CN1259240C - Method for preparing nanometer metal oxides by direct liquid phase precipitation - Google Patents
Method for preparing nanometer metal oxides by direct liquid phase precipitation Download PDFInfo
- Publication number
- CN1259240C CN1259240C CN 200410021008 CN200410021008A CN1259240C CN 1259240 C CN1259240 C CN 1259240C CN 200410021008 CN200410021008 CN 200410021008 CN 200410021008 A CN200410021008 A CN 200410021008A CN 1259240 C CN1259240 C CN 1259240C
- Authority
- CN
- China
- Prior art keywords
- metal
- ethanolic soln
- nano
- oxide
- precipitation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000000034 method Methods 0.000 title claims abstract description 105
- 238000001556 precipitation Methods 0.000 title claims abstract description 86
- 229910044991 metal oxide Inorganic materials 0.000 title claims abstract description 45
- 239000007791 liquid phase Substances 0.000 title claims abstract description 34
- 150000004706 metal oxides Chemical class 0.000 title claims abstract description 19
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 188
- 239000002244 precipitate Substances 0.000 claims abstract description 48
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 34
- 238000005406 washing Methods 0.000 claims abstract description 26
- 238000002360 preparation method Methods 0.000 claims abstract description 22
- 229910052751 metal Inorganic materials 0.000 claims abstract description 19
- 239000002184 metal Substances 0.000 claims abstract description 18
- 239000000843 powder Substances 0.000 claims abstract description 17
- 150000003839 salts Chemical class 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 238000003756 stirring Methods 0.000 claims abstract description 15
- 229910000000 metal hydroxide Inorganic materials 0.000 claims abstract description 12
- 150000004692 metal hydroxides Chemical class 0.000 claims abstract description 12
- 239000000706 filtrate Substances 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 3
- 239000000243 solution Substances 0.000 claims description 60
- 238000006243 chemical reaction Methods 0.000 claims description 57
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 31
- 239000012452 mother liquor Substances 0.000 claims description 19
- 238000001035 drying Methods 0.000 claims description 16
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 14
- 239000000047 product Substances 0.000 claims description 13
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 12
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 12
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 claims description 12
- 239000013078 crystal Substances 0.000 claims description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 8
- 239000000395 magnesium oxide Substances 0.000 claims description 8
- 239000011777 magnesium Substances 0.000 claims description 7
- 239000000347 magnesium hydroxide Substances 0.000 claims description 7
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 7
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 7
- 229910001510 metal chloride Inorganic materials 0.000 claims description 6
- XOLBLPGZBRYERU-UHFFFAOYSA-N tin dioxide Chemical compound O=[Sn]=O XOLBLPGZBRYERU-UHFFFAOYSA-N 0.000 claims description 6
- 229910052747 lanthanoid Inorganic materials 0.000 claims description 4
- 150000002602 lanthanoids Chemical class 0.000 claims description 4
- 238000013019 agitation Methods 0.000 claims description 2
- 229910021645 metal ion Inorganic materials 0.000 claims description 2
- 229910001960 metal nitrate Inorganic materials 0.000 claims description 2
- 239000011259 mixed solution Substances 0.000 claims description 2
- 229960004756 ethanol Drugs 0.000 claims 15
- 238000010790 dilution Methods 0.000 claims 14
- 239000012895 dilution Substances 0.000 claims 14
- 241000370738 Chlorion Species 0.000 claims 8
- 238000001914 filtration Methods 0.000 claims 8
- 238000005303 weighing Methods 0.000 claims 7
- ALHBQZRUBQFZQV-UHFFFAOYSA-N tin;tetrahydrate Chemical compound O.O.O.O.[Sn] ALHBQZRUBQFZQV-UHFFFAOYSA-N 0.000 claims 6
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 3
- 159000000003 magnesium salts Chemical class 0.000 claims 2
- 150000003608 titanium Chemical class 0.000 claims 2
- 239000002253 acid Substances 0.000 claims 1
- 230000001476 alcoholic effect Effects 0.000 claims 1
- 159000000013 aluminium salts Chemical class 0.000 claims 1
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 229960000935 dehydrated alcohol Drugs 0.000 claims 1
- 238000011084 recovery Methods 0.000 claims 1
- 241000894007 species Species 0.000 claims 1
- 238000005054 agglomeration Methods 0.000 abstract description 20
- 230000002776 aggregation Effects 0.000 abstract description 20
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 abstract description 17
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 abstract description 8
- 235000019270 ammonium chloride Nutrition 0.000 abstract description 4
- 239000006227 byproduct Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000009776 industrial production Methods 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 239000012429 reaction media Substances 0.000 abstract description 3
- 239000002245 particle Substances 0.000 description 25
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 18
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 8
- ZXVOCOLRQJZVBW-UHFFFAOYSA-N azane;ethanol Chemical compound N.CCO ZXVOCOLRQJZVBW-UHFFFAOYSA-N 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- CVNKFOIOZXAFBO-UHFFFAOYSA-J tin(4+);tetrahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[Sn+4] CVNKFOIOZXAFBO-UHFFFAOYSA-J 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 238000001228 spectrum Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 229910001887 tin oxide Inorganic materials 0.000 description 5
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000001354 calcination Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000007062 hydrolysis Effects 0.000 description 3
- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 150000004679 hydroxides Chemical class 0.000 description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 3
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 229910019440 Mg(OH) Inorganic materials 0.000 description 2
- 238000005411 Van der Waals force Methods 0.000 description 2
- RLWYTFZKQOKDFG-UHFFFAOYSA-N [Mg].CCO Chemical compound [Mg].CCO RLWYTFZKQOKDFG-UHFFFAOYSA-N 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 230000008602 contraction Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- WLPSNBGDESCKIL-UHFFFAOYSA-N ethanol;titanium Chemical compound [Ti].CCO WLPSNBGDESCKIL-UHFFFAOYSA-N 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000000053 physical method Methods 0.000 description 2
- 238000010532 solid phase synthesis reaction Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- IZMPACFDPANMBU-UHFFFAOYSA-N C(C)O.[AlH3] Chemical compound C(C)O.[AlH3] IZMPACFDPANMBU-UHFFFAOYSA-N 0.000 description 1
- 229910019427 Mg(NO3)2-6H2O Inorganic materials 0.000 description 1
- 238000003917 TEM image Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 238000010533 azeotropic distillation Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical group [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- PSFYVNVZQYWSRW-UHFFFAOYSA-N ethanol;tin Chemical compound [Sn].CCO PSFYVNVZQYWSRW-UHFFFAOYSA-N 0.000 description 1
- MRUQKCHUWQAJRP-UHFFFAOYSA-N ethanol;zirconium Chemical compound [Zr].CCO MRUQKCHUWQAJRP-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000004108 freeze drying Methods 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000005389 magnetism Effects 0.000 description 1
- 238000000593 microemulsion method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 238000004544 sputter deposition Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 229910001928 zirconium oxide Inorganic materials 0.000 description 1
- -1 zirconium oxide Chemical class 0.000 description 1
Images
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
本发明提供一种用直接液相沉淀法制备纳米金属氧化物的方法,其特征在于包括下列步骤:配制金属盐的乙醇溶液,配制氨水乙醇溶液,使两者在搅拌下充分混合,将得到的金属氢氧化物沉淀用乙醇洗涤,洗涤后的沉淀经过烘干、焙烧后,即得到松散的纳米金属氧化物粉体;将整个过程中产生的滤液经过蒸馏回收乙醇,同时得到氯化铵副产物,回收的乙醇可循环使用。本发明采用乙醇作为主要反应介质和洗涤液,有效地消除了制备过程中产生的团聚现象,使最终的纳米金属氧化物粉体分散性良好。本方法原料易得,操作简单,生产成本低,效率高,基本上实现“零排放”,工艺参数易控制,易于实现大规模工业生产,并且具有一定的通用性。The invention provides a method for preparing nanometer metal oxides by direct liquid phase precipitation, which is characterized in that it comprises the following steps: preparing an ethanol solution of a metal salt, preparing an ammonia water ethanol solution, mixing the two fully under stirring, and preparing the obtained The metal hydroxide precipitate is washed with ethanol, and the washed precipitate is dried and roasted to obtain loose nano-metal oxide powder; the filtrate produced in the whole process is distilled to recover ethanol, and ammonium chloride by-product is obtained at the same time , The recovered ethanol can be recycled. The invention adopts ethanol as the main reaction medium and washing liquid, effectively eliminates the agglomeration phenomenon generated in the preparation process, and makes the final nanometer metal oxide powder have good dispersibility. The method has easy-to-obtain raw materials, simple operation, low production cost, high efficiency, basically realizes "zero discharge", easy control of process parameters, easy realization of large-scale industrial production, and certain versatility.
