JP6246054B2 - Flyer - Google Patents

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JP6246054B2
JP6246054B2 JP2014087438A JP2014087438A JP6246054B2 JP 6246054 B2 JP6246054 B2 JP 6246054B2 JP 2014087438 A JP2014087438 A JP 2014087438A JP 2014087438 A JP2014087438 A JP 2014087438A JP 6246054 B2 JP6246054 B2 JP 6246054B2
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superheated steam
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教安 西
教安 西
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Osaka Gas Co Ltd
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Description

本発明は、調理油を収容する油槽と、その油槽内の調理油を加熱する加熱手段とが設けられたフライヤーに関する。   The present invention relates to a fryer provided with an oil tank for storing cooking oil and a heating means for heating the cooking oil in the oil tank.

かかるフライヤーは、加熱手段により油槽内の調理油を加熱する状態で、揚げ調理対象の食材を油槽内に入れて、食材を揚げ調理するものである。
このようなフライヤーにおいて、従来、バーナの燃焼ガスを通流させる燃焼ガス通流室を油槽の底部の外面を覆う状態で設けて、この燃焼ガス通流室を備えて加熱手段を構成したもの(以下、平底タイプと称する場合がある)があった(例えば、特許文献1参照。)。
又、バーナの燃焼ガスを通流させる複数の燃焼ガス通流管を油槽内の調理油に浸漬する状態で設けて、これら複数の燃焼ガス通流管を備えて加熱手段を構成したもの(以下、浸管タイプと称する場合がある)もあった(例えば、特許文献2参照。)。
Such a fryer is for fried cooking by putting the food to be fried in the oil tank in a state where the cooking oil in the oil tank is heated by the heating means.
In such a fryer, conventionally, a combustion gas flow chamber through which the combustion gas of the burner flows is provided so as to cover the outer surface of the bottom of the oil tank, and the heating means is configured by including this combustion gas flow chamber ( Hereinafter, there was a case called a flat bottom type) (for example, refer to Patent Document 1).
Also, a plurality of combustion gas flow pipes through which the burner combustion gas flows are provided so as to be immersed in cooking oil in the oil tank, and a heating means is configured by including these combustion gas flow pipes (hereinafter referred to as heating means). , Sometimes referred to as a dip tube type) (see, for example, Patent Document 2).

特開2012−34963号公報JP 2012-34963 A 特開2003−275105号公報JP 2003-275105 A

平底タイプのフライヤーは、加熱手段を構成する部材が油槽内に設けられていないため、油槽を清掃し易いので、フライヤーの清掃性に優れている。一方、調理油を加熱する加熱効率を向上するには、燃焼ガス通流室を広範囲に設けるには限度があるので、バーナの燃焼量を増大して、燃焼ガス通流室に通流させる燃焼ガス量を増大したり、燃焼ガス通流室内に燃焼ガスを蛇行状等に流動させる通流案内部材を設けて、燃焼ガスの通流経路を長くしたりする方法が想定されるが、いずれも、バーナが不完全燃焼になり易くなると共に、COガスが発生し易くなるため限界があるので、加熱効率を向上し難い。
浸管タイプのフライヤーは、複数の燃焼ガス通流管が油槽内の調理油に浸漬する状態で設けられているので、加熱効率に優れている。一方、フライヤーの清掃の際には、複数の燃焼ガス通流管が設けられた構造が複雑であり、又、油槽内の複数の燃焼ガス通流管が邪魔になるので、油槽を清掃し難い。
Since the flat bottom type fryer is not provided in the oil tank with the members constituting the heating means, it is easy to clean the oil tank, so that the fryer is excellent in cleanability. On the other hand, in order to improve the heating efficiency for heating cooking oil, there is a limit to providing a combustion gas flow chamber in a wide range, so combustion that increases the amount of burner combustion and flows to the combustion gas flow chamber A method of enlarging the flow path of the combustion gas by increasing the gas amount or by providing a flow guide member that causes the combustion gas to flow in a meandering manner in the combustion gas flow chamber is envisaged. The burner is likely to be incompletely combusted and CO gas is likely to be generated, so there is a limit, and it is difficult to improve the heating efficiency.
The immersion pipe type fryer is excellent in heating efficiency because a plurality of combustion gas flow pipes are provided in a state of being immersed in cooking oil in the oil tank. On the other hand, when the fryer is cleaned, the structure provided with a plurality of combustion gas flow pipes is complicated, and the plurality of combustion gas flow pipes in the oil tank are obstructive, so it is difficult to clean the oil tank. .

又、平底タイプのフライヤー及び浸管タイプのフライヤー共に、バーナの高温の燃焼ガスを加熱媒体として燃焼ガス通流室や燃焼ガス通流管に通流させるので、熱疲労により、油槽、燃焼ガス通流室及び燃焼ガス通流管が劣化し易い。
そして、劣化により、万が一、油槽や燃焼ガス通流室や燃焼ガス通流管にクラックが入ると、燃焼ガスの温度は調理油の自然発火温度よりも高いため、油槽内の調理油が自然発火する虞がある。そこで、調理油の自然発火を防止するために、耐熱性に優れた高価な材料を用いて、油槽、燃焼ガス通流室及び燃焼ガス通流管を構成する必要があるので、フライヤーの価格が高くなるという問題があった。
In addition, both the flat bottom type fryer and the dip tube type fryer allow the hot combustion gas of the burner to flow through the combustion gas flow chamber and the combustion gas flow tube as a heating medium. The flow chamber and the combustion gas flow pipe are likely to deteriorate.
If the oil tank, combustion gas flow chamber, or combustion gas flow pipe cracks due to deterioration, the temperature of the combustion gas is higher than the spontaneous ignition temperature of the cooking oil. There is a risk of doing. Therefore, in order to prevent spontaneous combustion of cooking oil, it is necessary to configure an oil tank, a combustion gas flow chamber, and a combustion gas flow tube using an expensive material excellent in heat resistance. There was a problem of becoming higher.

本発明は、かかる実情に鑑みてなされたものであり、その目的は、清掃性及び加熱効率の向上並びに低廉化を図りながら、油槽内の調理油の自然発火を防止し得るフライヤーを提供することにある。   This invention is made | formed in view of this situation, The objective is providing the fryer which can prevent the spontaneous combustion of the cooking oil in an oil tank, aiming at the improvement of cleaning property and heating efficiency, and cost reduction. It is in.

本発明に係るフライヤーは、調理油を収容する油槽と、その油槽内の調理油を加熱する加熱手段とが設けられたものであって、
第1特徴構成は、前記加熱手段が、過熱蒸気を生成する過熱蒸気生成装置と、その過熱蒸気生成装置にて生成された過熱蒸気を流動させる過熱蒸気通流部とを備えて構成され、
前記過熱蒸気通流部が、前記油槽の外側面を全周にわたって覆う状態で配置され、
前記過熱蒸気生成装置が、生成する過熱蒸気の温度を調整可能な蒸気温度調整部を備え、
前記蒸気温度調整部が、前記過熱蒸気の温度を前記油槽内の調理油の自然発火温度よりも低い温度に調整するように構成されている点にある。
The fryer according to the present invention is provided with an oil tank for storing cooking oil and a heating means for heating the cooking oil in the oil tank,
In the first characteristic configuration, the heating means includes a superheated steam generation device that generates superheated steam, and a superheated steam flow section that flows the superheated steam generated by the superheated steam generation device,
The superheated steam flow portion is arranged in a state of covering the entire outer surface of the oil tank,
The superheated steam generator includes a steam temperature adjustment unit capable of adjusting the temperature of the superheated steam to be generated,
The steam temperature adjusting unit is configured to adjust the temperature of the superheated steam to a temperature lower than the spontaneous ignition temperature of the cooking oil in the oil tank.

上記特徴構成によれば、蒸気温度調整部を備えた過熱蒸気生成装置により、調理油の自然発火温度よりも低い温度に温度が調整された過熱蒸気が生成され、そのように生成された過熱蒸気が、油槽の外側面を全周にわたって覆う状態で配置された過熱蒸気通流部に供給されて、その過熱蒸気通流部を流動することにより、油槽内の調理油が加熱される。   According to the above characteristic configuration, the superheated steam generated by the superheated steam generation device including the steam temperature adjusting unit generates the superheated steam whose temperature is adjusted to a temperature lower than the spontaneous ignition temperature of the cooking oil, and the superheated steam thus generated is generated. However, it is supplied to the superheated steam flow part arrange | positioned in the state which covers the outer surface of an oil tank over the perimeter, and the cooking oil in an oil tank is heated by flowing through the superheated steam flow part.

つまり、過熱蒸気通流部を油槽の外側面を全周にわたって覆う状態で配置する構成であることから、例えば、油槽の外側面の全面にわたって配置する等、過熱蒸気通流部を、油槽の外側面に対して効果的に広範囲に配置することが可能であるので、油槽内の調理油を広範囲にわたって加熱することが可能となり、加熱効率を向上することができる。
又、加熱手段を構成する部材が油槽内に設けられることがないので、油槽を清掃し易く、フライヤーの清掃性を向上することができる。
That is, since the superheated steam flow portion is arranged in a state of covering the outer surface of the oil tank over the entire circumference, the superheated steam flow portion is arranged outside the oil tank, for example, over the entire outer surface of the oil tank. Since it can arrange | position in the wide range effectively with respect to a side surface, it becomes possible to heat the cooking oil in an oil tank over a wide range, and can improve a heating efficiency.
Moreover, since the member which comprises a heating means is not provided in an oil tank, it is easy to clean an oil tank and can improve the cleanability of a fryer.

更に、加熱媒体として過熱蒸気通流部に供給される過熱蒸気の温度は、蒸気温度調整部により、調理油の自然発火温度よりも低い温度に調整されるので、従来のフライヤーで加熱媒体として用いられていたバーナの燃焼ガスの温度よりも低くなるため、油槽及び過熱蒸気通流部の熱疲労を効果的に抑制することができる。
そこで、加熱媒体として、調理油の自然発火温度よりも低い温度の過熱蒸気を用いることにより、加熱媒体としてバーナの燃焼ガスを用いる場合ほどには、油槽及び過熱蒸気通流部に高い耐熱性が要求されないので、熱疲労を効果的に抑制して、油槽及び過熱蒸気通流部にクラックが入るのを確実に防止しながら、油槽及び過熱蒸気通流部を熱伝導率が高くしかも比較的安価な材料を用いて構成することができる。
このことにより、フライヤーの低廉化を図ることができ、加熱効率も更に向上することができる。
従って、清掃性及び加熱効率の向上並びに低廉化を図りながら、油槽内の調理油の自然発火を防止し得るフライヤーを提供することができる。
Furthermore, since the temperature of the superheated steam supplied to the superheated steam flow section as a heating medium is adjusted to a temperature lower than the spontaneous ignition temperature of the cooking oil by the steam temperature adjusting section, it is used as a heating medium in a conventional fryer. Since it becomes lower than the temperature of the combustion gas of the burner which was made, the thermal fatigue of an oil tank and a superheated steam flow part can be suppressed effectively.
Therefore, by using superheated steam having a temperature lower than the spontaneous ignition temperature of cooking oil as the heating medium, the oil tank and the superheated steam flow section have higher heat resistance as much as when the combustion gas of the burner is used as the heating medium. Since it is not required, it effectively suppresses thermal fatigue and reliably prevents cracks in the oil tank and superheated steam flow part, while the oil tank and superheated steam flow part have high thermal conductivity and is relatively inexpensive. It can be configured using a simple material.
As a result, the cost of the fryer can be reduced and the heating efficiency can be further improved.
Therefore, it is possible to provide a fryer that can prevent spontaneous combustion of cooking oil in the oil tank while improving cleanability and heating efficiency and reducing the cost.

第2特徴構成は、上記第1特徴構成に加えて、
前記過熱蒸気通流部が、前記油槽の外側面における上方側の部分を覆うように配置されて、前記油槽における底部側に、上方側の部分よりも調理油の温度が低いクールゾーンが形成される点にある。
In addition to the first feature configuration, the second feature configuration is
The superheated steam flow part is disposed so as to cover the upper part of the outer surface of the oil tank, and a cool zone in which the cooking oil temperature is lower than that of the upper part is formed on the bottom side of the oil tank. There is in point.

即ち、食材を油槽内に入れて揚げ調理を行う際に生じた油カスや食品カスは、油槽内の底部に集まる。
上記特徴構成によれば、油槽における底部側に、上方側の部分よりも調理油の温度が低いクールゾーンが形成されるので、油カスや食品カスが焦げ難い。
従って、調理油の劣化を低減しながら、揚げ調理を行うことができる。
That is, the oil residue and food residue generated when the food is placed in the oil tank and fried are collected at the bottom of the oil tank.
According to the above characteristic configuration, a cool zone in which the temperature of cooking oil is lower than that of the upper portion is formed on the bottom side of the oil tank, so that oil residue and food residue are difficult to burn.
Therefore, fried cooking can be performed while reducing deterioration of cooking oil.

第3特徴構成は、上記第1又は第2特徴構成に加えて、
前記過熱蒸気生成装置が、供給される水をバーナを熱源として加熱して飽和水蒸気を生成する蒸気発生器と、その蒸気発生器から供給される飽和水蒸気を電気式加熱部を熱源として加熱して過熱蒸気を生成する過熱蒸気生成器とを備えて構成され、
前記蒸気温度調整部が、前記電気式加熱部に供給する電力を調整することにより、前記過熱蒸気の温度を調整するように構成されている点にある。
In addition to the first or second feature configuration, the third feature configuration is
The superheated steam generator heats supplied water using a burner as a heat source to generate saturated steam, and heats saturated steam supplied from the steam generator using an electric heating unit as a heat source. And a superheated steam generator for generating superheated steam,
The steam temperature adjusting unit is configured to adjust the temperature of the superheated steam by adjusting electric power supplied to the electric heating unit.

上記特徴構成によれば、蒸気発生器において、供給される水がバーナを熱源として加熱されて、飽和水蒸気が生成され、その飽和水蒸気が過熱蒸気生成器に供給されて、過熱蒸気生成器において、電気式加熱部を熱源として加熱されて、過熱蒸気が生成される。
そして、蒸気温度調整部により、電気式加熱部に供給する電力が調整されることにより、過熱蒸気の温度が調整される。
つまり、過熱蒸気生成器において過熱蒸気を生成するための熱源として、電気式加熱部を用いることにより、生成する過熱蒸気の温度を、調理油の自然発火温度よりも低い所定の温度に精度よく調整することができるようになる。このことにより、油槽内の調理油を、食材を揚げ調理するための所定の目標温度に精度良く加熱することができる。
従って、揚げ調理の調理品質を一層向上することができる。
According to the above characteristic configuration, in the steam generator, the supplied water is heated using the burner as a heat source to generate saturated steam, and the saturated steam is supplied to the superheated steam generator. In the superheated steam generator, Heating is performed using the electric heating unit as a heat source, and superheated steam is generated.
And the temperature of superheated steam is adjusted by adjusting the electric power supplied to an electric heating part by a steam temperature adjustment part.
In other words, by using an electric heating unit as a heat source for generating superheated steam in the superheated steam generator, the temperature of the generated superheated steam is accurately adjusted to a predetermined temperature lower than the spontaneous ignition temperature of cooking oil. Will be able to. Thereby, the cooking oil in the oil tank can be accurately heated to a predetermined target temperature for cooking the food.
Therefore, the cooking quality of fried cooking can be further improved.

第4特徴構成は、上記第1〜第3特徴構成のいずれか1つに加えて、
前記過熱蒸気通流部から排出された排蒸気と前記過熱蒸気生成装置に供給される過熱蒸気生成用の水とを熱交換させて、その過熱蒸気生成用の水を予熱する予熱器が設けられている点にある。
The fourth feature configuration is in addition to any one of the first to third feature configurations,
There is provided a preheater that preheats the superheated steam generation water by exchanging heat between the exhaust steam discharged from the superheated steam flow section and the superheated steam generation water supplied to the superheated steam generation device. There is in point.

上記特徴構成によれば、予熱器により、過熱蒸気通流部から排出された排蒸気と過熱蒸気生成装置に供給される過熱蒸気生成用の水とが熱交換されて、過熱蒸気生成装置に供給される過熱蒸気生成用の水が予熱される。
つまり、過熱蒸気通流部から排出される排蒸気によって廃棄される熱の一部を回収して、過熱蒸気生成用の水を予熱することができるので、加熱効率を更に向上することができる。
According to the above characteristic configuration, the preheater exchanges heat between the exhaust steam discharged from the superheated steam passage and the water for superheated steam generation supplied to the superheated steam generation apparatus, and supplies the heat to the superheated steam generation apparatus. Water for generating superheated steam is preheated.
That is, since a part of the heat discarded by the exhaust steam discharged from the superheated steam flow section can be recovered and the water for generating the superheated steam can be preheated, the heating efficiency can be further improved.

フライヤーの全体概略構成を示す図Diagram showing the overall structure of the flyer フライヤーの過熱蒸気生成装置及び制御構成を示すブロック図Block diagram showing fryer superheated steam generator and control configuration フライヤーの要部の縦断面図Longitudinal section of the main part of the flyer

以下、図面に基づいて、本発明の実施の形態を説明する。
図1に示すように、フライヤーは、調理油Lを収容する油槽1、その油槽1内の調理油Lを加熱する加熱手段H、フライヤーの運転を制御する制御部2、その制御部2に各種制御情報を指令する操作部3、及び、フライヤーの作動状態等、各種情報を表示する表示部4(例えば、液晶ディスプレイ)等を備えて構成されている。図示を省略するが、操作部3には、フライヤーの起動及び停止を指令する運転スイッチ、油槽1内の調理油Lを加熱する目標温度である加熱目標温度を設定する温度設定部等が備えられている。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
As shown in FIG. 1, the fryer is divided into an oil tank 1 that contains cooking oil L, heating means H that heats cooking oil L in the oil tank 1, a control unit 2 that controls the operation of the fryer, An operation unit 3 for instructing control information and a display unit 4 (for example, a liquid crystal display) for displaying various information such as an operating state of the fryer are configured. Although not shown, the operation unit 3 includes an operation switch for instructing start and stop of the fryer, a temperature setting unit for setting a heating target temperature that is a target temperature for heating the cooking oil L in the oil tank 1, and the like. ing.

図1及び図3に示すように、油槽1は、平面視が正方形状で、上部が略全体にわたって開口した容器状に形成され、この油槽1が、フライヤーの外装を形成する外装ケーシング5の上部開口部の縁部に吊り下げ支持された状態で、その外装ケーシング5に組み付けられている。
又、油槽1は、上方側の上方部分1uが、横断形状が正方形状で且つ横断面積が一定な四角筒状に形成され、底部側の底部部分1bが、横断形状が正方形状で且つ横断面積が下方ほど狭くなる截頭四角錐形状の器状に形成されて、全体として下窄まり状に構成されている。
そして、その油槽1の底部に、調理油Lを排出する管状の排油口6が設けられ、その排油口6には、その排油口6を開閉自在な排油コック7が設けられている。
As shown in FIGS. 1 and 3, the oil tank 1 is formed in a container shape having a square shape in plan view and an upper part opened substantially over the whole, and the oil tank 1 is an upper part of an outer casing 5 that forms an outer packaging of a fryer. It is assembled to the outer casing 5 in a state of being supported suspended from the edge of the opening.
The oil tank 1 has an upper portion 1u on the upper side formed in a square tube shape having a square cross-sectional shape and a constant cross-sectional area, and a bottom portion 1b on the bottom side having a square cross-sectional shape and a cross-sectional area. Is formed in a truncated quadrangular pyramid-like vessel shape that becomes narrower toward the lower side, and is configured to be constricted as a whole.
A tubular oil discharge port 6 for discharging cooking oil L is provided at the bottom of the oil tank 1, and an oil discharge cock 7 that can open and close the oil discharge port 6 is provided at the oil discharge port 6. Yes.

外装ケーシング5の上部の後端部には、上方に立ち上がる立ち上がり部5sが設けられ、その立ち上がり部5sに、前述の操作部3及び表示部4が装備された操作盤8が設けられている。   A rising portion 5s that rises upward is provided at the rear end of the upper portion of the outer casing 5, and an operation panel 8 equipped with the operation portion 3 and the display portion 4 described above is provided on the rising portion 5s.

図1及び図2に示すように、本発明では、加熱手段Hが、過熱蒸気Vaを生成する過熱蒸気生成装置Sと、その過熱蒸気生成装置Sにて生成された過熱蒸気Vaを流動させる過熱蒸気通流部Rとを備えて構成され、過熱蒸気通流部Rが、油槽1の外側面1sを全周にわたって覆う状態で配置されている。
又、過熱蒸気生成装置Sが、生成する過熱蒸気Vaの温度を調整可能な蒸気温度調整部Cを備え、その蒸気温度調整部Cが、過熱蒸気Vaの温度を油槽1内の調理油Lの自然発火温度よりも低い温度に調整するように構成されている。
As shown in FIG.1 and FIG.2, in this invention, the heating means H is the superheated steam generator S which produces | generates the superheated steam Va, and the superheat which makes the superheated steam Va produced | generated by the superheated steam generator S flow. The superheated steam flow portion R is arranged in a state of covering the outer surface 1 s of the oil tank 1 over the entire circumference.
The superheated steam generator S includes a steam temperature adjusting unit C that can adjust the temperature of the generated superheated steam Va, and the steam temperature adjusting unit C sets the temperature of the superheated steam Va to the cooking oil L in the oil tank 1. It is configured to adjust to a temperature lower than the spontaneous ignition temperature.

次に、過熱蒸気生成装置Sについて、説明を加える。
図1及び図3に示すように、過熱蒸気通流部Rは、油槽1の上方部分1uの外側面1sを全周にわたって覆う状態で配置されている。具体的には、上方部分1uの外側面1sを形成する側壁部分1wの全周にわたって、樋状の通流部形成部材9が、その開口縁部を側壁部分1wの外側面1sに当て付けた状態でその側壁部分1wに気密状に取り付けられている。そして、それら上方部分1uの側壁部分1wと通流部形成部材9とにより、過熱蒸気通流部Rが、油槽1の上方部分1uの外側面1sを全周にわたって覆う四角枠状に構成される。
Next, the superheated steam generator S will be described.
As shown in FIG.1 and FIG.3, the superheated steam flow part R is arrange | positioned in the state which covers the outer surface 1s of the upper part 1u of the oil tank 1 over a perimeter. Specifically, over the entire periphery of the side wall portion 1w that forms the outer side surface 1s of the upper portion 1u, the bowl-shaped flow portion forming member 9 applies the opening edge to the outer side surface 1s of the side wall portion 1w. In the state, it is attached to the side wall portion 1w in an airtight manner. And the superheated steam flow part R is comprised by the side wall part 1w of these upper part 1u, and the flow part formation member 9 in the shape of a square frame which covers the outer surface 1s of the upper part 1u of the oil tank 1 over the perimeter. .

詳細は後述するが、過熱蒸気通流部Rに過熱蒸気Vaが供給されることにより、油槽1の上方部分1u内の調理油Lが集中的に加熱されることになり、上方部分1u内に、揚げ調理対象の食材(図示省略)の揚げ調理を行う揚げ調理ゾーンZfが形成され、油槽1の底部部分1b内に、調理油Lの温度が上方部分1u内に形成される揚げ調理ゾーンZfよりも低いクールゾーンZcが形成される。
つまり、過熱蒸気通流部Rが、油槽1の外側面1sにおける上方側の部分を覆うように配置されて、油槽1における底部側に、上方部分1uよりも調理油Lの温度が低いクールゾーンZcが形成されることになる。
そして、図2及び図3に示すように、油槽1における揚げ調理ゾーンZfの調理油Lの温度を検出する調理油温度センサ10が設けられている。
Although details will be described later, when the superheated steam Va is supplied to the superheated steam flow portion R, the cooking oil L in the upper portion 1u of the oil tank 1 is heated intensively, and in the upper portion 1u. The deep-fried cooking zone Zf for deep-fried cooking ingredients (not shown) is formed, and the temperature of the cooking oil L is formed in the upper portion 1u in the bottom portion 1b of the oil tank 1. Lower cool zone Zc is formed.
That is, the superheated steam flow portion R is disposed so as to cover the upper portion of the outer surface 1 s of the oil tank 1, and the temperature of the cooking oil L is lower on the bottom side of the oil tank 1 than the upper portion 1 u. Zc is formed.
And the cooking oil temperature sensor 10 which detects the temperature of the cooking oil L of the fried cooking zone Zf in the oil tank 1 is provided as shown in FIG.2 and FIG.3.

図1及び図2に示すように、過熱蒸気生成装置Sが、給水路18を通して供給される水Wをガスバーナ31を熱源として加熱して飽和水蒸気Vbを生成する蒸気発生器30と、その蒸気発生器30から飽和水蒸気路11を通して供給される飽和水蒸気Vbを電気ヒータ41(電気式加熱部の一例)を熱源として加熱して過熱蒸気Vaを生成する過熱蒸気生成器40とを備えて構成されている。   As shown in FIGS. 1 and 2, the superheated steam generator S heats the water W supplied through the water supply channel 18 by using a gas burner 31 as a heat source to generate saturated steam Vb, and its steam generation. And a superheated steam generator 40 that generates superheated steam Va by heating the saturated steam Vb supplied from the vessel 30 through the saturated steam path 11 using an electric heater 41 (an example of an electric heating unit) as a heat source. Yes.

蒸気発生器30は、図2に詳細を示すように、両端が閉塞された円筒状の炉筒32内に、ガスバーナ31の燃焼ガスEを通流させる複数の円筒状の煙管33を、夫々の軸芯を炉筒32の軸心に沿わせた姿勢で環状に並べて配設して構成される。
炉筒32は、軸心を水平方向に沿わせた姿勢で配置され、その炉筒32の一端部には、複数の煙管33夫々の一端が連通する供給ヘッダ34が設けられ、炉筒32の他端部には、複数の煙管33夫々の他端が連通する排出ヘッダ35が設けられている。
ガスバーナ31は、燃焼ガスEを供給ヘッダ34に供給するように設けられている。
As shown in detail in FIG. 2, the steam generator 30 includes a plurality of cylindrical smoke pipes 33 through which the combustion gas E of the gas burner 31 flows in a cylindrical furnace cylinder 32 closed at both ends. The shaft cores are arranged in a ring shape in a posture along the axis of the furnace tube 32.
The furnace tube 32 is arranged in a posture in which the axis is aligned in the horizontal direction, and a supply header 34 in which one end of each of the plurality of smoke tubes 33 communicates is provided at one end of the furnace tube 32. The other end portion is provided with a discharge header 35 in which the other ends of the plurality of smoke pipes 33 communicate with each other.
The gas burner 31 is provided so as to supply the combustion gas E to the supply header 34.

ガスバーナ31には、ガス燃料(例えば、13A等の天然ガスベースの都市ガス)を供給する燃料供給路12、及び、空気ブロア13により燃焼用空気を供給する空気供給路14が接続されている。燃料供給路12には、ガスバーナ31へのガス燃料の供給を断続する燃料断続弁15、及び、ガス燃料の供給量を調整する燃料供給量調整弁16が設けられている。
又、炉筒32の底部には、給水ポンプ17により水Wを供給する給水路18が接続され、炉筒32の上部には、炉筒32内で生成された飽和水蒸気Vbを送出する飽和水蒸気路11が接続されている。
The gas burner 31 is connected to a fuel supply path 12 for supplying gas fuel (for example, natural gas-based city gas such as 13A) and an air supply path 14 for supplying combustion air by an air blower 13. The fuel supply path 12 is provided with a fuel interrupt valve 15 that intermittently supplies gas fuel to the gas burner 31 and a fuel supply amount adjustment valve 16 that adjusts the supply amount of gas fuel.
Further, a water supply path 18 for supplying water W by the feed water pump 17 is connected to the bottom of the furnace tube 32, and saturated steam for sending saturated steam Vb generated in the furnace tube 32 is connected to the upper part of the furnace tube 32. The path 11 is connected.

つまり、ガスバーナ31が燃焼してその燃焼ガスEが複数の煙管33を通流することにより、炉筒32内の水Wが加熱されて飽和水蒸気Vbが生成され、その飽和水蒸気Vbが飽和水蒸気路11を通して過熱蒸気生成器40に供給されることになる。   That is, when the gas burner 31 burns and the combustion gas E flows through the plurality of smoke pipes 33, the water W in the furnace tube 32 is heated to generate saturated steam Vb, and the saturated steam Vb is saturated steam path. 11 is supplied to the superheated steam generator 40.

過熱蒸気生成器40は、図2に詳細を示すように、両端が閉塞された容器42内に、U字状の電気ヒータ41を容器42の一端部に支持させた状態で配設して構成され、更に、電気ヒータ41を駆動するヒータ駆動部43も備えている。
容器42の一端側の上部には、一端が蒸気発生器30の炉筒32に接続された飽和水蒸気路11の他端が接続されている。
つまり、飽和水蒸気路11を通して飽和水蒸気Vbが蒸気発生器30から容器42内に供給され、その容器42内で飽和水蒸気Vbが電気ヒータ41により加熱されることにより、過熱蒸気Vaが生成される。又、ヒータ駆動部43により電気ヒータ41に通電される電力が調整されて、電気ヒータ41の加熱温度が調整されることにより、過熱蒸気生成器40にて生成される過熱蒸気Vaの温度が調整される。
As shown in detail in FIG. 2, the superheated steam generator 40 is configured by disposing a U-shaped electric heater 41 on one end of the container 42 in a container 42 closed at both ends. Furthermore, a heater drive unit 43 that drives the electric heater 41 is also provided.
The other end of the saturated steam channel 11, one end of which is connected to the furnace tube 32 of the steam generator 30, is connected to the upper portion on one end side of the container 42.
That is, saturated steam Vb is supplied from the steam generator 30 into the container 42 through the saturated steam path 11, and the saturated steam Vb is heated by the electric heater 41 in the container 42, thereby generating superheated steam Va. Further, the electric power supplied to the electric heater 41 is adjusted by the heater driving unit 43 and the heating temperature of the electric heater 41 is adjusted, so that the temperature of the superheated steam Va generated by the superheated steam generator 40 is adjusted. Is done.

図1及び図2に示すように、容器42における飽和水蒸気路11が接続された側とは反対側の端部の上部には、容器42内で生成された過熱蒸気Vaを送出する過熱蒸気路20の一端が接続され、図3にも示すように、この過熱蒸気路20の他端は、過熱蒸気通流部Rに接続され、更に、過熱蒸気通流部Rには、その過熱蒸気通流部Rから排蒸気Vcを排出させる排蒸気路21が接続されている。
図2に示すように、過熱蒸気路20における容器42側の部分には、内部を通流する過熱蒸気Vaの温度を検出する過熱蒸気温度センサ22が設けられている。
又、過熱蒸気通流部Rから排出されて排蒸気路21を通流する排蒸気Vcと給水路18を通流する過熱蒸気生成用の水Wとを熱交換させて、その過熱蒸気生成用の水Wを予熱する予熱器23が設けられている。
As shown in FIGS. 1 and 2, the superheated steam path for sending the superheated steam Va generated in the container 42 is disposed at the upper portion of the end of the container 42 opposite to the side where the saturated steam path 11 is connected. As shown in FIG. 3, the other end of the superheated steam passage 20 is connected to the superheated steam flow section R, and further, the superheated steam flow section R is connected to the superheated steam flow section R. An exhaust steam path 21 for discharging the exhaust steam Vc from the flow part R is connected.
As shown in FIG. 2, a superheated steam temperature sensor 22 that detects the temperature of the superheated steam Va flowing through the inside is provided at a portion of the superheated steam path 20 on the container 42 side.
Further, heat exchange is performed between the exhaust steam Vc discharged from the superheated steam flow section R and flowing through the exhaust steam path 21 and the superheated steam generation water W flowing through the water supply path 18 to generate the superheated steam. A preheater 23 for preheating the water W is provided.

次に、制御部2の制御動作について、説明する。
制御部2は、調理油温度センサ10にて検出される調理油Lの温度が操作部3の温度設定部にて設定された加熱目標温度になるように、ガスバーナ31へのガス燃料の供給量を調整すべく、燃料供給量調整弁16を制御すると共に、ガスバーナ31への燃焼用空気の供給量を燃料供給量調整弁16により調整されるガス燃料の供給量に応じて調整すべく、空気ブロア13を制御する。
又、制御部2は、炉筒32内の水Wの水位を検出する水位センサ(図示省略)の検出水位が予め設定された設定水位になるように、炉筒32への水Wの供給量を調整すべく、給水ポンプ17を制御する。
ちなみに、設定水位は、全ての煙管33が浸漬される状態で、炉筒32内の上部に気相部が形成される所定の水位に設定される。
Next, the control operation of the control unit 2 will be described.
The control unit 2 supplies the gas fuel to the gas burner 31 so that the temperature of the cooking oil L detected by the cooking oil temperature sensor 10 becomes the heating target temperature set by the temperature setting unit of the operation unit 3. In order to adjust the fuel supply amount adjustment valve 16, the supply amount of combustion air to the gas burner 31 is adjusted in accordance with the supply amount of gas fuel adjusted by the fuel supply amount adjustment valve 16. The blower 13 is controlled.
Further, the control unit 2 supplies the water W to the furnace tube 32 so that the detected water level of a water level sensor (not shown) that detects the water level of the water W in the furnace tube 32 becomes a preset water level. The feed water pump 17 is controlled to adjust the above.
Incidentally, the set water level is set to a predetermined water level in which a gas phase portion is formed in the upper part of the furnace tube 32 in a state where all the smoke pipes 33 are immersed.

制御部2は、過熱蒸気温度センサ22にて検出される過熱蒸気Vaの温度が調理油Lの自然発火温度よりも低い温度に設定された生成目標温度になるように、ヒータ駆動部43へ通電する電力を調整するように構成されている。ちなみに、調理油Lの自然発火温度が350℃程度の場合、生成目標温度は、例えば、250℃に設定される。
つまり、制御部2及びヒータ駆動部43により、蒸気温度調整部Cが構成されることになる。
The control unit 2 energizes the heater driving unit 43 so that the temperature of the superheated steam Va detected by the superheated steam temperature sensor 22 becomes a generation target temperature set to a temperature lower than the spontaneous ignition temperature of the cooking oil L. It is configured to adjust the power to be. Incidentally, when the spontaneous ignition temperature of the cooking oil L is about 350 ° C., the generation target temperature is set to 250 ° C., for example.
That is, the steam temperature adjustment unit C is configured by the control unit 2 and the heater driving unit 43.

次に、上述のように構成されたフライヤーの作動形態について、説明する。
給水路18を通して蒸気発生器30の炉筒32に供給されて炉筒32内に貯留される水Wが、炉筒32内で複数の煙管33により加熱されて、飽和水蒸気Vbが生成され、その飽和水蒸気Vbが飽和水蒸気路11を通して、過熱蒸気生成器40の容器42内に供給され、その容器42内で飽和水蒸気Vbが電気ヒータ41により加熱されることにより、温度が調理油Lの自然発火温度よりも低い生成目標温度に調整された過熱蒸気Vaが生成される。
Next, the operation mode of the fryer configured as described above will be described.
The water W supplied to the furnace tube 32 of the steam generator 30 through the water supply path 18 and stored in the furnace tube 32 is heated by the plurality of smoke pipes 33 in the furnace tube 32 to generate saturated steam Vb, The saturated steam Vb is supplied into the container 42 of the superheated steam generator 40 through the saturated steam path 11, and the saturated steam Vb is heated by the electric heater 41 in the container 42, so that the temperature of the cooking oil L is spontaneously ignited. Superheated steam Va adjusted to a generation target temperature lower than the temperature is generated.

そのように生成された過熱蒸気Vaが容器42から過熱蒸気路20を通して過熱蒸気通流部Rに供給されて、過熱蒸気通流部Rを通流することにより、油槽1における上方部分1u内の揚げ調理ゾーンZfの調理油Lが集中的に加熱され、油槽1における底部部分1b内に、揚げ調理ゾーンZfよりも調理油Lの温度が低いクールゾーンZcが形成される。
この際、ガスバーナ31の燃焼量が調整されて、過熱蒸気通流部Rに供給される過熱蒸気Vaの供給量が調整されることにより、油槽1における揚げ調理ゾーンZf内の調理油Lの温度が加熱目標温度に調整される。
The superheated steam Va thus generated is supplied from the container 42 through the superheated steam passage 20 to the superheated steam flow section R and flows through the superheated steam flow section R, so that the inside of the upper portion 1u in the oil tank 1 The cooking oil L in the fried cooking zone Zf is intensively heated, and a cool zone Zc in which the temperature of the cooking oil L is lower than that in the fried cooking zone Zf is formed in the bottom portion 1 b of the oil tank 1.
At this time, the combustion amount of the gas burner 31 is adjusted, and the supply amount of the superheated steam Va supplied to the superheated steam passage R is adjusted, whereby the temperature of the cooking oil L in the frying cooking zone Zf in the oil tank 1 is adjusted. Is adjusted to the heating target temperature.

過熱蒸気通流部Rを通流する過熱蒸気Vaは、調理油Lを加熱することにより温度が低下し、排蒸気Vcとして排蒸気路21を通して排出される。
そして、予熱器23において、排蒸気路21を通流する排蒸気Vcにより給水路18を通流する水Wが加熱されることにより、蒸気発生器30に供給される過熱蒸気生成用の水Wが予熱される。
The temperature of the superheated steam Va flowing through the superheated steam flow section R decreases as the cooking oil L is heated, and is discharged through the exhaust steam path 21 as exhaust steam Vc.
Then, in the preheater 23, the water W flowing through the water supply passage 18 is heated by the exhaust steam Vc flowing through the exhaust steam passage 21, whereby the superheated steam generation water W supplied to the steam generator 30. Is preheated.

即ち、過熱蒸気通流部Rを油槽1の外側面1sを全周にわたって覆う状態で配置する構成とすることにより、油槽1の外側面1sに対して、過熱蒸気通流部Rを効果的に広範囲に配置することができるので、油槽1内の調理油Lを広範囲にわたって加熱することが可能となり、加熱効率を向上することができる。
又、過熱蒸気通流部Rに供給される過熱蒸気Vaの温度が、油槽1内の調理油Lの自然発火温度よりも低くなるように調整されるので、油槽1及び過熱蒸気通流部Rの熱疲労を効果的に抑制することができる。このことにより、熱疲労を効果的に抑制して、油槽1及び過熱蒸気通流部Rにクラックが入るのを確実に防止しながら、油槽1及び過熱蒸気通流部Rを熱伝導率が高くしかも安価な材料を用いて構成することができる。
従って、フライヤーの清掃性及び加熱効率の向上並びに低廉化を図りながら、油槽1内の調理油Lの自然発火を防止することができる。
That is, the superheated steam flow portion R is effectively disposed on the outer surface 1 s of the oil tank 1 by arranging the superheated steam flow portion R so as to cover the outer surface 1 s of the oil tank 1 over the entire circumference. Since it can arrange | position in a wide range, it becomes possible to heat the cooking oil L in the oil tank 1 over a wide range, and can improve a heating efficiency.
Further, since the temperature of the superheated steam Va supplied to the superheated steam flow section R is adjusted to be lower than the spontaneous ignition temperature of the cooking oil L in the oil tank 1, the oil tank 1 and the superheated steam flow section R are adjusted. Thermal fatigue can be effectively suppressed. This effectively suppresses thermal fatigue and reliably prevents the oil tank 1 and the superheated steam flow part R from cracking, while making the oil tank 1 and the superheated steam flow part R have high thermal conductivity. And it can comprise using an inexpensive material.
Therefore, spontaneous combustion of the cooking oil L in the oil tank 1 can be prevented while improving the fryer cleaning performance and heating efficiency and reducing the cost.

又、油カスや食品カスは、油槽1内の底部に集まるが、油槽1内の底部側に、上方側の揚げ調理ゾーンZfよりも調理油Lの温度が低いクールゾーンZcが形成されるので、油カスや食品カスが焦げ難く、調理油Lの劣化を低減できる。   Oil residue and food residue are collected at the bottom of the oil tank 1, but a cool zone Zc is formed on the bottom side of the oil tank 1 where the cooking oil L is lower in temperature than the fried cooking zone Zf on the upper side. Oil residue and food residue are hard to burn and deterioration of cooking oil L can be reduced.

〔別実施形態〕
次に別実施形態を説明する。
(イ) 油槽1の外側面1sを全周にわたって覆う状態で配置する過熱蒸気通流部Rの配置形態は、上記の実施形態において例示した形態、即ち、油槽1の上方部分1uの外側面1sを全周にわたって覆う配置形態に限定されるものではない。例えば、油槽1の外側面1sの全面を覆う配置形態でも良い。又、過熱蒸気通流部Rとして、油槽1の外側面1sを全周にわたって覆う状態の部分に加えて、油槽1の底部の外面を覆う状態の部分を追加しても良い。
[Another embodiment]
Next, another embodiment will be described.
(A) The arrangement form of the superheated steam flow portion R arranged so as to cover the outer surface 1 s of the oil tank 1 over the entire circumference is the form illustrated in the above embodiment, that is, the outer surface 1 s of the upper portion 1 u of the oil tank 1. Is not limited to the arrangement form covering the entire circumference. For example, the arrangement | positioning form which covers the whole outer surface 1s of the oil tank 1 may be sufficient. Moreover, in addition to the part of the state which covers the outer surface 1s of the oil tank 1 over the whole periphery, you may add the part of the state which covers the outer surface of the bottom part of the oil tank 1 as the superheated steam flow part R.

(ロ) 過熱蒸気生成装置Sを蒸気発生器30と過熱蒸気生成器40とを備えて構成する場合に、蒸気発生器30の熱源や過熱蒸気生成器40の熱源は、上記の実施形態において例示した熱源に限定されるものではない。例えば、蒸気発生器30の熱源として、上記の実施形態のガスバーナ31に代えて、電気ヒータ等の電気式加熱部を用いても良い。又、過熱蒸気生成器40の熱源として、上記の実施形態の電気ヒータ41に代えて、ガスバーナ等のバーナを用いても良い。
又、上記の実施形態では、蒸気発生器30と過熱蒸気生成器40とを別体に構成したが、一体的に構成しても良い。
(B) When the superheated steam generator S is configured to include the steam generator 30 and the superheated steam generator 40, the heat source of the steam generator 30 and the heat source of the superheated steam generator 40 are exemplified in the above embodiment. The heat source is not limited to the above. For example, instead of the gas burner 31 of the above embodiment, an electric heating unit such as an electric heater may be used as the heat source of the steam generator 30. Further, as a heat source of the superheated steam generator 40, a burner such as a gas burner may be used instead of the electric heater 41 of the above-described embodiment.
Moreover, in said embodiment, although the steam generator 30 and the superheated steam generator 40 were comprised separately, you may comprise integrally.

(ハ) 過熱蒸気通流部R内に、過熱蒸気Vaを蛇行状等に通流させる通流案内部材を設けて、過熱蒸気通流部R内における過熱蒸気Vaの通流経路を長くしても良い。このことにより、加熱効率を更に向上させることができる。 (C) In the superheated steam flow section R, a flow guide member for flowing the superheated steam Va in a meandering manner is provided, and the flow path of the superheated steam Va in the superheated steam flow section R is lengthened. Also good. Thereby, the heating efficiency can be further improved.

(ニ) 油槽1の形状は、上記の実施形態において例示した形状、即ち、平面視形状が正方向で下窄まり状に限定されるものではない。例えば、平面視形状が長方形状や円状でも良い。そして、過熱蒸気通流部Rは、油槽1の形状に合わせて、油槽1の外周面のうち、少なくとも外側面1sを全周にわたって覆う状態で配置することになる。 (D) The shape of the oil tank 1 is not limited to the shape exemplified in the above-described embodiment, that is, the shape in plan view is constricted in the forward direction. For example, the planar view shape may be rectangular or circular. And the superheated steam flow part R is arrange | positioned in the state which covers at least the outer surface 1s over the perimeter among the outer peripheral surfaces of the oil tank 1 according to the shape of the oil tank 1. FIG.

以上説明したように、清掃性及び加熱効率の向上並びに低廉化を図りながら、油槽内の調理油の自然発火を防止し得るフライヤーを提供することができる。   As described above, it is possible to provide a fryer that can prevent spontaneous combustion of cooking oil in an oil tank while improving cleanability and heating efficiency and reducing the cost.

1 油槽
1s 外側面
23 予熱器
30 蒸気発生器
31 ガスバーナ(バーナ)
40 過熱蒸気生成器
41 電気ヒータ(電気式加熱部)
C 蒸気温度調整部
H 加熱手段
L 調理油
R 過熱蒸気通流部
S 過熱蒸気生成装置
Va 過熱蒸気
Vb 飽和水蒸気
Vc 排蒸気
W 水
Zc クールゾーン
DESCRIPTION OF SYMBOLS 1 Oil tank 1s outer surface 23 Preheater 30 Steam generator 31 Gas burner (burner)
40 Superheated steam generator 41 Electric heater (electric heating unit)
C Steam temperature adjusting part H Heating means L Cooking oil R Superheated steam flow part S Superheated steam generator Va Superheated steam Vb Saturated steam Vc Waste steam W Water Zc Cool zone

Claims (4)

調理油を収容する油槽と、その油槽内の調理油を加熱する加熱手段とが設けられたフライヤーであって、
前記加熱手段が、過熱蒸気を生成する過熱蒸気生成装置と、その過熱蒸気生成装置にて生成された過熱蒸気を流動させる過熱蒸気通流部とを備えて構成され、
前記過熱蒸気通流部が、前記油槽の外側面を全周にわたって覆う状態で配置され、
前記過熱蒸気生成装置が、生成する過熱蒸気の温度を調整可能な蒸気温度調整部を備え、
前記蒸気温度調整部が、前記過熱蒸気の温度を前記油槽内の調理油の自然発火温度よりも低い温度に調整するように構成されているフライヤー。
A fryer provided with an oil tank for containing cooking oil and a heating means for heating the cooking oil in the oil tank,
The heating means includes a superheated steam generator that generates superheated steam, and a superheated steam flow section that flows the superheated steam generated by the superheated steam generator,
The superheated steam flow portion is arranged in a state of covering the entire outer surface of the oil tank,
The superheated steam generator includes a steam temperature adjustment unit capable of adjusting the temperature of the superheated steam to be generated,
The said fryer is comprised so that the said steam temperature adjustment part may adjust the temperature of the said superheated steam to temperature lower than the spontaneous ignition temperature of the cooking oil in the said oil tank.
前記過熱蒸気通流部が、前記油槽の外側面における上方側の部分を覆うように配置されて、前記油槽における底部側に、上方側の部分よりも調理油の温度が低いクールゾーンが形成される請求項1に記載のフライヤー。   The superheated steam flow part is disposed so as to cover the upper part of the outer surface of the oil tank, and a cool zone in which the cooking oil temperature is lower than that of the upper part is formed on the bottom side of the oil tank. The flyer according to claim 1. 前記過熱蒸気生成装置が、供給される水をバーナを熱源として加熱して飽和水蒸気を生成する蒸気発生器と、その蒸気発生器から供給される飽和水蒸気を電気式加熱部を熱源として加熱して過熱蒸気を生成する過熱蒸気生成器とを備えて構成され、
前記蒸気温度調整部が、前記電気式加熱部に供給する電力を調整することにより、前記過熱蒸気の温度を調整するように構成されている請求項1又は2に記載のフライヤー。
The superheated steam generator heats supplied water using a burner as a heat source to generate saturated steam, and heats saturated steam supplied from the steam generator using an electric heating unit as a heat source. And a superheated steam generator for generating superheated steam,
The fryer according to claim 1 or 2, wherein the steam temperature adjusting unit is configured to adjust a temperature of the superheated steam by adjusting electric power supplied to the electric heating unit.
前記過熱蒸気通流部から排出された排蒸気と前記過熱蒸気生成装置に供給される過熱蒸気生成用の水とを熱交換させて、その過熱蒸気生成用の水を予熱する予熱器が設けられている請求項1〜3のいずれか1項に記載のフライヤー。   There is provided a preheater that preheats the superheated steam generation water by exchanging heat between the exhaust steam discharged from the superheated steam flow section and the superheated steam generation water supplied to the superheated steam generation device. The fryer according to any one of claims 1 to 3.
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