JPH0312862B2 - - Google Patents

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Publication number
JPH0312862B2
JPH0312862B2 JP58164013A JP16401383A JPH0312862B2 JP H0312862 B2 JPH0312862 B2 JP H0312862B2 JP 58164013 A JP58164013 A JP 58164013A JP 16401383 A JP16401383 A JP 16401383A JP H0312862 B2 JPH0312862 B2 JP H0312862B2
Authority
JP
Japan
Prior art keywords
plum juice
adsorption
pickled plum
salt
adsorption resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP58164013A
Other languages
Japanese (ja)
Other versions
JPS6054654A (en
Inventor
Koichi Mochida
Takao Oosaki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SOORAA KK
Original Assignee
SOORAA KK
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Filing date
Publication date
Application filed by SOORAA KK filed Critical SOORAA KK
Priority to JP58164013A priority Critical patent/JPS6054654A/en
Publication of JPS6054654A publication Critical patent/JPS6054654A/en
Publication of JPH0312862B2 publication Critical patent/JPH0312862B2/ja
Granted legal-status Critical Current

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  • Preparation Of Fruits And Vegetables (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • General Preparation And Processing Of Foods (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は有機酸及び食塩を含まない漬梅汁エキ
スの製造法に関するものである。 漬梅汁は、梅干の製造終了後、梅干をとり出し
た後に残される漬汁である。漬梅汁の特徴は食塩
の含有量が大きく、強酸性であるという点である
従つて1)食料品にならない。2)放棄不可能で
ある。3)生物処理ができないため放流できな
い。4)多量が排出される。など多くの問題点を
もつと共に利用もほとんどなされていない。現在
は天然物志向の風潮が強く、梅干に関連する提案
も、例えば、1)特公昭51−32707(特開昭48−
35064)新規梅干エキスの製造方法、2)特公昭
57−24103(特開昭50−88268)天然梅酸味料の製
造法にみられる。 以上のうちまず、1)は、蒸留によつて水分を
除去して濃縮液をつくり、アルコールを加えて、
溶かし不溶分を別後、該含水アルコール溶液を
濃縮することを特徴とする梅干エキスの製造法で
ある。次に2)は、イオン交換膜を使用し香気及
びエキスを濃縮保持せしめながら含有塩分を除去
せしめることを特徴とする香気性天梅酸味料の製
造法である。 発明者は漬梅汁とは、「高食塩濃度、高酸性下、
常温にて長期間を要して梅の実から得られた抽出
液であつて、貫重な有効成分を多量含有するもの
である。一、梅干の主成分は粗繊維であつて、有
効成分の大部分が漬梅汁へ溶出した残渣である。」
との観点から、漬梅汁こそ加工方法を検討すれ
ば、優れた食品となしうると考えた。 前記した従来の2法に共通する点は、食塩等の
不要な成分をとりだすために多量の熱又は電気エ
ネルギーを消費することである。 本発明は漬梅汁からまず有効成分のみを吸着樹
脂に吸着堆積させてゆき、不要な成分例えば食塩
及び水などは吸着させずに、何らの手段を加える
ことなくそのまま系外へ分離するものであつて、
前記従来法とは発想を異にするものである。 即ち本発明は、漬梅汁を吸着樹脂で処理し、有
機酸及び食塩を非吸着成分とし除去した後、前記
吸着樹脂に水、アルコール水溶液又は弱アルカリ
水溶液を加えて、吸着樹脂中から、赤色色素を含
有する吸着成分を溶出させることを特徴とする、
有機酸及び食塩を含まない漬梅汁エキスの製造法
を提供するものである。 漬梅汁の特徴の第一は16〜25%という高濃度の
食塩を含んでいる点である。第二に、PHが1〜
2であつて強い酸性を呈し多量の有機酸を含有し
ているという点である。成分はクエンン酸とリン
ゴ酸が主成分でクエン酸4.5%、リンゴ酸0.8%で
ある。他の有機酸は酢酸、乳酸などであるが極て
僅かである。第三は蛋白質、脂質、糖質、アミノ
酸、無機塩、及び色素などいずれをも僅かずつ含
有しているという点である。第四は梅干以上の芳
香を帯び長期に渉り安定な点である。この様に優
れた諸点をもちながら利用されなかつたのは、食
塩が高濃度であつたためと思われる。 吸着樹脂は巨大網状構造をもつた合成吸着剤例
えばアンバーライトXAD(ローム・アンド・ハー
ス社製)、ダイヤ樹脂HP(三菱化成製)の各種の
もの使用できる。これらにはスチンとジビニルベ
ンゼンの共重合体あるいはアクリル酸エステル共
重合体などがあり、多孔性で大きな表面積ををも
つ。孔径、表面積及び密度の種々異るものが市販
されている。漬梅汁はこれら吸着樹脂を膨潤した
ものに接触させると食塩、クエン酸の様に分子量
の小さい成分は吸着しない。 漬梅汁を吸着樹脂に接触させる方法はバツチ式
でもカラム式でもいづれによつても良いが、漬梅
汁の食塩濃度が大であるから密度の小さい吸着樹
脂は液面へ浮上することがある。カラム式の場合
は水に膨潤させた吸着樹脂を詰めたカカラムをつ
くりカラム上部へ漬梅汁を送ればよい。流出液は
食塩及びクエン酸などを含有する無色の液である
がカラムは種々の成分が吸着して着色する。バツ
チ式の場合は漬梅汁を入れた槽へ吸着樹脂を入
れ、撹拌して吸着せしめる。吸着後の液は無色で
ある。 吸着後カラム式の場合は少量の水で洗い非吸着
成分を流出させる。バツチ式では傾注して樹脂と
わけるかろ別するなどしてわけ少量の水で洗い付
着している非吸着成分を除去する。 吸着後の樹脂から吸着成分を溶出するには水又
はアルコール水溶液又は弱アルカリ水溶液を使用
する。吸着樹脂の種類により溶出溶媒の性状は選
択すべきであり、水で溶出できるものとできない
ものなどがある。溶出液量はなるべく少量ですむ
様な液を選択する方が得策であるのはいうまでも
ない。アルコール、エチルアルコール、焼酎、酒
類などが良い、他のアルコール例えばメタノー
ル、プロパノール、ブタノールなどでも溶出は可
能であるが、そのまま食品とするには好ましくな
い。この他弱アルカリ水溶液も可能である。ただ
し食品とすることを前提とするので水酸化ナトリ
ウムが最も望ましい。溶出液はそのままでもよい
が、濃縮を要するときは減圧蒸留、常圧蒸留など
で水又はアルコールを除去すればよい。吸着樹脂
を使用するため溶出液には酸を含まないので耐酸
性の蒸留装置の必要がない。 漬梅汁中の有機酸を不溶性のカルシウム塩とな
し漬梅汁から有機酸を除去するという前処理を採
用し、前処理後の漬梅汁を吸着樹脂で処理する場
合は予め滴定酸度を測定しておき必要量のカルシ
ウムを加えるべきである。有機酸はほとんどクエ
ン酸であつて約2時間以上放置すると結晶しはじ
める。PHは約4になり結晶の生成が終ればこれを
除去して、残液を吸着処理へ移せばよい。クエン
酸のカルシウム塩は酸性で溶けるので用途によつ
ては、本発明の漬梅汁エキスに前記クエン酸カル
シウムを加え、その後酸性にして溶かし、利用に
供することも可能である。 本発明方法の効果を実験例によつて詳細に説明
すれば次の通りである。 実験に使用した漬梅汁は第1表に示す性状のも
のである。
The present invention relates to a method for producing pickled plum juice extract that does not contain organic acids and salt. Pickled plum juice is the pickled juice that is left after the pickled plums are taken out after production. The characteristics of pickled plum juice are that it has a high salt content and is strongly acidic; therefore, 1) it cannot be used as a food product; 2) Not renounceable. 3) Cannot be discharged because biological treatment cannot be performed. 4) A large amount is excreted. It has many problems and is hardly used. Currently, there is a strong trend toward natural products, and proposals related to umeboshi are also being made.
35064) New method for producing umeboshi extract, 2) Tokkosho
57-24103 (Japanese Unexamined Patent Publication No. 50-88268) Seen in the method for producing natural plum sour agent. First of all, 1) is to remove water by distillation to create a concentrated liquid, add alcohol,
This is a method for producing a pickled plum extract, which is characterized by concentrating the hydroalcoholic solution after dissolving and separating insoluble matter. Next, 2) is a method for producing an aromatic tempura sour agent, which is characterized by using an ion exchange membrane to remove the salt content while concentrating and retaining the aroma and extract. The inventor explains that pickled plum juice is made from ``high salt concentration, high acidity,
It is an extract obtained from plum fruit over a long period of time at room temperature, and contains a large amount of powerful active ingredients. 1. The main component of pickled plums is crude fiber, and most of the active ingredients are residues dissolved into pickled plum juice. ”
From this perspective, I thought that pickled plum juice could be made into an excellent food by considering the processing method. What the two conventional methods described above have in common is that a large amount of heat or electrical energy is consumed in order to extract unnecessary components such as common salt. The present invention first adsorbs and deposits only the active ingredients from pickled plum juice onto an adsorption resin, and then separates unnecessary components such as salt and water from the system without adsorbing them and without adding any means. hand,
The concept is different from the conventional method described above. That is, in the present invention, pickled plum juice is treated with an adsorption resin to remove organic acids and salt as non-adsorbed components, and then water, an aqueous alcohol solution, or a weak alkali aqueous solution is added to the adsorption resin, and red pigment is extracted from the adsorption resin. characterized by eluting adsorbed components containing
The present invention provides a method for producing pickled plum juice extract that does not contain organic acids and salt. The first characteristic of pickled plum juice is that it contains a high concentration of salt, ranging from 16 to 25%. Second, the pH is 1~
2, exhibits strong acidity, and contains a large amount of organic acid. The main ingredients are citric acid and malic acid, with 4.5% citric acid and 0.8% malic acid. Other organic acids include acetic acid and lactic acid, but they are extremely rare. Third, it contains small amounts of proteins, lipids, carbohydrates, amino acids, inorganic salts, and pigments. Fourth, it has a more aromatic aroma than umeboshi and is stable over a long period of time. The reason why it was not used despite its many excellent features is thought to be due to the high concentration of common salt. As the adsorption resin, various kinds of synthetic adsorbents having a giant network structure, such as Amberlite XAD (manufactured by Rohm and Haas) and Diamond Resin HP (manufactured by Mitsubishi Kasei), can be used. These include copolymers of styne and divinylbenzene or acrylic acid ester copolymers, which are porous and have a large surface area. They are commercially available with different pore sizes, surface areas and densities. When pickled plum juice is brought into contact with swollen adsorption resins, components with small molecular weights such as salt and citric acid will not be adsorbed. The method of bringing the pickled plum juice into contact with the adsorption resin may be either a batch method or a column method, but since the salt concentration of the pickled plum juice is high, the adsorption resin with a low density may float to the surface of the liquid. In the case of a column type, you can make a column filled with adsorption resin swollen in water and send the pickled plum juice to the top of the column. The effluent is a colorless liquid containing salt, citric acid, etc., but the column is colored by adsorption of various components. If using the batch method, put the adsorption resin into a tank containing pickled plum juice and stir to make it adsorb. The liquid after adsorption is colorless. After adsorption, in the case of a column type, wash with a small amount of water to flush out non-adsorbed components. In the batch method, the mixture is poured and separated from the resin by filtration, and then washed with a small amount of water to remove non-adsorbed components. Water, an alcohol aqueous solution, or a weak alkaline aqueous solution is used to elute the adsorbed component from the resin after adsorption. The properties of the elution solvent should be selected depending on the type of adsorption resin, and some can be eluted with water and others cannot. It goes without saying that it is better to select an eluate that requires as little volume as possible. Alcohol, ethyl alcohol, shochu, alcoholic beverages, etc. are good, and other alcohols such as methanol, propanol, butanol, etc. can also be used for elution, but they are not preferred for use as foods. In addition, a weak alkaline aqueous solution is also possible. However, since it is intended to be used as food, sodium hydroxide is most desirable. The eluate may be used as it is, but if concentration is required, water or alcohol may be removed by vacuum distillation, normal pressure distillation, etc. Since an adsorption resin is used, the eluate does not contain acid, so there is no need for an acid-resistant distillation device. If a pretreatment is used to remove organic acids from pickled plum juice with insoluble calcium salts from pickled plum juice, and the pretreated pickled plum juice is treated with an adsorption resin, the titratable acidity should be measured in advance. The required amount of calcium should be added. The organic acid is mostly citric acid, which begins to crystallize if left for about 2 hours or more. Once the pH reaches about 4 and the formation of crystals is complete, they can be removed and the remaining liquid can be transferred to adsorption treatment. Since the calcium salt of citric acid dissolves in acidity, depending on the use, it is possible to add the calcium citrate to the pickled plum juice extract of the present invention, then make it acidic, dissolve it, and use it. The effects of the method of the present invention will be explained in detail using experimental examples as follows. The pickled plum juice used in the experiment had the properties shown in Table 1.

【表】 漬梅汁の有機酸組成を高速液体クロマトグラフ
イーで分析するとクエン酸4.40%、リンゴ酸0.8
%であり、他の有機酸はごく僅かであつた。クエ
ン酸はカルシウム塩として析出させるとその溶解
度が中性では18℃において0.0849、25℃では
0.0959である。リンゴ酸は18℃0.9214、25℃
0.8552であるから理論的にはクエン酸はほとんど
沈澱し、リンゴ酸は約1g以下が沈澱する。理論
量のCaOを加え沈澱を析出させるとを4.0となつ
た。カルシウム塩の沈澱をろ別した液についても
漬梅汁の場合と同様に吸着樹脂処理を行つた。
CaOで処理した後の沈澱をろ別した液のクエン酸
及びリンゴ酸の濃度はそれぞれ0.8%及び0.6%で
あつた。 吸着樹脂の市販品にはロームアンドハース社の
XAD−2、XAD−4、XAD−7があり、又三
菱樹脂のHP−10、HP−20、HP50などがある。
これらについて吸着の強弱を比較してみると第2
表通りであつた。吸着する成分は極めて多種類の
ものであるから全成分について分析することは不
可能に近いので漬梅汁の特徴である赤色の色素成
分をもつて吸着力を代表することとした。 吸着樹脂の気孔中の空気をメタノール、水の順
で置換しても16%食塩水中では浮上するものと、
この様な処理をしないでも沈降するものがある。
浮上する吸着樹脂はバツチ式に使用すると便利で
あり、吸着後は処理液を槽の底から抜きとれば簡
単に両者を分離できる。一方沈降する吸着樹脂の
場合はカラムをつくる便利である。なお、浮上す
る吸着樹脂でも上向式のカラム即ち漬梅液をカラ
ム下部から通ずる方式であればカラムの使用は可
能でる。
[Table] Analysis of the organic acid composition of pickled plum juice using high performance liquid chromatography reveals 4.40% citric acid and 0.8% malic acid.
%, and the amount of other organic acids was very small. When citric acid is precipitated as a calcium salt, its solubility is 0.0849 at 18℃ at neutral temperature and 0.0849 at 25℃.
It is 0.0959. Malic acid is 18℃0.9214, 25℃
Since it is 0.8552, theoretically most of the citric acid will precipitate, and less than about 1 g of malic acid will precipitate. When a theoretical amount of CaO was added and a precipitate was precipitated, the value was 4.0. The liquid obtained by filtering out the calcium salt precipitate was also treated with an adsorption resin in the same manner as the pickled plum juice.
The concentrations of citric acid and malic acid in the solution obtained by filtering the precipitate after treatment with CaO were 0.8% and 0.6%, respectively. Commercial adsorption resin products include Rohm and Haas Co.
There are XAD-2, XAD-4, and XAD-7, as well as Mitsubishi Plastics' HP-10, HP-20, and HP50.
Comparing the strength of adsorption for these, the second
It was right on the street. Since there are so many different types of adsorbed components that it is almost impossible to analyze all of them, we decided to use the red pigment component, which is a characteristic of pickled plum juice, to represent the adsorption power. Even if the air in the pores of the adsorption resin is replaced with methanol and water in that order, it will float in 16% saline solution.
Some substances settle even without such treatment.
It is convenient to use the floating adsorption resin in batches, and after adsorption, the two can be easily separated by draining the processing liquid from the bottom of the tank. On the other hand, in the case of an adsorption resin that settles, it is convenient to create a column. Incidentally, even if the adsorption resin floats, it is possible to use an upward type column, that is, a column in which the pickled plum liquid is passed from the bottom of the column.

【表】 XAD−7を水で膨潤させ55mlを直径1.8cm×高
さ31.5cmのカラムとなし吸着柱をつくつた。 これへ漬梅汁1000mlをSV=3.4の条件で通過さ
せた。赤色の色素はすべて吸着された。35%アル
コール水溶液135mlで溶出し橙色ないし赤色の色
素区分を得た。溶出力を60%アルコールのときと
比較すると35%アルコールの方が溶出力が大きか
つた。カラムに吸着せず流出した区分すなわち
XAD−7非吸着成分は249.4gであつた、漬梅汁
は1000mlの固形分は316gであり溶出液の固形分
は60gであつた。 HP−2015mlを水で膨潤し、これへ漬梅汁40ml
を加えて吸着処理し、ろ過して非吸着成分を含む
無色透明の液及び洗液を得た。ろ過してわけた吸
着樹脂をとり、35%アルコールで溶出し赤色の吸
着成分のアルコール溶液を得た。溶出液の固形分
は0.2gであつた。 溶出液のアルコール濃度と溶出の関係はアルコ
ール濃度が小さいときは吸着バンドは大きくなる
がアルコール濃度を大きくすると吸着バンドは小
さくなる。然し純アルコールではほとんど流出し
なくなる。従つて35〜60%が最もバンド幅が小さ
く適当に濃縮された溶出液が得られた。 次に本発明方法を実施例によつて説明する。 実施例 1 漬梅汁1をXAD−7でつくつたカラムφ1.8
×35cmに通過させ長さ7cmの赤色の吸着バンドを
つくつた。次いでイオン交換水を100ml通じ洗滌
し食塩及びクエン酸の流出後続けてイオン交換水
を通じ溶出した。溶出液を濃縮し350mlの赤色を
帯びた梅の芳香をもち、無塩、かつクエン酸を含
有しない梅エキスを得た。 実施例 2 漬梅汁1をXAD−7でつくつたカラムφ1.8
×40cmに通過させて長さ7cmの吸着バンドをつく
た。次いで水100mlで洗滌後、35%アルコール130
mlで溶出した。溶出液を集めて濃縮し20mlとな
し、梅干の芳香を放つエキスを得た。実施例1と
同様に食塩及び有機酸を含有しなかつた。 実施例 3 漬梅汁1000mlをXAD−7のカラムに通じ実施
例1と同様のカラムに吸着帯をつくつた。これへ
水100mlを加えて洗滌したのち、0.01N
NaOH100mlを加えて溶出した。溶出液の性状は
実施例1と同じであつた。 実施例 4 漬梅汁1000mlにCaO20gを少量ずつ撹拌しなが
ら加えて溶かし5時間静置して主としてクエン酸
カルシウムからなる結晶を析出させた。ろ過して
ろ液をとり、実施例1と同様のカラムにろ液を通
じ吸着させた。イオン交換水を通じ食塩の流出後
から溶出液を集めた。赤色の色素が溶出を終えた
ところで中止し溶出液を得た。溶出液にさきに得
たクエン酸カルシウムを加えて溶かし、食塩を含
有しない酸味を呈する漬梅汁の吸着樹脂処理液を
800ml得た。 実施例 5 漬梅汁1000mlを水400mlの水で2000ml容の水槽
に膨潤させたHP−20吸着樹脂300mlに加えて撹
拌して吸着処理し下層の漬梅汁層が無色透明にな
つたのち、吸着樹脂をろ過して集めた。300mlの
水で洗滌したのちこれへ35%アルコールを加えて
濃赤色の溶出液1000mlを得た。 以上の説明から明らかな如く、本発明によれ
ば、吸着樹脂を利用して有機酸及び食塩を含まな
い漬梅汁エキスを容易に得ることができる。ま
た、不要物を除去するたためのエネルキー消費が
ない、吸着樹脂からの漬梅汁エキスの溶出は、吸
着樹脂の再生操作の一部を兼ねるなど、本発明は
有利な点が多い。
[Table] An adsorption column was created by swelling 55 ml of XAD-7 with water and forming it into a column with a diameter of 1.8 cm and a height of 31.5 cm. 1000 ml of pickled plum juice was passed through this under the condition of SV = 3.4. All red dye was adsorbed. Elution was carried out with 135 ml of 35% alcohol aqueous solution to obtain an orange to red pigment fraction. When comparing the elution power with 60% alcohol, the elution power with 35% alcohol was greater. The fraction that did not adsorb to the column and flowed out, i.e.
The non-adsorbed component of XAD-7 was 249.4 g, the solid content of 1000 ml of pickled plum juice was 316 g, and the solid content of the eluate was 60 g. Swell HP-2015ml with water and add 40ml of pickled plum juice.
was added for adsorption treatment, and filtered to obtain a colorless and transparent liquid containing non-adsorbed components and a washing liquid. The filtered and separated adsorption resin was taken and eluted with 35% alcohol to obtain a red alcoholic solution of adsorbed components. The solid content of the eluate was 0.2 g. The relationship between the alcohol concentration of the eluate and elution is that when the alcohol concentration is low, the adsorption band becomes large, but when the alcohol concentration is increased, the adsorption band becomes small. However, pure alcohol hardly flows out. Therefore, an appropriately concentrated eluate with the narrowest band width between 35% and 60% was obtained. Next, the method of the present invention will be explained with reference to examples. Example 1 Column φ1.8 made of pickled plum juice 1 using XAD-7
A red adsorption band with a length of 7 cm was created by passing the sample through a 35 cm x 35 cm tube. Next, the solution was washed with 100 ml of ion-exchanged water, and after the salt and citric acid had flowed out, the solution was eluted through ion-exchanged water. The eluate was concentrated to obtain 350 ml of reddish plum extract, which had a plum aroma, was salt-free, and did not contain citric acid. Example 2 Column φ1.8 made of pickled plum juice 1 with XAD-7
A 7 cm long adsorption band was created by passing the sample through a 40 cm x 40 cm tube. Then, after washing with 100ml of water, 35% alcohol 130
eluted in ml. The eluate was collected and concentrated to 20 ml to obtain an extract with the aroma of umeboshi. As in Example 1, it did not contain salt or organic acid. Example 3 1000 ml of pickled plum juice was passed through an XAD-7 column to create an adsorption zone in the same column as in Example 1. After adding 100ml of water and washing, 0.01N
Elution was carried out by adding 100 ml of NaOH. The properties of the eluate were the same as in Example 1. Example 4 20 g of CaO was added little by little to 1000 ml of pickled plum juice while stirring, and the solution was allowed to stand for 5 hours to precipitate crystals mainly consisting of calcium citrate. The filtrate was collected by filtration, and passed through the same column as in Example 1 for adsorption. The eluate was collected after the sodium chloride was drained through ion-exchanged water. Elution was stopped when the red dye had finished elution, and an eluate was obtained. Add the calcium citrate obtained earlier to the eluate and dissolve it to create an adsorption resin treatment solution for pickled plum juice that does not contain salt and has a sour taste.
I got 800ml. Example 5 1000 ml of pickled plum juice was added to 300 ml of HP-20 adsorption resin swollen with 400 ml of water in a 2000 ml water tank, stirred and adsorbed. After the lower pickled plum juice layer became colorless and transparent, the adsorption resin was added. was collected by filtration. After washing with 300 ml of water, 35% alcohol was added to obtain 1000 ml of a deep red eluate. As is clear from the above description, according to the present invention, a pickled plum juice extract that does not contain organic acids and salt can be easily obtained using an adsorption resin. Furthermore, the present invention has many advantages, such as the elution of the pickled plum juice extract from the adsorption resin, which does not require energy consumption to remove unnecessary substances, and also serves as a part of the regeneration operation of the adsorption resin.

Claims (1)

【特許請求の範囲】[Claims] 1 漬梅汁を吸着樹脂で処理し、有機酸及び食塩
を非吸着成分として除去した後、前記吸着樹脂に
水、アルコール水溶液又は弱アルカリ水溶液を加
えて、吸着樹脂中から、赤色色素を含有する吸着
成分を溶出させることを特徴とする、有機酸及び
食塩を含まない漬梅汁エキスの製造法。
1. After treating the pickled plum juice with an adsorption resin to remove organic acids and salt as non-adsorbed components, water, an aqueous alcohol solution, or a weak alkaline aqueous solution is added to the adsorption resin, and the adsorption containing red pigment is extracted from the adsorption resin. A method for producing pickled plum juice extract free of organic acids and salt, characterized by eluting components.
JP58164013A 1983-09-05 1983-09-05 Production of japanese plum essence free from organic acids and salt from its pickling solution Granted JPS6054654A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58164013A JPS6054654A (en) 1983-09-05 1983-09-05 Production of japanese plum essence free from organic acids and salt from its pickling solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58164013A JPS6054654A (en) 1983-09-05 1983-09-05 Production of japanese plum essence free from organic acids and salt from its pickling solution

Publications (2)

Publication Number Publication Date
JPS6054654A JPS6054654A (en) 1985-03-29
JPH0312862B2 true JPH0312862B2 (en) 1991-02-21

Family

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JP58164013A Granted JPS6054654A (en) 1983-09-05 1983-09-05 Production of japanese plum essence free from organic acids and salt from its pickling solution

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Country Link
JP (1) JPS6054654A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63313557A (en) * 1987-03-26 1988-12-21 Reisenbai Honpo:Kk Ume (japanese apricot) food and production thereof
CN105581313A (en) * 2016-01-13 2016-05-18 山东鲁菱果汁有限公司 Highly-concentrated essence and preparation method

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