JP3363113B2 - Method and apparatus for selecting carbon nanofiber - Google Patents
Method and apparatus for selecting carbon nanofiberInfo
- Publication number
- JP3363113B2 JP3363113B2 JP21571699A JP21571699A JP3363113B2 JP 3363113 B2 JP3363113 B2 JP 3363113B2 JP 21571699 A JP21571699 A JP 21571699A JP 21571699 A JP21571699 A JP 21571699A JP 3363113 B2 JP3363113 B2 JP 3363113B2
- Authority
- JP
- Japan
- Prior art keywords
- magnetic
- slurry
- carbon
- carbon nanofibers
- metal catalyst
- 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
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims description 28
- 239000002134 carbon nanofiber Substances 0.000 title claims description 26
- 238000000034 method Methods 0.000 title claims description 7
- 230000005291 magnetic effect Effects 0.000 claims description 31
- 239000002002 slurry Substances 0.000 claims description 25
- 239000003054 catalyst Substances 0.000 claims description 16
- 229910052751 metal Inorganic materials 0.000 claims description 16
- 239000002184 metal Substances 0.000 claims description 16
- 239000006148 magnetic separator Substances 0.000 claims description 15
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 14
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 14
- 239000000126 substance Substances 0.000 claims description 14
- 239000007788 liquid Substances 0.000 claims description 12
- 239000006185 dispersion Substances 0.000 claims description 10
- 239000000047 product Substances 0.000 claims description 10
- 229910052742 iron Inorganic materials 0.000 claims description 7
- 229910052759 nickel Inorganic materials 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- 239000004094 surface-active agent Substances 0.000 claims description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 6
- 239000005977 Ethylene Substances 0.000 claims description 6
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 6
- 239000012265 solid product Substances 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 description 6
- 229910001416 lithium ion Inorganic materials 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 238000005979 thermal decomposition reaction Methods 0.000 description 5
- 229930195733 hydrocarbon Natural products 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- 239000000696 magnetic material Substances 0.000 description 4
- 239000007769 metal material Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000011232 storage material Substances 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 229910001111 Fine metal Inorganic materials 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 229940117927 ethylene oxide Drugs 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005294 ferromagnetic effect Effects 0.000 description 1
- 239000003302 ferromagnetic material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
Description
【0001】[0001]
【発明の属する技術分野】この発明は、水素吸蔵材など
に用いられるカーボンナノファイバーの精選方法及び装
置に係わる。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for carefully selecting carbon nanofibers used as a hydrogen storage material.
【0002】[0002]
【従来の技術】鉄やニッケルなどの金属触媒を用いてエ
チレンなどのハイドロカーボンガスや一酸化炭素などを
熱分解して得られるカーボンナノファイバーが、最近水
素吸蔵合金以上に水素ガスを吸蔵するという驚異的な実
験結果が発表され、水素貯蔵材料として注目されてい
る。この水素吸蔵のメカニズムは完全に明らかにされて
はいないが、水素吸蔵合金は比重が重く繰り返し使用で
粉化するなどの欠点があるので、合金と同等以上の貯蔵
性能が安定的に証明されれば、燃料電池などの水素貯蔵
材料として活用できるので、現在各所でその性能が追試
されている。2. Description of the Related Art Carbon nanofibers obtained by thermally decomposing hydrocarbon gases such as ethylene and carbon monoxide using a metal catalyst such as iron and nickel have recently been said to absorb hydrogen gas more than hydrogen storage alloys. Astonishing experimental results have been announced and attracted attention as a hydrogen storage material. Although the mechanism of hydrogen storage is not completely clarified, hydrogen storage alloys have the drawbacks of having a high specific gravity and being pulverized by repeated use, so that storage performance equivalent to or better than that of alloys has been stably proven. For example, it can be used as a hydrogen storage material for fuel cells, etc., so its performance is being tested in many places.
【0003】また、現在リチュームイオン二次電池の陰
極に使用されているカーボンのリチュームイオン吸蔵能
力は電池の容量を左右する重要な因子なので、この陰極
にカーボンナノファイバーを用いることによってリチュ
ームイオンの吸蔵能力を増やすことができれば、電池容
量の飛躍的向上が期待できる。Further, since the lithium ion storage capacity of carbon currently used for the cathode of a lithium ion secondary battery is an important factor that influences the capacity of the battery, the use of carbon nanofibers for this cathode will store the lithium ion. If the capacity can be increased, a dramatic increase in battery capacity can be expected.
【0004】しかしながらカーボンナノファイバーは熱
分解生成物なので、これ以外の構造を持ったカーボンや
ハイドロカーボンなどの好ましくない異物の生成・混在
は避けられない。これらの異物が混在することにより、
単位体積ないし単位重量当りの吸蔵容量は当然減少する
ので、カーボンナノファイバーのみを分離精選するプロ
セスが必要になるが、従来そのようなプロセスは存在し
なかった。However, since carbon nanofibers are thermal decomposition products, the production and mixing of undesired foreign substances such as carbon and hydrocarbon having other structures are unavoidable. By mixing these foreign substances,
Since the storage capacity per unit volume or unit weight naturally decreases, a process for separating and selecting only carbon nanofibers is required, but such a process has not existed in the past.
【0005】[0005]
【発明が解決しようとする課題】以上に鑑みこの発明
は、製造された熱分解生成物から好ましくない異物を除
去精選し、単位体積ないし単位重量当りの水素ガスやリ
チュームイオンなどの吸蔵能力を高めることを目的とす
る。SUMMARY OF THE INVENTION In view of the above, according to the present invention, undesired foreign substances are removed from the produced thermal decomposition product to be carefully selected, and the ability to store hydrogen gas or lithium ion per unit volume or unit weight is enhanced. The purpose is to
【0006】[0006]
【課題を解決するための手段】この発明は、カーボンナ
ノファイバーが鉄やニッケルなどの強磁性体に付着して
形成されている点に着目してなされたものである。すな
わち請求項1に記載の発明は、鉄やニッケル等の磁性体
を含む金属触媒を用いてエチレンや一酸化炭素などを熱
分解して得られた固体生成物を、界面活性剤と共に攪拌
して生成物を分散せしめてスラリー化した後に、磁気分
離機を通すことにより、磁性金属の触媒片を核として成
長したカーボンナノファイバーを磁力で非磁性スラリー
から分離することを特徴とする、カーボンナノファイバ
ーの精選方法である。The present invention has been made by paying attention to the fact that carbon nanofibers are formed by adhering to a ferromagnetic material such as iron or nickel. That is, the invention according to claim 1 is to stir a solid product obtained by thermally decomposing ethylene or carbon monoxide with a metal catalyst containing a magnetic substance such as iron or nickel together with a surfactant.
Then, the product is dispersed and made into a slurry, and then passed through a magnetic separator to cause the carbon nanofibers grown with the magnetic metal catalyst pieces as nuclei to be magnetically non-magnetic slurry.
It is a method for finely selecting carbon nanofibers, which is characterized by separating from carbon nanofibers.
【0007】また請求項2に記載の発明は、鉄やニッケ
ル等の磁性体を含む金属触媒を用いてエチレンや一酸化
炭素などを熱分解して得られた固体生成物を、界面活性
剤と共に液中で攪拌して生成物を分散せしめる分散槽
と、該分散槽のスラリーから磁性スラリーを分離する磁
気分離機と、分離された磁性スラリーから固体粒子を分
離する濾過機とで構成したことを特徴とする、カーボン
ナノファイバーの精選装置である。The invention according to claim 2 is a solid product obtained by thermally decomposing ethylene, carbon monoxide or the like using a metal catalyst containing a magnetic substance such as iron or nickel together with a surfactant. A dispersion tank for stirring the product in the liquid to disperse the product, a magnetic separator for separating the magnetic slurry from the slurry in the dispersion tank, and a filter for separating solid particles from the separated magnetic slurry. It is a characteristic carbon nanofiber selection device.
【0008】[0008]
【発明の実施の形態】以下、本発明の実施の形態を実施
例にもとずき図面を参照して説明する。図1はドラム型
磁気分離機を用いた実施例、図2は超電導磁気分離機を
用いた実施例、図3はカーボンナノファイバーの模式
図、をそれぞれ示す。なお、図2、図3において、図1
と同じ符号を付した部分は同一又は相当部分を示す。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below based on examples with reference to the drawings. 1 shows an example using a drum type magnetic separator, FIG. 2 shows an example using a superconducting magnetic separator, and FIG. 3 shows a schematic view of carbon nanofibers. In addition, in FIG. 2 and FIG.
The parts given the same reference numerals as in the above indicate the same or corresponding parts.
【0009】図3の模式図に示すようにカーボンナノフ
ァイバー3は、微細な金属触媒片1を核にして偏平な炭
素片2がほぼG=0.34ナノメートルの隙間をもって
成長した、太さD=10〜数百ナノメートル、長さL=
数ミクロン,程度の微小な炭素繊維である。微細な金属
触媒片1の生成過程は、原料ガスが触媒金属と接触して
堆積した炭素が金属内に拡散し、金属面に生成する炭化
物の体積変化に基ずく応力で触媒表面が破損崩壊して微
粒子になるものと推定されているが、いずれにせよ金属
触媒は消耗し、電子顕微鏡による観察結果では、図3に
示すような微細な金属触媒片1を核として規則的な形態
をもったカーボンナノファイバー3が形成されている。As shown in the schematic view of FIG. 3, the carbon nanofiber 3 has a thickness in which a flat carbon piece 2 is grown with a fine metal catalyst piece 1 as a nucleus with a gap of about G = 0.34 nm. D = 10 to several hundreds of nanometers, length L =
It is a minute carbon fiber of a few microns. In the process of forming the fine metal catalyst piece 1, the raw material gas comes into contact with the catalyst metal and the deposited carbon diffuses into the metal, and the catalyst surface is damaged and collapsed due to stress based on the volume change of the carbide formed on the metal surface. It is presumed that the metal catalyst is consumed in any case, but in any case, the metal catalyst is consumed, and the electron microscope observation shows that the metal catalyst piece 1 has a regular morphology with the fine metal catalyst piece 1 as a nucleus. The carbon nanofibers 3 are formed.
【0010】しかしながらカーボンナノファイバー3
は、エチレンなどのハイドロカーボンガスや一酸化炭素
などを550℃〜600℃程度の比較的低温下で還元性
熱分解によって製造されるものであるから、これらの条
件においては目的とするカーボンナノファイバー以外の
形態のカーボンやハイドロカーボンなどの同時生成・混
在を防止することは困難である。However, carbon nanofiber 3
Is produced by reductive thermal decomposition of hydrocarbon gas such as ethylene or carbon monoxide at a relatively low temperature of about 550 ° C. to 600 ° C. Therefore, under these conditions, the target carbon nanofiber It is difficult to prevent the simultaneous generation and mixing of other forms of carbon and hydrocarbons.
【0011】この発明は図1に示すように、熱分解で生
成したカーボンナノファイバー3を含む熱分解生成物4
を、まず水などの液体を蓄えた分散槽5に供給して界面
活性剤6と共に攪拌羽根15で攪拌し、生成物の固体粒
子を液中に単離分散せしめてスラリー化した後に、周知
のドラム型磁気分離機7に供給する。As shown in FIG. 1, the present invention is a pyrolysis product 4 containing carbon nanofibers 3 produced by pyrolysis.
Is first supplied to a dispersion tank 5 in which a liquid such as water is stored, and stirred with a surfactant 6 by a stirring blade 15 to isolate and disperse solid particles of the product in the liquid to form a slurry, The drum type magnetic separator 7 is supplied.
【0012】ドラム型磁気分離機7は図示のように、一
部欠損した円筒型の固定磁石16の外周を矢印17方向
に回転するドラム18と、非磁性スラリー貯槽19、磁
性スラリー貯槽20、スプレーノズル26などで構成さ
れており、ドラム18の頂部に供給されたスラリー中の
磁性体はドラム上に吸着されて回転し、固定磁石16の
欠損部で脱着すると共にスプレーノズル26で洗浄され
てドラムを離脱し、磁性スラリーとして磁性スラリー貯
槽20内に蓄えられ、磁力の影響を受けない非磁性スラ
リー11は非磁性スラリー貯槽19内に滞留する。As shown in the figure, the drum-type magnetic separator 7 includes a drum 18 which rotates the outer periphery of a partially-fixed cylindrical fixed magnet 16 in the direction of arrow 17, a non-magnetic slurry storage tank 19, a magnetic slurry storage tank 20, and a sprayer. The magnetic material in the slurry supplied to the top of the drum 18 is adsorbed on the drum and rotated, and is detached at the defective portion of the fixed magnet 16 and washed by the spray nozzle 26 to be washed by the drum. The non-magnetic slurry 11 stored in the magnetic slurry storage tank 20 as a magnetic slurry and not affected by the magnetic force stays in the non-magnetic slurry storage tank 19.
【0013】磁性スラリー8は周知の中空糸膜などで構
成されるフィルター9によって固形磁性体すなわちカー
ボンナノファイバー3が分離回収され、分離液10は分
散槽5に戻される。また、非磁性スラリー11はフィル
ター12によって固形非磁性体すなわち異物13と分離
液14とに分離され、分離液14は分散槽5に戻され
る。In the magnetic slurry 8, a solid magnetic material, that is, the carbon nanofibers 3 is separated and collected by a filter 9 composed of a well-known hollow fiber membrane and the separated liquid 10 is returned to the dispersion tank 5. The non-magnetic slurry 11 is separated by the filter 12 into a solid non-magnetic material, that is, a foreign substance 13 and a separation liquid 14, and the separation liquid 14 is returned to the dispersion tank 5.
【0014】図2は、その他の実施例として周知の超電
導磁気分離機7’を用いた場合の構成を示す。図1の例
と同様に熱分解生成物4は分散槽5内で界面活性剤6と
共に攪拌されて液中に分散してスラリー化した後に、周
知の超電導磁気分離機7’に供給される。FIG. 2 shows a configuration in which a known superconducting magnetic separator 7'is used as another embodiment. As in the example of FIG. 1, the thermal decomposition product 4 is stirred with the surfactant 6 in the dispersion tank 5 to be dispersed in the liquid to make a slurry, and then supplied to the well-known superconducting magnetic separator 7 ′.
【0015】超電導磁気分離機7’は図示のように、網
目状金属材22を囲む超電導磁石21と冷凍機23で構
成されている。該網目状金属材22は周知の高勾配磁気
型のウール状磁性金属で構成するとよい。非磁性スラリ
ー11は網目状金属材22を通過後フィルター12によ
って固形非磁性体すなわち異物13と分離液14とに分
離され、分離液14は分散槽5に戻される。一方、網目
状金属材22で捕捉された磁性体は一旦磁気を切った後
に逆洗して22から離脱させ、磁性体を含む磁性スラリ
ー8はフィルター9によって固形磁性体すなわちカーボ
ンナノファイバー3が分離回収され、分離液10は逆洗
液の貯槽24に戻される。図中25は逆洗液の補給液を
示す。The superconducting magnetic separator 7'is composed of a superconducting magnet 21 surrounding a mesh metal material 22 and a refrigerator 23 as shown in the figure. The mesh metal material 22 may be made of a well-known high gradient magnetic type wool magnetic metal. The non-magnetic slurry 11 is separated into a solid non-magnetic material, that is, a foreign substance 13 and a separation liquid 14 by the filter 12 after passing through the mesh metal material 22, and the separation liquid 14 is returned to the dispersion tank 5. On the other hand, the magnetic substance trapped by the mesh metal material 22 is once demagnetized and then backwashed to be separated from the magnetic substance 22, and the magnetic slurry 8 containing the magnetic substance is separated by the filter 9 into the solid magnetic substance, that is, the carbon nanofibers 3. The separated liquid 10 is recovered and returned to the backwash liquid storage tank 24. In the figure, 25 indicates a replenisher for the backwash solution.
【0016】[0016]
【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。Since the present invention is constructed as described above, it has the following effects.
【0017】鉄やニッケルなどの強磁性体に付着して形
成されるカーボンナノファイバーのみが選別分離され、
従来不可能だった異物除去が可能となる。したがって本
発明によって精選されたカーボンナノファイバーは、単
位体積ないし単位重量当りの水素ガスやリチュームイオ
ンなどの吸蔵能力が著しく高くなり、燃料電池の水素貯
蔵材料やリチュームイオン二次電池の陰極材料など、付
加価値の高い工業材料として利用できる。Only carbon nanofibers formed by adhering to a ferromagnetic substance such as iron or nickel are separated and separated,
It is possible to remove foreign matter, which was impossible in the past. Therefore, the carbon nanofibers selected according to the present invention have remarkably high storage capacity such as hydrogen gas and lithium ion per unit volume or unit weight, such as a hydrogen storage material for a fuel cell and a cathode material for a lithium ion secondary battery. It can be used as an industrial material with high added value.
【図1】ドラム型磁気分離機を用いた本発明の実施例を
示す図である。FIG. 1 is a diagram showing an embodiment of the present invention using a drum type magnetic separator.
【図2】超電導磁気分離機を用いた本発明の実施例を示
す図である。FIG. 2 is a diagram showing an embodiment of the present invention using a superconducting magnetic separator.
【図3】カーボンナノファイバーの模式図を示す。FIG. 3 shows a schematic view of carbon nanofibers.
1 金属触媒片 2 炭素片 3 カーボンナノファイバー 4 熱分解生成物 5 分散槽 6 界面活性剤 7 ドラム型磁気分離機 7’超電導磁気分離機 8 磁性スラリー 9、12 フィルター 11 非磁性スラリー 13 異物 15 攪拌羽根 16 固定磁石 18 ドラム 21 超電導磁石 22 網目状金属材 23 冷凍機 1 Metal catalyst piece 2 carbon pieces 3 Carbon nanofiber 4 Thermal decomposition products 5 dispersion tanks 6 Surfactant 7 Drum type magnetic separator 7'Superconducting magnetic separator 8 Magnetic slurry 9, 12 filters 11 Non-magnetic slurry 13 foreign matter 15 stirring blades 16 fixed magnet 18 drums 21 Superconducting magnet 22 Metal mesh material 23 refrigerator
Claims (2)
を用いてエチレンや一酸化炭素などを熱分解して得られ
た固体生成物を、界面活性剤と共に攪拌して生成物を分
散せしめてスラリー化した後に、磁気分離機を通すこと
により、磁性金属の触媒片を核として成長したカーボン
ナノファイバーを磁力で非磁性スラリーから分離するこ
とを特徴とする、カーボンナノファイバーの精選方法。1. A solid product obtained by thermally decomposing ethylene, carbon monoxide, or the like using a metal catalyst containing a magnetic substance such as iron or nickel is stirred with a surfactant to separate the product.
A method for finely selecting carbon nanofibers, characterized by separating carbon nanofibers grown with magnetic metal catalyst pieces as nuclei from a non-magnetic slurry by magnetic force after being dispersed and made into a slurry, and then passed through a magnetic separator. .
を用いてエチレンや一酸化炭素などを熱分解して得られ
た固体生成物を、界面活性剤と共に液中で攪拌して生成
物を分散せしめる分散槽と、該分散槽のスラリーから磁
性スラリーを分離する磁気分離機と、分離された磁性ス
ラリーから固体粒子を分離する濾過器とで構成したこと
を特徴とする、カーボンナノファイバーの精選装置。2. A solid product obtained by thermally decomposing ethylene, carbon monoxide or the like using a metal catalyst containing a magnetic substance such as iron or nickel, and stirring the resulting solid product in a liquid together with a surfactant. Characterized by comprising a dispersion tank for dispersing, a magnetic separator for separating the magnetic slurry from the slurry of the dispersion tank, and a filter for separating solid particles from the separated magnetic slurry, of carbon nanofibers Selector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21571699A JP3363113B2 (en) | 1999-06-24 | 1999-06-24 | Method and apparatus for selecting carbon nanofiber |
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| JP21571699A JP3363113B2 (en) | 1999-06-24 | 1999-06-24 | Method and apparatus for selecting carbon nanofiber |
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| JP2001010809A JP2001010809A (en) | 2001-01-16 |
| JP3363113B2 true JP3363113B2 (en) | 2003-01-08 |
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Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US7927567B2 (en) | 2004-12-20 | 2011-04-19 | Sharp Kabushiki Kaisha | Adsorbent, porous filter, air cleaning device, method of cleaning air, and method of manufacturing porous filter |
| CA2575479C (en) * | 2005-03-25 | 2012-05-22 | Institut National De La Recherche Scientifique | Methods and apparatuses for purifying carbon filamentary structures |
| KR100795903B1 (en) | 2006-08-10 | 2008-01-21 | 세메스 주식회사 | Carbon nanotube capture device and carbon nanotube production system and method using same |
| JP5430271B2 (en) * | 2009-07-29 | 2014-02-26 | 住友重機械ファインテック株式会社 | Rotating drum type abrasive recovery device |
| JP6457791B2 (en) | 2014-11-19 | 2019-01-23 | 株式会社日立製作所 | Magnetic separation device and raw water treatment device |
| CN112957871A (en) * | 2021-02-24 | 2021-06-15 | 江苏工程职业技术学院 | Automatic processing apparatus of machinery production waste gas |
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1999
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