JPS6279241A - Method of recovering magnetic powder from magnetic recording material - Google Patents

Method of recovering magnetic powder from magnetic recording material

Info

Publication number
JPS6279241A
JPS6279241A JP60218853A JP21885385A JPS6279241A JP S6279241 A JPS6279241 A JP S6279241A JP 60218853 A JP60218853 A JP 60218853A JP 21885385 A JP21885385 A JP 21885385A JP S6279241 A JPS6279241 A JP S6279241A
Authority
JP
Japan
Prior art keywords
solution
magnetic
magnetic powder
organic solvent
binder
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.)
Granted
Application number
JP60218853A
Other languages
Japanese (ja)
Other versions
JPH0455623B2 (en
Inventor
Setsuo Kawagishi
川岸 節夫
Etsuko Moriyama
森山 悦子
Osamu Yokoyama
修 横山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MITSUMARU KAGAKU KK
Original Assignee
MITSUMARU KAGAKU KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by MITSUMARU KAGAKU KK filed Critical MITSUMARU KAGAKU KK
Priority to JP60218853A priority Critical patent/JPS6279241A/en
Publication of JPS6279241A publication Critical patent/JPS6279241A/en
Publication of JPH0455623B2 publication Critical patent/JPH0455623B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Manufacturing Of Magnetic Record Carriers (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:To decompose a base film of a binder and to recover only magnetic powder in high purity, by treating coated type magnetic tape with a mixed solution of an organic solvent and an alkali aqueous solution, etc. CONSTITUTION:Waste magnetic tape is treated with a solution consisting of an organic solvent to partially dissolve or swell a binder in a coated type magnetic recording material and a solution of an alkali in water or an alcohol at normal temperature - the boiling point of the solution. The mixed solution consists of 60-95(V/V)% organic solvent and 40-5(V/V)% solution of an alkali in water or an alcohol. Acetone, chloroform, etc., are used as the organic solvent, caustic soda or caustic potash as the alkali and methanol, etc., as the alcohol.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は磁気テープ、磁気ディスク等の磁気記録材料か
ら磁性粉を回収する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for recovering magnetic powder from magnetic recording materials such as magnetic tapes and magnetic disks.

[従来の技術] 例えば、塗布型の磁気テープはベースフィルムとその上
に磁性粉、バインダー、有機溶剤等を混練した磁性塗料
を均一に塗布、屹燥した磁性層から成っている。
[Prior Art] For example, a coated magnetic tape consists of a base film and a magnetic layer on which a magnetic coating material containing magnetic powder, a binder, an organic solvent, etc. is uniformly applied and dried.

ベースフィルムとしてはポリエステル、ポリプロピレン
、ポリカーボネート等のフィルムが使用されている。
As the base film, films of polyester, polypropylene, polycarbonate, etc. are used.

一方、磁性粉はγ−Fe203 、Co含有γFe2O
3、CrO2等の金属酸化物の粉末又はFe、Fe−C
o−N i等の金属粉末が有り、又、バインダーは塩化
ビニル、酢酸ビニル、塩化ビニル−酢酸ビニル共重合物
、ポリウレタン樹脂、ポリエステル樹脂、エポキン樹脂
、硝化綿等が一般的である。
On the other hand, the magnetic powder is γ-Fe203, Co-containing γFe2O
3. Metal oxide powder such as CrO2 or Fe, Fe-C
There are metal powders such as o-Ni, and binders generally include vinyl chloride, vinyl acetate, vinyl chloride-vinyl acetate copolymer, polyurethane resin, polyester resin, Epoquin resin, and nitrified cotton.

バインダーは熱可塑性と熱硬化性に大別されるが、磁気
テープの強度、耐久性等の点で熱硬化性バインダーが含
まれる場合が多く、該熱硬化性バインダーは三次元構造
ができて溶剤に対してほとんど溶解しない。
Binders are broadly classified into thermoplastic and thermosetting binders, but thermosetting binders are often included in magnetic tapes for their strength and durability. hardly soluble in

製造工程から必然的に発生ずる塗布型の廃磁気テープよ
りベースフィルム及び磁性粉を回収する方法は従来から
研究され・ており、例をめげればアルカリ水溶液又はア
ルカリのアルコール溶液で処理るする方法(特開昭54
−66985号、同53−70404号、同53−1i
2979号)、アルカリ性グリコールで処理する方法(
英国特許第1134967号)、アルカリ性グリコール
で処理する工程と液状ハロゲン化炭化水素で処理する工
程の両工程で処理する方法(特開昭53−94381号
)、アルカリ゛性グリ]−ルで処理する工程とケトン、
エステル、エーテル基の少なくとも1つを有する有機溶
剤で処理する工程の両工程で処理する方法(特公昭60
−23134号)等が有る。
Methods for recovering base film and magnetic powder from coated waste magnetic tape that is inevitably generated during the manufacturing process have been studied for a long time, and for example, a method of treating it with an alkaline aqueous solution or an alkaline alcohol solution is a method that has been studied for a long time. (Unexamined Japanese Patent Publication No. 54
-66985, 53-70404, 53-1i
2979), a method of treatment with alkaline glycol (
British Patent No. 1134967), a method of treating with both alkaline glycol and liquid halogenated hydrocarbon (Japanese Patent Application Laid-open No. 53-94381), treatment with alkaline glycol process and ketones,
A method in which both steps are treated with an organic solvent having at least one of ester and ether groups (Japanese Patent Publication No. 1983)
-23134) etc.

[発明が解決しようとする問題点] しかしながら、これらの方法は主としてベースフィルム
の回収を目的としており、ベースフィルムから分離され
た磁性粉は残存バインダーによって結合されているため
、前述した理由により有機溶剤中で新たなバインダーと
混練しても均一/よ分散状態にする事は側底不可能でお
る。
[Problems to be Solved by the Invention] However, these methods are mainly aimed at recovering the base film, and since the magnetic powder separated from the base film is bound by a residual binder, organic solvents cannot be used for the reasons mentioned above. Even if it is kneaded with a new binder inside, it is impossible to achieve a uniform/well-dispersed state at the bottom of the side.

又、ベースフィルムと磁性粉を同時に回収する方法を実
際に行なう場合、磁気テープの切断、破砕1.撹拌等の
工程が不可欠であり、ベースフィルムの大部分は回収さ
れるにしても、一部のベースフィルムは破片、粉末状と
なって磁性層に混入してくる。
In addition, when actually carrying out the method of recovering the base film and magnetic powder at the same time, cutting and crushing the magnetic tape 1. Stirring and other steps are essential, and even if most of the base film is recovered, some of the base film becomes fragments or powder and mixes into the magnetic layer.

もし、この様な磁性粉を磁気テープの原料として利用し
ようとしても、出来た磁気テープは全く価値のないもの
である。
If such magnetic powder were to be used as a raw material for magnetic tape, the resulting magnetic tape would be completely worthless.

そこで、比重や磁気を利用して磁性粉とベースフィルム
を分離する事が考えられるが、実際上工業的に完全に分
離するのは収率、コスト等を考えればかなり無理がある
と推察される。
Therefore, it is conceivable to separate the magnetic powder and base film using specific gravity or magnetism, but it is presumed that it is quite impossible to completely separate the magnetic powder from an industrial point of view considering yield, cost, etc. .

従って、前述の如き方法で回収された磁性粉は、玩具、
ゴム磁石等の付加価値の小さい用途に限られている。
Therefore, the magnetic powder recovered by the method described above can be used for toys,
It is limited to applications with low added value such as rubber magnets.

価格的に見ると、磁気テープに使われる磁性粉はベース
フィルムに比べてかなり高価でおる。
In terms of price, the magnetic powder used in magnetic tape is considerably more expensive than the base film.

回収された磁性粉を磁気テープの原料として再利用出来
る様にする事は、資源の保全及びその有効利用の立場か
ら見て大いに価値の有る事である。
Making it possible to reuse the recovered magnetic powder as a raw material for magnetic tape is of great value from the standpoint of resource conservation and effective use.

[問題点を解決するための手段] そのためには、回収磁性粉中の残存バインダーffiを
出来る限り少なくし、磁性層中での磁性粉の分散状態を
良好ならしめる事が必要である。
[Means for Solving the Problems] For this purpose, it is necessary to reduce the residual binder ffi in the recovered magnetic powder as much as possible and to improve the dispersion state of the magnetic powder in the magnetic layer.

本発明においては、磁性粉の特性を損なう事なく、バイ
ンダーを実質的にほぼ完全に除去し、磁性粉の分散性が
最も重要視される磁気テープにも利用される様な磁性粉
として回収しようとするものである。
In the present invention, the binder is virtually completely removed without impairing the properties of the magnetic powder, and the magnetic powder is recovered as magnetic powder that can be used in magnetic tapes, where the dispersibility of magnetic powder is of paramount importance. That is.

すなわち、本発明は塗イ[型磁気記録材料中のバインダ
ーを部分的溶解或は膨潤させる様な有機溶剤とアルカリ
の水又はアルコール溶液から成る溶液中で、常温〜溶液
の沸点の温度で処理する事により磁気記録材料から磁性
粉を回収する方法にかかるものである。
That is, the present invention provides a coating method in which the binder in the magnetic recording material is treated in a solution consisting of an organic solvent and an alkaline water or alcohol solution that partially dissolves or swells the binder in the magnetic recording material at a temperature ranging from room temperature to the boiling point of the solution. The invention relates to a method for recovering magnetic powder from magnetic recording materials.

本発明において使用される有機溶剤としては、■ バイ
ンダーを部分的溶解或は膨潤させる事。
The organic solvent used in the present invention is: (1) Partially dissolving or swelling the binder.

■ 使用される条件下でアルカリと反応してそれを不活
性化せしめない事又はその反応速度が遅い事。
■ It does not react with alkali to inactivate it under the conditions in which it is used, or its reaction rate is slow.

の二つ、の条件を満しておればいかなるものでも良く、
具体的にはアセトン、メチルエチルケトン、シクロヘキ
サノン等のケ1〜ン頚、酢酸エヂル等のエステル類、ク
ロロホルム等のハロゲン化炭化水素類、ジメチルスルホ
キシド等のIa黄黄金合物がこの条件を満している。こ
の条件を満していないものを一部混合している場合でも
、混合溶剤として以上の条件を満していれば使用できる
Anything is fine as long as it satisfies the following two conditions:
Specifically, Ia yellow gold compounds such as acetone, methyl ethyl ketone, and cyclohexanone, esters such as ethyl acetate, halogenated hydrocarbons such as chloroform, and dimethyl sulfoxide meet this condition. . Even if a part of the solvent does not meet these conditions, it can be used as a mixed solvent as long as it satisfies the above conditions.

アルカリとしては苛性ソーダ、苛性カリ等一般的なもの
が使用できる。
As the alkali, common alkalis such as caustic soda and caustic potash can be used.

アルコールは必要な量のアルカリを溶かすだけの溶解性
が有れば良く、メタノール、エタノール、イソプロピル
アルコール等の安価なものが望ましい。
The alcohol only needs to have enough solubility to dissolve the necessary amount of alkali, and inexpensive ones such as methanol, ethanol, and isopropyl alcohol are preferable.

ω的関係を見ると、アルカリは反応終了後も溶液が強ア
ルカリを示す程度に加えれば良く、少ない場合は反応速
度が遅くなり、極端な場合は途中でアルカリが消滅して
分解反応がそれ以上進まなくなる。その適正量は磁性層
中のバインダー但及び混入したベースフィルム量によっ
て異なるが、通常の場合磁性層の5〜20(W/W)%
である。
Looking at the ω relationship, it is sufficient to add alkali to the extent that the solution remains strongly alkaline even after the reaction is complete; if there is too little, the reaction rate will slow down, and in extreme cases, the alkali will disappear midway through, causing the decomposition reaction to proceed further. It stops progressing. The appropriate amount varies depending on the binder in the magnetic layer and the amount of the base film mixed, but in general, it is 5 to 20 (W/W)% of the magnetic layer.
It is.

アルコール又は水の債は必要なアルカリを溶解出来るm
があれば良いが、工業的に行なう場合α理の終った溶液
は蒸預等で回収する必要が有り、回収された溶液は有機
溶剤と水又はアルコールの混合溶液でおる(両者を完全
に分離する事も可能であるが経済的見地から見て好まし
くない)。従って、アルカリはこの回収溶液に溶解させ
ることが便利でおるが、アルコール又は水の旧が少ない
場合はアルカリの??[が非常に困難となる。又その量
が多過ぎる場合は有機溶剤の割合が低くなり過ぎてしま
い、有機溶剤を使用すると言う本発明の効果がうすれる
。従って、溶液内に占るアルコール又は水の割合は5〜
40(V/V)%が好ましい。
Alcohol or water can dissolve the necessary alkali.
However, for industrial use, it is necessary to recover the solution after α-processing by evaporation, etc., and the recovered solution is a mixed solution of organic solvent and water or alcohol (the two must be completely separated). Although it is possible to do so, it is not desirable from an economic standpoint). Therefore, it is convenient to dissolve the alkali in this recovery solution, but if the amount of alcohol or water is low, it is better to dissolve the alkali in the recovered solution. ? [is extremely difficult. Furthermore, if the amount is too large, the proportion of the organic solvent will become too low, and the effect of the present invention of using an organic solvent will be lost. Therefore, the proportion of alcohol or water in the solution is between 5 and 5.
40 (V/V)% is preferred.

処理温度は高温の方が反応は早いが、他の制約により高
温に出来ない場合は低温で処理時間を長くすれば良い。
The reaction is faster at a higher treatment temperature, but if it is not possible to raise the temperature to a higher temperature due to other constraints, the treatment time may be increased at a lower temperature.

加圧状態で沸点以上の温度で51!l即する事も出来る
が一般には常温〜溶液の沸点迄の範囲が好ましい。
51 at a temperature above the boiling point under pressure! Although it is possible to do so immediately, it is generally preferred to use a temperature in the range from room temperature to the boiling point of the solution.

[作  用コ 本発明においては、磁性粉を結合しているバインダーは
勿論ベースフィルムをも分解し、水又は有機溶剤に可溶
なものに変え、磁性粉のみを高純度で回収する事が出来
る。その点で従来の方法とは根本的に異なる。
[Function] In the present invention, not only the binder that binds the magnetic powder but also the base film is decomposed and converted into something soluble in water or an organic solvent, making it possible to recover only the magnetic powder with high purity. . In this respect, it is fundamentally different from conventional methods.

更に詳しく説明すれば、ベースフィルムと磁性粉の両方
を回収する場合は、前工程で既知の方法によりベースフ
ィルムと磁性層を分離してまずベースフィルムを回収し
、次いで後工程も本発明による方法によって、磁性粉を
結合しているバインダー及び一部混入しているベースフ
ィルムを分解、溶解により除去し、磁性粉のみを高純度
で回収する事が出来る。
More specifically, when recovering both the base film and the magnetic powder, the base film and magnetic layer are separated in the pre-process by a known method and the base film is recovered first, and then the post-process is also carried out using the method according to the present invention. By decomposing and dissolving the binder binding the magnetic powder and the base film partially mixed in, it is possible to recover only the magnetic powder with high purity.

[実 施 例] 前処理工程 CO含含有−Fe203タイプのビデオテープを物理的
にベースフィルムと磁性層に剥離した。
[Example] Pre-treatment step A CO-containing Fe203 type videotape was physically separated into a base film and a magnetic layer.

得られた磁性層(以下剥am性層と略す)は23〜24
(W/W)%のバインダー及びベースフィルム(以下不
純物と略す)を含み、色は黒く、磁性粉が完全に結合さ
れた状態でおる。
The obtained magnetic layer (hereinafter abbreviated as peelable layer) was 23 to 24
It contains (W/W)% binder and base film (hereinafter referred to as impurities), is black in color, and is in a state in which the magnetic powder is completely bound.

実施例1及び比較例1 100rfの■ジメチルスルホキシド、■メチルエチル
ケトン、■アセトン(以上実施例)、■メタノール(比
較例)に10(W/V)%苛性ソーダーメタノール溶液
を101加えた溶液中で、10gの前記前処理工程で1
qられた剥1i1t[a性層を55℃で5時間撹拌し、
濾過、水洗、乾燥を行なった。
Example 1 and Comparative Example 1 In a solution of 100 rf of ■ dimethyl sulfoxide, ■ methyl ethyl ketone, ■ acetone (the above examples), ■ methanol (comparative example), 101 of a 10 (W/V)% caustic soda methanol solution was added. 1 in the above pretreatment step of 10 g
The peeled layer was stirred at 55°C for 5 hours,
Filtration, washing with water, and drying were performed.

