JP2015006970A - Magnesium oxide, production method thereof, and stacked ceramic capacitor containing the same as additive - Google Patents
Magnesium oxide, production method thereof, and stacked ceramic capacitor containing the same as additive Download PDFInfo
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- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 title claims abstract description 80
- 239000000395 magnesium oxide Substances 0.000 title claims abstract description 75
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 title claims abstract description 69
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 27
- 239000000654 additive Substances 0.000 title claims abstract description 13
- 230000000996 additive effect Effects 0.000 title claims abstract description 12
- 239000003985 ceramic capacitor Substances 0.000 title claims abstract description 9
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims abstract description 31
- 239000000347 magnesium hydroxide Substances 0.000 claims abstract description 31
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims abstract description 31
- 150000002681 magnesium compounds Chemical class 0.000 claims abstract description 27
- 238000001354 calcination Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000001035 drying Methods 0.000 claims abstract description 11
- 239000007864 aqueous solution Substances 0.000 claims abstract description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 12
- 238000006243 chemical reaction Methods 0.000 claims description 12
- 238000005406 washing Methods 0.000 claims description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 11
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 10
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- 239000000443 aerosol Substances 0.000 claims description 6
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 claims description 6
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 6
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 6
- 238000001308 synthesis method Methods 0.000 claims description 6
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 5
- UEGPKNKPLBYCNK-UHFFFAOYSA-L magnesium acetate Chemical compound [Mg+2].CC([O-])=O.CC([O-])=O UEGPKNKPLBYCNK-UHFFFAOYSA-L 0.000 claims description 3
- 239000011654 magnesium acetate Substances 0.000 claims description 3
- 235000011285 magnesium acetate Nutrition 0.000 claims description 3
- 229940069446 magnesium acetate Drugs 0.000 claims description 3
- QENHCSSJTJWZAL-UHFFFAOYSA-N magnesium sulfide Chemical compound [Mg+2].[S-2] QENHCSSJTJWZAL-UHFFFAOYSA-N 0.000 claims description 3
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- 239000000243 solution Substances 0.000 abstract description 4
- 238000004140 cleaning Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 30
- 230000008569 process Effects 0.000 description 18
- 239000000843 powder Substances 0.000 description 12
- 238000000445 field-emission scanning electron microscopy Methods 0.000 description 11
- 239000002245 particle Substances 0.000 description 11
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 5
- 229910002113 barium titanate Inorganic materials 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 238000002441 X-ray diffraction Methods 0.000 description 3
- 238000000498 ball milling Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- DHRRIBDTHFBPNG-UHFFFAOYSA-L magnesium dichloride hexahydrate Chemical compound O.O.O.O.O.O.[Mg+2].[Cl-].[Cl-] DHRRIBDTHFBPNG-UHFFFAOYSA-L 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910019092 Mg-O Inorganic materials 0.000 description 1
- 229910019395 Mg—O Inorganic materials 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 238000001856 aerosol method Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- UNYOJUYSNFGNDV-UHFFFAOYSA-M magnesium monohydroxide Chemical compound [Mg]O UNYOJUYSNFGNDV-UHFFFAOYSA-M 0.000 description 1
- CRGZYKWWYNQGEC-UHFFFAOYSA-N magnesium;methanolate Chemical compound [Mg+2].[O-]C.[O-]C CRGZYKWWYNQGEC-UHFFFAOYSA-N 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F5/00—Compounds of magnesium
- C01F5/02—Magnesia
- C01F5/06—Magnesia by thermal decomposition of magnesium compounds
- C01F5/08—Magnesia by thermal decomposition of magnesium compounds by calcining magnesium hydroxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F5/00—Compounds of magnesium
- C01F5/14—Magnesium hydroxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/20—Particle morphology extending in two dimensions, e.g. plate-like
- C01P2004/24—Nanoplates, i.e. plate-like particles with a thickness from 1-100 nanometer
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES, LIGHT-SENSITIVE OR TEMPERATURE-SENSITIVE DEVICES OF THE ELECTROLYTIC TYPE
- H01G4/00—Fixed capacitors; Processes of their manufacture
- H01G4/002—Details
- H01G4/018—Dielectrics
- H01G4/06—Solid dielectrics
- H01G4/08—Inorganic dielectrics
- H01G4/12—Ceramic dielectrics
- H01G4/1209—Ceramic dielectrics characterised by the ceramic dielectric material
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Ceramic Capacitors (AREA)
- Fixed Capacitors And Capacitor Manufacturing Machines (AREA)
Abstract
Description
本発明は、酸化マグネシウム、その製造方法、及びそれを添加剤として含む積層型セラミックキャパシタに関する。 The present invention relates to magnesium oxide, a method for producing the same, and a multilayer ceramic capacitor containing the same as an additive.
酸化マグネシウムはマグネシウムと酸素との化合物であり、マグネシア(magnesia)または苦土とも呼ばれる白色粉末の物質であって、MgOの化学式で表される。 Magnesium oxide is a compound of magnesium and oxygen, and is a white powder substance, also called magnesia or magnesia, represented by the chemical formula of MgO.
酸化マグネシウムは、融点が高く(2800℃)、高温で耐塩基性及び電気絶縁性に優れており、熱膨張係数及び熱伝導率が大きいだけでなく、光透過率が高い。このような酸化マグネシウムの様々な特性により、従来からルツボ、耐火レンガなどの耐熱構造用材料、防炎材料、絶縁材料、光透過材料などとして用いられているだけでなく、各種添加剤、触媒や吸着剤、マグネシアセメント、医薬品などとしても用いられている。 Magnesium oxide has a high melting point (2800 ° C.), excellent base resistance and electrical insulation at high temperatures, and has a high light transmittance as well as a large coefficient of thermal expansion and thermal conductivity. Due to the various properties of magnesium oxide, it has been used not only as heat-resistant structural materials such as crucibles and refractory bricks, flameproof materials, insulating materials, and light-transmitting materials, but also with various additives, catalysts, It is also used as an adsorbent, magnesia cement, and pharmaceuticals.
特に、酸化マグネシウムはMLCCの製造時に添加剤として用いられることができるが、粉末の表面にシェル(shell)を形成することで、焼結時にチタン酸バリウム(BaTiO3)の粒成長及び他の添加剤元素のコア(core)内部への拡散を防止する役割をする。 In particular, magnesium oxide can be used as an additive during the production of MLCC, but by forming a shell on the surface of the powder, grain growth of barium titanate (BaTiO 3 ) and other additions during sintering It serves to prevent diffusion of the agent element into the core.
一般的な産業用酸化マグネシウム粉末を製造するためには、通常、海水と生石灰とを反応させて乾燥→粒状→仮焼の段階を経ることで、多くの不純物を含有する初期酸化マグネシウム粉末を製造する。その後、高純度の酸化マグネシウム粉末を製造するために、前記不純物を含有する酸化マグネシウム粉末を粉砕→水和反応→水酸化マグネシウム→溶解→洗浄→仮焼の段階を経ることで、高純度の酸化マグネシウム粉末を得る。 In order to produce general industrial magnesium oxide powder, it is usually produced by reacting seawater and quicklime, followed by drying → granular → calcination, to produce initial magnesium oxide powder containing many impurities To do. Thereafter, in order to produce high-purity magnesium oxide powder, the magnesium oxide powder containing the impurities is pulverized, hydrated, magnesium hydroxide, dissolved, washed, calcined, and then subjected to high-purity oxidation. Obtain magnesium powder.
しかし、上記のような製造工程は、多くの段階の工程を経なければならないため、工程が複雑であり、酸化マグネシウム粉末の生産コストが上昇する要因として作用するという問題がある。また、製造される酸化マグネシウムの純度が99.7%以下であり、このような純度の限界のため、主に中低級のルツボに適用されている。 However, since the manufacturing process as described above has to go through many stages, there is a problem that the process is complicated and acts as a factor that increases the production cost of the magnesium oxide powder. Further, the purity of magnesium oxide to be produced is 99.7% or less, and due to such a limit of purity, it is mainly applied to middle and lower crucibles.
上記のような工程上の問題点を解決するための方法として、特許文献1には、燃焼気相法の一つである電磁波プラズマ装置から電磁波プラズマを発生させて、単一の工程により水酸化マグネシウムから高純度の酸化マグネシウム粉末を製造する方法が提案されている。しかし、前記工程は、工程の単純化は達成したが、気相法の製造方式の特徴である高価の装備が要求されるという問題があるため、コスト競争力の問題が依然として残っている。 As a method for solving the problems in the process as described above, Patent Document 1 discloses that an electromagnetic wave plasma is generated from an electromagnetic wave plasma apparatus which is one of combustion gas phase methods, and hydroxylated by a single process. A method for producing high-purity magnesium oxide powder from magnesium has been proposed. However, although the process has been simplified, there is still a problem of cost competitiveness because there is a problem that expensive equipment, which is a feature of the gas phase method, is required.
また、塩化マグネシウムと炭酸水素ナトリウムをボールミルして混合した後、乾燥→1次熱処理→未反応物の洗浄→最終熱処理の段階を経ることで純粋な酸化マグネシウム粉末を製造する方法が特許文献2に提案されている。
Further,
より詳細には、1段階のボールミル過程で、塩化マグネシウムと炭酸水素ナトリウムを混合した後、湿式ボールミルを3時間行い、2段階では、湿式ボールミルにより混合された混合物から水気を除去するために80℃で24時間乾燥する。3段階の1次熱処理過程では、非晶質相Mg‐O物質を安全なMgO結晶に転換させるために600〜900℃で2時間熱処理し、4段階では、熱処理された生成物に残留する塩化ナトリウムを除去するために、水を用いた洗浄及び濾過を4回繰り返す。5段階では、水で洗浄時に生成されたMgOHをさらに酸化させて酸化マグネシウムに転換させるが、この際の温度条件は少なくとも800℃〜1000℃である。 More specifically, after mixing magnesium chloride and sodium bicarbonate in a one-stage ball mill process, the wet ball mill is performed for 3 hours, and in the second stage, 80 ° C. is used to remove moisture from the mixture mixed by the wet ball mill. For 24 hours. In the three-stage primary heat treatment process, the amorphous phase Mg—O material is heat-treated at 600 to 900 ° C. for 2 hours in order to convert it into safe MgO crystals, and in the fourth stage, the residual chloride in the heat-treated product is obtained. In order to remove the sodium, washing with water and filtration are repeated four times. In the fifth stage, MgOH generated during washing with water is further oxidized and converted to magnesium oxide, and the temperature condition at this time is at least 800 ° C to 1000 ° C.
しかし、上記のような従来の方式は、その製造段階が1段階〜5段階と複雑であり、ボールミル、洗浄、濾過時に発生しえる酸化マグネシウムの損失量、及び二回の熱処理過程が非常に高温で行われる点などの問題を有する。得られた酸化マグネシウム粉末は、図1のFE‐SEM写真及び図2のXRD結果から確認できるように、約1〜5マイクロンの粒度を有し、繊維凝集の形態を示す。 However, the conventional method as described above has a complicated manufacturing process of 1 to 5 stages, and the amount of magnesium oxide that can be lost during ball milling, cleaning, and filtration, and the two heat treatment processes are extremely high. There are problems such as the point to be done in. As can be confirmed from the FE-SEM photograph of FIG. 1 and the XRD result of FIG. 2, the obtained magnesium oxide powder has a particle size of about 1 to 5 microns and exhibits a form of fiber aggregation.
また、他の酸化マグネシウムの合成法として、エアロゲル(AP‐MgO)方法がある(Chem.Mater.1991,3,175‐181)。メタノール/トルエン溶液にマグネシウムメチラート(Magnesium methylate)及び水を入れ、室温で徐々に加水分解させながら一晩反応することで、白色のゾルが製造される(図3参照)。この結果物をオートクレーブで窒素ガス注入した後、265℃で放置する。この際に加水分解されたヒドロキシ基(OH group)とトルエン溶媒との間の相互作用によりゲル構造を保護すると推定している。 Another method for synthesizing magnesium oxide is an airgel (AP-MgO) method (Chem. Mater. 1991, 3, 175-181). A white sol is produced by adding magnesium methylate and water to a methanol / toluene solution and reacting overnight while gradually hydrolyzing at room temperature (see FIG. 3). The resulting product is injected with nitrogen gas in an autoclave and then left at 265 ° C. It is estimated that the gel structure is protected by the interaction between the hydrolyzed hydroxy group (OH group) and the toluene solvent.
また、酸化マグネシウム金属粉末を合成する方法のうち液相法は様々な長所を有する。しかし、トルエンやエチレングリコールなどの有機溶媒を用いる製造法は、液相法の多くの長所にも関らず、物質を扱う作業者及び研究者に与えられる毒性や環境汚染の問題がある。 Among the methods for synthesizing magnesium oxide metal powder, the liquid phase method has various advantages. However, the production method using an organic solvent such as toluene and ethylene glycol has problems of toxicity and environmental pollution given to workers and researchers who handle materials, despite the many advantages of the liquid phase method.
上記のように、従来の酸化マグネシウムの製造方法は、非常に複雑な過程を経るだけでなく、大部分が高温で行われるため工程が難しく、高価の装備が要求されるなど、実際に工程に適用するには大きな困難があった。 As described above, the conventional method for producing magnesium oxide not only goes through a very complicated process, but the process is difficult because most of it is performed at high temperature, and expensive equipment is required. There were great difficulties to apply.
したがって、本発明は、水系で反応がなされ、比較的簡単な工程により低温で短時間に酸化マグネシウムを製造する方法を提供することをその目的とする。 Accordingly, an object of the present invention is to provide a method for producing magnesium oxide at a low temperature in a short time by a relatively simple process in which the reaction is carried out in an aqueous system.
また、本発明の他の目的は、上記の方法により製造され、六角板状の粒子を有する酸化マグネシウムを提供することにある。 Another object of the present invention is to provide magnesium oxide produced by the above method and having hexagonal plate-like particles.
本発明のさらに他の目的は、前記酸化マグネシウムを誘電層の添加剤として含む積層型セラミックキャパシタを提供することにある。 Still another object of the present invention is to provide a multilayer ceramic capacitor containing the magnesium oxide as an additive of a dielectric layer.
本発明の一形態による酸化マグネシウムは、直径が30〜100nmであり、厚さが5〜20nmである六角板状を有することを特徴とする。 Magnesium oxide according to one embodiment of the present invention has a hexagonal plate shape with a diameter of 30 to 100 nm and a thickness of 5 to 20 nm.
また、本発明の酸化マグネシウムの製造方法は、マグネシウム化合物を水に溶解させたマグネシウム化合物水溶液に塩基を添加し、50〜100℃で反応させて水酸化マグネシウムを析出させる段階と、前記析出された水酸化マグネシウムを洗浄及び乾燥する段階と、前記乾燥された水酸化マグネシウムを仮焼させることで酸化マグネシウムを製造する段階と、を含むことができる。 Also, the method for producing magnesium oxide of the present invention comprises adding a base to a magnesium compound aqueous solution in which a magnesium compound is dissolved in water and reacting at 50 to 100 ° C. to precipitate magnesium hydroxide, The step of washing and drying magnesium hydroxide and the step of producing magnesium oxide by calcining the dried magnesium hydroxide can be included.
前記マグネシウム化合物と塩基の反応は大気圧状態でなされることができる。 The reaction between the magnesium compound and the base can be performed at atmospheric pressure.
前記マグネシウム化合物と塩基の反応はエアロゾル合成法によりなされることができる。 The reaction between the magnesium compound and the base can be performed by an aerosol synthesis method.
前記マグネシウム化合物は、マグネシウム硝酸物、マグネシウム塩化物、マグネシウム硫化物、及びマグネシウム酢酸物からなる群から選択される1種以上であることができる。 The magnesium compound may be one or more selected from the group consisting of magnesium nitrate, magnesium chloride, magnesium sulfide, and magnesium acetate.
前記塩基は、水酸化ナトリウム、水酸化カリウム、炭酸ナトリウム、及び炭酸カリウムからなる群から選択される1種以上であることができる。 The base may be one or more selected from the group consisting of sodium hydroxide, potassium hydroxide, sodium carbonate, and potassium carbonate.
前記マグネシウム化合物に対する塩基の含量は1:1〜1:5の重量比であることが好ましい。 The base content with respect to the magnesium compound is preferably in a weight ratio of 1: 1 to 1: 5.
前記マグネシウム化合物水溶液の濃度は0.1〜1重量%であることが好ましい。 The concentration of the magnesium compound aqueous solution is preferably 0.1 to 1% by weight.
前記水酸化マグネシウムの洗浄には、水、メタノール、エタノール、n‐プロパノール、イソプロパノールから選択される1種以上を用いることができる。 For washing the magnesium hydroxide, at least one selected from water, methanol, ethanol, n-propanol, and isopropanol can be used.
前記水酸化マグネシウムの乾燥は80〜100℃で2〜6時間行われることができる。 The magnesium hydroxide can be dried at 80 to 100 ° C. for 2 to 6 hours.
前記水酸化マグネシウムの仮焼は400〜500℃で2〜4時間行われることができる。 The calcination of the magnesium hydroxide can be performed at 400 to 500 ° C. for 2 to 4 hours.
また、本発明は、前記六角板状の酸化マグネシウムを誘電体層の添加剤として含む積層型セラミックキャパシタを提供することができる。 In addition, the present invention can provide a multilayer ceramic capacitor containing the hexagonal plate-like magnesium oxide as an additive of a dielectric layer.
本発明によると、エアロゾル合成法により、30〜100nmの直径及び一定の厚さを有する六角板状の酸化マグネシウムを製造することができる。 According to the present invention, hexagonal plate-like magnesium oxide having a diameter of 30 to 100 nm and a constant thickness can be produced by an aerosol synthesis method.
また、本発明によると、従来のエアロゾル合成法より低い温度で反応が行われるため工程効率が高く、また有機溶媒を用いずに水系で反応させて酸化マグネシウムを製造することができる。 In addition, according to the present invention, since the reaction is performed at a temperature lower than that of the conventional aerosol synthesis method, the process efficiency is high, and magnesium oxide can be produced by reacting in an aqueous system without using an organic solvent.
このような本発明の酸化マグネシウムが積層型セラミックキャパシタの誘電体層の添加剤として含まれることで、チタン酸バリウムコアの粉末の表面にシェルを効果的に形成して、焼結時における前記チタン酸バリウムの粒成長及び他の添加剤元素のコア内部への拡散を効果的に防止することができる。 By including the magnesium oxide of the present invention as an additive in the dielectric layer of the multilayer ceramic capacitor, a shell is effectively formed on the surface of the barium titanate core powder, and the titanium during sintering It is possible to effectively prevent grain growth of barium acid and diffusion of other additive elements into the core.
以下、本発明をより詳細に説明すると次の通りである。 Hereinafter, the present invention will be described in more detail as follows.
本明細書で用いられる用語は、特定の実施形態を説明するために用いられ、本発明を限定しようとするものではない。本明細書に用いられたように、単数型は文脈上異なる場合を明白に指摘するものでない限り、複数型を含むことができる。また、本明細書で用いられる「含む(comprise)」及び/または「含んでいる(comprising)」は言及された形状、数字、段階、動作、部材、要素、及び/またはこれらの組み合わせが存在することを特定するものであり、一つ以上の他の形状、数字、動作、部材、要素、及び/またはこれらの組み合わせの存在または付加を排除するものではない。 The terminology used herein is for the purpose of describing particular embodiments and is not intended to be limiting of the invention. As used herein, the singular form may include the plural form unless the context clearly dictates otherwise. Also, as used herein, “comprise” and / or “comprising” includes the stated shapes, numbers, steps, actions, members, elements, and / or combinations thereof. It does not exclude the presence or addition of one or more other shapes, numbers, actions, members, elements, and / or combinations thereof.
本発明は、誘電体層でシェルを構成する添加剤として用いられることができる六角板状の酸化マグネシウムとその製造方法、及びそれを含む積層型セラミックキャパシタに関する。 The present invention relates to hexagonal plate-like magnesium oxide that can be used as an additive constituting a shell with a dielectric layer, a method for manufacturing the same, and a multilayer ceramic capacitor including the same.
本発明は、従来の液相法や エアロゾル法を利用して酸化マグネシウムを製造する際の、作業工程が難しく、複雑であるという問題を解決して、水を溶媒として用いて水系で反応させることができ、反応温度が従来の工程に比べ低いだけでなく、反応時間も比較的短い酸化マグネシウムの製造方法を提供することができる。 The present invention solves the problem that the manufacturing process is difficult and complicated when producing magnesium oxide using the conventional liquid phase method or aerosol method, and reacts in an aqueous system using water as a solvent. In addition, it is possible to provide a method for producing magnesium oxide that not only has a lower reaction temperature than conventional processes but also has a relatively short reaction time.
上記のような本発明による酸化マグネシウムの製造方法は、図4に図示されたように、合成‐洗浄‐乾燥‐仮焼の段階を含むことができる。 The method for producing magnesium oxide according to the present invention as described above may include a synthesis-washing-drying-calcination step as illustrated in FIG.
合成段階では、マグネシウム化合物を水に溶解させたマグネシウム化合物水溶液を製造し、これに塩基を添加及び反応させて水酸化マグネシウムを析出させる。 In the synthesis stage, a magnesium compound aqueous solution in which a magnesium compound is dissolved in water is produced, and a base is added and reacted to precipitate magnesium hydroxide.
前記マグネシウム化合物を水に溶解させることは、昇温させなくても撹拌だけで数分内に容易に行われることができる。この際、前記マグネシウム化合物を完全に溶解した後に塩基を添加することが好ましい。マグネシウム化合物が完全に溶解されていない状態で塩基を添加すると、結果物の粒子状が不均一に合成される恐れがあるため注意しなければならない。 Dissolving the magnesium compound in water can be easily performed within a few minutes only by stirring without raising the temperature. At this time, it is preferable to add the base after completely dissolving the magnesium compound. If the base is added in a state where the magnesium compound is not completely dissolved, care must be taken because the resulting particles may be synthesized non-uniformly.
前記マグネシウム化合物は、水溶液での濃度を0.1〜1重量%にすることが粒子の形状を維持するという点で好ましい。 The magnesium compound is preferably 0.1 to 1% by weight in aqueous solution in terms of maintaining the particle shape.
前記マグネシウム化合物は、マグネシウム硝酸物、マグネシウム塩化物、マグネシウム硫化物、及びマグネシウム酢酸物からなる群から選択される1種以上であることができる。 The magnesium compound may be one or more selected from the group consisting of magnesium nitrate, magnesium chloride, magnesium sulfide, and magnesium acetate.
また、本発明による前記塩基は、水に溶解させて添加するのではなく、前記マグネシウム化合物が溶解された水溶液に粉末状態の塩基を添加する。本発明による塩基としては、水酸化ナトリウム、水酸化カリウム、炭酸ナトリウム、及び炭酸カリウムからなる群から選択される1種以上が好ましく用いられることができる。 In addition, the base according to the present invention is not added after being dissolved in water, but a powdered base is added to an aqueous solution in which the magnesium compound is dissolved. As the base according to the present invention, one or more selected from the group consisting of sodium hydroxide, potassium hydroxide, sodium carbonate, and potassium carbonate can be preferably used.
また、本発明によると、前記マグネシウム化合物と塩基との反応は、特定ガス(gas)雰囲気が不要であり、大気圧条件で行うことができる。また、反応温度は従来のエアロゾル合成法の温度より遥かに低い50〜100℃で反応させることができ、反応時間も比較的短い1〜2時間の条件で行われることができる。 Also, according to the present invention, the reaction between the magnesium compound and the base does not require a specific gas atmosphere, and can be performed under atmospheric pressure conditions. Further, the reaction can be performed at 50 to 100 ° C., which is much lower than the temperature of the conventional aerosol synthesis method, and the reaction time can be carried out under a relatively short time of 1 to 2 hours.
前記反応温度が50℃未満である場合には、核が生成されても粒子形状が不均一であるという問題があり、100℃を超過する場合には、工程コストの問題があるため好ましくない。 When the reaction temperature is less than 50 ° C., there is a problem that the particle shape is non-uniform even when nuclei are generated, and when it exceeds 100 ° C., there is a problem in process cost, which is not preferable.
したがって、本発明の方法は、従来の エアロゾル合成法に比べ工程が単純化され、反応時間及び温度を効果的に低めることができるため、工程効率及びコストが改善されることができる。 Therefore, the method of the present invention is simplified in process as compared with the conventional aerosol synthesis method, and the reaction time and temperature can be effectively reduced, so that the process efficiency and cost can be improved.
本発明では、マグネシウム化合物に対する塩基の含量を調節して酸化マグネシウムのサイズを制御することができる。本発明の酸化マグネシウムの直径を30〜100nmに制御するための、マグネシウム化合物に対する塩基の含量は1:1〜1:5の重量比であることが好ましい。 In the present invention, the size of magnesium oxide can be controlled by adjusting the base content relative to the magnesium compound. In order to control the diameter of the magnesium oxide of the present invention to 30 to 100 nm, the content of the base with respect to the magnesium compound is preferably 1: 1 to 1: 5 by weight.
次に、前記合成段階で沈殿物として得られた水酸化マグネシウムを洗浄及び乾燥する。前記洗浄は、遠心分離機を用いて約2000〜4000rpmで数分間行うことで容易に固液分離され、分離された固体を溶媒で洗浄する。 Next, the magnesium hydroxide obtained as a precipitate in the synthesis step is washed and dried. The washing is easily carried out at about 2000 to 4000 rpm for several minutes using a centrifugal separator, and the solid is easily separated, and the separated solid is washed with a solvent.
前記溶媒としては、水、メタノール、エタノール、n‐プロパノール、イソプロパノールを用いることができる。また、前記洗浄は、前記洗浄溶媒を用いて2回以上繰り返して行うことが好ましい。洗浄過程は、沈澱された水酸化マグネシウムの凝集を最小化するために行われる過程であり、水及び有機溶媒を用いて連続的に洗浄することが好ましい。 As the solvent, water, methanol, ethanol, n-propanol, or isopropanol can be used. The washing is preferably repeated twice or more using the washing solvent. The washing process is a process performed to minimize the aggregation of the precipitated magnesium hydroxide, and it is preferable that the washing is performed continuously using water and an organic solvent.
前記洗浄された水酸化マグネシウムを十分に乾燥する過程が必要であり、本発明では、80〜100℃で2〜6時間行われることが好ましい。前記乾燥が十分に行われないと、粒子同士が互いに凝集するため好ましくない。 A process of sufficiently drying the washed magnesium hydroxide is necessary, and in the present invention, it is preferably performed at 80 to 100 ° C. for 2 to 6 hours. If the drying is not performed sufficiently, the particles aggregate with each other, which is not preferable.
最後に、前記乾燥された水酸化マグネシウムを仮焼させることで、酸化マグネシウムが得られる。従来は、前記仮焼を800〜1000℃で行っていたが、本発明では比較的低い温度である400〜500℃で2〜4時間行うことができる。 Finally, magnesium oxide is obtained by calcining the dried magnesium hydroxide. Conventionally, the calcination was performed at 800 to 1000 ° C., but in the present invention, it can be performed at 400 to 500 ° C., which is a relatively low temperature, for 2 to 4 hours.
前記焼成温度範囲で焼成させると、本発明による六角板状の粒子形態を有する酸化マグネシウムを製造することができる。 When calcined in the calcining temperature range, the magnesium oxide having a hexagonal plate-like particle form according to the present invention can be produced.
前記過程により最終製造された酸化マグネシウムは、直径が30〜100nmであり、厚さが5〜20nmである六角板状を有することができる。 The magnesium oxide finally manufactured by the above process may have a hexagonal plate shape with a diameter of 30 to 100 nm and a thickness of 5 to 20 nm.
また、本発明は、前記六角板状の酸化マグネシウムを誘電体層の添加剤として含む積層型セラミックキャパシタを提供することができる。 In addition, the present invention can provide a multilayer ceramic capacitor containing the hexagonal plate-like magnesium oxide as an additive of a dielectric layer.
前記酸化マグネシウムは、誘電体層の母材として用いられるチタン酸バリウムに添加され、前記チタン酸バリウム(BaTiO3)コアを覆うシェルを構成する物質であり、焼結時における前記チタン酸バリウムの粒成長及び他の添加剤元素のコア(core)内部への拡散を防止する役割をする。 The magnesium oxide is a substance that is added to barium titanate used as a base material of the dielectric layer and constitutes a shell that covers the barium titanate (BaTiO 3 ) core, and the particles of the barium titanate during sintering. It serves to prevent growth and diffusion of other additive elements into the core.
以下、本発明の好ましい実施例を詳細に説明する。以下の実施例は、本発明を例示するためのものに過ぎず、本発明の範囲がこれら実施例によって制限されることに解釈されてはならない。また、以下の実施例では、特定化合物を利用して例示したが、これらの均等物を用いた場合においても、同等類似の程度の効果を奏することができるということは、当業者において自明である。 Hereinafter, preferred embodiments of the present invention will be described in detail. The following examples are only for illustrating the present invention, and the scope of the present invention should not be construed as being limited by these examples. Further, in the following examples, specific compounds were used as examples. However, it is obvious to those skilled in the art that even when these equivalents are used, the same and similar effects can be obtained. .
[実施例1〜2]
塩化マグネシウム水和物を水に溶かして0.3重量%の塩化マグネシウム水和物水溶液を製造した後、水酸化ナトリウムを添加して80℃で2時間反応させた。前記塩化マグネシウム水和物に対する水酸化ナトリウムの含量はそれぞれ1:1、1:5の重量比となるようにした。
[Examples 1-2]
Magnesium chloride hydrate was dissolved in water to prepare a 0.3 wt% magnesium chloride hydrate aqueous solution, sodium hydroxide was added, and the mixture was reacted at 80 ° C. for 2 hours. The content of sodium hydroxide with respect to the magnesium chloride hydrate was set to a weight ratio of 1: 1 and 1: 5, respectively.
前記反応により水酸化マグネシウムが析出された。前記反応液を遠心分離機に入れて4000rpmの速度で4回遠心分離した。 Magnesium hydroxide was precipitated by the reaction. The reaction solution was placed in a centrifuge and centrifuged four times at a speed of 4000 rpm.
前記遠心分離された上層液を除去し、得られた水酸化マグネシウム沈殿物を水及びエタノールでそれぞれ2回ずつ洗浄した。 The centrifuged upper layer solution was removed, and the resulting magnesium hydroxide precipitate was washed twice with water and ethanol, respectively.
前記洗浄された水酸化マグネシウムを80℃で6時間完全乾燥した後、さらに400℃で2時間仮焼させて酸化マグネシウムを得た。 The washed magnesium hydroxide was completely dried at 80 ° C. for 6 hours and then calcined at 400 ° C. for 2 hours to obtain magnesium oxide.
[実験例1:FE‐SEM構造確認]
前記実施例1及び2の乾燥後に得られた水酸化マグネシウム、及び仮焼後に得られた酸化マグネシウムの構造をFE‐SEMで確認し、その結果を図5〜図8にそれぞれ示した。
[Experimental example 1: FE-SEM structure confirmation]
The structures of magnesium hydroxide obtained after drying in Examples 1 and 2 and magnesium oxide obtained after calcination were confirmed by FE-SEM, and the results are shown in FIGS.
実施例1及び2の乾燥後に得られた水酸化マグネシウムのFE‐SEM写真を示した図5及び図6を参照すると、六角板状の粒子を有することが分かる。 Referring to FIGS. 5 and 6 showing FE-SEM photographs of magnesium hydroxide obtained after drying in Examples 1 and 2, it can be seen that the particles have hexagonal plate-like particles.
また、実施例1及び2の仮焼後に得られた酸化マグネシウムのFE‐SEM写真を示した図7及び図8を参照すると、六角板状の粒子を有しており、30〜100nmの直径及び約5〜20nmの一定の厚さを有することを確認することができる。 Further, referring to FIG. 7 and FIG. 8 showing FE-SEM photographs of magnesium oxide obtained after calcining in Examples 1 and 2, it has hexagonal plate-like particles, and has a diameter of 30 to 100 nm and It can be seen that it has a constant thickness of about 5-20 nm.
[実験例2:XRD測定]
前記実施例1の仮焼前の水酸化マグネシウムから仮焼後の酸化マグネシウムへの転換が成されたかをXRD測定により確認し、その結果を図9に示した。
[Experimental example 2: XRD measurement]
Whether or not the magnesium hydroxide before calcination in Example 1 was converted to magnesium oxide after calcination was confirmed by XRD measurement, and the results are shown in FIG.
図9の結果のように、400℃で2時間仮焼させると、水酸化マグネシウムによるピークは減少し、酸化マグネシウムによるピークが増加することが分かる。 As shown in the results of FIG. 9, when calcined at 400 ° C. for 2 hours, the peak due to magnesium hydroxide decreases and the peak due to magnesium oxide increases.
Claims (12)
前記析出された水酸化マグネシウムを洗浄及び乾燥する段階と、
前記乾燥された水酸化マグネシウムを仮焼させることで酸化マグネシウムを製造する段階と、を含む、六角板状の酸化マグネシウムの製造方法。 Adding a base to a magnesium compound aqueous solution in which the magnesium compound is dissolved in water and reacting at 50 to 100 ° C. to precipitate magnesium hydroxide;
Washing and drying the precipitated magnesium hydroxide;
A step of producing magnesium oxide by calcining the dried magnesium hydroxide, and a method for producing hexagonal plate-like magnesium oxide.
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US20200075254A1 (en) * | 2018-08-29 | 2020-03-05 | Samsung Electro-Mechanics Co., Ltd. | Ceramic capacitor having metal oxide in side margin portions, and method of manufacturing the same |
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KR200446167Y1 (en) * | 2009-02-13 | 2009-10-05 | 나경원 | Tension adjusting apparatus for a cable |
CN108996530A (en) * | 2018-08-16 | 2018-12-14 | 军事科学院系统工程研究院卫勤保障技术研究所 | A kind of preparation method for nanometer magnesium oxide and a kind of nano magnesia-nanofiber composite felt and its preparation method and application |
CN108996530B (en) * | 2018-08-16 | 2020-09-22 | 军事科学院系统工程研究院卫勤保障技术研究所 | Preparation method of nano magnesium oxide, nano magnesium oxide-nano fiber composite felt, and preparation method and application thereof |
US20200075254A1 (en) * | 2018-08-29 | 2020-03-05 | Samsung Electro-Mechanics Co., Ltd. | Ceramic capacitor having metal oxide in side margin portions, and method of manufacturing the same |
US20200075256A1 (en) * | 2018-08-29 | 2020-03-05 | Samsung Electro-Mechanics Co., Ltd. | Ceramic capacitor and method of manufacturing the same |
US10650969B2 (en) * | 2018-08-29 | 2020-05-12 | Samsung Electro-Mechanics Co., Ltd. | Ceramic capacitor having metal or metal oxide in side margin portions, and method of manufacturing the same |
US10658114B2 (en) * | 2018-08-29 | 2020-05-19 | Samsung Electro-Mechanics Co., Ltd. | Ceramic capacitor having metal oxide in side margin portions, and method of manufacturing the same |
US10896781B2 (en) | 2018-08-29 | 2021-01-19 | Samsung Electro-Mechanics Co., Ltd. | Ceramic capacitor having metal or metal oxide in side margin portions, and method of manufacturing the same |
US11335503B2 (en) | 2018-08-29 | 2022-05-17 | Samsung Electro-Mechanics Co., Ltd. | Ceramic capacitor having metal or metal oxide in side margin portions, and method of manufacturing the same |
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