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JPH0364640B2 - - Google Patents
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JPH0364640B2 - - Google Patents

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Publication number
JPH0364640B2
JPH0364640B2 JP55167386A JP16738680A JPH0364640B2 JP H0364640 B2 JPH0364640 B2 JP H0364640B2 JP 55167386 A JP55167386 A JP 55167386A JP 16738680 A JP16738680 A JP 16738680A JP H0364640 B2 JPH0364640 B2 JP H0364640B2
Authority
JP
Japan
Prior art keywords
weight
pulp
calcium silicate
printing paper
paper
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
Application number
JP55167386A
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Japanese (ja)
Other versions
JPS5795400A (en
Inventor
Genji Taga
Takanori Tejima
Yoshiaki Watanabe
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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Filing date
Publication date
Application filed by Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP16738680A priority Critical patent/JPS5795400A/en
Publication of JPS5795400A publication Critical patent/JPS5795400A/en
Publication of JPH0364640B2 publication Critical patent/JPH0364640B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、強度、及び不透明度が高く、しかも
インクの裏抜け防止効果が優れた印刷用紙に関す
る。 近年、木材資源の不足による木材価格の高騰、
及び石油の値上りによる輸送価格の高騰に対処す
るため、新聞用紙をはじめとする印刷用紙の厚さ
を薄くして坪量の低減を図る、所謂紙の軽量化が
試みられている。しかしながら、紙の軽量化によ
り、新聞用紙等の印刷用紙に必要とされる特性で
ある強度、不透明度、及びインクの裏抜け防止効
果が低下するという問題が生ずる。そのため、従
来は強度が高い紙が得られる化学パルプと不透明
度が高い紙が得られる機械パルプとを混合して用
いることにより、前記各特性の向上を図り、上記
特性の低下を抑えて印刷用紙の軽量化を行なつて
いた。しかしながら、化学パルプは紙の強度を向
上させる反面、紙の不透明度を低下させ、機械パ
ルプは紙の不透明度を向上させる反面、紙の強度
を低下させる傾向がある。そのため、上記手段で
は強度、及び不透明度を共に満足して印刷用紙を
軽量化することは困難であつた。また、上記方法
によつて得られた紙は、インクの裏抜け防止効果
の向上をほとんど達成できないのが現状である。 本発明者等は、上述した印刷用紙の軽量化にお
ける問題を解決すべく研究を重ねた。その結果、
機械パルプと化学パルプとよりなる混合パルプに
特定の性状を有する無機粉体を添加することによ
り、強度、不透明度、及びインクの裏抜け防止効
果が共に優れ、軽量化に適した印刷用紙が得られ
ることを見い出し本発明を完了した。 即ち、本発明は機械パルプ95〜50重量%と化学
パルプ5〜50重量%よりなる混合パルプ100重量
部に対して、長手方向の平均直径が0.1〜30ミク
ロン、厚さが0.005〜0.1ミクロンの薄片の集合形
態を有する (a) ジヤイロライトを骨格とし、ジヤイロライト
基準で4乃至70重量%の範囲の二酸化珪素を取
込んだ形で含有する珪酸カルシウム (b) ジヤイロライトを骨格とし、ジヤイロライト
基準で4乃至70重量%の二酸化珪素と13重量%
までの硫酸カルシウムとを取込んだ形で含有す
る珪酸カルシウム・硫酸カルシウム複合体 (c) 前記珪酸カルシウム或いは珪酸カルシウム・
硫酸カルシウム複合体と酸化アルミニウムとの
複合体。 より選ばれた少なくとも1種の無機粉体を0.1
〜6重量部含有した印刷用紙である。 本発明において、印刷用紙を構成するパルプと
しては機械パルプ及び化学パルプよりなる混合パ
ルプが使用される。上記機械パルプは印刷用紙の
不透明性を維持するためのもので、木材またはチ
ツプを機械的に処理して得られたパルプが特に制
限なく使用される。例えば、砕木パルプ(GP)、
リフアイナー砕木パルプ(RGP)、サーモメカニ
カルパルプ(TMP)、ケミメカニカルパルプ等が
一般的である。また、該機械パルプとして上記パ
ルプの故紙パルプも使用することができる。上記
機械パルプのうち、砕木パルプ及びリフアイナー
砕木パルプは、不透明度が高いため特に好適に使
用される。また、前記化学パルプは印刷用紙の強
度を維持するためのもので、木材またはチツプを
化学的に処理して得られたパルプが特に制限なく
使用される。例えば、亜硫酸パルプ(SP)、クラ
フトパルプ(KP)、ソーダパルプ等が一般的であ
る。特に亜硫酸パルプ及びクラフトパルプは強度
があり本発明に好適に使用される。 本発明において、混合パルプにおける機械パル
プと化学パルプの混合比率は機械パルプ95〜50重
量%、好ましくは93〜70重量%、化学パルプ5〜
50重量%、好ましくは7〜30重量%が好適であ
る。該混合パルプにおいて、機械パルプの比率が
上記範囲より多いと得られる紙の不透明度はある
程度向上するが、強度が低下する傾向がある。ま
た、化学パルプの比率が前記範囲より多いと得ら
れる紙の強度は向上するが、不透明度が低下する
傾向があり、軽量化に適した紙を得ることが困難
となる。 本発明に用いる無機粉体は長手方向の平均直径
が0.1乃至30ミクロン、厚さが0.005乃至0.1ミクロ
ンの薄片の集合形態を有する (a) ジヤイロライトを骨格とし、ジヤイロライト
基準で4乃至70重量%の範囲の二酸化珪素を取
込んだ形で含有する珪酸カルシウム (b) ジヤイロライトを骨格とし、ジヤイロライト
基準で4乃至70重量%の二酸化珪素と13重量%
までの硫酸カルシウムとを取込んだ形で含有す
る珪酸カルシウム・硫酸カルシウム複合体 或いは (c) 前記珪酸カルシウム或いは珪酸カルシウム・
硫酸カルシウム複合体と酸化アルミニウムとの
複合体 の少なくとも1種からなつている。 これらの無機粉体は、次の方法で合成できる。
例えば、珪素ナトリウム、珪酸カリウム等の水溶
性珪酸塩と塩化カルシウム、硝酸カルシウム、石
膏等の水溶性カルシウム化合物をSiO2/CaOの
モル比が1.6〜3.2の範囲で150〜250℃の反応温度
下に反応させることによりジヤイロライト型結晶
構造を有し、SiO2/CaOのモル比が1.6〜3.2の珪
酸カルシウムが得られる。この珪酸カルシウムは
一般式2CaO・SiO2・nSiO2・mH2O(但し、mは
正の数でnは一般に0.1〜3.4の数)で示されるも
のと推定され無定形二酸化珪素が結晶中に取込ま
れた形で存在し、その粒界或いは構成結合形態に
ついては透過型電子顕微鏡を用いた2〜20万倍程
度の写真からも識別することができない。 また、活性白土、含水珪酸、珪藻土等の不溶性
二酸化珪素と消石灰、生石灰等のカルシウム化合
物とをSiO2/CaOモル比が1.8〜2.5の範囲で170
〜250℃の反応温度下に反応させることにより二
酸化珪素を混入した前記珪酸カルシウムを得るこ
とができる。上述した珪酸カルシウムの製造方法
のうち、水溶性珪酸塩を原料とする方法によつて
得られた珪酸カルシウムは、後述する紙の強度、
不透明度、及びインクの裏抜け防止効果を向上さ
せる効果が高く本発明に好適に使用される。 前記方法で得られた珪酸カルシウムは電子顕微
鏡写真(3000〜10000倍)をとることにより、バ
ラの花弁に類似する薄片が集合している形態を確
認できる。該薄片の大きさ、形状等は原料の種
類、原料比、製造条件等によつて異なり一概に限
定出来ないが一般には長手方向の平均直径が0.1
〜30ミクロン、厚みが0.005〜0.1ミクロン程度の
円状、楕円状等をしたものが多い。以下、本明細
書において前記珪酸カルシウムを花弁状珪酸カル
シウムという場合もある。 前記水溶性カルシウム化合物として硫酸カルシ
ウム即ち、石膏(本明細書において石膏とは二水
塩のみならず、半水塩、無水塩を含めた意味で用
いるものとする。)を用いる場合は、石膏水性懸
濁液中に珪素アルカリを徐々に加えて反応させた
混合系を、又は反応した沈澱物を濾別し、必要に
応じて洗浄後スラリー溶液としたものを水熱処理
することによつて花弁状珪酸カルシウムを得るこ
とができる。但し、原料中のCaSO4/Na2O又は
K2Oのモル比が1.1以上になると花弁状珪酸カル
シウムと石膏との複合体が得られる。該石膏は花
弁状珪酸カルシウム中の無定形二酸化珪素と同様
に花弁状珪酸カルシウム中に取込まれた形で存在
し、一般に石膏含有量が13重量%程度までは電子
顕微鏡写真をとつてもその粒界或いは構成結合形
態は確認できない。しかし、該石膏の含有量が一
般に13重量%を越えると前記花弁状珪酸カルシウ
ムと石膏との複合体の他に石膏がブレンドされた
ものが得られ、該ブレンド状で、即ち花弁状珪酸
カルシウムと石膏との複合体に混合された状態の
石膏が多くなると得られる印刷用紙の強度の向上
効果が低下する傾向がある。従つて、花弁状珪酸
カルシウムと石膏との複合体中の石膏含有量は10
重量%以下にするのが好ましい。 また、前記花弁状珪酸カルシウム或いは花弁状
珪酸カルシウムと石膏との複合体を硫酸バンド
〔Al2(SO43・18H2O〕と反応させることにより
珪酸カルシウム・酸化アルミニウム複合体にな
る。該複合体は一般式、aAl2O3・2−3a/2CaO・ bSiO2・mH2O(但し、aは0.06〜0.2、bは1.6〜
3.2であり、mは正の数である。)で示されるもの
でる。 本発明の印刷用紙の最大の特徴は前記特定の混
合パルプに対して上記無機粉体を含有させたこと
にある。前述した如く、化学パルプと機械パルプ
との混合パルプを用いても、強度及び不透明度が
共に優れた紙を得ることはほとんど不可能であ
る。またインクの裏抜け防止効果についてもほと
んど改善されない。本発明においては、該無機粉
体を前記した特定の混合パルプに含有させること
により、前記混合パルプのみでは達成できなかつ
た強度及び不透明度が共に優れ、しかもインクの
裏抜け防止効果にも優れた印刷用紙を得ることが
できる。本発明の印刷用紙において、混合パルプ
と無機粉体との割合は混合パルプ100重量部に対
して無機粉体0.1〜6重量部、好ましくは0.3〜4
重量部である。該無機粉体の量が上記範囲より少
ないと印刷用紙の強度、不透明度及びインクの裏
抜け防止効果が低減する傾向がある。また、該無
機粉体は上記範囲より多く用いても効果は頭打ち
となり経済的でない。 本発明の印刷用紙の製造方法は、公知の湿式抄
紙法が制限なく採用される。 また、本発明の印刷用紙は、前記特性に悪影響
を与えない範囲内の量、一般に混合パルプ、100
重量部に対して100重量部以下の量で公知の填料、
顔料、紙力増強剤等の添加物、及びセミケミカル
パルプ等の他のパルプを適宜含有させてもよい。 以上の説明より理解される如く、本発明の印刷
用紙は紙の強度、不透明度、及びインクの裏抜け
防止効果の総てにおいて優れているため、印刷用
紙の軽量化に有用である。特に、軽量化による上
記各特性の低下が激しい坪量40〜50g/m2の印刷
用紙として好適に使用される。 本発明を具体的に説明するため以下実施例を示
すが、本発明はこれらの実施例に限定されるもの
ではない。 参考例 1 880gの二水石膏と20の水を混合反応器に加
え、よく撹拌した。(反応工程)次いでこのスラ
リーを撹拌しながら、大気圧下25℃で0.243モ
ル/酸酸ナトリウム(SiO2/Na2Oモル比2.5)
20を0.5/分の速度で40分間かけて加えた。
この場合の仕込CaSO4/Na2O・nSiO2モル比は
1.05であつた。前記反応工程で得られたスラリー
を濾布をしいたヌツチエに取り出し減圧(400mm
Hg)濾過した後、水30を加え生成物を洗浄し
た。(洗浄工程)上記洗浄工程で得られたケーク
は撹拌槽に移送し水35を加え均一に撹拌しスラ
リー状物とした。(スラリー化工程)該スラリー
化工程で得られたスラリーをオートクレーブ(内
容積50)に移送し密閉して、200℃で5時間、
水熱処理を行なつた。反応終了後生成物スラリー
を得た。スラリーの一部をヌツチエに取り減圧濾
過して得られた生成物は110℃で8時間以上乾燥
し物性を測定した。嵩比容積は12.8c.c./g、吸油
量は4.2c.c./gであつた。尚、X線回折の結果、
ジヤイロライト型珪酸カルシウムのパターンを示
した。 化学分析の結果はCaO 24.9%、SiO2 65.8%、
灼熱減量が9.3%であつた。この結果より前記操
作で得られた珪酸カルシウムは2CaO・3SiO2
1.93SiO2・2.32H2Oであることが確認された。電
子顕微鏡の10000倍の写真から長手方向の平均直
径が約2μで、厚みが0.1μ以下の花弁の集合体で構
成されていることが確認された。 参考例 2 0.3144モル/の塩化カルシウム水溶液(100
c.c.)と0.3144モル/の珪酸ナトリウム(SiO2
Na2Oモル比2.6)水溶液(100c.c.)を大気圧下25
℃で混合(仕込SiO2/CaOモル比2.6)した。混
合と同時に白色の沈澱を生じたがそのままオート
クレーブに入れ密閉し200℃の温度下に5時間反
応させた。この時の圧力は15Kg/cm2Gで水比は30
であつた。反応物は過し、イオン交換100c.c.で
2回繰り返して水洗した後100℃で8時間乾燥し
た。この乾燥物の収量は7.35gであつた。 この乾燥物は、乾燥中にも収縮せず固化もせ
ず、柔かいもので簡単に粉化するものであつた。
また嵩比容積は、14.2c.c./g、吸油量は、4.21
c.c./g、屈折率は、1.50であつた。 前記操作で得られた珪酸カルシウムの一般式
は、化学分析の結果から2CaO・3SiO2
2.05SiO2・2.42H2Oと表示出来た。この珪酸カル
シウムを走査電子顕微鏡写真で1万倍に拡大した
結果から長手方向の平均直径が2ミクロンで、厚
さが0.1ミクロン以下の薄片の集合体で構成され、
あたかも花弁の如き形状が認められた。 また透過電子顕微鏡写真で10万倍に写した結
果、本実験で得られた珪酸カルシウムは、二酸化
珪素を含むにもかかわらずその粒界或いは結合形
態を判別することが出来なかつた。 また上記珪酸カルシウムのX線回折結果からジ
ヤイロライト結晶をしていることが判つた。更に
また前記で得られた花弁状珪酸カルシウム1gに
蒸溜水100c.c.を加え、卓上超音波洗浄器(50W)
によつて30分間分散させたところ二酸化珪素は全
く分散されなかつたことから二酸化珪素が混在し
ないことが確認された。 参考例 3 6.5gの二水石膏(100メツシユ全通)を98c.c.の
水に投じ20分間撹拌する。このスラリーを撹拌し
ながら大気圧下25℃で0.3144モル/の珪酸ナト
リウム(SiO2/Na2Oモル比2.6)100c.c.を6c.c./
分の速度で16分40秒かけて加えた。その後の操作
は参考例1と同様に行ない8.2gの粉体を得た。 この粉体のX線回折の結果は型無水石膏とジ
ヤイロライト型珪酸カルシウムのピークが混在し
ていた。また該粉体の一般式は化学分析の結果か
ら2CaO・3SiO2・2.05SiO2・0.20CaSO4
2.37H2Oで表示出来ることが確認された。上記粉
体を走査電子顕微鏡で1万倍に拡大して写した結
果、長手方向の直径2ミクロン、厚さ0.1ミクロ
ン以下の花弁状薄片で構成されていることが確認
された。しかしながら該写真では型無水石膏と
思われる結晶は外見上識別出来なかつた。該粉体
の嵩比容積は15.2c.c./g、吸油量は4.30c.c./gで
あつた。 参考例 4 参考例1と同様にして得た花弁状珪酸カルシウ
ム1.0gを10%スラリーとした後10%硫酸バンド
〔Al2(SO43・18H2O〕4mlをゆつくりと加え撹
拌しながら1時間反応させた。反応物は過し、
イオン交換水100c.c.で2回水洗した後100℃で8時
間乾燥した。この乾燥物は、乾燥して粉体化して
も或いはスラリーのままでも化学的に安定であつ
た。また上記乾燥物の嵩比容積は、13.8c.c./g、
吸油量は、4.09c.c./gであつた。また前記操作で
得られた乾燥物は珪酸カルシウムの酸化アルミニ
ウム複合体で、その一般式は化学分析の結果から
0.11Al2O3・0.835CaO・2.52SiO2・2.4H2Oで表示
出来るものであつた。 実施例 1 無機粉体として参考例1で得られた珪酸カルシ
ウムの水熱合成後のスラリーを用いた。パルプは
機械パルプとして、GP20重量%、RGP56重量%
と化学パルプとして、NBKP24重量%よりなる
混合パルプとその他にセミケミカルパルプとして
CGPを上記混合パルプ100重量部に対し33重量部
加えたものを用いた。 前述したパルプに水を加えて充分解綿したもの
に、前記無機粉体を水熱合成後のスラリー状態
で、該混合パルプに対する割合を夫々変えて加え
た後、硫酸バンド〔Al2(SO43・18H2O〕上記パ
ルプ(絶乾)100重量部に対し1重量部を水溶液
にして加え、均一に撹拌して、JISP 8209の「パ
ルプ試験用手すき紙調製方法」に準じ抄紙した。
尚、得られる印刷用紙の坪量が49g/m2になるよ
うに抄紙を行なつた。得られた印刷用紙の諸特性
を表−1に示す。また比較のために前記無機粉体
を加えない場合の抄紙結果も表−1に示す。
The present invention relates to printing paper that has high strength and opacity and is excellent in preventing ink from bleeding through. In recent years, wood prices have soared due to a lack of wood resources.
In order to cope with the soaring transportation prices due to the rise in oil prices, attempts have been made to reduce the weight of printing paper, such as newsprint, by thinning it and reducing its basis weight. However, reducing the weight of paper causes a problem in that strength, opacity, and the effect of preventing ink bleed through, which are properties required for printing paper such as newsprint, deteriorate. Therefore, conventionally, by mixing chemical pulp, which produces paper with high strength, and mechanical pulp, which produces paper with high opacity, it is possible to improve each of the above properties, suppress the deterioration of the above properties, and use printing paper. We were working on reducing the weight of the However, chemical pulp tends to improve the strength of the paper but decrease the opacity of the paper, and mechanical pulp tends to improve the opacity of the paper but decrease the strength of the paper. Therefore, with the above-mentioned means, it has been difficult to reduce the weight of printing paper while satisfying both strength and opacity. Furthermore, the paper obtained by the above method is currently unable to achieve almost any improvement in the effect of preventing ink bleed through. The present inventors have conducted repeated research in order to solve the above-mentioned problem in reducing the weight of printing paper. the result,
By adding inorganic powder with specific properties to mixed pulp consisting of mechanical pulp and chemical pulp, printing paper with excellent strength, opacity, and ink bleed-through prevention effect can be obtained, making it suitable for lightweight printing. We have completed the present invention by discovering that That is, in the present invention, for 100 parts by weight of mixed pulp consisting of 95 to 50% by weight of mechanical pulp and 5 to 50% by weight of chemical pulp, the average diameter in the longitudinal direction is 0.1 to 30 microns and the thickness is 0.005 to 0.1 micron. (a) Calcium silicate, which has the form of aggregates of flakes, has a skeleton of gyrolite and contains silicon dioxide in the range of 4 to 70% by weight based on gyrolite. (b) Calcium silicate has a skeleton of gyrolite and contains silicon dioxide in the range of 4 to 70% by weight based on gyrolite. 70% silicon dioxide and 13% by weight
Calcium silicate/calcium sulfate complex (c) containing the calcium silicate or calcium sulfate in an incorporated form (c)
Complex of calcium sulfate complex and aluminum oxide. 0.1 of at least one inorganic powder selected from
It is a printing paper containing ~6 parts by weight. In the present invention, a mixed pulp consisting of mechanical pulp and chemical pulp is used as the pulp constituting the printing paper. The mechanical pulp is used to maintain the opacity of the printing paper, and any pulp obtained by mechanically treating wood or wood chips can be used without particular limitation. For example, ground wood pulp (GP),
Commonly used pulps include refined groundwood pulp (RGP), thermomechanical pulp (TMP), and chemimechanical pulp. Moreover, waste paper pulp of the above-mentioned pulp can also be used as the mechanical pulp. Among the above-mentioned mechanical pulps, groundwood pulp and refined groundwood pulp are particularly preferably used because of their high opacity. Further, the chemical pulp is used to maintain the strength of the printing paper, and pulp obtained by chemically treating wood or chips can be used without particular limitation. For example, sulfite pulp (SP), kraft pulp (KP), soda pulp, etc. are common. In particular, sulfite pulp and kraft pulp are strong and are preferably used in the present invention. In the present invention, the mixing ratio of mechanical pulp and chemical pulp in the mixed pulp is 95 to 50% by weight, preferably 93 to 70% by weight of mechanical pulp, and 5 to 5% by weight of chemical pulp.
50% by weight, preferably 7-30% by weight is suitable. In the mixed pulp, if the ratio of mechanical pulp is greater than the above range, the opacity of the paper obtained will improve to some extent, but the strength will tend to decrease. Furthermore, if the ratio of chemical pulp is greater than the above range, the strength of the paper obtained will improve, but the opacity will tend to decrease, making it difficult to obtain paper suitable for weight reduction. The inorganic powder used in the present invention has an aggregate form of flakes with an average diameter in the longitudinal direction of 0.1 to 30 microns and a thickness of 0.005 to 0.1 micron. Calcium silicate (b) containing in incorporated form silicon dioxide in the range of 4 to 70% by weight of silicon dioxide and 13% by weight based on gyarolite, based on gyarolite.
or (c) a calcium silicate/calcium sulfate complex containing the calcium silicate or calcium sulfate in an incorporated form;
It consists of at least one of a calcium sulfate complex and an aluminum oxide complex. These inorganic powders can be synthesized by the following method.
For example, water-soluble silicates such as sodium silicate and potassium silicate and water-soluble calcium compounds such as calcium chloride, calcium nitrate, and gypsum are mixed at a reaction temperature of 150 to 250°C at a molar ratio of SiO 2 /CaO of 1.6 to 3.2. By reacting with , calcium silicate having a diairolite crystal structure and a SiO 2 /CaO molar ratio of 1.6 to 3.2 is obtained. This calcium silicate is estimated to be represented by the general formula 2CaO・SiO 2・nSiO 2・mH 2 O (where m is a positive number and n is generally a number from 0.1 to 3.4), and amorphous silicon dioxide is contained in the crystal. It exists in an incorporated form, and its grain boundaries and constituent bonding forms cannot be identified even from photographs taken with a transmission electron microscope at a magnification of 20,000 to 200,000 times. In addition, insoluble silicon dioxide such as activated clay, hydrated silicic acid, diatomaceous earth, etc. and calcium compounds such as slaked lime, quicklime, etc. are mixed at a SiO 2 /CaO molar ratio of 1.8 to 2.5.
By reacting at a reaction temperature of ~250°C, the calcium silicate mixed with silicon dioxide can be obtained. Among the above-mentioned methods for producing calcium silicate, calcium silicate obtained by a method using water-soluble silicate as a raw material has the following properties such as paper strength,
It is highly effective in improving the opacity and the effect of preventing ink bleed through, and is therefore preferably used in the present invention. By taking an electron micrograph (3,000 to 10,000 times magnification) of the calcium silicate obtained by the above method, it can be confirmed that the calcium silicate has a collection of flakes resembling rose petals. The size, shape, etc. of the flakes vary depending on the type of raw materials, raw material ratio, manufacturing conditions, etc., and cannot be absolutely limited, but generally the average diameter in the longitudinal direction is 0.1.
~30 microns, with a thickness of about 0.005 to 0.1 microns, often circular or elliptical. Hereinafter, in this specification, the calcium silicate may be referred to as petal-shaped calcium silicate. When using calcium sulfate, that is, gypsum (in this specification, gypsum is used to include not only dihydrate salts but also hemihydrate salts and anhydrous salts) as the water-soluble calcium compound, gypsum aqueous A mixed system in which silica alkali is gradually added to the suspension and reacted, or a reacted precipitate is filtered out and a slurry solution after washing if necessary is hydrothermally treated to form a petal-shaped product. Calcium silicate can be obtained. However, CaSO 4 /Na 2 O or
When the molar ratio of K 2 O is 1.1 or more, a composite of petal-shaped calcium silicate and gypsum is obtained. The gypsum exists in a form incorporated into the petal-like calcium silicate, similar to the amorphous silicon dioxide in the petal-like calcium silicate, and generally, when the gypsum content is up to about 13% by weight, there is no difference in electron micrographs. No grain boundaries or constitutive bonding forms can be confirmed. However, when the content of the gypsum generally exceeds 13% by weight, a blend of gypsum in addition to the above-mentioned composite of the petal-like calcium silicate and gypsum is obtained. When the amount of gypsum mixed in the composite with gypsum increases, the effect of improving the strength of the resulting printing paper tends to decrease. Therefore, the gypsum content in the composite of petal-like calcium silicate and gypsum is 10
It is preferable to make it less than % by weight. Further, by reacting the petal-shaped calcium silicate or a complex of petal-shaped calcium silicate and gypsum with sulfuric acid band [Al 2 (SO 4 ) 3.18H 2 O], a calcium silicate/aluminum oxide composite is obtained. The complex has the general formula aAl2O32-3a /2CaO・bSiO2mH2O (where a is 0.06 to 0.2 and b is 1.6 to
3.2, and m is a positive number. ) is shown. The greatest feature of the printing paper of the present invention is that the specific mixed pulp contains the inorganic powder. As mentioned above, even if a mixed pulp of chemical pulp and mechanical pulp is used, it is almost impossible to obtain paper with excellent strength and opacity. Further, the effect of preventing ink bleed-through is hardly improved. In the present invention, by incorporating the inorganic powder into the above-mentioned specific mixed pulp, it is possible to achieve both excellent strength and opacity that could not be achieved with the above-mentioned mixed pulp alone, and also to have an excellent ink strike-through prevention effect. You can get printing paper. In the printing paper of the present invention, the ratio of mixed pulp and inorganic powder is 0.1 to 6 parts by weight, preferably 0.3 to 4 parts by weight of inorganic powder to 100 parts by weight of mixed pulp.
Parts by weight. When the amount of the inorganic powder is less than the above range, the strength and opacity of the printing paper and the effect of preventing ink bleed through tend to decrease. Further, even if the inorganic powder is used in an amount exceeding the above range, the effect reaches a ceiling and is not economical. As the method for producing the printing paper of the present invention, any known wet papermaking method may be employed without any limitation. In addition, the printing paper of the present invention generally contains mixed pulp in an amount within a range that does not adversely affect the above-mentioned properties.
Known fillers in an amount of not more than 100 parts by weight,
Additives such as pigments and paper strength enhancers, and other pulps such as semi-chemical pulps may be included as appropriate. As understood from the above description, the printing paper of the present invention is excellent in all of paper strength, opacity, and ink strike-through prevention effect, and is therefore useful for reducing the weight of printing paper. In particular, it is suitably used as a printing paper with a basis weight of 40 to 50 g/m 2 where the above-mentioned properties are significantly deteriorated due to weight reduction. EXAMPLES Examples are shown below to specifically explain the present invention, but the present invention is not limited to these Examples. Reference Example 1 880 g of gypsum dihydrate and 20 g of water were added to a mixing reactor and stirred well. (Reaction step) Next, while stirring this slurry, 0.243 mol/sodium acid acid (SiO 2 /Na 2 O molar ratio 2.5) was added at 25°C under atmospheric pressure.
20 was added over 40 minutes at a rate of 0.5/min.
In this case, the charged CaSO 4 /Na 2 O・nSiO 2 molar ratio is
It was 1.05. The slurry obtained in the above reaction step was taken out into a filter cloth covered with a filter cloth and placed under reduced pressure (400 mm
Hg) After filtration, 30 g of water was added to wash the product. (Washing step) The cake obtained in the above washing step was transferred to a stirring tank, and 35% of water was added thereto and stirred uniformly to form a slurry. (Slurrying process) The slurry obtained in the slurrying process was transferred to an autoclave (inner volume 50), sealed, and heated at 200°C for 5 hours.
Hydrothermal treatment was performed. After the reaction was completed, a product slurry was obtained. A portion of the slurry was filtered under reduced pressure using a Nutssie filter, and the resulting product was dried at 110° C. for 8 hours or more and its physical properties were measured. The bulk specific volume was 12.8 cc/g, and the oil absorption amount was 4.2 cc/g. Furthermore, as a result of X-ray diffraction,
The pattern of gyrolite type calcium silicate was shown. Chemical analysis results are CaO 24.9%, SiO 2 65.8%,
Burning weight loss was 9.3%. From this result, the calcium silicate obtained in the above procedure is 2CaO・3SiO 2
It was confirmed that it was 1.93SiO 2 .2.32H 2 O. Photos taken with an electron microscope at 10,000x magnification confirmed that the flower is composed of a collection of petals with an average longitudinal diameter of approximately 2 μm and a thickness of less than 0.1 μm. Reference example 2 0.3144 mol/calcium chloride aqueous solution (100
cc) and 0.3144 mol/sodium silicate (SiO 2 /
Na 2 O molar ratio 2.6) aqueous solution (100 c.c.) under atmospheric pressure 25
The mixture was mixed at ℃ (SiO 2 /CaO molar ratio 2.6). A white precipitate was formed at the same time as the mixture was mixed, but the mixture was placed in an autoclave, sealed, and allowed to react at a temperature of 200°C for 5 hours. The pressure at this time is 15Kg/cm 2 G and the water ratio is 30
It was hot. The reaction product was filtered, washed twice with 100 c.c. of ion exchange, and then dried at 100° C. for 8 hours. The yield of this dried product was 7.35 g. This dried product did not shrink or solidify during drying, and was soft and easily powdered.
Also, bulk specific volume is 14.2cc/g, oil absorption is 4.21
cc/g, and the refractive index was 1.50. The general formula of calcium silicate obtained in the above procedure is 2CaO・3SiO 2
It was possible to display 2.05SiO 2・2.42H 2 O. A scanning electron micrograph of this calcium silicate, magnified 10,000 times, shows that it is composed of an aggregate of flakes with an average longitudinal diameter of 2 microns and a thickness of 0.1 micron or less.
The shape resembled the petals of a flower. Furthermore, as a result of a transmission electron micrograph taken at a magnification of 100,000 times, it was not possible to discern the grain boundaries or bonding form of the calcium silicate obtained in this experiment, even though it contained silicon dioxide. Further, from the results of X-ray diffraction of the above-mentioned calcium silicate, it was found that it was a gyrolite crystal. Furthermore, 100 c.c. of distilled water was added to 1 g of petal-shaped calcium silicate obtained above, and the mixture was heated in a tabletop ultrasonic cleaner (50 W).
When the mixture was dispersed for 30 minutes, no silicon dioxide was dispersed, confirming that no silicon dioxide was mixed. Reference Example 3 Pour 6.5 g of gypsum dihydrate (100 mesh) into 98 c.c. of water and stir for 20 minutes. While stirring this slurry, 100 c.c. of 0.3144 mol/sodium silicate (SiO 2 /Na 2 O molar ratio 2.6) was added to 6 c.c./at 25°C under atmospheric pressure.
It was added over a period of 16 minutes and 40 seconds at a speed of 1 minute. The subsequent operations were carried out in the same manner as in Reference Example 1 to obtain 8.2 g of powder. The results of X-ray diffraction of this powder showed a mixture of peaks of anhydrite type and gyrolite type calcium silicate. The general formula of the powder is 2CaO・3SiO 2・2.05SiO 2・0.20CaSO 4
It was confirmed that it can be displayed at 2.37H 2 O. When the above-mentioned powder was photographed with a scanning electron microscope at a magnification of 10,000 times, it was confirmed that it was composed of petal-like flakes with a longitudinal diameter of 2 microns and a thickness of 0.1 micron or less. However, in the photograph, crystals that appeared to be type anhydrite could not be visually identified. The powder had a bulk specific volume of 15.2 cc/g and an oil absorption of 4.30 cc/g. Reference Example 4 1.0 g of petal-shaped calcium silicate obtained in the same manner as Reference Example 1 was made into a 10% slurry, and then 4 ml of 10% sulfuric acid band [Al 2 (SO 4 ) 3.18H 2 O] was slowly added and stirred. The reaction was allowed to proceed for 1 hour. The reactants are filtered,
After washing twice with 100 c.c. of ion-exchanged water, it was dried at 100°C for 8 hours. This dried product was chemically stable whether it was dried and powdered or left as a slurry. The bulk specific volume of the dried product is 13.8cc/g.
The oil absorption amount was 4.09cc/g. In addition, the dried product obtained in the above procedure is an aluminum oxide complex of calcium silicate, and its general formula is based on the results of chemical analysis.
It could be expressed as 0.11Al 2 O 3・0.835CaO ・2.52SiO 2・2.4H 2 O. Example 1 The slurry obtained after hydrothermal synthesis of calcium silicate obtained in Reference Example 1 was used as an inorganic powder. Pulp is mechanical pulp, GP20% by weight, RGP56% by weight
and chemical pulp, mixed pulp consisting of 24% by weight of NBKP, and other semi-chemical pulps.
33 parts by weight of CGP was added to 100 parts by weight of the above mixed pulp. The above-mentioned inorganic powder was added in a slurry state after hydrothermal synthesis to the above-mentioned pulp which had been thoroughly decomposed by adding water, and the proportions to the mixed pulp were varied, and then sulfate band [Al 2 (SO 4 ) 3.18H 2 O] 1 part by weight was added as an aqueous solution to 100 parts by weight of the above pulp (absolutely dry), stirred uniformly, and paper was made according to JISP 8209 "Hand-sheeted paper preparation method for pulp testing".
The paper was made so that the basis weight of the resulting printing paper was 49 g/m 2 . Table 1 shows various properties of the obtained printing paper. For comparison, Table 1 also shows the papermaking results without the addition of the inorganic powder.

【表】 実施例 2 参考例1において、原料の珪酸塩とカルシウム
化合物のモル比を変えて表−2に示す3種類の花
弁状珪酸カルシウムを合成し実施例1と同様に水
熱合成後のスラリー状態で無機粉体として用い
た。尚、表−2のSiO2/CaOモル比、吸油量、
嵩比容積は、水熱合成後のスラリーをオーブン
(110℃で8時間以上)にて乾燥した後に測定した
値である。
[Table] Example 2 In Reference Example 1, three types of petal-shaped calcium silicates shown in Table 2 were synthesized by changing the molar ratio of the raw silicate and calcium compound, and the results were obtained after hydrothermal synthesis in the same manner as in Example 1. It was used as an inorganic powder in a slurry state. In addition, the SiO 2 /CaO molar ratio, oil absorption amount,
The bulk specific volume is a value measured after drying the slurry after hydrothermal synthesis in an oven (at 110° C. for 8 hours or more).

【表】 前記の花弁状珪酸カルシウムを無機粉体として
用いた以外は、実施例1と同様な操作を行ない抄
紙した。その結果を表−3に示す。
[Table] Paper was made in the same manner as in Example 1, except that the above-mentioned petal-shaped calcium silicate was used as the inorganic powder. The results are shown in Table-3.

【表】 尚、No.1は比較例である。
実施例 3 混合パルプとして表−4に示すものを用いた以
外は、実施例1と同様な操作を行ない抄紙した。
その結果を表−5に示す。
[Table] Note that No. 1 is a comparative example.
Example 3 Paper was made in the same manner as in Example 1, except that the mixed pulp shown in Table 4 was used.
The results are shown in Table-5.

【表】【table】

【表】 尚、1、2、3、7及び8は比較例であ
る。
実施例 4 パルプの組成を機械パルプとして、GP20重量
%、RGP10重量%、TMP45重量%、その他のパ
ルプとしてセミケミカルパルプCGP25重量%の
組成に固定し、これに化学パルプとしてNBKP
を用いた。得られる印刷用紙の引張強度が2.0Kg
fになるように無機粉体、NBKP、前記した組
成が固定されたパルプの量をかえた以外は実施例
1と同様にして抄紙を行なつた。結果を表−6に
示す。 表−6から明らかな如く、花弁状珪酸カルシウ
ムは紙力増強作用を有することから、NBKPの
添加量を減少でき、且つ白色度、不透明度および
裏抜け防止に効果を有することが確認された。 尚、表−6のNo.1は花弁状珪酸カルシウムを加
えない場合の比較例である。
[Table] Note that 1, 2, 3, 7 and 8 are comparative examples.
Example 4 The pulp composition was fixed as a mechanical pulp of 20% by weight of GP, 10% of RGP, and 45% of TMP, and a semichemical pulp of 25% by weight of CGP as other pulps, and NBKP as a chemical pulp.
was used. The tensile strength of the resulting printing paper is 2.0Kg
Paper was made in the same manner as in Example 1, except that the amounts of inorganic powder, NBKP, and pulp with the above-mentioned fixed composition were changed so that f. The results are shown in Table-6. As is clear from Table 6, it was confirmed that the petal-shaped calcium silicate has a paper strength-enhancing effect, which makes it possible to reduce the amount of NBKP added, and is effective in improving whiteness, opacity, and preventing strike-through. Note that No. 1 in Table 6 is a comparative example in which petal-shaped calcium silicate was not added.

【表】 実施例 5 実施例4において、印刷用紙の坪量49g/m2
45g/m2に軽量化した以外は、実施例4と同様に
して印刷用紙の引張強度を2.0Kgfに調整した。
結果を表−7に示す。 表−7から明らから如く、49g/m2の物性(引
張強度、不透明度)を保持させるためにはパルプ
の配合のみでは困難である。しかしながら花弁状
珪酸カルシウムを共存させた場合は、いずれも引
張強度、不透明度とも向上しており且つ白色度、
裏抜け防止に効果を有していることが確認でき
た。
[Table] Example 5 In Example 4, the basis weight of printing paper was 49g/ m2 .
The tensile strength of the printing paper was adjusted to 2.0 Kgf in the same manner as in Example 4, except that the weight was reduced to 45 g/m 2 .
The results are shown in Table-7. As is clear from Table 7, it is difficult to maintain the physical properties (tensile strength, opacity) of 49 g/m 2 by adding pulp alone. However, when petal-shaped calcium silicate was coexisting, both tensile strength and opacity improved, and whiteness and
It was confirmed that it was effective in preventing strike-through.

【表】 実施例 6 無機粉体として参考例2で得られた花弁状珪酸
カルシウムをスラリー状態で用いた以外は実施例
1と同様な操作を行なつた。比較のため填料を加
えない場合の抄紙結果を含めて表−8に示す。
[Table] Example 6 The same operation as in Example 1 was carried out except that the petal-shaped calcium silicate obtained in Reference Example 2 was used in a slurry state as the inorganic powder. For comparison, Table 8 includes the paper making results when no filler was added.

【表】 比較例 1 実施例1の無機粉体に代えてタルク(平均粒径
9〜10μ)を用いた以外は、実施例1と同様な操
作を行なつた。比較のため填料を加えない場合の
抄紙結果を含めて表−9に示す。
[Table] Comparative Example 1 The same operation as in Example 1 was performed except that talc (average particle size 9 to 10 μm) was used in place of the inorganic powder in Example 1. For comparison, Table 9 includes the papermaking results when no filler was added.

【表】 実施例 7 実施例1において、無機粉体として参考例3で
得られた珪酸カルシウムの石膏複合体及び参考例
4で得られた珪酸カルシウムの酸化アムミニウム
複合体を用い、且つパルプの成分にセミケミカル
パルプを加えなかつた以外は同様にして印刷用紙
を製造した。得られた印刷用紙の諸特性を表−10
に示す。
[Table] Example 7 In Example 1, the calcium silicate gypsum complex obtained in Reference Example 3 and the calcium silicate amminium oxide complex obtained in Reference Example 4 were used as the inorganic powder, and the pulp components Printing paper was produced in the same manner except that no semichemical pulp was added to the paper. Table 10 shows the properties of the obtained printing paper.
Shown below.

【表】【table】

Claims (1)

【特許請求の範囲】 1 機械パルプ95〜50重量%と化学パルプ5〜50
重量%よりなる混合パルプ100重量部に対して、
長手方向の平均直径が0.1〜30ミクロン、厚さが
0.005〜0.1ミクロンの薄片の集合形態を有する (a) ジヤイロライトを骨格とし、ジヤイロライト
基準で4乃至70重量%の範囲の二酸化珪素を取
込んだ形で含有する珪酸カルシウム。 (b) ジヤイロライトを骨格とし、ジヤイロライト
基準で4乃至70重量%の二酸化珪素と13重量%
までの硫酸カルシウムとを取込んだ形で含有す
る珪酸カルシウム・硫酸カルシウム複合体。 或いは (c) 前記珪酸カルシウム或いは珪酸カルシウム・
硫酸カルシウム複合体と酸化アルミニウムとの
複合体。 より選ばれた少なくとも1種の無機粉体を0.1〜
6重量部含有した印刷用紙。 2 坪量が40〜50g/m2である特許請求の範囲第
1項記載の印刷用紙。
[Claims] 1. Mechanical pulp 95 to 50% by weight and chemical pulp 5 to 50% by weight
For 100 parts by weight of mixed pulp consisting of % by weight,
The average longitudinal diameter is 0.1-30 microns and the thickness is
(a) Calcium silicate having an aggregate form of flakes of 0.005 to 0.1 micron, having a skeleton of gyrolite and containing silicon dioxide in an incorporated form in the range of 4 to 70% by weight based on gyrolite. (b) 4 to 70% by weight of silicon dioxide and 13% by weight based on gyrolite, with a skeleton of gyrolite;
Calcium silicate/calcium sulfate complex containing calcium sulfate. or (c) the calcium silicate or calcium silicate.
Complex of calcium sulfate complex and aluminum oxide. At least one kind of inorganic powder selected from 0.1~
Printing paper containing 6 parts by weight. 2. The printing paper according to claim 1, having a basis weight of 40 to 50 g/m 2 .
JP16738680A 1980-11-29 1980-11-29 Printing paper Granted JPS5795400A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16738680A JPS5795400A (en) 1980-11-29 1980-11-29 Printing paper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16738680A JPS5795400A (en) 1980-11-29 1980-11-29 Printing paper

Publications (2)

Publication Number Publication Date
JPS5795400A JPS5795400A (en) 1982-06-14
JPH0364640B2 true JPH0364640B2 (en) 1991-10-07

Family

ID=15848737

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16738680A Granted JPS5795400A (en) 1980-11-29 1980-11-29 Printing paper

Country Status (1)

Country Link
JP (1) JPS5795400A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5122872B2 (en) * 2006-06-23 2013-01-16 中越パルプ工業株式会社 Neutral paper and method for producing neutral paper

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5482015A (en) * 1977-12-12 1979-06-29 Nec Corp Reversible motor controller

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