その不純物は■2.2(W/W)%、■1.8(W/W
)%、■1.a(W/W)%、■3.9(す/W)%で
あり、磁性粉の色も■は黒味を帯びていたが、■〜■は
赤味を帯び本来のCO含含有−Fe203の色に近かっ
た。これはバインダーによる磁性粉の結合がかなり少な
くなったためと推察される。
The impurities are ■2.2 (W/W)%, ■1.8 (W/W)
)%, ■1. a(W/W)%, ■3.9(S/W)%, and the color of the magnetic powder was blackish in ■, but reddish in ■ to ■, which is the original CO content. The color was close to that of Fe203. This is presumed to be because the binding of the magnetic powder by the binder was considerably reduced.

実施例2 前記剥!lla性111000をメチルエチルケトン1
000xf、メタノール100if、苛性ソーダ10(
Jの溶液中で沸点下3時間撹拌し、を過後再度同じ処理
を繰返した後−過、水洗、乾燥を行なった。
Example 2 Peel off! lla 111000 to methyl ethyl ketone 1
000xf, methanol 100if, caustic soda 10(
The mixture was stirred in a solution of J at boiling point for 3 hours, filtered, and the same treatment was repeated again, followed by filtering, washing with water, and drying.

不純物は1.2(W/W)%で、色は赤味を帯びていた
Impurities were 1.2 (W/W)%, and the color was reddish.

実施例3 実施例2のメタノールの代りに水を使用する以外は実施
例2と全く同じ処理を行なった。
Example 3 The same procedure as in Example 2 was carried out except that water was used instead of methanol.

不純物は1.3(W/W)%で、色は赤味を帯びていた
Impurities were 1.3 (W/W)%, and the color was reddish.

実施例4 前記剥MIfi性sioogをメチルエチルケトン10
00if、メタノール30hyf、苛性ソーダ10(l
の溶液中で55℃5時間撹拌後、)濾過、水洗、乾燥を
行なった。
Example 4 The exfoliated MIfi sioog was treated with methyl ethyl ketone 10
00if, methanol 30hyf, caustic soda 10(l
After stirring in the solution at 55° C. for 5 hours, the mixture was filtered, washed with water, and dried.

不純物は2.2(W/W)%で、色は赤味を帯びていた
Impurities were 2.2 (W/W)%, and the color was reddish.

比較例2 ビデオテープ1001jを6 (W/V)%苛性ソーダ
水溶液51中で90℃1時間撹、拌後、)濾過、水洗に
より磁性層とベースフィルムに分離した。
Comparative Example 2 Videotape 1001j was stirred in a 6 (W/V)% caustic soda aqueous solution 51 at 90° C. for 1 hour, and then separated into a magnetic layer and a base film by filtration and washing with water.

ベースフィルムは無色透明のものが得られたが、磁性層
の不純物は6.6(W/W)%で黒味を帯びていた。
A colorless and transparent base film was obtained, but the impurities in the magnetic layer were 6.6 (W/W)% and were blackish.

比較例3 前記剥離磁性層100(lを12(t4/V)%苛性ソ
ーダ水溶液1000xf中で90℃■5時間、010時
間、■20時間撹拌し、−過、水洗によりpH9以下に
した後、80℃で乾燥した。
Comparative Example 3 The peelable magnetic layer 100 (l) was stirred at 90° C. for 5 hours, 10 hours, and 20 hours in a 12 (t4/V)% caustic soda aqueous solution of 1000xf, and then adjusted to pH 9 or less by filtering and washing with water. Dry at °C.

その不純物は■4.7(W/W)%、■4.1(W/W
)%、■3.9(W/W)%で磁性粉は黒味を帯びてい
た。
The impurities are ■4.7 (W/W)%, ■4.1 (W/W)%
)%, ■3.9 (W/W)%, the magnetic powder was blackish.

