JP2017125657A - Heating cooker - Google Patents

Heating cooker Download PDF

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JP2017125657A
JP2017125657A JP2016005684A JP2016005684A JP2017125657A JP 2017125657 A JP2017125657 A JP 2017125657A JP 2016005684 A JP2016005684 A JP 2016005684A JP 2016005684 A JP2016005684 A JP 2016005684A JP 2017125657 A JP2017125657 A JP 2017125657A
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exhaust gas
heat exchanger
exhaust
cooking
water
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富田 英夫
Hideo Tomita
英夫 富田
誠 澁谷
Makoto Shibuya
誠 澁谷
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Panasonic Intellectual Property Management Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a heating cooker that comprises a dissolution type heat exchanger and facilitates the replacement of a liquid medium.SOLUTION: A heating cooker comprises: a cooking container provided with heating means for heating food to be cooked; a dissolution type heat exchanger 3 for storing a liquid medium, and for treating exhaust gas through the liquid medium; a first exhaust passage 13 connected to the cooking container and the dissolution type heat exchanger 3, and for conveying exhaust gas; a second exhaust passage 18 connected to the dissolution type heat exchanger 3, and for conveying exhaust gas treated in the dissolution type heat exchanger 3 downstream from the dissolution type heat exchanger 3; gas transfer means 19 for transferring exhaust gas; and exhaust gas cooling means 4 for cooling the first exhaust passage 13.SELECTED DRAWING: Figure 5

Description

本発明は、一般家庭の台所や業務用の厨房等で使用される加熱調理機器の排熱処理に関するものである。   The present invention relates to waste heat treatment of a cooking device used in a general household kitchen or a commercial kitchen.

従来の加熱調理機器において、加熱調理機器で発生した蒸気を復水して回収する構成のものが提案されている(例えば、特許文献1参照)。特許文献1に記載されている加熱調理機器は、被加熱物が入れられる内鍋と、内鍋を収納する容器カバー及び内鍋を加熱する加熱装置を備えた本体と、内鍋を開閉自在に覆う内蓋と、本体を開閉自在に覆い、内蓋が着脱自在に装着される外蓋と、外蓋又は内蓋の内鍋側に設けられ、加熱装置による加熱動作中に被加熱物から発生するおねば成分を貯留し、内鍋に戻すおねば戻し部と、おねば戻し部の下流側でおねば戻し部と連通するように外蓋に設けられ、加熱装置による加熱動作中に被加熱物から発生する蒸気を外部又は本体内に収容されている水槽に導く蒸気導管部と、蒸気導管部の外周部に設けられ、蒸気導管部内を導通する蒸気から吸熱する蓄熱剤とから構成されている。   In the conventional cooking device, the thing of the structure which condenses and collect | recovers the vapor | steam generate | occur | produced with the cooking device is proposed (for example, refer patent document 1). The cooking device described in Patent Document 1 includes an inner pot in which an object to be heated is placed, a container cover that houses the inner pot, a main body that includes a heating device that heats the inner pot, and an inner pot that can be opened and closed freely. Covered with an inner lid, an outer lid that covers the main body so that it can be opened and closed, and an inner lid that is detachably mounted, and is provided on the inner lid side of the outer lid or the inner lid. It is provided on the outer lid so as to store the tobacco component to be stored and return to the inner pot, and to the tobacco return unit downstream of the tobacco return unit, and is heated during the heating operation by the heating device. A steam conduit portion that guides the steam generated from the product to the outside or the water tank accommodated in the main body, and a heat storage agent that is provided on the outer periphery of the steam conduit portion and absorbs heat from the steam conducted through the steam conduit portion. Yes.

上記構成において動作を説明すると、加熱装置が内鍋を加熱すると、内鍋内に封入された水などの液体が沸騰し、蒸気が発生する。この蒸気は、おねば戻し部に流入する。次に、おねば戻し部に流入した蒸気は、おねば戻し部と連結されている蒸気導管部を導通する。続いて、蒸気導管部を導通した蒸気は、水槽に封入された水の中まで誘導され、この水によって冷却されて凝縮する。そして、蒸気が冷却される際、蒸気の潜熱は水槽の水に吸熱され、水槽内の水の温度は蒸気凝縮量に応じて上昇する。また、蓄熱剤により吸熱された蒸気の一部は、凝縮されて復水することになる。   In the above configuration, the operation will be described. When the heating device heats the inner pot, a liquid such as water enclosed in the inner pot boils and steam is generated. This steam flows into the return part. Next, the steam that has flowed into the stick return part conducts through the steam conduit part connected to the stick return part. Subsequently, the steam that has passed through the steam conduit is guided into the water sealed in the water tank, and is cooled and condensed by the water. When the steam is cooled, the latent heat of the steam is absorbed by the water in the water tank, and the temperature of the water in the water tank rises according to the amount of steam condensation. A part of the steam absorbed by the heat storage agent is condensed and condensed.

特開2014−111218号公報JP 2014-1111218 A

しかしながら、前記従来の加熱調理機器では、水槽に封入された水は蒸気凝縮量に応じての温度上昇を考慮すると、大量の水量が必要になるという課題を有していた。例えば、加熱調理機器が炊飯器の場合、水槽の水は1L前後必要になり、多くの水が必要となり、水槽の容積が大きくなるとともに水槽の重量が重くなる。よって、水槽を収納する炊飯器本体の容積が必然的に大きくなるとともに、水槽内の水を入れ替える際に、重い水槽を取り扱う必要性があるという課題を有していた。   However, the conventional cooking device has a problem that a large amount of water is required for the water sealed in the water tank in consideration of a temperature rise according to the amount of steam condensation. For example, when the cooking device is a rice cooker, about 1 L of water is required in the aquarium, a lot of water is required, and the volume of the aquarium increases and the weight of the aquarium increases. Therefore, while the volume of the rice cooker main body which accommodates an aquarium inevitably becomes large, when replacing the water in an aquarium, it had the subject that it was necessary to handle a heavy aquarium.

本発明は、上記従来の課題を解決するもので、加熱調理機器で発生した排気ガスを液状媒体で冷却する事前に冷却することにより、液状媒体を貯留する溶解式熱交換器を軽量とする加熱調理機器を提供することを目的とする。   The present invention solves the above-described conventional problems, and heats the melting heat exchanger that stores the liquid medium by reducing the weight by cooling the exhaust gas generated in the cooking device with the liquid medium in advance. The purpose is to provide cooking equipment.

上記目的を達成するために本発明の加熱調理機器は、
調理食材を加熱する加熱手段を設けた調理容器と、
液状媒体を貯留し、液状媒体を介して排気ガスを冷却処理する溶解式熱交換器と、
調理容器と溶解式熱交換器に接続され、調理容器から溶解式熱交換器へ排気ガスを搬送させる第一の排気路と、
溶解式熱交換器に接続され、溶解式熱交換器内で処理された排気ガスを溶解式熱交換器の下流へ搬送させる第二の排気路と、
排気ガスを移送するガス移送手段と、を備え、
第一の排気路を冷却する排気ガス冷却手段を有するものである。
In order to achieve the above object, the cooking device of the present invention comprises:
A cooking container provided with a heating means for heating the cooking ingredients;
A melting heat exchanger for storing a liquid medium and cooling the exhaust gas through the liquid medium;
A first exhaust passage connected to the cooking vessel and the melting heat exchanger, and carrying exhaust gas from the cooking vessel to the melting heat exchanger;
A second exhaust passage connected to the melting heat exchanger and transporting the exhaust gas treated in the melting heat exchanger downstream of the melting heat exchanger;
Gas transfer means for transferring exhaust gas, and
An exhaust gas cooling means for cooling the first exhaust passage is provided.

加熱手段が調理食材を加熱すると、水蒸気、油、臭気成分などを含んだ排気ガスが発生する。続いて、ガス移送手段が排気ガスを調理容器から第一の排気路を経由して溶解式熱交換器へ移送する。その際、排気ガス冷却手段が第一の排気路を通過する排気ガスを第一の排気路壁を介して冷却し、温度低下した排気ガスが溶解式熱交換器に流入するので、溶解式熱交換器は軽量の樹脂を使用できる。そして、排気ガスは直接接触した液状媒体によって冷却されて、温度低下した排気ガスは含まれる水蒸気、油を凝縮し、かつ水溶性の臭気成分と共に液状媒体に溶解するので、排気ガスは低温の浄化ガスになり、浄化ガスはガス移送手段により第二の排気路を経由して排出される。ただし、液状媒体は、水蒸気や油の凝縮した量だけ増量し、かつ油や臭気成分が溶解すると、溶解能力が低下するので、調理後、液状媒体の入替が必要になる。   When the heating means heats the cooked food, exhaust gas containing water vapor, oil, odor components and the like is generated. Subsequently, the gas transfer means transfers the exhaust gas from the cooking container to the melting heat exchanger via the first exhaust path. At that time, the exhaust gas cooling means cools the exhaust gas passing through the first exhaust passage through the first exhaust passage wall, and the exhaust gas whose temperature has decreased flows into the melting heat exchanger. The exchanger can use lightweight resin. The exhaust gas is cooled by the liquid medium that is in direct contact, and the exhaust gas whose temperature has been reduced condenses the water vapor and oil contained therein and dissolves in the liquid medium together with water-soluble odor components. The purified gas is discharged via the second exhaust path by the gas transfer means. However, the liquid medium is increased by the amount of water vapor or oil condensed, and when the oil or odor component is dissolved, the dissolving ability is lowered. Therefore, the liquid medium needs to be replaced after cooking.

調理中、液状媒体は排気ガスから熱、特に潜熱を奪うので、温度上昇し、液状媒体は主に水蒸気の凝縮分増加する。他方、排気ガス冷却手段が排気ガスを冷却するので、液状媒体の温度上昇は抑えられる分、液状媒体の所定貯留量は沸騰の可能性のない量まで少なくでき、省資源が図れる。したがって、溶解式熱交換器が軽くなるので、液状媒体の入替は容易になる。   During cooking, the liquid medium takes heat, particularly latent heat, from the exhaust gas, so the temperature rises and the liquid medium mainly increases the condensation of water vapor. On the other hand, since the exhaust gas cooling means cools the exhaust gas, the amount of liquid medium stored can be reduced to an amount where there is no possibility of boiling because the temperature rise of the liquid medium can be suppressed, thereby saving resources. Therefore, since the melting type heat exchanger becomes light, replacement of the liquid medium is facilitated.

本発明の加熱調理機器は、加熱調理機器で発生した排気ガスを、液状媒体を貯留して冷却処理する溶解式熱交換器を軽量とすることができる。   The cooking device of the present invention can reduce the weight of the melting heat exchanger that stores the liquid medium and cools the exhaust gas generated by the cooking device.

本発明の実施の形態1における加熱調理機器を示した斜視図The perspective view which showed the heating cooking appliance in Embodiment 1 of this invention 本発明の実施の形態1における加熱調理機器の誘導加熱調理器などを除いた後方から見た部分断面斜視図The partial cross section perspective view seen from the back except the induction heating cooking appliance etc. of the heating cooking appliance in Embodiment 1 of this invention 本発明の実施の形態1における加熱調理機器の調理容器を示した断面図Sectional drawing which showed the cooking container of the heating cooking appliance in Embodiment 1 of this invention 本発明の実施の形態1における加熱調理機器の溶解式熱交換器を示した断面図Sectional drawing which showed the melting-type heat exchanger of the heating cooking appliance in Embodiment 1 of this invention 本発明の実施の形態1における加熱調理機器の溶解式熱交換器と排気ガス冷却手段とガス移送手段の位置関係を示す断面図Sectional drawing which shows the positional relationship of the melt | dissolution heat exchanger of the heating cooking appliance in Embodiment 1 of this invention, an exhaust-gas cooling means, and a gas transfer means.

第1の発明は、調理食材を加熱する加熱手段を設けた調理容器と、
液状媒体を貯留し、液状媒体を介して排気ガスを冷却処理する溶解式熱交換器と、
前記調理容器と前記溶解式熱交換器に接続され、前記調理容器から前記溶解式熱交換器へ排気ガスを搬送させる第一の排気路と、
前記溶解式熱交換器に接続され、前記溶解式熱交換器内で処理された排気ガスを前記溶解式熱交換器の下流へ搬送させる第二の排気路と、
排気ガスを移送するガス移送手段と、を備え、
前記第一の排気路を冷却する排気ガス冷却手段を有するものである。
1st invention has the cooking container provided with the heating means which heats cooking ingredients,
A melting heat exchanger for storing a liquid medium and cooling the exhaust gas through the liquid medium;
A first exhaust passage connected to the cooking vessel and the melting heat exchanger, for transporting exhaust gas from the cooking vessel to the melting heat exchanger;
A second exhaust path connected to the melting heat exchanger and transporting the exhaust gas treated in the melting heat exchanger downstream of the melting heat exchanger;
Gas transfer means for transferring exhaust gas, and
Exhaust gas cooling means for cooling the first exhaust passage is provided.

このような発明によって、加熱手段が調理容器内を加熱すると、調理食材が温度上昇して水蒸気、油、臭気成分などを含んだ排気ガスが発生する。続いて、ガス移送手段が排気ガスを調理容器から第一の排気路を経由して溶解式熱交換器へ移送する。その際、排気ガス冷却手段が第一の排気路を通過する排気ガスを第一の排気路壁を介して冷却し、温度低
下した排気ガスが溶解式熱交換器に流入するので、溶解式熱交換器は金属より低価格で軽量の樹脂を使える。特に、透明樹脂を使えば、溶解式熱交換器の中身をチェックできる。そして、排気ガスは直接接触した液状媒体によって冷却されて、温度低下した排気ガスは含まれる水蒸気、油を凝縮し、かつ水溶性の臭気成分と共に液状媒体に溶解する。すなわち、溶解式熱交換器は、排気ガスに対して冷却、除湿、除煙、脱臭などの排熱処理を行うので、排気ガスは低温の浄化ガスになり、浄化ガスはガス移送手段により第二の排気路を経由して排出される。ただし、液状媒体は、水蒸気や油の凝縮した量だけ増量し、かつ油や臭気成分が溶解すると、溶解能力が低下する。その後、溶解式熱交換器内に油が付着して汚れ、更に液状媒体、溶解式熱交換器内に菌やかびが発生し、かつ臭気が発生するので、調理後、液状媒体の入替と溶解式熱交換器の清掃が必要になる。
According to such an invention, when the heating means heats the inside of the cooking container, the temperature of the cooking food rises and exhaust gas containing water vapor, oil, odor components and the like is generated. Subsequently, the gas transfer means transfers the exhaust gas from the cooking container to the melting heat exchanger via the first exhaust path. At that time, the exhaust gas cooling means cools the exhaust gas passing through the first exhaust passage through the first exhaust passage wall, and the exhaust gas whose temperature has decreased flows into the melting heat exchanger. The exchanger can be made of lightweight resin at a lower price than metal. In particular, if a transparent resin is used, the contents of the melting heat exchanger can be checked. The exhaust gas is cooled by the liquid medium in direct contact with it, and the exhaust gas whose temperature has been reduced condenses the water vapor and oil contained therein and dissolves in the liquid medium together with water-soluble odor components. That is, the melting heat exchanger performs exhaust heat treatment such as cooling, dehumidification, smoke removal, and deodorization on the exhaust gas, so that the exhaust gas becomes a low-temperature purified gas, and the purified gas is converted into a second gas by the gas transfer means. It is discharged via the exhaust path. However, if the liquid medium is increased by the amount of water vapor or oil condensed, and the oil or odor component is dissolved, the dissolving ability is lowered. After that, oil adheres to the melting heat exchanger and becomes dirty, and further, the liquid medium, fungi and fungi are generated in the melting heat exchanger, and odor is generated. After cooking, replacement and dissolution of the liquid medium Cleaning of the heat exchanger is necessary.

調理中、液状媒体は排気ガスから熱、特に潜熱を奪うので、温度上昇し、液状媒体は主に水蒸気の凝縮分増加する。他方、排気ガス冷却手段が排気ガスを冷却するので、液状媒体の温度上昇は抑えられる分、液状媒体の所定貯留量は沸騰の可能性のない量まで少なくでき、省資源が図れる。したがって、溶解式熱交換器が軽くなるので、液状媒体の入替は容易になる。   During cooking, the liquid medium takes heat, particularly latent heat, from the exhaust gas, so the temperature rises and the liquid medium mainly increases the condensation of water vapor. On the other hand, since the exhaust gas cooling means cools the exhaust gas, the amount of liquid medium stored can be reduced to an amount where there is no possibility of boiling because the temperature rise of the liquid medium can be suppressed, thereby saving resources. Therefore, since the melting type heat exchanger becomes light, replacement of the liquid medium is facilitated.

第2の発明は、特に、第1の発明の前記排気ガス冷却手段は、少なくとも前記第一の排気路の一部を前記第二の排気路の一部で冷却する構成するものである。   In the second invention, in particular, the exhaust gas cooling means of the first invention is configured to cool at least a part of the first exhaust path with a part of the second exhaust path.

溶解式熱交換器から第二の排気路へ流入する浄化ガスは、ほぼ飽和状態である。第二の排気路を流れる浄化ガスは、第一の排気路を通過する排気ガスから熱を奪うので、浄化ガスは温度上昇して相対湿度を低下させる。この分、第二の排気路から排出される浄化ガスは外気により冷却されるが、浄化ガスの相対湿度は露点まで下がらないので、湯気が発生せず、台所が水滴で汚れることはない。   The purified gas flowing into the second exhaust path from the melting heat exchanger is almost saturated. Since the purified gas flowing through the second exhaust passage takes heat from the exhaust gas passing through the first exhaust passage, the purified gas rises in temperature and lowers the relative humidity. Accordingly, the purified gas discharged from the second exhaust path is cooled by the outside air, but the relative humidity of the purified gas does not drop to the dew point, so no steam is generated and the kitchen is not contaminated with water droplets.

第3の発明は、特に、第1または第2の発明の前記排気ガス冷却手段は、前記第一の排気路の一部と前記第二の排気路の一部を近接設置したことにより、第二の排気路の一部を通過する浄化ガスは第一の排気路の外壁に沿って流れるので、第一の排気路の一部を通過する排気ガスを十分に冷却できる。   According to a third aspect of the invention, in particular, the exhaust gas cooling means according to the first or second aspect of the invention is characterized in that a part of the first exhaust path and a part of the second exhaust path are installed close to each other. Since the purified gas passing through a part of the second exhaust path flows along the outer wall of the first exhaust path, the exhaust gas passing through a part of the first exhaust path can be sufficiently cooled.

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、この実施の形態によって本発明が限定されるものではない。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the embodiments.

(実施の形態1)
図1は本発明の実施の形態1における加熱調理機器を示した斜視図、図2は同加熱調理機器の誘導加熱調理器などを除いた後方から見た部分断面斜視図、図3は同加熱調理機器のグリルを示した断面図、図4は同加熱調理機器の溶解式熱交換器を示した断面図、図5は同加熱調理機器の溶解式熱交換器と排気ガス冷却手段とガス移送手段の位置関係を示す断面図である。
(Embodiment 1)
1 is a perspective view showing a cooking device according to Embodiment 1 of the present invention, FIG. 2 is a partially sectional perspective view seen from the rear, excluding an induction cooking device of the cooking device, and FIG. FIG. 4 is a sectional view showing a melting heat exchanger of the cooking device, FIG. 5 is a melting heat exchanger, exhaust gas cooling means, and gas transfer of the cooking device. It is sectional drawing which shows the positional relationship of a means.

図1〜図5に示すように、加熱調理機器1は、誘導加熱調理器(図示せず)とグリル2と溶解式熱交換器3及び二重管式の排気ガス冷却手段4を筐体5に挿入してトッププレート6で蓋をし、キッチンキャビネットに組み込まれている。   As shown in FIGS. 1 to 5, the cooking device 1 includes an induction heating cooker (not shown), a grill 2, a melting heat exchanger 3, and a double-pipe exhaust gas cooling means 4. It is inserted into and covered with a top plate 6 and incorporated in the kitchen cabinet.

図3に示すように、グリル2は、前方から後方へ略立方体に形成した調理食材を入れる調理容器7と、調理容器7内に配置した耐熱ガラス製のグリル床8と、グリル床8に載置するフッ素を塗布したアルミ製或いは鉄製のグリル皿9と、調理容器7内の上下に配置して調理食材を加熱する遠赤管ヒータからなる加熱手段10と、筐体5前方に配置した開閉自在のドア11とから構成される。   As shown in FIG. 3, the grill 2 is mounted on a cooking container 7 for storing cooking ingredients formed in a substantially cube from the front to the rear, a grill floor 8 made of heat-resistant glass disposed in the cooking container 7, and the grill floor 8. An aluminum or iron grill pan 9 coated with fluorine, a heating means 10 comprising a far-infrared tube heater disposed above and below the cooking container 7 to heat the cooking ingredients, and an open / close disposed in front of the housing 5 It is composed of a free door 11.

調理容器7と溶解式熱交換器3に接続され、調理容器7から溶解式熱交換器3へ排気ガスを搬送させる第一の排気路13を有している。   It has a first exhaust passage 13 that is connected to the cooking container 7 and the melting heat exchanger 3 and conveys the exhaust gas from the cooking container 7 to the melting heat exchanger 3.

図4に示すように、溶解式熱交換器3は、液状媒体を貯留し、液状媒体を介して排気ガスを処理する構成である。溶解式熱交換器3は、液状媒体としての水を200cc〜700cc(中型さんま10尾の場合、所定水量500cc)を貯水し、上部に空間を有する処理容器12と、調理容器7内に連通した第一の排気路13に結合し水内に排気ガスを噴出するガス噴出部14と、水表面より上方に設けたガス排出部15とから構成し、かつ水を冷却する液状媒体冷却手段16を組み込んでいる。ガス噴出部14はダクト形状で形成され、ガス噴出部14の上流端は水表面より上方で第一の排気路13と結合し、ガス噴出部14の下流端は処理容器12の底面近傍にガス噴出口17を開口している。ガス排出部15は、筐体5の後方内に開放した第二の排気路18と結合しており、排気ガスを溶解式熱交換器3から第二の排気路18に排気する。第二の排気路18は、溶解式熱交換器3に接続され、溶解式熱交換器3内で処理された排気ガスを溶解式熱交換器3の下流に搬送させることとなる。   As shown in FIG. 4, the melting heat exchanger 3 is configured to store a liquid medium and process exhaust gas through the liquid medium. The melting heat exchanger 3 stores 200 cc to 700 cc of water as a liquid medium (predetermined amount of water 500 cc in the case of 10 medium-sized samama), and communicates with the processing container 12 having a space in the upper portion and the cooking container 7. A liquid medium cooling means 16 that is composed of a gas ejection section 14 that is coupled to the first exhaust path 13 and ejects exhaust gas into water and a gas discharge section 15 provided above the water surface and that cools water. Incorporated. The gas ejection part 14 is formed in a duct shape, the upstream end of the gas ejection part 14 is connected to the first exhaust path 13 above the water surface, and the downstream end of the gas ejection part 14 is a gas near the bottom surface of the processing vessel 12. The spout 17 is opened. The gas discharge unit 15 is connected to a second exhaust path 18 opened in the rear of the housing 5, and exhausts exhaust gas from the melting heat exchanger 3 to the second exhaust path 18. The second exhaust path 18 is connected to the melting type heat exchanger 3, and the exhaust gas processed in the melting type heat exchanger 3 is conveyed downstream of the melting type heat exchanger 3.

また、カバー24が、ガス排出部15の入口前に間隙を有して設けられている。そして、Oリング等のシール部材を備えた嵌合部25は、第一の排気路13とガス噴出部14、ガス排出部15と誘引管23をそれぞれ着脱自在に結合し、かつ水表面より上方に位置している。なお、扉38を外した後、溶解式熱交換器3を構成する処理容器12は、嵌合部25により第一の排気路13と誘引管23から取外すことが可能となり、着脱自在の構成であり、処理容器12内に貯留した水を排水できる。   Further, the cover 24 is provided with a gap before the inlet of the gas discharge unit 15. And the fitting part 25 provided with sealing members, such as an O-ring, detachably couples the first exhaust passage 13 and the gas ejection part 14, the gas exhaust part 15 and the induction pipe 23, and is above the water surface. Is located. In addition, after removing the door 38, the processing vessel 12 constituting the melting heat exchanger 3 can be detached from the first exhaust passage 13 and the induction pipe 23 by the fitting portion 25, and has a detachable configuration. Yes, the water stored in the processing container 12 can be drained.

液状媒体冷却手段16は、ダクト形状の外気噴出部26で形成され、外気噴出部26の上流端は水表面より上方で溶解式熱交換器3の外部(筐体5内)と連通した(臨ました)外気口27を開口するとともに、外気噴出部26の下流端は処理容器12の底面近傍に外気噴出口28を開口している。したがって、外気噴出部26は、水内に外気を噴出することとなる。   The liquid medium cooling means 16 is formed by a duct-shaped outside air ejection portion 26, and the upstream end of the outside air ejection portion 26 communicates with the outside of the melting heat exchanger 3 (inside the casing 5) above the water surface (in front). The outside air outlet 27 is opened, and the downstream end of the outside air ejection portion 26 opens an outside air outlet 28 near the bottom surface of the processing container 12. Therefore, the outside air ejection part 26 will eject outside air into the water.

気泡板29は、ガス噴出口17と外気噴出口28との上方近傍に配置し、多数、分散して気泡口30(例えばφ1〜4)を開口している。また、仕切り板31は、処理容器12の底面と気泡板29とで挟まれた空間を、排気ガスと外気が混合しないように二分するように立設している。   The bubble plate 29 is disposed in the vicinity of the upper side of the gas jet port 17 and the outside air jet port 28, and is dispersed in large numbers to open the bubble ports 30 (for example, φ1 to φ4). Further, the partition plate 31 is erected so as to bisect the space sandwiched between the bottom surface of the processing container 12 and the bubble plate 29 so that the exhaust gas and the outside air are not mixed.

図5に示すように、排気ガスを移送するエジェクターであるガス移送手段19は、送風機20と、送風機20の吐出口に接続され、駆動用空気を絞り流速を高めるためのノズル21と、ノズル21から駆動用空気が噴出されるチェンバー22と、ガス排出部15とチェンバー22とをつなぐ誘引管23とから構成されている。なお、チェンバー22と誘引管23とは、第二の排気路18の一部である。したがって、ガス移送手段19は第二の排気路18に配置されていることになる。   As shown in FIG. 5, the gas transfer means 19 which is an ejector for transferring exhaust gas is connected to a blower 20, a discharge port of the blower 20, a nozzle 21 for reducing drive air and increasing a flow velocity, and a nozzle 21 And the induction tube 23 connecting the gas discharge part 15 and the chamber 22 to each other. The chamber 22 and the induction tube 23 are part of the second exhaust path 18. Therefore, the gas transfer means 19 is disposed in the second exhaust path 18.

排気ガス冷却手段4は、第一の排気路13の一部である円筒形状の放熱路32の外面を囲むように、第二の排気路18の一部であるリング形状の冷却路33を設けている。放熱路32と冷却路33とは、近接配置され、放熱路32を構成する外管は冷却路33を構成する内管と共用された二重管構成とし、冷却路33の両端には夫々冷却路入口34と冷却路出口35を開口している。また、チェンバー22の下流は第二の排気路18を介して冷却路入口34に接続している。なお、放熱路32には、熱伝達促進板36(例えば、長い板をリボンのようにねじった形状)を内蔵している。   The exhaust gas cooling means 4 is provided with a ring-shaped cooling path 33 which is a part of the second exhaust path 18 so as to surround the outer surface of the cylindrical heat radiation path 32 which is a part of the first exhaust path 13. ing. The heat radiation path 32 and the cooling path 33 are arranged close to each other, and the outer pipe constituting the heat radiation path 32 has a double pipe structure shared with the inner pipe constituting the cooling path 33, and cooling is performed at both ends of the cooling path 33. A passage inlet 34 and a cooling passage outlet 35 are opened. Further, the downstream side of the chamber 22 is connected to the cooling path inlet 34 via the second exhaust path 18. The heat radiation path 32 incorporates a heat transfer promotion plate 36 (for example, a shape obtained by twisting a long plate like a ribbon).

筐体5は、前面に吸引口37を多数開口し、また脱着自在の扉38を設けている。トッププレート6は、結晶化ガラスを素材として加熱調理機器1の上面に設け、鍋などの加熱容器(図示せず)を載置する。また、トッププレート6の後方と筐体5との間隙に排気口(図示せず)を形成し、かつ冷却路出口35を臨ませている。   The housing 5 has a large number of suction ports 37 on the front surface, and is provided with a detachable door 38. The top plate 6 is provided on the upper surface of the cooking device 1 using crystallized glass as a material, and a heating container (not shown) such as a pan is placed on the top plate 6. Further, an exhaust port (not shown) is formed in the gap between the rear side of the top plate 6 and the housing 5, and the cooling path outlet 35 is exposed.

制御部(図示せず)は、加熱手段10と送風機20とを制御する。   The control unit (not shown) controls the heating unit 10 and the blower 20.

以上のように構成された加熱調理機器1の動作について説明する。
図1および図3に示すように、まず、使用者は魚などの調理食材(図示せず)を置いたグリル皿9を、ドア11を開けてグリル床8に置き、その後ドア11を閉じる。また、使用者は加熱調理機器1の扉38を開け、溶解式熱交換器3における処理容器12を引き抜き、処理容器12内に所定量の常温の水を貯留し、処理容器12を押し込むことで、加熱調理機器1に処理容器12を装着する。また、使用者は入力手段である操作スイッチ(図示せず)を操作して加熱を指示する。
The operation of the cooking device 1 configured as described above will be described.
As shown in FIGS. 1 and 3, first, the user opens the door 11 on the grill pan 9 on which cooking ingredients (not shown) such as fish are placed, places the grill pan 8 on the grill floor 8, and then closes the door 11. Further, the user opens the door 38 of the cooking device 1, pulls out the processing container 12 in the melting heat exchanger 3, stores a predetermined amount of room temperature water in the processing container 12, and pushes the processing container 12. The processing container 12 is attached to the cooking device 1. Further, the user operates an operation switch (not shown) as input means to instruct heating.

次に、操作スイッチからの指示により制御部は、加熱手段10と送風機20を適宜通電する。上方の加熱手段10は、遠赤管ヒータからの輻射が直接、または調理容器7内壁での反射により調理食材の上面を焼く。下方の加熱手段10の遠赤管ヒータからの輻射が直接、または調理容器7内壁で反射して、次にグリル床8を通過して、グリル皿9の下面を加熱する。続いて、温度上昇したグリル皿9は、調理食材の下面を熱伝導により焼く。   Next, according to an instruction from the operation switch, the control unit appropriately energizes the heating unit 10 and the blower 20. The upper heating means 10 burns the upper surface of the cooking ingredients directly from the radiation from the far-red tube heater or by reflection on the inner wall of the cooking vessel 7. Radiation from the far-red tube heater of the lower heating means 10 is reflected directly or by the inner wall of the cooking vessel 7 and then passes through the grill floor 8 to heat the lower surface of the grill pan 9. Subsequently, the grill pan 9 whose temperature has risen burns the lower surface of the cooked food material by heat conduction.

例えば、調理食材が塩さんまの場合、制御部は送風機20の駆動を開始し、加熱手段10が塩さんまの上下表面を焼く。同時に、制御部は調理容器7に配された温度センサ(図示せず)の温度変化や所定温度到達時間などから塩さんまの数(熱容量)を推定し、塩さんまが焼き上がる焼き時間を決定する。その後、制御部は、決定した焼き時間が経過すると、加熱手段10を停止する。   For example, when the cooked food is sansan, the control unit starts driving the blower 20 and the heating means 10 burns the upper and lower surfaces of the sansan. At the same time, the control unit estimates the number (heat capacity) of salted sesame from the temperature change of a temperature sensor (not shown) arranged in the cooking container 7 or the predetermined temperature arrival time, and determines the baking time for simmering the salted sesame. . Thereafter, the control unit stops the heating means 10 when the determined baking time has elapsed.

また、加熱調理中、調理容器7内は200〜300℃程度に温度上昇し、その際に対流による加熱も加わり塩さんまも温度上昇して、塩さんまから水蒸気、油、臭気成分などが発生する。さらに、水蒸気や油などが上方の加熱手段10とグリル皿9に加熱され、かつ先の対流にも加熱されて、過熱蒸気、油蒸気、調理容器7の隙間などから流入する空気を含む排気ガス(太い黒矢印)が生成する。   Further, during cooking, the temperature in the cooking container 7 rises to about 200 to 300 ° C. At that time, heating by convection is also added, and the temperature of the salt is also raised, and steam, oil, odor components, etc. are generated from the salt. . Further, steam, oil, etc. are heated by the upper heating means 10 and grill pan 9 and also heated by the previous convection, and include exhaust gas containing superheated steam, oil vapor, and air flowing in from the gap between the cooking containers 7 and the like. (Thick black arrow) is generated.

他方、送風機20は図1、図2および図5に示すように、筐体5の前面に開口した吸引口37から外気(細い黒矢印)を筐体5内に吸引後、送風機20から駆動空気としてノズル21に吐出する(例えば、50〜200L/分)。駆動空気はノズル21で絞られて速度を速めてチェンバー22に噴出されると、チェンバー22内は負圧になる。この負圧による吸引作用(エジェクター効果)により、調理容器7内の排気ガス(例えば、10〜30L/分)は、第一の排気路13に流入し、排気ガス冷却手段4内の放熱路32、溶解式熱交換器3、ガス移送手段19、第二の排気路18、冷却路33の順に通って冷却路出口35から排出され、最後に排気口(図示せず)から外部へ排気される。   On the other hand, as shown in FIGS. 1, 2, and 5, the blower 20 sucks outside air (thin black arrows) from the suction port 37 opened in the front surface of the housing 5 into the housing 5, and then drives air from the blower 20. To the nozzle 21 (for example, 50 to 200 L / min). When the driving air is squeezed by the nozzle 21 to increase the speed and is ejected to the chamber 22, the inside of the chamber 22 becomes negative pressure. Due to this negative pressure suction action (ejector effect), the exhaust gas (for example, 10 to 30 L / min) in the cooking vessel 7 flows into the first exhaust path 13 and the heat dissipation path 32 in the exhaust gas cooling means 4. The melt heat exchanger 3, the gas transfer means 19, the second exhaust path 18, and the cooling path 33 are sequentially discharged from the cooling path outlet 35, and finally exhausted from the exhaust port (not shown) to the outside. .

放熱路32では、排気ガスが熱伝達促進板36により乱されて熱伝達率が向上し、かつ放熱路32の内壁に沿って流れる。冷却路33では、後述する浄化ガス(処理容器12の水とほぼ同温)が冷却路33を流れ、かつ放熱路32の外壁に沿って流れる。したがって、冷却路33を流れる浄化ガスは、放熱路32を流れる排気ガスを冷却することとなる。この結果、図4に示すように、排気ガス(太い黒矢印)は浄化ガスにより十分に冷却され、例えば100〜120℃に温度低下し溶解式熱交換器3内のガス噴出部14に流入する。この結果、処理容器12の材料として金属より安価な高耐熱性樹脂、例えば、ポリメチルペンテンが使用できる。特に、処理容器12の材料として透明樹脂を使えば、溶解式熱
交換器3の内部の状態をチェックできる。また、油煙、沸点の高い油蒸気、過熱蒸気も温度低下して放熱路32の内面に凝縮し下流へ流れ、ガス噴出部14に流入して処理容器12に流入する。すなわち、放熱路32には、油や凝縮水はほとんど残らない。
In the heat radiation path 32, the exhaust gas is disturbed by the heat transfer promotion plate 36 to improve the heat transfer rate, and flows along the inner wall of the heat radiation path 32. In the cooling path 33, purified gas (substantially the same temperature as the water in the processing container 12) described later flows through the cooling path 33 and along the outer wall of the heat radiation path 32. Therefore, the purified gas flowing through the cooling path 33 cools the exhaust gas flowing through the heat radiation path 32. As a result, as shown in FIG. 4, the exhaust gas (thick black arrow) is sufficiently cooled by the purified gas, drops in temperature to, for example, 100 to 120 ° C., and flows into the gas ejection portion 14 in the melting heat exchanger 3. . As a result, a high heat-resistant resin, such as polymethylpentene, which is cheaper than metal can be used as the material of the processing container 12. In particular, if a transparent resin is used as the material of the processing container 12, the internal state of the melting heat exchanger 3 can be checked. In addition, the temperature of oil smoke, oil vapor having a high boiling point, and superheated steam is also reduced in temperature, condensed on the inner surface of the heat radiation path 32, flows downstream, flows into the gas ejection part 14, and flows into the processing container 12. That is, almost no oil or condensed water remains in the heat radiation path 32.

溶解式熱交換器3では、処理容器12の水表面より上方の空間も負圧(例えば、0.5〜1.0kPa)になっている。負圧により吸引される排気ガスは、処理容器12内に設けられたガス噴出部14を通って気泡板29に形成された多数の気泡口30から多数の気泡(図4中、黒丸で示す)として水内へ噴出し上昇して、処理容器12の水表面より上方の空間に到達する。その際、排気ガスは水に熱を奪われ、ほぼ水温まで温度低下して過熱蒸気は凝縮し水に吸収(増水)され、油蒸気や油煙も凝縮し処理容器12に残る。また、水溶性の臭気成分は、水に溶解する。実験結果によれば、例えば、バレルアルデヒド(焦げ臭)は450μg/m3から100μg/m3、デカン(ガソリン臭)は860μg/m3から120μg/m3に減少した。   In the melting heat exchanger 3, the space above the water surface of the processing vessel 12 is also at a negative pressure (for example, 0.5 to 1.0 kPa). Exhaust gas sucked by the negative pressure passes through the gas jetting part 14 provided in the processing container 12, and many bubbles (shown by black circles in FIG. 4) from a large number of bubble ports 30 formed in the bubble plate 29. And then ascends into the water and reaches the space above the water surface of the processing vessel 12. At that time, the exhaust gas is deprived of heat by the water, the temperature is lowered to almost the water temperature, the superheated steam is condensed and absorbed (increase in water), and the oil vapor and the oil smoke are also condensed and remain in the processing vessel 12. Further, the water-soluble odor component is dissolved in water. According to the experimental results, for example, valeraldehyde (burnt odor) decreased from 450 μg / m3 to 100 μg / m3, and decane (gasoline odor) decreased from 860 μg / m3 to 120 μg / m3.

また、同時に、処理容器12の水表面より上方の空間の負圧により、外気(細い黒矢印)が外気口27から吸引(例えば、10〜30L/分)され、液状媒体冷却手段16である外気噴出部26を通って気泡板29に形成された多数の気泡口30から多数の気泡(図4中、白丸で示す)として水内へ噴出し上昇して、処理容器12の水表面より上方の空間に到達する。その際、外気は水から熱を奪い、ほぼ水温まで温度上昇して相対湿度を低下させるので、水は外気に蒸発する。この蒸発分、凝縮水による水の増加を抑える。言い換えると、水の温度上昇が抑えられる分、水の貯留量は沸騰の可能性のない量まで少なくでき、省資源が図れる。また、溶解式熱交換器3が軽くなるので、水の入替が容易になる。また、水の増加分を考慮して予め大きな容積を確保する必要がないので、処理容器12は小さくできる。なお、実験結果によれば、液状媒体冷却手段16が設けられない場合、処理容器12の水は1500ccから2000cc程度貯水しなければ、さんま10尾を調理すると、水は90℃を超える可能性がある。   At the same time, the outside air (thin black arrow) is sucked (for example, 10 to 30 L / min) from the outside air port 27 by the negative pressure in the space above the water surface of the processing container 12, and the outside air serving as the liquid medium cooling means 16. A large number of bubbles (shown by white circles in FIG. 4) are ejected into the water from a large number of bubble openings 30 formed in the bubble plate 29 through the ejection portion 26 and rise above the water surface of the processing vessel 12. Reach into space. At that time, the outside air takes heat from the water, and the temperature rises almost to the water temperature to lower the relative humidity, so that the water evaporates into the outside air. This increase in evaporation and water due to condensed water is suppressed. In other words, the amount of water stored can be reduced to the amount where there is no possibility of boiling as much as the temperature rise of the water is suppressed, thus saving resources. Moreover, since the melt | dissolution heat exchanger 3 becomes light, replacement | exchange of water becomes easy. In addition, since it is not necessary to secure a large volume in advance in consideration of the increase in water, the processing container 12 can be made smaller. According to the experimental results, when the liquid medium cooling means 16 is not provided, if the water in the processing container 12 does not store about 1500 cc to 2000 cc, the water may exceed 90 ° C. if 10 fishes are cooked. is there.

ここで、加熱開始の直後は、気泡板29の下方と、ガス噴出部14と外気噴出部26に水が貯留されているため、負圧により吸引される排気ガスはガス噴出部14と気泡板29の下方に有る水を気泡板29の上方へ押し出すと共に、外気口27から吸引される外気は外気噴出部26と気泡板29の下方に有る水を気泡板29の上方へ押し出すものである。そしてそれぞれ気泡口30から噴出した排気と外気は、水中に多数の別々の気泡を形成する。   Here, immediately after the start of heating, since water is stored below the bubble plate 29 and in the gas jetting portion 14 and the outside air jetting portion 26, the exhaust gas sucked by the negative pressure is the gas jetting portion 14 and the bubble plate. The water below the bubble plate 29 is pushed out above the bubble plate 29, and the outside air sucked from the outside air port 27 pushes the water below the bubble blowing plate 26 and the bubble plate 29 above the bubble plate 29. The exhaust gas and the outside air ejected from the bubble ports 30 respectively form a large number of separate bubbles in the water.

水蒸気を含んだ外気と除煙、脱臭された排気ガスは、処理容器12の上部空間で混合する。すなわち、排気ガスは低温、飽和状態で、水溶性の臭気成分を取除き、外気に希釈された浄化ガス(白抜き矢印)になる。なお、仕切り板31は、外気と排気ガスとを分離するので、外気と排気ガスとはお互い干渉することなく、安定して気泡板29から水内に噴出できる。   The outside air containing water vapor and the exhaust gas deodorized and deodorized are mixed in the upper space of the processing vessel 12. That is, the exhaust gas is purified at a low temperature and in a saturated state by removing water-soluble odor components and diluted to the outside air (white arrow). Since the partition plate 31 separates the outside air and the exhaust gas, the outside air and the exhaust gas can be stably ejected from the bubble plate 29 into the water without interfering with each other.

次に、浄化ガスは、ガス排出部15から誘引管23に流入する。その際、排気ガス、外気の気泡が水表面で弾けて水滴が飛散するが、ガス排出部15の入り口近傍にはカバー24が設けられており、弾けた水滴はカバー24に衝突して滴下するので、水滴がガス排出部15から誘引管23に流入することを防止できる。   Next, the purified gas flows from the gas discharge unit 15 into the induction pipe 23. At that time, exhaust gas and air bubbles bounce off the surface of the water, and water droplets scatter. However, a cover 24 is provided near the entrance of the gas discharge unit 15, and the bounced water droplets collide with the cover 24 and drop. Therefore, it is possible to prevent water droplets from flowing into the induction tube 23 from the gas discharge unit 15.

ここで、浄化ガスを誘引管23に排気するガス排出部15は、液状媒体表面より上方に配置したので、調理後液状媒体がガス排出部15から溢れ出ることはない。また、液状媒体の入替のために溶解式熱交換器3を取外しても溶解式熱交換器3から液状媒体が漏れることもない。   Here, since the gas discharge unit 15 for exhausting the purified gas to the induction pipe 23 is disposed above the surface of the liquid medium, the liquid medium after cooking does not overflow from the gas discharge unit 15. Further, even if the melting heat exchanger 3 is removed for replacement of the liquid medium, the liquid medium does not leak from the melting heat exchanger 3.

図5に示すように、誘引管23に流入した浄化ガスはチェンバー22で駆動空気と混合・希釈(低温化、臭気濃度の低下)して、第二の排気路18と冷却路入口34を介して冷却路33に流入する。前述の通り、第二の排気路18の一部である冷却路33を流れる浄化ガスは、第一の排気路13の一部である放熱路32の外壁に沿って流れる排気ガスを冷却し、冷却路出口35から排気され、その後排気口からトッププレート6近くに排出される。溶解式熱交換器3から第二の排気路18へ流入する浄化ガスは、ほぼ飽和状態である。第二の排気路18を流れる浄化ガスは、第一の排気路13を通過する排気ガスから熱を奪うので、浄化ガスは温度上昇して相対湿度を低下させる。その際、浄化ガスは温度上昇し、相対湿度が下がるので、排気口から外に排気された浄化ガスが外気により温度が下がっても、露点には達せず、浄化ガスから湯気が発生しない。この結果、トッププレート6が水滴で汚れることを防止でき、トッププレート6に置いてある品々に熱劣化を防げる。また、加熱調理機器1の使用者には、湯気による不快感がない。また、排気口がトッププレート6の上面にないので、トッププレート6は、掃除がし易く、広くて使い勝手がよく、デザイン性に優れた加熱調理機器1が提供できる。   As shown in FIG. 5, the purified gas that has flowed into the induction pipe 23 is mixed and diluted (dried at a low temperature and reduced in odor concentration) with drive air in the chamber 22, and then passed through the second exhaust path 18 and the cooling path inlet 34. Into the cooling passage 33. As described above, the purified gas flowing through the cooling path 33 that is a part of the second exhaust path 18 cools the exhaust gas that flows along the outer wall of the heat radiation path 32 that is a part of the first exhaust path 13, The air is exhausted from the cooling path outlet 35 and then exhausted near the top plate 6 from the exhaust outlet. The purified gas flowing into the second exhaust path 18 from the melting heat exchanger 3 is almost saturated. Since the purified gas flowing through the second exhaust path 18 takes heat from the exhaust gas passing through the first exhaust path 13, the purified gas rises in temperature and lowers the relative humidity. At that time, since the temperature of the purified gas rises and the relative humidity is lowered, even if the temperature of the purified gas exhausted from the exhaust port is lowered by the outside air, the dew point is not reached and no steam is generated from the purified gas. As a result, it is possible to prevent the top plate 6 from being contaminated with water droplets, and it is possible to prevent thermal deterioration of items placed on the top plate 6. In addition, the user of the cooking device 1 has no discomfort due to steam. Moreover, since there is no exhaust port in the upper surface of the top plate 6, the top plate 6 can be easily cleaned, can be provided with the cooking device 1 which is wide, easy to use and excellent in design.

以上のような構成により、本実施の形態における加熱調理機器1は、加熱手段10が調理容器7内を加熱すると、調理食材が温度上昇して水蒸気、油、臭気成分などを含んだ排気ガスが発生する。続いて、ガス移送手段19が排気ガスを調理容器7から第一の排気路13を経由して溶解式熱交換器3へ移送する。その際、排気ガス冷却手段4が第一の排気路13を通過する排気ガスを第一の排気路13壁を介して冷却し、温度低下した排気ガスが溶解式熱交換器3に流入するので、溶解式熱交換器3は金属より低価格で軽量の樹脂を使える。特に、透明樹脂を使えば、溶解式熱交換器3の中身をチェックできる。そして、排気ガスは直接接触した液状媒体によって冷却されて、温度低下した排気ガスは含まれる水蒸気、油を凝縮し、かつ水溶性の臭気成分と共に液状媒体に溶解する。すなわち、溶解式熱交換器3は、排気ガスに対して冷却、除湿、除煙、脱臭などの排熱処理を行うので、排気ガスは低温の浄化ガスになり、浄化ガスはガス移送手段19により第二の排気路18を経由して排出される。ただし、液状媒体は、水蒸気や油の凝縮した量だけ増量し、かつ油や臭気成分が溶解すると、溶解能力が低下する。その後、溶解式熱交換器3内に油が付着して汚れ、更に液状媒体、溶解式熱交換器3内に菌やかびが発生し、かつ臭気が発生するので、調理後、液状媒体の入替と溶解式熱交換器3の清掃が必要になる。   With the above configuration, when the heating means 10 heats the cooking container 7 in the cooking device 1 according to the present embodiment, the cooking ingredients rise in temperature and exhaust gas containing water vapor, oil, odor components, etc. Occur. Subsequently, the gas transfer means 19 transfers the exhaust gas from the cooking vessel 7 to the melting heat exchanger 3 via the first exhaust path 13. At that time, the exhaust gas cooling means 4 cools the exhaust gas passing through the first exhaust passage 13 through the wall of the first exhaust passage 13, and the exhaust gas whose temperature has decreased flows into the melting heat exchanger 3. The melting heat exchanger 3 can be made of a resin that is lower in price and lighter than metal. In particular, if a transparent resin is used, the contents of the melting heat exchanger 3 can be checked. The exhaust gas is cooled by the liquid medium in direct contact with it, and the exhaust gas whose temperature has been reduced condenses the water vapor and oil contained therein and dissolves in the liquid medium together with water-soluble odor components. That is, since the melting heat exchanger 3 performs exhaust heat treatment such as cooling, dehumidification, smoke removal, and deodorization on the exhaust gas, the exhaust gas becomes a low-temperature purified gas, and the purified gas is transferred by the gas transfer means 19. It is discharged via the second exhaust path 18. However, if the liquid medium is increased by the amount of water vapor or oil condensed, and the oil or odor component is dissolved, the dissolving ability is lowered. Thereafter, oil adheres to the melting heat exchanger 3 and becomes dirty, and further, the liquid medium, fungi and fungi are generated in the melting heat exchanger 3, and odor is generated. And the melting heat exchanger 3 needs to be cleaned.

調理中、液状媒体は排気ガスから熱、特に潜熱を奪うので、温度上昇し、液状媒体は主に水蒸気の凝縮分増加する。他方、排気ガス冷却手段4が排気ガスを冷却するので、液状媒体の温度上昇は抑えられる分、液状媒体の所定貯留量は沸騰の可能性のない量まで少なくでき、省資源が図れる。したがって、液状媒体の入替と溶解式熱交換器3の清掃を行うに際し、軽い溶解式熱交換器3を取り扱うことができるものである。   During cooking, the liquid medium takes heat, particularly latent heat, from the exhaust gas, so the temperature rises and the liquid medium mainly increases the condensation of water vapor. On the other hand, since the exhaust gas cooling means 4 cools the exhaust gas, the amount of liquid medium stored can be reduced to an amount where there is no possibility of boiling, so that resources can be saved. Therefore, when the liquid medium is replaced and the melting heat exchanger 3 is cleaned, the light melting heat exchanger 3 can be handled.

加熱手段10への通電を停止して調理食材の調理が終了しても、送風機20の駆動を継続すると、液状媒体冷却手段16は継続して水を冷却できるので、水は火傷の可能性がない温度まで短時間で下がり、調理後短時間で水の入替と溶解式熱交換器3の清掃ができる。なお、水の入替ると、再び加熱調理ができる。   Even if energization of the heating means 10 is stopped and cooking of the cooking ingredients is finished, if the drive of the blower 20 is continued, the liquid medium cooling means 16 can continue to cool the water, so that the water may be burned. The temperature can be lowered to a low temperature in a short time, and water can be replaced and the melting heat exchanger 3 can be cleaned in a short time after cooking. In addition, when water is replaced, cooking can be performed again.

実施の形態1では、液状媒体としての水を使用したが、蓄熱できる液体なら水の必要はなく、油などでもよい。   In the first embodiment, water as a liquid medium is used, but water is not necessary as long as it can store heat, and oil or the like may be used.

以上のように、本発明にかかる加熱調理機器は、排気ガスを冷却する排気ガス冷却手段を備えたものであり、調理中、液状媒体は排気ガスから熱を奪うので、温度上昇するが、他方、排気ガス冷却手段が排気ガスを冷却し、液状媒体の温度上昇は抑えられるので、液状媒体の所定貯留量は沸騰の可能性のない量まで少なくでき、省資源が図れるので、排気
を行う各種の加熱調理機器にも適用できるものである。
As described above, the cooking device according to the present invention includes the exhaust gas cooling means for cooling the exhaust gas. During cooking, the liquid medium takes heat from the exhaust gas, and thus the temperature rises. Since the exhaust gas cooling means cools the exhaust gas and the temperature rise of the liquid medium can be suppressed, the predetermined storage amount of the liquid medium can be reduced to an amount where there is no possibility of boiling, and resources can be saved. It can be applied to other cooking devices.

1 加熱調理機器
3 溶解式熱交換器
4 排気ガス冷却手段
7 調理容器
10 加熱手段
12 処理容器
13 第一の排気路
14 ガス噴出部
15 ガス排出部
16 液状媒体冷却手段
18 第二の排気路
19 ガス移送手段
23 誘引管
25 嵌合部
26 外気噴出部
27 外気口
29 気泡板
30 気泡口
32 放熱路
33 冷却路
35 冷却路出口
DESCRIPTION OF SYMBOLS 1 Cooking apparatus 3 Dissolving heat exchanger 4 Exhaust gas cooling means 7 Cooking container 10 Heating means 12 Processing container 13 First exhaust path 14 Gas ejection part 15 Gas discharge part 16 Liquid medium cooling means 18 Second exhaust path 19 Gas transfer means 23 Induction tube 25 Fitting portion 26 Outside air ejection portion 27 Outside air port 29 Bubble plate 30 Bubble port 32 Heat radiation path 33 Cooling path 35 Cooling path outlet

Claims (3)

調理食材を加熱する加熱手段を設けた調理容器と、
液状媒体を貯留し、液状媒体を介して排気ガスを冷却処理する溶解式熱交換器と、
前記調理容器と前記溶解式熱交換器に接続され、前記調理容器から前記溶解式熱交換器へ排気ガスを搬送させる第一の排気路と、
前記溶解式熱交換器に接続され、前記溶解式熱交換器内で処理された排気ガスを前記溶解式熱交換器の下流へ搬送させる第二の排気路と、
排気ガスを移送するガス移送手段と、を備え、
前記第一の排気路を冷却する排気ガス冷却手段を有する加熱調理機器。
A cooking container provided with a heating means for heating the cooking ingredients;
A melting heat exchanger for storing a liquid medium and cooling the exhaust gas through the liquid medium;
A first exhaust passage connected to the cooking vessel and the melting heat exchanger, for transporting exhaust gas from the cooking vessel to the melting heat exchanger;
A second exhaust path connected to the melting heat exchanger and transporting the exhaust gas treated in the melting heat exchanger downstream of the melting heat exchanger;
Gas transfer means for transferring exhaust gas, and
A cooking device having an exhaust gas cooling means for cooling the first exhaust passage.
前記排気ガス冷却手段は、少なくとも前記第一の排気路の一部を前記第二の排気路の一部で冷却する構成とした請求項1記載の加熱調理機器。 The cooking apparatus according to claim 1, wherein the exhaust gas cooling means cools at least a part of the first exhaust path with a part of the second exhaust path. 前記排気ガス冷却手段は、前記第一の排気路の一部と前記第二の排気路の一部を近接設置した請求項1または2に記載の加熱調理機器。 The cooking apparatus according to claim 1 or 2, wherein the exhaust gas cooling means is configured such that a part of the first exhaust path and a part of the second exhaust path are installed close to each other.
JP2016005684A 2016-01-15 2016-01-15 Heating cooker Withdrawn JP2017125657A (en)

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