JPH0689517B2 - Deinking agent - Google Patents
Deinking agentInfo
- Publication number
- JPH0689517B2 JPH0689517B2 JP40928390A JP40928390A JPH0689517B2 JP H0689517 B2 JPH0689517 B2 JP H0689517B2 JP 40928390 A JP40928390 A JP 40928390A JP 40928390 A JP40928390 A JP 40928390A JP H0689517 B2 JPH0689517 B2 JP H0689517B2
- Authority
- JP
- Japan
- Prior art keywords
- fatty acid
- deinking agent
- deinking
- acid
- salt
- 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 - Lifetime
Links
Classifications
-
- 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
- Y02W30/64—Paper recycling
Landscapes
- Paper (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は新聞、雑誌、OA古紙等
の古紙再生時に用いられる脱墨剤に関する。更に詳しく
は新聞、雑誌、OA古紙等をフロテーション法、洗浄法
及びそれらの折衷法で脱墨処理を行うに際し高b値のそ
して未剥離インキの少ない脱墨パルプを得る事の出来る
脱墨剤に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deinking agent used for recycling used paper such as newspapers, magazines and OA used paper. More specifically, a deinking agent capable of obtaining a deinked pulp having a high b value and less unpeeled ink when deinking a newspaper, a magazine, OA waste paper, etc., by a flotation method, a washing method and an eclectic method thereof. Regarding
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】新聞、
雑誌、OA古紙等の再生利用は古くから行われている
が、特に最近は森林資源保護、ごみ処理等の地球環境問
題とも連動し、古紙の有効利用は重要性を増してきてい
る。更に脱墨パルプの用途も新聞古紙から中質紙用への
例にも見られるように、ワンランク上のパルプへの高度
利用がなされて来ている。一方、最近の古紙は印刷技
術、印刷方式、印刷インキ成分等の変化により、脱墨と
いう観点からは、一層険しい状況になりつつある。この
ため、より以上に脱墨を促進するため、装置へも改良が
加えられて来ている。古紙からインキその他の不純物を
分離除去するため、従来から用いられてきた薬剤として
は、苛性ソーダ、硅酸ソーダ、炭酸ソーダ、リン酸ソー
ダ等のアルカリ剤、過酸化水素、次亜硫酸塩、次亜塩素
酸塩等の漂白剤、EDTA、DTPA等の金属イオン封
鎖剤と共に、脱墨剤として、アルキルベンゼンスルホン
酸塩、高級アルコール硫酸エステル塩、α−オレフィン
スルホン酸塩、ジアルキルスルホサクシネート等の陰イ
オン活性剤、高級アルコール、アルキルフェノール及び
脂肪酸のエチレンオキサイド付加物、アルカノールアマ
イド類等の非イオン活性剤が単独または2種以上配合さ
れて使用されて来た。しかし、これらの脱墨剤ではフロ
テーション処理における起泡性は大きいもののインキ捕
集能が小さく、また、洗浄法ではその洗浄力が弱いう
え、高起泡性のため排水処理での泡トラブルを引き起こ
し、結果として低グレードの脱墨パルプしか得られなか
った。更には、高白色度であってもくすみがあるため、
脱墨パルプの用途制限(板紙の表下への使用量減少、新
聞紙への配合量減少等)や、くすみを無くするため、漂
白剤使用量を増加せざるを得ない状況であった。くすみ
がなく、明るい色調の脱墨パルプを得るためにはハンタ
ー色差式のLab表示系のb値を高めればよい。b値が
高い脱墨パルプは4μm 以下の微細インキの除去率が高
い事を示す。b値が高いとパルプの色調が明るくなるの
で、過酸化水素等の漂白剤使用量低減、脱墨パルプの高
配合、ワングレード上の用途への利用が可能となる。2. Description of the Related Art Newspapers,
Recycling of magazines, OA waste paper, etc. has been done for a long time, but in recent years, especially in connection with global environmental problems such as forest resource protection and waste disposal, the effective use of waste paper is becoming more important. Further, the use of deinked pulp has been advanced to higher-grade pulp, as can be seen from the example of used newspaper to medium-quality paper. On the other hand, the recent waste paper is becoming more severe from the viewpoint of deinking due to changes in printing technology, printing method, printing ink components, and the like. For this reason, in order to further promote deinking, improvements have been made to the apparatus. Chemicals that have been conventionally used to separate and remove ink and other impurities from waste paper include alkaline agents such as caustic soda, sodium silicate, sodium carbonate, sodium phosphate, hydrogen peroxide, hyposulfite, and hypochlorite. Anion activity such as alkylbenzene sulfonate, higher alcohol sulfate ester salt, α-olefin sulfonate, dialkyl sulfosuccinate as deinking agent together with bleaching agent such as acid salt and sequestering agent such as EDTA and DTPA Nonionic activators such as agents, higher alcohols, ethylene oxide adducts of alkylphenols and fatty acids, and alkanolamides have been used alone or in combination of two or more. However, these deinking agents have a large foaming property in the flotation process, but have a low ink-collecting ability, and the cleaning method has a weak cleaning power, and the high foaming property causes foaming troubles in wastewater treatment. And resulted in only low grade deinked pulp. Furthermore, since it has dullness even with high whiteness,
There was no choice but to increase the amount of bleach used in order to eliminate the use restrictions of deinked pulp (reduction in the amount of paper below the surface of the board, reduction in the amount added to newsprint, etc.) and dullness. In order to obtain a deinked pulp having a dull and bright tone, the b value of the Hunter color difference type Lab display system may be increased. Deinked pulp with a high b value shows a high removal rate of fine ink of 4 μm or less. When the b value is high, the color tone of the pulp becomes lighter, so that it is possible to reduce the amount of bleaching agent such as hydrogen peroxide used, to add a high amount of deinking pulp, and to use it for one grade application.
【0003】b値を高めるための方法としては2つあ
り、前述した様な4μm 以下の微細インキを効率よく除
去してやるか、アルカリ類を多量使用する方法がある。
ところが、後者はスティッキー(粘着物)の増加、排水
負荷の増大かつパルプの脆化が生じるという欠点を有し
ている。前者の4μm 以下の微細インキを捕集除去する
技術に関しては、いくつか例示されているが効果のある
ものはなかった。There are two methods for increasing the b value, and there is a method of efficiently removing the fine ink of 4 μm or less as described above or using a large amount of alkalis.
However, the latter has the drawbacks of increased stickiness (sticky substances), increased drainage load and embrittlement of pulp. Some examples of the former technique for collecting and removing fine ink of 4 μm or less have been shown, but none have been effective.
【0004】インキ捕集能の大きい脱墨剤として、高級
脂肪酸が古くから知られている。例えば、日本特許登録
第80988号、日本特許登録第82089号、及び日
本特許登録第83901号には、単独で用いる事によっ
てインキ捕集能の優れた脱墨剤としての利用が開示され
ている。また、特開昭51−13762号公報、特開昭
53−130309号公報、及び特開昭54−6840
3号公報には他の界面活性剤との併用によって更に優れ
た効果を示す事が開示されている。Higher fatty acids have long been known as a deinking agent having a large ink collecting ability. For example, Japanese Patent Registration No. 80988, Japanese Patent Registration No. 82089, and Japanese Patent Registration No. 83901 disclose use as a deinking agent having excellent ink collecting ability when used alone. Further, JP-A-51-13762, JP-A-53-130309, and JP-A-54-6840.
Japanese Patent Publication No. 3 discloses that even more excellent effects can be obtained by using it together with other surfactants.
【0005】その後、技術の発達によりエチレンオキサ
イドやプロピレンオキサイド等のアルキレンオキサイド
を付加させた化合物よりなり、脱墨パルプの白色度を著
しく改善させる等の高性能の脱墨剤の発明がなされた
(特開昭58−109696号公報、特開昭59−13
0400号公報)。Thereafter, with the development of technology, the invention of a high-performance deinking agent comprising a compound obtained by adding an alkylene oxide such as ethylene oxide or propylene oxide and remarkably improving the whiteness of deinking pulp was made ( JP-A-58-109696, JP-A-59-13
0400).
【0006】しかし、これらの技術に開示されている脱
墨剤を用いても、高b値の脱墨パルプを得る事はできな
かった。また、従来公知の高級脂肪酸またはその塩を用
いた場合、未剥離インキが多いという欠点を有してい
た。However, even if the deinking agents disclosed in these techniques were used, it was not possible to obtain deinked pulp having a high b value. Further, when a conventionally known higher fatty acid or a salt thereof is used, there is a drawback that the amount of unpeeled ink is large.
【0007】[0007]
【課題を解決するための手段】本発明者等はフロテーシ
ョン法、洗浄法及びそれらの折衷法において、優れたイ
ンキ除去能を示し、操業性が良好で、特に高b値で未剥
離インキの少ない脱墨パルプを得る事の出来る脱墨剤を
開発すべく鋭意研究を行った結果、驚くべき事に炭素数
8〜24の高級脂肪酸又はその塩の混合物であって、該混
合物中の脂肪酸又はその塩の平均炭素数が12.7〜22.5の
範囲にあり、炭素数20〜24の高級脂肪酸又はその塩の含
有率が 9.6〜70.6重量%であり、且つヨウ素価(IV)が
45以下である混合物が上記欠点を克服できる事を見出
し、本発明を完成するに至った。The inventors of the present invention have shown excellent ink removing ability in flotation method, washing method and their eclectic method and have good operability. As a result of intensive research to develop a deinking agent capable of obtaining a small amount of deinked pulp, surprisingly, it is a mixture of a higher fatty acid having 8 to 24 carbon atoms or a salt thereof, and the fatty acid or the fatty acid in the mixture is The average carbon number of the salt is in the range of 12.7 to 22.5, the content of the higher fatty acid having 20 to 24 carbon atoms or the salt thereof is 9.6 to 70.6% by weight, and the iodine value (IV) is
The inventors have found that a mixture having a ratio of 45 or less can overcome the above-mentioned drawbacks, and completed the present invention.
【0008】即ち、本発明は炭素数8〜24の高級脂肪酸
又はその塩を、平均炭素数が12.7〜22.5となる範囲で含
有し、炭素数20〜24の高級脂肪酸又はその塩の含有率が
9.6〜70.6重量%であり、且つヨウ素価(IV)が45以下
である混合物を必須成分とする脱墨剤を提供するもので
ある。That is, the present invention contains a higher fatty acid having 8 to 24 carbon atoms or a salt thereof in the range of an average carbon number of 12.7 to 22.5, and the content of the higher fatty acid having 20 to 24 carbon atoms or a salt thereof is
It is intended to provide a deinking agent containing a mixture of 9.6 to 70.6% by weight and an iodine value (IV) of 45 or less as an essential component.
【0009】本発明に係わる脂肪酸混合物に関する数値
規定は臨界的であって、これに類似する化合物であって
も、本発明の規定に該当しないものは本発明の顕著な効
果は得られない。従って、本発明の化合物の炭素数の限
定等の数値の限定は極めて重要である。後記の実施例及
び比較例により明らかにされるが、平均炭素数が12.7よ
り小さいと微細インキ凝集効果が低下するため、高b値
の脱墨パルプを得る事ができない。また、平均炭素数が
22.5を越えてもフロテーション工程での起泡性が不足
し、凝集インキが系外へリジェクトされにくい。また、
炭素数20〜24の脂肪酸の含有率が9.6 重量%より少ない
場合、微細インキ凝集効果が低下するため、高b値の脱
墨パルプを得る事ができない。一方、70.6重量%より大
きければインキ剥離性が弱くなり、未剥離インキが多量
残存し、その結果、見栄えの悪い脱墨パルプしか得られ
ない。本発明の化合物は、炭素数8〜24の脂肪酸を本発
明の範囲内で任意に配合できる。特に炭素数20の脂肪酸
又はその塩を2.0 〜33.2重量%、且つ炭素数22の脂肪酸
を9.5 〜32.0重量%含有するのが好ましい。Numerical regulations regarding the fatty acid mixture according to the present invention are critical, and even compounds similar to these are not applicable to the regulation of the present invention, the remarkable effects of the present invention cannot be obtained. Therefore, it is extremely important to limit the numerical values such as the carbon number of the compound of the present invention. As will be clarified by Examples and Comparative Examples described later, if the average carbon number is less than 12.7, the fine ink aggregation effect is lowered, and it is not possible to obtain deinked pulp having a high b value. Also, if the average carbon number is
Even if it exceeds 22.5, the foaming property in the flotation process is insufficient, and the cohesive ink is less likely to be rejected to the outside of the system. Also,
When the content of the fatty acid having 20 to 24 carbon atoms is less than 9.6% by weight, the fine ink aggregation effect is deteriorated, so that the deinked pulp having a high b value cannot be obtained. On the other hand, if it is more than 70.6% by weight, the ink releasability becomes weak, and a large amount of unpeeled ink remains, and as a result, only deinked pulp with a poor appearance is obtained. The compound of the present invention may optionally contain a fatty acid having 8 to 24 carbon atoms within the scope of the present invention. In particular, it is preferable to contain a fatty acid having 20 carbon atoms or a salt thereof in an amount of 2.0 to 33.2% by weight and a fatty acid having 22 carbon atoms in an amount of 9.5 to 32.0% by weight.
【0010】また、ヨウ素価(IV)が45より大きいと、
フロテーション工程での起泡性が不足し、泡沫層上の凝
集インキが系外へリジェクトされにくく、その結果、低
白色度の脱墨パルプしか得られない。更には、インキ剥
離性が小さいため未剥離インキが多量に残存する。If the iodine value (IV) is larger than 45,
The foaming property in the flotation step is insufficient, and the agglomerated ink on the foam layer is not easily rejected outside the system, and as a result, only deinked pulp with low whiteness can be obtained. Furthermore, since the ink releasability is low, a large amount of unpeeled ink remains.
【0011】本発明の脱墨剤は、前述した様に炭素数8
〜24の脂肪酸及びその塩を本発明の範囲内で任意に配合
できるが、具体的には、カプリル酸、ペラルゴン酸、カ
プリン酸、ウンデカン酸、ラウリン酸、トリデカン酸、
ミリスチン酸、ペンタデカン酸、パルミチン酸、マルガ
リン酸、ステアリン酸、オレイン酸、エライジン酸、リ
ノール酸、リノレイン酸、ステアロール酸、リシノール
酸、リシノエライジン酸、ノナデカン酸、アラキジン
酸、ヘンイコサン酸、ベヘン酸、ブラシジン酸、エルカ
酸、トリコサン酸、テトラコサン酸、椰子油脂肪酸、牛
脂脂肪酸、パーム油脂肪酸、トール油脂肪酸、なたね油
脂肪酸、魚油脂肪酸、或いはこれらの半硬化乃至硬化さ
れた脂肪酸、及びこれら全ての脂肪酸の塩を挙げる事が
できる。塩としては、ナトリウム塩、カリウム塩、アン
モニウム塩、マグネシウム塩、カルシウム塩等を挙げる
事ができる。これらの中でもコスト面や単独で使用でき
る容易性から半硬化乃至硬化された魚油脂肪酸又はその
塩が好ましい。本発明の魚油脂肪酸の原料である魚油
は、タラ油、イワシ油、サンマ油、サバ油、ニシン油、
メンヘーデン油等やこれらの精製工程で得られる回収油
等が挙げられる。The deinking agent of the present invention has a carbon number of 8 as described above.
~ 24 fatty acids and salts thereof can be arbitrarily blended within the scope of the present invention, specifically, caprylic acid, pelargonic acid, capric acid, undecanoic acid, lauric acid, tridecanoic acid,
Myristic acid, pentadecanoic acid, palmitic acid, margaric acid, stearic acid, oleic acid, elaidic acid, linoleic acid, linoleic acid, stearolic acid, ricinoleic acid, ricinoelaidic acid, nonadecanoic acid, arachidic acid, henicosanoic acid, behenic acid , Brassic acid, erucic acid, tricosanoic acid, tetracosanoic acid, coconut oil fatty acid, beef tallow fatty acid, palm oil fatty acid, tall oil fatty acid, rapeseed oil fatty acid, fish oil fatty acid, or these semi-hardened or hardened fatty acids, and all these fatty acids You can list the salt. Examples of the salt include sodium salt, potassium salt, ammonium salt, magnesium salt, calcium salt and the like. Among these, semi-hardened or hardened fish oil fatty acid or a salt thereof is preferable from the viewpoint of cost and ease of use alone. Fish oil which is a raw material of the fish oil fatty acid of the present invention, cod oil, sardine oil, saury oil, mackerel oil, herring oil,
Menhaden oil and the like and recovered oil obtained in these refining steps and the like can be mentioned.
【0012】従来技術で高級脂肪酸を脱墨剤として使用
することは知られていたが、特定炭素数の脂肪酸を特定
比率で含有する混合物によってのみ、かかる脱墨効果が
示される事は全く知られていなかった。つまり、従来技
術は椰子油や牛脂油由来のアニオン性界面活性剤或いは
その原料として一般に用いられている高級脂肪酸を炭素
数にこだわる事無く用いているにすぎなかった。従来技
術には高級脂肪酸を特定比率で使用する事は開示されて
いない。上記特許公報においてもその実施例で本発明で
開示する脂肪酸混合物を使用するものは皆無に等しい。
更には、これらは炭素数12〜18の脂肪酸を主成分として
おり、本発明の範囲とは明らかに異なる。Although it has been known in the prior art to use a higher fatty acid as a deinking agent, it is completely known that such a deinking effect is exhibited only by a mixture containing a fatty acid having a specific carbon number in a specific ratio. Didn't. That is, the prior art has merely used the anionic surfactant derived from coconut oil or tallow oil or the higher fatty acid generally used as a raw material thereof without being concerned with the carbon number. The prior art does not disclose the use of higher fatty acids in specific proportions. Even in the above patent publications, none of the examples use the fatty acid mixture disclosed in the present invention.
Further, these are mainly composed of fatty acids having 12 to 18 carbon atoms, which is clearly different from the scope of the present invention.
【0013】本発明に用いられる脂肪酸の一つに魚油脂
肪酸またはその塩を挙げる事ができる。従来技術の特開
昭61−89394号公報、特開昭62−250291
号公報では炭素数20以上の脂肪酸を含有する魚油脂肪酸
の併用使用の記載があるものの具体例が記載されておら
ず、かつ本発明の4μm 以下の微細インキ除去によりb
値を高めるといった効果とは別の効果をうたっている。
更には、本発明はある特定のヨウ素価(IV)を有する事
が必須であり、上記従来技術の魚油脂肪酸はヨウ素価
(IV)がおよそ175 であり、魚油脂肪酸そのものではヨ
ウ素価(IV)が高すぎて本用途には使えない。One of the fatty acids used in the present invention is fish oil fatty acid or its salt. Prior art JP-A-61-89394, JP-A-62-250291
In the publication, although the use of fish oil fatty acid containing a fatty acid having 20 or more carbon atoms is used in combination, no specific example is described, and the removal of fine ink of 4 μm or less according to the present invention results in b
The effect is different from the effect of increasing the value.
Furthermore, the present invention is essential to have a certain iodine value (IV), and the above-mentioned conventional fish oil fatty acid has an iodine value (IV) of about 175, and the fish oil fatty acid itself has an iodine value (IV). It is too expensive to use for this purpose.
【0014】本発明の脱墨剤は、単独で使用しても十分
な脱墨効果を示すため、他の界面活性剤を併用したり、
アルキレンオキサイドを付加させたりしなくても構わな
い。よって、脱墨性能のみならず脱墨剤の製造や配合な
どの工程の簡略化、それに伴い汎用性や安全性が向上す
るといった産業上極めて有益な発明を開示するものであ
る。Since the deinking agent of the present invention exhibits a sufficient deinking effect even when used alone, it may be used in combination with another surfactant.
It is not necessary to add alkylene oxide. Therefore, an industrially extremely useful invention is disclosed in which not only the deinking performance but also the steps of manufacturing and blending the deinking agent are simplified, and the versatility and safety are improved accordingly.
【0015】本発明の脱墨剤の構成成分である脂肪酸
は、ほとんどが天然油脂由来のものであり、脂肪酸の製
造法としては従来公知技術のTwitchell 分解、中圧触媒
分解、連続高圧分解法がある。また、ヨウ素価(IV)を
下げる一般的な方法としては、ニッケル触媒を用い高温
高圧下で水素添加を行う方法を挙げる事ができる。Most of the fatty acids which are the constituent components of the deinking agent of the present invention are derived from natural fats and oils, and the conventional methods for producing fatty acids include Twitchell decomposition, intermediate pressure catalytic decomposition and continuous high pressure decomposition methods. is there. Further, as a general method for lowering the iodine value (IV), a method of performing hydrogenation under high temperature and high pressure using a nickel catalyst can be mentioned.
【0016】尚、本発明の脱墨剤は公知の脱墨剤、例え
ば高級アルコール硫酸塩、アルキルベンゼンスルホン酸
塩、高級アルコール及びアルキルフェノールのエチレン
オキサイド付加物、脂肪酸及びその塩、脂肪酸アルキレ
ンオキサイド付加物、油脂アルキレンオキサイド付加
物、モノステアリルグリセライドアルキレンオキサイド
付加物、多価アルコール部分エステルまたは完全エステ
ルアルキレンオキサイド付加物等と併用した場合も炭素
数20〜24の高級脂肪酸又はその塩の含有率が9.6〜70.6
重量%の範囲内であれば、優れた脱墨性能を発現する。
本発明の脱墨剤と従来公知の脱墨剤とを併用する場合、
その併用比率は、本発明品/従来品=90/10〜10/90
(重量比率)が好ましいが、特に好ましくは20/80〜60
/40(重量比率)である。The deinking agent of the present invention is a known deinking agent, for example, higher alcohol sulfates, alkylbenzene sulfonates, ethylene oxide adducts of higher alcohols and alkylphenols, fatty acids and salts thereof, fatty acid alkylene oxide adducts, Fat alkylene oxide adduct, monostearyl glyceride alkylene oxide adduct, polyhydric alcohol partial ester or complete ester alkylene oxide adduct and the like also when used in combination with a higher fatty acid having 20 to 24 carbon atoms or its salt content 9.6 to 70.6
When it is within the range of weight%, excellent deinking performance is exhibited.
When the deinking agent of the present invention and a conventionally known deinking agent are used in combination,
The combination ratio of the present invention product / conventional product = 90/10 to 10/90
(Weight ratio) is preferable, but 20/80 to 60 is particularly preferable.
/ 40 (weight ratio).
【0017】本発明の脱墨剤はいずれの工程へ添加して
も、より高品位の脱墨パルプを得る事ができる。一般に
は、脱墨剤はミキシング工程あるいはフロテーション工
程のいずれか、あるいは両方に添加するが、特に、硬度
の高い用水を用いる場合、フロテーション工程直前に添
加する方法が好ましい。各工程に分割添加する場合は、
パルピング、ニーディング、ディスパージング、ケミカ
ルミキシング、リファイニングの各工程に添加できる
が、前工程と後工程の脱墨剤の分割比率は10/90〜90/
10(重量比率)が好ましい。特に好ましくは40/60〜60
/40(重量比率)である。脱墨剤添加量は操業性を損な
わず、かつ経済的な範囲が望ましいが、原料古紙に対し
0.03〜1.0 重量%が好ましい。Even if the deinking agent of the present invention is added to any step, a higher quality deinking pulp can be obtained. Generally, the deinking agent is added to either or both of the mixing step and the flotation step, but when water with high hardness is used, the method of adding it immediately before the flotation step is preferable. When adding in divided steps,
It can be added to each process of pulping, kneading, dispersing, chemical mixing and refining, but the division ratio of the deinking agent in the previous process and the subsequent process is 10/90 to 90 /
10 (weight ratio) is preferable. Particularly preferably 40 / 60-60
/ 40 (weight ratio). Although it is desirable that the amount of deinking agent added be economical without impairing operability,
0.03 to 1.0% by weight is preferred.
【0018】[0018]
【作用】本発明の脱墨剤の機作はまだ明確ではないが、
次のように考えられる。高級脂肪酸の炭素数が大きくな
れば、微細インキ表面への吸着配向がほぼ垂直になるた
め、脱墨剤末端官能基密度は疎となる。よって単位面積
当りの表面電荷密度の絶対値は小さくなり、DLVO理論に
従えば微細インキは凝集しやすくなると考えられる。特
に炭素数20〜24の高級脂肪酸の含有率が9.6 重量%より
小さければ微細インキは凝集しにくい。一方その含有率
が70.6重量%を越えれば、インキ表面への吸着速度が急
激に小さくなるため脱墨剤によるインキ表面電荷密度制
御が十分でなくなる。よって微細インキは凝集しにくく
なる。以上のように炭素数20〜24の高級脂肪酸の含有率
が9.6 〜70.6重量%の範囲であれば微細インキを凝集
し、その結果高b値の脱墨パルプを得ることができる。
また、未剥離インキ低減は、インキとセルロースの界面
張力を低下させることにより可能となる。炭素数20〜24
の高級脂肪酸の含有率が70.6重量%を越えると急激に臨
界ミセル濃度が大きくなるため、実際の脱墨工程中では
臨界ミセル濃度以下での作用となり、十分なインキ剥離
力を発揮しない。以上のように、優れた微細インキ凝集
能(高b値を与える)と未剥離インキ低減という両機能
を満足させるためには、炭素数20〜24の高級脂肪酸又は
その塩の含有率が9.6 〜70.6重量%という臨界的な範囲
が存在する。Function The mechanism of the deinking agent of the present invention is not clear yet,
It can be considered as follows. As the carbon number of the higher fatty acid increases, the adsorption orientation on the surface of the fine ink becomes almost vertical, so that the density of functional groups at the terminal of the deinking agent becomes sparse. Therefore, the absolute value of the surface charge density per unit area becomes small, and it is considered that the fine ink tends to aggregate according to the DLVO theory. In particular, if the content of the higher fatty acid having 20 to 24 carbon atoms is less than 9.6% by weight, the fine ink will not easily aggregate. On the other hand, if the content exceeds 70.6% by weight, the adsorption speed on the ink surface decreases rapidly, and the ink surface charge density control by the deinking agent becomes insufficient. Therefore, the fine ink is less likely to aggregate. As described above, if the content of the higher fatty acid having 20 to 24 carbon atoms is in the range of 9.6 to 70.6% by weight, the fine ink is aggregated, and as a result, a deinked pulp having a high b value can be obtained.
Further, reduction of unpeeled ink is possible by reducing the interfacial tension between the ink and cellulose. Carbon number 20-24
When the content of the higher fatty acid in 7 is more than 70.6% by weight, the critical micelle concentration rapidly increases, so that the action is below the critical micelle concentration in the actual deinking process, and the sufficient ink peeling force is not exhibited. As described above, in order to satisfy both functions of excellent fine ink aggregation ability (which gives a high b value) and reduction of unpeeled ink, the content of the higher fatty acid having 20 to 24 carbon atoms or its salt is 9.6 to There is a critical range of 70.6% by weight.
【0019】また、ヨウ素価が大きいと脱墨剤がインキ
表面にほぼ平面的に吸着し、10Å程度の薄い吸着層とな
り、インキ自身の表面電位(ζ−電位で−30〜−40mV)
の影響が現れてくるため、単位面積当りの表面電荷密度
の絶対値は低下しない。よって、微細インキは凝集しに
くくなる。When the iodine value is large, the deinking agent is adsorbed on the ink surface almost flatly, forming a thin adsorption layer of about 10 Å, and the surface potential of the ink itself (-30 to -40 mV in ζ-potential).
Therefore, the absolute value of the surface charge density per unit area does not decrease. Therefore, the fine ink is less likely to aggregate.
【0020】以上のことより、本発明で規定する範囲内
において、高b値のそして未剥離インキの少ない脱墨パ
ルプを得ることができる。From the above, it is possible to obtain a deinked pulp having a high b value and less unpeeled ink within the range specified in the present invention.
【0021】[0021]
【実施例】以下、実施例により本発明を具体的に説明す
るが、本発明はこれらに限定されるものではない。EXAMPLES The present invention will now be described in detail with reference to examples, but the present invention is not limited thereto.
【0022】実施例1 本実施例は脱墨剤のパルピング工程一括添加の例であ
る。市中回収新聞古紙を2×5cmに細断後、その一定量
を卓上離解機に入れ、その中に水及び苛性ソーダ(対原
料)0.8 %、硅酸ソーダ3号(対原料)2.2 %、30%過
酸化水素(対原料)3.5 %、表1に示す脱墨剤(対原
料)0.5 %を加え、パルプ濃度15%、45℃で12分離解し
た後、55℃にて 120分間熟成処理を行った。その後、高
速脱水機で23%まで脱水し、回転速度300rpmの2軸型ラ
ボニーダーでニーディング処理を行った。その後、水を
加えて4%まで希釈し、卓上離解機で再度30秒離解す
る。そのスラリーを水で1%に希釈した後、30℃にて10
分間フロテーション処理を施した。なお、フロテーショ
ン時にCaCl2 (対原料)0.5 %を添加した。フロテーシ
ョン後のパルプスラリーを80メッシュワイヤーで4%濃
度まで濃縮後、水を加えて1%濃度に希釈しタッピース
タンダード抄紙機にてパルプシートを作製した。なお、
用いた用水の硬度は5°dHであり、硬度はCaCl2 、MgCl
2 を使用し、Ca/Mg=8/2(モル比)になる様に調整
した。得られたパルプシートを測色色差計にてb値を測
定し、画像解析装置(×100倍)にて未剥離インキ個数
を測定した。ここでいうb値とは、ハンター色差式のLa
b 表色系でのb値をいい、三刺激値XYZとの関係は下
式である。Example 1 This example is an example of batch addition of a deinking agent in the pulping step. After collecting the recovered newspaper waste paper into 2 x 5 cm pieces, put a certain amount into a table disintegrator, and water and caustic soda (vs. raw material) 0.8%, sodium silicate No. 3 (vs. raw material) 2.2%, 30% % Hydrogen peroxide (vs. raw material) 3.5% and deinking agent (vs. raw material) 0.5% shown in Table 1 were added, pulp concentration was 15%, 12 pieces were separated at 45 ° C, and then aged at 55 ° C for 120 minutes. went. Then, it was dehydrated to 23% with a high-speed dehydrator, and subjected to a kneading treatment with a twin-screw lab kneader with a rotation speed of 300 rpm. Then, add water to dilute it to 4% and disintegrate again for 30 seconds with a table disintegrator. After diluting the slurry to 1% with water, 10
Flotation treatment was performed for a minute. Note that 0.5% of CaCl 2 (vs. raw material) was added during flotation. After the flotation, the pulp slurry was concentrated with an 80-mesh wire to a concentration of 4%, water was added to dilute it to a concentration of 1%, and a pulp sheet was prepared with a tappy standard paper machine. In addition,
The hardness of the water used was 5 ° dH and the hardness was CaCl 2 , MgCl 2 .
2 was used and adjusted so that Ca / Mg = 8/2 (molar ratio). The b value of the obtained pulp sheet was measured with a colorimetric color difference meter, and the number of unpeeled inks was measured with an image analyzer (× 100). The b value here is La in the Hunter color difference formula.
b The b value in the color system, which has the following relationship with the tristimulus values XYZ.
【0023】[0023]
【数1】 [Equation 1]
【0024】この式からもわかる様に、b値はYとZの
関数であり、正の値ならば黄味、負の値ならば青味の強
さを表す。本発明の脱墨剤の平均炭素数及び炭素数20〜
24の脂肪酸の含有率を変えた系での脱墨性を表2に示
す。なお、表1中の脱墨剤は、脂肪酸単体を所定炭素数
組成になる様に配合したものである。また、No. 19はス
テアリン酸である。As can be seen from this expression, the b value is a function of Y and Z, and a positive value represents yellowish intensity, and a negative value represents bluish intensity. Average carbon number and carbon number of the deinking agent of the present invention 20 ~
Table 2 shows the deinkability of the system in which the content ratio of 24 fatty acids was changed. The deinking agent in Table 1 is a mixture of fatty acids so as to have a predetermined carbon number composition. Further, No. 19 is stearic acid.
【0025】[0025]
【表1】 [Table 1]
【0026】[0026]
【表2】 [Table 2]
【0027】[0027]
【表3】 [Table 3]
【0028】実施例2 本実施例は脱墨剤のパルピング工程とケミカルミキシン
グ工程分割添加の例である。市中回収新聞を2×5cmに
細断後、その一定量を卓上離解機に入れ、その中に水及
び苛性ソーダ(対原料)0.2 %、表3に示す脱墨剤(対
原料)0.1 %を加え、パルプ濃度15%、45℃で12分離解
した後、55℃で 120分間熟成処理を行った。その後、高
速脱水機で23%まで脱水し、苛性ソーダ(対原料)0.6
%、硅酸ソーダ3号(対原料)2.2 %、30%過酸化水素
(対原料)3.5 %、表3に示す脱墨剤(対原料)0.2 %
を添加し、水でパルプ濃度22%に調整し卓上離解機にて
1分間混合した。その後、回転速度300rpmの2軸型ラボ
ニーダーでニーディング処理を行った。その後、水を加
えて4%まで希釈し、卓上離解機で再度30秒離解する。
そのスラリーを水で1%に希釈した後、30℃にて10分間
フロテーション処理を施した。なお、フロテーション時
にCaCl2 (対原料)0.4 %添加した。フロテーション後
のパルプスラリーを80メッシュワイヤーで4%濃度まで
濃縮後、水を加えて1%濃度に希釈しタッピースタンダ
ート抄紙機にてパルプシートを作製した。なお、用いた
用水の硬度は5°dHであり、硬度はCaCl2 、MgCl2 を使
用し、Ca/Mg=8/2(モル比)になる様に調整した。
得られたパルプシートを測色色差計にてb値を測定し、
画像解析装置(×100倍)にて未剥離インキ個数を測定
した。各種脱墨剤のヨウ素価(IV)変化時の脱墨性結果
を表4に示す。Example 2 This example is an example of the splitting addition of the deinking agent and the chemical mixing step divided addition. The newspaper collected in the market is shredded into 2 x 5 cm pieces, and a certain amount is put into a table disintegrator, and water and caustic soda (vs. raw material) 0.2% and deinking agent (vs. raw material) 0.1% shown in Table 3 are put in it. In addition, the pulp concentration was 15% and 12 pieces were separated at 45 ° C, and then aged at 55 ° C for 120 minutes. Then, dehydrate to 23% with a high-speed dehydrator, and use 0.6% caustic soda (against raw materials).
%, Sodium silicate No. 3 (for raw material) 2.2%, 30% hydrogen peroxide (for raw material) 3.5%, deinking agent (for raw material) shown in Table 3 0.2%
Was added, the pulp concentration was adjusted to 22% with water, and the mixture was mixed with a table disintegrator for 1 minute. Then, a kneading process was performed with a twin-screw lab kneader with a rotation speed of 300 rpm. Then, add water to dilute it to 4% and disintegrate again for 30 seconds with a table disintegrator.
The slurry was diluted to 1% with water and then subjected to flotation treatment at 30 ° C for 10 minutes. Incidentally, 0.4% of CaCl 2 (vs. raw material) was added during flotation. After the flotation, the pulp slurry was concentrated to a 4% concentration with an 80-mesh wire, water was added to dilute the concentration to 1%, and a pulp sheet was produced using a tappies tandart paper machine. The hardness of the water used was 5 ° dH, and the hardness was adjusted to Ca / Mg = 8/2 (molar ratio) by using CaCl 2 and MgCl 2 .
The b value of the obtained pulp sheet is measured with a colorimetric color difference meter,
The number of unpeeled inks was measured with an image analyzer (× 100 times). Table 4 shows the results of deinking property when the iodine value (IV) of various deinking agents changed.
【0029】なお、表3中の脱墨剤は、脂肪酸単体を所
定炭素数組成になる様に配合したものである。The deinking agents shown in Table 3 are prepared by mixing fatty acids so as to have a predetermined carbon number composition.
【0030】[0030]
【表4】 [Table 4]
【0031】[0031]
【表5】 [Table 5]
【0032】実施例3 本実施例は脱墨剤のパルピング工程とニーディング工程
分割添加の例である。市中回収新聞を2×5cmに細断
後、その一定量を卓上離解機に入れ、その中に水及び苛
性ソーダ(対原料)0.2 %、表5に示す脱墨剤(対原
料)0.3 %を加え、パルプ濃度15%、45℃で12分離解し
た後、55℃で 120分間熟成処理を行った。その後、高速
脱水機で23%まで脱水し、苛性ソーダ(対原料)0.6
%、硅酸ソーダ3号(対原料)2.2 %、30%過酸化水素
(対原料)3.5 %、表5に示す脱墨剤(対原料)0.2 %
を添加し、水でパルプ濃度22%に調整し卓上離解機にて
1分間混合した。その後、回転速度300rpmの2軸型ラボ
ニーダーでニーディング処理を行った。その後、水を加
えて4%まで希釈し、卓上離解機で再度30秒離解する。
そのスラリーを水で1%に希釈した後、30℃にて10分間
フロテーション処理を施した。なお、フロテーション時
にCaCl2 (対原料)0.5 %を添加した。フロテーション
後のパルプスラリーを80メッシュワイヤーで4%濃度ま
で濃縮後、水を加えて1%濃度に希釈しタッピースタン
ダート抄紙機にてパルプシートを作製した。なお、用い
た用水の硬度は10°dHであり、硬度はCaCl2 、MgCl2 を
使用し、Ca/Mg=8/2(モル比)になる様に調整し
た。得られたパルプシートを測色色差計にてb値を測定
し、画像解析装置(×100倍)にて未剥離インキ個数を
測定した。各種脱墨剤の脱墨性能結果を表6に示す。な
お、表5中の脱墨剤は、No.37 〜40までそれぞれタラ、
イワシ、サンマ、サバ油脂肪酸の硬化品であり、No. 41
はNo. 37と38の50/50(重量比率)配合品である。ま
た、No. 42〜44はNo.37 のヨウ素価(IV)を変化させた
脱墨剤である。更に、No. 45〜49はそれぞれステアリン
酸、ミリスチン酸、市販ステアリン酸(花王株式会社
製、商品名ルナックS−40)及び牛脂脂肪酸の硬化品及
びイワシ油脂肪酸(ヨウ素価(IV)=175 )である。Example 3 This example is an example of adding a deinking agent in a pulping step and a kneading step. The newspaper collected in the market is shredded into 2 x 5 cm pieces, and a certain amount is put into a table disintegrator, and 0.2% of water and caustic soda (vs. raw material) and 0.3% of the deinking agent (vs. raw material) shown in Table 5 are put in it. In addition, the pulp concentration was 15% and 12 pieces were separated at 45 ° C, and then aged at 55 ° C for 120 minutes. Then, dehydrate to 23% with a high-speed dehydrator, and use 0.6% caustic soda (against raw materials).
%, Sodium silicate No. 3 (for raw material) 2.2%, 30% hydrogen peroxide (for raw material) 3.5%, deinking agent (for raw material) shown in Table 5 0.2%
Was added, the pulp concentration was adjusted to 22% with water, and the mixture was mixed with a table disintegrator for 1 minute. Then, a kneading process was performed with a twin-screw lab kneader with a rotation speed of 300 rpm. Then, add water to dilute it to 4% and disintegrate again for 30 seconds with a table disintegrator.
The slurry was diluted to 1% with water and then subjected to flotation treatment at 30 ° C for 10 minutes. Note that 0.5% of CaCl 2 (vs. raw material) was added during flotation. After the flotation, the pulp slurry was concentrated to a 4% concentration with an 80-mesh wire, water was added to dilute the concentration to 1%, and a pulp sheet was produced using a tappies tandart paper machine. The hardness of the water used was 10 ° dH, and the hardness was adjusted to Ca / Mg = 8/2 (molar ratio) by using CaCl 2 and MgCl 2 . The b value of the obtained pulp sheet was measured with a colorimetric color difference meter, and the number of unpeeled inks was measured with an image analyzer (× 100). Table 6 shows the results of deinking performance of various deinking agents. The deinking agents in Table 5 are cod up to No.37-40,
Hardened product of sardines, saury, mackerel oil fatty acid, No. 41
Is a 50/50 (weight ratio) mixture of Nos. 37 and 38. Nos. 42 to 44 are No. 37 deinking agents having a changed iodine value (IV). Further, Nos. 45 to 49 are stearic acid, myristic acid, commercially available stearic acid (Kao Corporation, trade name Lunac S-40) and hardened tallow fatty acid and sardine oil fatty acid (iodine value (IV) = 175). Is.
【0033】[0033]
【表6】 [Table 6]
【0034】[0034]
【表7】 [Table 7]
【0035】実施例4 本実施例は脱墨剤のパルピング工程とフロテーション工
程前分割添加の例である。市中回収新聞を2×5cmに細
断後、その一定量を卓上離解機に入れ、その中に水及び
苛性ソーダ(対原料)0.2 %、表7に示す脱墨剤(対原
料)0.2 %を加え、パルプ濃度15%、45℃で12分離解し
た後、55℃で 120分間熟成処理を行った。その後、高速
脱水機で23%まで脱水し、苛性ソーダ(対原料)0.6
%、硅酸ソーダ3号(対原料)2.2 %、30%過酸化水素
(対原料)3.5 %を加え、水でパルプ濃度22%に調整し
卓上離解機にて1分間混合した。その後、回転速度300r
pmの2軸型ラボニーダーでニーディング処理を行った。
その後、水を加えて4%まで希釈し、卓上離解機で再度
30秒離解する。そのパルプスラリーに表7に示す脱墨剤
(対原料)0.3 %を添加した後、スラリーを水で1%に
希釈した後、30℃にて10分間フロテーション処理を施し
た。なお、フロテーション後のパルプスラリーを60メッ
シュワイヤーで4%濃度まで濃縮後、水を加えて1%濃
度に希釈しタッピースタンダート抄紙機にてパルプシー
トを作製した。なお、用いた用水の硬度は40°dHであ
り、硬度はCaCl2 、MgCl2 を使用し、Ca/Mg=8/2
(モル比)になる様に調整した。得られたパルプシート
を測色色差計にてb値を測定し、画像解析装置(×100
倍)にて未剥離インキ個数を測定した。各種脱墨剤の脱
墨性能結果を表8に示す。Example 4 This example is an example of the splitting addition of the deinking agent before the pulping step and the flotation step. The newspaper collected in the market is shredded into 2 x 5 cm pieces, and a certain amount is placed in a table disintegrator, and 0.2% of water and caustic soda (vs. raw material) and 0.2% of the deinking agent (vs. raw material) shown in Table 7 are put in it. In addition, the pulp concentration was 15% and 12 pieces were separated at 45 ° C, and then aged at 55 ° C for 120 minutes. Then, dehydrate to 23% with a high-speed dehydrator, and use 0.6% caustic soda (against raw materials).
%, Sodium silicate No. 3 (for raw material) 2.2%, 30% hydrogen peroxide (for raw material) 3.5% were added, and the pulp concentration was adjusted to 22% with water and mixed for 1 minute with a table disintegrator. After that, the rotation speed is 300r
A kneading process was performed with a pm 2-axis lab kneader.
After that, add water to dilute it to 4%, and use a table top disintegrator again.
Disaggregate for 30 seconds. After adding 0.3% of the deinking agent (compared to the raw material) shown in Table 7 to the pulp slurry, the slurry was diluted to 1% with water and then subjected to flotation treatment at 30 ° C. for 10 minutes. The pulp slurry after flotation was concentrated with a 60-mesh wire to a concentration of 4%, water was added to dilute the concentration to 1%, and a pulp sheet was produced with a tappe tandart paper machine. The hardness of the water used was 40 ° dH, the hardness was CaCl 2 , MgCl 2 , and Ca / Mg = 8/2.
(Molar ratio) was adjusted. The b value of the obtained pulp sheet was measured with a colorimetric color difference meter, and the image analysis device (× 100
The number of unpeeled inks was measured. Table 8 shows the results of deinking performance of various deinking agents.
【0036】なお、表7中の脱墨剤のうち脂肪酸の場合
は、ナトリウム塩又はカルシウム塩である。また、No.5
0, 53 は、脂肪酸ナトリウム塩単体を、No.51, 52 は脂
肪酸カルシウム塩を所定炭素数組成になる様に配合した
ものである。また、No. 54はステアリン酸ナトリウムで
ある。Among the deinking agents in Table 7, the fatty acid is sodium salt or calcium salt. Also, No.5
0 and 53 are fatty acid sodium salts alone, and Nos. 51 and 52 are fatty acid calcium salts blended so as to have a predetermined carbon number composition. No. 54 is sodium stearate.
【0037】[0037]
【表8】 [Table 8]
【0038】[0038]
【表9】 [Table 9]
【0039】上記に例示した如く、炭素数8〜24の高級
脂肪酸又はその塩の混合物であって、該混合物中の脂肪
酸の平均炭素数が12.7〜22.5の範囲にあり、炭素数20〜
24の高級脂肪酸又はその塩の含有率が9.6 〜70.6重量%
であり、且つヨウ素価(IV)が45以下である混合物を脱墨
剤として使用することにより高b値で未剥離インキの少
ない脱墨パルプを得ることができる。As exemplified above, a mixture of a higher fatty acid having 8 to 24 carbon atoms or a salt thereof, wherein the fatty acid in the mixture has an average carbon number of 12.7 to 22.5 and a carbon number of 20 to
The content of 24 higher fatty acids or their salts is 9.6 to 70.6% by weight
And a mixture having an iodine value (IV) of 45 or less is used as a deinking agent, a deinked pulp having a high b value and less unpeeled ink can be obtained.
Claims (3)
を、平均炭素数が12.7〜22.5となる範囲で含有し、炭素
数20〜24の高級脂肪酸又はその塩の含有率が9.6 〜70.6
重量%であり、且つヨウ素価(IV)が45以下である混合
物を必須成分とする脱墨剤。1. A higher fatty acid having 8 to 24 carbon atoms or a salt thereof is contained within a range of an average carbon number of 12.7 to 22.5, and a content of the higher fatty acid having 20 to 24 carbon atoms or a salt thereof is 9.6 to 70.6.
A deinking agent containing a mixture having a iodine value (IV) of 45 or less by weight as an essential component.
3.2重量%、且つ炭素数22の脂肪酸を9.5 〜32.0重量%
含有する請求項1記載の脱墨剤。2. A fatty acid having 20 carbon atoms or a salt thereof is added in an amount of 2.0 to 3
3.2% by weight and 9.5 to 32.0% by weight of C22 fatty acid
The deinking agent according to claim 1, wherein the deinking agent is contained.
半硬化乃至硬化された魚油脂肪酸又はその塩である請求
項1又は2記載の脱墨剤。3. The deinking agent according to claim 1, wherein the higher fatty acid having 8 to 24 carbon atoms or a salt thereof is a semi-hardened or hardened fish oil fatty acid or a salt thereof.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP40928390A JPH0689517B2 (en) | 1990-12-28 | 1990-12-28 | Deinking agent |
| FI913447A FI913447A7 (en) | 1990-12-28 | 1991-07-17 | DEINKINGSFOERFARANDE OCH DEINKINGSSAMMANSAETTNING. |
| KR1019910013090A KR930009269B1 (en) | 1990-12-28 | 1991-07-30 | Deinking method and compositions thereof |
| MX9100439A MX9100439A (en) | 1990-12-28 | 1991-07-30 | METHOD AND COMPOSITION FOR DEINTINATING WASTE PAPER |
| CA 2048128 CA2048128A1 (en) | 1990-12-28 | 1991-07-30 | Deinking method and deinking composition |
| US07/796,608 US5288369A (en) | 1990-12-28 | 1991-11-22 | Deinking method and deinking composition |
| EP19910121953 EP0492507A1 (en) | 1990-12-28 | 1991-12-20 | Deinking method and deinking composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP40928390A JPH0689517B2 (en) | 1990-12-28 | 1990-12-28 | Deinking agent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04327279A JPH04327279A (en) | 1992-11-16 |
| JPH0689517B2 true JPH0689517B2 (en) | 1994-11-09 |
Family
ID=18518629
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP40928390A Expired - Lifetime JPH0689517B2 (en) | 1990-12-28 | 1990-12-28 | Deinking agent |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0689517B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6618146B2 (en) * | 2016-03-28 | 2019-12-11 | 日本製紙株式会社 | Method for deinking UV printed matter |
-
1990
- 1990-12-28 JP JP40928390A patent/JPH0689517B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04327279A (en) | 1992-11-16 |
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