JP3138749B2 - Method for producing carbides having deodorizing ability, ion exchange ability, and catalytic ability using plant materials - Google Patents
Method for producing carbides having deodorizing ability, ion exchange ability, and catalytic ability using plant materialsInfo
- Publication number
- JP3138749B2 JP3138749B2 JP5600699A JP5600699A JP3138749B2 JP 3138749 B2 JP3138749 B2 JP 3138749B2 JP 5600699 A JP5600699 A JP 5600699A JP 5600699 A JP5600699 A JP 5600699A JP 3138749 B2 JP3138749 B2 JP 3138749B2
- Authority
- JP
- Japan
- Prior art keywords
- ability
- wood
- ion exchange
- carbide
- cellulose
- 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
Links
- 238000005342 ion exchange Methods 0.000 title claims description 19
- 239000000463 material Substances 0.000 title claims description 19
- 230000001877 deodorizing effect Effects 0.000 title claims description 5
- 230000003197 catalytic effect Effects 0.000 title claims description 3
- 238000004519 manufacturing process Methods 0.000 title description 6
- 150000001247 metal acetylides Chemical class 0.000 title description 6
- 239000002023 wood Substances 0.000 claims description 25
- 230000002378 acidificating effect Effects 0.000 claims description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 20
- 239000001913 cellulose Substances 0.000 claims description 20
- 229920002678 cellulose Polymers 0.000 claims description 20
- 239000001301 oxygen Substances 0.000 claims description 20
- 229910052760 oxygen Inorganic materials 0.000 claims description 20
- 239000007789 gas Substances 0.000 claims description 19
- 238000010438 heat treatment Methods 0.000 claims description 16
- 229910052751 metal Inorganic materials 0.000 claims description 13
- 239000002184 metal Substances 0.000 claims description 13
- 229920002472 Starch Polymers 0.000 claims description 12
- 239000000243 solution Substances 0.000 claims description 12
- 239000008107 starch Substances 0.000 claims description 12
- 235000019698 starch Nutrition 0.000 claims description 12
- 239000003513 alkali Substances 0.000 claims description 11
- 238000003763 carbonization Methods 0.000 claims description 9
- 239000007858 starting material Substances 0.000 claims description 6
- 239000002699 waste material Substances 0.000 claims description 5
- 230000001590 oxidative effect Effects 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 239000010893 paper waste Substances 0.000 claims description 3
- 238000010000 carbonizing Methods 0.000 claims description 2
- 239000012266 salt solution Substances 0.000 claims description 2
- 241000220259 Raphanus Species 0.000 claims 2
- 235000006140 Raphanus sativus var sativus Nutrition 0.000 claims 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 27
- 238000001179 sorption measurement Methods 0.000 description 21
- 238000000034 method Methods 0.000 description 15
- 229910021529 ammonia Inorganic materials 0.000 description 14
- 239000003463 adsorbent Substances 0.000 description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 150000002500 ions Chemical class 0.000 description 8
- 239000003610 charcoal Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 241000196324 Embryophyta Species 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000002154 agricultural waste Substances 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 239000002781 deodorant agent Substances 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 235000013312 flour Nutrition 0.000 description 4
- 229940046892 lead acetate Drugs 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 3
- 229920000049 Carbon (fiber) Polymers 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000004917 carbon fiber Substances 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical compound [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 150000002596 lactones Chemical class 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 239000002916 wood waste Substances 0.000 description 2
- 241000256111 Aedes <genus> Species 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 229920002307 Dextran Polymers 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 1
- 235000011613 Pinus brutia Nutrition 0.000 description 1
- 241000018646 Pinus brutia Species 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229920002522 Wood fibre Polymers 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 150000008064 anhydrides Chemical group 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 239000002041 carbon nanotube Substances 0.000 description 1
- 229910021393 carbon nanotube Inorganic materials 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 244000309146 drought grass Species 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 229910001410 inorganic ion Inorganic materials 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229920003986 novolac Polymers 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 125000001174 sulfone group Chemical group 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 235000021419 vinegar Nutrition 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 239000002025 wood fiber Substances 0.000 description 1
Classifications
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/78—Recycling of wood or furniture waste
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
- Catalysts (AREA)
- Processing Of Solid Wastes (AREA)
- Separation Of Gases By Adsorption (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、低濃度域の塩基性
ガス例えばアンモニアなどに対して優れた脱臭能を持
ち、かつイオン交換能あるいは触媒能を有する、セルロ
ース、でんぷんあるいはこれらを含有する木質材、農産
廃棄物等植物資材の炭化・熱処理物およびその製造方法
に関する。[0001] The present invention relates to cellulose, starch or wood containing them, which has an excellent deodorizing ability against a basic gas in a low concentration range such as ammonia and has an ion exchange ability or a catalytic ability. The present invention relates to a carbonized and heat-treated product of plant material such as wood and agricultural waste, and a method for producing the same.
【0002】[0002]
【従来の技術】これまで畜舎、工場等排出される臭気が
問題となるような建物は住宅地から離れた場所に立地し
ていたが、住宅環境の悪化から、これらが互いに隣接す
るようになっている。さらに居住空間の気密化は様々な
臭いの問題を生み出している。2. Description of the Related Art Heretofore, buildings such as livestock pens and factories where the odor emitted is a problem have been located far from residential areas, but due to the deterioration of the residential environment, they have become adjacent to each other. ing. Furthermore, the tightness of the living space has created various odor problems.
【0003】その中の一つとして塩基性ガスによる悪臭
が挙げられる。塩基性ガスの中で法的に規制されている
物質としてアンモニア、トリメチルアミンがある。これ
らは数ppb〜ppmオーダーの微量でさえ強い臭気を
放つことから、この塩基性ガスに対する悪臭対策として
多くの脱臭剤が提案されてきた。特に活性炭は塩基性ガ
ス吸着性能が劣ること、また無機多孔質材料は塩基性ガ
ス吸着性は優れているものの選択性が低く吸着剤として
あまり効果的ではないことから、これを補う目的の製造
例が報告されている。One of them is an odor caused by a basic gas. Among the basic gases, ammonia and trimethylamine are legally regulated substances. Since they emit a strong odor even in a trace amount of the order of several ppb to ppm, many deodorants have been proposed as a countermeasure against the odor against the basic gas. In particular, activated carbon has poor basic gas adsorption performance, and inorganic porous materials have good basic gas adsorption, but have low selectivity and are not very effective as adsorbents. Have been reported.
【0004】脱臭剤としての性能を高める方法として例
えば硫酸と有機酸を活性炭に添着する方法(特開昭52
−63882)、活性炭・繊維・その他多孔質材料の表
面に金属塩を添着・担持させる方法(特開昭64−25
867、特開昭64−29264、特開昭64−582
58、特開昭63−229056、特開昭63−229
057)がある。As a method for enhancing the performance as a deodorant, for example, a method of impregnating activated carbon with sulfuric acid and an organic acid (Japanese Patent Laid-Open No.
-63882), a method of adhering and supporting a metal salt on the surface of activated carbon, fiber and other porous materials (JP-A-64-25)
867, JP-A-64-29264, JP-A-64-582
58, JP-A-63-229056, JP-A-63-229
057).
【0005】このような従来の脱臭剤は、いずれも単に
活性炭などに各種の成分を添着させたものであり、表面
に均質に付着させることは困難である。また燐酸、硫酸
などの無機酸性物質を添着させたものは気化による室内
の汚染なども懸念されることから、室内の清浄化という
点において深刻な問題となる。重金属化合物やキレート
化合物を用いたものは臭気物質の除去効果は大きいもの
の、コスト等の点から適用対象と使用条件が大きく限定
される。[0005] All of these conventional deodorizing agents are simply obtained by adhering various components to activated carbon or the like, and it is difficult to uniformly adhere them to the surface. In addition, a substance impregnated with an inorganic acidic substance such as phosphoric acid or sulfuric acid poses a serious problem in terms of indoor cleaning because there is a fear of indoor contamination due to vaporization. Although those using a heavy metal compound or a chelate compound have a great effect of removing odorous substances, their applications and use conditions are greatly limited in terms of cost and the like.
【0006】一方イオン交換体としては、無機イオン交
換体の他、ポリスチレンなど合成樹脂や、セルロース、
デキストラン等にスルホン基、カルボキシル基などを導
入したものなどがある。これらの製品は均質で性能は優
れているものの、高価であるため使用目的が限られる。
また使用後の廃棄処理方法を考慮した場合、合成樹脂は
好ましくなく、天然の植物材料を原料とした製品が望ま
しい。On the other hand, examples of the ion exchanger include inorganic ion exchangers, synthetic resins such as polystyrene, cellulose, and the like.
Dextran and the like include sulfone groups, carboxyl groups and the like introduced therein. Although these products are homogeneous and have excellent performance, they are expensive and have limited use.
Also, in consideration of the disposal method after use, synthetic resins are not preferred, and products made from natural plant materials are desirable.
【0007】400℃程度の低温度域で得られる木炭
は、炭化物表面にカルボキシル基、水酸基などの酸性基
が多く含まれることがよく知られている。この表面官能
基の吸着性能への関与について、これまでに低温域での
炭化物を用いたアンモニア吸着性能に関する報告例(人
見ら:炭素、No.160、247−254(199
3))、重金属吸着性能に関する報告例(桑垣、田村:
木炭と木酢液の新用途開発研究成果集、27−44(1
990))等がある。It is well known that charcoal obtained in a low temperature range of about 400 ° C. contains a large amount of acidic groups such as carboxyl groups and hydroxyl groups on the surface of a carbide. Regarding the contribution of this surface functional group to the adsorption performance, a report example on the ammonia adsorption performance using a carbide in a low temperature range (Hitami et al .: Carbon, No. 160, 247-254 (199)
3)), Examples of reports on heavy metal adsorption performance (Kuwaki, Tamura:
New Use Development Research Collection of Charcoal and Wood Vinegar, 27-44 (1
990)).
【0008】また500〜800℃の温度で製造した木
炭を270〜350℃で空気酸化を行うことによりガ
ス、重金属の吸着剤として用いることができる炭化物の
製造法に関する報告例(特開平7−241461)があ
る。A report on a method for producing a carbide that can be used as an adsorbent for gases and heavy metals by subjecting charcoal produced at a temperature of 500 to 800 ° C. to air oxidation at 270 to 350 ° C. (Japanese Patent Laid-Open No. 7-241461) ).
【0009】しかし木質材炭化物の塩基性ガス吸着性能
やイオン交換能はその能力が市販品と比べ劣るため、広
く用いられるに至っていない。However, the basic carbon gas-adsorbing performance and ion-exchange performance of woody carbides are inferior to those of commercial products, so that they have not been widely used.
【0010】木質物を出発原料とした環境浄化資材とし
てもっとも多く使用されているものとして活性炭があ
る。しかし活性炭は塩基性ガスに対する吸着能が低いこ
とから酸性基を導入して塩基性ガスやイオン交換体とし
て利用する方法が提案されている。例えば硝酸・硫酸な
ど酸化剤を用いて活性炭表面に酸性基を導入する方法、
活性炭または炭素繊維などに対し加熱とともに空気酸化
を行うことにより炭化物表面に酸性基を導入する方法な
どがある。Activated carbon is one of the most widely used environmental purification materials using wood as a starting material. However, activated carbon has a low ability to adsorb a basic gas, and thus a method has been proposed in which an acidic group is introduced and used as a basic gas or an ion exchanger. For example, a method of introducing an acidic group to the activated carbon surface using an oxidizing agent such as nitric acid or sulfuric acid,
There is a method in which an acidic group is introduced into the surface of a carbide by performing air oxidation together with heating on activated carbon or carbon fiber.
【0011】木質物類似物質として、芳香族スルホン酸
(塩)を原料として得られる炭素繊維を酸素存在下30
0〜600℃で熱処理することにより酸素含有量は7〜
25%、キレート能は0.05〜0.25mmol/g
の吸着剤が得られている(特開平7−185336)。As a wood-like substance, a carbon fiber obtained from an aromatic sulfonic acid (salt) as a raw material is treated in the presence of oxygen for 30 minutes.
Oxygen content is 7 ~ by heat treatment at 0 ~ 600 ° C.
25%, chelating ability is 0.05-0.25mmol / g
Of the adsorbent (JP-A-7-185336).
【0012】また硬化ノボラック樹脂を空気中130〜
500℃で熱処理することによる、イオン交換容量1.
5meq/g以上のイオン交換体製造例(特開昭55−
104325)がある。In addition, the cured novolak resin is used in air at 130 to
Ion exchange capacity by heat treatment at 500 ° C.
Example of ion exchanger production of 5 meq / g or more
104325).
【0013】未賦活の炭素繊維を酸素存在下250〜9
00℃で処理することによるアンモニアなど極性ガスに
対する吸着剤の製造例も報告されている(特開平2−2
53844)。[0013] The unactivated carbon fiber is removed in the presence of oxygen by 250 to 9
An example of producing an adsorbent for a polar gas such as ammonia by treating at 00 ° C. has also been reported (Japanese Patent Application Laid-Open No. 2-2).
53844).
【0014】また酸化処理を施して酸性官能基を導入し
た表面酸素の割合が10%以上の繊維状活性炭に、硫酸
あるいは燐酸を付着させる方法もある(特開平9−19
2484)。There is also a method in which sulfuric acid or phosphoric acid is attached to fibrous activated carbon in which the ratio of surface oxygen into which an acidic functional group has been introduced by oxidation treatment is 10% or more (JP-A-9-19).
2484).
【0015】このような活性炭表面への酸性基導入で
は、多孔性による物理吸着と、酸性基による化学吸着お
よびイオン交換体としての機能を期待できる一方、出発
原料を炭化、賦活した後さらに酸化剤処理、高温での空
気酸化と2〜3工程の熱処理が必要である。また炭化物
表面の酸化のみによる反応であることから高置換度の生
成物を得ることが困難であった。In the introduction of an acidic group to the surface of activated carbon, physical adsorption due to porosity, chemical adsorption by an acidic group and a function as an ion exchanger can be expected. Treatment, air oxidation at high temperature and heat treatment in a few steps are required. In addition, it is difficult to obtain a product having a high degree of substitution, because the reaction is caused only by oxidation of the carbide surface.
【0016】[0016]
【発明が解決しようとする課題】そこで本発明者らは、
木質物などの天然植物資材を原料とし、より簡便な工程
で高性能な環境浄化資材の製造方法を検討した。その結
果、セルロース、でんぷんあるいはこれらを含有する木
質材や農産廃棄物を250〜400℃の温度範囲で熱処
理するとき、その加熱雰囲気中の酸素濃度が得られる熱
処理物の酸性基量含有量と密接に関連すること、また適
正な温度と酸素濃度雰囲気下では生成物に多量の酸性基
が導入されること、さらにこれをアルカリ溶液に浸せき
処理することによりイオン交換容量が大きく増大するこ
とを見出し本発明に至った。SUMMARY OF THE INVENTION Accordingly, the present inventors
Using natural plant materials such as woody materials as raw materials, a method for producing high-performance environmental purification materials in a simpler process was studied. As a result, when heat-treating cellulose, starch or wood or agricultural waste containing them in a temperature range of 250 to 400 ° C., the oxygen concentration in the heating atmosphere is closely related to the acidic group content of the heat-treated product obtained. In addition, it was found that a large amount of acidic groups were introduced into the product under an appropriate temperature and oxygen concentration atmosphere, and that the ion exchange capacity was greatly increased by immersing it in an alkaline solution. Invented the invention.
【0017】本発明は、この熱分解反応を利用し、セル
ロース、でんぷんあるいはこれらを含有する木質系廃棄
物や農産廃棄物等の未利用植物資源を原料として、単に
250〜400℃の温度範囲で熱処理するという単純な
工程で、高性能な吸着剤、触媒、イオン交換体として利
用できる熱処理物の製造技術を提供するものである。The present invention utilizes this thermal decomposition reaction, and uses only unused plant resources such as cellulose, starch or woody waste or agricultural waste containing them as raw materials at a temperature of 250 to 400 ° C. The present invention provides a technique for producing a heat-treated product that can be used as a high-performance adsorbent, a catalyst, or an ion exchanger in a simple process of heat treatment.
【0018】[0018]
【課題を解決するための手段】出発原料となる木質材
は、木材加工工場から排出されるノコクズや樹皮、林地
残材、木粉、木材繊維、木材チップ、チップダスト、サ
ンダークズ、さらには、笹、わら、もみがらなどの植物
繊維、パルプかす、古紙などセルロースを含む木質材が
あげられる。でんぷんまたはセルロースを含む農産廃棄
物も出発原料としで用いることもできる。これらの木質
材等を非酸化性雰囲気下、350℃以下で熱処理した炭
化物を用いることもできる。形状の粗大なものは粉砕あ
るいは解繊して用いてもよい。幾つかの用途では木材表
面のみを処理して用いることもできる。Means for Solving the Problems Wood materials as starting materials are sawdust and bark, wood residue, wood flour, wood fiber, wood chips, chip dust, sun darks, and the like, which are discharged from a wood processing plant. Examples include vegetable fibers such as bamboo grass, straw, and rice husk, and wood materials containing cellulose such as pulp residue and waste paper. Agricultural wastes containing starch or cellulose can also be used as starting materials. A carbide obtained by heat-treating these wood materials and the like at 350 ° C. or lower in a non-oxidizing atmosphere can also be used. Those having a large shape may be pulverized or defibrated before use. In some applications, only the wood surface can be treated and used.
【0019】本発明で行う熱処理は熱風循環式オーブ
ン、電気炉、連続式炭化炉、流動層式炭化炉など200
〜400℃の範囲で温度制御ができ、かつ雰囲気を変え
られる装置を用いることができる。The heat treatment performed in the present invention is a hot air circulation oven, an electric furnace, a continuous carbonization furnace, a fluidized bed carbonization furnace, etc.
A device capable of controlling the temperature in the range of 400 ° C. and changing the atmosphere can be used.
【0020】 出発原料の熱処理は1〜25%の酸素を
含む気相雰囲気下、250〜400℃好ましくは300
〜350℃で熱処理する。熱処理終了後自然放冷する。
炭化時の気相雰囲気における酸素濃度を変えることによ
り、炭化物の化学構造変化及び酸性基生成量を制御する
ことができ、同時にアルカリ水溶液による浸せきあるい
は噴霧処理がイオン交換能を増大させる性質を付与する
ことができる。 The starting material is heat-treated at 250 to 400 ° C., preferably 300 ° C., in a gaseous atmosphere containing 1 to 25% oxygen.
Heat treatment at ~ 350 ° C. After the heat treatment, it is left to cool naturally.
By changing the oxygen concentration in the gas phase atmosphere during carbonization
To control the chemical structure change and the amount of acidic group generation of carbides
Can be simultaneously immersed in an aqueous alkaline solution
Imparts the property that spray treatment increases ion exchange capacity
be able to.
【0021】このようにして得られた炭化物は、重量比
約26〜40%の酸素、強酸性基0.5〜2.3mmo
l/g、弱酸性基3〜5mmol/gを含む。The carbide obtained in this manner is composed of about 26 to 40% by weight of oxygen and 0.5 to 2.3 mmol of a strongly acidic group.
1 / g, containing 3-5 mmol / g of weakly acidic groups.
【0022】こうして得られた炭化物中の酸性基のうち
強酸性基として定量される部分は主にカルボキシル基で
あると考えられる。弱酸性基として定量される部分は主
にラクトン、フェノール性水酸基、無水酸等であると考
えられる。It is considered that the portion of the acidic group in the carbide thus obtained, which is determined as a strongly acidic group, is mainly a carboxyl group. It is considered that the portion quantified as a weakly acidic group is mainly a lactone, a phenolic hydroxyl group, an acid anhydride or the like.
【0023】塩基性ガスや溶液中ではこれらの酸性基は
強酸性基、弱酸性基ともに吸着活性点として機能するの
でアンモニアなど塩基性ガス吸着剤として利用する場合
は得られた炭化物をそのまま使用することができる。In a basic gas or solution, these acidic groups function as adsorption active sites for both strongly acidic groups and weakly acidic groups. Therefore, when used as a basic gas adsorbent such as ammonia, the obtained carbide is used as it is. be able to.
【0024】一方酸性あるいは中性水溶液中ではほぼ強
酸性基に相当する部分のみが吸着活性点となる。そこで
得られた炭化物をアルカリ処理、好ましくは0.01〜
1.0N水酸化ナトリウム水溶液に浸せき、ろ別、水洗
後乾燥する。アルカリ処理により炭化物中のラクトン、
無水酸は開環し、ナトリウム塩が生成する。得られた炭
化物はイオン交換体として金属イオンの担持あるいは吸
着に用いることができる。On the other hand, in an acidic or neutral aqueous solution, only a portion substantially corresponding to a strongly acidic group becomes an adsorption active site. The resulting carbide is treated with an alkali, preferably from 0.01 to
It is immersed in a 1.0N aqueous sodium hydroxide solution, filtered, washed with water and dried. Lactone in carbide by alkali treatment,
The anhydride rings open to form the sodium salt. The obtained carbide can be used as an ion exchanger for supporting or adsorbing metal ions.
【0025】次にアルカリ処理した炭化物を金属塩溶
液、好ましくは0.01〜1.0N金属塩水溶液に浸せ
き、ろ別、水洗後乾燥する。得られた炭化物は金属担体
として触媒、脱臭剤などとして用いることができる。触
媒として用いる場合、用途に応じてさらに熱処理、酸化
処理等を行うことで、より性能を高めることができる。Next, the alkali-treated carbide is immersed in a metal salt solution, preferably a 0.01 to 1.0 N aqueous solution of a metal salt, filtered, washed with water and dried. The obtained carbide can be used as a catalyst, a deodorant, or the like as a metal carrier. When used as a catalyst, the performance can be further improved by further performing a heat treatment, an oxidation treatment, or the like according to the application.
【0026】[0026]
【発明の実施の形態】本発明の炭化物は、粒状、繊維状
のまま単独あるいは他の粒状物、繊維と混合してシート
状等に成形し、これらを収納体内に充填して使用するも
のである。BEST MODE FOR CARRYING OUT THE INVENTION The carbide of the present invention may be used alone or in the form of a sheet by mixing it with other particles or fibers in the form of granules or fibers, and these may be used by filling them in a container. is there.
【0027】[0027]
【実施例】(実施例1)試料としてセルロースを用い
た。試料を磁性るつぼに入れふたをした後、以下の条件
で炭化した。温度条件は昇温速度は3℃/min.とし
300℃で2時間保持した後放冷した。熱処理時の雰囲
気は空気と窒素ガスを混合し、酸素濃度を調整した。得
られた各炭化物のアルカリ処理前後のイオン交換容量を
定法により評価した。定容法ガス吸着量測定装置を用い
て吸着等温線を求め、得られた各炭化物のアンモニアガ
スに対する吸着特性を評価した。その結果イオン交換容
量は炭化時の酸素濃度との間に高い相関が見られ(図
1)、請求項1が読みとれる。さらにアルカリ処理によ
りイオン交換容量は大きく増大した(図1)。アンモニ
ア吸着量(図2)も同様に炭化時の酸素濃度の増加に伴
い増大した。EXAMPLES (Example 1) Cellulose was used as a sample. The sample was placed in a magnetic crucible, covered, and carbonized under the following conditions. As for the temperature conditions, the rate of temperature rise was 3 ° C./min. Then, the mixture was kept at 300 ° C. for 2 hours and allowed to cool. The atmosphere during the heat treatment was a mixture of air and nitrogen gas to adjust the oxygen concentration. The ion exchange capacity of each of the obtained carbides before and after the alkali treatment was evaluated by an ordinary method. The adsorption isotherm was determined using a constant volume gas adsorption amount measuring device, and the adsorption characteristics of the obtained carbides to ammonia gas were evaluated. As a result an ion exchange capacity high correlation was observed between the oxygen concentration at the time of carbonization (Figure 1), you can take readings claim 1. Further, the ion exchange capacity was greatly increased by the alkali treatment (FIG. 1). Similarly, the amount of adsorbed ammonia (FIG. 2) increased with an increase in the oxygen concentration during carbonization.
【0028】(実施例2) 試料として上記実施例1の
セルロースに換えトドマツ材木粉を用いた。以下の処理
は同様に行った。その結果イオン交換容量はアルカリ処
理により大きく増大し(図1)、かつアンモニア吸着量
(図3)とともに炭化時の酸素濃度の増加に伴い増大し
た。Example 2 As a sample, firwood wood flour was used instead of the cellulose of Example 1 above. The following processing was performed similarly. As a result, the ion exchange capacity was greatly increased by the alkali treatment (FIG. 1), and increased with the increase in the oxygen concentration during carbonization along with the amount of adsorbed ammonia (FIG. 3).
【0029】(実施例3) 試料としてセルロースを用
いた。試料を磁性るつぼに入れふたをした後、以下の条
件で炭化した。温度条件は昇温速度は3℃/min.と
し250〜400℃で2時間保持した後放冷した。酸素
濃度は21%とした。イオン交換容量、アンモニアガス
吸着特性は実施例1と同様に評価した。その結果イオン
交換容量、アンモニアガス吸着特性とも300℃付近で
の温度域での熱処理がより効果的であった。Example 3 Cellulose was used as a sample. The sample was placed in a magnetic crucible, covered, and carbonized under the following conditions. As for the temperature conditions, the rate of temperature rise was 3 ° C./min. After keeping at 250 to 400 ° C. for 2 hours, the mixture was allowed to cool. The oxygen concentration was 21%. The ion exchange capacity and ammonia gas adsorption characteristics were evaluated in the same manner as in Example 1. As a result, heat treatment in a temperature range around 300 ° C. was more effective for both the ion exchange capacity and the ammonia gas adsorption characteristics.
【0030】(実施例4) 試料として上記実施例3の
セルロースに換えトドマツ木粉を用いた。以下の処理は
同様に行った。その結果イオン交換容量、アンモニアガ
ス吸着特性とも300℃付近での温度域での熱処理がよ
り効果的であった。(Example 4) As a sample, Aedes pine wood flour was used in place of the cellulose of Example 3 above. The following processing was performed similarly. As a result, heat treatment in a temperature range around 300 ° C. was more effective for both the ion exchange capacity and the ammonia gas adsorption characteristics.
【0031】(実施例5) 試料として上記実施例3の
セルロースに換えでんぷんを用いた。以下の処理は同様
に行った。その結果イオン交換容量、アンモニアガス吸
着特性とも300℃付近での温度域での熱処理がより効
果的であった。さらに実施例3、4、5で得られたセル
ロース、トドマツ材、でんぷん炭化物のアンモニア吸着
等温線を図4に示す。比較として市販活性炭、アンモニ
ア用活性炭、木炭を用いた。その結果本発明で得られた
処理物は比較として用いた各吸着剤より優れたアンモニ
ア吸着特性を持つことが判明した。Example 5 Starch was used as a sample instead of the cellulose of Example 3 above. The following processing was performed similarly. As a result, heat treatment in a temperature range around 300 ° C. was more effective for both the ion exchange capacity and the ammonia gas adsorption characteristics. Further, FIG. 4 shows the ammonia adsorption isotherm of the cellulose, firwood and starch carbide obtained in Examples 3, 4, and 5. For comparison, commercially available activated carbon, activated carbon for ammonia, and charcoal were used. As a result, it was found that the treated product obtained in the present invention had better ammonia adsorption characteristics than each of the adsorbents used for comparison.
【0032】(実施例6) 試料としてトドマツ木粉を
用いた。試料を磁性るつぼに入れふたをした後、以下の
条件で炭化した。温度条件は昇温速度は3℃/min.
とし300℃で2時間保持した後放冷した。酸素濃度は
21%とした。得られた炭化物を0.5N酢酸鉛水溶液
中に浸せきし、24時間静置した後、ろ別、水洗した。
得られた残渣中の金属含有量を測定した結果、炭化物が
約1.2mmol/gの鉛を担持することが示された。Example 6 Todomatsu wood flour was used as a sample. The sample was placed in a magnetic crucible, covered, and carbonized under the following conditions. As for the temperature conditions, the rate of temperature rise was 3 ° C./min.
Then, the mixture was kept at 300 ° C. for 2 hours and allowed to cool. The oxygen concentration was 21%. The obtained carbide was immersed in a 0.5N aqueous lead acetate solution, allowed to stand for 24 hours, filtered, and washed with water.
Measurement of the metal content in the obtained residue showed that the carbide supported about 1.2 mmol / g of lead.
【0033】(実施例7) 実施例6の方法で得られた
炭化物を0.2N水酸化ナトリウム水溶液中に浸せき
し、24時間静置した後、ろ別、水洗した。乾燥後0.
5N酢酸鉛水溶液中に浸せきし、24時間静置した後、
ろ別、水洗した。得られた残渣中の金属含有量を測定し
た結果、アルカリ処理した炭化物が約3.8mmol/
gの鉛を担持することが示された。(Example 7) The carbide obtained by the method of Example 6 was immersed in a 0.2 N aqueous sodium hydroxide solution, allowed to stand for 24 hours, filtered and washed with water. After drying.
After immersing in a 5N aqueous lead acetate solution and allowed to stand for 24 hours,
It was filtered off and washed with water. As a result of measuring the metal content in the obtained residue, the alkali-treated carbide was found to be about 3.8 mmol /
g of lead.
【0034】(実施例8) 金属塩として上記実施例6
の0.5N酢酸鉛水溶液に換え0.5N酢酸銅水溶液を
用いた。その他の処理は実施例6と同様に行った。得ら
れた残渣中の金属含有量を測定した結果、炭化物が約
1.3mmol/gの銅を担持することが示された。Example 8 The above Example 6 was used as a metal salt.
Was replaced with a 0.5N aqueous lead acetate solution, and a 0.5N aqueous copper acetate solution was used. Other processes were performed in the same manner as in Example 6. Measurement of the metal content in the obtained residue showed that the carbide supported about 1.3 mmol / g of copper.
【0035】(実施例9) 金属塩として上記実施例7
の0.5N酢酸鉛水溶液に換え0.5N酢酸銅水溶液を
用いた。その他の処理は実施例7と同様に行った。得ら
れた残渣中の金属含有量を測定した結果、アルカリ処理
した炭化物が約3.9mmol/gの銅を担持すること
が示された。Example 9 The above Example 7 was used as a metal salt.
Was replaced with a 0.5N aqueous lead acetate solution, and a 0.5N aqueous copper acetate solution was used. Other processes were performed in the same manner as in Example 7. As a result of measuring the metal content in the obtained residue, it was shown that the alkali-treated carbide carried about 3.9 mmol / g of copper.
【0036】[0036]
【発明の効果】本発明はセルロース、でんぷんを含む木
質材、農産廃棄物等を酸化気相条件下250〜350℃
の低温域での炭化処理というきわめて単純な処理工程に
よる、新規の塩基性ガス吸着剤およびイオン交換体の製
造方法を提供するものである。According to the present invention, wood materials containing cellulose and starch, agricultural wastes and the like are oxidized at 250 to 350 ° C. under oxidative gas phase conditions.
It is intended to provide a novel method for producing a basic gas adsorbent and an ion exchanger by a very simple processing step of carbonizing in a low temperature range.
【0037】本発明によれば、炭化条件の制御により酸
性基生成量を効果的に高めることができ、高性能な塩基
性ガス吸着剤、イオン交換体として利用することができ
る。また金属担体としても触媒、脱臭剤など様々な用途
が期待できる。また酵素・微生物担体としての用途も期
待できる。According to the present invention, the amount of acidic groups generated can be effectively increased by controlling the carbonization conditions, and the carbon nanotubes can be used as high-performance basic gas adsorbents and ion exchangers. In addition, various uses such as a catalyst and a deodorant can be expected as a metal carrier. It can also be expected to be used as a carrier for enzymes and microorganisms.
【0038】したがって本発明は、木質材、特に林地や
木材加工工場の残廃材など未利用材さらには農産廃棄物
などの有効利用等に効果的である。Therefore, the present invention is effective for the effective use of wood materials, particularly unused materials such as residual materials from forests and wood processing plants, and agricultural wastes.
【0039】[0039]
【図1】炭化装置中の酸素濃度とトドマツ材、セルロー
ス炭化物、およびこれらの炭化物をアルカリ処理した生
成物のイオン交換容量との関係を示すグラフである。FIG. 1 is a graph showing the relationship between the oxygen concentration in a carbonizer and the ion exchange capacity of a fir tree material, a cellulose carbide, and a product obtained by alkali-treating these carbides.
【図2】セルロース炭化物のアンモニア吸着等温線図で
ある。FIG. 2 is an ammonia adsorption isotherm of cellulose carbide.
【図3】トドマツ材炭化物のアンモニア吸着等温線図で
ある。FIG. 3 is an ammonia adsorption isotherm of a firwood charcoal.
【図4】セルロース炭化物、トドマツ材炭化物、でんぷ
ん炭化物、市販活性炭、アンモニア用活性炭、木炭のア
ンモニア吸着等温線を比較したものである。FIG. 4 is a graph comparing the ammonia adsorption isotherms of cellulose carbide, firwood charcoal, starch carbide, commercially available activated carbon, activated carbon for ammonia, and charcoal.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C01B 31/10 C01B 31/10 // B01J 20/20 B01J 20/20 A B09B 3/00 B09B 3/00 303H 審査官 安齋 美佐子 (56)参考文献 特開 平9−241014(JP,A) 日本木材学会北海道支部講演集第29号 (平成9年10月)p49−51 (58)調査した分野(Int.Cl.7,DB名) C01B 31/02 101 B01D 53/02 B01J 21/18 B01J 32/00 B01J 39/22 C01B 31/10 B01J 20/20 B09B 3/00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI C01B 31/10 C01B 31/10 // B01J 20/20 B01J 20/20 A B09B 3/00 B09B 3/00 303H Examiner Misako Anzai (56) References JP-A-9-241014 (JP, A) Proceedings of the Japan Wood Research Society, Hokkaido Section No. 29 (October 1997), p. 49-51 (58) Fields investigated (Int. Cl. 7 , DB Name) C01B 31/02 101 B01D 53/02 B01J 21/18 B01J 32/00 B01J 39/22 C01B 31/10 B01J 20/20 B09B 3/00
Claims (2)
こくず、かんなくず、バルプかす、古紙のようなセルロ
ースを含む木質材、あるいは非酸化雰囲気下300℃以
下で熱処理した木質炭化物、ならびにでんぷんおよび農
産廃棄物等でんぷんを含む材料を出発原料とし、アルカ
リ水溶液による浸せきあるいは噴霧処理をした時にイオ
ン交換能が増大する性質を付与するように、粉砕された
原料を、6〜25容量%の酸素を含有する気相雰囲気下
での処理工程を含み、温度が250〜400℃の範囲
で、加熱、炭化処理すること、ならびに炭化時の気相雰
囲気における酸素濃度を変えることにより、酸性基生成
量を制御することを特徴とする脱臭能、イオン交換能を
有する炭化物製造方法。1. Wood material containing cellulose such as cellulose or wood, house waste material, sawdust, radish, pulp residue, waste paper, or wood char which has been heat-treated at 300 ° C. or less in a non-oxidizing atmosphere, and starch and agricultural products Starting material is starch-containing material such as waste, and pulverized so as to impart the property of increasing ion exchange capacity when dipped or sprayed with an aqueous alkali solution .
The raw material is placed in a gaseous atmosphere containing 6 to 25% by volume of oxygen.
And heating at a temperature in the range of 250 to 400 ° C., and controlling the amount of generated acidic groups by changing the oxygen concentration in the gas phase atmosphere during the carbonization. For producing a carbide having deodorizing ability and ion exchange ability.
こくず、かんなくず、パルプかす、古紙のようなセルロ
ースを含む木質材、あるいは非酸化雰囲気下300℃以
下で熱処理した木質炭化物、ならびにでんぷんおよび農
産廃棄物等でんぷんを含む材料を出発原料とし、アルカ
リ水溶液による浸せきあるいは噴霧処理をした時にイオ
ン交換能が増大する性質を付与するように、酸素を含む
気相雰囲気下で温度が250〜400℃の範囲で、加
熱、炭化処理すること、ならびに炭化時の気相雰囲気に
おける酸素濃度を変えることにより、酸性基生成量を制
御して製造した炭化物を、アルカリ水溶液および金属塩
水溶液により浸せきあるいは噴霧処理し、金属を担持さ
せることを特徴とする脱臭能、イオン交換能、触媒能を
有する炭化物製造方法。2. A wood material containing cellulose such as cellulose or wood, waste wood, sawdust, radish, pulp residue, waste paper, or wood char which has been heat-treated at 300 ° C. or lower in a non-oxidizing atmosphere, and starch and agricultural products. The starting material is a material containing starch such as waste, and a temperature of 250 to 400 ° C. in a gaseous atmosphere containing oxygen so as to impart a property of increasing ion exchange capacity when immersed or sprayed with an aqueous alkali solution. Within the range, by heating and carbonizing, and by changing the oxygen concentration in the gas phase atmosphere during carbonization, the carbide produced by controlling the amount of generated acidic groups is dipped or sprayed with an aqueous alkali solution and an aqueous metal salt solution. For producing a carbide having a deodorizing ability, an ion exchange ability and a catalytic ability, characterized by supporting a metal. .
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JP5600699A JP3138749B2 (en) | 1999-01-26 | 1999-01-26 | Method for producing carbides having deodorizing ability, ion exchange ability, and catalytic ability using plant materials |
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EP1878490A3 (en) | 2003-12-05 | 2008-03-05 | Nisshoku Corporation | Anion-adsorbing carbon material, and method and apparatus for producing same |
KR100732133B1 (en) | 2005-04-29 | 2007-06-25 | 한국생산기술연구원 | A Process for Manufacturing Synthetic Zeolites Using Organic Sludge |
JP5471142B2 (en) | 2008-09-29 | 2014-04-16 | ソニー株式会社 | POROUS CARBON MATERIAL COMPOSITE AND PROCESS FOR PRODUCING THE SAME, AND ADSORBENT, COSMETIC, PURIFIER, AND PHOTOCATALYST COMPOSITE MATERIAL |
JP2011225521A (en) | 2010-03-30 | 2011-11-10 | Sony Corp | Fungicide, photo catalytic composite material, adsorbent, and depurative |
KR101642359B1 (en) * | 2015-01-27 | 2016-07-27 | 주식회사 에스이씨 | Manufacturing of adsorbent by thermosetting plastic waste |
JP7380986B2 (en) * | 2019-03-29 | 2023-11-15 | 群馬県 | Bamboo charcoal and bamboo charcoal manufacturing method |
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1999
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日本木材学会北海道支部講演集第29号(平成9年10月)p49−51 |
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