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JPS6017981B2 - Refrigerator with air purifier - Google Patents
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JPS6017981B2 - Refrigerator with air purifier - Google Patents

Refrigerator with air purifier

Info

Publication number
JPS6017981B2
JPS6017981B2 JP54013150A JP1315079A JPS6017981B2 JP S6017981 B2 JPS6017981 B2 JP S6017981B2 JP 54013150 A JP54013150 A JP 54013150A JP 1315079 A JP1315079 A JP 1315079A JP S6017981 B2 JPS6017981 B2 JP S6017981B2
Authority
JP
Japan
Prior art keywords
filter
refrigerator
air
iii
activated carbon
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
Application number
JP54013150A
Other languages
Japanese (ja)
Other versions
JPS55105175A (en
Inventor
邦弘 鶴田
正雄 牧
清一 佐野
郁夫 小林
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP54013150A priority Critical patent/JPS6017981B2/en
Publication of JPS55105175A publication Critical patent/JPS55105175A/en
Publication of JPS6017981B2 publication Critical patent/JPS6017981B2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Separation Of Gases By Adsorption (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Cold Air Circulating Systems And Constructional Details In Refrigerators (AREA)

Description

【発明の詳細な説明】 本発明は空気清浄機付冷蔵庫に関するもので、その目的
とするところは、空気中に存在し人体に対して有害であ
る二酸化窒素(N02)や一酸化炭素(CO)を除去す
る為に冷蔵庫の圧縮機からの放熱を利用して空気流路中
に設けた空気浄化用のフィルターを温め、空気清浄機能
を高め、一般家庭でも手軽に利用できる空気清浄機付冷
蔵庫を提供しようとするものである。
Detailed Description of the Invention The present invention relates to a refrigerator with an air purifier, and its purpose is to eliminate nitrogen dioxide (N02) and carbon monoxide (CO), which exist in the air and are harmful to the human body. In order to remove air pollution, the heat released from the refrigerator's compressor is used to heat the air purifying filter installed in the air flow path, increasing the air purifying function and creating a refrigerator with an air purifier that can be easily used in ordinary homes. This is what we are trying to provide.

N02やCOは自動車等の内燃機関や大型ボイラー、石
油ストーブなどの燃焼によって多量に発生し、これを多
量に吸うと肺や中枢神経に障害が現われ最終的に死に至
る危険性がある。
Large amounts of N02 and CO are generated by combustion in internal combustion engines such as automobiles, large boilers, oil stoves, etc., and if inhaled in large quantities, there is a risk of damage to the lungs and central nervous system and ultimately death.

従来、空気清浄機器として集塵装置を有する空気清浄機
やエアコン等の空調設備に集塵用のプレフィルタ−や活
性炭フィル夕−を取付けた機器が一般的であった。
BACKGROUND ART Conventionally, air purifying equipment has generally been an air purifier having a dust collector, or an air conditioner such as an air conditioner, with a dust collecting pre-filter or activated carbon filter attached thereto.

しかし、これらの機器は高価且つ大型であるので、なか
なか普及せず、もっと低価格の小型で手軽に持ち運びで
きるタイプの空気清浄機器の開発が望まれていた。また
空気清浄用フィルターとして、空気中の浮遊ゴミを横集
するプレフィルターだけでなく、有害ガス、例えばN0
2やCOを除去するフィルターも望まれていた。NQを
除去するフィルターとしては活性炭があるが、除去容量
が小さいので、すぐ寿命に達したり、高温でN02をN
Oへ還元したり、操作条件により吸着したN02を脱離
する等の問題点があった。一方に○を除去するフィルタ
ーとして、ホプカラィトなどの金属酸化物触媒やアルミ
ナなどの担体に貴金属を担持した貴金属触媒があるが、
金属酸化物触媒は低温でもCOを酸化して除去すること
ができるが、水分の存在で活性が低下する欠点があり、
又貴金属触媒は高温でしか活性を発揮しない等の欠点が
あった。本発明は上記のような従来の欠点を解消すると
共に、冷蔵庫の圧縮機からの放熱を利用し、空気流路と
その流路中に空気浄化フィルターを設置して空気清浄機
能をもたせ一般家庭でも空気清浄が手軽に出来るように
したもので、以下実施例に従って詳細に説明する。
However, since these devices are expensive and large, they have not been widely used, and there has been a desire to develop a smaller, more easily portable type of air purifying device at a lower price. In addition, as an air purifying filter, it is not only a pre-filter that collects floating dust in the air, but also a filter that collects harmful gases such as N0.
A filter that removes 2 and CO was also desired. Activated carbon is a filter that removes NQ, but its removal capacity is small, so it may reach the end of its life quickly, or it may not be able to remove N02 at high temperatures.
There were problems such as reduction to O and desorption of adsorbed N02 depending on operating conditions. On the other hand, as filters for removing ○, there are metal oxide catalysts such as hopcalite and noble metal catalysts in which precious metals are supported on supports such as alumina.
Metal oxide catalysts can oxidize and remove CO even at low temperatures, but they have the disadvantage that their activity decreases in the presence of moisture.
Furthermore, noble metal catalysts have the disadvantage that they only exhibit their activity at high temperatures. The present invention solves the above-mentioned conventional drawbacks, and also utilizes the heat radiation from the compressor of the refrigerator to install an air flow path and an air purification filter in the flow path to provide an air purification function. This device allows air purification to be carried out easily, and will be explained in detail below according to examples.

第1図は空気清浄機を有する冷蔵庫の空気清浄部を示し
た斜視図で「 1は冷蔵庫、2は放熱板、3は被断線、
4は空気吸込口、5は圧縮機、6は送風機、7は空気吹
出口を示す。
Figure 1 is a perspective view showing the air purifying part of a refrigerator equipped with an air purifier. 1 is a refrigerator, 2 is a heat sink, 3 is a broken wire,
4 is an air inlet, 5 is a compressor, 6 is a blower, and 7 is an air outlet.

空気吸込口4より流入した室内空気は圧縮機5からの放
熱で加溢され、送風機6によって吹出し口Tより室内へ
吹き出される。
Indoor air flowing in through the air suction port 4 is flooded with heat radiated from the compressor 5, and is blown into the room through the air outlet T by the blower 6.

吹出口7にはフィルターが装着され、空気中の有臭ガス
やN02・COなどの有害ガスが除去される。第2図は
吹出口の断面図を示し、8は空気流路、9は活性炭を用
いたフィルター、10‘まN02除去剤を用いたフィル
ター、11はCO酸化触媒を用いたフィルターを表わす
A filter is attached to the outlet 7 to remove odor gases and harmful gases such as N02 and CO from the air. FIG. 2 shows a cross-sectional view of the outlet, where 8 represents an air flow path, 9 represents a filter using activated carbon, 10' represents a filter using an N02 removing agent, and 11 represents a filter using a CO oxidation catalyst.

CO酸化触媒は、空気中の有害ガスやNO叫こより被毒
される懸念があるので活性炭やN02除去剤の後流に遣
して被蓑を防止した。
There is a concern that the CO oxidation catalyst may be poisoned by harmful gases in the air and NO emissions, so it was placed downstream of the activated carbon and N02 remover to prevent it from being poisoned.

尚、CO酸化触媒は高温になるほどその反応性が高くな
る性質を有するので、活性炭、N02除去剤及びCO酸
化触媒を用いたフィルター9,10,11のそれぞれに
圧縮機5からの放熱が有効に得られるように設置場所を
選ばなければならない。しかし10000以上では不安
定であるので100qo以下での使用が最通である。上
記したNQ除去剤はアルカリとセメント材と粉末活性炭
の混練成型物(0)であり、アルカリとしてはNaOH
、KOH、Ca(OH)2、Mg(CH)2、K2C0
3、Na2C03、Na2S2Q、Naぶ03が適当で
あり、又セメント材としてはペントナィト、ケイソウ士
、アルミナセメント、アルミナゾル、シリカゾル、粘土
、焼石管、ボルトランドセメント、カオリン、水ガラス
等が適当である。
Incidentally, since the CO oxidation catalyst has a property that its reactivity increases as the temperature increases, the heat dissipated from the compressor 5 can be effectively dissipated from the filters 9, 10, and 11 using activated carbon, the NO2 remover, and the CO oxidation catalyst. The installation location must be chosen so that it can be obtained. However, since it is unstable when it is more than 10,000, it is best to use it at less than 100 qo. The above-mentioned NQ remover is a kneaded molded product (0) of alkali, cement material, and powdered activated carbon, and the alkali is NaOH.
, KOH, Ca(OH)2, Mg(CH)2, K2C0
3, Na2C03, Na2S2Q, and Nabu03 are suitable, and as cement materials, pentonite, diatomite, alumina cement, alumina sol, silica sol, clay, baked stone pipe, Bortland cement, kaolin, water glass, etc. are suitable.

しかし、特にアルカリとして炭酸カリウムと水酸化カル
シウムを用い、セメント材として焼石管(CaS04・
1′240)を用いたものはN02を高性能を除去した
。粉末活性炭は混線成型物の表面積を大きくするととも
にアルカリとN02との反応を促進する役割を果たして
いると考えられる。混練成型物とN02とは下記の様に
反応して空気中のN02を除去すると考えられる。2N
02十K2C03→KN03十KN02十C02州02
十Xa(OH)2一Ca(N03)2十Ca(N02)
2十2LO尚、NOとは反応しない。
However, in particular, potassium carbonate and calcium hydroxide are used as alkalis, and baked stone pipes (CaS04,
1'240) removed the high performance of N02. Powdered activated carbon is thought to play a role in increasing the surface area of the hybrid wire molding and promoting the reaction between alkali and N02. It is thought that the kneaded molded product and N02 react as described below to remove N02 from the air. 2N
020K2C03→KN030KN020C02 State 02
10Xa (OH) 21Ca (N03) 20Ca (N02)
22nd LO does not respond to NO.

混練成型物はその組成を炭酸カリウム:水酸化カルシウ
ム:焼石骨(CaS0401/額20):粉末活性炭=
3:3:2:2(重量比)とし水とともに混練成型した
後乾燥したものを使用した。
The composition of the kneaded molded product is potassium carbonate: calcium hydroxide: baked stone bone (CaS0401/frame 20): powdered activated carbon =
The mixture was kneaded and molded with water at a ratio of 3:3:2:2 (weight ratio), and then dried.

CO酸化触媒はアルカリとセメント材と粉末活性炭を混
練成型した担体に白金、ロジウム、ルテニウムより選ん
だ一種以上とパラジウムを同時に、もしくはパラジウム
単独で担持した触媒(血)である。この触媒の担体は担
持物質を純粋に粒径細かく広範囲に均一状態で担持する
とともに、坦体の比表面積が大きく高強度になる様に手
順の最適化を計った。アルカリは貴金属を担持させる場
合に貴金属塩化物を溶解した含浸液のpHをアルカリへ
変化させ貴金属が担体に粒径細かく均一に分散した状態
で吸着される手助けをすると思われる。粉末活性炭は担
体の比表面積を大きくするなどの担体の紬孔物性に寄与
しているものと考えられる。セメント材は担体の強度を
大きくするとともにその耐熱性「耐摩耗性を向上させる
よう寄与していると考えられる。アルカリとして炭酸カ
リウム、水酸化カリウム、水酸化カルシウム、炭酸ナト
リウム等があげられるが使い易さと性能面より炭酸カリ
ウムが最適であった。セメント材はボルトランドセメン
ト、焼石葛、ベントナイト、アルミン酸石灰を主成分と
するアルミナセメント等があげられるが性能面よりアル
ミナセメントが最適であった。その理由はアルミナセメ
ントに含有する酸化第二鉄と酸化カルシウムの助触媒的
な効果の影響であると思われる。また結合剤としてアル
ミナが安定な担体を構成する役割を果していると推定さ
れる。担持物質として白金、ロジウム「ルテニウム、パ
ラジウム等の貴金属を使用した。比較的安価なパラジウ
ムは単独か、もしくは他の貴金属との組合わせで高活性
な触媒となり特に白金、パラジウムの組合わせは相乗効
果を発揮して著しい酸化活性を得られた。従って、CO
酸化触媒を用いたフィルター11には、炭酸カリウムと
アルミン酸石灰と粉末活性炭の混練成型物に白金とパラ
ジウムを同時に担持させたものを使用するのが望ましい
。この触媒の調整方法について示すと次の通りである。
The CO oxidation catalyst is a catalyst (blood) in which one or more selected from platinum, rhodium, and ruthenium and palladium are supported simultaneously or palladium alone on a carrier made by kneading and molding alkali, cement material, and powdered activated carbon. The procedure for this catalyst carrier was optimized so that the supported substance was supported uniformly over a wide range with a fine particle size, and the specific surface area of the carrier was large and the strength was high. When supporting noble metals, alkali is thought to change the pH of the impregnating solution in which noble metal chloride is dissolved to alkaline, thereby helping the noble metals to be adsorbed onto the carrier in a fine and uniformly dispersed state. It is thought that the powdered activated carbon contributes to the porous physical properties of the carrier, such as increasing the specific surface area of the carrier. Cement material increases the strength of the carrier and is thought to contribute to improving its heat resistance and wear resistance. Potassium carbonate, potassium hydroxide, calcium hydroxide, sodium carbonate, etc. are examples of alkalis, but they are not used. Potassium carbonate was the most suitable in terms of ease and performance.Cement materials include Bortland cement, calcined kudzu, bentonite, alumina cement whose main component is lime aluminate, etc., but alumina cement was the most suitable in terms of performance. The reason for this is thought to be the cocatalytic effect of ferric oxide and calcium oxide contained in alumina cement.Also, it is assumed that alumina plays a role in forming a stable support as a binder. .Precious metals such as platinum, rhodium, ruthenium, and palladium were used as supporting materials. Palladium, which is relatively inexpensive, becomes a highly active catalyst when used alone or in combination with other noble metals, and in particular, the combination of platinum and palladium has a synergistic effect. The effect was demonstrated and remarkable oxidation activity was obtained.Therefore, CO
For the filter 11 using an oxidation catalyst, it is preferable to use a kneaded molded product of potassium carbonate, lime aluminate, and powdered activated carbon that supports platinum and palladium at the same time. The method for preparing this catalyst is as follows.

