JP2008271820A - Effervescence stabilizer, and food and drink added with effervescence stabilizer - Google Patents

Effervescence stabilizer, and food and drink added with effervescence stabilizer Download PDF

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JP2008271820A
JP2008271820A JP2007117929A JP2007117929A JP2008271820A JP 2008271820 A JP2008271820 A JP 2008271820A JP 2007117929 A JP2007117929 A JP 2007117929A JP 2007117929 A JP2007117929 A JP 2007117929A JP 2008271820 A JP2008271820 A JP 2008271820A
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yeast
cell wall
yeast cell
soluble fraction
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Kazuhiro Tamaoki
和弘 玉置
Tetsuya Ishida
哲也 石田
Atsushi Ouchi
敦史 大内
Yoshikazu Tanaka
美和 田中
Tetsuji Kotani
哲司 小谷
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Asahi Breweries Ltd
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<P>PROBLEM TO BE SOLVED: To offer an effervescent of natural derivation which can be added to food and drink and an effervescence stabilizer. <P>SOLUTION: The invention refers to the effervescent and the effervescence stabilizer of yeast cell wall derived soluble fraction, and by adding the effervescent stabilizer to the food and drink, they are given with the foamability and the effervescence stabilization nature. The yeast cell wall derived soluble fraction is the yeast soluble fraction obtained from the yeast containing the soluble fractions or yeast cell wall soluble fraction release capability derived from enzymatic treatment, alkaline treatment and acidic treatment of the debris after removing soluble component in the yeast cell. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、酵母細胞壁可溶性画分から得られる飲食品の泡安定化剤であり、当該泡安定化剤を含有する飲食品に関する。   The present invention is a foam stabilizer for foods and drinks obtained from a yeast cell wall soluble fraction, and relates to a food and drink containing the foam stabilizers.

飲食品にビールのような泡を付与したり、あるいはビールなどの発泡性飲料の泡の安定化を図ることは消費者の嗜好性にマッチした商品を開発するにあたり、重要な商品特性となる。これまで、飲食品の起泡剤及び発酵麦芽飲料(ビール等)の泡安定化剤としては複数の素材が提案されている。   Giving bubbles such as beer to foods and beverages, or stabilizing the foam of effervescent beverages such as beer is an important product characteristic in developing products that match consumer preferences. So far, a plurality of materials have been proposed as a foaming agent for foods and drinks and a foam stabilizer for fermented malt beverages (such as beer).

ビールや発泡酒のような麦芽とホップと水を主原料とするアルコール炭酸飲料は飲用時に液面を覆うクリーミーな泡が形成され、飲料の嗜好性を高めている。ビールの泡は麦芽由来の泡タンパクとホップ成分が結合し膜を形成し、その膜に空気が巻き込まれることにより形成されている。近年では、消費者の嗜好の多様性に応じて、原料に麦芽以外の糖質を用いるビアテイスト飲料(第3のビール)も開発されている。しかしながら、このようなビアテイスト飲料は麦芽由来の泡タンパクが存在しないため、ビールの特徴である泡品質(起泡性、泡付き、泡持ちなど)と比較しても劣っているのが現状である。   Alcohol carbonated drinks mainly composed of malt such as beer and sparkling liquor, hops and water are formed with creamy bubbles that cover the liquid surface during drinking, thereby enhancing the taste of the drink. The foam of beer is formed by combining a foam protein derived from malt and a hop component to form a film, and air is entrained in the film. In recent years, beer-taste beverages (third beer) that use sugars other than malt as raw materials have been developed according to the variety of consumer preferences. However, such beer-taste beverages are inferior to the foam quality (foaming, foamy, foamy, etc.) that is characteristic of beer because there is no malt-derived foam protein. is there.

ビールの泡を安定化するために、増粘性多糖類であるジェランガムを添加する方法(特許文献1、特許文献2)、キサンタンガムまたはガラクトマンナンを添加する方法(特許文献3)、キサンタンガムと低温水溶性タンパク質(コラーゲン、ゼラチン、乳タンパクなど)を添加する方法(特許文献4)、糖重合物(ポリデキストロース)を添加する方法(特許文献5)、ホップ苞溶媒抽出物を添加する方法(特許文献6)などが開示されている。   In order to stabilize the foam of beer, a method of adding gellan gum which is a thickening polysaccharide (Patent Document 1, Patent Document 2), a method of adding xanthan gum or galactomannan (Patent Document 3), xanthan gum and low-temperature water solubility A method of adding protein (collagen, gelatin, milk protein, etc.) (Patent Document 4), a method of adding a sugar polymer (polydextrose) (Patent Document 5), a method of adding a hop koji solvent extract (Patent Document 6) ) Etc. are disclosed.

また、ビアテイスト飲料や果汁を含むビール様起泡性飲料については、植物由来のサポニンを起泡剤として添加する方法(特許文献7)、植物から抽出したサポニン系と化学的に合成されたグリセリン脂肪酸エステル系、プロピレングリコール脂肪酸エステル系からなる起泡剤と増粘安定剤として作用し、飲料に適当な粘度を与え泡持ちを良くする寒天、ゼラチン、キサンタンガム、カラギーナン、ペクチン、タマリンドガム、ジェランガム、ローカストビーンガム等の泡保持剤を添加する方法(特許文献8)、茶葉の水またはエタノール抽出物を添加する方法(特許文献9)などが開示されている。   In addition, for beer-like foaming beverages including beer-taste beverages and fruit juices, a method of adding plant-derived saponin as a foaming agent (Patent Document 7), a saponin system extracted from plants and chemically synthesized glycerin Agar, gelatin, xanthan gum, carrageenan, pectin, tamarind gum, gellan gum, which acts as a foaming agent and thickening stabilizer consisting of fatty acid ester type, propylene glycol fatty acid ester type, giving appropriate viscosity to beverages and improving foam retention A method of adding a foam retaining agent such as locust bean gum (Patent Document 8), a method of adding tea leaf water or an ethanol extract (Patent Document 9), and the like are disclosed.

