JPH0374082A - Catalyst reactor - Google Patents
Catalyst reactorInfo
- Publication number
- JPH0374082A JPH0374082A JP1210924A JP21092489A JPH0374082A JP H0374082 A JPH0374082 A JP H0374082A JP 1210924 A JP1210924 A JP 1210924A JP 21092489 A JP21092489 A JP 21092489A JP H0374082 A JPH0374082 A JP H0374082A
- Authority
- JP
- Japan
- Prior art keywords
- microwave
- magnetron
- layer
- catalyst
- microwave absorbing
- 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.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 28
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000011358 absorbing material Substances 0.000 claims abstract description 6
- 239000011787 zinc oxide Substances 0.000 claims abstract description 5
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910010271 silicon carbide Inorganic materials 0.000 claims abstract description 3
- 238000006555 catalytic reaction Methods 0.000 claims description 11
- 238000001514 detection method Methods 0.000 claims description 8
- 239000011148 porous material Substances 0.000 claims description 6
- 238000010521 absorption reaction Methods 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 claims description 3
- 229910052863 mullite Inorganic materials 0.000 claims description 3
- 229910052878 cordierite Inorganic materials 0.000 claims description 2
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910000314 transition metal oxide Inorganic materials 0.000 claims description 2
- 230000000903 blocking effect Effects 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 241000264877 Hippospongia communis Species 0.000 abstract 4
- 241000894007 species Species 0.000 abstract 1
- 229910052723 transition metal Inorganic materials 0.000 abstract 1
- 150000003624 transition metals Chemical class 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 229910000420 cerium oxide Inorganic materials 0.000 description 3
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000012495 reaction gas Substances 0.000 description 2
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 1
- 239000005751 Copper oxide Substances 0.000 description 1
- HMDDXIMCDZRSNE-UHFFFAOYSA-N [C].[Si] Chemical compound [C].[Si] HMDDXIMCDZRSNE-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910000431 copper oxide Inorganic materials 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Control Of High-Frequency Heating Circuits (AREA)
- Constitution Of High-Frequency Heating (AREA)
- Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明はガス状物質を触媒反応により別のガス状物質に
転換する触媒反応装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a catalytic reaction apparatus for converting a gaseous substance into another gaseous substance by a catalytic reaction.
従来の技術
従来のこの種の触媒反応装置は第2図に示すように、反
応管1内に触媒2を配設し、外部熱源3により触媒体2
を一定温度に加熱し、ガス状物質4を別のガス状物質5
に転換するように構成されており、触媒体2の細孔6の
中をガス状物質4が通過する時、触媒反応が起こるよう
になっていた。BACKGROUND OF THE INVENTION A conventional catalytic reaction apparatus of this type, as shown in FIG.
is heated to a constant temperature, and the gaseous substance 4 is heated to another gaseous substance 5.
When the gaseous substance 4 passes through the pores 6 of the catalyst body 2, a catalytic reaction occurs.
触媒体2は第2図すに示すようなハニカム状の断面構造
をしており、細孔6の壁に触媒層8が担持されてい・る
。The catalyst body 2 has a honeycomb-like cross-sectional structure as shown in FIG. 2, and a catalyst layer 8 is supported on the walls of the pores 6.
発明が解決しようとする課題
しかしながら上記のような構成では、触媒体を外部熱源
により加熱するためエネルギー損失が大きいという問題
点を有していた。Problems to be Solved by the Invention However, the above configuration has a problem in that energy loss is large because the catalyst body is heated by an external heat source.
本発明はかかる従来の問題を解決するもので、エネルギ
ー損失の少ない触媒反応装置を提供することを目的とす
る。The present invention solves such conventional problems and aims to provide a catalytic reaction device with less energy loss.
課題を解決するための手段
上記課題点を解決するために本発明の触媒反応装置は、
アルミナ、ムライト、コージェライトの群から選ばれた
非マイクロ波吸収材料からなるハニカム構造体の細孔内
壁に炭化けい素、酸化亜鉛、遷移金属酸化物の群から選
ばれたマイクロ波吸収層を設け、前記マイクロ波吸収層
の表面に触媒層を設けた触媒体を、マグネトロン、1&
11の温度検出素子、マグネトロン出力制御回路を配設
したマイクロ波空洞共振器内に配設した構成を備えたも
のである。Means for Solving the Problems In order to solve the above problems, the catalytic reaction apparatus of the present invention includes:
A microwave absorbing layer selected from the group of silicon carbide, zinc oxide, and transition metal oxide is provided on the inner wall of the pores of a honeycomb structure made of a non-microwave absorbing material selected from the group of alumina, mullite, and cordierite. , the catalyst body with the catalyst layer provided on the surface of the microwave absorption layer was placed in a magnetron, 1&
This device has a configuration in which eleven temperature detection elements and a magnetron output control circuit are arranged inside a microwave cavity resonator.
作用
本発明は上記した構成によってマグネトロンで発生した
マイクロ波はハニカム構造体のマイクロ波吸収層に吸収
され、触媒層温度を上昇させる。Operation According to the present invention, the microwave generated by the magnetron is absorbed by the microwave absorbing layer of the honeycomb structure, thereby increasing the temperature of the catalyst layer.
内部に触媒体を配設したマイクロ波空洞共振器にはマグ
ネトロン、1組の温度検出素子とマグネトロン出力制御
回路を連結配設することにより、触媒体の温度を一定に
保持する。すなわち触媒体の入口と出口のガス温度を1
組の温度検出素子により測定しながらマグネトロンおよ
びマグネトロン出力制御回路を動作させて触媒体の温度
を一定に保持するものである。A magnetron, a set of temperature detection elements, and a magnetron output control circuit are connected to the microwave cavity resonator in which the catalyst body is arranged, thereby maintaining the temperature of the catalyst body constant. In other words, the gas temperature at the inlet and outlet of the catalyst body is 1
The temperature of the catalyst body is maintained constant by operating the magnetron and magnetron output control circuit while measuring the temperature using a set of temperature detection elements.
実施例
以下、本発明の実施例を添付図面にもとづいて説明する
。Embodiments Hereinafter, embodiments of the present invention will be described based on the accompanying drawings.
第1図aにおいて9は内径41閣、外径43m、長さ1
20−のステンレス製マイクロ波空洞共振器であり、そ
の内部に触媒体10、前記触媒体の前後にマイクロ波遮
蔽用金1M11、前記金網の外側に温度検出素子12を
配設し、空洞共振器9に接してマグネトロン13、前記
マグネトロンに接続してマグネトロン出力制御回路14
を配設し、同回路はは温度検出素子12と接続されてい
る。前記触媒体1oの断−面は第2図すに示すようにム
ライトからなる非マイクロ波吸収材料で構成した直径4
o■、長さ80m。In Figure 1a, 9 has an inner diameter of 41 m, an outer diameter of 43 m, and a length of 1
20- stainless steel microwave cavity resonator, which includes a catalyst body 10 inside, a microwave shielding metal 1M11 before and after the catalyst body, and a temperature detection element 12 outside the metal mesh. A magnetron 13 is connected to the magnetron 9, and a magnetron output control circuit 14 is connected to the magnetron.
This circuit is connected to the temperature detection element 12. As shown in FIG.
o ■, length 80m.
90セル/1n1のハニカム構造体15の細孔15aの
内壁に酸化亜鉛ウィスカーからなるマイクロ波吸収層1
6を設け、その表面に酸化セリウム触媒層17が設けら
れている。酸化セリウムは150”C以上になると一酸
化炭素を酸化して炭酸ガスに転換する触゛媒作用を示す
、前記触媒体をマイクロ波で150’Cに加熱するため
には100Wの高周波出力でよく、立上り時間も5秒で
あった8本触媒反応装置に一酸化炭素濃度1%の空気バ
ランスガス4を空間速度5ooo h −tで流すと出
口からは一酸化炭素を含まない反応ガス5が排出した。A microwave absorbing layer 1 made of zinc oxide whiskers is placed on the inner wall of the pores 15a of the honeycomb structure 15 of 90 cells/1n1.
6, and a cerium oxide catalyst layer 17 is provided on the surface thereof. Cerium oxide exhibits a catalytic effect that oxidizes carbon monoxide and converts it into carbon dioxide gas when the temperature exceeds 150'C. To heat the catalyst body to 150'C with microwaves, a high frequency output of 100W is sufficient. When air balance gas 4 with a carbon monoxide concentration of 1% is flowed at a space velocity of 5 ooo h -t through an 8-catalytic reactor with a rise time of 5 seconds, a reaction gas 5 containing no carbon monoxide is discharged from the outlet. did.
比較のため第2図に示す外部加熱式の従来装置で本実施
例と同じ立上り時間、同じ保持温度とするためには、初
期の3秒間はI KW、その後は400Wの電力が必要
であった。For comparison, in order to achieve the same rise time and the same holding temperature as in this example using the external heating type conventional device shown in Fig. 2, a power of I KW was required for the initial 3 seconds and 400 W thereafter. .
次に本発明の他の実施例を第1図を用いて説明する。前
記実施例と相異する点はムライトハニカムの代わりにア
ルミナハニカム、酸化亜鉛ウィスカー、マイクロ波吸収
層の代わりに炭素けい素からなるマイクロは波吸収層を
設け、その表面に酸化セリウム、酸化マンガン、酸化銅
からなる複合ペロブスカイト構造触媒層を設けた点であ
る。前記触媒は200℃以上になるとプロピレンなどの
炭化水素を酸化して炭酸ガスと水に転換する触媒作用を
示す。Next, another embodiment of the present invention will be described with reference to FIG. The difference from the above embodiment is that alumina honeycomb is used instead of mullite honeycomb, zinc oxide whiskers are used, and a microwave absorption layer made of carbon silicon is provided instead of a microwave absorption layer, and cerium oxide, manganese oxide, The feature is that a composite perovskite structure catalyst layer made of copper oxide is provided. The catalyst exhibits a catalytic action of oxidizing hydrocarbons such as propylene and converting them into carbon dioxide and water at temperatures above 200°C.
前記触媒体をブイクロ波で200℃に加熱するためには
150Wの高周波出力でよく、立上り時間も7秒であっ
た0本触媒反応装置にプロピレン濃度1%の空気バラン
スガスを空間速度5000 h −’で流すと出口から
はプロピレンを含まない反応ガスが排出した。比較のた
め第2図に示す外部加熱式の従来装置で本実施例と同じ
立上り時間、同じ保持温度とするためには、初期の5秒
間は1.5KW、その後は700Wの電力が必要であっ
た。In order to heat the catalyst body to 200° C. using a microwave, a high frequency output of 150 W is sufficient, and the rise time is 7 seconds. Air balance gas with a propylene concentration of 1% was fed into a zero catalytic reactor at a space velocity of 5000 h − When flowing at ', a reaction gas containing no propylene was discharged from the outlet. For comparison, in order to achieve the same rise time and the same holding temperature as in this example using the external heating type conventional device shown in Fig. 2, a power of 1.5 KW is required for the initial 5 seconds and 700 W thereafter. Ta.
発明の効果
以上のように本発明の触媒反応装置によれば次の効果が
得られる。Effects of the Invention As described above, the catalytic reaction apparatus of the present invention provides the following effects.
(1)非マイクロ波吸収材料からなるハニカム構造体の
細孔内壁にマイクロ波吸収層を設けた構成としているの
で従来と比較すると低エネルギーで短時間に昇温できる
触媒反応装置ができるという効果がある。(1) Since the honeycomb structure is made of a non-microwave absorbing material and has a microwave absorbing layer on the inner wall of the pores, it is possible to create a catalytic reaction device that can raise the temperature in a short time with lower energy than conventional methods. be.
■ マイクロ波空洞共振器内に1組の温度検出素子を配
設し、前記素子に連結してマグネトロン出力制御回路、
前記回路にマグネトロンを連結して配役する構成として
いるので、入口ガス温度と出口ガス温度の差より化学反
応速度(従って触媒体温度)の制御ができるという効果
がある。■ A set of temperature detection elements is arranged inside the microwave cavity resonator, and connected to the elements, a magnetron output control circuit,
Since a magnetron is connected to the circuit, the chemical reaction rate (therefore, the catalyst temperature) can be controlled based on the difference between the inlet gas temperature and the outlet gas temperature.
第1図aおよびbは本発明の実施例における触媒反応装
置および触媒体の各断面図、第2図碓aおよびbは従来
の触媒反応装置および触媒体の各断面図である。
9・・・・・・マイクロ波空洞共振器、IO・・・・・
・触媒体、11・・・・・・温度検出素子、12・・・
・・・マイクロ波遮蔽用金網、13・・・・・・マグネ
トロン、14・・・・・・マイクロ波出力制御回路、1
5・・・・・・非マイクロ波吸収ハニカム構造体、16
・・・・・・マイクロ波吸収層、17・・・・・・触媒
層。1A and 1B are cross-sectional views of a catalytic reaction apparatus and a catalyst body according to an embodiment of the present invention, and FIGS. 2A and 2B are cross-sectional views of a conventional catalytic reaction apparatus and a catalyst body. 9...Microwave cavity resonator, IO...
- Catalyst body, 11...Temperature detection element, 12...
...Microwave shielding wire mesh, 13...Magnetron, 14...Microwave output control circuit, 1
5...Non-microwave absorbing honeycomb structure, 16
...Microwave absorption layer, 17...Catalyst layer.
Claims (1)
非マイクロ波吸収材料からなるハニカム構造体の細孔内
壁に炭化けい素、酸化亜鉛、遷移金属酸化物の群から選
ばれたマイクロ波吸収層を設け、前記マイクロ波吸収層
表面に触媒層を設けた触媒体を、内部に1組のマイクロ
波遮断用金網および前記金網の外側に1組の温度検出素
子、外部にマグネトロンおよびマイクロ波出力制御回路
を配設したマイクロ波空洞共振器内に配設した触媒反応
装置。A microwave absorbing layer selected from the group of silicon carbide, zinc oxide, and transition metal oxide is provided on the inner wall of the pores of a honeycomb structure made of a non-microwave absorbing material selected from the group of alumina, mullite, and cordierite. , a catalyst body having a catalyst layer on the surface of the microwave absorption layer, a set of microwave blocking wire mesh inside, a set of temperature detection element outside the wire mesh, and a magnetron and a microwave output control circuit outside. A catalytic reaction device placed inside a microwave cavity resonator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1210924A JP2643467B2 (en) | 1989-08-16 | 1989-08-16 | Catalytic reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1210924A JP2643467B2 (en) | 1989-08-16 | 1989-08-16 | Catalytic reactor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0374082A true JPH0374082A (en) | 1991-03-28 |
JP2643467B2 JP2643467B2 (en) | 1997-08-20 |
Family
ID=16597332
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1210924A Expired - Fee Related JP2643467B2 (en) | 1989-08-16 | 1989-08-16 | Catalytic reactor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2643467B2 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009110245A1 (en) * | 2008-03-05 | 2009-09-11 | マイクロ波環境化学株式会社 | Microwave chemical reaction device and reaction method using said device |
JP2013043456A (en) * | 2011-08-22 | 2013-03-04 | Takumi:Kk | Heating unit of heating device for vehicle |
WO2014136456A1 (en) * | 2013-03-07 | 2014-09-12 | 国立大学法人東京工業大学 | Complex-heating method and device, catalytic reaction device, catalytic unit, and manufacturing method therefor |
KR101707043B1 (en) * | 2016-06-24 | 2017-02-16 | 이정식 | Soft-boiled roaster using perforated drum |
WO2020084934A1 (en) * | 2018-10-26 | 2020-04-30 | 富士電機株式会社 | Electric dust collector |
-
1989
- 1989-08-16 JP JP1210924A patent/JP2643467B2/en not_active Expired - Fee Related
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009110245A1 (en) * | 2008-03-05 | 2009-09-11 | マイクロ波環境化学株式会社 | Microwave chemical reaction device and reaction method using said device |
JP2013043456A (en) * | 2011-08-22 | 2013-03-04 | Takumi:Kk | Heating unit of heating device for vehicle |
WO2014136456A1 (en) * | 2013-03-07 | 2014-09-12 | 国立大学法人東京工業大学 | Complex-heating method and device, catalytic reaction device, catalytic unit, and manufacturing method therefor |
JP5892635B2 (en) * | 2013-03-07 | 2016-03-23 | 国立大学法人東京工業大学 | Composite heating method and heating apparatus |
JP2016106030A (en) * | 2013-03-07 | 2016-06-16 | 国立大学法人東京工業大学 | Heating method of composite body, heating apparatus for composite body, and catalyst unit |
JPWO2014136456A1 (en) * | 2013-03-07 | 2017-02-09 | 国立大学法人東京工業大学 | Composite heating method and heating apparatus |
KR101707043B1 (en) * | 2016-06-24 | 2017-02-16 | 이정식 | Soft-boiled roaster using perforated drum |
WO2020084934A1 (en) * | 2018-10-26 | 2020-04-30 | 富士電機株式会社 | Electric dust collector |
JPWO2020084934A1 (en) * | 2018-10-26 | 2021-02-15 | 富士電機株式会社 | Electrostatic precipitator |
Also Published As
Publication number | Publication date |
---|---|
JP2643467B2 (en) | 1997-08-20 |
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