CN101988158A - Comprehensive utilization method of titanium-containing waste residues - Google Patents

Comprehensive utilization method of titanium-containing waste residues Download PDF

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CN101988158A
CN101988158A CN2010105762569A CN201010576256A CN101988158A CN 101988158 A CN101988158 A CN 101988158A CN 2010105762569 A CN2010105762569 A CN 2010105762569A CN 201010576256 A CN201010576256 A CN 201010576256A CN 101988158 A CN101988158 A CN 101988158A
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titanium
waste residue
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CN101988158B (en
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薛向欣
张悦
杨合
白丽丽
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Northeastern University China
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Abstract

本发明涉及环保技术领域,具体涉及一种含钛废渣的综合利用方法,按如下步骤进行:实现本发明目的的技术方案是按如下步骤进行:⑴破碎和粉磨:将含钛废渣经破碎和粉磨得到直径50~160μm的粉末;⑵物料混料:将含钛废渣粉末与硫酸铵进行混合,然后再与硫酸钾混合均匀;⑶熔融:将上述混匀的物料升温至200~500℃并保温1~50min,得到块状固体和氨气;⑷溶解和过滤:将上述块状固体置于水中溶解、过滤得到滤液和残渣,残渣用作水泥添加剂;⑸钛的沉淀;⑹铝的沉淀。本发明的原料来源广泛,既解决了含钛废渣的大量排放造成的环境污染问题,又合理利用了钛和铝等资源,具有可观的环境效益、社会效益和经济效益。

Figure 201010576256

The present invention relates to the field of environmental protection technology, in particular to a method for comprehensive utilization of titanium-containing waste residue, which is carried out according to the following steps: the technical solution for realizing the purpose of the present invention is carried out according to the following steps: (1) crushing and grinding: the titanium-containing waste residue is crushed and Grinding to obtain a powder with a diameter of 50-160 μm; (2) material mixing: mix the titanium-containing waste slag powder with ammonium sulfate, and then mix it with potassium sulfate evenly; (3) melting: heat the above-mentioned mixed material to 200-500 ° C and Insulate for 1 to 50 minutes to obtain massive solids and ammonia gas; (4) Dissolving and filtering: dissolve the above massive solids in water and filter to obtain filtrate and residues, which are used as cement additives; (5) precipitation of titanium; (6) precipitation of aluminum. The invention has wide sources of raw materials, solves the problem of environmental pollution caused by massive discharge of titanium-containing waste residues, and rationally utilizes resources such as titanium and aluminum, and has considerable environmental, social and economic benefits.

Figure 201010576256

Description

一种含钛废渣的综合利用方法 A comprehensive utilization method of titanium-containing waste slag

技术领域technical field

本发明涉及环保技术领域,具体涉及一种含钛废渣的综合利用方法。The invention relates to the technical field of environmental protection, in particular to a comprehensive utilization method of titanium-containing waste residue.

背景技术Background technique

含钛废渣(包括含钛尾矿和含钛高炉渣)的排放造成了大量钛资源的流失,同时也污染了环境,因此,对它的利用已成为人们关注的焦点。含钛废渣不能直接用于水泥的生产,因此限制了它的使用。从60 年代末起,重庆大学和攀钢研究院等以含硅75%的硅铁为还原剂,生产出硅钛铁合金,用它代替钛铁生产出低钛合金钢。80 年代末,完成了用含钛废渣制取TiCl4的试验研究。东北大学将分散在多种物相中的钛组分尽可能地富集到一种物相(钙钛矿)中;然后再适当控制冷却速度促使富集了钛组分的物相长大粗化,达到选矿分离的粒度要求(﹥40μm),最后用选矿方法分离,即选择性富集、长大与分离,选出品位35%~40%的钙钛矿。此外,还有用含钛废渣制备釉面砖和Sialon陶瓷材料的报道。这些研究中将废渣整体利用的方案没有充分考虑利用渣中的钛资源,部分利用或以提取TiO2为目的的研究工艺过程复杂,钛资源利用率一般仅为65%~85%,且有新的废弃与新的污染。另外,未见有从含钛废渣中回收氧化铝的报道。因此,开发工艺简单、成本低廉、产品需求量大、钛等资源利用率高、对环境污染小,消除含钛废渣对环境的污染、同时能够对其大量地利用的新工艺,是目前急需解决的问题。The discharge of titanium-containing waste slag (including titanium-containing tailings and titanium-containing blast furnace slag) has caused the loss of a large amount of titanium resources and polluted the environment. Therefore, its utilization has become the focus of attention. Titanium-containing waste slag cannot be directly used in cement production, thus limiting its use. Since the end of the 1960s, Chongqing University and Panzhihua Iron and Steel Research Institute have used ferrosilicon containing 75% silicon as a reducing agent to produce silicon-titanium ferroalloy, which is used to replace ferro-titanium to produce low-titanium alloy steel. At the end of the 1980s, the experimental research on the preparation of TiCl 4 from titanium-containing waste slag was completed. Northeastern University enriches the titanium components dispersed in multiple phases into one phase (perovskite) as much as possible; then properly controls the cooling rate to promote the growth and coarsening of the phase enriched with titanium components to meet the particle size requirement of mineral separation (>40μm), and finally separated by mineral processing method, that is, selective enrichment, growth and separation, and the perovskite with a grade of 35% to 40% is selected. In addition, there are also reports on the preparation of glazed tiles and Sialon ceramic materials from titanium-containing waste residues. In these studies, the overall utilization of waste slag did not fully consider the utilization of titanium resources in slag, and the research process for partial utilization or for the purpose of extracting TiO2 is complicated, and the utilization rate of titanium resources is generally only 65% to 85%. waste and new pollution. In addition, there is no report on recovering alumina from titanium-containing waste slag. Therefore, the development of a new process with simple process, low cost, large demand for products, high utilization rate of titanium and other resources, little environmental pollution, elimination of environmental pollution from titanium-containing waste slag, and large-scale utilization of it is an urgent need to solve The problem.