■をもう一度繰返して処理したが不純物、色共に変らな
かった。
Although the process (2) was repeated once more, there was no change in impurities or color.

比較例4 比較例3−■の磁性粉10gを10011iの■ジメチ
ルホルムアミド、■エタノール、■アセトン中で80℃
(沸点の低いものはその沸点〉30分間撹拌し、)濾過
後もう一度同じ処理を繰返した後乾燥した。
Comparative Example 4 Comparative Example 3-10g of the magnetic powder of ■ was heated at 80°C in 10011i of ■ dimethylformamide, ■ ethanol, and ■ acetone.
(Those with a low boiling point were stirred for 30 minutes beyond that boiling point.) After filtration, the same process was repeated once and then dried.

その不純物は■3.1(W/W)%、■3.5(W/W
)%、■3.3(W/W)%で磁性粉は黒味を帯びてい
た。
The impurities are ■3.1 (W/W)%, ■3.5 (W/W)%
)%, ■3.3 (W/W)%, the magnetic powder was blackish.

なお、以上廃磁気テープからの回収について説明したが
、磁気テープ製造工程中に発生する廃磁気塗料或は洗浄
液からの磁性粉の回収についても全く同じ方法で可能で
おる事は言うまでもない。
Although recovery from waste magnetic tape has been described above, it goes without saying that the same method can be used to recover magnetic powder from waste magnetic paint or cleaning fluid generated during the magnetic tape manufacturing process.

[発明の効果][Effect of the invention]

Claims (1)

【特許請求の範囲】 1)塗布型磁気記録材料中のバインダーを部分的溶解或
は膨潤させる様な有機溶剤とアルカリの水又はアルコー
ル溶液から成る溶液中で、常温〜溶液の沸点の温度で処
理する事を特徴とする磁気記録材料からの磁性粉回収方
法。 2)塗布型磁気記録材料中のバインダーを部分的溶解或
は膨潤させる様な有機溶剤が60〜95(V/V)%、
アルカリの水又はアルコール溶液が40〜5(V/V)
%である特許請求の範囲第1)項に記載の磁気記録材料
からの磁性粉回収方法。
[Claims] 1) Treatment in a solution consisting of an organic solvent and an alkaline water or alcohol solution that partially dissolves or swells the binder in the coated magnetic recording material at a temperature between room temperature and the boiling point of the solution. A method for recovering magnetic powder from a magnetic recording material, characterized by: 2) 60 to 95 (V/V)% of an organic solvent that partially dissolves or swells the binder in the coating type magnetic recording material;
Alkaline water or alcohol solution is 40-5 (V/V)
% of magnetic powder from a magnetic recording material according to claim 1).
JP60218853A 1985-10-01 1985-10-01 Method of recovering magnetic powder from magnetic recording material Granted JPS6279241A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60218853A JPS6279241A (en) 1985-10-01 1985-10-01 Method of recovering magnetic powder from magnetic recording material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60218853A JPS6279241A (en) 1985-10-01 1985-10-01 Method of recovering magnetic powder from magnetic recording material

Publications (2)

Publication Number Publication Date
JPS6279241A true JPS6279241A (en) 1987-04-11
JPH0455623B2 JPH0455623B2 (en) 1992-09-03

Family

ID=16726348

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60218853A Granted JPS6279241A (en) 1985-10-01 1985-10-01 Method of recovering magnetic powder from magnetic recording material

Country Status (1)

Country Link
JP (1) JPS6279241A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5290505A (en) * 1990-11-26 1994-03-01 Wnc-Nitrochemie Gmbh Method of recycling adhesive-coated plastic sheet material
US5500849A (en) * 1990-10-23 1996-03-19 Asahi Kogaku Kogyo Kabushiki Kaisha Construction of optical disk

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5500849A (en) * 1990-10-23 1996-03-19 Asahi Kogaku Kogyo Kabushiki Kaisha Construction of optical disk
US5290505A (en) * 1990-11-26 1994-03-01 Wnc-Nitrochemie Gmbh Method of recycling adhesive-coated plastic sheet material

Also Published As

Publication number Publication date
JPH0455623B2 (en) 1992-09-03

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