JP2612785B2 - How to reduce juice acidity - Google Patents

How to reduce juice acidity

Info

Publication number
JP2612785B2
JP2612785B2 JP3152170A JP15217091A JP2612785B2 JP 2612785 B2 JP2612785 B2 JP 2612785B2 JP 3152170 A JP3152170 A JP 3152170A JP 15217091 A JP15217091 A JP 15217091A JP 2612785 B2 JP2612785 B2 JP 2612785B2
Authority
JP
Japan
Prior art keywords
juice
electrodialysis
chamber
acidity
tank
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 - Fee Related
Application number
JP3152170A
Other languages
Japanese (ja)
Other versions
JPH04349874A (en
Inventor
武蔵 小野
俊郎 寺本
正雄 沢田
Original Assignee
帝人エンジニアリング株式会社
富士食研株式会社
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 帝人エンジニアリング株式会社, 富士食研株式会社 filed Critical 帝人エンジニアリング株式会社
Priority to JP3152170A priority Critical patent/JP2612785B2/en
Publication of JPH04349874A publication Critical patent/JPH04349874A/en
Application granted granted Critical
Publication of JP2612785B2 publication Critical patent/JP2612785B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Non-Alcoholic Beverages (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、柑橘類、梅などの果汁
の酸度減少方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for reducing the acidity of juice such as citrus fruits and plums.

【0002】[0002]

【従来の技術】柑橘類や梅などの果汁には、酸味に関係
するクエン酸、リンゴ酸などの有機酸、甘味に関係する
グルコース、フラクトースなどの糖類、その他アミノ
酸、脂質、灰分、ビタミンCなどを含み、その香気、風
味は多くの人に好まれ食用に供されてきた。しかし、果
汁のなかには酸味の強いものもあり、これを減少させる
ことが望まれ、その方法が提案されている。
2. Description of the Related Art Juices such as citrus fruits and plums contain organic acids such as citric acid and malic acid related to sourness, sugars such as glucose and fructose related to sweetness, other amino acids, lipids, ash, and vitamin C. Including, its aroma and flavor have been favored by many people and used for food. However, some fruit juices have a strong sour taste, and it is desired to reduce them, and a method has been proposed.

【0003】例えば、柑橘類果汁から酸味に関係する酸
度を減少させる方法として、雑誌、Fla. Stat
e. Hort. Soc. Proc. 73,21
6(1978)には、陰極と陽極の間が陰イオン交換膜
のみで仕切られ、陰極室、陽極室、複数個の脱塩室およ
び複数個の洗浄室からなる電気透析槽を使用し、脱塩室
にはオレンジ果汁を通し、陰極室、陽極室、洗浄室に
は、KOHまたはNaOHなどのアルカリ溶液を通して
陰極と陽極の間に直流を通じると、オレンジ果汁中のク
エン酸は、洗浄室から陰イオン交換膜を通して移動して
きた水酸イオンによってクエン酸イオンとなり、陰イオ
ン交換膜を通して洗浄室へ移動除去されることが報告さ
れている。しかし、この方法によると、オレンジ果汁中
のクエン酸濃度は減少するが、pH値が上昇してアルカ
リ臭が発生し、オレンジ果汁としての味覚価値は却って
低下する。
[0003] For example, as a method for reducing acidity related to sourness from citrus juice, a magazine, Fla. Stat
e. Hort. Soc. Proc. 73, 21
No. 6 (1978), an electrodialysis tank comprising a cathode compartment, an anode compartment, a plurality of desalination compartments and a plurality of washing compartments is used, in which the cathode and the anode are separated only by an anion exchange membrane. When orange juice is passed through the salt compartment and a direct current is passed between the cathode and anode through an alkaline solution such as KOH or NaOH in the cathode compartment, the anode compartment, and the washing compartment, citric acid in the orange juice is removed from the washing compartment. It has been reported that hydroxyl ions transferred through an anion exchange membrane turn into citrate ions, which are transferred to and removed from a washing chamber through an anion exchange membrane. However, according to this method, although the citric acid concentration in the orange juice is reduced, the pH value is increased and an alkaline odor is generated, and the taste value as the orange juice is rather lowered.

【0004】また、雑誌、Z. Lebensmitt
el−Technol−Verfahren,28,2
29(1977)には、陰極と陽極の間に1枚の陽イオ
ン交換膜と2枚の陰イオン交換膜を交互に設置し、陰極
室、陽極室、複数個の洗浄室、複数個の脱塩室、および
複数個の濃縮室からなる電気透析槽を使用し、脱塩室に
は温州ミカン果汁を通し、洗浄室にはKOHまたはNa
OHなどのアルカリ溶液を通し、濃縮室には電解質溶液
を通して陰極と陽極の間に直流を通じると、温州ミカン
果汁のクエン酸は洗浄室から陰イオン交換膜を通して移
動してきた水酸イオンによりクエン酸イオンとなり、陰
イオン交換膜を通して濃縮室へ移動除去され、結果とし
て温州ミカン果汁中のクエン酸濃度は減少することが報
告されている。しかし、この方法では、オレンジ果汁の
クエン酸濃度は減少するが、オレンジ果汁のpH値が上
昇してアルカリ臭が発生し、オレンジ果汁としての味覚
価値は却って低下する。
[0004] Magazines, Z.A. Lebensmitt
el-Technol-Verfahren, 28, 2
29 (1977), one cation exchange membrane and two anion exchange membranes were alternately installed between a cathode and an anode, and a cathode chamber, an anode chamber, a plurality of washing chambers, and a plurality of An electrodialysis tank consisting of a salt chamber and a plurality of concentrating chambers is used. The desalting chamber is passed with Satsuma mandarin juice, and the washing chamber is KOH or Na.
When an alkaline solution such as OH is passed through, an electrolyte solution is passed through the concentration chamber, and a direct current is passed between the cathode and the anode, the citric acid in the Satsuma mandarin juice is transferred from the washing chamber through the anion exchange membrane to the citric acid. It has been reported that the ions become ions and are removed by moving to the concentration chamber through the anion exchange membrane. As a result, the concentration of citric acid in the juice of Satsuma mandarin is reduced. However, in this method, although the citric acid concentration of the orange juice is decreased, the pH value of the orange juice is increased to generate an alkaline odor, and the taste value of the orange juice is rather reduced.

