JP2933397B2 - Method for producing ferromagnetic iron oxide powder for magnetic recording - Google Patents
Method for producing ferromagnetic iron oxide powder for magnetic recordingInfo
- Publication number
- JP2933397B2 JP2933397B2 JP3001409A JP140991A JP2933397B2 JP 2933397 B2 JP2933397 B2 JP 2933397B2 JP 3001409 A JP3001409 A JP 3001409A JP 140991 A JP140991 A JP 140991A JP 2933397 B2 JP2933397 B2 JP 2933397B2
- Authority
- JP
- Japan
- Prior art keywords
- manganese
- particles
- iron oxide
- maghemite
- zinc
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 title claims description 110
- 230000005291 magnetic effect Effects 0.000 title claims description 59
- 239000000843 powder Substances 0.000 title claims description 44
- 230000005294 ferromagnetic effect Effects 0.000 title claims description 11
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 239000002245 particle Substances 0.000 claims description 71
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 49
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 claims description 42
- 230000005415 magnetization Effects 0.000 claims description 30
- 239000011701 zinc Substances 0.000 claims description 22
- 238000000034 method Methods 0.000 claims description 18
- 239000011572 manganese Substances 0.000 claims description 17
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 16
- 229910052725 zinc Inorganic materials 0.000 claims description 16
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 14
- 229910001437 manganese ion Inorganic materials 0.000 claims description 13
- 230000001590 oxidative effect Effects 0.000 claims description 13
- 229910017052 cobalt Inorganic materials 0.000 claims description 12
- 239000010941 cobalt Substances 0.000 claims description 12
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 12
- 229910052742 iron Inorganic materials 0.000 claims description 12
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 11
- 229910052748 manganese Inorganic materials 0.000 claims description 11
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 claims description 10
- 229910001289 Manganese-zinc ferrite Inorganic materials 0.000 claims description 8
- JIYIUPFAJUGHNL-UHFFFAOYSA-N [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[Mn++].[Mn++].[Mn++].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Zn++].[Zn++] Chemical compound [O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[O--].[Mn++].[Mn++].[Mn++].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Fe+3].[Zn++].[Zn++] JIYIUPFAJUGHNL-UHFFFAOYSA-N 0.000 claims description 8
- 229910052595 hematite Inorganic materials 0.000 claims description 8
- 239000011019 hematite Substances 0.000 claims description 8
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 8
- 150000001869 cobalt compounds Chemical class 0.000 claims description 7
- 150000001875 compounds Chemical class 0.000 claims description 7
- -1 iron ions Chemical class 0.000 claims description 7
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 7
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 claims description 7
- 208000005156 Dehydration Diseases 0.000 claims description 6
- 230000018044 dehydration Effects 0.000 claims description 6
- 238000006297 dehydration reaction Methods 0.000 claims description 6
- 229910001448 ferrous ion Inorganic materials 0.000 claims description 6
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 claims description 5
- 239000002243 precursor Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 description 30
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 23
- 239000007864 aqueous solution Substances 0.000 description 23
- 230000000052 comparative effect Effects 0.000 description 23
- 229910001873 dinitrogen Inorganic materials 0.000 description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 230000009467 reduction Effects 0.000 description 12
- 229940099596 manganese sulfate Drugs 0.000 description 10
- 239000011702 manganese sulphate Substances 0.000 description 10
- 235000007079 manganese sulphate Nutrition 0.000 description 10
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 10
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 10
- 229910000368 zinc sulfate Inorganic materials 0.000 description 10
- 229960001763 zinc sulfate Drugs 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 8
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 8
- 239000003513 alkali Substances 0.000 description 7
- 230000003647 oxidation Effects 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- WAEMQWOKJMHJLA-UHFFFAOYSA-N Manganese(2+) Chemical compound [Mn+2] WAEMQWOKJMHJLA-UHFFFAOYSA-N 0.000 description 6
- 229910021645 metal ion Inorganic materials 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000010419 fine particle Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000002585 base Substances 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000007858 starting material Substances 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000007900 aqueous suspension Substances 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 239000011790 ferrous sulphate Substances 0.000 description 2
- 235000003891 ferrous sulphate Nutrition 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052598 goethite Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- AEIXRCIKZIZYPM-UHFFFAOYSA-M hydroxy(oxo)iron Chemical compound [O][Fe]O AEIXRCIKZIZYPM-UHFFFAOYSA-M 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 238000001465 metallisation Methods 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 229920006026 co-polymeric resin Polymers 0.000 description 1
- 229910001429 cobalt ion Inorganic materials 0.000 description 1
- 229910000361 cobalt sulfate Inorganic materials 0.000 description 1
- 229940044175 cobalt sulfate Drugs 0.000 description 1
- XLJKHNWPARRRJB-UHFFFAOYSA-N cobalt(2+) Chemical compound [Co+2] XLJKHNWPARRRJB-UHFFFAOYSA-N 0.000 description 1
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 229940032950 ferric sulfate Drugs 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 230000010365 information processing Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002506 iron compounds Chemical class 0.000 description 1
- 239000006247 magnetic powder Substances 0.000 description 1
- WJZHMLNIAZSFDO-UHFFFAOYSA-N manganese zinc Chemical compound [Mn].[Zn] WJZHMLNIAZSFDO-UHFFFAOYSA-N 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229920006267 polyester film Polymers 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 150000003752 zinc compounds Chemical class 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
Landscapes
- Hard Magnetic Materials (AREA)
- Soft Magnetic Materials (AREA)
Description
【0001】産業上の利用分野 本発明は、塗布型高記録密度磁気記録媒体に用いられる
改良された磁性粉末及びその製造方法に関し、更に詳し
くはマグヘマイト粒子もしくは中間体粒子表面を微量の
金属イオンで変成させることにより飽和磁化量の向上を
計った強磁性酸化鉄粉末及びその製造方法に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improved magnetic powder used for a coating type high recording density magnetic recording medium and a method for producing the same, and more particularly, to a method for treating a surface of maghemite particles or intermediate particles with a trace amount of metal ions. The present invention relates to a ferromagnetic iron oxide powder having an improved saturation magnetization by being denatured and a method for producing the same.
【0002】本発明が解決しようとする問題点 近年の磁気記録再生機器の小型軽量化及び磁気記録にお
ける情報処理量の拡大化に伴い、磁気記録媒体の高記録
密度化、高出力化および低ノイズ化の指向が益々高まっ
てきている。これとあいまって、磁気記録媒体に使用さ
れる磁性酸化鉄粉末については、高保磁力化、高飽和磁
化量化、微粒子化かつ高配向高充填化など諸特性向上の
要求が一段と強まっている。Problems to be Solved by the Present Invention With the recent reduction in size and weight of magnetic recording / reproducing equipment and the increase in the amount of information processing in magnetic recording, higher recording density, higher output, and lower noise of magnetic recording media have been achieved. Increasingly, the direction of the shift is increasing. In conjunction with this, with respect to the magnetic iron oxide powder used for the magnetic recording medium, demands for improving various properties such as high coercive force, high saturation magnetization, fine particles and high orientation and high filling have been further increased.
【0003】ところで低ノイズ化を実現させるためには
微粒子化が最も有効な手段であるが、これに伴って飽和
磁化量の低下がさけられないという問題がある。また配
向性及び充填性の低下も同時に生ずる。すなわち低ノイ
ズ化と高出力化の両方の指向を満足させるためには微粒
子でかつ高飽和磁化量であるという相反する性状を両立
させた磁性酸化鉄の製造を実現させる必要がある。[0003] By the way, in order to realize low noise, fine particles are the most effective means, but there is a problem that a decrease in the saturation magnetization cannot be avoided. In addition, a decrease in the orientation and the filling property also occur at the same time. In other words, in order to satisfy both the low noise and high output directions, it is necessary to realize the production of magnetic iron oxide that is compatible with the opposite properties of fine particles and high saturation magnetization.
【0004】この問題を解決すべく、種々の試みが既に
成されている。例えばコバルト被着強磁性酸化鉄粉末の
出発原料をマグヘマイト粒子から中間体粒子もしくはマ
グネタイト粒子に転換して高飽和磁化量を実現させる方
法もある。しかし、その飽和磁化量は未だ不十分であ
る。[0004] Various attempts have been made to solve this problem. For example, there is a method in which the starting material of the cobalt-coated ferromagnetic iron oxide powder is converted from maghemite particles to intermediate particles or magnetite particles to achieve a high saturation magnetization. However, the saturation magnetization is still insufficient.
【0005】本発明の目的 本発明の目的は、前記の問題点を解決すべく微粒子でか
つ高飽和磁化量である塗布型高密度記録媒体に好適な強
磁性酸化鉄粉末の製造方法を提供することにある。この
新規な磁性酸化鉄粉末の製造方法は、マグヘマイト粒子
もしくはマグヘマイト化する前駆体の水和酸化鉄粒子に
マンガン、亜鉛、鉄もしくはマンガン、亜鉛を被着処理
し特定雰囲気下で熱処理させる工程を持つ点に特徴があ
り、これにより粒子結晶が該金属イオンを含み該粒子表
面がマンガン亜鉛フェライト層で変成されて高飽和磁化
量を示すマグヘマイト粒子もしくは中間体粒子を得るこ
とができるという利点がある。なお、本明細書におい
て、「中間体粒子」とは、マグヘマイトとマグネタイト
の中間体粒子をいう。さらにコバルト化合物もしくはコ
バルトと第一鉄塩の化合物を被着処理することで、より
一層磁気特性を好ましいものにすることができる。An object of the present invention is to provide a method for producing a ferromagnetic iron oxide powder suitable for a coating type high-density recording medium having fine particles and a high saturation magnetization in order to solve the above problems. It is in. This novel method for producing magnetic iron oxide powder has a process of applying manganese, zinc, iron or manganese, zinc to maghemite particles or hydrated iron oxide particles of a precursor to be maghemitized and heat-treating them under a specific atmosphere. There is an advantage in that maghemite particles or intermediate particles exhibiting a high saturation magnetization can be obtained because the particle crystals contain the metal ions and the surface of the particles is transformed with the manganese zinc ferrite layer. In this specification, “intermediate particles” refer to intermediate particles of maghemite and magnetite. Further, by applying a cobalt compound or a compound of cobalt and a ferrous salt, the magnetic properties can be further improved.
【0006】発明の構成 本発明の磁性酸化鉄粉末を得る一つの好ましい方法は、
以下の通りである。(1)マグヘマイト粒子にマンガ
ン、亜鉛及び任意に鉄を特定量被着処理して非酸化性雰
囲気下で熱処理を施すか、(2)マグヘマイト粒子にマ
ンガン、亜鉛及び任意に鉄を特定量被着処理して酸化性
もしくは非酸化性雰囲気下で熱処理を施した後に再還元
処理して中間体化するか、(3)マグヘマイト化する前
駆体の水和酸化鉄粒子にマンガン及び亜鉛を特定量被着
処理し、加熱脱水処理して得られたヘマタイト粒子を還
元、酸化処理してマグヘマイト化するか、もしくは還
元、微酸化処理するか、または還元、酸化処理してマグ
ヘマイト化した後に再還元処理して中間体化することに
より、粒子表面がマンガン亜鉛フェライト層で変成され
た高飽和磁化量を示すマグヘマイト粒子もしくは中間体
粒子を得ることができる。(4)前記(1)〜(3)の
マグヘマイト粒子もしくは中間体粒子にコバルト化合物
もしくはコバルトと第一鉄塩の化合物を含む溶液で処理
して保磁力や飽和磁化量を更に高めて、高記録磁気テー
プに極めて好適なものに仕上げることができる。本発明
のコバルト被着磁性酸化鉄粉末は、従来の金属で変成さ
れていないマグヘマイト粒子を出発原料としたものに比
べて、コバルト被着処理後の保磁力の発現性や配向特性
が優れる特徴も有している。以下に本発明の磁性酸化鉄
粉末を得る方法の詳細を、(1)〜(4)の順番で説明
する。One preferred method for obtaining the magnetic iron oxide powder of the present invention is as follows:
It is as follows. (1) A specific amount of manganese, zinc and optionally iron is applied to the maghemite particles and heat-treated in a non-oxidizing atmosphere, or (2) a specific amount of manganese, zinc and optionally iron is applied to the maghemite particles. Treated and heat-treated in an oxidizing or non-oxidizing atmosphere and then re-reducing to form an intermediate, or (3) manganese and zinc are added to the hydrated iron oxide particles of the precursor to be maghemitized in a specific amount. Hematite particles obtained by deposition and heat dehydration are reduced and oxidized to maghemite, or reduced and slightly oxidized, or reduced and oxidized to maghemite and then re-reduced. By forming the particles into an intermediate, maghemite particles or intermediate particles having a high saturation magnetization and having a particle surface modified with a manganese zinc ferrite layer can be obtained. (4) The maghemite particles or intermediate particles of the above (1) to (3) are treated with a solution containing a cobalt compound or a compound of cobalt and a ferrous salt to further increase the coercive force and the saturation magnetization to achieve high recording. It can be finished to be very suitable for a magnetic tape. The cobalt-coated magnetic iron oxide powder of the present invention also has a feature that the coercive force development and orientation characteristics after the cobalt-depositing process are excellent as compared with those using maghemite particles that are not denatured by a conventional metal as a starting material. Have. Hereinafter, details of the method for obtaining the magnetic iron oxide powder of the present invention will be described in the order of (1) to (4).
【0007】(1) マグヘマイト粒子の水性懸濁液に
マンガン、亜鉛及び任意に鉄化合物を含む水溶液を添加
する。本発明に用いるマンガン、亜鉛及び鉄成分として
種々の化合物が使用できるが、例えばその硫酸塩、硝酸
塩、塩化物などの水溶性のものが適当である。マンガン
成分は第一マンガンを用いる必要があるが鉄成分につい
ては第一鉄もしくは第二鉄のいづれを用いても本発明の
効果は変わらない。添加量については、マンガンイオン
はマンガン、亜鉛及び任意に鉄イオンで変成されたマグ
ヘマイト粒子中のMn/Feとして0.40〜2.50
原子重量%好ましくは0.80〜2.30原子重量%を
含有する量、一方亜鉛イオンはZn/Feとして0.4
0〜2.50原子重量%好ましくは0.80〜2.30
原子重量%を含有する量とする。鉄イオンは無添加にす
るかもしくはモル基準でマンガン及び亜鉛イオンの総添
加量の2倍量までを添加できる。更にアルカリを添加し
てpHを10〜11に調整し、該金属イオンを基体粒子
表面上に水酸化物として被着させてから、濾過、水洗し
懸濁液中に残存する余剰のアルカリなどを除去する。そ
して空気中で50〜110℃の乾燥を行う。引き続いて
非酸化性雰囲気下で熱処理を施す。雰囲気を非酸化性に
する理由は、第一マンガンイオンの酸化を防止するため
である。通常は窒素、二酸化炭素を用いるがヘリウム、
アルゴンなどの希ガスを用いてもかまわない。熱処理温
度は350〜525℃、好ましくは400〜500℃と
する。熱処理温度が前記の範囲より低い場合には所定の
飽和磁化量の向上が得られず、逆に高い場合にはα−ヘ
マタイトへの転移が起こり飽和磁化量が大きく低下して
しまう恐れがある。熱処理時間は0.5〜6時間好まし
くは1.5〜3時間とする。熱処理時間が前記の範囲よ
り短い場合はやはり所定の飽和磁化量が得られない。逆
に長くしても飽和磁化量を更に高くすることはできな
い。前記の熱処理前の段階においては、該金属イオンは
基体粒子表面上に非磁性の水酸化物もしくは酸化物とし
て存在するだけであるが、熱処理を施すことにより該金
属イオンが結晶内部に固溶して基体粒子表面にマンガン
亜鉛フェライト層を形成するために飽和磁化量が向上す
るものと考えられる。(1) To an aqueous suspension of maghemite particles is added an aqueous solution containing manganese, zinc and optionally an iron compound. Various compounds can be used as the manganese, zinc and iron components used in the present invention. For example, water-soluble compounds such as sulfates, nitrates and chlorides thereof are suitable. It is necessary to use ferrous manganese for the manganese component, but the effect of the present invention does not change even if ferrous or ferric iron is used for the iron component. Regarding the added amount, the manganese ion is 0.40 to 2.50 as Mn / Fe in maghemite particles modified with manganese, zinc and optionally iron ions.
Atomic weight%, preferably containing 0.80 to 2.30 atomic weight%, while zinc ion is 0.4% as Zn / Fe.
0 to 2.50 atomic weight%, preferably 0.80 to 2.30
It is an amount containing atomic weight%. Iron ions can be added without addition or up to twice the total addition amount of manganese and zinc ions on a molar basis. Further, the pH is adjusted to 10 to 11 by adding an alkali, and the metal ion is deposited as a hydroxide on the surface of the base particles, and then filtered, washed with water, and any excess alkali or the like remaining in the suspension is removed. Remove. Then, drying at 50 to 110 ° C. is performed in the air. Subsequently, heat treatment is performed in a non-oxidizing atmosphere. The reason why the atmosphere is made non-oxidizing is to prevent oxidation of the manganese ion. Usually, nitrogen and carbon dioxide are used, but helium,
A rare gas such as argon may be used. The heat treatment temperature is 350 to 525 ° C, preferably 400 to 500 ° C. When the heat treatment temperature is lower than the above range, a predetermined improvement in the saturation magnetization cannot be obtained, and when the heat treatment temperature is high, a transition to α-hematite may occur and the saturation magnetization may be greatly reduced. The heat treatment time is 0.5 to 6 hours, preferably 1.5 to 3 hours. If the heat treatment time is shorter than the above range, a predetermined saturation magnetization cannot be obtained. Conversely, even if the length is increased, the saturation magnetization cannot be further increased. In the stage before the heat treatment, the metal ions only exist as non-magnetic hydroxides or oxides on the surface of the base particles. However, the heat treatment causes the metal ions to form a solid solution inside the crystal. Therefore, it is considered that the saturation magnetization is improved because the manganese zinc ferrite layer is formed on the surface of the base particles.
【0008】(2) 金属の被着処理から乾燥工程まで
は(1)の場合と同様である。以降の工程は次の通りで
ある。熱処理雰囲気は(1)の場合と異なり、非酸化性
雰囲気または例えば空気のような酸化性雰囲気のいづれ
でもよい。酸化性雰囲気でも構わない理由は、熱処理で
第一マンガンイオンの一部が第二マンガンイオンや第三
マンガンイオンに酸化されて飽和磁化量の向上が現れな
くても次工程の再還元処理で第二マンガンイオン等が再
度第一マンガンイオンに還元され飽和磁化量の向上効果
が現れてくるからである。但し、再還元の度合を低くし
て第一鉄イオンの含有量が少ない中間体粒子を得ようと
する場合は、再還元処理での第二マンガンイオン等の第
一マンガンイオンへの還元が不十分となり所望の飽和磁
化量向上効果が達成されない恐れがある。従って、熱処
理雰囲気は好ましくは非酸化性雰囲気にした方がよい。
熱処理温度は(1)の場合と同様に350〜525℃、
好ましくは400〜500℃とする。引き続いて公知の
方法を適用することにより、再還元処理を施してFe2+
/Fe3+として最高0.45の第一鉄イオンを含有する
中間体に仕上げる。その方法は、例えば水素ガス流通下
で300〜350℃の還元処理をする方法であるが、第
一鉄イオンの含有量は還元時間を調整することで所望の
レベルにすることができる。(2) The process from the metal deposition process to the drying process is the same as in (1). The subsequent steps are as follows. Unlike the case (1), the heat treatment atmosphere may be a non-oxidizing atmosphere or an oxidizing atmosphere such as air. The reason why the oxidizing atmosphere may be used is that even if part of the manganese ions is oxidized to manganese ions or tertiary manganese ions by the heat treatment and the improvement of the saturation magnetization does not appear, This is because dimanganese ions and the like are reduced again to manganese ions and the effect of improving the saturation magnetization appears. However, when an attempt is made to obtain intermediate particles having a low content of ferrous ion by reducing the degree of re-reduction, reduction of manganese ion or the like to manganese ion in the re-reduction treatment is not possible. It may be sufficient, and the desired effect of improving the saturation magnetization may not be achieved. Therefore, the heat treatment atmosphere is preferably a non-oxidizing atmosphere.
The heat treatment temperature is 350 to 525 ° C as in the case of (1),
Preferably it is 400-500 degreeC. Subsequently, by applying a known method, a re-reduction treatment is performed to obtain Fe 2+
Finish to an intermediate containing up to 0.45 ferrous ions as / Fe 3+ . The method is, for example, a method of performing a reduction treatment at 300 to 350 ° C. under a flow of hydrogen gas. The content of ferrous ions can be adjusted to a desired level by adjusting the reduction time.
【0009】(3) 水和酸化鉄粒子の水性懸濁液にマ
ンガン及び亜鉛化合物の水溶液を添加する。添加量につ
いてはマンガンイオンは加熱、脱水処理してヘマタイト
化した段階でMn/Feとして0.40〜2.50原子
重量%好ましくは0.80〜2.30原子重量%を含有
する量、一方亜鉛イオンも同様にヘマタイト化した段階
でZn/Feとして0.40〜2.50原子重量%、好
ましくは0.80〜2.30原子重量%を含有する量と
する。更にアルカリを添加してpHを10〜11に調整
し、該金属イオンを基体粒子表面上に水酸化物として被
着させてから濾過、水洗し懸濁液中に残存する余剰のア
ルカリを除去する。後工程は公知の方法を適用すること
により、マグヘマイト粒子もしくは中間体粒子に仕上げ
ることができる。例えばマグヘマイト粒子に仕上げる場
合は以下の通りである。500〜600℃−0.5時間
の加熱脱水処理、水素ガス流通下で300〜350℃−
3時間の還元処理、空気流通下で250℃−3時間の酸
化処理を施してマグヘマイト化する。一方中間体粒子に
仕上げる場合は以下の通りである。500〜600℃−
0.5時間の加熱脱水処理、水素ガス流通下で300〜
350℃−3時間の還元処理、そして空気流通下で微酸
化処理を施して酸化が完結する前に取り出すか、または
250℃−3時間の酸化処理を施してマグヘマイト化し
た後に、水素ガス流通下で300〜350℃の再還元処
理を施して中間体化する。中間体粒子の第一鉄イオン含
有量は微酸化時間または再還元時間を調整することで所
望のレベルにすることができる。なお水和酸化鉄粒子を
出発原料とする場合は、前記(1),(2)のマグヘマ
イト粒子の場合と異なり金属被着処理後の熱処理工程を
付加する必要はない。なぜなら加熱脱水処理が熱処理と
同様の効果を与える為と考えられる。(3) An aqueous solution of a manganese and zinc compound is added to an aqueous suspension of hydrated iron oxide particles. Regarding the amount of manganese ion added, the manganese ion contains 0.40 to 2.50 at.%, Preferably 0.80 to 2.30 at.% As Mn / Fe when heated and dehydrated to be hematite. Similarly, zinc ions are made to contain 0.40 to 2.50 atomic weight%, preferably 0.80 to 2.30 atomic weight% as Zn / Fe at the stage of hematite formation. Further, the pH is adjusted to 10 to 11 by adding an alkali, and the metal ion is applied as a hydroxide on the surface of the base particles, followed by filtration and washing with water to remove excess alkali remaining in the suspension. . The post-process can be finished to maghemite particles or intermediate particles by applying a known method. For example, when finishing to maghemite particles is as follows. 500-600 ° C-0.5 hour heat dehydration, 300-350 ° C under hydrogen gas flow
A maghemite is formed by performing a reduction treatment for 3 hours and an oxidation treatment at 250 ° C. for 3 hours under flowing air. On the other hand, the case of finishing to intermediate particles is as follows. 500-600 ° C-
Heating dehydration treatment for 0.5 hour, 300 ~ under hydrogen gas flow
A reduction treatment at 350 ° C. for 3 hours and a slight oxidation treatment in a stream of air are performed to take out before the oxidation is completed, or an oxidation treatment at 250 ° C. for 3 hours is performed to form maghemite, and then a stream of hydrogen gas is passed. At 300 to 350 ° C. to form an intermediate. The ferrous ion content of the intermediate particles can be adjusted to a desired level by adjusting the time of the micro-oxidation or the time of the re-reduction. When the hydrated iron oxide particles are used as the starting material, it is not necessary to add a heat treatment step after the metal deposition treatment, unlike the maghemite particles (1) and (2). It is considered that the heat dehydration treatment gives the same effect as the heat treatment.
【0010】(4) 前記(1)〜(3)のマンガン、
亜鉛及び鉄もしくはマンガン及び亜鉛鉄イオンで変成さ
れたマグヘマイト粒子もしくは中間体粒子は、公知の方
法により粒子表面にコバルト化合物もしくはコバルトと
第一鉄塩の化合物を含む溶液で被着処理することで、保
磁力、飽和磁化量を高めて磁気特性をより一層向上させ
ることができる。被着処理の方法は、例えば以下の通り
である。マンガン、亜鉛及び任意に鉄イオンで変成され
たマグヘマイト粒子もしくは中間体粒子の水性懸濁液
に、アルカリ及びコバルト化合物もしくはアルカリ、コ
バルト化合物及び第一鉄化合物を添加して反応させる。
コバルトイオンの被着量は基体粒子基準で1.0〜6.
0wt%、好ましくは2.0〜6.0wt%、第一鉄化
合物を併用する場合、第一鉄イオンの被着量は10.0
wt%以下、好ましくは3.0〜7.0wt%とする。
さらに80〜95℃まで加熱して2〜7時間の熟成を行
う。被着反応後、濾過、水洗、乾燥して、コバルト被着
強磁性酸化鉄粉末に仕上げる。 本発明の効果 本発明によれば、マグヘマイト粒子もしくはマグヘマイ
ト化する前駆体の水和酸化鉄粒子の表面を微量の金属で
被着処理してマンガン亜鉛フェライト層で変成させるこ
とにより、飽和磁化量が向上したマグヘマイト粒子もし
くは中間体粒子を得ることができる。更にコバルト化合
物もしくはコバルトと第一鉄塩の化合物を被着処理する
ことで磁気特性をより一層好ましいものにして微粒子で
ありながら高飽和磁化量を示す高記録密度磁気テープに
極めて好適な強磁性酸化鉄粉末を製造することができ
る。本発明の効果については以下に実施例と比較例を挙
げて、具体的に説明する。(4) Manganese according to (1) to (3),
Maghemite particles or intermediate particles modified with zinc and iron or manganese and zinc iron ions are subjected to a coating treatment with a solution containing a cobalt compound or a compound of cobalt and a ferrous salt on the particle surface by a known method, By increasing the coercive force and the saturation magnetization, the magnetic properties can be further improved. The method of the deposition process is, for example, as follows. To an aqueous suspension of maghemite particles or intermediate particles modified with manganese, zinc and optionally iron ions, alkali and cobalt compounds or alkali, cobalt compounds and ferrous compounds are added and reacted.
The amount of cobalt ion to be applied is 1.0-6.
0 wt%, preferably 2.0 to 6.0 wt%, when a ferrous compound is used in combination, the amount of ferrous ion deposited is 10.0
wt% or less, preferably 3.0 to 7.0 wt%.
Further, the mixture is heated to 80 to 95 ° C. and aged for 2 to 7 hours. After the deposition reaction, the resultant is filtered, washed with water, and dried to obtain a cobalt-deposited ferromagnetic iron oxide powder. According to the present invention, the surface of the maghemite particles or the hydrated iron oxide particles of the precursor to be maghemitized is coated with a trace amount of metal and denatured by the manganese zinc ferrite layer, whereby the saturation magnetization is reduced. Improved maghemite particles or intermediate particles can be obtained. Further, by applying a cobalt compound or a compound of cobalt and a ferrous salt, the magnetic properties are further improved, and the ferromagnetic oxidation which is very suitable for a high recording density magnetic tape which shows a high saturation magnetization while being a fine particle is further preferable. Iron powder can be manufactured. The effects of the present invention will be specifically described below with reference to examples and comparative examples.
【0011】実施例 実施例1 保磁力Hc250Oe、飽和磁化量σs68.5emu
/g、比表面積62.0m2/gのマグヘマイト(γ−
Fe2O3)100gを純水1.5l中に分散させた後、
撹拌下で1mol/lの硫酸マンガン水溶液18.8m
l,1mol/lの硫酸亜鉛水溶液18.8ml、硫酸
第二鉄水溶液75.2mlの混合溶液を添加した。次い
で1.0Nの水溶化ナトリウム水溶液を徐添加しpH=
10.0に調整後30分保持し、濾過、水洗そして11
0℃で10時間乾燥した。次いで静置型管状炉において
窒素中450℃で3時間熱処理して目的の磁性酸化鉄粉
末を得た。(試料A−1) 比較例1 実施例1において窒素ガス中450℃の熱処理を空気中
450℃の熱処理に変更したこと以外は同様に処理して
比較試料の磁性酸化鉄粉末を得た。(試料A−2) 実施例2 実施例1において1mol/lの硫酸マンガン水溶液1
8.8mlを7.5mlに、1mol/lの硫酸亜鉛水
溶液18.8mlを30.1mlに変更したこと以外は
同様に処理して、目的の磁性酸化鉄粉末を得た。(試料
B−1) 実施例3 実施例1において1mol/lの硫酸マンガン水溶液1
8.8mlを30.1mlに、1mol/lの硫酸亜鉛
水溶液18.8mlを7.5mlに変更したこと以外は
同様に処理して、目的の磁性酸化鉄粉末を得た。(試料
B−2) 比較例2 実施例1において1mol/lの硫酸マンガン水溶液の
添加を無添加とし、1mol/lの硫酸亜鉛水溶液1
8.8mlを37.6mlに変更したこと以外は同様に
処理して、比較試料の磁性酸化鉄粉末を得た。(試料B
−3) 実施例4 実施例1において窒素ガス中450℃熱処理を窒素ガス
中400℃熱処理に変更したこと以外は同様に処理し
て、目的の磁性酸化鉄粉末を得た。(試料C−1) 実施例5 実施例1において窒素ガス中450℃熱処理を窒素ガス
中475℃熱処理に変更したこと以外が同様に処理し
て、目的の磁性酸化鉄粉末を得た。(試料C−2) 実施例6 実施例1において窒素ガス中450℃熱処理を窒素ガス
中500℃熱処理に変更したこと以外は同様に処理し
て、目的の磁性酸化鉄粉末を得た。(試料C−3) 実施例7 実施例1において窒素ガス中450℃熱処理を350℃
熱処理に変更したこと以外は同様に処理して、目的の磁
性酸化鉄粉末を得た。(試料C−4) 比較例3 実施例1において窒素ガス中450℃熱処理を窒素ガス
中550℃熱処理に変更したこと以外は同様に処理し
て、比較試料の磁性酸化鉄粉末を得た。(試料C−5) 実施例8 実施例5において硫酸第二鉄の添加を無添加とした以外
は同様に処理して、目的の磁性酸化鉄粉末を得た。(試
料D−1) 実施例9 実施例5において1mol/lの硫酸第二鉄水溶液7
5.2mlを37.6mlに変更したこと以外は同様に
処理して、目的の磁性酸化鉄粉末を得た。(試料D−
2) 実施例10 実施例5において1mol/lの硫酸マンガン水溶液1
8.8mlを9.4mlに、1mol/lの硫酸亜鉛水
溶液18.8mlを9.4mlに、1mol/lの硫酸
第二鉄水溶液75.2mlを37.6mlに変更したこ
と以外は同様に処理して、目的の磁性酸化鉄粉末を得
た。(試料E−1) 実施例11 実施例5において1mol/lの硫酸マンガン水溶液1
8.8mlを28.2mlに、1mol/lの硫酸亜鉛
水溶液18.8mlを28.2mlに、1mol/lの
硫酸第二鉄水溶液75.2mlを112.8mlに変更
したこと以外は同様に処理して、目的の磁性酸化鉄粉末
を得た。(試料E−2) 比較例4 実施例5において硫酸マンガン、硫酸亜鉛、硫酸第二鉄
の添加を無添加とした以外は同様に処理して、比較試料
の磁性酸化鉄粉末を得た。(試料E−3) 実施例12 実施例5において硫酸第二鉄を硫酸第一鉄に変更したこ
と以外は同様に処理して、目的の磁性酸化鉄粉末を得
た。(試料F−1) 実施例13 保磁力Hc384Oe、飽和磁化量σs72.6emu
/g、比表面積25.0m2/gのマグヘマイト(γ−
Fe2O3)100gを純水1.51中に分散させた後、
撹拌下で1mol/lの硫酸マンガン水溶液18.8m
l、1mol/lの硫酸亜鉛水溶液18.8ml、硫酸
第二鉄水溶液75.2mlの混合溶液を添加した。次い
で1.0Nの水酸化ナトリウム水溶液を徐添加しpH=
10.0に調整後30分保持し、濾過、水洗そして11
0℃で10時間乾燥した。次いで静置型管状炉において
窒素中500℃で3時間熱処理して目的の磁性酸化鉄粉
末を得た。(試料G−1) 実施例14 比較例1により得られた試料を、静置型管状炉において
窒素ガスを含む水素ガス流通下300℃で30分間還元
処理して、Fe2+/Fe3+として0.20の第一鉄を含
む目的の磁性酸化鉄粉末を得た。(試料H−1) 実施例15 実施例5により得られた試料を、静置型管状炉において
窒素ガスを含む水素ガス流通下300℃で30分間還元
処理して、Fe2+/Fe3+として0.20の第一鉄を含
む目的の磁性酸化鉄粉末を得た。(試料H−2) 比較例5 実施例1において使用したマグヘマイト粒子を、静置型
管状炉において窒素ガスを含む水素ガス流通下300℃
で30分間還元処理して、Fe2+/Fe3+として0.2
0の第一鉄を含む比較試料の磁性酸化鉄粉末を得た。
(試料H−3) 実施例16 実施例13により得られた試料を、静置型管状炉におい
て窒素ガスを含む水素ガス流通下300℃で30分間還
元処理して、Fe2+/Fe3+として0.20の第一鉄を
含む目的の磁性酸化鉄粉末を得た。(試料I−1) 比較例6 実施例13において使用したマグヘマイト粒子を、静置
型管状炉において窒素ガスを含む水素ガス流通下300
℃で30分間還元処理して、Fe2+/Fe3+として0.
20の第一鉄を含む比較試料の磁性酸化鉄粉末を得た。
(試料I−2) 実施例17 比表面積68m2/gのゲーサイト(α−Fe2O3)粒
子100gを純水31中に分散させた後、撹拌下で1m
ol/lの硫酸マンガン水溶液16.9mlと1mol
/lの硫酸亜鉛水溶液16.9mlを添加した。次いで
1.0Nの水酸化ナトリウム水溶液を徐添加しpH=1
0.0に調整後リン化合物を処理して濾過、水洗しアル
カリを除去した後110℃で10時間乾燥した。このゲ
ーサイトを620℃で3時間加熱脱水処理を行い、マン
ガン、亜鉛含有ヘマタイトを得た。このヘマタイトを炭
酸ガスを含む水素ガス流通下350℃−3時間加熱還元
してマグネタイト化した後空気流通下250℃−3時間
の酸化処理でマグヘマイト化して目的の磁性酸化鉄粉末
を得た。(試料J−1) 比較例7 実施例17において硫酸マンガン、硫酸亜鉛の添加を無
添加としたこと以外は同様に処理を行い、比較試料の磁
性酸化鉄粉末を得た。(試料J−2) 実施例18 実施例17で得られたマグヘマイト粒子を窒素ガスを含
む水素ガス流通下で300℃−30分の還元処理を行
い、目的の磁性酸化鉄粉末を得た。(試料K−1) 比較例8 比較例7で得られたマグヘマイト粒子を窒素ガスを含む
水素ガス流通下で300℃−30分の還元処理を行い、
比較試料の磁性酸化鉄粉末を得た。(試料K−2) 実施例19 実施例15において得られたマンガン、亜鉛含有マグネ
タイト100gを純水450mlに分散させた後窒素ガ
スを吹き込みながら撹拌下35℃で10N水酸化ナトリ
ウムを400ml添加した。次いで1mol/lの硫酸
コバルト水溶液88.2mlと1mol/lの硫酸第一
鉄水溶液89.5ml添加した後、95℃で5時間熟成
した。得られた沈澱物を濾過、水洗した後、大気中55
℃で3時間乾燥して目的のコバルト被着磁性酸化鉄粉末
を得た。(試料L−1) 比較例9 実施例15において得られたマグネタイトを比較例5で
得られたマグネタイトに変更したこと以外は実施例19
と同様に処理を行い、比較のコバルト被着磁性酸化鉄粉
末を得た。(試料L−2)前記実施例1〜18及び比較
例1〜8で作製した磁性酸化鉄試料(A−1)〜(L−
2)について、通常の方法にて保磁力(Hc)と飽和磁
化量(σs)を測定した。これらの結果を第1表と第2
表に示す。また磁性酸化鉄試料(L−1),(L−2)
については下記の配合割合に従って小型ニーダー及び小
型サンドグラインダーミル等を用いて磁性塗料を調整し
た。EXAMPLES Example 1 Coercive force Hc250Oe, saturation magnetization σs68.5 emu
/ G, maghemite having a specific surface area of 62.0 m 2 / g (γ-
After dispersing 100 g of Fe 2 O 3 ) in 1.5 l of pure water,
18.8 m of 1 mol / l manganese sulfate aqueous solution under stirring
A mixed solution of 18.8 ml of a 1 mol / l zinc sulfate aqueous solution and 75.2 ml of a ferric sulfate aqueous solution was added. Then, a 1.0N aqueous sodium hydroxide solution was gradually added, and pH =
After adjusting to 10.0, hold for 30 minutes, filter, wash and wash
Dry at 0 ° C. for 10 hours. Then, heat treatment was carried out in a stationary tubular furnace at 450 ° C. for 3 hours in nitrogen to obtain a target magnetic iron oxide powder. (Sample A-1) Comparative Example 1 A magnetic iron oxide powder of a comparative sample was obtained in the same manner as in Example 1, except that the heat treatment at 450 ° C. in nitrogen gas was changed to the heat treatment at 450 ° C. in air. (Sample A-2) Example 2 In Example 1, a 1 mol / l manganese sulfate aqueous solution 1 was used.
The same treatment was carried out except that 8.8 ml was changed to 7.5 ml, and 18.8 ml of a 1 mol / l aqueous solution of zinc sulfate was changed to 30.1 ml, to obtain a target magnetic iron oxide powder. (Sample B-1) Example 3 In Example 1, a 1 mol / l manganese sulfate aqueous solution 1 was used.
The same treatment was carried out except that 8.8 ml was changed to 30.1 ml and 18.8 ml of a 1 mol / l aqueous solution of zinc sulfate was changed to 7.5 ml, to obtain a target magnetic iron oxide powder. (Sample B-2) Comparative Example 2 In Example 1, the addition of a 1 mol / l manganese sulfate aqueous solution was omitted, and a 1 mol / l zinc sulfate aqueous solution 1 was added.
The same treatment was performed except that 8.8 ml was changed to 37.6 ml to obtain a magnetic iron oxide powder of a comparative sample. (Sample B
-3) Example 4 A target magnetic iron oxide powder was obtained in the same manner as in Example 1, except that the heat treatment at 450 ° C in nitrogen gas was changed to the heat treatment at 400 ° C in nitrogen gas. (Sample C-1) Example 5 A target magnetic iron oxide powder was obtained in the same manner as in Example 1, except that the heat treatment at 450 ° C in nitrogen gas was changed to the heat treatment at 475 ° C in nitrogen gas. (Sample C-2) Example 6 A target magnetic iron oxide powder was obtained in the same manner as in Example 1, except that the heat treatment at 450 ° C in nitrogen gas was changed to the heat treatment at 500 ° C in nitrogen gas. (Sample C-3) Example 7 A heat treatment at 450 ° C. in nitrogen gas at 350 ° C. in Example 1 was performed.
The same treatment was performed except that the heat treatment was changed to obtain the desired magnetic iron oxide powder. (Sample C-4) Comparative Example 3 A magnetic iron oxide powder of a comparative sample was obtained in the same manner as in Example 1, except that the heat treatment at 450 ° C in nitrogen gas was changed to the heat treatment at 550 ° C in nitrogen gas. (Sample C-5) Example 8 A target magnetic iron oxide powder was obtained in the same manner as in Example 5, except that ferric sulfate was not added. (Sample D-1) Example 9 In Example 5, a 1 mol / l ferric sulfate aqueous solution 7 was used.
The same treatment was carried out except that 5.2 ml was changed to 37.6 ml to obtain a target magnetic iron oxide powder. (Sample D-
2) Example 10 In Example 5, a 1 mol / l manganese sulfate aqueous solution 1 was used.
The same treatment was performed except that 8.8 ml was changed to 9.4 ml, a 1 mol / l aqueous solution of zinc sulfate 18.8 ml was changed to 9.4 ml, and a 1 mol / l aqueous solution of ferric sulfate 75.2 ml was changed to 37.6 ml. Thus, the desired magnetic iron oxide powder was obtained. (Sample E-1) Example 11 In Example 5, a 1 mol / l manganese sulfate aqueous solution 1 was used.
The same treatment was performed except that 8.8 ml was changed to 28.2 ml, 1 mol / l aqueous solution of zinc sulfate 18.8 ml was changed to 28.2 ml, and 15.2 ml of 1 mol / l aqueous solution of ferric sulfate was changed to 112.8 ml. Thus, the desired magnetic iron oxide powder was obtained. (Sample E-2) Comparative Example 4 A magnetic iron oxide powder of a comparative sample was obtained in the same manner as in Example 5, except that manganese sulfate, zinc sulfate and ferric sulfate were not added. (Sample E-3) Example 12 A target magnetic iron oxide powder was obtained in the same manner as in Example 5, except that ferric sulfate was changed to ferrous sulfate. (Sample F-1) Example 13 Coercive force Hc384Oe, saturation magnetization σs72.6 emu
/ G, maghemite having a specific surface area of 25.0 m 2 / g (γ-
After dispersing 100 g of Fe 2 O 3 ) in 1.51 of pure water,
18.8 m of 1 mol / l manganese sulfate aqueous solution under stirring
A mixed solution of 18.8 ml of an aqueous 1 mol / l zinc sulfate solution and 75.2 ml of an aqueous ferric sulfate solution was added. Then, a 1.0 N aqueous sodium hydroxide solution was gradually added to the mixture to adjust the pH to
After adjusting to 10.0, hold for 30 minutes, filter, wash and wash
Dry at 0 ° C. for 10 hours. Then, heat treatment was performed in a stationary tubular furnace at 500 ° C. for 3 hours in nitrogen to obtain a target magnetic iron oxide powder. (Sample G-1) Example 14 The sample obtained in Comparative Example 1 was subjected to a reduction treatment at 300 ° C. for 30 minutes in a stationary tubular furnace under a flow of hydrogen gas containing nitrogen gas to obtain Fe 2+ / Fe 3+. The desired magnetic iron oxide powder containing 0.20 ferrous iron was obtained. (Sample H-1) Example 15 The sample obtained in Example 5 was subjected to a reduction treatment at 300 ° C. for 30 minutes in a stationary tubular furnace under flowing hydrogen gas containing nitrogen gas to obtain Fe 2+ / Fe 3+. The desired magnetic iron oxide powder containing 0.20 ferrous iron was obtained. (Sample H-2) Comparative Example 5 The maghemite particles used in Example 1 were placed in a stationary tubular furnace at 300 ° C. under a flow of hydrogen gas containing nitrogen gas.
For 30 minutes to obtain a Fe 2+ / Fe 3+ of 0.2
A comparative magnetic iron oxide powder containing 0 ferrous iron was obtained.
(Sample H-3) Example 16 The sample obtained in Example 13 was subjected to reduction treatment at 300 ° C. for 30 minutes in a stationary tubular furnace under a flow of hydrogen gas containing nitrogen gas to obtain Fe 2+ / Fe 3+. The desired magnetic iron oxide powder containing 0.20 ferrous iron was obtained. (Sample I-1) Comparative Example 6 The maghemite particles used in Example 13 were placed in a stationary tubular furnace under flowing hydrogen gas containing nitrogen gas for 300 times.
Reduction treatment at 30 ° C. for 30 minutes to obtain Fe 2+ / Fe 3+ .
Thus, a comparative magnetic iron oxide powder containing 20 ferrous iron was obtained.
(Sample I-2) Example 17 After dispersing 100 g of goethite (α-Fe 2 O 3 ) particles having a specific surface area of 68 m 2 / g in pure water 31, 1 m of the dispersion was stirred.
ol / l manganese sulfate aqueous solution 16.9ml and 1mol
/ L zinc sulfate aqueous solution 16.9 ml was added. Then, a 1.0 N aqueous sodium hydroxide solution was gradually added to the mixture to adjust the pH to 1
After adjusting to 0.0, the phosphorus compound was treated, filtered and washed with water to remove alkali, and then dried at 110 ° C. for 10 hours. This goethite was heated and dehydrated at 620 ° C. for 3 hours to obtain manganese and zinc-containing hematite. This hematite was heated and reduced at 350 ° C. for 3 hours under a hydrogen gas containing carbon dioxide gas to form magnetite, and then maghemite was formed by oxidation at 250 ° C. for 3 hours under an air flow to obtain a target magnetic iron oxide powder. (Sample J-1) Comparative Example 7 A magnetic iron oxide powder of a comparative sample was obtained in the same manner as in Example 17, except that manganese sulfate and zinc sulfate were not added. (Sample J-2) Example 18 The maghemite particles obtained in Example 17 were subjected to a reduction treatment at 300 ° C. for 30 minutes under flowing hydrogen gas containing nitrogen gas to obtain a target magnetic iron oxide powder. (Sample K-1) Comparative Example 8 The maghemite particles obtained in Comparative Example 7 were subjected to a reduction treatment at 300 ° C. for 30 minutes under a flow of hydrogen gas containing nitrogen gas.
A magnetic iron oxide powder of a comparative sample was obtained. (Sample K-2) Example 19 After dispersing 100 g of the manganese- and zinc-containing magnetite obtained in Example 15 in 450 ml of pure water, 400 ml of 10N sodium hydroxide was added at 35 ° C with stirring while blowing nitrogen gas. Next, 88.2 ml of a 1 mol / l cobalt sulfate aqueous solution and 89.5 ml of a 1 mol / l ferrous sulfate aqueous solution were added, and the mixture was aged at 95 ° C. for 5 hours. The obtained precipitate was filtered and washed with water, and then dried in air.
Drying at 3 ° C. for 3 hours gave the desired cobalt-coated magnetic iron oxide powder. (Sample L-1) Comparative Example 9 Example 19 except that the magnetite obtained in Example 15 was changed to the magnetite obtained in Comparative Example 5.
In the same manner as described above, a comparative cobalt-coated magnetic iron oxide powder was obtained. (Sample L-2) Magnetic iron oxide samples (A-1) to (L-) prepared in Examples 1 to 18 and Comparative Examples 1 to 8.
Regarding 2), the coercive force (Hc) and the saturation magnetization (σs) were measured by an ordinary method. Table 1 and 2
It is shown in the table. In addition, magnetic iron oxide samples (L-1) and (L-2)
Was prepared using a small kneader and a small sand grinder mill according to the following mixing ratio.
【0012】 コバルト被着磁性酸化鉄粉末 100.0(重量部) 塩ビ・酢ビ共重合体樹脂 18.0 ポリウレタン樹脂 12.0 メチルエチルケトン 180.0 シクロヘキサノン 60.0 トルエン 60.0 上記磁性塗料をアプリケーターにて厚さ25μmのポリ
エステルフィルム上に塗布し、磁場配向した後乾燥して
乾燥塗膜厚10μmの磁気シートを仕上げた。そして通
常の方法によりこの磁気シートの保持力(Hc)、角形
比(SQ)、配向比(OR)及び反転磁界分布(SF
D)を測定した。これらの結果を第2表に示す。Cobalt-coated magnetic iron oxide powder 100.0 (parts by weight) PVC / vinyl acetate copolymer resin 18.0 Polyurethane resin 12.0 Methyl ethyl ketone 180.0 Cyclohexanone 60.0 Toluene 60.0 Applicator using the above magnetic paint Was applied on a polyester film having a thickness of 25 μm, magnetically oriented, and then dried to finish a magnetic sheet having a dry coating thickness of 10 μm. Then, the coercive force (Hc), the squareness ratio (SQ), the orientation ratio (OR), and the switching field distribution (SF) of the magnetic sheet are obtained by a usual method.
D) was measured. Table 2 shows the results.
【0013】以上の結果において本発明による実施例の
磁性酸化鉄試料は飽和磁化量が高く優れた磁気特性を示
すことは明らかである。コバルト被着した試料(L−
1)は、従来の金属無添加で熱処理を施さないマグヘマ
イト粒子を出発原料とした試料(L−2)と比較してH
c発現性が高く、仮に試料(L−2)と同一Hcにした
場合コバルト被着量が削減できるという利点があり工業
的に有利である。また磁気シートにおける角形比及び配
向比が良好で優れた分散性を示すことも明らかである。From the above results, it is apparent that the magnetic iron oxide sample of the embodiment according to the present invention has a high saturation magnetization and exhibits excellent magnetic properties. Cobalt-coated sample (L-
1) is higher than that of the conventional sample (L-2) in which maghemite particles without metal addition and without heat treatment are used as a starting material.
It has a high c-expressing property, and if the same Hc as that of the sample (L-2) is used, there is an advantage that the amount of deposited cobalt can be reduced, which is industrially advantageous. It is also clear that the magnetic sheet has a good squareness ratio and orientation ratio and exhibits excellent dispersibility.
【0014】[0014]
【表1】 [Table 1]
【0015】 [0015]
【0016】[0016]
【表2】 [Table 2]
フロントページの続き (72)発明者 渡辺 一 山口県宇部市大字小串1978番地の25 チ タン工業株式会社内 (56)参考文献 特開 昭55−141712(JP,A) (58)調査した分野(Int.Cl.6,DB名) H01F 1/34 Continuation of the front page (72) Inventor: Kazu Watanabe 1978 Kogushi, Ube City, Yamaguchi Prefecture, within 25 Hitachi Industries Ltd. (56) References JP-A-55-141712 (JP, A) (58) Fields investigated ( Int.Cl. 6 , DB name) H01F 1/34
Claims (5)
び任意に鉄を含む溶液で処理し、さらに非酸化性雰囲気
下で350−525℃で熱処理をし、Mn/Feとして
0.40−2.50原子重量%のマンガンと、Zn/F
eとして0.40−2.50原子重量%の亜鉛とを含
み、該粒子表面がマンガン亜鉛フェライト層で変成され
た、飽和磁化量が向上したマグヘマイト粒子を得ること
を特徴とする、磁気記録用強磁性酸化鉄粉末の製造方
法。1. The maghemite particles are treated with a solution containing manganese, zinc and optionally iron, and further heat-treated at 350-525 ° C. in a non-oxidizing atmosphere to obtain 0.40-2.50 atom as Mn / Fe. Wt% manganese and Zn / F
e) containing 0.40-2.50 atomic% by weight of zinc as e, and obtaining maghemite particles having an improved saturation magnetization, wherein the surface of the particles is denatured by a manganese zinc ferrite layer. A method for producing ferromagnetic iron oxide powder.
び任意に鉄を含む溶液で処理し、さらに酸化性雰囲気下
または非酸化性雰囲気下で350−525℃で熱処理を
し、Mn/Feとして0.40−2.50原子重量%の
マンガンイオンと、Zn/Feとして0.40−2.5
0原子重量%の亜鉛イオンとを含み、該粒子表面がマン
ガン亜鉛フェライト層で変成されたマグヘマイト粒子を
再還元処理して、Fe2+/Fe3+が0.45以下である
比率で第一鉄イオンを含有する、飽和磁化量が向上し
た、マグヘマイトとマグネタイトの中間体粒子を得るこ
とを特徴とする、磁気記録用強磁性酸化鉄粉末の製造方
法。2. The maghemite particles are treated with a solution containing manganese, zinc and optionally iron, and further heat-treated at 350-525 ° C. in an oxidizing atmosphere or a non-oxidizing atmosphere to obtain 0.40 as Mn / Fe. Manganese ions of -2.50 atomic weight% and 0.40-2.5 as Zn / Fe
Maghemite particles whose surface is denatured by a manganese zinc ferrite layer, and the particles are first reduced at a ratio of Fe 2+ / Fe 3+ of 0.45 or less. A method for producing ferromagnetic iron oxide powder for magnetic recording, comprising obtaining intermediate particles of maghemite and magnetite containing iron ions and having an improved saturation magnetization.
粒子をマンガンおよび亜鉛を含む溶液で処理し、さらに
加熱脱水処理を施し、Mn/Feとして0.40−2.
50原子重量%のマンガンイオンと、Zn/Feとして
0.40−2.50原子重量%の亜鉛イオンとを含み、
該粒子表面がマンガン亜鉛フェライト層で変成されたヘ
マタイト粒子を還元酸化処理して、飽和磁化量が向上し
たマグヘマイト粒子を得ることを特徴とする、磁気記録
用強磁性酸化鉄粉末の製造方法。3. The hydrated iron oxide particles of the precursor to be maghemitized are treated with a solution containing manganese and zinc, and further subjected to heat dehydration treatment to obtain Mn / Fe of 0.40-2.
50 atomic% by weight of manganese ions and 0.40-2.50 atomic% by weight of zinc ions as Zn / Fe,
A method for producing a ferromagnetic iron oxide powder for magnetic recording, comprising reducing and oxidizing hematite particles whose particle surfaces have been modified with a manganese zinc ferrite layer to obtain maghemite particles having an improved saturation magnetization.
粒子をマンガンおよび亜鉛を含む溶液で処理し、さらに
加熱脱水処理を施し、Mn/Feとして0.40−2.
50原子重量%のマンガンイオンと、Zn/Feとして
0.40−2.50原子重量%の亜鉛イオンとを含み、
該粒子表面がマンガン亜鉛フェライト層で変成されたヘ
マタイト粒子を還元処理後微酸化処理するかまたは還元
酸化処理してマグヘマイト化した後にさらに再還元処理
して、Fe2+/Fe3+として0.45以下の第一鉄イオ
ンを含有する、飽和磁化量が向上したマグヘマイトとマ
グネタイトの中間体粒子を得ることを特徴とする、磁気
記録用強磁性酸化鉄粉末の製造方法。4. A hydrated iron oxide particle of a precursor to be converted into maghemite is treated with a solution containing manganese and zinc, and further subjected to a heat dehydration treatment to obtain Mn / Fe of 0.40-2.
50 atomic% by weight of manganese ions and 0.40-2.50 atomic% by weight of zinc ions as Zn / Fe,
The hematite particles whose particle surfaces have been modified with a manganese zinc ferrite layer are reduced and then slightly oxidized, or reduced and oxidized to maghemite and then re-reduced to give Fe 2+ / Fe 3+ of 0.1. A method for producing a ferromagnetic iron oxide powder for magnetic recording, comprising obtaining intermediate particles of maghemite and magnetite containing 45 or less ferrous ions and having improved saturation magnetization.
法により得られる飽和磁化量が向上したマグヘマイト粒
子または中間体粒子をコバルト化合物またはコバルトと
第一鉄塩の化合物を含む溶液で処理することを特徴とす
る磁気記録用強磁性酸化鉄粉末の製造方法。5. A maghemite particle or an intermediate particle having an improved saturation magnetization obtained by the method according to claim 1, which is treated with a solution containing a cobalt compound or a compound of cobalt and a ferrous salt. A method for producing a ferromagnetic iron oxide powder for magnetic recording.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3001409A JP2933397B2 (en) | 1991-01-10 | 1991-01-10 | Method for producing ferromagnetic iron oxide powder for magnetic recording |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3001409A JP2933397B2 (en) | 1991-01-10 | 1991-01-10 | Method for producing ferromagnetic iron oxide powder for magnetic recording |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04252001A JPH04252001A (en) | 1992-09-08 |
| JP2933397B2 true JP2933397B2 (en) | 1999-08-09 |
Family
ID=11500692
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3001409A Expired - Fee Related JP2933397B2 (en) | 1991-01-10 | 1991-01-10 | Method for producing ferromagnetic iron oxide powder for magnetic recording |
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| Country | Link |
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| JP (1) | JP2933397B2 (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2916403A1 (en) * | 1979-04-23 | 1980-11-06 | Basf Ag | NEEDLE-SHAPED MAGNETIC IRON OXIDE AND METHOD FOR THE PRODUCTION THEREOF |
| JPS56109827A (en) * | 1980-02-05 | 1981-08-31 | Mitsui Toatsu Chem Inc | Manufacture of iron compound particle for magnetic recording medium |
| JPS59500739A (en) * | 1983-04-12 | 1984-04-26 | メモレックス・コーポレーション | ferromagnetic recording material |
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- 1991-01-10 JP JP3001409A patent/JP2933397B2/en not_active Expired - Fee Related
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