[go: up one dir, main page]

JP3051341B2 - Deinking agent - Google Patents

Deinking agent

Info

Publication number
JP3051341B2
JP3051341B2 JP17735596A JP17735596A JP3051341B2 JP 3051341 B2 JP3051341 B2 JP 3051341B2 JP 17735596 A JP17735596 A JP 17735596A JP 17735596 A JP17735596 A JP 17735596A JP 3051341 B2 JP3051341 B2 JP 3051341B2
Authority
JP
Japan
Prior art keywords
deinking
pulp
polyvinyl alcohol
modified polyvinyl
deinking agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP17735596A
Other languages
Japanese (ja)
Other versions
JPH101889A (en
Inventor
大 佐伯
鉄男 谷中
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.)
Mitsubishi Chemical Corp
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
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 Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP17735596A priority Critical patent/JP3051341B2/en
Publication of JPH101889A publication Critical patent/JPH101889A/en
Application granted granted Critical
Publication of JP3051341B2 publication Critical patent/JP3051341B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02W30/64Paper recycling

Landscapes

  • Compositions Of Macromolecular Compounds (AREA)
  • Paper (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は塗工紙、新聞紙等の
古紙再生時に用いられる脱墨剤に関する。更に詳しくは
塗工紙、新聞紙をフローテーション法で脱墨処理を行う
に際し、高白色度のそして残インキ数の少ない脱墨パル
プを得ることのできる脱墨剤に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deinking agent used for recycling used paper such as coated paper and newsprint. More specifically, the present invention relates to a deinking agent capable of obtaining a deinked pulp having high whiteness and a small number of residual inks when performing deinking treatment on coated paper or newsprint by a flotation method.

【0002】[0002]

【従来の技術】新聞、雑誌等の再生利用は古くから行わ
れているが、最近はパルプ資源の不足や価格の高騰、更
にはゴミ対策、森林資源保護といった観点からもその有
効利用は益々重要性を帯びてきている。その強まるニー
ズに応えるように脱墨されたパルプの高度利用技術開発
にも拍車がかかっている。一方、最近の古紙は印刷イン
キ成分の変化により脱墨という点から見れば、一層険し
い状況になってきている。
2. Description of the Related Art Recycling of newspapers, magazines, etc. has been practiced for a long time, but recently effective use of pulp resources has become increasingly important from the viewpoints of shortage of pulp resources, soaring prices, measures against garbage, and protection of forest resources. It is taking on sex. The development of advanced utilization technology of deinked pulp has been spurred to meet the growing needs. On the other hand, recently used paper has become more steep in terms of deinking due to changes in printing ink components.

【0003】そこで、より以上脱墨を促進させる為、装
置への改良が加えられて来ている。例えばタワーの設置
による高濃度熟成処理、物理力によってより一層インキ
剥離を促進させるためのディスパーザー、ニーダーの導
入更には高濃度離解パルパーの設置が挙げられる。また
フローテーターにおいても、高気泡型フローテーターの
導入が盛んになりつつある。そしてかかる方法において
は、古紙からインキその他の不純物を分離除去する為、
各種の薬剤と脱墨剤が併用して用いられている。具体的
には、水酸化ナトリウム、けい酸ナトリウム、炭酸ナト
リウム、リン酸ナトリウム等のアルカリ剤、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等の薬剤や脱墨剤として
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シド
付加物、アルカノールアマイド類等の非イオン活性剤が
単独又は2種以上配合されて使用されてきた。
[0003] In order to further promote deinking, improvements have been made to devices. For example, a high-concentration aging treatment by installing a tower, the introduction of a disperser and a kneader for further promoting the ink peeling by physical force, and the installation of a high-concentration pulverizing pulper can be mentioned. Also in the case of floaters, the introduction of high-bubble type floaters has become active. And in such a method, in order to separate and remove ink and other impurities from waste paper,
Various drugs and deinking agents are used in combination. Specifically, alkaline agents such as sodium hydroxide, sodium silicate, sodium carbonate and sodium phosphate, hydrogen peroxide, hyposulfite, bleaching agents such as hypochlorite, EDTA,
Agents such as sequestrants such as DTPA and deinking agents such as alkylbenzene sulfonates, higher alcohol sulfates, α-olefin sulfonates, anionic activators such as dialkyl sulfosuccinates, higher alcohols, alkylphenols and fatty acids Nonionic activators such as ethylene oxide adducts and alkanolamides have been used alone or in combination of two or more.

