CN104030330B - Method for preparing high-purity aluminum hydroxide through induced crystallization - Google Patents
Method for preparing high-purity aluminum hydroxide through induced crystallization Download PDFInfo
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- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 title claims abstract description 63
- 238000000034 method Methods 0.000 title claims abstract description 56
- 238000002425 crystallisation Methods 0.000 title claims abstract description 54
- 230000008025 crystallization Effects 0.000 title claims abstract description 54
- 239000013078 crystal Substances 0.000 claims abstract description 63
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 44
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 41
- 150000007530 organic bases Chemical class 0.000 claims abstract description 30
- 238000006243 chemical reaction Methods 0.000 claims abstract description 27
- 239000012498 ultrapure water Substances 0.000 claims abstract description 21
- 238000001035 drying Methods 0.000 claims abstract description 16
- 239000012535 impurity Substances 0.000 claims abstract description 15
- 150000003839 salts Chemical class 0.000 claims abstract description 12
- 238000005406 washing Methods 0.000 claims abstract description 8
- 239000011888 foil Substances 0.000 claims description 16
- 229910018626 Al(OH) Inorganic materials 0.000 claims description 13
- 239000007787 solid Substances 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 9
- -1 polytetrafluoroethylene Polymers 0.000 claims description 9
- 238000004458 analytical method Methods 0.000 claims description 8
- 238000006460 hydrolysis reaction Methods 0.000 claims description 8
- 230000007935 neutral effect Effects 0.000 claims description 6
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 6
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 6
- 239000011259 mixed solution Substances 0.000 claims description 4
- WGTYBPLFGIVFAS-UHFFFAOYSA-M tetramethylammonium hydroxide Chemical compound [OH-].C[N+](C)(C)C WGTYBPLFGIVFAS-UHFFFAOYSA-M 0.000 claims description 4
- 101100352919 Caenorhabditis elegans ppm-2 gene Proteins 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims description 3
- 239000003153 chemical reaction reagent Substances 0.000 claims description 2
- 238000001914 filtration Methods 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 229940073455 tetraethylammonium hydroxide Drugs 0.000 claims description 2
- LRGJRHZIDJQFCL-UHFFFAOYSA-M tetraethylazanium;hydroxide Chemical compound [OH-].CC[N+](CC)(CC)CC LRGJRHZIDJQFCL-UHFFFAOYSA-M 0.000 claims description 2
- LPSKDVINWQNWFE-UHFFFAOYSA-M tetrapropylazanium;hydroxide Chemical compound [OH-].CCC[N+](CCC)(CCC)CCC LPSKDVINWQNWFE-UHFFFAOYSA-M 0.000 claims description 2
- 230000008569 process Effects 0.000 abstract description 23
- 230000001939 inductive effect Effects 0.000 abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- 229910052594 sapphire Inorganic materials 0.000 abstract description 2
- 239000010980 sapphire Substances 0.000 abstract description 2
- MXRIRQGCELJRSN-UHFFFAOYSA-N O.O.O.[Al] Chemical compound O.O.O.[Al] MXRIRQGCELJRSN-UHFFFAOYSA-N 0.000 abstract 1
- OEYIOHPDSNJKLS-UHFFFAOYSA-N choline Chemical compound C[N+](C)(C)CCO OEYIOHPDSNJKLS-UHFFFAOYSA-N 0.000 description 9
- 229960001231 choline Drugs 0.000 description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 229910001679 gibbsite Inorganic materials 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000012452 mother liquor Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000000967 suction filtration Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- 239000001763 2-hydroxyethyl(trimethyl)azanium Substances 0.000 description 1
- 235000019743 Choline chloride Nutrition 0.000 description 1
- 150000004703 alkoxides Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- SGMZJAMFUVOLNK-UHFFFAOYSA-M choline chloride Chemical compound [Cl-].C[N+](C)(C)CCO SGMZJAMFUVOLNK-UHFFFAOYSA-M 0.000 description 1
- 229960003178 choline chloride Drugs 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 238000007306 functionalization reaction Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
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- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
