CN1260134C - Method for preparing zirconium oxide micro powder - Google Patents
Method for preparing zirconium oxide micro powder Download PDFInfo
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- CN1260134C CN1260134C CN 200410064520 CN200410064520A CN1260134C CN 1260134 C CN1260134 C CN 1260134C CN 200410064520 CN200410064520 CN 200410064520 CN 200410064520 A CN200410064520 A CN 200410064520A CN 1260134 C CN1260134 C CN 1260134C
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- 238000000034 method Methods 0.000 title claims abstract description 37
- 239000000843 powder Substances 0.000 title claims abstract description 24
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 title description 2
- 229910001928 zirconium oxide Inorganic materials 0.000 title description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims abstract description 64
- 239000002244 precipitate Substances 0.000 claims abstract description 45
- CMOAHYOGLLEOGO-UHFFFAOYSA-N oxozirconium;dihydrochloride Chemical compound Cl.Cl.[Zr]=O CMOAHYOGLLEOGO-UHFFFAOYSA-N 0.000 claims abstract description 29
- 235000011114 ammonium hydroxide Nutrition 0.000 claims abstract description 14
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000975 co-precipitation Methods 0.000 claims abstract description 8
- 238000002425 crystallisation Methods 0.000 claims abstract description 6
- 230000008025 crystallization Effects 0.000 claims abstract description 6
- 239000000243 solution Substances 0.000 claims description 75
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 238000006460 hydrolysis reaction Methods 0.000 claims description 18
- 230000007062 hydrolysis Effects 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 15
- 238000009835 boiling Methods 0.000 claims description 14
- 238000001556 precipitation Methods 0.000 claims description 14
- 239000008367 deionised water Substances 0.000 claims description 12
- 229910021641 deionized water Inorganic materials 0.000 claims description 12
- 239000011164 primary particle Substances 0.000 claims description 11
- IVORCBKUUYGUOL-UHFFFAOYSA-N 1-ethynyl-2,4-dimethoxybenzene Chemical compound COC1=CC=C(C#C)C(OC)=C1 IVORCBKUUYGUOL-UHFFFAOYSA-N 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 10
- 229910052726 zirconium Inorganic materials 0.000 claims description 10
- -1 zirconium ions Chemical class 0.000 claims description 10
- 239000000047 product Substances 0.000 claims description 8
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 238000001354 calcination Methods 0.000 claims description 7
- 239000013078 crystal Substances 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 6
- 238000004062 sedimentation Methods 0.000 claims description 5
- OBOSXEWFRARQPU-UHFFFAOYSA-N 2-n,2-n-dimethylpyridine-2,5-diamine Chemical compound CN(C)C1=CC=C(N)C=N1 OBOSXEWFRARQPU-UHFFFAOYSA-N 0.000 claims description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- SIWVEOZUMHYXCS-UHFFFAOYSA-N oxo(oxoyttriooxy)yttrium Chemical compound O=[Y]O[Y]=O SIWVEOZUMHYXCS-UHFFFAOYSA-N 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 229910001961 silver nitrate Inorganic materials 0.000 claims description 4
- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical compound [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 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 2
- 230000032683 aging Effects 0.000 claims description 2
- 238000005119 centrifugation Methods 0.000 claims description 2
- 238000000227 grinding Methods 0.000 claims description 2
- 239000007921 spray Substances 0.000 claims description 2
- 238000001694 spray drying Methods 0.000 claims description 2
- 239000013589 supplement Substances 0.000 claims description 2
- 229910021529 ammonia Inorganic materials 0.000 claims 1
- 238000010899 nucleation Methods 0.000 abstract description 7
- 230000006911 nucleation Effects 0.000 abstract description 7
- 150000003754 zirconium Chemical class 0.000 abstract description 4
- 238000002360 preparation method Methods 0.000 abstract description 3
- 238000001935 peptisation Methods 0.000 abstract 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 230000002269 spontaneous effect Effects 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000000499 gel Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
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Abstract
Description
技术领域technical field
本发明涉及一种制备氧化锆超细粉末的方法,用该方法制备的粉末具有均匀的颗粒分布,致密的结构,主要用于制备高强度、高密度的结构陶瓷。The invention relates to a method for preparing zirconia superfine powder. The powder prepared by the method has uniform particle distribution and compact structure, and is mainly used for preparing high-strength and high-density structural ceramics.
