CN109336618A - 一种高效制备高分散氧化锆陶瓷粉的方法 - Google Patents
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Abstract
本发明公开一种高效制备高分散氧化锆陶瓷粉的方法,包括如下步骤:步骤一、将化学共沉淀得到的氢氧化锆洗涤并压制成固态滤饼;步骤二、将滤饼与去离子水混合,进行球磨;步骤三、将球磨后浆料滤出,并烘干;步骤四、将烘干后物料进窑炉煅烧,得到氧化锆粉体。本发明方法可提高球磨效率,大大减少磨损引入的杂质,煅烧所需温度可降低至700~900℃,节省能源并利于提高生产效率;有效去除团聚,避免了对氧化锆球磨,减少其因外力作用造成的t→m相变;适用范围广。
Description
技术领域
本发明涉及材料技术领域,具体涉及一种高效制备高分散氧化锆陶瓷粉的方法。
背景技术
制造高性能陶瓷材料对所用的粉料有很高的要求,除对粉料的化学组成和相组成要求准确、均匀、杂质含量低之外,对粉料中的颗粒形状和尺寸有严格要求。大致可归纳如下:
1)颗粒尺寸小;
2)颗粒尺寸分布范围窄;
3)颗粒形状最好为球形或等轴粒状;
4)颗粒之间无团聚或团聚程度小。
目前氧化锆陶瓷的粉体大多使用化学共沉淀法生产,但其易产生团聚,造成粒度分布宽等问题。
发明内容
本发明的目的是提供一种高效制备高分散氧化锆陶瓷粉的方法,以解决现有技术的不足。
本发明采用以下技术方案:
一种高效制备高分散氧化锆陶瓷粉的方法,包括如下步骤:
步骤一、将化学共沉淀得到的氢氧化锆洗涤并压制成固态滤饼;
步骤二、将滤饼与去离子水混合,进行球磨;
步骤三、将球磨后浆料滤出,并烘干;
步骤四、将烘干后物料进窑炉煅烧,得到氧化锆粉体。
进一步地,步骤二滤饼与去离子水按质量比1:1~2:1混合。
进一步地,步骤二以280~350r/min球磨时间1~2h。
进一步地,步骤四700~900℃煅烧3~5h。
本发明的有益效果:
1、本发明通过对上游段氢氧化锆直接进行球磨细化,由于氢氧化锆硬度远小于氧化锆,故可提高球磨效率,且球磨时间的减少对于磨损引入的杂质大大减少;由于在煅烧前就对其进行了细化、表面改性,其煅烧所需温度可降低至700~900℃,节省能源并利于提高生产效率。
2、化学共沉淀法制备氧化锆粉体,沉淀生成及洗涤段最易发生团聚,而本发明直接作用在洗涤之后,可有效地去除团聚;避免了直接对氧化锆球磨,减少其因外力作用造成的t→m相变。
3、本发明方法适用于大多稳定剂稳定的氧化锆粉,如氧化钇、氧化镁、氧化铈、氧化钙等,适用范围广。
附图说明
图1为本发明方法与现有方法对比。
图2为实施例1中粉料在球磨前、球磨后、煅烧后的粒度分布。
图3为实施例2中粉料在球磨前、球磨后、煅烧后的粒度分布。
图4为按图1中现有方法制得的3Y氧化锆粉煅烧后、球磨后的粒度分布。
具体实施方式
下面结合实施例和附图对本发明做更进一步地解释。下列实施例仅用于说明本发明,但并不用来限定本发明的实施范围。
一种高效制备高分散氧化锆陶瓷粉的方法,包括如下步骤:
步骤一、将化学共沉淀得到的氢氧化锆洗涤并压制成固态滤饼;
步骤二、将滤饼与去离子水按质量比1:1~2:1混合,以280~350r/min球磨1~2h;
步骤三、将球磨后浆料滤出,并烘干;
步骤四、将烘干后物料进窑炉700~900℃煅烧3~5h,得到氧化锆粉体。
实施例1:
按3Y的比例称取171.2g氧氯化锆(含有结晶水)、六水合硝酸钇11.85g,溶于250ml去离子水中,取过量的氨水(25%浓度、600ml),将两溶液按一定流速滴定共沉淀反应,保持反应过程pH在8~10之间,反应过程中要一直搅拌;滴定结束后持续搅拌1h,后洗涤沉淀物至氯离子含量小于10mg/L,此沉淀前驱体主要为氢氧化锆,测此时的沉淀物粒度(本文粒度测量均使用OMEC ls-pop6型号激光粒度仪),结果如图2a所示。
将沉淀物用滤纸析出取120g,与去离子水按质量比2:1加入到球磨罐中,然后以300r/min球磨1h,取样测此时前驱体粒度,结果如图2b所示。
用滤纸析出浆料,烘干,并置于窑炉中煅烧(最高温度800℃、保温3h);煅烧后粉体为氧化锆,取样测粒度结果如图2c所示;比表面积为15.463m2/g。
实施例2:
称取171.2g氧氯化锆(含有结晶水)、氧化镁2.23g,溶于250ml去离子水中,取过量的氨水(25%浓度、600ml),将两溶液按一定流速滴定共沉淀反应,保持反应过程pH在8~10之间,反应过程中要一直搅拌;滴定结束后持续搅拌1h,后洗涤沉淀物至氯离子含量小于10mg/L,此沉淀前驱体主要为氢氧化锆,测此时的沉淀物粒度,结果如图3a所示。
将沉淀物用滤纸析出取120g,与去离子水按质量比2:1加入到球磨罐中,然后以300r/min球磨1h,取样测此时前驱体粒度,结果如图3b所示。
用滤纸析出浆料,烘干,并置于窑炉中煅烧(最高温度800℃、保温3h);煅烧后粉体为氧化锆,取样测粒度结果如图3c所示;比表面积为16.356m2/g。
对比例1
按3Y的比例称取171.2g氧氯化锆(含有结晶水)、六水合硝酸钇11.85g,溶于250ml去离子水中,取过量的氨水(25%浓度、600ml),将两溶液按一定流速滴定共沉淀反应,保持反应过程pH在8~10之间,反应过程中要一直搅拌;滴定结束后持续搅拌1h,后洗涤沉淀物至氯离子含量小于10mg/L,此沉淀前驱体主要为氢氧化锆,测此时的沉淀物粒度,结果如图2a所示。
将沉淀物用滤纸析出取120g,1000℃下煅烧4h,得到氧化锆粉体,取样测此时氧化锆粉体粒度,结果如图4a所示,将煅烧后得到的氧化锆粉体加入到球磨罐中,以300r/min球磨10h,取样测此时球磨后氧化锆粉体粒度,结果如图4b所示。
Claims (4)
1.一种高效制备高分散氧化锆陶瓷粉的方法,其特征在于,包括如下步骤:
步骤一、将化学共沉淀得到的氢氧化锆洗涤并压制成固态滤饼;
步骤二、将滤饼与去离子水混合,进行球磨;
步骤三、将球磨后浆料滤出,并烘干;
步骤四、将烘干后物料进窑炉煅烧,得到氧化锆粉体。
2.根据权利要求1所述的高效制备高分散氧化锆陶瓷粉的方法,其特征在于,步骤二滤饼与去离子水按质量比1:1~2:1混合。
3.根据权利要求1所述的高效制备高分散氧化锆陶瓷粉的方法,其特征在于,步骤二以280~350r/min球磨时间1~2h。
4.根据权利要求1所述的高效制备高分散氧化锆陶瓷粉的方法,其特征在于,步骤四700~900℃煅烧3~5h。
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CN1033750A (zh) * | 1987-12-26 | 1989-07-12 | 冶金部洛阳耐火材料研究所 | 高温陶瓷氧化物微粉生产方法 |
JPH02129032A (ja) * | 1988-11-09 | 1990-05-17 | Sumitomo Seika Chem Co Ltd | Plzt粉末の製造法 |
CN101098828A (zh) * | 2004-12-13 | 2008-01-02 | 多诺克斯颜料股份有限公司 | 微粒锆钛酸铅、锆钛水合物和钛酸锆及其制备方法 |
CN101698509A (zh) * | 2009-09-11 | 2010-04-28 | 淄博广通化工有限责任公司 | 纳米氧化锆的生产方法 |
CN101993248A (zh) * | 2009-08-10 | 2011-03-30 | 上海锦奕新材料科技有限公司 | 一种低温烧成钇稳定氧化锆的添加剂 |
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CN1033750A (zh) * | 1987-12-26 | 1989-07-12 | 冶金部洛阳耐火材料研究所 | 高温陶瓷氧化物微粉生产方法 |
JPH02129032A (ja) * | 1988-11-09 | 1990-05-17 | Sumitomo Seika Chem Co Ltd | Plzt粉末の製造法 |
CN101098828A (zh) * | 2004-12-13 | 2008-01-02 | 多诺克斯颜料股份有限公司 | 微粒锆钛酸铅、锆钛水合物和钛酸锆及其制备方法 |
CN101993248A (zh) * | 2009-08-10 | 2011-03-30 | 上海锦奕新材料科技有限公司 | 一种低温烧成钇稳定氧化锆的添加剂 |
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