WO2018233686A1 - Method for preparing metallurgical-level aluminum oxide by treating medium- and low-grade bauxite by using one-step alkali heat process of andradite - Google Patents

Method for preparing metallurgical-level aluminum oxide by treating medium- and low-grade bauxite by using one-step alkali heat process of andradite Download PDF

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WO2018233686A1
WO2018233686A1 PCT/CN2018/092422 CN2018092422W WO2018233686A1 WO 2018233686 A1 WO2018233686 A1 WO 2018233686A1 CN 2018092422 W CN2018092422 W CN 2018092422W WO 2018233686 A1 WO2018233686 A1 WO 2018233686A1
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calcium
medium
carbon
liquid
alumina
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PCT/CN2018/092422
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于海燕
潘晓林
吴艳
毕诗文
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东北大学
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F7/00Compounds of aluminium
    • C01F7/02Aluminium oxide; Aluminium hydroxide; Aluminates
    • C01F7/20Preparation of aluminium oxide or hydroxide from aluminous ores using acids or salts

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  • the invention belongs to the technical field of alumina production, and particularly relates to a method for producing metallurgical grade alumina in a medium-low grade bauxite by a one-step alkali heat treatment of calcium iron garnet.
  • the treatment methods of low-grade bauxite mainly include Bayer method, sintering method and Bayer-sintering method.
  • the enhanced Bayer method is a method based on the Bayer method to adapt to the treatment of low-grade bauxite, mainly including the beneficiation Bayer method and the lime Bayer method.
  • the beneficiation Bayer method uses the combination of smelting and smelting to treat medium and low grade bauxite.
  • the process is relatively simple, but there are problems such as difficulty in physical beneficiation, large consumption of raw ore, low recovery rate of alumina, and influence of Bayer process by flotation reagents.
  • the ore dressing process produces a large amount of aluminum and silicon tailings that are less than 2, which can not be used, resulting in great waste of resources.
  • the lime Bayer method is based on the Bayer method to increase the alkali consumption by adding excess lime, but the amount of lime added is large. The dissolution rate of alumina is greatly reduced, the red mud discharge is increased, and the red mud sedimentation load is increased.
  • the sintering method mainly includes the soda lime sintering method and the lime sintering method, but the high energy consumption and high production cost are the main shortcomings of the development.
  • the soda lime sintering method belongs to wet compounding and wet sintering.
  • Bayer-sintering combined method includes series method, parallel method and hybrid method, which can deal with medium and low grade bauxite, but it has complicated problems and high energy consumption. It has been basically replaced by Bayer method.
  • Other processes such as acid method and acid-base combination method mainly stay in the laboratory research stage, and there are many problems such as poor quality of alumina products and serious corrosion of equipment.
  • an object of the present invention is to provide a method for producing a metallurgical grade alumina in a medium-grade low-grade bauxite by a one-step alkali thermal treatment of calcium iron garnet, and adding sodium ferrite during high-temperature dissolution ( The method of calcium ferrite) and active lime, aluminum enters the solution in the form of sodium aluminate during high temperature dissolution, and the silicon remains in the dissolution slag in the form of calcium iron garnet.
  • the method of the invention can greatly improve the dissolution rate of the metallurgical grade alumina, and at the same time, the dissolution slag contains almost no alkali, and has the characteristics of short process and high efficiency, and the material realizes zero discharge in the whole process.
  • the main technical solutions adopted by the present invention include:
  • a method for producing metallurgical grade alumina of medium and low grade bauxite by one-step alkali heat treatment of calcium iron garnet comprising the following steps,
  • step S7 The carbon mother liquor obtained in step S5 is causticized with calcium oxide to obtain a caustic slurry, and the caustic slurry is subjected to liquid-solid separation to obtain a polymer ratio sodium aluminate solution and calcium carbonate, and the ratio of the polymer is The sodium aluminate solution is prepared as the circulating mother liquor in step S2.
  • the medium-low grade bauxite has a silicon to aluminum ratio of 2-6.
  • the total amount of iron, aluminum, calcium and silicon present in each form is determined by the oxide, and the formulation is as follows:
  • the mass ratio of the total amount of iron oxide to the total amount of alumina is 0.2 to 0.6:1;
  • the molar ratio of the total amount of calcium oxide to the total amount of iron oxide is from 3 to 6:1.
  • the liquid-solid ratio of the raw material slurry is 2 to 5:1.
  • the concentration of caustic in the circulating mother liquor in step S2 is 150 to 250 g/L, and the molecular ratio is 5 to 25.
  • the temperature of the dissolution reaction in the step S3 is 150 to 250 ° C, and the reaction time is 0.5 to 2 h.
  • step S5 carbon dioxide gas is introduced into the sodium aluminate obtained after elution and seed crystals are added to carry out carbon fractionation to obtain a slurry of crude aluminum hydroxide, followed by liquid-solid separation to obtain a carbon mother liquor and crude aluminum hydroxide.
  • step S5 the carbon content temperature is 60 to 90 ° C, the carbon end point is a decomposition rate of 90% or more, and the seed crystal addition coefficient is 0 to 1.0.
  • the method further includes:
  • Step S8 washing the eluted slag in step S4 and solid-liquid separation to obtain calcium garnet type slag and washing liquid;
  • Step S9 The washing liquid is used to dilute the dissolved slurry in step S4.
  • the method further comprises the step S10: calcining and decomposing the calcium carbonate obtained in the step S7 to obtain carbon dioxide gas and calcium oxide, and the obtained carbon dioxide gas is used for carbon separation in the step S5, and the obtained calcium oxide is used in the step.
  • Caustic treatment in S7 is used in the step S10.
  • the sodium ferrite in the step S1 is formed by sintering an iron-containing raw material and an industrial carbon base; the calcium ferrite is obtained by sintering the iron-containing raw material and the lime.
  • the method of the present invention produces a dissolution slag base content of 0.5% or less, and the slag contains almost no alkali;
  • the method of the invention has the characteristics of short process and high efficiency, and the material realizes zero discharge in the whole process.
  • FIG. 1 is a process flow diagram of a method for producing a metallurgical grade alumina in a low-grade bauxite by a one-step alkali thermal treatment of calcium iron garnet according to the present invention.
  • the ratio of silicon to aluminum (hereinafter referred to as A/S) is 2-6.
  • A/S the ratio of silicon to aluminum
  • F/A the mass ratio of the total amount of iron oxide to the total amount of alumina
  • C/F the total amount of calcium oxide
  • L/S The raw material slurry solid mass ratio
  • Calcium iron garnet one-step alkali heat treatment of medium-low grade bauxite to produce metallurgical grade alumina means that the dissolved slag is calcium iron garnet type slag, and the one-step alkali heat method refers to the oxidation of lye (circulating mother liquor)
  • the aluminum is subjected to a one-step hydrothermal dissolution treatment, and the produced product is metallurgical grade alumina.
  • a medium-low grade bauxite is used, and the main chemical components (mass percentage, wt%) are: alumina (Al 2 O 3 ) 60.60%, silica (SiO 2 ) 17.5%, others are impurities, and aluminum thereof
  • the silicon ratio is 3.5;
  • Calcium ferrite is sintered from iron-containing raw materials and lime
  • the concentration of caustic in the circulating mother liquor is 200 g / L, the molecular ratio is 25;
  • the extraction rate of alumina can reach 83%
  • step S7 The carbon mother liquor obtained in step S5 is causticized with lime milk to obtain a caustic slurry, and the caustic slurry is subjected to liquid-solid separation to obtain a polymer ratio sodium aluminate solution and calcium carbonate.
  • the sodium aluminate solution is prepared as the circulating mother liquor in step S2;
  • the carbon mother liquor is treated, and the obtained polymer can be used as a circulating mother liquor to participate in other process processes after adjusting the sodium aluminate solution, so that the process has no efflux and no pollution;
  • step S8 washing the eluted slag in step S4 and solid-liquid separation to obtain calcium garnet type slag and washing liquid;
  • the alkali-free calcium iron garnet type slag is obtained after treatment, so that the silicon and the added iron and calcium remain in the dissolution slag in the form of calcium iron garnet, thereby reducing the alkali content in the slag;
  • step S9 using the washing liquid for diluting the dissolved pulp in step S4;
  • the generated washing liquid is waste liquid, but the washing liquid is returned to the step S4 for diluting the dissolved pulp, which not only reduces the treatment and discharge of the waste liquid, but also achieves the effect of recycling, and achieves the recovery of the material. Reuse;
  • the decomposition and reuse of calcium carbonate realizes the recycling of resources, avoids waste of resources, and saves costs.
  • the resulting metallurgical grade alumina is the product.
  • a medium-low grade bauxite is used, and the main chemical components (mass percentage, wt%) are: alumina (Al 2 O 3 ) 65.22%, silica (SiO 2 ) 12.66%, others are impurities, and aluminum thereof
  • the silicon ratio is 5.15;
  • Sodium ferrite is sintered from iron-containing raw materials and industrial carbon base
  • the concentration of caustic in the circulating mother liquor was 230 g/L and the molecular ratio was 20.
  • the extraction rate of alumina can reach 83.7%
  • step S7 The carbon mother liquor obtained in step S5 is causticized with calcium oxide to obtain a caustic slurry, and the caustic slurry is subjected to liquid-solid separation to obtain a polymer ratio sodium aluminate solution and calcium carbonate, and the ratio of the polymer is The sodium aluminate solution is prepared as the circulating mother liquor in step S2;
  • the carbon mother liquor is treated, and the obtained polymer can be used as a circulating mother liquor to participate in other process processes after adjusting the sodium aluminate solution, so that the process has no efflux and no pollution;
  • step S8 washing the eluted slag in step S4 and solid-liquid separation to obtain calcium garnet type slag and washing liquid;
  • the alkali-free calcium iron garnet type slag is obtained after treatment, so that the silicon and the added iron and calcium remain in the dissolution slag in the form of calcium iron garnet, thereby reducing the alkali content in the slag;
  • step S9 using the washing liquid for diluting the dissolved pulp in step S4;
  • the generated washing liquid is waste liquid, but the washing liquid is returned to the step S4 for diluting the dissolved pulp, which not only reduces the treatment and discharge of the waste liquid, but also achieves the effect of recycling, and achieves the recovery of the material. Reuse;
  • the decomposition and reuse of calcium carbonate realizes the recycling of resources, avoids waste of resources, and saves costs.
  • the resulting metallurgical grade alumina is the product.
  • the method of the invention has the characteristics of short process and high efficiency, and the final products of the whole process are metallurgical grade alumina and alkali-free calcium iron garnet type slag, and the rest of the materials are recycled, and the materials in the whole process realize zero discharge.
  • This alkali-free calcium iron garnet type slag has been effectively utilized due to the reduction of alkali content, such as calcium ferrite additive used in steelmaking process, self-stressing, high strength, quick-setting Portland cement and highways, airports. Ideal aggregate for high-strength concrete such as runways, and as a potential raw material for higher value-added products such as glass-ceramics and silicon fertilizers.

Abstract

Provided is a method for preparing metallurgical-level aluminum oxide by treating medium- and low-grade bauxite by using a one-step alkali heat process of andradite. The method comprises the following steps: S1, crushing and finely grinding medium- and low-grade bauxite into mineral powder; S2, mixing the mineral powder, sodium ferrite or calcium ferrite, activated lime and circulating mother liquid to prepare raw-material mineral pulp; S3, allowing the raw-material mineral pulp to have an alkali heat dissolving-out reaction; S4, diluting dissolved-out mineral pulp, and allowing the diluted liquid to experience liquid-solid separation; S5, introducing a carbon dioxide gas into a sodium aluminate solution to carry out carbonation decomposition, so as to obtain crude aluminum hydroxide and carbonation-decomposed mother liquid; and S6, allowing the crude aluminum hydroxide to experience bayer-process treatment, so as to obtain the metallurgical-level aluminum oxide; and S7, causticizing the carbonation-decomposed mother liquid by using lime milk, and carrying out liquid-solid separation to obtain a sodium hydroxide solution, and using the blended sodium hydroxide solution as a circulating mother liquid in step 2. In the method, by adding the lime and the sodium ferrite or the calcium ferrite in a dissolving-out procedure, andradite-type slag instead of conventional dissolved-out slag is generated in the dissolving-out procedure; the dissolving-out rate of the aluminum oxide can be greatly improved; in addition, the metallurgical-level aluminum oxide is prepared; the method has the characteristics of a short procedure and a high efficiency, and the zero release of a material is achieved.

