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JPS6311478B2 - - Google Patents
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JPS6311478B2 - - Google Patents

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Publication number
JPS6311478B2
JPS6311478B2 JP54082015A JP8201579A JPS6311478B2 JP S6311478 B2 JPS6311478 B2 JP S6311478B2 JP 54082015 A JP54082015 A JP 54082015A JP 8201579 A JP8201579 A JP 8201579A JP S6311478 B2 JPS6311478 B2 JP S6311478B2
Authority
JP
Japan
Prior art keywords
paper
filler
petal
calcium silicate
shaped silica
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
Application number
JP54082015A
Other languages
Japanese (ja)
Other versions
JPS569499A (en
Inventor
Takanori Tejima
Yoshiaki Watanabe
Teruo Oikawa
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 JP8201579A priority Critical patent/JPS569499A/en
Publication of JPS569499A publication Critical patent/JPS569499A/en
Publication of JPS6311478B2 publication Critical patent/JPS6311478B2/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、印刷後の裏抜け防止に優れ、且つ強
さが良好な新規な紙に関するもので、より詳しく
は、特定の珪酸質粒子からなる填料とパルプを抄
紙することによつて得られた、細孔半径0.75ミク
ロン以下の細孔容積が、細孔半径7.5ミクロン以
上の細孔容積より大きく、且つ、細孔半径0.75ミ
クロン以下の細孔容積が0.1c.c./g以上である紙
に関するものである。なお、本発明における紙の
細孔半径及び細孔容積は水銀ポロシメーターによ
つて測定して得た値をいい、具体的には細孔半径
は水銀ポロシメーターで圧力(P・atm)を測定
し、γ=75000/Pから算出した半径γである。
また珪酸カルシウムに取込まれていない即ちブレ
ンドされて混入している二酸化珪素は蒸留水100
c.c.に珪酸カルシウム1gを入れ超音波(出力
50W)によつて30分間分散させて分離される二酸
化珪素をさすものである。 従来紙は種々の種類のものが使用されている。
一般にパルプのみから製造された紙は紙の強さ
(以下、裂断長をもつて表示する)が最も良好で
あるが、印刷後インクが裏抜けする欠点があるば
かりでなく、白色度、不透明度、平滑性が不十分
であつて一部の紙類を除くと使用されていない。
一般にはパルプにカオリン、タルク、酸化チタン
等の填料を添加することにより上記欠点を改良し
てきた。しかしながら、上記填料は吸油量がほと
んどないことから印刷インクの浸透を防止するこ
とができず、紙厚の増加、填料の増加等の手段で
実用に供する紙を製造していた。特に酸化チタン
を填料に用いた紙は不透明度が極めて高いので、
この影響により前記裏抜けはある程度防止できる
が酸化チタンの添加量が6(重量)%以上になる
と裂断長の低下が著しくなる欠陥がある。一方、
紙厚の増加、填料の増加等は不経済であるばかり
でなく、紙の取扱いが不便であるため吸油量を有
する填料をパルプに添加する試みも実施されてい
る。例えばホワイトカーボンと称される含水珪酸
が上記の代表的な填料である。しかしながら、上
記吸油量を有する填料は使用量が少なくて裏抜け
防止効果を発揮するが紙の強さが極端に低下する
ため必ずしも満足できる填料とは言えなかつた。
長ちパルプに添加する填料の種類によつて紙の性
状は変化するが、裏抜け防止効果と紙の強さとの
性状は表裏一体のもので両方の性状を満足する紙
の開発が大きな課題であつた。 本発明者等は前記裏抜け防止にすぐれ且つ紙の
強さが良好な紙を製造する研究を鋭意続けてき
た。その結果、紙の裏抜け防止が紙の小さい細孔
半径の細孔容積に影響され、紙の強さを低下させ
る要因が紙の大きい細孔半径の細孔容積に依存
し、上記相反する2つの目的は、特定の填料を使
用して抄紙し、特定の細孔容積の紙とすることに
よつて達成されることを見出し本発明を完成させ
るに至つた。 即ち、本発明は特定の珪酸質粒子からなる填料
とパルプを抄紙することによつて得られた、細孔
半径0.75ミクロン以下の細孔容積が細孔半径7.5
ミクロン以上の細孔容積より大きく且つ細孔半径
0.75ミクロン以下の細孔容積が0.10c.c./g以上で
ある紙である。 本発明の紙はその構成を特に限定されるもので
はないが、一般に合成紙において前記細孔半径を
制御することは難しく、通常はパルプと特定の填
料とで主に構成された紙が対象とされる。また通
常、市販されている紙例えばパルプと公知の填料
とで抄紙されたものは後述する比較例でも明らか
な如く、細孔半径0.75ミクロン以下の細孔容積が
細孔半径7.5ミクロン以上の細孔容積より小さい
ものである。この点からも本発明の紙が新規なも
のであることが判る。従来紙の裏抜け防止及び強
さを決定する要因は填料の性状であると考えられ
てきた。しかしながら、本発明者等の研究によれ
ば、填料の性質のみならず、紙自身の細孔半径分
布が裏抜け防止及び強さを決定する要因になり、
このような細孔半径分布を有する紙は、上記特定
の珪酸質粒子を填料として使用することによつて
得られることが発見された。すなわち、紙の細孔
半径分布は抄紙技術によつても変化するが、填料
の種類によつて最も大きな影響をうけるもので、
填料を選択することが重要な要因となる。該紙の
細孔半径分布を本発明で特定する範囲内におさめ
る技術については後述するが、本発明の紙につい
て詳細に述べると次ぎのような性質を与える。即
ち紙自身の細孔半径で0.75ミクロン以下の細孔容
積は裏抜け防止に影響し、細孔半径7.5ミクロン
以上の細孔容積は紙の強度低下に大きな影響を与
える。紙の強度はパルプの繊維同志の接着やから
みあいなどによつてもたらされるものであり、こ
れを妨げる要因があれば紙の強度は低下する。一
般的に紙に填料を加えることは、繊維間の接着や
からみあいなどを妨げる働きをすることから添加
量に相関して紙の強度が低下する傾向がある。ま
た填料の粒度、形態、粉体あるいは凝集粒のくず
れ易さなども強度と相関する。例えば粒度では余
りにも微粉砕すると繊維の表面に付着した状態と
なり、繊維の接着を妨げ強度低下を起し、逆に粒
度が粗いと加えられた填料の効果が充分に発揮さ
れない。また填料の形態はパルプの繊維とのから
みがよく、歩留のよい形をしたものである必要が
ある。更に粉体あるいは凝集粒の崩れ易さは抄紙
時の湿式プレスのときに填料がパルプの繊維同志
によつて構成される細孔へ崩れて流れてゆき、繊
維間の接着、からみあいなどを妨げないようにす
るために必要である。この時填料が崩れにくかつ
たりあるいは不純物などを含んでいたりするとパ
ルプの繊維によつて構成される細孔へ流れず、そ
の場所で填料に起因する新しい細孔を構成するこ
とになる。これがパルプの繊維間の接着やからみ
あいなどを妨げ強度低下を起す。こうした現象は
細孔半径7.5ミクロン以上の細孔容積値を観察す
ることによりより明確にすることができる。例え
ばホワイトカーボンと称される含水珪酸または不
溶性シリカを原料とした珪酸カルシウムを用いる
と、細孔半径7.5ミクロン以上の細孔容積は抄紙
時に湿式プレスを行つてもこの値を減少できず、
裂断長の低下が顕著である。また後述する特定の
珪酸カルシウムなどを用いるとこの値を容易に減
少でき裂断長低下の少ない紙を得ることができ
る。従つて、該細孔半径0.75ミクロン以下の細孔
容積が大きい程紙の裏抜け防止効果は大きく、細
孔半径7.5ミクロン以上の細孔容積が小さい程紙
の強度低下は小さい傾向がある。 また本発明における裏抜け防止効果が大きく、
強度低下の小さい紙を得るには紙の細孔半径0.75
ミクロン以下の細孔容積が細孔半径7.5ミクロン
以上の細孔容積より大きいことが必要である。し
かも紙の裏抜け防止を実用に供するに足るものと
するためには、細孔半径0.75ミクロン以下の細孔
容積は少くとも0.10c.c./g以上好ましくは0.15
c.c./g以上であることが必要である。また前記細
孔半径7.5ミクロン以上の細孔容積が0.3c.c./gよ
りも大になると細孔半径0.75ミクロン以下の細孔
容積が0.3c.c./gよりも大であつても紙の強度低
下が大きくなる傾向があるので、一般には細孔半
径が7.5ミクロン以上の細孔容積は0.3c.c./gまで
にとどめるのが好ましい。 本発明の紙は例えばパルプ化工程で製造された
パルプを必要に応じて漂白、乾燥、叩解処理を行
つたものに前記珪酸質填料を粉状又はスラリー状
で加え通常の方法で抄紙し乾燥すればよい。該填
料は抄紙に先だつてパルプと混合してもよく抄紙
時に添加してもよい。本発明の紙は前記した如く
細孔半径7.5ミクロン以上の細孔容積ができるだ
け小さい方が好ましいので、一般には抄紙時に湿
式プレスすることによつて該細孔容積を小さくす
る処置が好適に採用される。また該パルプは特に
限定されず公知のものを用いうるが、一般には新
聞紙、下級印刷紙、中級紙、上級紙、書籍紙等の
製紙用パルプとして使用される針葉樹及び広葉樹
から得られるパルプが好適に使用される。 前記した如く紙自身の細孔半径及び細孔容積は
抄紙技術例えば湿式プレスなどによつて変化する
が、最も影響をうけるのは填料の性状と添加量で
ある。該填料の添加量は填料の種類に応じて予め
決定するとよいが、一般にはパルプ100部に対し
て1〜40部好ましくは2〜25部の範囲で添加する
のが最も一般的である。一般には填料の粒子径が
小さすぎると抄紙時に紙から離脱しやすく逆に粒
子径が大きすぎると繊維とのからみあいが不均一
になる傾向がある。従つて、一般に填料は粒子径
2〜30ミクロン間の粒子を90(重量)%以上含む
ものが好適に使用される。 本発明の紙を得る填料としては長手方向の平均
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珪酸質粒子から
なつており、この珪酸質粒子は一層好適には (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または珪酸カルシウム・
硫酸カルシウム複合体の酸処理により得られた
シリカ。 或いは (d) 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。 の少くとも1種からなつている。 これらの無機質粒子は、次ぎの方法で合成でき
る。例えば珪酸ナトリウム、珪酸カリウ等の水溶
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とをSiO2/CaO
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・3SiO2・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。 前記の無定形2酸化珪素が結晶中に取込まれた
形とはジヤイロライト型珪酸カルシウム即ち
2CaO・3SiO2・2H2Oと無定形2酸化珪素即ち
nSiO2・mH2Oとで構成されるが、無定形2酸化
珪素は単なるブレンド形状でなくジヤイロライト
型珪酸カルシウムの生成時に無定形2酸化珪素を
含有してなるものである。透過電子顕微鏡写真な
どから推察すると、上記無定形2酸化珪素は非常
にミクロに分散され、例えば100Å以下で均一に
分散されてジヤイロライト型珪酸カルシウムと共
に結晶形成に関与しているものである。 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
の花の花弁に類似する薄片が集合している形態を
確認出来る。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
〜30μ、厚みが0.005〜0.1μ程度の円状、楕円状等
をしたものが多い。以下本明細書に於いては前記
珪酸カルシウムを花弁状珪カルと略記する場合も
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2水塩
のみならず、半水塩、無水物をも含めた意味で用
いるものとする。)を用いる場合は、石膏水性懸
濁液中に珪酸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カルを得ることが出来
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カルと石膏との複
合体が得られる。該石膏は花弁状珪カル中の無定
形2酸化珪素と同様に花弁状珪カル中に取込まれ
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出来ない。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
弁状珪カル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
弁状珪カルと石膏との複合体に混合された状態の
石膏が多くなると前記紙の細孔半径7.5μ以上の細
孔容積が大きくなる傾向があり紙の裂断長が低下
する。従つて該花弁状珪カルと石膏との複合体中
の石膏含有量は10%以下にするのが好ましい。 また前記花弁状珪カル或いは花弁状珪カルと石
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
ムの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。)で示されるものである。該複合
体もまた本発明の紙の填料として好適に用いう
る。 前記方法で得られた花弁状珪カルまたは花弁状
珪カルと石膏との複合体を塩酸等の鉱酸で加熱し
強制的にカルシウムを抜き出すと、元の花弁の形
態を保持したままの2酸化珪素を得ることができ
る。この花弁状珪カル又は花弁状珪カルと石膏と
の複合体から得られた2酸化珪素(以下、花弁状
シリカと略記する)も本発明の紙の填料として好
適に用いられる。この花弁状シリカは電子顕微鏡
写真(3000〜10000倍)をとることにより確認出
来るが、長手方向の平均直径が0.1〜30μ、厚みが
0.005〜0.1μ程度の薄片の集合体からなつている。
またその形状は円状、楕円状で外観がバラの花の
花弁に類似する薄片の集合形態を有するものが最
も多い。またX線回折の結果から非晶質2酸化珪
素であることが確認できた。 しかしながら前記花弁状珪カル又は花弁状珪カ
ルと他の化合物との複合体はその製造時に於ける
原料のSiO2/CaOモル比が大きくなると無定形
2酸化珪素が前記花弁状珪カルと石膏との複合体
で説明したと同様にブレンドされた状態で含まれ
て来る。該ブレンドされた状態の無定形2酸化珪
素即ち花弁状珪カルの結晶構造の外に存在する2
酸化珪素は紙の細孔半径7.5μ以上の細孔容積を大
きくする傾向があり出来るだけ混入をさけるのが
好ましい。同様に不溶性の2酸化珪素例えばホワ
イトカーボンと称される含水珪酸、珪素土等をシ
リカ源原料として使用する場合は一部花弁状珪カ
ルに類似の構造を有する珪酸カルシウムが反応条
件によつては得られる。しかしながら、この場合
は未反応の2酸化珪素が前記花弁状珪カルとブレ
ンドされて混入されるので本発明の紙を得る填料
とはなり得ない。後述する実施例及び比較例でも
詳しく述べるが上記不溶性2酸化珪素をシリカ源
原料として用いて得られる珪酸カルシウムは前記
花弁状珪カル或いは花弁状珪カルと他の化合物と
の複合体とは見掛上類似する点があるが、前者中
に未反応のブレンドされた2酸化珪素が含まれて
いることは試料1gを蒸留水100c.c.に入れ、超音
波(50W)によつて30分間分散させることによつ
て分離出来るので、前記花弁状珪カルとの区別が
容易に達成出来る。また透過電子顕微鏡を用いた
2〜20万倍程度の写真からも前記未反応の2酸化
珪素を識別できる。 本発明の紙は前記特定の細孔容積を有する範囲
内であれば酸化チタン、カオリン、タルクなどの
従来の填料と前記珪酸質填料とを併用して用いて
もよく、特に限定されるものではない。 例えば不透明度の高い紙の要求があれば、酸化
チタンを前記填料に添加してもよく、前記特定の
細孔容積内にあれば、不透明度の良好な裏抜け防
止された裂断長低下の少ない紙を得ることができ
る。また一般に紙の表面の光沢性を向上させるた
めに、塗被用顔料を接着剤その他の添加剤ととも
に水性塗料として紙の片面あるいは両面に塗被さ
れ、スーパーカレンダーその他の光沢機で仕上げ
られて印刷用、装飾用などの用途に適する紙が得
られるが、本発明の紙において同様の処理を施し
ても何ら支障なく、本発明の特徴は失なわれず良
好である。 本発明を詳細に説明するために以下の実施例比
較例及び参考例を挙げて説明するが、本発明はこ
れらの実施例等に限定されるものではない。尚、
以下の実施例、比較例ではパルプとしては特に記
さない限り針葉樹のサルフアイトパルプを用い、
予め叩解機で一定に解綿(シヨツパー・フリーネ
ス27.8゜SR)したものを用いた。 また以下の実施例、比較例の紙の坪量、厚さ、
裂断長、細孔容積などは手抄シートの標準状態
(20℃、65%RH)における値である。更に、ま
た填料の嵩比容積、吸油量、屈折率、粒度分布は
次のような方法で測定した。 (イ) 嵩比容積 粉体は乳鉢で200メツシユ篩80%通過粒度ま
で粉砕した。この粉砕物を用いてJIS K6220の
6.8項の嵩比重測定方法によつて測定した。 (ロ) 吸油量 粉体を乳鉢で200メツシユ篩80%通加粒度ま
で粉砕した。この粉砕物を用いてJIS K6220の
19項の吸油量測定方法によつて測定した。 (ハ) 屈折率 α―クロルナフタリンとシクロヘキサンを各
種割合に混合した溶媒を作り、この溶媒を用い
て、浸液法によつて測定した。浸液法は須藤俊
男著、粘土鉱物学P100〜103(1974)の方法を
採用した。 (ニ) 粒度分布 この測定には米国コールターエレクトロニク
ス社のコールターカウンタ―モデルTA―を
採用した。尚市販の填料の粒径は、カタログ値
を示した。 参考例 1 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殿を生じたがそのままオート
クレープに入れ密閉し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水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4.21c.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
2.4H2O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1万倍に拡大して写した結果
は第1図に示す通りであつた。第1図から明らか
な如く本参考例で得られた珪酸カルシウムは長手
方向の平均直径が2μで厚さが0.1μ以下の薄片の集
合体で構成されていることが認められた。 また透過電子顕微鏡写真で10万倍に写した結果
は第2図に示す通りであつた。第2図から明らか
な如く本実験で得られた珪酸カルシウムは2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カル1gに蒸留水
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離さ
れず二酸化珪素をブレンド物として含まないこと
が確認された。 参考例 2 参考例1と同様にして得られた花弁状珪カル10
gに6N―塩酸100mlを加えたのち、大気圧下70℃
において1時間反応させる。該反応物は過しイ
オン交換水100mlで2回繰り返し水洗した後100℃
で8時間乾燥した。この乾燥物の収量は7.75gで
あつた。この乾燥物は乾燥中収縮や固化はせず柔
かいものであつた。また該乾燥物の嵩比容積は
12.9c.c./g、吸油量は3.5c.c./g及び屈折率は1.45
であつた。 前記操作で得られた乾燥物は2酸化珪素で8.5
重量%の水分を含んでいた。この2酸化珪素を電
子顕微鏡写真で1万倍に拡大して写した結果第3
図に示す通りであつた。これから明らかな如く、
参考例1で得られた花弁状珪カルに似た形状をし
ていた。 参考例 3 6.5gの2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線回析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
果は第4図に示す通りであつた。第4図から明ら
かな如く長手方向の直径2μ厚さ0.1μ以下の花弁で
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カル10gを
10%スラリーとした後10%硫酸バンド〔Al2
(SO43・18H2O〕4mlをゆつくりと加えかくは
んしながら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あ
る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。 参考例 5 水に不溶な2酸化珪素を出発原料として珪酸カ
ルシウムを合成した。5%のホワイトカーボンス
ラリー(SiO2として5g)と5%の水酸化カル
シウムスラリー(CaOとして2.03g)を大気圧下
25℃で1時間混合する(仕込SiO2/CaOモル比
2.30)。そのままオートクレープに入れ密閉し200
℃の温度下で15時間反応させた。反応物は過し
イオン交換水100c.c.で2回繰り返し水洗した後100
℃で8時間乾燥した。この乾燥物の収量は8.56g
であつた。 この乾燥物は乾燥中に収縮も固化もせず柔かい
ものであつた。またこの乾燥物の嵩比容積は5.8
c.c./g、吸油量は1.52c.c./g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CaO・2.28SiO2・2.5H2Oで
表示出来るものであつた。 この珪酸カルシウムの走査電子顕微鏡写真で
5000倍に拡大して写した結果第5図に示す通りで
あつた。第5図から明らかな如く、参考例1の花
弁状珪カルに類似した形状であつた。この珪酸カ
ルシウムの透過電子顕微鏡5万倍で写した結果は
第6図に示す通りであつた。第6図から明らかな
如く未反応の2酸化珪素粒がブレンドされている
ことをはつきりと確認できた。この未反応の2酸
化珪素粒は以下の操作で分別した。この珪酸カル
シウム1gに蒸留水100c.c.を加え参考例1と同様
に超音波によつて30分間分散すると未反応2酸化
珪素と珪酸カルシウムが2相となつた。未反応2
酸化珪素相(この場合上相)を除去し珪酸カルシ
ウムのSiO2/CaOモル比を化学分析したところ
1.8となり計算からブレンドして混入している2
酸化珪素は12.1重量%であることが確認された。 実施例 1 填料として参考例1で得られたSiO2/CaOモ
ル比2.52の花弁状珪カルを細川鉄工所製のシクロ
ンミルで粉砕し粒径2〜30μが97重量%で平均粒
径16μであるものを用い、解綿したパルプ(パル
プ量は固定し無添加紙の坪量を48g/m2とした)
に硫酸バンド〔Al2(SO4318H2O〕をパルプ(絶
乾)に対し2.0重量%添加したのち填料をスラリ
ーとして加え、JIS P8209のパルプ試験用手すき
紙調整方法に準じ抄紙した。填料の添加量はパル
プ(絶乾)に対する重量%である。 比較のために填料を添加しない場合の抄紙結果
を含めて表―1に示す。表―1から明らかな如く
花弁状珪カルは裂断長の低下が少なく裏抜け防止
に効果を発揮するだけでなく白色度不透明度の向
上が良好であることが確認された。花弁状珪カル
は不純物の混入も少なく比較的ゆるい凝集粒であ
るため抄紙時のワイヤー摩耗も殆どなかつた。 尚、表―1のNo.1は、填料を用いない場合の比
較例である。
The present invention relates to a new paper that is excellent in preventing print-through after printing and has good strength. More specifically, the present invention relates to a new paper that is excellent in preventing print-through and has good strength. , relating to paper in which the volume of pores with a pore radius of 0.75 microns or less is larger than the volume of pores with a pore radius of 7.5 microns or more, and the volume of pores with a pore radius of 0.75 microns or less is 0.1 cc/g or more. be. Note that the pore radius and pore volume of paper in the present invention refer to values obtained by measuring with a mercury porosimeter, and specifically, the pore radius is determined by measuring the pressure (P atm) with a mercury porosimeter. This is the radius γ calculated from γ=75000/P.
In addition, silicon dioxide that is not incorporated into calcium silicate, that is, is blended with it, is contained in distilled water.
Put 1g of calcium silicate in cc and use ultrasonic wave (output
50W) for 30 minutes to separate silicon dioxide. Conventionally, various types of paper have been used.
In general, paper made only from pulp has the best strength (hereinafter expressed as tear length), but it not only has the disadvantage of ink bleed through after printing, but also has poor whiteness and poor paper strength. Due to insufficient transparency and smoothness, it is not used except for some papers.
Generally, the above-mentioned drawbacks have been improved by adding fillers such as kaolin, talc, and titanium oxide to the pulp. However, since the above-mentioned filler has almost no oil absorption, it is not possible to prevent printing ink from penetrating, and paper for practical use has been manufactured by increasing the thickness of the paper, increasing the amount of filler, etc. In particular, paper that uses titanium oxide as a filler has extremely high opacity, so
Due to this influence, the strike-through can be prevented to some extent, but when the amount of titanium oxide added exceeds 6% (by weight), there is a defect that the tearing length decreases significantly. on the other hand,
Increasing the paper thickness, increasing the amount of filler, etc. is not only uneconomical, but also makes handling of the paper inconvenient, so attempts have been made to add oil-absorbing fillers to the pulp. For example, hydrated silicic acid called white carbon is a typical filler mentioned above. However, although a filler having the above-mentioned oil absorption amount is used in a small amount and exhibits an effect of preventing bleed through, the strength of the paper is extremely reduced, so it cannot necessarily be said to be a satisfactory filler.
The properties of paper change depending on the type of filler added to the long-lasting pulp, but the anti-bleeding effect and the strength of the paper are two sides of the same coin, and the development of paper that satisfies both properties is a major challenge. It was hot. The inventors of the present invention have been diligently conducting research to produce paper that is excellent in preventing print-through and has good paper strength. As a result, the prevention of paper bleed-through is affected by the pore volume of the paper's small pore radius, and the factors that reduce paper strength depend on the pore volume of the paper's large pore radius. The present inventors have discovered that two objects can be achieved by making paper using a specific filler and producing paper with a specific pore volume, leading to the completion of the present invention. That is, in the present invention, the volume of pores with a pore radius of 0.75 microns or less is obtained by paper-making a pulp and a filler made of specific silicic acid particles.
Larger than micron pore volume and pore radius
The paper has a pore volume of 0.75 microns or less and 0.10 cc/g or more. Although the paper of the present invention is not particularly limited in its composition, it is generally difficult to control the pore radius in synthetic paper, and paper mainly composed of pulp and a specific filler is usually targeted. be done. In addition, commercially available paper, such as paper made from pulp and known fillers, usually has pores with a pore radius of 0.75 microns or less and a pore volume of 7.5 microns or more, as shown in the comparative examples described later. It is smaller than the volume. From this point as well, it can be seen that the paper of the present invention is novel. Conventionally, it has been thought that the properties of the filler are a factor that determines the bleed-through prevention and strength of paper. However, according to the research of the present inventors, not only the properties of the filler but also the pore radius distribution of the paper itself are factors that determine the prevention of bleed-through and strength.
It has been discovered that paper having such a pore radius distribution can be obtained by using the above-mentioned specific siliceous particles as a filler. In other words, although the pore radius distribution of paper changes depending on the papermaking technology, it is most influenced by the type of filler.
Filler selection is an important factor. A technique for keeping the pore radius distribution of the paper within the range specified by the present invention will be described later, but the paper of the present invention will have the following properties when described in detail. In other words, a pore volume of the paper itself with a pore radius of 0.75 microns or less has an effect on preventing strike-through, and a pore volume with a pore radius of 7.5 microns or more has a large effect on a decrease in the strength of the paper. The strength of paper is provided by the adhesion and entanglement of pulp fibers, and if there are any factors that interfere with this, the strength of paper will decrease. Generally, when filler is added to paper, it acts to prevent adhesion and entanglement between fibers, so the strength of the paper tends to decrease in relation to the amount added. In addition, the particle size and form of the filler, and the ease with which the powder or agglomerated grains break down, etc., also correlate with the strength. For example, if the particle size is too fine, the filler will adhere to the surface of the fibers, preventing adhesion of the fibers and causing a decrease in strength.On the other hand, if the particle size is too coarse, the added filler will not be fully effective. In addition, the filler must be in a shape that allows for good intertwining with pulp fibers and a good yield. Furthermore, the ease with which powder or aggregate particles crumble means that during wet pressing during papermaking, the filler crumbles and flows into the pores formed by the pulp fibers, without interfering with adhesion or entanglement between the fibers. It is necessary to do so. At this time, if the filler does not crumble easily or contains impurities, it will not flow into the pores formed by the pulp fibers, and new pores caused by the filler will be formed at that location. This prevents adhesion and entanglement between fibers of the pulp, resulting in a decrease in strength. These phenomena can be made clearer by observing the pore volume values with a pore radius of 7.5 microns or more. For example, when calcium silicate made from hydrated silicic acid or insoluble silica, which is called white carbon, is used, the volume of pores with a pore radius of 7.5 microns or more cannot be reduced even if wet pressing is performed during paper making.
The decrease in tear length is significant. Further, by using a specific calcium silicate, etc., which will be described later, this value can be easily reduced and paper with less decrease in tearing length can be obtained. Therefore, the larger the volume of pores with a pore radius of 0.75 microns or less, the greater the effect of preventing paper from bleeding through, and the smaller the volume of pores with a pore radius of 7.5 microns or more, the smaller the decrease in paper strength tends to be. In addition, the present invention has a large strike-through prevention effect,
To obtain paper with less strength loss, the paper pore radius is 0.75.
It is necessary that the pore volume of microns or less be larger than the pore volume of pores with a pore radius of 7.5 microns or more. Moreover, in order to effectively prevent paper from bleeding through, the pore volume with a pore radius of 0.75 microns or less should be at least 0.10 cc/g or more, preferably 0.15 cc/g or more.
It is necessary that it is cc/g or more. Furthermore, if the volume of pores with a pore radius of 7.5 microns or more is larger than 0.3 cc/g, the strength of the paper will decrease significantly even if the volume of pores with a pore radius of 0.75 microns or less is larger than 0.3 cc/g. Therefore, it is generally preferable to limit the volume of pores with a pore radius of 7.5 microns or more to 0.3 cc/g. The paper of the present invention can be produced, for example, by adding the siliceous filler in the form of powder or slurry to the pulp produced in the pulping process, which has been bleached, dried, and beaten as necessary, and then made into paper using a conventional method and dried. Bye. The filler may be mixed with the pulp prior to paper making or may be added during paper making. As mentioned above, it is preferable for the paper of the present invention to have a pore volume with a pore radius of 7.5 microns or more as small as possible, so it is generally preferable to reduce the pore volume by wet pressing during paper making. Ru. The pulp is not particularly limited and any known pulp may be used, but pulps obtained from softwoods and hardwoods, which are generally used as papermaking pulp for newspapers, low-grade printing paper, intermediate-grade paper, high-grade paper, book paper, etc., are preferred. used for. As mentioned above, the pore radius and pore volume of the paper itself change depending on the paper-making technique, such as wet pressing, but what is most affected are the properties and amount of filler added. The amount of the filler to be added may be determined in advance depending on the type of filler, but it is most commonly added in the range of 1 to 40 parts, preferably 2 to 25 parts per 100 parts of pulp. In general, if the particle size of the filler is too small, it tends to separate from the paper during paper making, and conversely, if the particle size is too large, it tends to become unevenly entangled with the fibers. Therefore, in general, a filler containing 90% (by weight) or more of particles having a particle size of 2 to 30 microns is preferably used. The filler for producing the paper of the present invention is composed of silicic acid particles having an aggregate form of flakes with an average longitudinal diameter of 0.1 to 30 microns and a thickness of 0.005 to 0.1 micron, and these silicic acid particles are more preferably used. (a) Calcium silicate having a skeleton of gyrolite and containing silicon dioxide in an incorporated form in a 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. (c) The calcium silicate or calcium silicate.
Silica obtained by acid treatment of calcium sulfate complex. or (d) the calcium silicate or calcium silicate.
Complex of calcium sulfate complex and aluminum oxide. It consists of at least one species. These inorganic particles 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 combined into SiO 2 /CaO
By reacting at a reaction temperature of 150 to 250° C. with a molar ratio in the range of 1.6 to 3.2, calcium silicate having a gairolite crystal structure and a SiO 2 /CaO molar ratio of 1.6 to 3.2 can be obtained. This calcium silicate has the general formula 2CaO・3SiO 2・nSiO 2・mH 2 O (however, m
is a positive number and n is generally a number from 0.1 to 3.4), and it is assumed that amorphous silicon dioxide exists in the form incorporated into the crystal, and its grain boundaries or constituent bonding form are transparent type. It cannot be identified even from photographs taken with an electron microscope at a magnification of 200,000 to 200,000 times. The form in which the above-mentioned amorphous silicon dioxide is incorporated into the crystal is gyirolite calcium silicate, that is,
2CaO・3SiO 2・2H 2 O and amorphous silicon dioxide i.e.
Although it is composed of nSiO 2 ·mH 2 O, amorphous silicon dioxide is not simply in a blended form, but is formed by containing amorphous silicon dioxide during the production of gyarolite type calcium silicate. Judging from transmission electron micrographs and the like, the amorphous silicon dioxide is very microscopically dispersed, for example, uniformly dispersed at 100 Å or less, and participates in crystal formation together with gyrolite calcium silicate. 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 an aggregated form similar to the petals of a rose flower. The size, shape, etc. of the flakes vary depending on the type of raw materials, raw material ratio, manufacturing conditions, etc., and cannot be unconditionally limited, but generally the average diameter in the longitudinal direction is 0.1.
Most of them are circular, elliptical, etc. with a thickness of ~30μ and a thickness of about 0.005~0.1μ. Hereinafter, in this specification, the calcium silicate may be abbreviated as petal-like silica. When using calcium sulfate, that is, gypsum (in this specification, gypsum is used to include not only dihydrate salts but also hemihydrate salts and anhydrides) as the water-soluble calcium compound, gypsum aqueous A mixed system in which alkali silicate is gradually added to the suspension and reacted, or a reacted precipitate is filtered and washed if necessary, and then a slurry solution is hydrothermally treated to form petal-shaped silica. You can get Cal. However, if the molar ratio of CaSO 4 /Na 2 O or K 2 O in the raw material is 1.1 or more, a composite of petal-shaped silica and gypsum is obtained. The gypsum exists in a form incorporated in the petal-shaped silica, similar to the amorphous silicon dioxide in the petal-shaped silica, and the gypsum content is generally 13% (by weight).
To a certain extent, even if an electron micrograph is taken, the grain boundaries or the constituent bond form cannot 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-shaped silica and gypsum is obtained. When the amount of gypsum mixed in the composite of gypsum and gypsum increases, the volume of pores with a pore radius of 7.5 μm or more tends to increase, and the tearing length of the paper decreases. Therefore, the gypsum content in the composite of the petal-shaped silica and gypsum is preferably 10% or less. In addition, the petal-shaped silica or a composite of the petal-shaped silica and gypsum is treated with sulfate band [Al 2 (SO 4 ) 3 .
18H 2 O] to form an aluminum oxide complex of calcium silicate. The complex has the general formula aAl2O3.2-3a / 2CaO.bSiO2.mH2O (where a is 0.06 to 0.2 , b is 1.6 to 3.2 , and m is a positive number). This is what is shown. The composite can also be suitably used as a filler for the paper of the present invention. When the petal-shaped silica or the composite of petal-shaped silica and gypsum obtained by the above method is heated with a mineral acid such as hydrochloric acid to forcefully extract calcium, 2 oxide is formed while retaining the original petal form. Silicon can be obtained. Silicon dioxide obtained from this petal-shaped silica or a composite of petal-shaped silica and gypsum (hereinafter abbreviated as petal-shaped silica) is also suitably used as a filler for the paper of the present invention. This petal-shaped silica can be confirmed by taking electron micrographs (3,000 to 10,000 times magnification), and it can be seen that the average diameter in the longitudinal direction is 0.1 to 30μ, and the thickness is
It consists of a collection of thin flakes of about 0.005 to 0.1μ.
In addition, most of them have a circular or elliptical shape, with an appearance similar to the petals of a rose flower. Moreover, it was confirmed from the results of X-ray diffraction that it was amorphous silicon dioxide. However, when the petal-shaped silica or a composite of the petal-shaped silica and other compounds increases the SiO 2 /CaO molar ratio of the raw materials during production, the amorphous silicon dioxide is mixed with the petal-shaped silica and gypsum. It comes in a blended form similar to that described in the complex. 2 that exists outside the crystal structure of the amorphous silicon dioxide in the blended state, that is, the petal-shaped silica.
Silicon oxide tends to increase the volume of pores with a radius of 7.5 μm or more in paper, so it is preferable to avoid contamination as much as possible. Similarly, when insoluble silicon dioxide, such as hydrated silicic acid called white carbon, siliceous earth, etc., is used as a silica source material, calcium silicate, which has a structure similar to petal-shaped silica, may be used depending on the reaction conditions. can get. However, in this case, unreacted silicon dioxide is blended and mixed with the petal-shaped silica, and therefore cannot serve as a filler for obtaining the paper of the present invention. As will be described in detail in Examples and Comparative Examples below, the calcium silicate obtained by using the above-mentioned insoluble silicon dioxide as a silica source material does not appear to be the petal-shaped silica or a composite of the petal-shaped silica and other compounds. There are similarities between the above, but the fact that the former contains unreacted blended silicon dioxide is that 1 g of the sample is placed in 100 c.c. of distilled water and dispersed for 30 minutes using ultrasound (50 W). Since it can be separated by allowing the silica to separate, it can be easily distinguished from the petal-shaped silica. The unreacted silicon dioxide can also be identified from a photograph taken with a transmission electron microscope at a magnification of about 200,000 to 200,000 times. The paper of the present invention may be used in combination with conventional fillers such as titanium oxide, kaolin, talc, etc. and the siliceous filler as long as it has the specific pore volume, and is not particularly limited. do not have. For example, if a paper with high opacity is required, titanium oxide may be added to the filler, and if within the specified pore volume, it will provide good opacity, anti-bleed through and reduced tear length. You can get less paper. Generally, in order to improve the glossiness of the paper surface, coating pigments are applied as a water-based paint along with adhesives and other additives to one or both sides of the paper, and the paper is finished using a supercalender or other gloss machine and then printed. The paper obtained is suitable for purposes such as personal and decorative purposes, and the paper of the present invention can be subjected to similar treatments without any problems and the characteristics of the present invention are not lost. In order to explain the present invention in detail, the following Examples, Comparative Examples, and Reference Examples will be given and explained, but the present invention is not limited to these Examples. still,
In the following Examples and Comparative Examples, coniferous sulfite pulp was used as the pulp unless otherwise specified.
The cotton used was one that had been pre-defined using a beating machine (shopper freeness 27.8°SR). In addition, the basis weight and thickness of the paper in the following examples and comparative examples,
The tear length, pore volume, etc. are the values under the standard conditions of handmade sheets (20°C, 65%RH). Furthermore, the bulk specific volume, oil absorption, refractive index, and particle size distribution of the filler were measured by the following methods. (b) Bulk specific volume The powder was ground in a mortar to a particle size that could pass 80% through a 200 mesh sieve. Using this crushed material, JIS K6220
It was measured using the bulk specific gravity measurement method described in Section 6.8. (b) Oil absorption The powder was crushed in a mortar to a particle size of 80% through a 200 mesh sieve. Using this crushed material, JIS K6220
It was measured according to the oil absorption measurement method described in Section 19. (c) Refractive index Solvents were prepared by mixing α-chlornaphthalene and cyclohexane in various proportions, and measurements were made using the immersion method using this solvent. The immersion method was based on Toshio Sudo's Clay Mineralogy P100-103 (1974). (d) Particle size distribution For this measurement, Coulter Counter Model TA manufactured by Coulter Electronics, Inc. of the United States was used. The particle size of commercially available fillers is the catalog value. Reference example 1 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 produced at the same time as the mixture was mixed, but the mixture was placed in an autoclave, sealed, and reacted at 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 washed twice with 100 c.c. of filtered ion-exchanged water 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. The bulk specific volume is 14.2cc/g, the oil absorption is 4.21cc/g, and the refractive index is
It was 1.50. The general formula of calcium silicate obtained in the above procedure is 2CaO・3SiO 2・2.05SiO 2
I was able to display 2.4H 2 O. A scanning electron micrograph of this calcium silicate, magnified 10,000 times, was as shown in FIG. As is clear from FIG. 1, the calcium silicate obtained in this reference example was found to be composed of an aggregate of flakes with an average diameter in the longitudinal direction of 2 μm and a thickness of 0.1 μm or less. In addition, a transmission electron micrograph taken at a magnification of 100,000 times was as shown in Figure 2. As is clear from FIG. 2, although the calcium silicate obtained in this experiment contained silicon dioxide, it was not possible to discern its grain boundaries or bond form. Further, from the results of X-ray diffraction of the above-mentioned calcium silicate, it was found that it was a gyrolite crystal. Furthermore, distilled water was added to 1 g of the petal-shaped silica obtained above.
Add 100c.c. and use a tabletop ultrasonic cleaner (50W)
When the mixture was dispersed for 30 minutes, it was confirmed that silicon dioxide was not separated at all, and that no silicon dioxide was contained as a blend. Reference Example 2 Petal-shaped silica 10 obtained in the same manner as Reference Example 1
After adding 100ml of 6N-hydrochloric acid to
Allow to react for 1 hour. The reaction product was washed twice with 100 ml of filtered ion-exchanged water and heated to 100°C.
It was dried for 8 hours. The yield of this dried product was 7.75 g. This dried material did not shrink or solidify during drying and was soft. Also, the bulk specific volume of the dried product is
12.9cc/g, oil absorption 3.5cc/g and refractive index 1.45
It was hot. The dry product obtained in the above operation has a silicon dioxide content of 8.5
It contained % water by weight. This silicon dioxide was photographed using an electron microscope and magnified 10,000 times.
It was as shown in the figure. As is clear from this,
It had a shape similar to the petal-shaped silica obtained in Reference Example 1. Reference Example 3 Pour 6.5 g of dihydrate gypsum (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. The above powder was photographed with a scanning electron microscope at a magnification of 10,000 times, and the results were as shown in FIG. As is clear from Fig. 4, it was confirmed that the flower was composed of petals with a longitudinal diameter of 2 μm and a thickness of 0.1 μm or less. However, in the photograph, crystals that appeared to be type anhydrite could not be visually identified. The bulk specific volume of the powder is 15.2cc/
g, and the oil absorption amount was 4.30 cc/g. Reference Example 4 10g of petal-shaped silica obtained in the same manner as Reference Example 1 was
After making 10% slurry, 10% sulfuric acid band [Al 2
(SO 4 ) 3.18H 2 O] 4 ml was slowly added and the reaction was allowed to proceed for 1 hour while stirring. The reaction product was washed twice with 100 c.c. of filtered ion-exchanged water and then dried at 100°C for 8 hours. This dried product was chemically stable even when it was dried and powdered or 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, whose general formula was determined from the results of chemical analysis.
It could be expressed as 0.11Al 2 O 3・0.835CaO ・2.52SiO 2・2.4H 2 O. Reference Example 5 Calcium silicate was synthesized using water-insoluble silicon dioxide as a starting material. 5% white carbon slurry (5g as SiO2 ) and 5% calcium hydroxide slurry (2.03g as CaO) under atmospheric pressure.
Mix for 1 hour at 25℃ (Prepared SiO 2 /CaO molar ratio
2.30). Place it in an autoclave and seal it for 200 minutes.
The reaction was carried out for 15 hours at a temperature of ℃. The reaction product was washed twice with 100 c.c. of filtered ion-exchanged water and then washed with 100 c.c.
It was dried at ℃ for 8 hours. The yield of this dry matter is 8.56g
It was hot. This dried material did not shrink or solidify during drying and was soft. Also, the bulk specific volume of this dried product is 5.8
cc/g, and the oil absorption amount was 1.52 cc/g. The general formula of calcium silicate obtained in the above procedure could be expressed as CaO.2.28SiO 2.2.5H 2 O from the results of chemical analysis. This scanning electron micrograph of calcium silicate
The result of enlarging the image 5000 times was as shown in Figure 5. As is clear from FIG. 5, the shape was similar to the petal-like silica of Reference Example 1. This calcium silicate was photographed using a transmission electron microscope at a magnification of 50,000 times, and the results were as shown in FIG. As is clear from FIG. 6, it was clearly confirmed that unreacted silicon dioxide particles were blended. The unreacted silicon dioxide particles were separated by the following procedure. 100 c.c. of distilled water was added to 1 g of this calcium silicate and dispersed for 30 minutes using ultrasonic waves as in Reference Example 1, resulting in two phases of unreacted silicon dioxide and calcium silicate. Unreacted 2
After removing the silicon oxide phase (upper phase in this case), we chemically analyzed the SiO 2 /CaO molar ratio of calcium silicate.
It becomes 1.8 and is mixed by blending from calculation2
Silicon oxide was confirmed to be 12.1% by weight. Example 1 As a filler, the petal-shaped silica obtained in Reference Example 1 with a molar ratio of SiO 2 /CaO of 2.52 was ground with a cyclone mill manufactured by Hosokawa Iron Works, and the particle size was 97% by weight from 2 to 30μ, and the average particle size was 16μ. (The amount of pulp was fixed and the basis weight of additive-free paper was 48 g/ m2 )
After adding 2.0% by weight of sulfuric acid band [Al 2 (SO 4 ) 3 18H 2 O] to the pulp (absolutely dry), a filler was added as a slurry, and paper was made according to the JIS P8209 method for preparing handmade paper for pulp testing. The amount of filler added is % by weight based on the pulp (bone dry). For comparison, Table 1 includes the papermaking results when no filler was added. As is clear from Table 1, it was confirmed that the petal-shaped silica not only exhibits a small decrease in tearing length and is effective in preventing strike-through, but also improves whiteness and opacity. Since the petal-shaped silica contains relatively few impurities and is a relatively loose agglomerated grain, there was almost no wire abrasion during paper making. Note that No. 1 in Table 1 is a comparative example in which no filler was used.

【表】 (*2) インキ受理量
(*3) 印刷後の紙の印刷面とは反対側の面の白色
度を示した。
実施例 2 参考例1と同様な操作で表―2に示す4種類の
花弁状珪カルを合成し、実施例1と同様にシクロ
ンミルで粉砕した。
[Table] (*2) Amount of ink accepted (*3) Indicates the whiteness of the side of the paper opposite to the printed side after printing.
Example 2 Four types of petal-shaped silica shown in Table 2 were synthesized in the same manner as in Reference Example 1, and ground in a cyclone mill in the same manner as in Example 1.

【表】【table】

【表】 前記の珪カルを填料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。 表―3から明らかな如くこれ等の花弁状珪カル
は裂断長の低下が少なく裏抜け防止に効果を発揮
するだけでなく白色度、不透明度の向上が良好で
あつた。
[Table] Paper was made in the same manner as in Example 1 except that the above-mentioned silica was used as a filler. The results are shown in Table-3. As is clear from Table 3, these petal-shaped silicas not only exhibited a small decrease in tearing length and were effective in preventing strike-through, but also improved whiteness and opacity.

【表】【table】

【表】 実施例 3 填料として参考例2で得られた花弁状シリカを
実施例1と同様に粉砕し粒径2〜30μが97重量%
で平均粒径12.7μである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―4に示す。 表―4の結果から明らかな如く花弁状シリカを
添加した紙の裂断長は花弁状珪カルより若干劣る
ものの後述する比較例1のホワイトカーボンのよ
うに極端に裂断長が低下しないことが確認され
た。 尚、表―4のNo.1は填料を用いない場合の比較
例である。
[Table] Example 3 As a filler, the petal-shaped silica obtained in Reference Example 2 was pulverized in the same manner as in Example 1, and 97% by weight of particle size 2-30μ was obtained.
Paper was made in the same manner as in Example 1, except that particles having an average particle size of 12.7 μm were used. The results are shown in Table 4. As is clear from the results in Table 4, the tearing length of paper to which petal-like silica has been added is slightly inferior to that of petal-like silica, but the tearing length does not decrease drastically like that of white carbon in Comparative Example 1, which will be described later. confirmed. Note that No. 1 in Table 4 is a comparative example in which no filler was used.

【表】 実施例 4 填料として参考例3で得られた花弁状珪カル―
石膏複合体を実施例1と同様に粉砕し粒径2〜
30μで94重量%で平均粒径16μであるものを用い
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。 表―5の結果から明らかな如く、花弁状珪カル
―石膏複合体の抄紙結果は実施例1と同様良好な
結果が確認された。 尚、表―5のNo.1は填料を用いない場合の比較
例である。
[Table] Example 4 Petal-shaped silica obtained in Reference Example 3 as a filler
The gypsum composite was crushed in the same manner as in Example 1, and the particle size was 2~
Paper was made in the same manner as in Example 1, except that 30μ, 94% by weight, and an average particle size of 16μ were used. The results are shown in Table-5. As is clear from the results in Table 5, the paper-making results of the petal-shaped silica-gypsum composite were confirmed to be as good as in Example 1. Note that No. 1 in Table 5 is a comparative example in which no filler was used.

【表】 実施例 5 填料として参考例4で得られた花弁状珪カルの
酸化アルミニウム複合体を実施例1と同様に粉砕
し粒径2〜30μが92重量%で平均粒径16μである
ものを用いた以外は実施例1と同様な操作を行な
い抄紙した結果を表―6に示す。 表―6から明らかな如く、花弁状珪カルの酸化
アルミニウム複合体は実施例1と同様良好な結果
が得られた。 尚、表―6のNo.1は填料を用いない場合の比較
例である。
[Table] Example 5 As a filler, the petal-shaped silica aluminum oxide composite obtained in Reference Example 4 was ground in the same manner as in Example 1, and the particle size was 92% by weight from 2 to 30μ, and the average particle size was 16μ. Table 6 shows the results of paper making performed in the same manner as in Example 1 except that . As is clear from Table 6, similar to Example 1, good results were obtained with the petal-shaped silica aluminum oxide composite. Note that No. 1 in Table 6 is a comparative example in which no filler was used.

【表】 実施例 6 填料として参考例1で得られた花弁状珪カル
(実施例1と同一粒度分布)と酸化チタン〔石原
産業(株)の商品名タイペータW―10粒径0.15〜
0.25μ〕の等量混合物を用い、硫酸バンドをパル
プ(絶乾)に対し4重量%添加した以外は実施例
1と同様な操作を行ない抄紙した。その結果を表
―7に示す。 表―7から明らかな如く、花弁状珪カルと酸化
チタンを用いた本発明の範囲内の紙を抄紙すれば
相乗作用により、更に有効であることが確認され
た。この紙は実施例1の花弁状珪カル単独に比較
し裂断長の低下が若干大きいものの白色度、不透
明度、印刷後の白色度に特徴があることが認めら
れた。 尚、表―7のNo.1は填料を用いない場合の比較
例である。
[Table] Example 6 Petal-shaped silica obtained in Reference Example 1 (same particle size distribution as Example 1) and titanium oxide [Ishihara Sangyo Co., Ltd. trade name Typeta W-10 particle size 0.15 to
Paper was made in the same manner as in Example 1, except that 4% by weight of sulfuric acid was added to the pulp (absolutely dried) using a mixture of equal amounts of 0.25μ]. The results are shown in Table-7. As is clear from Table 7, it was confirmed that paper making within the scope of the present invention using petal-shaped silica and titanium oxide would be more effective due to the synergistic effect. This paper was found to have characteristics in whiteness, opacity, and whiteness after printing, although the tearing length was slightly reduced compared to the petal-shaped silica of Example 1 alone. Note that No. 1 in Table 7 is a comparative example in which no filler was used.

【表】 実施例 7 填料として参考例3で得られた花弁状珪カル―
石膏複合体(実施例4と同一粒度分布)と酸化チ
タンの等量混合物を用いた以外は、実施例6と同
様な操作を行ない抄紙した。その結果を表―8に
示す。 表―8から明らかな如く、花弁状珪カル―石膏
複合体と酸化チタンの混合物は実施例6と同様良
好な結果が確認された。 尚、表―8のNo.1は填料を用いない場合の比較
例である。
[Table] Example 7 Petal-shaped silica obtained in Reference Example 3 as a filler
Paper was made in the same manner as in Example 6, except that a mixture of equal amounts of gypsum composite (same particle size distribution as in Example 4) and titanium oxide was used. The results are shown in Table 8. As is clear from Table 8, good results were confirmed with the mixture of the petal-shaped silica-gypsum composite and titanium oxide as in Example 6. Note that No. 1 in Table 8 is a comparative example in which no filler was used.

【表】 比較例 1 填料として、市販されているカオリン〔大盛産
業(有)製の商品名特―S 粒径10μ以下87重量
%〕、タルク(日本タルク社製 平均粒径9〜
10μ)、酸化チタン〔石原産業(株)製 商品名 タ
イペークW―10 粒径0.15〜0.25μ〕及びホワイ
トカーボン〔徳山曹達(株)製 商品名 トクシール
GU―N 単粒子径15〜25mμ〕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―9に示す。 表―9から明らかな如くホワイトカーボンを用
いた紙は細孔径7.5μ以上の細孔容積をコントロー
ルすることが難しく、裏抜け防止にある程度の効
果はあるものの裂断長低下ということで使用に限
界があつた。同様なことが酸化チタンを用いた場
合でも明らかとなつた。 またカオリン、タルクは裂断長低下が少ないも
のの白色度、不透明度、印刷後の白色度が劣るこ
とが確認された。
[Table] Comparative Example 1 As a filler, commercially available kaolin [trade name Toku-S, manufactured by Omori Sangyo Co., Ltd., particle size 10μ or less, 87% by weight], talc (manufactured by Nippon Talc Co., Ltd., average particle size 9 ~
10μ), titanium oxide [manufactured by Ishihara Sangyo Co., Ltd., product name: Taipeke W-10, particle size 0.15-0.25μ], and white carbon [manufactured by Tokuyama Soda Co., Ltd., product name: Tokusil
Paper was made in the same manner as in Example 1, except that GU-N (single particle size: 15 to 25 mμ) was used. The results are shown in Table 9. As is clear from Table 9, it is difficult to control the volume of pores with a pore diameter of 7.5μ or more in paper using white carbon, and although it is somewhat effective in preventing bleed-through, its use is limited due to a decrease in tear length. It was hot. A similar phenomenon was found when titanium oxide was used. Kaolin and talc were also confirmed to have poor whiteness, opacity, and whiteness after printing, although the decrease in tearing length was small.

【表】 比較例 2 填料として参考例5の珪酸カルシウムを実施例
1と同様に粉砕し粒径2〜30μが92重量%で平均
粒径16μである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―10に
示す。 表―10から明らかな如く水に不溶な2酸化珪素
を出発原料とした珪酸カルシウムは前述した理由
から裂断長の低下の著しいことが確認できた。 また細孔径0.75μ以下の細孔容積が実施例1の
花弁状珪カルに比較して少さく、充分な裏抜け防
止効果は期待されないことが判つた。細孔径7.5μ
以上の細孔容積値を細孔径0.75μ以下の細孔容積
値以下にすることが出来ず、本発明を満足する紙
は得られないことが確認された。 尚、表―10のNo.1は填料を用いない場合の比較
例である。
[Table] Comparative Example 2 Same as Example 1, except that the calcium silicate of Reference Example 5 was crushed in the same manner as in Example 1, and the filler had a particle size of 2 to 30μ at 92% by weight and an average particle size of 16μ. The paper was made by performing the following operations. The results are shown in Table 10. As is clear from Table 10, it was confirmed that calcium silicate made from water-insoluble silicon dioxide as a starting material significantly reduced the fracture length for the reasons mentioned above. It was also found that the volume of pores with a pore diameter of 0.75 μm or less was smaller than that of the petal-shaped silica of Example 1, and a sufficient effect of preventing strike-through was not expected. Pore diameter 7.5μ
It was confirmed that the above pore volume value could not be reduced to a pore volume value of 0.75 μm or less in pore diameter, and that paper satisfying the present invention could not be obtained. Note that No. 1 in Table 10 is a comparative example in which no filler was used.

【表】 実施例 8 パルプとして広葉樹のグラウンド・パルプ(予
め叩解機で一定に解綿(シヨツパーフリーネス
25.8゜SR)したもの)を用い、填料として参考例
1で得られた花弁状珪カル(実施例1と同一粒度
分布)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―11に示す。 表―11から明らかな如く、裂断長の低下の少な
く、裏抜け防止された紙を得ることが出来た。こ
の裂断長の低下の割合は比較例―3のタルクと同
様であつた。 尚、表―11のNo.1は填料を用いない場合の比較
例である。
[Table] Example 8 Hardwood ground pulp as pulp (previously defibrated to a constant level with a beater (shotzper freeness)
Paper was made in the same manner as in Example 1, except that the petal-shaped silica obtained in Reference Example 1 (same particle size distribution as Example 1) was used as the filler. The results are shown in Table-11. As is clear from Table 11, it was possible to obtain paper with little decrease in tearing length and in which bleed-through was prevented. The rate of decrease in fracture length was similar to that of talc in Comparative Example-3. Note that No. 1 in Table 11 is a comparative example in which no filler was used.

【表】 比較例 3 パルプとして実施例8で用いたものと同様の広
葉樹のグラウンド・パルプを用い、填料として比
較例1に示したタルクとホワイトカーボンを用い
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―12に示す。 表―12から明らかな如く、裂断長の低下は、比
較例1と同傾向でタルクにおいて少なくホワイト
カーボンにおいて著しいことが確認された。また
裏抜け防止効果は、タルク、ホワイトカーボンと
も少なかつた。
[Table] Comparative Example 3 The same method as in Example 1 was used, except that the same hardwood ground pulp as that used in Example 8 was used as the pulp, and the talc and white carbon shown in Comparative Example 1 were used as fillers. The operation was performed and paper was made. The results are shown in Table-12. As is clear from Table 12, it was confirmed that the decrease in fracture length was in the same trend as Comparative Example 1, less in talc, and more significant in white carbon. In addition, both talc and white carbon had little effect on preventing bleed-through.

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

第1図及び第2図は花弁状珪酸カルシウムの顕
微鏡写真、第3図は花弁状シリカの顕微鏡写真、
第4図は花弁状珪酸カルシウム―石膏複合体の顕
微鏡写真、第5図及び第6図は比較例としての珪
酸カルシウムの顕微鏡写真である。
Figures 1 and 2 are micrographs of petal-shaped calcium silicate, Figure 3 is a micrograph of petal-shaped silica,
FIG. 4 is a micrograph of a petal-shaped calcium silicate-gypsum composite, and FIGS. 5 and 6 are micrographs of calcium silicate as a comparative example.

Claims (1)

【特許請求の範囲】 1 パルプと無機質填料を抄紙することによつて
得られた紙において、 該無機質填料が、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
態を有する珪酸質粒子であり、 得られた紙が、細孔半径0.75ミクロン以下の細
孔容積が、細孔半径7.5ミクロン以上の細孔容積
より大きく、且つ、細孔半径0.75ミクロン以下の
細孔容積が0.1c.c./g以上であることを特徴とす
る紙。
[Claims] 1. Paper obtained by paper-making pulp and inorganic filler, wherein the inorganic filler has an aggregate form of flakes with an average diameter of 0.1 to 30 microns and a thickness of 0.005 to 0.1 micron. The resulting paper has a pore volume with a pore radius of 0.75 microns or less that is larger than a pore volume with a pore radius of 7.5 microns or more, and a pore volume with a pore radius of 0.75 microns or less. 0.1cc/g or more.
JP8201579A 1979-06-30 1979-06-30 Filler used in producing paper Granted JPS569499A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8201579A JPS569499A (en) 1979-06-30 1979-06-30 Filler used in producing paper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8201579A JPS569499A (en) 1979-06-30 1979-06-30 Filler used in producing paper

Publications (2)

Publication Number Publication Date
JPS569499A JPS569499A (en) 1981-01-30
JPS6311478B2 true JPS6311478B2 (en) 1988-03-14

Family

ID=13762686

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8201579A Granted JPS569499A (en) 1979-06-30 1979-06-30 Filler used in producing paper

Country Status (1)

Country Link
JP (1) JPS569499A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60500264A (en) * 1982-12-30 1985-02-28 ルユヒトラ−ト,ベルン Filler for paper or cardboard-like material and method for producing the same
JPS6399397A (en) * 1987-06-12 1988-04-30 株式会社トクヤマ Filler for paper
CA1251603A (en) * 1988-03-18 1989-03-28 Roger A. Crawford Saturating grade paper
JPH0796759B2 (en) * 1991-06-14 1995-10-18 日本インシュレーション株式会社 paper
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 (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS548632A (en) * 1977-06-23 1979-01-23 Shiraishi Kogyo Kaisha Ltd Calcium carbonate pigment and method of making same
JPS5450605A (en) * 1977-09-29 1979-04-20 Honshu Paper Co Ltd Paper making method

Also Published As

Publication number Publication date
JPS569499A (en) 1981-01-30

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