背景技术Background technique
已有的制备氧化锆超细粉末的方法有:均匀沉淀法、共沉淀法、加热水解法等。Existing methods for preparing zirconia ultrafine powder include: uniform precipitation method, co-precipitation method, heating hydrolysis method, etc.
均匀沉淀法:把氯氧化锆与尿素溶液混合均匀,将其加热到70℃以上,尿素发生分解,分解反应方程式如下:Uniform precipitation method: Mix zirconium oxychloride and urea solution evenly, heat it above 70°C, urea will decompose, and the decomposition reaction equation is as follows:
随着尿素的不断分解,产生的氨水使溶液的PH值不断升高,到一定程度,溶液突然黏度变大,产生沉淀,是由于长大过程的不可控制性,最后形成的沉淀是一种空间网格状凝胶,过滤和洗涤非常困难,很难用于大规模生产。With the continuous decomposition of urea, the ammonia water produced will continuously increase the pH value of the solution. To a certain extent, the viscosity of the solution will suddenly increase, and precipitation will occur due to the uncontrollability of the growth process. The final precipitation is a kind of space. Grid-like gels are very difficult to filter and wash, making them difficult to use in large-scale production.
共沉淀法:即先将锆盐在水中制成一定浓度的溶液,称为溶液B;再将氨水稀释到一定浓度,称为溶液A。采用正滴法(即将溶液A加入到溶液B中)或反滴法(将溶液B加入到溶液A中),进行反应,得到凝胶状沉淀。将这种凝胶洗涤、煅烧得到超细粉末,此方法的缺点是颗粒度大小不均匀、成分分布不均匀。特别是反滴法,在很短的时间内形成大量核心,成核和长大基本上是在瞬间、交叉完成的,没有办法将成核和长大完全分开。由此可以推断,一次颗粒的大小也是不均匀的,并且一次颗粒和比表面积的大小控制基本只能依靠煅烧温度和时间来控制,延长煅烧时间在经济上是不合算的,一般情况下,控制煅烧温度是唯一手段。其后果是造成颗粒结晶的不完善,一次颗粒内部存在孔洞。Co-precipitation method: first make a solution of zirconium salt in water to a certain concentration, called solution B; then dilute ammonia water to a certain concentration, called solution A. Using the forward drop method (that is, adding solution A to solution B) or the reverse drop method (adding solution B to solution A), the reaction is carried out to obtain a gel-like precipitate. The gel is washed and calcined to obtain ultrafine powder. The disadvantage of this method is that the particle size is uneven and the composition distribution is uneven. Especially in the reverse drop method, a large number of nuclei are formed in a short period of time, and the nucleation and growth are basically instantaneous and cross-over, and there is no way to completely separate the nucleation and growth. It can be inferred from this that the size of primary particles is also uneven, and the size control of primary particles and specific surface area can only be controlled by calcination temperature and time. Prolonging calcination time is economically uneconomical. In general, control Calcination temperature is the only means. The consequence is that the crystallization of the particles is not perfect, and there are holes inside the primary particles.
水解法:即将氯氧化锆水溶液加热到一定温度,使氯化氢不断挥发出来,在PH值升高到一定程度后,溶液中自发成核形成结晶核心,制备的超细粉末大小不一致,另外就是其加热时间长,通常需要5-10天,耗费大量能源,成本高。Hydrolysis method: Heating the zirconium oxychloride aqueous solution to a certain temperature to continuously volatilize hydrogen chloride. After the pH value rises to a certain level, the solution spontaneously nucleates to form a crystal core, and the prepared ultrafine powder is inconsistent in size. In addition, it is heated It takes a long time, usually takes 5-10 days, consumes a lot of energy, and the cost is high.
发明内容Contents of the invention
本发明的目的是提供一种制备氧化锆超细粉末的方法,用该方法制备出的氧化锆一次颗粒大小可控、均匀一致,品质高且制备成本低、效率高。The object of the present invention is to provide a method for preparing zirconia ultrafine powder, the zirconia primary particles prepared by the method are controllable, uniform, high in quality, low in preparation cost and high in efficiency.
本发明的目的是这样实现的:一种制备氧化锆超细粉末的方法,其特征在于:利用共沉淀的方法使氨水和氯氧化锆在溶液中反应,产生的沉淀在经过洗涤、过滤后,加入到氯氧化锆溶液中使沉淀产生胶溶,把溶胶作为结晶核心,连续慢慢加入氯氧化锆溶液,加热使溶液进一步水解产生沉淀,将水解物洗涤、煅烧、研磨,制备出一次颗粒大小可控、均匀一致的纳米氧化锆超细粉末。The object of the present invention is achieved like this: a kind of method for preparing zirconia superfine powder, is characterized in that: utilize the method for co-precipitation to make ammoniacal liquor and zirconium oxychloride react in solution, the precipitate that produces is after washing, filtering, Add it to the zirconium oxychloride solution to peptize the precipitate, use the sol as the crystallization core, add the zirconium oxychloride solution continuously and slowly, heat the solution to further hydrolyze to produce a precipitate, wash, calcinate, and grind the hydrolyzate to prepare a primary particle size Controllable and uniform nano-zirconia ultrafine powder.
本发明的目的还可以这样实现:上述制备氧化锆超细粉末的方法,其特征在于:依次按下述步骤操作:The purpose of the present invention can also be achieved like this: the above-mentioned method for preparing zirconia ultrafine powder is characterized in that: operate according to the following steps successively:
i)将氨水与氯氧化锆分别制备成均匀溶液A和B,将溶液B加入到溶液A中,使PH=7,得到氢氧化锆的沉淀;i) Aqueous ammonia and zirconium oxychloride are prepared into homogeneous solutions A and B respectively, and solution B is added to solution A to make PH=7 to obtain precipitation of zirconium hydroxide;
ii)将沉淀充分洗涤、过滤,加入到氯氧化锆溶液中,加热至沸腾,使它们充分反应,发生胶溶;ii) fully washing and filtering the precipitate, adding it to the zirconium oxychloride solution, and heating to boiling to make them fully react and peptize;
iii)用离心的方法将溶胶和未胶溶的沉淀物分离,得到均匀的氢氧化锆溶胶;iii) separating the sol and the unpeptized precipitate by centrifugation to obtain a uniform zirconium hydroxide sol;
iv)将此溶胶作为水解反应的晶种,加热到80-105℃之间,连续慢慢加入氯氧化锆溶液,补充水解消耗的锆离子,最后得到粒度均匀、大小可控的氢氧化锆沉淀物,iv) Use the sol as the seed crystal of the hydrolysis reaction, heat to 80-105°C, continuously and slowly add zirconium oxychloride solution to supplement the zirconium ions consumed by hydrolysis, and finally obtain zirconium hydroxide precipitation with uniform particle size and controllable size things,
v)将沉淀物洗涤、煅烧、研磨、喷雾干燥得到纳米氧化锆超细粉末。v) Washing, calcining, grinding, and spray drying the precipitate to obtain ultrafine nano zirconia powder.
本发明与现有技术相比具有以下优点:本发明将共沉淀法与加热水解法相结合,取长补短,从而解决了结晶成核和长大无法控制,一次颗粒的大小不均匀的问题。在本发明中,加入外来结晶核心后,不再发生自发成核,晶核的数量是一定的,最终颗粒的大小可通过水解时间的长短来控制。此方法的另一优点是依靠加入外来晶核代替自发成核,节省了自发成核的孕育时间,把直接水解法所需要的时间缩短到原来的1/2,大大提高了效率。Compared with the prior art, the present invention has the following advantages: the present invention combines the co-precipitation method and the heating hydrolysis method to learn from each other, thereby solving the problems of uncontrollable crystal nucleation and growth and uneven primary particle size. In the present invention, after adding foreign crystal cores, no spontaneous nucleation occurs, the number of crystal nuclei is constant, and the final particle size can be controlled by the length of hydrolysis time. Another advantage of this method is that it relies on the addition of foreign crystal nuclei instead of spontaneous nucleation, which saves the incubation time of spontaneous nucleation, shortens the time required for direct hydrolysis to 1/2 of the original, and greatly improves the efficiency.
附图说明Description of drawings
附图为本发明氧化锆超细粉末的X射线衍射图谱Accompanying drawing is the X-ray diffraction pattern of zirconia ultrafine powder of the present invention
具体实施方式Detailed ways
本发明主要针对现有技术的缺点,将共沉淀法与加热水解法相结合,取长补短,提出了一种制备高品质低成本的超细氧化锆粉末的方法。其基本工艺过程是,利用共沉淀的方法使氨水和锆盐在溶液中反应,产生的沉淀在经过过滤、洗涤后,加入氯氧化锆使沉淀产生胶溶,把溶胶作为结晶核心,连续慢慢加入氯氧化锆溶液,加热使溶液进一步水解产生沉淀,将水解物洗涤、煅烧、研磨,制备出一次颗粒大小可控、均匀一致的氧化锆颗粒。关键步骤有:1)用加氨水的方法使锆盐溶液发生沉淀,洗涤、过滤沉淀物;2)将干净的沉淀物加入氯氧化锆溶液中,加热使之发生胶溶;3)离心沉降,把没有胶溶的沉淀物去掉,得到均匀的溶胶;4)连续慢慢加入氯氧化锆溶液,将上述溶液加热水解,制备出大小均匀的纳米氧化锆颗粒。The present invention mainly aims at the shortcomings of the prior art, combines the co-precipitation method and the heating hydrolysis method, learns from each other, and proposes a method for preparing ultrafine zirconia powder with high quality and low cost. The basic process is to make ammonia water and zirconium salt react in the solution by co-precipitation method, and after the resulting precipitate is filtered and washed, zirconium oxychloride is added to peptize the precipitate, and the sol is used as the crystallization core, continuously and slowly Zirconium oxychloride solution is added, heated to further hydrolyze the solution to produce precipitation, and the hydrolyzate is washed, calcined, and ground to prepare uniform zirconia particles with a controllable primary particle size. The key steps are: 1) Precipitate the zirconium salt solution by adding ammonia water, wash and filter the precipitate; 2) Add the clean precipitate into the zirconium oxychloride solution, heat to make it peptized; 3) Centrifugal sedimentation, Remove the unpeptized precipitate to obtain a uniform sol; 4) continuously and slowly add a zirconium oxychloride solution, heat and hydrolyze the above solution, and prepare nano zirconium oxide particles of uniform size.
根据目前研究,在氧化锆中掺杂氧化钇等其它氧化物可获得稳定的四方相结构的氧化锆,可提高氧化锆的材料强度和断裂韧性,故可在氧化锆溶液中加入氧化钇溶液制成混合溶液制备高性能的纳米氧化锆超细粉末。According to current research, doping yttrium oxide and other oxides in zirconia can obtain zirconia with a stable tetragonal phase structure, which can improve the material strength and fracture toughness of zirconia, so yttrium oxide solution can be added to zirconia solution to produce Prepare high-performance nano-zirconia ultrafine powder by forming a mixed solution.
实施例1Example 1
依次按下述步骤操作:Follow the steps below in order:
i)将氯氧化锆制备成浓度1.0M的溶液B,将14M的氨水稀释成1.0M的溶液A,在不断搅拌条件下,将溶液A加入到溶液B中,产生氢氧化锆的沉淀,到PH=7.0中止,老化12小时;i) Prepare zirconium oxychloride into solution B with a concentration of 1.0M, dilute 14M ammonia water into solution A of 1.0M, and add solution A to solution B under constant stirring conditions to produce precipitation of zirconium hydroxide. Stop at PH=7.0, aging for 12 hours;
ii)将沉淀用去离子水充分洗涤,直到用硝酸银检测不到白色沉淀为止,得到沉淀C;取氯氧化锆溶解在去离子水中,得到溶液D;把沉淀C加入到溶液D中,加水到锆离子的浓度达到1.0M,在搅拌条件下,加热到沸腾,直到全部沉淀发生胶溶;ii) Wash the precipitate fully with deionized water until no white precipitate can be detected with silver nitrate, and obtain precipitate C; dissolve zirconium oxychloride in deionized water to obtain solution D; add precipitate C to solution D, add water When the concentration of zirconium ions reaches 1.0M, heat to boiling under stirring conditions until all the precipitates are peptized;
iii)离心沉降,分离出未胶溶的沉淀物:把溶胶装入密闭容器,在分离因数3600的离心机上沉降1小时,得到溶胶E;iii) Centrifugal sedimentation to separate the unpeptized precipitate: put the sol into a closed container and settle for 1 hour on a centrifuge with a separation factor of 3600 to obtain Sol E;
iv)将溶胶E加热到沸腾,不断缓慢加入溶液B,保持加入量与水解量相等,在达到预期的一次颗粒大小后,停止加入,保持沸腾,直到溶液中的锆离子水解完毕;在加热过程中,水分不断蒸发,需要经常补充水,使溶液体积保持不变;iv) Heat sol E to boiling, continuously and slowly add solution B, keep the amount added equal to the amount of hydrolysis, stop adding after reaching the expected primary particle size, and keep boiling until the hydrolysis of zirconium ions in the solution is completed; during the heating process In the medium, the water evaporates continuously, and water needs to be replenished frequently to keep the volume of the solution constant;
v)将水解产物用去离子水洗涤、过滤,800℃×5h煅烧,得到颗粒状氧化锆,用球磨机将颗粒氧化锆加水研磨,粒度达到0.2-0.3μm,喷雾干燥得到成品。v) The hydrolyzed product is washed with deionized water, filtered, and calcined at 800° C. for 5 hours to obtain granular zirconia. Grind the granular zirconia with water to a particle size of 0.2-0.3 μm with a ball mill, and spray dry to obtain a finished product.
实施例2Example 2
依次按下述步骤操作:Follow the steps below in order:
i)按下述比例制备氯氧化锆和氯化钇混合溶液和制备氨水溶液:将322克氯氧化锆与可折合为氧化钇6.4克的43克氯化钇溶液,混合制备成浓度1.0M的溶液B,将14M的氨水稀释成1.0M的溶液A,在不断搅拌条件下,将溶液A加入到溶液B中,产生氢氧化锆的沉淀,到PH=7.0中止,老化12小时;i) Prepare zirconium oxychloride and yttrium chloride mixed solution and prepare ammonia solution according to the following ratio: 322 grams of zirconium oxychloride and 43 grams of yttrium chloride solution that can be converted to 6.4 grams of yttrium oxide are mixed and prepared into a concentration of 1.0M For solution B, dilute 14M ammonia water into 1.0M solution A, add solution A to solution B under constant stirring conditions, and produce zirconium hydroxide precipitation, stop when pH=7.0, and age for 12 hours;
ii)将沉淀用去离子水充分洗涤,直到用硝酸银检测不到白色沉淀为止,得到沉淀C;取氯氧化锆966克溶解在去离子水中,得到溶液D;把沉淀C加入到溶液D中,加水到锆离子的浓度达到1.0M,在搅拌条件下,加热到沸腾,直到全部沉淀发生胶溶;ii) Wash the precipitate fully with deionized water until no white precipitate can be detected with silver nitrate, and obtain precipitate C; dissolve 966 grams of zirconium oxychloride in deionized water to obtain solution D; add precipitate C to solution D , add water until the concentration of zirconium ions reaches 1.0M, and heat to boiling under stirring conditions until all the precipitates are peptized;