专利申请号为200810011305.7的技术利用含钛高炉渣和硫酸铵等原料制备植物肥料,但该工艺存在如下缺点:⑴含钛高炉渣中钛的溶解率为82%,仍有18%的钛不能利用,造成了钛资源的流失;⑵工艺过程中有氨气挥发,会产生较严重的空气污染及操作人员中毒等问题,如果考虑回收氨气将大大增加工艺的复杂程度和成本;⑶含钛高炉渣中的铝没能回收利用,造成了铝资源的流失;⑷产品附加值较低,经济效益不高。The technology with the patent application number 200810011305.7 utilizes raw materials such as titanium-containing blast furnace slag and ammonium sulfate to prepare plant fertilizers, but the process has the following disadvantages: (1) The dissolution rate of titanium in titanium-containing blast furnace slag is 82%, and 18% of the titanium is still unusable , resulting in the loss of titanium resources; (2) ammonia volatilization during the process will cause serious air pollution and operator poisoning, etc. If consideration is given to recycling ammonia, it will greatly increase the complexity and cost of the process; (3) high titanium content The aluminum in the slag cannot be recycled, resulting in the loss of aluminum resources; (4) the added value of the product is low, and the economic benefit is not high.

专利申请号为200810229589.7的技术提供了一种用含钛高炉渣制备钾氮硫镁钛铁硅叶面肥和钙硫硅肥的方法,该工艺除存在上述四条缺点外,还存在这一问题:含钛高炉渣中的部分CaTiO3作为杂质存在于提取钛后剩余的残渣中,因CaTiO3含量较大,且结晶能力强,故不能用作水泥添加剂,而仅能用作钙硫硅肥。The technology with patent application number 200810229589.7 provides a method for preparing potassium nitrogen sulfur magnesium titanium ferrosilicon foliar fertilizer and calcium sulfur silicon fertilizer with titanium-containing blast furnace slag. In addition to the above four shortcomings, this process also has this problem: Part of CaTiO3 in titanium-containing blast furnace slag exists as an impurity in the remaining residue after titanium extraction. Because of the large content of CaTiO3 and strong crystallization ability, it cannot be used as a cement additive, but can only be used as calcium sulfur silicon fertilizer.

发明内容Contents of the invention

本发明的目的是针对现有技术存在的不足,提供一种含钛废渣的综合利用方法,解决环境污染问题的同时充分利用了钛和铝资源。The object of the present invention is to provide a comprehensive utilization method of titanium-containing waste slag to solve the problem of environmental pollution and make full use of titanium and aluminum resources at the same time.

实现本发明目的的技术方案是按如下步骤进行: The technical scheme that realizes the object of the present invention is to carry out as follows:

⑴破碎和粉磨:将含钛废渣经破碎和粉磨得到直径50~160μm的粉末;(1) Crushing and grinding: The titanium-containing waste residue is crushed and ground to obtain a powder with a diameter of 50-160 μm;

⑵混料:将含钛废渣粉末与硫酸铵进行混合,然后再与硫酸钾混合均匀,物料混合按重量百分比为含钛废渣粉末:硫酸铵:硫酸钾=1:3~14:1~8;(2) Mixing: Mix the titanium-containing waste residue powder with ammonium sulfate, and then mix it with potassium sulfate evenly. The material is mixed to obtain titanium-containing waste residue powder by weight percentage: ammonium sulfate: potassium sulfate=1:3~14:1~8;

⑶熔融:将上述混匀的物料升温至200~500℃并保温1~50min,得到块状固体和氨气;(3) Melting: heat up the above-mentioned mixed material to 200-500°C and keep it warm for 1-50 minutes to obtain massive solid and ammonia gas;

⑷溶解和过滤:将上述所获块状固体置于水中溶解,然后过滤得到滤液和残渣,残渣用作水泥添加剂;(4) Dissolving and filtering: dissolving the above-mentioned blocky solid in water, then filtering to obtain filtrate and residue, and the residue is used as cement additive;

⑸钛的沉淀:向上述的滤液中通入步骤(3)得到的氨气,并控制pH为1.8~3.5,使滤液中的钛沉淀、分离,获取二氧化钛和母液1;(5) Precipitation of titanium: pass the ammonia gas obtained in step (3) into the above-mentioned filtrate, and control the pH to 1.8-3.5, so that the titanium in the filtrate is precipitated and separated, and titanium dioxide and mother liquor 1 are obtained;

⑹铝的沉淀:向母液1中通入步骤(3)得到的氨气,并控制pH为5.8~7.5,使母液1中的铝沉淀、分离,获取氧化铝和母液2;将母液2加热蒸干,得到含硫酸铵和硫酸钾的混合物,该混合物循环到步骤⑵进行再利用。(6) Precipitation of aluminum: pass the ammonia gas obtained in step (3) into the mother liquor 1, and control the pH to 5.8-7.5, so that the aluminum in the mother liquor 1 can be precipitated and separated to obtain alumina and the mother liquor 2; the mother liquor 2 is heated and evaporated Dry to obtain a mixture containing ammonium sulfate and potassium sulfate, which is recycled to step (2) for reuse.

所述的含钛废渣中二氧化钛的重量百分数为4%~36%。The weight percentage of titanium dioxide in the titanium-containing waste slag is 4%-36%.

所述的步骤(4)的滤液中,水溶性钛占含钛废渣中钛的总重量的百分比≥97.1%,水溶性铝占含钛废渣中铝的总重量的百分比≥97.2%。In the filtrate of the step (4), the percentage of water-soluble titanium to the total weight of titanium in the titanium-containing waste slag is ≥97.1%, and the percentage of water-soluble aluminum to the total weight of aluminum in the titanium-containing waste slag is ≥97.2%.

所述的步骤(5)中以二氧化钛形式沉淀的钛占滤液中钛总重量的百分≥95.4%。The titanium precipitated in the form of titanium dioxide in the step (5) accounts for more than 95.4% of the total weight of titanium in the filtrate.

所述的步骤(6)中以氧化铝形式沉淀的铝占母液1中铝总重量的百分比≥98.0%。The aluminum precipitated in the form of alumina in the step (6) accounts for ≥98.0% of the total weight of aluminum in the mother liquor 1.

所述的产物二氧化钛重量纯度≥99%,粒度为纳米级;水泥添加剂的成分为65.8wt%~69.3wt%的硫酸钙、30wt%~33wt%的硅酸钙和含量为0.3~1.2wt%的二氧化钛。The weight purity of the titanium dioxide product is ≥99%, and the particle size is nanoscale; the cement additive consists of 65.8wt% to 69.3wt% of calcium sulfate, 30wt% to 33wt% of calcium silicate and 0.3 to 1.2wt% of calcium silicate Titanium dioxide.

与现有技术相比,本发明的特点及其有益效果是:Compared with prior art, feature of the present invention and beneficial effect thereof are:

本发明选用的原料硫酸钾在加热条件下化学性质活泼,能穿透矿物晶格,与含钛废渣发生熔融反应,与硫酸铵发生协同作用,促进含钛废渣的分解,缩短反应时间并提高二氧化钛的溶解率,使其达到97%以上,彻底解决了钛资源流失的问题,同时从含钛废渣中回收了铝资源;另外,本发明的产物水泥添加剂中二氧化钛含量为3%以下,根据国家标准,可以用于水泥的生产,是现有技术无法实现的。The raw material potassium sulfate selected in the present invention has active chemical properties under heating conditions, can penetrate the mineral lattice, undergo a melting reaction with titanium-containing waste residue, and have a synergistic effect with ammonium sulfate to promote the decomposition of titanium-containing waste residue, shorten the reaction time and increase the concentration of titanium dioxide. The dissolution rate of the invention makes it reach more than 97%, which completely solves the problem of loss of titanium resources, and at the same time recovers aluminum resources from the titanium-containing waste residue; in addition, the content of titanium dioxide in the product cement additive of the present invention is less than 3%, according to the national standard , can be used in the production of cement, which cannot be realized by the prior art.

一般认为,矿物原料中有价组分的百分含量越低,其处理的难度越大。因此,对二氧化钛的重量百分比为4%~13%的含钛废渣,如含钛尾矿的处理工艺一直是研究的空白,本发明很好的处理了含钛尾矿,是技术上显著的进步。It is generally believed that the lower the percentage of valuable components in mineral raw materials, the more difficult it is to process. Therefore, the treatment process for titanium-containing waste residues with a weight percentage of 4% to 13% of titanium dioxide, such as titanium-containing tailings, has always been a blank in research. The present invention handles titanium-containing tailings very well, which is a significant technical progress. .

综上所述,本发明的原料来源广泛,一次性整体利用含钛废渣,并实现中间产物循环利用,降低了原材料和水的消耗,无二次污染,工艺简单,成本低,产品附加值高,经济效益高。既解决了含钛废渣的大量排放造成的环境污染问题,又合理利用了钛和铝等资源,彻底解决了钛和铝等资源流失的问题,且本发明方法易于实现工业化生产,具有可观的环境效益、社会效益和经济效益。In summary, the present invention has a wide range of sources of raw materials, one-time overall utilization of titanium-containing waste residue, and the recycling of intermediate products, reducing the consumption of raw materials and water, no secondary pollution, simple process, low cost, and high added value of products , high economic benefit. It not only solves the problem of environmental pollution caused by a large amount of titanium-containing waste residue, but also rationally utilizes resources such as titanium and aluminum, and completely solves the problem of loss of resources such as titanium and aluminum, and the method of the invention is easy to realize industrial production and has considerable environmental protection. benefit, social benefit and economic benefit.

附图说明Description of drawings

图1为含钛废渣的综合利用方法工艺流程方块图。Fig. 1 is a block diagram of the process flow of the comprehensive utilization method of titanium-containing waste slag.

图2为本发明制备的二氧化钛的XRD图。Fig. 2 is an XRD pattern of titanium dioxide prepared in the present invention.

具体实施方式Detailed ways

下面结合实施例对本发明作详细说明,但本发明的保护范围不仅限于下述的实施例。The present invention will be described in detail below in conjunction with the examples, but the protection scope of the present invention is not limited to the following examples.

实施例1:Example 1:

⑴破碎和粉磨:将含二氧化钛的重量百分比为4%的含钛废渣经破碎和粉磨得到直径50μm的粉末;(1) Crushing and grinding: the titanium-containing waste residue containing 4% by weight of titanium dioxide is crushed and ground to obtain a powder with a diameter of 50 μm;

⑵混料:按重量比含钛废渣粉末:硫酸铵:硫酸钾=1:4:8称取原料,将含钛废渣粉末与硫酸铵混合后,然后再与硫酸钾混合均匀;(2) Mixing: According to the weight ratio of titanium-containing waste residue powder: ammonium sulfate: potassium sulfate=1:4:8, weigh the raw materials, mix the titanium-containing waste residue powder with ammonium sulfate, and then mix it with potassium sulfate evenly;

⑶熔融:将上述混匀的物料升温至370℃并保温50min,得到块状固体和氨气;(3) Melting: raise the temperature of the above mixed material to 370°C and keep it warm for 50 minutes to obtain massive solid and ammonia gas;

⑷溶解和过滤:将上述块状固体置于水中溶解,然后过滤得到滤液和残渣,滤液中水溶性钛,占含钛废渣中钛总重量的百分比为97.1%,水溶性铝占含钛废渣中铝总重量的百分比为97.2%,残渣用作水泥添加剂;(4) Dissolving and filtering: Dissolve the above massive solid in water, then filter to obtain the filtrate and residue, the water-soluble titanium in the filtrate accounts for 97.1% of the total weight of titanium in the titanium-containing waste residue, and the water-soluble aluminum accounts for 97.1% of the total weight of titanium in the titanium-containing waste residue. The percentage of the total weight of aluminum is 97.2%, and the residue is used as a cement additive;

⑸钛的沉淀:向上述的滤液中通入步骤(3)得到的氨气,并控制pH为2.1,使滤液中的钛沉淀,生成二氧化钛和母液1,以二氧化钛形式沉淀的钛占滤液中钛总重量的百分比为95.4%;(5) Precipitation of titanium: pass the ammonia gas obtained in step (3) into the above filtrate, and control the pH to 2.1, so that the titanium in the filtrate is precipitated to generate titanium dioxide and mother liquor 1, and the titanium precipitated in the form of titanium dioxide accounts for the titanium in the filtrate The percentage of total weight is 95.4%;

⑹铝的沉淀:向母液1中通入步骤(3)得到的氨气,并控制pH为7.5,使母液1中的铝沉淀,生成氧化铝和母液2,以氧化铝形式沉淀的铝占滤液中铝总重量的百分比为99%;将母液2加热蒸干,得到含硫酸铵和硫酸钾的混合物,该混合物作为循环到步骤⑵进行再利用。(6) Precipitation of aluminum: pass the ammonia gas obtained in step (3) into the mother liquor 1, and control the pH to 7.5, so that the aluminum in the mother liquor 1 is precipitated to form alumina and mother liquor 2, and the aluminum precipitated in the form of alumina accounts for the filtrate The percentage of the total weight of aluminum in the mixture is 99%; the mother liquor 2 is heated and evaporated to dryness to obtain a mixture containing ammonium sulfate and potassium sulfate, which is recycled to step (2) for reuse.

所述的产物二氧化钛重量纯度为99.2%,粒度为25nm;水泥添加剂的成分为68wt%的硫酸钙、31.7wt%的硅酸钙和含量为0.3wt%的二氧化钛。The titanium dioxide product has a weight purity of 99.2% and a particle size of 25nm; the cement additive consists of 68wt% calcium sulfate, 31.7wt% calcium silicate and 0.3wt% titanium dioxide.

实施例2:Example 2:

⑴破碎和粉磨:将含二氧化钛的重量百分比为33%的含钛废渣经破碎和粉磨得到直径150μm的粉末;(1) Crushing and grinding: the titanium-containing waste residue containing 33% by weight of titanium dioxide is crushed and ground to obtain a powder with a diameter of 150 μm;

⑵物料混料:按重量比含钛废渣粉末:硫酸铵:硫酸钾=1:12:5称取原料,将含钛废渣粉末与硫酸铵混合后,然后再与硫酸钾混合均匀;(2) Material mixing: according to the weight ratio of titanium-containing waste residue powder: ammonium sulfate: potassium sulfate=1:12:5, weigh the raw materials, mix the titanium-containing waste residue powder with ammonium sulfate, and then mix with potassium sulfate evenly;

⑶熔融:将上述混匀的物料升温至480℃并保温3min,得到块状固体和氨气;(3) Melting: raise the temperature of the above-mentioned mixed material to 480°C and keep it warm for 3 minutes to obtain massive solid and ammonia gas;

⑷溶解和过滤:将上述块状固体置于水中溶解,然后过滤得到滤液和残渣,滤液中水溶性钛,占含钛废渣中钛总重量的百分比为98.9%,水溶性铝占含钛废渣中铝总重量的百分比为98.6%,残渣用作水泥添加剂;(4) Dissolving and filtering: Dissolve the above massive solid in water, and then filter to obtain the filtrate and residue. The water-soluble titanium in the filtrate accounts for 98.9% of the total weight of titanium in the titanium-containing waste residue, and the water-soluble aluminum accounts for 98.9% of the total weight of titanium in the titanium-containing waste residue. The percentage of the total weight of aluminum is 98.6%, and the residue is used as a cement additive;

⑸钛的沉淀:向上述的滤液中通入步骤(3)得到的氨气,并控制pH为3.3,使滤液中的钛沉淀,生成二氧化钛和母液1,以二氧化钛形式沉淀的钛占滤液中钛总重量的百分比为99.1%;(5) Precipitation of titanium: pass the ammonia gas obtained in step (3) into the above-mentioned filtrate, and control the pH to 3.3, so that the titanium in the filtrate is precipitated to generate titanium dioxide and mother liquor 1, and the titanium precipitated in the form of titanium dioxide accounts for the titanium in the filtrate The percentage of total weight is 99.1%;

⑹铝的沉淀:向母液1中通入步骤(3)得到的氨气,并控制pH为6.9,使母液1中的铝沉淀,生成氧化铝和母液2,以氧化铝形式沉淀的铝占滤液中铝总重量的百分比为98.3%;将母液2加热蒸干,得到含硫酸铵和硫酸钾的混合物,该混合物循环到步骤⑵进行再利用。(6) Precipitation of aluminum: pass the ammonia gas obtained in step (3) into the mother liquor 1, and control the pH to 6.9, so that the aluminum in the mother liquor 1 is precipitated to form alumina and mother liquor 2, and the aluminum precipitated in the form of alumina accounts for the filtrate The percentage of the total weight of aluminum in the mixture is 98.3%; the mother liquor 2 is heated and evaporated to dryness to obtain a mixture containing ammonium sulfate and potassium sulfate, which is recycled to step (2) for reuse.

所述的产物二氧化钛重量纯度为99.4%,粒度为50nm;水泥添加剂的成分为69.3wt%的硫酸钙、30wt%的硅酸钙和含量为0.7wt%的二氧化钛。The titanium dioxide product has a weight purity of 99.4% and a particle size of 50nm; the cement additive consists of 69.3wt% calcium sulfate, 30wt% calcium silicate and 0.7wt% titanium dioxide.

实施例3:Example 3:

⑴破碎和粉磨:将含二氧化钛的重量百分比为21%的含钛废渣经破碎和粉磨得到直径95μm的粉末;(1) Crushing and grinding: the titanium-containing waste residue containing 21% by weight of titanium dioxide is crushed and ground to obtain a powder with a diameter of 95 μm;

⑵按重量比含钛废渣粉末:硫酸铵:硫酸钾=1:9:2称取原料,将含钛废渣粉末与硫酸铵混合后,然后再与硫酸钾混合均匀;(2) Weigh the raw materials according to the weight ratio of titanium-containing waste residue powder: ammonium sulfate: potassium sulfate = 1:9:2, mix the titanium-containing waste residue powder with ammonium sulfate, and then mix with potassium sulfate evenly;

⑶熔融:将上述混匀的物料升温至240℃并保温32min,得到块状固体和氨气;(3) Melting: raise the temperature of the above mixed material to 240°C and keep it warm for 32 minutes to obtain massive solid and ammonia gas;

⑷溶解和过滤:将上述块状固体置于水中溶解,然后过滤得到滤液和残渣,滤液中水溶性钛,占含钛废渣中钛总重量的百分比为97.5%,水溶性铝占含钛废渣中铝总重量的百分比为97.8%,残渣用作水泥添加剂;(4) Dissolving and filtering: Dissolve the above massive solid in water, and then filter to obtain the filtrate and residue. The water-soluble titanium in the filtrate accounts for 97.5% of the total weight of titanium in the titanium-containing waste residue, and the water-soluble aluminum accounts for 97.5% of the total weight of titanium in the titanium-containing waste residue. The percentage of the total weight of aluminum is 97.8%, and the residue is used as a cement additive;

⑸钛的沉淀:向上述的滤液中通入步骤(3)得到的氨气,并控制pH为2.6,使滤液中的钛沉淀,生成二氧化钛和母液1,以二氧化钛形式沉淀的钛占滤液中钛总重量的百分比为98.7%;(5) Precipitation of titanium: pass the ammonia gas obtained in step (3) into the above-mentioned filtrate, and control the pH to 2.6, so that the titanium in the filtrate is precipitated to generate titanium dioxide and mother liquor 1, and the titanium precipitated in the form of titanium dioxide accounts for the titanium in the filtrate The percentage of total weight is 98.7%;

⑹铝的沉淀:向母液1中通入步骤(3)得到的氨气,并控制pH为6.2,使母液1中的铝沉淀,生成氧化铝和母液2,以氧化铝形式沉淀的铝占滤液中铝总重量的百分比为98.1%;将母液2加热蒸干,得到含硫酸铵和硫酸钾的混合物,该混合物循环到步骤⑵进行再利用。(6) Precipitation of aluminum: pass the ammonia gas obtained in step (3) into the mother liquor 1, and control the pH to 6.2, so that the aluminum in the mother liquor 1 is precipitated to form alumina and mother liquor 2, and the aluminum precipitated in the form of alumina accounts for the filtrate The percentage of the total weight of aluminum in the mixture is 98.1%; the mother liquor 2 is heated and evaporated to dryness to obtain a mixture containing ammonium sulfate and potassium sulfate, which is recycled to step (2) for reuse.

所述的产物二氧化钛重量纯度为99.3%,粒度为70nm;水泥添加剂的成分为65.8wt%的硫酸钙、33wt%的硅酸钙和含量为1.2wt%的二氧化钛。The titanium dioxide product has a weight purity of 99.3% and a particle size of 70nm; the cement additive consists of 65.8wt% calcium sulfate, 33wt% calcium silicate and 1.2wt% titanium dioxide.

Claims (6)

1. the method for comprehensive utilization of a titaniferous waste residue is characterized in that carrying out according to the following steps:
⑴ fragmentation and grinding: the powder that the titaniferous waste residue is obtained diameter 50~160 μ m through broken and grinding;
⑵ batch mixing: titaniferous waste residue powder is mixed with ammonium sulfate, and then mix with vitriolate of tartar, mixing of materials is titaniferous waste residue powder by weight percentage: ammonium sulfate: vitriolate of tartar=1:3~14:1~8;
⑶ fusion: the material of above-mentioned mixing is warming up to 200~500 ℃ and be incubated 1~50min, obtains blocks of solid and ammonia;
⑷ dissolving and filtration: place water to dissolve the above-mentioned blocks of solid that obtains, filter then and obtain filtrate and residue, residue is as cement additire;
⑸ the precipitation of titanium: in above-mentioned filtrate, feed the ammonia that step (3) obtains, and control pH is 1.8~3.5, makes titanium precipitation in the filtrate, separate, obtain titanium dioxide and mother liquor 1;
⑹ the precipitation of aluminium: in mother liquor 1, feed the ammonia that step (3) obtains, and control pH be 5.8~7.5, make aluminum precipitation, separation in the mother liquor 1, obtain aluminum oxide and mother liquor 2; With mother liquor 2 heating evaporates to dryness, obtain the mixture of sulfur acid ammonium and vitriolate of tartar, this mixture is recycled to step ⑵ and utilizes.
2. the method for comprehensive utilization of a kind of titaniferous waste residue according to claim 1, the weight percentage that it is characterized in that titanium dioxide in the described titaniferous waste residue is 4%~36%.
3. the method for comprehensive utilization of a kind of titaniferous waste residue according to claim 1, it is characterized in that in the filtrate of described step (4), water-soluble titanium accounts for per-cent 〉=97.1% of the gross weight of titanium in the titaniferous waste residue, and water-soluble aluminum accounts for per-cent 〉=97.2% of the gross weight of aluminium in the titaniferous waste residue.
4. the method for comprehensive utilization of a kind of titaniferous waste residue according to claim 1 is characterized in that accounting for the sedimentary titanium of titanium dioxide form in the described step (5) percentage 〉=95.4% of titanium gross weight in the filtrate.
5. the method for comprehensive utilization of a kind of titaniferous waste residue according to claim 1 is characterized in that accounting for the sedimentary aluminium of aluminum oxide form in the described step (6) per-cent 〉=98.0% of aluminium gross weight in the mother liquor 1.
6. the method for comprehensive utilization of a kind of titaniferous waste residue according to claim 1 is characterized in that described product titanium dioxide weight purity 〉=99%, and granularity is a nano level; The composition of cement additire is that the calcium sulfate of 65.8wt%~69.3wt%, Calucium Silicate powder and the content of 30wt%~33wt% are the titanium dioxide of 0.3~1.2wt%.
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106082322A (en) * 2016-07-19 2016-11-09 四川大学 A method for the mineralization of titanium-containing blast furnace slag and the co-production of carbon dioxide and TiO2 and Al2O3
CN106430264A (en) * 2016-07-19 2017-02-22 四川大学 A method of using ironmaking blast furnace slag to mineralize CO2 and co-produce alumina
CN106795586A (en) * 2014-07-08 2017-05-31 阿瓦塔纳有限公司 Product is extracted from titaniferous ore
CN106830037A (en) * 2017-02-17 2017-06-13 四川大学 One kind is using blast furnace slag mineralising CO2The method of coproduction ammonia-alum
CN109174918A (en) * 2018-09-18 2019-01-11 四川大学 The method of microwave activation blast furnace slag
CN114408964A (en) * 2022-01-22 2022-04-29 北京工业大学 A method for preparing nano-scale titanium-containing magnesium-aluminum hydrotalcite by using titanium-containing blast furnace slag
US12172905B2 (en) 2018-12-14 2024-12-24 Avertana Limited Methods of extraction of products from titanium-bearing materials

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1253185A (en) * 1998-11-10 2000-05-17 东北大学 Process for separating titanium component from titanium-contained slags
WO2005014867A2 (en) * 2003-08-09 2005-02-17 Sachtleben Chemie Gmbh Use of tio2 residues from a sulfate method
CN1952188A (en) * 2006-11-14 2007-04-25 隋智通 Process for separation and production of titanium-rich materials from titanium-containing blast furnace slag
CN101125772A (en) * 2007-07-19 2008-02-20 东北大学 Method for preparing solid titanium-calcium-sulfur-magnesium-iron-nitrogen-silicon compound fertilizer with titanium-containing blast furnace slag
CN101265136A (en) * 2008-05-08 2008-09-17 东北大学 Method for preparing solid calcium-magnesium-titanium-iron-sulfur-nitrogen-silicon compound fertilizer by quenching titanium-containing blast furnace slag with water
CN101429068A (en) * 2008-12-11 2009-05-13 东北大学 Method for producing kalium-nitrogen-sulphur-magnesium-ferrotitanium silicon foliage fertilizer and calcium-sulphur silicon fertilizer with titanium-containing furnace cinder
CN101724755A (en) * 2009-12-18 2010-06-09 邓元忠 Method for recovering titanium dioxide from blast furnace slag of vanadium titano-magnetite
CN101768673A (en) * 2010-03-08 2010-07-07 中南大学 Method for preparing titanium-rich material from titanium-containing slag

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1253185A (en) * 1998-11-10 2000-05-17 东北大学 Process for separating titanium component from titanium-contained slags
WO2005014867A2 (en) * 2003-08-09 2005-02-17 Sachtleben Chemie Gmbh Use of tio2 residues from a sulfate method
CN1952188A (en) * 2006-11-14 2007-04-25 隋智通 Process for separation and production of titanium-rich materials from titanium-containing blast furnace slag
CN101125772A (en) * 2007-07-19 2008-02-20 东北大学 Method for preparing solid titanium-calcium-sulfur-magnesium-iron-nitrogen-silicon compound fertilizer with titanium-containing blast furnace slag
CN101265136A (en) * 2008-05-08 2008-09-17 东北大学 Method for preparing solid calcium-magnesium-titanium-iron-sulfur-nitrogen-silicon compound fertilizer by quenching titanium-containing blast furnace slag with water
CN101429068A (en) * 2008-12-11 2009-05-13 东北大学 Method for producing kalium-nitrogen-sulphur-magnesium-ferrotitanium silicon foliage fertilizer and calcium-sulphur silicon fertilizer with titanium-containing furnace cinder
CN101724755A (en) * 2009-12-18 2010-06-09 邓元忠 Method for recovering titanium dioxide from blast furnace slag of vanadium titano-magnetite
CN101768673A (en) * 2010-03-08 2010-07-07 中南大学 Method for preparing titanium-rich material from titanium-containing slag

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106795586A (en) * 2014-07-08 2017-05-31 阿瓦塔纳有限公司 Product is extracted from titaniferous ore
US10287176B2 (en) 2014-07-08 2019-05-14 Avertana Limited Extraction of products from titanium-bearing minerals
US10294117B2 (en) 2014-07-08 2019-05-21 Avertana Limited Extraction of products from titanium-bearing minerals
US10407316B2 (en) 2014-07-08 2019-09-10 Avertana Limited Extraction of products from titanium-bearing minerals
CN106082322A (en) * 2016-07-19 2016-11-09 四川大学 A method for the mineralization of titanium-containing blast furnace slag and the co-production of carbon dioxide and TiO2 and Al2O3
CN106430264A (en) * 2016-07-19 2017-02-22 四川大学 A method of using ironmaking blast furnace slag to mineralize CO2 and co-produce alumina
CN106082322B (en) * 2016-07-19 2018-01-16 四川大学 A kind of titanium-containing blast furnace slag mineralization of carbon dioxide coproduction TiO2、Al2O3Method
CN106830037A (en) * 2017-02-17 2017-06-13 四川大学 One kind is using blast furnace slag mineralising CO2The method of coproduction ammonia-alum
CN106830037B (en) * 2017-02-17 2018-07-06 四川大学 It is a kind of to utilize blast furnace slag mineralising CO2The method of coproduction ammonia-alum
CN109174918A (en) * 2018-09-18 2019-01-11 四川大学 The method of microwave activation blast furnace slag
US12172905B2 (en) 2018-12-14 2024-12-24 Avertana Limited Methods of extraction of products from titanium-bearing materials
CN114408964A (en) * 2022-01-22 2022-04-29 北京工业大学 A method for preparing nano-scale titanium-containing magnesium-aluminum hydrotalcite by using titanium-containing blast furnace slag

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