JP7190627B2 - Superheated steam generator and cooker - Google Patents

Superheated steam generator and cooker Download PDF

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JP7190627B2
JP7190627B2 JP2018155890A JP2018155890A JP7190627B2 JP 7190627 B2 JP7190627 B2 JP 7190627B2 JP 2018155890 A JP2018155890 A JP 2018155890A JP 2018155890 A JP2018155890 A JP 2018155890A JP 7190627 B2 JP7190627 B2 JP 7190627B2
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heater
pipe
superheater
evaporative
superheated steam
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JP2020029991A (en
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周平 野村
浩朗 新田
孝夫 後藤
裕二 平石
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Panasonic Intellectual Property Management Co Ltd
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Panasonic Intellectual Property Management Co Ltd
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Priority to EP19761039.7A priority patent/EP3760923A4/en
Priority to PCT/JP2019/002160 priority patent/WO2019167488A1/en
Priority to CN201980003856.5A priority patent/CN111051775A/en
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Description

本発明は、100℃以上の蒸気を生成する過熱蒸気発生装置、及びこの過熱蒸気発生装置を備える調理器に関するものである。 TECHNICAL FIELD The present invention relates to a superheated steam generator that generates steam of 100° C. or higher, and a cooker equipped with this superheated steam generator.

従来の過熱蒸気発生装置としては、特許文献1に開示されたものがある。図11は特許文献1に記載の過熱蒸気発生装置の断面図である。図11に示すように、この過熱蒸気発生装置の蒸気生成容器30内には蒸発ヒータ32が埋設されており、蒸気生成容器30内の蒸発ヒータ32よりも高所の位置には過熱ヒータ33が埋設されている。蒸気生成容器30内には蒸気生成室31が設けられており、蒸発ヒータ32は給水口35から蒸気生成室31内に供給された水を蒸発させ、蒸気を生成する。生成された蒸気bは蒸気生成室31内を上昇途中に、過熱ヒータ33により加熱されたフィン群34と接触し、フィン群34によって蒸気bは過熱され、蒸気口36から蒸気生成容器30外部に放出される。この構成にすることで、蒸気bを過熱ヒータ33に供給するためのファン装置が不要になるため、構成を簡略化させることができる。また、過熱蒸気発生装置を取り付ける調理器内の調理室の有効面積がファン装置の影響で削減されることもなくなる。 As a conventional superheated steam generator, there is one disclosed in Patent Document 1. FIG. 11 is a cross-sectional view of the superheated steam generator described in Patent Document 1. FIG. As shown in FIG. 11, an evaporating heater 32 is embedded in the steam generating vessel 30 of this superheated steam generator, and a superheating heater 33 is positioned higher than the evaporating heater 32 in the steam generating vessel 30 . Buried. A steam generating chamber 31 is provided in the steam generating container 30, and the evaporation heater 32 evaporates water supplied from the water supply port 35 into the steam generating chamber 31 to generate steam. The generated steam b, on the way up in the steam generation chamber 31, comes into contact with the fin group 34 heated by the superheater 33, is superheated by the fin group 34, and flows out of the steam generation container 30 through the steam port 36. released. This configuration eliminates the need for a fan device for supplying the steam b to the superheater 33, thereby simplifying the configuration. Also, the effective area of the cooking chamber in the cooker to which the superheated steam generator is installed is not reduced due to the influence of the fan device.

特開2006-349313号公報JP-A-2006-349313

特許文献1の過熱蒸気発生装置では、同一の蒸気生成容器30内に蒸発ヒータ32と過熱ヒータ33を埋設した構成にすることで、蒸発ヒータ32の熱をフィン群34まで伝達させることができ、蒸発ヒータ32の熱を蒸気の過熱にも使用することができる。また、過熱ヒータ33の熱は蒸気生成容器30の蒸発ヒータ32近傍に伝達することで蒸気生成室31内の水を蒸発させることに使用することもできる。このような構成にすることで、蒸発ヒータ32による水の昇温、蒸発に使用される熱もしくは過熱ヒータ33で蒸気を過熱する熱に使用されない熱の余剰分をもう一方に供給することで、熱を有効活用し、より効率的な加熱を実現できる。 In the superheated steam generator of Patent Document 1, the evaporation heater 32 and the superheater 33 are embedded in the same steam generation container 30, so that the heat of the evaporation heater 32 can be transmitted to the fin group 34. The heat of the evaporative heater 32 can also be used to superheat the steam. The heat of the superheater 33 can also be used to evaporate the water in the steam generation chamber 31 by transferring it to the vicinity of the evaporation heater 32 of the steam generation container 30 . With such a configuration, the surplus heat not used for raising the temperature of the water by the evaporation heater 32, the heat used for evaporation, or the heat for superheating the steam by the superheater 33 is supplied to the other. Heat can be effectively used to achieve more efficient heating.

しかしながら、特許文献1の過熱蒸気発生装置では、蒸発ヒータ32により生成された蒸気が、上昇途中で過熱ヒータ33によって加熱されたフィン群34によって過熱される構成のため、フィン群34と蒸気の伝熱面積を十分に確保するためには、蒸気生成容器30の高さ方向の寸法を大きくする必要がある。この場合、蒸発ヒータ32と過熱ヒータ33の軸間距離が大きくなり、蒸発ヒータ32もしくは過熱ヒータ33の熱がもう一方の過熱ヒータ33もしくは蒸発ヒータ32に伝達するまでの経路において放熱量が増加し、熱効率が低減してしまう課題がある。 However, in the superheated steam generator of Patent Document 1, the steam generated by the evaporating heater 32 is superheated by the fin group 34 heated by the superheating heater 33 in the process of rising. In order to secure a sufficient heat area, it is necessary to increase the height dimension of the steam generating vessel 30 . In this case, the distance between the axes of the evaporative heater 32 and the superheating heater 33 increases, and the amount of heat released in the path until the heat of the evaporating heater 32 or the superheating heater 33 is transmitted to the other superheating heater 33 or the evaporating heater 32 increases. , there is a problem that the thermal efficiency is reduced.

本発明は、蒸発ヒータの直線部の軸間距離と過熱ヒータの直線部の軸間距離よりも、蒸発ヒータと過熱ヒータの軸間距離を短くする構成にすることで、蒸発ヒータが過熱ヒータ近傍に伝達させる経路もしくは過熱ヒータが蒸発ヒータ近傍に伝達させる経路での放熱量を低減させることができ、熱効率を向上させることができる過熱蒸気発生装置及びこの過熱蒸気発生装置を備える調理器を提供することを目的とする。 According to the present invention, the distance between the axes of the evaporating heater and the superheating heater is shorter than the distance between the axes of the straight parts of the evaporating heater and the distance between the axes of the straight parts of the superheating heater. Provided is a superheated steam generator and a cooker equipped with the superheated steam generator capable of reducing the amount of heat released in a path that transmits heat to a superheater or a path that a superheater transmits to the vicinity of an evaporating heater, thereby improving thermal efficiency. for the purpose.

前記従来の課題を解決するために、本発明の過熱蒸気発生装置は、
加熱容器と、前記加熱容器に水を供給する給水口と、前記加熱容器を加熱することで前記給水口から前記加熱容器に供給された水を蒸発させる蒸発ヒータと、前記蒸発ヒータにより生成した蒸気が通るパイプと、前記パイプの外側に配置され、前記パイプを加熱することで前記パイプ内を通過する蒸気を過熱する過熱ヒータと、を備え、前記蒸発ヒータと前記過熱ヒータはそれぞれ2つ以上の直線部を有しており、前記蒸発ヒータと前記過熱ヒータの軸間距離の最小距離が、前記蒸発ヒータの直線部の軸間距離の最大距離および前記過熱ヒータの直線部の軸間距離の最大距離よりも短くなるように構成するものである。
In order to solve the conventional problems, the superheated steam generator of the present invention includes:
a heating container, a water inlet for supplying water to the heating container, an evaporative heater for heating the heating container to evaporate the water supplied from the water inlet to the heating container, and steam generated by the evaporative heater and a superheater disposed outside the pipe for superheating the steam passing through the pipe by heating the pipe, wherein the evaporative heater and the superheater each have two or more The minimum distance between the axes of the evaporative heater and the superheating heater is the maximum distance between the axes of the straight part of the evaporating heater and the maximum distance between the axes of the straight parts of the superheating heater. It is configured to be shorter than the distance.

これによって、蒸発ヒータが過熱ヒータ近傍に伝達させる経路もしくは過熱ヒータが蒸発ヒータ近傍に伝達させる経路での放熱量を低減することで、熱効率を向上させた過熱蒸気生成装置を提供することができる。 As a result, it is possible to provide a superheated steam generator with improved thermal efficiency by reducing the amount of heat released in the path in which the evaporating heater transmits heat to the vicinity of the superheater or in the path in which the superheating heater transmits heat to the vicinity of the evaporating heater.

本発明では、蒸発ヒータの直線部の軸間距離と過熱ヒータの直線部の軸間距離よりも、蒸発ヒータと過熱ヒータの軸間距離を短くする構成にすることで、蒸発ヒータが過熱ヒータ近傍に伝達させる経路もしくは過熱ヒータが蒸発ヒータ近傍に伝達させる経路での放熱量を低減させることができ、熱効率を向上させることができる。 In the present invention, the distance between the axes of the evaporating heater and the superheating heater is shorter than the distance between the axes of the straight parts of the evaporating heater and the distance between the axes of the straight parts of the superheating heater. The amount of heat radiated in the path through which the heat is transmitted to or through the path through which the overheating heater transmits to the vicinity of the evaporative heater can be reduced, and the thermal efficiency can be improved.

本発明の実施の形態1における過熱蒸気発生装置の斜視図BRIEF DESCRIPTION OF THE DRAWINGS The perspective view of the superheated steam generator in Embodiment 1 of this invention. 本発明の実施の形態1における過熱蒸気発生装置の分解斜視図1 is an exploded perspective view of a superheated steam generator according to Embodiment 1 of the present invention; 図1におけるX方向から見た同過熱蒸気発生装置の外観図External view of the superheated steam generator viewed from the X direction in FIG. 図1におけるY方向から見た同過熱蒸気発生装置の外観図External view of the same superheated steam generator viewed from the Y direction in FIG. 図3におけるA-A線断面図AA line sectional view in FIG. 図4におけるB-B線断面図BB line sectional view in FIG. 図4におけるC-C線断面図CC line sectional view in FIG. 本発明の実施の形態1における過熱蒸気発生装置を搭載したオーブンの構成の模式図Schematic diagram of the configuration of an oven equipped with a superheated steam generator according to Embodiment 1 of the present invention 本発明の実施の形態2における過熱蒸気発生装置の斜視図A perspective view of a superheated steam generator according to Embodiment 2 of the present invention. 本発明の実施の形態2における過熱蒸気発生装置の分解斜視図An exploded perspective view of a superheated steam generator according to Embodiment 2 of the present invention. 特許文献1に示す従来の過熱蒸気発生装置の概略構成を示す模式断面図Schematic cross-sectional view showing a schematic configuration of a conventional superheated steam generator shown in Patent Document 1

第1の発明は、加熱容器と、前記加熱容器に水を供給する給水口と、前記加熱容器を加熱することで前記給水口から前記加熱容器に供給された水を蒸発させる蒸発ヒータと、前記蒸発ヒータにより生成した蒸気が通るパイプと、前記パイプの外側に配置され、前記パイプを加熱することで前記パイプ内を通過する蒸気を過熱する過熱ヒータと、を備え、前記蒸発ヒータと前記過熱ヒータはそれぞれ2つ以上の直線部を有しており、前記蒸発ヒータと前記過熱ヒータの軸間距離の最小距離が、前記蒸発ヒータの直線部の軸間距離の最大距離および前記過熱ヒータの直線部の軸間距離の最大距離よりも短くなるように構成された過熱蒸気生成装置である。 A first invention comprises a heating container, a water supply port for supplying water to the heating container, an evaporation heater for heating the heating container to evaporate the water supplied from the water supply port to the heating container, and a pipe through which steam generated by an evaporative heater passes; and a superheater disposed outside the pipe for superheating the steam passing through the pipe by heating the pipe, wherein the evaporative heater and the superheater each has two or more straight parts, and the minimum distance between the axes of the evaporative heater and the superheater is the maximum distance between the axes of the straight parts of the evaporative heater and the straight part of the superheater The superheated steam generator is configured to be shorter than the maximum distance between the axes of the.

これにより、蒸発ヒータと過熱ヒータの距離が近づくことで、蒸発ヒータの熱が過熱ヒータ近傍に熱が伝達するもしくは過熱ヒータの熱が蒸発ヒータ近傍に伝達する経路での放熱量を低減することができ、熱効率を向上させることできる。 As a result, the distance between the evaporative heater and the superheater is reduced, so that the heat of the evaporative heater is transferred to the vicinity of the superheater, or the heat of the superheater is transferred to the vicinity of the evaporative heater. It is possible to improve the thermal efficiency.

第2の発明は、特に、第1の発明において、前記給水口から給水された水は前記蒸発ヒータの長手方向に沿って移動し、前記蒸発ヒータによって生成した蒸気は、前記蒸発ヒータもしくは前記過熱ヒータの長手方向に沿って移動するように構成された過熱蒸気発生装
置である。
In a second invention, particularly in the first invention, the water supplied from the water supply port moves along the longitudinal direction of the evaporative heater, and the steam generated by the evaporative heater is transferred to the evaporative heater or the superheater. The superheated steam generator is configured to move along the longitudinal direction of the heater.

これにより、水が移動する加熱容器内の流路に対して蒸発ヒータの距離が近い状態を維持しやすくなり、蒸発ヒータからの熱が水に伝達しやすくなることで、水を効率的に昇温、蒸発させることができる。また、蒸発した蒸気が移動する流路においても、蒸発ヒータの距離が近い状態を維持しやすくなり、過熱ヒータの熱が蒸気に伝達しやすくなることで、蒸気の温度を効率的に高められる。また、蒸発ヒータで加熱される水は、蒸発ヒータに沿った流路途中で蒸発した場合、残りの蒸発ヒータに沿った流路において100℃以上に過熱することもできる。 As a result, it becomes easier to keep the evaporating heater close to the flow path in the heating container where the water moves, and the heat from the evaporating heater can be easily transferred to the water, so that the water can be raised efficiently. Warm and allow to evaporate. Also, in the flow path through which the evaporated steam moves, the evaporative heaters are easily kept close to each other, and the heat of the superheater is easily transferred to the steam, so that the temperature of the steam can be efficiently increased. Further, when the water heated by the evaporation heater evaporates in the middle of the flow path along the evaporation heater, it can be superheated to 100° C. or more in the remaining flow path along the evaporation heater.

第3の発明は、特に、第1の発明において、前記パイプ内には熱交換促進部が設けられ、前記熱交換促進部は芯棒と、前記芯棒の外周に巻きつけられた螺旋体で構成された過熱蒸気発生装置である。 In a third invention, in particular, in the first invention, a heat exchange promoting portion is provided in the pipe, and the heat exchange promoting portion is composed of a core rod and a helical body wound around the outer periphery of the core rod. It is a superheated steam generator.

これにより、パイプ内を通過する蒸気は、螺旋体に沿ってパイプ内を移動することで、過熱ヒータにより昇温したパイプ内面と蒸気の接触面積が拡大することでき、熱交換効率を向上させることができる。 As a result, the steam passing through the pipe moves inside the pipe along the helical body, increasing the contact area between the inner surface of the pipe heated by the superheater and the steam, thereby improving the heat exchange efficiency. can.

第4の発明は、特に、第1の発明において、前記蒸発ヒータと、前記パイプと、前記過熱ヒータそれぞれが前記加熱容器と密着するように構成された過熱蒸気発生装置である。 A fourth invention is the superheated steam generator according to the first invention, wherein the evaporating heater, the pipe, and the superheating heater are configured to be in close contact with the heating vessel.

これにより、蒸発ヒータの熱が過熱ヒータ近傍に熱が伝達するもしくは過熱ヒータの熱が蒸発ヒータ近傍に伝達するときに、熱を介する物質を加熱容器のみにすることで、素早い熱移動が可能となる。 As a result, when the heat of the evaporative heater is transferred to the vicinity of the superheater, or when the heat of the superheater is transferred to the vicinity of the evaporative heater, the heat is transferred only to the heating container, enabling rapid heat transfer. Become.

第5の発明は、特に、第1の発明において、前記パイプと前記過熱ヒータの間に伝熱部が設けられ、前記加熱容器と前記給水口と前記蒸発ヒータで構成された蒸発部と、前記パイプと前記過熱ヒータと前記伝熱部で構成された過熱部が接合する接合部を備えた過熱蒸気発生装置である。 In a fifth aspect, in particular, in the first aspect, a heat transfer section is provided between the pipe and the overheating heater, and an evaporating section composed of the heating vessel, the water supply port, and the evaporating heater; The superheated steam generator is provided with a joint where a superheating section composed of a pipe, the superheater, and the heat transfer section is joined.

これにより、パイプの外部に設けられた過熱ヒータの熱が伝熱部を介してパイプに伝達されることで、過熱ヒータの熱がパイプに効率的に伝達され、過熱ヒータの熱で効率的に蒸気を過熱することが可能となる。また、接合部で蒸発部と過熱部を接合させることで、蒸発ヒータの熱が過熱部に熱が伝達するもしくは過熱ヒータの熱が蒸発部に伝達するときに、熱伝達の抵抗になる物質を介することを極力減らすことで、素早い熱移動が可能となる。 As a result, the heat of the superheater provided outside the pipe is transferred to the pipe via the heat transfer section, so that the heat of the superheater is efficiently transferred to the pipe, and the heat of the superheater efficiently heats the pipe. Steam can be superheated. In addition, by joining the evaporating part and the superheating part at the joining part, when the heat of the evaporating heater is transferred to the superheating part or when the heat of the superheating heater is transferred to the evaporating part, the substance that acts as resistance to heat transfer is eliminated. By minimizing the amount of intervening heat, quick heat transfer becomes possible.

第6の発明は、第1~5のいずれか1つの発明の過熱蒸気発生装置を備えた調理器である。これにより、過熱蒸気を使用した高性能な調理が可能となる。 A sixth invention is a cooker equipped with the superheated steam generator of any one of the first to fifth inventions. This enables high-performance cooking using superheated steam.

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。また、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。 BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, embodiments of the present invention will be described with reference to the drawings. Also, the present invention is not limited by this embodiment.

(実施の形態1)
図1~図8を用いて、本発明の実施の形態1における過熱蒸気発生装置の構成とその過熱蒸気発生装置を備えた調理器について説明する。図1には本発明の実施の形態1における過熱蒸気発生装置の斜視図を示す。図2には本発明の実施の形態1における過熱蒸気発生装置の分解斜視図を示す。図3には図1におけるX方向から見た同過熱蒸気発生装置の外観図を示す。図4には図1におけるY方向から見た同過熱蒸気発生装置の外観図を示す。図5には図3におけるA-A線断面図を示す。図6には図4におけるB-B線断面図を
示す。図7には図4におけるC-C線断面図を示す。図8には本発明の実施の形態1における過熱蒸気発生装置を搭載したオーブンの構成の模式図を示す。
(Embodiment 1)
A configuration of a superheated steam generator and a cooker equipped with the superheated steam generator according to Embodiment 1 of the present invention will be described with reference to FIGS. 1 to 8. FIG. FIG. 1 shows a perspective view of a superheated steam generator according to Embodiment 1 of the present invention. FIG. 2 shows an exploded perspective view of the superheated steam generator according to Embodiment 1 of the present invention. FIG. 3 shows an external view of the superheated steam generator viewed from the X direction in FIG. FIG. 4 shows an external view of the superheated steam generator viewed from the Y direction in FIG. FIG. 5 shows a cross-sectional view taken along line AA in FIG. FIG. 6 shows a cross-sectional view taken along line BB in FIG. FIG. 7 shows a sectional view taken along line CC in FIG. FIG. 8 shows a schematic diagram of the configuration of an oven equipped with a superheated steam generator according to Embodiment 1 of the present invention.

図1~図7に示すように、本実施の形態1における過熱蒸気発生装置10は、空間状の加熱容器内11Aを有する加熱容器11と、加熱容器11の開口部を塞ぐように構成された加熱容器カバー12と、加熱容器カバー12の外側面に取り付けられ、加熱容器内11Aに水を供給する給水管13Aを有している。給水管13Aの一端である給水口13は、加熱容器内11Aと連通している。加熱容器内11Aには、給水口13から供給された水が流れる流路が蛇行するように複数のフィンが形成されている。 As shown in FIGS. 1 to 7, the superheated steam generator 10 according to the first embodiment includes a heating container 11 having a space-like heating container interior 11A and an opening of the heating container 11. It has a heating container cover 12 and a water supply pipe 13A attached to the outer surface of the heating container cover 12 and supplying water to the inside 11A of the heating container. A water supply port 13, which is one end of the water supply pipe 13A, communicates with the inside of the heating container 11A. A plurality of fins are formed in the inside 11A of the heating container so that the flow path through which the water supplied from the water supply port 13 flows meanders.

加熱容器内11Aは、略直方体で形成され、一方の短辺部がU字形状で形成されている。過熱蒸気発生装置10は、U字形状で形成されたヒータである蒸発ヒータ14と過熱ヒータ15をさらに有している。加熱容器内11Aに蒸発ヒータ14と過熱ヒータ15とパイプ16が密着するように、加熱容器11に蒸発ヒータ14と過熱ヒータ15とパイプ16が埋設されている。蒸発ヒータ14は、加熱容器11を加熱することで給水口13から加熱容器11に供給された水を蒸発させる構成である。パイプ16は、蒸発ヒータ14により加熱容器内11Aで生成された蒸気が通る構成である。パイプ16の一端は加熱容器カバー12と離間し、加熱容器内11Aと連通している。過熱ヒータ15は、パイプ16の外側に配置され、パイプ16を加熱することでパイプ16内を通過する蒸気を過熱する構成である。 The inside 11A of the heating container is formed in a substantially rectangular parallelepiped shape, and one short side portion is formed in a U shape. The superheated steam generator 10 further includes an evaporating heater 14 and a superheating heater 15 which are U-shaped heaters. An evaporative heater 14, a superheater 15 and a pipe 16 are embedded in the heating container 11 so that the evaporative heater 14, the superheater 15 and the pipe 16 are in close contact with each other in the heating container 11A. The evaporation heater 14 is configured to evaporate the water supplied to the heating container 11 from the water supply port 13 by heating the heating container 11 . The pipe 16 has a structure through which the vapor generated in the heating container 11A by the evaporation heater 14 passes. One end of the pipe 16 is separated from the heating container cover 12 and communicates with the inside 11A of the heating container. The superheater 15 is arranged outside the pipe 16 and heats the pipe 16 to superheat the steam passing through the pipe 16 .

図4と図6に示すように、外部から給水管13Aを通して給水口13から水が加熱容器内11Aに供給される。外部から供給される水は水道水を想定しており、通常0~30℃の温度で供給される。加熱容器内11Aに供給された水aは加熱容器内11Aの蒸発ヒータ14の長手方向となる直線部14bに沿った流路を通る。直線部14bに沿った流路を形成することで、加熱容器内11Aの流路と蒸発ヒータ14の距離が近い構成となり、流路に蒸発ヒータ14の熱が伝達しやすくなる。加熱容器内11Aに給水された水aは加熱容器内11Aの流路を通り、水aは蒸発ヒータ14によって加熱された加熱容器11から熱を受けて加熱される。加熱容器11の流路は水aが蛇行するように構成することで、加熱容器11と水aとの接触面積を増加させ、熱交換効率を向上させることもできる。加熱容器内11Aで加熱された水aは加熱容器内11Aが大気圧とした場合、100℃付近に達すると蒸発し始める。蒸発した水aは図6中、点線で示す蒸気bとして加熱容器内11Aを移動する。加熱容器内11Aの流路途中で蒸発した場合、蒸気bはパイプ16に到達するまでの加熱容器内11Aの流路で100℃以上に過熱させることも可能である。 As shown in FIGS. 4 and 6, water is supplied from the outside through a water supply pipe 13A into the heating vessel 11A from a water supply port 13. As shown in FIG. The water supplied from the outside is assumed to be tap water, and is usually supplied at a temperature of 0 to 30°C. The water a supplied to the inside 11A of the heating container passes through the flow path along the straight portion 14b which is the longitudinal direction of the evaporation heater 14 inside the heating container 11A. By forming the flow path along the straight portion 14b, the distance between the flow path in the heating container 11A and the evaporative heater 14 becomes short, and the heat of the evaporative heater 14 is easily transferred to the flow path. The water a supplied to the inside 11A of the heating container passes through the flow path of the inside 11A of the heating container, and the water a receives heat from the heating container 11 heated by the evaporation heater 14 and is heated. By configuring the flow path of the heating container 11 so that the water a meanders, the contact area between the heating container 11 and the water a can be increased, and the heat exchange efficiency can be improved. The water a heated in the heating container 11A starts to evaporate when the pressure in the heating container 11A reaches around 100° C. when the pressure in the heating container 11A is atmospheric pressure. The evaporated water a moves inside the heating container 11A as steam b indicated by a dotted line in FIG. When the vapor b evaporates in the flow path of the heating container 11A, it can be superheated to 100.degree.

蒸発ヒータ14により蒸発した加熱容器内11Aの蒸気bは、図5と図6に示すようにパイプ16へ移動する。図7ないし図9に示すようにパイプ16の外部には過熱ヒータ15が設けてあり、過熱ヒータ15の熱は加熱容器11を介してパイプ16に伝達する構成となっている。パイプ16を通過する100℃以上の蒸気bは、過熱ヒータ15によって加熱されたパイプ16内面と接触し、過熱されることでさらに昇温し、パイプ16の他端から外部に排出される。 The vapor b in the heating vessel 11A evaporated by the evaporation heater 14 moves to the pipe 16 as shown in FIGS. As shown in FIGS. 7 to 9, a superheater 15 is provided outside the pipe 16, and the heat of the superheater 15 is transferred to the pipe 16 via the heating container 11. As shown in FIG. The steam b passing through the pipe 16 and having a temperature of 100° C. or more contacts the inner surface of the pipe 16 heated by the superheater 15 , is further heated, and is discharged from the other end of the pipe 16 to the outside.

また、図5と図7に示すように、パイプ16内には熱交換促進部17が設けられており、熱交換促進部17はパイプ16中央に配置された芯棒17aと芯棒17aの外周に巻きつけられた螺旋体17bで構成されている。芯棒17aと螺旋体17bは、螺旋体17bと芯棒17aの接合部17cの位置で溶接され、固定される。螺旋体17bとパイプ16は、螺旋体17bとパイプ16の接合部17dの位置で溶接され、固定される。蒸発ヒータ14で蒸発した加熱容器内11Aの蒸気bはパイプ16中央部の芯棒17aの外側を流れ、螺旋体17bに沿って流れ、一部の蒸気bは芯棒17aと螺旋体17b、螺旋体17bとパイプ16それぞれの隙間を直進する。螺旋体17bに沿って移動する蒸気は、パイ
プ16内面との接触面積が大きくなり、熱交換効率を向上させることができる。螺旋体17bに沿わない蒸気も芯棒17aによりパイプ16内面から距離が離れ、熱が伝わりにくいパイプ16中央部に蒸気を通過させないようにすることで、パイプ16内面近傍を蒸気が通過するようにすることで熱交換効率を向上させる効果もある。また、熱交換促進部17を設けることで、パイプ16内の流路面積が小さくなり、蒸気bの流速が早くなることで、パイプ16内面と蒸気bの対流熱流束を大きくすることができる。熱交換促進部17を設けることで、例えば過熱ヒータ15を300℃を越えない温度で制御したとしても、過熱蒸気の温度を250℃以上に昇温させることも可能となる。
Further, as shown in FIGS. 5 and 7, a heat exchange promoting portion 17 is provided in the pipe 16, and the heat exchange promoting portion 17 is formed between a core rod 17a arranged in the center of the pipe 16 and an outer periphery of the core rod 17a. It is composed of a spiral body 17b wound around. The core rod 17a and the spiral body 17b are welded and fixed at the joint 17c of the spiral body 17b and the core rod 17a. The spiral body 17b and the pipe 16 are welded and fixed at the joint 17d of the spiral body 17b and the pipe 16. As shown in FIG. The steam b in the heating container 11A evaporated by the evaporation heater 14 flows outside the core rod 17a at the center of the pipe 16 and along the spiral body 17b. Go straight through the gaps between the pipes 16 . The steam moving along the spiral body 17b has a larger contact area with the inner surface of the pipe 16, and can improve the heat exchange efficiency. The steam that does not follow the spiral body 17b is also separated from the inner surface of the pipe 16 by the core rod 17a, so that the steam does not pass through the central part of the pipe 16 where heat is difficult to transfer, so that the steam passes near the inner surface of the pipe 16. This also has the effect of improving the heat exchange efficiency. Further, by providing the heat exchange promoting portion 17, the flow passage area in the pipe 16 is reduced, and the flow velocity of the steam b is increased, so that the convective heat flux between the inner surface of the pipe 16 and the steam b can be increased. By providing the heat exchange promoting section 17, even if the superheater 15 is controlled at a temperature not exceeding 300°C, the temperature of the superheated steam can be increased to 250°C or higher.

図3と図4と図7を用いて蒸発ヒータ14と過熱ヒータ15の位置関係について説明する。蒸発ヒータ14と過熱ヒータ15は断面が円形となる形状、例えばシーズヒータとした場合、図7のように断面の中央部が蒸発ヒータ軸14a、過熱ヒータ軸15aとなる。 The positional relationship between the evaporation heater 14 and the superheater 15 will be described with reference to FIGS. 3, 4 and 7. FIG. The evaporating heater 14 and the superheating heater 15 have a circular cross-section.

蒸発ヒータ14と過熱ヒータ15の各ヒータの形状をU字形状とした場合、図6の蒸発ヒータ14の直線部14bのように同一ヒータ内に2つの直線部を有する。また、蒸発ヒータ14と過熱ヒータ15の直線部が平行になるように構成した場合、図7における蒸発ヒータ軸間距離dおよび過熱ヒータ軸間距離eはそれぞれ蒸発ヒータ14の直線部の軸間距離および過熱ヒータ15の直線部の軸間距離の最大の軸間距離となる。 When each heater of the evaporative heater 14 and the superheat heater 15 is U-shaped, the same heater has two straight portions like the straight portion 14b of the evaporative heater 14 in FIG. When the straight portions of the evaporative heater 14 and the superheater 15 are arranged in parallel, the distance d between the evaporative heater axes and the distance e between the superheater heater axes in FIG. and the maximum inter-axis distance of the linear portion of the overheating heater 15 .

本実施の形態における過熱蒸気発生装置10は蒸発ヒータ14の直線部14bの軸間距離dの最大距離および過熱ヒータ15の直線部の軸間距離eの最大距離よりも蒸発ヒータ14と過熱ヒータ15の軸間距離cの最小値が小さくなるように構成している。このような構成にすることで、蒸発ヒータ14の熱が過熱ヒータ15近傍までの伝達しやすくなり、蒸発ヒータ14の熱をパイプ16を通過する蒸気の過熱にも使用することができる。また、反対に過熱ヒータ15の熱が蒸発ヒータ14近傍に伝達しやすくなることで、過熱ヒータ15の熱を水の蒸発に使用することもできる。 In the superheated steam generator 10 of the present embodiment, the distance between the evaporative heater 14 and the superheater 15 is greater than the maximum distance d between the axes of the linear portion 14 b of the evaporative heater 14 and the maximum distance e between the axes of the linear portion 15 of the superheater 15 . is configured so that the minimum value of the inter-axis distance c of is small. With such a configuration, the heat of the evaporative heater 14 can be easily transmitted to the vicinity of the superheater 15 , and the heat of the evaporative heater 14 can also be used to superheat the steam passing through the pipe 16 . On the contrary, the heat of the superheater 15 can be easily transferred to the vicinity of the evaporation heater 14, so that the heat of the superheater 15 can be used for evaporating water.

蒸発ヒータや過熱ヒータは1つのU字形状のヒータだけでなはなく、2本以上の直線形状のヒータで構成されるものや、2回以上曲げた構成のものも考えられ、このような構成においても、蒸発ヒータの直線部の軸間距離の最大距離および過熱ヒータの直線部の軸間距離の最大距離よりも蒸発ヒータと過熱ヒータの軸間距離の最小値が小さくなるように構成することで、同様の効果を得られる。 Evaporation heaters and overheating heaters are not limited to one U-shaped heater, but may be composed of two or more linear heaters, or may be composed of two or more curved heaters. Also, the minimum value of the distance between the axes of the evaporative heater and the superheater shall be smaller than the maximum distance between the axes of the straight parts of the evaporative heater and the maximum distance between the axes of the straight parts of the superheater. to get the same effect.

本実施の形態の過熱蒸気発生装置10の想定する使用方法としては、まず過熱ヒータ15を100℃以上の所定の温度になるまで予熱し、その後給水口13から加熱容器内11Aに水を供給し、蒸発ヒータ14で水を蒸発させ、蒸発した蒸気を過熱ヒータ15で加熱されたパイプ16を通過させることで過熱して、100℃以上の所定の温度の過熱蒸気を外部に排出する。 As an assumed usage method of the superheated steam generator 10 of the present embodiment, first, the superheater 15 is preheated to a predetermined temperature of 100° C. or higher, and then water is supplied from the water supply port 13 to the heating container 11A. , water is evaporated by the evaporation heater 14, the evaporated steam is superheated by passing it through the pipe 16 heated by the superheater 15, and the superheated steam at a predetermined temperature of 100° C. or higher is discharged to the outside.

例えば、10℃の水を0.3g/sで供給する条件において、水の比熱を4.2J/(g・℃)、蒸発潜熱を2250J/gとした場合、1秒間で水を蒸発させるには最低約790Wの電力が必要となる。100℃の蒸気が0.3g/sでパイプ16を通過する条件において、過熱ヒータ15で250℃まで昇温させる場合は、水蒸気の比熱を2.1J/(g・℃)とした場合、必要な最低電力は約100Wであり、蒸発ヒータ14と比較して、消費電力は小さくて済む。 For example, under the condition that water at 10°C is supplied at 0.3g/s, when the specific heat of water is 4.2J/(g°C) and the latent heat of vaporization is 2250J/g, it takes 1 second to evaporate water. requires a minimum power of about 790 W. Under the condition that steam of 100°C passes through the pipe 16 at 0.3 g/s, when the temperature is raised to 250°C by the superheater 15, the specific heat of the steam is 2.1 J/(g·°C). The lowest power required is approximately 100 W, which is less power consumption than the evaporation heater 14 .

しかしながら、蒸気を過熱するためには、過熱ヒータ15、パイプ16、パイプ16周囲の加熱容器11の温度も予熱段階で所定の温度まで昇温させる必要があり、予熱時間が規定されている場合、100Wでは規定された予熱時間内に所定の温度まで昇温させることができない可能性がある。 However, in order to superheat the steam, it is necessary to raise the temperature of the superheater 15, the pipe 16, and the heating container 11 around the pipe 16 to a predetermined temperature in the preheating stage. At 100 W, there is a possibility that the temperature cannot be raised to the predetermined temperature within the specified preheating time.

反対に、規定された予熱時間内に所定の温度まで昇温させるために過熱ヒータ15の消費電力を100W以上に設計した場合、予熱完了後は消費電力が過剰となり、過熱ヒータ15を所定の温度で制御するためにON/OFFを繰り返すこととなるが、過熱蒸気発生装置全体で使用できる消費電力が限られている場合、過熱ヒータ15がOFFの状態での電力が熱として使用できず、無駄になってしまう。 Conversely, if the power consumption of the superheater 15 is designed to be 100 W or more in order to raise the temperature to a predetermined temperature within the specified preheating time, the power consumption becomes excessive after preheating is completed, and the superheater 15 is kept at a predetermined temperature. However, if the power consumption that can be used by the entire superheated steam generator is limited, the power cannot be used as heat when the superheater 15 is off, and is wasted. Become.

例えば過熱蒸気装置全体の消費電力を1300W以下とする条件で、予熱時間内に過熱ヒータ15、パイプ16、パイプ16周囲の加熱容器11を所定の温度まで昇温させるのに600W必要とした場合、蒸発ヒータ14で使用できる消費電力は700W以下となる。水を0.3g/sで蒸発させたい場合、蒸発ヒータ14の消費電力は足りない。 For example, under the condition that the power consumption of the entire superheated steam device is 1300 W or less, if 600 W is required to raise the temperature of the superheater 15, the pipe 16, and the heating container 11 around the pipe 16 to a predetermined temperature within the preheating time, The power consumption that can be used by the evaporation heater 14 is 700 W or less. If it is desired to evaporate water at 0.3 g/s, the power consumption of the evaporation heater 14 is insufficient.

また、一旦予熱が完了した過熱ヒータ15は蒸気の過熱には100Wで十分なため、蒸発ヒータ14では消費電力が不足しているにも関わらず過熱ヒータ15では500Wが余剰となってしまうことになる。 In addition, since 100 W is sufficient for the superheating heater 15 once preheating is completed to superheat the steam, 500 W becomes redundant in the superheating heater 15 even though the power consumption of the evaporating heater 14 is insufficient. Become.

このとき、本実施の形態のように蒸発ヒータ14と過熱ヒータ15の軸間距離cの距離を小さくし、過熱ヒータ15の熱を蒸発ヒータ14近傍に伝達しやすくした構成にすることで、過熱ヒータ15の余剰電力を熱として蒸発ヒータ14近傍に伝達し、水の昇温、蒸発に使用することで、蒸発ヒータ14の消費電力の不足分を補填することが可能となる。また、反対に予熱段階では蒸発ヒータ14の熱は水の蒸発には使用されないため、予熱段階において蒸発ヒータ14の熱を過熱ヒータ15近傍に伝達させることで過熱ヒータ15、パイプ16、パイプ16周囲の加熱容器11を所定の温度まで昇温させることに用いることができる。 At this time, as in the present embodiment, the distance c between the axes of the evaporative heater 14 and the overheating heater 15 is reduced so that the heat of the overheating heater 15 can be easily transmitted to the vicinity of the evaporating heater 14. By transferring the surplus electric power of the heater 15 as heat to the vicinity of the evaporation heater 14 and using it to raise the temperature and evaporate the water, it is possible to make up for the shortage of the power consumption of the evaporation heater 14 . On the contrary, in the preheating stage, the heat of the evaporation heater 14 is not used for evaporating water. can be used to raise the temperature of the heating container 11 to a predetermined temperature.

本実施の形態の過熱蒸気発生装置10は過熱蒸気を使用して調理を行う調理器、例えば図8のような加熱オーブンへの搭載が可能である。図8において、貯水タンク4内に溜められた水を、ポンプ5によって過熱蒸気発生装置10内に供給する。過熱蒸気発生装置10内に供給された水は、過熱蒸気発生装置10で100℃以上の所定の過熱蒸気として、加熱オーブン本体1内の加熱室2に投入することで、過熱蒸気を使用した調理が可能となる。また、調理器は加熱オーブンに限らず、炊飯器やオーブンレンジ等の調理器にも用いることができる。 The superheated steam generator 10 of the present embodiment can be mounted on a cooking device that uses superheated steam for cooking, such as a heating oven as shown in FIG. In FIG. 8 , the water stored in the water storage tank 4 is supplied into the superheated steam generator 10 by the pump 5 . The water supplied into the superheated steam generator 10 is turned into a predetermined superheated steam of 100° C. or higher by the superheated steam generator 10 and introduced into the heating chamber 2 in the heating oven main body 1, thereby cooking using superheated steam. becomes possible. Moreover, the cooker is not limited to a heating oven, and can be used as a cooker such as a rice cooker or a microwave oven.

(実施の形態2)
図9、図10を用いて、本発明の実施の形態2における過熱蒸気発生装置の構成について説明する。図9には本発明の実施の形態2における過熱蒸気発生装置が接合部で接合した状態を示す斜視図を示す。図8には本発明の実施の形態2における過熱蒸気発生装置の分解斜視図を示す。
(Embodiment 2)
The configuration of the superheated steam generator according to Embodiment 2 of the present invention will be described with reference to FIGS. 9 and 10. FIG. FIG. 9 shows a perspective view showing a state where the superheated steam generator according to Embodiment 2 of the present invention is joined at the joining portion. FIG. 8 shows an exploded perspective view of a superheated steam generator according to Embodiment 2 of the present invention.

本発明の実施の形態においては、実施の形態1と相違する事項について説明し、実施の形態1と同様の構成及び作用効果等を有するものについては説明を省略する。 In the embodiment of the present invention, matters different from those of Embodiment 1 will be explained, and explanations of those having the same configuration, effect, etc. as those of Embodiment 1 will be omitted.

図9、図10に示すように本実施の形態2における過熱蒸気発生装置10は加熱容器11と加熱容器11内に水を供給する給水管13Aと蒸発ヒータ14で構成された蒸発部20と、過熱ヒータ15とパイプ16と過熱ヒータ15とパイプ16の間に設けられた伝熱部18で構成された過熱部21が、蒸発部接合部19aと過熱部接合部19bで接合された構成となっている。 As shown in FIGS. 9 and 10, the superheated steam generator 10 according to the second embodiment includes a heating vessel 11, a water supply pipe 13A for supplying water into the heating vessel 11, an evaporating section 20 composed of an evaporating heater 14, A superheating section 21 composed of the superheating heater 15, the pipe 16, and the heat transfer section 18 provided between the superheating heater 15 and the pipe 16 is joined at the evaporating section joining section 19a and the superheating section joining section 19b. ing.

本実施の形態2における過熱蒸気発生装置10は、蒸発部20と過熱部21とに分離可能な構成である。 The superheated steam generator 10 in Embodiment 2 has a configuration that can be separated into an evaporating section 20 and a superheating section 21 .

過熱部21において、伝熱部18を過熱ヒータ15とパイプ16との隙間や周囲を覆い、密着するように配置することで、過熱ヒータ15の表面からの熱を伝熱部18を介して、パイプ16に素早く伝達させることができる。 In the overheating unit 21, the heat transfer unit 18 is arranged so as to cover the gap and the surroundings of the overheating heater 15 and the pipe 16 so as to be in close contact with each other, so that the heat from the surface of the overheating heater 15 is It can be transmitted to the pipe 16 quickly.

本実施の形態2にように過熱蒸気発生装置10を蒸発部20と過熱部21に分離する構造にすることで、蒸発部20と過熱部21を接合するときに、蒸発部20と過熱部21の接触面に断熱材もしくは空気層を設けることで、部分的に蒸発ヒータ14もしくは過熱ヒータ15の熱を過熱ヒータ15近傍もしくは蒸発ヒータ14近傍に伝達する熱量を抑えることができる。例えば、過熱部21における、パイプ16近傍の熱は蒸気を過熱するために重要となるため、パイプ16近傍に水が接触し、過剰に熱が水に奪われると、パイプ16近傍の熱量が不足し、パイプ16を通過する蒸気が十分に過熱されない可能性がある。そこで、過熱部21のパイプ16近傍と蒸発部20の接触箇所の一部に断熱材を設けることで、過熱部21のパイプ16近傍から蒸発部20への熱移動を抑制し、パイプ16内を通過する蒸気を過熱するための熱量を保持することができる。 By configuring the superheated steam generator 10 to be separated into the evaporating section 20 and the superheating section 21 as in the second embodiment, when the evaporating section 20 and the superheating section 21 are joined together, the evaporating section 20 and the superheating section 21 By providing a heat insulating material or an air layer on the contact surface, it is possible to partially suppress the amount of heat transmitted from the evaporative heater 14 or the superheater 15 to the vicinity of the superheater 15 or the vicinity of the evaporative heater 14 . For example, the heat in the vicinity of the pipe 16 in the superheating unit 21 is important for superheating the steam, so if water comes into contact with the vicinity of the pipe 16 and excessive heat is taken away by the water, the amount of heat in the vicinity of the pipe 16 becomes insufficient. However, the steam passing through pipe 16 may not be sufficiently superheated. Therefore, by providing a heat insulating material in a part of the contact portion between the pipe 16 of the superheating part 21 and the evaporating part 20, heat transfer from the pipe 16 of the superheating part 21 near the evaporating part 20 is suppressed, and the inside of the pipe 16 is suppressed. The amount of heat can be retained to superheat the passing steam.

本発明は過熱蒸気発生装置の熱交換効率向上を実現するものであり、調理機以外にも過熱蒸気を使用する、乾燥装置、殺菌装置等の他分野での活用も可能である。 INDUSTRIAL APPLICABILITY The present invention realizes an improvement in the heat exchange efficiency of a superheated steam generator, and can be used in other fields such as drying equipment and sterilizing equipment that use superheated steam in addition to cooking machines.

a 水
b 蒸気
c 軸間距離
d 軸間距離
e 軸間距離
1 加熱オーブン本体
2 加熱室
4 貯水タンク
5 ポンプ
10 過熱蒸気発生装置
11 加熱容器
11A 加熱容器内
12 加熱容器カバー
13 給水口
13A 給水管
14 蒸発ヒータ
14a 蒸発ヒータ軸
14b 直線部
15 過熱ヒータ
15a 過熱ヒータ軸
16 パイプ
17 熱交換促進部
17a 芯棒
17b 螺旋体
17c 接合部
17d 接合部
18 伝熱部
19a 蒸発部接合部
19b 過熱部接合部
20 蒸発部
21 過熱部
a water b steam c distance between axes d distance between axes e distance between axes 1 heating oven main body 2 heating chamber 4 water storage tank 5 pump 10 superheated steam generator 11 heating vessel 11A heating vessel interior 12 heating vessel cover 13 water inlet 13A water supply pipe 14 Evaporation heater 14a Evaporation heater shaft 14b Straight part 15 Overheating heater 15a Overheating heater shaft 16 Pipe 17 Heat exchange promoting part 17a Core rod 17b Spiral body 17c Joint part 17d Joint part 18 Heat transfer part 19a Evaporation part joint part 19b Superheating part joint part 20 Evaporator 21 Superheater

Claims (6)

加熱容器と、
前記加熱容器に水を供給する給水口と、
前記加熱容器を加熱することで前記給水口から前記加熱容器に供給された水を蒸発させる蒸発ヒータと、
前記蒸発ヒータにより生成した蒸気が通るパイプと、
前記パイプの外側に配置され、前記パイプを加熱することで前記パイプ内を通過する蒸気を過熱する過熱ヒータと、を備え、
前記蒸発ヒータと前記過熱ヒータは2つ以上の直線部を有し、
対向する前記蒸発ヒータの直線部と前記過熱ヒータの直線部とが並列且つ平行になるように構成し、
前記蒸発ヒータと前記過熱ヒータの断面中心の軸間距離の最小距離が、
前記蒸発ヒータの直線部の断面中心の軸間距離の最大距離および前記過熱ヒータの直線部の断面中心の軸間距離の最大距離よりも短くなるように構成された過熱蒸気発生装置。
a heating vessel;
a water supply port for supplying water to the heating container;
an evaporation heater that heats the heating container to evaporate the water supplied to the heating container from the water supply port;
a pipe through which the vapor generated by the evaporative heater passes;
a superheater disposed outside the pipe and heating the pipe to superheat steam passing through the pipe;
the evaporating heater and the superheating heater have two or more linear portions ,
The linear portion of the evaporative heater and the linear portion of the overheating heater facing each other are configured to be parallel and parallel,
The minimum distance between the axes of the cross-sectional centers of the evaporative heater and the superheater is
A superheated steam generator configured to be shorter than the maximum distance between the axes of the cross-sectional centers of the straight portions of the evaporative heater and the maximum distance between the axes of the cross-sectional centers of the straight portions of the overheating heater.
前記給水口から給水された水は前記蒸発ヒータの長手方向に沿って移動し、前記蒸発ヒータによって生成した蒸気は、前記蒸発ヒータもしくは前記過熱ヒータの長手方向に沿って移動するように構成された請求項1に記載の過熱蒸気発生装置。 The water supplied from the water inlet moves along the longitudinal direction of the evaporative heater, and the steam generated by the evaporative heater moves along the longitudinal direction of the evaporative heater or the superheater. The superheated steam generator according to claim 1. 前記パイプ内には熱交換促進部が設けられ、
前記熱交換促進部は芯棒と、前記芯棒の外周に巻きつけられた螺旋体で構成された請求項1に記載の過熱蒸気発生装置。
A heat exchange promoting part is provided in the pipe,
2. The superheated steam generator according to claim 1, wherein the heat exchange promoting part comprises a core rod and a spiral body wound around the outer periphery of the core rod.
加熱容器と、
前記加熱容器に水を供給する給水口と、
前記加熱容器を加熱することで前記給水口から前記加熱容器に供給された水を蒸発させる蒸発ヒータと、
前記蒸発ヒータにより生成した蒸気が通るパイプと、
前記パイプの外側に配置され、前記パイプを加熱することで前記パイプ内を通過する蒸気を過熱する過熱ヒータと、を備え、
前記蒸発ヒータと前記過熱ヒータは2つ以上の直線部を有しており、
前記蒸発ヒータと前記過熱ヒータの軸間距離の最小距離が、
前記蒸発ヒータの直線部の軸間距離の最大距離および前記過熱ヒータの直線部の軸間距離の最大距離よりも短くなるように構成され、
前記蒸発ヒータと、前記パイプと、前記過熱ヒータがそれぞれ前記加熱容器と密着するように構成された過熱蒸気発生装置。
a heating vessel;
a water supply port for supplying water to the heating container;
an evaporation heater that heats the heating container to evaporate the water supplied to the heating container from the water supply port;
a pipe through which the vapor generated by the evaporative heater passes;
a superheater disposed outside the pipe and heating the pipe to superheat steam passing through the pipe;
the evaporating heater and the superheating heater have two or more linear portions,
The minimum distance between the axes of the evaporative heater and the superheater is
configured to be shorter than the maximum distance between the axes of the straight portions of the evaporative heater and the maximum distance between the axes of the straight portions of the overheating heater,
A superheated steam generator, wherein the evaporating heater, the pipe, and the superheating heater are in close contact with the heating vessel.
前記パイプと前記過熱ヒータの間に伝熱部が設けられ、
前記加熱容器と前記給水口と前記蒸発ヒータで構成された蒸発部と、前記パイプと前記過熱ヒータと前記伝熱部で構成された過熱部が接合する接合部を備えた請求項1に記載の過熱蒸気発生装置。
A heat transfer section is provided between the pipe and the superheater,
2. The apparatus according to claim 1, further comprising a joining portion for joining an evaporating portion including the heating container, the water inlet, and the evaporating heater, and a superheating portion including the pipe, the superheater, and the heat transfer portion. Superheated steam generator.
請求項1~5のいずれか1つに記載の過熱蒸気発生装置を備えた調理器。 A cooker comprising the superheated steam generator according to any one of claims 1 to 5.
JP2018155890A 2018-02-28 2018-08-23 Superheated steam generator and cooker Active JP7190627B2 (en)

Priority Applications (4)

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JP2018155890A JP7190627B2 (en) 2018-08-23 2018-08-23 Superheated steam generator and cooker
EP19761039.7A EP3760923A4 (en) 2018-02-28 2019-01-24 Superheated steam generator and cooker
PCT/JP2019/002160 WO2019167488A1 (en) 2018-02-28 2019-01-24 Superheated steam generator and cooker
CN201980003856.5A CN111051775A (en) 2018-02-28 2019-01-24 Superheated steam generator and cooking device

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Citations (2)

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Publication number Priority date Publication date Assignee Title
JP2006317085A (en) 2005-05-13 2006-11-24 Sanden Corp Fluid heating device
JP2016044880A (en) 2014-08-22 2016-04-04 パナソニックIpマネジメント株式会社 Superheated steam generation device and rice cooker

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006317085A (en) 2005-05-13 2006-11-24 Sanden Corp Fluid heating device
JP2016044880A (en) 2014-08-22 2016-04-04 パナソニックIpマネジメント株式会社 Superheated steam generation device and rice cooker

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