iii)离心沉降,分离出未胶溶的沉淀物:把溶胶装入密闭容器,在分离因数3600的离心机上沉降1小时,得到溶胶E;iii) Centrifugal sedimentation to separate the unpeptized precipitate: put the sol into a closed container and settle for 1 hour on a centrifuge with a separation factor of 3600 to obtain Sol E;
iv)将溶胶E加热到沸腾,不断缓慢加入溶液B,保持加入量与水解量相等,在达到预期的一次颗粒大小后,停止加入,保持沸腾,直到溶液中的锆离子水解完毕;在加热过程中,水分不断蒸发,需要经常补充水,使溶液体积保持不变;iv) Heat sol E to boiling, continuously and slowly add solution B, keep the amount added equal to the amount of hydrolysis, stop adding after reaching the expected primary particle size, and keep boiling until the hydrolysis of zirconium ions in the solution is completed; during the heating process In the medium, the water evaporates continuously, and water needs to be replenished frequently to keep the volume of the solution constant;
v)将水解产物用去离子水洗涤、过滤,800℃×5h煅烧,得到颗粒状氧化锆,用球磨机将颗粒氧化锆加水研磨,粒度达到0.2-0.3μm,喷雾干燥得到成品;v) The hydrolyzed product is washed with deionized water, filtered, and calcined at 800°C for 5 hours to obtain granular zirconia, which is ground with water in a ball mill until the particle size reaches 0.2-0.3 μm, and spray-dried to obtain a finished product;
煅烧后,氧化锆颗粒的XRD如附图所示,全部由四方相构成;将喷雾干燥的粉体在200Mpa下冷等静压,1500℃烧结2小时,检测密度为6.07。After calcination, the XRD of the zirconia particles is shown in the attached figure, all of which are composed of tetragonal phases; the spray-dried powder is cold isostatically pressed at 200Mpa, sintered at 1500°C for 2 hours, and the detected density is 6.07.
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| CN1321066C (en) * | 2005-08-12 | 2007-06-13 | 安泰科技股份有限公司 | A kind of manufacturing method of zirconia nanopowder material |
| CN103771513B (en) * | 2014-01-25 | 2016-02-17 | 东莞市地大纳米材料有限公司 | A kind of high dispersion nanometer oxide zirconium raw powder's production technology |
| CN104529440B (en) * | 2015-02-02 | 2016-10-05 | 福建省智胜矿业有限公司 | The high abrasion zirconia ceramics material powder of composite crystal phase structure and preparation technology thereof |
| CN105272226A (en) * | 2015-10-28 | 2016-01-27 | 金业新材料科技(昆山)有限公司 | Preparation method of composite stabilized zirconia feed for injection molding by thermal release |
| EP3502060B1 (en) * | 2016-12-22 | 2022-01-05 | Daiichi Kigenso Kagaku Kogyo Co., Ltd. | Zirconia sol and method for manufacturing same |
| CN106830918B (en) * | 2017-03-10 | 2020-05-29 | 南通通州湾新材料科技有限公司 | Preparation of MgAl by temperature-changing pressure-changing hydrothermal method2O4Complex phase nano powder method and its application |
| CN108529672A (en) * | 2018-04-03 | 2018-09-14 | 苏州化联高新陶瓷材料有限公司 | Chemical coprecipitation produces yttrium stable zirconium oxide spherical powder production technology used for hot spraying |
| CN111072383A (en) * | 2019-12-18 | 2020-04-28 | 常熟理工学院 | Preparation method of high-performance composite zirconium oxide powder |
| CN112174662A (en) * | 2020-10-28 | 2021-01-05 | 中科传感技术(青岛)研究院 | Method for preparing zirconium-aluminum composite ball by titration method |
| CN113058447B (en) * | 2021-04-23 | 2022-11-08 | 常州苏南水环境研究院有限公司 | Preparation method of porous flat ceramic nanofiltration body based on silicon-zirconium sol |
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