JPH03232718A - Device for synthesizing ammonia by plasma reaction - Google Patents

Device for synthesizing ammonia by plasma reaction

Info

Publication number
JPH03232718A
JPH03232718A JP2673090A JP2673090A JPH03232718A JP H03232718 A JPH03232718 A JP H03232718A JP 2673090 A JP2673090 A JP 2673090A JP 2673090 A JP2673090 A JP 2673090A JP H03232718 A JPH03232718 A JP H03232718A
Authority
JP
Japan
Prior art keywords
reaction
plasma
section
nitrogen
ammonia
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.)
Pending
Application number
JP2673090A
Other languages
Japanese (ja)
Inventor
Hideaki Hayano
早野 秀明
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.)
NEC Corp
Original Assignee
NEC Corp
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
Application filed by NEC Corp filed Critical NEC Corp
Priority to JP2673090A priority Critical patent/JPH03232718A/en
Publication of JPH03232718A publication Critical patent/JPH03232718A/en
Pending legal-status Critical Current

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  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PURPOSE:To efficiently synthesize ammonia by disposing a hydrogen peroxide water tank between a plasma reaction section and an exhaustion section and subjecting the plasma of nitrogen gas and hydroperoxide water as a hydrogen source to an interfacial reaction to produce the ammonia. CONSTITUTION:A gas supply section 20, a plasma reaction section 30 and an exhaustion section 40 are disposed and a hydrogen peroxide water tank 7 is further disposed between the reaction section 30 and the exhaustion section 40 to constitute an ammonia synthesis apparatus. The reaction system is evacuated to a high vacuum with a vacuum pump 12 and nitrogen gas is charged into a reaction oven 5 of the plasma reaction section 30 through a gas bomb 1. High frequency electric current produced from a high frequency electric power oscillated with a high frequency oscillator 10 is discharged into a reaction oven 5 to provide nitrogen plasma. Nitrogen molecule ions in the nitrogen plasma are sputtered to the hydrogen peroxide water tank 7 to generate hydrogen atoms, which interfacially react with nitrogen plasma to synthesise ammonia.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、プラズマ反応を用いたアンモニア合成装置に
関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an ammonia synthesis apparatus using plasma reaction.

〔従来の技術〕[Conventional technology]

従来、この種のプラズマ反応を用いたアンモニア合成装
置は、ガス供給機構部と、プラズマ反応機構部と、それ
らに付属する真空系形成用の真空ポンプ群とから構成さ
れており、プラズマ反応ガスとして水素ガスと窒素ガス
を用いてアンモニアの合成を行なっていた。
Conventionally, an ammonia synthesis apparatus using this type of plasma reaction consists of a gas supply mechanism section, a plasma reaction mechanism section, and a group of attached vacuum pumps for forming a vacuum system. Ammonia was synthesized using hydrogen gas and nitrogen gas.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上述した従来のプラズマ反応によるアンモニア合成装置
は、プラズマ反応ガスとして水素ガスと窒素ガスを用い
ており、アンモニア合成過程において反応に関与しない
水素ガスを多量に排出しているという欠点がある。
The conventional ammonia synthesis apparatus using a plasma reaction described above uses hydrogen gas and nitrogen gas as plasma reaction gases, and has the disadvantage that a large amount of hydrogen gas that does not participate in the reaction is discharged during the ammonia synthesis process.

〔課題を解決するための手段〕[Means to solve the problem]

本発明のプラズマ反応を用いたアンモニア合成装置は、
装置内に過酸化水素水を張った層がプラズマ反応部の下
流に設けられており、窒素プラズマと過酸化水素水と・
の界面反応によりアンモニアが合成される。
The ammonia synthesis apparatus using plasma reaction of the present invention is
A layer filled with hydrogen peroxide is installed in the device downstream of the plasma reaction section, and nitrogen plasma and hydrogen peroxide are mixed together.
Ammonia is synthesized through an interfacial reaction.

〔実施例〕〔Example〕

次に、本発明について図面を参照して説明する。第1図
は本発明のプラズマ反応を用いたアンモニア合成装置の
一実施例の構成図である。プラズマ反応を用いたアンモ
ニア合成装置は、N2ガスボンベ1とニードルバルブ2
とガスラインフィルタ3とマスフローコントローラ4よ
りなるガス供給部20と、反応炉5と誘導コイル6と過
酸化水素水槽7と圧力計8と電力計9と高周波発振器1
0とからなる反応部30と、ストップバルブ11と真空
ポンプ12と液体窒素トラップ13よりなる排気部40
の三部から構成されている。反応に際し、反応系内を5
0Torr前後まで液体窒素トラップ13を通して真空
ポンプ12により排気し、反応ガスとしての窒素ガスを
ガスボンベ1よリマスフローコントローラ4を通し、所
定の流量にてプラズマ反応部30の反応炉5へ導入する
Next, the present invention will be explained with reference to the drawings. FIG. 1 is a block diagram of an embodiment of an ammonia synthesis apparatus using plasma reaction according to the present invention. The ammonia synthesis device using plasma reaction consists of N2 gas cylinder 1 and needle valve 2.
A gas supply section 20 consisting of a gas line filter 3 and a mass flow controller 4, a reactor 5, an induction coil 6, a hydrogen peroxide tank 7, a pressure gauge 8, a power meter 9, and a high frequency oscillator 1
0, an exhaust section 40 consisting of a stop valve 11, a vacuum pump 12, and a liquid nitrogen trap 13.
It consists of three parts. During the reaction, the inside of the reaction system is
The gas is evacuated by the vacuum pump 12 through the liquid nitrogen trap 13 to around 0 Torr, and nitrogen gas as a reaction gas is introduced into the reaction furnace 5 of the plasma reaction section 30 at a predetermined flow rate from the gas cylinder 1 through the remass flow controller 4.

ガス圧力は、圧力計8にて所定の圧力に設定する。電力
は周波数13.56MHz、出力200Wの高周波発振
器10より誘導結合方式により移送する0反応炉5内の
放電によって生成された窒素プラズマ中の窒素分子イオ
ンによるプラズマ反応アフターグロ一部下端に張られた
過酸化水素水槽7へのスパッタリングによりアンモニア
合成の水素源である水素が供給され、下記の反応が進行
し、アンモニアが合成される。
The gas pressure is set to a predetermined pressure using a pressure gauge 8. Electric power is transferred by an inductive coupling method from a high frequency oscillator 10 with a frequency of 13.56 MHz and an output of 200 W.A plasma reaction afterglow caused by nitrogen molecular ions in the nitrogen plasma generated by the discharge in the reactor 5 is applied to a part of the lower end. Hydrogen, which is a hydrogen source for ammonia synthesis, is supplied by sputtering to the hydrogen peroxide tank 7, and the following reaction proceeds to synthesize ammonia.

N2 +e−+N” 2 +2e      −−−−
(a)N” 2 +H202+e→2NH+02−・・
(b)NH十H−+NH2・・・・・・(C)NH2+
H4NH3・・・・・・(d)〔発明の効果〕 以上説明したように本発明は、プラズマ反応を用いたア
ンモニア合成装置に過酸化水素水を張った槽を設けるこ
とにより、過酸化水素水を水素源とし、窒素プラズマと
の界面反応からアンモニア合成ができるという効果があ
る。
N2 +e-+N" 2 +2e ---
(a)N" 2 +H202+e→2NH+02-...
(b) NH1H-+NH2... (C) NH2+
H4NH3... (d) [Effects of the Invention] As explained above, the present invention provides hydrogen peroxide solution by providing a tank filled with hydrogen peroxide solution in an ammonia synthesis apparatus using plasma reaction. The effect is that ammonia can be synthesized from an interfacial reaction with nitrogen plasma using hydrogen as a hydrogen source.

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

第1図は、本発明の一実施例のプラズマ反応を用いたア
ンモニア合成装置の構成図である。 1・・・N2ガスボンベ、2・・・ニードルバルブ、3
・・・ガスラインフィルタ、4・・・マスフローコント
ローラ、5・・・反応炉、6・・・誘導コイル、7・・
・過酸化水素水槽、8・・・圧力計、9・・・電力計、
10・・・高周波発振器、11・・・ストップバルブ、
12・・・真空ポンプ、13・・・液体窒素トラップ、
20・・・ガス供給部、20・・・反応部、40・・・
排気部。
FIG. 1 is a block diagram of an ammonia synthesis apparatus using plasma reaction according to an embodiment of the present invention. 1...N2 gas cylinder, 2...needle valve, 3
... Gas line filter, 4... Mass flow controller, 5... Reactor, 6... Induction coil, 7...
・Hydrogen peroxide tank, 8...pressure gauge, 9...power meter,
10... High frequency oscillator, 11... Stop valve,
12... Vacuum pump, 13... Liquid nitrogen trap,
20... Gas supply section, 20... Reaction section, 40...
Exhaust part.

Claims (1)

【特許請求の範囲】[Claims] ガス供給部とプラズマ反応部と排気部とを有しているプ
ラズマ反応を用いたアンモニア合成装置において、前記
プラズマ反応部と排気部との間にプラズマと界面反応を
生じる過酸化水素水槽を含むことを特徴とするプラズマ
反応を用いたアンモニア合成装置。
An ammonia synthesis apparatus using a plasma reaction that includes a gas supply section, a plasma reaction section, and an exhaust section, including a hydrogen peroxide tank that causes an interfacial reaction with plasma between the plasma reaction section and the exhaust section. An ammonia synthesis device using a plasma reaction characterized by:
JP2673090A 1990-02-05 1990-02-05 Device for synthesizing ammonia by plasma reaction Pending JPH03232718A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2673090A JPH03232718A (en) 1990-02-05 1990-02-05 Device for synthesizing ammonia by plasma reaction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2673090A JPH03232718A (en) 1990-02-05 1990-02-05 Device for synthesizing ammonia by plasma reaction

Publications (1)

Publication Number Publication Date
JPH03232718A true JPH03232718A (en) 1991-10-16

Family

ID=12201434

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2673090A Pending JPH03232718A (en) 1990-02-05 1990-02-05 Device for synthesizing ammonia by plasma reaction

Country Status (1)

Country Link
JP (1) JPH03232718A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010132469A (en) * 2008-12-02 2010-06-17 Toyota Gakuen Method and apparatus for producing nitrogen compound

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010132469A (en) * 2008-12-02 2010-06-17 Toyota Gakuen Method and apparatus for producing nitrogen compound

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