JP4621469B2 - Adsorption sheet and manufacturing method thereof - Google Patents

Adsorption sheet and manufacturing method thereof Download PDF

Info

Publication number
JP4621469B2
JP4621469B2 JP2004300100A JP2004300100A JP4621469B2 JP 4621469 B2 JP4621469 B2 JP 4621469B2 JP 2004300100 A JP2004300100 A JP 2004300100A JP 2004300100 A JP2004300100 A JP 2004300100A JP 4621469 B2 JP4621469 B2 JP 4621469B2
Authority
JP
Japan
Prior art keywords
paper
porous particles
sheet
binder
bamboo charcoal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP2004300100A
Other languages
Japanese (ja)
Other versions
JP2006112000A (en
Inventor
啓栄 上井
Original Assignee
株式会社タナック
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 株式会社タナック filed Critical 株式会社タナック
Priority to JP2004300100A priority Critical patent/JP4621469B2/en
Publication of JP2006112000A publication Critical patent/JP2006112000A/en
Application granted granted Critical
Publication of JP4621469B2 publication Critical patent/JP4621469B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Description

本発明は吸着シートおよびその製造法に関する。   The present invention relates to an adsorption sheet and a method for producing the same.

特公昭56−49608号公報Japanese Examined Patent Publication No. 56-49608 特開2002−69895号公報JP 2002-69895 A 特開2003−118024号公報Japanese Patent Laid-Open No. 2003-118024 特開平10−314580号公報Japanese Patent Laid-Open No. 10-314580

特許文献1には、活性炭シートを湿式抄紙法で製造するに際し、天然セルロース繊維の水中分散液に、該セルロース繊維の0.0〜0.5重量%のポリエチレンイミン及び10〜95重量%の活性炭を添加する製造法が開示されている。この場合、活性炭の割合は、シート全体の約5〜48重量%程度である。また、活性炭を繊維間に充分に保持させるために、天然ゴムラテックス又は合成ゴムラテックス等の活性炭の凝集剤を添加することが開示されている。また、実施例1において、シートマシンによる手抄きで製造することが開示されている。   In Patent Document 1, when an activated carbon sheet is produced by a wet papermaking method, 0.0 to 0.5% by weight of polyethyleneimine and 10 to 95% by weight of activated carbon are added to a dispersion of natural cellulose fibers in water. A manufacturing method for adding is disclosed. In this case, the ratio of activated carbon is about 5 to 48% by weight of the entire sheet. Also, it is disclosed that an aggregating agent of activated carbon such as natural rubber latex or synthetic rubber latex is added in order to sufficiently retain the activated carbon between the fibers. In Example 1, it is disclosed that the sheet is manufactured by hand-drawing with a sheet machine.

特許文献2には、竹炭微粉末を含有する和紙本体と、その和紙本体の少なくとも一面に散布状態に定着する竹酢成分とからなる消臭用炭シートが開示されている。さらに和紙パルプに竹炭微粉末を混合して、液状バインダを所要量混合し、和紙漉き枠を用いて和紙を漉き、得られた和紙を剥離して乾燥させる製造法も開示されている。竹炭微粉末は100メッシュ以上、299メッシュ以内が好ましいこと、原料に竹炭微粉末を混合する割合は30%ないし40%であること(和紙パルプ:竹炭微粉末=7:3あるいは6:4など)、水溶性糊剤としてのバインダ(液)の混入量は15ないし25%であることも開示されている。また、和紙本体の竹炭微粉末の含有量は、40〜70g/1平方メートルとするのが望ましいことが開示されている。   Patent Document 2 discloses a deodorizing charcoal sheet comprising a Japanese paper main body containing bamboo charcoal fine powder and a bamboo vinegar component fixed in a sprayed state on at least one surface of the Japanese paper main body. Further, a manufacturing method is disclosed in which bamboo paper charcoal fine powder is mixed with Japanese paper pulp, a required amount of liquid binder is mixed, Japanese paper is spread using a Japanese paper-making frame, and the obtained Japanese paper is peeled off and dried. Bamboo charcoal fine powder is preferably 100 mesh or more and within 299 mesh, and the ratio of mixing bamboo charcoal fine powder to the raw material is 30% to 40% (Japanese paper pulp: bamboo charcoal fine powder = 7: 3 or 6: 4, etc.) It is also disclosed that the amount of binder (liquid) as a water-soluble paste is 15 to 25%. Moreover, it is disclosed that the content of the fine powder of bamboo charcoal in the Japanese paper body is desirably 40 to 70 g / 1 square meter.

他方、特許文献3には、古紙やパルプなどのセルロース繊維を打解して水中に溶解した分散液を湿式抄紙法により漉いて帯状の抄紙に形成し、その上に木材や竹材などから形成した多孔性炭化物の微粉末を均一に散布し、その上にさらに湿式抄紙法により形成した別の帯状の抄紙を重ね、全体を圧着ロールおよび乾燥ロールに通して形成した積層シートが開示されている。積層シートは接着剤などで一体に接着されている。また、特許文献3には、セルロース繊維に多孔性の微粉末を混入、攪拌した溶液から形成した微粉炭入りの抄紙を中間層として用いることも開示されている。これらは紙の表面層の間に竹炭の微粉末あるいは微粉炭入りの抄紙をサンドイッチにした3層の積層シートである。微粉末を挟む場合は2g/m2程度、微粉炭入りの抄紙の場合は10g/m2程度が適量とされている。 On the other hand, in Patent Document 3, a dispersion liquid in which cellulose fibers such as waste paper and pulp are beaten and dissolved in water is spun by a wet paper making method to form a belt-like paper, and then formed from wood, bamboo, or the like. There is disclosed a laminated sheet in which a fine powder of porous carbide is uniformly sprayed, another belt-like paper formed by a wet papermaking method is further stacked thereon, and the whole is passed through a pressure roll and a drying roll. The laminated sheets are bonded together with an adhesive or the like. Patent Document 3 also discloses that papermaking containing pulverized coal formed from a solution obtained by mixing and stirring porous fine powder into cellulose fibers is used as an intermediate layer. These are three-layer laminate sheets in which bamboo charcoal fine paper or papermaking containing pulverized coal is sandwiched between paper surface layers. An appropriate amount is about 2 g / m 2 in the case of sandwiching fine powder, and about 10 g / m 2 in the case of papermaking with pulverized coal.

また、特許文献4には、和紙の間に竹炭粉末と糊との混合物を挟んで加熱圧縮した3層構造のシート材およびボード材が開示されている。   Patent Document 4 discloses a sheet material and a board material having a three-layer structure in which a mixture of bamboo charcoal powder and glue is sandwiched between Japanese paper and heated and compressed.

特許文献1の活性炭シートは、活性炭がシート全体の5〜48重量%であるので、活性炭の効果が充分でない。特許文献2の炭シートの場合も、竹炭微粉末が30〜40重量%程度であり、竹炭の消臭効果が充分でない。他方、特許文献3および特許文献4の場合は、表面に紙の層が形成されているので、印刷ができる利点はあるが、竹炭の含有量が少なく、表面に露出していないので、吸着作用などの竹炭の脱臭作用や浄化作用が低くなる。   Since the activated carbon sheet of Patent Document 1 is 5 to 48% by weight of the activated carbon, the effect of the activated carbon is not sufficient. Also in the case of the charcoal sheet of Patent Document 2, bamboo charcoal fine powder is about 30 to 40% by weight, and the deodorizing effect of bamboo charcoal is not sufficient. On the other hand, in the case of Patent Document 3 and Patent Document 4, since a paper layer is formed on the surface, there is an advantage that printing is possible, but since the content of bamboo charcoal is small and not exposed on the surface, the adsorption action The deodorizing action and purification action of bamboo charcoal etc. become low.

本発明は吸着作用が高く、リサイクルや廃棄処理が容易で、環境負荷が少ない吸着シートを提供することを技術課題としている。さらに本発明は、その吸着シートを効率的に製造することができ、しかも種々の厚さのものを容易に製造しうる吸着シートの製造法を提供することを技術課題としている。   An object of the present invention is to provide an adsorption sheet that has a high adsorption action, is easy to recycle and discard, and has a low environmental load. Furthermore, it is a technical object of the present invention to provide a method for producing an adsorbing sheet that can efficiently produce the adsorbing sheet and that can easily produce various thicknesses.

本発明の吸着シートは、竹炭を粉砕した多孔質粒子60〜90wt%と、植物性パルプ10〜40wt%と、前記多孔質粒子と植物性パルプとを合わせた重量の1〜3%の重量のバインダとを水中で混合し、その混合液内で内部を負圧にした丸網抄紙機の円筒状の金網を回転させて、その金網の外表面に複数回抄紙する操作を繰り返して多数の抄紙の層を形成することにより、各抄紙の層の内部および上下の抄紙の層の間に前記多孔質粒子を保持させたことを特徴としている(請求項1)。
本発明の吸着シートの第2の態様は、竹炭を粉砕した多孔質粒子60〜90wt%と、植物性パルプ10〜40wt%と、使用する水1リットル当たり5gのバインダとを水中で混合し、その混合液内で内部を負圧にした丸網抄紙機の金網を回転させて、その金網の外表面に複数回抄紙する操作を繰り返して多数の抄紙の層を形成することにより、各抄紙の層の内部および上下の抄紙の層の間に前記多孔質粒子を保持させたことを特徴としている(請求項2)。
これらの吸着シートでは、前記竹炭の粉砕前の表面電気抵抗が50Ω/cm以下であるものが好ましい(請求項3)。さらに前記バインダが天然ゴムラテックスであるものが好ましい(請求項4)。吸着シートはたとえば厚さ0.5〜10mm程度とする。
The adsorbing sheet of the present invention has a weight of 1 to 3% of the total weight of the porous particles obtained by pulverizing bamboo charcoal 60 to 90 wt%, the vegetable pulp 10 to 40 wt%, and the porous particles and the vegetable pulp. A large number of papermaking is performed by rotating a cylindrical wire net of a round net paper machine with a binder mixed in water and negative pressure inside the mixed liquid, and making paper on the outer surface of the metal net multiple times. By forming this layer, the porous particles are held inside each paper-making layer and between the upper and lower paper-making layers (claim 1).
The second aspect of the adsorbing sheet of the present invention is a mixture of porous particles 60 to 90 wt% pulverized bamboo charcoal, 10 to 40 wt% vegetable pulp, and 5 g of binder per liter of water used in water. By rotating the wire net of a round net paper machine with a negative pressure inside the mixed liquid and repeating the operation of making a plurality of times on the outer surface of the metal net, a number of paper making layers are formed. The porous particles are held in the inner layer and between the upper and lower papermaking layers (claim 2).
In these adsorbent sheets, those having a surface electrical resistance before pulverization of the bamboo charcoal of 50 Ω / cm or less are preferred (Claim 3). Further, it is preferable that the binder is natural rubber latex. For example, the suction sheet has a thickness of about 0.5 to 10 mm.

本発明の吸着シートの製造法は、竹炭を粉砕した多孔質粒子60〜90wt%と、植物性パルプ10〜30wt%と、前記多孔質粒子と植物性パルプとを合わせた重量の1〜3%の重量のバインダまたは使用する水1リットル当たり5gのバインダとを水中で混合し、その混合液内で内部を負圧にした丸網抄紙機の金網を回転させて、その金網の外表面に複数回抄紙する操作を繰り返して多数の抄紙の層を形成し、乾燥させることを特徴としている(請求項5)。
The production method of the adsorbing sheet of the present invention is as follows: porous charcoal 60 to 90 wt% pulverized bamboo charcoal, vegetable pulp 10 to 30 wt%, and 1 to 3% of the total weight of the porous particles and vegetable pulp A binder of 5 g per liter of water or a binder of 5 g per 1 liter of water to be used is mixed in water, and the wire net of a round net paper machine having a negative pressure inside is rotated in the mixed solution, and the outer surface of the metal net is rotated. A plurality of papermaking operations are repeated to form a number of papermaking layers and dried (claim 5).

本発明の吸着シート(請求項1)および第2の態様(請求項2)は、竹炭を粉砕した多孔質粒子を60〜90wt%と多量に含有しているので、従来のものに比して吸着作用が高い。そのため、脱臭作用や空気浄化作用が高い。さらに竹炭の多孔質粒子が抄紙の層の内部および抄紙の層の間に保持するので、バインダーが少なくても、多量の多孔質粒子を含有できる。また、竹酢成分が多い場合は、抗菌作用ないし殺菌作用も得られる。さらに材料が竹炭と植物性パルプを主体としており、接着剤などを使用していないため、粉砕されて得られる多孔質粒子の微細な孔が詰まりにくく、吸着作用が高い。さらに天然材料が主成分であるので、そのまま廃棄することができ、さらに畑などの土壌改良材などとして土中に散布して再利用することも可能である。 Since the adsorbing sheet (Claim 1) and the second aspect (Claim 2) of the present invention contain a large amount of porous particles obtained by pulverizing bamboo charcoal, such as 60 to 90 wt%, compared to conventional ones. Adsorption is high. Therefore, the deodorizing action and the air purification action are high. Further, since the bamboo charcoal porous particles are retained inside and between the papermaking layers, a large amount of porous particles can be contained even if there is little binder. Moreover, when there are many bamboo vinegar components, an antibacterial action or a bactericidal action is also obtained. Furthermore, since the materials are mainly bamboo charcoal and vegetable pulp and no adhesive is used, the fine pores of the porous particles obtained by pulverization are not easily clogged, and the adsorbing action is high. Furthermore, since a natural material is a main component, it can be discarded as it is, and it can also be reused by being sprayed into the soil as a soil improvement material for a field or the like.

このような吸着シートにおいて、前記抄紙の操作が複数回行われているのでシートの厚さが0.5〜10mmとなっている場合でも柔軟性が損なわれず、しかも比較的厚いので、紙として用いるだけでなく、天井裏や壁の下地など、種々の用途に採用することができる。また、抄紙の操作が複数回行われていることから、薄く剥いで使用することもでき、厚いまま使用することもできる。さらに廃棄時に薄く剥いで細分化しやすい。そのため、畑の土壌改良材として容易に再利用できる。 In such a suction sheet, since the operation of the paper is being performed multiple times, it does not lose its flexibility even if the thickness of the sheet is in the 0.5 to 10 mm, and since a relatively thick paper It can be used for various purposes such as ceilings and wall foundations. Further, since the papermaking operation is performed a plurality of times, it can be used by being peeled thinly or can be used as it is thick. Furthermore, it is easy to subdivide by thinly peeling at the time of disposal. Therefore, it can be easily reused as a soil conditioner for fields.

また前記竹炭の粉砕前の表面電気抵抗が50Ω/cm以下である場合(請求項3)は、竹炭の炭素純度が高く、粉砕後の粉末でもタールなどの不純物が少ない。そのため、粉砕された竹炭の多孔質粒子の微細な孔が詰まりにくく、吸着作用が一層高い。   When the surface electrical resistance before pulverization of the bamboo charcoal is 50 Ω / cm or less (Claim 3), the carbon purity of the bamboo charcoal is high, and even the powder after pulverization has few impurities such as tar. Therefore, the fine pores of the pulverized bamboo charcoal porous particles are less likely to be clogged, and the adsorption action is even higher.

前記バインダが天然ゴムラテックスである場合(請求項4)は、シート全体を天然材料(植物材料)で構成することができるので、廃棄時の環境負荷が一層低い。   When the binder is a natural rubber latex (Claim 4), the entire sheet can be made of a natural material (plant material), so that the environmental load at the time of disposal is further reduced.

本発明の吸着シートの製造法(請求項5)によれば、前述の吸着シートを効率よく製造することができる。   According to the manufacturing method of the suction sheet of the present invention (Claim 5), the above-mentioned suction sheet can be efficiently manufactured.

つぎに図面を参照しながら本発明の吸着シートおよびその製造法の実施の形態を説明する。図1は本発明の吸着シートの一実施形態を示す斜視図、図2はその吸着シートの断面図、図3は本発明に用いる多孔質粒子の製造法の一実施形態を示す工程図、図4は本発明の吸着シートの製造法の一実施形態を示す工程図である。   Next, embodiments of the suction sheet and the manufacturing method thereof according to the present invention will be described with reference to the drawings. FIG. 1 is a perspective view showing an embodiment of the adsorbing sheet of the present invention, FIG. 2 is a cross-sectional view of the adsorbing sheet, FIG. 3 is a process diagram showing an embodiment of the method for producing porous particles used in the present invention, and FIG. 4 is a process diagram showing an embodiment of the method for producing an adsorbing sheet of the present invention.

図1に示す吸着シート10は、竹炭を粉砕した多孔質粒子11と、植物性パルプ12とを主成分とするシートであり、図2に示すように多層の抄紙層13の積層状態になっている。吸着シート10には少量のバインダも含まれている。多孔質粒子11の割合は全体の60〜90wt%で、とくに75〜85wt%程度が好ましい。植物性パルプ12の割合は、残りの40〜10wt%、好ましくは15〜25wt%程度である。使用するバインダは、たとえば多孔質粒子11と植物性パルプ12を合わせた重量の1〜3%程度であるが、抄紙するときの水中に分散するので、得られる吸着シート10には微量が残るだけである。なお図1の符号14は吸着シート10を引き破ったときに現れる植物性パルプ12の繊維端である。   An adsorbing sheet 10 shown in FIG. 1 is a sheet mainly composed of porous particles 11 obtained by pulverizing bamboo charcoal and vegetable pulp 12, and is in a laminated state of a plurality of papermaking layers 13 as shown in FIG. Yes. The adsorption sheet 10 also includes a small amount of binder. The ratio of the porous particles 11 is 60 to 90 wt% of the whole, and particularly preferably about 75 to 85 wt%. The proportion of the vegetable pulp 12 is the remaining 40 to 10 wt%, preferably about 15 to 25 wt%. The binder to be used is, for example, about 1 to 3% of the total weight of the porous particles 11 and the vegetable pulp 12, but since it is dispersed in the water when making paper, only a trace amount remains in the obtained adsorption sheet 10. It is. In addition, the code | symbol 14 of FIG. 1 is the fiber end of the vegetable pulp 12 which appears when the adsorption sheet 10 is torn.

前記多孔質粒子11は、図3に示すように、竹炭を製造して粉砕機ないし微粉砕機で平均粒径10〜500μm程度まで粉砕したものが用いられる。平均粒径が500μmより大きい場合は、多孔質粒子11が植物性パルプ12に付着しにくい。そのため、全体の付着量が少なくなりがちである。逆に平均粒径が10μmより小さい場合は、植物性パルプ12の表面に充分に付着するが、薄く付着することになり、多孔質粒子の付着量が全体として少なくなりがちである。   As shown in FIG. 3, the porous particles 11 are made of bamboo charcoal and pulverized to an average particle size of about 10 to 500 μm by a pulverizer or fine pulverizer. When the average particle diameter is larger than 500 μm, the porous particles 11 are difficult to adhere to the vegetable pulp 12. Therefore, the total amount of adhesion tends to be reduced. On the contrary, when the average particle size is smaller than 10 μm, it adheres sufficiently to the surface of the vegetable pulp 12, but it adheres thinly, and the amount of porous particles attached tends to decrease as a whole.

竹炭の材料の生竹(図3の第1ステップS1の符号15参照)としては、孟宗竹、真竹、淡竹など、微小な孔を多数有するものが好ましく、生育年数が3〜5年の竹がとくに好ましい。このような生竹は乾燥させ、第1ステップS1のように半割りにした上で、炭焼き用の焼成炉16中で、700〜900℃で蒸し焼きにして竹炭とする(第2ステップS2)。焼成路16は空気取り入れ口に調整弁17を備え、ガスバーナー18で着火させるものなどが用いられる。炭化処理が完了すると、得られた竹炭にブラシをかけ、洗浄する(第3ステップS3)する。そして前述のように微粉砕機などで粉砕する(第4ステップS4)。   As the raw bamboo material (see reference numeral 15 in the first step S1 in FIG. 3), those having a large number of fine holes, such as 孟 宗 bamboo, true bamboo, and light bamboo, are preferred, and bamboo having a growth age of 3 to 5 years is particularly preferable. preferable. Such raw bamboo is dried and halved as in the first step S1, and then steamed and burned at 700 to 900 ° C. in the baking furnace 16 for charcoal (second step S2). The firing path 16 is provided with a regulating valve 17 at the air intake and is ignited by a gas burner 18. When the carbonization process is completed, the obtained bamboo charcoal is brushed and washed (third step S3). And as mentioned above, it grind | pulverizes with a fine grinder etc. (4th step S4).

なお、焼成炉16で焼くと、始めは温度が上昇していき、90〜110℃程度で一旦温度が安定する。そしてさらに焼成を続けると、500〜700℃程度で再び温度が一定になる。このように温度が段階的に変化するのは、始めの90〜110℃の段階では生竹から水分が蒸発し、竹酢液が抽出されるためと考えられ、つぎの500〜700℃の段階では、タールが抽出されて蒸発するためと考えられる。したがって炭焼きの最終温度は少なくとも750℃以上とするのが好ましい。   In addition, when baking with the baking furnace 16, a temperature will rise first, and temperature will once stabilize at about 90-110 degreeC. And if baking is further continued, temperature will become constant again at about 500-700 degreeC. The reason why the temperature changes stepwise in this way is considered to be that water is evaporated from the raw bamboo in the first 90 to 110 ° C. stage, and the bamboo vinegar is extracted, and the next 500 to 700 ° C. stage. Then, it is considered that tar is extracted and evaporated. Therefore, the final temperature of charcoal baking is preferably at least 750 ° C. or higher.

炭焼きのための時間は使用する生竹15の重量により異なるが、通常は12〜18時間程度、より好ましくは14〜15時間程度である。焼成炉16の内部では生竹15の炭化の過程で一酸化炭素が発生し、その一酸化炭素がさらに燃焼して二酸化炭素に変化するので、充分に空気を供給する必要がある。ただし最終工程では酸素濃度を低い状態に維持して灰になることを防ぐ。   The time for charcoal baking varies depending on the weight of the raw bamboo 15 to be used, but is usually about 12 to 18 hours, more preferably about 14 to 15 hours. Inside the firing furnace 16, carbon monoxide is generated during the carbonization of the raw bamboo 15, and the carbon monoxide is further burned and changed to carbon dioxide. Therefore, it is necessary to supply air sufficiently. However, in the final process, the oxygen concentration is kept low to prevent ashing.

上記のように高温で焼くことにより、タールや竹酢液などが分離され、炭素純度が高い竹炭が得られる。この場合の竹炭の表面の電気抵抗は50Ω/cm以下、とくに10Ω/cm以下のものが好ましい。電気抵抗がそれより高い場合は、純度が低く、タールなどの不純物が多いので、多孔質粒子の微細な孔が詰まり、吸着作用が低くなる。竹炭の電気抵抗はたとえば図3の第1ステップS1に想像線19で示すように、テスターの2本の電極棒を数センチメートルの間隔で竹炭の表面に当てて測定する。ちなみに図3の生竹15のままでは通電しない。   By baking at a high temperature as described above, tar, bamboo vinegar, and the like are separated, and bamboo charcoal with high carbon purity is obtained. In this case, the electric resistance of the surface of bamboo charcoal is preferably 50 Ω / cm or less, particularly preferably 10 Ω / cm or less. When the electrical resistance is higher than that, the purity is low and there are many impurities such as tar, so that the fine pores of the porous particles are clogged and the adsorption action is lowered. For example, as shown by an imaginary line 19 in the first step S1 of FIG. 3, the electric resistance of the bamboo charcoal is measured by placing two electrode bars of the tester on the surface of the bamboo charcoal at intervals of several centimeters. Incidentally, no current is supplied with the raw bamboo 15 shown in FIG.

前記植物性パルプ12としては、通常の洋紙の抄紙に用いる米松、杉などの針葉樹から得た晒しパルプが好ましい。パルプの平均長さは2〜3mm程度、平均太さは0.1〜0.2mm程度のものが用いられる。なお、コウゾ、ミツマタ、ガンピなどの和紙のパルプであってもよい。さらに前述の種々の竹から得た竹パルプを用いることもできる。   The vegetable pulp 12 is preferably bleached pulp obtained from conifers such as rice pine and cedar used for ordinary papermaking. A pulp having an average length of about 2 to 3 mm and an average thickness of about 0.1 to 0.2 mm is used. In addition, Japanese paper pulp such as kouzo, mitsumata, and ganpi may be used. Furthermore, bamboo pulp obtained from the various bamboos described above can also be used.

前記バインダとしては、天然ゴムラテックス、コーンスターチなどの植物由来のバインダが好ましい。天然ゴム加硫型のラテックスなども使用しうる。バインダの使用量は前述のように多孔質粒子と植物性パルプの比率、および得ようとするシートの形状維持性などによって異なるが、たとえば多孔質粒子11と植物性パルプ12を合わせた重量の1〜3%程度、あるいは紙するときに用いる水1リットルに対し5g程度である。 The binder is preferably a plant-derived binder such as natural rubber latex or corn starch. Natural rubber vulcanized latex can also be used. The amount of the binder used varies depending on the ratio of the porous particles and the vegetable pulp and the shape maintaining property of the sheet to be obtained as described above. For example, the amount of the binder used is 1 of the total weight of the porous particles 11 and the vegetable pulp 12. about 3%, or about 5g to 1 liter of water to be used when Extract paper.

吸着シート10の厚さは通常は0.5〜10mm程度であるが、厚さ0.5mm以下でもよく、10mm以上に抄紙することもできる。ただし0.5〜10mm程度のシート、とくに3〜5mm程度のシートが取り扱い易いので好ましい。この程度の厚さでは、プレスにより所定の形状に切断することも容易であり、切断後もばらけることが少ない。また、木材など基材の表面にステープラ(ホッチキス)や止めピンなどで容易に接合させることができる。接着剤によって接着することも可能であるが、リサイクルする場合を考えれば、分離しやすい接合手段を用いるのが好ましい。接着剤としては植物由来の糊、たとえばデンプン糊などを用いるのが好ましい。   The thickness of the adsorbing sheet 10 is usually about 0.5 to 10 mm, but it may be 0.5 mm or less, and paper can be made to 10 mm or more. However, a sheet of about 0.5 to 10 mm, particularly a sheet of about 3 to 5 mm is preferable because it is easy to handle. With such a thickness, it is easy to cut into a predetermined shape with a press, and it is less likely to break after cutting. Moreover, it can be easily joined to the surface of a base material such as wood with a stapler (stapler) or a set pin. Although bonding with an adhesive is possible, considering the case of recycling, it is preferable to use a bonding means that is easy to separate. As the adhesive, it is preferable to use plant-derived paste, such as starch paste.

つぎに図4を参照して前記吸着シート10の製造法を説明する。始めに多孔質微粒子11、植物性パルプ12およびバインダ20を準備する(第5ステップS5)。ついでそれらの材料を所定の重量比で抄紙機21の水槽22内に入れ、混合攪拌する(第2ステップS6)。抄紙は複数回行い、全体として厚さ0.5〜10mmの積層状態にする(第3ステップS3)。その場合、1回の抄紙層(図2の符号13)の厚さは乾燥重量で10〜50g/m2程度とする。 Next, a manufacturing method of the suction sheet 10 will be described with reference to FIG. First, the porous fine particles 11, the vegetable pulp 12 and the binder 20 are prepared (fifth step S5). Next, these materials are put in a water tank 22 of the paper machine 21 at a predetermined weight ratio, and mixed and stirred (second step S6). Papermaking is performed a plurality of times to form a laminated state having a thickness of 0.5 to 10 mm as a whole (third step S3). In that case, the thickness of one papermaking layer (reference numeral 13 in FIG. 2) is about 10 to 50 g / m 2 in terms of dry weight.

このような薄い抄紙層を積層する抄紙工程を数十回、好ましくは300〜500回程度繰り返す。それにより図2に示すような多層構造の吸着シート10が得られる。この吸着シート10では、多孔質粒子11は抄紙層13の内部だけでなく、上下の抄紙層13の間にも挟まれて保持される。そのため多孔質微粒子11の割合が60〜90%と高い比率でも、安定して担持される。   The paper making process of laminating such thin paper making layers is repeated several tens of times, preferably about 300 to 500 times. Thereby, the adsorption sheet 10 having a multilayer structure as shown in FIG. 2 is obtained. In the adsorption sheet 10, the porous particles 11 are held not only inside the paper making layer 13 but also between the upper and lower paper making layers 13. Therefore, even when the proportion of the porous fine particles 11 is as high as 60 to 90%, the particles are stably supported.

