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JP2001131893A - Laminated photocatalyst pulp paper, its manufacturing method and defibrator used in the process, paper string comprising laminated photocatalyst pulp paper and its manufacturing method, and formed article comprising the paper string - Google Patents

Laminated photocatalyst pulp paper, its manufacturing method and defibrator used in the process, paper string comprising laminated photocatalyst pulp paper and its manufacturing method, and formed article comprising the paper string

Info

Publication number
JP2001131893A
JP2001131893A JP2000182179A JP2000182179A JP2001131893A JP 2001131893 A JP2001131893 A JP 2001131893A JP 2000182179 A JP2000182179 A JP 2000182179A JP 2000182179 A JP2000182179 A JP 2000182179A JP 2001131893 A JP2001131893 A JP 2001131893A
Authority
JP
Japan
Prior art keywords
pulp
paper
laminated
titanium oxide
photocatalytic
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.)
Granted
Application number
JP2000182179A
Other languages
Japanese (ja)
Other versions
JP4634573B2 (en
Inventor
Sadao Nishibori
貞夫 西堀
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.)
AIN KOSAN KK
Original Assignee
AIN KOSAN KK
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 AIN KOSAN KK filed Critical AIN KOSAN KK
Priority to JP2000182179A priority Critical patent/JP4634573B2/en
Priority to NO20005869A priority patent/NO20005869L/en
Priority to CA 2326608 priority patent/CA2326608A1/en
Priority to DE2000609471 priority patent/DE60009471T2/en
Priority to EP20000125713 priority patent/EP1164221B1/en
Priority to KR1020000069839A priority patent/KR100627437B1/en
Priority to ES00125713T priority patent/ES2216804T3/en
Priority to AT00125713T priority patent/ATE263279T1/en
Priority to CNB001346288A priority patent/CN1318698C/en
Priority to TW89125081A priority patent/TW546434B/en
Priority to US09/718,375 priority patent/US6673207B1/en
Priority to BR0005963A priority patent/BR0005963A/en
Priority to MXPA00011630 priority patent/MXPA00011630A/en
Publication of JP2001131893A publication Critical patent/JP2001131893A/en
Priority to HK02104230.0A priority patent/HK1042930B/en
Priority to US10/749,413 priority patent/US20040140071A1/en
Application granted granted Critical
Publication of JP4634573B2 publication Critical patent/JP4634573B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
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Abstract

PROBLEM TO BE SOLVED: To obtain a laminated photocatalyst pulp paper having an antibacterial effect, a decomposition effect on offensive odor and an oxidative decomposition effect on toxic substances, widely useful for filters, packaging materials, construction materials, or the like, and effective in using for atmospheric treatment, water treatment, soil treatment and capable of increasing the photocatalytic effect of titanium oxide itself. SOLUTION: The laminated photocatalyst pulp paper comprises a photocatalyst composition comprising 5-60 wt.% of titanium oxide compounded with 40-95 wt.% of pulp and/or paper having <=3 wt.% water content, 5-300 μm of an average fiber diameter and 0.1-70 mm of an average fiber length, laminated with waste paper pulp, and a paper string comprising the pulp paper is produced.

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、パルプ及び/又は
紙及び古紙、好ましくは新聞古紙を主たる成形素材とし
た光触媒活性効果を有する積層光触媒パルプ紙及びその
製造方法に関し、より詳しくは、新聞古紙のリサイクル
を考慮して、パルプ及び/又は紙に酸化チタンを吸着さ
せた後、好ましくはDIP工程を経た新聞古紙を例えば抄
紙工程において積層し、あるいは、別途乾燥し、古紙回
収紙としたものを接着剤を介して積層して酸化チタンの
光触媒性、すなわち、脱臭、抗菌など、紫外線により活
性化され、有機物、アンモニア、N0x,S0xなどを酸化分
解する性質を向上ないし有効に発揮させることのできる
脱臭、抗菌性を有する濾材、障子、襖用紙、壁紙、ブラ
インド、パネル、ランプシェード、シーツ、カーテン、
カーペット、ソファー、シートの素材など家具、建材そ
して一般の包装材料、そしてフレキシブル複合包装材
料、並びに防黴など特殊包装材料、自動車の内装材、家
庭電気製品の表装材等、また、その他の日用品などを始
めとする各種成形品の原料および製品、そしてフィル
ム、シート、接着剤もしくは接着樹脂層、多様なコーテ
ィング材もしくはコーティング樹脂膜、あるいは塗料も
しくは塗装樹脂膜として各種用途に広く適応できる光触
媒活性効果を有する積層光触媒パルプ紙を提供するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a laminated photocatalytic pulp paper having a photocatalytic activity effect using pulp and / or paper and waste paper, preferably newspaper waste paper as a main molding material, and a method for producing the same. Considering the recycling of paper, after adsorbing titanium oxide on pulp and / or paper, it is preferable to laminate newspaper waste paper that has passed through the DIP process, for example, in the paper making process, or dry it separately to obtain recycled paper. Photocatalytic properties of titanium oxide when laminated via an adhesive, that is, activated by ultraviolet rays, such as deodorization and antibacterial, can improve or effectively exhibit the property of oxidatively decomposing organic substances, ammonia, NOx, SOx, etc. Deodorizing and antibacterial filter media, shoji, sliding paper, wallpaper, blinds, panels, lamp shades, sheets, curtains,
Furniture, building materials and general packaging materials such as carpets, sofas and seats, flexible composite packaging materials, special packaging materials such as fungicides, car interior materials, household electrical products surface materials, and other daily necessities And photo-catalytic activity that can be widely applied to various uses as films, sheets, adhesives or adhesive resin layers, various coating materials or coating resin films, or paint or coating resin films. And a laminated photocatalytic pulp paper having the same.

【0002】又、本発明は、前記積層光触媒パルプ紙の
新たな用途開発係るもので、脱臭、抗菌性を有する包装
材料並びにマット、籠、簾、暖簾、帽子などを始めとす
るその他の日用品、及び衣料品、ペットの糞尿より発生
する悪臭処理のより効率の良い抗菌・消臭機能を持ち水
洗トイレに流せる水溶性のペット砂、その他各種成形品
又は材料としての前記積層光触媒パルプ紙から成る紙紐
およびこの紙紐から成る成形体を提供するものである。
The present invention also relates to the development of a new use of the laminated photocatalytic pulp paper. The present invention relates to a packaging material having deodorizing and antibacterial properties and other daily necessities such as mats, baskets, screens, curtains, hats, and the like. Water-soluble pet sand that has an antibacterial and deodorizing function that is more efficient in treating odors generated from clothing and manure of pets and that can be poured into flush toilets, and paper made of the laminated photocatalytic pulp paper as various molded articles or materials It is intended to provide a cord and a molded article made of the paper cord.

【0003】[0003]

【従来の技術】従来から、この種酸化チタンは、脱臭フ
ィルターとして使用され、また、コーティング剤として
提供されており、対象物へ塗布乾燥して被膜を形成し、
表面の防汚効果、抗菌効果を得るために用いられてい
る。また、これまで、光触媒活性効果を有する紙紐は提
供されていない。
2. Description of the Related Art Conventionally, this kind of titanium oxide has been used as a deodorizing filter, and has been provided as a coating agent.
It is used to obtain antifouling and antibacterial effects on the surface. Further, a paper cord having a photocatalytic activity effect has not been provided so far.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、これら
の従来品は、コーティングしたものあるいは、繊維と繊
維との間隙に侵入固定したものにあっては反応速度も遅
く、また、反応の終了が著しく遅いとう不利な結果をも
たらすものであった。
However, these conventional products have a slow reaction speed when coated or fixed in a space between fibers, and the completion of the reaction is extremely slow. It had a negative consequence.

【0005】本発明は、前記問題点を解消し、包装材
料、建材、濾材など各種広範な用途の抗菌、抗徽、防汚
(汚れの)及び悪臭の分解、脱臭処理、有害物質の酸化分
解効果を有する積層光触媒パルプ紙及びその製造方法を
提供することを目的とする。
[0005] The present invention solves the above problems and provides antibacterial, antifouling, and antifouling materials for a wide variety of uses such as packaging materials, building materials, and filter media.
It is an object of the present invention to provide a laminated photocatalytic pulp paper having an effect of decomposing (soil) and malodor, deodorizing treatment, and oxidative decomposition of harmful substances, and a method for producing the same.

【0006】また、本発明は、引張り強さなどの包装資
材としての物性を保持し、前記各種用途に適合する包装
材料として、あるいは各種成形品の素材としての紙紐及
び成形体を提供しようとするものである。
Another object of the present invention is to provide a paper cord and a molded article which retain physical properties as a packaging material such as tensile strength and are suitable for the above-mentioned various uses or as a raw material of various molded articles. Is what you do.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、本発明の積層光触媒パルプ紙は、酸化チタン5〜60w
t%に、含有水分量を3wt%以内とし平均繊維径5〜300μ
m、平均繊維長0.1〜70mmのパルプ及び/又は紙40〜95wt
%の割合で配合して成る配合物としての光触媒パルプ組
成物に対してバージンパルプ又は古紙パルプを積層して
成ることを特徴とする。
In order to achieve the above object, the laminated photocatalytic pulp paper of the present invention comprises titanium oxide 5 to 60 watts.
t%, moisture content within 3 wt% and average fiber diameter 5 ~ 300μ
m, pulp and / or paper 40-95wt with average fiber length 0.1-70mm
% Of a virgin pulp or a waste paper pulp on a photocatalytic pulp composition as a composition prepared by blending at a ratio of 0.1%.

【0008】又、前記酸化チタンと、パルプ及び/又は
紙の合計重量に対して25〜100wt%の熱可塑性樹脂を配合
し、前記配合物に対してバージンパルプ又は古紙パルプ
を積層したものとすることができる。
In addition, the titanium oxide and 25 to 100% by weight of a thermoplastic resin based on the total weight of pulp and / or paper are blended, and virgin pulp or waste paper pulp is laminated on the blend. be able to.

【0009】前記積層光触媒パルプ紙の製造方法は、酸
化チタン5〜60wt%に、平均繊維径5〜300μm、平均繊維
長0.1〜70mmに解繊離解したパルプ及び/又は紙40〜95w
t%の割合で配合して成る光触媒パルプ組成物に対して撹
拌衝撃力を付加して撹拌して、前記撹拌衝撃力に基づく
剪断力により剪断発熱を生じさせ、この剪断発熱により
前記配合物を乾燥し含有水分量を3wt%以内に低下せしめ
る工程と、前記パルプ及び/又は紙を前記乾燥に伴い膨
潤し、三次元繊維絡合体とする工程と、前記撹拌衝撃力
により、前記酸化チタンを前記パルプ及び/又は紙の繊
維表面に押し付け固定化する処理工程と、該酸化チタン
を押し付け固定化する処理工程後の抄紙工程においてバ
ージンパルプ又は古紙パルプを積層して成ることを特徴
とする。
The method for producing the laminated photocatalytic pulp paper is as follows: Pulp and / or paper defibrated and defibrated to 5 to 60% by weight of titanium oxide to an average fiber diameter of 5 to 300 μm and an average fiber length of 0.1 to 70 mm.
The photocatalytic pulp composition, which is blended at a ratio of t%, is stirred by applying a stirring impact force to generate shear heat by a shearing force based on the stirring impact force, and the shear heat is applied to the composition to generate the shear heat. Drying to reduce the water content to 3 wt% or less, swelling the pulp and / or paper with the drying to form a three-dimensional fiber entangled body, and stirring the titanium oxide by the stirring impact force. Virgin pulp or waste paper pulp is laminated in a papermaking process after the treatment process of pressing and fixing the pulp and / or paper on the fiber surface and the papermaking process after the treatment process of pressing and fixing the titanium oxide.

【0010】また、前記製造工程において、前記酸化チ
タン、パルプ及び/又は紙の合計重量に対して25〜100w
t%の熱可塑性樹脂を配合することができる。
In the above-mentioned manufacturing process, the total weight of the titanium oxide, pulp and / or paper is 25 to 100 watts.
t% thermoplastic resin can be blended.

【0011】前記古紙パルプがDIP工程を経た新聞古紙
から成るものとすれば、新聞古紙の再利用に好適であ
り、この古紙パルプを芯材あるいは基材として積層して
用いることができる。
If the used paper pulp is made of used newspaper used in the DIP process, it is suitable for reuse of used newspaper. This used pulp can be used as a core material or a base material.

【0012】さらに、前記酸化チタン5〜60wt%及びパル
プ及び/又は紙40〜95wt%に対して平均繊維長1〜100m
m、平均径10〜40μm、融点120℃以上の合成繊維を最大
1:9の割合で配合することができる。
Further, the average fiber length is 1 to 100 m with respect to the titanium oxide of 5 to 60 wt% and the pulp and / or paper of 40 to 95 wt%.
m, average diameter 10 ~ 40μm, synthetic fiber with melting point 120 ° C or higher
It can be blended at a ratio of 1: 9.

【0013】光触媒パルプ組成物としての前記原料パル
プが板紙状の乾式パルプのときは、該乾式パルプを複数
の被処理小片に細断して形成された個々の被処理小片に
対して衝撃摩砕力を付加して摩砕され綿状に凝集した繊
維状の原料パルプと略同様の長さと、前記摩砕によって
も繊毛の生じていないパルプ繊維とする解繊離解工程3
03を含む。
When the raw material pulp as the photocatalytic pulp composition is a paperboard dry pulp, the dry pulp is shattered into a plurality of small pieces to be subjected to impact milling. Fibrillation and disintegration step 3 which is substantially the same length as the fibrous raw material pulp which has been milled by applying force and flocculated into floc, and which has no cilia even after the above-mentioned milling.
03 is included.

【0014】また、上記乾式パルプの解繊離解装置は、
板状の乾式パルプを処理対象とし、複数に細断された被
処理小片の供給投入口132に中心部を連通した固定円
盤131上にあって、複数の回転軌跡上で各固定ピン1
34を順次に植設した固定側衝撃摩砕手段と、前記固定
円盤131に対向して回転駆動可能に設けた可動円盤1
41上にあって、前記各固定ピン134とは異なる複数
の回転軌跡上で各可動ピン144を順次植設した可動側
衝撃摩砕手段と、好ましくは、異物を排除するため、前
記各固定ピン134と各可動ピン144との組み合せ外
周部にあって、所定径の細孔が穿設されたスクリーン1
51を介して排出口に連通した回収手段を備え、さら
に、前記スクリーン151内に残留する、摩砕され綿状
に凝集した繊維状のパルプ繊維84となった被処理小片を
取出口に取出す取出し手段とを備える。
Further, the above-mentioned dry pulp defibration and defibration apparatus comprises:
A plate-shaped dry pulp is to be processed, and is located on a fixed disk 131 having a central portion communicating with a supply inlet 132 for small pieces to be processed which are to be processed.
And a movable disk 1 provided so as to be rotatable and opposed to the fixed disk 131.
41, a movable-side impact grinding means in which the movable pins 144 are sequentially implanted on a plurality of rotation trajectories different from the fixed pins 134, and preferably, the fixed pins 134 for removing foreign matter. A screen 1 having a hole of a predetermined diameter in the outer peripheral portion of the combination of the movable pin 134 and the movable pin 144
A collecting means communicating with the discharge port through the discharge port 51; and removing the treated small pieces remaining in the screen 151 into the pulp fibers 84 in the form of the crushed and flocculent fibrous fibers. Means.

【0015】このようにして回収されたパルプ繊維84
は、次工程の酸化チタンの固定化処理工程に移送され
る。
The pulp fibers 84 thus recovered
Is transferred to the next step of titanium oxide fixing.

【0016】さらに、本発明にかかる積層光触媒パルプ
紙から成る紙紐は、5〜50mmの任意幅に切断して成る前
記積層光触媒パルプ紙、好ましくは坪量約20〜80g/m2
撚糸して成ることを特徴とする。包装材料等としての用
途の他、直径約 2〜5mm、長さ約5〜30mmに切断し、ペッ
トの糞尿処理としてのペットの糞尿より発生する悪臭処
理のより効率の良い抗菌・消臭機能を持ち水洗トイレに
流せる水溶性のペット砂として使用できる。
Further, the paper string made of the laminated photocatalytic pulp paper according to the present invention is obtained by twisting the laminated photocatalytic pulp paper, preferably having a basis weight of about 20 to 80 g / m 2, which is cut to an arbitrary width of 5 to 50 mm. It is characterized by comprising. In addition to its use as a packaging material, etc., it is cut to a diameter of about 2 to 5 mm and a length of about 5 to 30 mm to provide a more efficient antibacterial and deodorant function for the treatment of foul odors generated from pet manure as pet manure processing. Can be used as water-soluble pet sand that can be flushed into flush toilets.

【0017】製造方法としては、前記積層光触媒パルプ
紙を幅5〜50mmに切断し、ロール状に巻き取った後、例
えば15〜30回転程度、撚糸することを特徴とする。
The production method is characterized in that the laminated photocatalytic pulp paper is cut into a width of 5 to 50 mm, wound up in a roll shape, and then twisted, for example, for about 15 to 30 rotations.

【0018】また、前記紙紐を同一平面上において、複
数本例えば10〜40本重畳して、例えば水溶性接着剤に浸
漬・乾燥する工程を3回程度繰り返し、サンディングに
より前記接着剤層を除去して、ベルト状の平紐を成形す
ることができる。
In addition, the process of superposing a plurality of, for example, 10 to 40, of the paper cords on the same plane and immersing and drying the same in a water-soluble adhesive is repeated about three times, and the adhesive layer is removed by sanding. Thus, a belt-shaped flat cord can be formed.

【0019】また、前記紙紐を横糸とし、縦糸を綿糸な
ど天然繊維又はレーヨンなど化学繊維から成る糸として
織物を製造でき、さらに、前記紙紐、平紐あるいは、織
物を組み合わせて広汎な用途に対応することができる。
Also, a woven fabric can be manufactured by using the paper cord as the weft yarn and the warp yarn as a yarn made of natural fiber such as cotton yarn or chemical fiber such as rayon. Further, the paper cord, flat cord or woven fabric can be combined to meet a wide range of applications. can do.

【0020】[0020]

【発明の実施の形態】〔被積層材料の光触媒パルプ組成
物:実施例(1)〕本例では、原材料として用いるパル
プ及び/又は紙は製紙工程でのいわゆるバージンパルプ
のみでなく、古紙パルプあるいは例えば1:1で両者を
混合したパルプを含み、又、上記紙は、普通紙あるいは
広く新聞古紙などの古紙を含む。10mm× l0mmスクリー
ンを有するカッターミルで破砕してから処理し、また、
印刷インクを多量に含有する古紙は、後述積層される古
紙と同様製紙工程においてDIP処理など漂白あるいは着
色することが好ましい。
DESCRIPTION OF THE PREFERRED EMBODIMENTS [Photocatalytic pulp composition of material to be laminated: Example (1)] In this example, the pulp and / or paper used as a raw material is not only virgin pulp in the papermaking process but also waste paper pulp or For example, it contains pulp in which both are mixed at a ratio of 1: 1, and the paper includes waste paper such as plain paper or widely used newspaper. After crushing with a cutter mill having a 10 mm × 10 mm screen,
Used paper containing a large amount of printing ink is preferably bleached or colored by DIP treatment or the like in the paper making process similarly to used paper to be laminated later.

【0021】そして、平均繊維径5〜300μmm、平均繊維
長0.1〜70mmで嵩比重が0.005〜0.04、バージンパルプ及
び/又は紙で0.24のものが80wt%(このときのパルプ及び
/又は紙は水分を約8wt%含む)および酸化チタンを20wt%
配合してなる。
Then, 80% by weight of virgin pulp and / or paper having an average fiber diameter of 5 to 300 μmm, an average fiber length of 0.1 to 70 mm, a bulk specific gravity of 0.005 to 0.04, and 0.24 of virgin pulp and / or paper (the pulp and / or paper About 8 wt%) and 20 wt% titanium oxide
It is compounded.

【0022】なお、前記パルプ及び/又は紙の平均繊維
径5〜300μm、平均繊維長0.1〜70mmとは、当該パルプ及
び/又は紙の累積重量パーセント分布の50重量パーセン
トの粒子径を意味する。
The average fiber diameter of the pulp and / or paper of 5 to 300 μm and the average fiber length of 0.1 to 70 mm mean a particle diameter of 50% by weight in the cumulative weight percentage distribution of the pulp and / or paper.

【0023】紙では、クラッシャなどにより好ましくは
10mmメッシュのスクリーンをパスした粉砕処理をしたも
のを用いる。
In the case of paper, it is preferable to use a crusher or the like.
Use what has been crushed through a 10 mm mesh screen.

【0024】また、古紙における印刷インクは、製品に
若干の色彩が付着している以外には処理の上で問題はな
い。
The printing ink on the used paper has no problem in processing, except that a slight color is attached to the product.

【0025】板紙状の乾式パルプを処理対象とする場
合、該乾式パルプを複数の被処理小片に細断して形成さ
れた個々の被処理小片に対して衝撃摩砕力を付加して上
記パルプと同様、摩砕され綿状に凝集した繊維状の原料
パルプと略同様の長さと、前記摩砕によっても繊毛の生
じていないパルプ繊維とする解繊離解工程303を経た
ものを用いる。
When the dry pulp in the form of paperboard is to be treated, the dry pulp is subjected to an impact milling force on each of the small pieces to be treated formed by chopping the dry pulp into a plurality of small pieces to be treated. In the same manner as described above, a pulp fiber which is substantially the same length as the fibrous raw material pulp which has been ground and flocculently flocculated and which has undergone the fibrillation / disintegration step 303 to be a pulp fiber having no cilia even after the grinding is used.

【0026】本工程に使用される衝撃摩砕手段は本実施
例において便宜上「セパレータ」という。
The impact grinding means used in this step is referred to as a "separator" in this embodiment for convenience.

【0027】図3〜図6において、セパレータ130
は、固定円盤131の中心部に各被処理小片を投入する
供給投入口132を連通開口させ、前記固定円盤131
に固定端板133を処理空間155を隔てて対向させ、
前記固定円盤131に固定端板133のそれぞれの外周
端縁を周側板135で固定する。前記処理空間155内
には回転横軸142によって回転駆動される可動円盤1
41を設け、回転横軸142は各軸受143,143に
よって枢支されている。前記回転横軸142は、モータ
等の回転駆動手段により回転駆動される。そして、前記
固定円盤131上には、複数の、本実施例では6の同心
円上の(可動円板141に対する相対的な)回転軌跡a1
〜a6(図5)上で各固定ピン134を、この実施例で
は、各固定ピン134は前記固定円盤131上の中心か
ら前記同心円上に外周縁に向かって、16-24-32-36-40-4
2本、順次植設され、一方、前記可動円盤141上に
は、前記各固定ピン134とは異なる複数の本実施例で
は6の回転軌跡b1〜b6上で交互に人り込む、可動ピ
ン144を、前記可動円盤141上の中心から前記同心
円上に外周縁に向かって、4-4-4-4-4-6本、順次植設し
て、これらの固定、可動の各ピン134,144の相互
間で衝撃摩砕力により上記解繊離解作用を得られるよう
に位置する。
3 to 6, the separator 130
A communication opening is formed at a central portion of the fixed disk 131 with a supply inlet 132 for inputting each of the small pieces to be processed.
The fixed end plate 133 is opposed to the processing space 155,
The outer peripheral edge of each fixed end plate 133 is fixed to the fixed disk 131 by a peripheral side plate 135. In the processing space 155, the movable disk 1 that is rotationally driven by the rotating horizontal shaft 142
41, and the rotating horizontal shaft 142 is pivotally supported by the bearings 143, 143. The rotation horizontal shaft 142 is rotationally driven by a rotation driving means such as a motor. On the fixed disk 131, a plurality of, in this embodiment, six concentric rotation trajectories a1 (relative to the movable disk 141)
A6 (FIG. 5). In this embodiment, each fixing pin 134 is moved from the center on the fixed disk 131 toward the outer peripheral edge on the concentric circle 16-16-32-36-. 40-4
On the other hand, two movable pins 144 are implanted on the movable disk 141 alternately on a plurality of rotation trajectories b1 to b6 in the present embodiment, which are different from the fixed pins 134. 4-4-4-4-4-6 pieces are sequentially planted from the center on the movable disk 141 toward the outer peripheral edge on the concentric circle, and these fixed and movable pins 134 and 144 are sequentially implanted. Are positioned so that the above-described defibrating and disintegrating action can be obtained by the impact grinding force.

【0028】さらに、可動円盤141の外周側で前記周
側板135との間には、排出空間156を隔てて所望径
の細孔をパンチング形成した所定メッシュのスクリーン
151を周設させ、排出空間156の下方に排出口15
2を設ける。なお、前記排出口152に図6に示すよう
にセパレータ130にブロワー157を連通する。
Further, a screen 151 having a predetermined mesh formed by punching pores having a desired diameter is provided around the outer peripheral side of the movable disk 141 and the peripheral side plate 135 with a discharge space 156 therebetween. Outlet 15 below
2 is provided. A blower 157 is connected to the separator 130 as shown in FIG.

【0029】そして、排出口152をブロワー157を
設けた排出管239を介して回収タンク250に連通す
る。
Then, the discharge port 152 is connected to the collection tank 250 via a discharge pipe 239 provided with a blower 157.

【0030】なお、前記スクリーン151は、後述可動
ピンの回転数にもよるが、直径約0.8mm〜2.0mmが用いら
れる。さらに、処理空間155のスクリーン151内の
下部に取出口153を形成する(図3)。前記固定、可動
の各ピン134,144の相互間のクリアランスを大き
くすることにより被処理小片に付加する摩砕力を弱め、
クリアランスを小さくすることにより摩砕力を強めるこ
とになる。なお、前記取出口153に、図6に示すよう
に、セパレータ130内のエアーを吸引するブロワー1
57を連通し、このブロワー157を介して供給投入口
132へ連通してもよい。
The screen 151 has a diameter of about 0.8 mm to 2.0 mm, depending on the number of rotations of a movable pin to be described later. Further, an outlet 153 is formed below the screen 151 in the processing space 155 (FIG. 3). By increasing the clearance between the fixed and movable pins 134 and 144, the grinding force applied to the small pieces to be processed is reduced,
By reducing the clearance, the grinding power is increased. As shown in FIG. 6, the blower 1 for sucking air in the separator 130 is provided in the outlet 153.
57 may be connected to the supply inlet 132 via the blower 157.

【0031】また、図3および図6に示すように、取出
口153と処理空間155を連通管235を介して連通
し、取出口153から処理空間155に環流する図示せ
ざる圧縮空気供給源からの圧縮空気を配管236を介し
て連通管235に導入し、取出口153より排出された
摩砕されたパルプ繊維及び異物を再度セパレータ130
内の処理空間155内に環流するように構成することも
できる。
As shown in FIGS. 3 and 6, the outlet 153 and the processing space 155 communicate with each other through a communication pipe 235, and a compressed air supply source (not shown) circulating from the outlet 153 to the processing space 155. Is introduced into the communication pipe 235 through the pipe 236, and the milled pulp fibers and foreign matter discharged from the outlet 153 are again separated by the separator 130.
It can also be configured to recirculate in the processing space 155 in the inside.

【0032】また、前記連通管235の供給投入口側を
分岐して前記パルプ繊維、又はパルプ繊維及び異物の回
収タンク240へ連通する分岐管237を設け、この分
岐管237の分岐点に、例えばタイマ回路により適宜設
定時間毎に切り替えられる二方電磁弁238を設け、前
記連通管235の下流側を電磁弁で閉塞し且つ前記分岐
管237側を開放し、スクリーン151内に残されたパ
ルプ繊維を吸引し分岐管237を介して回収タンク24
0内に回収する。あるいは、前記分岐管237を開閉す
る電磁弁と前記連通管235の下流側を開閉する電磁弁
を設け、これらの二の電磁弁を交互に開閉するように設
けることもできる(図6)。
A branch pipe 237 for branching the supply inlet side of the communication pipe 235 and communicating with the pulp fiber or the pulp fiber and foreign matter recovery tank 240 is provided. A two-way solenoid valve 238 that can be switched at appropriate intervals by a timer circuit is provided, the downstream side of the communication pipe 235 is closed with a solenoid valve and the branch pipe 237 side is opened, and the pulp fiber remaining in the screen 151 To the collection tank 24 via the branch pipe 237.
Collect within 0. Alternatively, an electromagnetic valve for opening and closing the branch pipe 237 and an electromagnetic valve for opening and closing the downstream side of the communication pipe 235 may be provided, and these two electromagnetic valves may be alternately opened and closed (FIG. 6).

【0033】モータ等の回転駆動手段により回転横軸1
42を回転して可動円盤141を回転し、各被処理小片
を供給投入口132に供給すると、各被処理小片は、処
理空間155の中心部にあって、固定、可動の各ピンl
34,144の相互間で衝撃摩砕力により前記被処理小
片は、より細かにほぐされて繊維状となり、一方、異物
は前記衝撃摩砕力により不定型ではあるが直径が約2〜6
mm程度となる。すなわち、各被処理小片が固定、可動
の各ピン134,144による衝撃で叩かれて細かく破
砕ないし粉砕され、各被処理小片に折り曲げ作用が繰り
返し加わるために細かく粉砕した板紙が被処理小片から
分離される。このようにして、被処理小片を構成するパ
ルプ繊維及び異物が、その種類毎にそれぞれ分離され、
板紙は繊維状にほぐされ、異物は薄片状にそれぞれ摩砕
される。この間、可動円盤141の回転による遠心力、
ブロワー157による吸引又は配管236を介して処理
空間155内に供給される圧縮空気により生ずる気流に
より、次第に前記分離され、繊維状にされた紙層とパル
プ繊維又は繊維状にされた紙層及び若干の異物が混在し
た状態でスクリーンl51の周設されたセパレータ13
0の外周側に接近する。その後、繊維状にされたパルプ
が直径約0.8〜2mmのメッシュに形成されたスクリーン1
51を通過して、排出空間156内に排出された後、排
出口152からブロワーl57を経て外部へ吸引され、
排出管239を介して回収タンク250内に回収され
る。一方、薄片状の異物や若干の綿状に凝集された形態
のパルプ繊維はスクリーン151を通過することができ
ず、処理室内部に残留する。前記パルプ繊維の回収が終
了すると、処理空間155内部に残留した異物を取出口
153から外部へ排出する。
The rotating horizontal shaft 1 is driven by a rotating drive means such as a motor.
When the movable disk 141 is rotated by rotating the movable disk 141 and each of the small pieces to be processed is supplied to the supply inlet 132, each small piece to be processed is located at the center of the processing space 155 and each of the fixed and movable pins
Due to the impact attrition force between the particles 34 and 144, the small pieces to be treated are more finely loosened into fibrous shapes, while the foreign substances are irregular in shape due to the impact attrition force but have a diameter of about 2 to 6 mm.
mm. That is, each piece to be treated is beaten by the impact of each of the fixed and movable pins 134 and 144 to be finely crushed or crushed, and the finely crushed paperboard is separated from the piece to be treated because the folding action is repeatedly applied to each piece to be treated. Is done. In this way, the pulp fibers and foreign substances constituting the small pieces to be treated are separated for each type,
The paperboard is unraveled into fibrous forms, and the foreign matter is ground into flakes. During this time, the centrifugal force due to the rotation of the movable disc 141,
The separated and fibrous paper layer and the pulp fiber or fibrous paper layer are gradually removed by suction by the blower 157 or an air current generated by compressed air supplied into the processing space 155 via the pipe 236. The separator 13 provided around the screen l51 in a state in which
0 approaching the outer circumference. Then, the screen 1 in which the fibrous pulp is formed into a mesh having a diameter of about 0.8 to 2 mm
After passing through the discharge space 156 and being discharged into the discharge space 156, the air is sucked from the discharge port 152 to the outside through the blower 157,
It is collected in the collection tank 250 via the discharge pipe 239. On the other hand, flaky foreign matter and pulp fibers in a slightly flocculated form cannot pass through the screen 151 and remain inside the processing chamber. When the collection of the pulp fiber is completed, the foreign matter remaining in the processing space 155 is discharged from the outlet 153 to the outside.

【0034】この排出された異物は、前記連通管23の
供給投入口側を分岐した前記パルプ繊維等の回収タンク
240へ連通する分岐管237の二方電磁弁238によ
り、前記連通管235の下流側を電磁弁で閉塞し且つ前
記分岐管237側を開放して、スクリーン151内に残
された異物を吸引し分岐管237を介して回収タンク2
40内に回収される。
The discharged foreign matter is transferred downstream of the communication pipe 235 by a two-way solenoid valve 238 of a branch pipe 237 that communicates with a recovery tank 240 of the pulp fiber or the like branched from the supply inlet side of the communication pipe 23. Side is closed by a solenoid valve and the side of the branch pipe 237 is opened, foreign matter left in the screen 151 is sucked, and the collection tank 2 is sucked through the branch pipe 237.
Collected in 40.

【0035】図3においては、分岐管237への連通管
235の連結は、連通管235の上流側、取り出し口1
53側を(図3紙面後方に)分岐した配管に設けたフラ
ンジ154を介して行っている。
In FIG. 3, the connection of the communication pipe 235 to the branch pipe 237 is performed on the upstream side of the communication pipe 235, at the outlet 1
This is through a flange 154 provided on a pipe branching off the 53 side (to the rear in FIG. 3).

【0036】このようにして回収されたパルプ繊維84
は、次工程に移送される。 酸化チタンは、粒径は、小
さいほど能力がよいが、例えばX線粒径7〜50 nmを用い
ることができる。
The pulp fiber 84 thus recovered
Is transferred to the next step. The smaller the particle size of titanium oxide, the better the performance. For example, an X-ray particle size of 7 to 50 nm can be used.

【0037】前記パルプ及び/又は紙及び酸化チタン、
又はこれらと共に合成繊維を投入し、ミキサー内で高速
回転する攪拌衝撃翼による攪拌衝撃力に基づく剪断力に
より剪断発熱を生じさせ、温度約120℃に上昇させ、酸
化チタンおよびパルプ及び/又は紙の水分含有量を3wt%
好ましくは、1wt%以下とする。この工程で、パルプ及び
/又は紙から水分が蒸発し、乾燥すると共に、前記パル
プ及び/又は紙は、紙の場合には前記衝撃力により粉砕
作用を受け繊維状となり、さらに前記乾燥に伴い膨潤
し、繊維を毛羽ただせ、解綿状に凝集し、三次元繊維絡
合体とした上でこの繊維表面及び繊維内にも酸化チタン
を前記撹拌衝撃翼による撹拌衝撃力ないし剪断力に伴う
押し付け外力によって付着、浸入固定させる。
The pulp and / or paper and titanium oxide,
Alternatively, synthetic fibers are charged together with them, and shear heat is generated by shearing force based on the stirring impact force of the stirring impact blade rotating at high speed in the mixer, the temperature is increased to about 120 ° C., and titanium oxide and pulp and / or paper 3wt% moisture content
Preferably, it is 1 wt% or less. In this step, moisture evaporates from the pulp and / or paper and dries, and in the case of paper, the pulp and / or paper becomes fibrous due to the pulverizing action by the impact force and further swells with the drying. Then, the fibers are fluffed, agglomerated in a defatted shape, and a three-dimensional fiber entangled body, and titanium oxide is also adhered to the fiber surface and inside the fiber by a pressing external force caused by the stirring impact force or the shearing force by the stirring impeller, Infiltrate and fix.

【0038】合成繊維は、例えば、平均繊維長1〜100m
m、平均径10〜40μm、融点12℃以上のものが好ましい。
The synthetic fiber may have, for example, an average fiber length of 1 to 100 m.
m, an average diameter of 10 to 40 μm, and a melting point of 12 ° C. or higher are preferred.

【0039】なお、バージンパルプは、通常、板状の乾
式パルプのとき、10wt%程度の含水率であるが、これよ
り含水率が高い場合も、酸化チタン混入前に上記ミキサ
ーあるいは、既知のドライヤーにより水分10wt%以下に
予備乾燥が行われることになり、あるいは行うことが好
ましい。
The virgin pulp usually has a water content of about 10% by weight in the case of a plate-shaped dry pulp. However, even when the water content is higher than that, the above-mentioned mixer or a known dryer may be used before mixing the titanium oxide. As a result, predrying is performed or preferably performed to a water content of 10 wt% or less.

【0040】この工程において酸化チタンの付着、固定
が完了し光触媒パルプ組成物を形成する。
In this step, the attachment and fixation of titanium oxide are completed to form a photocatalytic pulp composition.

【0041】この工程で、原材料内のパルプ及び/又は
紙は大きな塊とはならず、個々の繊維が相互に硬く絡み
合ったりせずに解綿状に緩んだ繊維状のままで凝集し、
この意味で三次元繊維絡合体に形成され、この個々のパ
ルプ及び/又は紙がそのパルプ及び/又は紙の繊維単体
の表面全体に酸化チタンを付着した状態に形成され、こ
れらの個々のパルプ及び/又は紙が集合した解綿状の塊
であるため、パルプ及び/又は紙単体間の密着性がなく
塊そのものは嵩比重の高いものである。したがって、こ
の工程により形成された光触媒パルプ組成物は、多様な
既知の製紙工程で製紙可能な光触媒パルプ紙として良好
な材料である。
In this step, the pulp and / or paper in the raw material does not form a large lump, and the individual fibers agglomerate in the form of a loosened fiber without being entangled with each other hard,
In this sense, a three-dimensional fiber entangled body is formed, and the individual pulp and / or paper is formed with titanium oxide attached to the entire surface of the pulp and / or paper fiber alone, and these individual pulp and / or paper are formed. Since the lumps are paper-like lumps in which paper is gathered, there is no adhesion between pulp and / or paper alone, and the lumps themselves have a high bulk density. Therefore, the photocatalytic pulp composition formed by this process is a good material as a photocatalytic pulp paper that can be made in various known papermaking processes.

【0042】上記工程をさらに詳述すると、パルプ及び
/又は紙の水分含有量は、3wt%以下となっているため、
酸化チタンとパルプ及び/又は紙との界面をなくし、パ
ルプ及び/又は紙へ均一な密度で酸化チタンが分散さ
れ、パルプ及び/又は紙へ吸着ないしは、付着しやすく
すると共に完全にパルプ及び/又は紙外周を包囲するか
たちで、混合分散される。
The above process is described in more detail. Since the pulp and / or paper has a water content of 3 wt% or less,
The interface between the titanium oxide and the pulp and / or paper is eliminated, and the titanium oxide is dispersed at a uniform density in the pulp and / or the paper, and the pulp and / or the paper is easily adsorbed or adhered to the pulp and / or the paper. The paper is mixed and dispersed so as to surround the outer periphery of the paper.

【0043】上記のように製造した光触媒パルプ組成物
は、そのままパルプ原料として各種製紙法により紙とし
て成形することができる。
The photocatalytic pulp composition produced as described above can be used as a pulp raw material and formed into paper by various papermaking methods.

【0044】また、プラスチック繊維、あるいは、にか
わ、澱粉、蝋又は、酢酸ビニール、アクリル系の樹脂接
着剤をバインダーとして製紙工程で混入し、光触媒パル
プ紙とする。
Further, photocatalytic pulp paper is obtained by mixing plastic fibers, glue, starch, wax, vinyl acetate, and an acrylic resin adhesive as a binder in a paper making process.

【0045】上記光触媒活性を有するパルプ組成物を用
いて光触媒パルプ紙を製造した。
Using the pulp composition having photocatalytic activity, a photocatalytic pulp paper was produced.

【0046】光触媒パルプ組成物を用いた光触媒パルプ
紙の実施例及び比較例として、酸化チタンは、ST-01(石
原テクノ社)、X線粒径7nm、酸化チタン含有量90wt%以
上、比表面積m/g:300のものを用い前記ミキサー内
(120℃)で高速回転する攪拌衝撃翼による攪拌衝撃
力により処理。
As examples and comparative examples of the photocatalytic pulp paper using the photocatalytic pulp composition, titanium oxide was ST-01 (Ishihara Techno Co., Ltd.), X-ray particle diameter 7 nm, titanium oxide content 90 wt% or more, specific surface area. Treated by a stirring impact force of a stirring impeller that rotates at a high speed in the mixer (120 ° C.) using a m 2 / g: 300.

【0047】〔光触媒パルプ組成物1;実施例1〕 板状乾式パルプ約2.5kgを上記解繊離解工程において処
理 含水率10 wt%、約2.0kgの解綿状パルプを得た。
[Photocatalytic Pulp Composition 1; Example 1] About 2.5 kg of a plate-like dry pulp was treated in the defibration and defibration step to obtain a defibrated pulp having a water content of 10 wt% and a water content of about 2.0 kg.

【0048】これを固定化処理工程において、約2.0kg
の酸化チタンを固定化し、約3.90 kgの光触媒パルプ組
成物を得た(含水率0.5 wt%)。 〔光触媒パルプ組成物2;実施例2〕(図1及び図2) 粉砕紙繊維2kg(80wt%)含水率10wt%:上記解繊離解工程に
おいて処理 酸化チタン;0.5kg(20wt%) これを固定化処理工程を経て、約2.3 kgの光触媒パルプ
組成物を得た 処理後含水率;0.6wt%
In the immobilization process, about 2.0 kg
Was immobilized to obtain about 3.90 kg of a photocatalytic pulp composition (water content: 0.5 wt%). [Photocatalyst pulp composition 2; Example 2] (FIGS. 1 and 2) Ground paper fiber 2 kg (80 wt%) water content 10 wt%: treated in the above defibration and defibration step Titanium oxide; 0.5 kg (20 wt%) Fix this Approximately 2.3 kg of a photocatalyst pulp composition was obtained through the hydrotreating process.

【0049】光触媒パルプ組成紙:実施例1 上記〔光触媒パルプ組成物1;実施例1〕で得られた光
触媒パルプ組成物を用い、ビーターによりパルプ濃度8w
t%になる様希釈して叩解処理を1h(時間)行った。
Photocatalyst pulp composition paper: Example 1 Using the photocatalyst pulp composition obtained in the above [Photocatalyst pulp composition 1; Example 1], a pulp concentration of 8 watts was measured by a beater.
The mixture was diluted to t% and beaten for 1 hour (hour).

【0050】一方、和紙を含むバージンパルプなどの叩
解したパルプ原料、ここでは例えば、DIP(脱インキ処
理)工程を経た新聞古紙から成る古紙パルプをパルプ濃
度8wt%になる様水で希釈し、1h叩解処理を行い、次い
で、既知の抄紙工程においてすき合わせ抄紙機を用い
て、光触媒パルプと新聞古紙から成るパルプのウエット
シートをすき合わせる。叩解処理後の光触媒パルプ(50g
/m)と新聞古紙から成るパルプ(10g/m)をそれぞれ円
網及び長網抄紙機で抄紙し、重ね合わせ、プレスパート
へ移送し、さらに乾燥してすき合わせる。
On the other hand, a beaten pulp raw material such as virgin pulp containing Japanese paper, for example, used paper pulp made of used newspaper that has been subjected to a DIP (deinking treatment) process is diluted with water so as to have a pulp concentration of 8 wt% for 1 hour. A beating treatment is performed, and then, in a known papermaking process, a wet paper sheet of pulp composed of photocatalytic pulp and old newspaper is used using a papermaking machine. Photocatalytic pulp after beating (50 g
/ m 2 ) and pulp (10 g / m 2 ) consisting of used newspaper are respectively made by a circular net and a fourdrinier paper machine, overlapped, transported to a press part, and further dried and glued.

【0051】以上で、新聞古紙から成る透光性、通気性
白色基材層を光触媒パルプ層に積層した(実施例1)。
As described above, a translucent and air-permeable white base material layer made of used newspaper was laminated on the photocatalytic pulp layer (Example 1).

【0052】光触媒パルプ組成紙:実施例2 〔光触媒パルプ組成物2;実施例2〕で得られた光触媒
パルプ組成物を実施例1と同様に新聞古紙のパルプとす
き合わせた。
Photocatalyst pulp composition paper: Example 2 The photocatalyst pulp composition obtained in [Photocatalyst pulp composition 2; Example 2] was combined with used newspaper pulp in the same manner as in Example 1.

【0053】 ビータ処理時間 1時間 光触媒パルプ濃度 8wt% 新聞古紙パルプ濃度 8wt% 坪量 合計 60g/m 光触媒パルプ層 50g/m 新聞古紙パルプ層 10g/m Beater treatment time 1 hour Photocatalytic pulp concentration 8 wt% Newspaper pulp concentration 8 wt% Basis weight Total 60 g / m 2 Photocatalytic pulp layer 50 g / m 2 Newspaper waste pulp layer 10 g / m 2

【0054】〔光触媒パルプ+紙;比較例1〕前記実施
態様及び実施例におけるミキサーを用いず、単に、紙繊
維;2kg(80wt%)酸化チタン;0.5kg(20wt%)をビーターによ
りパルプ濃度を8wt%になるよう、希釈して叩解して抄
紙、坪量 合計 50g/m
[Photocatalytic pulp + paper; Comparative example 1] The paper fiber; 2 kg (80 wt%) titanium oxide; 0.5 kg (20 wt%) was simply pulp-concentrated with a beater without using the mixer in the above embodiment and example. so as to be 8 wt%, paper and beating diluted basis weight total 50 g / m 2.

【0055】以下に上記実施例1,2及び比較例1によ
る試験結果を示す。 実験条件 添加アセトアルデヒド濃度約820ppm 光強度 約1mW/cm 反応容器 1リットル 光触媒パルプ紙及び他の比較例 サンプル大きさ:8×8cm 坪量合計:実施例1,2 60g/m
比較例1 50g/m
The test results of Examples 1 and 2 and Comparative Example 1 are shown below. Experimental conditions Added acetaldehyde concentration approx. 820 ppm Light intensity approx. 1 mW / cm 2 reaction vessels 1 liter Photocatalytic pulp paper and other comparative examples Sample size: 8 × 8 cm Total grammage: Examples 1,2 60 g / m
2 Comparative Example 1 50 g / m 2

【0056】[0056]

【表1】 光触媒CO2初期生成速度は、次式; (見かけのCO2初期生成速度)−(1ight control CO2生成
速度) 1h,2hでの生成率(%)は、理論値に対する生成比で光触媒
分だけで計算したもの アセトアルデヒド初期消滅速度は、光照射後30minでの
消減速度 1hでのアセトアルデヒド消滅率(%)は、1hでの 濃度/初期濃度×100 光触媒+パルプ紙;比較例1の紙は、光触媒活性が極め
て低く、アセトアルデヒドの消滅速度も遅い。
[Table 1] The initial generation rate of the photocatalyst CO 2 is expressed by the following formula; (apparent CO 2 initial generation rate)-(1ight control CO 2 generation rate) The production rate (%) at 1h and 2h is the photocatalytic component in the production ratio to the theoretical value. The initial acetaldehyde extinction rate is the extinction rate at 30 min after light irradiation. The acetaldehyde extinction rate (%) at 1 h is: concentration at 1 h / initial concentration x 100 photocatalyst + pulp paper; The photocatalytic activity is extremely low, and the acetaldehyde disappearance rate is slow.

【0057】これに対し、光触媒パルプ紙;実施例1
は、2hでのCO2生成率では、実施例2と共に100%を示し、
アセトアルデヒドの濃度が減少してから十分な反応をす
ることがわかる。
On the other hand, photocatalytic pulp paper;
Indicates 100% with the CO 2 generation rate in 2h together with Example 2.
It turns out that sufficient reaction is performed after the concentration of acetaldehyde decreases.

【0058】単に酸化チタンの混合のみでは効果は得ら
れず、本願発明が極めて光触媒活性性能を向上させてい
ることが分かった。
The effect was not obtained only by mixing titanium oxide alone, and it was found that the present invention significantly improved the photocatalytic activity performance.

【0059】図1(A)、(B)および図2(A)は、
それぞれ、実施例2における光触媒パルプ組成物及び光
触媒パルプ紙(実施例2)の古紙の積層された光触媒パル
プ紙における光触媒側の走査顕微鏡写真で、酸化チタン
がパルプ原料の外面に固着結合し、また、水を用いた製
紙法によってもパルプ外面及び紙内部においても酸化チ
タンの固着状態か維持されていることが削る。これは、
試験例における製紙実験で撹拌時添加した水に殆ど酸化
チタンが溶出していないことからも明らかである。
FIGS. 1 (A), 1 (B) and 2 (A)
In each of the photocatalyst pulp composition and the photocatalytic pulp paper (Example 2) in the photocatalytic pulp paper of the laminated photocatalytic pulp paper of the waste paper, the titanium oxide is fixedly bonded to the outer surface of the pulp raw material, In addition, it is required that the titanium oxide is maintained in a fixed state both on the outer surface of the pulp and inside the paper by the paper-making method using water. this is,
It is clear from the fact that almost no titanium oxide was eluted in the water added during stirring in the papermaking experiment in the test example.

【0060】〔光触媒パルプ組成物:実施例(3)、光
触媒パルプ紙:実施例3〕本例において、光触媒パルプ
組成物を形成する酸化チタン、パルプ及び/又は紙の配
合比率は、前記製造例(1)の場合と同様である。
[Photocatalytic pulp composition: Example (3), photocatalytic pulp paper: Example 3] In this example, the mixing ratio of titanium oxide, pulp and / or paper forming the photocatalytic pulp composition was determined according to the production example described above. This is the same as the case (1).

【0061】また、原材料として用いる酸化チタン、パ
ルプ及び/又は紙についても、前述の製造例(1)と同
様のものを使用できる。
Further, the same titanium oxide, pulp and / or paper used as raw materials as in the above-mentioned production example (1) can be used.

【0062】本例にあっては、前記実施例(1)と同様
に酸化チタン及びパルプ及び/又は紙を配合すると共
に、各酸化チタン及びパルプ及び/又は紙の合計重量に
対して25〜100wt%の熱可塑性樹脂を添加して光触媒パル
プ組成物(光触媒パルプ組成物:実施例(3))を形成
し、これに新聞古紙をDIP処理した古紙パルプから成る
再生紙を積層したものである(光触媒パルプ紙:実施例
3)。
In this example, titanium oxide and pulp and / or paper were mixed in the same manner as in Example (1), and the total weight of each titanium oxide and pulp and / or paper was 25 to 100 wt. % Of a thermoplastic resin was added to form a photocatalyst pulp composition (photocatalyst pulp composition: Example (3)), on which a recycled paper made of wastepaper pulp obtained by DIP-processing newspaper wastepaper was laminated. Photocatalytic pulp paper: Example 3).

【0063】この熱可塑性樹脂としては、各種のものを
使用することができ、また、熱可塑性樹脂は粉体、粒体
状のものの他、シート状のものであっても使用すること
ができ、粉体、粒体状のものにあっては好ましくは粒径
1mm以下、シート状のものにあっては好ましくは厚さ1mm
以下のものを一辺10mm以下に破砕して使用する。
As the thermoplastic resin, various types can be used, and the thermoplastic resin can be used in the form of a sheet, in addition to powders and granules. In the case of powder or granules, the particle size is preferably
1mm or less, preferably 1mm thick for sheet
The following are used by crushing each side to 10 mm or less.

【0064】生成された光触媒組成物を加熱成形して光
触媒パルプ成形体を形成する場合、高温により加熱する
と光触媒パルプ組成物内のパルプがこの熱により焼ける
場合があることから、比較的融点の高いポリエステル、
ポリカーボン等熱可塑性樹脂に比べ、PE(LLD:直鎖状低
密度),酢酸ビニル等の低融点の熱可塑性樹脂を使用する
ことが好ましい。
When the formed photocatalyst composition is formed by heating to form a photocatalyst pulp molded body, the pulp in the photocatalyst pulp composition may be burned by this heat when heated at a high temperature, so that it has a relatively high melting point. polyester,
It is preferable to use a thermoplastic resin having a low melting point, such as PE (LLD: linear low density) or vinyl acetate, as compared with a thermoplastic resin such as polycarbonate.

【0065】前記光触媒パルプを構成するパルプ及び/
又は紙、及び熱可塑性樹脂は、必ずしもそれぞれを独立
した原料としてミキサ内に投入する必要はなく、例えば
牛乳パック等に使用されている、熱可塑性樹脂フィルム
にてラミネートされた紙層を有する複合フィルムを例え
ば一辺10mm程度の小片に破砕した後前述のミキサに投入
することもでき、この場合、該複合フィルムの紙層が光
触媒パルプ組成物を構成するパルプ繊維を、熱可塑性樹
脂層が、形成される光触媒パルプ組成物を構成する熱可
塑性樹脂と成る。したがって、複合フィルム中に含まれ
るパルプ分と熱可塑性樹脂分との比率を考慮して酸化チ
タンの配合量を決定すると共に、必要に応じて熱可塑性
樹脂及び/又はパルプ及び/又は紙を加えて各原料の配
合が前述の比率と成るよう調整する。
The pulp constituting the photocatalytic pulp and / or
Or, the paper and the thermoplastic resin do not necessarily need to be charged into the mixer as independent raw materials, for example, used for milk packs and the like, a composite film having a paper layer laminated with a thermoplastic resin film. For example, after crushing into small pieces of about 10 mm on a side, it can be put into the above-mentioned mixer.In this case, the paper layer of the composite film forms pulp fibers constituting the photocatalytic pulp composition, and the thermoplastic resin layer is formed. It becomes a thermoplastic resin constituting the photocatalytic pulp composition. Therefore, the amount of titanium oxide is determined in consideration of the ratio between the pulp component and the thermoplastic resin component contained in the composite film, and the thermoplastic resin and / or pulp and / or paper are added as necessary. The blending of each raw material is adjusted so as to have the above-mentioned ratio.

【0066】前記パルプ及び/又は紙及び酸化チタン、
及び熱可塑性樹脂を投入後、ミキサーを作動させてミキ
サー内で高速回転する撹拌衝撃翼による撹拌衝撃力に基
づく剪断力により剪断発熱を生じさせ、温度約120℃に
上昇させ、パルプ及び/又は紙の水分含有量を3wt%好ま
しくは、1wt%以下とする。この工程で、パルプ及び/又
は紙から水分が蒸発し、乾燥すると共に、前記パルプ及
び/又は紙を、紙の場合には前記衝撃力により粉砕作用
を受け繊維状となり、さらに前記乾燥に伴い膨潤し、繊
維を毛羽ただせ、解綿状に凝集し、三次元繊維絡合体と
した上でこの繊維表面及び繊維内にも酸化チタンを前記
撹拌衝撃翼による攪拌衝撃力ないし剪断力に伴う押し付
け外力によって付着、浸入固定させる。
The pulp and / or paper and titanium oxide,
After the thermoplastic resin is charged, the mixer is operated to generate shear heat by shearing force based on the stirring impact force of the stirring impeller rotating at high speed in the mixer, and the temperature is increased to about 120 ° C., and the pulp and / or paper Is 3 wt%, preferably 1 wt% or less. In this step, moisture evaporates from the pulp and / or paper and dries, and, in the case of paper, the pulp and / or paper is crushed by the impact force and becomes fibrous, and further swells with the drying. Then, the fibers are fluffed, agglomerated in a defatted shape, and a three-dimensional fiber entangled body, and titanium oxide is also adhered to the fiber surface and within the fiber by a pressing external force accompanying a stirring impact force or a shear force by the stirring impeller, Infiltrate and fix.

【0067】また、同時にミキサー内に投入された熱可
塑性樹脂も少なくとも一部が粉砕作用を受けて細かに粉
砕されて、前記酸化チタン同様に繊維表面及び繊維内に
前記攪拌衝撃翼による撹拌衝撃力ないし剪断力に伴う押
し付け外力によって付着、浸入固定される。
At the same time, at least a part of the thermoplastic resin charged into the mixer is also finely pulverized by the pulverizing action, and the stirring impact force by the stirring impeller on the fiber surface and in the fiber like the titanium oxide. Or, it is attached and penetrated and fixed by an external pressing force caused by a shearing force.

【0068】前記パルプ及び/又は紙、及び熱可塑性樹
脂として、牛乳パック等の複合フイルムを使用する場合
には、ミキサー内に投入された複合フィルムの小片が攪
拌衝撃翼による攪拌衝撃力により熱可塑性樹脂層と紙層
とに分離され、分離された紙層はさらに撹拌衝撃力によ
り粉砕されて前述の紙と同様に繊維状にほぐされる。
When a composite film such as a milk pack is used as the pulp and / or paper and the thermoplastic resin, small pieces of the composite film put into the mixer are mixed with the thermoplastic resin by the stirring impact force of the stirring impact blade. The paper layer is separated into a layer and a paper layer, and the separated paper layer is further pulverized by a stirring impact force and loosened into a fiber like the above-described paper.

【0069】また、熱可塑性樹脂層も少なくとも一部が
撹拌衝撃力により細かく粉砕されて、別途投入された前
述の熱可塑性樹脂と同様パルプ繊維の表面及び内部に押
し付けられて付着、浸入固定される。
Further, at least a part of the thermoplastic resin layer is also finely pulverized by the stirring impact force, and is pressed and adhered to the surface and inside of the pulp fiber similarly to the above-mentioned thermoplastic resin which is separately charged, and is fixed. .

【0070】なお、熱可塑性樹脂はミキサーによる撹拌
の際の熱により溶融される必要はなく、パルプ繊維に付
着、浸入固定されるものであればよい。
The thermoplastic resin does not need to be melted by the heat at the time of stirring by the mixer, but may be any one as long as it adheres to the pulp fiber and penetrates and fixes it.

【0071】上記光触媒パルプ組成物は、例えばこれを
加熱下でプレス等することによりフレスシート等の光触
媒パルプ成形体に容易に成形することができ、また、該
方法によって成形された成形体はパルプ繊維の表面及び
内部に付着、浸入固定された熱可塑性樹脂がバインダと
なってパルプ繊維間を強固に結合するため、強靭なプレ
スシート等の成形体と成る。
The photocatalyst pulp composition can be easily formed into a photocatalyst pulp molded article such as a fleece sheet by, for example, pressing the composition under heating, and the molded article formed by the method is pulp. Since the thermoplastic resin adhered to and infiltrated on the surface and inside of the fiber serves as a binder to firmly bond between the pulp fibers, a molded article such as a tough press sheet is formed.

【0072】上記製造例により得られた光触媒活性を有
するパルプ組成物を用いて光触媒パルプ成形体(プレス
シート)を製造した。
A photocatalytic pulp molded article (press sheet) was produced using the pulp composition having photocatalytic activity obtained in the above Production Example.

【0073】光触媒パルプ組成物を用いた光触媒パルプ
紙の実施例及び比較例 実施例として、熱可塑性樹脂は、PE〔ウルドゼックス40
30P(パウダー):三井石油化学工業杜〕を使用し、他の
原料については、前記実施例2と同様とし、上記プレス
シートの成形体にDIP(脱インキ処理)工程を経た新聞
古紙から成る古紙パルプを抄紙して乾燥したものを接着
剤を介してホットプレスで片面に積層した。
Examples and Comparative Examples of Photocatalytic Pulp Paper Using Photocatalytic Pulp Composition As examples, the thermoplastic resin was PE [Uldzex 40
30P (powder: Mitsui Petrochemical Industry Co., Ltd.), and the other raw materials are the same as in Example 2 above. Used paper made of used newspaper obtained through the DIP (deinking treatment) process on the pressed sheet compact The dried pulp was laminated on one side by hot pressing via an adhesive.

【0074】光触媒パルプ紙;実施例3 粉砕紙繊維;2kg(80wt%) 含水率10wt% 酸化チタン;0.5kg(20wt%) 熱可塑性樹脂:PE 1.5kg (紙繊維+酸化チタンの合計
重量に対し60wt%) 処理後含水率:0.5wt% 上記原料をミキサー内に投入して撹拌し、約120℃まで
温度上昇させ、紙繊維の含有水分量を3wt%、好ましくは
1wt%以下にする。
Photocatalytic pulp paper; Example 3 Ground paper fiber; 2 kg (80 wt%) Water content 10 wt% Titanium oxide; 0.5 kg (20 wt%) Thermoplastic resin: PE 1.5 kg (based on the total weight of paper fiber + titanium oxide (60 wt%) Water content after treatment: 0.5 wt% The above raw materials are put into a mixer and stirred, the temperature is raised to about 120 ° C, and the water content of the paper fiber is 3 wt%, preferably
Reduce to 1 wt% or less.

【0075】上記により得られた光触媒パルプ組成物0.
51gを8×8cmに広げ、テフロン(登録商標)シートで挟
み、1kgの荷重をかけながら150℃で2時間、恒温室にて
加熱して、坪量50g/mの光触媒パルプ成形体(プレスシ
ート)を形成し、上記プレスシートの成形体にDIP(脱イ
ンキ処理)工程を経た新聞古紙から成る古紙パルプを抄
紙して乾燥したも坪量10g/mを接着剤を介してホット
プレスで片面に積層し、これを試料とした(実施例3)。
The photocatalytic pulp composition obtained as described above was used.
Spread 51g to 8 × 8 cm, sandwiched by Teflon sheets, 2 hours at 0.99 ° C. while applying a load of 1 kg, and heated in a thermostatic chamber, the photocatalytic pulp molded article having a basis weight of 50 g / m 2 (Press to form a sheet), the molded body in DIP (deinking process of the pressed sheet) was also dried from the used paper pulp consisting of waste newspaper through the steps a basis weight 10 g / m 2 by a hot press via an adhesive This was laminated on one side and used as a sample (Example 3).

【0076】 ビータ処理時間 1時間 光触媒パルプ濃度 8wt% 光触媒パルプは、ビーター処理なし 坪量 合計60g/m 光触媒パルプ層 50 g/m 新聞古紙パルプ層 10 g/m Beater treatment time 1 hour Photocatalytic pulp concentration 8 wt% Photocatalytic pulp, no beater treatment Basis weight Total 60 g / m 2 Photocatalytic pulp layer 50 g / m 2 Newspaper pulp layer 10 g / m 2

【0077】〔比較例2(前出光触媒パルプ紙;実施例
2)〕 粉砕紙繊維;2kg(80wt%) 含水率10wt% 酸化チタン;0.5kg (20wt%) 処理後含水率;0.6wt% 上記実施例(2)で得られた光触媒パルプ組成物を用
い、比較例1の工程と同じく製紙し(坪量 合計50g/
m)、この光触媒パルプの成形体にDIP(脱インキ処
理)工程を経た新聞古紙から成る古紙パルプを抄紙して
乾燥したもの(坪量合計10g/m)を接着剤を介してホ
ットプレスで片面に積層した。
Comparative Example 2 (Photocatalytic pulp paper described above; Example 2) Ground paper fiber; 2 kg (80 wt%) Water content 10 wt% Titanium oxide; 0.5 kg (20 wt%) Water content after treatment; 0.6 wt% Using the photocatalytic pulp composition obtained in Example (2), papermaking was performed in the same manner as in the process of Comparative Example 1 (basis weight: 50 g / g).
m 2 ), a molded article of this photocatalyst pulp, a waste paper pulp made of waste newspaper that has been subjected to a DIP (deinking treatment) process, made and dried (total basis weight: 10 g / m 2 ) is hot-pressed via an adhesive. Was laminated on one side.

【0078】 ビータ処理時間 1時間 光触媒パルプ濃度 8wt% 新聞古紙濃度 8wt% 坪量 合計60g/m 光触媒パルプ層 50 g/m 新聞古紙パルプ層 10 g/m Beater treatment time 1 hour Photocatalytic pulp concentration 8 wt% Newspaper wastepaper concentration 8 wt% Basis weight Total 60 g / m 2 Photocatalytic pulp layer 50 g / m 2 Newspaper wastepaper pulp layer 10 g / m 2

【0079】上記実施例3の光触媒パルプ成形体と、比
較例2を下記の条件において比較した結果を表2に示
す。 実験条件 添加アセトアルデヒド濃度約820ppm 光強度 約1mmW/cm 反応容器1リットル 光触媒パルプ紙及び他の比較例 サンプル大きさ:8×8cm 坪量 合計60g/m
Table 2 shows the results of comparison between the photocatalyst pulp compact of Example 3 and Comparative Example 2 under the following conditions. Experimental conditions Added acetaldehyde concentration about 820 ppm Light intensity about 1 mmW / cm 2 reaction vessel 1 liter Photocatalytic pulp paper and other comparative examples Sample size: 8 × 8 cm Basis weight Total 60 g / m 2

【0080】[0080]

【表2】 実施例3により製造された光触媒パルプ組成物により形
成した光触媒パルプ成形体(プレスシート+古紙)は、前
述の光触媒パルプ紙(比較例2)と略同様の特性を有する
ことが確認された。
[Table 2] It was confirmed that the photocatalyst pulp molded article (press sheet + waste paper) formed from the photocatalyst pulp composition produced in Example 3 had substantially the same characteristics as the photocatalyst pulp paper (Comparative Example 2) described above.

【0081】従って、前記実施例3の光触媒パルプ成形
体は、光触媒活性性能の向上という単に酸化チタンの混
合のみでは得ることのできない効果が得られていること
が明らかとなった。
Accordingly, it was clarified that the photocatalytic pulp molded article of Example 3 had an effect of improving photocatalytic activity, which could not be obtained by simply mixing titanium oxide.

【0082】また、2時間でのCO2生成率が100%となって
いることから、アセトアルデヒドの濃度が減少してから
も十分な反応をすることがわかる。
Further, since the CO 2 generation rate in 2 hours is 100%, it can be seen that a sufficient reaction can be performed even after the concentration of acetaldehyde is reduced.

【0083】上述した古紙を積層した光触媒活性機能を
有する再生紙は、光触媒側の紙を内、外又は中間層とし
て、古紙パルプ芯材あるいは基材等の積層材として普通
紙、合成紙、プラスチックフィルム、不織布を2層ある
いは3層などに積層したものとすることができ、この場
合、芯材あるいは基材として透光性を有し、あるいは、
開孔を多数有する普通紙、合成紙、不織布、織布、繊維
密度の低い不織布、織り目の粗い織布、透明フィルム
等、透光性の優れたものを使用することにより、光触媒
パルプが光源側に位置し、直接露光し得る状態で配置さ
れた場合はもとより、芯材あるいは基材間に光触媒パル
プが挟持されている場合等、光触媒パルプが直接光源側
に位置しない場合においても、芯材あるいは基材を通過
した光が光触媒パルプに照射されて酸化チタンの光触媒
性が好適に発揮されると共に、芯材あるいは基材を開孔
等を備えた通気性を有するものとすることで、該光触媒
パルプ成形体をフィルター等として使用することが容易
となる。
Recycled paper having the photocatalytic activity function obtained by laminating the above-mentioned waste paper is a paper on the photocatalyst side as an inner layer, an outer layer, or an intermediate layer. Film, nonwoven fabric can be laminated in two or three layers and the like, in this case, having a light-transmitting core or base material, or
The use of plain paper, synthetic paper, non-woven fabric, woven fabric, non-woven fabric with low fiber density, coarse-woven woven fabric, transparent film, etc., which have excellent light transmission, has a large number of apertures. In the case where the photocatalytic pulp is not directly located on the light source side, such as when the photocatalytic pulp is sandwiched between the core material or the base material, the core material or The photocatalyst pulp is irradiated with light that has passed through the base material, whereby the photocatalytic property of titanium oxide is suitably exhibited, and the core material or the base material is made to have air permeability with openings and the like, whereby It becomes easy to use the pulp molded article as a filter or the like.

【0084】〔前記積層光触媒パルプ紙から成る成形体
としての紙紐の実施例1〕実施例1と同様の解繊離解工
程において牛乳パックを処理し、パルプを得た。これを
前記固定化処理工程において、約23wt%の酸化チタンを
固定化し、光触媒パルプ組成物を得た。次いで、得られ
た光触媒パルプ組成物を用い、ビーターによりパルプ濃
度8wt%になる様希釈して叩解処理を1h(時間)行った。
Example 1 of Paper String as Molded Article Made of the Laminated Photocatalytic Pulp Paper In the same defibration and defibration step as in Example 1, a milk pack was treated to obtain pulp. In the immobilization step, about 23 wt% of titanium oxide was immobilized to obtain a photocatalytic pulp composition. Next, the obtained photocatalytic pulp composition was diluted with a beater so as to have a pulp concentration of 8% by weight and beaten for 1 hour (hour).

【0085】一方、上記と同様の牛乳パックを処理して
得たパルプを43g/m2パルプ濃度8wt%になる様水で希釈
し、1h叩解処理を行い、次いで、既知の抄紙工程におい
てすき合わせ抄紙機を用いて、光触媒パルプを15wt%配
合してある光触媒層(20g/m2)と牛乳パックから成るパ
ルプの層(43g/m)をそれぞれ円網及び長網抄紙機で抄
紙し、重ね合わせ、プレスパートへ移送し、さらに乾燥
してすき合わせ、63g/m2の2層光触媒パルプ紙を得た。
On the other hand, the pulp obtained by treating the same milk pack as described above was diluted with water so as to have a pulp concentration of 43 g / m 2 at a concentration of 8 wt%, beaten for 1 hour, and then subjected to laminating paper making in a known paper making process. The photocatalyst layer (20 g / m 2 ) containing 15 wt% of the photocatalytic pulp and the pulp layer (43 g / m 2 ) composed of milk packs are made with a circular net and fourdrinier paper machine, respectively, using a paper machine. Then, it was transferred to a press part, and further dried and laced to obtain a two-layer photocatalytic pulp paper of 63 g / m 2 .

【0086】下表、試験例1は、上述光触媒パルプ紙の
物性評価である。恒温、恒室内で24時間放置した後、JI
S P8124、JIS P8113、JIS P8135に準じて測定した。
The following table, Test Example 1, is an evaluation of the physical properties of the photocatalytic pulp paper. After standing in a constant temperature and constant temperature room for 24 hours, JI
It was measured according to S P8124, JIS P8113 and JIS P8135.

【0087】この光触媒パルプ紙をスリッターにより幅
48mmに切断し、約500mのロール状に巻き取り、これを既
知のリング撚糸機により前記光触媒パルプ層を外表面と
なるよう撚糸し、約φ3mmの紙紐を製造した。
This photocatalytic pulp paper was slit with a slitter.
It was cut into 48 mm, wound up into a roll of about 500 m, and twisted by a known ring twisting machine so that the photocatalytic pulp layer became the outer surface, thereby producing a paper cord of about φ3 mm.

【0088】下表、試験例2は、上述光触媒パルプ紙か
ら成る紙紐の物性評価である。紙紐は、105℃で乾燥し
ないよう、20±5℃、相対湿度65±2%で48時間以上調湿
してから、JIS Z1518-1976に準じて測定した。
The following Table, Test Example 2, is an evaluation of the physical properties of a paper string made of the photocatalytic pulp paper. The paper string was conditioned at 20 ± 5 ° C. and 65 ± 2% relative humidity for 48 hours or more so as not to dry at 105 ° C., and then measured according to JIS Z1518-1976.

【0089】[0089]

【表3】試験例1、2 [Table 3] Test Examples 1 and 2

【0090】〔前記積層光触媒パルプ紙から成る紙紐の
実施例2〕上記紙紐の実施例1と同様、光触媒パルプ組
成物:酸化チタン 23 wt%固定を約15%添加した光触媒層
(12g/m)に対して牛乳パックを処理して得たパルプ
層(26g/m2)から成るすき合わせ38g/m2の2層光触媒パ
ルプを得た。そして、前記光触媒パルプ層を外表面とな
るよう撚糸し、約φ1mmの紙紐を製造した。
[Example 2 of paper string made of the laminated photocatalytic pulp paper] As in Example 1 of the above-described paper string, a photocatalytic pulp composition: a photocatalyst layer (12 g / A two-layer photocatalytic pulp having a pulp layer (26 g / m 2 ) obtained by treating a milk pack with respect to m 2 ) and having a clearance of 38 g / m 2 was obtained. Then, the photocatalyst pulp layer was twisted so as to be on the outer surface to produce a paper cord of about φ1 mm.

【0091】〔前記積層光触媒パルプ紙紐で成る成形体
としての帯状紐の実施例3〕紙紐の実施例2で製造した
紙紐16本を同一平面で重畳し、水溶性接着剤として水
溶性ポリビニルアルコールに濃度(1回目30wt%、2回目1
5wt%、3回目3wt%水溶液とした)を変えて3回浸漬、乾燥
を繰り返し幅20mmの帯状紐を製造した。ついで、上記帯
状紐の少なくとも片面をサンディング(アミテック社
製:NS-15D;砥紙400 番)して光触媒層を露出した。
[Embodiment 3 of the band-shaped cord as a molded product made of the laminated photocatalytic pulp pulp cord] The 16 paper cords produced in the embodiment 2 of the paper cord are overlapped on the same plane, and a water-soluble adhesive is used. Concentration in polyvinyl alcohol (30wt% for the first time, 1
The immersion and drying were repeated three times while changing 5 wt% and a third 3 wt% aqueous solution to produce a 20-mm-wide strip. Then, at least one side of the strip was sanded (NS-15D, manufactured by Amitec Co., Ltd .; abrasive paper No. 400) to expose the photocatalyst layer.

【0092】下表5、試験例3は、上記紙紐の実施例
1,2及び帯状紐の実施例3のサンディング前後及び比
較例1として光触媒を含有しない帯状紐を試料とした。 実験条件 ガス/濃度:添加アセトアルデヒドガス/20ppm(紙への
吸着後の濃度) 照射強度 約1mW/cm 反応容器 3リットル 試料:全面積が5cm×10cmとなるよう裁断。 光源 :40W ブラックライト 測定 :ガステック検知菅92Lにて測定 前処理 :1mW/cmの紫外線を十五時間照射後デシケ
ーター内で一日乾燥した。
In Table 5 and Test Example 3 below, before and after sanding of Examples 1 and 2 of the above-mentioned paper string and Example 3 of the strip-like string, and as Comparative Example 1, strip-like cords containing no photocatalyst were used as samples. Experimental conditions Gas / concentration: added acetaldehyde gas / 20 ppm (concentration after adsorption on paper) Irradiation intensity About 1 mW / cm 2 reaction vessel 3 liter Sample: Cut to total area of 5 cm x 10 cm. Light source: 40 W black light Measurement: Measured with 92 L of gas tech detection tube Pretreatment: Irradiated with ultraviolet rays of 1 mW / cm 2 for 15 hours and dried in a desiccator for one day.

【0093】[0093]

【表4】 [Table 4]

【0094】[0094]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。
Since the present invention is configured as described above, it has the following effects.

【0095】反応速度、反応の終了を著しく早めること
ができ、酸化チタンの光触媒活性効果を向上させること
が可能であり、包装材料、壁紙など建材、濾材など各種
広範な用途に適応できる抗菌、抗黴、防汚(汚れの)及び
悪臭の分解、脱臭処理、有害物質の酸化分解効果を有す
る古紙積層光触媒再生紙を含む光触媒パルプ紙、及び前
記積層光触媒パルプ紙から成る紙紐及び前記紙紐から成
る成形体を提供することができた。
The reaction speed and termination of the reaction can be remarkably accelerated, the photocatalytic activity of titanium oxide can be improved, and antibacterial and antimicrobial properties can be applied to a wide variety of applications such as packaging materials, wallpaper, building materials, and filter materials. Mold, antifouling (dirty) and odor decomposition, deodorizing treatment, photocatalytic pulp paper including waste paper laminated photocatalyst recycled paper having an oxidative decomposition effect of harmful substances, and paper string comprising the laminated photocatalytic pulp paper and the paper string The resulting molded article could be provided.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本願実施例における光触媒パルプ組成物の走査
顕微鏡による表面を示す。 (A)は、倍率×200、 (B)
は、倍率×750
FIG. 1 shows the surface of a photocatalytic pulp composition in a working example of the present application, as measured by a scanning microscope. (A) is magnification × 200, (B)
Is the magnification × 750

【図2】本願実施例における光触媒パルプ紙の走査顕微
鏡による表面及び断面を示す。 (A)は、表面を示すも
ので、倍率×750
FIG. 2 shows a surface and a cross section of a photocatalytic pulp paper in a working example of the present application by a scanning microscope. (A) shows the surface, magnification × 750

【図3】図3は、本発明の板紙状乾式パルプの解繊離解
工程に使用する衝撃摩砕装置の概要構成を模式的に示す
部分縦断面図である。
FIG. 3 is a partial vertical cross-sectional view schematically showing a schematic configuration of an impact milling apparatus used in the paperboard dry pulp defibration and defibration step of the present invention.

【図4】図3の平面図である。FIG. 4 is a plan view of FIG. 3;

【図5】図3の解繊離解工程における衝撃摩砕作用を説
明するための模式的正面図である。
FIG. 5 is a schematic front view for explaining an impact grinding operation in the defibration and defibration step of FIG. 3;

【図6】本発明の解繊離解工程に使用する衝撃摩砕手段
の使用例を示す概略図である。
FIG. 6 is a schematic view showing an example of use of an impact grinding means used in the defibration and defibration step of the present invention.

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) D21H 17/74 D21H 17/74 21/14 21/14 B 21/36 21/36 23/04 23/04 Fターム(参考) 4F100 AA21A AJ04A AJ04B AK01A BA02 DG03A DG10A EH41 GB07 GB15 GB56 GB90 JA04A JL08A JL16B YY00A 4L036 MA34 MA37 PA21 UA26 4L055 AA01 AA11 AF09 AF44 AG19 AH50 AJ01 BB30 BD17 EA16 EA32 FA20 GA05 GA21 GA23 GA24 GA27 GA31 Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) D21H 17/74 D21H 17/74 21/14 21/14 B 21/36 21/36 23/04 23/04 F-term ( 4F100 AA21A AJ04A AJ04B AK01A BA02 DG03A DG10A EH41 GB07 GB15 GB56 GB90 JA04A JL08A JL16B YY00A 4L036 MA34 MA37 PA21 UA26 4L055 AA01 AA11 AF09 AF44 AG19 AH50 AJ20 BB30 GA17

Claims (15)

