CN1153751C - Process for preparing functional superfine powder of multi-element composite metal oxide ceramics - Google Patents

Process for preparing functional superfine powder of multi-element composite metal oxide ceramics Download PDF

Info

Publication number
CN1153751C
CN1153751C CNB01108118XA CN01108118A CN1153751C CN 1153751 C CN1153751 C CN 1153751C CN B01108118X A CNB01108118X A CN B01108118XA CN 01108118 A CN01108118 A CN 01108118A CN 1153751 C CN1153751 C CN 1153751C
Authority
CN
China
Prior art keywords
metal oxide
composite metal
preparation
dispersing agent
calcination
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
Application number
CNB01108118XA
Other languages
Chinese (zh)
Other versions
CN1373106A (en
Inventor
刘杏芹
赖炜
孟广耀
彭定坤
高建峰
阎瑞强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Science and Technology of China USTC
Original Assignee
University of Science and Technology of China USTC
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by University of Science and Technology of China USTC filed Critical University of Science and Technology of China USTC
Priority to CNB01108118XA priority Critical patent/CN1153751C/en
Publication of CN1373106A publication Critical patent/CN1373106A/en
Application granted granted Critical
Publication of CN1153751C publication Critical patent/CN1153751C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Compositions Of Oxide Ceramics (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Abstract

The present invention relates to a preparation method of functional ceramic miropowder of multielement composite metal oxide. The preparation method comprises the steps: a water solution of an organic dispersing agent is added to primitive reaction materials such as metal oxide, hydroxide, salts, etc.; mechanical grinding and mixing are carried out to the mixture to form slurry; the slurry is dried and burned to carry out solid-state reaction to form desired composite metal oxide; and the metal oxide is pulverized and milled to obtain the functional ceramic miropowder of multielement composite metal oxide. The method has the advantages of process simplification, convenient operation, high efficiency, low cost and mass production. The obtained powder has the advantages of high purity and reactivity, and small particle diameter, and is basically spherical.

Description

A kind of method for preparing functional superfine powder of multi-element composite metal oxide ceramics
Technical field
The present invention relates to the preparation method of functional superfine powder of multi-element composite metal oxide ceramics.
Background technology
The polynary metal oxide function ceramics has excellent characteristic, and it has wide application at aspects such as piezoelectricity, conduction, magnetic, optics and sensor, Solid Oxide Fuel Cell and gas separation membrane materials.And the key of preparation high-performance polynary metal oxide function ceramics is the fine powder that preparation is highly active, granularity arrives submicron order at tens nanometer.
The traditional method of preparation functional ceramic powder is conventional solid reaction process.For example, (skill newspaper hall is published out city different formula commercial firm to " ceramic process " that the Japan mountain pass is tall and willow Tian Boming compiles, 1984) book is introduced, from metal oxide or metal carbonate, nitrate etc., through ground and mixed, briquetting, through the long calcination of high temperature, make it to take place solid state reaction, form material requested thing phase, and then mechanical disintegration forms powder then.High, time-consuming length that this method not only consumes energy, and in order to obtain single thing phase, also need promptly to carry out the solid state reaction of repeated multiple times through repeatedly grinding and high temperature sintering.Because the at high temperature long-time repeatedly calcination of material, may partially sinter the formation agglomerate between the powder, need again mechanical disintegration to obtain powder, the diameter of particle of Xing Chenging is big and uncontrollable like this, and the particle diameter shape that obtains differs, the poor activity of powder, and in milled processed, also inevitably sneak into container and abrasive impurity, thereby influence its functional property, so the powder of this method preparation does not often conform with continuous thereafter requirement of using.
For above-mentioned reasons, people have been developed a series of wet chemical preparation methods.Such as good that think S. Ruide (Janes S.Reed) work " Principle of Pottery Technology " (Principle of Ceramics Processing, U.S. John Wiley ﹠amp; Sons company, nineteen ninety-five publishes) described in chemical coprecipitation.Chemical coprecipitation at first is the mixing solutions of preparation metal-salt, add certain coprecipitator (normally alkali metal hydroxide, ammoniacal liquor or oxalic acid etc.) again, each metallic element is precipitated out simultaneously with the form of oxyhydroxide or oxalate, and drying, calcination obtain the composite oxides powder again.This method requires to find to all effective coprecipitator of all elements, otherwise the component non-uniform phenomenon can occur.When the preparation multicomponent composite oxide, the occasion that particularly needs strict control of material to form, this coprecipitator generally is difficult to find.The concentration of pH value, temperature and reagent during strict in addition control reaction etc., the solution-operated amount is big, the dry difficulty of filtration washing, process is numerous and diverse, power consumption is taken a lot of work etc., generally is unsuitable for producing in enormous quantities.
In recent years, some new wet chemical preparation methods receive publicity, and they relate to organic application.As chemical communication (Chem.Lett.) magazine the 665th page of report a kind of " the citric acid compound legal system is equipped with the perovskite composite oxide ceramics powder " in 1987, U.S.'s pottery can have been reported a kind of " metal-EDTA inner complex method prepares partially stabilized tetragonal zircite (PTZ) ceramic " by will (J.Am.Ceram.Soc.) 75 volume (nineteen ninety-five) 65-69 pages or leaves.These methods are all based on the principle of metal precursor chemical fixation, precursor costs an arm and a leg and organism consumption very big (its mole dosage often is several times as much as metal), this has improved preparation cost and has polluted easily, simultaneously because the existence of large amount of organic, in the afterglow process of back, tend to form carbonate, some carbonate chemistry combination is very stable (as alkaline earth metal carbonate) also, must could decompose by high temperature.For this reason, obtain required composite oxides thing phase, also must improve calcination temperature, thereby cause powder active poor.
Summary of the invention
The object of the present invention is to provide the method for active high, the functional superfine powder of multi-element composite metal oxide ceramics that granularity is little of a kind of preparation simple, with low cost.
Solution of the present invention is as follows: based on existing solid reaction process, its key is to add organic dispersing agent in the mixing process of primitive reaction material, that is: metal oxide, oxyhydroxide or salt are carried out mechanical mill with the aqueous solution of organic dispersing agent and mix, make slurry, carry out calcination after the drying again and make the generation solid state reaction, form required complex metal oxides, obtain micro mist after crushed; Described organic dispersing agent is organic polymer polyelectrolyte polymethyl acrylic acid, polyacrylic acid and its esters, or linear polymer polyvinyl alcohol, the polyoxyethylene glycol of non-ionic type, and dispersant dosage is 0.1~4% of an initial material weight.
Be that existing solid reaction process is reformed on the present invention is apparent, but come down to have utilized solution impregnation, surface chemistry dispersion, micromechanics chemistry effect effect even nanometer effect or the like Synthesis principle, in the mechanically mixing process of its primitive reaction material, add some organic dispersing agent, can improve mixed effect greatly like this and strengthen reactive behavior between the reactant, original solid reaction process must grind repeatedly for a long time to overcome, the shortcoming and the wet-chemical of compressing tablet and calcination prepare the shortcoming that method must be used special precursor, coprecipitate.Compared with the prior art the inventive method has following advantage:
(1) because raw material mixing process is to carry out mechanical mill to mix in containing the organic dispersing agent aqueous solution of (or claiming tensio-active agent), make feed composition be able to abundant pulverizing, dispersion and uniform mixing, the mechanochemical effect in the mixing process particularly, improved the reactive behavior of raw material greatly, form the mutually required calcination temperature of composite oxides thing thereby reduced, generally can reduce by 100 degree even hundreds of degree, and only need a calcination to get final product the production efficiency height.
(2) owing to once one-tenth phase and calcination temperature are low, thus compound oxidate ceramic powder purity height, the particle diameter little (tens nanometer or hundreds of nanometer) that make, the reactive behavior height of powder.
(3) raw material such as related metal oxide, oxyhydroxide or salt of present method and organic dispersing agent are simple and easy to, and are applicable to the preparation of multicomponent composite oxide micro mist widely.
(4) used organic dispersing agent consumption is few in present method, and is inexpensive nontoxic and be easy to remove, and makes the low and environmentally safe of preparation process cost.
(5) present method operating procedure is simple, need not specific installation, also need not can be mass-produced through the chemosynthesis operation, and facility investment and process cost are all low.
Embodiment
Detailed process of the present invention is: 1. with the primitive reaction material of the polynary metal oxide ceramic powder of required preparation in the required ratio of composite oxide material calculate, (used calculating, weighing technique are traditional method in weighing, repeat no more herein), used primitive reaction material is metal oxide, oxyhydroxide or salt etc.; 2. take by weighing 0.1~4% the organic dispersing agent consumption that accounts for the initial material gross weight, itself and an amount of water are mixed and made into slurry, the consumption of water is relevant with the consumption and the wettability thereof of primitive reaction material, the primitive reaction material can be soaked into, to be easy to wet-milling and to get final product; Described organic dispersing agent is the linear polymer of polyelectrolyte or non-ionic type, as polymethyl acrylic acid, polyacrylic acid and its esters, polyvinyl alcohol, polyoxyethylene glycol etc.; 3. the aqueous solution with above-mentioned primitive reaction material and organic dispersing agent carry out fully, homogeneous mechanical ground and mixed (as adopting various forms of ball millings), make mixture paste; 4. the said mixture slurry is carried out drying treatment; Described drying can adopt conventional heat drying, and also vacuum-pumping to be to shorten time of drying or to reduce drying temperature, and the moisture of looking time of drying in the mixture is as the criterion by evaporation fully; 5. dried material is carried out complete calcination, makes it to carry out solid state reaction by certain temperature schedule, to remove organism and to obtain required composite oxides, calcination temperature system (comprising calcination temperature and time) determines by the experimental technique of routine according to concrete reaction system---different with traditional solid reaction process is, here general as long as through a calcination, need not repeated multiple times; 6. with firing product again mechanical disintegration (as broken, levigate) form powder.
Below be several operational instances:
Embodiment 1: oxygen permeable film material La 0.6Sr 0.4Co 0.8Fe 0.2O 3-δThe preparation of ceramic.
Get 4.891g La 2O 3, 4.254g Sr (NO 3) 3, 3.351g Co 2O 3, 0.806g Fe 2O 3, the 0.532g polyacrylic acid, 14ml distilled water, ball milling is made slurry after mixing, and drying is 12 hours under 90 ℃, and being heated to 1000 ℃ of calcinations then became La in 5 hours 0.6Sr 0.4Co 0.8Fe 0.2O 3-δPottery obtains powder after the pulverizing.Powder particle size is about 200nm, and is spherical in shape substantially.
Embodiment 2: solid electrolyte Ce 0.8Sm 0.2O 1.9The preparation of ceramic.
Get 17.631g Ce (NO 3) 36.37H 2O, 1.744g Sm 2O 3, the 0.019g polyoxyethylene glycol, 20ml distilled water is made slurry after ball milling mixes, and drying is 8 hours under 60 ℃, and being heated to 700 ℃ of calcinations then became Ce in 2 hours 0.8Sm 0.2O 1.9Pottery obtains powder after the pulverizing.Diameter of particle is at 10~20nm, basic globulate.
Embodiment 3: middle temperature oxygen ion conductor La 0.8Sr 0.2Ga 0.8Mg 0.2O 3-δThe preparation of ceramic.
Get 3.261g La 2O 3, 1.064g Sr (NO 3) 2, 1.912g Ga 2O 3, 0.297g Mg (OH) 2, the 0.065g polymethyl acrylic acid, 8.3ml distilled water is made slurry after the mixing and ball milling, and drying is 10 hours under 70 ℃, and being heated to 1400 ℃ of calcinations then became La in 6 hours 0.8Sr 0.2Ga 0.8Mg 0.2O 3-δPottery obtains powder after the pulverizing.Diameter of particle is about 100nm, basic globulate.

Claims (1)

1, a kind of method for preparing functional superfine powder of multi-element composite metal oxide ceramics, comprise to metal oxide, oxyhydroxide or salt mix, the process of calcination and pulverizing, it is as follows to it is characterized by detailed process: metal oxide, oxyhydroxide or salt are carried out mechanical mill with the aqueous solution of organic dispersing agent mix, make slurry, carry out calcination after the drying again and make the generation solid state reaction, form required complex metal oxides, obtain micro mist after crushed; Described organic dispersing agent is complex polyelectrolyte particle polymethyl acrylic acid, polyacrylic acid and its esters, or linear polymer polyvinyl alcohol, the polyoxyethylene glycol of non-ionic type, and dispersant dosage is 0.1~4% of an initial material weight.
CNB01108118XA 2001-03-06 2001-03-06 Process for preparing functional superfine powder of multi-element composite metal oxide ceramics Expired - Fee Related CN1153751C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB01108118XA CN1153751C (en) 2001-03-06 2001-03-06 Process for preparing functional superfine powder of multi-element composite metal oxide ceramics

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB01108118XA CN1153751C (en) 2001-03-06 2001-03-06 Process for preparing functional superfine powder of multi-element composite metal oxide ceramics

Publications (2)

Publication Number Publication Date
CN1373106A CN1373106A (en) 2002-10-09
CN1153751C true CN1153751C (en) 2004-06-16

Family

ID=4657006

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB01108118XA Expired - Fee Related CN1153751C (en) 2001-03-06 2001-03-06 Process for preparing functional superfine powder of multi-element composite metal oxide ceramics

Country Status (1)

Country Link
CN (1) CN1153751C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11845198B2 (en) 2015-01-30 2023-12-19 Cambria Company Llc Processed slabs, and systems and methods related thereto
US11845235B2 (en) 2014-08-19 2023-12-19 Cambria Company Llc Synthetic molded slabs, and systems and methods related thereto

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109437930B (en) * 2018-12-13 2021-07-02 云南大学 Method for homogeneously dispersing sintering aid and use of sintering aid in such method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11845235B2 (en) 2014-08-19 2023-12-19 Cambria Company Llc Synthetic molded slabs, and systems and methods related thereto
US11845198B2 (en) 2015-01-30 2023-12-19 Cambria Company Llc Processed slabs, and systems and methods related thereto

Also Published As

Publication number Publication date
CN1373106A (en) 2002-10-09

Similar Documents

Publication Publication Date Title
CN1837055B (en) Indium oxide powder and method for producing same
US5298469A (en) Fluxed lanthanum chromite for low temperature air firing
EP0670819B1 (en) Air-sinterable lanthanum chromite and process for its preparation
US20150053898A1 (en) Composite oxide powder for solid oxide fuel cell and its production method
US9379391B2 (en) Air electrode material powder for solid oxide fuel cell and its production process
CN101891471B (en) Method for preparing zirconium oxide nanopowder stabilized by yttrium oxide
CN1153751C (en) Process for preparing functional superfine powder of multi-element composite metal oxide ceramics
Jasira et al. Barium cerate and its composite perovskites–synthesis techniques: a comprehensive review
CN111205088A (en) Method for preparing scandia-stabilized zirconia powder by hydrothermal method and scandia-stabilized zirconia powder prepared by method
Zhai et al. A microwave-induced solution-polymerization synthesis of doped LaGaO3 powders
TW202101816A (en) Powder for solid oxide fuel cell air electrode, and method for manufacturing said powder for solid oxide fuel cell air electrode
CN101250056B (en) Method for low-temperature preparation of pure phase oxide material
WO2020045540A1 (en) Electrolyte material for solid oxide fuel cell and method for producing precursor thereof
CN102683720A (en) Gradient composite cathode for solid oxide fuel cell and preparation method thereof
DE102005023048A1 (en) Cathode for a high surface area fuel cell
WO2012116506A1 (en) Preparation method of composite metal oxide powder
CN1112338C (en) Method for preparing composite metal oxide ceramic powder material by using organic polymerization auxiliary prosess
CN111517783B (en) Method for preparing calcium carbonate-YSZ composite solid electrolyte by ultrasonic microwave combination method
US9570754B2 (en) Process for producing anode material for solid oxide fuel cell
CN1410388A (en) Method of synthesizing nano grade calcium titanium ceramic powder
De Macedo et al. Synthesis, processing and characterization of ZrO2-8Y2O3, ZrO2-8CeO2 and La0. 78Sr0. 22MnO3 powders
EP1730074A1 (en) Process for manufacturing an electrochemical device
Filonenko et al. Ceramic Materials Based on BaCe0. 9M0. 1O3–δ for Intermediate Temperature Solid Oxide Fuel Cell
CN111592353B (en) Hydrogen-substituted garnet-type oxide, method for producing sintered body, and method for producing hydrogen-substituted garnet-type oxide
RU2651009C1 (en) Method for synthesis of nano-dimensional powder material based on lanthanum scandate

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
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
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee