JPS6322786B2 - - Google Patents
Info
- Publication number
- JPS6322786B2 JPS6322786B2 JP55091785A JP9178580A JPS6322786B2 JP S6322786 B2 JPS6322786 B2 JP S6322786B2 JP 55091785 A JP55091785 A JP 55091785A JP 9178580 A JP9178580 A JP 9178580A JP S6322786 B2 JPS6322786 B2 JP S6322786B2
- Authority
- JP
- Japan
- Prior art keywords
- fruit juice
- juice
- treatment
- content
- insoluble solids
- 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
Links
- 235000015203 fruit juice Nutrition 0.000 claims description 37
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims description 18
- 235000020971 citrus fruits Nutrition 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 11
- 238000007796 conventional method Methods 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 239000003957 anion exchange resin Substances 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 description 6
- 238000000909 electrodialysis Methods 0.000 description 5
- 239000000796 flavoring agent Substances 0.000 description 5
- 235000019634 flavors Nutrition 0.000 description 5
- 230000001954 sterilising effect Effects 0.000 description 5
- 108090000790 Enzymes Proteins 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 4
- 229940088598 enzyme Drugs 0.000 description 4
- 239000003456 ion exchange resin Substances 0.000 description 4
- 229920003303 ion-exchange polymer Polymers 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 2
- 241001672694 Citrus reticulata Species 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 230000002255 enzymatic effect Effects 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 235000019614 sour taste Nutrition 0.000 description 2
- 235000019605 sweet taste sensations Nutrition 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- 238000005199 ultracentrifugation Methods 0.000 description 2
- 108010059892 Cellulase Proteins 0.000 description 1
- 241000207199 Citrus Species 0.000 description 1
- 240000002319 Citrus sinensis Species 0.000 description 1
- 235000005976 Citrus sinensis Nutrition 0.000 description 1
- 101710196208 Fibrinolytic enzyme Proteins 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 108010059820 Polygalacturonase Proteins 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 108010093305 exopolygalacturonase Proteins 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000703 high-speed centrifugation Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000019629 palatability Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 235000019640 taste Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Non-Alcoholic Beverages (AREA)
Description
本発明は、酸味の少ない甘酸味のバランスのと
れた柑橘果汁の製造法に関する。
従来、うんしゆうみかん,なつみかん,伊予か
ん,バレンシアオレンジ,はつさくその他の柑橘
果実を原料とする柑橘果汁は、一部(特に、なつ
みかんなど国内柑橘果汁)において酸・味が高
く、嗜好的に好まれない面がみられ、また果実の
品種,採取時間,形態,産地などの相異によつ
て、果汁の品質(特に、糖分と酸味のバランス)
に変動を生じることが欠点であつた。
酸度の高い原料果実を使用した場合において
は、電気透析またはイオン交換樹脂による脱酸法
が知られているが、柑橘果汁製造の搾汁・分離処
理で使用されるスクリユープレスまたはフイニツ
シヤーのスクリーンの孔径が、0.5〜0.8mm、また
はそれ以上であるため、果汁中のペクチン質、コ
ロイド物質,パルプ質等の不溶性固形分の粒形が
粗大となり、かつその含量が5%(V/V)以上
であつて、イオン交換樹脂や電気透析膜を急速に
劣化する欠点をもつているので実用化されていな
いのである。
特に電気透析によるときはその劣化を防ぐため
には果汁をかなり清澄化する必要があり、そのた
め限外過することがたとえば特開昭54−86653
号公報で提案されているがその場合かなりの時間
を必要とし、不利な条件が課せられ、又果汁成分
上重要な灰分含量ロスが大きく、或は外観、香味
ともに劣つた物しか得られない難点があつた。
本発明者は、従来の欠点を排除し、常に酸味と
糖分とのバランスのとれた柑橘果汁を製造するこ
とについて種々研究した結果、本発明を達成した
のである。
本発明は、酸度の高い柑橘果実として使用して
も、甘酸味のバランスの一定した果汁を製造する
ことができる柑橘果汁の製造法を提供することを
目的とする。
本発明の他の目的は、酸度の低い、香味の優れ
た柑橘果汁、または酸度の高い果汁へのブレンド
用柑橘果汁を提供することである。
本発明は、柑橘果汁の製造法において、常法に
よつて搾汁・分離処理して得た果汁を、必要によ
り殺菌処理し、次いで超遠心分離処理、または酵
素処理後過処理して、不溶性固形分の含有量を
0.5%(V/V)以下とした果汁を得、この得ら
れた0.5%(V/V)以下の不溶性固形分を含む
果汁を陰イオン交換樹脂処理して、脱酸処理され
た果汁を得、この脱酸果汁に、不溶性固形分の含
有量0.5%(V/V)以上の脱酸処理してない果
汁即ち上記常法により搾汁・分離処理して得た果
汁、または上記超遠心分離処理して得た果汁、も
しくは酵素処理後過処理して得た果汁を混合
し、殺菌処理することを特徴とする柑橘果汁の製
造法である。
本発明での常法による分離処理後の搾汁の遠心
分離処理は、高速遠心機で処理(例えば、12000
〜20000G,5〜20秒)するのが好ましい。これ
以下の遠心力の場合には、更に長い時間で処理す
ることが必要で実用的でない。また、酵素処理に
おける酵素剤としてはセルラーゼ,ペクチナーゼ
などが使用され、例えば上記、常法による分離処
理後の搾汁を、加熱殺菌後、品温を30〜40℃に冷
却し、該果汁100Kgに対し、市販のペクチン分解
酵素または繊維素分解酵素10〜100gを添加し、
1〜5時間混合撹拌処理する。そして、該処理に
よる反応終了後、多段式過機などの過機とけ
いそう土,セライトなどの過助剤とを用いて
過処理するのである。酵素処理工程前の殺菌処理
は果汁中の微生物を殺菌するためである。また、
陰イオン交換樹脂処理は、カラム法およびバツチ
法が使用され、弱塩基,強塩基性のイオン交換樹
脂が使用される。なお、不溶性固形分の含量が
0.5%(V/V)以下の果汁、清澄果汁を脱酸処
理するときには陰イオン交換樹脂は劣化を生じな
いばかりでなく、カラム法で処理する場合には目
詰りを生ずることもなく連続処理ができるのであ
る。
前記のように従来技術に従つて原料果汁を限外
過処理後電気透析するときは、不利な条件が課
せられ即ち限外過処理を経済的に行なうため20
〜30℃に保つ必要があり、製品果汁の香味が失な
われるおそれがあり、その処理時間にかなりの時
間を要する。そして電気透析膜により酸味成分や
金属イオンが除去されるため果汁成分上重要な灰
分含量のロスが大きい。又規格で定められている
量以下の灰分含量の製品が生産されるおそれも大
きい。
これに対して本発明の方法によるときは脱酸処
理するに際し遠心分離して固形分0.5%(V/V)
以下にしてイオン交換樹脂処理すればよく、遠心
分離処理も氷結点以上に保つてごく短時間内で済
ませうるので香味が失なわれることもない。又以
下の実施例からも明らかなように本発明による減
酸処理果汁の灰分含量のロスが少なく従つて製品
果汁の灰分含量も充分である。そして減酸処理果
汁のブレンド比を多くしても製品果汁の灰分含量
が規格(0.20%以上)以下となるおそれは殆どな
い。
次に本発明の実施態様を説明する。
実施例 1
常法により、うんしゆみかんを搾汁し、フイニ
ツシヤーで不溶性固形分を除去して得た果汁を殺
菌冷却機で加熱し冷却して得た果汁(1)は、酸度が
0.97%で、不溶性固形分が8%(V/V)であつ
た。
得られた果汁100Kgを連続式高速遠心分離機に
よつて、不溶性固形分を0.5%(V/V)含む果
汁(2)85Kgと残渣15Kgを得た。
常法により水酸化ナトリウム液で再生し、水洗
した陰イオン交換樹脂(第四級アンモニウム)4
を上記85Kgの果汁に投入し、20〜30分程度撹拌
した後静置し、次いで樹脂を分別して果汁(3)80Kg
を得た。
得られた果汁は酸味が低く、飲み易いものであ
つたが、橙黄色がやや薄く、淡白な傾向が見られ
た。
得られた80Kgの果汁に、上記常法によつて搾
汁・分離処理して得た果汁(連続式高速遠心分離
処理を行なつてない果汁)80Kgを混合して得た果
汁(4)を常法により加熱殺菌処理して澄黄色の色調
で香味豊かな製品を得た。
The present invention relates to a method for producing citrus fruit juice with low sourness and a well-balanced sweet and sour taste. Traditionally, citrus fruit juices made from Unshiyu mandarin oranges, Natsumikans, Iyokans, Valencia oranges, Hatsuzaku oranges, and other citrus fruits have had high acidity and taste (especially domestic citrus fruit juices such as Natsumikans), making them less palatable. In addition, the quality of fruit juice (especially the balance of sugar and acidity) may vary depending on the variety of the fruit, the time of collection, its shape, the place of production, etc.
The disadvantage was that fluctuations occurred. When raw fruits with high acidity are used, deacidification methods using electrodialysis or ion-exchange resins are known; Since the pore size is 0.5 to 0.8 mm or more, the particle shape of insoluble solids such as pectin, colloid, pulp, etc. in the fruit juice becomes coarse, and the content thereof is 5% (V/V) or more. However, it has the disadvantage of rapidly deteriorating the ion exchange resin and electrodialysis membrane, so it has not been put into practical use. Particularly when using electrodialysis, it is necessary to clarify the fruit juice considerably in order to prevent its deterioration.
However, it requires a considerable amount of time, imposes disadvantageous conditions, and suffers from a large loss of ash content, which is important for fruit juice components, or results in products with inferior appearance and flavor. It was hot. The present inventor has achieved the present invention as a result of various studies to eliminate the conventional drawbacks and to produce citrus fruit juice that always has a well-balanced acidity and sugar content. An object of the present invention is to provide a method for producing citrus fruit juice that can produce fruit juice with a constant balance of sweet and sour taste even when citrus fruits with high acidity are used. Another object of the present invention is to provide a citrus juice with low acidity and excellent flavor, or for blending into a high acidity juice. In the method for producing citrus fruit juice, the present invention involves sterilizing the fruit juice obtained by squeezing and separating it in a conventional manner, if necessary, and then subjecting it to ultracentrifugation treatment or enzymatic treatment followed by filtration treatment to make it insoluble. Solid content
A fruit juice with a concentration of 0.5% (V/V) or less is obtained, and the obtained fruit juice containing an insoluble solid content of 0.5% (V/V) or less is treated with an anion exchange resin to obtain a deacidified fruit juice. , to this deacidified fruit juice, undeacidized fruit juice with an insoluble solid content of 0.5% (V/V) or more, that is, fruit juice obtained by squeezing and separating by the above-mentioned conventional method, or the above-mentioned ultracentrifugation. This method of producing citrus fruit juice is characterized by mixing the fruit juice obtained by the treatment or the fruit juice obtained by enzymatic treatment and overtreatment and sterilizing the mixture. In the present invention, centrifugation of the squeezed juice after separation by a conventional method is performed using a high-speed centrifuge (for example, 12,000
~20000G, 5-20 seconds) is preferable. If the centrifugal force is less than this, a longer processing time is required, which is not practical. In addition, cellulase, pectinase, etc. are used as enzyme agents in enzyme treatment, and for example, the juice after the above-mentioned separation treatment is heat sterilized, cooled to a temperature of 30 to 40°C, and the juice is made into 100 kg. To this, add 10 to 100 g of commercially available pectin-degrading enzyme or fibrinolytic enzyme,
Mix and stir for 1 to 5 hours. After the reaction is completed, an overtreatment is performed using a filter such as a multi-stage filter and a supercharging agent such as diatomaceous earth or celite. The purpose of the sterilization treatment before the enzyme treatment step is to sterilize microorganisms in the fruit juice. Also,
For the anion exchange resin treatment, a column method and a batch method are used, and weakly basic and strongly basic ion exchange resins are used. Note that the content of insoluble solids is
When deacidifying fruit juice or clarified fruit juice with a concentration of 0.5% (V/V) or less, the anion exchange resin not only does not deteriorate, but also can be treated continuously without clogging when treated with a column method. It can be done. As mentioned above, when raw fruit juice is subjected to electrodialysis after ultrafiltration according to the prior art, disadvantageous conditions are imposed, namely, in order to carry out ultrafiltration economically, 20
It is necessary to maintain the temperature at ~30°C, which may cause the product juice to lose its flavor, and the processing time takes a considerable amount of time. Since sour components and metal ions are removed by the electrodialysis membrane, there is a large loss of ash content, which is important for fruit juice components. There is also a great possibility that products with an ash content lower than the amount stipulated by the standards will be produced. On the other hand, when using the method of the present invention, the solid content is reduced to 0.5% (V/V) by centrifugation during deoxidation treatment.
The ion exchange resin treatment can be carried out as follows, and the centrifugation treatment can be completed within a very short time by keeping the temperature above the freezing point, so that the flavor will not be lost. Furthermore, as is clear from the following examples, the acid-reduced fruit juice according to the present invention has little loss of ash content, and therefore the product fruit juice has a sufficient ash content. Even if the blending ratio of acid-reduced fruit juice is increased, there is almost no possibility that the ash content of the product fruit juice will fall below the standard (0.20% or more). Next, embodiments of the present invention will be described. Example 1 Fruit juice (1) obtained by squeezing Unshiyu mandarin oranges in a conventional manner and removing insoluble solids with a finisher and heating and cooling the juice with a sterilization cooler has a low acidity.
0.97%, and the insoluble solids content was 8% (V/V). 100 kg of the obtained fruit juice was passed through a continuous high-speed centrifuge to obtain 85 kg of fruit juice (2) containing 0.5% (V/V) insoluble solids and 15 kg of residue. Anion exchange resin (quaternary ammonium) regenerated with sodium hydroxide solution and washed with water using a conventional method 4
was added to the above 85 kg of fruit juice, stirred for about 20 to 30 minutes, then left to stand, then the resin was separated and 80 kg of fruit juice (3) was added.
I got it. The obtained juice had low acidity and was easy to drink, but the orange-yellow color was slightly pale and it tended to be bland. Fruit juice (4) obtained by mixing 80 kg of the obtained fruit juice with 80 kg of fruit juice obtained by squeezing and separating by the above-mentioned conventional method (fruit juice that has not been subjected to continuous high-speed centrifugation treatment). A product with a clear yellow color and rich flavor was obtained by heat sterilization using a conventional method.
【表】 なお、酸味の違いによる嗜好性を次表に示す。【table】 The following table shows the palatability based on the difference in sourness.
【表】
20名のパネルによる嗜好調査を実施し、酸度の
異なる3種類の果汁について、最も好ましいと答
えた人数で示した。[Table] A preference survey was conducted by a panel of 20 people, and the number of people who answered that they preferred the three types of fruit juices with different acidity was shown.
Claims (1)
汁・分離処理して得た果汁を、必要により殺菌処
理し、次いで遠心分離処理または酵素処理後過
処理して、不溶性固形分の含有量を0.5%(V/
V)以下下となした果汁を、陰イオン交換樹脂処
理して得た脱酸果汁に、不溶性固形分の含有量
0.5%(V/V)以上の脱酸処理してない果汁を
適宜量混合することを特徴とする柑橘果汁の製造
法。1. In the method for producing citrus fruit juice, the fruit juice obtained by squeezing and separating the juice by a conventional method is sterilized if necessary, and then centrifuged or enzymatically treated and overtreated to reduce the content of insoluble solids to 0.5. %(V/
V) The content of insoluble solids is added to the deacidified fruit juice obtained by treating the fruit juice below with an anion exchange resin.
A method for producing citrus fruit juice, which comprises mixing an appropriate amount of undeacidized fruit juice of 0.5% (V/V) or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9178580A JPS5718971A (en) | 1980-07-07 | 1980-07-07 | Preparation of citrus fruit juice |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9178580A JPS5718971A (en) | 1980-07-07 | 1980-07-07 | Preparation of citrus fruit juice |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5718971A JPS5718971A (en) | 1982-01-30 |
| JPS6322786B2 true JPS6322786B2 (en) | 1988-05-13 |
Family
ID=14036245
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9178580A Granted JPS5718971A (en) | 1980-07-07 | 1980-07-07 | Preparation of citrus fruit juice |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5718971A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6158566A (en) * | 1984-08-31 | 1986-03-25 | Wakayamaken Nousanbutsu Kako Kenkyusho | Production of citrus juice |
| US7074448B2 (en) | 2001-09-28 | 2006-07-11 | Tropicana Products, Inc. | Juice deacidification |
| US20040208966A1 (en) * | 2003-04-15 | 2004-10-21 | Cargill Inc. | Minimal pulp beverage and methods for producing the same |
| JP2014027884A (en) * | 2012-07-31 | 2014-02-13 | Sumitomo Bakelite Co Ltd | Method for preserving citrus |
-
1980
- 1980-07-07 JP JP9178580A patent/JPS5718971A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5718971A (en) | 1982-01-30 |
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