このような多数回の抄紙を繰り返しを効率的に行うには、丸網抄紙機を用いるのが好ましい。丸網抄紙機はたとえば図3の第6ステップS6に示すように、水槽22と、その水槽内に水平軸回りに回転自在に支持される円筒状の金網23と、その金網の内部を負圧にするポンプなどの吸引手段24とを備えている。したがって長いシートを形成することはできないが、金網23の内部側を負圧にしながら回転させ、金網23の表面に何回も薄い抄紙の層を形成することができる。そのため、厚さは比較的任意に設定することができる。   In order to efficiently repeat such many times of paper making, it is preferable to use a round net paper machine. For example, as shown in the sixth step S6 of FIG. 3, the round net paper machine has a water tank 22, a cylindrical wire mesh 23 supported in the water tank so as to be rotatable about a horizontal axis, and a negative pressure inside the wire mesh. And a suction means 24 such as a pump. Therefore, a long sheet cannot be formed, but a thin paper layer can be formed many times on the surface of the wire mesh 23 by rotating the inside of the wire mesh 23 while applying a negative pressure. Therefore, the thickness can be set relatively arbitrarily.

上記の抄紙・積層工程(第6ステップS6)により、金網23の周囲に円筒状(無端状)のシート25が形成される。その後、金網23ごと得られたシート2を引き上げ、一個所に切れ目を入れて矩形状のシート25を得る(第4ステップS4)。得られたシート25は第7ステップS7で乾燥機に通し、乾燥させる。それにより図1および図4に示すような吸着シート10が得られる。充分に乾燥させると、吸着シート10同士を重ねても、繊維同士が絡んでシートがくっつくことはない。
A cylindrical (endless) sheet 25 is formed around the wire mesh 23 by the paper making / laminating process (sixth step S6). Thereafter, pulling the sheet 2 5 obtained with wire mesh 23 us to obtain a rectangular sheet 25 scored in one place (fourth step S4). The obtained sheet 25 is passed through a dryer in the seventh step S7 and dried. Thereby, the suction sheet 10 as shown in FIG. 1 and FIG. 4 is obtained. When sufficiently dried, even if the adsorbing sheets 10 are stacked, the fibers are not entangled and the sheets do not stick together.

得られた吸着シート10は図2に示すように、多数の薄い紙状ないし綿状の抄紙層13を重ねた積層形態を呈する。そしてバインダの使用量が少ないので、柔軟で、張り(コシ)が弱く、紙というより綿を押し潰したような外観を呈している。そして数ミリメートルの厚さのものでも、簡単に折れ曲がり、1mm以下の薄い吸着シート10では、引きちぎることも容易である。引きちぎると図1に示すように、端縁に植物性パルプの繊維の端部14が現れる。またバインダの使用量が少なく、多孔質粒子11の使用量が多いため、層間の結合力も弱く、図2の想像線で示すように、表層13aを指で摘んで引っ張れば、簡単に引き剥がすことができる。   As shown in FIG. 2, the obtained adsorbing sheet 10 has a laminated form in which a number of thin paper-like or cotton-like paper-making layers 13 are stacked. And since there is little usage-amount of a binder, it is flexible, its tension (weakness) is weak, and it has the appearance which crushed cotton rather than paper. Even a thickness of several millimeters is easily bent, and the thin suction sheet 10 of 1 mm or less can be easily torn off. When it is torn off, as shown in FIG. 1, the end 14 of the fiber of the vegetable pulp appears at the end edge. Also, since the amount of binder used is small and the amount of porous particles 11 used is large, the bonding force between the layers is also weak, and as shown by the imaginary line in FIG. 2, if the surface layer 13a is picked and pulled, it can be easily peeled off. Can do.

さらにいずれの場合でも、剥がしたり引きちぎったりすると、バインダと植物性パルプ12の繊維で緩く接合されていた多孔質粒子11がバラバラとこぼれ落ちる。また、引きちぎった細片をさらに細かくほぐすと、ほとんどの多孔質粒子11がバラバラになり、表面に多孔質粒子11が薄く付着している綿状の繊維の塊が残る。このように吸着シート10自体はほとんど強度が期待できないので、木材や金網などの他の基材に貼り付けて使用する。   Furthermore, in any case, when the film is peeled off or torn, the porous particles 11 loosely bonded with the binder and the vegetable pulp 12 fibers fall apart. Further, when the torn pieces are further loosened, most of the porous particles 11 are separated, and a lump of cotton-like fibers having the porous particles 11 thinly adhered to the surface remains. As described above, since the suction sheet 10 itself cannot be expected to have any strength, it is used by being attached to another base material such as wood or a wire mesh.

上記のようにして形成される吸着シート10は、ロール状に巻き取って販売することもできるが、丸網抄紙機では長いシートを得ることは困難なため、通常は矩形状のシートとして販売する。所定の形状に切断して部品として用いることもできる。ロール状のシートないし定尺シートで販売する場合は、たとえば建築物の床材や天井材、壁材などの基材に貼り付けて使用する。それにより接着剤などから分離したホルムアルデヒド、その他のシックハウスの原因となる化学物質を吸着させることができる。吸着シートを貼り付ける基材は木材、パーティクルボード、石膏ボードなどがあげられる。   Although the suction sheet 10 formed as described above can be rolled up and sold, it is difficult to obtain a long sheet with a round net paper machine, and is usually sold as a rectangular sheet. . It can also be cut into a predetermined shape and used as a part. When selling as a roll sheet or a regular sheet, for example, it is attached to a base material such as a flooring material, a ceiling material, or a wall material of a building. As a result, it is possible to adsorb formaldehyde separated from the adhesive and other chemical substances that cause sick house. Examples of the base material on which the adsorption sheet is attached include wood, particle board, and gypsum board.

また、所定の形状に切断する場合は、金網の間に挟み込み、エアコンディショナや浄水器のフィルタとして使用したり、家具やキッチン製品の内層材として利用することができる。さらに合成樹脂やステンレスの網で挟んだ状態で浴槽内に沈め、水の浄化に役立てることができる。いずれの場合でも、竹炭が有する吸着作用に加えて、抗菌作用ないし殺菌作用を発揮させることができる。さらに廃棄する場合は、シート状のまま、あるいは細かく裁断した上で、畑の土壌中に埋めたり散布して、土壌改良材として再利用することができる。   Moreover, when cut | disconnecting to a defined shape, it can be pinched | interposed between metal-mesh, and can be used as a filter of an air conditioner or a water purifier, or can be utilized as an inner layer material of furniture or a kitchen product. Furthermore, it can be used to purify water by sinking in a bathtub while sandwiched between synthetic resin and stainless steel nets. In any case, an antibacterial action or a bactericidal action can be exhibited in addition to the adsorption action of bamboo charcoal. Further, when discarded, it can be reused as a soil conditioner by being buried in a field or after being finely cut and then sprayed in the field.

さらに前記吸着シート10は、そのまま利用するほか、吸着シート10同士を積層させて使用したり、通気性および通液性が高いシート、たとえば紙などを積層して積層シートにすることもできる。ただし積層する他のシートも植物性のパルプからなる紙などの天然材料を用い、接着剤も植物性の糊などの天然材料ないし植物性材料用いるのが好ましい。また、吸着シート10に蒸留した竹酢液などを散布することにより、抗菌ないし殺菌効果を増大させることもできる。   Further, the adsorbing sheet 10 can be used as it is, or the adsorbing sheets 10 can be laminated and used, or a sheet having high air permeability and liquid permeability, for example, paper can be laminated to form a laminated sheet. However, it is preferable to use a natural material such as paper made of vegetable pulp for the other sheets to be laminated, and also use a natural material or vegetable material such as vegetable glue for the adhesive. Moreover, antibacterial or sterilizing effect can be increased by spraying distilled bamboo vinegar or the like on the adsorbing sheet 10.

本発明の吸着シートの一実施形態を示す斜視図である。It is a perspective view which shows one Embodiment of the suction sheet of this invention. 図1の吸着シートの断面図である。It is sectional drawing of the adsorption sheet of FIG. 本発明に用いる多孔質粒子の製造法の一実施形態を示す工程図である。It is process drawing which shows one Embodiment of the manufacturing method of the porous particle used for this invention. 本発明の吸着シートの製造法の一実施形態を示す工程図である。It is process drawing which shows one Embodiment of the manufacturing method of the adsorption sheet of this invention.

符号の説明Explanation of symbols

10 吸着シート
11 多孔質粒子
12 植物性パルプ
13 抄紙層
14 繊維の端部
15 生竹
16 焼成炉
17 調整弁
18 ガスバーナー
19 電極棒
20 バインダ
21 抄紙機
22 水槽
23 金網
24 吸引手段
25 シート
DESCRIPTION OF SYMBOLS 10 Adsorption sheet 11 Porous particle 12 Vegetable pulp 13 Papermaking layer 14 End of fiber 15 Raw bamboo 16 Baking furnace 17 Regulating valve 18 Gas burner 19 Electrode rod 20 Binder 21 Paper machine 22 Water tank 23 Wire mesh 24 Suction means 25 Sheet

Claims (5)

竹炭を粉砕した多孔質粒子60〜90wt%と、植物性パルプ10〜40wt%と、前記多孔質粒子と植物性パルプとを合わせた重量の1〜3%の重量のバインダとを水中で混合し、
その混合液内で内部を負圧にした丸網抄紙機の円筒状の金網を回転させて、その金網の外表面に複数回抄紙する操作を繰り返して多数の抄紙の層を形成することにより、各抄紙の層の内部および上下の抄紙の層の間に前記多孔質粒子を保持させた吸着シート。
Porous particles 60 to 90 wt% pulverized bamboo charcoal, vegetable pulp 10 to 40 wt%, and a binder having a weight of 1 to 3% of the total weight of the porous particles and the vegetable pulp are mixed in water. ,
By rotating the cylindrical wire net of the round net paper machine with the negative pressure inside the mixed liquid and repeating the operation of making paper multiple times on the outer surface of the metal net, a large number of paper layers are formed, An adsorption sheet in which the porous particles are held inside each papermaking layer and between the upper and lower papermaking layers.
竹炭を粉砕した多孔質粒子60〜90wt%と、植物性パルプ10〜40wt%と、使用する水1リットル当たり5gのバインダとを水中で混合し、
その混合液内で内部を負圧にした丸網抄紙機の円筒状の金網を回転させて、その金網の外表面に複数回抄紙する操作を繰り返して多数の抄紙の層を形成することにより、各抄紙の層の内部および上下の抄紙の層の間に前記多孔質粒子を保持させた吸着シート。
60 to 90 wt% of porous particles obtained by pulverizing bamboo charcoal, 10 to 40 wt% of vegetable pulp, and 5 g of binder per liter of water used are mixed in water,
By rotating the cylindrical wire net of the round net paper machine with the negative pressure inside the mixed liquid and repeating the operation of making paper multiple times on the outer surface of the metal net, a large number of paper layers are formed, An adsorption sheet in which the porous particles are held inside each papermaking layer and between the upper and lower papermaking layers.
前記竹炭の粉砕前の表面電気抵抗が50Ω/cmである請求項1または2記載の吸着シート。 The adsorption sheet according to claim 1 or 2 whose surface electric resistance before crushing said bamboo charcoal is 50 ohms / cm. 前記バインダが天然ゴムラテックスである請求項1または2記載の吸着シート。 The adsorption sheet according to claim 1 or 2, wherein the binder is natural rubber latex. 竹炭を粉砕した多孔質粒子60〜90wt%と、植物性パルプ10〜30wt%と、前記多孔質粒子と植物性パルプとを合わせた重量の1〜3%の重量のバインダまたは使用する水1リットル当たり5gのバインダとを水中で混合し、
その混合液内で内部を負圧にした丸網抄紙機の円筒状の金網を回転させて、その金網の外表面に複数回抄紙する操作を繰り返して多数の抄紙の層を形成し、
乾燥させる吸着シートの製造方法。
Binder with a weight of 1 to 3% of the combined weight of the porous particles and vegetable pulp, or 60 to 90 wt% of porous particles obtained by pulverizing bamboo charcoal, 10 to 30 wt% of vegetable pulp, and 1 liter of water to be used Per 5 g of binder with water,
Rotate the cylindrical wire mesh of a round net paper machine with negative pressure inside the mixed liquid, and repeat the operation of making paper multiple times on the outer surface of the wire mesh to form a number of paper making layers,
A method for producing an adsorbent sheet to be dried.
JP2004300100A 2004-10-14 2004-10-14 Adsorption sheet and manufacturing method thereof Expired - Fee Related JP4621469B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004300100A JP4621469B2 (en) 2004-10-14 2004-10-14 Adsorption sheet and manufacturing method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004300100A JP4621469B2 (en) 2004-10-14 2004-10-14 Adsorption sheet and manufacturing method thereof

Publications (2)

Publication Number Publication Date
JP2006112000A JP2006112000A (en) 2006-04-27
JP4621469B2 true JP4621469B2 (en) 2011-01-26

Family

ID=36380752

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004300100A Expired - Fee Related JP4621469B2 (en) 2004-10-14 2004-10-14 Adsorption sheet and manufacturing method thereof

Country Status (1)

Country Link
JP (1) JP4621469B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101289822B (en) * 2007-04-20 2010-12-01 石伟 Nano far infrared anion carbon crystal conductive paper and method for preparing same
CN104005272A (en) * 2014-04-25 2014-08-27 蚌埠德美过滤技术有限公司 Glass fiber-containing highly waterproof air filter paper and making method thereof
KR102215615B1 (en) * 2019-05-10 2021-02-15 지리산한지(유) Papers for filter containing activated carbon and method for manufacturing the same

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5649608B2 (en) * 1974-09-06 1981-11-24
JPH08143083A (en) * 1994-11-22 1996-06-04 Fuji Corn Seisakusho:Kk Food distribution container with antibacterial, deodorizing and freshness preserving effects
JPH0913293A (en) * 1995-06-27 1997-01-14 Dainichi Kk Dust coal material and panel material
JPH09173429A (en) * 1995-12-22 1997-07-08 Moruza Kk Sheet container activated carbon particle
JP2001009812A (en) * 1999-06-28 2001-01-16 Takashi Ueda Mixture of cellulose and charcoal and manufacture thereof
JP2001032195A (en) * 1999-07-19 2001-02-06 Oki Kogei:Kk Carbon-containing paper

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5649608B2 (en) * 1974-09-06 1981-11-24
JPH08143083A (en) * 1994-11-22 1996-06-04 Fuji Corn Seisakusho:Kk Food distribution container with antibacterial, deodorizing and freshness preserving effects
JPH0913293A (en) * 1995-06-27 1997-01-14 Dainichi Kk Dust coal material and panel material
JPH09173429A (en) * 1995-12-22 1997-07-08 Moruza Kk Sheet container activated carbon particle
JP2001009812A (en) * 1999-06-28 2001-01-16 Takashi Ueda Mixture of cellulose and charcoal and manufacture thereof
JP2001032195A (en) * 1999-07-19 2001-02-06 Oki Kogei:Kk Carbon-containing paper

Also Published As

Publication number Publication date
JP2006112000A (en) 2006-04-27

Similar Documents

Publication Publication Date Title
TW440433B (en) Sheet tobacco, its manufacturing method, and system
BRPI1012561B1 (en) panels that include renewable components and methods for making them
RU2007107191A (en) THE SMOKED FILLER FROM THE TOBACCO SUBSTITUTION POSSESSING AN INCREASED SPECIFIC VOLUME AND THE METHOD OF ITS PRODUCTION
EP1276610B1 (en) Absorbent sheet material having cut-resistant particles and methods for making the same
KR101633779B1 (en) Panels including renewable components and methods for manufacturing
BRPI1014869B1 (en) Filter material for air and gas cleaning, use of filter material and cigarette filter
JP4621469B2 (en) Adsorption sheet and manufacturing method thereof
CN107206621A (en) Paper pulp fiber accumulates piece and paper pulp fiber accumulates the manufacture method of piece
JP4963832B2 (en) Method for producing charcoal-containing sheet
JP2008169515A (en) Paper
KR101717717B1 (en) Paper adhessive resin composition for enhanced compressive stress
JP2002028415A (en) Air purifying filter
KR100546789B1 (en) Environmental friendly functional base sheet for wallpaper
WO2002025014A1 (en) Processed board-type products made of non-wooden fibers
KR102215615B1 (en) Papers for filter containing activated carbon and method for manufacturing the same
CN1207964C (en) Substance delivery device
CN105746508A (en) Novel smokeless mosquito-repellent incense
KR100632462B1 (en) Wallpaper use nature vegetable long fiber and manufacture method
JP2003305321A (en) Air cleaning filter
JP6073548B2 (en) Humidity control wallpaper
CN102212981A (en) Method for preparing two-layer paper
KR101216992B1 (en) Method and apparatus of manufacturing agricultural cover sheet including nonwoven cloth made of natural material by air floating
JP2005307444A (en) Charcoal-containing tatami mat and its manufacturing method
JP2002067006A (en) Rush material, atricle using the same and method for manufacturing the rush material
JPS6261719B2 (en)

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20071012

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20100212

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100223

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100426

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20100615

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100812

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20101019

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20101101

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

Free format text: PAYMENT UNTIL: 20131105

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4621469

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees