JP2004222633A - Method for producing transparent extract of japanese plum - Google Patents

Method for producing transparent extract of japanese plum Download PDF

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Publication number
JP2004222633A
JP2004222633A JP2003016149A JP2003016149A JP2004222633A JP 2004222633 A JP2004222633 A JP 2004222633A JP 2003016149 A JP2003016149 A JP 2003016149A JP 2003016149 A JP2003016149 A JP 2003016149A JP 2004222633 A JP2004222633 A JP 2004222633A
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JP
Japan
Prior art keywords
extract
plum
plum extract
water
transparent
Prior art date
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JP2003016149A
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Japanese (ja)
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JP3801992B2 (en
Inventor
Nobuhiro Kanayama
伸広 金山
Hisashi Mitsuhara
久志 三津原
Hirosuke Kanayama
裕亮 金山
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SAN AKUTEISU KK
Sunactis Co Ltd
Original Assignee
SAN AKUTEISU KK
Sunactis Co Ltd
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Priority to JP2003016149A priority Critical patent/JP3801992B2/en
Publication of JP2004222633A publication Critical patent/JP2004222633A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an extract of Japanese plum excellent in transparency and clarity, hardly causing worsening of appearance of products because of transparency when the extract is used as a food raw material for seasonings or food additives and capable of controlling color by a coloring agent. <P>SOLUTION: The subject method for producing the extract of Japanese plum comprises a step for diluting Japanese plum extract with water, a step for separating a water-insoluble ingredient from the diluted Japanese plum extract and a step for concentrating the residual water solution. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は透明性及び清澄性に優れた梅エキスの製造方法に関する。
【0002】
【従来の技術】
梅には人体の健康増進に役立つ成分が豊富に含まれている。そのため、梅は様々な形態に加工されて食用に供されてきた。梅を加工した食品の一つに梅エキスがある。梅エキスは梅の有効成分を濃縮したものであり、従来から効用が特に高い食品、すなわち、いわゆる健康食品として珍重されている。
【0003】
しかしながら、梅エキスは梅の風味及び種々の優れた効用を有しながら、これまで調味料や食品添加物としては、それほど普及していない。
【0004】
その理由の一つは梅エキスの外観にある。梅エキスは黒色の粘性液体であり、梅から通常想像される桃色乃至赤色とはかけ離れた色をしている。しかも、黒色では着色剤を加えて色を調節することも困難である。
【0005】
従って、梅風味の加工食品や嗜好品に対する需要はあっても、梅エキスを原料に用いると製品の外観が汚れたように黒ずみ、製品に対する消費者の印象が極端に悪くなる。そのため、梅エキスを含む製品を大量生産することには抵抗があり、梅エキスの食品原料としての用途は限定されたものであった。
【0006】
【発明が解決しようとする課題】
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、透明性及び清澄性に優れ、着色の程度が緩和されているために調味料や食品添加物等の食品原料として使用しても製品の外観があまり悪化せず、しかも着色剤によって色を調節することも可能な梅エキスを提供することにある。
【0007】
【課題を解決するための手段】
本発明は、梅エキスを水で希釈する工程;
希釈した梅エキスから非水溶性成分を分離する工程;及び
残された水溶液を濃縮する工程;
を包含する、透明梅エキスの製造方法。
を提供するものであり、そのことにより上記目的が達成される。
【0008】
【発明の実施の形態】
本発明の方法においては、原料として梅エキスを使用する。梅エキスとは梅に含まれている液状の成分を加熱濃縮して得られる液体をいう。例えば、梅果汁を煮つめることによって得られる、「梅肉エキス」とよばれるものはここでいう梅エキスに含まれる。また、例えば、特開2001−17116号公報に記載の方法で製造された梅エキスもここでいう梅エキスに含まれる。
【0009】
梅エキスは通常粘性が高く、そのままでは加工を行い難いため、まず、適当な粘度までこれを希釈する。ただし粘度は測定が面倒なため、通常はブリックスでコントロールする。梅エキスは希釈によりブリックス3〜70%、好ましくは5〜50%、より好ましくは10〜40%に調節される。希釈されたブリックスが3より低いとろ過、あるいは脱色後の濃縮に工数がかかり、70%より高いと分離工程を行うことが困難になる。
【0010】
希釈は、梅エキスに清潔な水を加えて十分に撹拌することにより行うことができる。希釈水として、例えば、蒸留水やイオン交換水を用いることが好ましい。
【0011】
加える水の量は希釈した梅エキスに要求されるブリックスに応じて適宜増減することができる。一般には、水の量は梅エキスの量10重量部に対して1.4〜257重量部、好ましくは6〜150重量部、より好ましくは10〜70重量部の範囲で調整される。希釈した梅エキスは黒く濁っており、非水溶性成分が浮遊あるいは沈殿している。
【0012】
次いで、この水溶液から非水溶性成分を分離する。分離の方法は特に限定されないが、例えば、ろ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、分離効率も高いからである。
【0013】
ろ過法で分離を行う場合は、フィルタの孔径は0.001〜0.5μm、好ましくは0.003〜0.25μm、より好ましくは0.005〜0.1μmとする。フィルタの孔径が0.001μm未満であるとろ過効率が悪くなり、ろ過作業が煩雑となる。フィルタの孔径が0.5μmを超えると非水溶性成分の分離が不完全になり、得られる梅エキスの外観が不良となる。
【0014】
フィルタとして使えるものは、プレフィルタ、精密ろ過膜、限外ろ過膜、ナノフィルタ膜、逆浸透膜などが一般的であるが、本発明で用いて効果のある膜は、精密ろ過膜、限外ろ過及びナノフィルタ膜である。プレフィルタでは非水溶性成分の分離が不完全になり、逆浸透膜では溶解成分がろ過によって除かれてしまう欠点がある。
【0015】
ろ過の操作は、例えば原液タンク、循環ポンプ、ろ過モジュール、ろ液タンクを準備し、原液タンクと循環ポンプとろ過モジュールの間を配管で循環できるようにする。ろ過モジュールからのろ液は独立した配管でろ液タンクに導入する。原液タンクに希釈した梅エキスの液を入れ、ろ過モジュールの取扱説明書に記載された運転条件に合った圧力、循環量でろ過する。
【0016】
遠心分離法で分離を行う場合は、希釈した梅エキス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。バケット型の遠心分離器でも上澄み液を人為的に取り出す手間がかかるだけで本発明の効果のうえでなんら差し支えない。遠心分離にかける荷重は1000〜5000G、好ましくは2000〜3000Gが適当で、これ以上の荷重をかけても遠心分離の効果及び処理時間に大きな影響はない。
【0017】
このようにして梅エキスの水溶液から非水溶性成分を分離すると梅エキスを含む水溶液が残される。この水溶液は透明になっている。次いで、この残された水溶液を濃縮する。濃縮は粘度調節のために梅エキスに加えた水を除去するために行う。
【0018】
濃縮の方法は特に限定されないが、非加熱又は比較的低温に加熱して水を蒸発させることにより行うことが好ましい。高温に加熱すると非水溶性成分が生成する。そうなると得られる梅エキスの外観が黒く不透明化するからである。
【0019】
濃縮の際の温度は、一般に15〜80℃、好ましくは20〜70℃、より好ましくは25〜65℃に調節される。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。
【0020】
得られた梅エキスは透明及び清澄な液体であり、黒く不透明な従来の梅エキスと比べて着色の程度が著しく緩和されている。そのため、この梅エキスを調味料や食品添加物として使用しても製品の外観にそれほど影響を与えない。しかも、この梅エキスは、透明であるため着色力が弱く、食品用着色剤を加えて製品の色を調節することができる。例えば、食品添加物としてしそ色素を併用すれば、製品を梅らしい色調に仕上げることができる。
【0021】
本発明の方法で得た透明梅エキスの用途の例としては、製品外観に透明性が要求される清涼飲料、キャンデー、及び製品外観に淡色性が要求されるヨーグルト等が挙げられる。
【0022】
更に、この透明梅エキスは、官能検査の結果、従来の梅エキスよりも舌触りが滑らかで苦味や雑味が低減されており、そのまま摂取するための食品としても梅エキスよりも優れている。
【0023】
本発明の方法においては、梅エキスの水溶液から非水溶性成分を分離した後、濃縮工程の前に、梅エキスを含む水溶液を更に脱色してもよい。そうすればより着色が少ない、つまり無色透明に近い梅エキスを得ることができる。
【0024】
脱色工程は、例えば、梅エキスを含む水溶液を、吸着剤が充填されたカラムを通すかまたは、梅エキスを含む水溶液に吸着剤を投入し、一定時間攪拌した後静置し、デカンテーションで上澄みを取るか、あるいは、ろ過をして吸着剤を除くかして脱色液を得ることができる。その場合、吸着剤としては活性炭や吸着樹脂等を用いることができる。活性炭はその形状から粉状、粒状、布状などいろいろな種類があるが、処理のしやすさなどから、粒状の活性炭が好ましい。また、活性炭にする前の材質からもいろいろな種類があるが、これは特にこだわらない。吸着樹脂としては味の素ファインテクノ株式会社製の製品の中に両性型3種、弱塩基性型1種の4種あるが、これらのうちでも好ましい吸着樹脂としては両性型の樹脂である。
【0025】
脱色工程の後、上述の方法によって濃縮を行い、透明及び清澄な梅エキスを得ることができる。
【0026】
【実施例】
以下の実施例により本発明をさらに具体的に説明するが、本発明はこれらに限定されない。
【0027】
実施例1
青梅を窄汁してブリックス5.2%の梅果汁12Kgを得た。この梅果汁を濃縮装置に入れ、95℃の温度で、ブリックス76.4%まで加熱濃縮し、梅エキス0.8Kgを得た。この梅エキスは黒色粘性の液体であり、酸度53.1%、アミノ酸度2.5%であった。
【0028】
梅エキス755gを取り、蒸留水で5.1Kgに希釈した。このときのブリックスは11.94%、酸度8.6%、アミノ酸度0.39%であった。この希釈液を限外ろ過(MF)膜(旭化成株式会社製、商品名「PSP−103」、孔径0.1μm、寸法42φ×347mm)を用いてろ過を施した。
【0029】
ろ過条件は以下の通りとした。
【0030】
入口圧0.1MPa、出口圧0.08MPa、初期循環量9リットル/分。末期循環量1リットル/分以下。
【0031】
ろ過開始後2時間で循環量が1リットル/分以下になったので停止し、3.6Kgのろ液が得られた。このろ液は淡褐色透明の液体であった。次いで、これを減圧濃縮装置で、温度48〜29℃、真空度81〜25Torrにてブリックス82%になるまで濃縮し、梅エキス520gを得た。この梅エキスの酸度は59.0%、アミノ酸度は1.5%であった。
【0032】
この梅エキスについて10人で官能検査を行い、10人から従来の梅エキスよりも舌触りが滑らかで苦味、及び、雑味を感じないという評価を得た。得られた梅エキスの0.5gを取り、蒸留水で10gに希釈し、1410rpmで20分間遠心分離を施したところ、水に不溶性の沈殿物は全く認められなかった。また、従来の梅エキスと比べ透明感が高く透き通った外観であった。
【0033】
実施例2
特開2001−17116号公報に記載の方法で製造された梅エキス(ブリックス79.7%、酸度55.6%、アミノ酸度1.0%)760gを取り、蒸留水で5.1Kgに希釈した液を遠心分離器(株式会社トミー精工社製CM−60RN)を用いて2000〜3000Gで連続的に遠心分離し、1時間20分で4.1Kgの上澄み液を得た。この上澄み液も淡褐色透明の液体であった。次いで、これを減圧濃縮装置で、温度48〜29℃、真空度81〜25Torrにてブリックス82%になるまで濃縮し、梅エキス590gを得た。この梅エキスの酸度は60.2%、アミノ酸度は0.9%であった。
【0034】
実施例3
透明梅エキスを添加したヨーグルトの例
従来の梅エキスは黒褐色であり、ヨーグルト等へ添加した場合、色素を配合しても梅をイメージする色調を表現することが困難であった。そこで、本発明の透明梅エキスを用い、シソ色素を添加し梅をイメージする色調が実現できるか検討を行った。
【0035】
実施例1で得た透明梅エキス9gにシソ色素を1gを添加し、10%シソ色素含有の梅エキスを調製した。このシソ色素含有梅エキス1gを白色のヨーグルト50gに添加し攪拌した。得られたヨーグルトは、シソによる着色が梅エキスによって阻害されず、梅のイメージが的確にあらわされた色調となった。
【0036】
比較例
梅肉エキスを添加したヨーグルトの例
ろ過工程を行なっていない梅肉エキス9gにシソ色素1gを添加し、10%シソ色素含有の梅肉エキスを調製した。このシソ色素含有梅肉エキス1gを白色のヨーグルト50gに添加し攪拌した。得られたヨーグルトは、シソによる着色が梅肉エキスの暗色に阻害されて褐色となり、梅らしい色調を出すことができなかった。
【0037】
【発明の効果】
本発明の方法で得られる梅エキスは透明性及び清澄性に優れ、着色の程度が緩和されているために調味料や食品添加物等の食品原料として使用しても製品の外観があまり悪化せず、しかも着色剤によって色を調節することも可能である。
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for producing a plum extract excellent in transparency and clarity.
[0002]
[Prior art]
Plums are rich in ingredients that help improve human health. For this reason, plums have been processed into various forms for edible use. One of the processed foods of plum is plum extract. Plum extract is a concentrate of the active ingredient of plum, and has been prized as a food with particularly high utility, that is, a so-called health food.
[0003]
However, although the plum extract has the flavor of plum and various excellent effects, it has not been widely used as a seasoning or a food additive.
[0004]
One of the reasons is the appearance of plum extract. Plum extract is a black viscous liquid that has a color far from the pink or red color normally imagined from plums. In addition, it is difficult to adjust the color of a black color by adding a colorant.
[0005]
Therefore, although there is a demand for processed foods and favorite items having a plum flavor, use of a plum extract as a raw material causes the appearance of the product to become dark as if stained, and the consumer's impression of the product becomes extremely poor. Therefore, there is resistance to mass-producing a product containing the plum extract, and the use of the plum extract as a food material has been limited.
[0006]
[Problems to be solved by the invention]
The present invention is intended to solve the above-mentioned conventional problems, and the object thereof is as a raw material for foods such as seasonings and food additives because of excellent transparency and clarity, and the degree of coloring is reduced. It is an object of the present invention to provide a plum extract that does not significantly deteriorate the appearance of the product even when used, and that can control the color with a coloring agent.
[0007]
[Means for Solving the Problems]
The present invention provides a step of diluting the plum extract with water;
Separating the water-insoluble component from the diluted plum extract; and concentrating the remaining aqueous solution;
A method for producing a transparent plum extract, comprising:
Which achieves the above object.
[0008]
BEST MODE FOR CARRYING OUT THE INVENTION
In the method of the present invention, ume extract is used as a raw material. The ume extract is a liquid obtained by heating and concentrating a liquid component contained in ume. For example, what is called “plum extract” obtained by boiling plum juice is included in the plum extract herein. In addition, for example, ume extract produced by the method described in JP-A-2001-17116 is also included in the ume extract referred to herein.
[0009]
Plum extract is usually highly viscous and difficult to process as it is, so first dilute it to a suitable viscosity. However, viscosity is difficult to measure, so it is usually controlled by Brix. The ume extract is adjusted to 3 to 70% Brix, preferably 5 to 50%, more preferably 10 to 40% by dilution. If the diluted Brix is lower than 3, filtration or concentration after decolorization takes a lot of time, and if it is higher than 70%, it becomes difficult to perform the separation step.
[0010]
Dilution can be performed by adding clean water to the plum extract and thoroughly stirring. As the dilution water, for example, it is preferable to use distilled water or ion-exchanged water.
[0011]
The amount of water to be added can be appropriately increased or decreased according to the brix required for the diluted ume extract. Generally, the amount of water is adjusted in the range of 1.4 to 257 parts by weight, preferably 6 to 150 parts by weight, more preferably 10 to 70 parts by weight, based on 10 parts by weight of the ume extract. The diluted ume extract is black and cloudy, and the water-insoluble components are suspended or precipitated.
[0012]
Next, the water-insoluble component is separated from the aqueous solution. The method of separation is not particularly limited, and for example, can be performed by a filtration method, a centrifugation method, or the like. This is because these methods are easy to operate and have high separation efficiency.
[0013]
When separation is performed by a filtration method, the pore size of the filter is 0.001 to 0.5 μm, preferably 0.003 to 0.25 μm, and more preferably 0.005 to 0.1 μm. When the pore size of the filter is less than 0.001 μm, the filtration efficiency is deteriorated, and the filtration operation becomes complicated. If the pore size of the filter exceeds 0.5 μm, the separation of the water-insoluble components will be incomplete, and the appearance of the resulting ume extract will be poor.
[0014]
Filters that can be used are generally prefilters, microfiltration membranes, ultrafiltration membranes, nanofilter membranes, reverse osmosis membranes, etc. Filtration and nanofilter membranes. The pre-filter has a disadvantage that the separation of the water-insoluble component is incomplete, and the reverse osmosis membrane has a disadvantage that the dissolved component is removed by filtration.
[0015]
For the filtration operation, for example, a stock solution tank, a circulation pump, a filtration module, and a filtrate tank are prepared, and the pipes can be circulated between the stock solution tank, the circulation pump, and the filtration module. The filtrate from the filtration module is introduced into the filtrate tank via independent piping. Pour the diluted ume extract solution into the stock solution tank and filter at a pressure and circulation rate that match the operating conditions described in the instruction manual for the filtration module.
[0016]
When performing separation by centrifugation, the diluted ume extract solution is continuously introduced into the rotor, and the water-insoluble component is deposited on the wall of the rotor. Use a special centrifuge that is plumbed so that it goes out of the tube. Even with a bucket-type centrifuge, it takes time and effort to artificially remove the supernatant, which does not hinder the effects of the present invention. The load applied to the centrifugation is suitably from 1,000 to 5,000 G, preferably from 2,000 to 3,000 G, and the effect of the centrifugation and the processing time are not significantly affected even if a load more than this is applied.
[0017]
When the water-insoluble component is separated from the aqueous solution of the ume extract in this way, an aqueous solution containing the ume extract remains. This aqueous solution is transparent. Then, the remaining aqueous solution is concentrated. Concentration is performed to remove water added to the plum extract for viscosity control.
[0018]
The method of concentration is not particularly limited, but is preferably carried out by heating without heating or at a relatively low temperature to evaporate water. Heating to high temperatures produces water-insoluble components. This is because the appearance of the obtained plum extract becomes black and opaque.
[0019]
The temperature at the time of concentration is generally adjusted to 15 to 80 ° C, preferably 20 to 70 ° C, more preferably 25 to 65 ° C. To accelerate the process, it is better to carry out concentration under reduced pressure. At that time, the pressure is reduced to about 11 to 360 Torr, preferably about 17 to 230 Torr, and more preferably about 23 to 190 Torr.
[0020]
The obtained plum extract is a transparent and clear liquid, and the degree of coloring is remarkably reduced as compared with the conventional black and opaque plum extract. Therefore, even if this plum extract is used as a seasoning or a food additive, it does not significantly affect the appearance of the product. In addition, since the plum extract is transparent, it has a low coloring power, and the color of the product can be adjusted by adding a food coloring agent. For example, the use of a perilla pigment as a food additive allows the product to be finished in a plum-like color.
[0021]
Examples of uses of the transparent plum extract obtained by the method of the present invention include soft drinks and candy, which require transparency in product appearance, and yogurt, in which light appearance is required in product appearance.
[0022]
Further, as a result of a sensory test, this transparent plum extract has a smoother tongue and reduced bitterness and unpleasant taste as compared with the conventional plum extract, and is superior to the plum extract as a food to be taken as it is.
[0023]
In the method of the present invention, after the water-insoluble component is separated from the aqueous solution of the ume extract, the aqueous solution containing the ume extract may be further decolorized before the concentration step. By doing so, it is possible to obtain a plum extract with less coloring, that is, a colorless and nearly transparent plum extract.
[0024]
In the decolorization step, for example, the aqueous solution containing ume extract is passed through a column filled with the adsorbent, or the adsorbent is added to the aqueous solution containing ume extract, stirred for a certain period of time, allowed to stand, and then decanted. Or a decolorizing solution can be obtained by removing the adsorbent by filtration. In this case, activated carbon, an adsorption resin, or the like can be used as the adsorbent. There are various types of activated carbon, such as powder, granule, and cloth, depending on its shape, but granular activated carbon is preferable because of its ease of treatment. In addition, there are various types of materials before being made into activated carbon, but this is not particularly limited. Among the products manufactured by Ajinomoto Fine Techno Co., Ltd., there are three types of amphoteric type and one type of weakly basic type among the products manufactured by Ajinomoto Fine Techno Co., Ltd. Among these, the preferred type of the adsorption resin is an amphoteric type resin.
[0025]
After the decolorization step, concentration is performed by the above-described method, and a transparent and clear plum extract can be obtained.
[0026]
【Example】
The present invention will be described more specifically with reference to the following examples, but the present invention is not limited thereto.
[0027]
Example 1
Ome was squeezed to give 12 kg of plum juice with 5.2% Brix. This plum juice was placed in a concentrator and concentrated by heating at a temperature of 95 ° C. to a brix of 76.4% to obtain 0.8 kg of a plum extract. This plum extract was a black viscous liquid having an acidity of 53.1% and an amino acid content of 2.5%.
[0028]
755 g of plum extract was taken and diluted to 5.1 kg with distilled water. At this time, the Brix was 11.94%, the acidity was 8.6%, and the amino acid content was 0.39%. The diluted solution was filtered using an ultrafiltration (MF) membrane (trade name “PSP-103”, manufactured by Asahi Kasei Corporation, pore size: 0.1 μm, size: 42 × 347 mm).
[0029]
The filtration conditions were as follows.
[0030]
Inlet pressure 0.1 MPa, outlet pressure 0.08 MPa, initial circulation rate 9 liter / min. End-stage circulation rate is 1 liter / min or less.
[0031]
Two hours after the start of the filtration, the circulation was reduced to 1 liter / min or less, and the operation was stopped, and 3.6 kg of the filtrate was obtained. This filtrate was a light brown transparent liquid. Next, this was concentrated with a vacuum concentrator at a temperature of 48 to 29 ° C. and a degree of vacuum of 81 to 25 Torr until the Brix became 82% to obtain 520 g of a plum extract. The acidity of this plum extract was 59.0%, and the amino acid content was 1.5%.
[0032]
A sensory test was conducted by 10 persons on this plum extract, and the evaluation by the ten persons was that the tongue was smoother, had a bitter taste, and did not feel unpleasant than the conventional plum extract. 0.5 g of the obtained plum extract was taken, diluted to 10 g with distilled water, and centrifuged at 1410 rpm for 20 minutes. As a result, no insoluble precipitate was found in water. In addition, the appearance was higher and more transparent than the conventional plum extract.
[0033]
Example 2
Take 760 g of ume extract (79.7% Brix, 55.6% acidity, 1.0% amino acid content) produced by the method described in JP-A-2001-17116, and dilute to 5.1 kg with distilled water. The liquid was continuously centrifuged at 2000 to 3000 G using a centrifugal separator (CM-60RN manufactured by Tommy Seiko Co., Ltd.) to obtain a supernatant of 4.1 kg in 1 hour and 20 minutes. This supernatant was also a light brown transparent liquid. Next, this was concentrated by a reduced-pressure concentrator at a temperature of 48 to 29 ° C. and a degree of vacuum of 81 to 25 Torr until Brix became 82% to obtain 590 g of a plum extract. The acidity of this plum extract was 60.2% and the amino acid content was 0.9%.
[0034]
Example 3
Example of yogurt to which transparent plum extract is added Conventional plum extract is black-brown, and when added to yogurt or the like, it is difficult to express a color tone that resembles a plum even if a pigment is added. Therefore, it was examined whether or not the transparent plum extract of the present invention could be used to add a perilla pigment to achieve a color tone that images a plum.
[0035]
1 g of perilla pigment was added to 9 g of the transparent plum extract obtained in Example 1 to prepare a plum extract containing 10% perilla pigment. 1 g of the perilla pigment-containing plum extract was added to 50 g of white yogurt and stirred. In the obtained yogurt, the coloring by perilla was not inhibited by the plum extract, and the color of the plum was accurately expressed.
[0036]
Comparative example Example of yogurt to which plum meat extract was added 1 g of perilla pigment was added to 9 g of plum meat extract not subjected to the filtration step to prepare a plum meat extract containing 10% perilla pigment. 1 g of the perilla extract containing perilla pigment was added to 50 g of white yogurt and stirred. The obtained yogurt became brown due to the inhibition of the coloration of perilla by the dark color of the plum meat extract, and could not produce a color tone like plum.
[0037]
【The invention's effect】
The plum extract obtained by the method of the present invention has excellent transparency and clarity, and the appearance of the product is significantly deteriorated even when used as a food raw material such as a seasoning or a food additive because the degree of coloring is reduced. In addition, the color can be adjusted by a colorant.

Claims (8)

梅エキスを水で希釈する工程;
希釈した梅エキスから非水溶性成分を分離する工程;及び
残された水溶液を濃縮する工程;
を包含する、透明梅エキスの製造方法。
Diluting the plum extract with water;
Separating the water-insoluble component from the diluted plum extract; and concentrating the remaining aqueous solution;
A method for producing a transparent plum extract, comprising:
前記分離が、ろ過法により行われる請求項1記載の方法。The method according to claim 1, wherein the separation is performed by a filtration method. 前記ろ過が、フィルタとして精密ろ過膜、限外ろ過膜又はナノフィルタ膜を用いて行われる請求項2記載の方法。The method according to claim 2, wherein the filtration is performed using a microfiltration membrane, an ultrafiltration membrane, or a nanofilter membrane as a filter. 前記分離が、遠心分離法によって行われる請求項1記載の方法。The method according to claim 1, wherein the separation is performed by centrifugation. 前記濃縮が80℃以下の温度で行われる請求項1記載の方法。The method according to claim 1, wherein the concentration is performed at a temperature of 80C or less. 前記濃縮が減圧下で行われる請求項1又は5記載の方法。The method according to claim 1, wherein the concentration is performed under reduced pressure. 梅エキスを水で希釈する工程;
希釈した梅エキスから非水溶性成分を分離する工程;
残された水溶液を脱色する工程;及び
脱色された水溶液を濃縮する工程;
を包含する、透明梅エキスの製造方法。
Diluting the plum extract with water;
Separating water-insoluble components from the diluted plum extract;
Decolorizing the remaining aqueous solution; and concentrating the decolorized aqueous solution;
A method for producing a transparent plum extract, comprising:
請求項1〜7のいずれかに記載の方法により製造された透明梅エキス。A transparent plum extract produced by the method according to claim 1.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006348001A (en) * 2005-06-20 2006-12-28 Naris Cosmetics Co Ltd Poor circulation-improving agent and functional food
JP2011229419A (en) * 2010-04-23 2011-11-17 Manns Wine Co Ltd Plum liquor and method of producing the same
JP2014018125A (en) * 2012-07-17 2014-02-03 Sadaei Noso Production method of plum extract

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006348001A (en) * 2005-06-20 2006-12-28 Naris Cosmetics Co Ltd Poor circulation-improving agent and functional food
JP2011229419A (en) * 2010-04-23 2011-11-17 Manns Wine Co Ltd Plum liquor and method of producing the same
JP2014018125A (en) * 2012-07-17 2014-02-03 Sadaei Noso Production method of plum extract

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