | Light high-strength ceramsite and preparation method thereof | |
| CN101041449A (en) | Method for extracting aluminium oxide from coal ash and producing cement by using waste slag | |
| CN113185154B (en) | Method for preparing cement clinker by using rare earth tailings | |
| CN103601379B (en) | A kind of outer high calcium slag sand of throwing calcines phase-splitting grog technique | |
| CN111268929A (en) | Green environment-friendly cement and preparation method thereof | |
| CN114890702A (en) | Method for preparing high-strength ceramsite by self-sintering coal gasification fine slag | |
| CN117401916B (en) | Carbonizable low-carbon cement clinker, preparation method and application thereof | |
| CN106938895A (en) | A kind of method that lateritic nickel ore acid-soaked waste residue produces building porcelain granule | |
| CN105601134A (en) | Method for full use of coal gangue for preparing cement | |
| CN111606692A (en) | A kind of ceramsite proppant prepared from industrial waste gasification slag and preparation process | |
| CN111233353A (en) | Method for producing general cement clinker by using iron oxide slag to partially replace iron correction raw material | |
| CN119409436B (en) | A belite-aluminate mineral additive and its preparation method and application | |
| CN116903276A (en) | A powdery raw meal melting accelerator and its preparation method | |
| CN111057810B (en) | A kind of removal method of impurity iron in gasification slag | |
| CN113979775A (en) | Method for preparing ceramsite proppant by using secondary aluminum ash | |
| CN115838261B (en) | Method for preparing grouting material by using coal gangue and alkaline slag after activating carbon fixation by using flue gas | |
| CN107619952B (en) | A method for leaching lithium from fly ash | |
| CN104944814A (en) | Low-temperature calcining technology for cement clinker | |
| CN112126778A (en) | Iron ore direct reduction metallurgy method based on 3D printing | |
| CN115594518B (en) | A material processing method of high-iron red mud functional ceramsite and microwave-absorbing functional ceramsite | |
| CN110143770B (en) | A kind of preparation method of ternary composite inorganic cementitious material of existing slag slag | |
| CN116375367A (en) | Low-chlorine high-aluminum correction material based on secondary aluminum ash of secondary aluminum, production and application | |
| CN115626785B (en) | A method for fixing heavy metal zinc |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |