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JP6438736B2 - Umeboshi component leachate concentrate and Umeboshi extract - Google Patents
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JP6438736B2 - Umeboshi component leachate concentrate and Umeboshi extract - Google Patents

Umeboshi component leachate concentrate and Umeboshi extract Download PDF

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JP6438736B2
JP6438736B2 JP2014221832A JP2014221832A JP6438736B2 JP 6438736 B2 JP6438736 B2 JP 6438736B2 JP 2014221832 A JP2014221832 A JP 2014221832A JP 2014221832 A JP2014221832 A JP 2014221832A JP 6438736 B2 JP6438736 B2 JP 6438736B2
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umeboshi
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plum
dried
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JP2016086673A (en
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伸広 金山
伸広 金山
裕亮 金山
裕亮 金山
宏介 南部
宏介 南部
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Sunactis Co Ltd
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本発明は梅干しのエキスに関し、特に梅干しのエキスを含有する飲食品素材に関する。エキスは抽出物を意味し、動植物の成分を水等の媒体で浸出させた液体を濃縮したものをいう。エキスという文言の意味には液体も固体も含まれる。   The present invention relates to a pickled plum extract, and more particularly to a food or drink material containing a pickled plum extract. An extract means an extract, which is a concentrated liquid obtained by leaching animal and plant components with a medium such as water. The meaning of the word “extract” includes both liquid and solid.

梅干し風味の食品としては、梅干しの果肉(即ち、梅肉)、梅酢及び梅果汁等が加えられたキャンデー、シロップ等が存在する。梅干し風味の飲料として、特許文献1には、含有させるクエン酸量とナトリウム量を調節することで、梅干し感を再現したアルコール飲料が記載されている。特許文献2には、飲料の容器内に梅干しを丸ごと封入することで梅干し風味を付与した飲料が記載されている。   Plum-boiled flavored foods include umeboshi flesh (that is, plum meat), candy, syrup, etc. to which plum vinegar and plum juice are added. As a umeboshi-flavored beverage, Patent Document 1 describes an alcoholic beverage that reproduces the feeling of umeboshi by adjusting the amount of citric acid and sodium contained. Patent Document 2 describes a beverage that has been given a umeboshi flavor by enclosing a whole umeboshi in a beverage container.

特許文献1の飲料は、梅干しを使用していない。そのため、アルコール分を含まない飲料では自然な梅干し感が得られない問題がある。また、特許文献2の飲料には、梅干しの品質、寸法によって付与される梅干し風味がばらつくため、飲料に付与する梅干し風味を最適化することが困難であり、梅干し風味を一定に維持することも困難という問題がある。また、従来の梅干し由来の抽出液は濁るため、透明な飲料に添加した場合に飲料の外観が悪くなる問題がある。   The beverage of Patent Document 1 does not use umeboshi. For this reason, there is a problem that a natural plum dry feeling cannot be obtained with a beverage that does not contain alcohol. Moreover, in the drink of patent document 2, since the umeboshi flavor provided with the quality and size of an umeboshi varies, it is difficult to optimize the umeboshi flavor given to a drink, and it can also maintain a umeboshi flavor constant. There is a problem of difficulty. Moreover, since the extract extracted from the conventional umeboshi is cloudy, when added to a transparent beverage, there is a problem that the appearance of the beverage is deteriorated.

特開2014−158460号公報JP 2014-158460 A 特開2003−310159号公報JP 2003-310159 A

本発明は上記従来の問題を解決するものであり、その目的とするところは、透明性に優れた梅干し成分浸出液濃縮物を提供することである。   The present invention solves the above-mentioned conventional problems, and an object of the present invention is to provide a umeboshi component leachate concentrate excellent in transparency.

本発明は、果肉が粉砕されていない白干し梅から白干し梅の成分を浸出させた液を濃縮して得られる、梅干し成分浸出液濃縮物を提供する。   The present invention provides a umeboshi component leachate concentrate obtained by concentrating a liquid obtained by leaching a component of white dried ume from white dried ume that has not been pulverized.

ある一形態においては、前記白干し梅の成分を浸出させた液はBrix値が0.1〜18%である。   In one certain form, the liquid which leached the component of the said white dried plum has a Brix value of 0.1 to 18%.

ある一形態においては、前記白干し梅の成分を浸出させた液は、水を含む液に白干し梅を浸漬して得たものである。   In one certain form, the liquid which leached the component of the said white dried plum is obtained by immersing the white dried plum in the liquid containing water.

ある一形態においては、前記濃縮は減圧下30〜50℃の温度で行われる。   In one certain form, the said concentration is performed at the temperature of 30-50 degreeC under pressure reduction.

ある一形態においては、上記いずれかの梅干し成分浸出液濃縮物は、Brix値が20〜90%である。   In one certain form, the said umeboshi component leachate concentrate has a Brix value of 20 to 90%.

また、本発明は、果肉が粉砕されていない白干し梅から白干し梅の成分を液に浸出させる工程;及び
得られる液を濃縮する工程;
を包含する、梅干し成分浸出液濃縮物の製造方法を提供する。
Further, the present invention includes a step of leaching components of white dried plums from white dried plums in which the pulp has not been crushed; and a step of concentrating the resulting solution;
The manufacturing method of the umeboshi component leachate concentrate containing this is provided.

また、本発明は、果肉が粉砕されていない白干し梅から白干し梅の成分を浸出させた液を濃縮して得られる梅干しエキスを提供する。   Moreover, this invention provides the plum dried extract obtained by concentrating the liquid which leached the component of the white dried plum from the dried white plum which the pulp is not grind | pulverized.

また、本発明は、上記いずれかに記載の梅干し成分浸出液濃縮物又は上記梅干しエキスを含有する飲食品素材を提供する。   Moreover, this invention provides the food-drinks raw material containing the umeboshi component leachate concentrate in any one of the said, or the said umeboshi extract.

ある一形態においては、上記飲食品素材を添加する対象が飲料又は調味料である。   In one certain form, the object which adds the said food-drinks material is a drink or a seasoning.

また、本発明は、上記いずれかに記載の梅干し成分浸出液濃縮物又は上記梅干しエキスを含有する飲料又は調味料を提供する。   Moreover, this invention provides the drink or seasoning containing the umeboshi component leachate concentrate in any one of the said, or the said umeboshi extract.

本発明の梅干し成分浸出液濃縮物は透明性に優れ、透明な飲料に添加した場合にも飲料の外観が悪くなることがない。本発明の梅干し成分浸出液濃縮物は飲食品に含有させて、自然な梅干し風味を実現することができる。   The umeboshi component leachate concentrate of the present invention is excellent in transparency, and even when added to a transparent beverage, the appearance of the beverage does not deteriorate. The umeboshi component leachate concentrate of the present invention can be contained in food and drink to achieve a natural umeboshi flavor.

本発明の梅干し成分浸出液濃縮物は、梅干しの成分を浸出させた液を濃縮したものである。原料の梅干しとしては、白干し梅を使用することが好ましい。白干し梅とは、梅の果実を塩漬けにし、その後天日に干した状態の梅干しをいう。白干し梅は、塩分濃度が15〜25%である。   The umeboshi component leachate concentrate of the present invention is a concentrate obtained by leaching the umeboshi component. As the raw material plum dried, it is preferable to use white dried plum. White dried plums are plum dried in a state where the fruits of the plums are salted and then dried in the sun. White dried plums have a salt concentration of 15-25%.

白干し梅の製造方法の一例は次の通りである。
(1)熟した梅の果実を水洗いし、水気をとる。
(2)容器に梅と塩を入れ、重しを乗せ、1ヶ月程度放置する。塩の量は梅に対する重量比で15〜25%である。
(3)天気の良い日に3〜4日、天日干しにする。
An example of a method for producing white dried plums is as follows.
(1) Wash the ripe plum fruit with water.
(2) Put ume and salt in a container, put a weight, and leave it for about a month. The amount of salt is 15-25% by weight with respect to plum.
(3) Dry in the sun for 3-4 days when the weather is nice.

調味された梅干しを使用した場合、梅干しエキスを飲食品に含有させた際に自然な梅干し感が得られない可能性がある。即ち、調味された梅干し由来の梅干しエキスの場合は、糖類やアミノ酸類、ビタミンB1などの日持ち向上剤が使用されており、梅干し以外の風味が出てしまい、自然な梅干し感が得られない可能性がある。   When seasoned umeboshi is used, there is a possibility that a natural feeling of umeboshi cannot be obtained when the umeboshi extract is included in a food or drink. In other words, in the case of seasoned plum dried extract derived from dried plums, a shelf-life improver such as sugars, amino acids, vitamin B1, etc. is used, and flavors other than plum dried appear, and a natural feeling of dried plums may not be obtained. There is sex.

白干し梅の成分を浸出させる媒体は主成分として水を含む液である。白干し梅の成分を浸出させる媒体は水のみであってもよい。この媒体には雑菌の繁殖を防止するために、防腐剤を適量添加してよい。防腐剤の具体例としては、酢酸、オゾン水、さらし粉、次亜塩素酸ソーダ等が挙げられる。   The medium for leaching the components of white dried plums is a liquid containing water as a main component. The medium for leaching the components of white dried plums may be water alone. An appropriate amount of preservatives may be added to this medium in order to prevent the growth of various bacteria. Specific examples of the preservative include acetic acid, ozone water, bleached powder, sodium hypochlorite and the like.

媒体に含有させる防腐剤の濃度は0.01〜2重量%である。防腐剤の濃度が0.01%未満であると殺菌効果が不十分になり、2重量%を超えると風味に影響する。媒体に含有させる防腐剤の濃度は、好ましくは0.01〜1重量%、より好ましくは0.05〜0.3重量%である。例えば、防腐剤として酢酸を使用する場合は、濃度0.1〜0.3重量%になる量で使用することが好ましい。また、例えば、防腐剤としてさらし粉を使用する場合は、濃度0.05〜0.1重量%になる量で使用することが好ましい。防腐剤は2種類以上の材料を併用してもよい。   The concentration of the preservative contained in the medium is 0.01 to 2% by weight. If the concentration of the preservative is less than 0.01%, the bactericidal effect is insufficient, and if it exceeds 2% by weight, the flavor is affected. The concentration of the preservative contained in the medium is preferably 0.01 to 1% by weight, more preferably 0.05 to 0.3% by weight. For example, when acetic acid is used as a preservative, it is preferably used in an amount of 0.1 to 0.3% by weight. For example, when bleaching powder is used as a preservative, it is preferably used in an amount of 0.05 to 0.1% by weight. Two or more kinds of preservatives may be used in combination.

白干し梅の成分を浸出させた液は、上記媒体に白干し梅を所定の時間浸漬して得ることができる。媒体に白干し梅を浸漬する時間は、使用する媒体の種類又は温度に依存して適宜調節されるが、一般に10分〜150時間である。白干し梅の浸漬時間が10分未満では梅干し成分の浸出が不十分になり、150時間を超えて浸漬しても風味の向上が得られない。白干し梅の浸漬時間は、好ましくは1〜100時間、より好ましくは2〜66時間である。   The liquid in which the components of white dried plums are leached can be obtained by immersing the white dried plums in the medium for a predetermined time. The time for immersing the white dried plums in the medium is appropriately adjusted depending on the type or temperature of the medium to be used, but is generally 10 minutes to 150 hours. When the soaking time of white dried plum is less than 10 minutes, the leaching of the dried plum components becomes insufficient, and even if soaking for more than 150 hours, the flavor cannot be improved. The immersion time of white dried plums is preferably 1 to 100 hours, more preferably 2 to 66 hours.

白干し梅を媒体に浸漬して成分を浸出させる際に、白干し梅を粉砕した梅肉にしない。梅肉を粉砕すると梅に含まれている濁り成分が媒体に混入する。好ましい一形態では、白干し梅は分解せず、一部に皮が破れた梅干しの混入が有っても良いが、好ましくは完全な形態のまま媒体に浸漬する。   When brewing white dried plums in a medium and leaching the ingredients, do not make the dried plums pulverized. When the plum meat is crushed, turbid components contained in the plum are mixed into the medium. In a preferred form, the dried ume does not decompose and may contain some dried ume dried, but it is preferably immersed in the medium in its complete form.

白干し梅の成分を浸出させる際に、媒体は温度を調節してもよい。その場合、媒体の温度は5〜80℃に調節される。媒体の温度が5℃未満では梅干し成分の浸出が不十分になり、80℃を超えると梅干しに割れが生じる。白干し梅の成分を浸出させる際の媒体の温度は、好ましくは20〜70℃である。媒体に防腐剤を含有させない場合は、上記媒体の温度は50〜80℃、特に60〜80℃に調節することが好ましい。温度を高くすることで媒体の腐敗防止効果が得られる。   When leaching the components of white dried plums, the medium may adjust the temperature. In that case, the temperature of the medium is adjusted to 5-80 ° C. When the temperature of the medium is less than 5 ° C, the umeboshi component is not sufficiently leached, and when it exceeds 80 ° C, cracking occurs in the umeboshi. The temperature of the medium when leaching the components of white dried plums is preferably 20 to 70 ° C. When a preservative is not contained in the medium, the temperature of the medium is preferably adjusted to 50 to 80 ° C, particularly 60 to 80 ° C. By increasing the temperature, the medium can be prevented from being spoiled.

白干し梅の成分を浸出させた液は、必要に応じて不純物又は混入物を除去する。不純物又は混入物を除去する方法は、特に限定されないが、例えば、濾過法や遠心分離法等で行うことができる。これらの方法は操作が簡便であり、分離効率も高い。   The liquid in which the components of white dried plums are leached removes impurities or contaminants as necessary. A method for removing impurities or contaminants is not particularly limited, and can be performed by, for example, a filtration method or a centrifugal separation method. These methods are easy to operate and have high separation efficiency.

フィルタによる濾過法で分離を行う場合は、フィルタの孔径は0.001〜100μm、好ましくは0.1〜30μm、より好ましくは1〜10μmとする。フィルタの孔径が0.001μm未満であると濾過効率が悪くなり、濾過作業が煩雑となる。フィルタの孔径が100μmを超えると不純物又は混入物の分離が不完全になることがある。フィルタとしては、プレフィルタ、精密濾過膜、限外濾過膜、ナノフィルタ膜、逆浸透膜などを使用することができる。   When performing separation by a filtration method using a filter, the pore size of the filter is 0.001 to 100 μm, preferably 0.1 to 30 μm, and more preferably 1 to 10 μm. When the pore diameter of the filter is less than 0.001 μm, the filtration efficiency is deteriorated, and the filtration work becomes complicated. If the pore size of the filter exceeds 100 μm, the separation of impurities or contaminants may be incomplete. As the filter, a prefilter, a microfiltration membrane, an ultrafiltration membrane, a nanofilter membrane, a reverse osmosis membrane, or the like can be used.

遠心分離法で分離を行う場合は、必要に応じて、希釈した濃縮液の液を連続的にローターに導入し、非水溶性成分がローターの壁面に沈着し、非水溶性成分がなくなった上澄み液は溢れてローターの外に出るように配管した特殊な遠心分離器を用いることができる。遠心分離にかける荷重は、一般に1000〜5000G、好ましくは2000〜3000Gである。   When performing separation by centrifugation, if necessary, the diluted concentrated solution is continuously introduced into the rotor, so that the water-insoluble component is deposited on the rotor wall and the water-insoluble component is removed. A special centrifuge that is piped so that the liquid overflows out of the rotor can be used. The load applied to the centrifugation is generally 1000 to 5000 G, preferably 2000 to 3000 G.

白干し梅の成分を浸出させた液はBrix値が0.1〜18%である。白干し梅の成分を浸出させた液のBrix値が0.1%未満であると十分な風味が溶出しておらず、高濃度に濃縮する必要がある。18%を超えると梅干しの果皮が破れ清澄な液が得られない。白干し梅の成分を浸出させた液のBrix値は、好ましくは0.8〜15%であり、より好ましくは1.9〜12%である。   The liquid in which the components of white dried plums are leached has a Brix value of 0.1 to 18%. If the Brix value of the liquid in which the components of white dried plum are leached is less than 0.1%, sufficient flavor is not eluted and it is necessary to concentrate to a high concentration. If it exceeds 18%, the umeboshi peel is broken and a clear liquid cannot be obtained. The Brix value of the liquid in which the components of white dried plums are leached is preferably 0.8 to 15%, more preferably 1.9 to 12%.

白干し梅の成分を浸出させた液は酸度が0.05〜10%である。白干し梅の成分を浸出させた液の酸度が0.05%未満であると十分な風味が溶出しておらず、高濃度に濃縮する必要がある。10%を超えると20%を超えると梅干しの果皮が破れ清澄な液が得られない。白干し梅の成分を浸出させた液の酸度は、好ましくは0.1〜5%であり、より好ましくは0.2〜1.9%である。   The liquid which leached the component of white dried plum has an acidity of 0.05 to 10%. If the acidity of the liquid in which the components of white dried plums are leached is less than 0.05%, sufficient flavor is not eluted and it is necessary to concentrate to a high concentration. When it exceeds 10%, when it exceeds 20%, the skin of plum dried is torn and a clear liquid cannot be obtained. The acidity of the liquid in which the components of white dried plums are leached is preferably 0.1 to 5%, more preferably 0.2 to 1.9%.

白干し梅の成分を浸出させた液は塩度が0.1〜16%である。白干し梅の成分を浸出させた液の塩度が0.1%未満であると十分な風味が溶出しておらず、高濃度に濃縮する必要がある。16%を超えると梅干しの果皮が破れ清澄な液が得られない。白干し梅の成分を浸出させた液の塩度は、好ましくは0.8〜13%であり、より好ましくは1.3〜8.3%である。   The liquid in which the components of white dried plum are leached has a salinity of 0.1 to 16%. If the salinity of the liquid in which the components of white dried plums are leached is less than 0.1%, sufficient flavor is not eluted and it is necessary to concentrate to a high concentration. If it exceeds 16%, the umeboshi pericarp will break and a clear liquid cannot be obtained. The salinity of the liquid in which the components of white dried plums are leached is preferably 0.8 to 13%, more preferably 1.3 to 8.3%.

白干し梅の成分を浸出させた液は必要に応じて脱塩してよい。脱塩は、濃縮の途中で適宜行ってもよい。脱塩には、イオン交換膜電気透析処理法(特開2002−272432号公報)など、周知の手法を採用できる。また、特開2001−17116号公報、特開2002−186444号公報、特開2002−51752号公報に記載されている方法を用いてもよい。   You may desalinate the liquid which leached the component of white dried plum as needed. Desalting may be appropriately performed during the concentration. For the desalting, a well-known method such as an ion exchange membrane electrodialysis method (Japanese Patent Laid-Open No. 2002-272432) can be employed. Moreover, you may use the method described in Unexamined-Japanese-Patent No. 2001-17116, 2002-186444, 2002-51752.

白干し梅の成分を浸出させた液は、所定の水分量になるまで濃縮される。濃縮とは、白干し梅の成分を浸出させた液から上記媒体を蒸発させることをいう。濃縮は、効率の向上とコントロールの便利さを考えて低温・減圧の条件下で行うことが好ましい。濃縮の際の温度は、一般に15〜80℃に調節される。濃縮温度が15℃未満では工程に長時間を要するために効率が低下し、80℃を超えると濁りが発生する。濃縮温度は、好ましくは20〜70℃、より好ましくは30〜60℃である。工程を促進するために、減圧条件下で濃縮を行うほうが良い。その際には、圧力は11〜360Torr、好ましくは17〜230Torr、より好ましくは23〜190Torr程度に減圧される。   The liquid in which the components of white dried plum are leached is concentrated until a predetermined amount of water is obtained. Concentration means that the medium is evaporated from a liquid in which a component of white dried plum is leached. Concentration is preferably performed under conditions of low temperature and reduced pressure in consideration of improvement in efficiency and convenience of control. The temperature during the concentration is generally adjusted to 15 to 80 ° C. If the concentration temperature is less than 15 ° C., the process takes a long time, and thus the efficiency is reduced. The concentration temperature is preferably 20 to 70 ° C, more preferably 30 to 60 ° C. In order to accelerate the process, it is better to perform concentration under reduced pressure conditions. At that time, the pressure is reduced to about 11 to 360 Torr, preferably 17 to 230 Torr, more preferably about 23 to 190 Torr.

濃縮を完全に行うことで白干し梅の成分を浸出させた液から上記媒体を完全に蒸発させたものは、梅干しエキスである。しかしながら、本発明においては濃縮を完全に行う必要は無い。濃縮の程度は、濃縮物を使用する際の有用性及び利便性を考慮して調節してよい。例えば、食塩が析出しない程度の濃度まで濃縮することで、濃縮物は梅干し本来の酸味と塩味のバランスが維持されたものになる。   Plum dried extract is obtained by completely evaporating the medium from a solution obtained by leaching the components of white dried plum by concentrating completely. However, in the present invention, it is not necessary to perform concentration completely. The degree of concentration may be adjusted in view of the usefulness and convenience when using the concentrate. For example, by concentrating to a concentration that does not cause the salt to precipitate, the concentrate becomes one that maintains the balance between the original sourness and salty taste of umeboshi.

梅干し成分浸出液濃縮物はBrix値が20〜90%である。梅干し成分浸出液濃縮物のBrix値が20%未満であると常温で腐敗の危険性が高まり、輸送コストも増大する。90%を超えると粘性が高くなり作業性が低下する。梅干し成分浸出液濃縮物のBrix値は、好ましくは25〜60%であり、より好ましくは30〜36%である。   The umeboshi component leachate concentrate has a Brix value of 20-90%. If the Brix value of the umeboshi component leachate concentrate is less than 20%, the risk of rot increases at room temperature, and the transportation cost also increases. If it exceeds 90%, the viscosity becomes high and workability decreases. The Brix value of the umeboshi component leachate concentrate is preferably 25 to 60%, more preferably 30 to 36%.

梅干し成分浸出液濃縮物は酸度が1〜50%である。梅干し成分浸出液濃縮物の酸度が1%未満であると常温で腐敗の危険性が高まり、輸送コストも増大する。50%を超えると粘性が高くなり作業性が低下する。梅干し成分浸出液濃縮物の酸度は、好ましくは2〜20%であり、より好ましくは2.9〜7.5%である。   Plum dried component leachate concentrate has an acidity of 1-50%. If the acidity of the umeboshi component leachate concentrate is less than 1%, the risk of spoilage increases at room temperature and the transportation cost also increases. If it exceeds 50%, the viscosity becomes high and workability decreases. The acidity of the umeboshi component leachate concentrate is preferably 2 to 20%, more preferably 2.9 to 7.5%.

梅干し成分浸出液濃縮物は塩度が26%以下である。梅干しエキスはイオン交換膜電気透析法や晶析法などの処理により脱塩することが可能であり、26%を超えると過飽和となり析出する。梅干し成分浸出液濃縮物の塩度は、好ましくは22〜26%、より好ましくは22〜24%である。   The umeboshi component leachate concentrate has a salinity of 26% or less. Umeboshi extract can be desalted by treatment such as ion exchange membrane electrodialysis or crystallization, and when it exceeds 26%, it becomes supersaturated and precipitates. The salinity of the umeboshi component leachate concentrate is preferably 22-26%, more preferably 22-24%.

得られた梅干し成分浸出液濃縮物は乾燥して粉末化してもよい。粉末化した濃縮物は梅干しエキスの一形態である。   The obtained umeboshi component leachate concentrate may be dried to be powdered. The powdered concentrate is a form of umeboshi extract.

本発明の梅干し成分浸出液濃縮物又は梅干しエキスは飲食品素材として使用することができる。飲食品素材とは飲食品の成分として使用する材料をいう。本発明の梅干し成分浸出液濃縮物又は梅干しエキスが飲食品素材として使用される飲食品は、自然な梅干し風味を付与することで嗜好性が向上し、又は梅干しの成分を含有させることで機能が向上する飲食品である。そのような飲食品の例は、飲料、調味料、液体調味料、菓子、パン及び健康食品等が挙げられるが、これらに限定されない。   The umeboshi component leachate concentrate or the umeboshi extract of the present invention can be used as a food or drink material. A food / beverage material refers to a material used as a component of a food / beverage product. The food and drink in which the umeboshi component leachate concentrate or the umeboshi extract of the present invention is used as a material for food and drink is improved in palatability by adding a natural umeboshi flavor, or improved in function by containing a component of umeboshi It is a food and drink. Examples of such food and drink include, but are not limited to, beverages, seasonings, liquid seasonings, confectionery, bread and health foods.

本発明の梅干し成分浸出液濃縮物は薄い琥珀色で透明及び清澄な液体である。そのため、この梅干し成分浸出液濃縮物を飲食品素材として使用しても製品の外観に影響を与えない。この梅干し成分浸出液濃縮物は、透明であるため着色力が弱く、飲食品用着色剤を加えて製品の色を調節することが容易である。   The umeboshi component leachate concentrate of the present invention is a light amber, transparent and clear liquid. Therefore, even if this umeboshi component leachate concentrate is used as a food or drink material, the appearance of the product is not affected. Since this umeboshi component leachate concentrate is transparent, its coloring power is weak, and it is easy to add a colorant for food and drink to adjust the color of the product.

以下の実施例により本発明を更に具体的に説明するが、本発明はこれらに限定されない。   The following examples further illustrate the present invention, but the present invention is not limited thereto.

実施例1 N1
水槽に濃度0.3%の酢酸水溶液1600リットルを入れ、温度を20℃に調節した。ここに、塩分25%の白干し梅700kgを、果実を分解しないでそのまま浸漬し、水温を20℃に維持し、3時間放置した。水槽から白干し梅を除去した。孔径10μmのバグフィルターを使用して得られた浸出液を濾過した。濾液はBrix値2.84%、酸度0.60%、塩度2.07%を有していた。
Example 1 N1
1600 liters of acetic acid aqueous solution having a concentration of 0.3% was placed in a water tank, and the temperature was adjusted to 20 ° C. Here, 700 kg of white dried plums with a salt content of 25% were immersed as they were without decomposing the fruits, and the water temperature was maintained at 20 ° C. and left for 3 hours. White dried plums were removed from the aquarium. The leachate obtained using a bag filter with a pore size of 10 μm was filtered. The filtrate had a Brix value of 2.84%, acidity of 0.60% and salinity of 2.07%.

孔径10μのバグフィルターを使用して濾液を濾過し、濾液2.72kgをエバポレーターに仕込み、バス温度を60℃に設定し、圧力を30Torrに調節して、減圧濃縮した。   The filtrate was filtered using a bag filter having a pore size of 10 μm, and 2.72 kg of the filtrate was charged into an evaporator, the bath temperature was set to 60 ° C., the pressure was adjusted to 30 Torr, and the solution was concentrated under reduced pressure.

得られた濃縮液は200gであり、Brix値32.27%、酸度3.14%、塩度25.61%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The concentrated solution obtained was 200 g, and had a Brix value of 32.27%, an acidity of 3.14%, and a salinity of 25.61%. Further, this concentrated solution was almost colorless and transparent.

実施例2 N2
水槽に水1600リットルを入れ、温度を70℃に調節した。ここに、塩分25%の白干し梅700kgを、果実を分解しないでそのまま浸漬し、水温を60から70℃に維持し、3時間放置した。水槽から白干し梅を除去した。同じ浸出水を用いこれを3回繰り返し、浸出液を得た。孔径10μmのバグフィルターを使用して得られた浸出液を濾過した。濾液はBrix値4.61%、酸度0.48%、塩度3.42%を有していた。
Example 2 N2
1600 liters of water was placed in the water tank and the temperature was adjusted to 70 ° C. Here, 700 kg of white dried plums with a salt content of 25% were immersed as they were without decomposing the fruits, and the water temperature was maintained at 60 to 70 ° C. and left for 3 hours. White dried plums were removed from the aquarium. This was repeated 3 times using the same leachate to obtain a leachate. The leachate obtained using a bag filter with a pore size of 10 μm was filtered. The filtrate had a Brix value of 4.61%, acidity of 0.48% and salinity of 3.42%.

孔径10μのバグフィルターを使用して濾液を濾過し、濾液2.69kgをエバポレーターに仕込み、バス温度を60℃に設定し、圧力を30Torrに調節して、減圧濃縮した。   The filtrate was filtered using a bag filter having a pore size of 10 μm, 2.69 kg of the filtrate was charged into an evaporator, the bath temperature was set to 60 ° C., the pressure was adjusted to 30 Torr, and the solution was concentrated under reduced pressure.

得られた濃縮液は297gであり、Brix値33.35%、酸度3.91%、塩度24.75%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The concentrated liquid obtained was 297 g, and had a Brix value of 33.35%, an acidity of 3.91%, and a salinity of 24.75%. Further, this concentrated solution was almost colorless and transparent.

実施例3 N4
水槽に水1600リットルを入れ、温度を70℃に調節した。ここに、塩分25%の白干し梅700kgを、果実を分解しないでそのまま浸漬し、水温を60から70℃に維持し、3時間放置した。水槽から白干し梅を除去した。孔径10μmのバグフィルターを使用して得られた浸出液を濾過した。濾液はBrix値2.34%、酸度0.26%、塩度1.64%を有していた。
Example 3 N4
1600 liters of water was placed in the water tank and the temperature was adjusted to 70 ° C. Here, 700 kg of white dried plums with a salt content of 25% were immersed as they were without decomposing the fruits, and the water temperature was maintained at 60 to 70 ° C. and left for 3 hours. White dried plums were removed from the aquarium. The leachate obtained using a bag filter with a pore size of 10 μm was filtered. The filtrate had a Brix value of 2.34%, acidity of 0.26% and salinity of 1.64%.

濾液15.82kgをエバポレーターに仕込み、バス温度を80℃に設定し、圧力を−0.09Mpaに調節して、減圧濃縮した。   15.82 kg of the filtrate was charged into an evaporator, the bath temperature was set to 80 ° C., the pressure was adjusted to −0.09 MPa, and the solution was concentrated under reduced pressure.

得られた濃縮液は1.01kgであり、Brix値30.15%、酸度3.68%、塩度22.83%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The obtained concentrated liquid was 1.01 kg, and had a Brix value of 30.15%, an acidity of 3.68%, and a salinity of 22.83%. Further, this concentrated solution was almost colorless and transparent.

実施例4 N3
水槽に濃度0.2%の酢酸水溶液1600リットルを入れ、温度を常温に調節した。ここに、塩分25%の白干し梅700kgを、果実を分解しないでそのまま浸漬し、水温を常温に維持し、2時間放置した。水槽から白干し梅を除去した。孔径10μmのバグフィルター使用して得られた浸出液を濾過した。濾液はBrix値1.97%、酸度0.50%、塩度1.34%を有していた。
Example 4 N3
A 1600 liter acetic acid aqueous solution having a concentration of 0.2% was placed in a water tank, and the temperature was adjusted to room temperature. Here, 700 kg of white dried plums with a salt content of 25% were immersed as they were without decomposing the fruits, the water temperature was maintained at room temperature, and the mixture was left for 2 hours. White dried plums were removed from the aquarium. The leachate obtained using a bag filter with a pore size of 10 μm was filtered. The filtrate had a Brix value of 1.97%, acidity of 0.50% and salinity of 1.34%.

濾液17.12kgをエバポレーターに仕込み、バス温度を80℃に設定し、圧力を−0.09Mpaに調節して、減圧濃縮した。   17.12 kg of the filtrate was charged into an evaporator, the bath temperature was set to 80 ° C., the pressure was adjusted to −0.09 MPa, and the solution was concentrated under reduced pressure.

得られた濃縮液は0.83kgであり、Brix値31.84%、酸度2.99%、塩度25.49%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The obtained concentrate was 0.83 kg and had a Brix value of 31.84%, an acidity of 2.99%, and a salinity of 25.49%. Further, this concentrated solution was almost colorless and transparent.

実施例5 S1
水槽に濃度0.1%の酢酸水溶液1000リットルを入れ、温度を20℃に調節した。ここに、塩分25%の白干し梅600kgを、果実を分解しないでそのまま浸漬し、水温を20℃に維持し、16時間放置した。水槽から白干し梅を除去した。孔径10μmのバグフィルターを使用して得られた浸出液を濾過した。濾液はBrix値11.83%、酸度1.74%、塩度8.27%を有していた。
Example 5 S1
1000 liters of an acetic acid aqueous solution having a concentration of 0.1% was placed in a water tank and the temperature was adjusted to 20 ° C. Here, 600 kg of white dried plums having a salt content of 25% were immersed as they were without decomposing fruits, and the water temperature was maintained at 20 ° C., and left for 16 hours. White dried plums were removed from the aquarium. The leachate obtained using a bag filter with a pore size of 10 μm was filtered. The filtrate had a Brix value of 11.83%, an acidity of 1.74% and a salinity of 8.27%.

濾液5.03kgをエバポレーターに仕込み、バス温度を80℃に設定し、圧力を−0.09Mpaに調節して、減圧濃縮した。   5.03 kg of the filtrate was charged into an evaporator, the bath temperature was set to 80 ° C., the pressure was adjusted to −0.09 MPa, and the mixture was concentrated under reduced pressure.

得られた濃縮液は1.54kgであり、Brix値34.59%、酸度4.99%、塩度25.14%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The obtained concentrated liquid was 1.54 kg and had a Brix value of 34.59%, an acidity of 4.99%, and a salinity of 25.14%. Further, this concentrated solution was almost colorless and transparent.

実施例6 T1
水槽に濃度0.1%の酢酸及び濃度0.08%のさらし粉を含有する水溶液1600リットルを入れ、温度を20℃に調節した。ここに、塩分25%の白干し梅700kgを、果実を分解しないでそのまま浸漬し、水温を20℃に維持し、66時間放置した。水槽から白干し梅を除去した。孔径10μmバグフィルターを使用して得られた浸出液を濾過した。濾液はBrix値8.54%、酸度1.09%、塩度5.93%を有していた。
Example 6 T1
1600 liters of an aqueous solution containing acetic acid having a concentration of 0.1% and bleaching powder having a concentration of 0.08% was placed in a water tank, and the temperature was adjusted to 20 ° C. Here, 700 kg of white dried ume with a salt content of 25% was immersed as it was without decomposing the fruit, and the water temperature was maintained at 20 ° C. and left for 66 hours. White dried plums were removed from the aquarium. The leachate obtained using a 10 μm pore size bag filter was filtered. The filtrate had a Brix value of 8.54%, an acidity of 1.09% and a salinity of 5.93%.

濾液500gをエバポレーターに仕込み、バス温度を80℃に設定し、圧力を30Torrに調節して、減圧濃縮した。   500 g of the filtrate was charged into an evaporator, the bath temperature was set to 80 ° C., the pressure was adjusted to 30 Torr, and the solution was concentrated under reduced pressure.

得られた濃縮液は97.6gであり、Brix値33.69%、酸度4.46%、塩度24.53%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The obtained concentrated liquid was 97.6 g, and had a Brix value of 33.69%, an acidity of 4.46%, and a salinity of 24.53%. Further, this concentrated solution was almost colorless and transparent.

実施例7 T2
水槽に水1600リットルを入れ、温度を20℃に調節した。ここに、塩分25%の白干し梅700kgを、果実を分解しないでそのまま浸漬し、水温を20℃に維持し、4時間放置した。水槽から白干し梅を除去した。孔径10μmのバグフィルターを使用して得られた浸出液を濾過した。濾液はBrix値3.27%、酸度0.50%、塩度2.09%を有していた。
Example 7 T2
1600 liters of water was placed in the water tank and the temperature was adjusted to 20 ° C. Here, 700 kg of white dried plums with a salt content of 25% were immersed as they were without decomposing the fruits, and the water temperature was kept at 20 ° C., and left for 4 hours. White dried plums were removed from the aquarium. The leachate obtained using a bag filter with a pore size of 10 μm was filtered. The filtrate had a Brix value of 3.27%, acidity of 0.50% and salinity of 2.09%.

濾液500gをエバポレーターに仕込み、バス温度を80℃に設定し、圧力を30Torrに調節して、減圧濃縮した。   500 g of the filtrate was charged into an evaporator, the bath temperature was set to 80 ° C., the pressure was adjusted to 30 Torr, and the solution was concentrated under reduced pressure.

得られた濃縮液は17.2gであり、Brix値34.79、酸度7.1%、塩度22.80%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The obtained concentrated liquid was 17.2 g, and had a Brix value of 34.79, an acidity of 7.1%, and a salinity of 22.80%. Further, this concentrated solution was almost colorless and transparent.

実施例8 T3
水槽に濃度0.1%の酢酸及び濃度0.08%のさらし粉を含有する水溶液1600リットルを入れ、温度を20℃に調節した。ここに、塩分25%の白干し梅700kgを、果実を分解しないでそのまま浸漬し、水温を20℃に維持し、16時間放置した。水槽から白干し梅を除去した。孔径10μmバグフィルターを使用して得られた浸出液を濾過した。濾液はBrix値10.96%、酸度1.81%、塩度7.30%を有していた。
Example 8 T3
1600 liters of an aqueous solution containing acetic acid having a concentration of 0.1% and bleaching powder having a concentration of 0.08% was placed in a water tank, and the temperature was adjusted to 20 ° C. Here, 700 kg of white dried plums with a salt content of 25% were immersed as they were without decomposing the fruits, the water temperature was maintained at 20 ° C., and left for 16 hours. White dried plums were removed from the aquarium. The leachate obtained using a 10 μm pore size bag filter was filtered. The filtrate had a Brix value of 10.96%, an acidity of 1.81%, and a salinity of 7.30%.

濾液500gをエバポレーターに仕込み、バス温度を80℃に設定し、圧力を30Torrに調節して、減圧濃縮した。   500 g of the filtrate was charged into an evaporator, the bath temperature was set to 80 ° C., the pressure was adjusted to 30 Torr, and the solution was concentrated under reduced pressure.

得られた濃縮液は112.2gであり、Brix値35.55、酸度6.75%、塩度23.85%を有していた。また、この濃縮液はほぼ無色であり、透明であった。   The obtained concentrated liquid was 112.2 g, and had a Brix value of 35.55, an acidity of 6.75%, and a salinity of 23.85%. Further, this concentrated solution was almost colorless and transparent.

実施例9 S1(飲料試作)
実施例5で得られた濃縮液(濃縮液S1)を用いて、梅干し風味飲料を製造した。イオン交換水に果糖ぶどう糖液糖を4.50%、グラニュー糖を6.00%、クエン酸を1.20%、5倍濃縮梅果汁を0.3%の濃度になる量で添加し、梅飲料のベースを調製した。梅飲料のベースの外観は薄い鮮やかな琥珀色であった。この梅飲料のベースに、濃縮液S1を0.2%の濃度になる量で添加して、梅干し風味の飲料を得た。
Example 9 S1 (Beverage Trial)
Using the concentrated solution (concentrated solution S1) obtained in Example 5, a plum dried flavored beverage was produced. In ion-exchanged water, add fructose-glucose liquid sugar at a concentration of 4.50%, granulated sugar at 6.00%, citric acid at 1.20%, and 5-fold concentrated plum juice at a concentration of 0.3%. A beverage base was prepared. The appearance of the base of the plum drink was a thin and bright amber color. The concentrated liquid S1 was added to the base of this plum drink in an amount that would give a concentration of 0.2% to obtain a plum dried drink.

梅干し風味飲料の外観は梅飲料のベースと同様であり、着色や濁りの発生は認められなかった。つまり、濃縮液S1を使用することにより、梅飲料のベースの外観を損なうことなく、自然な梅干しの風味を実現することができた。   The appearance of the umeboshi flavored drink was the same as the base of the ume drink, and no coloring or turbidity was observed. That is, by using the concentrate S1, a natural umeboshi flavor could be realized without deteriorating the appearance of the base of the plum drink.

実施例10 N4(飲料試作)
濃縮液S1の代わりに実施例3で得られた濃縮液(濃縮液N4)を使用すること以外は実施例9と同様にして梅干し風味飲料を製造した。
Example 10 N4 (Beverage Trial)
A umeboshi-flavored beverage was produced in the same manner as in Example 9 except that the concentrate (concentrate N4) obtained in Example 3 was used instead of the concentrate S1.

梅干し風味飲料の外観は梅飲料のベースと同様であり、着色や濁りの発生は認められなかった。つまり、濃縮液N4を使用することにより、梅飲料のベースの外観を損なうことなく、自然な梅干しの風味を実現することができた。   The appearance of the umeboshi flavored drink was the same as the base of the ume drink, and no coloring or turbidity was observed. That is, by using the concentrated liquid N4, a natural umeboshi flavor could be realized without impairing the appearance of the base of the plum drink.

Claims (14)

果肉が粉砕されていない白干し梅から白干し梅の成分を、水を含み、糖類、アミノ酸類及びビタミンB1を含まない媒体に浸出させた液、を濃縮して得られる、梅干し成分浸出液濃縮物であって、
該白干し梅は塩分濃度が15〜25%であり、
該媒体の温度が常温であり、
白干し梅の成分を浸出させる時間が2〜66時間である、梅干し成分浸出液濃縮物
Plum-dried component leachate concentrate obtained by concentrating a solution of white-dried plum from white-dried plum that has not been pulverized into a medium containing water and not containing sugars, amino acids, and vitamin B1. Because
The white dried plum has a salt concentration of 15-25%,
The temperature of the medium is room temperature;
Plum-dried component leachate concentrate, in which the time for leaching the components of white-dried plum is 2 to 66 hours .
前記媒体は実質的に水のみである請求項1に記載の梅干し成分浸出液濃縮物。   The umeboshi component leachate concentrate according to claim 1, wherein the medium is substantially only water. 前記白干し梅の成分を浸出させた液はBrix値が0.1〜18%である請求項1又は2に記載の梅干し成分浸出液濃縮物。   3. The umeboshi component leachate concentrate according to claim 1 or 2, wherein the liquid obtained by leaching the component of white dried ume has a Brix value of 0.1 to 18%. 前記濃縮は減圧下30〜80℃の温度で行われる請求項1〜3のいずれか一項に記載の梅干し成分浸出液濃縮物。   The umeboshi component leachate concentrate according to any one of claims 1 to 3, wherein the concentration is performed at a temperature of 30 to 80 ° C under reduced pressure. Brix値が10〜90%である請求項1〜4のいずれか一項に記載の梅干し成分浸出液濃縮物。   Brix value is 10 to 90%, The umeboshi component leachate concentrate as described in any one of Claims 1-4. 果肉が粉砕されていない白干し梅から白干し梅の成分を、水を含み、糖類、アミノ酸類及びビタミンB1を含まない媒体に浸出させる工程;及び
得られる液を濃縮する工程;
を包含する、梅干し成分浸出液濃縮物の製造方法であって、
該白干し梅は塩分濃度が15〜25%であり、
該媒体の温度が常温であり、
白干し梅の成分を浸出させる時間が2〜66時間である、梅干し成分浸出液濃縮物の製造方法
A step of leaching components of white dried plums from white dried plums not pulverized in a medium containing water and not containing sugars, amino acids and vitamin B1, and a step of concentrating the resulting liquid;
A method for producing an umeboshi component leachate concentrate , comprising:
The white dried plum has a salt concentration of 15-25%,
The temperature of the medium is room temperature;
The manufacturing method of the umeboshi component leachate concentrate which is the leaching time of the component of white dried ume for 2 to 66 hours .
前記媒体は実質的に水のみである請求項6に記載の梅干し成分浸出液濃縮物の製造方法。   The method for producing a umeboshi component leachate concentrate according to claim 6, wherein the medium is substantially only water. 果肉が粉砕されていない白干し梅から白干し梅の成分を、水を含み、糖類、アミノ酸類及びビタミンB1を含まない媒体に浸出させた液、を濃縮して得られる梅干しエキスであって、
該白干し梅は塩分濃度が15〜25%であり、
該媒体の温度が常温であり、
白干し梅の成分を浸出させる時間が2〜66時間である、梅干しエキス
A plum dried extract obtained by concentrating a liquid obtained by leaching a component of white dried plum from white dried plum not pulverized into a medium containing water and not containing sugars, amino acids and vitamin B1 ,
The white dried plum has a salt concentration of 15-25%,
The temperature of the medium is room temperature;
An umeboshi extract in which the time for leaching the components of white dried ume is 2 to 66 hours .
前記媒体は実質的に水のみである請求項8に記載の梅干しエキス。   The umeboshi extract according to claim 8, wherein the medium is substantially water only. 請求項1に記載の梅干し成分浸出液濃縮物又は請求項8に記載の梅干しエキスを含有する飲食品素材。   The food-drinks material containing the umeboshi component leachate concentrate of Claim 1, or the umeboshi extract of Claim 8. 添加する対象が飲料又は調味料である請求項10に記載の飲食品素材。   The food / beverage material according to claim 10, wherein a target to be added is a beverage or a seasoning. 添加する対象がアルコール分を含まない飲料である請求項10に記載の飲食品素材。   The food / beverage material of Claim 10 whose object to add is a drink which does not contain alcohol. 請求項1に記載の梅干し成分浸出液濃縮物又は請求項8に記載の梅干しエキスを含有する飲料又は調味料。   The drink or seasoning containing the umeboshi component leachate concentrate of Claim 1, or the umeboshi extract of Claim 8. 請求項1に記載の梅干し成分浸出液濃縮物又は請求項8に記載の梅干しエキスを含有するアルコール分を含まない飲料。   The drink which does not contain the alcohol component containing the umeboshi component leachate concentrate of Claim 1, or the umeboshi extract of Claim 8.
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