Description
技术领域technical field
本发明属于新材料技术领域,特别是一种用直接液相沉淀法制备纳米金属氧化物的方法。The invention belongs to the technical field of new materials, in particular to a method for preparing nanometer metal oxides by direct liquid phase precipitation.
背景技术Background technique
纳米金属氧化物是一类粒径介于1~100nm之间的新型高功能精细无机材料,由于其颗粒细微化而具有不同于常规材料的热、光、电、磁、力学和化学等特殊功能。在精细化工催化、日用化工、新型陶瓷材料、新型耐火材料、高质量和特殊功能工程材料以及电子器件的制造等方面都具有重要的应用价值,有着广阔的应用前景。近年来,纳米金属氧化物的制备成为材料学科的热门课题。Nano-metal oxides are a new type of high-function fine inorganic materials with a particle size between 1 and 100nm. Due to the miniaturization of their particles, they have special functions such as heat, light, electricity, magnetism, mechanics and chemistry that are different from conventional materials. . It has important application value and broad application prospects in fine chemical catalysis, daily chemical industry, new ceramic materials, new refractory materials, high-quality and special functional engineering materials, and the manufacture of electronic devices. In recent years, the preparation of nano-metal oxides has become a hot topic in materials science.
到目前为止制备纳米金属氧化物的方法主要有物理方法和化学方法。物理方法包括机械粉碎法、蒸发凝聚法、离子溅射法等,这些方法所需能耗高。化学方法分为气相法、液相法和固相法,其中气相法设备复杂,而固相法又为非均相反应,所以,液相法是目前制备纳米金属氧化物的主要方法。液相法又包括:(1)溶胶-凝胶法;(2)沉淀法(均匀沉淀法、直接沉淀法、超重力反应沉淀法、超声沉淀法等);(3)水解法(醇盐水解法、微波水解法);(4)水热法;(5)微乳液法等等。So far, the methods for preparing nanometer metal oxides mainly include physical methods and chemical methods. Physical methods include mechanical pulverization, evaporation condensation, ion sputtering, etc. These methods require high energy consumption. Chemical methods are divided into gas-phase method, liquid-phase method and solid-phase method. The gas-phase method has complex equipment, while the solid-phase method is a heterogeneous reaction. Therefore, the liquid-phase method is currently the main method for preparing nanometer metal oxides. The liquid phase method also includes: (1) sol-gel method; (2) precipitation method (uniform precipitation method, direct precipitation method, supergravity reaction precipitation method, ultrasonic precipitation method, etc.); (3) hydrolysis method (alcohol salt hydrolysis method , microwave hydrolysis); (4) hydrothermal method; (5) microemulsion method and so on.
众所周知,制备金属氧化物的最简单、最易实现工业化的途径即为直接液相沉淀法,但该过程因团聚现象的存在而不能制备均分散的纳米金属氧化物,正如Tadao Sugimoto在《FINE PARTICLES》一书(第2页)指出的那样:“一般情况下,直接用金属盐水溶液与碱反应不能产生均匀分散颗粒,所以必须克服团聚。”因此,克服团聚是采用直接液相沉淀法制备纳米金属氧化物需解决的瓶颈。As we all know, the easiest and most industrialized way to prepare metal oxides is the direct liquid phase precipitation method, but due to the existence of agglomeration, uniformly dispersed nano metal oxides cannot be prepared in this process, as Tadao Sugimoto said in "FINE PARTICLES "One book (page 2) pointed out: "Under normal circumstances, the direct reaction of metal salt solution and alkali cannot produce uniformly dispersed particles, so it is necessary to overcome agglomeration." Therefore, to overcome agglomeration is to use direct liquid phase precipitation to prepare nano The bottleneck that needs to be solved by metal oxides.
