JP2005350292A - Fibrous porous carbonized product and its production method - Google Patents
Fibrous porous carbonized product and its production method Download PDFInfo
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
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Abstract
Description
本発明は、抄紙の生産過程で生ずる残渣を原料とし、良好な吸着力を有する繊維状多孔質炭化物を得る方法及びそれにより得られる繊維状多孔質炭化物に関する。 The present invention relates to a method for obtaining a fibrous porous carbide having a good adsorptive power using a residue generated during the papermaking production process, and a fibrous porous carbide obtained thereby.
従来、和紙等の製造過程で生ずる残渣は、そのごく一部が製紙用原料として再利用されている。しかしながら、日々製紙工場の生産活動から生ずる残渣の量はきわめて多く、その有効な処理方法や利用方法が求められている。処理方法のひとつとして化石燃料を用いて焼却処分することも行われているが、それによってダイオキシン等の有毒物質を発生する危険性も含んでおり、環境保全の観点から早急な対策が望まれている。 Conventionally, a small part of the residue generated in the manufacturing process of Japanese paper or the like is reused as a raw material for papermaking. However, the amount of residue resulting from daily paper mill production activities is extremely large, and there is a need for effective treatment and utilization methods. One of the treatment methods is incineration using fossil fuels, but it also includes the risk of generating toxic substances such as dioxins, and immediate measures are desired from the viewpoint of environmental conservation. Yes.
従って、当該技術分野では、環境への汚染を考慮することなく、焼却廃棄されている抄紙残液を容易に処理することが可能で、かつ当該処理によってできた炭化物も完全に無臭、無害とすることが可能な廃棄物の処理方法が熱望されていた。 Therefore, in this technical field, it is possible to easily treat the papermaking liquor discarded by incineration without considering environmental pollution, and the carbides produced by the treatment are completely odorless and harmless. There is a keen desire for a method for treating waste.
本発明者らは、焼却廃棄物である抄紙残渣の有効利用について研究を重ねた結果、紙漉き残渣と云えども良質なセルロースを含む原料であるとの見方をし、その残渣を炭化処理することによって、ダイオキシン等の有毒物質を発生することなく、繊維状を保ちつつ活性炭の二倍に達する極めて多孔質の炭化物となることを見出した。 As a result of repeated research on the effective use of papermaking residue, which is an incineration waste, the present inventors consider that papermaking residue is a raw material containing high-quality cellulose, and carbonizes the residue. It has been found that, without generating toxic substances such as dioxin, it becomes an extremely porous carbide that doubles the activated carbon while maintaining the fibrous form.
しかも、この炭化処理において、一般の活性炭製造時に行われている賦活処理をすることなく、高い表面積を持つ炭素材料が得られたことは極めて重要であり、そのまま低コストな消臭、脱臭剤としての利用が考えられる。 Moreover, in this carbonization treatment, it is extremely important that a carbon material having a high surface area is obtained without performing the activation treatment that is performed at the time of production of general activated carbon, and as it is a low-cost deodorizing and deodorizing agent as it is. Can be used.
本発明の繊維状多孔質炭化物の製造方法は、抄紙残渣に水を添加して混練分散し、その後、水分を除去して乾燥残渣固形物とし、さらに、この乾燥残渣固形物を低酸素雰囲気下及び/又は不活性ガス雰囲気下で加熱焼成することを特徴とする。本発明の繊維状多孔質炭化物は、上記方法により得られることを特徴とする。 The method for producing the fibrous porous carbide of the present invention is to add water to a papermaking residue and knead and disperse, then remove the water to obtain a dry residue solid, and further, the dry residue solid is subjected to a low oxygen atmosphere. And / or heating and firing in an inert gas atmosphere. The fibrous porous carbide of the present invention is obtained by the above method.
市販の木質系活性炭は、炭素分が約99重量%程度を占め、灰分が1重量%程度と少ない性状を有している。また比表面積や細孔容積を大きくするため、一次炭素化後、薬品賦活処理やガス賦活処理という二次的な処理が行われている。これに対し、本発明の繊維状多孔質炭化物は、賦活処理することなく、一段階の炭素化処理、すなわち、低酸素雰囲気下または不活性ガス雰囲気下での加熱焼成による炭化処理のみで、高い表面積を有する繊維状の炭化物を得ることができる。 Commercially available wood-based activated carbon has about 99% by weight of carbon and low ash content of about 1%. In order to increase the specific surface area and pore volume, secondary treatment such as chemical activation treatment and gas activation treatment is performed after primary carbonization. On the other hand, the fibrous porous carbide of the present invention is high by only one-stage carbonization treatment, that is, carbonization treatment by heating and firing in a low oxygen atmosphere or an inert gas atmosphere without activation treatment. A fibrous carbide having a surface area can be obtained.
後述の実験データから裏付けられるように、本発明による多孔質活性炭化物のアンモニアやホルムアルデヒドガス等の吸着力は、市販されている備長炭や竹炭等の吸着力の倍以上の値を示していて、実用レベルの吸着力を備えた多孔質活性炭化物ということができる。また、活性炭製造時に行われている賦活処理工程が必要でなくなるので、省エネルギーも達成することもできる。 As supported by the experimental data described below, the adsorption power of the porous activated carbide according to the present invention, such as ammonia and formaldehyde gas, shows a value more than double the adsorption power of commercially available Bincho charcoal, bamboo charcoal, etc. It can be said to be a porous activated carbide having a practical level of adsorption power. Moreover, since the activation process process currently performed at the time of activated carbon manufacture becomes unnecessary, energy saving can also be achieved.
図1は本発明の繊維状多孔質炭化物を製造する作業のフローチャートである。図2は、本発明の繊維状多孔質炭化物を焼成する作業の概略図である。 FIG. 1 is a flowchart of an operation for producing the fibrous porous carbide of the present invention. FIG. 2 is a schematic view of an operation for firing the fibrous porous carbide of the present invention.
図1に示すように、本発明の多孔質炭化物は、その原材料が製紙工場より発生する抄紙残渣であるが、その主成分はセルロースを含む各種パルプ類であれば特に限定はない。例えば、針葉樹や広葉樹の木材パルプ、竹、三椏、楮、雁皮などの靭皮繊維、マニラパルプなどの植物繊維、新聞・雑誌等の故紙資源ごみ又はこれらの混合物を利用することができる。 As shown in FIG. 1, the porous carbide of the present invention is a papermaking residue whose raw material is generated from a paper mill, but is not particularly limited as long as its main component is various pulps containing cellulose. For example, coniferous or hardwood wood pulp, bast fibers such as bamboo, three bases, cocoons and husks, plant fibers such as Manila pulp, waste paper resource waste such as newspapers and magazines, or mixtures thereof can be used.
本発明の多孔質炭化物は、セルロースを含む抄紙残渣を焼成し炭素含有量が90重量%以上となるように製造されたものである。 The porous carbide of the present invention is produced by firing a papermaking residue containing cellulose to have a carbon content of 90% by weight or more.
本発明の多孔質炭化物の製造方法を説明する。まず抄紙残渣に水を適宜添加し、攪拌器で混練、分散する。混練分散された抄紙残渣を成型のため例えば円筒形状の容器に入れる。そこで加圧、脱水し、残渣固形物を生成させる。容器より出された残渣固形物の水分除去のため、乾燥機等によって乾燥させ、乾燥残渣固形物を得る。 The manufacturing method of the porous carbide | carbonized_material of this invention is demonstrated. First, water is appropriately added to the papermaking residue and kneaded and dispersed with a stirrer. The kneaded and dispersed papermaking residue is placed in, for example, a cylindrical container for molding. Then, it pressurizes and spin-dry | dehydrates and produces | generates a residue solid substance. In order to remove moisture from the solid residue from the container, it is dried by a dryer or the like to obtain a dry residue solid.
ついで、図2に示すように、容器内部を金属等の遮蔽板で被った状態の容器内に入れて密閉する。この密閉容器を、例えば電気炉等のように加熱温度を自在に変えることができる加熱炉に入れて加熱する。乾燥残渣固形物は固化し、固形物が形成される。このとき、炉内に不活性ガス(窒素、アルゴン等)を送入し、炉内を置換させる。容器内の酸素濃度は低いため、乾燥残渣固形物に含まれる酸素が除去され、その成分中の炭素が固形物に残留される。したがって、固形物内部には空洞が形成されるので、多孔質炭化物を作ることができる。 Next, as shown in FIG. 2, the inside of the container is put in a container covered with a shielding plate such as metal and sealed. This sealed container is heated in a heating furnace in which the heating temperature can be freely changed, such as an electric furnace. The dried residue solids solidify and solids are formed. At this time, an inert gas (nitrogen, argon, etc.) is fed into the furnace to replace the inside of the furnace. Since the oxygen concentration in the container is low, oxygen contained in the dry residue solid is removed, and carbon in the component remains in the solid. Therefore, since a cavity is formed inside the solid material, porous carbide can be made.
密閉した容器の加熱温度は、800℃〜900℃が好適である。もし加熱温度が1000℃以上であれば、多孔性は失われ、繊維同士の接着箇所が増加し、隙間が減少することにより密度が増加し、表面積が減少することが考えられる。加熱時間は、炭化に必要な時間であり、加熱炉の大きさにより異なるが、通常10時間以上であり、15〜30時間が好適である。 The heating temperature of the sealed container is preferably 800 ° C to 900 ° C. If the heating temperature is 1000 ° C. or higher, the porosity is lost, the number of bonding points between fibers increases, the gap decreases, the density increases, and the surface area decreases. The heating time is the time required for carbonization and varies depending on the size of the heating furnace, but is usually 10 hours or longer, and preferably 15 to 30 hours.
上記のごとく、本発明の繊維状多孔質炭化物は、固形物の内部に空洞が形成されるので、大気中の二酸化炭素やアンモニア、ホルムアルデヒド等の悪臭物質や有害物質を吸着することができる。また、前記のような物質だけでなく、すすなどの粒状化物質、畜産農家から発生する異臭の除去にもその吸着効果を発揮することができる。 As described above, the fibrous porous carbide of the present invention has a cavity formed inside the solid, and can adsorb malodorous substances and harmful substances such as carbon dioxide, ammonia and formaldehyde in the atmosphere. Moreover, the adsorption effect can be exhibited not only for the substances as described above but also for removing granulated substances such as soot and off-flavors generated from livestock farmers.
本発明の繊維状多孔質炭化物は、焼却廃棄処分されている抄紙残渣を原料として有効活用することができ、環境汚染防止等の効果を得ることができる。
The fibrous porous carbide of the present invention can effectively utilize the papermaking residue that is disposed of by incineration as a raw material, and can obtain effects such as prevention of environmental pollution.
和紙の抄紙残渣1500gに水を3L添加し、攪拌器で混練、分散させた。混練分散された抄紙残渣を円筒形状の容器に入れ、加圧、脱水し、残渣固形物を生成させた。容器より出された残渣固形物は、水分除去のため、乾燥機等によって乾燥させ、乾燥残渣固形物1500gを得た。この乾燥残渣固形物を密閉した容器に入れ、加熱温度、加熱時間を任意に設定することのできる電気炉内で、24時間850℃で炭化処理し、繊維状多孔質炭化物80gを得た。 3 L of water was added to 1500 g of Japanese papermaking residue, and kneaded and dispersed with a stirrer. The kneaded and dispersed papermaking residue was placed in a cylindrical container, and pressurized and dehydrated to produce a solid residue. Residual solids put out from the container were dried by a drier or the like to remove moisture, to obtain 1500 g of dry residual solids. This dry residue solid was put into a sealed container and carbonized at 850 ° C. for 24 hours in an electric furnace in which the heating temperature and heating time could be arbitrarily set, to obtain 80 g of fibrous porous carbide.
<吸着力比較実験>
1.試料の準備
実施例1で得られた繊維状多孔質炭化物を粉砕し、50μmふるい(325メッシュパス)で篩別を行い、乾燥器で乾燥して得た粉末を試料Aとした。また、市販の消臭用竹炭を比較試料Bとして準備した。
<Adsorption force comparison experiment>
1. Sample Preparation The fibrous porous carbide obtained in Example 1 was pulverized, sieved with a 50 μm sieve (325 mesh pass), and dried in a drier to give Sample A. A commercially available bamboo charcoal for deodorization was prepared as Comparative Sample B.
2.試験方法
試料Aについて、同試料粉末10gを容量2Lのテドラーバッグに入れ、次いで初期濃度の臭気物質を封入密閉した後、ガスクロマトグラフィーで1、2、3、24、48、72時間経過ごとの臭気物質のガス濃度を測定し、その経時変化を調べた。比較試料Bについても同様に試験を行った。
2. Test method For sample A, put 10 g of the same sample powder in a 2 L Tedlar bag, and then seal and seal the initial concentration of odorous substance. The gas concentration of the substance was measured and the change with time was examined. A test was conducted in the same manner for Comparative Sample B.
3.結果
表1−3及び図3−5に示すとおりである。
(表1)
3. Results As shown in Table 1-3 and Figure 3-5.
(Table 1)
アンモニア濃度 (ppm)
経過時間 試料A 試料B
0 20.0 20.0
1 13.9 15.3
2 9.80 13.0.
3 6.90 11.0
24 3.10 8.70
48 1.50 8.00
72 1.30 8.00
(表2)
Ammonia concentration (ppm)
Elapsed time Sample A Sample B
0 20.0 20.0
1 13.9 15.3
2 9.80 13.0.
3 6.90 11.0
24 3.10 8.70
48 1.50 8.00
72 1.30 8.00
(Table 2)
ホルムアルデヒド濃度(ppm)
経過時間 試料A 試料B
0 8.00 8.00
1 5.06 5.70
2 3.65 4.40
3 1.90 3.15
24 0.70 2.00
48 0.65 1.95
72 0.58 1.95
(表3)
Formaldehyde concentration (ppm)
Elapsed time Sample A Sample B
0 8.00 8.00
1 5.06 5.70
2 3.65 4.40
3 1.90 3.15
24 0.70 2.00
48 0.65 1.95
72 0.58 1.95
(Table 3)
ジメチルアミン濃度(ppm)
経過時間 試料A 試料B
0 16.0 16.0
1 9.40 13.5
2 6.50 11.5
3 3.35 9.00
24 0.90 5.50
48 0.30 5.10
72 0.30 4.60
Dimethylamine concentration (ppm)
Elapsed time Sample A Sample B
0 16.0 16.0
1 9.40 13.5
2 6.50 11.5
3 3.35 9.00
24 0.90 5.50
48 0.30 5.10
72 0.30 4.60
これらの表と図から明らかなように、何れの臭気物質に対しても本発明に従った繊維状多孔質炭化物は、竹炭に比較して著しい脱臭効果を示した。 As is apparent from these tables and figures, the fibrous porous carbide according to the present invention showed a significant deodorizing effect compared to bamboo charcoal for any odorous substance.
Claims (5)
The fibrous porous carbide according to claim 4, wherein the carbon content is 90% by weight or more.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2338981A1 (en) * | 2010-01-27 | 2010-05-13 | Universidad Politecnica De Madrid | Absorbent-adsorbent bifunctional material obtained from paper destination sludge, process of obtaining and use. (Machine-translation by Google Translate, not legally binding) |
CN108539154A (en) * | 2018-03-29 | 2018-09-14 | 龙岩学院 | A kind of porous carbon, carbon-selenium composite material and the method for preparing anode with carbon-selenium composite material |
CN109850894A (en) * | 2019-03-20 | 2019-06-07 | 西安理工大学 | A kind of method and application preparing porous carbon materials using useless corrugation paper fiber as raw material |
JP2022502574A (en) * | 2019-09-05 | 2022-01-11 | 韓 建華HAN, Jianhua | Antibacterial non-woven fabric, its manufacturing method, and a mask equipped with this antibacterial non-woven fabric. |
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JPH0465492A (en) * | 1990-07-04 | 1992-03-02 | Norihiro Mitsunaga | Fuel by using old paper residue |
JP2003500322A (en) * | 1999-05-25 | 2003-01-07 | エムビーアール テクノロジーズ,インコーポレイテッド | Rapid activation method, process, and apparatus for making pelletized activated carbon from carbonaceous waste |
JP2003226513A (en) * | 2002-02-05 | 2003-08-12 | Japan Science & Technology Corp | Continuous carbonization system |
JP2004138097A (en) * | 2002-10-15 | 2004-05-13 | Ishizuka Kenkyusho:Kk | Hydrogen storage medium, and method for manufacturing the same |
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2004
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH0465492A (en) * | 1990-07-04 | 1992-03-02 | Norihiro Mitsunaga | Fuel by using old paper residue |
JP2003500322A (en) * | 1999-05-25 | 2003-01-07 | エムビーアール テクノロジーズ,インコーポレイテッド | Rapid activation method, process, and apparatus for making pelletized activated carbon from carbonaceous waste |
JP2003226513A (en) * | 2002-02-05 | 2003-08-12 | Japan Science & Technology Corp | Continuous carbonization system |
JP2004138097A (en) * | 2002-10-15 | 2004-05-13 | Ishizuka Kenkyusho:Kk | Hydrogen storage medium, and method for manufacturing the same |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2338981A1 (en) * | 2010-01-27 | 2010-05-13 | Universidad Politecnica De Madrid | Absorbent-adsorbent bifunctional material obtained from paper destination sludge, process of obtaining and use. (Machine-translation by Google Translate, not legally binding) |
CN108539154A (en) * | 2018-03-29 | 2018-09-14 | 龙岩学院 | A kind of porous carbon, carbon-selenium composite material and the method for preparing anode with carbon-selenium composite material |
CN109850894A (en) * | 2019-03-20 | 2019-06-07 | 西安理工大学 | A kind of method and application preparing porous carbon materials using useless corrugation paper fiber as raw material |
JP2022502574A (en) * | 2019-09-05 | 2022-01-11 | 韓 建華HAN, Jianhua | Antibacterial non-woven fabric, its manufacturing method, and a mask equipped with this antibacterial non-woven fabric. |
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