JPH0747487B2 - Method for producing powder for easily sinterable microwave dielectric - Google Patents
Method for producing powder for easily sinterable microwave dielectricInfo
- Publication number
- JPH0747487B2 JPH0747487B2 JP2199273A JP19927390A JPH0747487B2 JP H0747487 B2 JPH0747487 B2 JP H0747487B2 JP 2199273 A JP2199273 A JP 2199273A JP 19927390 A JP19927390 A JP 19927390A JP H0747487 B2 JPH0747487 B2 JP H0747487B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- particle size
- slurry
- dielectric
- precipitate
- 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 - Lifetime
Links
- 239000000843 powder Substances 0.000 title claims description 69
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000002245 particle Substances 0.000 claims description 31
- 238000001027 hydrothermal synthesis Methods 0.000 claims description 9
- 229910000000 metal hydroxide Inorganic materials 0.000 claims description 8
- 150000004692 metal hydroxides Chemical class 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 24
- 239000000203 mixture Substances 0.000 description 23
- 239000002002 slurry Substances 0.000 description 22
- 239000012535 impurity Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 16
- 239000013078 crystal Substances 0.000 description 15
- 238000009826 distribution Methods 0.000 description 15
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 14
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 14
- 238000010304 firing Methods 0.000 description 13
- 239000007864 aqueous solution Substances 0.000 description 12
- 239000002994 raw material Substances 0.000 description 12
- 238000003756 stirring Methods 0.000 description 12
- 239000000460 chlorine Substances 0.000 description 10
- -1 chlorine ions Chemical class 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 229910052801 chlorine Inorganic materials 0.000 description 9
- 239000006228 supernatant Substances 0.000 description 9
- 239000010936 titanium Substances 0.000 description 9
- 239000000919 ceramic Substances 0.000 description 8
- 239000003989 dielectric material Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 7
- 239000000395 magnesium oxide Substances 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- 229910001961 silver nitrate Inorganic materials 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 239000004372 Polyvinyl alcohol Substances 0.000 description 6
- 229910010413 TiO 2 Inorganic materials 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 6
- 230000007547 defect Effects 0.000 description 6
- 229920002451 polyvinyl alcohol Polymers 0.000 description 6
- 238000005259 measurement Methods 0.000 description 5
- 230000001590 oxidative effect Effects 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 238000003723 Smelting Methods 0.000 description 4
- 238000002441 X-ray diffraction Methods 0.000 description 4
- 238000005452 bending Methods 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 4
- 238000001354 calcination Methods 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 4
- 238000004891 communication Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 150000004679 hydroxides Chemical class 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 238000005065 mining Methods 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- 239000003929 acidic solution Substances 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 230000003287 optical effect Effects 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000003746 solid phase reaction Methods 0.000 description 3
- ZIRLXLUNCURZTP-UHFFFAOYSA-I tantalum(5+);pentahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[Ta+5] ZIRLXLUNCURZTP-UHFFFAOYSA-I 0.000 description 3
- 229910052719 titanium Inorganic materials 0.000 description 3
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 2
- 229910021193 La 2 O 3 Inorganic materials 0.000 description 2
- 229910017682 MgTi Inorganic materials 0.000 description 2
- 229910017493 Nd 2 O 3 Inorganic materials 0.000 description 2
- 241000849798 Nita Species 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 229910052788 barium Inorganic materials 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 229910052758 niobium Inorganic materials 0.000 description 2
- 239000010955 niobium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 2
- 229910006404 SnO 2 Inorganic materials 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- WAIPAZQMEIHHTJ-UHFFFAOYSA-N [Cr].[Co] Chemical group [Cr].[Co] WAIPAZQMEIHHTJ-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000012736 aqueous medium Substances 0.000 description 1
- 238000001636 atomic emission spectroscopy Methods 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 1
- 229910002113 barium titanate Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical class [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 125000005587 carbonate group Chemical group 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910001510 metal chloride Inorganic materials 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- WPCMRGJTLPITMF-UHFFFAOYSA-I niobium(5+);pentahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[Nb+5] WPCMRGJTLPITMF-UHFFFAOYSA-I 0.000 description 1
- AJCDFVKYMIUXCR-UHFFFAOYSA-N oxobarium;oxo(oxoferriooxy)iron Chemical compound [Ba]=O.O=[Fe]O[Fe]=O.O=[Fe]O[Fe]=O.O=[Fe]O[Fe]=O.O=[Fe]O[Fe]=O.O=[Fe]O[Fe]=O.O=[Fe]O[Fe]=O AJCDFVKYMIUXCR-UHFFFAOYSA-N 0.000 description 1
- CMOAHYOGLLEOGO-UHFFFAOYSA-N oxozirconium;dihydrochloride Chemical compound Cl.Cl.[Zr]=O CMOAHYOGLLEOGO-UHFFFAOYSA-N 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- OEIMLTQPLAGXMX-UHFFFAOYSA-I tantalum(v) chloride Chemical compound Cl[Ta](Cl)(Cl)(Cl)Cl OEIMLTQPLAGXMX-UHFFFAOYSA-I 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- HPGGPRDJHPYFRM-UHFFFAOYSA-J tin(iv) chloride Chemical compound Cl[Sn](Cl)(Cl)Cl HPGGPRDJHPYFRM-UHFFFAOYSA-J 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 238000004876 x-ray fluorescence Methods 0.000 description 1
Landscapes
- Compositions Of Oxide Ceramics (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Inorganic Insulating Materials (AREA)
- Control Of Motors That Do Not Use Commutators (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明はマイクロ波誘電体用粉体、特に水熱合成法によ
り合成されたすぐれた誘電特性を持つ粉体に関する。Description: TECHNICAL FIELD The present invention relates to a powder for microwave dielectric material, and more particularly to a powder having excellent dielectric properties synthesized by a hydrothermal synthesis method.
(従来の技術) 通信情報量の増加と共にマイクロ波を用いた通信システ
ム、即ち衛星通信及び衛星放送等が急速に発達してお
り、通信、放送装置の共振素子に比誘電率が大きく、誘
電損失が小さい(Q値が大きい)誘電体が用いられてい
る。一般にマイクロ波とは500MHz程度以上の高周波数の
電磁波をいう。この誘電体の材料粉体には比誘電率が20
以上でQ値の大きいものが用いられているがQ値は比誘
電率によって種々の値のものが用いられる。比誘電率が
大きい程、誘電体素子の大きさを小さくすることがで
き、Q値が大きい程エネルギー損失が少ないので、比誘
電率とQ値を適当に選択して利用されるが、比誘電率が
同じ場合にはQ値が大きい程好ましい。実際に用いられ
ている材質としては下記のものが使用されている。すな
わち、MgTiO3、(CaLa)TiO3‐MgTiO3、MgTi2O5‐TiO2、M
gO-Nd2O3、(La2O3)‐TiO2、(CaSrBa)(ZrTi)O3、Ba(Mg
1/3Ta2/3)O3、Ba(Zn1/3Nb2/3)O3‐Ba(Zn1/3Ta2/3)O3、B
a(Zn1/3Nb2/3)O3‐Sr(Zn1/3Nb2/3)O3、Ba(NiTa)O3‐Ba
(ZrZnTa)O3、Ba(ZnTa)O3‐BaZrO3、(SrCa)(LiNbTi)O3、
(ZrSn)TiO4、BaTi4O9、Ba2Ti9O20及びBaO・4TiO2・O.1WO3
などである。(Prior Art) A communication system using microwaves, that is, satellite communication and satellite broadcasting is rapidly developing with the increase of communication information amount, and a relative dielectric constant is large in a resonance element of a communication or broadcasting device, resulting in a dielectric loss. Is used (a large Q value). Generally, a microwave refers to an electromagnetic wave having a high frequency of about 500 MHz or higher. This dielectric material powder has a relative dielectric constant of 20.
Although a material having a large Q value has been used as described above, various Q values are used depending on the relative dielectric constant. The larger the relative permittivity, the smaller the size of the dielectric element. The larger the Q value, the smaller the energy loss. Therefore, the relative permittivity and the Q value are appropriately selected and used. When the ratio is the same, the larger the Q value is, the more preferable. The following materials are used as the materials actually used. That is, MgTiO 3 , (CaLa) TiO 3 -MgTiO 3 , MgTi 2 O 5 -TiO 2 , M
gO-Nd 2 O 3 , (La 2 O 3 ) -TiO 2 , (CaSrBa) (ZrTi) O 3 , Ba (Mg
1/3 Ta 2/3 ) O 3 , Ba (Zn 1/3 Nb 2/3 ) O 3 -Ba (Zn 1/3 Ta 2/3 ) O 3 , B
a (Zn 1/3 Nb 2/3 ) O 3- Sr (Zn 1/3 Nb 2/3 ) O 3 , Ba (NiTa) O 3 -Ba
(ZrZnTa) O 3 , Ba (ZnTa) O 3 -BaZrO 3 , (SrCa) (LiNbTi) O 3 ,
(ZrSn) TiO 4 , BaTi 4 O 9 , Ba 2 Ti 9 O 20 and BaO ・ 4TiO 2・ O.1WO 3
And so on.
従来、上記した各組成を有するマイクロ波誘電体用粉体
は普通のセラミックスと同様に、原料の秤量、混合、焼
成などの工程を経て製造されていた。例えば、Ba(Zn1/3
Ta2/3)O3‐Ba(Zn1/3Nb2/3)O3セラミックス(略称BSTN)
について(「マイクロ波誘電体セラミックスの動向(総
論)」、エレクトロニクセラミックス、1988年3月号、
19巻)に紹介されている。これによれば、すなわち、ま
ず入手した固体原料中の有効成分を定量分析し、所望の
化学組成比になるように秤量採取する。次に固相反応を
均一に行わせるために、らいかい機などによる乾式混
合、或はボールミルなどによる湿式混合を行う。混合の
終った原料は焼成温度よりやや低い温度(約1000℃)で
仮焼した後、粉砕する。仮焼の条件は焼結時に炭酸塩の
熱分解でガス発生がなく、粉末の焼結性が失われないよ
うに900℃〜1100℃で2〜10時間行う。仮焼後の粉砕は
粉末の粒度を調製し平均粒径を2〜10μmとし、その後
の工程での異常膨張や収縮が減少し、緻密なセラミック
スを得られやすくする。粉砕の終った粉末に結合剤や潤
滑剤や水分を加えて顆粒を作る。結合剤にはポリビニル
アルコールや澱粉など、潤滑剤にはステアリン酸塩、カ
ーボワックス等が使用される。造粒粉末は所定の形状の
金型に入れ、油圧プレスや機械プレスで加圧圧縮して成
形する。厚手の板や柱状或は円筒状の試料を成形すると
きは、金型の中の粉体流動を滑らかにし、応力分布を均
一にすることが必要である。応力分布が不均一のとき
は、焼成歪を生じ、焼結体の密度などの分布が不均一に
なる。成形圧力は1〜3t/cm2程度を使用する。成形体は
ふた付きのマグネシヤまたはアルミナのさやにいれて、
結合剤や潤滑剤を焼尽ののち酸化性雰囲気中で、所定の
温度(1350〜1550℃)で所要時間(2〜120時間)焼成
する。これらの焼結体は所要の寸法に研削や研磨で仕上
げられ最終製品とする。Conventionally, microwave dielectric powders having the above-described compositions have been manufactured through processes such as weighing of raw materials, mixing, and firing, like ordinary ceramics. For example, Ba (Zn 1/3
Ta 2/3 ) O 3 -Ba (Zn 1/3 Nb 2/3 ) O 3 ceramics (abbreviation BSTN)
About ("Trends in Microwave Dielectric Ceramics (Overview)", Electronic Ceramics, March 1988 issue,
19). According to this, that is, first, the active ingredient in the obtained solid raw material is quantitatively analyzed, and weighed and collected so as to have a desired chemical composition ratio. Next, in order to carry out the solid-phase reaction uniformly, dry mixing is carried out by using a ladle machine or wet mixing is carried out by a ball mill. The raw materials that have been mixed are calcined at a temperature slightly lower than the firing temperature (about 1000 ° C) and then pulverized. The conditions of calcination are 900 ° C to 1100 ° C for 2 to 10 hours so that no gas is generated due to thermal decomposition of carbonate during sintering and the sinterability of the powder is not lost. The pulverization after calcination adjusts the particle size of the powder to an average particle size of 2 to 10 μm, and abnormal expansion and contraction in the subsequent steps are reduced to facilitate the production of dense ceramics. Binder, lubricant and water are added to the crushed powder to make granules. Polyvinyl alcohol and starch are used as the binder, and stearates, carbowaxes and the like are used as the lubricant. The granulated powder is put into a mold having a predetermined shape, and is pressed and compressed by a hydraulic press or a mechanical press to be molded. When molding a thick plate or a columnar or cylindrical sample, it is necessary to smooth the powder flow in the mold and make the stress distribution uniform. When the stress distribution is non-uniform, firing strain occurs and the density distribution of the sintered body becomes non-uniform. The molding pressure is about 1 to 3 t / cm 2 . The molded body is put in a magnesia with a lid or an alumina sheath,
After the binder and the lubricant are burned out, they are fired in an oxidizing atmosphere at a predetermined temperature (1350 to 1550 ° C.) for a required time (2 to 120 hours). These sinters are finished by grinding or polishing to the required dimensions to make the final products.
(発明が解決しようとする課題) マイクロ波用誘電体の品質係数Qは、誘電損失の逆数で
与えられるが、誘電損失を小さくし、Qを大きくするに
は、粒界などの不純物格子欠陥などを除き、均質で、反
り、曲がりの少ない緻密なセラミックスとする必要があ
る。なぜならマイクロ波誘電体の比誘電率の温度安定性
や誘電損失がそのまま誘電体素子や部品、例えば誘電体
共振器の良否を決定するからである。(Problems to be Solved by the Invention) The quality factor Q of a microwave dielectric is given by the reciprocal of the dielectric loss, but in order to reduce the dielectric loss and increase Q, impurity lattice defects such as grain boundaries are required. Except for the above, it is necessary to make a dense ceramic that is homogeneous and has little warpage and bending. This is because the temperature stability of the relative permittivity and the dielectric loss of the microwave dielectric material directly determine the quality of the dielectric element or component, for example, the dielectric resonator.
従来は、上述のように固体粉末原料を混合・仮焼してマ
イクロ誘電体用粉体を製造していたため、混合・仮焼工
程中で種々の不純物を含みやすく、製造した粉体の平均
粒径は1μm以上と大きく、粒度分布が広いため、焼成
温度を高くする必要があった。このため高温焼成中に組
成変動が起こりやすく、焼結体としたときに不純物、格
子欠陥などが入りやすく、粒径が不均一で、反り、曲が
りが入りやすく、緻密になりにくく、Q値が小さくなる
という問題を有していた。Conventionally, as described above, solid powder raw materials were mixed and calcined to produce powders for microdielectrics, so various impurities are likely to be included during the mixing and calcination process, and the average grain size of the produced powders. Since the diameter was as large as 1 μm or more and the particle size distribution was wide, it was necessary to raise the firing temperature. For this reason, the composition is likely to change during high-temperature firing, impurities and lattice defects are likely to enter the sintered body, the grain size is not uniform, warpage and bending are likely to occur, it is difficult to be dense, and the Q value is It had the problem of becoming smaller.
本発明者らは前記した従来のマイクロ波誘電体用粉体の
課題を解決すべく、従来バリウムフェライト、チタン酸
バリウム(BaTiO3)や圧電セラミックス用及びコンデン
サー用の鉛含有酸化物粉末等の合成のみに用いられてい
た水熱合成法を、マイクロ波誘電体用粉体の製造に用い
られるように改良を重ね、鋭意努力した結果、不純物含
有量が少なく、平均粒径が小さく、粒度分布が狭く、焼
成温度が低く、焼成中に組成変動を起こしにくく、焼結
体としたときに粒界、不純物、格子欠陥などがはいりに
くく、均一で、反り、曲がりがはいりにくく、緻密にな
りやすく、Q値が大きくなる粉体を製造する方法を見い
だし、本発明に至った。In order to solve the above-mentioned problems of the conventional powder for microwave dielectrics, the present inventors have synthesized conventional barium ferrite, barium titanate (BaTiO 3 ) and lead-containing oxide powder for piezoelectric ceramics and capacitors. The hydrothermal synthesis method, which was used only for the above, was improved so that it could be used for the production of powders for microwave dielectrics, and as a result of diligent efforts, the content of impurities was small, the average particle size was small, and the particle size distribution was small. Narrow, low firing temperature, less likely to cause compositional changes during firing, grain boundaries, impurities, lattice defects, etc. are less likely to enter when made into a sintered body, uniform, warpage, bending are less likely to occur, and it tends to be dense, The inventors have found a method for producing a powder having a large Q value, and have reached the present invention.
(課題を解決するための手段) すなわち、本発明は以下を要旨とするものである。(Means for Solving the Problem) That is, the present invention is summarized as follows.
金属水酸化物に付着している塩素イオンを除去したもの
を原料として、オートクレーブに仕込み、水熱合成した
後、乾燥することを特徴とする粒径0.1〜0.5μmの易焼
結性マイクロ波誘電体用粉体の製造方法。Easily sinterable microwave dielectric with a particle size of 0.1-0.5 μm characterized by charging an autoclave with the material from which the chlorine ions adhering to the metal hydroxide have been removed, and then hydrothermally synthesizing it. A method for producing body powder.
以下、本発明について更に詳しく説明する。Hereinafter, the present invention will be described in more detail.
本発明にいうマイクロ波誘電体用粉体とは、周波数500M
Hz程度以上のマイクロ波回路用の誘電体素子や部品、例
えば誘電体共振器等に使用される比誘電率が20程度以上
で、Q値が高いセラミックスの原料粉体である。The microwave dielectric powder referred to in the present invention has a frequency of 500M.
It is a raw material powder of ceramics having a high relative dielectric constant of about 20 or more and a high Q value, which is used for a dielectric element or part for microwave circuits of about Hz or higher, such as a dielectric resonator.
本発明の適用粉体組成を具体的に下記に示すならば、例
えば、MgTiO3、(CaLa)TiO3‐MgTiO3、MgTi2O5‐TiO2、M
gO-Nd2O3、(La2O3)‐TiO2、(CaSrBa)(ZrTi)O3、Ba(Mg
1/3Ta2/3)O3、Ba(Zn1/3Nb2/3)O3‐Ba(Zn1/3Ta2/3)O3、B
a(Zn1/3Nb2/3)O3‐Sr(Zn1/3Nb2/3)O3、Ba(NiTa)O3‐Ba
(ZrZnTa)O3、Ba(ZnTa)O3‐BaZrO3、(SrCa)(LiNbTi)O3、
(ZrSn)TiO4、BaTi4O9、Ba2Ti9O20、BaO・4TiO2・O.1WO3な
どがあげられる。しかしながら、本発明は上記組成のみ
に限定されるものではない。If the application powder composition of the present invention is specifically shown below, for example, MgTiO 3 , (CaLa) TiO 3 -MgTiO 3 , MgTi 2 O 5 -TiO 2 , M
gO-Nd 2 O 3 , (La 2 O 3 ) -TiO 2 , (CaSrBa) (ZrTi) O 3 , Ba (Mg
1/3 Ta 2/3 ) O 3 , Ba (Zn 1/3 Nb 2/3 ) O 3 -Ba (Zn 1/3 Ta 2/3 ) O 3 , B
a (Zn 1/3 Nb 2/3 ) O 3- Sr (Zn 1/3 Nb 2/3 ) O 3 , Ba (NiTa) O 3 -Ba
(ZrZnTa) O 3 , Ba (ZnTa) O 3 -BaZrO 3 , (SrCa) (LiNbTi) O 3 ,
(ZrSn) such as TiO 4, BaTi 4 O 9, Ba 2 Ti 9 O 20, BaO · 4TiO 2 · O.1WO 3 and the like. However, the present invention is not limited to the above composition.
本発明でいう金属水酸化物とは、例えば上記に示した本
発明の適用粉体組成を構成する金属の金属水酸化物をい
う。The metal hydroxide referred to in the present invention means, for example, the metal hydroxide of the metal constituting the powder composition to which the present invention is applied.
本発明の易焼結性マイクロ波誘電体用粉体を製造するに
当たっては、水熱合成法を用いる。水熱合成法は高温高
圧の水あるいは水溶液が反応に関与する単結晶合成法と
してよく知られているが、マイクロ波誘電体用粉体の微
粒子であって、形状、粒径が均一で、純度の高い粉体の
合成にも適した方法である。A hydrothermal synthesis method is used for producing the powder for easily sinterable microwave dielectric material of the present invention. The hydrothermal synthesis method is well known as a single crystal synthesis method in which high-temperature and high-pressure water or an aqueous solution participates in the reaction, but it is a fine particle of microwave dielectric powder and has a uniform shape and particle size and a high purity. This method is also suitable for the synthesis of high-quality powder.
金属水酸化物に付着している塩素イオンを除去したもの
とは、あらかじめ作製された金属水酸化物、あるいは金
属塩化物などの金属化合物を酸性溶液などで中和して生
成される水酸化物を水や溶剤でスラリーとし、スラリー
の液中に遊離してくる塩素イオンを除去したものをい
う。塩素イオンが除去されたかどうかは、該金属水酸化
物の洗浄液に硝酸銀を滴下しても、白濁しない程度、す
なわち塩素イオン10ppm以下程度の状態をいう。What removed the chloride ion adhering to the metal hydroxide is a metal hydroxide prepared in advance, or a hydroxide produced by neutralizing a metal compound such as metal chloride with an acidic solution. Is made into a slurry with water or a solvent, and chlorine ions liberated in the liquid of the slurry are removed. Whether or not chlorine ions have been removed refers to a state in which even if silver nitrate is dropped into the cleaning solution for the metal hydroxide, it does not become cloudy, that is, a state where chlorine ions are 10 ppm or less.
ここではBaTi4O9を合成する場合について説明する。水
熱合成の原料にはBaとTiの水酸化物が好ましく、市販の
水酸化物の結晶を用いても良く、酸性溶液などを中和し
て水酸化物沈殿を合成しても良い。酸性溶液を中和する
場合には、沈殿を一旦ろ過し、塩素イオン等の不純物イ
オンが10ppm以下となるように充分に洗浄することが好
ましい。この様なイオンが残存すると、水熱合成によっ
て合成されたマイクロ波誘電体用粉体の結晶粒界や結晶
中へ不純物が混入しやすく結晶欠陥を発生し易くした
り、最終の焼結体の誘電特性を阻害したりするからであ
る。洗浄の際、Baなどの塩基性の元素の水酸化物は水に
溶解してしまうので、水に溶解しやすい元素の水酸化物
原料は、中和によって沈殿を得るのではなく、純度の高
い水酸化物結晶を用いる方が好ましい。製造する粉体の
化学量論を合わせやすいからである。Here, the case of synthesizing BaTi 4 O 9 will be described. As a raw material for hydrothermal synthesis, hydroxides of Ba and Ti are preferable, and commercially available hydroxide crystals may be used, or a hydroxide precipitate may be synthesized by neutralizing an acidic solution or the like. When the acidic solution is neutralized, it is preferable to filter the precipitate once and sufficiently wash it so that impurity ions such as chlorine ions are 10 ppm or less. When such ions remain, impurities are easily mixed into the crystal grain boundaries and crystals of the microwave dielectric powder synthesized by hydrothermal synthesis, and crystal defects are easily generated. This is because it may impair the dielectric properties. During cleaning, basic element hydroxides such as Ba dissolve in water, so hydroxides of elemental elements that are easily soluble in water do not get a precipitate by neutralization, but have high purity. It is preferable to use hydroxide crystals. This is because it is easy to match the stoichiometry of the manufactured powders.
次に水酸化物結晶または水酸化物沈殿を純水に分散させ
る。Baなど塩基性の元素は水への溶解度が高いので、水
酸化物の量と水の量の比を適当に選ぶ必要がある。水の
量が多すぎる場合には、水熱反応後もBa等の塩基性元素
が水媒体中に溶存し、目的とする組成を有する粉体を合
成できないためである。BaTi4O9の場合には(Ba(OH)2・8
H2O結晶/H2O)の質量比にしておおよそ1/20以上で反応
させれば良い。Next, the hydroxide crystal or hydroxide precipitate is dispersed in pure water. Since basic elements such as Ba have high solubility in water, it is necessary to appropriately select the ratio of the amount of hydroxide to the amount of water. This is because if the amount of water is too large, the basic element such as Ba will be dissolved in the aqueous medium even after the hydrothermal reaction, and the powder having the intended composition cannot be synthesized. In the case of BaTi 4 O 9 (Ba (OH ) 2 · 8
The reaction may be performed at a mass ratio of H 2 O crystal / H 2 O) of about 1/20 or more.
BaとTiの水酸化物を分散した水をオートクレーブに仕込
み、水熱反応を進行させる。反応温度及び反応圧力の条
件は反応速度や粉体粒径を制御するだけでなく、合成さ
れる粉体の結晶系を変えるので、合成すべき結晶系にあ
った温度と圧力の条件を選ばなければならない。BaTi4O
9の場合には、150℃〜300℃、10kg/cm2〜100kg/cm2で反
応させれば、結晶粒径0.3μm程度の粉体を合成でき
る。オートクレーブの容積に対する水の充填率によっ
て、反応温度における系の圧力が決定されるので、水の
充填率は反応させるべき温度と圧力に従って適当な値を
選ばねばならない。BaTi4O9を200℃かつ30kg/cm2程度で
反応させる場合には、充填率を約50%に選べはよい。Water in which hydroxides of Ba and Ti are dispersed is charged into an autoclave to allow the hydrothermal reaction to proceed. The reaction temperature and reaction pressure conditions not only control the reaction rate and powder particle size, but also change the crystal system of the powder to be synthesized, so the temperature and pressure conditions suitable for the crystal system to be synthesized must be selected. I have to. BaTi 4 O
In the case of 9, 150 ℃ ~300 ℃, is reacted with 10kg / cm 2 ~100kg / cm 2 , it can be synthesized powder of about grain size 0.3 [mu] m. Since the filling rate of water with respect to the volume of the autoclave determines the pressure of the system at the reaction temperature, the filling rate of water should be selected appropriately according to the temperature and pressure to be reacted. When BaTi 4 O 9 is reacted at 200 ° C. and about 30 kg / cm 2 , the filling rate can be selected to be about 50%.
本発明の易焼結性マイクロ波誘電体用粉体の場合、反応
は100℃以上の高温で行う。100℃以下では反応速度が小
さすぎ、実用に適さないからである。高温にすると反応
速度が大きくなると共に、製造される粉体の粒径が大き
くなる。水の臨界点である374℃以上では、反応速度及
び粉体の粒径は特に大きくなる。粉体に低温焼結性を与
えるには粒径0.1〜0.5μmで、平均粒径0.3μm程度の
粉体とする必要があるので、反応温度は臨界点以下に抑
えることが必要である。合成した粉体はろ過または遠心
分離などにより取り出し、乾燥させる。必要に応じてス
プレードライ法により造粒しても良い。In the case of the easily sinterable microwave dielectric powder of the present invention, the reaction is carried out at a high temperature of 100 ° C. or higher. This is because at 100 ° C or lower, the reaction rate is too small to be suitable for practical use. When the temperature is increased, the reaction rate increases and the particle size of the produced powder increases. Above 374 ° C, which is the critical point of water, the reaction rate and the particle size of the powder become particularly large. In order to impart low-temperature sinterability to the powder, it is necessary to make the powder have a particle size of 0.1 to 0.5 μm and an average particle size of about 0.3 μm, so it is necessary to keep the reaction temperature below the critical point. The synthesized powder is taken out by filtration or centrifugation and dried. You may granulate by a spray dry method as needed.
オートクレーブはバッチ型のものでもよく、連続型のも
のでも良い。一般には多品質の製品を少量ずつ製造する
場合にはバッチ型のものが適当であり、少品種のものを
大量に製造する場合には連続型のものが適当である。The autoclave may be a batch type or a continuous type. Generally, a batch type is suitable for producing small quantities of multi-quality products, and a continuous type is suitable for producing a large number of small kinds of products.
(作用) 本発明では、マイクロ波誘電体用粉体を構成する金属の
金属水酸化物に付着している塩素イオンを除去したもの
を原料としてオートクレーブに仕込み、水熱合成した
後、乾燥することによって、平均粒径が1μm以下と小
さく、粒径が0.1〜0.5μmと粒度分布が狭く、低温焼結
性に優れ、結晶粒界や結晶中の不純物の混入が少なく、
結晶欠陥が発生しにくい高純度の粉体であり、焼成温度
を低く選ぶことができ、焼結体としたときのQ値が高い
マイクロ波誘電体用粉体を得ることができる。(Function) In the present invention, a material obtained by removing chloride ions adhering to metal hydroxide of a metal constituting a powder for microwave dielectrics is charged as a raw material into an autoclave, hydrothermally synthesized, and then dried. The average grain size is as small as 1 μm or less, the grain size distribution is narrow at 0.1-0.5 μm, the low-temperature sinterability is excellent, and the inclusion of impurities in crystal grain boundaries and crystals is small.
It is a high-purity powder in which crystal defects are less likely to occur, the firing temperature can be selected to be low, and a powder for microwave dielectric having a high Q value when made into a sintered body can be obtained.
(実施例) 以下更に実施例を挙げて詳しく説明する。(Examples) Hereinafter, examples will be described in detail.
〔実施例1〕 16%塩化チタン水溶液を250gに2NのNaOH水溶液を撹拌し
ながらpH=10となるまで滴下し、水酸化チタン沈殿のス
ラリーを得た。このスラリーを遠心分離器に掛け、上澄
み液を除いて沈殿物を得た。次にこの沈殿物にイオン交
換水を加え、超音波洗浄器中で撹拌しながら分散させ、
再びスラリーとした。この様に沈殿物の遠心分離と再分
散の工程を3度繰り返して、沈殿物に付着した塩素イオ
ンを洗浄した。4度目に遠心分離したのちの上澄み液を
採取して、硝酸銀を滴下したところ白色の沈殿を生じな
かったので、沈殿に付着していた塩素イオンがほぼ除か
れたことが分かった。[Example 1] A 16% titanium chloride aqueous solution was added dropwise to 250 g of a 2N NaOH aqueous solution with stirring until pH = 10 to obtain a titanium hydroxide precipitate slurry. This slurry was put into a centrifuge and the supernatant was removed to obtain a precipitate. Next, ion-exchanged water was added to this precipitate and dispersed with stirring in an ultrasonic cleaner.
It was made into a slurry again. In this way, the steps of centrifugation and redispersion of the precipitate were repeated three times to wash chloride ions attached to the precipitate. When the supernatant was collected after the fourth centrifugation and silver nitrate was added dropwise, a white precipitate did not occur, so it was found that chlorine ions adhering to the precipitate were almost removed.
更にこの水酸化チタン沈殿のスラリーに純度98%のBa(O
H)2・8H2Oを67.876g混合し、この沈殿混合物にイオン交
換水を加えて全量を1500mlとした。その上澄み液を10ml
分取し、硝酸銀を滴下したところ白色の沈殿は生じなか
った。残りを超音波洗浄器中で撹拌して分散させて得た
スラリーをハステロC製の4lのオートグレーブに仕込ん
で100〜150rpmで撹拌しながら120分で240℃まで昇温
し、0.5時間水熱処理した。Further, this titanium hydroxide precipitate slurry was added with Ba (O
H) 2 · 8H 2 O was 67.876g mixture, was 1500ml added to bring the total amount of ion-exchanged water to the precipitation mixture. 10 ml of the supernatant
When it was separated and silver nitrate was added dropwise, a white precipitate was not formed. The rest was stirred and dispersed in an ultrasonic cleaner, and the resulting slurry was placed in a Hasteloh C 4l autograve and heated to 240 ° C in 120 minutes while stirring at 100 to 150 rpm, and hydrothermally treated for 0.5 hours. did.
反応終了後、スラリーを濾別して水洗した。真空乾燥器
内で乾燥させた後、理学電気製RAD-IIB型回折装置によ
りエックス線回折パターンを測定し、更に化学組成を蛍
光エックス線測定により分析したところ、期待した通り
Ba1.0Ti4.0O9.0の組成を保育する結晶が得られたことが
明らかになった。また、遠心沈降法粒度分布測定器によ
り測定した粉体の粒度分布は、0.1μmから0.5μmの間
に分布し、そのヒストグラムは単一のピークを持ってい
た。また平均粒径は第1表に示すごとく0.3μmであっ
た。また、不純物含有量を発光分析法によって測定した
結果を第2表に示したが、いずれの元素も10ppm以下で
あり、純度の高いものであった。After the reaction was completed, the slurry was filtered and washed with water. After drying in a vacuum drier, the X-ray diffraction pattern was measured with the RAD-IIB type diffractometer manufactured by Rigaku Denki, and the chemical composition was analyzed by fluorescent X-ray measurement.
It was revealed that crystals were obtained that maintained the composition of Ba 1.0 Ti 4.0 O 9.0 . The particle size distribution of the powder measured by the centrifugal sedimentation method particle size distribution analyzer was distributed between 0.1 μm and 0.5 μm, and the histogram had a single peak. The average particle size was 0.3 μm as shown in Table 1. The results of measuring the content of impurities by the optical emission spectrometry are shown in Table 2. All elements were 10 ppm or less, and the purity was high.
この粉体にPVAの5wt%水溶液を粉体質量に対して5wt%
加えて造粒した。造粒粉末を直径8mmの円筒形状の金型
に入れ、油圧プレスで1t/cm2で加圧圧縮して成形した。
成形体をふた付きのマグネシヤのさやにいれて、酸化性
雰囲気中、1200℃で5時間焼成した。その結果第1表に
示すとおり、焼結体の密度は理論密度の99%であった。
またεとQ値を測定したところ、室温におけるεは40で
あり、Qは12300であった。測定にはYHP社製ネットワー
クアナライザーを用いて、サンプル保持具に村田製作所
製治具を用いた。測定周波数は1GHzであった。A 5 wt% PVA aqueous solution was added to this powder in an amount of 5 wt% based on the mass of the powder.
In addition, it granulated. The granulated powder was put into a cylindrical mold having a diameter of 8 mm, and was compressed by a hydraulic press at 1 t / cm 2 to be molded.
The molded body was put into a pod of a magnesia with a lid and fired at 1200 ° C. for 5 hours in an oxidizing atmosphere. As a result, as shown in Table 1, the density of the sintered body was 99% of the theoretical density.
Further, when the ε and Q values were measured, ε at room temperature was 40 and Q was 12300. A YHP network analyzer was used for the measurement, and a Murata jig was used as the sample holder. The measurement frequency was 1 GHz.
〔比較例1〕 BsCO3とTiO2原料をBa:Tiの比が1:4となるように秤量し
た。次に固相反応を均一に行わせるために、ボールミル
などによる湿式混合を行った。混合の終った原料を1000
℃で10時間仮焼した後、ボールミルを用いて湿式粉砕し
た。Comparative Example 1 BsCO 3 and TiO 2 raw materials were weighed so that the ratio of Ba: Ti was 1: 4. Next, in order to carry out the solid-phase reaction uniformly, wet mixing was performed with a ball mill or the like. 1000 mixed raw materials
After calcination at 10 ° C. for 10 hours, it was wet pulverized using a ball mill.
エックス線回折パターンを測定したところ、BaTi4O9の
回折パターンが得られた。この粉体の化学組成を蛍光エ
ックス線測定により分析したところ、期待した通りBa
1.0Ti4.0O9.0の組成を保有することが明らかになった。
また、遠心沈降法粒度分布測定器により粉体の粒度分布
を測定したところ、0.5μmから7.5μmの間に分布し、
そのヒストグラムは複数のピークを持っていた。また平
均粒径は第1表に示すとおり2.3μmであった。しか
し、発光分析による不純物量は第2表に示すとおりであ
り、Na、Ca、Al、Fe、Mnの含有量が実施例1に比較して
多くなっていた。When the X-ray diffraction pattern was measured, a BaTi 4 O 9 diffraction pattern was obtained. When the chemical composition of this powder was analyzed by X-ray fluorescence analysis, the expected Ba
It was revealed that it possesses the composition of 1.0 Ti 4.0 O 9.0 .
In addition, when the particle size distribution of the powder was measured with a centrifugal sedimentation method particle size distribution analyzer, it was found to be distributed between 0.5 μm and 7.5 μm.
The histogram had multiple peaks. The average particle size was 2.3 μm as shown in Table 1. However, the amount of impurities measured by optical emission analysis is as shown in Table 2, and the contents of Na, Ca, Al, Fe, and Mn were larger than those in Example 1.
この粉体にPVAの5wt%水溶液を粉体質量に対して5wt%
加えて造粒した。造粒粉末を円筒形状の金型に入れ、油
圧プレスで1t/cm2で加圧圧縮して成形した。成形体をふ
た付きのマグネシャのさやにいれて、酸化性雰囲気中、
1200℃で5時間焼成しても充分な焼結体密度が得られな
かった。順次焼成温度をあげて焼結性を確かめた結果、
第1表に示すとおり、1380℃で5時間焼成したとき焼結
体の密度は理論密度の99%となり、実施例1と同等の密
度が得られた。しかし、室温における比誘電率は38であ
り、Q値は8800であって、特にQ値が実施例1に比較し
てかなり劣っていた。A 5 wt% PVA aqueous solution was added to this powder in an amount of 5 wt% based on the mass of the powder.
In addition, it granulated. The granulated powder was put into a cylindrical mold and pressed by a hydraulic press at 1 t / cm 2 to be molded. Put the molded body in the pod of a magnesia with a lid, in an oxidizing atmosphere,
Even after firing at 1200 ° C. for 5 hours, a sufficient sintered body density could not be obtained. As a result of increasing the firing temperature and confirming the sinterability,
As shown in Table 1, when sintered at 1380 ° C. for 5 hours, the density of the sintered body was 99% of the theoretical density, and the same density as in Example 1 was obtained. However, the relative dielectric constant at room temperature was 38, and the Q value was 8800, which was particularly inferior to that of Example 1.
〔実施例2〕 25wt%の塩化タンタル水溶液250gに2NのNaOH水溶液を撹
拌しながらpH=10となるまで滴下し、水酸化タンタル沈
澱のスラリーを得た。スラリーを遠心分離器に掛け、上
澄み液を除いて沈澱物を得た。沈澱物にイオン交換水を
加え、超音波洗浄器中で撹拌しながら分散させ、再びス
ラリーとした。この用に沈澱物の遠心分離と再分散の工
程を3度繰り返して、沈澱物に付着した塩素イオンを洗
浄した。4度目に遠心分離したのちの上澄み液を採取し
て、硝酸銀を滴下したところ白色の沈澱は生じなかった
ので、沈澱に付着した塩素イオンがほぼ除かれたことが
分かった。Example 2 To 250 g of a 25 wt% tantalum chloride aqueous solution, a 2N NaOH aqueous solution was added dropwise with stirring until pH = 10 to obtain a slurry of tantalum hydroxide precipitation. The slurry was put into a centrifuge and the supernatant was removed to obtain a precipitate. Ion-exchanged water was added to the precipitate and dispersed with stirring in an ultrasonic cleaner to form a slurry again. For this purpose, the steps of centrifuging and redispersing the precipitate were repeated three times to wash chloride ions attached to the precipitate. When the supernatant was collected after the fourth centrifugation and silver nitrate was added dropwise, a white precipitate did not occur, so it was found that the chlorine ions adhering to the precipitate were almost removed.
更にこの水酸化タンタルの沈澱に純度99.8%、粒径約0.
3μmのMgOの微粉3.5gとBa(OH)2・8H2Oを315.3gを混合
し、この沈澱混合物にイオン交換水を加えて全量を1500
mlとした。その上澄み液を10ml分取し、硝酸銀を滴下し
たところ白色の沈殿は生じなかった。残りを超音波洗浄
器中で撹拌して分散させて得たスラリーをハステロイC
製の4lのオートクレーブに仕込んで100〜150rpmで撹拌
しながら120分で240℃まで昇温し、0.5時間水熱処理し
た。Furthermore, this tantalum hydroxide precipitate has a purity of 99.8% and a particle size of about 0.
3.5 g of 3 μm MgO powder and 315.3 g of Ba (OH) 2 · 8H 2 O were mixed, and ion-exchanged water was added to this precipitation mixture to bring the total amount to 1500.
ml. When 10 ml of the supernatant was taken and silver nitrate was added dropwise, white precipitate was not formed. The slurry obtained by stirring and dispersing the rest in an ultrasonic cleaner is Hastelloy C.
It was charged in a 4 liter autoclave manufactured by Kuraray Co., Ltd., heated to 240 ° C. in 120 minutes with stirring at 100 to 150 rpm, and hydrothermally treated for 0.5 hour.
反応終了後、スラリーを濾別して水洗した。真空乾燥器
内で乾燥させた後エックス線回折パターンを測定したこ
とろ、Ba(Mg1/3Ta2/3)O3の回折パターン以外にはピーク
が現れておらず、単相であることが分かった。この粉体
の化学組成を蛍光エックス線測定により分析したとこ
ろ、期待した通りBa:Mg:Ta=3.0:1.0:2.0の組成を保有
することが明らかになった。遠心沈降法粒度分布測定器
により測定した粉体の粒度分布は、0.1μmから0.5μm
の間に分布し、そのヒストグラムは単一のピークを持っ
ていた。また、平均粒径は第1表に示すように0.3μm
であった。発光分析法により見いだされた含有不純物元
素は第2表に示すものであり、いずれの元素も10ppm以
下の含有量であった。After the reaction was completed, the slurry was filtered and washed with water. The X-ray diffraction pattern was measured after drying in a vacuum drier, and no peaks appeared other than the diffraction pattern of Ba (Mg 1/3 Ta 2/3 ) O 3 , indicating a single phase. Do you get it. Analysis of the chemical composition of this powder by fluorescent X-ray measurement revealed that it possessed the composition of Ba: Mg: Ta = 3.0: 1.0: 2.0 as expected. The particle size distribution of the powder measured by the centrifugal sedimentation method particle size distribution measuring device is 0.1 μm to 0.5 μm.
And the histogram had a single peak. The average particle size is 0.3 μm as shown in Table 1.
Met. The contained impurity elements found by optical emission analysis are shown in Table 2, and the content of each element was 10 ppm or less.
この粉体にPVAの5wt%水溶液を粉体質量に対して5wt%
加えて造粒した。造粒粉末を円筒形状の金型にいれ、油
圧プレスで1t/cm2で加圧圧縮して成形した。成形体をふ
た付きのマグネシヤのさやにいれて、酸化性雰囲気中、
1200℃で5時間焼成した。結果を第1表に示すが、焼結
体の密度は理論密度の99%であった。また比誘電率とQ
値を測定したところ、室温における比誘電率は20であ
り、Q値は19,200であった。A 5 wt% PVA aqueous solution was added to this powder in an amount of 5 wt% based on the mass of the powder.
In addition, it granulated. The granulated powder was put into a cylindrical mold and compressed by a hydraulic press at 1 t / cm 2 to be molded. Put the molded body in a pod of magnesia with a lid, in an oxidizing atmosphere,
It was baked at 1200 ° C. for 5 hours. The results are shown in Table 1, and the density of the sintered body was 99% of the theoretical density. Also, the relative permittivity and Q
When the values were measured, the relative dielectric constant at room temperature was 20, and the Q value was 19,200.
〔比較例2〕 BaCO3とMgOとTa2O5原料をBa:Mg:Taの比が3:1:2の比にな
るように秤量採取した。次に固相反応を均一に行わせる
ために、ボールミルなどによる湿式混合を行なった。混
合の終った原料を1000℃で10時間仮焼した後、ボールミ
ルを用いて湿式粉砕した。Comparative Example 2 BaCO 3 , MgO and Ta 2 O 5 raw materials were weighed and sampled so that the ratio of Ba: Mg: Ta was 3: 1: 2. Next, in order to carry out the solid-phase reaction uniformly, wet mixing using a ball mill or the like was performed. The mixed raw material was calcined at 1000 ° C. for 10 hours and then wet-milled using a ball mill.
エックス線回折パターンを測定したところ、Ba(Mg1/3Ta
2/3)O3の回折パターンが得られた。この粉体の化学組成
を蛍光エックス線測定により分析したところ、期待した
通りBa:Mg:Ta=3.0:1.0:2.0の組成を保有することが明
らかになった。しかし、発光分析による不純物量は第2
表に示すとおりであり、Na、Ca、Al、Fe、Mn及びNbの含
有量が実施例2に比較して多くなっていた。更に、遠心
沈降法粒度分布測定器により粉体の粒度分布を測定した
ところ、0.5μmから7.5μmの間に分布し、そのヒスト
グラムは複数のピークを持っていた。また平均粒径は2.
3μmであった。When the X-ray diffraction pattern was measured, Ba (Mg 1/3 Ta
A diffraction pattern of 2/3 ) O 3 was obtained. Analysis of the chemical composition of this powder by fluorescent X-ray measurement revealed that it possessed the composition of Ba: Mg: Ta = 3.0: 1.0: 2.0 as expected. However, the amount of impurities measured by optical emission analysis is the second
As shown in the table, the contents of Na, Ca, Al, Fe, Mn and Nb were higher than those in Example 2. Furthermore, when the particle size distribution of the powder was measured by a centrifugal sedimentation method particle size distribution analyzer, it was found to be distributed between 0.5 μm and 7.5 μm, and its histogram had a plurality of peaks. The average particle size is 2.
It was 3 μm.
この粉体にPVAの5wt%水溶液を粉体質量に対して5wt%
加えて造粒した。造粒粉末を円筒形状の金型に入れ、油
圧プレスで1t/cm2で加圧圧縮して成形した。第1表に示
すように、形成体をふた付きのマグネシヤのさやにいれ
て、酸化性雰囲気中、1200℃で5時間焼成しても充分な
焼結体密度が得られなかった。さらに順次焼成温度をあ
げて焼結性を確かめていくと、1500℃で5時間焼成した
とき、焼結体の密度は理論密度の99%となり、実施例2
と同等の密度が得られた。しかし、室温における比誘電
率は20であり、Q値は14900であって、特にQ値が実施
例2に比較してかなり劣っていた。A 5 wt% PVA aqueous solution was added to this powder in an amount of 5 wt% based on the mass of the powder.
In addition, it granulated. The granulated powder was put into a cylindrical mold and pressed by a hydraulic press at 1 t / cm 2 to be molded. As shown in Table 1, even if the formed body was placed in a sheath of a magnesia with a lid and fired at 1200 ° C. for 5 hours in an oxidizing atmosphere, a sufficient sintered body density could not be obtained. When the sinterability was confirmed by further raising the firing temperature in sequence, the density of the sintered body was 99% of the theoretical density when fired at 1500 ° C. for 5 hours.
The same density was obtained. However, the relative dielectric constant at room temperature was 20 and the Q value was 14900, which was particularly inferior to that of Example 2.
〔実施例3〕 アンモニア塩基性水酸化タンタルスラリー(三井金属鉱
業、Ta2O599.5%、Nb2O50.05%、Fe2O3<0.0005%、SiO
20.0020%、灼熱損失71.4%)にイオン交換水を加え、T
a2O5換算で24.4wt%のスラリーを調製した。また、アン
モニア塩基性水酸化ニオブスラリー(三井金属鉱業、Ta
2O5<0.02%、Fe2O3<0.0005%、SiO20.0020%、灼熱損
失67%)も同様に、Nb2O5換算で24.2wt%のスラリーを
調製した。調製したタンタルスラリー113.652gをビーカ
ーに採取し、調製したニオブスラリー7.658gを混合した
後、ZnO(正同化学、99.82%)の微粉5.7382gとBa(OH)2
・8H2O(和光純薬工業、98%)76.677gを加え、イオン交
換水を加えて全量を500mlとした。その上澄み液10mlを
分取し、硝酸銀を滴下したところ白色の沈殿は生じなか
った。残りを撹拌式ホモジナイザーを用いて均一分散さ
せた。実施例1と同じオートクレーブ内に入れたアルミ
ナビーカー中に仕込んで、スターラーにより150rpmで撹
拌しながら、120分で290℃まで昇温し、30分保持して反
応させた後、室温まで冷却し、反応物を遠沈管に採取し
た。遠心分離処理により遠沈管底部に分離した粉体を、
実施例1と同様の方法で洗浄し、塩素イオンを取り除い
た。実施例1と同様の方法で粉体を分析したところ、Ba
(Zn1/3Ta2/3)O3の単相であり、期待した通りBa:Zn:Ta:N
b=3.07:1.00:1.90:0.10の組成を保有し、含有不純物量
はいずれの元素も10ppm以下であり、その平均粒径は0.3
μmであった。[Example 3] Ammonia basic tantalum hydroxide slurry (Mitsui Mining & Smelting, Ta 2 O 5 99.5%, Nb 2 O 5 0.05%, Fe 2 O 3 <0.0005%, SiO 2
2 0.0020%, burning loss 71.4%) with ion-exchanged water
A 24.4 wt% slurry in terms of a 2 O 5 was prepared. Also, ammonia basic niobium hydroxide slurry (Mitsui Mining & Smelting, Ta
2 O 5 <0.02%, Fe 2 O 3 <0.0005%, SiO 2 0.0020%, and burning loss 67%), and similarly, a slurry of 24.2 wt% in terms of Nb 2 O 5 was prepared. After collecting 113.652 g of the prepared tantalum slurry in a beaker and mixing 7.658 g of the prepared niobium slurry, 5.7382 g of fine powder of ZnO (Shodo Kagaku, 99.82%) and Ba (OH) 2
・ 76.677 g of 8H 2 O (Wako Pure Chemical Industries, 98%) was added, and ion-exchanged water was added to bring the total amount to 500 ml. When 10 ml of the supernatant was collected and silver nitrate was added dropwise, white precipitate was not formed. The rest was uniformly dispersed using a stirring homogenizer. The mixture was placed in an alumina beaker placed in the same autoclave as in Example 1, heated to 290 ° C. in 120 minutes while stirring at 150 rpm with a stirrer, held for 30 minutes to react, and then cooled to room temperature, The reaction product was collected in a centrifuge tube. The powder separated at the bottom of the centrifuge tube by centrifugal separation,
It was washed in the same manner as in Example 1 to remove chlorine ions. When the powder was analyzed by the same method as in Example 1, it was found that Ba
(Zn 1/3 Ta 2/3 ) O 3 single phase, as expected Ba: Zn: Ta: N
b = 3.07: 1.00: 1.90: 0.10, the content of impurities is 10ppm or less, and the average particle size is 0.3.
was μm.
この粉体を実施例1と同様の方法で成形し、1200℃で5
時間焼成すると、焼結体の密度は7.63g/cm3に達した。
また、実施例1と同様の方法で誘電特性を測定したとこ
ろ、共振周波数10.0GHzでの室温比誘電率は30.5であ
り、Q値は10,500であった。This powder was molded in the same manner as in Example 1
After time firing, the density of the sintered body reached 7.63 g / cm 3 .
Further, when the dielectric properties were measured by the same method as in Example 1, the room temperature relative permittivity at the resonance frequency of 10.0 GHz was 30.5, and the Q value was 10,500.
〔比較例3〕 BaCO3(99.98%、石原産業)18.4696g、ZnO(99.82%、
正同化学)2.5179g、Ta2O5(99.8%、三井金属鉱業)1
2.3095g及びNb2O5(99.8%、三井金属鉱業)0.8218gを2
50mlポットに秤量し、媒体をクロロセンとしてボールミ
ル混合した。混合粉を乾燥し、700kg/cm2の圧力でディ
スク状に成形した後、1050℃で8時間仮焼し、これを水
を媒体としてボールミル解砕して微粉化したところ、平
均粒径は1.8μmとなった。バインダーを添加した後、1
t/cm2の圧力でディスク状に成形し、1350℃から1575℃
で焼成したが、緻密な焼結体は得られなかった。[Comparative Example 3] BaCO 3 (99.98%, Ishihara Sangyo) 18.4696 g, ZnO (99.82%,
Shodo Kagaku) 2.5179g, Ta 2 O 5 (99.8%, Mitsui Mining & Smelting) 1
2.3095g and Nb 2 O 5 (99.8%, Mitsui Mining & Smelting) 0.8218g 2
Weighed into a 50 ml pot and ball mill mixed with chlorothene as the medium. The mixed powder was dried, shaped into a disc at a pressure of 700 kg / cm 2 , and then calcined at 1050 ° C for 8 hours, and this was crushed into fine particles by ball milling with water as a medium. became μm. After adding the binder, 1
Disc-shaped at a pressure of t / cm 2 , 1350 ℃ to 1575 ℃
However, a dense sintered body could not be obtained.
〔実施例4〕 16%塩化チタン水溶液(大阪チタニウム)100.00gと16
%オキシ塩化ジルコニウム水溶液(第一稀元素化学)7
5.20gを混合し、塩化スズ(97wt%、和光純薬工業)4.5
29gを加えて溶解し、2NのNaOH水溶液をpH=10となるま
で撹拌しながら滴下し、共沈物を得た。このスラリーを
遠心分離器に掛け、上澄み液を除いて沈澱物を分離し
た。更に、実施例1と同じ方法で洗浄し、塩素イオンを
取り除いた。この混合物にイオン交換水を加えて全量を
500mlとした。その上澄み液10mlを分取し、硝酸銀を滴
下したところ白色の沈殿は生じなかった。残りを超音波
洗浄器で撹拌して分散させて得たスラリーをオートクレ
ーブに、実施例3と同様に仕込んで、100〜150rpmで撹
拌しながら120分で240℃まで昇温し、0.5時間水熱処理
した。[Example 4] 16% titanium chloride aqueous solution (Osaka Titanium) 100.00 g and 16
% Zirconium oxychloride aqueous solution (first rare element chemistry) 7
Mix 5.20g, tin chloride (97wt%, Wako Pure Chemical Industries) 4.5
29 g was added and dissolved, and 2N NaOH aqueous solution was added dropwise with stirring until pH = 10 to obtain a coprecipitate. This slurry was put into a centrifuge, and the supernatant was removed to separate the precipitate. Further, it was washed in the same manner as in Example 1 to remove chlorine ions. Ion-exchanged water was added to this mixture to make the total amount.
It was set to 500 ml. When 10 ml of the supernatant was collected and silver nitrate was added dropwise, white precipitate was not formed. The slurry obtained by stirring and dispersing the rest with an ultrasonic cleaner was charged into an autoclave in the same manner as in Example 3, heated to 240 ° C. in 120 minutes while stirring at 100 to 150 rpm, and hydrothermally treated for 0.5 hour. did.
反応終了後、スラリーを濾別して水洗し、真空乾燥器内
で乾燥させた。実施例1と同様の方法で分析したとこ
ろ、ZrTiO4と同じ結晶相が確認され、期待した通りZr:S
n:Ti=0.80:0.20:1.00の組成を保有しており、含有不純
物量はいずれの元素も10ppm以下であり、その平均粒径
は0.2μmであった。After the reaction was completed, the slurry was filtered, washed with water, and dried in a vacuum dryer. When analyzed by the same method as in Example 1, the same crystal phase as ZrTiO 4 was confirmed, and as expected, Zr: S
The composition had a composition of n: Ti = 0.80: 0.20: 1.00, the content of impurities in each element was 10 ppm or less, and the average particle size was 0.2 μm.
この粉体を実施例1と同様の方法で成形し、1250℃で5
時間焼成すると、焼結体の密度は5.17g/cm3に達した。
実施例1と同様の方法で誘電特性を測定したところ、共
振周波数10GHzでの室温比誘電率は37であり、Q値は7,3
00であった。This powder was molded in the same manner as in Example 1, and was molded at 1250 ° C for 5
After time firing, the density of the sintered body reached 5.17 g / cm 3 .
When the dielectric characteristics were measured by the same method as in Example 1, the room temperature relative permittivity at a resonance frequency of 10 GHz was 37, and the Q value was 7,3.
It was 00.
〔比較例4〕 ZrO2、TiO2及びSnO2を原料として、250mlボールミルで
クロロセンを用いて20時間混合を行い、乾燥後、950℃
で2時間仮焼した。これをボールミルで2時間水解砕し
たところ、平均粒径は1.5μmとなった。5%PVA溶液を
用いて造粒し、1t/cm2でディスク状に成形して、1400℃
で5時間焼成すると、密度は5.16g/cm3となった。実施
例1と同様の方法で誘電特性を測定したところ、共振周
波数10GHzでの室温比誘電率は36であり、Q値は6,680で
あった。[Comparative Example 4] Using ZrO 2 , TiO 2 and SnO 2 as raw materials, mixing was performed for 20 hours using chlorothene in a 250 ml ball mill, and after drying, 950 ° C.
It was calcined for 2 hours. When this was hydrolyzed with a ball mill for 2 hours, the average particle size was 1.5 μm. Granulate using 5% PVA solution, shape into a disk at 1t / cm 2 , and 1400 ℃
When baked for 5 hours, the density became 5.16 g / cm 3 . When the dielectric characteristics were measured by the same method as in Example 1, the room temperature relative dielectric constant at a resonance frequency of 10 GHz was 36, and the Q value was 6,680.
〔発明の効果〕 本発明の易焼結性マイクロ波誘電体用粉末は、平均粒径
が1μm以下と小さく、粒度分布が狭く、低温焼結性に
優れ、不純物を含まない高純度の粉体であり、焼結体と
したとき、粒界、不純物、格子欠陥などがはいりにく
く、均質で、反り、曲がりが少ない、緻密で、Q値が高
いマイクロ波誘電体用粉体を得ることができ、その産業
上の意義は極めて大きい。 [Advantages of the Invention] The easily sinterable microwave dielectric powder of the present invention has a small average particle size of 1 μm or less, a narrow particle size distribution, excellent low-temperature sinterability, and a high-purity powder containing no impurities. Therefore, when it is made into a sintered body, grain boundaries, impurities, lattice defects, etc. are hard to be introduced, and it is possible to obtain a powder for microwave dielectric material that is homogeneous, has little warpage and bending, is dense, and has a high Q value. , Its industrial significance is extremely large.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 // C04B 35/46 35/49 35/495 H01P 7/10 11/00 J C04B 35/49 Z ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location // C04B 35/46 35/49 35/495 H01P 7/10 11/00 J C04B 35/49 Z
Claims (1)
除去したものを原料として、オートクレーブに仕込み、
水熱合成した後、乾燥することを特徴とする粒径0.1〜
0.5μmの易焼結性マイクロ波誘電体用粉体の製造方
法。1. A material obtained by removing chloride ions attached to a metal hydroxide is charged into an autoclave,
Particle size 0.1 ~ characterized by drying after hydrothermal synthesis
A method for producing a powder for a 0.5 μm easily sinterable microwave dielectric.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2199273A JPH0747487B2 (en) | 1990-07-30 | 1990-07-30 | Method for producing powder for easily sinterable microwave dielectric |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2199273A JPH0747487B2 (en) | 1990-07-30 | 1990-07-30 | Method for producing powder for easily sinterable microwave dielectric |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0489317A JPH0489317A (en) | 1992-03-23 |
| JPH0747487B2 true JPH0747487B2 (en) | 1995-05-24 |
Family
ID=16405045
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2199273A Expired - Lifetime JPH0747487B2 (en) | 1990-07-30 | 1990-07-30 | Method for producing powder for easily sinterable microwave dielectric |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0747487B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104815636B (en) * | 2015-04-24 | 2017-07-04 | 黑龙江大学 | A kind of Mg1.2Ti1.8O5The preparation method of nanocatalyst |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5949650B2 (en) * | 1977-08-12 | 1984-12-04 | 松下電器産業株式会社 | Materials for dielectric resonators |
| JPS6131345A (en) * | 1984-07-25 | 1986-02-13 | 堺化学工業株式会社 | Manufacture of composition |
| JPH06649B2 (en) * | 1984-10-12 | 1994-01-05 | ソニー株式会社 | Method for producing fine dielectric particles |
| JPS6227328A (en) * | 1985-07-23 | 1987-02-05 | Ube Ind Ltd | Method for producing easily sinterable perovskite and its solid solution raw material powder |
| JPS6272525A (en) * | 1985-09-27 | 1987-04-03 | Fuji Titan Kogyo Kk | Production of barium titanate or strontium titanate |
-
1990
- 1990-07-30 JP JP2199273A patent/JPH0747487B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0489317A (en) | 1992-03-23 |
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