JP2006149219A - Food material, food, and method for producing the food material - Google Patents

Food material, food, and method for producing the food material Download PDF

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JP2006149219A
JP2006149219A JP2004340449A JP2004340449A JP2006149219A JP 2006149219 A JP2006149219 A JP 2006149219A JP 2004340449 A JP2004340449 A JP 2004340449A JP 2004340449 A JP2004340449 A JP 2004340449A JP 2006149219 A JP2006149219 A JP 2006149219A
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red bean
food material
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Yasushi Ifuku
靖 伊福
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Abstract

<P>PROBLEM TO BE SOLVED: To provide food material efficiently produced from seed coats of small red beans or bean jam lees highly containing the seed coats, and containing a large amount of active ingredients derived from the small red beans; and to provide food containing the food material: and to provide a method for producing the food material. <P>SOLUTION: The food material comprises concentrated liquid K, T obtained through boiling small red bean seed coats D or small red bean jam lees L, and heating cooking liquid I, J, O, S separated from the boiled small red bean seed coats D or the small red bean jam lees L to evaporate the liquid under normal pressure. The method for producing the food material comprises boiling the small red bean seed coats D or the small red bean jam lees L, and heating the cooking liquid I, J, O, S separated from the boiled small red bean seed coats D or the small red bean jam lees L to have such a temperature as to evaporate the liquid under normal pressure, and evaporating the heated cooking liquid I, J, O, S under normal pressure to concentrate the cooking liquid. The food is obtained through using the thus-obtained food material. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、小豆由来の有用な食品材料、食品、および食品材料の製造方法に関するものである。   The present invention relates to a useful food material derived from red beans, a food, and a method for producing the food material.

小豆はデンプン質から主としてなり、日本食品分析表(四訂版)に記載のように、タンパク質、食物繊維、ビタミンB1、サポニンなどを多く含む栄養価の高い食品原料として知られている。かかる小豆は昔からの民間療法に用いられており、脚気、便秘、二日酔、疲労回復、むくみ、動脈硬化、利尿などに効くといわれてきた。また、最近の研究では、ガン細胞のアポトーシス誘導を促すこと、ポリフェノール(アントシアニンなど)やサポニンで血液をサラサラにすること、サポニンに抗菌性および抗炎症性があり脂質代謝を促すこと、カリウムが多く高血圧に効くこと、鉄分が多く貧血によいこと、ポリフェノール以外にビタミンEも多く抗酸化力が大きいこと、食物繊維が多く便秘の解消によりダイエットによいことなど数々の研究成果が発表されている。   Azuki beans are mainly made of starch and are known as highly nutritious food materials containing a large amount of protein, dietary fiber, vitamin B1, saponin, etc., as described in the Japanese Food Analysis Table (4th edition). Such azuki beans have been used in traditional folk remedies and have been said to be effective for beriberi, constipation, hangover, recovery from fatigue, swelling, arteriosclerosis, diuresis and the like. In recent studies, it has been suggested that cancer cells are induced to induce apoptosis, blood is smoothened with polyphenols (such as anthocyanins) and saponins, saponins have antibacterial and anti-inflammatory properties, promote lipid metabolism, and a large amount of potassium Numerous research results have been announced, such as being effective for high blood pressure, being rich in iron and good for anemia, being rich in vitamin E in addition to polyphenols and having high antioxidant power, and being good for dieting due to the elimination of constipation.

上記のように有用な小豆は例えば生あんの原料として用いられてきた。生あんは、例えば図4に示すような一連の製あん工程を経て製造される。ここで、生あん製造の一例を説明すると、まず、原料豆300kgを煮釜に入れ(工程S1)、水道水1〜1.5トンを給水する(給水工程S2)。そして、渋抜き煮炊工程S3において小豆を常圧下110℃で40分間煮炊する。これにより、小豆から渋が抽出されて煮汁Aに移行する。この煮汁Aは渋切り工程S4において、いわゆる渋切り液として煮釜から抜き出される。取り出された1トン程度の煮汁Aは赤みを帯びてほとんど透明な液体である。
続いて、渋切り後の小豆に水1トンを給水し(工程S5)、本煮炊工程S6として小豆を常圧下110℃で30〜50分間煮炊し、湯を煮釜から抜き出したのち(工程S7)、煮釜に残った煮小豆を磨砕し(工程S8)、磨砕した練小豆を篩分けする(工程S9)。この篩分けにより、主に種皮の磨砕片から成るあん粕Lが練小豆から分別される。上記のように篩分けされた練小豆は大量の水にさらされたのちに(工程S10)脱水される(工程S11)。脱水後の練小豆は生あん製品化工程S12で袋詰されたのち、冷蔵保存される。
As described above, useful red beans have been used as raw materials for raw bean paste, for example. The raw bean paste is manufactured through a series of process steps as shown in FIG. 4, for example. Here, an example of raw bean production will be described. First, 300 kg of raw beans are placed in a boiled pot (step S1), and 1 to 1.5 tons of tap water is supplied (water supply step S2). Then, the red beans are boiled at 110 ° C. for 40 minutes under normal pressure in the astringent boil cooking step S3. Thereby, astringents are extracted from red beans and it transfers to soup A. This soup A is extracted from the boiling pot as a so-called astringent cutting liquid in the astringent cutting step S4. About 1 ton of the extracted soup A is reddish and almost transparent.
Subsequently, 1 ton of water is fed to the azuki beans after astringency cutting (step S5), and the red beans are boiled and cooked at 110 ° C. for 30 to 50 minutes under normal pressure, and the hot water is extracted from the boiling pot ( Step S7), the boiled red beans remaining in the boiled kettle are ground (step S8), and the ground kneaded red beans are sieved (step S9). By this sieving, the ground bean L consisting mainly of ground seed coat is separated from the kneaded red beans. The kneaded red beans screened as described above are dehydrated (step S11) after being exposed to a large amount of water (step S10). The dehydrated kneaded red beans are packaged in the raw bean product production step S12 and then refrigerated.

ところで、渋切り時に取り出された煮汁Aは腐敗しやすく保存性が低い。殊に、夏場は半日も放置すると強い腐敗臭を発する。そのため、煮汁Aは有用なサポニン、ポリフェノール、カリウムなどを大量に含んでいるにも拘わらず何ら利用されることがなく、排水処理により廃棄されていた。
そこで、本発明者は、渋抜き用の煮炊後に小豆から分離した煮汁を常圧下で蒸発する温度に加熱し、加熱した煮汁を常圧下で蒸発させることにより濃縮した濃縮液を食品材料として得る技術を創出した。かかる技術は下記の特許文献1に記載されている。
By the way, the broth A taken out at the time of astringency is easy to rot and has low storage stability. In particular, a strong rotting odor is emitted when left for half a day in summer. Therefore, the broth A was not used at all even though it contained a large amount of useful saponin, polyphenol, potassium, etc., and was discarded by waste water treatment.
Therefore, the present inventor obtains a concentrated concentrate as a food material by heating the broth separated from the red beans after boiling for astringency to a temperature that evaporates under normal pressure, and evaporating the heated broth under normal pressure. Created technology. Such a technique is described in Patent Document 1 below.

また、前掲の日本食品分析表(四訂版)によれば、小豆は胚乳と胚芽と種皮とから成り、可食部(乾燥状態)100g中に、水分15.5g、タンパク質20.3g、炭水化物58.7g(うち、糖質54.4g、繊維質4.3g)、灰分3.3g他を含んでいるとされている。これらの栄養素のうちタンパク質と炭水化物が生あんの主成分となっている。生あんは主に小豆の胚乳および胚芽から成っている。これら胚乳部分および胚芽部分の色はもともと白色ないし灰白色であるが、種皮の色素成分を吸着して特有の小豆色を呈している。小豆の種皮は堅い棚状細胞で構成され小豆全体重量の10〜11wt%を占めており、この種皮に小豆中のポリフェノールおよびサポニンのほとんどが含まれている。   According to the Japanese Food Analysis Table (4th edition), azuki beans are composed of endosperm, germ and seed coat. In 100 g of edible portion (dried), 15.5 g of water, 20.3 g of protein, carbohydrates It contains 58.7 g (of which 54.4 g of saccharides, 4.3 g of fibers), 3.3 g of ash, etc. Of these nutrients, protein and carbohydrates are the main ingredients of raw sauce. Raw bean paste consists mainly of red bean endosperm and germ. The endosperm part and germ part are originally white or grayish white, but have a unique red bean color by adsorbing the pigment component of the seed coat. The seed coat of red beans is composed of hard shelf cells and occupies 10-11 wt% of the total weight of the red beans, and this seed coat contains most of the polyphenols and saponins in the red beans.

特開2003−250476号公報JP 2003-250476 A

ところで、白あんの製造では、乾燥小豆から種皮を機械的に剥ぎ取って残った胚乳および胚芽や、しばらく水に浸漬した小豆から種皮を剥ぎ取って残った胚乳および胚芽が原料として使用される。すなわち、前記のように種皮が除去された胚乳および胚芽に、煮炊、磨砕、ろ別、水さらし、脱水などを施して白い練小豆を得ている。
しかしながら、製あんにおける篩分け工程S9(図4)で生じたあん粕Lや、白あん製造のために取り除かれた種皮は、既述したように有用成分(ポリフェノール、サポニン、カリウムなど)を多量に含有しているにも拘わらず、何ら利用されることなく産業廃棄物として処分されていたのである。
By the way, in the production of white bean, the endosperm and the germ remaining after mechanically peeling the seed coat from the dried red beans, and the endosperm and the germ remaining after peeling the seed coat from the red beans soaked in water for a while are used as raw materials. That is, the endosperm and germ from which the seed coat has been removed as described above are boiled, ground, filtered, exposed to water, dehydrated, and the like to obtain white kneaded red beans.
However, as described above, the soy sauce L produced in the sieving step S9 (FIG. 4) and the seed coat removed for the production of white sauce contain a large amount of useful components (polyphenol, saponin, potassium, etc.). Despite being contained, it was disposed of as industrial waste without any use.

本発明は、上記した従来の問題点に鑑みてなされたものであって、小豆の種皮から、または該種皮を多く含むあん粕から効率よく製造されて、小豆由来の有用成分を多量に含む食品材料、食品、および食品材料の製造方法の提供を目的とする。   The present invention has been made in view of the above-described conventional problems, and is efficiently produced from red bean seed coat or an anchovy containing a large amount of the seed coat, and contains a large amount of useful components derived from red beans. An object is to provide a material, a food, and a method for producing the food material.

上記目的を達成するために、本発明に係る食品材料は、小豆の種皮または小豆のあん粕を煮炊し、煮炊した小豆の種皮または小豆のあん粕から分離した煮汁を加熱し常圧下で蒸発させて得られた濃縮液から成る構成にしてある。   In order to achieve the above object, the food material according to the present invention is prepared by boiling a red bean seed coat or red bean paste, heating the boiled red bean seed coat or red bean paste and heating under normal pressure. It is made up of a concentrated solution obtained by evaporation.

また、本発明に係る食品は、前記構成の食品材料を含んで成るものである。   Moreover, the foodstuff which concerns on this invention comprises the foodstuff material of the said structure.

そして、本発明に係る食品材料の製造方法は、小豆の種皮または小豆のあん粕を煮炊し、煮炊した小豆の種皮または小豆のあん粕から分離した煮汁を常圧下で蒸発する温度に加熱し、加熱した煮汁を常圧下で蒸発させることにより濃縮して食品材料を得るものである。   The method for producing a food material according to the present invention includes cooking a red bean seed coat or red bean paste, and heating the boiled broth separated from the cooked red bean seed coat or red bean paste to a temperature at which it evaporates under normal pressure. Then, the heated boiled juice is concentrated by evaporation under normal pressure to obtain a food material.

以上詳述したように、本発明によれば、常圧下における蒸発温度で煮汁を加熱したことにより腐敗菌が殺菌されるとともに濃縮に伴って抗菌性が高まり腐敗しにくくなる。従って、抗菌性ないし殺菌性が高く保存性に優れた小豆の種皮由来の安全な食品材料を得ることができる。本発明により得た食品材料は渋味がないうえ、有用成分を多く含み、濃縮倍率によって有用成分の含有量を加減することもできる。また、本発明製法は常圧下で実施されるので簡素な構成で済み、発泡や飛沫ロスの問題を生じることがない。特に、ポリフェノールなどの有用成分を多量に含む種皮の煮汁から食品材料を製造するので、従来技術のように小豆全体の煮汁から食品材料を製造する場合と比べて、製造装置の規模や所要エネルギーが小さくて済み効率よく食品材料を得ることができる。そのうえ、これまではそのまま廃棄物処理されていた種皮を有効に活用できる。そして、種皮の磨砕片から成るあん粕にも相当量の有用成分が残存していることから、種皮の場合と同様、あん粕からも余すことなく、有用成分を含む食品材料を得ることができる。   As described in detail above, according to the present invention, the rot bacteria are sterilized by heating the broth at the evaporation temperature under normal pressure, and the antibacterial property increases with concentration, making it difficult to rot. Therefore, it is possible to obtain a safe food material derived from red bean seed coat having high antibacterial and bactericidal properties and excellent storage stability. The food material obtained according to the present invention has no astringency, contains many useful ingredients, and can adjust the content of useful ingredients depending on the concentration factor. In addition, since the production method of the present invention is carried out under normal pressure, a simple structure is sufficient, and there is no problem of foaming or splash loss. In particular, since food materials are produced from the soup of seed coats containing a large amount of useful components such as polyphenols, compared to the case of producing food materials from the soup of whole red beans as in the prior art, the scale and required energy of the production equipment are reduced. The food material can be obtained efficiently with a small size. In addition, seed coats that have been treated as waste can be used effectively. And since a considerable amount of useful ingredients remain in the groundnut made from the ground pieces of seed coat, a food material containing useful ingredients can be obtained without leaving any excess from the sauce like in the case of seed coat. .

また、本発明の食品材料を用いた食品は、渋味が付加されず、ポリフェノールなどの有用成分を多量に含むこととなり、食しやすい健康食品として好適である。   Moreover, the foodstuff using the food material of this invention does not add astringency, contains a lot of useful components, such as polyphenol, and is suitable as an easy-to-eat health food.

以下、本発明の実施の形態を図面に基づいて説明する。
図1は本発明の一実施形態に係る食品材料を製造するための加熱濃縮装置を示す概略構成図である。
加熱濃縮装置1は、煮汁を加熱する加熱機2と、加熱した煮汁から蒸発分を蒸発させて煮汁を濃縮する大気開放式の濃縮機3とから主に構成されている。濃縮機3の上方には濃縮機3からの蒸発分を排気処理する排気装置4が配備されている。加熱機2内には加熱管8が通され、加熱管8は供給管16から供給される熱源15(ここでは飽和蒸気圧が0.245MPa.G程度の水蒸気)により加熱されるようになっている。熱源15としては、原料煮汁を常圧下で蒸発(沸騰)し得る温度に加熱できるものであれば特に限定されないが、前記の水蒸気以外に、例えばガスバーナ、オイルバーナ、電気ヒータなどが挙げられる。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic configuration diagram showing a heating and concentration apparatus for producing a food material according to an embodiment of the present invention.
The heating and concentration apparatus 1 mainly includes a heater 2 for heating the broth and an open-air type concentrator 3 for concentrating the broth by evaporating evaporated components from the heated broth. Above the concentrator 3, an exhaust device 4 for exhausting the evaporated component from the concentrator 3 is disposed. A heating pipe 8 is passed through the heater 2, and the heating pipe 8 is heated by a heat source 15 supplied from a supply pipe 16 (here, steam having a saturated vapor pressure of about 0.245 MPa.G). Yes. The heat source 15 is not particularly limited as long as it can be heated to a temperature at which the raw material soup can evaporate (boiling) under normal pressure. Examples of the heat source 15 include a gas burner, an oil burner, and an electric heater.

そして、加熱管8の一端は濃縮機3への移送管9とつながり、加熱管8の他端は煮汁を一時的に貯留する貯留槽5からの供給配管7とつながっている。供給配管7の途中には供給ポンプ6が配備されている。濃縮機3の底部には循環配管10の一端が接続され、循環配管10の他端は加熱機2手前の供給配管7に接続されている。循環配管10の途中には循環ポンプ11が配備されている。循環ポンプ11出側における循環配管10には、得られた濃縮液を取り出すための取出配管12が分岐接続されている。そして、分岐位置よりも下流側の循環配管10に開閉弁13が設けられ、取出配管12にも開閉弁14が設けられている。   And one end of the heating pipe 8 is connected to the transfer pipe 9 to the concentrator 3, and the other end of the heating pipe 8 is connected to the supply pipe 7 from the storage tank 5 for temporarily storing the broth. A supply pump 6 is arranged in the middle of the supply pipe 7. One end of the circulation pipe 10 is connected to the bottom of the concentrator 3, and the other end of the circulation pipe 10 is connected to the supply pipe 7 in front of the heater 2. A circulation pump 11 is provided in the middle of the circulation pipe 10. An extraction pipe 12 for taking out the obtained concentrated liquid is branched and connected to the circulation pipe 10 on the outlet side of the circulation pump 11. An open / close valve 13 is provided in the circulation pipe 10 downstream of the branch position, and an open / close valve 14 is provided in the take-out pipe 12.

ここで、小豆の種皮から食品材料を製造する態様を図2を参照しながら説明する。まず、小豆の種皮Dを用意する。この種皮Dは、乾燥小豆から機械的に剥ぎ取って得られたもの、あるいは乾燥小豆をしばらく水に浸漬したのちに剥ぎ取って得られたものでも構わない。10kgの種皮Dを入れた煮釜に水30Lを給水し、そのまま常温(20〜30℃)で10時間程度浸漬させる(浸漬工程S21)。次に、煮炊工程S22において種皮Dを常圧下110℃で40分間煮炊する。これにより、種皮Dから渋が抽出されて煮汁に移行する。種皮Dおよび煮汁をそのまま放置して自然冷却し常温近くまで温度を低下させる(工程S23)。温度の下がった種皮Dおよび煮汁を円筒型スクリーンで篩分けし、篩に留まった粕Eと、篩を通過した煮汁Iとに分別する(篩分け工程S24)。円筒型スクリーンによる篩分けは、目開き1mmのパルパー型篩と目開き0.5mmのフィニシャー型篩を順次用いて行なった。   Here, the aspect which manufactures food material from the seed coat of red beans is demonstrated, referring FIG. First, the seed coat D of red beans is prepared. The seed coat D may be obtained by mechanically peeling off dried red beans, or obtained by immersing the dried red beans in water for a while and then peeling them off. 30 L of water is supplied to a boiled pot containing 10 kg of seed coat D, and is immersed as it is at room temperature (20 to 30 ° C.) for about 10 hours (immersion step S21). Next, in the cooking step S22, the seed coat D is cooked for 40 minutes at 110 ° C. under normal pressure. Thereby, astringent is extracted from the seed coat D, and it transfers to boiled juice. The seed coat D and the broth are left as they are, and then naturally cooled to lower the temperature to near room temperature (step S23). The seed coat D and the broth having fallen in temperature are sieved with a cylindrical screen, and are separated into rice cake E remaining on the sieve and the broth I passing through the sieve (sieving step S24). The sieving with the cylindrical screen was performed using a pulper type sieve having an opening of 1 mm and a finisher type sieve having an opening of 0.5 mm.

上記の粕Eは種皮Dの固形分とわずかな水分とから成っており、固形分には有用なポリフェノールやサポニンが比較的多量に残っている。そこで、粕Eを煮釜に入れて水10Lを給水し、再び常圧下110℃で40分間煮炊した(煮炊工程S27)。煮炊した粕Eを前記と同様に円筒型スクリーンでパルパー型篩とフィニシャー型篩を順次用いて篩分けし(篩分け工程S28)、粕Fを分別した。篩分け工程S28で分離された煮汁は先の篩分け工程S24の円筒型スクリーンで分離された煮汁Iと混合される(混合工程S25)。混合工程S25で混合された煮汁は遠心分離機(回転数3000rpm)にかけられて沈降粕Gと煮汁Jとに分離される(遠心分離工程S29)。沈降粕Gは篩分け工程S28からの粕Fと混合されて固形分Hとなる。この固形分Hはほとんどが食物繊維から成る食品材料として利用される。固形分Hは種皮Dの粉砕物とわずかな水分とから成っている。   The cocoon E is composed of a solid content of seed coat D and a slight amount of water, and a relatively large amount of useful polyphenols and saponins remain in the solid content. Therefore, the rice cake E was put into a boiling pot, 10 L of water was supplied, and the mixture was again boiled for 40 minutes at 110 ° C. under normal pressure (boiling step S27). The boiled rice cake E was sieved using a pulper type sieve and a finisher type sieve in order using a cylindrical screen in the same manner as above (screening step S28), and rice cake F was fractionated. The broth separated in the sieving step S28 is mixed with the broth I separated in the cylindrical screen of the previous sieving step S24 (mixing step S25). The boiled juice mixed in the mixing step S25 is subjected to a centrifuge (number of revolutions 3000 rpm) and separated into the sediment G and the broth J (centrifugal step S29). The settled soot G is mixed with the soot F from the sieving step S28 to become a solid content H. This solid content H is mostly used as a food material composed of dietary fiber. The solid content H consists of a ground product of seed coat D and a slight amount of moisture.

一方、遠心分離工程S29で分離された煮汁Jは約30Lであり、赤みを帯びてほとんど透明で清浄な液体であった。このようにして得られた煮汁Jは加熱濃縮装置1で処理される。煮汁Jはいったん貯留槽5に貯留される。貯留槽5の煮汁Jは供給ポンプ6で供給配管7に送り出され、加熱機2の加熱管8を通過する際に加熱される(加熱工程S30)。加熱機2で沸騰温度(100〜105℃程度)に加熱された煮汁Jは移送管9から濃縮機3内に勢いよく吹き込まれる。大気開放下(常圧下)の濃縮機3内で、煮汁Aは水分その他の蒸発分が蒸発して濃縮される(濃縮工程S31)。煮汁Jから生じた蒸発分は排気装置4に吸引され凝縮後に排水処理される。すなわち、前記の加熱工程S30と濃縮工程S31とから、種皮由来の煮汁Jを加熱濃縮して濃縮液Kを得る加熱濃縮工程が構成される。   On the other hand, the broth J separated in the centrifugal separation step S29 was about 30 L, and it was reddish and almost transparent and clean. The soup J obtained in this way is processed by the heating concentration apparatus 1. The broth J is once stored in the storage tank 5. The broth J in the storage tank 5 is sent to the supply pipe 7 by the supply pump 6 and heated when passing through the heating pipe 8 of the heater 2 (heating step S30). The broth J heated to the boiling temperature (about 100 to 105 ° C.) by the heater 2 is blown into the concentrator 3 vigorously from the transfer tube 9. In the concentrator 3 under open air (under normal pressure), the soup A is concentrated by evaporating moisture and other evaporated components (concentration step S31). The evaporated portion generated from the broth J is sucked into the exhaust device 4 and condensed after being drained. That is, the heating and concentration step in which the concentrated liquid K is obtained by heating and concentrating the seed juice-derived boiled juice J is constituted by the heating step S30 and the concentration step S31.

そして、濃縮機3で濃縮された煮汁Jの濃縮液は循環ポンプ11により開閉弁13および循環配管10を経て供給配管7に戻され、加熱濃縮が繰り返される。そうして、濃縮液の濃縮倍率が所望の倍率に達したとき開閉弁14を開けることにより、取出配管12から濃縮液Kが取り出される。濃縮液Kの濃縮倍率は、適時にサンプリングした煮汁Jおよび濃縮液についてそれぞれ測定したBrix糖度から算出される。
この例において、煮汁Jの糖度は1.3°Brix、濃縮液Kの糖度は5.9°Brixであり、濃縮倍率は4.5倍であった。
And the concentrate of the boiled juice J concentrated by the concentrator 3 is returned to the supply piping 7 through the on-off valve 13 and the circulation piping 10 by the circulation pump 11, and heating concentration is repeated. Then, when the concentration ratio of the concentrate reaches a desired ratio, the concentrate K is extracted from the extraction pipe 12 by opening the on-off valve 14. The concentration ratio of the concentrated solution K is calculated from the Brix sugar content measured for each of the boiled juice J and the concentrated solution sampled in a timely manner.
In this example, the sugar content of the broth J was 1.3 ° Brix, the sugar content of the concentrate K was 5.9 ° Brix, and the concentration factor was 4.5 times.

そして、煮汁Jおよび濃縮液Kについて、ポリフェノールとサポニンの含有量を測定した。ポリフェノールの含有量はFolin-Denis法によりタンニン酸を標準物質として測定した。また、サポニンの含有量はリッチ画分法に従って測定した。
「煮汁J」
ポリフェノール 139.2mg/100mL
サポニン 8.5mg/100mL
「濃縮液K」
ポリフェノール 665.5mg/100mL
サポニン 37.8mg/100mL
測定結果から明らかなように、煮汁Jを加熱濃縮処理してもポリフェノールの含有量は減っていない。すなわち、この加熱濃縮処理によれば、ポリフェノールを分解させないで済むことがわかる。
And about the broth J and the concentrate K, content of polyphenol and saponin was measured. The content of polyphenol was measured by Folin-Denis method using tannic acid as a standard substance. The saponin content was measured according to the rich fraction method.
"Boiled soup J"
Polyphenol 139.2mg / 100mL
Saponin 8.5mg / 100mL
"Concentrate K"
Polyphenol 665.5mg / 100mL
Saponin 37.8mg / 100mL
As is clear from the measurement results, the content of polyphenol is not reduced even when the broth J is heated and concentrated. That is, according to this heat concentration treatment, it is understood that polyphenols need not be decomposed.

濃縮液Kは煮汁Jに存在していた枯草菌などの腐敗菌が高温(常圧煮沸)での加熱処理により殺菌され、直後の濃縮により腐敗菌その他を寄せつけなくなったためと考えられる。因みに、煮汁Jに糖、塩、酢を添加した場合も腐敗しにくくなるが、抗菌性は向上していない。   It is considered that the concentrate K was sterilized by heat treatment at high temperature (normal pressure boiling), such as Bacillus subtilis present in the broth J, and the rotten bacteria and others were not brought close by concentration immediately thereafter. Incidentally, even when sugar, salt and vinegar are added to the broth J, it becomes difficult to rot, but antibacterial properties have not improved.

一方、濃縮液Kを水で還元(4.5倍希釈)した飲料を試飲したところ、渋味は感じなかった。これは100℃前後の加熱により、煮汁J中の渋いサポニンが渋味のないサポゲニンに変化し、同じく渋いタンニンも渋味のない重合物に変化したためと考えられる。   On the other hand, when the beverage obtained by reducing the concentrate K with water (diluted 4.5 times) was sampled, no astringency was felt. This is presumably because the astringent saponin in the broth J was changed to a sapogenin with no astringency, and the astringent tannin was also changed to a polymer without astringency by heating at around 100 ° C.

尚、低温(常温程度)下での減圧濃縮によっても煮汁Jを濃縮することはできるが、サポニンに起因する厄介な発泡の問題を生じ、飛沫ロスが多くなる。また、温度に関して殺菌作用を持たないので、抗菌性が出現しない。因みに、1週間位でカビが発生し腐敗が進んだ。更に2週間もすると、腐敗の進行による自然の泡立ちが始まった。   Although the juice J can be concentrated by vacuum concentration at a low temperature (about room temperature), it causes troublesome foaming problems due to saponins, resulting in increased droplet loss. Moreover, since it does not have a bactericidal action regarding temperature, antibacterial properties do not appear. By the way, mold occurred in about a week, and corruption progressed. After another two weeks, the natural bubbling started as the decay progressed.

続いて、上記で得られた濃縮液Kを食品材料として用いて食品を調製した例を以下に示す。
[調製例1・・・缶詰プリン]
「配合」
牛乳 3800mL
濃縮液K(4.5倍濃縮) 40mL
卵 2000g
砂糖 1900g
バター 7g
バニラエッセンス 12mL
カラメル 5〜600g
前記の配合により202mm径75g入りの缶詰プリン100缶(総7500g)を得た。
Then, the example which prepared the foodstuff using the concentrate K obtained above as a foodstuff material is shown below.
[Preparation Example 1 ... Canned Pudding]
"Combination"
Milk 3800mL
Concentrate K (4.5 times concentrated) 40 mL
2000g egg
1900g sugar
7g butter
12ml vanilla extract
Caramel 5-600g
According to the above formulation, 100 cans of canned pudding (total 7500 g) with a diameter of 202 g and 75 g were obtained.

[調製例2・・・濃厚ドリンク]
「配合」
濃縮液K(4.5倍濃縮) 300mL
黒砂糖 90g
昆布微粉末 20g
アルコール 5mL
水 残分
前記の配合により濃厚ドリンク500mLを得た。
[Preparation Example 2 ... Dense drink]
"Combination"
Concentrate K (4.5 times concentrated) 300 mL
90g brown sugar
Kelp fine powder 20g
Alcohol 5mL
Water residue 500 mL of a concentrated drink was obtained by the above formulation.

前記した調製例1,2の食品はそれぞれの食品種に応じた通常の保存条件下で放置しても腐敗しにくく、濃縮液K(食品材料)を含まない食品と同等の保存性を示した。また、食味も濃縮液Kを含まない食品とほとんど変わることがなかった。一方で、有用成分(ポリフェノール、サポニン、カリウムなど)を多量に含んでいる。従って、各調製例の食品は食しやすい健康食品として有用に提供される。   The foods of Preparation Examples 1 and 2 described above were not easily spoiled even when left under normal storage conditions corresponding to each food type, and exhibited the same storage stability as foods that did not contain the concentrate K (food material). . In addition, the taste was almost the same as that of the food containing no concentrate K. On the other hand, it contains a large amount of useful components (polyphenol, saponin, potassium, etc.). Therefore, the food of each preparation example is usefully provided as an easy-to-eat health food.

次に、生あん製造における本煮炊、磨砕後の篩分け(図4の篩分け工程S9)で生あんから分別されたあん粕Lを用いて食品材料を製造する例を用いて説明する。あん粕Lはほとんど種皮の磨砕片から成り、ポリフェノールやサポニンなどが残存している。まず、貯蔵のために乾燥させていたあん粕Lの400gを煮釜に入れ、この煮釜に、水10Lと、あん粕Lに対し0.5wt%の重曹Mとを投入し、常温(20〜30℃)で10時間程度浸漬させる(浸漬工程S41)。次に、煮炊工程S42においてあん粕Lを常圧下110℃で40分間煮炊する(煮炊工程S42)。かかる弱アルカリ熱水抽出により、あん粕L中の種皮Dから渋が抽出されて煮汁に移行する。あん粕Lおよび煮汁を放置により自然冷却して常温近くまで温度を低下させる(冷却工程S43)。冷やしたあん粕Lを磨砕機で微小に磨砕し(磨砕工程S44)、煮釜中のあん粕Lおよび煮汁にクエン酸などを加えて中和する(中和工程S45)。
中和後のあん粕Lおよび煮汁をろ過機にかけて粕Nと煮汁Oとにろ別する(ろ別工程S46)。粕Nは搾汁機で更に煮汁を搾りだし(搾汁工程S48)、ろ別工程S46からの煮汁Oと混合する(混合工程S47)。混合工程S47で混合された煮汁は3000rpmの遠心分離機にかけられて沈降粕Qと煮汁Sとに分離される(遠心分離工程S49)。沈降粕Qは搾汁工程S48で搾汁機に残った粕Pと混合されて固形分Rとなる。この固形分Rは主に食物繊維から成っており、食品材料として健康食品などに使用される。固形分Rは種皮Dの粉砕物とわずかな水分とから成っており、有用なポリフェノールやサポニンを比較的多く含んでいる。
Next, a description will be given by using an example of producing food material using the ground bean paste L that has been separated from the raw bean paste in the simmered cooking and the sieving after grinding (sieving step S9 in FIG. 4). . Anzu L consists mostly of ground seed pieces, and polyphenols and saponins remain. First, 400 g of Anzu L that had been dried for storage was placed in a boiling pot, and 10 L of water and 0.5 wt% baking soda M were added to the boiling pot at room temperature (20 (About 30 ° C.) for about 10 hours (dipping step S41). Next, in the cooking step S42, the Anzu L is cooked for 40 minutes at 110 ° C. under normal pressure (cooking step S42). By this weak alkaline hot water extraction, the astringent is extracted from the seed coat D in the anchovy L and transferred to the broth. The anzu L and boiled juice are naturally cooled by leaving them to cool to near room temperature (cooling step S43). The chilled ground bean paste L is finely ground with a grinder (grinding step S44), and neutralized by adding citric acid or the like to the ground bean paste L and the broth in the boiling pot (neutralizing step S45).
The neutralized Anmochi L and boiled juice are filtered through a filter to obtain Niwa and Nojiru O (filtering step S46).粕 N further squeezes the broth with a squeezer (squeezing step S48) and mixes with the broth O from the filtration step S46 (mixing step S47). The broth mixed in the mixing step S47 is subjected to a centrifuge at 3000 rpm and separated into the sedimentation slag Q and the broth S (centrifugation step S49). The settling slag Q is mixed with the slag P remaining in the squeezing machine in the squeezing step S48 to become a solid content R. This solid content R is mainly composed of dietary fiber and is used as a food material in health foods and the like. The solid content R consists of a ground product of seed coat D and a slight amount of water, and contains a relatively large amount of useful polyphenols and saponins.

遠心分離工程S49での分離により得た煮汁Sは約7Lであり、赤みを帯びたほとんど透明で清浄な液体であった。このようにして得られた煮汁Sは加熱濃縮装置1で処理される。煮汁Sはいったん貯留槽5に貯留される。貯留槽5の煮汁Sは供給ポンプ6で供給配管7に送り出され、加熱機2の加熱管8を通過する際に加熱される(加熱工程S50)。加熱機2で沸騰温度(100〜105℃程度)に加熱された煮汁Sは移送管9から濃縮機3内に勢いよく吹き込まれる。大気開放下(常圧下)の濃縮機3内で煮汁Sは水分その他の蒸発分が蒸発し、約1/5に濃縮されて約1.4Lの濃縮液Tが得られた(濃縮工程S51)。濃縮液T中のポリフェノールは350.5mg/100mLであった。煮汁Sから生じた蒸発分は排気装置4に吸引され凝縮後に排水処理される。すなわち、前記の加熱工程S50と濃縮工程S51とから、煮汁Sを加熱濃縮して濃縮液Tを得る加熱濃縮工程が構成される。   The broth S obtained by the separation in the centrifugal separation step S49 was about 7 L, which was a reddish almost transparent and clean liquid. The soup S thus obtained is processed by the heating and concentration apparatus 1. The broth S is once stored in the storage tank 5. The broth S in the storage tank 5 is sent out to the supply pipe 7 by the supply pump 6 and heated when passing through the heating pipe 8 of the heater 2 (heating step S50). The broth S heated to the boiling temperature (about 100 to 105 ° C.) by the heater 2 is blown into the concentrator 3 vigorously from the transfer tube 9. In the concentrator 3 under the open atmosphere (under normal pressure), the water and other evaporated components of the broth S were evaporated and concentrated to about 1/5 to obtain about 1.4 L of concentrated liquid T (concentration step S51). . The polyphenol in the concentrate T was 350.5 mg / 100 mL. The evaporated portion generated from the broth S is sucked into the exhaust device 4 and condensed after being drained. That is, the heating concentration step of obtaining the concentrated liquid T by heating and concentrating the broth S is constituted by the heating step S50 and the concentration step S51.

このように、あん粕Lを原料として得られた濃縮液Tは、種皮Dを原料として得られた濃縮液Kと比べると、ポリフェノールおよびカテキンの含有量が小さい。しかしながら、飲用品としての支障はなく、赤飯用の天然着色料などの食品材料として利用することも可能である。   As described above, the concentrate T obtained from the bean paste L as a raw material has a smaller content of polyphenols and catechins than the concentrate K obtained from the seed coat D as a raw material. However, there is no hindrance as a drink, and it can be used as a food material such as a natural colorant for red rice.

尚、小豆の種皮Dから食品材料を製造する場合(図2の工程図参照)において、篩分け工程S24で分別した粕Eに関して給水工程S26、煮炊工程S27、篩分け工程S28、および混合工程S25の処理を施すことなく、篩分け工程S24からの煮汁Iのみを2点鎖線で示すように遠心分離(工程S29)して得た煮汁Jを加熱濃縮装置1で加熱濃縮処理して濃縮液を得る態様も本発明に含まれる。   In addition, when manufacturing food materials from the seed coat D of red beans (refer to the process diagram of FIG. 2), the water supply process S26, the cooking process S27, the sieving process S28, and the mixing process for the rice cake E sorted in the sieving process S24. Without performing the process of S25, the boiled juice J obtained by centrifuging only the broth I from the sieving step S24 as indicated by the two-dot chain line (step S29) is heated and concentrated in the heating and concentrating device 1 to be concentrated. An embodiment of obtaining the above is also included in the present invention.

同様に、小豆のあん粕Lから食品材料を製造する場合(図3の工程図参照)において、ろ別工程S46でろ別した粕Nに関して搾汁工程S48および混合工程S47の処理を施すことなく、ろ別工程S46からの煮汁Oのみを2点鎖線で示すように遠心分離(S29)して得た煮汁Sを加熱濃縮装置1で加熱濃縮処理して濃縮液を得る態様も本発明にふくまれる。   Similarly, when producing food materials from red bean paste L (see the process diagram of FIG. 3), without performing the processing of the squeezing step S48 and the mixing step S47 for the strawberry N filtered in the filtration step S46, The present invention also includes an embodiment in which only the broth O from the filtration step S46 is centrifuged (S29) as shown by a two-dot chain line to obtain a concentrate by heating and concentrating with the heating and concentration apparatus 1. .

本発明の一実施形態に係る食品材料を製造するための加熱濃縮装置を示す概略構成図である。It is a schematic block diagram which shows the heating concentration apparatus for manufacturing the food material which concerns on one Embodiment of this invention. 前記加熱濃縮装置を用いて種皮から食品材料を製造する工程を示す工程図である。It is process drawing which shows the process of manufacturing food material from a seed coat using the said heating concentration apparatus. 前記加熱濃縮装置を用いてあん粕から食品材料を製造する工程を示す工程図である。It is process drawing which shows the process of manufacturing food material from an anther using the said heating concentration apparatus. 一般的な生あん製造工程を示す工程図である。It is process drawing which shows a general raw sauce manufacturing process.

符号の説明Explanation of symbols

1 加熱濃縮装置
2 加熱機
3 濃縮機
D 種皮
L あん粕
I,J,O,S 煮汁
K,T 濃縮液(食品材料)
S22,S27,S42 煮炊工程
S30,S50 加熱工程
S31,S51 濃縮工程
DESCRIPTION OF SYMBOLS 1 Heating concentration apparatus 2 Heating machine 3 Concentrator D Seed coat L Anzu I, J, O, S Boiled juice K, T Concentrated liquid (foodstuff material)
S22, S27, S42 Cooking step S30, S50 Heating step S31, S51 Concentration step

Claims (3)

小豆の種皮または小豆のあん粕を煮炊し、煮炊した小豆の種皮または小豆のあん粕から分離した煮汁を加熱し常圧下で蒸発させて得られた濃縮液から成ることを特徴とする食品材料。 Boiled and cooked red bean seed coat or red bean seed meal, and a concentrated food obtained by heating and evaporating the boiled broth separated from the cooked red bean seed coat or red bean paste under normal pressure material. 請求項1に記載の食品材料を含んで成る食品。 A food comprising the food material according to claim 1. 小豆の種皮または小豆のあん粕を煮炊し、煮炊した小豆の種皮または小豆のあん粕から分離した煮汁を常圧下で蒸発する温度に加熱し、加熱した煮汁を常圧下で蒸発させることにより濃縮して食品材料を得ることを特徴とする食品材料の製造方法。 By boiling the red bean seed coat or red bean paste, heating the broth separated from the cooked red bean seed coat or red bean paste to a temperature that evaporates under normal pressure, and evaporating the heated broth under normal pressure A method for producing a food material, characterized by being concentrated to obtain a food material.
JP2004340449A 2004-11-25 2004-11-25 Food material, food, and method for producing the food material Pending JP2006149219A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008295365A (en) * 2007-05-31 2008-12-11 Cosmo Shokuhin Kk Method for producing azuki bean-color coloring agent

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008295365A (en) * 2007-05-31 2008-12-11 Cosmo Shokuhin Kk Method for producing azuki bean-color coloring agent

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