JP3421804B2 - Discharge gas treatment method and treatment apparatus utilizing heat cycle - Google Patents

Discharge gas treatment method and treatment apparatus utilizing heat cycle

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Publication number
JP3421804B2
JP3421804B2 JP2000021586A JP2000021586A JP3421804B2 JP 3421804 B2 JP3421804 B2 JP 3421804B2 JP 2000021586 A JP2000021586 A JP 2000021586A JP 2000021586 A JP2000021586 A JP 2000021586A JP 3421804 B2 JP3421804 B2 JP 3421804B2
Authority
JP
Japan
Prior art keywords
gas
discharge
pressure
gas treatment
heat cycle
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 - Lifetime
Application number
JP2000021586A
Other languages
Japanese (ja)
Other versions
JP2001205038A (en
Inventor
正純 藤原
政義 石田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
National Institute of Advanced Industrial Science and Technology AIST
Priority date (The priority date 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 date listed.)
Filing date
Publication date
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Priority to JP2000021586A priority Critical patent/JP3421804B2/en
Publication of JP2001205038A publication Critical patent/JP2001205038A/en
Application granted granted Critical
Publication of JP3421804B2 publication Critical patent/JP3421804B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、放電励起化学反応
を用いた排ガスNOx処理やVOC汚染空気処理、オゾン
生成等のガス処理に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to exhaust gas NOx treatment using discharge-excited chemical reaction, VOC polluted air treatment, and gas treatment such as ozone generation.

【0002】[0002]

【従来の技術】大気圧近傍のガス中で放電を行い、N、
O、OH等の活性種を生成し、それらの関与する化学反
応を利用してガス中に含まれるNOxやVOC(揮発性
有機化合物)等の汚染物質を処理する方法について開発
が進められている。また、同様な方式でオゾン生成を行
う装置はオゾナイザとして市販されている。
2. Description of the Related Art Discharge is performed in a gas near atmospheric pressure, and N,
Development of a method for generating active species such as O and OH and treating pollutants such as NOx and VOC (volatile organic compounds) contained in gas by utilizing chemical reactions involved in them is under way. . A device that produces ozone in a similar manner is commercially available as an ozonizer.

【0003】このような放電励起化学反応を利用するガ
ス処理装置では、ガス圧を低下させることにより、活性
種の生成効率の向上や印加電圧の低減が可能である。こ
のような減圧放電を適用することにより性能向上を実現
する方式に関する提案は既に行われている。(電気学会
論文誌A,116−9,P791(1996)、特開平11−475
44)これらの方式では、ガス注入等の方法に工夫がな
されてはいるが、放電容器の減圧に関しては、図2に示
すように、放電容器21内を真空ポンプ22により減圧
状態に保ち、被処理ガスを放電容器内でガス処理して排
気する方式である。
In the gas treatment apparatus utilizing such a discharge-excited chemical reaction, it is possible to improve the generation efficiency of active species and the applied voltage by lowering the gas pressure. Proposals have already been made regarding a method of improving performance by applying such reduced-pressure discharge. (The Institute of Electrical Engineers of Japan, A, 116-9, P791 (1996), JP-A-11-475.
44) In these methods, although a method such as gas injection is devised, as for the pressure reduction of the discharge vessel, as shown in FIG. This is a system in which the processing gas is processed in the discharge vessel and exhausted.

【0004】[0004]

【発明が解決しようとする課題】このような減圧放電を
適用するガス処理方法に関しては、減圧に要するエネル
ギーが大きく、真空ポンプを駆動するときには多くの電
力を必要とするという問題がある。しかしながら、この
点に関しては、これまで十分な検討が行われていない。
なお、被処理ガスが大気圧以上の圧力を有する場合に
は、大気圧までの減圧は、エネルギー注入は不要であ
り、大気圧以下に減圧する場合にエネルギーが必要とな
る。そこで、以下では、被処理ガスを大気圧とし、これ
を減圧する場合について考察する。
The gas treatment method applying such a reduced pressure discharge has a problem that the energy required for the pressure reduction is large and a large amount of electric power is required to drive the vacuum pump. However, this point has not been sufficiently studied so far.
When the gas to be processed has a pressure of atmospheric pressure or higher, depressurization to atmospheric pressure does not require energy injection, and energy is required when depressurizing to atmospheric pressure or lower. Therefore, in the following, a case will be considered in which the gas to be treated is at atmospheric pressure and the pressure is reduced.

【0005】この場合、減圧過程を断熱膨張として取扱
うことにより、減圧に要するエネルギーを見積ることが
できる。すなわち、熱力学的考察により断熱膨張に要す
る最小エネルギーは、被処理ガスのエンタルピー減少量
で与えられる。例えば、常温の窒素ガスを1気圧から
0.5気圧まで断熱膨張させる場合の所要エネルギー
は、54J/gである。このエネルギーを濃度300pp
mのガス成分の処理に使用する場合には、1分子を処理
するための消費エネルギーは、52eVとなる。大気圧放
電によりNOx処理を行う場合に、NOx1分子の処理に要す
るエネルギーは、20〜200eV/moleculeであるか
ら、減圧に要するエネルギーを上回る効果を生み出すこ
とは容易ではない。
In this case, the energy required for decompression can be estimated by treating the decompression process as adiabatic expansion. That is, the minimum energy required for adiabatic expansion is given by the amount of enthalpy reduction of the gas to be treated from thermodynamic considerations. For example, the required energy for adiabatic expansion of nitrogen gas at room temperature from 1 atm to 0.5 atm is 54 J / g. This energy has a concentration of 300 pp
When it is used for processing the gas component of m, the energy consumption for processing one molecule is 52 eV. When NOx treatment is performed by atmospheric pressure discharge, the energy required to treat one NOx molecule is 20 to 200 eV / molecule, so it is not easy to produce an effect that exceeds the energy required to reduce pressure.

【0006】[0006]

【課題を解決するための手段】本願発明は、上記課題を
解決するため、請求項1に係る発明は、被処理ガスを膨
張させることにより減圧し、減圧下で放電を行った後圧
縮し、この圧縮過程に要した仕事量の一部を膨張過程に
おいて回収し、その後、放電により注入・熱化したエネ
ルギーを放熱するサイクルを繰り返すことを特徴とする
熱サイクル利用放電ガス処理方法としたものである。
In order to solve the above-mentioned problems, the present invention according to claim 1 reduces the pressure by expanding the gas to be treated, discharges it under reduced pressure, and then compresses it. A part of the work required for this compression process is recovered in the expansion process, and then the cycle of releasing the energy injected / heated by the discharge is repeated. is there.

【0007】上記目的を達成するため、請求項2に係る
発明は、被処理ガスを膨張させることにより圧縮過程に
要した仕事量の一部を回収する減圧器と、減圧器通過後
減圧下で放電を行い被処理ガスを処理する処理容器
と、処理容器内で処理したガスを圧縮して排気し、放電
により注入・熱化したエネルギーを放熱する圧縮器とか
らなることを特徴とする熱サイクル利用放電ガス処理装
置としたものである。
In order to achieve the above object, the invention according to claim 2 is to perform a compression process by expanding the gas to be treated.
A pressure reducer that collects a part of the required work , and after passing through the pressure reducer
The processing container that discharges under a reduced pressure to process the gas to be processed, and the gas processed in the processing container is compressed and exhausted to discharge
A discharge gas treatment device utilizing a heat cycle, which is characterized by comprising a compressor for radiating the energy injected / heated by.

【0008】[0008]

【発明の実施の形態】最初、本発明の基本原理について
述べる。本発明では、膨張(減圧)→放電→圧縮→放熱
のサイクルを繰返す。放電により注入し熱化したエネル
ギーは、放熱過程により放出される。
First, the basic principle of the present invention will be described. In the present invention, the cycle of expansion (decompression) → discharge → compression → heat dissipation is repeated. The energy injected and heated by the discharge is released by the heat dissipation process.

【0009】本サイクルは、ヒートポンプサイクルの1
種であり、加熱過程を放電で行うことに相当する。ガス
処理を行う場合のヒートポンプサイクルとしては、ブレ
イトンサイクルの利用が最も現実的である。この場合、
断熱膨張→等圧加熱(放電)→断熱圧縮→等圧冷却とい
うサイクルとなる。この場合には、圧縮過程において仕
事を行い、その仕事量の一部を膨張過程において回収し
ている。理想的な場合を考えると、放電入力Einと外部
から投入する仕事量Winの比率は、圧縮/膨張の圧力比
βと、被処理ガスの定圧比熱/定積比熱であるγを用い
て、
This cycle is one of the heat pump cycles.
It is a seed and corresponds to performing the heating process by electric discharge. The most practical use of the Brayton cycle is as a heat pump cycle for gas treatment. in this case,
The cycle is adiabatic expansion → isobaric heating (discharge) → adiabatic compression → isobaric cooling. In this case, work is performed in the compression process, and a part of the work amount is recovered in the expansion process. Considering an ideal case, the ratio of the discharge input Ein and the work amount Win input from the outside is calculated by using the compression / expansion pressure ratio β and the constant pressure specific heat / constant volume specific heat γ of the gas to be treated.

【数1】 で与えられる。[Equation 1] Given in.

【0010】例えば、前述の常温窒素ガスを1/2気圧
に減圧する場合には、Win/Einは0.22となる。即
ち、放電入力の約1/5のエネルギーを減圧仕事に投入
することにより、圧力を1/2に減圧できる。それに伴
い、活性種の生成効率向上や印加電圧の半減が可能であ
り、トータルのエネルギー効率の向上が期待できる。
For example, when the normal temperature nitrogen gas is decompressed to 1/2 atm, Win / Ein becomes 0.22. That is, the pressure can be reduced to 1/2 by putting about 1/5 of the energy of the discharge input into the decompression work. Along with this, it is possible to improve the generation efficiency of active species and halve the applied voltage, and it can be expected that the total energy efficiency will be improved.

【0011】図1に本発明の一実施例を示す。図1はガス
タービンエンジンと類似の機構を用いた実施例である。
ガスタービンエンジンとの違いは、中央の放電容器を減
圧するために、タービンと圧縮機の配置が逆になってい
る点である。
FIG. 1 shows an embodiment of the present invention. FIG. 1 shows an embodiment using a mechanism similar to that of a gas turbine engine.
The difference from the gas turbine engine is that the arrangement of the turbine and the compressor is reversed in order to reduce the pressure in the central discharge vessel.

【0012】図1に示す装置においては、モーター1に
より圧縮器2を駆動し、放電容器3内を減圧する。減圧
した放電容器3内で放電を行い、放電励起化学反応によ
りNOx除去等のガス処理を行う。大気圧の被処理ガスが
減圧された放電容器3内に流入する際に、タービン4を
駆動する。タービン4と圧縮器2は駆動軸5が直結して
おり、タービン4で得られた駆動力は、圧縮器2の駆動
に利用される。その結果、放電容器3内を減圧するため
のモータ1の負荷を軽減することができる。放電容器3
内で放電処理されたガスは、圧縮機2により大気圧まで
加圧され、排出される。
In the apparatus shown in FIG. 1, the motor 1 drives the compressor 2 to reduce the pressure in the discharge vessel 3. Discharge is performed in the discharge vessel 3 under reduced pressure, and gas treatment such as NOx removal is performed by a discharge-excited chemical reaction. The turbine 4 is driven when the atmospheric pressure target gas flows into the reduced pressure discharge vessel 3. The drive shaft 5 is directly connected to the turbine 4 and the compressor 2, and the driving force obtained by the turbine 4 is used to drive the compressor 2. As a result, the load on the motor 1 for reducing the pressure inside the discharge vessel 3 can be reduced. Discharge vessel 3
The gas that has been subjected to the discharge treatment is pressurized to the atmospheric pressure by the compressor 2 and is discharged.

【0013】[0013]

【発明の効果】本願発明は上記のように構成したので、
請求項1及び請求項2に係る発明は、放電励起化学反応
を利用したNOx除去やオゾン生成等のガス処理におい
て、減圧下で放電を行うことにより、活性種の生成効率
向上や印加電圧の低減が可能となる。その結果、ガス処
理装置の総合的エネルギー効率を向上させることが可能
となる。
Since the present invention is configured as described above,
The invention according to claim 1 and claim 2 improves the generation efficiency of active species and reduces the applied voltage by performing discharge under reduced pressure in gas treatment such as NOx removal and ozone generation using discharge-excited chemical reaction. Is possible. As a result, it is possible to improve the overall energy efficiency of the gas treatment device.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例を示すガス処理装置の槻略構
成図である。
FIG. 1 is a schematic configuration diagram of a gas treatment device according to an embodiment of the present invention.

【図2】従来の減圧放電式ガス処理装置の一例を示す槻
略構成図である。
FIG. 2 is a schematic configuration diagram showing an example of a conventional low pressure discharge gas treatment apparatus.

【符号の説明】[Explanation of symbols]

1 モータ 2 圧縮機 3 放電容器 4 タービン 5 駆動軸 1 motor 2 compressor 3 discharge vessel 4 turbine 5 drive shaft

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 53/32 B01D 53/34 B01J 19/08 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields surveyed (Int.Cl. 7 , DB name) B01D 53/32 B01D 53/34 B01J 19/08

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 被処理ガスを膨張させることにより減圧
し、減圧下で放電を行った後圧縮し、この圧縮過程に要
した仕事量の一部を膨張過程において回収し、その後、
放電により注入・熱化したエネルギーを放熱するサイク
ルを繰り返すことを特徴とする熱サイクル利用放電ガス
処理方法。
1. A gas to be treated is decompressed by expanding it, discharged under reduced pressure and then compressed, and a part of the work required for this compression process is recovered in the expansion process.
A discharge gas treatment method using a heat cycle, characterized in that a cycle of releasing the energy injected / heated by discharge is repeated.
【請求項2】 被処理ガスを膨張させることにより圧縮
過程に要した仕事量の一部を回収する減圧器と、減圧器
通過後の減圧下で放電を行い被処理ガスを処理する処理
容器と、処理容器内で処理したガスを圧縮して排気し、
放電により注入・熱化したエネルギーを放熱する圧縮器
とからなることを特徴とする熱サイクル利用放電ガス処
理装置。
2. Compressing by expanding the gas to be treated
A pressure reducer that recovers a part of the work required for the process, and a pressure reducer
After the passage, a processing container that discharges under reduced pressure to process the gas to be processed, and the gas processed in the processing container is compressed and exhausted ,
A discharge gas treatment device using a heat cycle, which comprises a compressor that radiates the energy injected / heated by electric discharge.
JP2000021586A 2000-01-31 2000-01-31 Discharge gas treatment method and treatment apparatus utilizing heat cycle Expired - Lifetime JP3421804B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000021586A JP3421804B2 (en) 2000-01-31 2000-01-31 Discharge gas treatment method and treatment apparatus utilizing heat cycle

Publications (2)

Publication Number Publication Date
JP2001205038A JP2001205038A (en) 2001-07-31
JP3421804B2 true JP3421804B2 (en) 2003-06-30

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Country Status (1)

Country Link
JP (1) JP3421804B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100635283B1 (en) * 2003-03-04 2006-10-17 주식회사 엘지화학 VENT GAS ABSORPTION SYSTEM AND METHOD FOR RECOVERY VOCs
US8968438B2 (en) 2007-07-10 2015-03-03 Innovalight, Inc. Methods and apparatus for the in situ collection of nucleated particles
US8471170B2 (en) 2007-07-10 2013-06-25 Innovalight, Inc. Methods and apparatus for the production of group IV nanoparticles in a flow-through plasma reactor

Also Published As

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