JP2912651B2 - Cooking device - Google Patents
Cooking deviceInfo
- Publication number
- JP2912651B2 JP2912651B2 JP1337142A JP33714289A JP2912651B2 JP 2912651 B2 JP2912651 B2 JP 2912651B2 JP 1337142 A JP1337142 A JP 1337142A JP 33714289 A JP33714289 A JP 33714289A JP 2912651 B2 JP2912651 B2 JP 2912651B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust passage
- top plate
- cooking
- heater
- catalyst
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C15/00—Details
- F24C15/20—Removing cooking fumes
- F24C15/2007—Removing cooking fumes from oven cavities
- F24C15/2014—Removing cooking fumes from oven cavities with means for oxidation of cooking fumes
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Baking, Grill, Roasting (AREA)
- Catalysts (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明はオーブンやグリル調理の際に発生する油煙、
臭気を分解除去する機能を有する調理器に関するもので
ある。The present invention relates to an oily smoke generated when cooking an oven or grill,
The present invention relates to a cooker having a function of decomposing and removing odors.
従来の技術 調理中に発生する油煙、臭気の浄化は特に箱型のオー
ブンを触媒を使った手段が実用化されている。構成には
大別して次の2つがある。2. Description of the Related Art For purifying oily smoke and odor generated during cooking, a method using a catalyst using a box-shaped oven has been put to practical use. The configuration is roughly classified into the following two.
まず第1には、触媒を担持したハニカムとハニカム加
熱用ヒータを排気孔に設けファンで調理排ガスを吸引し
て触媒担持ハニカムを通過させ排ガスを触媒的に酸化分
解するものである。First, a honeycomb supporting a catalyst and a heater for heating the honeycomb are provided in an exhaust hole, and cooking exhaust gas is sucked by a fan and passed through the catalyst-supporting honeycomb to catalytically oxidize and decompose the exhaust gas.
第2には第3図に示したように調理室1の天板2の一
部に排気孔3を設け、更に天板2と断熱材4の間に排気
通路5を設け排気通路の上面に酸化触媒を分散担持した
無機繊維多孔体6を配置する。調理物7から発生した油
煙は自然対流により排気孔3、排気通路5を通りヒータ
8によって加熱された無機繊維多孔体6で酸化分解され
排気孔9から放出するという手段が提案されている。Secondly, as shown in FIG. 3, an exhaust hole 3 is provided in a part of the top plate 2 of the cooking chamber 1, and an exhaust passage 5 is further provided between the top plate 2 and the heat insulating material 4 to form an upper surface of the exhaust passage. An inorganic fiber porous body 6 carrying an oxidation catalyst dispersed therein is arranged. A means has been proposed in which oil smoke generated from the cooking product 7 is oxidatively decomposed by the inorganic fiber porous body 6 heated by a heater 8 through an exhaust hole 3 and an exhaust passage 5 by natural convection, and is discharged from the exhaust hole 9.
調理用のヒータの余熱を利用するため触媒加熱用の補
助ヒータがいらず、排気通路が広く触媒との接触時間が
長いため浄化性能が高いという利点がある。Since there is no need for an auxiliary heater for heating the catalyst because the residual heat of the heater for cooking is used, there is an advantage that the purification performance is high because the exhaust passage is wide and the contact time with the catalyst is long.
発明が解決しようとする課題 しかしながら上記した従来技術には次のような課題が
ある。Problems to be Solved by the Invention However, the above-mentioned prior art has the following problems.
第1に示した触媒を担持したハニカムを用いる方式で
は、触媒と排ガスとの接触時間を長くするためにハニカ
ムの形状やセル数を大きくすると圧力損失が大きくなり
排気が通過しにくく、またコスト高となる。最近のオー
ブンはより高い温度での本格的な焼きもの調理が可能と
なり、従って特に魚や肉等、油煙の発生量の多い調理に
対してはハニカム方式は処理能力が低く、その割にはコ
ストが高いという欠点がある。In the first method using a honeycomb supporting a catalyst, if the shape and the number of cells of the honeycomb are increased in order to extend the contact time between the catalyst and the exhaust gas, the pressure loss becomes large, so that the exhaust gas is difficult to pass and the cost is high. Becomes Recent ovens allow full-fledged cooking at higher temperatures, so the honeycomb method has a lower processing capacity, especially for cooking with a large amount of oil smoke, such as fish and meat, and the cost is high for that There is a disadvantage that.
第2に示した無機繊維多孔体を用いた自然排気方式で
は、排気の抵抗を低くするために排気通路の一部を空洞
にしておく必要がある。通常排気通路内は、400℃以上
の高温になっているため油煙は排気通路の上面を通過す
る。従って排気通路の上面に板状の無機繊維多孔体を固
定しておけば油煙はそこで酸化分解される。In the second natural exhaust method using an inorganic fiber porous body, it is necessary to make a part of an exhaust passage hollow to reduce exhaust resistance. Usually, the inside of the exhaust passage has a high temperature of 400 ° C. or more, so that the oil smoke passes through the upper surface of the exhaust passage. Therefore, if a plate-like inorganic fiber porous body is fixed on the upper surface of the exhaust passage, the oil smoke is oxidized and decomposed there.
しかし上記したように本格的な焼きもの調理器で上ヒ
ータと下ヒータに交互に出力を集中して通電する両面焼
きの場合には下ヒータの通電時、酸化触媒の温度が下が
ると油煙は酸化分解されずにそのまま空洞部を通過して
しまうという欠点があった。However, as described above, in the case of a double-sided baking where the power is alternately concentrated and applied to the upper and lower heaters in a full-fledged grilled cooker, when the lower heater is energized and the temperature of the oxidation catalyst falls, the oil smoke is oxidized and decomposed. There is a drawback that they pass through the cavity as it is.
課題を解決するための手段 上記課題を解決するために本発明では、食品を加熱す
るための加熱室と、前記加熱室の天板の内側に設けたヒ
ータと、前記天板の外側に設けた断熱材と、前記天板と
前記断熱材との間に設けた排気通路と、前記排気通路全
体に配設した前記天板よりやや小さい面積を有するセリ
ウム、銅およびマンガンより成る複合酸化物を分散・担
持した無機繊維多孔体と、前記加熱室と前記排気通路を
連通するために前記天板の後部に設けた開孔部と、前記
排気通路後方に設けられたファンとを有し、調理中に発
生した油煙を前記ファンで吸引し前記排気通路内で、前
記ヒータの熱により加熱された前記酸化触媒で酸化分解
する調理排気の処理手段を有する構成とした。これによ
って上ヒータ通電時はヒータの熱で油煙を触媒的に酸化
分解し、下ヒータの通電等で触媒の温度が下がった時は
無機繊維多孔体が油煙に対するフィルターの役割を果た
しかなりの割合の油煙が無機繊維多孔体内に吸着・保持
され後で上ヒータ通電時に浄化される。吸着力を上げる
ために活性炭繊維等を無機繊維多孔体中に混合させるこ
とも容易である。Means for Solving the Problems In order to solve the above problems, in the present invention, a heating chamber for heating food, a heater provided inside a top plate of the heating chamber, and a heater provided outside the top plate are provided. A heat insulating material, an exhaust passage provided between the top plate and the heat insulating material, and a composite oxide made of cerium, copper, and manganese having an area slightly smaller than the top plate disposed throughout the exhaust passage are dispersed. A porous inorganic body carried, an opening provided at the rear of the top plate for communicating the heating chamber with the exhaust passage, and a fan provided at the rear of the exhaust passage, during cooking; The exhaust gas is sucked by the fan, and the cooking exhaust gas is treated by the oxidation catalyst heated by the heat of the heater in the exhaust passage. As a result, when the upper heater is energized, the soot is catalytically oxidized and decomposed by the heat of the heater, and when the temperature of the catalyst is lowered by energizing the lower heater, the inorganic fiber porous material acts as a filter for the soot and a considerable percentage of it. The oily smoke is adsorbed and held in the inorganic fiber porous body, and is subsequently purified when the upper heater is turned on. It is also easy to mix activated carbon fibers or the like into the inorganic fiber porous material in order to increase the adsorptive power.
作用 上記手段の作用について説明する。Operation The operation of the above means will be described.
本発明では触媒としての無機繊維多孔体を加熱する方
法として、加熱室の天板の内側に設けた調理用のヒータ
を利用している。そのため、熱損失で無駄になっている
熱を有効に利用できると共に、新たに触媒加熱用のヒー
タを設ける必要がなくなる。また調理室天板の面積より
やや小さい面積を排気通路とし非常に高い空隙率を持つ
無機繊維多孔体に触媒を分散担持させて排気通路全体に
配置してあるため、排ガスと触媒との接触時間が極端に
長く高い浄化性能が得られる。また上ヒータをOFFにし
触媒の温度が下がった時はフィルターとして油煙を吸着
するため低温時の浄化特性も良好である。In the present invention, as a method for heating the inorganic fiber porous body as a catalyst, a cooking heater provided inside a top plate of a heating chamber is used. Therefore, the heat wasted due to the heat loss can be effectively used, and it is not necessary to newly provide a heater for heating the catalyst. In addition, since the catalyst is dispersed and supported on an inorganic fiber porous body having a very high porosity and disposed throughout the exhaust passage, the contact time between the exhaust gas and the catalyst is set as an exhaust passage with an area slightly smaller than the area of the cooking chamber top plate. Is extremely long and high purification performance is obtained. When the temperature of the catalyst is lowered by turning off the upper heater, the filter absorbs oily smoke, so that the purification characteristics at low temperatures are good.
以上の作用で本発明では調理中の油煙・臭気を容易に
分解除去できる。According to the present invention, oil smoke and odor during cooking can be easily decomposed and removed in the present invention.
実施例 以下本発明の一実施例について図面を用いて説明す
る。第1図は本発明による油煙浄化手段を取り入れた調
理器の一実施例の簡単な断面図であり、第2図は触媒を
担持させた無機繊維多孔体の概念断面図である。調理室
1の天板2の後部にパンチングで排気孔3が開けてあ
り、天板2と断熱材4のすき間に設けられた排気通路5
につながっている。排気通路5には酸化触媒を分散担持
したバルク状の無機繊維多孔体6(本発明ではSiO2/Al2
O3の不織布を使用)が固定されてある。調理物7から発
生した油煙はファン11で吸引され排気孔3から無機繊維
多孔体6を通って排気孔9から排出される。この例では
排気通路5の高さを10mmとした。この間、排気中の油煙
あるいは臭気成分は上ヒーター8で加熱された触媒によ
り分解除去される。また下ヒータ10の通電時通、無機繊
維多孔体6の温度が下がった場合には、無機繊維多孔体
6は油煙のフィルターの役割を果たしかなりの割合の油
煙を吸着させておき、再度温度が上昇した際に焼ききる
ことができる。本発明では排ガスを自然排気ではなくフ
ァン11で吸引するため排気通路5に無機繊維多孔体6を
かなり高密度に充填しても抵抗になりにくく、吸着特性
も向上する。第2図に酸化触媒12と分散担持した無機繊
維多孔体の概念断面図を示す。実際に第1図の構成の調
理器でサバ、サンマ、鳥肉等を上下ヒータの交互通電で
両面焼きをしてみたが、どちらのヒータ通電時にも発生
した油煙や臭気成分は完全に浄化され調理器からの油煙
のもれ等はなかった。これに対して第1図の同じ構成で
無機繊維多孔体6を取り除いたものでは油煙、臭気のも
れがひどかった。このことから本発明の有効性と単にヒ
ータの熱だけによる浄化ではないことは明らかである。Embodiment An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a simple cross-sectional view of an embodiment of a cooking device incorporating an oil and smoke purifying means according to the present invention, and FIG. 2 is a conceptual cross-sectional view of a porous inorganic fiber body carrying a catalyst. An exhaust hole 3 is opened by punching at the rear of the top plate 2 of the cooking chamber 1, and an exhaust passage 5 provided between the top plate 2 and the heat insulating material 4.