【0004】しかしながら、脱墨剤に着目してみるとこ
れらの脱墨剤ではフロテーション処理における気泡性は
大きいものの気泡の安定性が悪く、またインキ捕集能が
小さく、更には洗浄性においてもその洗浄力が弱い故、
低品質の脱墨パルプしか得られなかった。例えば高白色
度が得られたとしても、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)をせざるをえないという状況であった。
However, when attention is paid to deinking agents, these deinking agents have a large bubble property in flotation treatment, but have poor bubble stability, a low ink collecting ability, and a detergency. Because its washing power is weak,
Only low quality deinked pulp was obtained. For example, even if a high whiteness is obtained, there is dullness, and there is no choice but to limit the use of deinked pulp (reduce the amount of paperboard used below and below, and reduce the amount of paperboard used in newspapers). there were.

【0005】この改良技術として、エチレンオキシドあ
るいはアルキレンオキシド変性した特定のOH含有化合
物と多価カルボン酸又はその無水物との反応生成物を有
効成分とする脱墨剤(特開平4−202881号公報)
や油脂又は該油脂を予めグリセリンと反応させた生成物
と1〜14価のアルコールとの混合物にエチレンオキサ
イドとプロピレンオキサイドを特定の割合で付加させた
エステル混合物を用いた脱墨剤(特開平4−35289
1号公報)などが開示されている。
As an improved technique, a deinking agent containing, as an active ingredient, a reaction product of a specific OH-containing compound modified with ethylene oxide or alkylene oxide and a polyvalent carboxylic acid or its anhydride (JP-A-4-202881).
A deinking agent using an ester mixture obtained by adding ethylene oxide and propylene oxide at a specific ratio to a mixture of oil or fat or a product obtained by previously reacting the oil or fat with glycerin and a 1 to 14-valent alcohol (Japanese Patent Laid-Open No. -35289
No. 1) is disclosed.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、近年ニ
ーダーやディスパーザーを用いた脱墨プラントで、剥離
時にかかる機械力のためにしばしば分散インキの粒径が
細かくなり、フローテーション工程でのインキの除去が
むずかしくなり、特開平4−202881号公報、特開
平4−352891号公報開示技術でもいまだインキの
除去については未だ満足のいくものではなく、剥離イン
キをより効率的に除去する脱墨剤が望まれている。
However, in recent years, in a deinking plant using a kneader or a disperser, the particle size of the dispersed ink often becomes fine due to the mechanical force applied at the time of peeling, and the ink is removed in the flotation step. However, the techniques disclosed in JP-A-4-202881 and JP-A-4-352891 are still unsatisfactory in removing ink, and a deinking agent that removes release ink more efficiently is desired. It is rare.

【0007】[0007]

【課題を解決するための手段】本発明者等は上記の問題
を解決するため鋭意研究を重ねた結果、平均重合度が5
0〜2000の特定の変性ポリビニルアルコール系樹脂
を有効成分とする脱墨剤を用いると、剥離インキをより
効率的に除去でき、白色度の高いパルプが得られること
を見出し本発明を完成するに到った。
The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, the average degree of polymerization was 5%.
It has been found that the use of a deinking agent containing 0 to 2000 specific modified polyvinyl alcohol-based resin as an active ingredient makes it possible to remove the release ink more efficiently and to obtain a pulp having a high whiteness. It has arrived.

【0008】[0008]

【発明の実施の形態】以下に本発明を詳細に説明する。
本発明に用いられる特定の変性ポリビニルアルコール系
樹脂としては、酢酸ビニルと共重合可能な特定のエチレ
ン性不飽和単量体を共重合してケン化して得られた共重
合体や、ポリビニルアルコール(以下PVAと略記する
ことがある)を特定の後変性したものが挙げられる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail.
Specific modified polyvinyl alcohol used in the present invention
Examples of the resin include a copolymer obtained by copolymerizing a specific ethylenically unsaturated monomer copolymerizable with vinyl acetate and saponifying the same or polyvinyl alcohol (hereinafter abbreviated as PVA).
It is) include those modified after a specific a.

【0009】かかる酢酸ビニルと共重合可能な特定のエ
チレン性不飽和単量体としては、アクリル酸、メタクリ
ル酸、クロトン酸、マレイン酸、無水マレイン酸、イタ
コン酸等のカルボン酸類あるいはその塩あるいはモノ又
はジアルキルエステル等、エチレンスルホン酸、アリル
スルホン酸、メタアリルスルホン酸等のオレフィンスル
ホン酸あるいはその塩、2−アクリルアミド−2−メチ
ルプロパンスルホン酸あるいはその塩、ポリオキシエチ
レン(メタ)アリルエーテル、ポリオキシプロピレン
(メタ)アリルエーテルなどのポリオキシアルキレン
(メタ)アリルエーテル、ポリオキシエチレン(メタ)
アクリレート、ポリオキシプロピレン(メタ)アクリレ
ート等のポリオキシアルキレン(メタ)アクリレート、
ポリオキシエチレン(メタ)アクリルアミド、ポリオキ
シプロピレン(メタ)アクリルアミド等のポリオキシア
ルキレン(メタ)アクリルアミド、ポリオキシエチレン
(1ー(メタ)アクリルアミド−1,1−ジメチルプロ
ピル)エステル、ポリオキシエチレンビニルエーテル、
ポリオキシプロピレンビニルエーテル、ポリオキシエチ
レンアリルアミン、ポリオキシプロピレンアリルアミ
ン、ポリオキシエチレンビニルアミン、ポリオキシプロ
ピレンビニルアミン等が挙げられる。
[0009] Such a specific copolymerizable with vinyl acetate.
Acrylic acid, methacrylic acid, etc.
Luic acid, crotonic acid, maleic acid, maleic anhydride, ita
Carboxylic acids such as conic acid or its salts or mono- or
Is dialkyl ester, etc., ethylene sulfonic acid, allyl
Olefins such as sulfonic acid and methallyl sulfonic acid
Honic acid or a salt thereof, 2-acrylamide-2-methyl
Polyoxyalkylene (meth) allyl ether such as lepropanesulfonic acid or a salt thereof , polyoxyethylene (meth) allyl ether, polyoxypropylene (meth) allyl ether, polyoxyethylene (meth)
Acrylates, polyoxyalkylene (meth) acrylates such as polyoxypropylene (meth) acrylate,
Polyoxyalkylene (meth) acrylamide such as polyoxyethylene (meth) acrylamide and polyoxypropylene (meth) acrylamide, polyoxyethylene (1- (meth) acrylamide-1,1-dimethylpropyl) ester, polyoxyethylene vinyl ether,
Examples thereof include polyoxypropylene vinyl ether, polyoxyethylene allylamine, polyoxypropylene allylamine, polyoxyethylene vinylamine, and polyoxypropylene vinylamine.

【0010】カルボン酸基含有単量体との共重合体ケン
化物であるカルボン酸変性PVAや下記式で表される
(ポリ)オキシアルキレン基含有単量体
Carboxylic acid-modified PVA which is a saponified copolymer of a carboxylic acid group-containing monomer and a (poly) oxyalkylene group-containing monomer represented by the following formula

【化1】 〔但しR1、R2は水素又はアルキル基、Xは水素、アル
キル基、アルキルエステル基、アルキルエーテル基、ア
ルキルアミド基、スルホン酸塩基等の有機残基、縮合度
nは1〜300の整数を示す〕との共重合体ケン化物で
ある(ポリ)オキシアルキレン基変性PVAについて
、かかるポリオキシアルキレンの縮合度は1〜30
0、特に4〜50が適当であり、それぞれの変性度は
0.1〜10モル%、好ましくは0.5〜5モル%が適
する。
Embedded image [However, R 1 and R 2 are hydrogen or an alkyl group, X is hydrogen, an organic residue such as an alkyl group, an alkyl ester group, an alkyl ether group, an alkyl amide group, a sulfonate group, and the condensation degree n is an integer of 1 to 300. (Poly) oxyalkylene group-modified PVA which is a saponified copolymer of
Is, the degree of condensation of such polyoxyalkylene 1 to 30
0, especially 4 to 50, is suitable, and the degree of modification of each is 0.1 to 10 mol%, preferably 0.5 to 5 mol%.

【0011】又後変性の方法としては、ポリビニルアル
コールをオキシアルキレン化したものも挙げられる。ま
た、本発明に用いられるPVA樹脂の平均重合度は50
〜2000であることが必要で、該平均重合度が50未
満では充分な界面活性が得られず、逆に2000を越え
ると高粘度となり取扱いが困難であり不適当である。
As a method of post-modification, a method in which polyvinyl alcohol is oxyalkylenated may be mentioned. The average degree of polymerization of the PVA resin used in the present invention is 50.
When the average degree of polymerization is less than 50, sufficient surface activity cannot be obtained. On the other hand, when the average polymerization degree exceeds 2,000, the viscosity becomes high and the handling becomes difficult and unsuitable.

【0012】本発明で脱墨の対象となる古紙の種類とし
ては、新聞紙、塗工紙、ダンボール紙等が挙げられる
が、好ましくは新聞紙、中質紙である。
The types of used paper to be deinked in the present invention include newsprint, coated paper, corrugated cardboard, and the like, and are preferably newsprint and medium quality paper.

【0013】次に本発明の脱墨剤を用いた脱墨処理方法
について具体的に説明する。かかる脱墨方法としては、
公知の方法を採用することができ、脱墨剤の添加方法と
しては古紙溶解工程、ニーダー処理工程、熟成タワー工
程及びフローテーションの何れかもしくは各工程へ分割
添加してもよいが、古紙溶解工程へ添加した場合が最も
効果が高く、該方法について具体的に説明する。
Next, a deinking treatment method using the deinking agent of the present invention will be specifically described. Such deinking methods include:
A known method can be employed. As a method for adding the deinking agent, any of the waste paper dissolving step, the kneading step, the aging tower step and the flotation may be added to each of the respective steps or may be separately added to the waste paper dissolving step. Is most effective when it is added, and the method will be specifically described.

