JPH0428348B2 - - Google Patents
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- Publication number
- JPH0428348B2 JPH0428348B2 JP63293616A JP29361688A JPH0428348B2 JP H0428348 B2 JPH0428348 B2 JP H0428348B2 JP 63293616 A JP63293616 A JP 63293616A JP 29361688 A JP29361688 A JP 29361688A JP H0428348 B2 JPH0428348 B2 JP H0428348B2
- Authority
- JP
- Japan
- Prior art keywords
- chlorella
- twin
- product
- screw extruder
- functional food
- 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
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- Seeds, Soups, And Other Foods (AREA)
- Medicines Containing Plant Substances (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Beans For Foods Or Fodder (AREA)
- Grain Derivatives (AREA)
Description
[産業上の利用分野]
本発明は機能性食品の製造方法に関し、更に詳
しくはクロレラを利用した機能性食品の製造方法
に関する。
[従来の技術]
クロレラはクロレラ目に属する単細胞緑藻の属
名であり、その蛋白含量は50〜60重量%(乾物基
準)にも及び、また、リジンやメチオニンなどの
必須アミノ酸にも富んでいて栄養価が高い。この
ため、工業的に大量培養生産が行われており、健
康食品として使用されたり、養魚用配合飼料への
添加物として使用されている。また、乳酸菌の発
育促進物質を含んでおり、クロレラ乳酸菌飲料
(商品名:クロレラヤクルト)として実用化され
ている。
このうち、健康食品としては水中で培養された
クロレラを収集し、湿重量基準で約5%まで乾燥
し、この乾燥クロレラを既知の造粒技術で直径が
2〜5mmの粒としたもので、いわゆる丸薬のよう
にして使用されていた。
ところで、クロレラの単細胞はセルロースやヘ
ミセルロースなどの食物繊維と呼ばれている難消
化性多糖類を含む細胞壁に包まれており、消化性
を向上させるにはこの細胞壁を破壊する必要があ
る。また、クロレラは緑藻特有の臭いがある。
上述のような直径が2〜5mmの粒状のクロレラ
は、丸薬のようにして通常使用されるので、これ
らの点は問題とならないが、通常の食品としてク
ロレラを使用する場合には問題となる。
[発明が解決しようとする課題]
最近、食品は第1次機能(栄養)、第2次機能
(嗜好)と共に第3次機能(生体機能調節作用)
が注目されるようになり、特に、健康へのニーズ
から第3次機能をもつ食品が望まれている。
クロレラは高蛋白性であると共に必須アミノ酸
も豊富であり、また、各種の生体機能調整作用物
質の存在も指摘されており、機能性食品として使
用可能なものである。
しかし、このような第3次機能を有する食品に
クロレラをそのまま使用する場合には、消化性を
向上させるために細胞壁を破壊したり、緑藻特有
の臭いを除去する必要がある。
従つて、本発明の目的はクロレラの細胞壁の破
壊と脱臭を同時に行なうことができるクロレラを
利用した機能性食品の製造方法を提供することに
ある。
[課題を解決するための手段]
クロレラを利用して、更に、クロレラの細胞壁
の破壊と脱臭を同時に行なうことができる機能性
食品の製造方法はこれまでなく、このため日夜研
究を行つたところ、クロレラの細胞壁を破壊する
にはクロレラに圧縮及び剪断力を与え、脱臭する
ためにはダイ流出時に膨化させる必要があり、二
軸スクリユ押出機によつて加工処理すれば、この
目的を同時に達成できることが判つた。
即ち、本発明はクロレラまたはクロレラと澱粉
及び/または植物蛋白粉の混合物を、二軸スクリ
ユ押出機にて押出し、膨化させることを特徴とす
るクロレラ含有機能性食品の製造方法に係る。
[作用]
本発明方法において、クロレラの細胞壁を破壊
するためには二軸スクリユ押出機の使用が必須の
条件となるが、使用する押出機としてはフイー
ダ、シリンダ、二軸スクリユ、ダイ、シリンダの
加熱・冷却装置、水添加装置並びに切断装置を備
えた公知のものを使用することができる。
前述のように、クロレラは水中で培養されてい
るので、このままでは80〜90重量%(湿重量基
準)の水分を含有しているが、長期間の保存を可
能にしたり、取り扱いを容易にするために、約5
重量%(湿重量基準)まで水分含量を低下した形
態で通常入手できる。なお、水分含量の低減は公
知の手段により行われている。
なお、クロレラは数〜数十μmの粒子形態で入
手することができ、従つて、二軸スクリユ押出機
で加工処理するために粉砕等の予備処理を行う必
要はない。
上述のような約5重量%の水を含有するクロレ
ラ単独で、またはクロレラを、コーンフラワー、
小麦粉、コーンスターチ、米粉などの澱粉類や脱
脂大豆粉などの植物蛋白と混合する。この混合は
公知の方法で行えばよく、特に限定されるもので
はない。なお、クロレラ以外の原料は通常入手で
きるいずれものをも使用することができ、通常粒
度は数十〜数μm程度であり、水分含量は10〜15
重量%程度である。
次に、クロレラまたは上述のような混合物をフ
イーダを介して二軸スクリユ押出機に供給し、二
軸スクリユの回転数、シリンダの温度及び水添加
量を適宜選択して二軸スクリユ押出機を運転する
ことによつて細胞壁が破壊されて消化性が向上
し、且つ緑藻特有の臭いが脱臭された食品が製造
できる。
これは、二軸スクリユ押出機が有している混
合、混練、圧縮、剪断の機能の単独あるいは相乗
効果によつてクロレラの細胞壁が破壊されるため
と、ダイから流出して膨化する時に水蒸気と一緒
に臭いが蒸発して脱臭されるためである。
本発明に使用するクロレラは約5重量%の水分
を含有しており、通常使用される(市販されてい
る)澱粉類や植物蛋白は上述のように10〜15重量
%の水分を含有しており、食品として口当りが良
い膨化物を押出すには、二軸スクリユ押出機に供
給されるクロレラまたはクロレラと澱粉及び/ま
たは植物蛋白の混合物の水分含量を15〜40重量%
にする必要がある。クロレラまたは前記混合物の
水分含量が40重量%を超えると膨化が不十分で、
ベタベタした押出物となり、該水分含量が15重量
%未満であると過熱気味で若干コゲ臭がある押出
物となるために好ましくない。このため、水添加
装置を設置することが必要であり、しかも水添加
量を調節できるものが望ましい。
フイーダから供給された所定の水分含量をもつ
クロレラまたは混合物のシリンダ内での加工処理
は100〜200°Cの温度の下で行うことが好ましい。
ここで、シリンダ内の温度が100°C未満であると、
クロレラまたは混合物中に含有される水分が水蒸
気にならないので膨化が起こらず、クロレラ固有
の臭気の発散が十分でないために好ましくなく、
また、該温度が200°Cを超えると、クロレラまた
は混合物が加工処理中に焦げたりするために好ま
しくない。なお、シリンダ内の温度は二軸スクリ
ユ押出機への原料の供給速度、二軸スクリユの回
転数、シリンダの加熱・冷却装置により制御する
ことができる。
また、シリンダ内の圧力を10〜100Kg/cm2の範
囲内に維持することが好ましい。ここで、該圧力
が10Kg/cm2未満であると大気圧(約1Kg/cm2)と
の差が少なく、膨化が不十分でクロレラ固有の臭
気の発散が十分でないために好ましくなく、ま
た、該圧力が100Kg/cm2を超えると逆に大気圧
(約1Kg/cm2)との差が大きいので押出物がダイ
から粉末状となつて吹き出すことがあるために好
ましくない。
なお、シリンダ内の圧力は二軸スクリユ押出機
への原料の供給速度、二軸スクリユの回転数の制
御や使用するダイの流路形状を選択することによ
り調整できる。
上述のようなシリンダ内条件下では、クロレラ
または前記混合物に含まれている水分が水蒸気に
なろうとするが、シリンダ内は上述のように10〜
100Kg/cm2の高圧となつているため、水分は過熱
水あるいは圧縮された水蒸気の状態となつてい
る。この過熱水あるいは圧縮された水蒸気を含む
クロレラまたは前記押出物がダイから流出する
と、圧力が高圧(10〜100Kg/cm2)から大気圧
(約1Kg/cm2)まで開放されて過熱水あるいは圧
縮された水蒸気が一気に膨化して水蒸気と一緒に
クロレラ固有の臭気が発散して脱臭される。
また、ダイ及び切断装置は製品の形状を決定す
るものであり、適宜選択すれば良いが、前述の理
由によつてダイは10〜100Kg/cm2の高圧がシリン
ダ内に発生するような流路を有している必要があ
る。
上述のように本発明方法によればクロレラまた
はクロレラと澱粉類及び/または植物蛋白の混合
物を二軸スクリユ押出機で加工処理してクロレラ
含有機能性食品を得ることができる。
なお、上述のようにして得られたクロレラ含有
機能性食品はまだ製品に味付けが行われていない
が、切断後の膨化物に通常使用されているスプレ
ー方式またはフライ方式などによつて任意に味付
けができる。また、製品を湯戻しして使用する場
合には、この湯戻しの時や湯戻し後に味付けを行
うこともできる。
[実施例]
以下に実施例を挙げて本発明のクロレラ含有機
能性食品の製造方法について更に説明する。
実施例 1
水分含量が5重量%(湿重量基準)のクロレ
ラ、コーンフラワー、小麦粉、コーンスターチ及
び米粉を重量比でそれぞれ1.5:4:3:2:1
の割合で混合し、この混合物をフイーダにより二
軸スクリユ押出機[(株)日本製鋼所製:TEX52F]
に40〜50Kg/時間の量で供給し、第1表に示す製
造条件にて実施した。また、ダイは出口形状が4
mmφ×2個の孔のものを使用し、切断装置は切断
後の製品形状の縦と横の長さがほぼ同じになるよ
うに切断速度を調整した。
[Industrial Application Field] The present invention relates to a method for producing a functional food, and more particularly to a method for producing a functional food using chlorella. [Prior art] Chlorella is the genus name of unicellular green algae belonging to the order Chlorella, and its protein content is 50 to 60% by weight (dry weight basis), and it is also rich in essential amino acids such as lysine and methionine. Highly nutritious. For this reason, large-scale culture production is carried out industrially, and it is used as a health food or as an additive to mixed feed for fish farming. It also contains a substance that promotes the growth of lactic acid bacteria, and has been put into practical use as a chlorella lactic acid bacteria drink (trade name: Chlorella Yakult). Among these, as a health food, chlorella cultured in water is collected, dried to about 5% on a wet weight basis, and this dried chlorella is made into particles with a diameter of 2 to 5 mm using known granulation techniques. It was used like a so-called pill. By the way, single cells of Chlorella are surrounded by a cell wall containing indigestible polysaccharides called dietary fibers such as cellulose and hemicellulose, and in order to improve digestibility it is necessary to destroy this cell wall. In addition, chlorella has a characteristic odor of green algae. Since granular chlorella with a diameter of 2 to 5 mm as described above is usually used in the form of pills, these points do not pose a problem, but they become a problem when chlorella is used as a regular food. [Problem to be solved by the invention] Recently, food has a primary function (nutrition), a secondary function (preference), and a tertiary function (biological function regulation effect).
In particular, foods with tertiary functions are desired due to health needs. Chlorella is high in protein and rich in essential amino acids, and it has also been pointed out that it contains various substances that regulate biological functions, so it can be used as a functional food. However, if chlorella is used as it is in foods with such tertiary functions, it is necessary to destroy the cell walls and remove the odor characteristic of green algae in order to improve digestibility. Therefore, an object of the present invention is to provide a method for producing a functional food using chlorella, which can simultaneously destroy the cell walls of chlorella and deodorize it. [Means for solving the problem] There has never been a method for producing a functional food that uses chlorella and can simultaneously destroy the cell walls of chlorella and deodorize it, so after conducting day and night research, we found that: In order to destroy the cell walls of chlorella, it is necessary to apply compression and shear force to chlorella, and in order to deodorize it, it is necessary to swell it when it exits the die, and these purposes can be achieved at the same time by processing it with a twin-screw extruder. I found out. That is, the present invention relates to a method for producing a chlorella-containing functional food, which comprises extruding and expanding chlorella or a mixture of chlorella and starch and/or vegetable protein powder using a twin-screw extruder. [Function] In the method of the present invention, the use of a twin-screw extruder is an essential condition in order to destroy the cell walls of chlorella. Known devices equipped with heating/cooling devices, water addition devices and cutting devices can be used. As mentioned above, since chlorella is cultured in water, it contains 80 to 90% water by weight (wet weight basis), but it can be stored for a long period of time and handled easily. For about 5
It is usually available in a form with reduced moisture content up to % by weight (wet weight basis). Note that the water content is reduced by known means. Note that chlorella can be obtained in the form of particles of several to several tens of micrometers, and therefore, there is no need to perform pretreatment such as pulverization in order to process it with a twin-screw extruder. Chlorella alone or chlorella containing about 5% water by weight as described above, cornflour,
It is mixed with starches such as wheat flour, cornstarch, and rice flour, and vegetable proteins such as defatted soybean flour. This mixing may be performed by a known method and is not particularly limited. In addition, any commonly available raw materials other than chlorella can be used, and the particle size is usually about several tens to several μm, and the moisture content is about 10 to 15 μm.
It is about % by weight. Next, chlorella or the above-mentioned mixture is fed to a twin-screw extruder through a feeder, and the twin-screw extruder is operated by appropriately selecting the rotation speed of the twin-screw, the temperature of the cylinder, and the amount of water added. By doing so, the cell walls are destroyed, the digestibility is improved, and it is possible to produce food that is free from the odor characteristic of green algae. This is because the cell walls of chlorella are destroyed by the mixing, kneading, compression, and shearing functions of the twin-screw extruder, either singly or in synergy, and also because water vapor is generated when it flows out of the die and expands. This is because the odor evaporates and is deodorized. Chlorella used in the present invention contains approximately 5% water by weight, and commonly used (commercially available) starches and vegetable proteins contain 10 to 15% water by weight, as mentioned above. In order to extrude a puffed product that is palatable as food, the water content of the chlorella or mixture of chlorella and starch and/or vegetable protein fed to the twin-screw extruder should be 15-40% by weight.
It is necessary to If the moisture content of chlorella or the above mixture exceeds 40% by weight, swelling will be insufficient;
The extrudate becomes sticky, and if the water content is less than 15% by weight, the extrudate tends to be overheated and has a slightly burnt odor, which is not preferable. For this reason, it is necessary to install a water addition device, and it is desirable that the amount of water added can be adjusted. The processing of chlorella or a mixture with a predetermined moisture content fed from a feeder in a cylinder is preferably carried out at a temperature of 100 to 200°C.
Here, if the temperature inside the cylinder is less than 100°C,
Since the moisture contained in chlorella or the mixture does not turn into water vapor, swelling does not occur, and the odor peculiar to chlorella is not sufficiently released, which is undesirable.
Furthermore, if the temperature exceeds 200°C, the chlorella or the mixture may burn during processing, which is not preferable. Note that the temperature inside the cylinder can be controlled by the feed rate of raw materials to the twin-screw extruder, the rotation speed of the twin-screw extruder, and the cylinder heating/cooling device. Further, it is preferable to maintain the pressure inside the cylinder within a range of 10 to 100 Kg/cm 2 . Here, if the pressure is less than 10 Kg/cm 2 , the difference from atmospheric pressure (approximately 1 Kg/cm 2 ) is small, swelling is insufficient, and chlorella-specific odor is not sufficiently released, which is not preferable. If the pressure exceeds 100 Kg/cm 2 , the difference from atmospheric pressure (approximately 1 Kg/cm 2 ) is so large that the extrudate may blow out from the die in the form of powder, which is not preferable. Note that the pressure inside the cylinder can be adjusted by controlling the feed rate of raw materials to the twin-screw extruder, the rotational speed of the twin-screw extruder, and selecting the flow path shape of the die used. Under the above-mentioned conditions inside the cylinder, the water contained in chlorella or the mixture tends to turn into water vapor, but inside the cylinder, as mentioned above,
Due to the high pressure of 100 kg/cm 2 , the water is in the form of superheated water or compressed steam. When the chlorella or the extrudate containing this superheated water or compressed water vapor flows out from the die, the pressure is released from high pressure (10 to 100 Kg/cm 2 ) to atmospheric pressure (approximately 1 Kg/cm 2 ), and the superheated water or compressed water vapor is released. The water vapor is expanded all at once, and together with the water vapor, the unique odor of chlorella is emitted and deodorized. In addition, the die and cutting device determine the shape of the product, so they can be selected appropriately, but for the reasons mentioned above, the die should not be used in a flow path where a high pressure of 10 to 100 kg/ cm2 is generated inside the cylinder. Must have. As described above, according to the method of the present invention, a chlorella-containing functional food can be obtained by processing chlorella or a mixture of chlorella and starches and/or vegetable proteins using a twin-screw extruder. Although the chlorella-containing functional food obtained as described above has not yet been seasoned, it can be seasoned arbitrarily by spraying or frying, which is the method usually used for cutting the puffed product. I can do it. In addition, when the product is used after being rehydrated in hot water, flavoring can be added at the time of or after rehydrating the product. [Example] The method for producing the chlorella-containing functional food of the present invention will be further explained with reference to Examples below. Example 1 Chlorella, corn flour, wheat flour, cornstarch, and rice flour with a water content of 5% by weight (wet weight basis) were mixed in a weight ratio of 1.5:4:3:2:1, respectively.
This mixture is passed through a feeder using a twin-screw extruder [manufactured by Japan Steel Works, Ltd.: TEX52F].
The production was carried out under the production conditions shown in Table 1. In addition, the die has an outlet shape of 4
A cutter having 2 mmφ holes was used, and the cutting speed of the cutting device was adjusted so that the length and width of the product shape after cutting were approximately the same.
【表】
実施結果を第1表に示したが、総合して言え
ば、得られた製品は直径が約15mmのほぼ球状の膨
化物であり、これを試食したところ口当りのよい
スナツク風の食品であつた。製品は切断直後は若
干緑藻特有の臭いを有していたが、室温で約3〜
5分間放置しておくと殆ど臭いは感じられなかつ
た。また、製品を走査型電子顕微鏡(SEM)で
観察したところ、クロレラの細胞壁は殆どが破壊
されており、微少な植物繊維として製品中に分散
されていた。
実施例 2
水分含量が5重量%(湿重基準)のクロレラ及
び米粉を重量比で2:8の割合で混合し、この混
合物を二軸フイーダにより実施例1と同様の二軸
スクリユ押出機に50Kg/時間の量で供給し、第2
表に示す製造条件にて実施した。また、ダイは出
口形状が4mmφ×2個の孔を有するものを使用
し、切断装置は切断後の製品形状の縦と横の長さ
がほぼ同じになるように切断速度を調整した。[Table] The results are shown in Table 1. Overall, the obtained product was a nearly spherical puffed product with a diameter of about 15 mm, and when I tried it, it was a snack-like food with a good taste. It was hot. Immediately after cutting, the product had a slight odor characteristic of green algae, but at room temperature it
After leaving it for 5 minutes, almost no odor was detected. Furthermore, when the product was observed using a scanning electron microscope (SEM), it was found that most of the cell walls of Chlorella were destroyed and were dispersed in the product as minute plant fibers. Example 2 Chlorella and rice flour with a water content of 5% by weight (wet weight basis) were mixed at a weight ratio of 2:8, and this mixture was transferred to the same twin-screw extruder as in Example 1 using a twin-screw feeder. Supplied in an amount of 50Kg/hour,
It was carried out under the manufacturing conditions shown in the table. Further, a die having an exit shape of 4 mmφ×2 holes was used, and the cutting speed of the cutting device was adjusted so that the vertical and horizontal lengths of the product shape after cutting were approximately the same.
【表】
実施結果を第2表に示したが、総合して言え
ば、得られた製品は直径が約12mmのほぼ球状の膨
化物であり、これを試食したところ口当りのよい
スナツク風の食品てあつた。製品は切断直後は若
干の緑藻特有の臭いを有していたが、室温で3〜
5分間放置しておくとほとんど感じられなくなつ
た。また、製品をSEMにより観察したところ、
クロレラの細胞壁は殆どが破壊されており、微少
な植物繊維として製品中に分散されていた。
実施例 3
水分含量が5重量%(湿重基準)のクロレラ、
脱脂大豆粉及び小麦粉を重量比でそれぞれ1.5:
7.5:1の割合で混合し、この混合物をフイーダ
により実施例1と同様の二軸スクリユ押出機に40
Kg/時間の量で供給し、第3表に示す製造実条件
にて実施した。また、ダイは出口形状が厚さ:3
mm、幅:45mmのものを使用し、切断装置は切断後
の製品の長さが約100mmとなるように切断速度を
調整した。[Table] The results are shown in Table 2. Overall, the obtained product was a nearly spherical puffed product with a diameter of about 12 mm, and when I tried it, it was a snack-like food with a good taste. It was hot. The product had a slight odor peculiar to green algae immediately after cutting, but it was
After leaving it for 5 minutes, I could hardly feel it anymore. In addition, when the product was observed using SEM,
Most of the cell walls of Chlorella were destroyed and were dispersed in the product as minute plant fibers. Example 3 Chlorella with a water content of 5% by weight (wet weight basis),
Weight ratio of defatted soybean flour and wheat flour is 1.5:
Mixed at a ratio of 7.5:1, this mixture was transferred to a twin-screw extruder similar to Example 1 using a feeder.
It was supplied in an amount of Kg/hour and conducted under the actual manufacturing conditions shown in Table 3. Also, the die has an exit shape with a thickness of 3
mm, width: 45 mm, and the cutting speed of the cutting device was adjusted so that the length of the cut product was approximately 100 mm.
【表】
実施結果を第3表に示したが、総合して言え
ば、得られた製品は厚さ:約5mm、幅:約50mm、
長さ:約100mmの板状の膨化物であつた。これを
試食したところ、僅かに海草風味があり、歯ごた
えは畜肉様であつた。製品は切断直後は若干緑藻
特有の臭いを有していたが、室温で5〜10分間放
置しておくと殆ど感じられなくなつた。また、製
品をSEMで観察したところ、クロレラの細胞壁
は殆どが破壊されており、微少な植物繊維として
製品中に分散されていた。
実施例 4
水分含量が5重量%(湿重量基準)のクロレラ
をフイーダにより実施例1と同様の二軸スクリユ
押出機に20Kg/時間の量で供給し、第4表に示す
製造条件にて実施した。また、ダイは出口形状が
6mmφの孔を2個有するものであり、切断装置は
切断後の製品形状の縦と横の長さがほぼ同じにな
るように切断速度を調整した。[Table] The results are shown in Table 3. Overall, the obtained product has a thickness of about 5 mm, a width of about 50 mm,
It was a plate-shaped swelling with a length of approximately 100 mm. When I tried this, it had a slight seaweed flavor and the texture was similar to meat. Immediately after cutting, the product had a slight odor characteristic of green algae, but after being left at room temperature for 5 to 10 minutes, it became almost unnoticeable. Furthermore, when the product was observed using SEM, it was found that most of the cell walls of Chlorella were destroyed and were dispersed in the product as minute plant fibers. Example 4 Chlorella with a moisture content of 5% by weight (wet weight basis) was fed into the same twin-screw extruder as in Example 1 at a rate of 20 kg/hour using a feeder, and the production was carried out under the manufacturing conditions shown in Table 4. did. Furthermore, the die had two holes with an exit shape of 6 mmφ, and the cutting speed of the cutting device was adjusted so that the vertical and horizontal lengths of the product shape after cutting were approximately the same.
【表】【table】
【表】
実施結果を第4表に示したが、総合した言え
ば、得られた製品は直径が約8mmのほぼ球形の膨
化物であり、これを試食したところ、乾燥した海
草風味であつた。製品は切断直後には緑藻特有の
臭いを有していたが、室温に5〜10分間放置して
おくと緑藻特有の臭いではなく香ばしい焼き海苔
の臭いとなつた。また、製品をSEMにより観察
したところクロレラの細胞壁は殆どが破壊されて
おり、微少な食物繊維として製品中に分散されて
いた。
[発明の効果]
以上の説明で明らかなように、本発明によれば
二軸スクリユ押出機を使用するため、混合、混
練、圧縮、剪断、膨化の機能が単独あるいは相乗
して作用するのでクロレラの細胞壁が破壊されて
消化性が向上し且つ緑藻特有の臭いを除去するこ
とができる。また、破壊されて製品中に分散され
た細胞壁は食物繊維として生体に作用し、クロレ
ラに含まれている高分子の薬効成分も二軸スクリ
ユ押出機の圧縮、剪断機能によつて低分子に寸断
されて体内で吸収され易くなる効果も期待でき
る。
更に、二軸スクリユ押出機を使用しているの
で、短時間で連続的に処理でき、その処理コスト
も他の方法に比べて安価である。[Table] The results are shown in Table 4. Overall, the obtained product was a nearly spherical puffed product with a diameter of about 8 mm, and when I tasted it, it had a dried seaweed flavor. . Immediately after cutting, the product had a characteristic odor of green algae, but after being left at room temperature for 5 to 10 minutes, the odor changed from the characteristic odor of green algae to that of fragrant roasted seaweed. Furthermore, when the product was observed using SEM, it was found that most of the cell walls of Chlorella were destroyed and were dispersed in the product as minute amounts of dietary fiber. [Effects of the Invention] As is clear from the above explanation, according to the present invention, since a twin-screw extruder is used, the functions of mixing, kneading, compression, shearing, and swelling work independently or in synergy. The cell walls of green algae are destroyed, improving digestibility and eliminating the odor characteristic of green algae. In addition, the cell walls that are destroyed and dispersed in the product act on the living body as dietary fiber, and the high-molecular medicinal ingredients contained in chlorella are also shredded into low molecules by the compression and shearing functions of the twin-screw extruder. It can also be expected to have the effect of making it more easily absorbed in the body. Furthermore, since a twin-screw extruder is used, the process can be performed continuously in a short period of time, and the process cost is lower than that of other methods.
Claims (1)
植物蛋白粉の混合物を、二軸スクリユ押出機にて
押出し、膨化させることを特徴とするクロレラ含
有機能性食品の製造方法。 2 押出時の押出機シリンダ内の温度が100〜
200°Cである請求項1記載のクロレラ含有機能性
食品の製造方法。 3 押出時の押出機シリンダ内の圧力が10〜100
Kg/cm2である請求項1または2記載のクロレラ含
有機能性食品の製造方法。 4 二軸スクリユ押出機に供給されるクロレラま
たはクロレラと澱粉及び/または植物蛋白粉の混
合物の水分含量が15〜40重量%である請求項1か
ら3までのいずれか1項記載のクロレラ含有機能
性食品の製造方法。[Scope of Claims] 1. A method for producing a functional food containing chlorella, which comprises extruding and swelling chlorella or a mixture of chlorella and starch and/or vegetable protein powder using a twin-screw extruder. 2 The temperature inside the extruder cylinder during extrusion is 100~
The method for producing a chlorella-containing functional food according to claim 1, wherein the temperature is 200°C. 3 The pressure inside the extruder cylinder during extrusion is 10 to 100
The method for producing a chlorella-containing functional food according to claim 1 or 2, wherein the chlorella-containing functional food is 1 kg/cm 2 . 4. The chlorella-containing function according to any one of claims 1 to 3, wherein the moisture content of chlorella or a mixture of chlorella and starch and/or vegetable protein powder supplied to the twin-screw extruder is 15 to 40% by weight. Method of manufacturing sex food.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63293616A JPH02142447A (en) | 1988-11-22 | 1988-11-22 | Production of chlorella-containing functional food |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63293616A JPH02142447A (en) | 1988-11-22 | 1988-11-22 | Production of chlorella-containing functional food |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02142447A JPH02142447A (en) | 1990-05-31 |
| JPH0428348B2 true JPH0428348B2 (en) | 1992-05-14 |
Family
ID=17797019
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63293616A Granted JPH02142447A (en) | 1988-11-22 | 1988-11-22 | Production of chlorella-containing functional food |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02142447A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU2015208703A1 (en) * | 2014-01-27 | 2016-08-04 | Hinoman Ltd. | Using Wolffia genus plant material for preparing dough |
-
1988
- 1988-11-22 JP JP63293616A patent/JPH02142447A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02142447A (en) | 1990-05-31 |
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