Description

钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法Method for producing metallurgical grade alumina by low-grade bauxite by calcium-iron garnet one-step alkali heat treatment 技术领域Technical field
本发明属于氧化铝生产的技术领域,具体涉及一种钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法。The invention belongs to the technical field of alumina production, and particularly relates to a method for producing metallurgical grade alumina in a medium-low grade bauxite by a one-step alkali heat treatment of calcium iron garnet.
背景技术Background technique
现有铝土矿资源中绝大多数为中低品位铝土矿,具有高铝,高硅,低铝硅比(A/S)等特点。随着矿石品位的降低,各氧化铝生产工艺成本均在逐渐增加,其中拜耳法工艺增幅最大。根据拜耳法的基本工艺和原理,当铝土矿A/S下降到5以下时,将很难再用拜耳法处理。针对于低品位铝土矿,近年来氧化铝工业界主要采用如下几种方法。Most of the existing bauxite resources are medium and low grade bauxite with high aluminum, high silicon and low aluminum to silicon ratio (A/S). With the reduction of ore grade, the cost of each alumina production process is gradually increasing, and the Bayer process has the largest increase. According to the basic process and principle of the Bayer process, when the bauxite A/S drops below 5, it will be difficult to use the Bayer process. In view of low-grade bauxite ore, in recent years, the alumina industry has mainly adopted the following methods.
中低品位铝土矿处理方法主要有强化拜耳法、烧结法、拜耳-烧结联合法等。强化拜耳法是在拜耳法基础上进行改进以适应处理中低品位铝土矿的方法,主要包括选矿拜耳法和石灰拜耳法。其中,选矿拜耳法采用选冶联合处理中低品位铝土矿,流程相对简单,但存在物理选矿难度大、原矿消耗量大、氧化铝回收率低、浮选药剂影响拜耳法流程等问题,同时选矿过程产生大量铝硅比低于2的尾矿无法利用,造成资源的极大浪费;石灰拜耳法是在拜耳法基础上通过添加过量石灰以达到降低碱耗等作用,但石灰添加量大导致氧化铝溶出率大幅降低、赤泥排出量增加、赤泥沉降负荷增大等问题。烧结法主要包括碱石灰烧结法和石灰烧结法,但能耗高、生产成本高是其发展的主要短板。碱石灰烧结法属于湿法配料、湿法烧结,在烧结过程生料浆中40%左右的水分蒸发极大增加了生产总能耗,且烧结熟料中2CaO·SiO 2稳定性较低,二次反应严重;石灰烧结法存在石灰配比高、弃渣量大、熟料氧化铝浸出率低等问题。拜耳-烧结联合法包括串联法、并联法和混联法,能够处理中低品位铝土矿, 但存在流程复杂、能耗高等问题,目前已基本被拜耳法所取代。其它如酸法和酸碱联合法等工艺目前主要停留在实验室研究阶段,存在氧化铝产品质量差、设备腐蚀严重等诸多问题。 The treatment methods of low-grade bauxite mainly include Bayer method, sintering method and Bayer-sintering method. The enhanced Bayer method is a method based on the Bayer method to adapt to the treatment of low-grade bauxite, mainly including the beneficiation Bayer method and the lime Bayer method. Among them, the beneficiation Bayer method uses the combination of smelting and smelting to treat medium and low grade bauxite. The process is relatively simple, but there are problems such as difficulty in physical beneficiation, large consumption of raw ore, low recovery rate of alumina, and influence of Bayer process by flotation reagents. The ore dressing process produces a large amount of aluminum and silicon tailings that are less than 2, which can not be used, resulting in great waste of resources. The lime Bayer method is based on the Bayer method to increase the alkali consumption by adding excess lime, but the amount of lime added is large. The dissolution rate of alumina is greatly reduced, the red mud discharge is increased, and the red mud sedimentation load is increased. The sintering method mainly includes the soda lime sintering method and the lime sintering method, but the high energy consumption and high production cost are the main shortcomings of the development. The soda lime sintering method belongs to wet compounding and wet sintering. The evaporation of about 40% of the water in the raw slurry of the sintering process greatly increases the total energy consumption, and the stability of 2CaO·SiO 2 in the sintered clinker is low. The secondary reaction is serious; the lime sintering method has problems such as high lime ratio, large amount of waste slag, and low leaching rate of clinker alumina. Bayer-sintering combined method includes series method, parallel method and hybrid method, which can deal with medium and low grade bauxite, but it has complicated problems and high energy consumption. It has been basically replaced by Bayer method. Other processes such as acid method and acid-base combination method mainly stay in the laboratory research stage, and there are many problems such as poor quality of alumina products and serious corrosion of equipment.
纵观以上处理中低品位铝土矿的方法,烧结法和拜耳-烧结联合法由于其能耗和成本问题已基本被弃用,石灰拜耳法是特定历史时期为解决碱耗问题而研发的,目前只有选矿拜耳法在个别企业应用。然而,经过近些年的工业实践,选矿拜耳法日益暴露出的问题已经严重阻碍了生产过程的正常运行,成为其继续推广发展的瓶颈。Throughout the above methods of treating low-grade bauxite, the sintering method and Bayer-sintering method have been basically abandoned due to their energy consumption and cost. The lime Bayer method was developed in response to the problem of alkali consumption in a specific historical period. At present, only the mineral processing Bayer method is applied in individual enterprises. However, after industrial practice in recent years, the problems exposed by the mineral processing Bayer method have seriously hindered the normal operation of the production process and become a bottleneck for its continued promotion and development.
发明内容Summary of the invention
(一)要解决的技术问题(1) Technical problems to be solved
为了解决现有技术的上述问题,本发明的目的在于提供一种钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,在高温溶出过程中添加铁酸钠(铁酸钙)及活性石灰的方法,高温溶出过程中铝以铝酸钠形式进入溶液,而硅以钙铁榴石的形式留在溶出渣中。本发明的方法能够大幅度提高冶金级氧化铝的溶出率,同时使溶出渣中几乎不含碱,具有流程短效率高的特点,整个流程中物料实现了零排放。In order to solve the above problems of the prior art, an object of the present invention is to provide a method for producing a metallurgical grade alumina in a medium-grade low-grade bauxite by a one-step alkali thermal treatment of calcium iron garnet, and adding sodium ferrite during high-temperature dissolution ( The method of calcium ferrite) and active lime, aluminum enters the solution in the form of sodium aluminate during high temperature dissolution, and the silicon remains in the dissolution slag in the form of calcium iron garnet. The method of the invention can greatly improve the dissolution rate of the metallurgical grade alumina, and at the same time, the dissolution slag contains almost no alkali, and has the characteristics of short process and high efficiency, and the material realizes zero discharge in the whole process.
(二)技术方案(2) Technical plan
为了达到上述目的,本发明采用的主要技术方案包括:In order to achieve the above object, the main technical solutions adopted by the present invention include:
一种钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,包括下述步骤,A method for producing metallurgical grade alumina of medium and low grade bauxite by one-step alkali heat treatment of calcium iron garnet, comprising the following steps,
S1:将中低品位铝土矿破碎磨细成矿粉;S1: crushing and grinding fine ore powder of medium and low grade bauxite;
S2:将矿粉、铁酸钠或铁酸钙、活性石灰及循环母液混合制备成原料矿浆;S2: mixing mineral powder, sodium ferrite or calcium ferrite, active lime and circulating mother liquor into raw material pulp;
S3:将原料矿浆进行碱热溶出反应,反应结束后得到溶出矿浆;S3: performing alkali thermal elution reaction on the raw material slurry, and obtaining a dissolved pulp after the reaction is completed;
S4:将溶出矿浆进行稀释得到稀释液,将稀释液进行液固分离,得到溶出渣和溶出液,其中溶出液为铝酸钠溶液;S4: diluting the eluted slurry to obtain a diluent, and performing liquid-solid separation on the diluted solution to obtain a dissolution slag and an eluate, wherein the eluate is a sodium aluminate solution;
S5:向所述铝酸钠溶液中通入二氧化碳气体进行碳分,得到粗氢氧 化铝和碳分母液;S5: introducing carbon dioxide gas into the sodium aluminate solution to carry out carbon to obtain crude aluminum hydroxide and carbon mother liquor;
S6:将所述粗氢氧化铝进行拜耳法处理,得到冶金级氧化铝;S6: subjecting the crude aluminum hydroxide to a Bayer process to obtain a metallurgical grade alumina;
S7:将步骤S5中得到的碳分母液采用氧化钙进行苛化,得到苛化料浆,将苛化料浆进行液固分离,得到高分子比铝酸钠溶液和碳酸钙,将高分子比铝酸钠溶液进行调制,作为步骤S2中的循环母液。S7: The carbon mother liquor obtained in step S5 is causticized with calcium oxide to obtain a caustic slurry, and the caustic slurry is subjected to liquid-solid separation to obtain a polymer ratio sodium aluminate solution and calcium carbonate, and the ratio of the polymer is The sodium aluminate solution is prepared as the circulating mother liquor in step S2.
优选地,所述中低品位铝土矿的硅铝比为2~6。Preferably, the medium-low grade bauxite has a silicon to aluminum ratio of 2-6.
优选地,在铝土矿、铁酸钠或铁酸钙、活性石灰组成的原料矿浆中,各形态存在的铁、铝、钙、硅总量分别以氧化物计,配料配方如下::Preferably, in the raw material slurry composed of bauxite, sodium ferrite or calcium ferrite, or active lime, the total amount of iron, aluminum, calcium and silicon present in each form is determined by the oxide, and the formulation is as follows:
氧化铁的总量与氧化铝的总量的质量比为0.2~0.6∶1;The mass ratio of the total amount of iron oxide to the total amount of alumina is 0.2 to 0.6:1;
氧化钙的总量与氧化铁的总量的摩尔比为3~6∶1。The molar ratio of the total amount of calcium oxide to the total amount of iron oxide is from 3 to 6:1.
优选地,步骤S1中,原料矿浆的液固比为2~5∶1。Preferably, in step S1, the liquid-solid ratio of the raw material slurry is 2 to 5:1.
优选地,步骤S2中循环母液中的苛碱浓度为150~250g/L,分子比为5~25。Preferably, the concentration of caustic in the circulating mother liquor in step S2 is 150 to 250 g/L, and the molecular ratio is 5 to 25.
优选地,步骤S3中溶出反应的温度为150~250℃,反应时间为0.5~2h。Preferably, the temperature of the dissolution reaction in the step S3 is 150 to 250 ° C, and the reaction time is 0.5 to 2 h.
优选地,步骤S5中,向溶出后得到的铝酸钠内通入二氧化碳气体并加入晶种进行碳分,得到粗氢氧化铝料浆后进行液固分离,得到碳分母液和粗氢氧化铝,Preferably, in step S5, carbon dioxide gas is introduced into the sodium aluminate obtained after elution and seed crystals are added to carry out carbon fractionation to obtain a slurry of crude aluminum hydroxide, followed by liquid-solid separation to obtain a carbon mother liquor and crude aluminum hydroxide. ,
步骤S5中碳分温度为60~90℃,碳分终点为分解率在90%以上,晶种添加系数为0~1.0。In step S5, the carbon content temperature is 60 to 90 ° C, the carbon end point is a decomposition rate of 90% or more, and the seed crystal addition coefficient is 0 to 1.0.
优选地,所述方法还包括:Preferably, the method further includes:
步骤S8:将步骤S4中的溶出渣进行洗涤并固液分离,得到钙铁榴石型渣和洗涤液;Step S8: washing the eluted slag in step S4 and solid-liquid separation to obtain calcium garnet type slag and washing liquid;
步骤S9:将所述洗涤液用于步骤S4中稀释所述溶出矿浆。Step S9: The washing liquid is used to dilute the dissolved slurry in step S4.
优选地,所述方法还包括步骤S10:将步骤S7中得到的碳酸钙进行煅烧分解,得到二氧化碳气体和氧化钙,得到的二氧化碳气体用于步骤S5中碳分处理,得到的氧化钙用于步骤S7中苛化处理。Preferably, the method further comprises the step S10: calcining and decomposing the calcium carbonate obtained in the step S7 to obtain carbon dioxide gas and calcium oxide, and the obtained carbon dioxide gas is used for carbon separation in the step S5, and the obtained calcium oxide is used in the step. Caustic treatment in S7.
优选地,步骤S1中的铁酸钠是含铁原料与工业碳碱烧结而成;铁酸钙是含铁原料与石灰烧结而成。Preferably, the sodium ferrite in the step S1 is formed by sintering an iron-containing raw material and an industrial carbon base; the calcium ferrite is obtained by sintering the iron-containing raw material and the lime.
(三)有益效果(3) Beneficial effects
本发明的有益效果是:The beneficial effects of the invention are:
(1)与常规拜耳法相比,本发明的方法产生的冶金级氧化铝实际溶出率提高了15%以上,大幅度地提高了氧化铝的溶出率;(1) Compared with the conventional Bayer process, the actual dissolution rate of the metallurgical grade alumina produced by the method of the invention is increased by more than 15%, and the dissolution rate of the alumina is greatly improved;
(2)与常规拜耳法相比,本发明的方法产生的溶出渣碱含量在0.5%以下,渣中几乎不含碱;(2) Compared with the conventional Bayer process, the method of the present invention produces a dissolution slag base content of 0.5% or less, and the slag contains almost no alkali;
(3)本发明的方法具有流程短效率高的特点,整个流程中物料实现了零排放。(3) The method of the invention has the characteristics of short process and high efficiency, and the material realizes zero discharge in the whole process.
附图说明DRAWINGS
图1为本发明钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法的工艺流程图。1 is a process flow diagram of a method for producing a metallurgical grade alumina in a low-grade bauxite by a one-step alkali thermal treatment of calcium iron garnet according to the present invention.
具体实施方式Detailed ways
下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明,而不用于限制本发明的范围。The invention is further illustrated below in conjunction with specific embodiments. It is to be understood that the examples are only illustrative of the invention and are not intended to limit the scope of the invention.
本发明实施例中的中低品位铝土矿,硅铝比(以下简称A/S)为2~6。在铝土矿、铁酸钠(或铁酸钙)、活性石灰组成的原料矿中,氧化铁的总量与氧化铝的总量的质量比以下简写为F/A;氧化钙的总量与氧化铁的总量的摩尔比为简写为C/F。原料矿浆液固质量比以下简写为L/S。In the low-grade bauxite in the embodiment of the present invention, the ratio of silicon to aluminum (hereinafter referred to as A/S) is 2-6. In the raw material ore consisting of bauxite, sodium ferrite (or calcium ferrite) and activated lime, the mass ratio of the total amount of iron oxide to the total amount of alumina is abbreviated as F/A; the total amount of calcium oxide The molar ratio of the total amount of iron oxide is abbreviated as C/F. The raw material slurry solid mass ratio is abbreviated as L/S.
钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,是指溶出渣为钙铁榴石型渣,一步碱热法是指利用碱液(循环母液)对氧化铝进行一步水热溶出处理的方法,生产的产品为冶金级氧化铝。Calcium iron garnet one-step alkali heat treatment of medium-low grade bauxite to produce metallurgical grade alumina means that the dissolved slag is calcium iron garnet type slag, and the one-step alkali heat method refers to the oxidation of lye (circulating mother liquor) The aluminum is subjected to a one-step hydrothermal dissolution treatment, and the produced product is metallurgical grade alumina.
实施例1Example 1
本实施例采用中低品位铝土矿,主要化学成分(质量百分比,wt%)为:氧化铝(Al 2O 3)  60.60%,二氧化硅(SiO 2)  17.5%,其它为杂 质,其铝硅比为3.5; In this embodiment, a medium-low grade bauxite is used, and the main chemical components (mass percentage, wt%) are: alumina (Al 2 O 3 ) 60.60%, silica (SiO 2 ) 17.5%, others are impurities, and aluminum thereof The silicon ratio is 3.5;
铁酸钙为含铁原料与石灰烧结而成;Calcium ferrite is sintered from iron-containing raw materials and lime;
循环母液中的苛碱浓度为200g/L,分子比为25;The concentration of caustic in the circulating mother liquor is 200 g / L, the molecular ratio is 25;
F/A=0.5∶1;F/A = 0.5:1;
C/F=4.5∶1。C/F = 4.5:1.
按照本图1所示的本发明钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法:A method for producing metallurgical grade alumina by treating a medium-low grade bauxite according to the one-step alkali heat treatment of the calcium iron garnet of the present invention shown in FIG. 1 :
S1:将中低品位铝土矿破碎磨细成矿粉;S1: crushing and grinding fine ore powder of medium and low grade bauxite;
S2:将矿粉、铁酸钙、活性石灰混合后,按照L/S=4∶1的比例与循环母液混合制备成原料矿浆;S2: mixing the mineral powder, calcium ferrite, and active lime, and mixing with the circulating mother liquor according to the ratio of L/S=4:1 to prepare a raw material slurry;
S3:将原料矿浆进行碱热溶出反应,溶出反应温度为250℃,溶出反应时间为2h,反应结束后得到溶出矿浆;S3: the raw material slurry is subjected to alkali thermal elution reaction, the dissolution reaction temperature is 250 ° C, the dissolution reaction time is 2 h, and the dissolution slurry is obtained after the reaction is completed;
经过本步骤的溶出反应处理,氧化铝的提取率能够达到83%;After the dissolution reaction treatment of this step, the extraction rate of alumina can reach 83%;
S4:将溶出矿浆进行稀释得到稀释液,将稀释液进行液固分离,得到溶出渣和溶出液,其中:溶出液为铝酸钠溶液;S4: diluting the eluted slurry to obtain a diluent, and performing liquid-solid separation on the diluted solution to obtain a dissolution slag and an eluate, wherein: the eluate is a sodium aluminate solution;
S5:将铝酸钠在80℃、晶种添加系数为0.8的条件下,通二氧化碳并加入晶种进行碳分(碳酸化分解)至分解率达到95%,得到粗氢氧化铝料浆,并进行液固分离,得到碳分母液和粗氢氧化铝;S5: sodium aluminate at 80 ° C, seed crystal addition coefficient of 0.8, carbon dioxide and seed crystals for carbon (carbonation decomposition) to a decomposition rate of 95%, to obtain a crude aluminum hydroxide slurry, and Performing liquid-solid separation to obtain a carbon mother liquor and crude aluminum hydroxide;
S6:将步骤S5中得到的粗氢氧化铝进行拜耳法处理,得到冶金级氧化铝;S6: subjecting the crude aluminum hydroxide obtained in the step S5 to a Bayer process to obtain a metallurgical grade alumina;
S7:将步骤S5中得到的碳分母液采用石灰乳进行苛化,得到苛化料浆,将苛化料浆进行液固分离,得到高分子比铝酸钠溶液和碳酸钙,将高分子比铝酸钠溶液进行调制,作为步骤S2中的循环母液;S7: The carbon mother liquor obtained in step S5 is causticized with lime milk to obtain a caustic slurry, and the caustic slurry is subjected to liquid-solid separation to obtain a polymer ratio sodium aluminate solution and calcium carbonate. The sodium aluminate solution is prepared as the circulating mother liquor in step S2;
本步骤中,将碳分母液进行处理,得到的高分子比铝酸钠溶液调整后能够作为循环母液参与其他工艺流程,使得工艺流程无外排无污染;In this step, the carbon mother liquor is treated, and the obtained polymer can be used as a circulating mother liquor to participate in other process processes after adjusting the sodium aluminate solution, so that the process has no efflux and no pollution;
S8:将步骤S4中的溶出渣进行洗涤并固液分离,得到钙铁榴石型渣和洗涤液;S8: washing the eluted slag in step S4 and solid-liquid separation to obtain calcium garnet type slag and washing liquid;
本步骤中,经过处理得到了无碱钙铁榴石型渣,使硅与加入的铁和钙以钙铁榴石的形式留在溶出渣中,降低了渣中的碱含量;In this step, the alkali-free calcium iron garnet type slag is obtained after treatment, so that the silicon and the added iron and calcium remain in the dissolution slag in the form of calcium iron garnet, thereby reducing the alkali content in the slag;
S9:将洗涤液用于步骤S4中稀释所述溶出矿浆;S9: using the washing liquid for diluting the dissolved pulp in step S4;
本步骤中,产生的洗涤液为废液,但将洗涤液返回到步骤S4中用于稀释溶出矿浆,既减少了废液的处理和排放,又达到了重复利用的效果,达到了物料的回收再利用;In this step, the generated washing liquid is waste liquid, but the washing liquid is returned to the step S4 for diluting the dissolved pulp, which not only reduces the treatment and discharge of the waste liquid, but also achieves the effect of recycling, and achieves the recovery of the material. Reuse;
S10:将步骤S7中得到的碳酸钙在1000℃下进行煅烧分解,得到二氧化碳气体和氧化钙,得到的二氧化碳气体用于步骤S5中碳分处理,得到的氧化钙用于步骤S7中苛化处理;S10: calcining the calcium carbonate obtained in the step S7 at 1000 ° C to obtain carbon dioxide gas and calcium oxide, and the obtained carbon dioxide gas is used for carbon separation in the step S5, and the obtained calcium oxide is used for causticization in the step S7. ;
本步骤中,碳酸钙的分解再利用,实现了资源的回收利用,避免了资源的浪费,节约了成本。In this step, the decomposition and reuse of calcium carbonate realizes the recycling of resources, avoids waste of resources, and saves costs.
得到的冶金级氧化铝即为产品。The resulting metallurgical grade alumina is the product.
实施例2Example 2
本实施例采用中低品位铝土矿,主要化学成分(质量百分比,wt%)为:氧化铝(Al 2O 3)  65.22%,二氧化硅(SiO 2)  12.66%,其它为杂质,其铝硅比为5.15; In this embodiment, a medium-low grade bauxite is used, and the main chemical components (mass percentage, wt%) are: alumina (Al 2 O 3 ) 65.22%, silica (SiO 2 ) 12.66%, others are impurities, and aluminum thereof The silicon ratio is 5.15;
铁酸钠为含铁原料与工业碳碱烧结而成;Sodium ferrite is sintered from iron-containing raw materials and industrial carbon base;
循环母液中的苛碱浓度为230g/L,分子比为20。The concentration of caustic in the circulating mother liquor was 230 g/L and the molecular ratio was 20.
F/A=0.6∶1;F/A = 0.6:1;
C/F=4∶1。C/F = 4:1.
按照本图1所示的本发明钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法:A method for producing metallurgical grade alumina by treating a medium-low grade bauxite according to the one-step alkali heat treatment of the calcium iron garnet of the present invention shown in FIG. 1 :
S1:将中低品位铝土矿破碎磨细成矿粉;S1: crushing and grinding fine ore powder of medium and low grade bauxite;
S2:将矿粉、铁酸钠、活性石灰混合后,按照L/S=4∶1的比例与循环母液混合制备成原料矿浆;S2: mixing the mineral powder, sodium ferrite, and active lime, and mixing with the circulating mother liquor according to the ratio of L/S=4:1 to prepare a raw material slurry;
S3:将原料矿浆在反应釜中进行溶出反应,溶出反应温度为250℃,溶出反应时间为1h,反应结束后得到溶出矿浆;S3: the raw material slurry is subjected to a dissolution reaction in the reaction vessel, the dissolution reaction temperature is 250 ° C, the dissolution reaction time is 1 h, and the dissolution slurry is obtained after the reaction is completed;
经过本步骤的溶出反应处理,氧化铝的提取率能够达到83.7%;After the dissolution reaction treatment in this step, the extraction rate of alumina can reach 83.7%;
S4:将溶出矿浆进行稀释得到稀释液,将稀释液进行液固分离,得到溶出渣和溶出液,其中溶出液为铝酸钠溶液;S4: diluting the eluted slurry to obtain a diluent, and performing liquid-solid separation on the diluted solution to obtain a dissolution slag and an eluate, wherein the eluate is a sodium aluminate solution;
S5:将低分子比铝酸钠在80℃、晶种添加系数为0.8的条件下,通二氧化碳并加入晶种进行碳分,碳分终点为分解率95%以上。碳分得到粗氢氧化铝料浆后进行液固分离,得到碳分母液和粗氢氧化铝;S5: Under the condition of low molecular ratio sodium aluminate at 80 ° C and a seed crystal addition coefficient of 0.8, carbon dioxide is added to the seed crystal to carry out carbon, and the carbon end point is a decomposition rate of 95% or more. After the carbon is obtained, the crude aluminum hydroxide slurry is subjected to liquid-solid separation to obtain a carbon mother liquor and crude aluminum hydroxide;
S6:将步骤S5中得到的粗氢氧化铝进行拜耳法处理,得到冶金级氧化铝;S6: subjecting the crude aluminum hydroxide obtained in the step S5 to a Bayer process to obtain a metallurgical grade alumina;
S7:将步骤S5中得到的碳分母液采用氧化钙进行苛化,得到苛化料浆,将苛化料浆进行液固分离,得到高分子比铝酸钠溶液和碳酸钙,将高分子比铝酸钠溶液进行调制,作为步骤S2中的循环母液;S7: The carbon mother liquor obtained in step S5 is causticized with calcium oxide to obtain a caustic slurry, and the caustic slurry is subjected to liquid-solid separation to obtain a polymer ratio sodium aluminate solution and calcium carbonate, and the ratio of the polymer is The sodium aluminate solution is prepared as the circulating mother liquor in step S2;
本步骤中,将碳分母液进行处理,得到的高分子比铝酸钠溶液调整后能够作为循环母液参与其他工艺流程,使得工艺流程无外排无污染;In this step, the carbon mother liquor is treated, and the obtained polymer can be used as a circulating mother liquor to participate in other process processes after adjusting the sodium aluminate solution, so that the process has no efflux and no pollution;
S8:将步骤S4中的溶出渣进行洗涤并固液分离,得到钙铁榴石型渣和洗涤液;S8: washing the eluted slag in step S4 and solid-liquid separation to obtain calcium garnet type slag and washing liquid;
本步骤中,经过处理得到了无碱钙铁榴石型渣,使硅与加入的铁和钙以钙铁榴石的形式留在溶出渣中,降低了渣中的碱含量;In this step, the alkali-free calcium iron garnet type slag is obtained after treatment, so that the silicon and the added iron and calcium remain in the dissolution slag in the form of calcium iron garnet, thereby reducing the alkali content in the slag;
S9:将洗涤液用于步骤S4中稀释所述溶出矿浆;S9: using the washing liquid for diluting the dissolved pulp in step S4;
本步骤中,产生的洗涤液为废液,但将洗涤液返回到步骤S4中用于稀释溶出矿浆,既减少了废液的处理和排放,又达到了重复利用的效果,达到了物料的回收再利用;In this step, the generated washing liquid is waste liquid, but the washing liquid is returned to the step S4 for diluting the dissolved pulp, which not only reduces the treatment and discharge of the waste liquid, but also achieves the effect of recycling, and achieves the recovery of the material. Reuse;
S10:将步骤S7中得到的碳酸钙在1000℃下进行煅烧分解,得到二氧化碳气体和氧化钙,得到的二氧化碳气体用于步骤S5中碳分处理,得到的氧化钙用于步骤S7中苛化处理;S10: calcining the calcium carbonate obtained in the step S7 at 1000 ° C to obtain carbon dioxide gas and calcium oxide, and the obtained carbon dioxide gas is used for carbon separation in the step S5, and the obtained calcium oxide is used for causticization in the step S7. ;
本步骤中,碳酸钙的分解再利用,实现了资源的回收利用,避免了资源的浪费,节约了成本。In this step, the decomposition and reuse of calcium carbonate realizes the recycling of resources, avoids waste of resources, and saves costs.
得到的冶金级氧化铝即为产品。The resulting metallurgical grade alumina is the product.
本发明的方法具有流程短、效率高的特点,全流程的最终产物为冶金级氧化铝和无碱钙铁榴石型渣,其余物料均实现了循环利用,整个流程中物料实现了零排放。这种无碱钙铁榴石型渣因碱含量的降低得到了有效利用,如用于炼钢过程的铁酸钙添加剂、做自应力、高强度、速凝硅酸盐水泥和高速公路、机场跑道等高强度混凝土的理想骨料,以及作为微晶玻璃、硅肥等附加值较高产品的潜在原料。The method of the invention has the characteristics of short process and high efficiency, and the final products of the whole process are metallurgical grade alumina and alkali-free calcium iron garnet type slag, and the rest of the materials are recycled, and the materials in the whole process realize zero discharge. This alkali-free calcium iron garnet type slag has been effectively utilized due to the reduction of alkali content, such as calcium ferrite additive used in steelmaking process, self-stressing, high strength, quick-setting Portland cement and highways, airports. Ideal aggregate for high-strength concrete such as runways, and as a potential raw material for higher value-added products such as glass-ceramics and silicon fertilizers.

Claims (10)

  1. 一种钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:包括下述步骤,Method for producing metallurgical grade alumina by low-grade bauxite by one-step alkali heat treatment of calcium iron garnet, characterized in that it comprises the following steps:
    S1:将中低品位铝土矿破碎磨细成矿粉;S1: crushing and grinding fine ore powder of medium and low grade bauxite;
    S2:将矿粉、铁酸钠或铁酸钙、活性石灰及循环母液混合制备成原料矿浆;S2: mixing mineral powder, sodium ferrite or calcium ferrite, active lime and circulating mother liquor into raw material pulp;
    S3:将原料矿浆进行碱热溶出反应,反应结束后得到溶出矿浆;S3: performing alkali thermal elution reaction on the raw material slurry, and obtaining a dissolved pulp after the reaction is completed;
    S4:将溶出矿浆进行稀释得到稀释液,将稀释液进行液固分离,得到溶出渣和溶出液,其中溶出液为铝酸钠溶液;S4: diluting the eluted slurry to obtain a diluent, and performing liquid-solid separation on the diluted solution to obtain a dissolution slag and an eluate, wherein the eluate is a sodium aluminate solution;
    S5:将铝酸钠溶液中通入二氧化碳气体进行碳分,得到粗氢氧化铝和碳分母液;S5: introducing carbon dioxide gas into the sodium aluminate solution to carry out carbon, to obtain crude aluminum hydroxide and carbon mother liquor;
    S6:将所述粗氢氧化铝进行拜耳法处理,得到冶金级氧化铝;S6: subjecting the crude aluminum hydroxide to a Bayer process to obtain a metallurgical grade alumina;
    S7:将步骤S5中得到的碳分母液采用石灰乳进行苛化,得到苛化料浆,将苛化料浆进行液固分离,得到氢氧化钠溶液和碳酸钙,将氢氧化钠溶液进行调制,作为步骤S2中的循环母液。S7: The carbon mother liquor obtained in step S5 is causticized with lime milk to obtain a caustic slurry, and the caustic slurry is subjected to liquid-solid separation to obtain a sodium hydroxide solution and calcium carbonate, and the sodium hydroxide solution is prepared. As the circulating mother liquor in step S2.
  2. 根据权利要求1所述的钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:所述中低品位铝土矿的硅铝比为2~6。The method for producing a metallurgical grade alumina of a medium-low grade bauxite by the one-step alkali thermal treatment of the calcium iron garnet according to claim 1, wherein the medium-low grade bauxite has a silicon to aluminum ratio of 2-6 .
  3. 根据权利要求1所述的钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:铝土矿、铁酸钠或铁酸钙、活性石灰组成的原料矿浆中,各形态存在的铁、铝、钙、硅总量分别以氧化物计,配料配方如下:The method for producing a metallurgical grade alumina of a medium-low grade bauxite by a one-step alkali thermal treatment of calcium iron garnet according to claim 1, characterized in that: bauxite, sodium ferrite or calcium ferrite, active lime In the raw material pulp, the total amount of iron, aluminum, calcium and silicon present in each form is determined by the oxide, and the formulation of the ingredients is as follows:
    氧化铁的总量与氧化铝的总量的质量比为0.2~0.6∶1;The mass ratio of the total amount of iron oxide to the total amount of alumina is 0.2 to 0.6:1;
    氧化钙的总量与氧化铁的总量的摩尔比为3~6∶1。The molar ratio of the total amount of calcium oxide to the total amount of iron oxide is from 3 to 6:1.
  4. 根据权利要求1或2所述的钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:步骤S1中,原料矿浆的液固比为2~5∶1。The method for producing a metallurgical grade alumina of a medium-low grade bauxite by the one-step alkali thermal treatment of calcium iron garnet according to claim 1 or 2, wherein in step S1, the liquid-solid ratio of the raw material slurry is 2 to 5 : 1.
  5. 根据权利要求1所述的钙铁榴石一步碱热法处理中低品位铝土矿 生产冶金级氧化铝的方法,其特征在于:步骤S2中循环母液中的苛碱浓度为150~250g/L,分子比为5~25。The method for producing metallurgical grade alumina in a medium-low grade bauxite by the one-step alkali thermal treatment of calcium iron garnet according to claim 1, wherein the concentration of caustic in the circulating mother liquor in step S2 is 150-250 g/L The molecular ratio is 5 to 25.
  6. 根据权利要求1所述的钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:步骤S3中溶出反应的温度为150~250℃,反应时间为0.5~2h。The method for producing a metallurgical grade alumina of a medium-low grade bauxite by the one-step alkali thermal treatment of the calcium iron garnet according to claim 1, wherein the temperature of the dissolution reaction in the step S3 is 150 to 250 ° C, and the reaction time is 0.5 to 2 hours.
  7. 根据权利要求1所述的钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:The method for producing a metallurgical grade alumina from a medium-low grade bauxite by a one-step alkali thermal treatment of calcium iron garnet according to claim 1, wherein:
    步骤S5中,向低分子比铝酸钠内通入二氧化碳气体并加入晶种进行碳分,得到粗氢氧化铝料浆后进行液固分离,得到碳分母液和粗氢氧化铝,In step S5, a carbon dioxide gas is introduced into the low molecular ratio sodium aluminate and a seed crystal is added to carry out carbon, and a crude aluminum hydroxide slurry is obtained, followed by liquid-solid separation to obtain a carbon mother liquor and a crude aluminum hydroxide.
    步骤S5中碳分温度为60~90℃,碳分终点为分解率在90%以上,晶种添加系数为0~1.0。In step S5, the carbon content temperature is 60 to 90 ° C, the carbon end point is a decomposition rate of 90% or more, and the seed crystal addition coefficient is 0 to 1.0.
  8. 根据权利要求1所述的钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:所述方法还包括:The method for producing a metallurgical grade alumina of a medium-low grade bauxite by a one-step alkali thermal treatment of the calcium iron garnet according to claim 1, wherein the method further comprises:
    步骤S8:将步骤S4中的溶出渣进行洗涤并固液分离,得到钙铁榴石型渣和洗涤液;Step S8: washing the eluted slag in step S4 and solid-liquid separation to obtain calcium garnet type slag and washing liquid;
    步骤S9:将所述洗涤液用于步骤S4中稀释所述溶出矿浆。Step S9: The washing liquid is used to dilute the dissolved slurry in step S4.
  9. 根据权利要求1所述的钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:所述方法还包括步骤S10:将步骤S7中得到的碳酸钙进行煅烧分解,得到二氧化碳气体和氧化钙,得到的二氧化碳气体用于步骤S5中碳分处理,得到的氧化钙用于步骤S7中苛化碳分母液。The method for producing a metallurgical grade alumina of a medium-low grade bauxite by the one-step alkali thermal treatment of the calcium iron garnet according to claim 1, wherein the method further comprises the step S10: the calcium carbonate obtained in the step S7 Calcination decomposition is carried out to obtain carbon dioxide gas and calcium oxide, and the obtained carbon dioxide gas is used for carbon separation in step S5, and the obtained calcium oxide is used in the causticized carbon mother liquid in step S7.
  10. 根据权利要求1所述钙铁榴石一步碱热法处理中低品位铝土矿生产冶金级氧化铝的方法,其特征在于:步骤S1中的铁酸钠是含铁原料与工业碳碱烧结而成;铁酸钙是含铁原料与石灰烧结而成。The method for producing a metallurgical grade alumina of a medium-low grade bauxite by the one-step alkali thermal treatment of the calcium iron garnet according to claim 1, wherein the sodium ferrite in the step S1 is sintered by the iron-containing raw material and the industrial carbon alkali. Calcium ferrite is a sintered iron-containing material and lime.
PCT/CN2018/092422 2017-06-23 2018-06-22 Method for preparing metallurgical-level aluminum oxide by treating medium- and low-grade bauxite by using one-step alkali heat process of andradite WO2018233686A1 (en)

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CN107857285A (en) * 2017-12-01 2018-03-30 东北大学设计研究院(有限公司) A kind of method that aluminic acid sodium crystal is produced using low-grade aluminum-containing raw material
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