Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP2932456B2 - Heating element - Google Patents
[go: Go Back, main page]

JP2932456B2 - Heating element - Google Patents

Heating element

Info

Publication number
JP2932456B2
JP2932456B2 JP6207945A JP20794594A JP2932456B2 JP 2932456 B2 JP2932456 B2 JP 2932456B2 JP 6207945 A JP6207945 A JP 6207945A JP 20794594 A JP20794594 A JP 20794594A JP 2932456 B2 JP2932456 B2 JP 2932456B2
Authority
JP
Japan
Prior art keywords
heating element
zeolite
casing
copper
deodorizing
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 - Fee Related
Application number
JP6207945A
Other languages
Japanese (ja)
Other versions
JPH0847645A (en
Inventor
明 北田
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.)
GO SHOJI KK
NIPPON KAGAKU KOGYO KK
Original Assignee
GO SHOJI KK
NIPPON KAGAKU KOGYO KK
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 GO SHOJI KK, NIPPON KAGAKU KOGYO KK filed Critical GO SHOJI KK
Priority to JP6207945A priority Critical patent/JP2932456B2/en
Priority to TW084100033A priority patent/TW286294B/zh
Priority to KR1019950001293A priority patent/KR950031209A/en
Priority to CN95115203.3A priority patent/CN1135936A/en
Publication of JPH0847645A publication Critical patent/JPH0847645A/en
Application granted granted Critical
Publication of JP2932456B2 publication Critical patent/JP2932456B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)
  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Resistance Heating (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、優れた持続性を保有す
る発熱体、更に詳しくは、主として暖房器具、給湯機
器、乾燥器、調理器、冷蔵庫、炬燵、空調機器などの民
生用電化製品の発熱体として使用することができ、使用
に際して、人体に不快な悪臭成分ガスを効果的に吸着
し、かつその脱臭能を安定して持続することのできる発
熱体に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating element having excellent durability, and more particularly, to a consumer appliance such as a heater, a hot water supply, a dryer, a cooker, a refrigerator, a kotatsu, and an air conditioner. The present invention relates to a heat generating element which can be used as a heat generating element, can effectively adsorb a malodorous component gas which is unpleasant to the human body at the time of use, and can stably maintain its deodorizing ability.

【0002】[0002]

【従来の技術】脱臭剤として従来から汎用されている活
性炭は、物理吸着である関係で吸着能が劣化した場合に
は新たなものと交換する必要がある。このため、有効性
や交換などの管理が煩雑であるうえ、長期的な使用コス
トが高くなる欠点がある。これに代わる化学的な脱臭手
段として、近時、オゾンガスを用いて悪臭ガスを酸化分
解する方法が実用化されているが、この脱臭操作にはオ
ゾン発生機が必要であり、またオゾン自体に不快具があ
るため余剰のガス処理に問題がある。このほか、過マン
ガン酸カリ系、沃素酸カリ系あるいは次亜塩素酸塩系な
どの酸化剤からなる脱臭剤、逆に還元剤を用いた脱臭剤
等も知られているが、高度の安全性が求められる民生用
脱臭剤としては使用範囲が極めて限定される。
2. Description of the Related Art Activated carbon, which has been widely used as a deodorant, needs to be replaced with a new one when its adsorption capacity is deteriorated due to physical adsorption. For this reason, there are drawbacks that management of effectiveness and replacement is complicated, and that long-term use costs are increased. As an alternative to chemical deodorization, a method of oxidizing and decomposing malodorous gas using ozone gas has recently been put to practical use. However, this deodorizing operation requires an ozone generator, and the ozone itself is unpleasant. There is a problem with excess gas treatment due to the presence of tools. In addition, deodorizers composed of oxidizing agents such as potassium permanganate, potassium iodate or hypochlorite, and conversely, deodorants using reducing agents, etc. are also known. The range of use as a consumer deodorant which is required is extremely limited.

【0003】このような背景から、安全性に優れ再生使
用が可能な酸化分解触媒の開発が盛んに進められてい
る。この種の酸化分解を利用する触媒系脱臭剤として
は、例えばゼオライトを主剤とするもの(特開平5−9
8185号公報)、ゼオライトと貴金属担持酸化物を主
剤とするもの(特開平5−96176号公報)、ゼオラ
イトと珪酸マグネシウム、あるいはこれらの1種以上と
白金族金属塩を主剤とするもの(特開平5−98194
号公報、特開平5−98185号公報)、ゼオライトと
銅またはマンガンの酸化物を主剤とするもの(特開平1
−151938号公報)、銀やマンガンあるいはその化
合物を多孔質単体に担持したもの(特開平4−1147
44号公報)、銀とマンガンの複合酸化物を主剤とする
もの(特開平4−200638号公報)等が提案されて
おり、また、特開平5−96178号公報においては、
ゼオライトと貴金属担持酸化物を主剤とする触媒系脱臭
剤を発熱体のケーシングの表面に形成することが開示さ
れている。
[0003] Against this background, the development of oxidative decomposition catalysts that are safe and can be reused has been actively pursued. As a catalytic deodorant utilizing this kind of oxidative decomposition, for example, a catalyst mainly composed of zeolite (JP-A-5-9-9)
No. 8185), one containing zeolite and a noble metal-supported oxide as main agents (Japanese Patent Application Laid-Open No. 5-96176), one containing zeolite and magnesium silicate, or one or more of these and a platinum group metal salt (Japanese Patent Application Laid-Open No. 5-98194
Japanese Patent Application Laid-Open No. 5-98185), one containing a zeolite and an oxide of copper or manganese as main components (Japanese Patent Application Laid-Open No. HEI 5-98185).
JP-A-151938), those in which silver or manganese or a compound thereof is supported on a porous body (Japanese Patent Laid-Open No. 4-1147)
No. 44), and those using a composite oxide of silver and manganese as a main agent (Japanese Patent Application Laid-Open No. 4-200638) have been proposed. In Japanese Patent Application Laid-Open No. 5-96178,
It is disclosed that a catalytic deodorant mainly composed of zeolite and a noble metal-supported oxide is formed on the surface of a casing of a heating element.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、従来技
術による酸化分解触媒系の脱臭剤には、全般的な脱臭能
が十分でない、例えばメチルメルカプタン等の硫黄系悪
臭ガスのような特定ガスに対する脱臭能が劣る、酸化分
解が不十分で長期間の脱臭能が持続されない、あるいは
再生化が容易でない、等のいずれかの問題を抱えてお
り、改良すべき課題が残されている。又、銀、白金など
の貴金属を主剤とするものは、原材料費が高く、高価な
ものとなってしまう。
However, the deodorizing agents of the oxidative decomposition catalyst system according to the prior art do not have a sufficient deodorizing ability, for example, a deodorizing ability for a specific gas such as a sulfur-based malodorous gas such as methyl mercaptan. Poor reproducibility, insufficient oxidative decomposition to maintain the deodorizing ability for a long period of time, or difficulty in regenerating, and other problems remain to be improved. In addition, a material containing a noble metal such as silver or platinum as a main component has a high raw material cost and is expensive.

【0005】本発明は、上記の事実を艦みて開発された
もので、その目的とするところは、不快な悪臭ガスを効
率よく吸着し、酸化分解性に優れ、かつ長期に亘り安定
した高脱臭能を持続することができる発熱体を安価に提
供することにある。
The present invention has been developed in view of the above-mentioned facts, and it is an object of the present invention to efficiently adsorb unpleasant odorous gas, to have excellent oxidative decomposition properties, and to stably maintain high deodorization for a long period of time. An object of the present invention is to provide an inexpensive heating element capable of maintaining its function.

【0006】[0006]

【課題を解決するための手段】上記の目的を達成するた
め、本発明は、ケーシングと、このケーシング内に配位
された電気抵抗部材等の発熱部材とを備え、このケーシ
ングの表面に活性二酸化マンガン、銅イオン担持ゼオラ
イトおよび銅酸化物を有効成分とした酸化分解性脱臭触
媒を付与したことを特徴とする発熱体を提供する。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention comprises a casing and a heating member such as an electric resistance member arranged in the casing. Provided is a heating element characterized by having provided an oxidatively decomposable deodorizing catalyst containing manganese, copper ion-supporting zeolite and copper oxide as effective components.

【0007】本発明において、ケーシングには、石英や
ガラス体から構成された管状や球状のものを採用するこ
とができる。発熱部材としては、電気抵抗部材等の通電
によって発熱し得る部材を適宜選択して用いることがで
きる。具体例を上げると、この発熱部材1は、通常、図
1に示すように、碍子又は耐熱ゴム製の保持端部2によ
って支持された状態で、ケーシング3内に配位される。
そして、このケーシング3の外周面に、酸化分解性脱臭
触媒層4が付与される。この付与の方法は自由である
が、酸化分解性脱臭触媒を塗料形態にして実施すること
により、ケーシング3の外周面に塗装するだけで、容易
に且つ能率的に配位することができる。塗装の方法は自
由であり、浸漬塗装、スプレー塗装、静電塗装、ナイフ
やロールコータ法、スクリーン印刷等、適宜方法を採用
し得る。尚、ケーシング3に対する酸化分解性脱臭触媒
層4の付着性を向上させるために、ケーシング表面に小
さな凹凸を形成したり、或いは、ケーシングを構成する
石英やガラス体の表面を脱脂しておいてもよい。
In the present invention, a tubular or spherical casing made of quartz or glass can be used as the casing. As the heat generating member, a member such as an electric resistance member that can generate heat when energized can be appropriately selected and used. More specifically, as shown in FIG. 1, the heat generating member 1 is generally arranged in a casing 3 while being supported by a holding end 2 made of an insulator or heat-resistant rubber.
Then, an oxidatively decomposable deodorizing catalyst layer 4 is provided on the outer peripheral surface of the casing 3. The method of giving the coating is free. However, by using the oxidatively decomposable deodorizing catalyst in the form of a coating, the coating can be easily and efficiently coordinated only by coating the outer peripheral surface of the casing 3. The method of coating is free, and any appropriate method such as dip coating, spray coating, electrostatic coating, knife or roll coater method, screen printing, etc. can be adopted. In order to improve the adhesion of the oxidatively decomposable deodorizing catalyst layer 4 to the casing 3, it is possible to form small irregularities on the casing surface, or to degrease the surface of the quartz or glass body constituting the casing. Good.

【0008】本発明において、活性二酸化マンガンと
は、マンガン塩を少なくとも湿式酸化分解して得られる
比表面積が大きな多孔質の二酸化マンガンを指し、電池
用のような電解酸化で得られた比重の大きなものとは材
質が異なるものである。したがって、一般式MnOX
表したとき、多くの場合1.8<x<2.0の範囲にあ
って、必ずしもMnO2 とはならないことを理解すべき
である。かかる活性二酸化マンガンの組成性状として
は、窒素吸着比表面積(BET)が50m2 /g以上、
好ましくは200〜1000m2 /gのものが好適に使
用される。
In the present invention, active manganese dioxide refers to porous manganese dioxide having a large specific surface area obtained by at least wet oxidative decomposition of a manganese salt, and having a large specific gravity obtained by electrolytic oxidation such as for a battery. The material is different from the material. Therefore, it should be understood that, when represented by the general formula MnO X, it is often in the range of 1.8 <x <2.0, and is not necessarily MnO 2 . The composition of the activated manganese dioxide has a nitrogen adsorption specific surface area (BET) of 50 m 2 / g or more,
Preferably, those having a mass of 200 to 1000 m 2 / g are suitably used.

【0009】このような活性二酸化マンガンは、例えば
2価のマンガン塩を加水分解したのち酸化処理する方
法、2価マンガン塩と過マンガン酸塩との反応生成物、
銅塩と2価マンガン塩との混液を中和して金属水酸化物
と共沈させ、これを酸化処理する方法、該酸化処理に過
マンガン酸塩を用いて生成する方法などによって、得る
ことができる。また、本発明者の経験によると、活性二
酸化マンガンとして、銅イオンを担持した活性二酸化マ
ンガンを用いることが好ましいと思われる。
Such active manganese dioxide is obtained, for example, by subjecting a divalent manganese salt to hydrolysis and then an oxidation treatment, a reaction product of a divalent manganese salt and a permanganate,
A method of neutralizing a mixed solution of a copper salt and a divalent manganese salt, coprecipitating the mixed solution with a metal hydroxide, and oxidizing the metal hydroxide, a method of using a permanganate for the oxidation treatment, and the like. Can be. Further, according to the experience of the present inventors, it is preferable to use active manganese dioxide supporting copper ions as the active manganese dioxide.

【0010】銅イオン担持ゼオライトは、ゼオライトの
イオン交換能を利用して銅イオンをゼオライトカチオン
と置換担持させたものである。担体となるゼオライトと
しては、ゼオライトA、ゼオライトL、ゼオライトX、
ゼオライトY、ゼオライトP、クリノプチロライト、モ
ルデナイト、その他のハイシリカゼオライトなどを挙げ
ることができるが、性能およびコストの面からゼオライ
トAを用いることが好ましい。銅イオンは、通常Cu2+
であるが、錯イオンであっても差し支えない。銅イオン
の担持量は、特に限定的ではないが、ゼオライトのカチ
オン交換容量に対して少なくとも30%以上であること
が望ましい。
The copper ion-carrying zeolite is obtained by substituting and supporting copper ions with zeolite cations by utilizing the ion exchange capacity of zeolite. Zeolite A, zeolite L, zeolite X,
Examples include zeolite Y, zeolite P, clinoptilolite, mordenite, and other high silica zeolites, but zeolite A is preferably used in view of performance and cost. Copper ions are usually Cu 2+
However, it may be a complex ion. The amount of copper ions carried is not particularly limited, but is preferably at least 30% or more based on the cation exchange capacity of the zeolite.

【0011】銅酸化物としては、酸化銅、亜酸化銅、水
酸化銅、塩基性酸化銅などが挙げられる。このうちで
は、酸化銅が好ましく用いられる。
Examples of the copper oxide include copper oxide, cuprous oxide, copper hydroxide, and basic copper oxide. Among them, copper oxide is preferably used.

【0012】上記成分の組成比はそれぞれの物性ならび
に使用目的に応じて変化させることができるが、その範
囲は、活性二酸化マンガン:銅イオン担持ゼオライト:
銅酸化物の組成比が重量比率として1:0.5〜1:
0.05〜0.5の範囲内とする。
[0012] The composition ratio of the components can be varied depending on the respective physical properties and the intended use, but its range
Boxes indicate activated manganese dioxide: zeolite supporting copper ions:
The composition ratio of the copper oxide is from 1: 0.5 to 1: as a weight ratio.
The range is 0.05 to 0.5.

【0013】本発明に係る酸化分解性脱臭触媒は、上記
の三成分を所定の組成比に配合し、乾式もしくは湿式系
で均一混合して調製される。ケーシング表面に付与する
形態は自由であるが、ケーシングへの付与の容易性や脱
落防止の観点からは、混合粉末のままよりも、これを所
望の形状に成形した成形体としてケーシングの外周に装
着するか、またはスラリー状の塗料として塗布すること
が望ましい。
The oxidatively decomposable deodorizing catalyst according to the present invention is prepared by mixing the above three components in a predetermined composition ratio and uniformly mixing them in a dry or wet system. The form of application to the casing surface is free, but from the viewpoint of ease of application to the casing and prevention of falling off, it is attached to the outer periphery of the casing as a molded body formed into a desired shape, rather than as a mixed powder. Or as a slurry-like coating.

【0014】上記のように使用形態を成形体あるいは塗
料とする場合には、有効成分となる活性二酸化マンガ
ン、銅イオン担持ゼオライトおよび銅酸化物の三成分系
に、必要に応じて、例えば樹脂、シリカゾルなどの有機
質または無機質バインダー、塗料ビヒクル等を適宜に添
加して調製される。
When the form of use is a molded article or paint as described above, the active ingredient manganese dioxide, zeolite carrying copper ions and copper oxide may be added, if necessary, to a three-component system such as resin, It is prepared by appropriately adding an organic or inorganic binder such as silica sol, a paint vehicle and the like.

【0015】[0015]

【作用】本発明の発熱体に用いられる酸化分解性脱臭触
媒は、微量な複合汚染悪臭ガスに対して極めて効率的な
脱臭効果を示す。この脱臭機構の詳細については未だ解
明するに至っていないが、触媒を構成する三成分系が相
互に機能して脱臭効率を高める作用に基づくものと推測
され、特に活性二酸化マンガンおよび銅イオン担持ゼオ
ライトは相乗してメチルメルカプタン等の硫黄系悪臭ガ
スの除去に優れた脱臭機能を発揮する。
The oxidatively decomposable deodorizing catalyst used in the heating element of the present invention exhibits an extremely efficient deodorizing effect on a small amount of complex polluting malodorous gas. Although the details of the deodorizing mechanism have not been elucidated yet, it is presumed that the three-component system constituting the catalyst is based on an action of increasing the deodorizing efficiency by mutually acting.In particular, active manganese dioxide and copper ion-supported zeolite are Synergistically exerts an excellent deodorizing function for removing sulfur-based malodorous gases such as methyl mercaptan.

【0016】また、本発明では、発熱部材を内蔵したケ
ーシングの表面に酸化分解性脱臭触媒を付与したため、
発熱部材を発熱させることにより、ケーシングを介して
酸化分解性脱臭触媒を加熱することができる。そして、
触媒体に吸着された悪臭ガスは、上記の加熱下にて、酸
化能力の高い活性二酸化マンガンにより容易に分解反応
が促進され、脱臭能を容易に回復再生することができ
る。例えば、トリメチルアミンなどの窒素系悪臭ガスに
対しては、NO2 まで酸化されて、効果的に脱臭能が再
生される。
In the present invention, the oxidative decomposable deodorizing catalyst is provided on the surface of the casing containing the heat generating member.
By causing the heat generating member to generate heat, the oxidatively decomposable deodorizing catalyst can be heated via the casing. And
Under the above-mentioned heating, the malodorous gas adsorbed by the catalyst is easily decomposed by active manganese dioxide having high oxidizing ability, and the deodorizing ability can be easily recovered and regenerated. For example, for nitrogen-based malodorous gases such as trimethylamine, it is oxidized to NO 2, effectively deodorizing ability is played.

【0017】本発明の発熱体は、従来の各種の発熱体に
替えて用いることができ、特に、ストーブや炬燵等の暖
房器具用の発熱体、給湯機器の加熱用発熱体、乾燥器の
加熱用発熱体、調理器のグリル用発熱体、冷蔵庫の霜取
り用発熱体、空調機器の加熱殺菌用用発熱体などの各種
民生用電化製品に装着される発熱体として使用すること
ができる。
The heating element of the present invention can be used in place of conventional various heating elements, and in particular, a heating element for a heating appliance such as a stove or a kotatsu, a heating element for heating a hot water supply device, and a heating device for a dryer. It can be used as a heating element mounted on various consumer electric appliances such as a heating element for cooking, a heating element for grill of a cooker, a heating element for defrosting a refrigerator, and a heating element for heat sterilization of an air conditioner.

【0018】[0018]

【実施例】以下、本発明の具体的な実施例を比較例と対
比して説明する。 実施例1 (1) 酸化分解性脱臭触媒塗料の調製 CuOを25重量%含有する窒素吸着比表面積(BE
T)290m2 /gの活性二酸化マンガン60重量部
に、銅イオン担持ゼオライトA(CuOとして11.0
重量%担持、平均粒径2.35μm)50重量部および
酸化銅10重量部を配合し、水100重量部を加えて十
分に湿式混合した。ついで、シリカゾル(SiO:30
重量%)50重量部と共にボールミルに入れ、均一とな
るまで混合操作を行って酸化分解性脱臭触媒の塗料を調
製した。この塗料を、全長326mm、外径10.5mmの
ガラス管内に、140Wの発熱用電気抵抗体を配位した
発熱体のガラス管表面の中央に、258mmの範囲に渡っ
てスプレー塗りで2回塗布し、ついで4000Cの温度で
1時間乾燥して酸化分解性脱臭触媒の被覆層を形成し
た。
EXAMPLES Hereinafter, specific examples of the present invention will be described in comparison with comparative examples. Example 1 (1) Preparation of oxidatively decomposable deodorizing catalyst paint Nitrogen adsorption specific surface area containing 25% by weight of CuO (BE)
T) Zeolite A supporting copper ions (11.0% as CuO) was added to 60 parts by weight of active manganese dioxide of 290 m 2 / g.
50 parts by weight (weight% supported, average particle size: 2.35 μm) and 10 parts by weight of copper oxide were blended, and 100 parts by weight of water was added, followed by wet mixing. Then, silica sol (SiO: 30
(% By weight) in a ball mill together with 50 parts by weight, and a mixing operation was performed until the mixture became uniform to prepare a coating material for an oxidatively decomposable deodorizing catalyst. This paint is applied twice by spray coating over a range of 258 mm to the center of the glass tube surface of a heating element in which a 140 W heating electric resistor is arranged in a glass tube having a total length of 326 mm and an outer diameter of 10.5 mm. and, then dried 1 hour at a temperature of 400 0 C to form a coating layer of oxidative degradation deodorizing catalyst.

【0019】(2) 脱臭能の評価 上記実施例の発熱体につき、下記の試験方法によりメチ
ルメルカプタンおよびトリメチルアミンの脱臭試験を行
い、脱臭能を評価した。その結果を表1に示した。 メチルメルカプタン脱臭試験方法:10リットルガス捕
集袋に実施例の発熱体を入れ、ガス捕集袋内のメチルメ
ルカプタン濃度を20ppmに調製した。その後、1時
間後のガス捕集袋内のメチルメルカプタン濃度をガステ
ック検知管で測定し、その残存率を求めた。酸化分解性
脱臭触媒で被覆しない発熱体を入れ、同様に測定しブラ
ンクとした。 トリメチルアミン脱臭試験方法:10リットルガス捕集
袋に実施例の発熱体を入れ、ガス捕集袋内のトリメチル
アミン濃度を20ppmに調製した。その後、1時間後
のガス捕集袋内のトリメチルアミン濃度をガステック検
知管で測定し、その残存率を求めた。また、酸化分解性
脱臭触媒で被覆しない発熱体を入れ、同様に測定し、ブ
ランクとした。
(2) Evaluation of Deodorizing Ability The heating elements of the above Examples were subjected to a deodorizing test of methyl mercaptan and trimethylamine by the following test method, and the deodorizing ability was evaluated. The results are shown in Table 1. Methyl mercaptan deodorization test method: The heating element of the example was placed in a 10-liter gas collecting bag, and the methyl mercaptan concentration in the gas collecting bag was adjusted to 20 ppm. Thereafter, the concentration of methyl mercaptan in the gas collecting bag after 1 hour was measured with a gas tech detector tube, and the residual ratio was determined. A heating element not covered with the oxidatively decomposable deodorizing catalyst was placed, and measured in the same manner as a blank. Trimethylamine deodorizing test method: The heating element of the example was placed in a 10-liter gas collecting bag, and the concentration of trimethylamine in the gas collecting bag was adjusted to 20 ppm. Thereafter, the concentration of trimethylamine in the gas collection bag after 1 hour was measured with a gas tech detector tube, and the residual ratio was determined. In addition, a heating element not covered with the oxidatively decomposable deodorizing catalyst was put therein, measured in the same manner, and used as a blank.

【0020】実施例2 活性二酸化マンガン(比表面積246m2 /g)70重
量部、銅イオン担持ゼオライトX(CuOとして11.
7重量%担持、平均粒径2.76μm)45重量部およ
び酸化銅5重量部の組成比とし、その他は実施例1と同
一条件により酸化分解性脱臭触媒の塗料を調製した。こ
の塗料を実施例1と同様の発熱体のガラス管の表面に同
様の塗布条件で付与し、脱臭能の評価を行い、結果を表
1に併載した。
Example 2 70 parts by weight of active manganese dioxide (specific surface area: 246 m 2 / g), zeolite X supporting copper ions (11.
A coating composition of an oxidatively decomposable deodorizing catalyst was prepared under the same conditions as in Example 1 except that the composition ratio was 45 parts by weight (7% by weight supported, average particle size 2.76 μm) and 5 parts by weight of copper oxide. This coating material was applied to the surface of the glass tube of the same heating element as in Example 1 under the same application conditions, the deodorizing ability was evaluated, and the results are shown in Table 1.

【0021】実施例3 CuOを21重量%含有する窒素吸着比表面積(BE
T)268m2 /gの活性二酸化マンガン65重量部
に、銅イオン担持ゼオライトA(CuOとして8.6重
量%担持、平均粒径2.56μm)50重量部および亜
酸化銅(平均粒径2.25μm)5重量部の組成比と
し、その他は実施例1と同一条件により酸化分解性脱臭
触媒の塗料を調製した。この塗料を実施例1と同様の発
熱体のガラス管の表面に同様の塗布条件で付与し、脱臭
能の評価を行い、結果を表1に併載した。
Example 3 Nitrogen adsorption specific surface area (BE) containing 21% by weight of CuO
T) 50 parts by weight of zeolite A supporting copper ions (8.6% by weight supported as CuO, average particle size 2.56 μm) and 65 parts by weight of activated manganese dioxide of 268 m 2 / g and cuprous oxide (average particle size of 2. A coating composition of an oxidative decomposable deodorizing catalyst was prepared under the same conditions as in Example 1 except that the composition ratio was 5 parts by weight. This coating material was applied to the surface of the glass tube of the same heating element as in Example 1 under the same application conditions, the deodorizing ability was evaluated, and the results are shown in Table 1.

【0022】比較例1 実施例1で使用した銅イオン担持ゼオライトA100重
量部を水20重量部を加えて湿式混合し、ついでシリカ
ゾル(SiO2 :30重量%)30重量部を加えてボー
ルミルで十分均一に混合処理して塗料を調製した。この
塗料を実施例1と同様の発熱体のガラス管の表面に同様
の塗布条件で付与し、脱臭能の評価を行い、結果を表1
に併載した。
Comparative Example 1 100 parts by weight of the zeolite A carrying copper ions used in Example 1 was added to 20 parts by weight of water and wet-mixed, and then 30 parts by weight of silica sol (SiO 2 : 30% by weight) was added, followed by a ball mill. A paint was prepared by uniformly mixing. This paint was applied to the surface of the glass tube of the same heating element as in Example 1 under the same application conditions, and the deodorizing ability was evaluated.
It was also attached to.

【0023】比較例2 活性二酸化マンガン(比表面積228m2 /g)70重
量部、ゼオライトAを50重量部に水90重量部を加え
て比較例1と同様にして塗料を調製した。この塗料を実
施例1と同様の発熱体のガラス管の表面に同様の塗布条
件で付与し、脱臭能の評価を行い、結果を表1に併載し
た。
Comparative Example 2 A coating material was prepared in the same manner as in Comparative Example 1 by adding 70 parts by weight of active manganese dioxide (specific surface area: 228 m 2 / g), 50 parts by weight of zeolite A and 90 parts by weight of water. This coating material was applied to the surface of the glass tube of the same heating element as in Example 1 under the same application conditions, the deodorizing ability was evaluated, and the results are shown in Table 1.

【0024】比較例3 酸化銅5重量部、ゼオライトAを100重量部に水40
重量部を加え、比較例1と同様に処理して塗料を調製し
た。この塗料を実施例1と同様の発熱体のガラス管の表
面に同様の塗布条件で付与し、脱臭能の評価を行い、結
果を表1に併載した。
Comparative Example 3 5 parts by weight of copper oxide, 100 parts by weight of zeolite A and 40 parts of water
A part by weight was added and treated in the same manner as in Comparative Example 1 to prepare a paint. This coating material was applied to the surface of the glass tube of the same heating element as in Example 1 under the same application conditions, the deodorizing ability was evaluated, and the results are shown in Table 1.

【0025】比較例4 活性二酸化マンガン(比表面積256m2 /g)60重
量部、酸化銅10重量部、ゼオライトAを50重量部に
水50重量部を加え、比較例1と同様に塗料を調製し
た。この塗料を実施例1と同様の発熱体のガラス管の表
面に同様の塗布条件で付与し、脱臭能の評価を行い、結
果を表1に併載した。
Comparative Example 4 A coating material was prepared in the same manner as in Comparative Example 1 by adding 60 parts by weight of activated manganese dioxide (specific surface area: 256 m 2 / g), 10 parts by weight of copper oxide, 50 parts by weight of zeolite A and 50 parts by weight of water. did. This coating material was applied to the surface of the glass tube of the same heating element as in Example 1 under the same application conditions, the deodorizing ability was evaluated, and the results are shown in Table 1.

【0026】[0026]

【表1】 [Table 1]

【0027】表1の結果から、実施例による発熱体は比
較例に比べて優れた脱臭効果を示すことが認められた。
From the results shown in Table 1, it was confirmed that the heating elements according to the examples exhibited a superior deodorizing effect as compared with the comparative examples.

【0028】実施例4〜11 実施例1と同一の活性二酸化マンガン、銅イオン担持ゼ
オライトAおよび酸化銅を、表2に示す重量部割合で配
合し、実施例1と同様にして酸化分解性脱臭触媒の塗料
を調製した。
Examples 4 to 11 The same active manganese dioxide, copper ion-supporting zeolite A and copper oxide as in Example 1 were blended in the proportions by weight shown in Table 2, and oxidatively decomposed and deodorized in the same manner as in Example 1. A paint for the catalyst was prepared.

【0029】[0029]

【表2】 [Table 2]

【0030】調製した各塗料を実施例1と同様の発熱体
のガラス管の表面に同様の塗布条件で付与し、この発熱
体につき下記の方法によりメチルメルカプタンおよびト
リメチルアミンの脱臭試験を行った。その結果を表3に
示した。 メチルメルカプタン脱臭試験方法:500×500×5
00mmのアクリル板内の中央に実施例の発熱体を設置
し、密閉されたアクリル板内のメチルメルカプタン濃度
を20ppmに調製した。そして2時間常温にて吸着さ
せた。その時の濃度をガステック検知管にて測定し、そ
の残存率を求めた。 トリメチルアミン脱臭試験方法:実施例の発熱体に温度
コントローラを装着して、500×500×500mm
のアクリル板内の中央に設置し、外部の電源と結線し、
密閉されたアクリル板内のトリメチルアミン濃度を20
ppmに調製し、2時間常温にて吸着させ、その時のト
リメチルアミンの濃度をガステック検知管で測定し、そ
の残存率を求めた。ついで、電気ヒーターに通電して、
発熱体の温度を3000Cまで上昇させ、吸着したアミン
を1時間酸化分解させ、その時の一酸化窒素、二酸化窒
素の濃度をガステック検知管で測定し、一酸化窒素と二
酸化窒素の割合を調べた。
Each of the prepared paints was applied to the surface of a glass tube of the same heating element as in Example 1 under the same application conditions, and the heating element was subjected to a deodorizing test of methyl mercaptan and trimethylamine by the following method. Table 3 shows the results. Methyl mercaptan deodorization test method: 500 × 500 × 5
The heating element of the example was installed in the center of a 00 mm acrylic plate, and the methyl mercaptan concentration in the sealed acrylic plate was adjusted to 20 ppm. Then, adsorption was performed at room temperature for 2 hours. The concentration at that time was measured with a gas tech detector tube, and the residual ratio was determined. Trimethylamine deodorization test method: A temperature controller was attached to the heating element of the example, and 500 × 500 × 500 mm
Installed in the center of the acrylic plate, connected to an external power supply,
Trimethylamine concentration in the sealed acrylic plate was 20
ppm, and adsorbed at room temperature for 2 hours. At that time, the concentration of trimethylamine was measured with a gas tech detector tube, and the residual ratio was determined. Then turn on the electric heater,
The temperature of the heating element is increased to 300 0 C, the adsorbed amine is 1 hour oxidative decomposition, nitrogen monoxide at that time, the concentration of nitrogen dioxide was measured with Gastec detector tube, the proportion of nitrogen monoxide and nitrogen dioxide Examined.

【0031】[0031]

【表3】 [Table 3]

【0032】表3の結果から、本発明による酸化分解性
脱臭触媒は優れた脱臭効果ならびに酸化分解による再生
化が可能であることが認められたが、実施例4および実
施例11は成分組成が適性範囲(活性二酸化マンガン:
銅イオン担持ゼオライト:銅酸化物=1:0.5〜1:
0.05〜0.5)を外れるため、前者ではメチルメル
カプタン残存率が、また後者ではトリメチルアミン残存
率が多くなる傾向を示した。
From the results shown in Table 3, it was confirmed that the oxidatively decomposable deodorizing catalyst according to the present invention has an excellent deodorizing effect and can be regenerated by oxidative decomposition. Suitable range (active manganese dioxide:
Copper ion-supported zeolite: copper oxide = 1: 0.5 to 1:
0.05-0.5), the former tended to increase the residual ratio of methyl mercaptan, and the latter tended to increase the residual ratio of trimethylamine.

【0033】実施例12 実施例1で調製した酸化分解性脱臭触媒の塗料を、前述
と同一の条件で塗布した発熱体を、10リットルガス捕
集袋に入れ、ガス捕集袋内のメチルメルカプタン濃度を
20ppmに調製した。その後、1時間を経過した後の
ガス捕集袋内のメチルメルカプタン濃度をガステック検
知管で測定した。ついで、発熱体を取り出し、電気ヒー
ターに通電して、発熱体の温度を3000Cまで上昇させ
た状態で30分間通電を続け、次に通電を停止して大気
中で30分放冷した。再び発熱体を10リットルガス捕
集袋に入れ、ガス捕集袋内のトリメチルアミン濃度を2
0ppmに調製し、1時間後、ガス捕集袋内のトリメチ
ルアミン濃度をガステック検知管で測定してその残存率
を求めた。ついで、上記と同一の条件で通電と放熱を行
った。この実験を20回繰り返し、このようにして処理
した結果を表4に示した。
Example 12 A heating element obtained by applying the coating material of the oxidatively decomposable deodorizing catalyst prepared in Example 1 under the same conditions as described above was placed in a 10-liter gas collection bag, and methyl mercaptan in the gas collection bag was placed. The concentration was adjusted to 20 ppm. Thereafter, the concentration of methyl mercaptan in the gas collecting bag after 1 hour was measured with a gas tech detector tube. Then, the heating element is taken out, by energizing the electric heater, continued energization 30 minutes with raising the temperature of the heating element to 300 0 C, and allowed to cool 30 minutes in the air and then stops energizing. The heating element was placed again in the 10-liter gas collection bag, and the concentration of trimethylamine in the gas collection bag was adjusted to 2%.
The concentration was adjusted to 0 ppm, and after one hour, the concentration of trimethylamine in the gas collecting bag was measured with a gas tech detector tube to determine the residual ratio. Next, energization and heat radiation were performed under the same conditions as described above. This experiment was repeated 20 times, and the results of such treatment are shown in Table 4.

【0034】表4の結果から、発熱体表面の酸化分解性
脱臭触媒は、これに吸着されたメチルメルカプタンガス
及びトリメチルアミンガスを、電気ヒーターによる発熱
により容易に酸化分解して無臭ガスに変化させて脱着す
るものであることが確認され、繰り返しの操作による脱
臭能の低下は認められなかった。したがって、吸着ガス
成分を酸化分解し、無臭ガスに変化して脱着することに
より長期間に渡り安定した脱臭能を維持出来ることが確
認された。
According to the results shown in Table 4, the oxidatively decomposable deodorizing catalyst on the surface of the heating element easily oxidizes and decomposes the methyl mercaptan gas and the trimethylamine gas adsorbed thereon by the heat generated by an electric heater to change to an odorless gas. It was confirmed that the substance was desorbed, and no reduction in deodorizing ability due to repeated operations was observed. Therefore, it was confirmed that stable deodorizing ability can be maintained for a long period of time by oxidatively decomposing the adsorbed gas component, changing to an odorless gas, and desorbing.

【0035】[0035]

【表4】 [Table 4]

【0036】実施例13 実施例1で調製した酸化分解性脱臭触媒の塗料を、前述
と同一の条件で塗布した発熱体を、清浄な30リットル
デシケータに入れ、30分間電気ヒーターに定格通電し
た後、デシケータ内で30分放冷した。その後、デシケ
ータ内にメチルメルカプタンを濃度100ppmとなる
ように注入し、30分経過後のデシケータ内のメチルメ
ルカプタン濃度をガスクロマトグラフで測定した(第1
回測定)。ついで、電気ヒーターに通電して、発熱体の
温度を2000Cまで上昇させた状態で10分間通電を続
けた後のデシケータ内のメチルメルカプタン濃度をガス
クロマトグラフで測定した(第2回測定)。その後、非
通電の状態の発熱体をデシケータに入れた状態を維持
し、30分間経過後のメチルメルカプタン濃度をガスク
ロマトグラフで測定した(第3回測定)。また、メチル
メルカプタンに代えて、ジメチルサルファイド濃度10
0ppmにより同様の試験を行った。メチルメルカプタ
ン及びジメチルサルファイドの測定結果と、残存率を表
5に示した。
Example 13 A heating element obtained by applying the coating material of the oxidatively decomposable deodorizing catalyst prepared in Example 1 under the same conditions as described above was placed in a clean 30-liter desiccator, and the electric heater was energized for 30 minutes. And allowed to cool in a desiccator for 30 minutes. Thereafter, methyl mercaptan was injected into the desiccator so as to have a concentration of 100 ppm, and after 30 minutes, the methyl mercaptan concentration in the desiccator was measured by gas chromatography (first example).
Times). Then, by energizing the electric heater, the methyl mercaptan concentration in the desiccator was continued energization 10 minutes with raising the temperature of the heating element up to 200 0 C as measured by gas chromatograph (2nd measurement). Thereafter, the state in which the non-energized heating element was placed in the desiccator was maintained, and the concentration of methyl mercaptan after 30 minutes was measured by gas chromatography (third measurement). Also, instead of methyl mercaptan, a dimethyl sulfide concentration of 10
A similar test was performed at 0 ppm. Table 5 shows the measurement results of methyl mercaptan and dimethyl sulfide and the residual ratio.

【0037】[0037]

【表5】 [Table 5]

【0038】表5の結果から、電気ヒーターによる発熱
により、メチルメルカプタン及びジメチルサルファイド
に対して優れた脱臭能が発揮出来ることが確認された。
From the results shown in Table 5, it was confirmed that the heat generated by the electric heater can exert an excellent deodorizing ability on methyl mercaptan and dimethyl sulfide.

【0039】[0039]

【発明の効果】以上のとおり、本発明によれば不快感を
与える悪臭ガスを効率よく吸着することができ、発熱部
材の発熱により、吸着したガス成分を容易に酸化分解し
て実質的に除去し、長期間安定した高脱臭能を持続する
発熱体を安価に提供することができる。したがって、こ
れを民生用電化製品の発熱体として用いることにより、
発熱作用を行いつつ、民生用電化製品の内部やその周辺
の脱臭を行うことが可能となったものである。
As described above, according to the present invention, the offensive odor gas which gives an unpleasant sensation can be efficiently adsorbed, and the adsorbed gas component is easily oxidized and decomposed and substantially removed by the heat generated by the heat generating member. In addition, it is possible to provide an inexpensive heating element that maintains stable high deodorizing ability for a long time. Therefore, by using this as a heating element for consumer electronics,
This makes it possible to deodorize the interior and surroundings of consumer electronics while generating heat.

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

【図1】本発明の一実施例に係る発熱体の構造説明図で
ある。
FIG. 1 is a structural explanatory view of a heating element according to one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 発熱部材 2 保持端部 3 ケーシング 4 酸化分解性脱臭触媒層 DESCRIPTION OF SYMBOLS 1 Heat generating member 2 Holding end 3 Casing 4 Oxidative decomposable deodorizing catalyst layer

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI H05B 3/44 B01D 53/36 H (58)調査した分野(Int.Cl.6,DB名) B01J 29/072 A61L 9/01 B01J 20/18 B01J 35/02 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 identification code FI H05B 3/44 B01D 53/36 H (58) Field surveyed (Int.Cl. 6 , DB name) B01J 29/072 A61L 9 / 01 B01J 20/18 B01J 35/02

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ケーシングと、このケーシング内に配位
された電気抵抗部材等の発熱部材とを備え、このケーシ
ングの表面に活性二酸化マンガン、銅イオン担持ゼオラ
イトおよび銅酸化物を有効成分とした酸化分解性脱臭触
媒が付与され、上記活性二酸化マンガンは、窒素吸着比
表面積(BET)が50m2 /g以上の多孔質の二酸化
マンガンであると共に、一般式MnOX で表したとき、
1.8<x<2.0の範囲にあり、 この活性二酸化マンガンと銅イオン担持ゼオライトと銅
酸化物との組成比が、重量比率として1:0.5〜1:
0.05〜0.5の範囲にあることを特徴とする発熱
体。
1. A casing comprising: a casing; and a heat generating member such as an electric resistance member disposed in the casing. The casing has an active manganese dioxide, a copper ion-supporting zeolite, and an oxide containing copper oxide as active components. A decomposable deodorizing catalyst is provided, and the activated manganese dioxide has a nitrogen adsorption ratio.
Porous dioxide with a surface area (BET) of 50 m2 / g or more
When it is manganese and represented by the general formula MnOX,
1.8 <x <2.0, and the activated manganese dioxide, zeolite supporting copper ions and copper
The composition ratio with the oxide is 1: 0.5 to 1: as a weight ratio.
Heat generation characterized by being in the range of 0.05 to 0.5
body.
【請求項2】 活性二酸化マンガンが銅イオン担持活性
二酸化マンガン、銅イオン担持ゼオライトが銅イオン担
持ゼオライトA、銅酸化物が酸化銅である請求項に記
載の発熱体。
2. The heating element according to claim 1 , wherein the active manganese dioxide is copper ion-loaded active manganese dioxide, the copper ion-loaded zeolite is copper ion-loaded zeolite A, and the copper oxide is copper oxide.
【請求項3】 酸化分解性脱臭触媒が、少なくとも無機
質バインダーを配合した塗料形態をなし、この塗料形態
の酸化分解性脱臭触媒をケーシングの表面に塗布したこ
とを特徴とする請求項1又は2に記載の発熱体。
Wherein oxidative decomposition deodorizing catalyst, without the paint forms formulated with at least inorganic binder, the oxidative decomposition of deodorizing catalysts of this paint form to claim 1 or 2, characterized in that applied to the surface of the casing Heating element as described.
JP6207945A 1994-04-18 1994-08-08 Heating element Expired - Fee Related JP2932456B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP6207945A JP2932456B2 (en) 1994-08-08 1994-08-08 Heating element
TW084100033A TW286294B (en) 1994-04-18 1995-01-05
KR1019950001293A KR950031209A (en) 1994-04-18 1995-01-25 Oxidative deodorizing catalyst and heating element using the same
CN95115203.3A CN1135936A (en) 1994-08-08 1995-08-07 Oxidative decomposing deodorizing catalyst and heating element using same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6207945A JP2932456B2 (en) 1994-08-08 1994-08-08 Heating element

Publications (2)

Publication Number Publication Date
JPH0847645A JPH0847645A (en) 1996-02-20
JP2932456B2 true JP2932456B2 (en) 1999-08-09

Family

ID=16548145

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6207945A Expired - Fee Related JP2932456B2 (en) 1994-04-18 1994-08-08 Heating element

Country Status (2)

Country Link
JP (1) JP2932456B2 (en)
CN (1) CN1135936A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6267941B1 (en) 1997-01-08 2001-07-31 Nec Corporation Catalyst system for deodorization of a mixture of sulfur compounds and compounds such as aldehydes, alcohols and/or hydrocarbons
CN101219232B (en) * 2007-01-12 2010-07-14 中山市洁鼎过滤制品有限公司 A kind of manufacturing method of multifunctional deozone honeycomb net
CN100569334C (en) * 2007-01-12 2009-12-16 中山市洁鼎过滤制品有限公司 A kind of manufacturing method of ceramic net for removing fishy smell
KR101538000B1 (en) * 2014-12-19 2015-07-20 주식회사 퓨어스피어 The method of oxidizing hazardous compounds by the mixture containing manganese
CN105233614A (en) * 2015-11-13 2016-01-13 无锡桥阳机械制造有限公司 Air filter
CN108286723A (en) * 2018-01-31 2018-07-17 吴冬新 A kind of smoke exhaust ventilator free of cleaning
CN118950025B (en) * 2024-07-01 2025-08-12 佛山市乐华恒业厨卫有限公司 Adsorption catalytic material, deodorizing device, deodorizing method and intelligent toilet

Also Published As

Publication number Publication date
JPH0847645A (en) 1996-02-20
CN1135936A (en) 1996-11-20

Similar Documents

Publication Publication Date Title
KR960007587B1 (en) Catalytic bodies and the process for producing the same
JP2932456B2 (en) Heating element
JPH0956799A (en) Self-regenerative adsorbent
JPH10137591A (en) Oxidative decomposable deodorizing catalyst
JPH08173512A (en) Deodorizing element
JP3485350B2 (en) Oxidative decomposable deodorizing catalyst
JPH0598185A (en) Coating material
JPH0924272A (en) Self-regeneration type adsorbent
JPH08308917A (en) Deodorizing device
TW443073B (en) Adsorption, decomposition and deodorization element
JP3618186B2 (en) Manufacturing method of improved deodorant
JPH05146683A (en) Catalyst body and method for producing the same
JP3521091B2 (en) Deodorant
JPH08168649A (en) Deodorizing device
JP3283593B2 (en) Method for producing catalyst body
JP2678079B2 (en) refrigerator
JP2722891B2 (en) Catalyst for deodorization
JPH04281177A (en) refrigerator
JPH0811787B2 (en) Paint
JPH0838584A (en) Deodorizing device
JP2532722B2 (en) Decompressor
JPH0657172A (en) Paint
JPH10155882A (en) Deodorant
JP2001070417A (en) Deodorizing device
JPH09313931A (en) Deodorant

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees