JPS5813817B2 - Cooker equipped with a smoke removal device - Google Patents
Cooker equipped with a smoke removal deviceInfo
- Publication number
- JPS5813817B2 JPS5813817B2 JP50101398A JP10139875A JPS5813817B2 JP S5813817 B2 JPS5813817 B2 JP S5813817B2 JP 50101398 A JP50101398 A JP 50101398A JP 10139875 A JP10139875 A JP 10139875A JP S5813817 B2 JPS5813817 B2 JP S5813817B2
- Authority
- JP
- Japan
- Prior art keywords
- oil smoke
- cooking
- oxidation catalyst
- oil
- removal device
- 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
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Description
【発明の詳細な説明】
本発明は調理器における油煙の除去装置に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for removing oil smoke from a cooking appliance.
これまでの調理器たとえば、電子式電気自動オーブンを
例にとると、熱源としては上部に料理物にこげ目をつけ
るための赤外線ヒータを、下部には庫内温度を均一にす
るためのシーズヒータを有し、シーズヒータの上に焼汁
を受けるための受皿がある。For example, if we take an electric automatic oven as an example, the heat source is an infrared heater at the top to brown the food, and a sheathed heater at the bottom to even out the internal temperature. There is a saucer on top of the sheathed heater to receive the grilled juices.
料理温度は料理物に合わせて正確に制御できるような構
造を有するものが一般的であり、正確な温度制御ができ
ることから料理の巾が広いという特徴を有する。Generally, the structure is such that the cooking temperature can be controlled accurately according to the food being cooked, and because the temperature can be precisely controlled, the cooking range is wide.
しかしながら、高温料理、特に油脂分の多い鳥肉、魚等
の焼料理においては大量の油煙と調理臭を発生すると共
に、調理庫内の内壁に蒸発した油脂分が附着して焼付け
られ、庫内を汚し、いつまでも臭いが消えず、次の料理
に悪影響をおよぼすと言う大きな欠点があった。However, high-temperature cooking, especially grilled dishes such as chicken and fish that contain a lot of oil and fat, generates a large amount of oil smoke and cooking odors, and the evaporated oil and fat sticks to the inner walls of the cooking chamber and burns, causing the inside of the cooking chamber to burn. It has a major drawback: it stains the food, the smell persists, and it has a negative impact on the next dish.
その後の研究の結果、調理庫内の内壁に附着する油脂分
の除去については、セルフ・クリーニング方式が開発さ
れてきたが、性能的にはまだ不満足な点が多い。As a result of subsequent research, a self-cleaning method was developed to remove fats and oils adhering to the inner walls of the cooking chamber, but there are still many unsatisfactory points in terms of performance.
セルフクリーニング方式とは鉄板にホーローをほどこし
た上に酸化触媒を担持させて、附着油滴を酸化反応を利
用して除去する方式であるが、表面積が少ないので、性
能の劣化が早く、寿命が短いという欠点がある。The self-cleaning method is a method in which an oxidation catalyst is supported on an enameled iron plate and adhering oil droplets are removed using an oxidation reaction, but because the surface area is small, performance deteriorates quickly and the service life is shortened. It has the disadvantage of being short.
又、油煙、調理臭の除去についても酸化触媒を用いる方
法が種々検討されてきたがいまだに実用に耐えるものが
出現していない。In addition, various methods using oxidation catalysts have been investigated for removing oil smoke and cooking odors, but no method has yet emerged that is suitable for practical use.
調理物から飛散する物質の主なものは油脂類、炭水化物
、たん白質、食塩などで、このうち油煙、油滴に含まれ
るものは主に油脂類である。The main substances that fly off from cooked food are oils and fats, carbohydrates, proteins, and salt, among which oils and fats are mainly contained in oil smoke and oil droplets.
油脂には植物性と動物性があり、代表的な成分はパルミ
チレン酸、ステアリン酸、オレイン酸、リノール酸など
で、構成成分は炭素数C16〜024程度の脂肪酸であ
る。Fats and oils come in both vegetable and animal origin, and typical components include palmitynic acid, stearic acid, oleic acid, linoleic acid, etc., and the constituent components are fatty acids with approximately C16 to C024 carbon atoms.
この脂肪酸は実際の食品中ではトリグリャライドとして
含有されている。This fatty acid is contained in actual foods as triglyalide.
これらの脂肪酸は飽和脂肪酸と不飽和脂肪酸からなり、
油煙、油滴に含まれるものは主に後者の不飽和脂肪酸で
あると考えられている。These fatty acids consist of saturated fatty acids and unsaturated fatty acids.
It is thought that what is contained in oil smoke and oil droplets is mainly the latter type of unsaturated fatty acids.
これらの脂肪酸の分解過程は種々の分献に見られるよう
に次の過程を経て分解するものと考えられている。The decomposition process of these fatty acids is thought to occur through the following process, as seen in various fractions.
本発明における油煙分解層は上記のような分解ガスにす
る分解反応と、過酸化物から重合反応を経てできるポリ
マーの生成を抑制する作用をするものである。The oil smoke decomposition layer in the present invention has the function of suppressing the decomposition reaction to produce cracked gas as described above and the formation of a polymer produced from peroxide through a polymerization reaction.
つまり、クラツキング反応を促進させることが主な目的
である。In other words, the main purpose is to promote the cracking reaction.
しかし、酸化触媒は油煙、油滴に対して主に酸化、重合
反応を促進させるのであり、タール状の生成物を多量に
発生させる。However, the oxidation catalyst mainly promotes the oxidation and polymerization reactions of oil smoke and oil droplets, and generates a large amount of tar-like products.
ところが、分解ガスに対しては重合反応を伴わずに酸化
反応を進行させ、CO2,H20に変化させる。However, the cracked gas undergoes an oxidation reaction without a polymerization reaction, and is converted into CO2 and H20.
したがって本発明は油煙分解層により油煙、油滴を分解
ガス化し、この分解ガスを酸化触媒により無害、無臭の
CO2,H20に変化させることができるものである。Therefore, the present invention is capable of decomposing and gasifying oil smoke and oil droplets using an oil smoke decomposition layer, and converting this cracked gas into harmless and odorless CO2 and H20 using an oxidation catalyst.
以下、その実施例と実験結果にもとづいて、本発明者等
の意図している点について具体的な説明を行う。Hereinafter, based on the examples and experimental results, the points intended by the present inventors will be specifically explained.
まず本発明者等が考案した油煙除去装置の一実施例につ
いて説明する。First, an embodiment of the oil smoke removal device devised by the present inventors will be described.
第1図のように触媒筒1の最下部にステンレス鋼を発泡
させて無数多数の微細な通気孔5を形成した油煙分解層
2を着脱自在に装備し、その上部に無数多数の細孔4を
有する酸化触媒3を3層積層して構成した。As shown in Fig. 1, the lowest part of the catalyst cylinder 1 is removably equipped with an oil smoke decomposition layer 2 made of foamed stainless steel with countless fine ventilation holes 5, and the upper part is equipped with an oil smoke decomposition layer 2 with countless fine holes 4. The oxidation catalyst 3 was constructed by laminating three layers.
酸化触媒3の形状は第2図のような円筒型のものを第3
図のように多数組合せて使用する方法と、第4図のよう
に円板型あるいは第5図のように角型に無数の細孔4を
有するもの等について本発明者等は検討した。The shape of the oxidation catalyst 3 is cylindrical as shown in Figure 2.
The present inventors have studied methods in which a large number of pores 4 are used in combination as shown in the figure, and a disc-shaped one as shown in FIG. 4 or a square-shaped one as shown in FIG. 5 having numerous pores 4.
酸化触媒3の組成は二酸化マンガン( Mn O 2
)を主成分とし、助触媒としてCu ,Fe,Co,N
i等の金属酸化物を用い、結合材として、アルミン酸石
灰(Al20B・Cab)を用いた。The composition of the oxidation catalyst 3 is manganese dioxide (MnO2
) as the main component, and Cu, Fe, Co, N as co-catalysts.
A metal oxide such as i was used, and lime aluminate (Al20B.Cab) was used as a binder.
その具体的な実施例の一例としての組成比は次の表1の
通りである。The composition ratio as an example of a specific example is shown in Table 1 below.
次に酸化触媒3の製造方法の一実施例について説明する
。Next, an example of a method for manufacturing the oxidation catalyst 3 will be described.
第一方法は加圧成型によるものである.その概略工程を
第6図に示す。The first method is by pressure molding. The schematic process is shown in FIG.
第2図の形状を例にとって説明すると、まず、上表に明
記した組成比の酸化触媒を30分間混合し、それに重量
比5〜10%の水(H20)を添加し、次いで、15分
間混合すると水分を含んだ粉末状の混合物となる。Taking the shape shown in Figure 2 as an example, first, the oxidation catalyst with the composition ratio specified in the table above is mixed for 30 minutes, then water (H20) with a weight ratio of 5 to 10% is added, and then mixed for 15 minutes. This results in a powdery mixture containing water.
その混合物を第2図の形状をした金型に投入し加圧成型
を行うと所望の形はできるが、まだ強度的に非常に弱い
。When the mixture is put into a mold having the shape shown in Fig. 2 and pressure molded, the desired shape can be obtained, but the strength is still very weak.
したがって強度を増すために続いて、lOO℃の蒸気中
で1時間養生、乾煤を行うとアルミン酸石灰(Al20
22Cab)が水(H20)と反応して、ポーラスで固
い酸化触媒層が形成され、第2図のような形状の酸化触
媒ができる。Therefore, in order to increase the strength, after curing for 1 hour in steam at 100°C and drying soot, lime aluminate (Al20
22Cab) reacts with water (H20) to form a porous and hard oxidation catalyst layer, resulting in an oxidation catalyst having the shape shown in FIG.
第2の方法は注入法によるものである。The second method is by injection.
その概略工程を第7図に示す。The schematic process is shown in FIG.
第4図の円板型を例にとって説明すると、まず、所望の
形状の金属型を作りそれを母型6として第7図に示すよ
うに母型6を外枠7と固定し、シリコンゴム8を注入す
る。Taking the disk mold shown in FIG. 4 as an example, first, a metal mold of a desired shape is made, and it is used as the mother mold 6. As shown in FIG. inject.
その後80℃の空気中で2Hr乾燥し、続いてIHr沸
湯水中で煮沸すると、シリコンゴム8が硬化する。Thereafter, the silicone rubber 8 is cured by drying in air at 80° C. for 2 hours and then boiling in IHr boiling water.
冷却後母型6と外枠7をはずし、硬化したシリコンゴム
樹脂8を離型してとりだし、それを酸化触媒の注入型と
する。After cooling, the mother mold 6 and the outer frame 7 are removed, and the cured silicone rubber resin 8 is released and taken out, and used as an oxidation catalyst injection mold.
その仮称を以後SR型9と呼ぶ。Its tentative name will be referred to as SR type 9 from now on.
次に第一の方法で用いた組成の酸化触媒を30分間混合
し、それに重量比20〜30%の水(H20)を添加し
、次いで、15分間混合するとスラリー状の混合物10
ができる。Next, the oxidation catalyst having the composition used in the first method was mixed for 30 minutes, water (H20) of 20 to 30% by weight was added thereto, and then mixed for 15 minutes to form a slurry mixture of 10
I can do it.
次に第9図に示すようにSR型9にスラリー状の混合物
10を注入する。Next, as shown in FIG. 9, a slurry-like mixture 10 is poured into the SR mold 9.
その後80℃の空気中でIHr湿式乾燥を行うとスラリ
ー状の混合物10は完全養生し、酸化触媒3となる。Thereafter, the slurry-like mixture 10 is completely cured by performing IHr wet drying in air at 80° C., and becomes the oxidation catalyst 3.
冷却後SR型9から酸化触媒3を離型し、さらに強度を
増すために80℃の温水中で10〜20分間養生し、次
いで150℃の空気中でIHr乾燥すると第4図に示す
ような酸化触媒が完成する。After cooling, the oxidation catalyst 3 was released from the SR mold 9, cured in hot water at 80°C for 10 to 20 minutes to further increase its strength, and then dried by IHr in air at 150°C, resulting in the product shown in Figure 4. The oxidation catalyst is completed.
この方法の特徴は所望の形状が任意に製作できる点にあ
る。A feature of this method is that any desired shape can be produced.
以上本発明者等が考案した油燥除去装置の一実施例につ
いて示したが、次にこの油燥除去装置を調理器に応用し
た例について述べる。An embodiment of the oil-drying removal device devised by the present inventors has been described above.Next, an example in which this oil-drying removal device is applied to a cooking appliance will be described.
従来例 1
第10図は前述した従来の電子式電気自動オーブンの代
表例である。Conventional Example 1 FIG. 10 is a representative example of the conventional electronic electric automatic oven mentioned above.
図において調理庫内11の下部に電熱ヒータ12、上部
には料理にこげ目をつける赤外線ヒータ13がそれぞれ
設けられ、その間に料理を載せる網棚14があり、さら
にその下部に焼汁を受ける受皿15が設けられている。In the figure, an electric heater 12 is installed in the lower part of the cooking chamber 11, and an infrared heater 13 is installed in the upper part to brown the food.In between, there is a mesh shelf 14 on which the food is placed, and further below that there is a saucer 15 for receiving the grilled juices. is provided.
尚前面は開閉扉16となっている。The front side is an opening/closing door 16.
この場合の熱源は赤外線ヒータ13と電熱ヒータ12で
あり、電子式の温度制御ができるように構成されている
。The heat sources in this case are an infrared heater 13 and an electric heater 12, which are configured to allow electronic temperature control.
この電子式電気自動オーブンで鳥肉を焼いた場合の実験
結果は次の通りである。The experimental results of roasting chicken meat using this electronic electric automatic oven are as follows.
尚実験条件は料理温度が300℃、料理物は鳥のももや
き、料理時間は15分間とした。The experimental conditions were that the cooking temperature was 300°C, the food was chicken momoyaki, and the cooking time was 15 minutes.
料理時に油滴状の油脂を含んだ多量の油煙が排気口17
から排出され、目にしみることはなはだしく、油煙と調
理臭が部屋中に充満した。During cooking, a large amount of oil smoke containing oil droplets is emitted from the exhaust port 17.
The room was filled with oily smoke and cooking smells that stung the eyes.
測定した炭化水素(HC)の最高濃度は1 3 0 0
p.p.mであった。The highest concentration of hydrocarbons (HC) measured was 1300
p. p. It was m.
第14.17図にイとしてその測定結果を示す。Figure 14.17 shows the measurement results as A.
料理終了後調理庫内11を調べると、内壁18に蒸発し
た油脂分が附着して、焼付けられ、汚れがひどく、いつ
までも臭いが消えなかった。When the inside of the cooking chamber 11 was inspected after cooking, it was found that the inner walls 18 were stained with evaporated oil and fat, and were badly stained, with a persistent odor.
従来例 2
又第11図に示すように調理庫内壁18の汚れを防止す
るために先に述べたセルフクリーニング方式を採用し、
油煙、調理臭の除去には酸化触媒3を排気口17に装備
したものも実験した。Conventional Example 2 In addition, as shown in FIG. 11, the self-cleaning method described above is adopted to prevent the inner wall 18 of the cooking chamber from getting dirty.
In order to remove oil smoke and cooking odors, an experiment was also conducted in which an oxidation catalyst 3 was installed in the exhaust port 17.
この電子式電気自動オーブンで鳥肉を焼いた場合の実験
結果は第14,15,16,17図に口として示す通り
である。The experimental results of roasting chicken meat using this electronic electric automatic oven are as shown in Figures 14, 15, 16, and 17.
尚、実験条件は、先の従来例1と同一とし、その他の条
件はセルフクリーニンクをほどこした料理庫内壁18の
面積が0.36m’、排気口17に装備した酸化触媒3
の量は750CC、排気ガス量は0.7m’/Hr(開
閉扉16からもれない程度の排気ガス量)とした。The experimental conditions were the same as those in Conventional Example 1, except that the area of the self-cleaning cooking cabinet inner wall 18 was 0.36 m', and the oxidation catalyst 3 installed at the exhaust port 17 was used.
The amount of exhaust gas was 750 cc, and the amount of exhaust gas was 0.7 m'/Hr (an amount of exhaust gas that would not leak from the opening/closing door 16).
図から明らかな通り、初期性能は非常にすぐれているが
、使用回数が増加するにしたがって、浄化性能の劣化が
激しいことが判明した。As is clear from the figure, the initial performance was very good, but as the number of times it was used increased, the purification performance deteriorated significantly.
さらに従来例2の試験条件の中で排気口17に装備した
酸化触媒3の量を1/2にした場合の実験結果は第14
.15.16,17図のハに示す通り、油煙、調理臭共
に、初期性能から悪く、使用回数が増加すればさらに悪
くなる。Furthermore, the experimental results when the amount of oxidation catalyst 3 installed in the exhaust port 17 was reduced to 1/2 under the test conditions of Conventional Example 2 are as follows.
.. 15. As shown in Figures 16 and 17, the oil smoke and cooking odor are both poor from the initial performance, and become even worse as the number of uses increases.
次に本発明の実施例を説明する。Next, examples of the present invention will be described.
実施例 1
第12図に示すように従来例2に本発明者等が考案した
油煙分解層と酸化触媒からなる油煙除去装置19(酸化
触媒量750Ce)を排気口17へ装備し、その他の試
験条件は従来例2と同一条件とした。Example 1 As shown in FIG. 12, the conventional example 2 was equipped with an oil smoke removal device 19 (oxidation catalyst amount: 750 Ce) consisting of an oil smoke decomposition layer and an oxidation catalyst devised by the present inventors, and other tests were carried out. The conditions were the same as those in Conventional Example 2.
実験結果は第14,15.16.17図の二に示す通り
、使用回数が増加しても油煙及び調理臭の浄化能力の低
下が少ないことが判明した。As shown in Figures 14, 15, 16, and 17-2, the experimental results revealed that the ability to purify oil smoke and cooking odors did not decrease much even when the number of times of use increased.
実施例 2
実施例1の試験条件の中で油煙除去装置19に用いた酸
化触媒3の量を1/2にしたものである。Example 2 Under the test conditions of Example 1, the amount of oxidation catalyst 3 used in the oil smoke removal device 19 was reduced to 1/2.
実験結果は第14,15,16.17図のホに示す通り
、実施例1と同等の性能であった。The experimental results, as shown in Figs. 14, 15, 16 and 17, showed that the performance was equivalent to that of Example 1.
実施例 3
実施例2の試験条件の中で第13図に示すように セル
フクリーニング処理をほどこした調理庫内壁18に凹凸
をつけて壁面積を0.60mとこれまでより2/3増加
し、その他の条件は実施例2と同一条件とした。Example 3 As shown in Fig. 13 under the test conditions of Example 2, the inner wall 18 of the cooking chamber, which had undergone self-cleaning treatment, was made uneven to increase the wall area by 2/3 to 0.60 m, compared to the previous one. Other conditions were the same as in Example 2.
実験結果は第14.15,16.17図のへに示す通り
、使用回数が増加しても、油煙、調理臭の浄化能力の低
下が少,なく、調理庫内壁18に附着する池脂量も従来
例2の半分以下となった。As shown in Figures 14.15 and 16.17, the experimental results show that even when the number of uses increases, the ability to purify oil smoke and cooking odors does not decrease significantly, and the amount of pond fat adhering to the inner wall 18 of the cooking chamber decreases. was also less than half that of Conventional Example 2.
実施例 4
実施例3の試験条件の中で料理温度を300℃にかえて
400℃にした。Example 4 The cooking temperature was changed from 300°C to 400°C under the test conditions of Example 3.
これにより料理時間が10分間に短縮され、高速料理が
可能となり、油煙、調理臭の発生もさらに少なくなり、
調理庫内壁18への附着も少なく調理臭もすぐに消えた
。This shortens the cooking time to 10 minutes, enabling high-speed cooking, and further reducing the generation of oil smoke and cooking odors.
There was little adhesion to the inner wall 18 of the cooking chamber, and the cooking odor quickly disappeared.
以上、本発明者等が考案した油煙除去装置の構造、製造
法、電子式電気自動オーブンへの応用実施例等について
詳細に述べたが、このような本発明では以下のような効
果がある。The structure, manufacturing method, and application example to an electronic electric automatic oven of the oil smoke removal device devised by the present inventors have been described in detail above.The present invention has the following effects.
(1) 料理物から発生する油煙、調理臭をほとんど
、長期にわたって除去できる。(1) Almost all oil smoke and cooking odors generated from cooking can be removed for a long period of time.
(2)調理庫内壁へ附着する油脂を従来に比べて半分以
下に出来る。(2) The amount of fat and oil that adheres to the inner walls of the cooking chamber can be reduced by more than half compared to conventional methods.
(3)料理温度が上げれるので、料理の巾がさらに広が
る。(3) Since the cooking temperature can be raised, the range of dishes can be further expanded.
(4)調理庫内壁の汚れを防ぎ、掃除の回数がさらに少
なくなる。(4) Prevents stains on the inner walls of the cooking chamber, further reducing the number of cleaning operations.
(5)油滴を油煙分解層で除去するので、酸化触媒の寿
命が非常に長くなる。(5) Since oil droplets are removed by the oil smoke decomposition layer, the life of the oxidation catalyst is greatly extended.
(6)浄化能を変えずに酸化触媒量を従来の半分以下に
することができる。(6) The amount of oxidation catalyst can be reduced to less than half of the conventional amount without changing the purification performance.
(力 油煙除去装置は調理庫内壁に着脱自在に装備して
いるので、保守が非常に簡単である。(The oil smoke removal device is removably installed on the inner wall of the cooking chamber, making maintenance extremely easy.
(8)酸化触媒の形状は任意に設定できる。(8) The shape of the oxidation catalyst can be set arbitrarily.
(9)従来通り調理器として正確な温度制御を行うこと
ができるので、従来の長所はそのまま生かせる。(9) Accurate temperature control can be performed as in the conventional cooker, so the advantages of the conventional cooker can be utilized as is.
Ql 完全な万能調理器と言える。Ql It can be said to be a complete all-purpose cooker.
なお、本発明は主に電子式電気自動オーブンについて説
明したが、ガスオーブン、電子レンジについても基本的
には全く同じ考えで応用可能である。Although the present invention has mainly been described with respect to an electronic electric automatic oven, it can also be applied to gas ovens and microwave ovens with the same concept.
なお前述の油煙、油滴を分解する分解層の材質として前
記のステンレス鋼の発泡体の他に、アルミニウム、ニッ
ケル、鉄、銅、亜鉛等の単体金属またはこれらの合金か
らなる連続気孔を有する発泡体またはこれら金属の繊維
状のマット状のものも本発明の目的を果すことが可能で
あり、また連続気孔を有するセラミック体も本発明の目
的を充分果すことが可能である。In addition to the stainless steel foam mentioned above, the material of the decomposition layer that decomposes the oil smoke and oil droplets may also be a foam with open pores made of a single metal such as aluminum, nickel, iron, copper, zinc, or an alloy thereof. The object of the present invention can also be achieved by a body or a fibrous mat of these metals, and a ceramic body having continuous pores can also satisfactorily achieve the object of the invention.
またこのような油煙、油滴を分解する分解層の温度は2
30〜40.0℃が好ましい。In addition, the temperature of the decomposition layer that decomposes such oil smoke and oil droplets is 2
30-40.0°C is preferred.
230℃以下であるならば、油煙、油滴が十分分解せず
、結露して、調理排ガスを閉塞するので好ましくなくま
た油煙分解層の厚みを大とする必要がある。If the temperature is below 230°C, the oil smoke and oil droplets will not be sufficiently decomposed and will condense and block the cooking exhaust gas, which is undesirable and requires a thicker oil smoke decomposition layer.
また400℃以上では油煙分解を目的とするには好まし
いが、本発明の触媒層の保温材や調理器具の安全性、調
理効果を考えると400℃以下が好ましい。Further, a temperature of 400° C. or higher is preferable for the purpose of decomposing oil smoke, but a temperature of 400° C. or lower is preferable in consideration of the safety of the heat insulating material of the catalyst layer of the present invention, cooking utensils, and cooking effectiveness.
さらにこの油煙、油滴分解層の厚みは3〜15m/mの
範囲が好ましい。Furthermore, the thickness of this oil smoke and oil droplet decomposition layer is preferably in the range of 3 to 15 m/m.
3m/m以下ではその効果が発揮し難く、また充分な効
果を得るには分解層の温度を高温に保持せねばならない
。If the thickness is less than 3 m/m, it is difficult to exhibit this effect, and in order to obtain a sufficient effect, the temperature of the decomposition layer must be maintained at a high temperature.
また15%以上の厚さは調理器具のサイズを勘案すると
厚くなり過ぎて好ましくなく15X以下で目的を果すよ
うに、分解層の多孔度を決定する必要がある。Further, a thickness of 15% or more is too thick considering the size of the cooking utensil, which is undesirable, and it is necessary to determine the porosity of the decomposition layer so that the purpose is achieved at a thickness of 15X or less.
分解層の多孔度は15〜80%程度が好ましい.この油
煙、油滴分解層は分子量の大きな油脂分を分子量の小さ
な炭化水素、炭素化合物に分解することが主目的であっ
て、その後の酸化触媒の効率を改善させることであるが
、このような目的の他にい調料理物が高温で調理される
とき一特に料理物にこげをつけるような高温での調理時
には、料理物の表面は次第に蛋白質がゲル化し、ざらに
ヒゲル化して行くが、しかし料理物の内部はなお充分の
水分と油脂物を含有するので、料理物の表面にこげのつ
く状態のとき発生する油煙、油滴は常に一定量が流れる
のでなく、小さなばく発をともなって、油脂分は表面の
コゲであるヒゲルの表面をつき破って発生するので、油
煙の量の変動は激しい。The porosity of the decomposition layer is preferably about 15 to 80%. The main purpose of this oil smoke and oil droplet decomposition layer is to decompose fats and oils with a large molecular weight into hydrocarbons and carbon compounds with a small molecular weight, and to improve the efficiency of the subsequent oxidation catalyst. In addition to the intended purpose, when delicious foods are cooked at high temperatures, especially when they are cooked at high temperatures that cause the food to burn, the surface of the food gradually becomes a gel, and the surface of the food becomes rough. However, the inside of the food still contains sufficient water and oil, so the oil smoke and oil droplets that occur when the surface of the food is scorched do not always flow in a constant amount, but are accompanied by small explosions. Since the oil and fat content is generated by breaking through the surface of the burnt surface, the amount of oil smoke fluctuates dramatically.
このためこの多孔質状の油煙油滴分解層は、この油煙量
を平均化させる目的をも果し、またその後に通過する触
媒体にできるだけ油煙が均一に接触するよう分散の役割
をもかね、さらに触媒体の組成が万一物理的なショック
により脱落を生じた場合に料理物の表面に触媒体組成が
落下するのを防ぐ目的をも兼ねるものである。Therefore, this porous oil droplet decomposition layer serves the purpose of equalizing the amount of oil smoke, and also plays a dispersing role so that the oil smoke contacts the catalyst body that passes through it as uniformly as possible. Furthermore, it also serves the purpose of preventing the catalyst composition from falling onto the surface of the food in the event that the catalyst composition falls off due to physical shock.
第1図は本発明の実施例における油煙除去装置の断面図
、第2図〜第5図は酸化触媒を示す図、第6図、第7図
は酸化触媒の製造過程を示す概略ブロック図、第8図、
第9図は第7図に示す方法による酸化触媒の注入過程を
示す断面図、第10図は従来の電子式電気自動オーブン
を示す略図、第11図はセルフクリーニング方式を採用
したオーブンの略図、第12図は第1図に示す本発明の
実施例における油煙除去装置を着脱自在に装着したオー
ブンの略図、第13図はセルフクリーニング処理を施し
た調理庫内壁に凹凸をつけて壁面積を増加させた本発明
の他の実施例におけるオーブンの略図、第14図は従来
例および本発明の実施例についての排気ガス中のHC濃
度と料理時間との関係を表したものであり、第15図は
同じく料理回数とHC浄化率との関係を表わした図、第
16図は同じく臭気指数と料理回数との関係を表わした
図、第17図は料理回数と調理庫内壁への油脂附着重量
との関係を示したものである。
1・・・・・・触媒筒、2・・・・・・油煙分解層、3
・・・・・・酸化触媒、4・・・・・・多数の細孔、5
・・・・・・通気孔、11・・・・・・調理庫内。FIG. 1 is a sectional view of an oil smoke removal device in an embodiment of the present invention, FIGS. 2 to 5 are diagrams showing an oxidation catalyst, and FIGS. 6 and 7 are schematic block diagrams showing the manufacturing process of the oxidation catalyst. Figure 8,
FIG. 9 is a cross-sectional view showing the oxidation catalyst injection process according to the method shown in FIG. 7, FIG. 10 is a schematic diagram showing a conventional electronic electric automatic oven, and FIG. 11 is a schematic diagram of an oven adopting a self-cleaning method. Fig. 12 is a schematic diagram of an oven in which the oil smoke removal device according to the embodiment of the present invention shown in Fig. 1 is removably attached, and Fig. 13 is a self-cleaning inner wall of the cooking chamber that is roughened to increase the wall area. FIG. 14 is a schematic diagram of an oven according to another embodiment of the present invention, and FIG. Figure 16 is a diagram showing the relationship between the number of times of cooking and the HC purification rate, Figure 16 is a diagram showing the relationship between the odor index and the number of times of cooking, and Figure 17 is the relationship between the number of times of cooking and the weight of fats and oils attached to the inner walls of the cooking chamber. This shows the relationship between 1... Catalyst tube, 2... Oil smoke decomposition layer, 3
...oxidation catalyst, 4... many pores, 5
...Vent, 11...Inside the cooking cabinet.
Claims (1)
解層の下流に設けた多数の細孔をもつ二酸化マンガンを
主成分とした酸化触媒層とからなる油煙除去装置を調理
庫内に着脱自在に装備してなる油煙除去装置を備えた調
理器。1. An oil smoke removal device consisting of an oil smoke decomposition layer that decomposes oil smoke and oil droplets, and an oxidation catalyst layer containing manganese dioxide as a main component and having a large number of pores provided downstream of this oil smoke decomposition layer is installed and removed in the cooking cabinet. A cooking appliance equipped with a smoke removal device that can be freely equipped.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50101398A JPS5813817B2 (en) | 1975-08-20 | 1975-08-20 | Cooker equipped with a smoke removal device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50101398A JPS5813817B2 (en) | 1975-08-20 | 1975-08-20 | Cooker equipped with a smoke removal device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5224771A JPS5224771A (en) | 1977-02-24 |
JPS5813817B2 true JPS5813817B2 (en) | 1983-03-16 |
Family
ID=14299618
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50101398A Expired JPS5813817B2 (en) | 1975-08-20 | 1975-08-20 | Cooker equipped with a smoke removal device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5813817B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0233928Y2 (en) * | 1984-02-18 | 1990-09-12 |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58136905A (en) * | 1982-02-08 | 1983-08-15 | Matsushita Electric Ind Co Ltd | Burner |
JP4994352B2 (en) * | 2008-12-12 | 2012-08-08 | 三菱電機株式会社 | Heating cooker and induction heating cooker having this heating cooker |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2940835A (en) * | 1957-05-01 | 1960-06-14 | Philco Corp | Apparatus for removing smoke and odors from domestic cooking vapors |
JPS4834766A (en) * | 1971-09-09 | 1973-05-22 | ||
JPS4955883A (en) * | 1972-10-06 | 1974-05-30 | ||
JPS501901U (en) * | 1973-05-02 | 1975-01-10 |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4842140U (en) * | 1971-09-18 | 1973-05-30 | ||
JPS4920827U (en) * | 1972-05-23 | 1974-02-21 | ||
JPS4964542U (en) * | 1972-09-18 | 1974-06-06 | ||
JPS49132240U (en) * | 1973-03-19 | 1974-11-13 | ||
JPS5145749Y2 (en) * | 1973-05-31 | 1976-11-05 |
-
1975
- 1975-08-20 JP JP50101398A patent/JPS5813817B2/en not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2940835A (en) * | 1957-05-01 | 1960-06-14 | Philco Corp | Apparatus for removing smoke and odors from domestic cooking vapors |
JPS4834766A (en) * | 1971-09-09 | 1973-05-22 | ||
JPS4955883A (en) * | 1972-10-06 | 1974-05-30 | ||
JPS501901U (en) * | 1973-05-02 | 1975-01-10 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0233928Y2 (en) * | 1984-02-18 | 1990-09-12 |
Also Published As
Publication number | Publication date |
---|---|
JPS5224771A (en) | 1977-02-24 |
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