【0005】また、他の果汁、特に梅果汁については、
香気と風味の特長は生かしたまま酸味を減少させること
が望まれているにもかかわらず未だ行われていないのが
現状である。
[0005] Further, for other juices, especially plum juice,
Although it is desired to reduce acidity while keeping the characteristics of aroma and flavor, it has not yet been performed.

【0006】[0006]

【発明が解決しようとする課題】本発明は、果汁の酸度
を減少させ、香味、風味、甘味の特長は生かしたまま酸
味の調節され、アルカリ臭を感じさせない果汁を製造す
る技術を提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention provides a technique for producing juice which reduces the acidity of the juice, regulates the acidity while keeping the characteristics of flavor, flavor and sweetness alive and does not give an alkaline odor. With the goal.

【0007】[0007]

【課題を解決するための手段】本発明は、陰極と陽極の
間が陽イオン交換膜と陰イオン交換膜により交互に仕切
られ、陰極室、陽極室、複数個の脱塩室および複数個の
濃縮室からなる電気透析槽を用い、該電気透析槽の、脱
塩室にはアルカリを添加してpH値を3.20以上にし
た果汁を循環させ、濃縮室には電解質溶液を循環させて
陰極と陽極の間に直流を通じて電気透析処理を行うこと
を特徴とする果汁の酸度減少方法である。
According to the present invention, a cathode and an anode are alternately partitioned by a cation exchange membrane and an anion exchange membrane, and a cathode compartment, an anode compartment, a plurality of desalination compartments and a plurality of desalination compartments are provided. An electrodialysis tank composed of a concentration chamber is used. In the desalination chamber of the electrodialysis tank, an alkali is added to circulate fruit juice having a pH value of 3.20 or more, and an electrolyte solution is circulated in the concentration chamber. This is a method for reducing the acidity of fruit juice, which comprises performing an electrodialysis treatment by passing a direct current between a cathode and an anode.

【0008】本発明の果汁としては、柑橘類果汁、梅果
汁が挙げられる。柑橘類果汁としては、温州ミカン、ネ
ーブル、バレンシアオレンジ、グレープフルーツ、レモ
ン、ライム、ユズ、カボス、スダチなどの柑橘類から搾
汁した果汁が挙げられるが、天然柑橘類から搾汁した果
汁の水分を蒸発させ、例えば1/3〜1/10に濃縮し
た濃縮柑橘類果汁も含まれる。梅果汁とは、梅の実(核
を除く)からその成分が溶出した液体である。梅果汁の
具体例は、梅の実を破砕微粒化し酵素を作用させてペク
チン量を低下させたのち遠心分離機にかけてパルプ質を
除き、濾過して梅果汁を得る破砕濾過法によるもの:梅
の実と粉状砂糖を混合し浸透圧抽出により梅果汁を得る
抽出法によるもの:梅の実を急速冷凍して一定期間放置
したのち解凍し遠心分離や圧搾法により梅果汁を得る冷
凍搾汁法によるもの:梅の実を塩漬にして梅干しを造る
とき梅の実から溶出した梅酢:イオン交換樹脂処理また
はイオン交換膜電気透析処理などにより塩漬終了後の梅
酢を脱塩して得られた脱塩梅酢などが挙げられるが、梅
果汁または梅酢の水分を蒸発させ、例えば1/3〜1/
10に濃縮した濃縮梅果汁または濃縮梅酢も含まれる。
The juice of the present invention includes citrus juice and plum juice. Examples of citrus juice include juices squeezed from citrus fruits such as Satsuma mandarin orange, navel, Valencia orange, grapefruit, lemon, lime, yuzu, kabosu, sudachi, etc. For example, concentrated citrus juice concentrated to 1/3 to 1/10 is also included. Plum juice is a liquid in which the components are eluted from plum fruits (excluding nuclei). Specific examples of plum juice are obtained by crushing and filtering plum nuts to reduce the amount of pectin by crushing and pulverizing ume nuts, and then removing the pulp using a centrifuge, followed by filtration to obtain plum juice. Extraction method by mixing fruit and powdered sugar to obtain plum juice by osmotic pressure extraction: Frozen juice method in which plum fruit is rapidly frozen, left for a certain period of time, then thawed and centrifuged or pressed to obtain plum juice. According to: Plum vinegar eluted from ume nuts when making ume dried by salting plum fruits: Desalted ume vinegar after completion of salting by ion exchange resin treatment or ion exchange membrane electrodialysis treatment Desalted plum vinegar and the like can be mentioned, but the moisture of plum juice or plum vinegar is evaporated, for example, 1/3 to 1 /
The concentrated plum juice or concentrated plum vinegar concentrated to 10 is also included.

【0009】本発明において酸度とは、果汁に含まれる
酸性成分の濃度を意味し酸味に関係する因子である。一
般に、酸度が大きいときは強い酸味を感じ、酸度が小さ
いときは弱い酸味を感ずる。果汁の酸味はそれらのなか
に含まれる有機酸、特にクエン酸濃度によるところが大
きい。本発明において、pH値とは、25℃における果
汁の水素イオン濃度の負の常用対数値である。
In the present invention, the acidity means the concentration of an acidic component contained in fruit juice, and is a factor relating to acidity. Generally, when the acidity is high, a strong acidity is felt, and when the acidity is low, a weak acidity is felt. The sourness of fruit juice largely depends on the concentration of organic acids contained therein, especially citric acid. In the present invention, the pH value is a negative logarithmic value of the hydrogen ion concentration of fruit juice at 25 ° C.

【0010】以下、図面を用いて本発明の方法を説明す
る。図1は、本発明の実施に使用される装置の概略図で
ある。図1において、11はイオン交換膜電気透析槽で
ある。電気透析槽11は、陰極12と陽極13の間が陽
イオン交換膜14と陰イオン交換膜15により交互に仕
切られ、陰極室16、陽極室17、複数個の脱塩室1
8、複数個の濃縮室19が形成されている。20は脱塩
液タンク、21はアルカリ添加ライン、22は酸添加ラ
イン、23は攪拌機である。24は濃縮液タンク、25
は水供給ライン、26は濃縮液排出ラインである。
The method of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram of an apparatus used to carry out the present invention. In FIG. 1, reference numeral 11 denotes an ion exchange membrane electrodialysis tank. In the electrodialysis tank 11, a cathode 12 and an anode 13 are alternately partitioned by a cation exchange membrane 14 and an anion exchange membrane 15, and a cathode chamber 16, an anode chamber 17, and a plurality of desalination chambers 1 are provided.
8. A plurality of concentration chambers 19 are formed. Reference numeral 20 denotes a desalting solution tank, 21 denotes an alkali addition line, 22 denotes an acid addition line, and 23 denotes a stirrer. 24 is a concentrate tank, 25
Is a water supply line, and 26 is a concentrate discharge line.