【特許請求の範囲】[Claims] 【請求項1】酸化チタン5〜60wt%に、含有水分量を3wt%
以内とし平均繊維径5〜300μm、平均繊維長0.1〜70mmの
パルプ及び/又は紙40〜95wt%の割合で配合して成る光
触媒パルプ組成物に対してバージンパルプ又は古紙パル
プを積層して成ることを特徴とする積層光触媒パルプ
紙。
Claims: 1. A titanium oxide of 5 to 60% by weight and a water content of 3% by weight.
Virgin pulp or waste paper pulp laminated on a photocatalytic pulp composition blended in a ratio of pulp and / or paper of 40 to 95 wt% with an average fiber diameter of 5 to 300 μm and an average fiber length of 0.1 to 70 mm. A laminated photocatalytic pulp paper characterized by the following.
【請求項2】酸化チタン5〜60wt%と、含有水分量を3wt%
以内とし平均繊維径5〜300μm、平均繊維長0.1〜70mmの
パルプ及び/又は紙40〜95wt%と、前記酸化チタン、パ
ルプ及び/又は紙の合計重量に対して25〜100wt%の熱可
塑性樹脂を配合して成る光触媒パルプ組成物に対してバ
ージンパルプ又は、古紙パルプを積層して成ることを特
徴とする積層光触媒パルプ紙。
2. A titanium oxide of 5 to 60 wt% and a water content of 3 wt%.
Pulp and / or paper having an average fiber diameter of 5 to 300 μm and an average fiber length of 0.1 to 70 mm, and a thermoplastic resin of 25 to 100 wt% based on the total weight of the titanium oxide, pulp and / or paper. A laminated photocatalytic pulp paper characterized by laminating a virgin pulp or a waste paper pulp with a photocatalytic pulp composition comprising the following.
【請求項3】酸化チタン5〜60wt%に、平均繊維径5〜300
μm、平均繊維長0.1〜70mmに解繊離解したパルプ及び/
又は紙40〜95wt%の割合で配合して成る配合物に対して
撹拌衝撃力を付加して撹拌して、前記撹拌衝撃力に基づ
く剪断力により剪断発熱を生じさせ、この剪断発熱によ
り前記配合物を乾燥し含有水分量を3wt%以内に低下せし
める工程と、前記パルプ及び/又は紙を前記乾燥に伴い
膨潤し、三次元繊維絡合体とする工程と、前記撹拌衝撃
力により、前記酸化チタンを前記パルプ及び/又は紙の
繊維表面に押し付け固定化する処理工程と、該酸化チタ
ンを押し付け固定化処理工程後においてバージンパルプ
又は古紙パルプを積層して成ることを特徴とする積層光
触媒パルプ紙の製造方法。
3. An average fiber diameter of 5 to 300 wt% of titanium oxide.
pulp defibrated and disintegrated to an average fiber length of 0.1 to 70 mm
Alternatively, a composition formed by mixing 40 to 95% by weight of paper is stirred by applying a stirring impact force to generate shear heat by shearing force based on the stirring impact force. Drying the material to reduce the water content to 3 wt% or less; swelling the pulp and / or paper with the drying to form a three-dimensional fiber entangled body; A virgin pulp or a waste paper pulp after pressing and fixing the titanium oxide to the fiber surface of the pulp and / or paper, and fixing the titanium oxide. Production method.
【請求項4】酸化チタン5〜60wt%と、含有水分量を3wt%
以内とし平均繊維径5〜300μm、平均繊維長0.1〜70mmの
パルプ及び/又は紙40〜95wt%と前記酸化チタン、パル
プ及び/又は紙の合計重量に対して25〜100wt%の熱可塑
性樹脂を配合して成る配合物に対して撹拌衝撃力を付加
して撹拌して、前記撹拌衝撃力に基づく剪断力により剪
断発熱を生じさせ、この剪断発熱により前記配合物を乾
燥し含有水分量を3wt%以内に低下せしめる工程と、前記
パルプ及び/又は紙を前記乾燥に伴い膨潤し、三次元繊
維絡合体とする工程と、前記攪拌衝撃力により、前記酸
化チタン及び熱可塑性樹脂を前記パルプ及び/又は紙の
繊維表面に押し付け固定化する処理工程と、チタンを前
記パルプ及び/又は紙の繊維表面に押し付け固定化する
処理工程と、該酸化チタンの押し付け固定化処理工程後
においてバージンパルプ又は古紙パルプを積層して成る
ことを特徴とする積層光触媒パルプ紙の製造方法。
4. A titanium oxide of 5 to 60% by weight and a water content of 3% by weight.
The average fiber diameter is 5 to 300 μm, the average fiber length is 0.1 to 70 mm, pulp and / or paper is 40 to 95 wt%, and the titanium oxide, the thermoplastic resin is 25 to 100 wt% based on the total weight of the pulp and / or paper. Stirring is performed by applying a stirring impact force to the blended composition to generate shear heat by the shearing force based on the stirring impact force, and the shear heat is used to dry the blend to reduce the water content to 3 wt. %, A step of swelling the pulp and / or paper with the drying to form a three-dimensional fiber entangled body, and a step of stirring the titanium oxide and the thermoplastic resin into the pulp and / or Or a step of pressing and fixing to the fiber surface of paper, a step of pressing and fixing titanium to the surface of the pulp and / or paper fiber, and a step of pressing and fixing the titanium oxide to virgin pulp or virgin pulp. Method for manufacturing a laminated photocatalytic pulp paper which is characterized by formed by laminating pulp.
【請求項5】前記酸化チタンの押し付け固定化処理工程
後の抄紙工程においてバージンパルプあるいは古紙パル
プをすき合わせ積層して成る請求項3又は4に記載の積
層光触媒パルプ紙の製造方法。
5. The method for producing a laminated photocatalytic pulp paper according to claim 3, wherein virgin pulp or waste paper pulp is laminated by lamination in a papermaking step after the step of pressing and fixing the titanium oxide.
【請求項6】前記古紙パルプがDIP工程を経た新聞古紙
から成る請求項1又は2記載の積層光触媒パルプ紙又は
請求項3又は4に記載の積層光触媒パルプ紙の製造方
法。
6. The method for producing a laminated photocatalytic pulp paper according to claim 1 or 2, or the laminated photocatalytic pulp paper according to claim 3 or 4, wherein the waste paper pulp is composed of waste newspaper subjected to a DIP process.
【請求項7】前記古紙パルプが新聞古紙から成り、該古
紙パルプを芯材あるいは基材として積層して成る請求項
1〜5いずれか1項記載の積層光触媒パルプ紙又は積層
光触媒パルプ紙の製造方法。
7. The laminated photocatalytic pulp paper or the laminated photocatalytic pulp paper according to any one of claims 1 to 5, wherein the waste paper pulp is made of waste newspaper, and the waste paper pulp is laminated as a core material or a base material. Method.
【請求項8】酸化チタン5〜60wt%及びパルプ及び/又は
紙40〜95wt%に対して平均繊維長1〜100mm、平均径10〜4
0μm、融点120℃以上の合成繊維を最大1:9の割合で配合
して成る請求項1〜6いずれか1項記載の積層光触媒パ
ルプ紙又は積層光触媒パルプ紙の製造方法。
8. An average fiber length of 1 to 100 mm and an average diameter of 10 to 4 with respect to 5 to 60% by weight of titanium oxide and 40 to 95% by weight of pulp and / or paper.
The laminated photocatalytic pulp paper or the method for producing a laminated photocatalytic pulp paper according to any one of claims 1 to 6, wherein synthetic fibers having 0 µm and a melting point of 120 ° C or higher are mixed at a maximum of 1: 9.
【請求項9】前記パルプが、板紙状の乾式パルプであっ
て、該乾式パルプを処理対象とし、該乾式パルプを複数
の被処理小片に細断して形成された個々の被処理小片に
対して衝撃摩砕力を付加して摩砕され綿状に凝集した繊
維状の原料パルプと略同様の長さと、前記摩砕によって
も繊毛の生じていないパルプ繊維とする解繊離解工程を
含む請求項3又は4記載の積層光触媒パルプ紙の製造方
法。
9. The dry pulp as a paperboard-like pulp, wherein the dry pulp is to be processed, and the dry pulp is shredded into a plurality of pieces to be processed. And a fibrillation and disintegration step of obtaining a pulp fiber having substantially the same length as the fibrous raw material pulp that has been subjected to impact grinding power to be ground and flocculated and flocculently flocculated, and has no cilia even after the grinding. Item 5. The method for producing a laminated photocatalytic pulp paper according to item 3 or 4.
【請求項10】請求項9記載の積層光触媒パルプ紙の製
造方法に用い装置であって、複数に細断された被処理小
片の供給投入口に中心部を連通した固定円盤上にあっ
て、複数の回転軌跡上で各固定ピンを順次に植設した固
定側衝撃摩砕手段と、前記固定円盤に対向して回転駆動
可能に設けた可動円盤上にあって、前記各固定ピンとは
異なる複数の回転軌跡上で各可動ピンを順次植設した可
動側衝撃摩砕手段と、摩砕され綿状に凝集した繊維状の
被処理小片を取出口に取出す取出し手段とを備える解繊
離解装置。
10. An apparatus for use in the method for producing a laminated photocatalytic pulp paper according to claim 9, wherein the apparatus is provided on a fixed disk having a central portion communicating with a supply inlet of a plurality of small pieces to be processed, A fixed-side impact grinding means in which each fixed pin is sequentially implanted on a plurality of rotation trajectories; and a plurality of fixed disks different from each of the fixed pins on a movable disk provided rotatably opposite to the fixed disk. A defibrating and disintegrating apparatus comprising: a movable impact milling means in which respective movable pins are sequentially implanted on the rotation trajectory; and a takeout means for taking out a crushed and flocculent fiber-like small piece to be processed into an outlet.
【請求項11】酸化チタン5〜60wt%に、含有水分量を3w
t%以内とし平均繊維径5〜300μm、平均繊維長0.1〜70mm
のパルプ及び/又は紙40〜95wt%の割合で配合して成る
光触媒パルプ組成物に対してバージンパルプ又は古紙パ
ルプを積層し、任意幅に切断して成る積層光触媒パルプ
紙を撚糸して成ることを特徴とする紙紐。
11. A titanium oxide having a water content of 3w to 5-60wt%.
within 5%, average fiber diameter 5 ~ 300μm, average fiber length 0.1 ~ 70mm
A virgin pulp or waste paper pulp is laminated on a photocatalytic pulp composition blended at a ratio of 40 to 95 wt% of pulp and / or paper, and the laminated photocatalytic pulp paper obtained by cutting to an arbitrary width is twisted. A paper string characterized by the following.
【請求項12】前記積層光触媒パルプ紙を幅5〜50mmに
切断し、ロール状に巻き取った後、撚糸することを特徴
とする請求項11記載の光触媒パルプ紙から成る紙紐の
製造方法。
12. The method according to claim 11, wherein the laminated photocatalytic pulp paper is cut into a width of 5 to 50 mm, wound into a roll, and then twisted.
【請求項13】前記紙紐を同一平面上において、複数本
重畳してなる平紐である請求項11記載の紙紐から成る
成形体。
13. A molded article made of a paper cord according to claim 11, wherein said molded article is a flat cord formed by superposing a plurality of said paper cords on the same plane.
【請求項14】請求項11記載の紙紐を横糸とし、縦糸
を天然又は化学繊維から成る糸として成る織物である請
求項1記載の紙紐から成る成形体。
14. A molded article comprising the paper cord according to claim 1, wherein the paper cord according to claim 11 is a woven fabric comprising a weft yarn and the warp yarn a yarn comprising a natural or chemical fiber.
【請求項15】請求項11,13及び14記載の成形体
のいずれか2種又は3種の組み合わせから成る請求項11
記載の紙紐から成る成形体。
15. A molded article according to claim 11, 13 or 14 comprising a combination of two or three kinds.
A molded article comprising the paper cord according to any one of the preceding claims.
JP2000182179A 1999-08-20 2000-06-16 Laminated photocatalytic pulp paper and method for producing the same, paper string made of the laminated photocatalytic pulp paper, method for producing the same, and molded article made of the paper string Expired - Fee Related JP4634573B2 (en)

Priority Applications (15)

Application Number Priority Date Filing Date Title
JP2000182179A JP4634573B2 (en) 1999-08-20 2000-06-16 Laminated photocatalytic pulp paper and method for producing the same, paper string made of the laminated photocatalytic pulp paper, method for producing the same, and molded article made of the paper string
NO20005869A NO20005869L (en) 2000-06-16 2000-11-21 Laminated photocatalytic pulp paper and process for making the same
CA 2326608 CA2326608A1 (en) 2000-06-16 2000-11-22 Laminated photocatalytic pulp paper and process for producing the same as well as splitting and disaggregating apparatus using for the process, paper string comprising the laminated photocatalytic pulp paper and process for producing the same and molded article comprising the paper string
EP20000125713 EP1164221B1 (en) 2000-06-16 2000-11-23 Laminated photocatalytic paper, process for preparing and molded article comprising the paper
KR1020000069839A KR100627437B1 (en) 2000-06-16 2000-11-23 Multi-layered photocatalyst pulp paper and its manufacturing method, separation and decomposing apparatus used in the production method, paper string made of the laminated photocatalyst pulp paper and manufacturing method thereof, and molded body made of the paper string
ES00125713T ES2216804T3 (en) 2000-06-16 2000-11-23 LAMINATED PHOTOCATALYTIC PAPER, PROCESS FOR PREPARATION AND MOLDED ARTICLE UNDERSTANDING PAPER.
AT00125713T ATE263279T1 (en) 2000-06-16 2000-11-23 MULTI-LAYER PHOTOCATALYTIC PAPER, METHOD OF PRODUCTION AND MOLDING INCLUDING THE PAPER
DE2000609471 DE60009471T2 (en) 2000-06-16 2000-11-23 Multilayered photocatalytic paper, method of manufacture and molding containing the paper
CNB001346288A CN1318698C (en) 2000-06-16 2000-11-24 Laminated photocatalysis paper and producing process and device, paper-tape and producing tecnology and product
TW89125081A TW546434B (en) 2000-06-16 2000-11-24 Laminated photocatalytic pulp paper and process for producing the same as well as splitting and disaggregating apparatus using for the process, paper string comprising the laminated photocatalytic pulp paper and process for producing the same and molded
US09/718,375 US6673207B1 (en) 2000-06-16 2000-11-24 Laminated photocatalytic pulp paper and process for making thereof
BR0005963A BR0005963A (en) 2000-06-16 2000-11-24 Photocatalytically laminated pulp paper and the process for producing it, as well as the division and disaggregation apparatus used for the process; cord made with paper including photocatalytically laminated pulp paper and process for producing it; and molded article comprising the cord made with paper
MXPA00011630 MXPA00011630A (en) 2000-06-16 2000-11-24 Laminated photocatalyst pulp paper, its manufacturing method and defibrator used in the process, paper string comprising laminated photocatalyst pulp paper and its manufacturing method, and formed article comprising the paper string.
HK02104230.0A HK1042930B (en) 2000-06-16 2002-06-04 Laminated photocatalytic pulp paper and process for producing the same as well as paper string and process for producing the same and paper product comprising the paper string
US10/749,413 US20040140071A1 (en) 2000-06-16 2004-01-02 Laminated photocatalytic pulp paper and process for producing the same as well as splitting and disaggregating apparatus using for the process, paper string comprising the laminated photocatalytic pulp paper and process for producing the same and molded article comprising the paper string

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JP11-234790 1999-08-20
JP23479099 1999-08-20
JP2000182179A JP4634573B2 (en) 1999-08-20 2000-06-16 Laminated photocatalytic pulp paper and method for producing the same, paper string made of the laminated photocatalytic pulp paper, method for producing the same, and molded article made of the paper string

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