Is connected to In the exhaust passage 5, a bulk inorganic fiber porous body 6 (in the present invention, SiO 2 / Al 2
O 3 non-woven fabric) is fixed. Oil smoke generated from the cooked food 7 is sucked by the fan 11, passes through the exhaust hole 3, passes through the inorganic fiber porous body 6, and is discharged from the exhaust hole 9. In this example, the height of the exhaust passage 5 was set to 10 mm. During this time, oily smoke or odor components in the exhaust gas are decomposed and removed by the catalyst heated by the upper heater 8. In addition, when the temperature of the inorganic fiber porous body 6 decreases when the lower heater 10 is energized, the inorganic fiber porous body 6 acts as a filter for oil smoke, adsorbs a considerable amount of oil smoke, and the temperature is again increased. You can bake when you rise. In the present invention, the exhaust gas is sucked not by natural exhaust but by the fan 11, so that even if the exhaust passage 5 is filled with the inorganic fiber porous body 6 at a considerably high density, resistance is hardly generated and the adsorption characteristics are improved. FIG. 2 is a conceptual cross-sectional view of the inorganic fiber porous body dispersedly supported with the oxidation catalyst 12. As shown in FIG. Actually, the mackerel, saury, poultry, etc. were burned on both sides by alternately energizing the upper and lower heaters in the cooker having the configuration shown in FIG. 1. Oil smoke and odor components generated when both heaters were energized were completely purified. There was no leakage of oil smoke from the cooker. On the other hand, when the inorganic fiber porous body 6 was removed in the same configuration as in FIG. 1, oil smoke and odor leaked were severe. From this, it is clear that the effectiveness of the present invention and that the purification is not simply based on the heat of the heater.
次に触媒について説明する。本発明で用いる触媒は、
白金属元素、遷移金属酸化物(複合酸化物も含む)、希
土類酸化物のうちいずれでもよいが、コストの点からは
遷移金属酸化物が好ましい。Next, the catalyst will be described. The catalyst used in the present invention,
Any of a white metal element, a transition metal oxide (including a composite oxide), and a rare earth oxide may be used, but a transition metal oxide is preferable in terms of cost.
これらの触媒系の中で、特に、希土類元素のセリウム
の酸化物と遷移金属酸化物の組み合わせが油煙浄化に優
れた効果を持つ。その理由は以下のように考えられる。
すなわち、調理の進行とともに、油煙はある時期から急
激に発生する。この際、一時的に庫内は酸素濃度が少し
減少する。また油煙は酸化触媒に接触すると還元剤とし
て作用し、酸化触媒表面の吸着酸素を奪うため、酸化能
力が低下し、油煙が浄化できなくなって、油煙が漏れ出
す課題がある。これに対して、セルウム酸化物を共存さ
せるとセリウム酸化物は、酸素ドナーとして働き、酸化
触媒表面に吸着酸素を補給し、触媒活性を再生させる。
従って、両者の共存により、調理器の油煙の負荷が最大
となる状況で有効な浄化効果が得られる。特に、セリウ
ム酸化物と遷移金属酸化物の組み合わせとししては、
銅、マンガン酸化物の複合酸化物が高活性である。その
理由は明確ではないが、複合酸化物の電子状態と関係が
あると考えられる。本発明では、Ce,Cu,Mnの複合酸化物
CeO2・CuxMn3−xO4(O<X<1.5),Fe2O3・Mn2O3・Cu
O,La1-XCexCoO3(0<X≦0.2)を用いた。無機繊維不
織布への担持は不織布の製造時に同時に行った。一方織
布への担持は、液相での含浸法で行った。不織布、織布
いずれに触媒を担持しても、サラダ油は250℃で分解し
てしまう。(サラダ油は、油脂のトレーサーとして用い
た。) 次に、油煙・臭気処理の条件について説明する。まず
油煙の粒子サイズであるが、あじ、さば、さんま、鳥
肉、サラダ油からの油煙の粒子径は約0.1〜5μmの幅
囲にあった。よってこれら粒子を捕獲し分解するにはこ
れよりも大きな孔径をもった多孔体が好ましいが、本発
明で用いる無機繊維多孔体は数μm〜数100μmの孔径
をもつので触媒担体として適している。さらに酸化反応
を進行させるためには酸素供給が必要であるが、無機繊
維多孔体は空隙率が数10%、大きいもので80〜90%にも
なり、空気中からの酸素取込みには最適であり、このこ
とが反応応を進める点に対して大きく影響している。Among these catalyst systems, in particular, a combination of a rare earth element cerium oxide and a transition metal oxide has an excellent effect on oil and smoke purification. The reason is considered as follows.
That is, as cooking progresses, oil smoke is rapidly generated from a certain time. At this time, the oxygen concentration in the refrigerator temporarily decreases slightly. In addition, when the oil smoke comes into contact with the oxidation catalyst, it acts as a reducing agent, and desorbs oxygen adsorbed on the surface of the oxidation catalyst. Therefore, the oxidation ability is reduced, so that the oil smoke cannot be purified and the oil smoke leaks. On the other hand, when coexisting with cell oxide, cerium oxide functions as an oxygen donor, replenishes the surface of the oxidation catalyst with adsorbed oxygen, and regenerates the catalytic activity.
Therefore, by the coexistence of both, an effective purifying effect can be obtained in a situation where the load of the oil smoke of the cooking appliance is maximized. In particular, as a combination of cerium oxide and transition metal oxide,
A composite oxide of copper and manganese oxide is highly active. Although the reason is not clear, it is considered to be related to the electronic state of the composite oxide. In the present invention, Ce, Cu, Mn composite oxide
CeO 2 · CuxMn 3 - x O 4 (O <X <1.5), Fe 2 O 3 · Mn 2 O 3 · Cu
O, La 1-X CexCoO 3 (0 <X ≦ 0.2) was used. The support on the inorganic fiber nonwoven fabric was performed simultaneously with the production of the nonwoven fabric. On the other hand, the support on the woven fabric was performed by the impregnation method in the liquid phase. The salad oil is decomposed at 250 ° C. regardless of whether the catalyst is carried on non-woven fabric or woven fabric. (The salad oil was used as a tracer for fats and oils.) Next, the conditions for oil smoke and odor treatment will be described. First, regarding the particle size of oil smoke, the particle diameter of oil smoke from horse mackerel, mackerel, saury, poultry, and salad oil was in the range of about 0.1 to 5 μm. Therefore, in order to capture and decompose these particles, a porous body having a larger pore diameter is preferable. However, the inorganic fiber porous body used in the present invention has a pore diameter of several μm to several hundred μm and is suitable as a catalyst carrier. In order to further promote the oxidation reaction, it is necessary to supply oxygen.However, the inorganic fiber porous material has a porosity of tens of percent, and as large as 80 to 90%, it is optimal for taking in oxygen from the air. Yes, this has a significant effect on the point at which the reaction is advanced.
次に無機繊維多孔体の空隙率と油の浄化特性と相関に
ついて説明する。Next, the correlation between the porosity of the porous inorganic fiber and the purification properties of the oil will be described.
第4図に空隙率の変化に対するサラダ油の300℃での
分解時間を示した。試料として厚さ1mm、サイズ50mm×5
0mmのSiO2/Al2O3不織布に25重量%の触媒CeO2・CuxMn
3-XO4(x=0.9)を担持したものを用いサラダ油は0.5g
滴下した。第4図より空隙率は40%以上がよいと思われ
るが、より高温になれば30%程度で十分である。触媒の
担持量は、第5図に空隙率60%、厚さ1mm、サイズ5cm×
5cmのSiO2−Al2O3不織布に触媒La1-XCexCoO3(x=0.
1)を担持した時の担持量(wt%)とサラダ油0.5gの300
℃における分解時間を示したように、10%以上がよいと
思われるがこれも温度との関係で当然変わるものであ
る。FIG. 4 shows the decomposition time of the salad oil at 300 ° C. with respect to the change in the porosity. 1mm thick, size 50mm x 5 as sample
0 mm 25% by weight SiO 2 / Al 2 O 3 nonwoven catalyst CeO 2 · CuxMn
Use 3-X O 4 (x = 0.9) supported and 0.5g salad oil
It was dropped. From FIG. 4, it is considered that the porosity is preferably 40% or more, but at a higher temperature, about 30% is sufficient. The supported amount of the catalyst is shown in Fig. 5 with a porosity of 60%, a thickness of 1mm, and a size of 5cm.
5cm SiO 2 -Al 2 O 3 nonwoven catalyst La 1-X CexCoO 3 of (x = 0.
1) Loading amount (wt%) when supporting and 300g of salad oil 0.5g
As shown in the decomposition time in ° C., it is considered that 10% or more is preferable, but this also naturally changes depending on the temperature.
次に第1図の構成において排気通路5の高さ(つまり
無機繊維多孔体6の高さ)であるがファン11の吸引によ
る排気速度、圧力損失、反応温度(多孔体温度)の関係
で適当な高さがある。第1図の構成で排気通路5の高さ
を5mm、10mm、15mm、20mm、30mmとして上記と同じく0.5
gのサラダ油の煙を使って評価した。その結果、5mmでは
通気に対する抵抗が大きいためファンの吸引力が強すぎ
て無機繊維多孔体の固定が困難となる。一方30mmになる
と無機繊維多孔体の上部と下部に温度勾配ができ、また
コスト的にも不利になる。よって高さは10〜20mmがよ
い。この場合、多孔体の温度は殆どの部分で400℃以上
であった。Next, in the structure shown in FIG. 1, the height of the exhaust passage 5 (that is, the height of the inorganic fiber porous body 6) is appropriate in relation to the exhaust speed by suction of the fan 11, the pressure loss, and the reaction temperature (porous body temperature). There is a height. The height of the exhaust passage 5 is set to 5 mm, 10 mm, 15 mm, 20 mm, and 30 mm in the configuration shown in FIG.
The evaluation was made using smoke of g salad oil. As a result, if the diameter is 5 mm, the resistance to ventilation is large, and the suction force of the fan is too strong, so that it is difficult to fix the inorganic fiber porous body. On the other hand, when the thickness is 30 mm, a temperature gradient is formed between the upper and lower portions of the inorganic fiber porous body, and the cost is disadvantageous. Therefore, the height is preferably 10 to 20 mm. In this case, the temperature of the porous body was 400 ° C. or higher in most parts.
次に、油煙の分解に必要な温度について説明する。こ
れについても、第1図構成の調理器を使い、調理室内で
サラダ油を酸化分解しながら実調理の数倍の油煙を発生
させ、ヒータの出力を変化させながらSiO2−Al2O3繊維
不織布の温度を変えて評価した。多孔体の大きさは200m
m×150mmあり、ヒータも温度むらがあるので、全体に温
度は均一にはなり得ないが、多孔体中心点より排気の流
れ方向に前後5cmのところにK型熱電対を設け温度を測
定した。温度は、約350℃、400℃、450℃となるように
ヒータ入力をコントロールした。その結果、目視で煙が
なくなったと判断できたのは約400℃のときであった。
臭気についても同様であった。従って上記したように第
1図の構成で無機繊維多孔体の高さを10〜20mmにした場
合、多孔体の温度が400℃以上であったことから多孔体
は浄化に対して十分な温度になっていると言うことがで
きる。Next, the temperature required for decomposing the oil smoke will be described. This will also use the cooker Figure 1 configuration, salad oil and to generate several times the smoke of oxidative decomposition while actual cooking cooking chamber, SiO 2 -Al 2 O while changing the output of the heater 3 fiber nonwoven fabric Was evaluated at different temperatures. The size of the porous body is 200m
m × 150 mm, the heater also has uneven temperature, so the temperature can not be uniform as a whole, but a K-type thermocouple was placed 5 cm before and after in the exhaust flow direction from the center of the porous body and the temperature was measured. . The heater input was controlled so that the temperature was about 350 ° C, 400 ° C, and 450 ° C. As a result, it was possible to visually judge that the smoke had disappeared at about 400 ° C.
The same was true for the odor. Therefore, as described above, when the height of the inorganic fiber porous body is set to 10 to 20 mm in the configuration of FIG. 1, since the temperature of the porous body was 400 ° C. or higher, the porous body was brought to a temperature sufficient for purification. It can be said that it has become.
上記実施例では無機繊維多孔体としてSiO2−Al2O3繊
維不織布を用いているが、不織布材質としてはSiO2−Al
2O3の他にSiO2単独又はZrO2でもよい。必要な条件は基
本的に空隙率がとれるかとれないかであるから材質の面
では本発明では特に制限を受けるものではない。ただし
コスト面からSiO2−Al2O3系がよい。一方織布ではSiCを
主成分としたものが市場にでているが、Al2O3あるいはS
iO2やZrO2よりなる織布でもよい。繊維径は通常数μm
〜10μm程度であるが、繊維間に油煙粒子を捕獲できる
程度の空隙を設けて織布し、空隙率を高めなければなら
ない。In the above embodiment uses a SiO 2 -Al 2 O 3 fiber nonwoven fabric as the inorganic fibrous porous material. The preferred non-woven material SiO 2 -Al
In addition to 2 O 3 , SiO 2 alone or ZrO 2 may be used. Since the necessary condition is basically whether or not the porosity can be obtained, the present invention is not particularly limited in terms of the material. However, the SiO 2 —Al 2 O 3 system is preferred from the viewpoint of cost. On the other hand, woven fabrics containing SiC as a main component are on the market, but Al 2 O 3 or S
A woven fabric made of iO 2 or ZrO 2 may be used. Fiber diameter is usually several μm
It is about 10 μm, but it is necessary to provide voids between the fibers so as to capture oil and smoke particles, and woven fabric to increase the porosity.
以上、オーブン調理の特に両面焼き調理の際の油煙及
び臭気の浄化に有効な手段を有した調理器について説明
したが、本発明による手段は、その構成から調理器に限
らず応用分野が広く簡便なものであると考えられる。The cooker having means effective for purifying oily smoke and odor in oven cooking, particularly during double-sided baking, has been described above. However, the means according to the present invention is not limited to a cooker because of its configuration, and its application field is wide and simple. It is thought that it is something.
発明の効果 以上説明したように本発明によれば、次のような効果
が得られる。Effects of the Invention As described above, according to the present invention, the following effects can be obtained.
(1) 高活性な触媒と空隙率の高い無機繊維多孔体を
用いているため調理中に発生した油煙の浄化性能が高く
大量の煙が処理できるため特に本格的な焼きもの調理器
に有効である。また調理用ヒータの余熱を利用するため
新たに触媒加熱用補助ヒータを付ける必要がなく低コス
トである。(1) The use of a highly active catalyst and a porous material with a high porosity makes it highly effective in purifying oily smoke generated during cooking and can process a large amount of smoke. . Further, since the residual heat of the cooking heater is utilized, it is not necessary to newly provide an auxiliary heater for heating the catalyst, so that the cost is low.
(2) 排気通路を広面積にとり、内部に酸化触媒を含
む無機繊維多孔体を充填し、ファンで吸引して排気する
方式であるため、上ヒータの交互通電による両面焼き調
理で触媒の温度が下がった場合には油煙を吸着させてお
くことができるため低温時にも油煙や臭いがオーブン庫
内からもれることがない。(2) Since the exhaust passage is widened, the inside is filled with an inorganic fiber porous material containing an oxidation catalyst, and the air is exhausted by suction with a fan, the temperature of the catalyst can be reduced by double-sided baking cooking by alternately energizing the upper heater. When the temperature drops, oil fumes and odors can be prevented from leaking from the oven chamber even at a low temperature because oil fumes can be adsorbed.
第1図は本発明の一実施例による油煙浄化手段を取り入
れた調理器の断面図、第2図は同触媒を担持した無機繊
維多孔体の概念断面図、第3図は従来例による油煙浄化
手段を取り入れた調理器の断面図、第4図は無機繊維多
孔体の空隙率の油の焼き切り時間との相関を示した特性
図、第5図は無機繊維多孔体への触媒の担持量と油の焼
き切り時間との相関を示した特性図である。 1……加熱室、3……開孔部、4……断熱材、5……排
気通路、6……無機繊維多孔体、8、10……ヒータ、11
……ファン、12……酸化触媒。FIG. 1 is a sectional view of a cooker incorporating an oil and smoke purifying means according to one embodiment of the present invention, FIG. 2 is a conceptual sectional view of a porous inorganic fiber body carrying the catalyst, and FIG. FIG. 4 is a characteristic diagram showing the correlation between the porosity of the inorganic fiber porous body and the oil burning-off time, and FIG. 5 is a diagram showing the amount of catalyst carried on the inorganic fiber porous body. FIG. 4 is a characteristic diagram showing a correlation with an oil burning time. DESCRIPTION OF SYMBOLS 1 ... Heating chamber, 3 ... Opening part, 4 ... Heat insulation material, 5 ... Exhaust passage, 6 ... Inorganic porous material, 8, 10 ... Heater, 11
... fans, 12 ... oxidation catalysts.
フロントページの続き (72)発明者 金子 康典 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (72)発明者 福田 明雄 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (56)参考文献 特開 昭55−6132(JP,A) 特開 昭64−54128(JP,A) 特開 昭52−39475(JP,A) 実開 昭55−159913(JP,U) (58)調査した分野(Int.Cl.6,DB名) F24C 15/20 F24C 14/00 Continued on the front page (72) Inventor Yasunori Kaneko 1006 Kazuma Kadoma, Osaka Prefecture Inside Matsushita Electric Industrial Co., Ltd. (72) Inventor Akio Fukuda 1006 Okadoma Kazuma Kadoma City, Osaka Matsushita Electric Industrial Co., Ltd. (56 ) References JP-A-55-6132 (JP, A) JP-A-64-54128 (JP, A) JP-A-52-39475 (JP, A) Japanese Utility Model Showa 55-159913 (JP, U) (58) Field surveyed (Int. Cl. 6 , DB name) F24C 15/20 F24C 14/00
Claims (2)
の天板の内側に設けたヒータと、前記天板の外側に設け
た断熱材と、前記天板と前記断熱材との間に設けた排気
通路と、前記排気通路全体に配設した前記天板よりやや
小さい面積を有するセリウム、銅およびマンガンより成
る複合酸化物を分散・担持した無機繊維多孔体と、前記
加熱室と前記排気通路を連通するために前記天板の後部
に設けた開孔部と、前記排気通路後方に設けられたファ
ンとを有し、調理中に発生した油煙を前記ファンで吸引
し前記排気通路内で、前記ヒータの熱により加熱された
前記酸化触媒で酸化分解する調理排気の処理手段を有す
る調理器。1. A heating chamber for heating food, a heater provided inside a top plate of the heating chamber, a heat insulating material provided outside the top plate, and a heat insulating material provided between the top plate and the heat insulating material. An exhaust passage provided therebetween, an inorganic fiber porous body dispersing and supporting a composite oxide made of cerium, copper, and manganese having an area slightly smaller than the top plate provided in the entire exhaust passage, and the heating chamber; An opening provided in a rear portion of the top plate for communicating with the exhaust passage, and a fan provided behind the exhaust passage, wherein the fan sucks oil smoke generated during cooking with the fan; A cooking device having cooking exhaust processing means for oxidizing and decomposing by the oxidation catalyst heated by the heat of the heater.
2のうちいずれか一種以上からなる繊維の不織布あるい
は織布、もしくはSiCが主成分の繊維の織布である特許
請求の範囲第1項記載の調理器。2. The inorganic transition porous material is made of SiO 2 , Al 2 O 3 , ZrO.
2. The cooking device according to claim 1, wherein the cooking device is a non-woven fabric or woven fabric of a fiber composed of any one or more of the two , or a woven fabric of a fiber mainly composed of SiC.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1337142A JP2912651B2 (en) | 1989-12-26 | 1989-12-26 | Cooking device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1337142A JP2912651B2 (en) | 1989-12-26 | 1989-12-26 | Cooking device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03195826A JPH03195826A (en) | 1991-08-27 |
JP2912651B2 true JP2912651B2 (en) | 1999-06-28 |
Family
ID=18305841
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1337142A Expired - Lifetime JP2912651B2 (en) | 1989-12-26 | 1989-12-26 | Cooking device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2912651B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2398628B (en) * | 2003-02-20 | 2005-09-21 | Merrychef Ltd | Ovens with catalytic converters |
CN110192781A (en) * | 2018-02-24 | 2019-09-03 | 青岛海尔智能技术研发有限公司 | Oven |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5239475A (en) * | 1975-09-23 | 1977-03-26 | Terukatsu Teraoka | Portable range |
JPS5949500B2 (en) * | 1978-06-26 | 1984-12-03 | 松下電器産業株式会社 | heating cooker |
JPS55159913U (en) * | 1979-05-02 | 1980-11-17 | ||
JPS6454128A (en) * | 1987-08-24 | 1989-03-01 | Matsushita Electric Ind Co Ltd | Heating and cooking appliance |
-
1989
- 1989-12-26 JP JP1337142A patent/JP2912651B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH03195826A (en) | 1991-08-27 |
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