【0014】対パルプ0.1〜0.5重量%水酸化ナト
リウム及び0.1〜0.35重量%の脱墨剤を含む水溶
液に、古紙をパルプ濃度が5〜20重量%、好ましくは
10〜15重量%になるように投入した水分散液を、3
0〜50℃で10〜20分間、撹拌する。次に水分散液
を濾過機、遠心分離機でパルプ濃度が25〜30重量%
になるまで脱水する。その後研磨剤(水酸化ナトリウ
ム、ケイ酸ナトリウム、亜硫酸ソーダ、リン酸ソーダ)
や漂白剤(過酸化水素水、次亜塩素酸ソーダ、次亜硫酸
ソーダ)を投入し、55℃で2時間撹拌する。更にパル
プ濃度が1重量%になるように水を加え、塩化カルシウ
ムを10〜50℃で5〜60分間撹拌する。パルプ濃度
は最終的に0.1〜10重量%になる様に固形分濃度を
調整する。研磨剤や漂白剤は脱墨剤と一緒に仕込んでも
よい。
In an aqueous solution containing 0.1 to 0.5% by weight of sodium hydroxide and 0.1 to 0.35% by weight of a deinking agent based on pulp, waste paper is prepared by pulp concentration of 5 to 20% by weight, preferably 10 to 10% by weight. -15% by weight of the aqueous dispersion,
Stir at 0-50 ° C. for 10-20 minutes. Next, the aqueous dispersion is filtered with a filter and a centrifuge to have a pulp concentration of 25 to 30% by weight.
Dehydrate until it is. Then abrasives (sodium hydroxide, sodium silicate, sodium sulfite, sodium phosphate)
And a bleaching agent (hydrogen peroxide solution, sodium hypochlorite, sodium hyposulfite) are added, and the mixture is stirred at 55 ° C. for 2 hours. Further, water is added so that the pulp concentration becomes 1% by weight, and the calcium chloride is stirred at 10 to 50 ° C. for 5 to 60 minutes. The pulp concentration is adjusted to a solid content concentration of 0.1 to 10% by weight. Abrasives and bleaching agents may be charged together with the deinking agent.

【0015】[0015]

【実施例】以下、実施例を挙げて本発明を具体的に説明
する。尚、実施例中「%」とあるのは、特に断りのない
限り重量基準である。 実施例1〜 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、水及び水酸化ナトリウムを
1.0%(対パルプ)、けい酸ナトリウム3.0%(対
パルプ)、30%過酸化水素水3.0%(対パルプ)に
なるように加え、表1に示す各種変性PVA系樹脂を
0.4%(対パルプ)になるように加え、パルプ濃度5
%、55℃、20分間離解した後、50℃にて60分間
熟成した。その後、水を加えてパルプ濃度を1.0%に
希釈し、塩化カルシウムを1.0%になるように加え、
30℃にて10分間フローテーション処理を施した。フ
ローテーション後のパルプスラリーを6%濃度まで濃縮
後、水を加えて1%程度に希釈し、TAPPIシートマ
シンにてパルプシートを作製した。得られたパルプシー
トを用いて白色度、全インキ数、泡末高、インキ捕集力
について以下の通り測定した。
The present invention will be specifically described below with reference to examples. In the examples, “%” is based on weight unless otherwise specified. Examples 1 to 6 Collected used newspaper collected in the market Shredded newspaper was cut into 2 x 5 cm pieces, and a certain amount was put into a table disintegrator, in which water and sodium hydroxide were 1.0% (relative to pulp) and silica. Sodium 3.0% (relative to pulp), 30% hydrogen peroxide solution 3.0% (relative to pulp), and various modified PVA resins shown in Table 1 are reduced to 0.4% (relative to pulp). Pulp concentration of 5
%, At 55 ° C for 20 minutes, and then aged at 50 ° C for 60 minutes. Thereafter, water was added to dilute the pulp concentration to 1.0%, and calcium chloride was added to 1.0%,
A flotation treatment was performed at 30 ° C. for 10 minutes. After the pulp slurry after flotation was concentrated to a concentration of 6%, water was added to dilute it to about 1%, and a pulp sheet was prepared using a TAPPI sheet machine. Using the obtained pulp sheet, the whiteness, the total number of inks, the foam height, and the ink collecting power were measured as follows.

【0016】(白色度)ハンター色差計にて測定。 (全インキ数)画像解析装置(×100倍)にて測定。 (泡末高)ラボフローテーターより3分間にかき出され
た泡の量を2lのシリンダーで測定した。 (インキ捕集力)インキ捕集力は以下の式にて計算し
た。インキの面積は画像解析処理装置で測定した。 インキ捕集力=[(b−a)/b]×100 a:残インキの面積(フローテーション後) b:インキの面積(フローテーション前)
(Whiteness) Measured by a Hunter color difference meter. (Total number of inks) Measured with an image analyzer (× 100). (Foam powder height) The amount of foam scraped out from the laboratory floatator for 3 minutes was measured with a 2 liter cylinder. (Ink Collecting Power) The ink collecting power was calculated by the following equation. The area of the ink was measured with an image analysis processor. Ink collecting force = [(ba) / b] × 100 a: Area of remaining ink (after flotation) b: Area of ink (before flotation)

【0017】比較例1 実施例1において変性PVA系樹脂の替りに、表1に示
す未変性PVA系樹脂を用いて同様に実施した。 比較例 実施例1で変性PVAの替わりに、12−ヒドロキシス
テアリン酸にエチレンオキシド(EO)29モル、プロ
ピレンオキシド(PO)10モルをブロック付加した化
合物570.8gと無水コハク酸29.2gを1lのフ
ラスコに仕込み、反応温度100℃、撹拌速度400r
pmで窒素雰囲気下で反応させて得られた、12−ヒド
ロキシステアリン酸EO・PO付加物を同量用いた以外
は同様に、実施した。
Comparative Example 1 The same procedure as in Example 1 was carried out except that the unmodified PVA resin shown in Table 1 was used instead of the modified PVA resin. Comparative Example 2 In place of the modified PVA in Example 1, 57 l of a compound obtained by block addition of 29 mol of ethylene oxide (EO) and 10 mol of propylene oxide (PO) to 12-hydroxystearic acid and 29.2 g of succinic anhydride were added in 1 l. , The reaction temperature is 100 ° C., and the stirring speed is 400r.
The reaction was carried out in the same manner except that the same amount of the EO / PO adduct of 12-hydroxystearic acid obtained by reacting at pm in a nitrogen atmosphere was used.

【0018】比較例 実施例1で変性PVAの替わりに、ヤシ油/グリセリン
(1/0.6モル比)にエチレンオキシド(EO)45
モル、プロピレンオキシド(PO)23モルをブロック
付加した化合物350gと無水コハク酸9.5gを1l
のフラスコに仕込み、反応温度100℃、撹拌速度40
0rpmで窒素雰囲気下で反応させて得られた、ヤシ油
・グリセリンEO・PO付加物を同量用いた以外は同様
に、実施した。
COMPARATIVE EXAMPLE 3 Instead of the modified PVA in Example 1, coconut oil / glycerin (1 / 0.6 molar ratio) and ethylene oxide (EO) 45 were used.
1 g of 350 g of a compound obtained by block addition of 23 mol of propylene oxide (PO) and 9.5 g of succinic anhydride.
At a reaction temperature of 100 ° C. and a stirring speed of 40.
The same procedure was performed except that the same amount of coconut oil / glycerin EO / PO adduct obtained by reacting at 0 rpm under a nitrogen atmosphere was used.

【0019】比較例 実施例1で変性PVAの替わりに、ステアリン酸アンモ
ニウムを同量用いた以外は同様に実施した。
Comparative Example 4 Example 1 was repeated except that the same amount of ammonium stearate was used instead of the modified PVA.

【0020】比較例 実施例1で変性PVAの替わりに、ドデシルベンゼンス
ルホン酸ナトリウムを同量用いた以外は同様に実施し
た。
Comparative Example 5 The same procedure was performed as in Example 1 except that the same amount of sodium dodecylbenzenesulfonate was used instead of the modified PVA.

【0021】実施例及び比較例の測定結果を表2に示
す。
Table 2 shows the measurement results of the examples and comparative examples.

【表1】 変性PVA系樹脂 ケン化度 重合度 変性種 (モル%) (モル%、縮合度*) 実施例1 90 600 ポリオキシエチレン (2モル%、n=5) 実施例2 88 1200 ポリオキシエチレン (1モル%、n=13) 実施例3 80 700 ポリオキシプロピレン (0.5モル%、n=18) 実施例4 88 1000 ポリオキシプロピレン (1モル%、n=3) 実施例5 97 1800 マレイン酸 (3モル%) 実施例6 91 600 マレイン酸 (1モル%) 比較例1 88 500 −−− *:nは次式の縮合度を表す。 〔但しR1、R2は水素又はアルキル基、Xは水素、アル
キル基、アルキルエステル基、アルキルアミド基、スル
ホン酸塩基等の有機残基〕
TABLE 1 Degree of saponification of modified PVA resin Resin degree of polymerization Modified species (mol%) (mol%, degree of condensation *) Example 1 90 600 Polyoxyethylene (2 mol%, n = 5) Example 2 88 1200 Poly Oxyethylene (1 mol%, n = 13) Example 3 80 700 Polyoxypropylene (0.5 mol%, n = 18) Example 4 88 1000 Polyoxypropylene (1 mol%, n = 3) Example 5 97 1800 Maleic acid (3 mol%) Example 6 91 600 Maleic acid (1 mol%) Comparative Example 1 88 500 --- *: n represents the condensation degree of the following formula. [However, R 1 and R 2 are hydrogen or an alkyl group, X is hydrogen, an organic residue such as an alkyl group, an alkyl ester group, an alkylamide group, a sulfonate group, etc.]

【0022】[0022]

【表2】 白色度 全残インキ数 泡量(ml) インク捕集力 (%) (cm/2分) (%) 実施例1 57 38 490 90 実施例2 60 50 380 96 実施例3 63 39 470 92 実施例4 66 37 370 90 実施例5 59 46 390 89実施例6 55 32 290 95 比較例1 65 37 350 89 比較例2 45 50 430 85 比較例3 40 60 600 82 比較例4 50 70 400 72比較例5 40 55 650 80 Table 2 Whiteness Total number of remaining inks Bubble amount (ml) Ink collecting power (%) (cm / 2 min) (%) Example 1 57 38 490 90 Example 2 60 50 380 96 Example 3 63 39 470 92 Example 4 66 37 370 90 Example 5 59 46 390 89 Example 6 55 32 290 95 Comparative Example 1 65 37 350 89 Comparative Example 2 45 50 430 85 Comparative Example 3 40 60 600 600 82 Comparative Example 4 50 70 400 72 Comparative Example 5 40 55 650 80

【0023】[0023]

【発明の効果】本発明の脱墨剤は、平均重合度が50〜
2000の特定の変性PVA系樹脂を有効成分としてい
るので、脱墨の際の泡末高が適切で、インク捕集力が大
きく、高白色度で、残インキ数の少ない脱墨パルプを得
ることができる。
The deinking agent of the present invention has an average degree of polymerization of 50 to 50.
Since 2000 specific modified PVA resin is used as an active ingredient, it is possible to obtain deinked pulp with an appropriate bubble height during deinking, high ink collecting power, high whiteness, and a small number of remaining inks. Can be.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) D21C 5/02 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 7 , DB name) D21C 5/02

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】平均重合度が50〜2000の変性ポリビ1. A modified polyvinyl alcohol having an average degree of polymerization of 50 to 2,000.
ニルアルコール系樹脂からなり、該樹脂が(ポリ)オキA (poly) oxyl resin,
シアルキレン変性ポリビニルアルコール、カルボン酸変Sialkylene modified polyvinyl alcohol, carboxylic acid modified
性ポリビニルアルコール、スルホン酸変性ポリビニルアPolyvinyl alcohol, sulfonic acid-modified polyvinyl alcohol
ルコールから選ばれる変性ポリビニルアルコール樹脂をModified polyvinyl alcohol resin selected from
有効成分とすることを特徴とする脱墨剤。A deinking agent characterized by being an active ingredient.
【請求項2】脱墨する紙が塗工紙、新聞紙であることを2. The paper to be deinked is coated paper or newspaper.
特徴とする請求項1記載の脱墨剤。The deinking agent according to claim 1, characterized in that:
【請求項3】脱墨処理時の使用量が、パルプに対して、3. The amount used at the time of deinking treatment is based on pulp.
0.1〜10重量%であることを特徴とする請求項1あ2. The composition according to claim 1, wherein the content is 0.1 to 10% by weight.
るいは2記載の脱墨剤。Or the deinking agent according to 2.
【請求項4】フローテション法で脱墨処理を行う際に用4. A method for performing a deinking process by a floatation method.
いることを特徴とする請求項1〜3いずれか記載の脱墨The deinking according to any one of claims 1 to 3, wherein
剤。Agent.
JP17735596A 1996-06-17 1996-06-17 Deinking agent Expired - Fee Related JP3051341B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17735596A JP3051341B2 (en) 1996-06-17 1996-06-17 Deinking agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17735596A JP3051341B2 (en) 1996-06-17 1996-06-17 Deinking agent

Publications (2)

Publication Number Publication Date
JPH101889A JPH101889A (en) 1998-01-06
JP3051341B2 true JP3051341B2 (en) 2000-06-12

Family

ID=16029525

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17735596A Expired - Fee Related JP3051341B2 (en) 1996-06-17 1996-06-17 Deinking agent

Country Status (1)

Country Link
JP (1) JP3051341B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4695517A (en) * 1985-05-31 1987-09-22 Ngk Spark Plug Co., Ltd. Composite layer aluminum nitride base sintered body

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4886575A (en) 1985-10-08 1989-12-12 Betz Laboratories, Inc. Detackification of adhesive materials contained in secondary fiber with polyvinyl alcohol
WO1992017638A1 (en) 1991-03-28 1992-10-15 Stephan Kleeman Process for removing printing ink from waste paper

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4886575A (en) 1985-10-08 1989-12-12 Betz Laboratories, Inc. Detackification of adhesive materials contained in secondary fiber with polyvinyl alcohol
WO1992017638A1 (en) 1991-03-28 1992-10-15 Stephan Kleeman Process for removing printing ink from waste paper

Also Published As

Publication number Publication date
JPH101889A (en) 1998-01-06

Similar Documents

Publication Publication Date Title
JPH064947B2 (en) Deinking agent for recycled waste paper
KR960007320B1 (en) Deinking agent and method of deinking waste paper using the same
JP3051341B2 (en) Deinking agent
JP3213320B2 (en) Processing of cellulosic materials and compositions used therefor
US5637191A (en) Treatment of cellulosic material and compositions for use in this
JPS6411756B2 (en)
JP3313046B2 (en) Deinking method
JP3086439B2 (en) Deinking agent for recycled paper
JP6713299B2 (en) Deinking agent and method for producing deinking pulp
EA008834B1 (en) Method of deinking
JP2003119683A (en) Coagulant for ink and deinking method of waste paper
JP2810479B2 (en) Deinking agent for recycled paper
JPH11200269A (en) Deinking method of printed waste paper
JP2810477B2 (en) Deinking agent for recycled paper
JP2020094324A (en) Deinking agent and method for producing deinking pulp
JP4571290B2 (en) How to deink waste paper
JP2807248B2 (en) Deinking agent for recycled paper
JP4170510B2 (en) Deinking aid and method for producing deinked recycled pulp
JPS59173393A (en) Deinking agent for regenerating waste paper
JP3124493B2 (en) Deinking method
JP3824214B2 (en) Deinking agent composition
JP2951737B2 (en) Deinking agent
JP2810538B2 (en) Deinking agent for recycled paper
JP3518224B2 (en) Deinking agent for recycled paper
JPH111883A (en) Method for producing high brightness deinked pulp

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080331

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090331

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090331

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090331

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100331

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100331

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110331

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120331

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120331

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120331

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130331

Year of fee payment: 13

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130331

Year of fee payment: 13

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130331

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140331

Year of fee payment: 14

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees