JPH0576723A - Method for reducing greenhouse-effect gas - Google Patents
Method for reducing greenhouse-effect gasInfo
- Publication number
- JPH0576723A JPH0576723A JP3273261A JP27326191A JPH0576723A JP H0576723 A JPH0576723 A JP H0576723A JP 3273261 A JP3273261 A JP 3273261A JP 27326191 A JP27326191 A JP 27326191A JP H0576723 A JPH0576723 A JP H0576723A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- reaction
- greenhouse
- discharge
- carbon dioxide
- 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- Withdrawn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
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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、炭酸ガス等の温室効果
ガスを削減する方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for reducing greenhouse gases such as carbon dioxide.
【0002】[0002]
【従来技術とその問題点】地球温暖化は各種の地球環境
問題の中でも、最も深刻な影響を人類社会や生態系に与
えると懸念されており、我が国においても、地球温暖化
の原因となる炭酸ガス、フロンおよびメタン等の温室効
果ガスの排出量を削減することが計画されている。温室
効果ガスの中で最も多量に排出される炭酸ガスなどの排
ガスを削減、除去する方法として、従来から、物理およ
び化学的吸収法、吸着法、膜分離法、蒸留法などが知ら
れている。[Prior art and its problems] It is feared that global warming will have the most serious impact on human society and ecosystem among various global environmental problems. In Japan, carbon dioxide that causes global warming It is planned to reduce emissions of greenhouse gases such as gas, freon and methane. Conventionally, physical and chemical absorption methods, adsorption methods, membrane separation methods, distillation methods, etc. are known as methods for reducing and removing exhaust gases such as carbon dioxide gas, which is the most exhausted of greenhouse gases. ..
【0003】また、前記排ガス中には微粒子が含まれる
ことが多く、例えば、室内汚染ガス中には喫煙により生
じるアルデヒド類、オレフィン系炭化水素類などの固体
または液状の微粒子が含有されている。この種の微粒子
は、従来、各種のフィルターを用いた濾過分離法により
分離除去されている。Further, the exhaust gas often contains fine particles. For example, indoor polluting gas contains solid or liquid fine particles such as aldehydes and olefinic hydrocarbons produced by smoking. Fine particles of this type are conventionally separated and removed by a filtration separation method using various filters.
【0004】しかしながら、温室効果ガス、特に炭酸ガ
スを効率的に分離除去して、その排出量を低減する技術
は未だ確立されていない。However, a technique for efficiently separating and removing greenhouse gases, particularly carbon dioxide, to reduce the emission amount thereof has not yet been established.
【0005】[0005]
【発明の目的】本発明は前記課題を解決しようとするも
のであり、その目的は、火力発電所、工場その他の産業
施設等からの排出ガス、あるいは、ヒーター、ガス機器
等から排出される炭酸ガス、一酸化炭素、NOX などの
室内環境汚染ガスをエアロゾル化して、温室効果ガスを
削減することにある。また、本発明は前記温室効果ガス
を低減し、分離除去することを目的とする。SUMMARY OF THE INVENTION The present invention is intended to solve the above-mentioned problems, and an object thereof is to emit exhaust gas from thermal power plants, factories and other industrial facilities, or carbon dioxide emitted from heaters, gas appliances and the like. gas, carbon monoxide, indoor environmental pollution gas such as NO X by aerosolization is to reduce greenhouse gases. Moreover, this invention aims at reducing the said greenhouse effect gas, and separating and removing.
【0006】[0006]
【発明の概要】本発明に係る温室効果ガスの削減方法
は、温室効果ガスを、このガスと反応性の高いガスまた
はエアロゾルと反応させて、温室効果ガスの一部を液体
または固体に変換することを特徴とする。更に、前記反
応を反応ガスの励起状態において行うこと、または、前
記温室効果ガスの変換物を、温室効果ガスからフィルタ
ーにより分離することを特徴とする。SUMMARY OF THE INVENTION The greenhouse gas reduction method according to the present invention reacts a greenhouse gas with a gas or an aerosol having a high reactivity with the gas to convert a part of the greenhouse gas into a liquid or a solid. It is characterized by Furthermore, the reaction is carried out in the excited state of the reaction gas, or the converted greenhouse gas is separated from the greenhouse gas by a filter.
【0007】[0007]
【発明の具体的な説明】本発明において、温室効果ガス
である気体を、固体または液体に変換する方法には、
気体を反応させて、その気体よりも高沸点の物質を生成
させる方法と、気体とその気体との反応性に富むエア
ロゾルを反応させて新たに安定な物質を生成させる方法
とがある。DETAILED DESCRIPTION OF THE INVENTION In the present invention, a method for converting a gas which is a greenhouse effect gas into a solid or a liquid includes:
There are a method of reacting a gas to generate a substance having a boiling point higher than that of the gas, and a method of reacting a gas and an aerosol having high reactivity with the gas to generate a new stable substance.
【0008】例えば、二酸化炭素については、具体的に
次のような反応を利用する。 (1)尿素合成反応 2NH3 +CO2 →NH2 CO2 NH4 NH2 CO2 NH4 →CO(NH2)2 +H2 O (2)β−アミノエチルアルコールとの反応 2HOC2 H4 NH2 +H2 O+CO2 →(HOC2 H4 NH3 )2CO3 For example, for carbon dioxide, the following reactions are specifically utilized. (1) Urea synthesis reaction 2NH 3 + CO 2 → NH 2 CO 2 NH 4 NH 2 CO 2 NH 4 → CO (NH 2 ) 2 + H 2 O (2) Reaction with β-aminoethyl alcohol 2HOC 2 H 4 NH 2 + H 2 O + CO 2 → (HOC 2 H 4 NH 3) 2 CO 3
【0009】 また、前記の方法については、次のよ
うな反応を利用する。 (3)噴霧消石灰水溶液と二酸化炭素との接触反応 Ca(OH)2 +CO2 →CaCO3 +H2 O (4)水ガラスと二酸化炭素との接触反応 H2 O+CO2 +Na2 O・nSiO2 →Na2 CO3 +nSiO2 +H2 O[0009] The following reaction is used for the above method. (3) Catalytic reaction of sprayed slaked lime aqueous solution and carbon dioxide Ca (OH) 2 + CO 2 → CaCO 3 + H 2 O (4) Catalytic reaction of water glass and carbon dioxide H 2 O + CO 2 + Na 2 O · nSiO 2 → Na 2 CO 3 + nSiO 2 + H 2 O
【0010】上記反応において、反応気体の活性を高め
ることにより常温、常圧に近い状態でも反応を促進する
ことができる。具体的には、前記反応気体をコロナ放
電、火花放電、グロー放電、アーク放電などの自続放
電、レーザー照射または紫外線照射等の方法により、化
学的に不安定な状態まで励起させる方法を挙げることが
できる。特に、自続放電は、レーザーや紫外線がピンポ
イントを反応させるのに対して、後記するような反応器
を採用することにより、反応面積を多くとることができ
る。In the above reaction, by increasing the activity of the reaction gas, the reaction can be promoted even at room temperature and near normal pressure. Specifically, a method of exciting the reaction gas to a chemically unstable state by a method such as corona discharge, spark discharge, glow discharge, self-sustaining discharge such as arc discharge, laser irradiation or ultraviolet irradiation is given. You can In particular, in the self-sustaining discharge, the reaction area can be increased by adopting a reactor as described later, while the laser and the ultraviolet rays make pinpoint reaction.
