JPH0687759B2 - Decolorization method for liquid foods - Google Patents
Decolorization method for liquid foodsInfo
- Publication number
- JPH0687759B2 JPH0687759B2 JP60178073A JP17807385A JPH0687759B2 JP H0687759 B2 JPH0687759 B2 JP H0687759B2 JP 60178073 A JP60178073 A JP 60178073A JP 17807385 A JP17807385 A JP 17807385A JP H0687759 B2 JPH0687759 B2 JP H0687759B2
- Authority
- JP
- Japan
- Prior art keywords
- substance
- decolorizing
- molecular weight
- membrane
- liquid foods
- 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
Links
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、限外過膜、塩阻止率の低い逆浸透膜等を用
いて液状食品を任意の脱色度で効率よく脱色する方法に
関する。Description: TECHNICAL FIELD The present invention relates to a method for efficiently decolorizing liquid foods at an arbitrary degree of decolorization using an ultrapermeation membrane, a reverse osmosis membrane having a low salt rejection rate, or the like.
脱色は液状食品を精製する上で重要であり、例えば、植
物蛋白の酸分解液や醤油等においては、保存中の酸化に
より増色し、品質が著しく劣化することから、色の安定
性を高める目的での脱色が行われるのが一般である。Decolorization is important for refining liquid foods.For example, in acid decomposed solution of vegetable protein, soy sauce, etc., the color is increased due to oxidation during storage, and the quality is significantly deteriorated. Decolorization for the purpose is generally performed.
従来の液状食品の脱色法としては、活性炭やイオン交換
樹脂等の吸着剤を用いて色素を除去する方法、或いは、
色素を阻止できる限外過膜や塩阻止率の低い逆浸透膜
を用いて色素を分離する方法等が知られている。しかし
ながら、吸着剤を用いる方法は、吸着剤が色素だけでな
く、精製しようとする目的物質をもある程度吸着するた
め、目的物質の収率の低下をまぬがれない。また、吸着
剤を再生する際、大量の廃液を生ずるという欠点を有し
ている。一方、膜を用いる方法は、目標とする脱色性を
得ることが可能な膜が存在しなかったり、膜を定めてし
まうと脱色性が自動的に決定し、自由に変えられないと
いう欠点を有していた。この欠点は、限外過膜、逆浸
透膜等の膜の種類の如何を問わず存在する。As a conventional decolorization method of liquid foods, a method of removing a pigment using an adsorbent such as activated carbon or an ion exchange resin, or
There is known a method of separating dyes using an ultrapermeable membrane capable of blocking dyes or a reverse osmosis membrane having a low salt rejection. However, in the method using the adsorbent, the adsorbent adsorbs not only the dye but also the target substance to be purified to some extent, so that the yield of the target substance cannot be reduced. Further, there is a drawback that a large amount of waste liquid is produced when the adsorbent is regenerated. On the other hand, the method using a film has the drawback that there is no film that can obtain the target decolorizing property, or that once the film is set, the decolorizing property is automatically determined and cannot be freely changed. Was. This defect exists regardless of the type of membrane such as ultrapermeabilization membrane or reverse osmosis membrane.
本発明は、従来の膜脱色法の有する欠点、即ち、膜の選
定により脱色性が決定されてしまい、かつ、目標とする
脱色性の得られる膜が必ずしも得られないことから、脱
色性への柔軟な目標設定が困難であり、かつ、収率及び
得られる製品の品質安定性が低い点を解決し、塩阻止率
の低い膜を用いても、任意に脱色性を設定及び変更で
き、目標とする品質安定性の高い液状食品を得られる脱
色法の開発を目的とする。The present invention has a drawback of the conventional film decolorizing method, that is, the decolorizing property is determined by the selection of the film, and the film having the target decolorizing property cannot always be obtained. It is difficult to set a flexible target, and the problem that the yield and the quality stability of the obtained product are low is solved, and even if a membrane with a low salt rejection rate is used, the decolorizing property can be set and changed arbitrarily, The purpose is to develop a decolorization method that can obtain a liquid food with high quality stability.
本発明者らは、上記膜を用いた液状食品の脱色における
問題点の解決につき鋭意研究を重ねた結果、高分子物質
又は難溶性物質の微細粒子を予め原液中に加えた後膜脱
色すると、添加物の種類、濃度により任意の脱色性が得
られることを見い出し本発明を完成したものである。The present inventors have conducted intensive research on solving the problems in decolorizing liquid foods using the above-mentioned film, and after decolorizing the film after adding fine particles of a polymer substance or a poorly soluble substance to the stock solution in advance, The present invention has been completed by finding that any decolorizing property can be obtained depending on the kind and concentration of the additive.
本発明で用いる膜は、分画分子量5000以上の限外過
膜、食塩阻止率30%以下の逆浸透膜等、分画分子量5,00
0以上又は食塩阻止率30%以下の膜である。このような
膜の具体例としては、UM-10、PM-10、UM-20E(アミコン
社製)、HFA-180(バイオエンジニアリング社製)、G-1
0T(日本真空技術社製)、NTU-3502(日東電工製)、SI
P-3013(旭化成製)、PBIL・TL-230(帝人製)等が挙げ
られる。分画分子量が5,000より小さい又は塩阻止率が3
0%より大の膜の場合には、添加物を加えることにより
脱色性を変化せしめる効果は少なく、また、透過流束の
低下により脱色効率が著しく悪くなるおそれがある。従
って、本発明の効果を十分に発揮するには膜の分画分子
量は5,000以上又は膜の食塩阻止率が30%以下であり、
分画分子量の上限については、分画分子量300,000を越
えるものは、脱色性が悪く、本発明の対象として適当で
はない。The membrane used in the present invention includes an ultrapermeaion having a molecular weight cutoff of 5000 or more, a reverse osmosis membrane having a salt inhibition rate of 30% or less, and a molecular weight cutoff of 5,00.
It is a membrane with 0 or more or a salt inhibition rate of 30% or less. Specific examples of such a membrane include UM-10, PM-10, UM-20E (manufactured by Amicon), HFA-180 (manufactured by Bioengineering), G-1.
0T (Nippon Vacuum Engineering Co., Ltd.), NTU-3502 (Nitto Denko), SI
P-3013 (manufactured by Asahi Kasei), PBIL / TL-230 (manufactured by Teijin) and the like can be mentioned. Fractionated molecular weight is less than 5,000 or salt rejection is 3
In the case of a film of more than 0%, the effect of changing the decolorizing property by adding the additive is small, and the decolorizing efficiency may be significantly deteriorated due to the reduction of the permeation flux. Therefore, in order to fully exert the effect of the present invention, the molecular weight cutoff of the membrane is 5,000 or more or the salt inhibition rate of the membrane is 30% or less,
Regarding the upper limit of the molecular weight cutoff, those having a molecular weight cutoff of more than 300,000 have poor decolorization properties and are not suitable for the present invention.
添加する高分子物質は、分子量5,000以上のもの、例え
ば、ゼラチン、大豆蛋白、卵白、ペクチン、寒天、ガ
ム、デキストラン、ポリアクリル酸ソーダ等である。ま
た、難溶性物質としては、分子量が5,000以下のものも
含めて、用いる膜を通過しない程度の粒度を有するもの
で、用いる膜の種類に応じて要求される粒度が異なる
が、具体的には、アミノ酸、有機酸、無機物質及びその
塩類等が挙げられる。これらの高分子物質及び難溶性物
質の中から1種単独で又は2種以上を組合せて原液に添
加するが、一般的には、用いる膜の分画分子量の2倍〜
60倍程度の可食性高分子物質、又は、チロシン、シスチ
ン等の難溶性アミノ酸結晶の添加が望ましい。The polymer substance added has a molecular weight of 5,000 or more, for example, gelatin, soybean protein, egg white, pectin, agar, gum, dextran, sodium polyacrylate and the like. Further, as the poorly soluble substance, including those having a molecular weight of 5,000 or less, those having a particle size that does not pass through the membrane to be used, and the required particle size varies depending on the type of the membrane to be used. , Amino acids, organic acids, inorganic substances and salts thereof, and the like. Of these polymeric substances and sparingly soluble substances, one kind alone or a combination of two or more kinds is added to the stock solution, but generally, it is twice the molecular weight cutoff of the membrane to be used.
It is desirable to add about 60 times the edible polymer substance or the hardly soluble amino acid crystals such as tyrosine and cystine.
原液に対する高分子物質又は難溶性物質の添加量は、添
加物質の種類、目標とする脱色性により変化する。従っ
て、これらの条件に応じて添加量を設定する必要がある
が、一般的には、原液に対し、0.01〜1重量%添加する
ことにより十分に目標とする脱色性が得られる。The amount of the polymer substance or the hardly soluble substance added to the stock solution varies depending on the type of the added substance and the target decolorizing property. Therefore, it is necessary to set the addition amount according to these conditions, but generally, by adding 0.01 to 1% by weight to the stock solution, a sufficient target decolorizing property can be obtained.
膜処理の方法は、原液に予め上記物質を添加して膜処理
装置に供給することを除き、常法に従って行えばよい。The membrane treatment method may be carried out according to a conventional method, except that the above substance is added to the stock solution in advance and supplied to the membrane treatment apparatus.
本発明の対象となる液状食品は、例えば、植物蛋白加水
分解液(HVP)、動物蛋白加水分解液(HAP)等の蛋白分
解液、醤油等の発酵液、肉エキス、魚介類エキス、野菜
エキス等の抽出液等が挙げられ、その種類に特に制限は
ないが、種々の脱色性の製品取得の必要があるHVP,HAP
等の脱色において、膜の選定における制約が緩和され、
かつ、1種類の膜で目的とする複数の脱色性が得られる
点で有用性が高い。The liquid food subject to the present invention includes, for example, a proteolytic solution such as a vegetable protein hydrolyzate (HVP) and an animal protein hydrolyzate (HAP), a fermented solution such as soy sauce, a meat extract, a seafood extract, and a vegetable extract. There are no particular restrictions on the type of extract such as HVP, HAP that requires the acquisition of various decolorizing products.
In bleaching, etc., the restrictions on the selection of the film are eased,
Moreover, it is highly useful in that a plurality of desired decolorizing properties can be obtained with one type of film.
以下、実施例により本発明を更に説明する。The present invention will be further described below with reference to examples.
実施例1 大豆蛋白加水分解液(以下HVP液と称す)をスパイラル
型限外過膜(分画分子量:6000、膜面積:0.25m2、材
質:ポリスルフォン系)を用いて脱色した。実験は供給
液を20用意し、濃縮液、透過液を総べて供給液槽に戻
しながら行なった。限外過装置の操作条件は圧力10kg
f/cm2、温度40℃、循環流量3/minであった。添加物
としてはポリアクリル酸ソーダ(平均分子量20万)0.05
%、ゼラチン(平均分子量10万)0.05%、チロシン微細
結晶0.4%を用い無添加の場合と透過流束と脱色性を比
較した。結果を第1表に示す。Example 1 A soybean protein hydrolyzed solution (hereinafter referred to as HVP solution) was decolorized using a spiral ultrafiltration membrane (molecular cutoff: 6000, membrane area: 0.25 m 2 , material: polysulfone type). The experiment was carried out by preparing 20 supply solutions and returning all the concentrated solution and the permeated solution to the supply solution tank. The operating condition of the ultrafiltration device is a pressure of 10 kg.
The f / cm 2 , the temperature was 40 ° C, and the circulation flow rate was 3 / min. As an additive, sodium polyacrylate (average molecular weight 200,000) 0.05
%, Gelatin (average molecular weight 100,000) 0.05%, and tyrosine fine crystals 0.4% were used to compare the permeation flux and decolorization property with no addition. The results are shown in Table 1.
実施例2 醤油を実施例‐1と同様の条件で膜脱色した。添加物と
してはゼラチン(平均分子量10万)0.05%を用い無添加
の場合と透過流束と脱色性を比較した。結果を第2表に
示す。 Example 2 Soy sauce was subjected to film decolorization under the same conditions as in Example-1. As an additive, 0.05% gelatin (average molecular weight 100,000) was used, and the permeation flux and the decolorizing property were compared with those without addition. The results are shown in Table 2.
実施例3 実施例2と同一の処理を、帝人(株)製PBIL逆浸透膜
(名称TL-230、食塩阻止率10%)を用いて行い、ゼラチ
ン0.05%添加区と無添加区の透過流束と脱色性を比較し
た。結果を第3表に示す。 Example 3 The same treatment as in Example 2 was carried out using a Teijin Ltd. PBIL reverse osmosis membrane (name TL-230, salt inhibition rate 10%), and the permeation flow of the gelatin 0.05% addition group and non-addition group The bleaching and decolorizing properties were compared. The results are shown in Table 3.
Claims (3)
以下の膜を用いて液状食品を脱色する際、原液中に予
め、分子量5,000以上の高分子物質又は膜を通過しない
粒度を有する難溶性物質の粒子を添加し、膜処理装置に
供給することを特徴とする液状食品の脱色方法。1. A molecular weight cutoff of 5,000 or more or a salt inhibition rate of 30%
When decolorizing liquid foods using the following membranes, in advance in the undiluted solution, add a high molecular weight substance of 5,000 or more or particles of a poorly soluble substance having a particle size that does not pass through the membrane, and supply it to the membrane treatment device. A characteristic method for decolorizing liquid foods.
ン、大豆蛋白、卵白、ペクチン、寒天、ガム、デキスト
ラン、ポリアクリル酸ソーダ、難溶性のアミノ酸、有機
酸、無機物質及びその塩類の中から選ばれた1種以上を
添加することを特徴とする特許請求の範囲第1項記載の
液状食品の脱色方法。2. A gelatin or soybean protein, egg white, pectin, agar, gum, dextran, sodium polyacrylate, a sparingly soluble amino acid, an organic acid, an inorganic substance or a salt thereof as a polymer substance or a sparingly soluble substance. The method for decolorizing liquid foods according to claim 1, characterized in that one or more selected from the above are added.
又は難溶性物質を添加することを特徴とする特許請求の
範囲第1項記載の液状食品の脱色方法。3. The method for decolorizing a liquid food according to claim 1, wherein 0.01 to 1.0% by weight of the high molecular weight substance or the hardly soluble substance is added to the stock solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60178073A JPH0687759B2 (en) | 1985-08-13 | 1985-08-13 | Decolorization method for liquid foods |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60178073A JPH0687759B2 (en) | 1985-08-13 | 1985-08-13 | Decolorization method for liquid foods |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6240260A JPS6240260A (en) | 1987-02-21 |
JPH0687759B2 true JPH0687759B2 (en) | 1994-11-09 |
Family
ID=16042144
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60178073A Expired - Lifetime JPH0687759B2 (en) | 1985-08-13 | 1985-08-13 | Decolorization method for liquid foods |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0687759B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2762087B2 (en) * | 1988-12-26 | 1998-06-04 | 株式会社中埜酢店 | Decolorization method for liquid food |
US7201523B2 (en) | 2003-08-08 | 2007-04-10 | Silverbrook Research Pty Ltd | Print engine for a pagewidth inkjet printer |
US6612240B1 (en) | 2000-09-15 | 2003-09-02 | Silverbrook Research Pty Ltd | Drying of an image on print media in a modular commercial printer |
JP2012200696A (en) * | 2011-03-28 | 2012-10-22 | Panasonic Corp | Desalting method and desalting apparatus |
CN117225189B (en) * | 2023-11-10 | 2024-03-08 | 河北格润德生物科技有限公司 | Amino acid film decoloring equipment and process |
-
1985
- 1985-08-13 JP JP60178073A patent/JPH0687759B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS6240260A (en) | 1987-02-21 |
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Legal Events
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EXPY | Cancellation because of completion of term |