JP3798671B2 - Superheated steam cooking device - Google Patents
Superheated steam cooking device Download PDFInfo
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- JP3798671B2 JP3798671B2 JP2001325025A JP2001325025A JP3798671B2 JP 3798671 B2 JP3798671 B2 JP 3798671B2 JP 2001325025 A JP2001325025 A JP 2001325025A JP 2001325025 A JP2001325025 A JP 2001325025A JP 3798671 B2 JP3798671 B2 JP 3798671B2
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- superheated steam
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
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Description
【0001】
【発明の属する技術分野】
本発明は、100℃よりも高い温度の蒸気、即ち過熱蒸気で食材を加熱調理する過熱蒸気調理装置に関する。
【0002】
【従来の技術】
従来の過熱蒸気調理装置は、ボイラーから発生した過熱蒸気を調理容器に供給し、調理容器内に収容した食材を過熱蒸気で調理し、使用済の過熱蒸気を調理容器から大気中へ放出するものであった。
【0003】
【発明が解決しようとする課題】
使用済の過熱蒸気は未だ熱を多く含んでいる事から、その熱を再利用することがエネルギーの有効利用の観点から望ましい。しかし、使用済みの過熱蒸気をボイラー内にそのまま戻して再度、調理容器に供給して使用するとなれば、使用済みの過熱蒸気に含まれる食材からの油分や種々の微粒子が循環して、ボイラー、調理容器及び配管内に付着し、カビ等が繁殖する原因となり、食品衛生上好ましくない。
【0004】
本発明は上記実情に鑑みて成されたものであって、その目的は、使用済の過熱蒸気の熱のみを効率よく回収し再利用することである。
【0005】
【課題を解決するための手段】
請求項1の発明は、調理容器内に収容した食材を過熱蒸気で調理する過熱蒸気調理装置において、蒸気発生装置の貯水槽に熱交換器を内蔵すると共に湯水を供給可能に設け、貯水槽とブロワを第一パイプで接続し、ブロワと調理容器を第二パイプで接続し、過熱蒸気を送り出す加熱装置内に第二パイプの中間部分を通し、調理容器に過熱蒸気の排出パイプを接続し、排出パイプの中間部分に前記した蒸気発生装置の熱交換器を接続し、排出パイプの先端を貯水槽外に開口してあること特徴とする。
【0006】
上述した過熱蒸気調理装置は、起動時には、貯水槽に水が蓄えられていると、ブロワで吸引しても蒸気発生装置から蒸気は発生しない。従って、起動時には、貯水槽に湯を供給して蒸気発生装置から蒸気を発生させる。一方、定常運転時には、貯水槽内の湯が十分に温まっているのでブロワで吸引することによって通常より低い温度で蒸気発生装置から蒸気が発生し、その蒸気をブロワで加熱装置に送り込み、所望の温度の過熱蒸気にした後に調理容器に供給する。調理容器から排出される使用済みの過熱蒸気は、排出パイプの途中で熱交換器を通り、顕熱と潜熱を回収して貯水装置内の湯を温めて蒸気を発生させ、排出パイプの先端から最終的には水となって放出される。定常運転時に貯水槽内の水量が不足した場合には、湯か水を供給すれば良いが、湯を供給した方が蒸気になりやすいので望ましい。なお、ブロワは、貯水槽内の圧力を調理容器から排出される過熱蒸気の圧力より低くするもので、それによって過熱蒸気の顕熱と潜熱を熱交換器で回収する。
【0007】
また、起動時に貯水槽に水が蓄えられた状態で調理容器に過熱蒸気を供給するには、加熱装置に過熱蒸気を作る元となる、気体や湯水を別途、供給する必要がある。従って、請求項2の発明のように、第一パイプの中間部分に気体供給パイプを分岐しても良いし、請求項3の発明のように、第二パイプは加熱装置とブロワの間から注水パイプを分岐しても良い。
【0008】
【発明の実施の形態】
本発明の過熱蒸気調理装置の第一実施形態は図1に示すように、蒸気発生装置1と、ブロワ2と、加熱装置3としての蓄熱槽と、調理容器4を有し、蒸気発生装置1の貯水槽5の上部とブロワ2を第一パイプ6で接続し、ブロワ2と調理容器4の下部を第二パイプ7で接続し、第二パイプ7の一部を伝熱管8とし、伝熱管8を蓄熱槽3内に通すと共に、蒸気を直に調理容器4に送り込むバイパス管9を第二パイプ7に接続し、バイパス管9のブロワ側の接続部分にバイパス弁10を有する。また、調理容器4の上部から排出パイプ11を延長し、排出パイプ11の中間部分に熱交換器12を接続し、その熱交換器12を蒸気発生装置の貯水槽5に内蔵し、排出パイプ11の先端を蒸気発生装置1の外部に向けてある。
【0009】
蒸気発生装置1は、貯水槽5に熱交換器12を内蔵し、湯及び水を補給バルブ13から供給可能に設けると共に、フロート式水面高さ検出器14を備え、フロート式水面高さ検出器14が所定の高さより低い場合は、補給バルブ13を連動機構によって開き、所定の高さに達した場合は、連動機構によって補給バルブ13を閉じることにより水面を規定値の高さに保つ。
【0010】
ブロワ2は、蒸気を蓄熱槽側に送り込んで、貯水槽5内の圧力を調理容器4から排出される過熱蒸気の圧力より低くするもので、それによって過熱蒸気の顕熱と潜熱を熱交換器12で回収する。
【0011】
蓄熱槽3は、内部に収容する蓄熱材15に、電気ヒータ16と前述した伝熱管8を通し、過熱蒸気を作り出すものである。また、蓄熱材15はマグネシア、マグネタイトなどの固体蓄熱材と、硝酸ナトリウムと亜硝酸ナトリウム、硝酸カリウムの三種類の硝酸塩を混合した液体蓄熱材とで構成されている。
【0012】
調理容器4は、開閉可能な密閉容器内に複数段の棚17を備え、棚17の上に載せた食材18に過熱蒸気が当たるものである。
【0013】
バイパス弁10は、蓄熱槽側に流す蒸気量とバイパス側に流す蒸気量の比率を、開閉操作により調整可能に設け、それによって調理容器4内の雰囲気を調整するものである。また、その開閉操作は、コンピュータ制御で自動的に行っており、制御装置に調理容器4内の目標温度を設定し、調理容器4内の温度検出器19から受ける調理装置4内の実際の温度と目標温度を比較し、実際の温度が目標温度に一致するようにバイパス弁10の開度を自動的に操作する。
【0014】
本発明の過熱蒸気調理装置の第二実施形態は図2に示すように、第一パイプ6の途中に気体供給パイプ20を分岐し、気体供給パイプ20に接続した気体供給バルブ21を開閉するものである。なお、気体としては、空気や蒸気が挙げられる。
【0015】
本発明の過熱蒸気調理装置の第三実施形態は図3に示すように、第二パイプ7の伝熱管8の前に注水パイプ22を分岐し、注水パイプ22に接続した注水バルブ23を開閉するものである。なお、注水パイプ22へ供給する水は、図面のように貯水槽5や補給バルブ13の供給源側から取り込んでも良いし、他の箇所から取り込んでも良い。
【0016】
本発明品の定常運転時に肉1kgを調理する際に必要なエネルギー消費量を、従来品と比較する。まず、肉1kgを調理するには1200kJの加熱が必要になる。また、調理容器内に過熱蒸気が400℃で突入し、300℃で排出されるとすれば、大気圧400℃の蒸気のエンタルピーが3280、大気圧300℃の蒸気のエンタルピーが3075として計算すると、
過熱蒸気量(kg)=1200kJ/(3280−3075)=5.9となる。
【0017】
ここで本発明品のブロワでの消費エネルギーは、ブロワの効率を30%とし、ブロワ出口の蒸気温度を大気圧123℃(蒸気エンタルピー2728)とし、ブロワ入口の蒸気温度を負圧90℃(蒸気エンタルピー2627)として計算すると、
また、本発明品の蓄熱槽での消費エネルギーを計算すると、
消費エネルギー(kJ)=5.9×(3280−2728)=3257となる。
従って、本発明品の全消費エネルギーは、ブロワと蓄熱槽との両消費エネルギーを合計して、
消費エネルギー=1986+3257=5243kJとなる。
【0018】
一方、従来品としては、15℃の水(エンタルピー63)をボイラで400℃まで過熱して調理容器に供給するものを想定して消費エネルギーを計算すれば、消費エネルギー=5.9×(3280−63)=18980kJとなる。
従って、従来品と比べて本発明品は、消費エネルギーが1/3〜1/4で済むことなる。
【0019】
本発明は、ブロワの出力が一定である場合にバイパス弁の開度を調整することによって、調理容器内を所望の雰囲気にするものであるが、ブロワに出力が可変なものを用いれば、バイパス管及びバイパス弁は不要となる。
【0020】
【発明の効果】
請求項1の発明は、調理容器内で食材を加熱した後の過熱蒸気の排出パイプの中間部分に蒸気発生装置の熱交換器を備え、排出パイプの先端を貯水槽外に向けて、使用済みの過熱蒸気から貯水槽の湯水を隔絶してあるので、蒸気発生装置で発生する蒸気は清潔であり、その顕熱と潜熱のみを回収して再利用することができる。
【0021】
請求項2の発明は、起動時に蒸気発生装置内に水が溜まっていても、気体供給パイプから蒸気や空気を供給すれば、加熱装置の熱によって過熱蒸気に変わるので、過熱蒸気が調理容器に供給できる。
【0022】
請求項3の発明は、起動時に蒸気発生装置内に水が溜まっていても、注水パイプから湯水を供給すれば、加熱装置の熱によって過熱蒸気に変わるので、過熱蒸気が調理容器に供給できる。
【図面の簡単な説明】
【図1】本発明の過熱蒸気調理装置の第一実施形態を示す説明図である。
【図2】本発明の過熱蒸気調理装置の第二実施形態を示す説明図である。
【図3】本発明の過熱蒸気調理装置の第三実施形態を示す説明図である。
【符号の説明】
1 蒸気発生装置
2 ブロワ
3 加熱装置(蓄熱槽)
4 調理容器
5 貯水槽
6 第一パイプ
7 第二パイプ
11 排出パイプ
12 熱交換器
18 食材
20 気体供給パイプ
22 注水パイプ[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a superheated steam cooking apparatus that cooks food with steam having a temperature higher than 100 ° C., that is, superheated steam.
[0002]
[Prior art]
A conventional superheated steam cooking device supplies superheated steam generated from a boiler to a cooking container, cooks food stored in the cooking container with superheated steam, and releases used superheated steam from the cooking container to the atmosphere. Met.
[0003]
[Problems to be solved by the invention]
Since used superheated steam still contains a lot of heat, it is desirable to reuse the heat from the viewpoint of effective use of energy. However, if the used superheated steam is returned to the boiler as it is and then supplied to the cooking container again, the oil and various fine particles from the ingredients contained in the used superheated steam circulate, and the boiler, It adheres to cooking containers and piping and causes mold to grow, which is not preferable for food hygiene.
[0004]
The present invention has been made in view of the above circumstances, and an object of the present invention is to efficiently recover and reuse only the heat of used superheated steam.
[0005]
[Means for Solving the Problems]
The invention of claim 1 is a superheated steam cooking apparatus for cooking food contained in a cooking vessel with superheated steam, and a heat exchanger is built in the water tank of the steam generator so that hot water can be supplied, Connect the blower with the first pipe, connect the blower and the cooking container with the second pipe, pass the middle part of the second pipe into the heating device that sends out the superheated steam, connect the exhaust pipe of the superheated steam to the cooking container, The heat exchanger of the steam generator is connected to the middle part of the discharge pipe, and the tip of the discharge pipe is opened outside the water storage tank.
[0006]
When the above-described superheated steam cooking apparatus is activated, if water is stored in the water storage tank, no steam is generated from the steam generating apparatus even if it is sucked by a blower. Therefore, at startup, hot water is supplied to the water storage tank to generate steam from the steam generator. On the other hand, at the time of steady operation, the hot water in the water tank is sufficiently warmed up, so that the steam is generated from the steam generator at a lower temperature than normal by sucking with the blower, and the steam is sent to the heating device with the blower. The steam is heated to superheated steam and then supplied to the cooking vessel. Used superheated steam discharged from the cooking vessel passes through a heat exchanger in the middle of the discharge pipe, recovers sensible heat and latent heat, warms the hot water in the water storage device, generates steam, and then from the end of the discharge pipe Eventually it is released as water. If the amount of water in the water tank is insufficient during steady operation, hot water or water may be supplied, but it is desirable to supply hot water because it tends to become steam. In addition, a blower makes the pressure in a water tank lower than the pressure of the superheated steam discharged | emitted from a cooking container, and collect | recovers sensible heat and latent heat of a superheated steam with a heat exchanger by it.
[0007]
Moreover, in order to supply superheated steam to a cooking container in the state by which the water was stored in the water storage tank at the time of starting, it is necessary to supply separately the gas and hot water which are the origins which produce superheated steam to a heating apparatus. Therefore, the gas supply pipe may be branched to the intermediate portion of the first pipe as in the invention of
[0008]
DETAILED DESCRIPTION OF THE INVENTION
As shown in FIG. 1, the first embodiment of the superheated steam cooking device of the present invention has a steam generator 1, a
[0009]
The steam generator 1 includes a
[0010]
The
[0011]
The
[0012]
The cooking container 4 includes a plurality of
[0013]
The
[0014]
As shown in FIG. 2, the second embodiment of the superheated steam cooking apparatus of the present invention branches the
[0015]
As shown in FIG. 3, the third embodiment of the superheated steam cooking device of the present invention branches the
[0016]
The energy consumption required when cooking 1 kg of meat during steady operation of the product of the present invention is compared with that of the conventional product. First, 1200 kJ heating is required to cook 1 kg of meat. If superheated steam enters the cooking vessel at 400 ° C. and is discharged at 300 ° C., the enthalpy of steam at an atmospheric pressure of 400 ° C. is 3280 and the enthalpy of steam at an atmospheric pressure of 300 ° C. is calculated as 3075.
The amount of superheated steam (kg) = 1200 kJ / (3280-3075) = 5.9.
[0017]
Here, the energy consumption of the blower of the present invention is such that the efficiency of the blower is 30%, the steam temperature at the blower outlet is 123 ° C. (steam enthalpy 2728), and the steam temperature at the blower inlet is 90 ° C. (steam Calculated as enthalpy 2627)
Moreover, when calculating the energy consumption in the heat storage tank of the present invention product,
Energy consumption (kJ) = 5.9 × (3280-2728) = 3257.
Therefore, the total energy consumption of the product of the present invention is the sum of the energy consumption of both the blower and the heat storage tank,
Consumption energy = 1986 + 3257 = 5243 kJ.
[0018]
On the other hand, as a conventional product, if the energy consumption is calculated assuming that 15 ° C. water (enthalpy 63) is heated to 400 ° C. with a boiler and supplied to the cooking container, energy consumption = 5.9 × (3280) −63) = 18980 kJ.
Therefore, compared with the conventional product, the product of the present invention requires only 1/3 to 1/4 of energy consumption.
[0019]
In the present invention, when the output of the blower is constant, the opening of the bypass valve is adjusted so that the inside of the cooking container has a desired atmosphere. Pipes and bypass valves are not required.
[0020]
【The invention's effect】
The invention of claim 1 includes a heat exchanger of a steam generator in the middle part of the superheated steam discharge pipe after the food is heated in the cooking container, and the end of the discharge pipe faces the outside of the water tank. Since the hot water in the water tank is isolated from the superheated steam, the steam generated by the steam generator is clean, and only the sensible heat and latent heat can be recovered and reused.
[0021]
According to the second aspect of the present invention, even if water is accumulated in the steam generator at the time of startup, if steam or air is supplied from the gas supply pipe, it is changed to superheated steam by the heat of the heating device. Can supply.
[0022]
According to the third aspect of the present invention, even if water is accumulated in the steam generator at the time of startup, if hot water is supplied from the water injection pipe, it is changed to superheated steam by the heat of the heating device, so that the superheated steam can be supplied to the cooking container.
[Brief description of the drawings]
FIG. 1 is an explanatory view showing a first embodiment of the superheated steam cooking apparatus of the present invention.
FIG. 2 is an explanatory view showing a second embodiment of the superheated steam cooking apparatus of the present invention.
FIG. 3 is an explanatory view showing a third embodiment of the superheated steam cooking apparatus of the present invention.
[Explanation of symbols]
1
4
Claims (3)
蒸気発生装置(1)の貯水槽(5)に熱交換器(12)を内蔵すると共に湯水を供給可能に設け、貯水槽(5)とブロワ(2)を第一パイプ(6)で接続し、ブロワ(2)と調理容器(4)を第二パイプ(7)で接続し、過熱蒸気を送り出す加熱装置(3)内に第二パイプ(7)の中間部分を通し、調理容器(4)に過熱蒸気の排出パイプ(11)を接続し、排出パイプ(11)の中間部分に前記した蒸気発生装置の熱交換器(12)を接続し、排出パイプ(11)の先端を貯水槽(5)外に開口してあること特徴とする過熱蒸気調理装置。In the superheated steam cooking apparatus which cooks the foodstuff (18) accommodated in the cooking vessel (4) with superheated steam,
The water storage tank (5) of the steam generator (1) has a built-in heat exchanger (12) and can supply hot water, and the water storage tank (5) and the blower (2) are connected by the first pipe (6). The blower (2) and the cooking vessel (4) are connected by the second pipe (7), and the intermediate portion of the second pipe (7) is passed through the heating device (3) for sending out superheated steam, and the cooking vessel (4) The superheated steam discharge pipe (11) is connected to the middle, the heat exchanger (12) of the steam generator is connected to the middle part of the discharge pipe (11), and the tip of the discharge pipe (11) is connected to the water storage tank (5 ) A superheated steam cooking device that is open to the outside.
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JP2001325025A JP3798671B2 (en) | 2001-10-23 | 2001-10-23 | Superheated steam cooking device |
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JP2001325025A JP3798671B2 (en) | 2001-10-23 | 2001-10-23 | Superheated steam cooking device |
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JP2003125930A JP2003125930A (en) | 2003-05-07 |
JP3798671B2 true JP3798671B2 (en) | 2006-07-19 |
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KR102072694B1 (en) * | 2019-07-30 | 2020-02-03 | 주식회사 효신테크 | A combi oven including the heat exchange module |
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