【0011】通常の果汁、例えばpH値が1.20〜
3.00の柑橘類、梅などの果汁を図1の脱塩タンク2
0に満たし、攪拌機23で攪拌してアルカリ添加ライン
21よりアルカリを添加してpH値を3.20以上に調
整する。アルカリ添加により、果汁中には有機酸以外に
有機酸イオンとアルカリイオンが存在するようになる。
Normal fruit juice, for example, having a pH value of 1.20
Fruit juice such as citrus fruits and plums of 3.00 is desalted in tank 2 of Fig. 1.
Then, the pH value is adjusted to 3.20 or more by adding alkali through the alkali addition line 21 while stirring with a stirrer 23. By the addition of the alkali, organic acid ions and alkali ions other than the organic acid are present in the fruit juice.

【0012】このpH値が3.20以上の果汁を、脱塩
液循環ポンプ27、脱塩液循環パイプライン28、29
を用いて電気透析槽11の脱塩室18に循環させる。濃
縮液タンク24には、最初硫酸ナトリウムや食塩のよう
な電解質溶液を満たし、循環ポンプ30、濃縮液循環パ
イプライン31、32を用いて電気透析槽11の陰極室
16、陽極室17および濃縮室19に循環させる。
The fruit juice having a pH value of 3.20 or more is supplied to a desalting solution circulating pump 27 and a desalting solution circulating pipeline 28, 29.
Is circulated through the desalting chamber 18 of the electrodialysis tank 11 using The concentrate tank 24 is first filled with an electrolyte solution such as sodium sulfate or salt, and the circulating pump 30 and the concentrate circulating pipelines 31 and 32 are used to store the cathode chamber 16, the anode chamber 17 and the concentration chamber of the electrodialysis tank 11. Circulate to 19.

【0013】かかる状態で電気透析槽11の陰極12と
陽極13の間に直流を通ずると、果汁のなかの有機酸イ
オンは脱塩室18から陰イオン交換膜15を通して陽極
室17および濃縮室19へ移動除去される。アルカリイ
オンは、脱塩室18から陽イオン交換膜14を通して
極室16および濃縮室19へ移動除去される。濃縮液タ
ンク24には水供給ライン25より水が供給され、有機
酸イオンとアルカリイオンを含んだ濃縮液が濃縮液排出
ライン26より排出される。
In this state, when a direct current is passed between the cathode 12 and the anode 13 of the electrodialysis tank 11, the organic acid ions in the fruit juice pass from the desalting chamber 18 through the anion exchange membrane 15 to the anode.
It is moved to and removed from the chamber 17 and the concentration chamber 19. Alkali ions, anions through cation exchange membrane 14 from the desalting chamber 18
It is moved to and removed from the pole chamber 16 and the concentration chamber 19. Water is supplied to the concentrate tank 24 from a water supply line 25, and a concentrate containing organic acid ions and alkali ions is discharged from a concentrate discharge line 26.

【0014】本発明においては、前記電気透析処理にお
ける果汁のpH値は3.20以上にすることが必要であ
る。pH値が3.20以上では、果汁に含まれる有機酸
の大半は有機酸イオンとなり電気透析により除去され
る。pH値が3.20未満では、有機酸から生ずる有機
酸イオンの比率は小さく電気透析による除去は困難であ
る。pH値の上限はいくら高くてもよいが、pH値が高
くなるとアルカリイオン濃度が増加し、これの電気透析
除去に時間がかかるので、上限は6.0程度にするのが
よい。好ましいpH値は3.50〜4.50である。
In the present invention, the pH value of the juice in the electrodialysis treatment must be 3.20 or more. When the pH value is 3.20 or more, most of the organic acids contained in the juice become organic acid ions and are removed by electrodialysis. When the pH value is less than 3.20, the ratio of organic acid ions generated from the organic acid is small, and removal by electrodialysis is difficult. The upper limit of the pH value may be as high as possible, but as the pH value increases, the concentration of alkali ions increases, and it takes time to remove this by electrodialysis. Therefore, the upper limit is preferably about 6.0. Preferred pH values are between 3.50 and 4.50.

【0015】前記電気透析処理において、果汁に継続し
てアルカリを添加しない場合、果汁のpH値は徐々に低
下する。pH値が3.00〜1.20に低下したとき果
汁中の有機酸イオンは殆ど除去されており電気透析処理
は終了とする。
In the electrodialysis treatment, when no alkali is continuously added to the juice, the pH value of the juice gradually decreases. When the pH value has dropped to 3.00 to 1.20, organic acid ions in the fruit juice have been almost completely removed, and the electrodialysis treatment is completed.

【0016】アルカリを添加してpH値を3.20以上
にする果汁の電気透析処理において、処理されている果
汁中の有機酸と有機酸イオンの合計は既に目標の濃度ま
で減少しているのにpH値が目標の値より高い場合、処
理されている果汁に酸を添加してpH値を、例えば3.
20以下のある値まで下げると、果汁中には有機酸イオ
ンと水素イオンが結合した有機酸、酸添加で生じた無機
酸陰イオンおよび最初のアルカリ添加の残存物質である
アルカリイオンが共存するようになる。
[0016] In the electrodialysis treatment of fruit juice to increase the pH value to 3.20 or more by adding an alkali, the total of organic acids and organic acid ions in the fruit juice being treated has already been reduced to the target concentration. If the pH value is higher than the target value, acid is added to the juice being treated to increase the pH value, for example, to 3.
When the value is lowered to a certain value of 20 or less, the fruit juice contains an organic acid in which an organic acid ion and a hydrogen ion are bonded, an inorganic acid anion generated by the addition of an acid, and an alkali ion which is a residual substance of the first alkali addition. become.

【0017】この酸添加果汁について電気透析処理を続
行すると、無機酸陰イオンは脱塩室18から陰イオン交
換膜15を通して陽極室17および濃縮室19へ移動除
去される。アルカリイオンは脱塩室18から陽イオン交
換膜14を通して陰極室16および濃縮室19へ移動除
去され、最後に有機酸濃度が減少しpH値が所定値にな
った果汁が得られる。濃縮液タンク24からは無機酸陰
イオンとアルカリイオンを含んだ濃縮液が濃縮液排出ラ
イン26より排出される。
When the electrodialysis treatment is continued on the acid-added fruit juice, the inorganic acid anions are removed from the desalting chamber 18 through the anion exchange membrane 15 to the anode chamber 17 and the concentrating chamber 19. The alkali ions move from the desalting chamber 18 through the cation exchange membrane 14 to the cathode chamber 16 and the concentrating chamber 19 and are removed. Finally, fruit juice having a reduced organic acid concentration and a predetermined pH value is obtained. From the concentrate tank 24, a concentrate containing inorganic acid anions and alkali ions is discharged from a concentrate discharge line 26.

【0018】電気透析槽11の陰極12の材料として
は、鉄、ニッケル、ステンレススチールなどが、陽極1
3の材料としては、黒鉛、白金、白金メッキチタンなど
が用いられる。電気透析槽11の本体および配管の材料
としてはポリ塩化ビニルが好ましい。
The material of the cathode 12 of the electrodialysis tank 11 is iron, nickel, stainless steel or the like.
As the material of No. 3, graphite, platinum, platinum-plated titanium, or the like is used. As a material of the main body and the piping of the electrodialysis tank 11, polyvinyl chloride is preferable.

【0019】電気透析処理における電気透析槽の陰極と
陽極間の電圧は、陰イオン交換膜と陽イオン交換膜1対
当たりの電圧が0.5〜2.0Vになるように、またイ
オン交換膜に流れる電流は、イオン交換膜1dm2 当た
り0.1〜3Aになるよに調節するのが望ましい。濃縮
液タンクに供給する水の量は、濃縮液タンクの電解質濃
度が1.0〜10.0重量%になるように調節するのが
好ましい。
In the electrodialysis treatment, the voltage between the cathode and the anode of the electrodialysis tank is set so that the voltage per pair of anion exchange membrane and cation exchange membrane is 0.5 to 2.0 V, and the ion exchange membrane is used. Is preferably adjusted to be 0.1 to 3 A per 1 dm 2 of the ion exchange membrane. The amount of water supplied to the concentrate tank is preferably adjusted so that the concentration of the electrolyte in the concentrate tank becomes 1.0 to 10.0% by weight.

【0020】本発明の果汁に添加するアルカリとして
は、食添用水酸化カリウムまたは食添用水酸化ナトリウ
ムが好ましい。アルカリ添加の際は、発熱が起こるので
アルカリは徐々に添加するか、冷却しつつ添加すること
が必要である。また、酸を使用する場合、酸としては食
添用塩酸または食添用リン酸が好ましい。
The alkali added to the fruit juice of the present invention is preferably potassium hydroxide for food supplementation or sodium hydroxide for food supplementation. When the alkali is added, heat is generated, so it is necessary to add the alkali gradually or with cooling. When an acid is used, the acid is preferably hydrochloric acid for food addition or phosphoric acid for food addition.

【0021】本発明の方法によると、糖分、アミノ態チ
ッソ、灰分、ビタミンCなどの濃度およびpH値に変化
はなく、有機酸のみが任意の濃度に減少した果汁が製造
される。本発明の方法によると、酸味が緩和され、香
気、風味、酸味の揃った非常に優れた果汁が得られる。
また、果汁からアルカリ臭は発生しない。本発明の方法
によって製造される果汁の用途は、今後一段と拡大する
ものと考えられる。
According to the method of the present invention, there is no change in the concentration and the pH value of sugar, amino-type nitrogen, ash, vitamin C, etc., and fruit juice in which only organic acids are reduced to an arbitrary concentration is produced. ADVANTAGE OF THE INVENTION According to the method of this invention, sourness is relieved and very excellent fruit juice with aroma, flavor, and acidity is obtained.
Also, no alkaline odor is generated from the juice. It is believed that the use of the juice produced by the method of the present invention will further expand in the future.

【0022】[0022]

【実施例】以下実施例をあげて本発明を説明する。本発
明がこれに限定されないのはもちろんである。なお、実
施例中、pH値は果汁の25℃における値であり、クエ
ン酸濃度はクエン酸イオン濃度も含んだ値である。
The present invention will be described below with reference to examples. Of course, the present invention is not limited to this. In the examples, the pH value is a value of the juice at 25 ° C., and the citric acid concentration is a value including the citrate ion concentration.

【0023】実施例1 表1A欄に示す組成の天然レモン果汁2.0リットル
を、図1に示す脱塩液タンク20に満たし、水酸化ナト
リウムを添加して表1のB欄に示す組成の液にした。こ
の液を図1の11に示すような、ステンレススチール陰
極12と白金メッキチタン陽極13の間が20枚の強酸
性型陽イオン交換膜(1枚の膜有効面積=2.0dm2)
と20枚の強塩基型陰イオン交換膜(1枚の膜有効面積
=2.0dm2)により交互に仕切られたイオン交換膜電
気透析槽の脱塩室18に循環させた。濃縮液タンク24
には50g/lの塩化ナトリウム溶液を満たして陰極室
16、陽極室17および濃縮室19に循環させ、陰極1
2と陽極13の間に1.0Aの直流を通じて電気透析処
理を行った。電気透析開始と同時に、濃縮液タンク24
には電解質の濃度が約50g/lになるように水を供給
し、濃縮液排出ライン26より排出させた。8.0時間
の電気透析処理において、槽電圧およびレモン果汁の組
成は表1B欄からF欄に示すように変化した。また、官
能試験の結果、電気透析処理終了後のレモン果汁の酸味
はかなり減少していた。
EXAMPLE 1 2.0 liters of natural lemon juice having the composition shown in Table 1A is filled in a desalting solution tank 20 shown in FIG. Liquid. As shown in FIG. 1, this solution was applied to a stainless steel cathode 12 and a platinum-plated titanium anode 13 between 20 strongly acidic cation exchange membranes (effective membrane area of one sheet = 2.0 dm 2 ) as shown in FIG.
And a strong base type anion exchange membrane (effective membrane area of one sheet = 2.0 dm 2 ). Concentrate tank 24
Is filled with 50 g / l sodium chloride solution and circulated through the cathode chamber 16, the anode chamber 17 and the concentration chamber 19,
Electrodialysis treatment was performed by passing a 1.0 A direct current between the anode 2 and the anode 13. Concentrate tank 24
Was supplied with water so that the concentration of the electrolyte became about 50 g / l, and was discharged from the concentrated liquid discharge line 26. In the electrodialysis treatment for 8.0 hours, the cell voltage and the composition of the lemon juice changed from the column in Table 1B to the column F. As a result of the sensory test, the acidity of the lemon juice after the electrodialysis treatment was significantly reduced.

【0024】実施例2 実施例1で使用したと同一の天然レモン果汁2.0リッ
トルを脱塩液タンク20に満たし、これに水酸化ナトリ
ウムを添加して実施例1と同じ組成(B欄)の液にし、
この液を実施例1と同一のイオン交換膜電気透析槽の脱
塩室に循環させ、実施例1と同一の条件で2.0時間電
気透析処理を施したところ、槽電圧およびレモン果汁の
組成は表1C欄に示すようになった。この液に35%の
塩酸を添加して表1D欄に示す組成の液とし、実施例1
と同一の条件で電気透析の総時間が4.0時間になるま
で電気透析処理を続けたところ、槽電圧およびレモン果
汁の組成は表1E欄に示すように変化した。また、官能
試験の結果、電気透析処理終了後のレモン果汁の酸味は
かなり減少していた。
Example 2 The desalted solution tank 20 was filled with 2.0 liters of the same natural lemon juice as used in Example 1, and sodium hydroxide was added thereto to obtain the same composition as in Example 1 (column B). Into the liquid
This solution was circulated through the desalting chamber of the same ion exchange membrane electrodialysis tank as in Example 1, and subjected to electrodialysis treatment for 2.0 hours under the same conditions as in Example 1. The cell voltage and the composition of lemon juice Was as shown in Table 1C. To this solution was added 35% hydrochloric acid to obtain a solution having the composition shown in Table 1D.
The electrodialysis treatment was continued under the same conditions until the total electrodialysis time reached 4.0 hours. As a result, the cell voltage and the composition of the lemon juice changed as shown in Table 1E. As a result of the sensory test, the acidity of the lemon juice after the electrodialysis treatment was significantly reduced.

【0025】比較例1 実施例1と同じ天然レモン果汁2.0リットルを実施例
1と同様に脱塩液タンク20に満たし、この液を実施例
1と同一のイオン交換膜電気透析槽の脱塩室に循環さ
せ、実施例1と同一の条件で8.0時間電気透析処理を
施したところ、槽電圧およびレモン果汁の組成は表1B
欄からF欄に示すように変化した。また、官能試験の結
果、電気透析処理終了後のレモン果汁の酸味は、原液の
それと変化は認められなかった。
Comparative Example 1 The same desalting solution tank 20 as in Example 1 was filled with 2.0 liters of the same natural lemon juice as in Example 1, and this solution was drained from the same ion exchange membrane electrodialysis tank as in Example 1. When circulated in a salt room and subjected to electrodialysis treatment under the same conditions as in Example 1 for 8.0 hours, the cell voltage and the composition of lemon juice were as shown in Table 1B.
It changed from the column to the column F. As a result of the sensory test, the acidity of the lemon juice after the electrodialysis treatment was not changed from that of the undiluted solution.

【0026】[0026]

【表1】 [Table 1]

【0027】実施例1および実施例2において、電気透
析処理後のレモン果汁は原液に比べてクエン酸濃度は小
さく酸味もかなり減少した。糖分、アミノ態チッソ濃度
に減少は見られなかった。比較例1から明らかなとお
り、レモン果汁はそのまま電気透析処理を行ってもクエ
ン酸濃度は減少せず酸味も減少しない。
In Examples 1 and 2, the lemon juice after the electrodialysis treatment had a lower citric acid concentration and a considerably lower acidity than the undiluted solution. No decrease was observed in the sugar and amino nitrogen concentrations. As is clear from Comparative Example 1, even if the lemon juice is subjected to electrodialysis treatment as it is, the citric acid concentration does not decrease and the sourness does not decrease.

【0028】実施例3 表2A欄に示す組成の1/3濃縮レモン果汁2.0リッ
トルを、図1に示す脱塩液タンク20に満たし、水酸化
ナトリウムを添加して表2B欄に示す組成の液にした。
この液を実施例1で使用したのと同一のイオン交換膜電
気透析槽の脱塩室に循環させ、実施例1と同一の条件で
16.0時間電気透析処理を施したところ、槽電圧およ
び濃縮レモン果汁組成は表2F欄に示すように変化し
た。また、官能試験の結果、電気透析処理終了後の濃縮
レモン果汁の酸味はかなり減少していた。
Example 3 2.0 L of 1/3 concentrated lemon juice having the composition shown in Table 2A was filled in the desalting solution tank 20 shown in FIG. 1, sodium hydroxide was added thereto, and the composition shown in Table 2B was obtained. Solution.
This solution was circulated in the same desalting chamber of the same ion-exchange membrane electrodialysis tank as used in Example 1 under the same conditions as in Example 1.
When the electrodialysis treatment was performed for 16.0 hours, the cell voltage and the concentrated lemon juice composition changed as shown in Table 2F. As a result of the sensory test, the acidity of the concentrated lemon juice after the electrodialysis treatment was significantly reduced.

【0029】実施例4 実施例3で使用したのと同一の1/3濃縮レモン果汁
2.0リットルを脱塩液タンク20に満たし、これに水
酸化ナトリウムを添加して実施例3と同じ組成(B欄)
の液にし、この液を実施例1と同一のイオン交換膜電気
透析槽の脱塩室に循環させ、実施例1と同一の条件で
5.0時間電気透析処理を施したところ、槽電圧および
レモン果汁の組成は表2C欄に示すようになった。この
液に35%の塩酸を添加して表2D欄に示す組成の液と
し、実施例1と同一の条件で電気透析の総時間が8.0
時間になるまで電気透析処理を続けたところ、槽電圧お
よびレモン果汁の組成は表2E欄に示すように変化し
た。また、官能試験の結果、電気透析処理終了後の濃縮
レモン果汁の酸味はかなり減少していた。
Example 4 The desalted solution tank 20 was filled with 2.0 liters of the same 1/3 concentrated lemon juice as used in Example 3, and sodium hydroxide was added thereto to obtain the same composition as in Example 3. (Column B)
This solution was circulated to the desalting chamber of the same ion exchange membrane electrodialysis tank as in Example 1, and subjected to electrodialysis treatment under the same conditions as in Example 1 for 5.0 hours. The composition of the lemon juice was as shown in Table 2C. To this solution was added 35% hydrochloric acid to obtain a solution having the composition shown in Table 2D, and the total time of electrodialysis was 8.0 under the same conditions as in Example 1.
When the electrodialysis treatment was continued until the time reached, the cell voltage and the composition of lemon juice changed as shown in Table 2E. As a result of the sensory test, the acidity of the concentrated lemon juice after the electrodialysis treatment was significantly reduced.

【0030】比較例2 実施例3で使用したのと同一の1/3濃縮レモン果汁
2.0リットルを実施例3と同様に脱塩液タンク20に
満たし、この液を実施例3と同一のイオン交換膜電気透
析槽の脱塩室に循環させ、実施例3と同一の条件で1
6.0時間電気透析処理を施したところ、槽電圧および
レモン果汁の組成は表2B欄からF欄に示すように変化
した。また、官能試験の結果、電気透析処理終了後の濃
縮レモン果汁の酸味に変化は認められなかった。
Comparative Example 2 2.0 liters of the same 1/3 concentrated lemon juice used in Example 3 was filled in the desalting solution tank 20 in the same manner as in Example 3, and the same solution as in Example 3 was used. Circulating in the desalting chamber of the ion exchange membrane electrodialysis tank,
When the electrodialysis treatment was performed for 6.0 hours, the cell voltage and the composition of the lemon juice changed from the column in Table 2B to the column in Table F. As a result of the sensory test, no change was found in the acidity of the concentrated lemon juice after the electrodialysis treatment.

【0031】[0031]

【表2】 [Table 2]

【0032】実施例3および実施例4において、電気透
析処理後の濃縮レモン果汁は原液に比べてクエン酸濃度
は小さく酸味もかなり減少した。糖分、アミノ態チッソ
濃度に減少は見られなかった。比較例2から明らかなと
おり、濃縮レモン果汁はそのまま電気透析処理を行って
もクエン酸濃度は減少せず酸味も減少しない。
In Examples 3 and 4, the concentrated lemon juice after the electrodialysis treatment had a lower citric acid concentration and a considerably lower acidity than the undiluted solution. No decrease was observed in the sugar and amino nitrogen concentrations. As is clear from Comparative Example 2, even if the concentrated lemon juice is subjected to the electrodialysis treatment as it is, the citric acid concentration does not decrease and the sourness does not decrease.

【0033】実施例5 表3A欄に示す組成の天然梅果汁2.0リットルを図1
に示す脱塩液タンク20に満たし、水酸化ナトリウムを
添加して表3B欄に示す組成の液にした。この液を実施
例1で使用したのと同一のイオン交換膜電気透析槽の脱
塩室18に循環させ、実施例1と同一の条件で6.0時
間電気透析処理を施したところ、槽電圧および梅果汁の
組成は表3F欄に示すように変化した。また、官能試験
の結果、電気透析処理終了後の梅果汁の酸味はかなり減
少していた。
Example 5 2.0 liters of natural plum juice having the composition shown in column 3A of FIG.
And the sodium hydroxide was added to obtain a liquid having the composition shown in Table 3B. This solution was circulated to the desalting chamber 18 of the same ion exchange membrane electrodialysis tank used in Example 1, and subjected to electrodialysis treatment under the same conditions as in Example 1 for 6.0 hours. And the composition of plum juice changed as shown in Table 3F. In addition, as a result of the sensory test, the acidity of plum juice after the electrodialysis treatment was considerably reduced.

【0034】実施例6 実施例5で使用したのと同一の天然梅果汁2.0リット
ルを脱塩液タンク20に満たし、これに水酸化ナトリウ
ムを添加して実施例5と同じ組成(B欄)の液にし、こ
の液を実施例1と同一のイオン交換膜電気透析槽の脱塩
室に循環させ、実施例1と同一の条件で2.0時間電気
透析処理を施したところ、槽電圧および梅果汁の組成は
表3C欄に示すようになった。この液に35%の塩酸を
添加して表3D欄に示す組成の液とし、実施例1と同一
の条件で電気透析の総時間が3.0時間になるまで電気
透析処理を続けたところ、槽電圧および梅果汁の組成は
表3E欄に示すように変化した。また、官能試験の結
果、電気透析処理終了後の梅果汁の酸味はかなり減少し
ていた。
Example 6 A desalted solution tank 20 was filled with 2.0 liters of the same natural plum juice as used in Example 5, and sodium hydroxide was added thereto to obtain the same composition as in Example 5 (column B). ), And the solution was circulated through the desalting chamber of the same ion exchange membrane electrodialysis tank as in Example 1, and subjected to electrodialysis treatment under the same conditions as in Example 1 for 2.0 hours. The composition of plum juice was as shown in Table 3C. To this solution was added 35% hydrochloric acid to obtain a solution having the composition shown in Table 3D, and the electrodialysis treatment was continued under the same conditions as in Example 1 until the total electrodialysis time was 3.0 hours. The cell voltage and the composition of plum juice were changed as shown in Table 3E. In addition, as a result of the sensory test, the acidity of plum juice after the electrodialysis treatment was considerably reduced.

【0035】比較例3 実施例5で使用したのと同一の天然梅果汁2.0リット
ルを実施例5と同様に脱塩液タンク20に満たし、この
液を実施例5と同一のイオン交換膜電気透析槽の脱塩室
に循環させ、実施例5と同一の条件で6.0時間電気透
析処理を施したところ、槽電圧および梅果汁の組成は表
3B欄からF欄に示すように変化した。また、官能試験
の結果、電気透析処理終了後の梅果汁の酸味に変化は認
められなかった。
Comparative Example 3 The same 2.0-liter natural plum juice as used in Example 5 was filled in the desalting solution tank 20 in the same manner as in Example 5, and this solution was filled with the same ion exchange membrane as in Example 5. When circulated through the desalting chamber of the electrodialysis tank and subjected to electrodialysis treatment under the same conditions as in Example 5 for 6.0 hours, the cell voltage and the composition of plum juice changed as shown in Table 3B from Column F to Column F. did. As a result of the sensory test, no change was observed in the acidity of plum juice after the completion of the electrodialysis treatment.

【0036】[0036]

【表3】 [Table 3]

【0037】実施例5および実施例6において、電気透
析処理後の梅果汁は原液に比べてクエン酸濃度は小さく
酸味もかなり減少した。糖分、アミノ態チッソ濃度に減
少は見られなかった。比較例3から明らかなとおり、天
然梅果汁はそのまま電気透析処理を行ってもクエン酸濃
度は減少せず、酸味も減少しない。
In Examples 5 and 6, the plum juice after the electrodialysis treatment had a lower citric acid concentration and a much lower acidity than the undiluted solution. No decrease was observed in the sugar and amino nitrogen concentrations. As is clear from Comparative Example 3, even if the natural plum juice is subjected to electrodialysis treatment as it is, the citric acid concentration does not decrease and the sourness does not decrease.

【0038】実施例7 天然梅酢をイオン交換樹脂処理により脱塩し蒸発缶で水
を蒸発させて製造した表4A欄に示す1/5濃縮梅酢
2.0リットルを図1に示す脱塩液タンク20に満た
し、水酸化ナトリウムを添加して表4B欄に示す組成の
液にした。この液を実施例1で使用したのと同一のイオ
ン交換膜電気透析槽の脱塩室18に循環させ、実施例1
と同一の条件で17.0時間電気透析処理を施したとこ
ろ、槽電圧および濃縮梅酢の組成は表4F欄に示すよう
に変化した。また、官能試験の結果、電気透析処理終了
後の濃縮梅果汁の酸味はかなり減少していた。
EXAMPLE 7 2.0 liters of 1/5 concentrated ume vinegar shown in Table 4A was prepared by desalinating natural ume vinegar by ion-exchange resin treatment and evaporating water with an evaporator. 20 and sodium hydroxide was added to give a solution having the composition shown in Table 4B. This solution was circulated to the desalting chamber 18 of the same ion-exchange membrane electrodialysis tank as used in Example 1.
When the electrodialysis treatment was performed for 17.0 hours under the same conditions as those described above, the cell voltage and the composition of the concentrated ume vinegar changed as shown in Table 4F. As a result of the sensory test, the acidity of the concentrated plum juice after the electrodialysis treatment was considerably reduced.

【0039】実施例8 実施例7で使用したのと同一の1/5濃縮梅酢2.0リ
ットルを脱塩液タンク20に満たし、これに水酸化ナト
リウムを添加して実施例7と同じ組成(B欄)の液に
し、この液を実施例1と同一のイオン交換膜電気透析槽
の脱塩室に循環させ、実施例1と同一の条件で6.0時
間電気透析処理を施したところ、槽電圧および梅果汁の
組成は表4C欄に示すようになった。この液に35%の
塩酸を添加して表4D欄に示す組成の液とし、実施例1
と同一の条件で電気透析の総時間が8.0時間になるま
で電気透析処理を続けたところ、槽電圧および濃縮梅酢
の組成は表4E欄に示すように変化した。また、官能試
験の結果、電気透析処理終了後の濃縮梅果汁の酸味はか
なり減少していた。
Example 8 The desalting solution tank 20 was filled with 2.0 liters of the same 1/5 concentrated ume vinegar as used in Example 7, and sodium hydroxide was added thereto to obtain the same composition as in Example 7 ( (B column), and the solution was circulated to the desalting chamber of the same ion exchange membrane electrodialysis tank as in Example 1, and subjected to electrodialysis treatment under the same conditions as in Example 1 for 6.0 hours. The cell voltage and the composition of plum juice were as shown in Table 4C. To this solution was added 35% hydrochloric acid to obtain a solution having the composition shown in column 4D of Table 4.
The electrodialysis treatment was continued under the same conditions until the total electrodialysis time reached 8.0 hours. As a result, the cell voltage and the composition of the concentrated ume vinegar changed as shown in Table 4E. As a result of the sensory test, the acidity of the concentrated plum juice after the electrodialysis treatment was considerably reduced.

【0040】比較例4 実施例7で使用したのと同一の1/5濃縮梅酢2.0リ
ットルを実施例7と同様に脱塩液タンク20に満たし、
この液を実施例7と同一のイオン交換膜電気透析槽の脱
塩室に循環させ、実施例7と同一の条件で17.0時間
電気透析処理を施したところ、槽電圧および濃縮梅酢の
組成は表4B欄からF欄に示すように変化した。また、
官能試験の結果、電気透析処理終了後の濃縮梅果汁の酸
味に変化は認められなかった。
Comparative Example 4 2.0 liters of the same 1/5 concentrated ume vinegar used in Example 7 was filled in the desalting solution tank 20 in the same manner as in Example 7,
This solution was circulated through the same desalting chamber of the same ion exchange membrane electrodialysis tank as in Example 7, and subjected to electrodialysis treatment under the same conditions as in Example 7, for 17.0 hours. Changed from the column in Table 4B to the column F. Also,
As a result of the sensory test, no change was observed in the acidity of the concentrated plum juice after the completion of the electrodialysis treatment.

【0041】[0041]

【表4】 [Table 4]

【0042】実施例7および実施例8において、電気透
析処理後の濃縮梅酢は原液に比べてクエン酸濃度は小さ
く酸味もかなり減少した。糖分、アミノ態チッソ濃度に
減少は見られなかった。比較例4から明らかなとおり、
濃縮梅酢はそのまま電気透析処理を行ってもクエン酸濃
度は減少せず、酸味も減少しない。
In Examples 7 and 8, the concentration of citric acid in the concentrated ume vinegar after the electrodialysis treatment was smaller than that of the undiluted solution, and the acidity was considerably reduced. No decrease was observed in the sugar and amino nitrogen concentrations. As is clear from Comparative Example 4,
Even if the concentrated ume vinegar is subjected to electrodialysis treatment as it is, the citric acid concentration does not decrease and the sourness does not decrease.

【0043】[0043]

【発明の効果】本発明によれば、アルカリ臭がなく、有
機酸濃度のみが減少することにより、酸味が緩和され、
香気、風味に優れた果汁を得ることができる。
According to the present invention, there is no alkali odor and only the concentration of organic acid is reduced, so that the acidity is reduced.
Fruit juice with excellent aroma and flavor can be obtained.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明に使用されるイオン交換膜電気透析装置
の概略図である。
FIG. 1 is a schematic diagram of an ion exchange membrane electrodialysis device used in the present invention.

【符号の説明】[Explanation of symbols]

11 イオン交換膜電気透析槽 20 脱塩液タンク 24 濃縮液タンク 11 Ion exchange membrane electrodialysis tank 20 Desalinated liquid tank 24 Concentrated liquid tank

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 陰極と陽極の間が陽イオン交換膜と陰イ
オン交換膜により交互に仕切られ、陰極室、陽極室、複
数個の脱塩室および複数個の濃縮室からなる電気透析槽
を用い、該電気透析槽の、脱塩室にはアルカリを添加し
てpH値を3.20以上にした果汁を循環させ、濃縮室
には電解質溶液を循環させて陰極と陽極の間に直流を通
じて電気透析処理を行うことを特徴とする果汁の酸度減
少方法。
1. An electrodialysis tank comprising a cathode chamber, an anode chamber, a plurality of desalination chambers, and a plurality of concentration chambers, wherein a cathode and an anode are alternately partitioned by a cation exchange membrane and an anion exchange membrane. In the electrodialysis tank, an alkaline solution was added to the desalting chamber to circulate fruit juice having a pH value of 3.20 or more, and an electrolyte solution was circulated to the concentrating chamber to pass a direct current between the cathode and the anode. A method for reducing acidity of fruit juice, which comprises performing an electrodialysis treatment.
【請求項2】 果汁のpH値が3.00〜1.20に減
少するまで電気透析処理を続ける請求項1記載の果汁の
酸度減少方法。
2. The method for reducing acidity of juice according to claim 1, wherein the electrodialysis treatment is continued until the pH value of the juice decreases to 3.0 to 1.20.
【請求項3】 電気透析処理の中途において、果汁に酸
を添加して電気透析処理を続ける請求項1記載の果汁の
酸度減少方法。
3. The method according to claim 1, wherein an acid is added to the juice during the electrodialysis treatment to continue the electrodialysis treatment.
【請求項4】 果汁が柑橘類果汁である請求項1記載の
果汁の酸度減少方法。
4. The method according to claim 1, wherein the juice is a citrus juice.
【請求項5】 果汁が梅果汁である請求項1記載の果汁
の酸度減少方法。
5. The method of reducing juice acidity according to claim 1, wherein the juice is plum juice.
JP3152170A 1991-05-29 1991-05-29 How to reduce juice acidity Expired - Fee Related JP2612785B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3152170A JP2612785B2 (en) 1991-05-29 1991-05-29 How to reduce juice acidity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3152170A JP2612785B2 (en) 1991-05-29 1991-05-29 How to reduce juice acidity

Publications (2)

Publication Number Publication Date
JPH04349874A JPH04349874A (en) 1992-12-04
JP2612785B2 true JP2612785B2 (en) 1997-05-21

Family

ID=15534571

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3152170A Expired - Fee Related JP2612785B2 (en) 1991-05-29 1991-05-29 How to reduce juice acidity

Country Status (1)

Country Link
JP (1) JP2612785B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010193866A (en) * 2009-02-27 2010-09-09 San Akuteisu:Kk Method for reducing sodium concentration in plum juice
CN114105264A (en) * 2021-11-26 2022-03-01 青岛科技大学 Pretreatment device and method for improving pollution resistance and flux increase of pressure membrane

Also Published As

Publication number Publication date
JPH04349874A (en) 1992-12-04

Similar Documents

Publication Publication Date Title
JPS61111673A (en) Production of asceptic concentrated juice having improved flavor and reduced in acidity
KR100944538B1 (en) Method for producing high hardness mineral water containing mineral using sea water
EA002226B1 (en) Method for producing sugar syrup from sugar-containing raw materials
AU2004212401B2 (en) Method of desalting
JP2612785B2 (en) How to reduce juice acidity
US4857343A (en) Process for the low temperature pasteurization of liquid comestibles
EP0049497A2 (en) Electrodialysis of food products
RU2192749C2 (en) Method for demineralization of milk products and their derivatives (versions)
JPS6024696B2 (en) Method for producing citrus fruit drinks
JP2018014978A (en) As mineral component magnesium and calcium-containing soft drink
CN101481167B (en) Preparation of mineral substance composition
JP3270732B2 (en) Method for reducing sodium concentration in plum juice and method for producing plum juice beverage
JP3325855B2 (en) Mineral water obtained by electrolyzing deep ocean water and health drink containing it
JP3692302B2 (en) Method for producing low sodium concentration plum juice and method for producing plum juice drink
PL187893B1 (en) Method of demineralising sweet whey
JP2705813B2 (en) Activated carbon treatment method
JP3977139B2 (en) Production methods for non-suspension plum juice and non-swelling / non-foaming plum extract
US3325389A (en) Process for pretreatment of whey to increase demineralization rate
JP3765716B2 (en) Method for producing concentrated plum juice for beverages
JP2010193866A (en) Method for reducing sodium concentration in plum juice
RU2010861C1 (en) Process for producing diffusion juice from sugar beet
JP2002114512A (en) Method for producing brine, multipurpose salt and multipurpose bittern using brine obtained by the same and method for producing these
JP4159395B2 (en) Method for removing nitrate nitrogen from vegetable juice
JPH0367661B2 (en)
SU1125203A1 (en) Method for preparing high purity water

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19961203

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080227

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090227

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100227

Year of fee payment: 13

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110227

Year of fee payment: 14

LAPS Cancellation because of no payment of annual fees