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JP2009165459A - Method for dissolving mixture of hydrogen gas and nitrogen gas in food, apparatus therefor and food in which hydrogen gas and nitrogen gas are dissolved - Google Patents

Method for dissolving mixture of hydrogen gas and nitrogen gas in food, apparatus therefor and food in which hydrogen gas and nitrogen gas are dissolved Download PDF

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JP2009165459A
JP2009165459A JP2008124410A JP2008124410A JP2009165459A JP 2009165459 A JP2009165459 A JP 2009165459A JP 2008124410 A JP2008124410 A JP 2008124410A JP 2008124410 A JP2008124410 A JP 2008124410A JP 2009165459 A JP2009165459 A JP 2009165459A
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hydrogen gas
food
gas
reaction vessel
nitrogen gas
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Akinobu Fujiwara
昭信 藤原
Hideo Nishiwaki
英夫 西脇
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Shinwa Kogyo Inc
Shinwa Industry Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for dissolving hydrogen gas and nitrogen gas in food and cake, an apparatus therefor, and the food and the cake. <P>SOLUTION: A food material is finely pulverized and agitated by adding water to be a gel state. Subsequently, the gelled food material is put in a reaction vessel 1 and agitated by mixing a mixture of micro-bubbled hydrogen gas and nitrogen gas. Subsequently, for example, when the food material is cooled to solidify, the agitation is stopped to obtain a product. Thereby, a large amount of hydrogen gas and nitrogen gas is included in the food and functional food in which the dissolved amount of the gases do not time of day-dependently decrease and qualities are not deteriorated can be obtained. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、水素ガス及び窒素ガスを菓子及び食品(以下単に「食品」という。)中に均一に溶存させる方法及びその装置並びに水素ガスと窒素ガスを溶存させて成る食品に関する。   The present invention relates to a method and apparatus for uniformly dissolving hydrogen gas and nitrogen gas in confectionery and food (hereinafter simply referred to as “food”), and a food obtained by dissolving hydrogen gas and nitrogen gas.

成人病や老化現象を引き起こす体内の過酸化物質を中和する作用があるとされる水素ガスを溶解した水素水が飲料水として用いられている。
この水素水は、水の電気分解によって発生する水素ガスを飲料水中に溶解させたものであるが、この溶解工程において同時に発生する酸素ガスも飲料水中に溶解してしまうことと、殺菌などのために飲料水に含まれる塩素イオンまでが分解されて有害な塩素ガスが発生するなどの問題がある。
Hydrogen water in which hydrogen gas, which is said to have an action of neutralizing peroxidative substances in the body that cause adult diseases and aging, is used as drinking water.
This hydrogen water is obtained by dissolving hydrogen gas generated by electrolysis of water in drinking water. Oxygen gas generated at the same time in this dissolving step is also dissolved in drinking water and for sterilization and the like. In addition, there is a problem that even chlorine ions contained in drinking water are decomposed to generate harmful chlorine gas.

そこで、陽極と陰極をイオン交換膜などの半透膜で分離させて陰極から発生する水素ガスを溶解した水素水が商品として販売されているが、水の電気分解を膜で仕切って電気分解すると陽極は酸性化し、陰極はアルカリ化してくるので水素水の水素濃度を上げようとして長い時間電気分解するとアルカリが強くなり飲料には適さない危険な水となる。   Therefore, hydrogen water in which hydrogen gas generated from the cathode is dissolved by separating the anode and the cathode with a semipermeable membrane such as an ion exchange membrane is sold as a product. Since the anode is acidified and the cathode is alkalinized, if electrolysis is performed for a long time to increase the hydrogen concentration of hydrogen water, the alkali becomes strong and becomes dangerous water that is not suitable for beverages.

そこで、本発明者は、飲料水に含まれている窒素ガスや酸素ガスを真空装置やガス交換膜を用いて除去してから、水素ガスを飲料水中に溶解すると理論値に近い水素ガスを飲料水に溶解させることが出来ることが解った。
このデータを表1に示す。
Therefore, the present inventor removes nitrogen gas and oxygen gas contained in drinking water using a vacuum device or a gas exchange membrane, and then dissolves hydrogen gas in drinking water to produce hydrogen gas close to the theoretical value in the drinking water. It was found that it can be dissolved in water.
This data is shown in Table 1.

Figure 2009165459
Figure 2009165459

しかし、水素ガスを溶解した水素水は不安定で時間の経過とともに水素水から水素ガスが抜けて行くので長期の保存が出来ない。また飲料水に水素ガスを微細な気泡(マイクロバブル)として存在させれば理論値より多くの水素ガスを存在させることは出来るが、液体の水では水素ガスの上昇気化により長時間に渡って水素ガスを固定(閉じ込める、封入)させることは出来ない。   However, hydrogen water in which hydrogen gas is dissolved is unstable and cannot be stored for a long time because hydrogen gas escapes from the hydrogen water over time. In addition, if hydrogen gas is present in the drinking water as fine bubbles (microbubbles), more hydrogen gas than the theoretical value can be present, but in liquid water, the hydrogen gas rises and vaporizes for a long time. Gas cannot be fixed (confined, sealed).

実験によれば、ペットボトルのようなプラスチックス容器では水素ガスが透過するため、一日で半分以上の水素ガスが抜けてゆく。
アルミニウム容器やアルミニウム箔をラミネートした容器は水素ガスの透過を遅らせ保存性は向上するが、それでも一ヶ月でおよそ半分の水素ガスが失われることが解った。
According to experiments, since hydrogen gas permeates in plastic containers such as PET bottles, more than half of the hydrogen gas escapes in a day.
It was found that aluminum containers and containers laminated with aluminum foil delayed hydrogen gas permeation and improved storage stability, but still lost about half of the hydrogen gas in a month.

現在公知の水素水及び水素ガスを含有させた菓子、食品等としては、次のようなものが紹介されている。
特開2006‐275441号 密閉が完全ではない容器内においても長時間にわたって還元性雰囲気を保ち、鮮魚の腐敗防止、メト化(変色)の進行を抑制することができる水素ガス含有氷、その製造方法および生鮮食品の保存方法を提供するために、生鮮食品と水素ガス含有氷とを容器内で同梱する生鮮食品の保存方法であって、水素ガス含有氷は原料水に水素ガス、または水素ガスと不活性ガスの混合ガスを溶解させ、製氷して氷を得る。
The following are introduced as confectionery, foods, etc. containing hydrogen water and hydrogen gas which are currently known.
JP, 2006-275441, A Hydrogen gas-containing ice that can maintain a reducing atmosphere for a long time even in a container that is not completely sealed, can prevent the decay of fresh fish, and can prevent the progress of metrification (discoloration), and its production method In order to provide a method for preserving fresh food, fresh food and hydrogen gas-containing ice are packaged in a container, and the hydrogen gas-containing ice contains hydrogen gas or hydrogen gas in raw water. And a mixed gas of inert gas are melted and iced to obtain ice.

特開2005‐348706号 2〜5℃の保管状態で、酸化還元電位を−400mVに60日間以上維持するゼラチンから成る冷菓或いはデザート菓子を得るため、浄化水20リットルに、水素ガス(純度99.97%)を、水素注入圧0.9MPa、放出圧0.02MPaで2.5分間吹き込んで製造した酸化還元電位が−615mV、pHが7.23、溶存水素量が1.20ppm、水温が10.3℃の加水素水を490mlを、予めアルミパウチに注入しておいたゼラチン10gに注入し、シェイクし、口栓をして、アルミパウチを密封し、密封状態のまま、85℃で30分間温浴加熱してゼラチンを完全に溶解させる。JP, 2005-348706, A In order to obtain frozen confectionery or dessert confectionery made of gelatin whose oxidation-reduction potential is maintained at -400 mV for 60 days or more in a state of storage at 2 to 5 ° C., hydrogen gas (purity: 99.000) is added to 20 liters of purified water. 97%) was blown for 2.5 minutes at a hydrogen injection pressure of 0.9 MPa and a discharge pressure of 0.02 MPa, an oxidation-reduction potential of −615 mV, a pH of 7.23, a dissolved hydrogen content of 1.20 ppm, and a water temperature of 10 490 ml of 3 ° C hydrogenated water was poured into 10 g of gelatin previously poured into an aluminum pouch, shaken, capped, the aluminum pouch was sealed, and kept at 85 ° C at 85 ° C for 30 minutes. Heat in a warm bath for minutes to dissolve the gelatin completely.

特開2005‐245427号 分散媒体としての水と、分散媒質としての食物繊維を含有する食品、高タンパク質を含む食品、コンドロイチン硫酸を含む食品から成る群から選択された食品とから成り、酸化還元電位が少なくとも−400mVであるゲル状の機能性食品を得るため、水温10℃の水道水500mlを殺菌、脱塩素処理を施し、精密濾過処理を施して異味、異臭、不純物を除去し、シリカ系石英斑岩に金属を担持させた還元触媒に接触させながら、水素ガスを、ガス圧0.9MPaで2.5分間吹き込んで製造した酸化還元電位が−615mVの水490ccをアルミパウチに充填し、次いで牛軟骨起源で腸管で消化吸収しやすいように酵素発酵によって低分子化した市販のゼラチン10グラムを、添加し密封する。JP, 2005-245427, A Food selected from the group consisting of water as a dispersion medium, food containing dietary fiber as a dispersion medium, food containing high protein, food containing chondroitin sulfate, and redox potential In order to obtain a gel-like functional food with a water content of at least −400 mV, sterilize and dechlorinate 500 ml of tap water with a water temperature of 10 ° C., and perform microfiltration to remove off-flavors, off-flavors and impurities, and silica-based quartz The aluminum pouch was filled with 490 cc of water having a oxidation-reduction potential of −615 mV produced by blowing hydrogen gas at a gas pressure of 0.9 MPa for 2.5 minutes while contacting a reduction catalyst having a metal supported on porphyry. 10 grams of commercially available gelatin, which is of bovine cartilage origin and has been reduced in molecular weight by enzymatic fermentation to be easily digested and absorbed in the intestinal tract, is added and sealed.

特許第3944786号 所定の方法で処理して異味、異臭、不純物を除去した浄化水に、シリカ系石英斑岩に金属を担持させた還元触媒に接触させながらガス圧0.9MPaで水素ガスを所定時間吹き込んで酸化還元電位が−600mV以下の分散媒体としての加水素水を予め製造する工程と、前記工程で製造した分散媒体としての加水素水と、分散質としての寒天またはゼラチンを含有する食品を混合してゲル状生成物を製造する工程と、前記工程で製造したゲル状生成物をアルミパウチに充填・密封する工程と、密封状態のまま加熱して、寒天またはゼラチンを含有する食品を完全に溶解する工程とを含む方法で製造された、分散媒としての水の酸化還元電位を加熱工程から60日後も−520mVに維持した加水素水を含むゲル状の機能性食品及び所定の方法で処理して異味、異臭、不純物を除去した分散媒体としての水に、分散質としての寒天またはゼラチンを含有する食品を混合し、アルミパウチに充填・密封する工程と、密封状態のまま加熱して、寒天またはゼラチンを含有する食品を完全に溶解してゲル状生成物を製造する工程と、前記工程で製造したゲル状生成物に、シリカ系石英斑岩に金属を担持させた還元触媒に接触させながらガス圧0.9MPaで水素ガスを所定時間吹き込む工程とを含む方法で製造された、分散媒としての水の酸化還元電位を水素ガスを吹き込んでから60日後も−520mVに維持した加水素水を含むゲル状の機能性食品。Patent No. 3944786 Predetermined hydrogen gas at a gas pressure of 0.9 MPa while being brought into contact with a reduction catalyst in which a metal is supported on silica-based quartz porphyry to purified water that has been treated by a predetermined method to remove off-flavors, off-flavors, and impurities A step of producing hydrogenated water as a dispersion medium having a redox potential of −600 mV or less in advance by blowing in time, a hydrogenated water as a dispersion medium produced in the above step, and agar or gelatin as a dispersoid To produce a gel product by mixing the gel product, the step of filling and sealing the gel product produced in the above step into an aluminum pouch, and heating in a sealed state to prepare a food containing agar or gelatin. In the form of a gel containing hydrogenated water having a redox potential of water as a dispersion medium maintained at -520 mV after 60 days from the heating step. Mixing a food containing agar or gelatin as a dispersoid with water as a dispersion medium that has been treated with a predetermined method to remove off-flavors, off-flavors, and impurities, and filling and sealing the aluminum pouch; Heating in a sealed state to completely dissolve the food containing agar or gelatin to produce a gel-like product, and to the gel-like product produced in the previous step, silica-based quartz porphyry 60 days after the hydrogen gas was blown into the oxidation-reduction potential of water as a dispersion medium, which was produced by a method including a step of blowing hydrogen gas at a gas pressure of 0.9 MPa for a predetermined time while being in contact with the reduction catalyst carrying the catalyst. Is a gel-like functional food containing hydrogenated water maintained at -520 mV.

しかし、上記した公知例では、すべて水に水素ガスを一旦溶存させた後でこの水素ガス溶存水を用いて菓子や食品を加工するため、経時的あるいは加熱により水素ガスが逃失してしまい、商品としては成立しないという問題がある。   However, in the above-described known examples, all hydrogen gas is once dissolved in water, and then the confectionery and food are processed using this hydrogen gas-dissolved water. There is a problem that it is not established as a product.

また、水素ガス溶存水を用いると、食品としての品質に悪い影響が生じてしまうという問題もある。
また、水素ガスを容器内で食品類に溶存させる際に、この容器内に空気が残留していると、この空気も食品中に溶存してしまい、食品の酸化や変色が進行しやすくなり、品質が短期間で悪化するという問題がある。但し、窒素ガス雰囲気中に食品を置換して密封することにより酸化防止を図る方法は周知の技術である。
In addition, when hydrogen gas-dissolved water is used, there is a problem that the quality as a food is adversely affected.
In addition, when hydrogen gas is dissolved in food in the container, if air remains in the container, this air also dissolves in the food, and the oxidation and discoloration of the food easily progress. There is a problem that quality deteriorates in a short period of time. However, a method for preventing oxidation by replacing food in a nitrogen gas atmosphere and sealing it is a well-known technique.

また、特開2006―304762号公報には、食品の組織内部のガス交換を行い、内部組織に還元性の水素ガスを送り込み、加熱加工に際して組織内部の酸化を防止するため、真空脱気により食材組織内部に含まれる気泡を吸出し、これに水素ガスを送り込み、組織周辺を水素ガスで満たし、さらに炭酸ガスを送り込み、加圧して水素ガスを組織内部まで浸透させるガス交換技術が紹介されている。   Japanese Patent Laid-Open No. 2006-304762 discloses that food is exchanged by vacuum degassing in order to exchange gas inside the tissue of food, send reducing hydrogen gas into the internal tissue, and prevent oxidation inside the tissue during heat processing. Gas exchange technology has been introduced in which bubbles contained in the tissue are sucked out, hydrogen gas is fed into the tissue, the surroundings of the tissue are filled with hydrogen gas, carbon dioxide is further fed in, and pressurized to penetrate the hydrogen gas into the tissue.

しかし、上記技術の場合、先ず食材組織内部に水素ガスを満たした後から炭酸ガスを加圧することにより先に満たした水素ガスを内部まで浸透させる技術であって、窒素ガスを商品の酸化防止のために浸透させる技術ではないことと、水素がスと炭酸ガスは組織内で混合することはない。
特開2006―304762号
However, in the case of the above technique, first, after filling the food material structure with hydrogen gas, carbon dioxide gas is pressurized and then the previously filled hydrogen gas is infiltrated into the interior. For this reason, it is not a permeating technique, and hydrogen does not mix with carbon dioxide in the tissue.
JP 2006-304762 A

また容器内から排出される排気中において、水素ガスの濃度が高いと発火の心配や作業環境の悪化を招くという問題がある。
また、水素ガスを単独で食品類に溶存させる場合、攪拌を加えてもどうしても不均一となりがちなことから、均一化するためには時間がかかり、商品の場合に生産性が低下する。
In addition, when the concentration of hydrogen gas is high in the exhaust gas discharged from the container, there is a problem that ignition may be caused and the working environment may be deteriorated.
In addition, when hydrogen gas is dissolved in foods alone, even if agitation is added, it tends to be non-uniform, so it takes time to make it uniform, and productivity is reduced in the case of products.

本発明の目的は、食品中に水素ガスを効率的に、そして均一に溶存させると共に水素ガスを溶存させた商品の品質を長時間に亘り保持することができ、更に作業の安全性にも配慮した水素ガス及び窒素ガスを食品に溶存させる方法及びその装置並びに水素ガス及び窒素ガスを溶存させた食品を提供することである。   The object of the present invention is to efficiently and uniformly dissolve hydrogen gas in foods and maintain the quality of products in which hydrogen gas is dissolved over a long period of time, and also consider work safety. It is to provide a method and apparatus for dissolving hydrogen gas and nitrogen gas dissolved in food and a food in which hydrogen gas and nitrogen gas are dissolved.

上記目的を達成するため、請求項1に記載の発明においては、水素ガスを食品に溶存させる方法において、食品材料を微粉砕し、これに水を加えてゲル状になるまで攪拌する、次に上記ゲル状化した食品材料を容器に入れ、これを冷却しながらマイクロバブル化した水素ガスを食品材料中に混入しつつ攪拌する、次に食品材料が冷却されて凝固したところで攪拌を止め、製品とする、ことを特徴とするものである。   In order to achieve the above object, in the invention according to claim 1, in the method of dissolving hydrogen gas in food, the food material is finely pulverized, and water is added to this and stirred until gelled, Put the gelled food material into a container and stir while cooling the microbubbled hydrogen gas while mixing it in the food material, then stop the stirring when the food material is cooled and solidified, and the product It is characterized by that.

更に、請求項2に記載の発明において、水素ガスを食品に溶存させる方法において、ゼリー状を呈している食品材料を容器に入れて一旦煮沸させたのち、これにマイクロバブル化した水素ガスを混入しながら攪拌を行い、ゲル状化させて製品とする、ことを特徴とするものである。   Furthermore, in the invention according to claim 2, in the method of dissolving hydrogen gas in food, the food material presenting a jelly shape is put in a container and once boiled, and then mixed with microbubbled hydrogen gas The mixture is stirred while being gelled to obtain a product.

更に、請求項3に記載の発明においては、水素ガスを食品に溶存させるための装置において、密閉反応容器内に攪拌子を挿入し、この攪拌子を回転するための可変速攪拌モータを前記密閉反応容器の密閉蓋上に組み付けたこと、
前記密閉蓋は、クランプ装置により反応容器の上口に気密に固定されていて、この密閉蓋には放気口が設けられていること、
前記反応容器内の底部には、発生装置から送られて来た水素ガスを反応容器内においてマイクロバブル化してバブリングするマイクロバブル発生器が組み付けられていること、
を特徴とするものである。
Furthermore, in the invention described in claim 3, in the apparatus for dissolving hydrogen gas in food, a variable speed stirring motor for rotating the stirrer is inserted into the hermetically sealed reaction vessel, and the variable speed stirrer motor is rotated. Assembled on the sealing lid of the reaction vessel,
The sealing lid is airtightly fixed to the upper mouth of the reaction vessel by a clamp device, and the airtight opening is provided in the sealing lid;
The bottom of the reaction vessel is assembled with a microbubble generator for bubbling the hydrogen gas sent from the generator into microbubbles in the reaction vessel,
It is characterized by.

更に、請求項4に記載の発明においては、食品において、マイクロバブル化した水素ガスを溶存することを特徴とするものである。   Furthermore, the invention according to claim 4 is characterized in that the microbubbled hydrogen gas is dissolved in the food.

更に、請求項5に記載の発明においては、水素ガスを食品に溶存させる方法において、食品材料を微粉砕し、これに水を加えてゲル状になるまで攪拌する、次に上記ゲル状化した食品材料を容器に入れ、これを冷却又は加熱しながらマイクロバブル化した水素ガスと窒素ガスの混合体を食品材料中に混入しつつ攪拌する、次に食品材料が冷却されて凝固したところで攪拌を止め、製品とする、ことを特徴とするものである。   Furthermore, in the invention according to claim 5, in the method of dissolving hydrogen gas in the food, the food material is finely pulverized, and water is added thereto and stirred until it becomes a gel. Put the food material in a container, stir while mixing or mixing the microbubbled hydrogen gas and nitrogen gas into the food material while cooling or heating it, and then stir when the food material is cooled and solidified. It is characterized by being stopped and made into a product.

更に、請求項6に記載の発明においては、水素ガス及び窒素ガスを食品に溶存させる方法において、ゼリー状を呈している食品材料を容器に入れて加熱しながら、これにマイクロバブル化した水素ガスと窒素ガスの混合体を混入しながら攪拌を行い、ゲル状化させて製品とする、ことを特徴とするものである。   Furthermore, in the invention according to claim 6, in the method of dissolving hydrogen gas and nitrogen gas in food, hydrogen gas gasified into microbubbles while heating the food material presenting a jelly shape in a container The mixture is stirred while mixing a mixture of nitrogen gas and gelled to obtain a product.

更に、請求項7に記載の発明においては、請求項5乃至6のいずれか1項に記載の水素ガス及び窒素ガスを食品に溶存させる方法において、前記水素ガスの濃度は、窒素ガス100に対して容積比で10%以下に調整されることを特徴とするものである。   Furthermore, in the invention described in claim 7, in the method of dissolving the hydrogen gas and the nitrogen gas according to any one of claims 5 to 6 in the food, the concentration of the hydrogen gas is relative to the nitrogen gas 100. Thus, the volume ratio is adjusted to 10% or less.

更に、請求項8に記載の発明においては、水素ガスと窒素ガスを食品に溶存させるための装置において、密閉反応容器内に攪拌子を挿入し、この攪拌子を回転するための可変速攪拌モータを前記密閉反応容器の密閉蓋上に組み付けたこと、
前記密閉蓋は、クランプ装置により反応容器の上口に気密に固定されていて、この密閉蓋には放気口が設けられていること、
前記反応容器内の底部には、発生装置から送られて来た水素ガスと窒素ガスの混合体を反応容器内においてマイクロバブル化してバブリングするためのマイクロバブル発生器が組み付けられていること、
前記反応容器の下半は、加熱又は冷却用の熱媒容器内に収容されていること、
を特徴とするものである。
Furthermore, in the invention described in claim 8, in a device for dissolving hydrogen gas and nitrogen gas in food, a variable speed stirring motor for inserting a stirring bar into a sealed reaction vessel and rotating the stirring bar Assembled on the sealed lid of the sealed reaction vessel,
The sealing lid is airtightly fixed to the upper mouth of the reaction vessel by a clamp device, and the airtight opening is provided in the sealing lid;
At the bottom of the reaction vessel, a microbubble generator for bubbling a mixture of hydrogen gas and nitrogen gas sent from the generator into microbubbles in the reaction vessel is assembled,
The lower half of the reaction vessel is accommodated in a heating medium container for heating or cooling,
It is characterized by.

更に、請求項9に記載の発明においては、請求項8に記載の水素ガスと窒素ガスを食品に溶存させるための装置において、前記密閉反応容器の放気口から排出される窒素ガスに対する水素ガスの残留濃度は、容積比で10%以下となるように設定されていること、を特徴とするものである。   Furthermore, in the invention according to claim 9, in the apparatus for dissolving the hydrogen gas and nitrogen gas according to claim 8 in the food, hydrogen gas with respect to the nitrogen gas discharged from the vent of the sealed reaction vessel The residual concentration is set to be 10% or less by volume ratio.

更に、請求項10に記載の発明においては、食品において、マイクロバブル化した水素ガスと窒素ガスをともに溶存させて成ることを特徴とするものである。   Furthermore, the invention according to claim 10 is characterized in that in the food, both hydrogen gas and nitrogen gas in the form of microbubbles are dissolved.

本発明は、水素ガスを食品中に含有させる手段として、この水素ガスに窒素ガスを混合し、この混合体をマイクロバブル化して食品材料中に混入するようにした。
この結果、食品の分子及び水素ガスに比較して分子の大きい窒素ガスによりマイクロバブル化した水素ガスは包囲され、窒素ガスと共に食品中に封じ込められるため、水素ガスの経時的な減少が抑えられて多量に水素ガスを摂取することができ、機能性食品としての品質向上と安定性の高い製品を提供することができる。
In the present invention, as a means for containing hydrogen gas in the food, nitrogen gas is mixed with the hydrogen gas, and the mixture is microbubbled to be mixed into the food material.
As a result, hydrogen gas microbubbled by nitrogen gas with larger molecules compared to food molecules and hydrogen gas is surrounded and contained in the food together with nitrogen gas, so the decrease in hydrogen gas over time is suppressed. A large amount of hydrogen gas can be ingested, and a product with improved quality and high stability as a functional food can be provided.

また、水素ガスより分子の大きい窒素ガスの混入により食品中に水素ガスは均一に溶存するため、食品に対する水素ガスの混入効果が高まり、併せて商品中に窒素ガスが溶存することで、酸化防止効果が食品中においても高められることから、長期間に亘って品質を保持することができる。   In addition, the mixing of nitrogen gas, which has a larger molecule than hydrogen gas, dissolves the hydrogen gas uniformly in the food, which increases the effect of mixing the hydrogen gas with the food, and the nitrogen gas is dissolved in the product to prevent oxidation. Since the effect is enhanced even in food, the quality can be maintained over a long period of time.

また、窒素ガスを送入することで反応容器内から排出される水素ガスの温度を低下させて発火や作業環境の悪化を防止する効果がある。   In addition, the introduction of nitrogen gas has the effect of reducing the temperature of the hydrogen gas discharged from the reaction vessel to prevent ignition and deterioration of the working environment.

本発明者は、水素ガスを飽和させた水を液体ではなくゲル状や固体にすれば水素ガスを封入できると考え、氷、コンニャク、寒天、ゼラチンなどを水を主成分とするゲル化食品を用いて水素ガスの封入について実証実験を行った結果、従来の方法で保存した場合に比較して、長期に渡って水素水を安定して保存できると同時に多量(飽和水素水として含まれる水素ガスの2〜3倍)の微細な水素ガスが封入できることが解った。また、水溶液やゾル状では水素ガスは気泡が上昇して離脱するが、ゲル状や固形化して封入された水素ガスは離脱しにくいことも解った。   The present inventor thinks that hydrogen gas can be sealed if water saturated with hydrogen gas is made into a gel or solid instead of liquid, and gelled foods mainly composed of water such as ice, konjac, agar, gelatin, etc. As a result of conducting a verification experiment on the sealing of hydrogen gas, it was possible to stably store hydrogen water for a long period of time compared to the case where it was stored by conventional methods, and at the same time a large amount (hydrogen gas contained as saturated hydrogen water) It was found that 2 to 3 times as much fine hydrogen gas could be enclosed. In addition, in the aqueous solution or sol form, hydrogen gas is lifted and separated, but the gelled or solidified hydrogen gas is difficult to separate.

更に、水素ガスの混入に併せて、窒素ガスを混入すると、水素ガスが均一に、効率良く混入することができると共に安全対策と食品の品質維持に有効であることが解った。   Furthermore, it was found that when nitrogen gas is mixed with hydrogen gas, hydrogen gas can be mixed uniformly and efficiently and is effective for safety measures and food quality maintenance.

本発明は、このような知見に基づいて提供されるものであって、先ず、水素ガスを含有する食品を製造する装置(請求項3)を図1に示す。
1はステンレス製の反応容器であって、ゲル化あるいは氷を含め、冷凍冷却で固形化する原料を原料投入口10から投入する構成である。反応容器1の底にはマイクロバブル発生器2が取付けられ、これに窒素ガスや水素ガスの導入パイプ3が接続されている。
マイクロバブル発生器2は数ミクロンの気孔を有する多孔質アルミナなどのセラミック素材で水素ガスを微気泡(マイクロバブル)に変える。
The present invention is provided based on such knowledge. First, an apparatus for manufacturing a food containing hydrogen gas (Claim 3) is shown in FIG.
Reference numeral 1 denotes a stainless steel reaction vessel having a structure in which raw materials to be solidified by freezing and cooling, including gelation or ice, are fed from a raw material inlet 10. A microbubble generator 2 is attached to the bottom of the reaction vessel 1, and an introduction pipe 3 for nitrogen gas or hydrogen gas is connected to the microbubble generator 2.
The microbubble generator 2 is a ceramic material such as porous alumina having pores of several microns and changes hydrogen gas into microbubbles.

シール用パッキング4を介して攪拌子7とガスの漏れを防ぐためのメカニカルシール9と防爆型可変速攪拌モーター8を一体化した密閉蓋5は、固定用クランプ6で反応容器1を完全に密閉化する。ゲル化食品混合物12はゲル化される前に流動性がある状態、すなわちゾル状で原料投入口10から投入する、あるいは密閉蓋5を開いて投入する。搬出する場合も同様である。   A sealing lid 5 that integrates a stirrer 7 and a mechanical seal 9 for preventing gas leakage and an explosion-proof variable speed stirring motor 8 through a sealing packing 4 completely seals the reaction vessel 1 with a fixing clamp 6. Turn into. The gelled food mixture 12 is put into a fluid state before being gelled, that is, charged in a sol form from the raw material inlet 10 or opened with the sealing lid 5 open. The same applies to carrying out.

先ず反応容器1に水と食材原料あるいはゾル状態の食材合成物を投入し、密閉蓋5を固定クランプ6で密閉してから内部の空気(主に酸素)を除去するため、導入パイプ3から窒素ガスを吹き込み、ガスの排気口14から反応容器1内の空気(酸素)を完全に追い出してから、導入パイプ3より水素ガスを吹き込み、防爆型の可変速攪拌モーター8の回転を調整しながら攪拌子7を回転してマイクロバブル発生器2から発生する水素ガスを供給し、ゾル化食品をゲル化あるいは冷凍冷却で固形化させるとマイクロバブル化した水素ガスを食品に封入固定した。   First, water and a raw material material or a sol-state food composition are put into the reaction vessel 1, and the sealing lid 5 is sealed with a fixed clamp 6, and then internal air (mainly oxygen) is removed. Gas is blown in, and air (oxygen) in the reaction vessel 1 is completely expelled from the gas exhaust port 14, then hydrogen gas is blown in from the introduction pipe 3, and stirring is performed while adjusting the rotation of the explosion-proof variable speed stirring motor 8. When the child 7 is rotated to supply hydrogen gas generated from the microbubble generator 2 and the sol food is solidified by gelation or refrigeration cooling, the microbubble hydrogen gas is sealed and fixed in the food.

空気の排気、窒素ガスや水素ガスの排気はガスの排気口14から図外のガスセンサを経由して排気される。
安全性のため、ガスセンサは酸素と水素濃度を計測し、必要に応じて警報やガスの開閉弁を制御するように設計されている。
Air exhaust, nitrogen gas and hydrogen gas exhaust are exhausted from a gas exhaust port 14 via a gas sensor (not shown).
For safety, the gas sensor is designed to measure oxygen and hydrogen concentrations and control alarms and gas on / off valves as needed.

(請求項1、4に対応)
氷菓子の原料としてアイスクリームやシャーベットの原料(700ml)を反応容器1に投入、これにマイクロバブル化した150mlの水素ガスを反応容器1内に送入し、―70℃の冷凍庫に入れたまま15分攪拌するとマイクロバブル化された水素ガスを含んだまま材料は固形化する。この状態で冷凍保存することで長期に渡って水素ガスを含有したままのアイスクリームやシャーベットが完成し、一ヶ月の保存後に残留した水素ガスはアイスクリームの場合で食品100g当たりの水素ガス含有は以下の通りであった。
(Corresponding to claims 1 and 4)
Ice cream and sherbet raw materials (700 ml) are put into the reaction vessel 1 as ice confectionery raw materials, and 150 ml of hydrogen gas made into microbubbles is sent into the reaction vessel 1 and kept in a freezer at -70 ° C. When stirred for 15 minutes, the material solidifies while containing microbubbled hydrogen gas. By storing frozen in this state, ice cream or sherbet containing hydrogen gas for a long period of time is completed, and the hydrogen gas remaining after storage for one month is ice cream. It was as follows.

バニラアイスクリーム:製造直後…3〜5ml/100g
10日後…2〜4ml/100g
30日後…1〜2ml/100g
ORP参考値…製造直後 −401mV
11日後 −304mV
Vanilla ice cream: Immediately after production ... 3-5ml / 100g
10 days later… 2-4ml / 100g
30 days later ... 1-2ml / 100g
ORP reference value: Immediately after production -401 mV
11 days later -304 mV

氷シャーベット :製造直後…3〜5ml/100g
10日後…2.5 〜4.5ml/100g
30日後…2〜4ml/100g
ORP参考値…製造直後 −316mV
11日後 −259mV
Ice sherbet: Immediately after production ... 3-5ml / 100g
10 days later ... 2.5-4.5ml / 100g
30 days later ... 2-4ml / 100g
ORP reference value: Immediately after production -316 mV
11 days later -259 mV

(請求項2、4に対応)
約40℃に加熱した800mlの水を反応容器1に入れ、内部を窒素ガスで満たしてからコンニャク粉25gを原料投入口10から投入し、攪拌子7で攪拌しながら導入パイプ3から水素ガスを200ml導入し、マイクロバブル発生器2からマイクロバブル化した水素ガスを反応容器1内において原料中に混入し、ゲル化したら一度攪拌と水素ガスを止め、約30分放置してから、1パーセントの水酸化カルシウム100mlを原料投入口10から入れて再度水素ガスを導入しながら攪拌し、粘性のあるゲル状になったら攪拌と水素ガスの供給を止め、密閉蓋5を開き容器に移して整形し、30分放置後30分位湯がいて製品とした。
(Corresponding to claims 2 and 4)
800 ml of water heated to about 40 ° C. is put into the reaction vessel 1, and the inside is filled with nitrogen gas, then 25 g of konjac powder is introduced from the raw material inlet 10, and hydrogen gas is introduced from the introduction pipe 3 while stirring with the stirrer 7. 200 ml was introduced, and microbubbled hydrogen gas from the microbubble generator 2 was mixed into the raw material in the reaction vessel 1 and once gelled, the stirring and hydrogen gas were stopped and left for about 30 minutes. Stir in 100 ml of calcium hydroxide from the raw material inlet 10 while introducing hydrogen gas again. When it becomes a viscous gel, stop stirring and supplying hydrogen gas, open the sealing lid 5 and transfer to a container for shaping. After leaving for 30 minutes, hot water was poured for about 30 minutes to obtain a product.

《水素ガス含有データ》
※製造直後の水素ガス含有量…コンニャク100g当たり水素ガスは5〜7
ml含有し、10日後の含有量は4.5〜6m
lであった。
《Hydrogen gas content data》
* Hydrogen gas content immediately after production: 5 to 7 hydrogen gas per 100 grams of konjac
Contains 10 ml, the content after 10 days is 4.5-6m
l.

なお、水素ガスの含有の目安として酸化還元電位(ORP値)を参考値として用いることが多いので、本実施例2の水素ガスを含むコンニャクのORP値を次に説明するが、ORP値は、経日、煮沸時間とともに減少する。   In addition, since an oxidation-reduction potential (ORP value) is often used as a reference value as a measure of the hydrogen gas content, the ORP value of konjac containing hydrogen gas in Example 2 will be described below. It decreases with time and boiling time.

ORP値の経時変化
・冷蔵庫内で保存の場合
経過日数 ORP値
1日 −836mV
7日 −450mV
19日 −117mV
・煮沸の場合
経過時間
0時間 −160mV
2時間 −110mV
使用計測器:業務用酸化還元電位計ORPプロ(株式会社佐藤商事製)
Change in ORP value over time ・ When stored in the refrigerator Elapsed days ORP value 1 day −836 mV
7th -450mV
19th -117mV
・ In the case of boiling Elapsed time 0 hours -160 mV
2 hours -110 mV
Measuring instrument used: Commercial redox potentiometer ORP Pro (manufactured by Sato Corporation)

(請求項1、4に対応)
水約500mlと寒天4gを火にかけ、2分ほど沸騰させ煮沸したのち、火を止め、好みの味付けをする。
次に、この味付けを行った寒天を反応容器1に入れてその後は実施例1と同様な操作で水素ガスを通じながら攪拌し、冷却固化(ゲル化)直前で型枠に入れて完成品とした。
(Corresponding to claims 1 and 4)
Boil about 500 ml of water and 4 g of agar, boil for 2 minutes, boil, stop the fire, and season.
Next, the seasoned agar was put into the reaction vessel 1, and then stirred while passing hydrogen gas in the same manner as in Example 1, and put into a mold just before cooling and solidification (gelation) to obtain a finished product. .

《水素ガス含有データ》
※製造直後の水素ガス含有量…寒天100g当たり水素ガスは2.5〜3.
5ml含有し、10日後の含有量は2〜3ml
であった。
ORP参考値…製造直後 −554mV
10日後 +35mV
《Hydrogen gas content data》
* Hydrogen gas content immediately after production: Hydrogen gas per 100g of agar is 2.5-3.
Contains 5ml, and content after 10 days is 2-3ml
Met.
ORP reference value: Immediately after production -554 mV
10 days later +35 mV

(請求項2、4に対応)
先ず、ゼラチンパウダー20gを500mlの水にふり入れてふやかし、次に鍋にジュース150ml、牛乳150ml、白砂糖小さじ1杯を入れて溶解し、次にこれを沸騰しない程度に軽く50〜60℃になるまで温める。
(Corresponding to claims 2 and 4)
First, add 20 g of gelatin powder to 500 ml of water, and then add 150 ml of juice, 150 ml of milk, and a teaspoon of white sugar to dissolve, and then lightly heat it to 50-60 ° C so that it does not boil. Warm up to.

次に、反応容器1に入れて実施例1と同様の方法で水素ガス約150mlを混入しながらゲル化するまで反応容器1を冷却し、ゲル化直前に攪拌と水素ガスの供給を止め、型枠に入れて製品とした。   Next, the reaction vessel 1 is cooled in the reaction vessel 1 in the same manner as in Example 1 until gelation while mixing about 150 ml of hydrogen gas, and stirring and the supply of hydrogen gas are stopped immediately before gelation. The product was put in a frame.

《水素ガス含有データ》
※製造直後の水素ガス含有量…食品100g当たり水素ガスは3〜4ml含
有し、10日後の含有量は2.5〜3.5ml
であった。
ORP参考値…製造直後 −427mV
11日後 −229mV
《Hydrogen gas content data》
* Hydrogen gas content immediately after production: 3-4ml of hydrogen gas per 100g of food
It has a content of 2.5 to 3.5 ml after 10 days
Met.
ORP reference value-immediately after production -427 mV
11 days later -229 mV

(請求項1、4に対応)
氷を製造する過程で、過冷却された水500mlにマイクロバブルの水素ガスを約100ml吹き込んで攪拌しつつ急速に結晶化させて結氷させる、あるいは攪拌しながら氷を作る過程で、流動性あるシャーベット状態になった段階でマイクロバブルの水素ガスを吹き込みながら結氷させ、氷100ml当たり約3〜5mlの水素ガスを閉じ込める。
(Corresponding to claims 1 and 4)
In the process of producing ice, about 100 ml of microbubble hydrogen gas is blown into 500 ml of supercooled water and rapidly crystallized with stirring to form ice, or in the process of making ice while stirring, fluid sherbet At the stage when it is in a state, it is frozen while blowing microbubble hydrogen gas, and about 3 to 5 ml of hydrogen gas per 100 ml of ice is confined.

《水素ガス含有データ》
※製造直後の水素ガス含有量…氷100g当たり水素ガスは5〜8ml含有
し、10日後4.5〜7.5ml、30日後4
〜6mlであった。
ORP参考値…製造直後 −201mV
11日後 −200mV
以上に説明した実施例1〜5では、実施例5の氷に閉じ込めた水素ガスが最も保存性が良かった。
《Hydrogen gas content data》
* Hydrogen gas content immediately after production: 5-8ml of hydrogen gas per 100g of ice
4.5 to 7.5 ml after 10 days, 4 after 30 days
~ 6ml.
ORP reference value: Immediately after production -201 mV
11 days later -200 mV
In Examples 1 to 5 described above, the hydrogen gas confined in the ice of Example 5 had the best preservation.

(請求項5、7、8に対応)
図2に基づいて請求項7、9に記載した装置の実施例を説明すると共に請求項5及び6に記載した方法の実施例を詳述する。
図2において、図1と同一の符号は同一物を指しているので、ここでの説明は省略し、異なる部分についてのみ新規の符号を付して説明する。
(Corresponding to claims 5, 7 and 8)
An embodiment of the apparatus according to claims 7 and 9 will be described with reference to FIG. 2 and an embodiment of the method according to claims 5 and 6 will be described in detail.
2, the same reference numerals as those in FIG. 1 indicate the same components, and therefore, description thereof is omitted here, and only different portions are described with new reference numerals.

符号の15は反応容器1の下半1aを収容している熱媒加熱容器であって、この熱媒加熱容器15内には、加熱又は冷却用熱媒16が図示しない熱媒発生装置から送給パイプ15a、還りパイプ15bを経由して循環自在に構成されている。
本実施例においては、この熱媒加熱容器15内には熱媒16が循環するようになっているが、材料によっては、熱媒加熱容器15内に熱媒16を満たし、ヒーター28で加熱又は冷却するように構成しても良い。
Reference numeral 15 denotes a heating medium heating container that accommodates the lower half 1a of the reaction container 1. In the heating medium heating container 15, a heating or cooling heating medium 16 is sent from a heating medium generator (not shown). It is configured to be circulated through a supply pipe 15a and a return pipe 15b.
In the present embodiment, the heating medium 16 is circulated in the heating medium heating container 15, but depending on the material, the heating medium 16 is filled in the heating medium heating container 15 and heated by the heater 28. You may comprise so that it may cool.

17は反応容器1内の底部に設けられた水素ガスと窒素ガスの混合体を反応容器1内に噴出させるためのマイクロバブル発生器18に送給するための水素ガス及び窒素ガス送入パイプであって、この送入パイプ17には流量制御器19が取り付けてあり、反応容器1内に送給する水素ガスと窒素ガスの混合流体の量を制御する。   Reference numeral 17 denotes a hydrogen gas and nitrogen gas feed pipe for feeding a mixture of hydrogen gas and nitrogen gas provided at the bottom of the reaction vessel 1 to the microbubble generator 18 for jetting into the reaction vessel 1. The flow rate controller 19 is attached to the feed pipe 17 and controls the amount of the mixed fluid of hydrogen gas and nitrogen gas fed into the reaction vessel 1.

20は制御バルブであって、上流側に設けた水素ガスと窒素ガスの混合器27から送給されてくるガスの制御及び反応容器1内の水素ガス濃度をガスセンサ25で検出し、この濃度(水素ガス濃度)が窒素ガス100に対して容積比(濃度)で10%以上となったときに制御バルブ20を遮断する。   Reference numeral 20 denotes a control valve, which controls the gas supplied from the hydrogen gas / nitrogen gas mixer 27 provided on the upstream side and detects the hydrogen gas concentration in the reaction vessel 1 with the gas sensor 25. When the volume ratio (concentration) of the hydrogen gas concentration is 10% or more with respect to the nitrogen gas 100, the control valve 20 is shut off.

なお、反応容器1内の水素ガス濃度は常時このガスセンサ25で検出されていて、前記10%以下の設定値となるように混合器をフィードバック制御しているが、水素ガスの濃度は、当然のこととして10%に近いことが望ましい。
23は反応容器1内から水素ガスと窒素ガスを排出するための排気パイプであって、このパイプ23には制御弁24が取り付けられていて、排気量の制御を行うことができる。
26は反応容器1内の食品材料12の品温を温度センサ27で検出し、この品温が設定値となるように前記熱媒加熱容器15内に循環又は貯留する熱媒の量及び温度を制御する。
図中28は熱媒加熱容器15内の熱媒を加熱するときに用いる電気ヒータである。
The hydrogen gas concentration in the reaction vessel 1 is always detected by the gas sensor 25, and the mixer is feedback-controlled so that the set value is 10% or less. In particular, it is desirable to be close to 10%.
Reference numeral 23 denotes an exhaust pipe for discharging hydrogen gas and nitrogen gas from the reaction vessel 1, and a control valve 24 is attached to the pipe 23 so that the exhaust amount can be controlled.
26 detects the product temperature of the food material 12 in the reaction container 1 with a temperature sensor 27, and determines the amount and temperature of the heat medium circulated or stored in the heat medium heating container 15 so that the product temperature becomes a set value. Control.
In the figure, 28 is an electric heater used when heating the heating medium in the heating medium heating container 15.

以上に説明した装置を用いて行う請求項5に記載の溶存方法を説明する。
反応容器1内にゲル化食品材料12を投入したあと、窒素ガス導入パイプ3から窒素ガスを反応容器1内に送入して反応容器1内に残留している空気を排気パイプ23から追い出して反応容器1内の空間を窒素ガスに置換する。
The dissolution method of Claim 5 performed using the apparatus demonstrated above is demonstrated.
After the gelled food material 12 is introduced into the reaction vessel 1, nitrogen gas is fed into the reaction vessel 1 from the nitrogen gas introduction pipe 3, and air remaining in the reaction vessel 1 is expelled from the exhaust pipe 23. The space in the reaction vessel 1 is replaced with nitrogen gas.

次に、水素ガスと窒素ガスが容積比1:9で混合された窒素と水素のガスを送入パイプ17からマイクロバブル発生器18に供給し、ここで多孔質アルミナなどのセラミック素材により数ミクロン単位の微気泡(マイクロバブル)に調整し、これを攪拌子7で攪拌されている状態の食品材料12中に混入し、食品材料12中に水素ガスと窒素ガスを溶存させる。   Next, nitrogen and hydrogen gas in which hydrogen gas and nitrogen gas are mixed at a volume ratio of 1: 9 is supplied from the feed pipe 17 to the microbubble generator 18 where the ceramic material such as porous alumina is used for several microns. It adjusts to the microbubble of a unit, this is mixed in the food material 12 of the state stirred with the stirring element 7, and hydrogen gas and nitrogen gas are dissolved in the food material 12. FIG.

この水素ガスと窒素ガスの溶存に際し、食品材料12によっては加熱した方が溶存効率の良いもの例えば粘性の高いものもあるので、この際は熱媒加熱容器15内に熱媒16を循環させて食品材料12を一定の温度に加熱しながら行う。   When the hydrogen gas and the nitrogen gas are dissolved, some food materials 12 are heated more efficiently, for example, are more viscous. In this case, the heating medium 16 is circulated in the heating medium heating container 15. This is performed while heating the food material 12 to a certain temperature.

本実施例7で行った食品材料と加工条件及び水素ガスと窒素ガスの溶存データを次に示す。
氷菓子の原料としてアイスクリームやシャーベットの原料(700ml)を反応容器1に投入、これにマイクロバブル化した150mlの水素ガスと1500mlの窒素ガスを反応容器1内に送入し、冷蔵庫に入れたまま材料は固形化する。この状態で冷凍保存することで長期に渡って水素ガスと窒素ガスを含有したままのアイスクリームやシャーベットが完成し、一ヶ月の保存後に残留した水素ガスの溶存量はアイスクリームの場合で食品100g当たり以下の通りであった。
また、窒素ガスの溶存率は以下のとおりであった。
The food material, processing conditions, and dissolved data of hydrogen gas and nitrogen gas performed in Example 7 are shown below.
Ice cream and sherbet raw materials (700 ml) were put into the reaction container 1 as ice confectionery raw materials, and 150 ml of hydrogen gas and 1500 ml of nitrogen gas made into microbubbles were fed into the reaction container 1 and placed in the refrigerator. The material solidifies as it is. By storing frozen in this state, ice cream and sherbet containing hydrogen gas and nitrogen gas for a long time are completed, and the dissolved amount of hydrogen gas remaining after storage for one month is 100 g of food in the case of ice cream. It was as follows.
Moreover, the dissolved rate of nitrogen gas was as follows.

バニラアイスクリーム:製造直後…3〜5ml/100g(窒素ガス8ml/100g) 10日後…2〜4ml/100g(窒素ガス6ml/100g)
30日後…1〜2ml/100g(窒素ガス3ml/100g)
ORP参考値…製造直後 −401mV
(窒素ガス8ml/100g)
11日後 −304mV
(窒素ガス6ml/100g)
Vanilla ice cream: immediately after production ... 3-5 ml / 100 g (nitrogen gas 8 ml / 100 g) 10 days later ... 2-4 ml / 100 g (nitrogen gas 6 ml / 100 g)
30 days later… 1-2 ml / 100 g (nitrogen gas 3 ml / 100 g)
ORP reference value: Immediately after production -401 mV
(Nitrogen gas 8ml / 100g)
11 days later -304 mV
(Nitrogen gas 6ml / 100g)

なお、製品の経時的品質変化を調べたが、アルミ箔複合ラミネートフィルムで密封した状態での保存では14ヵ月後においても水素ガス、窒素ガスの溶存量に変化がなく、品質にも変化は認められなかった。   The quality of the product over time was examined, but when stored in a sealed state with an aluminum foil composite laminate film, the dissolved amount of hydrogen gas and nitrogen gas did not change even after 14 months, and the quality was also changed. I couldn't.

氷シャーベットの場合は次のとおりであった。
氷シャーベット :製造直後…3〜5ml/100g(窒素ガス8ml/100g)
10日後…2.5 〜4.5ml/100g
(窒素ガス6ml/100g)
30日後…2〜4ml/100g(窒素ガス3ml/100g)
ORP参考値…製造直後 −316mV
(窒素ガス8ml/100g)
11日後 −259mV
(窒素ガス6ml/100g)
In the case of ice sherbet:
Ice sherbet: Immediately after production ... 3-5 ml / 100 g (nitrogen gas 8 ml / 100 g)
10 days later ... 2.5-4.5ml / 100g
(Nitrogen gas 6ml / 100g)
30 days later ... 2-4 ml / 100 g (nitrogen gas 3 ml / 100 g)
ORP reference value: Immediately after production -316 mV
(Nitrogen gas 8ml / 100g)
11 days later -259 mV
(Nitrogen gas 6ml / 100g)

本実施例は、請求項6に記載した発明に対応するものであり、食品材料12を加熱して煮沸させ、これに水素ガスと窒素ガスを混合して混入し、溶存させる加工法である。
約40℃に加熱した800mlの水を反応容器1に入れ、内部を窒素ガスで置換してからコンニャク粉25gを原料投入口10から投入し、攪拌子7で攪拌しながら導入パイプ3から水素ガスを200ml、窒素ガスを2000ml導入し、マイクロバブル発生器2からマイクロバブル化した水素ガスと窒素ガスを反応容器1内において原料中に混入し、ゲル化したら一度攪拌と水素ガス及び窒素ガスを止め、約30分放置してから、1パーセントの水酸化カルシウム100mlを原料投入口10から入れて再度水素ガスと窒素ガスを導入しながら攪拌し、粘性のあるゲル状になったら攪拌と水素ガスと窒素ガスの供給を止め、密閉蓋5を開き容器に移して成形し、30分放置後30分位湯がいて製品とした。
この製品とした直後の水素ガスの溶存量は5〜7ml/100g、10日後で4.5〜6ml/100gであった。
The present embodiment corresponds to the invention described in claim 6, and is a processing method in which the food material 12 is heated and boiled, mixed with hydrogen gas and nitrogen gas, and dissolved.
800 ml of water heated to about 40 ° C. is put into the reaction vessel 1, the inside is replaced with nitrogen gas, and then 25 g of konjac powder is introduced from the raw material introduction port 10, and hydrogen gas is introduced from the introduction pipe 3 while stirring with the stirrer 7. 200 ml of nitrogen gas and 2000 ml of nitrogen gas were introduced, and the hydrogen gas and nitrogen gas made into microbubbles from the microbubble generator 2 were mixed in the raw material in the reaction vessel 1 and once gelled, the stirring, hydrogen gas and nitrogen gas were stopped Then, after leaving for about 30 minutes, 100 ml of 1% calcium hydroxide is introduced from the raw material inlet 10 and stirred again while introducing hydrogen gas and nitrogen gas. The supply of nitrogen gas was stopped, the sealing lid 5 was opened, transferred to a container, molded, left for 30 minutes, and then hot water was added for about 30 minutes to obtain a product.
The dissolved amount of hydrogen gas immediately after making this product was 5 to 7 ml / 100 g, and 4.5 to 6 ml / 100 g after 10 days.

なお、水素ガスの含有の目安として酸化還元電位(ORP値)を参考値として用いることが多いので、実施例8の水素ガスと窒素ガスを含むコンニャクのORP値を次に説明するが、ORP値は、経日、煮沸時間とともに減少する。   In addition, since the oxidation-reduction potential (ORP value) is often used as a reference value as a measure of the hydrogen gas content, the ORP value of konjac containing hydrogen gas and nitrogen gas in Example 8 will be described below. Decreases with time and boiling time.

ORP値の経時変化
・冷蔵庫内で保存の場合
経過日数 ORP値
1日 −836mV(窒素ガス8ml/100g)
7日 −450mV(窒素ガス5ml/100g)
19日 −117mV(窒素ガス4ml/100g)
Temporal change of ORP value ・ When stored in the refrigerator Elapsed days ORP value 1 day -836 mV (Nitrogen gas 8 ml / 100 g)
7th -450mV (Nitrogen gas 5ml / 100g)
19th -117mV (nitrogen gas 4ml / 100g)

・煮沸の場合
経過時間
0時間 −160mV(窒素ガス4.5ml/100g)
2時間 −110mV(窒素ガス4ml/100g)
-In the case of boiling Elapsed time 0 hours -160 mV (nitrogen gas 4.5 ml / 100 g)
2 hours -110 mV (nitrogen gas 4 ml / 100 g)

なお、製品の経時的品質変化を調べたが、アルミ箔複合ラミネートフィルムで密封した状態での保存では14ヵ月後においても水素ガス、窒素ガスの溶存量(含有率)に変化がなく、品質にも変化は認められなかった。
使用計測器:業務用酸化還元電位計ORPプロ(株式会社佐藤商事製)
The quality of the product over time was examined, but when it was stored in a sealed state with an aluminum foil composite laminate film, the dissolved amount (content rate) of hydrogen gas and nitrogen gas did not change even after 14 months. No change was observed.
Measuring instrument used: Commercial redox potentiometer ORP Pro (manufactured by Sato Corporation)

本発明は、次のような加工食品あるいは菓子の製造工程にとり込むことにより、水素ガス及び窒素ガスを多量に含有した機能性食品及び菓子、氷等を得ることができる。
ねり加工の工程で水素ガスを混入する食品及び菓子としては、
1.豆腐
2.ソーセージ
3.ヨーグルト
4.かまぼこ、ちくわ、半ペイ、さつま揚げ、肉団子
5.もち、大福、だんご
6.マシュマロ、求肥
7.餃子、しゅうまい、シュークリームの皮
8.羊羹、ういろう
9.あん、クリーム、ジャム、カレー、プリン
10.小麦、米、もち米、とうもろこしなど穀物粉および豆類、芋類、野菜、コーヒー
、カカオ類粉体からの加工食品
11.氷
In the present invention, functional foods and confectionery, ice, and the like containing a large amount of hydrogen gas and nitrogen gas can be obtained by incorporating them into the following process for producing processed foods or confectionery.
As food and confectionery mixed with hydrogen gas in the batter processing process,
1. Tofu 2. Sausages; Yogurt 4. Kamaboko, chikuwa, half-pay, deep-fried sweet potato, meat dumpling Mochi, Daifuku, Dango 6. Marshmallow, fertilization 7. Dumplings, sweet potatoes, cream puff skin Yokan, Uiro 9 An, cream, jam, curry, pudding 10. Processed foods from wheat flour, rice, glutinous rice, corn and other cereal flour and beans, potatoes, vegetables, coffee and cacao powder. ice

ところで、水1Lに溶解(溶存)する気体は、水から完全に気体を脱気した場合の条件で溶解する窒素ガスは20℃1気圧で14.3ml、水素ガスは17.5mlであるが、水道水など一般の飲料水には酸素ガスや窒素ガス、炭酸ガスなどが溶解しており、長時間かけてガスを吹き込んでも窒素ガス、水素ガスともに5〜10ml位しか溶解しないが、これらのガスを10μ以下の微気泡(マイクロバブル)として吹き込むと、気泡として残留する、食品として、コンニャクの製造工程で窒素ガスと水素ガスを容積比10対1で微気泡の通気で加工した直後で、完成コンニャク1kgに微気泡を含めた窒素ガス、水素ガス共に60〜80mlが存在し、常温で3日経過した後の窒素ガスは約50〜60ml、水素ガスは2〜3ml残留する。
窒素ガスの方が残留しやすいが、食品の中に窒素ガスが存在すると酸化、腐敗を防止するので都合良い。
By the way, the gas dissolved (dissolved) in 1 L of water is 14.3 ml at 20 ° C. and 1 atmosphere, and 17.5 ml of hydrogen gas at 20 ° C. under 1 atm when the gas is completely degassed from water. In general drinking water such as tap water, oxygen gas, nitrogen gas, carbon dioxide gas, etc. are dissolved, and even if gas is blown in over a long time, both nitrogen gas and hydrogen gas dissolve only about 5 to 10 ml. Is blown as fine bubbles (microbubbles) of 10 μm or less, and it remains as bubbles. As a food product, nitrogen gas and hydrogen gas are processed by aeration of fine bubbles at a volume ratio of 10: 1 in the manufacturing process of konjac. There are 60 to 80 ml of nitrogen gas and hydrogen gas including fine bubbles in 1 kg of konjac, about 50 to 60 ml of nitrogen gas after 3 days at room temperature, and 2 to 3 ml of hydrogen gas remain.
Nitrogen gas tends to remain, but if nitrogen gas is present in the food, it is convenient because it prevents oxidation and spoilage.

本発明に係る水素ガス含有食品及び菓子の製造装置を示す説明図Explanatory drawing which shows the manufacturing apparatus of the hydrogen gas containing foodstuffs and confectionery which concern on this invention 熱媒加熱容器を有する装置を示す説明図Explanatory drawing which shows the apparatus which has a heat-medium heating container

符号の説明Explanation of symbols

1 反応容器
2 マイクロバブル発生器
3 窒素ガスと水素ガスの入口
4 シール用パッキング
5 密閉蓋
6 固定用クランプ
7 攪拌子
8 可変速攪拌モータ
9 メカニカルシール
10 原料投入口
11 パッキング
12 ゲル化食品混合物
13 窒素と水素ガス
14 ガスの排出口
15 熱媒加熱容器
16 熱媒
17 水素ガスと窒素ガス送給パイプ
23 排気パイプ
25 水素ガス濃度検出ガスセンサ
27 食品材料温度検出センサ
DESCRIPTION OF SYMBOLS 1 Reaction container 2 Microbubble generator 3 Inlet of nitrogen gas and hydrogen gas 4 Sealing packing 5 Sealing lid 6 Fixing clamp 7 Stirrer 8 Variable speed stirring motor 9 Mechanical seal 10 Raw material inlet 11 Packing 12 Gelled food mixture 13 Nitrogen and hydrogen gas 14 Gas outlet 15 Heat medium heating vessel 16 Heat medium 17 Hydrogen gas and nitrogen gas supply pipe 23 Exhaust pipe 25 Hydrogen gas concentration detection gas sensor 27 Food material temperature detection sensor

Claims (10)

食品材料を微粉砕し、これに水を加えてゲル状になるまで攪拌する、次に上記ゲル状化した食品材料を容器に入れ、これを冷却しながらマイクロバブル化した水素ガスを食品材料中に混入しつつ攪拌する、次に食品材料が冷却されて凝固したところで攪拌を止め、製品とする、ことを特徴とする水素ガスを食品に溶存させる方法。   Finely pulverize the food material, add water to it and stir until it forms a gel, then place the gelled food material in a container and cool the microbubbled hydrogen gas in the food material A method of dissolving hydrogen gas in a food, characterized in that the mixture is stirred while being mixed, and then stopped when the food material is cooled and solidified to produce a product. ゼリー状を呈している食品材料を容器に入れて一旦煮沸させたのち、これにマイクロバブル化した水素ガスを混入しながら攪拌を行い、ゲル状化させて製品とする、ことを特徴とする水素ガスを食品に溶存させる方法。   A hydrogen substance characterized in that after a food material presenting a jelly shape is put in a container and boiled once, it is stirred while mixing microbubbled hydrogen gas and gelled into a product. A method of dissolving gas in food. 密閉反応容器内に攪拌子を挿入し、この攪拌子を回転するための可変速攪拌モータを前記密閉反応容器の密閉蓋上に組み付けたこと、
前記密閉蓋は、クランプ装置により反応容器の上口に気密に固定されていて、この密閉蓋には放気口が設けられていること、
前記反応容器内の底部には、発生装置から送られて来た水素ガスを反応容器内においてマイクロバブル化してバブリングするマイクロバブル発生器が組み付けられていること、
を特徴とする水素ガスを食品に溶存させるための装置。
A stirrer was inserted into the sealed reaction vessel, and a variable speed agitation motor for rotating the stirrer was assembled on the sealed lid of the sealed reaction vessel,
The sealing lid is airtightly fixed to the upper mouth of the reaction vessel by a clamp device, and the airtight opening is provided in the sealing lid;
The bottom of the reaction vessel is assembled with a microbubble generator for bubbling the hydrogen gas sent from the generator into microbubbles in the reaction vessel,
A device for dissolving hydrogen gas in foods.
マイクロバブル化した水素ガスを溶存する食品。   Foods that dissolve microbubbled hydrogen gas. 食品材料を微粉砕し、これに水を加えてゲル状になるまで攪拌する、次に上記ゲル状化した食品材料を容器に入れ、これを冷却又は加熱しながらマイクロバブル化した水素ガスと窒素ガスの混合体を食品材料中に混入しつつ攪拌する、次に食品材料が冷却されて凝固したところで攪拌を止め、製品とする、ことを特徴とする水素ガスを食品に溶存させる方法。   Finely pulverize the food material, add water to this and stir until gelled, then put the gelled food material into a container and cool or heat it into microbubbled hydrogen gas and nitrogen A method of dissolving hydrogen gas in a food, characterized in that the mixture of gas is stirred while being mixed in the food material, and then the stirring is stopped when the food material is cooled and solidified to produce a product. ゼリー状を呈している食品材料を容器に入れて加熱しながらこれにマイクロバブル化した水素ガスと窒素ガスの混合体を混入しながら攪拌を行い、ゲル状化させて製品とする、ことを特徴とする水素ガス及び窒素ガスを食品に溶存させる方法。   A food material that is in the form of a jelly is put in a container and heated while stirring and mixed with a mixture of hydrogen gas and nitrogen gas that has been made into microbubbles. A method of dissolving hydrogen gas and nitrogen gas in food. 前記水素ガスの濃度は、窒素ガス100に対して容積比で10%以下に調整されることを特徴とする請求項5乃至6のいずれか1項に記載の水素ガス及び窒素ガスを食品に溶存させる方法。   7. The hydrogen gas and nitrogen gas according to claim 5, wherein the concentration of the hydrogen gas is adjusted to 10% or less by volume ratio with respect to the nitrogen gas 100. How to make. 密閉反応容器内に攪拌子を挿入し、この攪拌子を回転するための可変速攪拌モータを前記密閉反応容器の密閉蓋上に組み付けたこと、
前記密閉蓋は、クランプ装置により反応容器の上口に気密に固定されていて、この密閉蓋には放気口が設けられていること、
前記反応容器内の底部には、発生装置から送られて来た水素ガスと窒素ガスの混合体を反応容器内においてマイクロバブル化してバブリングするためのマイクロバブル発生器が組み付けられていること、
前記反応容器の下半は、加熱又は冷却用の熱媒容器内に収容されていること、
を特徴とする水素ガスと窒素ガスを食品に溶存させるための装置。
A stirrer was inserted into the sealed reaction vessel, and a variable speed agitation motor for rotating the stirrer was assembled on the sealed lid of the sealed reaction vessel,
The sealing lid is airtightly fixed to the upper mouth of the reaction vessel by a clamp device, and the airtight opening is provided in the sealing lid;
At the bottom of the reaction vessel, a microbubble generator for bubbling a mixture of hydrogen gas and nitrogen gas sent from the generator into microbubbles in the reaction vessel is assembled,
The lower half of the reaction vessel is accommodated in a heating medium container for heating or cooling,
A device for dissolving hydrogen gas and nitrogen gas in food.
前記密閉反応容器の放気口から排出される窒素ガスに対する水素ガスの残留濃度は、容積比で10%以下となるように設定されていること、を特徴とする請求項8に記載の水素ガスと窒素ガスを食品に溶存させるための装置。   9. The hydrogen gas according to claim 8, wherein the residual concentration of the hydrogen gas with respect to the nitrogen gas discharged from the vent of the sealed reaction vessel is set to be 10% or less by volume ratio. And equipment for dissolving nitrogen gas in food. マイクロバブル化した水素ガスと窒素ガスをともに溶存させて成る食品。   Food made by dissolving both hydrogen gas and nitrogen gas in microbubbles.
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