JPH0423037B2 - - Google Patents
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- JPH0423037B2 JPH0423037B2 JP1041903A JP4190389A JPH0423037B2 JP H0423037 B2 JPH0423037 B2 JP H0423037B2 JP 1041903 A JP1041903 A JP 1041903A JP 4190389 A JP4190389 A JP 4190389A JP H0423037 B2 JPH0423037 B2 JP H0423037B2
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
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Description
[産業上の利用分野]
本発明は印刷古紙の脱インキ法に関し、特に軽
量コート紙に印刷した古紙の脱インキに適した印
刷古紙の脱インキ法に関する。
[従来の技術]
従来より木材資源の有効活用の見地から新聞、
雑誌、一般印刷物等の印刷古紙を脱インキし、バ
ージンパルプと共に利用することが行われてい
る。
印刷古紙の脱インキ法は、古くはパルパー等の
難解機で古紙にアルカリ、界面活性剤等の脱墨剤
を加えて原料濃度10%以下の低濃度で離解した
後、希釈し、洗浄又はフローテーシヨンにより脱
墨処理を行い、必要に応じ漂白する方法が行われ
ていた。その後多くの改良提案が見られるが、例
えば白色度を向上させる方法として、特公昭52−
20563号公報が知られている。同発明はアルカリ、
脱墨剤を加えて低原料濃度で離解し、濃度15%以
上に脱水し、脱墨剤等を再添加して再脱インキ及
び漂白を行い、その後、希釈、洗浄又はフローテ
ーシヨンを行う方法である。
更に白色度と紙力を向上させる提案として、特
開昭52−1102号公報は、脱墨薬品を加えて低濃度
離解し、濃度15%以上に脱水して長時間熟成処理
した後、洗浄処理を行う方法が開示されている。
しかしながら、印刷古紙は近年印刷技術の面から
凸版印刷より印刷が美麗なオフセツト印刷が増加
したため、上記の脱インキ法では十分な脱墨が難
しい状況になつてきた。これはオフセツトインキ
の合成樹脂や植物油が印刷後、経時的に酸化重合
して繊維に付着し、従来の脱インキ法ではインキ
が繊維から剥れにくく、未剥離インキになりやす
いためである。
このため、オフセツト印刷古紙の脱墨法の提案
がなされ、たとえば、特開昭54−120705号公報に
は濃度10%以下の原料古紙に脱墨薬品を加えて離
解するA工程、原料濃度を10%以上に脱水するB
工程、古紙に対し3%以上のアルカリを添加する
C工程、濃度10%以上で3時間以上アルカリ浸漬
するD工程、捏和機(ニーダー)などで1分以上
撹拌処理するE工程、その後、希釈、洗浄、浮
遊、漂白等の後処理を行うF工程をこの順で含む
方法が開示されている。また、特開昭55−40850
号公報にはオフセツト古紙を含有した印刷古紙に
アルカリ、界面活性剤より成る脱墨剤及び過酸化
水素漂白剤を添加し、15%以上の濃度並びに5.0
g/(NaOHとして)以上のアルカリ濃度に
おいて、レフアイナー、ニーダー等を使用し、加
温下で圧縮力を与えながら機械的撹拌を行う方法
が見られる。最近では前記特開昭55−40850号公
報の改良方法として、特開昭63−28992号公報に
機械的撹拌処理の後、0.5時間以上熟成し、再び
濃度15〜25%で機械的撹拌処理を行う方法が開示
されている。
一方、印刷古紙に脱墨しにくいオフセツト印刷
古紙が増加したことは前述の通りであるが、近年
は一般雑誌のカラー印刷の増加に伴い、印刷古紙
にもコート紙の多印刷再が目立つている。殊にゲ
ートロールコーターなどで塗工された塗布量10
g/m2未満の中質軽量コート紙の古紙は、塗布量
10g/m2以上のコート紙に比べて、コート層上の
インキが紙層まで浸透している。従つて前記のオ
フセツトインキを対象とした脱墨法により未剥離
インキはほとんど無くなるが、フローテーシヨン
前記に機械的撹拌処理を行うので、剥離したイン
キが微細化し、フローテーシヨン工程でのインキ
の捕修が極めて困難となる。その結果フローテー
シヨン効率を低下させ得られる脱インキパルプ
(DIP)に微細化したインキが残つて、灰色にく
すみ、白色度の向上にも限界があり、高グレード
の中級紙への大量配合は難しいのが現状である。
[発明が解決しようとする課題]
これらの現状に鑑み、本発明者等は次のような
ことを考察した。即ち、従来の脱インキ法では古
紙の脱墨工程でアルカリ浸漬後、ニーダー等で機
械的撹拌処理を行なつて、フローテーシヨン、洗
浄の後処理を行うか、或いは、機械的撹拌−アル
カリ浸漬−機械的撹拌してフローテーシヨン、洗
浄を行つている。
このため、軽量コート紙の印刷古紙の場合、ア
ルカリ浸漬で繊維から剥離した又は剥離し易い状
態になつたコート層とその上のオフセツトインキ
を次の機械的撹拌処理によつて分散させるが、未
剥離インキと同時に剥離しているインキをも分散
し、微細化してしまい、インキ粒子の繊維への再
付着さえ起つてくる。従つて、インキ粒子が微細
化しているために後処理のフローテーシヨンの効
率が低下し、更にインキ粒子の繊維表面への再付
着さえ起り、繊維の色のくすみが増えることにな
る。
また、中質軽量コート紙に限らず、オフセツト
印刷古紙を含む古紙原料から高白色度を得るため
に漂白剤として過酸化水素を高率添加しても(1)古
紙中の汚濁物により過酸化水素の無効消費がある
(2)ニーダー等により過酸化水素が分解する(3)アル
カリ浸漬での白色度向上には限界があり過酸化水
素の効率が悪い等の問題があつた。
本発明は上述の問題点を解決するためになされ
たもので、本発明者等はアルカリ浸漬を2段で行
うことを着想し、前段のアルカリ浸漬により、前
記中質軽量コート紙を含む印刷古紙から剥離した
コート層とインキの粗い粒子の脱インキ法とは逆
に機械的撹拌前にフローテーシヨンを行うことに
より除去して、従来問題となつていた剥離したイ
ンキが機械的撹拌により微細化して繊維に再付着
するのを防止できるとの知見を得て、鋭意研究の
結果、本発明を完成するに至つた。
また、本発明の脱インキ法は同時に近年脱イン
キしにくい印刷古紙として課題となつている前記
中質軽量コート紙以外の中質、新聞オフセツト印
刷古紙の脱インキにも効果があることの知見を得
た。
本発明の主な目的は上述の問題点を解決して、
印刷古紙、殊に中質軽量コート紙を含む印刷古紙
の脱インキに適し、未剥離インキが殆んどなく、
且つ高白色度の脱インキパルプ(DIP)が得られ
る印刷古紙の脱インキ法を提供することである。
また、他の目的は、前記中質軽量コート紙を含
む印刷古紙以外に中質コート、ノーコート印刷古
紙、上質コート印刷古紙、新聞古紙を含む一般回
収印刷古紙から未剥離インキが殆んどなく、且つ
高白色度の脱インキパルプが得られる印刷古紙の
脱インキ法を提供することである。
[課題を解決するための手段]
本発明は、回収された印刷古紙にアルカリ薬
剤、界面活性剤よりなる脱墨剤を添加し、10%以
上の原料濃度で前段のアルカリ浸漬を行う工程、
次いで原料を希釈してフローテーシヨンを行う工
程、更に原料を脱水して再びアルカリ薬剤、界面
活性剤よりなる脱墨剤を添加し、10%以上の原料
濃度で後段のアルカリ浸漬を行う工程並びに前記
後段のアルカリ浸漬の前または後、もしくは前記
後段のアルカリ浸漬の前後双方で、10%以上の原
料濃度の下に機械的撹拌を行う工程を連ね、更に
前記各工程のうちの最終段において洗浄を行う工
程を付帯させたことを特徴とする印刷古紙の脱イ
ンキ法である。
また、本発明はアルカリ浸漬工程で、漂白剤を
添加し、アルカリ浸漬と同時に漂白を行う前記の
印刷古紙の脱インキ法である。
本発明の脱インキ法は、近年の低濃度離解〜高
濃度アルカリ浸漬〜高濃度機械的撹拌〜フローテ
ーシヨン又は洗浄を基本工程とする脱インキ法に
おいて、アルカリ浸漬を前後2段とし、前段のア
ルカリ浸漬後にフローテーシヨンを行い、後段の
アルカリ浸漬の前又は後、或いは前後で機械的撹
拌処理を行うことを特徴とする。従来のように、
アルカリ浸漬後にニーダー等により高濃度で機械
的撹拌を行うと、アルカリ浸漬によりせつかく繊
維から剥離したインキ粒子が必要以上に細粒化さ
れ、後処理のフローテーシヨンで除去できないも
のが多くなり、フローテーシヨンの脱インキ効率
を悪くし、インキの除去が十分できないおそれが
あつた。殊にゲートロールコーターなどにより塗
料が塗工された中質軽量コート紙の印刷古紙は、
塗料の塗布量が少なく、印刷されたインキはコー
ト層を通して紙層に達しているため、未剥離イン
キを剥離するために機械的撹拌を行うとコート層
上のインキはコート層と共に細粒化されるので、
余計にインキ粒子の除去が難しかつた。
本発明の方法によれば、前段のアルカリ浸漬で
繊維から剥離したインキ粒子を比較的大きい状態
でフローテーシヨンによる除去を行い、フローテ
ーシヨンの効率を高めることができる。フローテ
ーシヨン法では、一般にインキ粒子径が10〜
100μm程度の比較的大きい粒子でインキの除去
効率が良く、洗浄法では25μm以下の細かい粒子
が効率的であると言われていることから、本発明
の方法で、アルカリ浸漬後、必要以上にインキ粒
子を細かくしないで、フローテーシヨンを行うこ
とは、フローテーシヨンのインキ除去効率を最も
高くすることができるのである。
また、後段のアルカリ浸漬では、未剥離インキ
とフローテーシヨンで除去されなかつたインキ
を、アルカリ浸漬前又は後或いは前後でニーダー
等で機械的撹拌処理を行い、後処理の洗浄工程で
洗浄効率が最も高くなるように、インキ粒子をで
きるだけ微細化して洗浄を行うのである。
更に、アルカリ浸漬を2段で行うと、同時に過
酸化水素等による漂白も2段で行うことができる
ので、漂白剤の効率も良い。また、漂白を1段で
行う場合は後段のアルカリ浸漬と同時に行うこと
が好ましい。かくして、印刷古紙から未剥離イン
キが殆んどなく、しかも高白色度のDIPを効率よ
く得られる。
本発明の印刷古紙にアルカリ薬剤、界面活性剤
よりなる脱墨剤を添加し、10%以上の原料濃度で
アルカリ浸漬を行う工程は、通常、古紙脱インキ
の最初の工程である古紙をパルパー等で離解した
後、行われる。
アルカリ薬剤としては苛性ソーダ、ケイ酸ソー
ダ等公知のアルカリが用いられ、界面活性剤は従
来脱インキに用いられる公知のものが用いられ
る。
アルカリ浸漬は、別に熟成とも称される工程
で、繊維から剥離していないインキをアルカリと
十分に反応させるために必要なもので、原料濃
度、アルカリ添加量、温度等により浸漬時間は異
なるが、本発明では0.5時間以上、好ましくは1
時間以上必要である。アルカリ添加量はアルカリ
濃度として3g/(NaOHとして)、好ましく
は5g/(NaOHとして)必要である。
原料濃度は10%以上、好ましくは15%以上は必
要で、アルカリ浸漬においては、濃度を高めるこ
とにより、アルカリ濃度を高くすることができる
一方、アルカリ濃度を抑えればアルカリ添加量の
節減も可能である。
アルカリ浸漬工程では、脱墨剤のほかに過酸化
水素等の漂白剤も同時に添加して、古紙原料の漂
白作用も同時に行う。
上記のアルカリ浸漬、漂白の実施条件は、後段
のアルカリ浸漬、漂白の実施に際しても同様であ
るが、印刷古紙の性状に応じて、好ましい条件の
範囲内において、前段の後段の条件を変えること
は、実際上有効である。
次に古紙原料を希釈してフローテーターを用い
て、公知の低い濃度で、原料中の剥離されたイン
キ粒子並びにコート紙古紙から剥離した顔料、合
成樹脂などからなるコート層の比較的粗い粒子を
分離、除去する。
比較的粗いインキ粒子を除去した低濃度古紙原
料を脱水して、再びアルカリ薬剤、界面活性剤よ
りなる脱墨剤を添加し、10%以上の原料濃度でア
ルカリ浸漬を行う工程にかける。この後段のアル
カリ浸漬で、前段のアルカリ浸漬とフローテーシ
ヨンで除去できなかつた繊維の未剥離インキを再
び脱墨剤と反応させて繊維から剥離し、アルカリ
浸漬の前又は後或いは前後で10%以上の原料濃度
でニーダー等による機械的撹拌処理を行う工程を
通すことにより、インキ粒子等は後処理の洗浄工
程で効率よく洗浄除去され易いように、細粒化さ
れる。
ニーダー等による機械的撹拌処理は、知られる
ように、50℃以上の加温下に10%以上の高い原料
濃度で圧縮力を与えながら、アルカリ等の脱墨剤
の存在下で、ニーダー、ミキサー、デイスパーザ
ー等により繊維に強固に付着しているオフセツト
インキなどの未剥離インキの被膜を破壊し、イン
キを繊維から剥離させることができる。
本発明の方法では、この機械的撹拌処理を前段
のアルカリ浸漬とフローテーシヨン処理で比較的
粗いインキ粒子等を除去した後に、更にアルカリ
浸漬を行つて繊維から未剥離インキの剥離或いは
剥離したインキの繊維への再付着を防止する措置
を講じた上で、機械的撹拌処理を行つているの
で、上述の従来の脱インキ法における機械的撹拌
処理の効果に比較して効率的に細かいインキ粒子
を除去できる点ですぐれている。
以下本発明の実施例を示す。
[実施例]
実施例 1
中質微塗工紙からなる印刷古紙200gを、予め
脱墨剤(苛性ソーダ0.8%、ケイ酸ソーダ4.0%、
界面活性剤0.25%)添加後、離解し脱水した後、
古紙(風乾)に対し脱墨剤として苛性ソーダ2
%、ケイ酸ソーダ6%(アルカリ濃度NaOHと
して5.4g/)、界面活性剤0.15%、漂白剤とし
て過酸化水素1.2%を添加し、よく混合した後、
原料濃度15%、60℃で2時間浸漬を行つた。次い
で、原料濃度4%に希釈し、5分間離解した後、
原料濃度1%に希釈して試験用フローテーター
(極東振興製)でフローテーシヨン処理した。再
