JPH04361621A - Carbon fiber for removing nitrogen oxide - Google Patents
Carbon fiber for removing nitrogen oxideInfo
- Publication number
- JPH04361621A JPH04361621A JP3160752A JP16075291A JPH04361621A JP H04361621 A JPH04361621 A JP H04361621A JP 3160752 A JP3160752 A JP 3160752A JP 16075291 A JP16075291 A JP 16075291A JP H04361621 A JPH04361621 A JP H04361621A
- Authority
- JP
- Japan
- Prior art keywords
- carbon fiber
- nitrogen oxides
- pitch
- exhaust gases
- carbon
- 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.)
- Withdrawn
Links
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 title claims abstract description 128
- 229920000049 Carbon (fiber) Polymers 0.000 title claims abstract description 42
- 239000004917 carbon fiber Substances 0.000 title claims abstract description 42
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 239000000835 fiber Substances 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 7
- 239000011261 inert gas Substances 0.000 claims abstract description 6
- 238000010304 firing Methods 0.000 claims description 9
- 239000011148 porous material Substances 0.000 abstract description 15
- 239000007789 gas Substances 0.000 abstract description 13
- 239000011295 pitch Substances 0.000 abstract description 9
- 238000000354 decomposition reaction Methods 0.000 abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 4
- 239000001301 oxygen Substances 0.000 abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000011337 anisotropic pitch Substances 0.000 abstract description 2
- 230000001590 oxidative effect Effects 0.000 abstract description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 239000003054 catalyst Substances 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 229910021529 ammonia Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 239000003575 carbonaceous material Substances 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229940068105 nitrogen 99.9 % Drugs 0.000 description 1
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 1
- -1 p. 204 Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B3/00—Engines characterised by air compression and subsequent fuel addition
- F02B3/06—Engines characterised by air compression and subsequent fuel addition with compression ignition
Landscapes
- Carbon And Carbon Compounds (AREA)
- Inorganic Fibers (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】排ガスからの窒素酸化物の除去、
特にディーゼルエンジン排ガスからの窒素酸化物除去に
適した窒素酸化物除去用炭素繊維に関する。[Industrial application field] Removal of nitrogen oxides from exhaust gas,
In particular, the present invention relates to carbon fibers for removing nitrogen oxides, which are suitable for removing nitrogen oxides from diesel engine exhaust gas.
【0002】0002
【従来の技術】従来の窒素酸化物除去には、例えば火力
発電所排ガスのような固定型の大規模処理に対するアン
モニアを還元剤に、5酸化バナジウム―酸化チタン触媒
を用いた次の反応式(1式)で窒素酸化物を除去する窒
素酸化物除去(触媒講座、第7巻、P.253、講談社
)、NOx+NH3+O2 → N2+H2O
・・・(1)[Prior Art] Conventionally, nitrogen oxides are removed using the following reaction equation ( Nitrogen oxide removal (Catalyst Course, Vol. 7, P. 253, Kodansha), NOx + NH3 + O2 → N2 + H2O
...(1)
【0003】ガソリンエンジン自動車のよ
うな移動体の小規模処理に対する3元触媒を用いた次の
反応式(2式)で窒素酸化物を除去する窒素酸化物除去
(触媒講座、第9巻、P.195、講談社)が存在する
。
NOx+CO+炭化水素 → N2+CO2+H2
O ・・・(2)Nitrogen oxide removal using the following reaction equation (2 equations) using a three-way catalyst for small-scale treatment of mobile objects such as gasoline engine automobiles (Catalyst Lecture, Vol. 9, P. .195, Kodansha) exists. NOx+CO+hydrocarbon → N2+CO2+H2
O...(2)
【0004】また、一般にピッ
チ系炭素繊維は紡糸したピッチを不融化したものを不活
性ガス雰囲気で800〜1200℃で炭素化、1500
〜3000℃で黒鉛化処理をすることにより製造される
(改訂 炭素材料入門、P.204、炭素材料学会)
。In addition, pitch-based carbon fibers are generally produced by infusible spun pitch, which is carbonized at 800 to 1200°C in an inert gas atmosphere, then heated to 1500°C.
Manufactured by graphitizing at ~3000℃ (Revised Introduction to Carbon Materials, p. 204, Carbon Materials Society of Japan)
.
【0005】炭素繊維による窒素酸化物の除去は炭素繊
維の炭素を還元剤として次の反応式(3式)で示される
。
NOx+C → N2+CO+CO2 ・・
・(3)Removal of nitrogen oxides by carbon fibers is shown by the following reaction formula (Equation 3) using carbon in the carbon fibers as a reducing agent. NOx+C → N2+CO+CO2 ・・
・(3)
【0006】[0006]
【発明が解決しようとする課題】しかしながら、ディー
ゼル自動車の排ガスの窒素酸化物除去に対してアンモニ
アを用いる場合はアンモニアの毒性のため取扱いが難し
く移動体には不向きであり、三元触媒を用いる場合はデ
ィーゼル自動車の排ガスのような高酸素濃度のもとでは
作用しない。[Problems to be Solved by the Invention] However, when ammonia is used to remove nitrogen oxides from the exhaust gas of diesel automobiles, it is difficult to handle due to the toxicity of ammonia and is not suitable for moving objects.When using a three-way catalyst, however, does not work under high oxygen concentrations such as diesel car exhaust gas.
【0007】通常の方法で製造した炭素繊維はNOxと
の反応性に乏しく窒素酸化物の除去効率は低い。Carbon fibers produced by conventional methods have poor reactivity with NOx and have low nitrogen oxide removal efficiency.
【0008】本発明の目的は、ディーゼル自動車排ガス
のような高濃度の酸素を含む移動体の排ガスからの窒素
酸化物の除去に適した窒素酸化物除去用炭素繊維を提供
することにある。An object of the present invention is to provide carbon fibers for removing nitrogen oxides that are suitable for removing nitrogen oxides from the exhaust gas of moving vehicles containing high concentration of oxygen, such as diesel automobile exhaust gas.
【0009】[0009]
【課題を解決するための手段】本発明の窒素酸化物除去
用炭素繊維は、不融化したピッチ系炭素繊維の原糸を不
活性ガス雰囲気にて600℃以上、800℃未満の温度
で焼成してなる炭素繊維であることを特徴とする。本発
明により窒素酸化物の除去性能を大幅に向上できる。[Means for Solving the Problems] The carbon fiber for removing nitrogen oxides of the present invention is produced by firing infusible pitch-based carbon fiber yarn at a temperature of 600°C or more and less than 800°C in an inert gas atmosphere. It is characterized by being made of carbon fiber. The present invention can significantly improve the nitrogen oxide removal performance.
【0010】0010
【作用】以下、図面を参照にしながら本発明を具体的に
説明する。[Operation] The present invention will be explained in detail below with reference to the drawings.
【0011】図2は本発明の炭素繊維の製造工程の一例
を示す。図2において(1)等方性または、異方性ピッ
チを(2)溶融紡糸し、(3)150〜400℃の酸化
性雰囲気中で不融化した後、(4)純度が95%以上の
不活性ガス雰囲気中で600℃以上、800℃未満で焼
成することにより本発明の炭素繊維を得ることができる
。FIG. 2 shows an example of the manufacturing process of the carbon fiber of the present invention. In Figure 2, (1) isotropic or anisotropic pitch is (2) melt-spun, (3) infusible in an oxidizing atmosphere at 150 to 400°C, and (4) purity is 95% or more. The carbon fiber of the present invention can be obtained by firing in an inert gas atmosphere at a temperature of 600°C or higher and lower than 800°C.
【0012】本発明で得られた炭素繊維を用いて本発明
者らがおこなった窒素酸化物除去試験の結果を図1に示
す。FIG. 1 shows the results of a nitrogen oxide removal test conducted by the present inventors using the carbon fiber obtained in the present invention.
【0013】窒素濃度99.99%以上の不活性雰囲気
中で約500〜1500℃の温度で焼成した各々の炭素
繊維について一酸化窒素1000ppm、ブランク窒素
の標準ガスを用いて、SV:2187hr−1、400
℃にて窒素酸化物除去性能の評価を行った。[0013] For each carbon fiber fired at a temperature of about 500 to 1500°C in an inert atmosphere with a nitrogen concentration of 99.99% or more, SV: 2187 hr-1 using 1000 ppm of nitrogen monoxide and a standard gas of blank nitrogen. ,400
The nitrogen oxide removal performance was evaluated at ℃.
【0014】図2に示すように焼成温度が600℃以上
、800℃未満の間で焼成した炭素繊維による窒素酸化
物除去率が高い値を示す。As shown in FIG. 2, the nitrogen oxide removal rate of carbon fibers fired at a firing temperature of 600° C. or higher and lower than 800° C. is high.
【0015】焼成温度が600℃以上、800℃未満の
間でも700℃前後が好ましい。[0015] Even if the firing temperature is between 600°C and above and below 800°C, around 700°C is preferable.
【0016】その理由は600℃以上で炭素の結晶子の
生成と成長により結晶子間に細孔が形成され窒素酸化物
の分解に関与する細孔が増加するが一方700℃以上で
は熱処理による炭素繊維の収縮が起こり始め、形成され
た細孔の細孔径が小さくなり窒素酸化物の分解に関与す
る細孔が減少する。The reason for this is that at temperatures above 600°C, pores are formed between the crystallites due to the generation and growth of carbon crystallites, and the number of pores involved in the decomposition of nitrogen oxides increases, while at temperatures above 700°C, carbon due to heat treatment increases. The fibers begin to shrink, and the pore diameters of the formed pores become smaller, reducing the number of pores involved in the decomposition of nitrogen oxides.
【0017】この炭素の結晶子の生成と成長による窒素
酸化物の分解に関与する細孔の増加と熱処理による炭素
繊維の収縮に伴う窒素酸化物の分解に関与する細孔の減
少の相互作用により窒素酸化物除去性能が焼成温度70
0℃で最大値を持つ。[0017] Due to the interaction between the increase in the number of pores involved in the decomposition of nitrogen oxides due to the generation and growth of carbon crystallites and the decrease in the number of pores involved in the decomposition of nitrogen oxides due to shrinkage of the carbon fibers due to heat treatment. Nitrogen oxide removal performance at 70% firing temperature
It has a maximum value at 0℃.
【0018】600℃未満では炭素の結晶子の生成と成
長による結晶子間の細孔が形成されず窒素酸化物の分解
に関与する細孔がほとんど存在しないため窒素酸化物の
分解は炭素繊維表面での反応が大部分を占めるため窒素
酸化物除去性能が低くなる。[0018] Below 600°C, pores between crystallites are not formed due to the generation and growth of carbon crystallites, and there are almost no pores involved in the decomposition of nitrogen oxides, so the decomposition of nitrogen oxides occurs on the carbon fiber surface. Since most of the reactions occur in
【0019】800℃以上では形成された細孔の細孔径
が小さくなり窒素酸化物の分解に関与する細孔が減少し
窒素酸化物の分解は炭素繊維表面での反応が大部分を占
めるため窒素酸化物除去性能が低くなる。[0019] At temperatures above 800°C, the pore diameter of the formed pores becomes smaller and the number of pores involved in the decomposition of nitrogen oxides decreases. Oxide removal performance decreases.
【0020】本発明は不融化した繊維を600℃以上、
800℃未満の比較的低い温度で焼成することを特徴と
している。[0020] In the present invention, the infusible fiber is heated to 600°C or higher.
It is characterized by firing at a relatively low temperature of less than 800°C.
【0021】[0021]
【実施例】表1にディーゼルエンジン排ガスに対する各
種窒素酸化物除去の比較を示す。[Example] Table 1 shows a comparison of various nitrogen oxide removal methods for diesel engine exhaust gas.
【0022】ここで炭素繊維A、Bは本発明の炭素繊維
で、炭素繊維Aはピッチ繊維を不融化後、窒素99.9
9%以上の不活性雰囲気中で700℃、1分焼成した炭
素繊維であり、炭素繊維Bはピッチ繊維を不融化後、窒
素99%の不活性雰囲気中で620℃、1分焼成した炭
素繊維である。Here, carbon fibers A and B are the carbon fibers of the present invention, and carbon fiber A is a pitch fiber that is made infusible and then treated with nitrogen 99.9%.
Carbon fibers are carbon fibers fired at 700°C for 1 minute in an inert atmosphere containing 9% or more nitrogen, and carbon fiber B is a carbon fiber fired at 620°C for 1 minute in an inert atmosphere containing 99% nitrogen after infusible pitch fibers. It is.
【0023】また、比較例として従来の炭素繊維Cはピ
ッチ繊維を不融化後、窒素99.99%の不活性雰囲気
中で1500℃、1分焼成した炭素繊維である。Further, as a comparative example, conventional carbon fiber C is a carbon fiber obtained by infusibleizing pitch fibers and then firing them at 1500° C. for 1 minute in an inert atmosphere containing 99.99% nitrogen.
【0024】[0024]
【表1】[Table 1]
【0025】本発明の炭素繊維では窒素酸化物が十分に
除去される。[0025] Nitrogen oxides are sufficiently removed from the carbon fiber of the present invention.
【0026】本発明の炭素繊維A、Bは従来の炭素繊維
Cよりも非常に高い窒素酸化物除去性能を示し、700
℃焼成の炭素繊維Aは最も高い窒素酸化物除去性能を示
す。The carbon fibers A and B of the present invention exhibit much higher nitrogen oxide removal performance than the conventional carbon fiber C, and have a nitrogen oxide removal performance of 700
Carbon fiber A fired at °C shows the highest nitrogen oxide removal performance.
【0027】620℃焼成の炭素繊維Bは実用上有効な
高い窒素酸化物除去性能を示している。炭素繊維Aは、
ほぼアンモニアを還元剤に用いる場合と同等の性能であ
った。Carbon fiber B fired at 620° C. shows a high nitrogen oxide removal performance that is practically effective. Carbon fiber A is
The performance was almost the same as when ammonia was used as the reducing agent.
【0028】一方、本実験条件下では三元触媒はほとん
ど窒素酸化物を除去しない。On the other hand, under the present experimental conditions, the three-way catalyst hardly removes nitrogen oxides.
【0029】[0029]
【発明の効果】本発明の炭素繊維を窒素酸化物除去に用
いた場合以下の効果がある。
(1)排ガス中に酸素が存在していても窒素酸化物を除
去することができる。
(2)アンモニアなどの有毒物質を使用しないため移動
体への搭載が容易である。
(3)従来の炭素繊維に比べて非常に高い窒素酸化物除
去性能を示す。[Effects of the Invention] When the carbon fiber of the present invention is used for removing nitrogen oxides, the following effects can be obtained. (1) Nitrogen oxides can be removed even if oxygen is present in the exhaust gas. (2) Since no toxic substances such as ammonia are used, it is easy to mount on a mobile vehicle. (3) Exhibits extremely high nitrogen oxide removal performance compared to conventional carbon fibers.
【図1】焼成温度と窒素酸化物除去率の関係図。FIG. 1 is a diagram showing the relationship between firing temperature and nitrogen oxide removal rate.
【図2】本発明の炭素繊維の製造工程図。FIG. 2 is a diagram showing the manufacturing process of the carbon fiber of the present invention.
Claims (1)
不活性ガス雰囲気にて600℃以上800℃未満の温度
で焼成してなる炭素繊維であることを特徴とする窒素酸
化物除去用炭素繊維。1. Carbon for removing nitrogen oxides, which is carbon fiber obtained by firing infusible pitch-based carbon fiber yarn at a temperature of 600°C or higher and lower than 800°C in an inert gas atmosphere. fiber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3160752A JPH04361621A (en) | 1991-06-06 | 1991-06-06 | Carbon fiber for removing nitrogen oxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3160752A JPH04361621A (en) | 1991-06-06 | 1991-06-06 | Carbon fiber for removing nitrogen oxide |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04361621A true JPH04361621A (en) | 1992-12-15 |
Family
ID=15721699
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3160752A Withdrawn JPH04361621A (en) | 1991-06-06 | 1991-06-06 | Carbon fiber for removing nitrogen oxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04361621A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0768113A (en) * | 1993-06-10 | 1995-03-14 | Jiyabisu:Kk | Bag filter for treatment of exhaust gas containing nitrogen oxide |
-
1991
- 1991-06-06 JP JP3160752A patent/JPH04361621A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0768113A (en) * | 1993-06-10 | 1995-03-14 | Jiyabisu:Kk | Bag filter for treatment of exhaust gas containing nitrogen oxide |
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Legal Events
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---|---|---|---|
A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19980903 |