JPS6313938B2 - - Google Patents
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- Publication number
- JPS6313938B2 JPS6313938B2 JP7351280A JP7351280A JPS6313938B2 JP S6313938 B2 JPS6313938 B2 JP S6313938B2 JP 7351280 A JP7351280 A JP 7351280A JP 7351280 A JP7351280 A JP 7351280A JP S6313938 B2 JPS6313938 B2 JP S6313938B2
- Authority
- JP
- Japan
- Prior art keywords
- acicular
- particles
- feooh
- suspension
- water
- 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
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- 239000002245 particle Substances 0.000 claims description 106
- 229910006540 α-FeOOH Inorganic materials 0.000 claims description 58
- 239000013078 crystal Substances 0.000 claims description 34
- 159000000003 magnesium salts Chemical class 0.000 claims description 27
- 239000000725 suspension Substances 0.000 claims description 22
- 229910002588 FeOOH Inorganic materials 0.000 claims description 19
- 239000007864 aqueous solution Substances 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 18
- 238000004519 manufacturing process Methods 0.000 claims description 16
- 239000007789 gas Substances 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 14
- 239000001301 oxygen Substances 0.000 claims description 14
- 229910052760 oxygen Inorganic materials 0.000 claims description 14
- 239000011777 magnesium Substances 0.000 claims description 13
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 12
- 239000000843 powder Substances 0.000 claims description 12
- 238000007254 oxidation reaction Methods 0.000 claims description 8
- 230000003647 oxidation Effects 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 25
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 8
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical group [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 8
- 229910001425 magnesium ion Inorganic materials 0.000 description 7
- 239000006249 magnetic particle Substances 0.000 description 7
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 6
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 6
- 239000007771 core particle Substances 0.000 description 5
- 238000000635 electron micrograph Methods 0.000 description 5
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 5
- 235000019341 magnesium sulphate Nutrition 0.000 description 5
- 230000001590 oxidative effect Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000007858 starting material Substances 0.000 description 5
- 239000003513 alkali Substances 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 229910021645 metal ion Inorganic materials 0.000 description 4
- 239000011790 ferrous sulphate Substances 0.000 description 3
- 235000003891 ferrous sulphate Nutrition 0.000 description 3
- 230000004907 flux Effects 0.000 description 3
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 159000000007 calcium salts Chemical class 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910021506 iron(II) hydroxide Inorganic materials 0.000 description 2
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 description 2
- 239000000696 magnetic material Substances 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 230000035945 sensitivity Effects 0.000 description 2
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- XPPKVPWEQAFLFU-UHFFFAOYSA-N diphosphoric acid Chemical compound OP(O)(=O)OP(O)(O)=O XPPKVPWEQAFLFU-UHFFFAOYSA-N 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000004663 powder metallurgy Methods 0.000 description 1
- 229940005657 pyrophosphoric acid Drugs 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 1
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Hard Magnetic Materials (AREA)
- Compounds Of Iron (AREA)
Description
【発明の詳細な説明】
本発明は、磁気記録用磁性粒子粉末を製造する
際の出発原料として使用される針状晶α−
FeOOH粒子粉末の製造法に関するものであり、
平均値で長軸0.3〜2.0μm、軸比(長軸:短軸)
20:1以上という優れた針状晶を有する針状晶α
−FeOOH粒子粉末を得ることを目的とする。
近年、磁気記録再生用機器の小型軽量化が進む
につれて磁気テープ、磁気デイスク等の磁気記録
媒体に対する高性能化の必要性が益々生じてきて
いる。すなわち、高密度記録特性、高出力特性、
高感度特性、周波数特性等の諸特性の向上が要求
されている。
磁気記録媒体に対する上記のような要求を満足
させる為に適した磁性材料の特性は、高い保磁力
Hcと大きな飽和磁束密度Osとを有することであ
る。
周知の如く、磁性粒子粉末の保磁力の大きさ
は、形状異方性、結晶異方性、歪異方性および交
換異方性のいずれか若しくはそれらの相互作用に
依存している。
また、磁気テープ、磁気デイスク等磁気記録媒
体の出力特性、感度特性は、残留磁束密度Brに
依存し、残留磁束密度Brは、磁性粒子粉末のビ
ークル中での分散性、塗膜中での配向性及び充填
性に依存している。
そして、塗膜中での配向性及び充填性を向上さ
せるためには、ビークル中に分散させる磁性粒子
粉末ができるだけ優れた針状晶を有する事が要求
される。
現在、磁気記録用材料として主に針状晶マグネ
タイト粒子粉末または、針状晶マグヘマイト粒子
粉末が用いられている。これらは一般に、第一鉄
塩水溶液とアルカリとを反応させて得られる水酸
化第一鉄粒子を含むPH11以上のコロイド水溶液を
空気酸化し(通常、「湿式反応」と呼ばれてい
る。)て得られる針状晶α−FeOOH粒子を、水
素等還元性ガス中300〜400℃で還元して針状晶マ
グネタイト粒子とし、または次いでこれを、空気
中200〜300℃で酸化して針状晶マグヘマイト粒子
とすることにより得られている。
現在、磁気記録用磁性粒子粉末として使用され
ている針状晶マグネタイト粒子粉末、又は、針状
晶マグヘマイト粒子粉末は、その形状磁気異方性
を利用して比較的高い保磁力を得、その配向性の
すぐれていることを利用して、比較的大きな角型
(Br/Bm)及び配向度を得ているものであるが、
更に、針状晶マグネタイト粒子粉末並びに針状晶
マグヘマイト粒子粉末の特性をより優れたものと
すべく研究開発がすすめられている。
上述したように、優れた針状晶を有する針状晶
磁性粒子粉末は、現在、最も要求されているとこ
ろであり、このような特性を備えた磁性粒子粉末
を得るためには、出発原料である針状晶α−
FeOOH粒子が優れた針状晶を有することが必要
である。
従来、PH11以上のアルカリ領域で針状晶α−
FeOOH粒子を製造する方法として最も代表的な
公知方法は、第一鉄塩溶液に当量以上のアルカリ
溶液を加えて得られる水酸化第一鉄粒子を含む溶
液をPH11以上にて80℃以下の温度で酸化反応を行
うことにより、針状晶α−FeOOH粒子を得るも
のである。この方法により得られた針状晶α−
FeOOH粒子粉末は、長さ0.5〜1.5μ程度の針状形
態を呈した粒子であるが、軸比(長軸:短軸)は
高々10:1程度であり、優れた針状晶を有する粒
子であるとは言い難い。
このように軸比が10:1程度の針状晶α−
FeOOH粒子を還元工程、酸化工程を経て針状晶
磁性酸化鉄粒子とする場合には、還元、酸化の各
工程に於て粒子が収縮するので得られた針状晶磁
性酸化鉄粒子の軸比は、高々6:1程度のものと
なつてしまう。
一方、本発明者は、長年にわたり針状晶α−
FeOOH粒子粉末の製造及び開発にたずさわつて
いるものであるが、その過程において、針状晶α
−FeOOH粒子の製造に際して原料鉄塩である第
一鉄塩水溶液に、Fe以外のある種の異種金属イ
オンを添加した場合には、一般に、粒子の長軸方
向に成長しやすくなり、軸比の大きなα−
FeOOH粒子が得られるという現象を見い出して
いる。
Fe以外のある種の異種金属イオンとしては、
例えば、Co、Ni、Cr、Mn、Cd等である。
しかし、これらFe以外の異種金属イオンの添
加は、一般的に、針状晶α−FeOOH粒子の極微
細化を招来し、添加量の増加に伴つて、その傾向
は益々、顕著になることが知られている。このよ
うに極微細化した針状晶α−FeOOH粒子は、磁
気記録用磁性粒子粉末の出発原料としては適さな
いものである。
本発明者は、上述した従来技術に鑑み、PH11以
上のアルカリ領域で得られる針状晶α−FeOOH
粒子粉末の極微細化を招来することなく軸比の向
上をはかるべく、種々検討を重ねた結果、本発明
に到達したのである。
即ち、本発明は、第一鉄塩水溶液とアルカリ水
溶液とを反応させて得られたFe(OH)2を含むPH
11以上の懸濁液に酸素含有ガスを通気して酸化す
ることにより針状晶α−FeOOH粒子粉末を製造
する方法において、酸素含有ガスを通気して酸化
する前にあらかじめ上記懸濁液中に水可溶性マグ
ネシウム塩をFeに対しMg換算で0.5〜7.0原子%
存在させ、しかる後、酸素含有ガスを通気して少
くとも12時間以上の針状晶α−FeOOH生成反応
を行うことにより平均値で長軸0.3〜2.0μm、軸比
(長軸:短軸)20:1以上である針状晶α−
FeOOH粒子を得ることよりなる針状晶α−
FeOOH粒子粉末の製造法である。
先ず、本発明を完成するに至つた技術的背景及
び本発明の構成について述べる。
本発明者は、前述した従来技術に鑑み、PH11以
上のアルカリ領域で得られる針状晶α−FeOOH
粒子粉末の極微細化を招来することなく軸比の向
上をはかるようなFe以外の異種金属イオンの種
類、存在量、及び反応系における存在時期につい
て検討を重ねた結果、第一鉄塩水溶液とアルカリ
水溶液とを反応させて得られたFe(OH)2を含む
PH11以上の懸濁液に酸素含有ガスを通気して酸化
することにより針状晶α−FeOOH粒子粉末を製
造する方法において、酸素含有ガスを通気して酸
化する前にあらかじめ上記懸濁液中に水可溶性マ
グネシウム塩をFeに対しMg換算で0.5〜7.0原子
%存在させ、しかる後、酸素含有ガスを通気して
少くとも12時間以上の針状晶α−FeOOH生成反
応を行なつた場合には、針状晶α−FeOOH粒子
の極微細化を招来させることなく軸比を向上させ
ることができ、平均値で長軸0.3〜2.0μm、軸比
(長軸:短軸)20:1以上の針状晶α−FeOOH
粒子を得ることができるという新しい知見を得
た。
即ち、針状晶α−FeOOH粒子の生成反応は、
Fe(OH)2を含む懸濁液からの針状晶α−FeOOH
核粒子の発生という段階と該針状晶α−FeOOH
核粒子の成長という段階の二段階からなるもので
あるが、酸素含有ガスを通気して酸化する前にあ
らかじめ、Fe(OH)2を含む懸濁液中に水可溶性
マグネシウム塩を存在させるという本発明方法に
よれば、マグネシウムイオンが、針状晶α−
FeOOH核粒子の発生の段階で軸比の優れた針状
晶α−FeOOH核粒子を生成させ、更に、該針状
晶α−FeOOH核粒子の成長段階では粒子の短軸
方向への成長を抑制し、粒子の長軸方向への成長
を促進させるので軸比の優れた針状晶α−
FeOOH粒子を得ることができるのである。
この現象における水可溶性マグネシウム塩の作
用についての理論的な解明はいまだ充分には行つ
てはいないが、本発明者は、マグネシウムイオン
が針状晶α−FeOOH核粒子の成長段階で粒子の
短軸方向への成長を抑制し、且つ、粒子の長軸方
向への成長を促進させるという作用・効果を有す
るのは、マグネシウムイオンが、粒子の長軸に垂
直な面に比べ、長軸に平行な面に吸着しやすいこ
とが一要因と考えている。マグネシウムイオンの
上記作用・効果を発揮させる為には、後出の実施
例に示した通り針状晶α−FeOOH粒子の生成反
応を12時間以上かけてゆつくり行うことが肝要で
ある。即ち、針状晶α−FeOOH粒子の生成反応
をゆつくり行うことにより、マグネシウムイオン
が選択的に針状晶α−FeOOH粒子の長軸に平行
な面に吸着し、針状晶α−FeOOHの長軸方向へ
の成長を促進させるのである。
従来、α−FeOOH粒子粉末の生成においてマ
グネシウムを存在させるものとして粉体粉末治金
協会昭和49年度春季大会講演概要集108頁に記載
の方法がある。この方法の反応系は、アルカリと
して炭酸アルカリを用い、PH7〜11の領域でα−
FeOOH粒子を生成させるものであり、得られる
粒子の形状は紡錘形を呈したものである。
この反応系において「炭酸アルカリ中にヘキサ
メタリン酸、ピロリン酸、酒石酸等のナトリウム
塩を、あるいは、第一鉄塩中にZn、Cu、Mg、
Mn、Cr、Al等の硫酸塩を第一鉄に対し0.2〜2
重量%添加した場合、反応生成物は微細な粒径を
有する」ものとなる旨記載されている。
例えば、この反応系において、温度50℃で得ら
れたα−FeOOH粒子の長軸は平均値で1.0μmで
あるが、ヘキサメタリン酸ナトリウムを2%添加
した場合は平均値で0.15μm程度となる。
従つて、この反応系においては、上記添加剤を
添加した場合には粒子の微細化を招来しこれは本
発明における水可溶性マグネシウム塩の作用効果
とはまつたく相異するものである。尚、水可溶性
マグネシウム塩に類似したものとして同じアルカ
リ土類金属である水溶性カルシウム塩があるが、
本発明においては水可溶性マグネシウム塩に代え
て水可溶性カルシウム塩を使用しても針状晶α−
FeOOH粒子の長軸方向への成長を促進させ軸比
20:1以上にするという効果は得られない。
次に、本発明者が行つた数多くの実験例から、
その一部を抽出して説明すれば次の通りである。
図1は、水可溶性マグネシウム塩の存在量と針
状晶α−FeOOH粒子の軸比との関係図である。
即ち、Feに対しMg換算で0.1〜10.0原子%を含
むように硫酸マグネシウムを存在させて得られた
硫酸第一鉄1.0mol/水溶液と苛性ソーダ水溶
液とを用いてPH13のFe(OH)2を含む懸濁液を得、
該懸濁液に、温度45℃において毎分100の空気
を12時間以上通気して酸化することにより得られ
た針状晶α−FeOOH粒子の軸比と硫酸マグネシ
ウムの存在量の関係を示したものである。
図1に示されるように水可溶性マグネシウム塩
の存在量の増加に伴つて針状晶α−FeOOH粒子
の軸比は向上する傾向を示す。
図2は、水可溶性マグネシウム塩の存在量と図
1の場合と同一の反応条件のもとで生成された針
状晶α−FeOOH粒子の長軸との関係を示したも
のである。
図2に示されるように、水可溶性マグネシウム
塩の存在量がFeに対しMg換算で2原子%まで
は、水可溶性マグネシウム塩の増加に伴つて針状
晶α−FeOOH粒子は、粒子の長軸方向に成長す
る傾向を示す。
水可溶性マグネシウム塩の存在量がFeに対し
Mg換算で2原子%を越えて増加すると次第に長
軸が減少する。
この現象は、水可溶性マグネシウム塩の存在量
が増加した為にマグネシウムイオンが粒子の長軸
に垂直な面にも吸着し粒子の長軸方向への成長も
抑制されたものと考えられる。
しかし、同時に粒子の長軸に平行な面に対して
もマグネシウムイオンの吸着が増加する為に短軸
方向への成長は益々抑制されることになり、従つ
て、粒子自体の軸比は図1に示されるように、水
可溶性マグネシウム塩の存在量がFeに対しMg換
算で2原子%以上になつても低下することはな
い。
図3は、本発明の方法(後述する実施例2)に
より得られた針状晶α−FeOOH粒子粉末の電子
顕微鏡写真(X20000)を示したものである。
図3から明らかなように、本発明方法により得
られた針状晶α−FeOOH粒子粉末は優れた針状
晶を有するものである。
次に、本発明方法実施にあたつての諸条件につ
いて述べる。
本発明において使用される第一鉄塩水溶液とし
ては、硫酸第一鉄水溶液、塩化第一鉄水溶液等が
ある。
本発明において使用される水可溶性マグネシウ
ム塩としては硫酸マグネシウム、塩化マグネシウ
ム、硝酸マグネシウム等を使用することができ
る。
本発明における水可溶性マグネシウム塩の存在
は、Fe(OH)2を含む懸濁液中に酸素含有ガスを
通気してα−FeOOH粒子粉末を生成する前であ
ることが必要であり、第一鉄塩水溶液中、アルカ
リ水溶液中又は、Fe(OH)2を含む懸濁液中のい
づれにおいても存在させることができる。
尚、酸素含有ガス通気開始後、既に、一部針状
晶α−FeOOH核粒子が生成している段階で水可
溶性マグネシウム塩を存在させても充分な効果は
得られない。
本発明において、水可溶性マグネシウム塩の存
在量は、Feに対しMg換算で0.5〜7.0原子%であ
る。
水可溶性マグネシウム塩の存在量がFeに対し
Mg換算で0.5原子%以下である場合には本発明の
目的を十分達成することができない。
7.0原子%以上である場合も、本発明の目的を
達成することができるが、その場合の効果は顕著
でなく、また、得られた針状晶α−FeOOH粒子
を加熱還元、酸化して得られた針状晶磁性酸化鉄
粒子粉末は純度の低下により、飽和磁束密度が大
巾に減少し好ましくない。
得られる針状晶α−FeOOH粒子の軸比及び長
軸を考慮した場合1.0〜3.0原子%が好ましい。本
発明における針状晶α−FeOOH粒子の生成反応
時間は12時間以上である。12時間以下である場合
には、本発明の目的とする軸比(長軸:短軸)
20:1以上の針状晶α−FeOOH粒子が得られな
い。
得られる針状晶α−FeOOH粒子粉末は、平均
値で長軸0.3〜2.0μm、軸比(長軸:短軸)20:1
以上である。
長軸が平均値で0.3μm以下、2.0μm以上である
場合は磁気記録用出発原料として好ましくない。
針状晶α−FeOOH粒子粉末の軸比(長軸:短
軸)が20:1以下である場合には、該針状晶α−
FeOOH粒子粉末を還元、酸化して得られた針状
晶磁性酸化鉄粒子粉末は、還元、酸化の各工程に
於いて粒子が収縮するので軸比が優れたものとは
言い難く、従つて、磁気記録用出発原料としての
針状晶α−FeOOH粒子粉末の軸比は20:1以上
であることが好ましい。
以上の通りの構成の本発明は、次の通りの効果
を奏するものである。
即ち、本発明によれば、酸素含有ガスを通気し
て酸化する前にあらかじめFe(OH)2を含む懸濁
液中に水可溶性マグネシウム塩を存在させ、しか
る後、酸素含有ガスを通気して少くとも12時間以
上の針状晶α−FeOOH生成反応を行うことによ
り、PH11以上のアルカリ領域で得られる針状晶α
−FeOOH粒子の極微細化を招来することなく軸
比を向上させることができ、平均値で長軸0.3〜
2.0μm、軸比(長軸:短軸)20:1以上である優
れた針状晶を有する針状晶α−FeOOH粒子粉末
を得ることができる。
このようにして得られた針状晶α−FeOOH粒
子粉末を出発原料とし、加熱還元、酸化して得ら
れた針状晶マグネタイト粒子、針状晶マグヘマイ
ト粒子もまた、優れた針状晶を有するものである
ので、現在、最も要求されている高出力、高感
度、高密度記録用磁性材料として使用することが
できる。
また、磁性塗料の製造に際して、上記の針状晶
マグネタイト粒子粉末または針状晶マグヘマイト
粒子粉末を用いた場合には、塗膜中での配向性及
び充填性が極めてすぐれ、好ましい磁気記録媒体
を得ることができる。
次に、実施例並びに比較例により本発明を説明
する。
尚、前出の実験例及び以下の実施例並びに比較
例における粒子の軸比(長軸:短軸)、長軸は、
いずれも電子顕微鏡写真から測定した数値の平均
値で示した。
実施例 1
Feに対しMg換算で1.0原子%を含むように硫酸
マグネシウムMgSO4・7H2O49.7gを存在させて
得られた硫酸第一鉄1.00mol/水溶液20.0を、
あらかじめ反応器中に準備された4.75−Nの
NaOH水溶液20.0に加え、PH13.5、温度45℃に
おいてFe(OH)2の生成反応を行つた。
上記Fe(OH)2を含む懸濁液に温度45℃におい
て、毎分100の空気を16.5時間通気して針状晶
α−FeOOH粒子を生成した。
酸化反応終点は、反応液の一部を抜き取り塩酸
酸性に調整した後、赤血塩浴液を用いてFe2+の
青色呈色反応の有無で判定した。
生成粒子は、常法により、水洗、別、乾燥、
粉砕した。この針状晶α−FeOOH粒子は、電子
顕微鏡観察の結果、平均値で長軸0.70μm、軸比
(長軸:短軸)31:1であり、針状晶が優れたも
のであつた。
実施例 2〜8
第一鉄塩水溶液の種類、NaOH水溶液の濃度、
水可溶性マグネシウム塩の種類、存在量、存在時
期を種々変化させた以外は実施例1と同様にして
針状晶α−FeOOH粒子を生成した。
この時の主要製造条件及び特性を表1に示す。
実施例2〜8で得られた針状晶α−FeOOH粒
子粉末はいずれも電子顕微鏡観察の結果、針状晶
が優れたものであつた。
実施例2で得られた針状晶α−FeOOH粒子粉
末の電子顕微鏡写真(X20000)を図3に示す。
比較例 1
硫酸マグネシウムを存在させないで、他の諸条
件は実施例1と同様にして針状晶α−FeOOH粒
子粉末を生成した。
この時の主要製造条件及び特性を表1に示す。
得られた針状晶α−FeOOH粒子粉末の電子顕
微鏡写真(X20000)を図4に示す。
図4から明らかなように、得られた針状晶α−
FeOOH粒子粉末は、平均値で長軸0.50μm、軸比
(長軸:短軸)10:1であり、針状晶が悪いもの
であつた。
【表】DETAILED DESCRIPTION OF THE INVENTION The present invention provides acicular crystal α-
It relates to a method for producing FeOOH particle powder,
Average value of major axis 0.3 to 2.0 μm, axial ratio (major axis: short axis)
Acicular crystal α with excellent needle crystals of 20:1 or more
- Aim to obtain FeOOH particle powder. In recent years, as magnetic recording and reproducing equipment has become smaller and lighter, there has been an increasing need for higher performance magnetic recording media such as magnetic tapes and magnetic disks. In other words, high density recording characteristics, high output characteristics,
Improvements in various characteristics such as high sensitivity characteristics and frequency characteristics are required. The characteristics of magnetic materials suitable for satisfying the above requirements for magnetic recording media are high coercive force.
Hc and a large saturation magnetic flux density Os. As is well known, the magnitude of the coercive force of magnetic particles depends on shape anisotropy, crystal anisotropy, strain anisotropy, exchange anisotropy, or their interaction. In addition, the output characteristics and sensitivity characteristics of magnetic recording media such as magnetic tapes and magnetic disks depend on the residual magnetic flux density Br, which is determined by the dispersibility of magnetic particles in the vehicle and the orientation in the coating film. It depends on the properties and filling properties. In order to improve the orientation and filling properties in the coating film, it is required that the magnetic particles dispersed in the vehicle have acicular crystals as excellent as possible. Currently, acicular magnetite particles or acicular maghemite particles are mainly used as magnetic recording materials. These are generally produced by air oxidizing a colloidal aqueous solution with a pH of 11 or higher containing ferrous hydroxide particles obtained by reacting an aqueous ferrous salt solution with an alkali (usually called a "wet reaction"). The obtained acicular α-FeOOH particles are reduced to acicular magnetite particles in a reducing gas such as hydrogen at 300 to 400°C, or are then oxidized in air at 200 to 300°C to form acicular crystals. It is obtained by making it into maghemite particles. Acicular magnetite particles or acicular maghemite particles, which are currently used as magnetic particles for magnetic recording, utilize their shape magnetic anisotropy to obtain a relatively high coercive force, and their orientation It takes advantage of its excellent properties to obtain a relatively large square shape (Br/Bm) and degree of orientation.
Furthermore, research and development efforts are underway to improve the properties of acicular magnetite particles and acicular maghemite particles. As mentioned above, acicular magnetic particles with excellent acicular crystals are currently in high demand, and in order to obtain magnetic particles with such characteristics, starting materials are required. Needle crystal α−
It is necessary that the FeOOH particles have excellent acicular crystal structure. Conventionally, acicular crystals α-
The most typical known method for producing FeOOH particles is to add an equivalent or more alkaline solution to a ferrous salt solution to obtain a solution containing ferrous hydroxide particles at a pH of 11 or higher and a temperature of 80°C or lower. Acicular α-FeOOH particles are obtained by performing an oxidation reaction. Acicular crystals α- obtained by this method
FeOOH particles are particles with a needle-like shape with a length of about 0.5 to 1.5μ, but the axial ratio (long axis: short axis) is about 10:1 at most, and particles with excellent needle crystals. It is difficult to say that it is. In this way, the acicular crystal α− with an axial ratio of about 10:1
When FeOOH particles are made into acicular crystal magnetic iron oxide particles through a reduction process and an oxidation process, the particles shrink in each reduction and oxidation process, so the axial ratio of the obtained acicular crystal magnetic iron oxide particles is The ratio is about 6:1 at most. On the other hand, the present inventor has been working on needle-like α-
We are involved in the production and development of FeOOH particle powder, but in the process, acicular crystals α
-When producing FeOOH particles, when some kind of dissimilar metal ion other than Fe is added to the ferrous salt aqueous solution, which is the raw material iron salt, the particles generally grow more easily in the long axis direction and the axial ratio decreases. big α−
We have discovered a phenomenon in which FeOOH particles are obtained. Certain types of foreign metal ions other than Fe include
For example, Co, Ni, Cr, Mn, Cd, etc. However, the addition of these metal ions other than Fe generally causes the acicular α-FeOOH particles to become extremely fine, and this tendency becomes more pronounced as the amount added increases. Are known. These extremely fine acicular α-FeOOH particles are not suitable as a starting material for magnetic particles for magnetic recording. In view of the above-mentioned prior art, the present inventor has discovered that acicular crystals α-FeOOH obtained in an alkaline region with a pH of 11 or higher
The present invention was achieved as a result of various studies aimed at improving the axial ratio without making the particles extremely fine. That is, the present invention provides a PH containing Fe(OH) 2 obtained by reacting a ferrous salt aqueous solution with an alkaline aqueous solution.
In a method for producing acicular α-FeOOH particle powder by passing an oxygen-containing gas through a suspension of 11 or more particles to oxidize it, the above suspension is preliminarily injected into the suspension before being oxidized by passing an oxygen-containing gas through the suspension. Water-soluble magnesium salt is 0.5 to 7.0 atomic% as Mg based on Fe.
After that, by aerating oxygen-containing gas and performing a needle-shaped α-FeOOH production reaction for at least 12 hours, the average value of the long axis is 0.3 to 2.0 μm, and the axial ratio (long axis: short axis) Acicular crystal α− with a ratio of 20:1 or more
Acicular crystals α− consisting of obtaining FeOOH particles
This is a method for producing FeOOH particle powder. First, the technical background that led to the completion of the present invention and the structure of the present invention will be described. In view of the prior art described above, the present inventor has discovered that acicular crystals α-FeOOH obtained in an alkaline region with a pH of 11 or higher
As a result of repeated studies on the type, abundance, and period of presence in the reaction system of different metal ions other than Fe, which would improve the axial ratio without causing ultrafine particle size, we found that a ferrous salt aqueous solution and Contains Fe(OH) 2 obtained by reacting with an aqueous alkaline solution
In a method for producing acicular α-FeOOH particle powder by passing an oxygen-containing gas through a suspension having a pH of 11 or higher for oxidation, the suspension is preliminarily injected into the suspension before being oxidized by passing an oxygen-containing gas through the suspension. In the case where a water-soluble magnesium salt is present in an amount of 0.5 to 7.0 atomic % based on Fe in terms of Mg, and then an oxygen-containing gas is aerated to carry out a reaction for producing needle-shaped α-FeOOH for at least 12 hours. , the axial ratio can be improved without causing ultra-fineness of the acicular α-FeOOH particles, and the average value of the long axis is 0.3 to 2.0 μm, and the axial ratio (long axis: short axis) is 20:1 or more. Needle crystal α−FeOOH
We obtained new knowledge that it is possible to obtain particles. In other words, the reaction for producing acicular α-FeOOH particles is as follows:
Acicular α−FeOOH from a suspension containing Fe(OH) 2
The stage of nuclear particle generation and the acicular α-FeOOH
The process consists of two steps: the growth of nuclear particles, and this method involves pre-existing a water-soluble magnesium salt in a suspension containing Fe(OH) 2 before oxidizing it by passing in an oxygen-containing gas. According to the method of the invention, magnesium ions form needle-shaped α-
At the stage of FeOOH core particle generation, acicular α-FeOOH core particles with excellent axial ratio are generated, and at the growth stage of the acicular α-FeOOH core particles, growth in the short axis direction of the particles is suppressed. and promotes growth in the long axis direction of the particles, resulting in acicular crystals α- with an excellent axial ratio.
FeOOH particles can be obtained. Although the theoretical elucidation of the effect of water-soluble magnesium salts on this phenomenon has not yet been fully elucidated, the present inventors have demonstrated that magnesium ions are absorbed into the short axis of the acicular α-FeOOH core particles during their growth stage. The reason why magnesium ions have the action and effect of suppressing growth in the long axis direction of the particle and promoting growth in the long axis direction of the particle is that magnesium ions have the effect of suppressing growth in the long axis direction of the particle and promoting growth in the long axis direction of the particle. We believe that one of the reasons is that it easily sticks to surfaces. In order to exhibit the above-mentioned functions and effects of magnesium ions, it is important to slowly carry out the reaction for producing acicular α-FeOOH particles over a period of 12 hours or more, as shown in the Examples below. In other words, by slowly performing the reaction to generate acicular α-FeOOH particles, magnesium ions are selectively adsorbed to the plane parallel to the long axis of the acicular α-FeOOH particles, and the acicular α-FeOOH particles are This promotes growth in the longitudinal direction. Conventionally, in the production of α-FeOOH particles, there is a method described on page 108 of the collection of lecture summaries of the 1971 Spring Conference of the Powder and Powder Metallurgy Association, which involves the presence of magnesium. The reaction system of this method uses alkali carbonate as the alkali, and α-
FeOOH particles are generated, and the resulting particles have a spindle shape. In this reaction system, ``sodium salts such as hexametaphosphoric acid, pyrophosphoric acid, tartaric acid, etc. are added to an alkali carbonate, or Zn, Cu, Mg, etc. are added to a ferrous salt.
Sulfate of Mn, Cr, Al, etc. is 0.2 to 2 to ferrous iron.
% by weight, the reaction product has a fine particle size.'' For example, in this reaction system, the long axis of α-FeOOH particles obtained at a temperature of 50° C. has an average value of 1.0 μm, but when 2% sodium hexametaphosphate is added, the average value becomes about 0.15 μm. Therefore, in this reaction system, when the above-mentioned additive is added, particles become finer, which is completely different from the effect of the water-soluble magnesium salt in the present invention. In addition, water-soluble calcium salts, which are also alkaline earth metals, are similar to water-soluble magnesium salts.
In the present invention, even if water-soluble calcium salt is used instead of water-soluble magnesium salt, needle-shaped α-
Promotes the growth of FeOOH particles in the long axis direction and increases the axial ratio.
The effect of increasing the ratio to 20:1 or higher cannot be obtained. Next, from the numerous experimental examples conducted by the present inventor,
Some of them can be extracted and explained as follows. FIG. 1 is a diagram showing the relationship between the amount of water-soluble magnesium salt present and the axial ratio of acicular α-FeOOH particles. In other words, Fe(OH) 2 with a pH of 13 is prepared by using a 1.0 mol/aqueous solution of ferrous sulfate obtained in the presence of magnesium sulfate so as to contain 0.1 to 10.0 atomic % of Fe in terms of Mg, and an aqueous solution of caustic soda. obtain a suspension;
The relationship between the axial ratio of the acicular α-FeOOH particles and the amount of magnesium sulfate obtained by oxidizing the suspension by passing 100 air per minute at a temperature of 45°C for 12 hours or more was shown. It is something. As shown in FIG. 1, the axial ratio of the acicular α-FeOOH particles tends to improve as the amount of water-soluble magnesium salt increases. FIG. 2 shows the relationship between the amount of water-soluble magnesium salt present and the long axis of acicular α-FeOOH particles produced under the same reaction conditions as in FIG. As shown in Figure 2, when the amount of water-soluble magnesium salt is up to 2 atomic % based on Fe (calculated as Mg), as the amount of water-soluble magnesium salt increases, the long axis of the acicular α-FeOOH particle changes. Shows a tendency to grow in the direction. Abundance of water-soluble magnesium salt relative to Fe
When the amount increases by more than 2 atomic % in terms of Mg, the long axis gradually decreases. This phenomenon is considered to be due to the increase in the amount of water-soluble magnesium salt present, which caused magnesium ions to be adsorbed also on the plane perpendicular to the long axis of the particles, thereby suppressing growth in the long axis direction of the particles. However, at the same time, adsorption of magnesium ions also increases on planes parallel to the long axis of the particle, so growth in the short axis direction is increasingly suppressed, and the axial ratio of the particle itself is as shown in Figure 1. As shown in , even if the amount of water-soluble magnesium salt present exceeds 2 atomic % in terms of Mg based on Fe, it does not decrease. FIG. 3 shows an electron micrograph (X20000) of acicular α-FeOOH particles obtained by the method of the present invention (Example 2 described later). As is clear from FIG. 3, the acicular α-FeOOH particles obtained by the method of the present invention have excellent acicular crystals. Next, various conditions for carrying out the method of the present invention will be described. Examples of the ferrous salt aqueous solution used in the present invention include a ferrous sulfate aqueous solution and a ferrous chloride aqueous solution. As the water-soluble magnesium salt used in the present invention, magnesium sulfate, magnesium chloride, magnesium nitrate, etc. can be used. The presence of the water-soluble magnesium salt in the present invention is required prior to bubbling oxygen-containing gas into the Fe(OH) 2- containing suspension to produce α-FeOOH particle powder; It can be present in any of a salt aqueous solution, an alkaline aqueous solution, or a suspension containing Fe(OH) 2 . Incidentally, even if the water-soluble magnesium salt is present at a stage when some acicular α-FeOOH core particles have already been formed after the start of oxygen-containing gas ventilation, a sufficient effect cannot be obtained. In the present invention, the amount of water-soluble magnesium salt present is 0.5 to 7.0 atomic % based on Fe in terms of Mg. Abundance of water-soluble magnesium salt relative to Fe
If it is less than 0.5 atomic % in terms of Mg, the object of the present invention cannot be fully achieved. The purpose of the present invention can also be achieved when the concentration is 7.0 at% or more, but the effect in that case is not remarkable, and the obtained acicular α-FeOOH particles are heated and oxidized. The resulting acicular crystalline magnetic iron oxide particles are undesirable because their saturation magnetic flux density is greatly reduced due to a decrease in purity. Considering the axial ratio and long axis of the resulting acicular α-FeOOH particles, the content is preferably 1.0 to 3.0 at %. The reaction time for producing acicular α-FeOOH particles in the present invention is 12 hours or more. If it is 12 hours or less, the axial ratio (long axis: short axis) targeted by the present invention
Acicular α-FeOOH particles with a ratio of 20:1 or more cannot be obtained. The obtained acicular α-FeOOH particles have an average long axis of 0.3 to 2.0 μm and an axial ratio (long axis: short axis) of 20:1.
That's all. If the long axis has an average value of 0.3 μm or less and 2.0 μm or more, it is not preferred as a starting material for magnetic recording.
When the axial ratio (major axis: short axis) of the acicular α-FeOOH particles is 20:1 or less, the acicular α-
The acicular magnetic iron oxide particles obtained by reducing and oxidizing FeOOH particles cannot be said to have an excellent axial ratio because the particles shrink in each reduction and oxidation process. The axial ratio of the acicular α-FeOOH particles as a starting material for magnetic recording is preferably 20:1 or more. The present invention configured as described above has the following effects. That is, according to the present invention, a water-soluble magnesium salt is made to exist in a suspension containing Fe(OH) 2 before oxidation by passing an oxygen-containing gas through the solution, and then a water-soluble magnesium salt is made to exist in the suspension containing Fe(OH) 2 before being oxidized by passing an oxygen-containing gas through the suspension. Acicular crystals α obtained in an alkaline region with a pH of 11 or higher by carrying out a needle-shaped α-FeOOH production reaction for at least 12 hours or more.
-The axial ratio can be improved without causing ultra-fineness of FeOOH particles, and the average value of major axis is 0.3~
It is possible to obtain acicular α-FeOOH particles having excellent acicular crystals with a diameter of 2.0 μm and an axial ratio (long axis: short axis) of 20:1 or more. Acicular crystal magnetite particles and acicular crystal maghemite particles obtained by thermally reducing and oxidizing the thus obtained acicular α-FeOOH particle powder as a starting material also have excellent acicular crystals. Therefore, it can be used as a magnetic material for high-output, high-sensitivity, and high-density recording, which are currently most required. In addition, when the above-mentioned acicular magnetite particles or acicular maghemite particles are used in the production of a magnetic coating material, the orientation and filling properties in the coating film are extremely excellent, and a desirable magnetic recording medium can be obtained. be able to. Next, the present invention will be explained with reference to Examples and Comparative Examples. In addition, the axial ratio (long axis: short axis) and long axis of the particles in the above experimental examples, the following examples, and comparative examples are as follows:
All values are shown as average values of values measured from electron micrographs. Example 1 Ferrous sulfate 1.00 mol/20.0 aqueous solution obtained by making 49.7 g of magnesium sulfate MgSO 4 7H 2 O so as to contain 1.0 atomic % in terms of Mg based on Fe,
4.75-N prepared in advance in the reactor
In addition to NaOH aqueous solution 20.0, Fe(OH) 2 production reaction was performed at pH 13.5 and temperature 45°C. Acicular α-FeOOH particles were produced by passing 100 air per minute through the Fe(OH) 2 -containing suspension for 16.5 hours at a temperature of 45°C. The end point of the oxidation reaction was determined by the presence or absence of blue coloring reaction of Fe 2+ using a red blood salt bath after a portion of the reaction solution was extracted and acidified with hydrochloric acid. The generated particles are washed with water, separated, dried, and
Shattered. As a result of electron microscopic observation, the acicular α-FeOOH particles had an average long axis of 0.70 μm and an axial ratio (long axis:short axis) of 31:1, indicating that the particles were excellent in acicular crystals. Examples 2 to 8 Type of ferrous salt aqueous solution, concentration of NaOH aqueous solution,
Acicular α-FeOOH particles were produced in the same manner as in Example 1, except that the type, amount, and time of presence of the water-soluble magnesium salt were varied. Table 1 shows the main manufacturing conditions and characteristics at this time. As a result of electron microscopic observation, all of the acicular crystal α-FeOOH particles obtained in Examples 2 to 8 were found to have excellent acicular crystals. An electron micrograph (X20000) of the acicular α-FeOOH particles obtained in Example 2 is shown in FIG. Comparative Example 1 Acicular α-FeOOH particles were produced in the same manner as in Example 1 except for the absence of magnesium sulfate. Table 1 shows the main manufacturing conditions and characteristics at this time. An electron micrograph (X20000) of the obtained acicular α-FeOOH particles is shown in FIG. As is clear from FIG. 4, the obtained acicular crystals α-
The FeOOH particles had an average long axis of 0.50 μm and an axial ratio (long axis:short axis) of 10:1, and had bad needle-like crystals. 【table】
図1は、水可溶性マグネシウム塩の存在量と針
状晶α−FeOOH粒子の軸比との関係図である。
図2は、水可溶性マグネシウム塩の存在量と図1
の場合と同一の反応条件のもとで生成された針状
晶α−FeOOH粒子の長軸との関係を示したもの
である。図3及び図4は、いずれも電子顕微鏡写
真(X20000)であり、図3は実施例2で得られ
た針状晶α−FeOOH粒子粉末、図4は比較例1
で得られた針状晶α−FeOOH粒子粉末である。
FIG. 1 is a diagram showing the relationship between the amount of water-soluble magnesium salt present and the axial ratio of acicular α-FeOOH particles.
Figure 2 shows the abundance of water-soluble magnesium salts and Figure 1
This figure shows the relationship between the long axis of acicular α-FeOOH particles produced under the same reaction conditions as in the case of . 3 and 4 are electron micrographs (X20000), and FIG. 3 is the acicular α-FeOOH particle powder obtained in Example 2, and FIG. 4 is Comparative Example 1.
This is the acicular α-FeOOH particle powder obtained in .
Claims (1)
せて得られたFe(OH)2を含むPH11以上の懸濁液
に酸素含有ガスを通気して酸化することにより針
状晶α−FeOOH粒子粉末を製造する方法におい
て、酸素含有ガスを通気して酸化する前にあらか
じめ上記懸濁液中に水可溶性マグネシウム塩を
Feに対しMg換算で0.5〜7.0原子%存在させ、し
かる後、酸素含有ガスを通気して少くとも12時間
以上の針状晶α−FeOOH生成反応を行うことに
より平均値で長軸0.3〜2.0μm、軸比(長軸:短
軸)20:1以上である針状晶α−FeOOH粒子を
得ることを特徴とする針状晶α−FeOOH粒子粉
末の製造法。 2 懸濁液中に存在させておく水可溶性マグネシ
ウム塩がFeに対しMg換算で1.0〜3.0原子%であ
る特許請求の範囲第1項記載の針状晶α−
FeOOH粒子粉末の製造法。[Claims] 1. A suspension containing Fe(OH) 2 obtained by reacting a ferrous salt aqueous solution with an alkaline aqueous solution and having a pH of 11 or higher is oxidized by passing an oxygen-containing gas through it to form a acicular shape. In the method for producing crystalline α-FeOOH particles, a water-soluble magnesium salt is added to the suspension in advance before oxidation by passing oxygen-containing gas through the suspension.
The average value of major axis is 0.3 to 2.0 by making the presence of Fe 0.5 to 7.0 at% in terms of Mg, and then aerating oxygen-containing gas to carry out a reaction to produce needle-shaped α-FeOOH for at least 12 hours. 1. A method for producing acicular α-FeOOH particles, the method comprising obtaining acicular α-FeOOH particles having an axial ratio (long axis: short axis) of 20:1 or more. 2. Acicular crystal α- according to claim 1, wherein the water-soluble magnesium salt present in the suspension is 1.0 to 3.0 atomic % based on Fe in terms of Mg.
Production method of FeOOH particle powder.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7351280A JPS56169133A (en) | 1980-05-30 | 1980-05-30 | Manufacture of needlelike alpha-feooh particle |
| US06/512,661 US4495164A (en) | 1980-05-30 | 1983-07-11 | Process for producing acicular magnetite or acicular maghemite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7351280A JPS56169133A (en) | 1980-05-30 | 1980-05-30 | Manufacture of needlelike alpha-feooh particle |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56169133A JPS56169133A (en) | 1981-12-25 |
| JPS6313938B2 true JPS6313938B2 (en) | 1988-03-28 |
Family
ID=13520368
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7351280A Granted JPS56169133A (en) | 1980-05-30 | 1980-05-30 | Manufacture of needlelike alpha-feooh particle |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56169133A (en) |
-
1980
- 1980-05-30 JP JP7351280A patent/JPS56169133A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56169133A (en) | 1981-12-25 |
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