び原料濃度20%まで脱水して、古紙(風乾)に対
し脱墨剤として苛性ソーダ2%、ケイ酸ソーダ9
%(アルカリ濃度NaOHとして6.1g/)、界面
活性剤0.12%、漂白剤・過酸化水素2.4%を添加
し、よく混合した後、原料濃度15%、70℃で3時
間浸漬を行つた。浸漬後の古紙原料を70℃の加温
下、試験用ニーダー(山本百馬製作所製)で1分
間、機械的撹拌処理を行つた後、原料濃度2%に
希釈し、2分間離解した後原料濃度1%に希釈
し、これを原料濃度10%に脱水する脱水、洗浄を
2回繰返し、DIPを得た。得られたDIPで
TAPPI標準法により秤量100g/m2の手抄シート
を作成し、下記の試験方法でDIPの未剥離インキ
量及び白色度を測定した。
試験方法
未剥離インキ量:手抄シートを画像解析装置((株)
シー・シー・デー製CCD粒度分布測定装置)
にかけ、100mm×100mmの面積中に認められる光
線反射率60%以下の格子部分の面積を集計し
て、手抄シート中の残留インキ面積とした。
白色度:JIS P8123の手順によりフオトボルト白
色度試験器で測定
比較例 1
実施例1において、アルカリ浸漬工程を1段の
みとし、その脱墨剤及び漂白剤の添加量を実施例
1の前段と後段の合計とした。すなわち、苛性ソ
ーダ4%、ケイ酸ソーダ15%(アルカリ濃度
NaOHとして11.5g/)、界面活性剤0.27%、
過酸化水素3.6%を添加し、よく混合した後、原
料濃度15%、70℃、5時間浸漬を行つた。
以下、実施例1と同様にしてニーダーで機械的
撹拌処理を行つた後、原料濃度2%に希釈し、2
分間離解した後、原料濃度1%に希釈してフロー
テーシヨン処理した。その後、実施例1と同様に
原料濃度10%に脱水し、1%に希釈する脱水が、
洗浄を2回繰返しDIPを得た。
実施例 2
実施例1において、古紙としてチラシ20%、オ
フセツト30%、凸板50%からなる一般回収新聞古
紙を用い、ニーダーによる機械的撹拌処理を後段
のアルカリ浸漬工程の前で行う以外は、実施例1
と全く同様にしてDIPを得た。
実施例 3、4
実施例2において、ニーダーによる機械的撹拌
処理を後段のアルカリ浸漬工程の後(実施例3)
又は前と後で2回行う(実施例4)以外は、実施
例1と全く同様にしてDIPを得た。機械的撹拌処
理の条件はアルカリ浸漬工程の前後とも同一で行
つた。
比較例 2
比較例1において、古紙としてチラシ20%、オ
フセツト30%、凸板50%からなる一般回収新聞古
紙を用い、ニーダーによる機械的撹拌処理を行わ
ない以外は、比較例1全く同様にしてDIPを得
た。
比較例 3
比較例2において、ニーダーによる機械的撹拌
処理をアルカリ浸漬後に行うように変更した以外
は、比較例2と全く同様にしてDIPを得た。
比較例 4
比較例2において、ニーダーによる機械的撹拌
処理をアルカリ浸漬前後に2回行うように変更し
た以外は、比較例2と全く同様にしてDIPを得
た。
比較例 5
比較例3において過酸化水素漂白剤の添加率を
3.6%から6%まで増量するように変更した以外
は、比較例3と全く同様にしてDIPを得た。
実施例 5
実施例1において、中質微塗工紙印刷古紙の代
わりに、オフセツト印刷新聞古紙を用い、アルカ
リ浸漬処理の前段を45℃、16時間で行つた以外
は、実施例1と全く同様にしてDIPを得た。
比較例 6
比較例1において、中質微塗工紙印刷古紙の代
りに、オフセツト印刷新聞古紙を用い、アルカリ
浸漬処理を60℃、16時間で行つた以外は、比較例
1と全く同様に処理してDIPを得た。
比較例 7
比較例1において、中質微塗工紙印刷古紙の代
りに、オフセツト印刷新聞古紙を用い、アルカリ
浸漬処理を70℃、16時間で行つた以外は、比較例
1と全く同様にしてDIPを得た。
以上述べた実施例、比較例で得られたDIPの試
験結果を表に示す。
表に示す結果によれば、本発明の中質軽量コー
ト紙印刷古紙の脱インキにおいて、アルカリ浸漬
を前後2段にして、同時に漂白を行い、且つ、前
段の後でフローテーシヨンを行い、後段の後で機
械的撹拌処理を行う実施例1は、従来のアルカリ
浸漬及び漂白が1段で、その後に機械的撹拌処理
を行つた後、フローテーシヨンを行う比較例1と
比較して、未剥離インキ面積が減少し、殆んどな
い状態になり、白色度を大幅に高くすることがで
きる。
また、一般回収新聞古紙についても、本発明の
実施例2〜4は中質軽量コート紙印刷古紙と同様
にアルカリ浸漬1段と機械的撹拌を行う従来の脱
インキ法(比較例2〜4)に比べて高白色度が得
られる。更に、比較例5で過酸化水素漂白剤を大
幅に増量してみたが、実施例のような高白色度は
得られなかつた。
また、オフセツト新聞古紙についてもアルカリ
浸漬と漂白を2段行う本発明の実施例5は、アル
カリ浸漬を1段で行う比較例6よりも両者の漂白
剤使用量が同量でも大巾に白色度を向上すること
ができる。なお、比較例7のようにアルカリ浸漬
の温度を上げるとアルカリ焼けを起し、白色度が
低下するので好ましくない。
これらの結果から、本発明の脱インキ法は従来
のようにインキ粒子を微細化し、フローテーシヨ
ン効率を低下させ、微細化されたインキ粒子によ
りパルプの色をくすませることがないので、中質
軽量コート紙、一般回収新聞古紙、オフセツト新
聞古紙のすべてにおいて高白色度のDIPが得られ
る。
[Industrial Application Field] The present invention relates to a method for deinking printed waste paper, and particularly to a method for deinking printed waste paper suitable for deinking waste paper printed on lightweight coated paper. [Conventional technology] Newspapers,
BACKGROUND ART Waste printed paper such as magazines and general printed matter is deinked and used together with virgin pulp. In the old days, deinking of used printed paper was done by adding deinking agents such as alkali and surfactants to the used paper using a difficult-to-disintegrate machine such as a pulper, and disintegrating it at a low concentration of less than 10% of the raw material, diluting it, and washing or flowing it. The deinking process was carried out using a stationary machine, followed by bleaching if necessary. Since then, many improvement proposals have been made; for example, as a method for improving whiteness,
Publication No. 20563 is known. The invention is based on alkali,
A method of adding a deinking agent to disintegrate at a low raw material concentration, dewatering to a concentration of 15% or more, adding the deinking agent, etc. again to perform re-deinking and bleaching, and then diluting, washing or flotation. It is. Furthermore, as a proposal to improve whiteness and paper strength, JP-A-52-1102 proposes that deinking chemicals be added to disintegrate at a low concentration, dehydrated to a concentration of 15% or more, aged for a long time, and then washed. A method is disclosed.
However, in recent years, printing technology has increased the use of offset printing, which produces more beautiful prints than letterpress printing, for used printed paper, making it difficult to sufficiently remove ink using the above-mentioned deinking method. This is because the synthetic resin and vegetable oil of the offset ink undergo oxidative polymerization and adhere to the fibers over time after printing, and the ink is difficult to peel off from the fibers using conventional deinking methods, resulting in unreleased ink. For this reason, a method for deinking offset printed waste paper has been proposed. For example, Japanese Patent Application Laid-Open No. 120705/1987 describes a step A in which a deinking chemical is added to the waste paper with a concentration of 10% or less to disintegrate it, and the concentration of the raw material is reduced to 10%. B dehydrated to more than %
Step C: adding 3% or more alkali to waste paper; D step: soaking in alkali for 3 hours or more at a concentration of 10% or more; E step: stirring for 1 minute or more using a kneader; then dilution. , washing, flotation, bleaching, and other post-treatments in this order. Also, JP-A-55-40850
In the publication, a deinking agent consisting of an alkali and a surfactant and a hydrogen peroxide bleaching agent are added to printed waste paper containing offset waste paper to achieve a concentration of 15% or more and 5.0%.
When the alkali concentration is higher than g/g/(as NaOH), there is a method of mechanical stirring using a refiner, kneader, etc. while applying compressive force under heating. Recently, as an improvement method of JP-A-55-40850, in JP-A-63-28992, after mechanical stirring treatment, aging for 0.5 hours or more, and then mechanical stirring treatment again at a concentration of 15 to 25%. A method is disclosed. On the other hand, as mentioned above, there has been an increase in the use of offset printed waste paper, which is difficult to deink, but in recent years, with the increase in color printing of general magazines, there has been a noticeable reprinting of coated paper in used paper. . Especially when applied with a gate roll coater etc., the coating amount is 10.
For waste paper of medium-quality lightweight coated paper less than g/ m2 ,
Compared to coated paper with a weight of 10 g/m 2 or more, the ink on the coat layer penetrates into the paper layer. Therefore, although the deinking method for offset ink described above eliminates most of the unpeeled ink, since mechanical agitation treatment is performed before flotation, the peeled ink becomes finer and the ink is removed during the flotation process. It becomes extremely difficult to catch. As a result, the flotation efficiency decreases, and finely divided ink remains on the resulting deinked pulp (DIP), resulting in a dull gray color, and there is a limit to the improvement of whiteness. The current situation is difficult. [Problems to be Solved by the Invention] In view of these current circumstances, the present inventors have considered the following. That is, in the conventional deinking method, in the deinking process of used paper, after immersion in alkali, mechanical agitation treatment is performed using a kneader or the like to perform flotation and post-washing treatment, or mechanical agitation-alkali immersion treatment is performed. - Floatation and washing are performed by mechanical stirring. For this reason, in the case of printed waste paper made of lightweight coated paper, the coating layer that has peeled off from the fibers or has become easily peeled off due to alkali immersion and the offset ink thereon are dispersed by the following mechanical stirring process. At the same time, the unpeeled ink and the peeled ink are dispersed and made finer, and the ink particles even re-adhere to the fibers. Therefore, the finer ink particles reduce the efficiency of flotation in the post-treatment, and even cause the ink particles to re-adhere to the fiber surface, resulting in an increase in the dullness of the color of the fibers. In addition, even if hydrogen peroxide is added at a high rate as a bleaching agent to obtain high whiteness from waste paper raw materials, including offset printed waste paper, it is not limited to medium-weight and lightweight coated paper. There is ineffective consumption of hydrogen.
(2) Hydrogen peroxide decomposes when using a kneader, etc. (3) There is a limit to the improvement of whiteness by alkali immersion, and there are problems such as poor efficiency of hydrogen peroxide. The present invention was made in order to solve the above-mentioned problems, and the present inventors came up with the idea of performing alkali immersion in two stages. In contrast to the deinking method, the peeled off coating layer and coarse ink particles are removed by flotation before mechanical stirring, and the peeled ink, which was a problem in the past, is made finer by mechanical stirring. After obtaining the knowledge that it is possible to prevent re-adhesion to fibers, the present invention was completed as a result of intensive research. Furthermore, we have also discovered that the deinking method of the present invention is also effective in deinking medium-weight, newspaper offset printed waste paper other than the above-mentioned medium-weight lightweight coated paper, which has recently become an issue as printed paper that is difficult to deink. Obtained. The main purpose of the present invention is to solve the above problems and
Suitable for removing ink from printed waste paper, especially medium-weight, lightweight coated paper, with almost no unpeeled ink.
Another object of the present invention is to provide a method for deinking printed waste paper that yields deinked pulp (DIP) with high brightness. Another object of the present invention is to remove almost no unreleased ink from general recycled printed waste paper, including medium-quality coated, uncoated printed waste paper, high-quality coated printed waste paper, and newspaper waste paper, in addition to the printed waste paper containing the medium-weight lightweight coated paper; Another object of the present invention is to provide a method for deinking printed waste paper that yields deinked pulp with high brightness. [Means for Solving the Problems] The present invention includes a step of adding a deinking agent consisting of an alkaline agent and a surfactant to recovered printed waste paper and performing a preliminary alkaline immersion at a raw material concentration of 10% or more;
Next, a step of diluting the raw material and performing flotation, a further step of dehydrating the raw material, adding a deinking agent consisting of an alkaline agent and a surfactant again, and performing a subsequent alkaline immersion at a raw material concentration of 10% or more; A series of steps of performing mechanical stirring at a raw material concentration of 10% or more before or after the latter alkali immersion, or both before and after the latter alkali immersion, and further washing in the final step of each of the above steps. This is a method for removing ink from printed waste paper, which is characterized by the addition of a step of performing this process. Further, the present invention is a method for deinking printed waste paper as described above, in which a bleaching agent is added in the alkali dipping step and bleaching is carried out simultaneously with the alkali dipping. The deinking method of the present invention is based on the recent deinking method whose basic steps are low-concentration disintegration, high-concentration alkali immersion, high-concentration mechanical stirring, and flotation or washing. It is characterized in that flotation is performed after immersion in alkali, and mechanical stirring treatment is performed before or after the subsequent immersion in alkali. As before,
If mechanical stirring is performed at a high concentration using a kneader or the like after alkali immersion, the ink particles that have been peeled off from the fibers due to alkali immersion will become finer than necessary, and many of them will not be able to be removed by flotation in post-treatment. There was a risk that the ink removal efficiency of the flotation system would be deteriorated and that the ink could not be removed sufficiently. In particular, printed waste paper, such as medium-weight lightweight coated paper that has been coated with paint using a gate roll coater, etc.
Since the amount of paint applied is small and the printed ink reaches the paper layer through the coat layer, when mechanical stirring is performed to peel off the unreleased ink, the ink on the coat layer becomes fine particles together with the coat layer. Because
It was even more difficult to remove the ink particles. According to the method of the present invention, the ink particles peeled off from the fibers in the preceding alkali immersion can be removed by flotation in a relatively large state, thereby increasing the efficiency of flotation. In the flotation method, the ink particle size is generally 10~
It is said that ink removal efficiency is good with relatively large particles of about 100 μm, and fine particles of 25 μm or less are effective in cleaning methods. By performing floatation without making the particles finer, the ink removal efficiency of floatation can be maximized. In addition, in the subsequent alkali immersion, unpeeled ink and ink that was not removed by flotation are mechanically agitated using a kneader or the like before or after the alkali immersion, and cleaning efficiency is improved in the post-treatment cleaning step. The ink particles are made as fine as possible for cleaning so that the ink particles become the highest. Furthermore, if the alkali immersion is performed in two stages, bleaching with hydrogen peroxide or the like can be performed in two stages at the same time, so that the efficiency of the bleaching agent is improved. Moreover, when bleaching is carried out in one stage, it is preferable to carry out the bleaching at the same time as the subsequent alkali immersion. In this way, it is possible to efficiently obtain DIP with high whiteness and almost no unreleased ink from used printed paper. The step of adding a deinking agent consisting of an alkaline chemical and a surfactant to the printed waste paper of the present invention and immersing it in alkali at a raw material concentration of 10% or more is usually the first step in waste paper deinking. This is done after disaggregation. As the alkaline agent, a known alkali such as caustic soda or sodium silicate is used, and as the surfactant, a known one conventionally used for deinking is used. Alkali immersion is a process also called aging, and is necessary to fully react the ink that has not been peeled off from the fibers with alkali.The immersion time varies depending on the raw material concentration, amount of alkali added, temperature, etc. In the present invention, for 0.5 hours or more, preferably 1 hour
It takes more than an hour. The amount of alkali added is required as an alkali concentration of 3 g/(as NaOH), preferably 5 g/(as NaOH). The raw material concentration needs to be 10% or more, preferably 15% or more, and in alkali immersion, the alkali concentration can be increased by increasing the concentration, but it is also possible to reduce the amount of alkali added by reducing the alkali concentration. It is. In the alkaline dipping process, in addition to the deinking agent, a bleaching agent such as hydrogen peroxide is also added at the same time to bleach the waste paper raw material. The above-mentioned conditions for alkali immersion and bleaching are the same for the subsequent alkali immersion and bleaching, but depending on the properties of the printed waste paper, the conditions for the latter stage of the first stage may be changed within the range of preferred conditions. , is actually valid. Next, the waste paper raw material is diluted and a floatator is used to remove the peeled ink particles in the raw material as well as the relatively coarse particles of the coated layer consisting of pigments and synthetic resins peeled from the coated waste paper at a known low concentration. Separate and remove. The low-concentration waste paper raw material from which relatively coarse ink particles have been removed is dehydrated, a deinking agent consisting of an alkaline agent and a surfactant is added again, and the paper is subjected to an alkali immersion process at a raw material concentration of 10% or more. In this latter step of alkaline immersion, the unreleased ink on the fibers that could not be removed by the previous step of alkali immersion and flotation is reacted again with the deinking agent and peeled off from the fibers, and the ink is removed by 10% before or after the alkali immersion, or before and after the alkali immersion. By passing through the process of performing mechanical agitation treatment using a kneader or the like at the above raw material concentration, ink particles etc. are made into fine particles so that they can be efficiently washed and removed in the post-treatment washing process. As is known, mechanical agitation treatment using a kneader, etc. is performed by heating the material to a temperature of 50°C or higher, applying compressive force at a high raw material concentration of 10% or more, and using a kneader or mixer in the presence of a deinking agent such as an alkali. , a disperser or the like can be used to destroy the film of unreleased ink such as offset ink that is firmly attached to the fibers, and the ink can be peeled off from the fibers. In the method of the present invention, after this mechanical stirring treatment is preceded by alkaline immersion and flotation treatment to remove relatively coarse ink particles, an alkali immersion is further performed to peel off the unpeeled ink from the fibers or remove the peeled ink. Since mechanical agitation treatment is performed after taking measures to prevent re-adhesion of ink to the fibers, fine ink particles can be effectively removed compared to the effect of mechanical agitation treatment in the conventional deinking method described above. It is excellent in that it can remove Examples of the present invention will be shown below. [Example] Example 1 200 g of printed waste paper made of medium-weight lightly coated paper was pretreated with deinking agents (caustic soda 0.8%, sodium silicate 4.0%,
After adding surfactant (0.25%), disintegrating and dehydrating,
Caustic soda 2 as a deinking agent for waste paper (air-dried)
%, sodium silicate 6% (alkali concentration NaOH: 5.4 g/), surfactant 0.15%, and hydrogen peroxide 1.2% as a bleaching agent, and after mixing well,
Soaking was carried out at 60°C for 2 hours at a raw material concentration of 15%. Next, after diluting the raw material concentration to 4% and disintegrating it for 5 minutes,
The raw material was diluted to a concentration of 1% and subjected to flotation treatment using a test floatator (manufactured by Kyokuto Shinko). Dehydrate the raw material again to a concentration of 20%, and use 2% caustic soda and 9% sodium silicate as deinking agents for the waste paper (air-dried).
% (alkaline concentration NaOH: 6.1 g/), surfactant 0.12%, bleach/hydrogen peroxide 2.4%, and after thorough mixing, immersion was performed at 70° C. for 3 hours at a raw material concentration of 15%. After soaking, the waste paper raw material was heated to 70°C and mechanically stirred for 1 minute in a test kneader (manufactured by Yamamoto Hyakuma Seisakusho), diluted to a raw material concentration of 2%, and disintegrated for 2 minutes. DIP was obtained by diluting the raw material to a concentration of 1%, dehydrating it to a raw material concentration of 10%, and washing twice. With the resulting DIP
A handmade sheet with a weight of 100 g/m 2 was prepared using the TAPPI standard method, and the amount of unpeeled ink and whiteness of DIP were measured using the following test method. Test method: Amount of unpeeled ink: A handmade sheet was analyzed using an image analysis device (Co., Ltd.)
CCD particle size distribution analyzer)
The area of the lattice portions with a light reflectance of 60% or less observed in an area of 100 mm x 100 mm was totaled and determined as the residual ink area in the handsheet. Whiteness: Measured using a photovolt whiteness tester according to the procedure of JIS P8123 Comparative Example 1 In Example 1, the alkali immersion step was only one stage, and the amount of deinking agent and bleach added was the same as in the first and second stages of Example 1. The sum of That is, 4% caustic soda, 15% sodium silicate (alkali concentration
11.5g/) as NaOH, 0.27% surfactant,
After adding 3.6% hydrogen peroxide and mixing well, immersion was performed at 70° C. for 5 hours at a raw material concentration of 15%. Hereinafter, in the same manner as in Example 1, mechanical stirring was performed using a kneader, and then the raw material concentration was diluted to 2%.
After being disintegrated for a minute, the raw material was diluted to a concentration of 1% and subjected to flotation treatment. After that, the raw material concentration was dehydrated to 10% and diluted to 1% in the same manner as in Example 1.
Washing was repeated twice to obtain DIP. Example 2 In Example 1, general recycled newspaper waste paper consisting of 20% flyers, 30% offset, and 50% convex plates was used as the waste paper, except that mechanical agitation treatment using a kneader was performed before the subsequent alkali immersion process. Example 1
DIP was obtained in exactly the same way. Examples 3 and 4 In Example 2, mechanical stirring treatment using a kneader was performed after the latter alkali immersion step (Example 3)
Alternatively, DIP was obtained in exactly the same manner as in Example 1, except that it was performed twice before and after (Example 4). The conditions for the mechanical stirring treatment were the same before and after the alkali immersion step. Comparative Example 2 Comparative Example 1 was carried out in exactly the same manner as in Comparative Example 1, except that generally recycled newspaper waste paper consisting of 20% leaflet, 30% offset, and 50% convex board was used as waste paper, and no mechanical agitation treatment using a kneader was performed. Got a DIP. Comparative Example 3 DIP was obtained in exactly the same manner as in Comparative Example 2, except that the mechanical stirring treatment using a kneader was changed to be performed after the alkali immersion. Comparative Example 4 DIP was obtained in exactly the same manner as in Comparative Example 2, except that the mechanical stirring treatment using a kneader was performed twice before and after the alkali immersion. Comparative Example 5 In Comparative Example 3, the addition rate of hydrogen peroxide bleach was
DIP was obtained in exactly the same manner as in Comparative Example 3, except that the amount was increased from 3.6% to 6%. Example 5 Completely the same as Example 1, except that offset printed waste newspaper was used instead of printed waste paper with medium weight slightly coated paper, and the first step of the alkali immersion treatment was carried out at 45°C for 16 hours. And got a DIP. Comparative Example 6 Comparative Example 1 was treated in exactly the same manner as in Comparative Example 1, except that offset-printed newspaper waste paper was used instead of printed waste paper with medium-weight slightly coated paper, and the alkali immersion treatment was performed at 60°C for 16 hours. and got DIP. Comparative Example 7 Comparative Example 1 was carried out in exactly the same manner as in Comparative Example 1, except that offset printed old newspaper was used instead of printed waste paper with medium weight slightly coated paper, and an alkali immersion treatment was performed at 70°C for 16 hours. Got a DIP. The DIP test results obtained in the Examples and Comparative Examples described above are shown in the table. According to the results shown in the table, in the deinking of used paper printed on medium-weight lightweight coated paper according to the present invention, alkaline immersion is performed in two stages, front and rear, and bleaching is performed at the same time. Example 1, in which a mechanical agitation treatment is performed after the drying process, has a single step of conventional alkali immersion and bleaching, and then a mechanical stirring treatment, followed by flotation, compared to Comparative Example 1. The area of release ink is reduced to almost nothing, and the whiteness can be significantly increased. In addition, for general recycled newspaper waste paper, Examples 2 to 4 of the present invention are the same as those for medium-weight lightweight coated paper printed waste paper, using the conventional deinking method (Comparative Examples 2 to 4) that includes one stage of alkali immersion and mechanical stirring. High whiteness can be obtained compared to Furthermore, in Comparative Example 5, the amount of hydrogen peroxide bleaching agent was significantly increased, but the high whiteness as in the example could not be obtained. In addition, Example 5 of the present invention, in which offset newspaper waste was subjected to two stages of alkali immersion and bleaching, had a much higher whiteness than Comparative Example 6, which performed one stage of alkali immersion, even when the amount of bleach used was the same for both. can be improved. It should be noted that raising the temperature of alkali immersion as in Comparative Example 7 is not preferable because it causes alkali burn and reduces whiteness. From these results, the deinking method of the present invention does not make the ink particles finer than in the past, reduce the flotation efficiency, and dull the color of the pulp due to the fine ink particles, so it is possible to DIP with high whiteness can be obtained for all types of lightweight coated paper, general recycled newspaper, and offset newspaper.
【表】
[発明の効果]
本発明は従来の印刷古紙の脱インキ法では、高
グレードの中級紙に効率配合できるまで脱インキ
できなかつた印刷古紙、特に中質軽量コート紙を
含む印刷古紙の脱インキを可能にしたものであ
る。本発明により得られるDIPは未剥離インキが
殆んどなく、本発明の方法の前後2段のアルカリ
浸漬工程で漂白を同時に行うことにより過酸化水
素などの漂白剤の使用効率がよく、従来の脱イン
キ法より高白色度のDIPが得られ、高グレードの
中級紙に高率の配合が可能である。
また、本発明は従来の脱インキ法とは異なり、
アルカリ浸漬工程を前後2段とし、前段のインキ
量が多い所では、インキ粒子を大きいままで、フ
ローテーシヨンにより除去し、インキ量が少なく
なつた後段のアルカリ浸漬処理前後では、ニーダ
ー等を用いた機械的撹拌処理によりインキ粒子を
細かくして、後の洗浄工程で除去するという特徴
ある脱インキ法であるので、前記中質軽量コート
紙を含む印刷古紙のほか近年脱インキのしにくさ
で問題になつているオフセツト印刷新聞古紙をは
じめ、中質コート、ノーコート印刷古紙、上質コ
ート印刷古紙を含む一般回収新聞古紙の脱インキ
に有効である。更に近年の新聞、雑誌、広告など
一般印刷物のカラー化及び用紙の軽量化傾向に伴
う古紙繊維に対するインキ量の相対的な増加など
の難脱インキ化によるフローテーシヨンの効率低
下の問題解決にも対応でき、効果を発揮すること
ができるすぐれた脱インキ法である。[Table] [Effects of the Invention] The present invention is a method for removing ink from used printed paper, which cannot be effectively deinked to the extent that it can be efficiently blended into high-grade, intermediate-grade paper using conventional deinking methods for used printed paper. This makes it possible to remove ink. The DIP obtained by the present invention has almost no unreleased ink, and by simultaneously performing bleaching in the two alkali immersion steps before and after the method of the present invention, the use of bleaching agents such as hydrogen peroxide is more efficient than in the conventional method. DIP with high whiteness can be obtained using the deinking method, and it can be incorporated at a high rate into high-grade intermediate paper. Furthermore, unlike conventional deinking methods, the present invention
The alkali immersion process is carried out in two stages, one before and one after the other, and in the first stage where the amount of ink is large, the ink particles are removed by flotation while remaining large, and in the second stage where the amount of ink is small before and after the alkali immersion process, a kneader etc. is used. This is a unique deinking method in which the ink particles are broken down by a mechanical agitation process and then removed in a subsequent washing process. It is effective for removing ink from commonly collected used newspapers, including the problematic offset-printed used newspapers, as well as medium-quality coated, uncoated, and high-quality coated used newspapers. Furthermore, in recent years, general printed matter such as newspapers, magazines, advertisements, etc. have become colored, and paper has become lighter.As a result, the amount of ink relative to waste paper fibers has increased, making it difficult to remove ink, which can reduce the efficiency of flotation. This is an excellent deinking method that can be used and is effective.
Claims (1)
る脱墨剤を添加し、10%以上の原料濃度で前段の
アルカリ浸漬を行う工程、次いで原料を希釈して
フローテーシヨンを行う工程、更に原料を脱水し
て再びアルカリ薬剤、界面活性剤よりなる脱墨剤
を添加し、10%以上の原料濃度で後段のアルカリ
浸漬を行う工程並びに前記後段のアルカリ浸漬の
前に10%以上の原料濃度で機械的撹拌を行う工程
を含み、かつ後段のアルカリ浸漬工程に続いて洗
浄を行う工程を連ねたことを特徴とする印刷古紙
の脱インキ法。 2 印刷古紙にアルカリ薬剤、界面活性剤よりな
る脱墨剤を添加し、10%以上の原料濃度で前段の
アルカリ浸漬を行う工程、次いで原料を希釈して
フローテーシヨンを行う工程、更に原料を脱水し
て再びアルカリ薬剤、界面活性剤よりなる脱墨剤
を添加し、10%以上の原料濃度で後段のアルカリ
浸漬を行う工程並びに前記後段のアルカリ浸漬の
後で10%以上の原料濃度で機械的撹拌を行う工程
を経由した後に洗浄を行う工程を含むようにして
成る印刷古紙の脱インキ法。 3 印刷古紙にアルカリ薬剤、界面活性剤よりな
る脱墨剤を添加し、10%以上の原料濃度で前段の
アルカリ浸漬を行う工程、次いで原料を希釈して
フローテーシヨンを行う工程、更に原料を脱水し
て再びアルカリ薬剤、界面活性剤よりなる脱墨剤
を添加し、10%以上の原料濃度で後段のアルカリ
浸漬を行う工程並びに前記後段のアルカリ浸漬の
前および後で、10%以上の原料濃度で機械的撹拌
を行う工程を連ね、更に前記後段の機械的撹拌を
行う工程を経た後に、洗浄を行う工程を含むよう
にして成る印刷古紙の脱インキ法。 4 アルカリ浸漬工程で漂白剤を添加し、アルカ
リ浸漬と同時に漂白を行う請求項1〜3何れかに
記載の印刷古紙の脱インキ法。[Scope of Claims] 1. A step of adding a deinking agent consisting of an alkaline chemical and a surfactant to printed waste paper and performing alkali immersion in the first stage at a raw material concentration of 10% or more, then diluting the raw material and performing floatation. Further, the step of dehydrating the raw material, adding a deinking agent consisting of an alkali agent and a surfactant again, and carrying out a subsequent alkali immersion at a raw material concentration of 10% or more, and a step of 10% or more before the latter alkali immersion. A method for deinking printed waste paper, characterized by including a step of performing mechanical stirring at the above raw material concentration, and further comprising a subsequent step of washing with an alkaline immersion step. 2 A step in which a deinking agent consisting of an alkali agent and a surfactant is added to the printed waste paper, and the first stage is immersed in alkali at a raw material concentration of 10% or more, then a step in which the raw material is diluted and floatation is performed, and the raw material is further diluted. After dehydration, a deinking agent consisting of an alkali agent and a surfactant is added again, and a subsequent alkaline immersion is performed at a raw material concentration of 10% or more, and a machine is applied at a raw material concentration of 10% or more after the latter alkaline immersion. A method for deinking printed waste paper, which includes a step of washing after passing through a step of agitating the paper. 3 A step in which a deinking agent consisting of an alkali agent and a surfactant is added to the printed waste paper, and the first stage is immersed in an alkali at a raw material concentration of 10% or more, followed by a step in which the raw material is diluted and floatation is carried out, and then the raw material is further diluted. The process of dehydrating and adding a deinking agent consisting of an alkali agent and a surfactant again, and performing a subsequent alkali immersion at a raw material concentration of 10% or more, and before and after the latter alkali immersion, the raw material has a concentration of 10% or more. A method for deinking printed waste paper, comprising a series of steps of performing mechanical stirring at a concentration, and a step of washing after passing through the latter step of mechanical stirring. 4. The method for deinking printed waste paper according to any one of claims 1 to 3, wherein a bleaching agent is added in the alkali immersion step and bleaching is carried out simultaneously with the alkali immersion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1041903A JPH02221480A (en) | 1989-02-23 | 1989-02-23 | Method for deinking printed waste paper |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1041903A JPH02221480A (en) | 1989-02-23 | 1989-02-23 | Method for deinking printed waste paper |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02221480A JPH02221480A (en) | 1990-09-04 |
| JPH0423037B2 true JPH0423037B2 (en) | 1992-04-21 |
Family
ID=12621243
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1041903A Granted JPH02221480A (en) | 1989-02-23 | 1989-02-23 | Method for deinking printed waste paper |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02221480A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08127989A (en) * | 1994-10-28 | 1996-05-21 | Honshu Paper Co Ltd | Method for deinking old printed paper |
| JP5310995B2 (en) * | 2008-04-11 | 2013-10-09 | 凸版印刷株式会社 | Recycled printed paper |
| WO2025105478A1 (en) * | 2023-11-16 | 2025-05-22 | Dic株式会社 | Composition for deinking agent, deinking agent, and method for producing deinked printed fabric |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2534819C2 (en) * | 1975-08-05 | 1983-12-15 | L. Schuler GmbH, 7320 Göppingen | Device for destacking and transporting blanks |
| JPH0683714B2 (en) * | 1985-09-09 | 1994-10-26 | 松下電工株式会社 | electric toothbrush |
| JPS6328992A (en) * | 1986-07-23 | 1988-02-06 | 新王子製紙株式会社 | How to deink printed waste paper |
-
1989
- 1989-02-23 JP JP1041903A patent/JPH02221480A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02221480A (en) | 1990-09-04 |
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| LAPS | Cancellation because of no payment of annual fees |