アルカリとして炭酸カリウムを用い、セメント材として
アルミナセメンを用い、炭酸カリウムは100メッシュ
全通、粉末活性炭は300メッシュ全通の粒度のもの、
アルミナセメンはその組成がアルミナが45%以上、酸
化第二鉄が10%以下のものを使用した。坦体は重量比
で炭酸カリウム10部、粉末活性炭3碇部、アルミン酸
石灰6碇部‘こバインダーとしてカルボキシメチルセル
ロースナトリウム(CMC)0.5部を添加して水とと
もに混練成型した。混練物は充分に乾燥した後8〜20
メッシュに分級して担体とした。上記担体を充分に乾燥
した後パラジウムと白金を溶かした溶液に浸糟して吸着
をおこなわせた。パラジウムと白金は迫体に対して各0
.3×%吸着される様にその量を調整した。吸着された
担体は水素化ホウ素ナトリウムで還元した後充分に乾燥
して触媒とした。本発明は上記のように電気温風機の空
気通路中にフィルターを構成する活性炭やN02除去剤
又はCO酸化触媒層を設けたので、次のような効果が得
られた。
Potassium carbonate is used as the alkali, alumina cement is used as the cement material, potassium carbonate has a particle size of 100 mesh, and powdered activated carbon has a particle size of 300 mesh.
The alumina cement used had a composition of 45% or more alumina and 10% or less ferric oxide. The carrier was prepared by weight ratio of 10 parts of potassium carbonate, 3 parts of powdered activated carbon, 6 parts of lime aluminate, and 0.5 parts of sodium carboxymethyl cellulose (CMC) as a binder, and kneaded and molded with water. After the kneaded material is sufficiently dried, 8 to 20
It was classified into a mesh and used as a carrier. After thoroughly drying the above carrier, it was soaked in a solution containing palladium and platinum to effect adsorption. Palladium and platinum are each 0 for the mortar.
.. The amount was adjusted so that 3x% was adsorbed. The adsorbed carrier was reduced with sodium borohydride and thoroughly dried to obtain a catalyst. In the present invention, as described above, the activated carbon, N02 remover, or CO oxidation catalyst layer constituting the filter is provided in the air passage of the electric hot air fan, so that the following effects can be obtained.

第3図、第4図に示したのは、本発明を応用した空気清
浄機付冷蔵庫を運転した場合‘ィ}と空気清浄機なしの
場合‘o}について、換気回数1.幻副/hrを有する
6畳(室内容積29.3〆)の部屋で試験した時のN0
2濃度及びCO濃度を表わすものである。空気清浄機付
冷蔵庫は流量4.0〆′minをもちフィルターの構成
は前流より粒状活性炭のフィルター9、N02除去剤の
フィルター10、CO酸化触媒層のフィルター11より
成り、各層3側厚でフィルター面積20×1比ネであっ
た。フィルターは発熱部を発熱させた場合に80qo以
下になる様に設置した。測定は25℃、湿度62%の室
内空気にN02とCOを同時に注入して室内空気をN0
21.0脚、COlQ側の濃度に設定し、温風機を運転
してその濃度減衰を非分散型赤外方式CO分析計と化学
発光方式NO広分析計で測定した。その結果、第3図、
第4図のイに示すように本発明を用いた場合、高性能で
N02は急激に除去されおよそ3び分以内で0に近くな
ると共に、COについても30分以内に急速に減少して
いることが確認できた。上記のように本発明により家庭
内のガスコンロや石油ストーブ等で発生したN02やC
Oを効率的に浄化でき、有害ガスの少ない状態を現出す
ることができるようになった。
FIGS. 3 and 4 show the case of operating a refrigerator with an air purifier to which the present invention is applied, 'i}, and the case of no air purifier, 'o}, when the ventilation frequency is 1. N0 when tested in a 6 tatami room (interior volume 29.3〆) with phantom sub/hr
2 concentration and CO concentration. The refrigerator with air purifier has a flow rate of 4.0 min, and the filter structure consists of a granular activated carbon filter 9, an N02 remover filter 10, and a CO oxidation catalyst layer filter 11 from the front, and each layer has a thickness of 3 on the side. The filter area was 20×1 ratio. The filter was installed so that when the heat generating part generated heat, the amount of heat was 80 qo or less. Measurements were made by simultaneously injecting N02 and CO into indoor air at 25°C and 62% humidity.
21.0, the concentration was set on the COlQ side, the hot air fan was operated, and the concentration attenuation was measured using a non-dispersive infrared CO analyzer and a chemiluminescent NO wide analyzer. As a result, Figure 3,
As shown in Figure 4A, when the present invention is used, N02 is rapidly removed at high performance and becomes close to 0 within about 30 minutes, and CO also rapidly decreases within 30 minutes. This was confirmed. As mentioned above, the present invention can reduce the amount of N02 and C generated from gas stoves, oil stoves, etc. in the home.
It has become possible to efficiently purify O and create a state with less harmful gases.

従って、N02やCO濃度の高い都心部や高速道路料金
徴収所近辺でも、本発明の空気清浄機付冷蔵庫を使用す
ることによって、NQ・CO濃度の低い状態下で生活で
きることになり、特に本発明を利用した空気清浄機はC
O酸化触媒層の温度が圧縮機からの放熱を利用している
ので他の空気清浄機器へ応用した触媒層の温度よりも高
いので、COを高性能に除去できる。またCO酸化触媒
層を昇温させるのに要する発熱部(ヒータ−)も不用に
なり省エネルギーの面からもその効果が大いに期待でき
る。
Therefore, by using the refrigerator with air purifier of the present invention, even in urban areas or near expressway toll collection offices where N02 and CO concentrations are high, it is possible to live under conditions with low NQ and CO concentrations. Air purifier using C
Since the temperature of the O oxidation catalyst layer utilizes heat radiation from the compressor, it is higher than the temperature of the catalyst layer applied to other air cleaning devices, so CO can be removed with high performance. Moreover, the heat generating part (heater) required to raise the temperature of the CO oxidation catalyst layer is also unnecessary, and a great effect can be expected from the aspect of energy saving.

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

第1図は空気清浄機を有する冷蔵庫の要部破断斜視図、
第2図は空気通路の断面図、第3図は本発明と従来例と
の比較を示すN02濃度の変化図、第4図は同CG農度
の変化図1・・・・・・冷蔵庫、5・・・・・・圧縮機
、6・・・・・・送風機、8・・・…空気流路、9,1
0,11・・・・・・フィル夕−−。 第1図 第2図 第3図 第4図
Figure 1 is a cutaway perspective view of the main parts of a refrigerator with an air purifier.
Fig. 2 is a cross-sectional view of the air passage, Fig. 3 is a change in N02 concentration showing a comparison between the present invention and a conventional example, and Fig. 4 is a change in CG agricultural rate. 5...Compressor, 6...Blower, 8...Air flow path, 9,1
0,11...Fill evening--. Figure 1 Figure 2 Figure 3 Figure 4

Claims (1)

【特許請求の範囲】 1 冷蔵庫において、送風機により室内空気を吸込み吹
出すようにした空気流路中に冷蔵庫の圧縮機を設けると
共に下記の(I)、(II)より選んだ1種以上と(III)
を同時に、もしくは(III)のみから成るフイルターを
設け、このフイルターを圧縮機からの放熱により温める
ようにしたことを特徴とする空気清浄機付冷蔵庫。 (I)活性炭 (II)アルカリとセメント材と粉末活性炭の混練成型物
(III)アルカリとセメント材と粉末活性炭を混練成型
した担体に白金、ロジウム、ルテニウムより選んだ1種
以上とパラジウムを同時にもしくはパラジウム単独で担
持した触媒2 フイルターを構成する(II)において、
アルカリとして炭酸カリウムや水酸化カルシウムを用い
、セメント材として焼石膏(CaSO_4・1/2H_
2O)を用いた特許請求の範囲第1項記載の空気清浄機
付冷蔵庫。 3 フイルターを構成する(III)において、アルカリ
として炭酸カリウムを用い、セメント材としてアルミン
酸石灰を用いた特許請求の範囲第1項記載の空気清浄機
付冷蔵庫。4 フイルターを構成する(III)において
、白金とパラジウムを同時に担持された触媒を用いた特
許請求の範囲第1項記載の空気清浄機付冷蔵庫。 5 フイルターを構成する(III)を空気流路の後流に
設置した特許請求の範囲第1項記載の空気清浄機付冷蔵
庫。
[Scope of Claims] 1. In a refrigerator, a refrigerator compressor is provided in an air flow path in which indoor air is sucked in and blown out by a blower, and one or more types selected from the following (I) and (II) and ( III)
A refrigerator with an air purifier, characterized in that a filter consisting of (III) or (III) is provided, and the filter is heated by heat radiation from a compressor. (I) Activated carbon (II) Kneaded molded product of alkali, cement material, and powdered activated carbon (III) One or more selected from platinum, rhodium, and ruthenium and palladium are added simultaneously or to a carrier obtained by kneading and molding alkali, cement material, and powdered activated carbon. Catalyst 2 supporting palladium alone In (II) constituting the filter,
Potassium carbonate or calcium hydroxide is used as the alkali, and calcined gypsum (CaSO_4・1/2H_
2O). 3. The refrigerator with an air cleaner according to claim 1, wherein in (III) constituting the filter, potassium carbonate is used as the alkali and lime aluminate is used as the cement material. 4. The refrigerator with an air purifier according to claim 1, wherein in (III) constituting the filter, a catalyst on which platinum and palladium are simultaneously supported is used. 5. The refrigerator with an air purifier according to claim 1, wherein (III) constituting the filter is installed downstream of the air flow path.
JP54013150A 1979-02-06 1979-02-06 Refrigerator with air purifier Expired JPS6017981B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54013150A JPS6017981B2 (en) 1979-02-06 1979-02-06 Refrigerator with air purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54013150A JPS6017981B2 (en) 1979-02-06 1979-02-06 Refrigerator with air purifier

Publications (2)

Publication Number Publication Date
JPS55105175A JPS55105175A (en) 1980-08-12
JPS6017981B2 true JPS6017981B2 (en) 1985-05-08

Family

ID=11825128

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54013150A Expired JPS6017981B2 (en) 1979-02-06 1979-02-06 Refrigerator with air purifier

Country Status (1)

Country Link
JP (1) JPS6017981B2 (en)

Also Published As

Publication number Publication date
JPS55105175A (en) 1980-08-12

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