【0011】図1は、放電場を利用したガス反応器の概
要図である。ガス反応器10は円筒状の反応管11の軸
心方向に電極棒12を配設し、反応管11の外周部には
コイル13が巻回され、電極棒12は図示してない高電
圧発生装置に接続されている。高電圧発生装置の電圧を
調節することにより、放電場に自続放電を起こすことが
できる。反応管11は通常の電極材でもよいし、反応管
11の内表面を触媒剤で被覆したものでもよい。更に、
反応管11の材質を温室効果ガスと反応性の高い材料、
即ち、温室効果ガスが二酸化炭素であれば、生石灰やナ
トリウム塩等としてもよい。反応管11の材質をこのよ
うな反応性材料で構成すれば、反応性ガスの貯蔵装置や
供給装置等が不要となり、気体変換システムを簡略化す
ることができる。FIG. 1 is a schematic diagram of a gas reactor utilizing a discharge field. The gas reactor 10 has an electrode rod 12 arranged in the axial direction of a cylindrical reaction tube 11, a coil 13 is wound around the outer periphery of the reaction tube 11, and the electrode rod 12 generates a high voltage (not shown). It is connected to the device. By adjusting the voltage of the high voltage generator, self-sustaining discharge can be generated in the discharge field. The reaction tube 11 may be a normal electrode material, or the inner surface of the reaction tube 11 may be coated with a catalyst agent. Furthermore,
The material of the reaction tube 11 is a material highly reactive with greenhouse gases,
That is, if the greenhouse effect gas is carbon dioxide, quicklime or sodium salt may be used. If the material of the reaction tube 11 is made of such a reactive material, a storage device or a supply device for the reactive gas becomes unnecessary, and the gas conversion system can be simplified.
【0012】図2は、放電場を利用した別のガス反応器
の概要図である。ガス反応器20内には、間隔をあけて
電極ネット21、21が配置され、その間に反応性材料
からなる球体22が充填されている。球体22は高誘電
体の表面を反応性材料または触媒剤で被覆したものでも
よい。電極ネット21、21間の放電により、気体変換
反応は球体22の表面付近で促進される。FIG. 2 is a schematic view of another gas reactor using a discharge field. Electrode nets 21, 21 are arranged at intervals in the gas reactor 20, and spheres 22 made of a reactive material are filled between them. The sphere 22 may be a high dielectric material whose surface is coated with a reactive material or a catalyst. Due to the discharge between the electrode nets 21, 21, the gas conversion reaction is promoted near the surface of the sphere 22.
【0013】また、気体変換反応システムを構成する上
で必要があれば、反応ガスを反応器に供給する前に、乾
燥機および/またはガス混合器に通してもよい。反応後
のガスから固体または液状の生成微粒子を分離するに
は、適宜の分離器を用いることができる。分離器とし
て、電気集塵機、HEPAフィルター、インパクター等
を例示することができる。If necessary in constructing the gas conversion reaction system, the reaction gas may be passed through a dryer and / or a gas mixer before being supplied to the reactor. An appropriate separator can be used to separate solid or liquid fine particles produced from the gas after the reaction. Examples of the separator include an electric dust collector, a HEPA filter, and an impactor.
【0014】[0014]
【実施例】実施例1 二酸化炭素とアンモニアガスを原料とし、図1に示すガ
ス反応器を用いて、ガス変換反応を行った。反応容器1
0内の反応温度は20℃、反応圧力は1Kgf/cm2、放電
圧は5.0KVとした。二酸化炭素とアンモニアガスは
1:2の理論比で供給し、滞留時間は1分であった。変
換反応の結果を表1に示す。なお、生成したエアロゾル
中の粒子径を粒度分布計で測定した結果、殆ど0.01
μm以下であった。 Example 1 A gas conversion reaction was carried out using carbon dioxide and ammonia gas as raw materials and using the gas reactor shown in FIG. Reaction vessel 1
The reaction temperature in 0 was 20 ° C., the reaction pressure was 1 Kgf / cm 2 , and the discharge voltage was 5.0 KV. Carbon dioxide and ammonia gas were supplied at a theoretical ratio of 1: 2, and the residence time was 1 minute. The results of the conversion reaction are shown in Table 1. In addition, as a result of measuring the particle size in the generated aerosol with a particle size distribution analyzer, almost 0.01
It was less than μm.
【0015】実施例2、3 実施例1において、原料二酸化炭素の濃度を代えて反応
を行った。変換反応の結果を表1に示す。In Examples 2 and 3 , the reaction was carried out by changing the concentration of the raw material carbon dioxide. The results of the conversion reaction are shown in Table 1.
【0016】比較例1、2、3 実施例1〜3において、放電を行わなかった他は同一の
条件で比較実験を行った。しかし、いずれの濃度におい
ても二酸化炭素の変換反応は起こらなかった。 Comparative Examples 1, 2, 3 In Examples 1 to 3, comparative experiments were conducted under the same conditions except that the discharge was not performed. However, no conversion reaction of carbon dioxide occurred at any concentration.
【0017】参考例1、2、3 二酸化炭素とアンモニアガスを原料とし、図1と同様の
ガス反応器を用いて、ガス変換反応を行った。放電は行
わず、反応温度を190℃、反応圧力を175Kgf /cm2
とした。二酸化炭素とアンモニアガスは1:2の理論比
で供給し、滞留時間は1分であった。変換反応の結果を
表1に示す。 Reference Examples 1, 2 and 3 Using carbon dioxide and ammonia gas as raw materials, a gas conversion reaction was carried out using the same gas reactor as in FIG. No discharge was performed, reaction temperature was 190 ° C, reaction pressure was 175 Kgf / cm 2
And Carbon dioxide and ammonia gas were supplied at a theoretical ratio of 1: 2, and the residence time was 1 minute. The results of the conversion reaction are shown in Table 1.
【0018】[0018]
【表1】 [Table 1]
【0019】[0019]
【発明の効果】本発明の方法によれば、温室効果ガス、
特に炭酸ガスを効率的に削減することができる。また、
気体の励起状態で変換反応を行うことにより、常温、常
圧に近い状態でも反応を促進することが可能となる。更
に、変換物をフィルターに通すことにより、確実に分離
除去することができるという優れた効果を有する。According to the method of the present invention, a greenhouse gas,
In particular, carbon dioxide gas can be efficiently reduced. Also,
By carrying out the conversion reaction in the excited state of gas, it becomes possible to promote the reaction even in a state close to normal temperature and pressure. Furthermore, by passing the converted product through a filter, there is an excellent effect that it can be reliably separated and removed.
【図1】放電場を利用したガス反応器の概要図である。FIG. 1 is a schematic diagram of a gas reactor using a discharge field.
【図2】放電場を利用した別のガス反応器の概要図であ
る。FIG. 2 is a schematic view of another gas reactor using a discharge field.
10、20 ガス反応器 11 反応管 12 電極棒 13 コイル 21 電極ネット 22 球体 10, 20 Gas reactor 11 Reaction tube 12 Electrode rod 13 Coil 21 Electrode net 22 Sphere
───────────────────────────────────────────────────── フロントページの続き (72)発明者 森 邦夫 東京都新宿区津久戸町2番1号 株式会社 熊谷組東京本社内 (72)発明者 小林 正宏 東京都新宿区津久戸町2番1号 株式会社 熊谷組東京本社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kunio Mori No. 1 Tsukutocho, Shinjuku-ku, Tokyo Kumagai Gumi Tokyo Head Office Co., Ltd. (72) Masahiro Kobayashi No. 2 Tsukudo-cho, Shinjuku-ku, Tokyo Kumagai Gumi Tokyo Head Office
Claims (3)
いガスまたはエアロゾルと反応させて、温室効果ガスの
一部を液体または固体に変換することを特徴とする温室
効果ガスの削減方法。1. A method for reducing a greenhouse effect gas, which comprises reacting a greenhouse effect gas with a gas or an aerosol highly reactive with the gas to convert a part of the greenhouse effect gas into a liquid or a solid.
行う請求項1記載の温室効果ガスの削減方法。2. The greenhouse gas reduction method according to claim 1, wherein the reaction is performed in an excited state of the reaction gas.
ガスからフィルターにより分離する請求項1記載の温室
効果ガスの削減方法。3. The greenhouse gas reduction method according to claim 1, wherein the converted greenhouse gas is separated from the greenhouse gas by a filter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3273261A JPH0576723A (en) | 1991-09-25 | 1991-09-25 | Method for reducing greenhouse-effect gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3273261A JPH0576723A (en) | 1991-09-25 | 1991-09-25 | Method for reducing greenhouse-effect gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0576723A true JPH0576723A (en) | 1993-03-30 |
Family
ID=17525367
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3273261A Withdrawn JPH0576723A (en) | 1991-09-25 | 1991-09-25 | Method for reducing greenhouse-effect gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0576723A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6290238A (en) * | 1985-09-23 | 1987-04-24 | 旭化成株式会社 | Antistatic sheet-shaped article |
JP2007222867A (en) * | 2006-01-20 | 2007-09-06 | Erubu:Kk | Carbon dioxide gas purifying material, carbon dioxide gas purifying fiber and carbon dioxide gas purifying cloth, and carbon dioxide gas purifying apparatus |
WO2013028568A1 (en) * | 2011-08-19 | 2013-02-28 | Hychar Energy, Llc | Electronegative-ion-aided method and apparatus for synthesis of ethanol and organic compounds |
JP2013519513A (en) * | 2010-02-19 | 2013-05-30 | コモンウェルス サイエンティフィック アンド インダストリアル リサーチ オーガニゼーション | Solvent treatment method |
CN103796751A (en) * | 2011-08-19 | 2014-05-14 | 海加能源有限公司 | Electronegative-ion-aided method and apparatus for synthesis of ethanol and organic compounds |
CN113244768A (en) * | 2021-04-27 | 2021-08-13 | 薛保生 | Light oxygen exhaust-gas treatment equipment for industrial waste gas purification |
-
1991
- 1991-09-25 JP JP3273261A patent/JPH0576723A/en not_active Withdrawn
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6290238A (en) * | 1985-09-23 | 1987-04-24 | 旭化成株式会社 | Antistatic sheet-shaped article |
JP2007222867A (en) * | 2006-01-20 | 2007-09-06 | Erubu:Kk | Carbon dioxide gas purifying material, carbon dioxide gas purifying fiber and carbon dioxide gas purifying cloth, and carbon dioxide gas purifying apparatus |
JP4746569B2 (en) * | 2006-01-20 | 2011-08-10 | 株式会社エルブ | Carbon dioxide purification material, carbon dioxide purification fiber, carbon dioxide purification cloth, and carbon dioxide purification device |
JP2013519513A (en) * | 2010-02-19 | 2013-05-30 | コモンウェルス サイエンティフィック アンド インダストリアル リサーチ オーガニゼーション | Solvent treatment method |
WO2013028568A1 (en) * | 2011-08-19 | 2013-02-28 | Hychar Energy, Llc | Electronegative-ion-aided method and apparatus for synthesis of ethanol and organic compounds |
CN103796751A (en) * | 2011-08-19 | 2014-05-14 | 海加能源有限公司 | Electronegative-ion-aided method and apparatus for synthesis of ethanol and organic compounds |
CN102993053A (en) * | 2011-09-28 | 2013-03-27 | 海加能源有限公司 | Electronegative plasma assisted carbon dioxide emission reduction processing method and device thereof |
CN113244768A (en) * | 2021-04-27 | 2021-08-13 | 薛保生 | Light oxygen exhaust-gas treatment equipment for industrial waste gas purification |
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Legal Events
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