本发明属于高纯氧化铝材料领域,提供一种诱导结晶制备高纯氢氧化铝的方法。该方法采用高纯铝与电子级有机碱、高纯水反应生成的含铝复盐,通过添加晶种诱导结晶,含铝复盐分解得到氢氧化铝和有机碱,将得到的氢氧化铝经过过滤,洗涤,干燥制备出纯度高、晶型一致的高纯氢氧化铝晶体,有机碱可循环利用。该方法流程短、原料易得、产品质量高、成本低、无污染。所得氢氧化铝粉体的纯度为≥99.999%,Fe、Si、Na等杂质含量均小于3ppmw。产品高纯氢氧化铝特别适用于高纯氧化铝,LED蓝宝石、发光材料等领域。
The invention belongs to the field of high-purity alumina materials and provides a method for inducing crystallization to prepare high-purity aluminum hydroxide. The method adopts the aluminum-containing double salt generated by the reaction of high-purity aluminum, electronic-grade organic base and high-purity water. By adding seeds to induce crystallization, the aluminum-containing double salt is decomposed to obtain aluminum hydroxide and organic base, and the obtained aluminum hydroxide is filtered. Washing and drying produce high-purity aluminum hydroxide crystals with high purity and consistent crystal form, and the organic base can be recycled. The method has the advantages of short process flow, easy-to-obtain raw materials, high product quality, low cost and no pollution. The purity of the obtained aluminum hydroxide powder is more than or equal to 99.999%, and the contents of impurities such as Fe, Si and Na are all less than 3ppmw. The product high-purity aluminum hydroxide is especially suitable for high-purity alumina, LED sapphire, luminescent materials and other fields.
Description
技术领域technical field
本发明属化工产品制备领域,具体涉及一种通过诱导结晶技术制备晶型一致的高纯氢氧化铝的制备方法。更具体地,本发明涉及一种采用高纯铝箔与电子级有机碱和高纯水反应生成含铝复盐,通过晶种诱导结晶作用,含铝复盐分解生成氢氧化铝晶体和有机碱,将得到的氢氧化铝经过过滤,洗涤,干燥制备出晶型一致的高纯氢氧化铝晶体,有机碱循环利用的方法。The invention belongs to the field of chemical product preparation, and in particular relates to a method for preparing high-purity aluminum hydroxide with consistent crystal forms through induced crystallization technology. More specifically, the present invention relates to a method that uses high-purity aluminum foil to react with electronic-grade organic bases and high-purity water to generate aluminum-containing double salts. Through seed crystal-induced crystallization, the aluminum-containing double salts decompose to generate aluminum hydroxide crystals and organic bases, which will be obtained The aluminum hydroxide is filtered, washed, and dried to prepare high-purity aluminum hydroxide crystals with consistent crystal forms, which is a method for recycling organic bases.
背景技术Background technique
结晶是一种从液态(溶液或熔融物)或气态原料中析出晶体物质,属于热、质传递过程的单元操作。结晶过程宏观上是一个从气、液或固相到固相的复杂相变过程,微观上是一个将很多原子、离子、分子或分子集团排列到一个规则的三维周期性阵列中的过程,是一个复杂的多相态体系间传质的结果。根据液固平衡的特点,结晶操作不仅能够从溶液中取得固体溶质,而且能够从杂质相当多的溶液或者多组元的混合物中分离出高纯或超纯的晶体。晶体的形态,大小以及纯度等性质不但在晶体生长学中有重要的作用,而且还决定着产物晶体的应用。但是晶体生长是一个复杂的过程,容易受到很多因素的影响。为了得到特定的晶体,可以采用人为因素来控制晶体的生长过程,即诱导结晶。诱导结晶是通过分析结晶机理,控制影响结晶过程的因素,形成特定的物理化学环境,调控成核和晶体生长两个重要步骤,强化和控制结晶过程方法的统称。诱导结晶技术主要用于材料纯化与功能化并成为主要发展方向之一。Crystallization is a kind of crystallization from liquid (solution or melt) or gaseous raw materials, which belongs to the unit operation of heat and mass transfer process. Macroscopically, the crystallization process is a complex phase transition process from gas, liquid or solid phase to solid phase. Microscopically, it is a process of arranging many atoms, ions, molecules or molecular groups into a regular three-dimensional periodic array. A result of mass transfer between complex multiphase systems. According to the characteristics of liquid-solid equilibrium, the crystallization operation can not only obtain solid solutes from solutions, but also separate high-purity or ultra-pure crystals from solutions with considerable impurities or multi-component mixtures. Crystal morphology, size and purity not only play an important role in crystal growth, but also determine the application of the product crystal. But crystal growth is a complex process that is easily affected by many factors. In order to obtain specific crystals, artificial factors can be used to control the growth process of crystals, that is, induced crystallization. Induced crystallization is a general term for strengthening and controlling the crystallization process by analyzing the crystallization mechanism, controlling the factors affecting the crystallization process, forming a specific physical and chemical environment, and regulating the two important steps of nucleation and crystal growth. Induced crystallization technology is mainly used for material purification and functionalization and has become one of the main development directions.