在直接液相沉淀法中,团聚现象几乎存在于任何一个操作步骤。颗粒的团聚一般分软团聚和硬团聚。软团聚主要是由于颗粒间的范德华力和库仑力所致,该团聚可以通过一些化学作用或施加机械能的方式来消除。粉末的硬团聚体内除了颗粒之间的范德华力和库仑力外,还存在化学键作用。因此,硬团聚体在以后的加工过程中其结构不易被破坏,导致材料性能反而变差。一般认为硬团聚的形成与氢氧化物沉淀胶体结构中含有的非架桥羟基、结构配位水和吸附水有关,其中,吸附水多以颗粒间毛细管水的形式存在,随着液体的不断蒸发,沉淀颗粒中出现空隙,在空隙中形成大量的弯月面,于是,毛细收缩作用将粒子压到一起。沉淀中液体的表面张力越大,毛细收缩作用就越强,沉淀在干燥过程中,越容易在粒子间形成较强的结合力,颗粒之间的聚集就越严重,颗粒表面的吸附水与颗粒之间由于氢键作用使颗粒结合的更紧密,随着水的进一步脱除,相邻胶粒的非架桥羟基即可自发转变为架桥羟基;并将沉淀中的部分结构配位水排除,从而形成硬团聚,而这种硬团聚在随后的焙烧过程中又可能得到进一步的加强。In the direct liquid phase precipitation method, agglomeration phenomenon exists in almost any operation step. The agglomeration of particles is generally divided into soft agglomeration and hard agglomeration. Soft agglomeration is mainly caused by van der Waals force and Coulomb force between particles, and the agglomeration can be eliminated by some chemical action or by applying mechanical energy. In addition to the van der Waals force and Coulomb force between particles, there are also chemical bonds in the hard aggregate of powder. Therefore, the structure of hard aggregates is not easy to be destroyed in the subsequent processing, which leads to the deterioration of material properties. It is generally believed that the formation of hard agglomerates is related to the non-bridging hydroxyl groups, structural coordination water and adsorbed water contained in the hydroxide precipitated colloidal structure. Among them, the adsorbed water mostly exists in the form of capillary water between particles, and as the liquid continues to evaporate , voids appear in the precipitated particles, and a large number of menisci are formed in the voids, so capillary contraction presses the particles together. The greater the surface tension of the liquid in the precipitation, the stronger the capillary contraction, the easier it is for the precipitation to form a stronger binding force between the particles during the drying process, and the more serious the aggregation between the particles is, the adsorbed water on the surface of the particles and the particles Due to the hydrogen bond between the particles, the particles are combined more tightly. With the further removal of water, the non-bridging hydroxyl groups of adjacent colloidal particles can spontaneously transform into bridging hydroxyl groups; and part of the structural coordination water in the precipitation is excluded. , thus forming hard agglomerates, and this hard agglomeration may be further strengthened in the subsequent firing process.
为了消除直接液相沉淀法所产生的硬团聚,人们做了大量的工作,目前还处于探索阶段。反团聚可分两步进行:第一步,在形成胶体沉淀过程中控制颗粒的团聚,如高分子保护法,目前在该方面的研究较少;第二步,在干燥过程前,采用如有机物洗涤、共沸蒸馏、冷冻干燥、喷射干燥、超临界流体干燥等方法控制沉淀的团聚。In order to eliminate the hard agglomeration produced by the direct liquid phase precipitation method, people have done a lot of work, which is still in the exploration stage. Anti-agglomeration can be carried out in two steps: the first step is to control the agglomeration of particles in the process of forming colloidal precipitation, such as polymer protection method, and there are few researches in this area; the second step is to use such as organic Washing, azeotropic distillation, freeze drying, spray drying, supercritical fluid drying and other methods control the agglomeration of precipitates.
在现有的制备纳米金属氧化物液相法中,有的工艺流程复杂,有的设备及技术要求高,有的原材料成本高,有的生产周期长,有的产率低,有的产生污染,有的不能从根本上消除制备过程中产生的团聚现象导致产品的分散性差,限制了其在工业生产中的应用。且现有方法中适用制备不同种类的纳米金属氧化物的通用方法并不多,大都是关于某一具体氧化物的制备方法。In the existing liquid-phase methods for preparing nanometer metal oxides, some have complex technological processes, some have high equipment and technical requirements, some have high raw material costs, some have long production cycles, some have low yields, and some produce pollution. , Some cannot fundamentally eliminate the agglomeration phenomenon produced in the preparation process, resulting in poor dispersion of the product, which limits its application in industrial production. Moreover, there are not many general methods suitable for preparing different kinds of nanometer metal oxides in the existing methods, and most of them are about the preparation method of a specific oxide.
发明内容Contents of the invention
本发明的目的是提供一种操作简单,成本低,效率高,产品无团聚,无环境污染,易于实现工业化生产的,且具有一定通用性的制备纳米金属氧化物的方法。The purpose of the present invention is to provide a kind of simple operation, low cost, high efficiency, no agglomeration of products, no environmental pollution, easy to realize industrialized production, and a method for preparing nanometer metal oxides with certain versatility.
按照本发明的用直接液相沉淀法制备纳米金属氧化物的方法,其特征在于包括下列步骤:According to the method for preparing nanometer metal oxides by direct liquid phase precipitation method of the present invention, it is characterized in that comprising the following steps:
1)选用金属盐为能溶于乙醇的金属氯化物、带有结晶水的金属氯化物或带有结晶水的金属氯化物加上带有结晶水的金属硝酸盐,1) select metal salt to be the metal chloride that can be dissolved in ethanol, the metal chloride that has crystal water or the metal chloride that has crystal water plus the metal nitrate that has crystal water,
2)配制金属盐乙醇溶液,用体积百分比为≤25%的水将金属盐溶解,然后用乙醇稀释至浓度范围为0.05mol/L~1mol/L的金属盐乙醇溶液,2) preparing metal salt ethanol solution, dissolving the metal salt with water with a volume percentage of ≤25%, and then diluting with ethanol to a metal salt ethanol solution with a concentration range of 0.05mol/L to 1mol/L,
3)配制氨水乙醇溶液,将浓氨水用乙醇稀释,配制成浓度0.05mol/L~4mol/L的氨水乙醇溶液,3) prepare the ammonia water ethanol solution, dilute the concentrated ammonia water with ethanol, and prepare the ammonia water ethanol solution with a concentration of 0.05mol/L~4mol/L,
4)使配制好的金属盐乙醇溶液和氨水的乙醇溶液在搅拌下充分混合,混合时反应的温度可控制在5℃至70℃范围内,4) Fully mix the prepared metal salt ethanol solution and the ethanol solution of ammonia water under stirring, and the reaction temperature during mixing can be controlled within the range of 5°C to 70°C,
5)将反应终点的pH值控制在5~11的范围内,使金属氢氧化物沉淀完全,5) Control the pH value at the end of the reaction in the range of 5 to 11, so that the metal hydroxide is completely precipitated,
6)将反应液过滤,使金属氢氧化物沉淀与母液分离,6) the reaction solution is filtered to separate the metal hydroxide precipitate from the mother liquor,
7)用乙醇将分离出的金属氢氧化物沉淀洗涤至无氯离子,7) washing the isolated metal hydroxide precipitate with ethanol to no chloride ion,
8)将洗涤后的金属氢氧化物在30℃~120℃下烘干1~6小时,8) drying the washed metal hydroxide at 30°C to 120°C for 1 to 6 hours,
9)将烘干后的金属氢氧化物在500℃~1000℃下焙烧1~4小时,即可得到松散的纳米金属氧化物粉体。9) Calcining the dried metal hydroxide at 500° C. to 1000° C. for 1 to 4 hours to obtain loose nanometer metal oxide powder.
在本方法中采用乙醇为主要反应介质来替代直接液相沉淀法反应体系中的大量水分子,其作用如下:(1)降低表面张力,减弱毛细作用;(2)大大降低颗粒表面的吸附水,减少颗粒之间氢键的形成,这两种作用使硬团聚不易发生,从根本上消除了团聚现象。另外,以乙醇为主要介质降低了氢氧化物的溶解度,使沉淀物相对过饱和度提高,这有利于爆发成核,形成均分散胶体体系。对于某些溶解度较大的氢氧化物来说,通过降低其溶解度可减少损失。In this method, ethanol is used as the main reaction medium to replace a large amount of water molecules in the direct liquid precipitation method reaction system, and its effect is as follows: (1) reduce surface tension, weaken capillary action; , to reduce the formation of hydrogen bonds between particles, these two effects make hard agglomeration difficult to occur, and fundamentally eliminate the agglomeration phenomenon. In addition, using ethanol as the main medium reduces the solubility of hydroxide and increases the relative supersaturation of the precipitate, which is conducive to explosive nucleation and the formation of a homodisperse colloidal system. For some hydroxides with high solubility, the loss can be reduced by reducing their solubility.
用甲醇、丙醇、异丙醇等有机溶液替代乙醇,基本可获得相同的效果,但是,相对乙醇来说,甲醇毒性大,而其它醇类价格高,且金属盐在其中溶解度小。Substituting organic solutions such as methanol, propanol, and isopropanol for ethanol can basically achieve the same effect. However, compared with ethanol, methanol is more toxic, while other alcohols are expensive, and the solubility of metal salts in them is small.
按照本发明,所述的金属盐可选自元素周期表IIA~VA族、IIIB~VIIB族及镧系中的至少1种金属离子。According to the present invention, the metal salt can be selected from at least one metal ion in groups II A to VA , III B to VII B and lanthanides of the periodic table of elements.
按照本发明,所述的纳米金属氧化物为含元素周期表IIA~VA族、IIIB~VIIB族及镧系中的至少1种金属元素的氧化物,例如氧化锆、掺杂Y2O3的氧化锆、掺杂MgO的氧化锆、氧化镁、氧化钛、氧化锡、氧化铝等。According to the present invention, the nanometer metal oxide is an oxide containing at least one metal element in the Periodic Table of Elements II A to V A , III B to VII B and Lanthanide, such as zirconium oxide, doped Y 2 O 3 zirconia, MgO-doped zirconia, magnesia, titanium oxide, tin oxide, aluminum oxide, etc.
按照本发明,所述的金属盐乙醇溶液的配制方法是先用少量的水将金属盐溶解,以增加其在乙醇中的溶解度,然后,用乙醇稀释至所需浓度。According to the present invention, the preparation method of the metal salt ethanol solution is to dissolve the metal salt with a small amount of water to increase its solubility in ethanol, and then dilute it to the required concentration with ethanol.
按照本发明,所述的金属盐乙醇溶液的浓度为0.2mol/L~0.5mol/L。According to the present invention, the concentration of the metal salt ethanol solution is 0.2mol/L-0.5mol/L.
按照本发明,所述的沉淀反应的温度为室温,此时能耗最小。According to the present invention, the temperature of the precipitation reaction is room temperature, and the energy consumption is minimum at this time.
按照本发明,所述的沉淀反应终点pH可控制在5.5~11的范围内。对于溶度积较小的氢氧化物,沉淀反应终点pH可控制在5.5~9的范围内,可使沉淀完全;对于溶度积较大的氢氧化物,沉淀反应终点pH可控制在8~11的范围内,以保证沉淀完全。According to the present invention, the pH at the end point of the precipitation reaction can be controlled within the range of 5.5-11. For hydroxides with a small solubility product, the pH at the end point of the precipitation reaction can be controlled within the range of 5.5-9, which can make the precipitation complete; for hydroxides with a large solubility product, the pH at the end point of the precipitation reaction can be controlled at 8-9. 11 to ensure complete precipitation.
按照本发明,所述的用乙醇洗涤可进一步脱除吸附水。According to the present invention, the said washing with ethanol can further remove the adsorbed water.
按照本发明,所述的烘干过程可用普通烘箱,温度为100℃~120℃,烘干时间为1~3h;也可用真空干燥箱,温度为30℃~100℃,烘干时间为2~5h。According to the present invention, the drying process can be an ordinary oven with a temperature of 100°C to 120°C and a drying time of 1 to 3 hours; a vacuum drying oven can also be used with a temperature of 30°C to 100°C and a drying time of 2 to 3 hours. 5h.
按照本发明,所述的焙烧过程的温度视具体氧化物而定,其范围是500℃~1000℃,焙烧时间为1~4h。本工艺中因沉淀前期处理妥当(乙醇既为反应介质又为洗涤液),直接得到松散的纳米氧化物粉体。According to the present invention, the temperature of the calcination process depends on the specific oxide, the range is 500°C-1000°C, and the calcination time is 1-4h. In this process, due to the proper pre-precipitation treatment (ethanol is both the reaction medium and the washing liquid), loose nano-oxide powders are directly obtained.
按照本发明,所述的乙醇采用无水乙醇、95%乙醇或循环回收乙醇。According to the present invention, the ethanol is dehydrated ethanol, 95% ethanol or recycled ethanol.
按照本发明,所述的回收乙醇为对整个制备过程中产生的滤液,包括母液,进行蒸馏得到的乙醇,蒸馏回收乙醇过程的同时得到氯化铵副产物,基本实现“零排放”。According to the present invention, the recovered ethanol is the ethanol obtained by distilling the filtrate produced in the whole preparation process, including the mother liquor, and ammonium chloride by-product is obtained during the process of distilling and recovering ethanol, basically realizing "zero discharge".
按照本发明的用直接液相沉淀法制备纳米金属氧化物的方法,具有下列突出的特点:According to the method for preparing nanometer metal oxides with direct liquid phase precipitation method of the present invention, has the following prominent features:
1.在本发明中,乙醇既为沉淀反应的主要介质又为洗涤液,由此消除了制备过程中因吸附水而产生的团聚现象,使得金属氢氧化物沉淀易过滤洗涤,在最佳条件下得到的最终纳米金属氧化物粉体松软,不必研磨。1. In the present invention, ethanol is not only the main medium of the precipitation reaction but also the washing liquid, thereby eliminating the agglomeration phenomenon caused by the adsorption of water in the preparation process, making the metal hydroxide precipitate easy to filter and wash, and under optimal conditions The final nano-metal oxide powder obtained under the method is soft and does not need to be ground.
2.本发明整个过程中所使用的乙醇均可蒸馏回收,循环利用,同时可得到副产物氯化铵,基本实现“零排放”,可称为绿色化学合成法。2. The ethanol used in the whole process of the present invention can be distilled and recycled, and the by-product ammonium chloride can be obtained at the same time, and "zero discharge" can be basically realized, which can be called a green chemical synthesis method.
3.本发明原料易得、操作简单、无需复杂设备、成本低、效率高、方法参数极易控制、易于实现大规模工业化生产,且具有一定通用性。3. The present invention has easy-to-obtain raw materials, simple operation, no need for complex equipment, low cost, high efficiency, easy control of method parameters, easy realization of large-scale industrial production, and certain versatility.
附图说明Description of drawings
图1为本发明提供的由实施例1方法所获得的纳米氧化锆的透射电镜照片(TEM照片)。Fig. 1 is the transmission electron micrograph (TEM photo) of nano zirconia obtained by the method of
图2为本发明提供的由实施例1方法所获得的纳米氧化锆的XRD谱图。Figure 2 is the XRD spectrum of the nano-zirconia obtained by the method of Example 1 provided by the present invention.
图3为本发明提供的由实施例2方法所获得的掺杂Y2O3的纳米氧化锆TEM照片。Fig. 3 is a TEM photograph of nano-zirconia doped with Y 2 O 3 obtained by the method in Example 2 provided by the present invention.
图4为本发明提供的由实施例3方法所获得的掺杂MgO的纳米氧化锆TEM照片。FIG. 4 is a TEM photo of MgO-doped nano-zirconia obtained by the method of Example 3 provided by the present invention.
图5为本发明提供的由实施例4方法所获得的纳米氧化镁的TEM照片。Fig. 5 is the TEM picture of the nano magnesium oxide obtained by the method of embodiment 4 provided by the present invention.
图6为本发明提供的由实施例4方法所获得的纳米氧化镁的XRD谱图。Figure 6 is the XRD spectrum of the nano-magnesia obtained by the method of Example 4 provided by the present invention.
图7为本发明提供的由实施例5方法所获得的纳米氧化钛的TEM照片。FIG. 7 is a TEM photo of nano-titanium oxide obtained by the method of Example 5 provided by the present invention.
图8为本发明提供的由实施例5方法所获得的纳米氧化钛的XRD谱图。Fig. 8 is the XRD spectrum of nano-titanium oxide obtained by the method of Example 5 provided by the present invention.
图9为本发明提供的由实施例6方法所获得的纳米氧化锡的TEM照片。Fig. 9 is a TEM photograph of nano-tin oxide obtained by the method of Example 6 provided by the present invention.
图10为本发明提供的由实施例6方法所获得的纳米氧化锡的XRD谱图。Figure 10 is the XRD spectrum of the nano-tin oxide obtained by the method of Example 6 provided by the present invention.
图11为本发明提供的由实施例7方法所获得的纳米氧化铝的TEM照片。Figure 11 is a TEM photo of the nano-alumina obtained by the method of Example 7 provided by the present invention.
图12为本发明提供的由实施例7方法所获得的纳米氧化铝的XRD谱图。Figure 12 is the XRD spectrum of the nano-alumina obtained by the method of Example 7 provided by the present invention.
具体实施方式Detailed ways
下面结合附图并通过一系列实施例来说明本发明的具体实施方式。The specific implementation manner of the present invention will be described below with reference to the accompanying drawings and through a series of embodiments.
实施例1Example 1
用直接液相沉淀法制备纳米氧化锆的方法,包括以下步骤:The method for preparing nano zirconia by direct liquid phase precipitation method comprises the following steps:
1)配制锆盐乙醇溶液,称取一定量的ZrOCl2·8H2O溶于体积百分比为12%的水中,再加入乙醇配成浓度为0.5mol/L的ZrOCl2乙醇溶液,1) Prepare a zirconium salt ethanol solution, weigh a certain amount of ZrOCl 2 8H 2 O and dissolve it in 12% water by volume, then add ethanol to form a ZrOCl 2 ethanol solution with a concentration of 0.5mol/L,
2)将浓氨水用乙醇稀释,配制成浓度为2mol/L的氨水乙醇溶液,2) Dilute the strong ammonia water with ethanol to prepare a 2mol/L ammonia ethanol solution,
3)在充分搅拌下,将氨水乙醇溶液滴入ZrOCl2乙醇溶液中,生成白色ZrO(OH)2沉淀,反应温度为室温,3) under sufficient stirring, the ammoniacal ethanol solution is dropped into the ZrOCl ethanol solution to generate white ZrO(OH) Precipitation , the reaction temperature is room temperature,
4)滴加至溶液pH为6.8时,反应结束,ZrO(OH)2沉淀完全,4) dropwise until the solution pH is 6.8, the reaction ends, ZrO(OH) Precipitation is complete,
5)将反应液过滤,使ZrO(OH)2沉淀与母液分离,5) the reaction solution is filtered to make ZrO(OH) Precipitation is separated from the mother liquor,
6)用乙醇将ZrO(OH)2沉淀洗涤至无氯离子,6) ZrO(OH) 2 precipitation is washed with ethanol to no chloride ion,
7)将洗涤后的ZrO(OH)2沉淀置于烘箱中,在115℃下烘干2小时,7) Place the washed ZrO(OH) 2 precipitate in an oven and dry it at 115°C for 2 hours,
8)将烘干后的ZrO(OH)2沉淀置于马弗炉中,在600℃下焙烧2小时,即得到白色的分散纳米氧化锆粉体。8) Place the dried ZrO(OH) 2 precipitate in a muffle furnace, and bake it at 600°C for 2 hours to obtain white dispersed nano-zirconia powder.
本实施例的产率为93.8%,分析图1和图2,数据表明,产品的平均粒径为14nm,为单斜晶型。The yield rate of this embodiment is 93.8%. Analysis of Fig. 1 and Fig. 2 shows that the average particle diameter of the product is 14nm, and it is monoclinic crystal form.
实施例2Example 2
用直接液相沉淀法制备掺杂Y2O3的纳米氧化锆的方法,包括以下步骤::The method for preparing doped Y 2 O 3 nanometer zirconia by direct liquid phase precipitation method comprises the following steps::
1)配制金属盐乙醇溶液,称取一定量的ZrOCl2·8H2O和一定量的Y(NO3)3·6H2O,使最终产品的Y2O3摩尔百分比为3%,将它们溶于体积百分比为10%的水中,再加入乙醇配制成含Y(NO3)3的浓度为0.48mol/L的ZrOCl2乙醇溶液,1) Prepare a metal salt ethanol solution, weigh a certain amount of ZrOCl 2 8H 2 O and a certain amount of Y(NO 3 ) 3 6H 2 O, so that the Y 2 O 3 molar percentage of the final product is 3%, and they are Dissolve in 10% water by volume, then add ethanol to prepare a ZrOCl ethanol solution containing Y(NO 3 ) 3 at a concentration of 0.48mol/L,
2)将浓氨水用乙醇稀释,配制成浓度为2mol/L的氨水乙醇溶液,2) Dilute the strong ammonia water with ethanol to prepare a 2mol/L ammonia ethanol solution,
3)在充分搅拌下,将氨水乙醇溶液滴入ZrOCl2-Y(NO3)3乙醇溶液中,生成含Y(OH)3的ZrO(OH)2白色沉淀,反应温度为室温,3) Under full stirring, the ammonia water ethanol solution is dropped into the ZrOCl 2 -Y(NO 3 ) 3 ethanol solution to form a white precipitate of ZrO(OH) 2 containing Y(OH) 3 , and the reaction temperature is room temperature.
4)滴加至溶液pH为6.8时,反应结束,含Y(OH)3的ZrO(OH)2沉淀完全,4) dropwise until the solution pH is 6.8, the reaction ends, and ZrO(OH) containing Y(OH) Precipitation is complete,
5)将反应液过滤,使沉淀物与母液分离,5) filter the reaction solution to separate the precipitate from the mother liquor,
6)用乙醇将沉淀物洗涤至无氯离子,6) the precipitate is washed with ethanol until there is no chloride ion,
7)将洗涤后的沉淀物置于烘箱中在115℃下烘干2小时,7) Place the washed precipitate in an oven and dry it at 115°C for 2 hours,
8)将烘干后的沉淀物置于马弗炉中在700℃下焙烧2小时,即得到分散的掺杂Y2O3的纳米氧化锆粉体。8) Put the dried precipitate in a muffle furnace and bake at 700° C. for 2 hours to obtain dispersed nano-zirconia powder doped with Y 2 O 3 .
本实施例的产率为91.1%,由图3测得产品的平均粒径为19nm。The productive rate of the present embodiment is 91.1%, and the average particle diameter of the product measured by Fig. 3 is 19nm.
实施例3Example 3
用直接液相沉淀法制备掺杂MgO的纳米氧化锆的方法,包括以下步骤::The method for preparing MgO-doped nano zirconia by direct liquid phase precipitation method comprises the following steps::
1)配制金属盐乙醇溶液,称取一定量的ZrOCl2·8H2O和一定量的Mg(NO3)2·6H2O,使最终产品的MgO摩尔百分比为9%,用体积百分比为12%的水将其溶解,然后用乙醇稀释配制成含Mg(NO3)2的浓度为0.45mol/L的ZrOCl2乙醇溶液,1) Prepare a metal salt ethanol solution, weigh a certain amount of ZrOCl 2 8H 2 O and a certain amount of Mg(NO 3 ) 2 6H 2 O, so that the molar percentage of MgO in the final product is 9%, and the volume percentage is 12% % water to dissolve it, and then dilute with ethanol to prepare the ZrOCl ethanol solution containing Mg(NO 3 ) 2 concentration of 0.45mol/L,
2)将浓氨水用乙醇稀释,配制成浓度为2mol/L的氨水乙醇溶液,2) Dilute the strong ammonia water with ethanol to prepare a 2mol/L ammonia ethanol solution,
3)在充分搅拌下,将氨水乙醇溶液滴入ZrOCl2-Mg(NO3)3乙醇溶液中,生成含Mg(OH)2的ZrO(OH)2白色沉淀,反应温度为室温,3) Under full stirring, the ammonia water ethanol solution is dropped into the ZrOCl 2 -Mg(NO 3 ) 3 ethanol solution to form a white precipitate of ZrO(OH) 2 containing Mg(OH) 2 , the reaction temperature is room temperature,
4)滴加至溶液pH为6.8时,反应结束,含Mg(OH)2的ZrO(OH)2沉淀完全, 4 ) when dropping to solution pH is 6.8, reaction finishes, and contains Mg(OH) ZrO(OH) Precipitation is complete,
5)将反应液过滤,使沉淀物与母液分离,5) filter the reaction solution to separate the precipitate from the mother liquor,
6)用乙醇将沉淀物洗涤至无氯离子,6) the precipitate is washed with ethanol until there is no chloride ion,
7)将洗涤后的沉淀物置于烘箱中在115℃下烘干2小时,7) Place the washed precipitate in an oven and dry it at 115°C for 2 hours,
8)将烘干后的沉淀物置于马弗炉在800℃下焙烧2小时,即得到分散的掺杂MgO的纳米氧化锆粉体。8) Put the dried precipitate in a muffle furnace and bake at 800° C. for 2 hours to obtain dispersed MgO-doped nano-zirconia powder.
本实施例的产率为87.2%,由图4测得产品的平均粒径为29nm。The productive rate of the present embodiment is 87.2%, and the average particle diameter of product recorded by Fig. 4 is 29nm.
实施例4Example 4
用直接液相沉淀法制备纳米氧化镁的方法,包括以下步骤:The method for preparing nano magnesium oxide by direct liquid phase precipitation method comprises the following steps:
1)配制镁盐乙醇溶液,称取一定量的MgCl2·6H2O,用体积百分比为6%的水将其溶解,然后用乙醇稀释,配制成浓度为0.2mol/L的MgCl2乙醇溶液,1) Prepare a magnesium salt ethanol solution, weigh a certain amount of MgCl 2 6H 2 O, dissolve it with 6% water by volume, then dilute it with ethanol, and prepare a MgCl 2 ethanol solution with a concentration of 0.2mol/L ,
2)将浓氨水用乙醇稀释,配制成浓度为0.4mol/L的氨水乙醇溶液,2) Dilute the concentrated ammonia water with ethanol to prepare a 0.4mol/L ammonia ethanol solution,
3)在充分搅拌下,向配制好的镁盐乙醇溶液中滴入氨水乙醇溶液,生成氢氧化镁白色沉淀,反应温度为室温,3) under sufficient stirring, drip ammonia water ethanol solution in the prepared magnesium salt ethanol solution, generate magnesium hydroxide white precipitate, and reaction temperature is room temperature,
4)滴加至溶液pH为9.6时,反应结束,氢氧化镁沉淀完全,4) when dropping to solution pH is 9.6, reaction finishes, and magnesium hydroxide precipitation is complete,
5)将反应液过滤,使氢氧化镁沉淀与母液分离,5) the reaction solution is filtered to separate the magnesium hydroxide precipitation from the mother liquor,
6)用乙醇将分离出的氢氧化镁沉淀洗涤至无氯离子,6) washing the separated magnesium hydroxide precipitate with ethanol to no chloride ion,
7)将洗涤后的氢氧化镁沉淀置于烘箱中在115℃下烘干2小时,7) Place the washed magnesium hydroxide precipitate in an oven and dry it at 115°C for 2 hours,
8)将烘干后的氢氧化镁沉淀置于马弗炉中在800℃下焙烧2小时,即获得分散的纳米氧化镁粉体。8) The dried magnesium hydroxide precipitate is placed in a muffle furnace and roasted at 800° C. for 2 hours to obtain dispersed nano magnesium oxide powder.
本实施例的产率为79.2%,分析图5和图6,数据表明,产品的平均粒径为48nm,为立方晶型。The yield rate of this embodiment is 79.2%. Analysis of Fig. 5 and Fig. 6 shows that the average particle diameter of the product is 48nm, and it is a cubic crystal form.
实施例5Example 5
用直接液相沉淀法制备纳米氧化钛的的方法,包括以下步骤:The method for preparing nano-titanium oxide by direct liquid phase precipitation method comprises the following steps:
1)配制钛盐乙醇溶液,称取一定量的TiCl4液体,直接用乙醇稀释,配制成浓度为0.5mol/L的TiCl4乙醇溶液,1) prepare titanium salt ethanol solution, take a certain amount of TiCl Liquid , directly dilute with ethanol, be mixed with the TiCl ethanol solution that concentration is 0.5mol /L,
2)将浓氨水用乙醇稀释,配制成浓度为2mol/L的氨水乙醇溶液,2) Dilute the strong ammonia water with ethanol to prepare a 2mol/L ammonia ethanol solution,
3)在充分搅拌下,向配制好的钛盐乙醇溶液中滴入氨水乙醇溶液,生成白色氢氧化钛沉淀,反应温度为室温,3) under full stirring, drip ammonia water ethanol solution into the prepared titanium salt ethanol solution to generate white titanium hydroxide precipitate, the reaction temperature is room temperature,
4)将混合反应终点的pH值控制在7.2,反应结束,氢氧化钛沉淀完全,4) The pH value at the end point of the mixed reaction is controlled at 7.2, the reaction ends, and the precipitation of titanium hydroxide is complete.
5)将反应液过滤,使氢氧化钛沉淀与母液分离,5) the reaction solution is filtered to separate the titanium hydroxide precipitate from the mother liquor,
6)用乙醇将分离出的氢氧化钛沉淀洗涤至无氯离子,6) washing the separated titanium hydroxide precipitate with ethanol until there is no chloride ion,
7)将洗涤后的氢氧化钛沉淀置于烘干箱内在110℃下烘干2小时,7) Put the washed titanium hydroxide precipitate in a drying box and dry it at 110°C for 2 hours,
8)将烘干后的氢氧化钛沉淀置于马弗炉中在600℃下焙烧2小时,即获得分散的纳米氧化钛粉体。8) Put the dried titanium hydroxide precipitate in a muffle furnace and bake at 600° C. for 2 hours to obtain dispersed nano-titanium oxide powder.
本实施例的产率为91.5%,分析图7和图8,数据表明,产品的平均粒径为28nm,为锐钛矿和金红石混合晶型(以锐钛矿为主)。The yield rate of this embodiment is 91.5%. Analysis of Fig. 7 and Fig. 8 shows that the average particle size of the product is 28nm, and it is a mixed crystal form of anatase and rutile (mainly anatase).
实施例6Example 6
用直接液相沉淀法制备纳米氧化锡的的方法,包括以下步骤:The method for preparing nano-tin oxide by direct liquid phase precipitation method may further comprise the steps:
1)配制锡盐乙醇溶液,称取一定量的SnCl4·5H2O,用体积百分比为8%的水将其溶解,然后用乙醇稀释,配制成浓度为0.5mol/L的SnCl4乙醇溶液,1) Prepare tin salt ethanol solution, weigh a certain amount of SnCl 4 5H 2 O, dissolve it with 8% water by volume, then dilute it with ethanol, and prepare a SnCl 4 ethanol solution with a concentration of 0.5mol/L ,
2)将浓氨水用乙醇稀释,配制成浓度为2mol/L的氨水乙醇溶液,2) Dilute the strong ammonia water with ethanol to prepare a 2mol/L ammonia ethanol solution,
3)在充分搅拌下,向配制好的SnCl4的乙醇溶液中滴入氨水乙醇溶液,生成氢氧化锡沉淀,反应温度为室温,3) under sufficient agitation, in the ethanolic solution of prepared SnCl , drip ammonia water ethanol solution, generate tin hydroxide precipitation, and reaction temperature is room temperature,
4)将混合液反应终点的pH值控制在6.8,反应结束,氢氧化锡沉淀完全,4) the pH value of the reaction end point of the mixed solution is controlled at 6.8, the reaction ends, and the precipitation of tin hydroxide is complete,
5)将反应液过滤,使氢氧化锡沉淀与母液分离,5) the reaction solution is filtered to separate the tin hydroxide precipitation from the mother liquor,
6)用乙醇将分离出的氢氧化锡沉淀洗涤至无氯离子,6) washing the isolated tin hydroxide precipitate with ethanol to no chloride ion,
7)将洗涤后的氢氧化锡沉淀置于烘箱内在110℃下烘干2小时,7) Place the washed tin hydroxide precipitate in an oven and dry it at 110°C for 2 hours,
8)将烘干后的氢氧化锡沉淀置于马弗炉中在600℃下焙烧2小时,即获得分散的纳米氧化锡粉体。8) Put the dried tin hydroxide precipitate in a muffle furnace and bake at 600° C. for 2 hours to obtain dispersed nano tin oxide powder.
本实施例的产率为92.5%,分析图9和图10,数据表明,产品的平均粒径为11nm,为四方晶型。The yield rate of this embodiment is 92.5%. Analysis of Fig. 9 and Fig. 10 shows that the average particle size of the product is 11nm, and it is tetragonal crystal form.
实施例7Example 7
用直接液相沉淀法制备纳米氧化铝的方法,包括以下步骤:The method for preparing nano-alumina by direct liquid phase precipitation method comprises the following steps:
1)配制铝盐乙醇溶液,称取一定量的AlCl3·6H2O,用体积百分比为15%的水将其溶解,然后用乙醇稀释,配制成浓度为0.5mol/L的AlCl3的乙醇溶液,1) Prepare aluminum salt ethanol solution, weigh a certain amount of AlCl 3 6H 2 O, dissolve it with 15% water by volume, then dilute it with ethanol, and prepare ethanol with a concentration of 0.5mol/L AlCl 3 solution,
2)将浓氨水用乙醇稀释,配制成浓度为1.5mol/L的氨水乙醇溶液,2) Dilute the strong ammonia water with ethanol to prepare a 1.5mol/L ammonia ethanol solution,
3)在充分搅拌下,向配制好的AlCl3的乙醇溶液中滴入氨水乙醇溶液,生成氢氧化铝沉淀,反应温度为室温,3) under sufficient stirring, in the ethanolic solution of prepared AlCl3 , drop ammoniacal ethanol solution, generate aluminum hydroxide precipitation, reaction temperature is room temperature,
4)控制反应终点的pH值为7.0,反应结束,氢氧化铝沉淀完全,4) the pH value of the control reaction end point is 7.0, the reaction ends, and the precipitation of aluminum hydroxide is complete,
5)将反应液过滤,使氢氧化铝沉淀与母液分离,5) the reaction solution is filtered to separate the aluminum hydroxide precipitation from the mother liquor,
6)用乙醇将分离出的氢氧化铝沉淀洗涤至无氯离子,6) washing the separated aluminum hydroxide precipitate with ethanol to no chloride ion,
7)将洗涤后的氢氧化铝沉淀置于烘箱内在110℃下烘干2小时,7) Place the washed aluminum hydroxide precipitate in an oven and dry it at 110°C for 2 hours,
8)将烘干后的氢氧化铝沉淀置于马弗炉在800℃下焙烧2小时,即获得松散的纳米氧化铝粉体。8) Put the dried aluminum hydroxide precipitate in a muffle furnace and bake at 800° C. for 2 hours to obtain loose nano-alumina powder.
本实施例的产率为95.2%,分析图11和图12,数据表明,产品的平均粒径为5nm,为γ-Al2O3。The yield rate of this example is 95.2%. Analysis of Figure 11 and Figure 12 shows that the average particle size of the product is 5nm, which is γ-Al 2 O 3 .
在上述各制备过程中,滤液包括母液经过蒸馏可回收乙醇,同时得到氯化铵副产品,基本上实现零排放,可称为绿色化学合成方法。In the above-mentioned preparation processes, ethanol can be recovered by distilling the filtrate including the mother liquor, and ammonium chloride by-product can be obtained at the same time, which basically realizes zero discharge, which can be called a green chemical synthesis method.
Claims (14)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200410021008 CN1259240C (en) | 2004-01-06 | 2004-01-06 | Method for preparing nanometer metal oxides by direct liquid phase precipitation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200410021008 CN1259240C (en) | 2004-01-06 | 2004-01-06 | Method for preparing nanometer metal oxides by direct liquid phase precipitation |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1611448A CN1611448A (en) | 2005-05-04 |
CN1259240C true CN1259240C (en) | 2006-06-14 |
Family
ID=34763335
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200410021008 Expired - Fee Related CN1259240C (en) | 2004-01-06 | 2004-01-06 | Method for preparing nanometer metal oxides by direct liquid phase precipitation |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1259240C (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103771512B (en) * | 2014-01-14 | 2015-07-01 | 辽宁科技大学 | Preparation method of metallic oxide nanometer powder |
CN104556224A (en) * | 2014-12-15 | 2015-04-29 | 江苏省陶瓷研究所有限公司 | Improved preparation method of zirconium dioxide micropowder |
CN104815634A (en) * | 2015-04-02 | 2015-08-05 | 吴肖颜 | Preparation method of TiO2-ZrO2 composite nanopowder |
CN105327685B (en) * | 2015-09-15 | 2019-05-17 | 湖州欧美新材料有限公司 | A kind of preparation method of arsenic removal material |
CN105923651B (en) * | 2016-04-21 | 2017-11-10 | 常州大学 | A kind of new method for preparing dental colored nano-zirconia powder |
CN106495193A (en) * | 2016-10-31 | 2017-03-15 | 航天推进技术研究院 | Based on the method that ethanol auxiliary agent extracts aluminum oxide in flyash using ammonium sulfate method |
CN107267846B (en) * | 2017-05-12 | 2019-07-26 | 江苏金基特钢有限公司 | A kind of Al2O3The preparation method of particle reinforced iron matrix composites |
CN109534378A (en) * | 2018-11-27 | 2019-03-29 | 东华大学 | A kind of preparation method of anti-hard aggregation nano alumina particles |
CN111135794B (en) * | 2020-01-13 | 2022-09-23 | 唐山师范学院 | Alumina modified expanded graphite adsorbent and its preparation method and application |
CN111792667A (en) * | 2020-05-25 | 2020-10-20 | 先导薄膜材料有限公司 | Preparation method of hydroxide nano powder |
-
2004
- 2004-01-06 CN CN 200410021008 patent/CN1259240C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
CN1611448A (en) | 2005-05-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102030352B (en) | A method for preparing nanomaterials | |
CN1184167C (en) | Preparation method of composite oxide powder and composite oxide powder | |
CN1630616A (en) | Barium titanate and production process thereof | |
CN100503450C (en) | A kind of preparation method of high-purity nano zirconia powder | |
CN101062780A (en) | Nano titanium oxide and mechanical force chemical reaction preparation method for its composite powder | |
CN1259240C (en) | Method for preparing nanometer metal oxides by direct liquid phase precipitation | |
CN1301911C (en) | Method for producing powder of ITO comprising indium oxide anty tin dissolved therein and method for producing ITO target | |
CN101044092A (en) | Fine-particled alkaline-earth titanates and method for the production thereof using titan oxide particles | |
CN110407238A (en) | A kind of method that crystal seed method prepares flaky alpha-alumina crystals | |
CN113797919A (en) | High-exposure {001} crystal face bismuth niobate titanate nanosheet piezoelectric catalyst and preparation method and application thereof | |
CN1666956A (en) | A kind of synthesis method of nanometer size mordenite | |
CN1267356C (en) | Method for preparing barium carbonate powder | |
CN105883910A (en) | A kind of preparation method and product of perovskite SrTiO3 porous nanoparticles | |
CN101050118A (en) | Method for preparing ceramics powder body of perovskite | |
CN1038629A (en) | Preparation method with the submicronic powders of yttria-stabilized zirconia | |
CN105727922B (en) | A kind of Li adulterates SrTiO3The preparation method and product of ten octahedron nanometer particles | |
CN1283587C (en) | Process for preparing tetra phase barium titanate powder | |
CN1159226C (en) | Preparation method of nano-rare earth oxides by solid-state chemical reaction by ball milling | |
CN110342572B (en) | Preparation method of anatase type nano titanium dioxide | |
CN1412117A (en) | Method for preparing indium tin oxide powder by aqueous solution method | |
CN1800099A (en) | Barium titanium oxalate power and method for manufacturing titanium type perovskite ceramic raw material powder | |
CN102963925A (en) | Method for preparing nanometer n-zinc titanate spinel by virtue of taking zinc-titanium hydrotalcite as precursor | |
CN1868949A (en) | Preparation method of nanometer grade indium tin oxide composite powder | |
CN1273384C (en) | Preparation of nano aluminum oxide without hard coacervation | |
CN109133161B (en) | A kind of preparation method of strontium titanate nanoparticles |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20060614 Termination date: 20100208 |