高纯氢氧化铝具有广泛的应用。氢氧化铝具有阻燃、消烟、填充等功能可以用作阻燃剂。高纯氢氧化铝可以制备高纯氧化铝,进而制备蓝宝石等。氢氧化铝晶体的纯度、晶型对其应用领域具有决定性作用。High-purity aluminum hydroxide has a wide range of applications. Aluminum hydroxide has the functions of flame retardancy, smoke elimination and filling, and can be used as a flame retardant. High-purity aluminum hydroxide can be used to prepare high-purity alumina, and then to prepare sapphire and so on. The purity and crystal form of aluminum hydroxide crystals play a decisive role in its application fields.
目前制备高纯氢氧化铝的主要工艺是醇盐水解法,包括活性醇铝法和胆碱法等。At present, the main process for preparing high-purity aluminum hydroxide is alkoxide hydrolysis, including active aluminum alkoxide method and choline method.
(一)醇铝法是日本住友专利技术,分两步进行,首先铝和异丙醇等有机醇反应生成醇铝盐,醇铝盐经过精馏去除过量有机醇后成为高纯醇铝盐,最后水解得到氢氧化铝。其缺点是:工艺路线长,醇和铝的反应必须在无水条件下进行,在水存在的条件下,会大大抑制铝和醇的反应。此外需要精馏回收有机醇,膜过滤杂质等工序,设备投资大。(1) The aluminum alcohol method is a Japanese Sumitomo patented technology, which is carried out in two steps. First, aluminum and isopropanol and other organic alcohols are reacted to form aluminum alcohol salts, which become high-purity aluminum alcohol salts after rectification to remove excess organic alcohols. Finally, it is hydrolyzed to obtain aluminum hydroxide. Its disadvantages are: the process route is long, the reaction of alcohol and aluminum must be carried out under anhydrous conditions, and the reaction of aluminum and alcohol will be greatly inhibited in the presence of water. In addition, processes such as rectification and recovery of organic alcohol and membrane filtration of impurities are required, and the investment in equipment is large.
(二)胆碱法是铝和胆碱反应生成复盐,在过饱和条件下,铝的胆碱复盐水解生成氢氧化铝并放出氢气。中国专利CN02108991.4和中国专利200510028367.5都公开了此方法。但是高纯胆碱需要通过氯化胆碱离子交换分离精制获得,胆碱纯度难保证,因此高纯胆碱的获得决定了产品质量和成本。(2) The choline method is that aluminum and choline react to generate a double salt. Under supersaturated conditions, the choline double salt of aluminum is hydrolyzed to generate aluminum hydroxide and emit hydrogen. Both Chinese patent CN02108991.4 and Chinese patent 200510028367.5 disclose this method. However, high-purity choline needs to be separated and refined by choline chloride ion exchange, and the purity of choline is difficult to guarantee. Therefore, the acquisition of high-purity choline determines the product quality and cost.
发明内容Contents of the invention
本发明的目的是针对现有高纯氢氧化铝生产方法工艺过程中所存在的上述不足,提供一种通过诱导结晶制备高纯氢氧化铝的方法,既能制备出纯度高,晶型一致的高纯氢氧化铝,又能缩短工艺流程,降低成本,绿色环保。The object of the present invention is to aim at the above-mentioned deficiencies existing in the existing high-purity aluminum hydroxide production process, and to provide a method for preparing high-purity aluminum hydroxide by induced crystallization, which can produce high-purity aluminum hydroxide with consistent crystal form, It can also shorten the technological process, reduce costs, and be environmentally friendly.
本发明提出的一种诱导结晶制备高纯氢氧化铝的新方法是通过以下技术方案加以实现的:A new method for preparing high-purity aluminum hydroxide by induced crystallization proposed by the present invention is realized through the following technical solutions:
一种诱导结晶制备高纯氢氧化铝的方法,采用高纯铝箔与电子级有机碱和高纯水反应生成含铝复盐,通过晶种诱导结晶作用,含铝复盐分解生成氢氧化铝晶体和有机碱,将得到的氢氧化铝经过过滤,洗涤,干燥制备出晶型一致的高纯氢氧化铝晶体,有机碱循环利用,包括如下步骤:A method of inducing crystallization to prepare high-purity aluminum hydroxide, which uses high-purity aluminum foil to react with electronic-grade organic bases and high-purity water to generate aluminum-containing double salts, and induces crystallization through seed crystals to decompose aluminum-containing double salts to generate aluminum hydroxide crystals and organic bases. The obtained aluminum hydroxide is filtered, washed, and dried to prepare high-purity aluminum hydroxide crystals with consistent crystal forms, and the organic base is recycled, including the following steps:
(1)将高纯铝箔加入到电子级有机碱、高纯水的混合溶液中,使混合后有机碱浓度为0.1mol/L~3mol/L,搅拌反应;(1) Add high-purity aluminum foil to the mixed solution of electronic-grade organic base and high-purity water, so that the concentration of organic base after mixing is 0.1mol/L~3mol/L, and stir to react;
(2)将高纯氢氧化铝晶种分阶段加入到(1)混合反应体系中;(2) adding high-purity aluminum hydroxide seed crystals into (1) mixed reaction system in stages;
(3)将(2)反应完的多相体系进行固液分离,得到固体粉末和混合溶液;(3) performing solid-liquid separation on the heterogeneous system that has been reacted in (2), to obtain solid powder and a mixed solution;
(4)用高纯水洗涤(3)所得的固体粉末,然后对固体进行干燥处理。(4) washing the solid powder obtained in (3) with high-purity water, and then drying the solid.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中高纯铝箔的纯度为99.999%以上,铝箔厚度≤40μm。According to the method for preparing high-purity aluminum hydroxide by induced crystallization, the purity of the high-purity aluminum foil is above 99.999%, and the thickness of the aluminum foil is less than or equal to 40 μm.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中电子级有机碱为四甲基氢氧化铵、四乙基氢氧化铵、四丙基氢氧化铵中的一种或几种的混合物。According to the method for preparing high-purity aluminum hydroxide by induced crystallization, the electronic-grade organic base is one or a mixture of tetramethylammonium hydroxide, tetraethylammonium hydroxide, and tetrapropylammonium hydroxide.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中高纯氢氧化铝晶种的添加量为产品氢氧化铝重量的10%~100%。According to the method for preparing high-purity aluminum hydroxide by induced crystallization, the amount of high-purity aluminum hydroxide seed crystals added is 10% to 100% of the weight of the product aluminum hydroxide.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中第(2)步骤反应体系温度为50~95℃,反应时间为1~8小时。According to the method for preparing high-purity aluminum hydroxide by induced crystallization, the temperature of the reaction system in step (2) is 50-95° C., and the reaction time is 1-8 hours.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中电子级有机碱浓度为0.1mol/L~3mol/L,且循环利用。According to the method for preparing high-purity aluminum hydroxide by induced crystallization, the concentration of the electronic-grade organic base is 0.1 mol/L-3 mol/L, which is recycled.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中氢氧化铝过滤为离心分离或真空过滤。According to the method for preparing high-purity aluminum hydroxide by inducing crystallization, the aluminum hydroxide filtration is centrifugal separation or vacuum filtration.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中氢氧化铝干燥温度为100~250℃。According to the method for preparing high-purity aluminum hydroxide by induced crystallization, the drying temperature of aluminum hydroxide is 100-250°C.
按所述的诱导结晶制备高纯氢氧化铝的方法,其中高纯水电阻率为≥15MΩ·cm.。According to the method for preparing high-purity aluminum hydroxide by inducing crystallization, the resistivity of high-purity water is ≥15MΩ·cm.
本发明针对现有技术的不足,通过采用高纯铝箔与电子级有机碱和高纯水反应生成含铝复盐,通过晶种诱导结晶作用,含铝复盐分解生成氢氧化铝晶体和有机碱,将得到的氢氧化铝经过过滤,洗涤,干燥制备出晶型一致的高纯氢氧化铝晶体。The present invention aims at the deficiencies of the prior art, by reacting high-purity aluminum foil with electronic-grade organic base and high-purity water to generate aluminum-containing double salt, and through crystal seed-induced crystallization, the aluminum-containing double salt decomposes to generate aluminum hydroxide crystals and organic base. The obtained aluminum hydroxide is filtered, washed, and dried to prepare high-purity aluminum hydroxide crystals with consistent crystal forms.
本发明的新方法的基本原理如下:The basic principle of the new method of the present invention is as follows:
水解反应:Al+ROH+3H2O→R[Al(OH)4]+1.5H2 Hydrolysis reaction: Al+ROH+3H 2 O→R[Al(OH) 4 ]+1.5H 2
诱导结晶: Induced crystallization:
本发明的新方法的工艺流程特点如下:The technological process characteristics of new method of the present invention are as follows:
1、流程短:相比醇铝法,本工艺由高纯铝和水直接反应,母液循环使用,大大缩短了工艺流程,而且母液不需精馏提纯。1. Short process: Compared with the aluminum alcohol method, this process directly reacts high-purity aluminum and water, and the mother liquor is recycled, which greatly shortens the process flow, and the mother liquor does not need to be purified by distillation.
2、原料易得:与胆碱法相比,本项目采用的高纯特效有机碱易获得,能够在市场上方便采购,而且纯度高,所有金属离子小于10ppb,保证了产品质量。2. Raw materials are easy to obtain: Compared with the choline method, the high-purity special-effect organic base used in this project is easy to obtain and can be easily purchased in the market, and its purity is high. All metal ions are less than 10ppb, which ensures product quality.
3、成本低:本工艺实现了铝和水直接反应生成高纯氢氧化铝,设备操作条件温和,由于催化剂循环使用,消耗量很少,所以总体成本低于醇铝法和胆碱法。3. Low cost: This process realizes the direct reaction of aluminum and water to produce high-purity aluminum hydroxide. The operating conditions of the equipment are mild. Due to the recycling of the catalyst, the consumption is very small, so the overall cost is lower than that of the aluminum alcohol method and the choline method.
4、无污染:工艺中主要原料是水和铝,产物是氢氧化铝和氢气,产生的大量氢气可以回收利用。没有任何废渣、废水、废气排放。4. Pollution-free: The main raw materials in the process are water and aluminum, and the products are aluminum hydroxide and hydrogen, and a large amount of hydrogen produced can be recycled. There is no waste residue, waste water, or exhaust gas discharge.
与现有技术相比,本发明提供的诱导结晶制备高纯氢氧化铝工艺具有如下优益性:Compared with the prior art, the induced crystallization process for preparing high-purity aluminum hydroxide provided by the present invention has the following advantages:
(1)通过诱导结晶,产品纯度高(99.999%),Fe、Si、Na等元素含量均小于3ppm。并且,晶型均为α氢氧化铝。(1) By inducing crystallization, the product has high purity (99.999%), and the contents of Fe, Si, Na and other elements are all less than 3ppm. Moreover, the crystal forms are all alpha aluminum hydroxide.
(2)成本低,生成工艺过程要求低,操作条件温和。(2) The cost is low, the requirements for the production process are low, and the operating conditions are mild.
(3)有机碱可以循环使用,消耗量很少,生产成本低。(3) The organic base can be recycled, the consumption is very little, and the production cost is low.
(4)流程短:相比醇铝法,本工艺由铝和水直接反应,母液循环使用,大大缩短了工艺流程,而且母液不需精馏提纯。(4) Short process: Compared with the aluminum alcohol method, this process directly reacts aluminum and water, and the mother liquor is recycled, which greatly shortens the process flow, and the mother liquor does not need to be purified by rectification.
(5)无污染:工艺中主要原料是水和铝,产物是氢氧化铝和氢气,产生的大量氢气可以回收利用。没有任何废渣、废水、废气排放。(5) Pollution-free: the main raw materials in the process are water and aluminum, and the products are aluminum hydroxide and hydrogen, and a large amount of hydrogen produced can be recycled. There is no waste residue, waste water, or exhaust gas discharge.
附图说明Description of drawings
图1为本发明的工艺流程图;Fig. 1 is a process flow diagram of the present invention;
图2为氢氧化铝晶种的SEM照片;Fig. 2 is the SEM photograph of aluminum hydroxide seed crystal;
图3为氢氧化铝晶种的XRD物相分析;Fig. 3 is the XRD phase analysis of aluminum hydroxide crystal seed;
图4为诱导结晶产物的SEM照片;Fig. 4 is the SEM photo of induced crystallization product;
图5为诱导结晶产物的XRD物相分析。Figure 5 is the XRD phase analysis of the induced crystallization product.
具体实施方式detailed description
下面结合附图,通过本发明实施例进一步来说明本发明的突出优点和创新点,但并不以此来限定本发明。The outstanding advantages and innovations of the present invention will be further described through the embodiments of the present invention below in conjunction with the accompanying drawings, but the present invention is not limited thereto.
实施例1Example 1
取300mL的有机碱于聚四氟乙烯反应器中,浓度为3mol/L,并且设置搅拌器转速为240rpm,反应温度为70℃,加入5g铝箔进行水解反应,同时加入三水铝石晶种进行诱导结晶,晶种添加量为1.45g,反应结晶时间1小时。用高速离心机将生成的Al(OH)3与反应试剂分离,并用高纯水洗涤固体粉末至洗液为中性,放入温度为100℃的干燥箱内进行干燥。产品氢氧化铝质量为14.4g,晶型为α-Al(OH)3,其杂质含量结果见表1。Take 300mL of organic base in a polytetrafluoroethylene reactor with a concentration of 3mol/L, set the stirrer speed at 240rpm, and the reaction temperature at 70°C, add 5g of aluminum foil for hydrolysis reaction, and add gibbsite seed crystals at the same time Inducing crystallization, the amount of seed crystals added was 1.45 g, and the reaction crystallization time was 1 hour. Use a high-speed centrifuge to separate the generated Al(OH) 3 from the reaction reagents, wash the solid powder with high-purity water until the washing liquid is neutral, and put it in a drying oven at 100°C for drying. The product aluminum hydroxide has a mass of 14.4g and a crystal form of α-Al(OH) 3 . The results of its impurity content are shown in Table 1.
表1诱导结晶产物纯度分析Table 1 Induced crystallization product purity analysis
实施例2Example 2
取10mL有机碱(3mol/L)和290mL高纯水于聚四氟乙烯反应器中,搅拌转速为240rpm,反应温度为95℃,加入5g铝箔进行水解反应,同时加入三水铝石晶种进行诱导结晶,晶种添加量为14.4g,反应结晶时间8小时。反应结束后,用真空泵进行抽滤,并用高纯水洗涤晶体至洗液为中性,然后置于250℃的干燥箱内进行干燥。产品氢氧化铝质量为15.0g,晶型为α-Al(OH)3,其杂质含量结果见表2。Take 10mL of organic base (3mol/L) and 290mL of high-purity water in a polytetrafluoroethylene reactor, the stirring speed is 240rpm, the reaction temperature is 95°C, add 5g of aluminum foil for hydrolysis reaction, and at the same time add gibbsite seed crystals to induce crystallization , the seed crystal addition amount is 14.4g, and the reaction crystallization time is 8 hours. After the reaction, use a vacuum pump to perform suction filtration, and wash the crystals with high-purity water until the washing liquid is neutral, and then place them in a drying oven at 250° C. for drying. The product aluminum hydroxide has a mass of 15.0g and a crystal form of α-Al(OH) 3 . The results of its impurity content are shown in Table 2.
表2诱导结晶产物纯度分析Table 2 Induced crystallization product purity analysis
实施例3Example 3
取100mL有机碱(3mol/L)和200mL高纯水于聚四氟乙烯反应器中,搅拌转速为240rpm,反应温度为90℃,加入5g铝箔进行水解反应,同时加入三水铝石晶种进行诱导结晶,晶种添加量为14.4g,反应结晶时间4小时。反应结束后,用真空泵进行抽滤,并用高纯水洗涤晶体至洗液为中性,然后置于250℃的干燥箱内进行干燥。产品氢氧化铝质量为14.5g,晶型为α-Al(OH)3,其杂质含量结果见表3。Take 100mL of organic base (3mol/L) and 200mL of high-purity water in a polytetrafluoroethylene reactor, the stirring speed is 240rpm, the reaction temperature is 90°C, add 5g of aluminum foil for hydrolysis reaction, and at the same time add gibbsite seed crystals to induce crystallization , the seed crystal addition amount is 14.4g, and the reaction crystallization time is 4 hours. After the reaction, use a vacuum pump to perform suction filtration, and wash the crystals with high-purity water until the washing liquid is neutral, and then place them in a drying oven at 250° C. for drying. The product aluminum hydroxide has a mass of 14.5g and a crystal form of α-Al(OH) 3 . The results of its impurity content are shown in Table 3.
表3诱导结晶产物纯度分析Table 3 Induced crystallization product purity analysis
实施例4Example 4
取50mL有机碱(3mol/L)和200mL高纯水于聚四氟乙烯反应器中,搅拌转速为240rpm,反应温度为80℃,加入5g铝箔进行水解反应,同时加入三水铝石晶种进行诱导结晶,晶种添加量为7.222g,反应结晶时间3小时。反应结束后,用真空泵进行抽滤,并用高纯水洗涤晶体至洗液为中性,然后置于250℃的干燥箱内进行干燥。产品氢氧化铝质量为14.8g,晶型为α-Al(OH)3,其杂质含量结果见表4。Take 50mL of organic base (3mol/L) and 200mL of high-purity water in a polytetrafluoroethylene reactor, the stirring speed is 240rpm, the reaction temperature is 80°C, add 5g of aluminum foil for hydrolysis reaction, and at the same time add gibbsite seed crystals to induce crystallization , the seed crystal addition amount is 7.222g, and the reaction crystallization time is 3 hours. After the reaction, use a vacuum pump to perform suction filtration, and wash the crystals with high-purity water until the washing liquid is neutral, and then place them in a drying oven at 250° C. for drying. The product aluminum hydroxide has a mass of 14.8g and a crystal form of α-Al(OH) 3 . The results of its impurity content are shown in Table 4.
表4诱导结晶产物纯度分析Table 4 Induced crystallization product purity analysis
实施例5Example 5
取50mL有机碱(3mol/L)和200mL高纯水于聚四氟乙烯反应器中,搅拌转速为240rpm,反应温度为50℃,加入5g铝箔进行水解反应,同时加入三水铝石晶种进行诱导结晶,晶种添加量为7.2g,反应结晶时间5小时。反应结束后,用真空泵进行抽滤,并用高纯水洗涤晶体至洗液为中性,然后置于250℃的干燥箱内进行干燥。产品氢氧化铝质量为14.8g,晶型为α-Al(OH)3,其杂质含量结果见表5。Take 50mL of organic base (3mol/L) and 200mL of high-purity water in a polytetrafluoroethylene reactor, the stirring speed is 240rpm, the reaction temperature is 50°C, add 5g of aluminum foil for hydrolysis reaction, and at the same time add gibbsite seed crystals to induce crystallization , the seed crystal addition amount is 7.2g, and the reaction crystallization time is 5 hours. After the reaction, use a vacuum pump to perform suction filtration, and wash the crystals with high-purity water until the washing liquid is neutral, and then place them in a drying oven at 250° C. for drying. The product aluminum hydroxide has a mass of 14.8g and a crystal form of α-Al(OH) 3 . The results of its impurity content are shown in Table 5.
表5诱导结晶产物纯度分析Table 5 Induced crystallization product purity analysis
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