ビアテイスト飲料においては、窒素源として細胞壁を除いた酵母エキスを使用する方法(特許文献10)も開示されているが、酵母細胞壁が除かれているため、泡の安定化効果はほとんどみられない。   In beer-taste beverages, a method using a yeast extract excluding the cell wall as a nitrogen source is also disclosed (Patent Document 10), but since the yeast cell wall is removed, the effect of stabilizing the foam is hardly seen. .

天然物由来の水溶性の食物繊維としてはコンニャクマンナン、ペクチン、グァーガム、タマリンド種子ガム、カラギーナンなどの多糖類が飲食品素材として利用されているが、それらはいずれも水に対する溶解性、色、味、臭い、等のいくつかの点で問題がある。更に、これらは粘度が高く(通常103cps/1%以上、25℃)、汎用性に欠け、特定の分野にしか利用できず。また、飲食品素材として広く用いられているポリデキストロースは合成品であり、天然志向の消費者意識にマッチしていない。従って、飲料用の食物繊維としては、白色、無味無臭で水溶性が高い低粘性の天然物由来の素材が望まれている。
特開平4-228060号公報 特開平4-22806号公報 米国特許第4720389号明細書 米国特許第4729900号明細書 特表2004-536604公報 特許3551995号号公報 特開昭60-126065号公報 特開平11-299473号公報 WO2003/105610パンフレット 特開2005-323585号公報
As water-soluble dietary fiber derived from natural products, polysaccharides such as konjac mannan, pectin, guar gum, tamarind seed gum and carrageenan are used as food and drink materials, all of which are soluble in water, color and taste. There are problems in several respects, such as odor, etc. Furthermore, they have high viscosity (usually 103 cps / 1% or more, 25 ° C.), lack general versatility, and can be used only in specific fields. Polydextrose, which is widely used as a food and drink material, is a synthetic product and does not match the natural-oriented consumer consciousness. Therefore, as a dietary fiber for beverages, a white, tasteless and odorless, highly water-soluble material derived from a low-viscosity natural product is desired.
JP-A-4-28060 Japanese Patent Laid-Open No. 4-22806 U.S. Pat.No. 4,720,389 US Patent No. 4729900 Special Table 2004-536604 Japanese Patent No. 3551995 Japanese Unexamined Patent Publication No. 60-126065 Japanese Patent Laid-Open No. 11-299473 WO2003 / 105610 brochure Japanese Patent Laid-Open No. 2005-323585

本発明が解決しようとする課題は、発泡性炭酸飲料の泡品質を改良するための技術であり、飲料液面に形成された泡の安定性を向上させるものである。   The problem to be solved by the present invention is a technique for improving the foam quality of an effervescent carbonated beverage, and improves the stability of the foam formed on the beverage liquid surface.

本発明者らが上記課題を解決すべく鋭意研究を重ねたところ、酵母細胞壁由来可溶性画分を用いることにより炭酸飲料に起泡を付与できることを見いだし本発明を完成するに至った、
すなわち、本発明は以下に関するものである、
(1) 酵母細胞壁由来可溶性画分からなることを特徴とする泡安定化剤。
(2) 酵母細胞壁由来可溶性画分が、酵母細胞壁から抽出された酵母細胞壁由来可溶性画分であることを特徴とする(1)記載の泡安定化剤。
(3) 酵母由来可溶性画分が,酵母細胞壁画分放出能を有する酵母により産生された酵母細胞壁由来可溶性画分であることを特徴とする(1)記載の泡安定化剤。
(4) 酵母細胞壁由来可溶解性画分中のマンノース含量が乾物重量あたり75〜95%であることを特徴とする(1)〜(3)のいずれか1項に記載の泡安定化剤。
(5) 酵母可溶解性画分を添加したことを特徴とする起泡性を付与されたまたは泡安定化された飲食品。
(6) 酵母可溶解性画分を100ppm〜200000ppm添加したことを特徴とする(5)記載の飲食品。
(7) さらに炭酸ガスを含有することを特徴とする(5)または(6)に記載の飲食品。
When the present inventors repeated earnest research to solve the above-mentioned problems, they found that it is possible to impart foaming to a carbonated beverage by using a soluble fraction derived from the yeast cell wall, which led to the completion of the present invention.
That is, the present invention relates to the following:
(1) A foam stabilizer comprising a soluble fraction derived from a yeast cell wall.
(2) The foam stabilizer according to (1), wherein the yeast cell wall-derived soluble fraction is a yeast cell wall-derived soluble fraction extracted from the yeast cell wall.
(3) The foam stabilizer according to (1), wherein the yeast-derived soluble fraction is a yeast cell wall-derived soluble fraction produced by a yeast having a yeast cell wall fraction releasing ability.
(4) The foam stabilizer according to any one of (1) to (3), wherein the mannose content in the yeast cell wall-derived soluble fraction is 75 to 95% per dry matter weight.
(5) A food / beverage product imparted with foamability or foam-stabilized, characterized by adding a yeast soluble fraction.
(6) The food or drink according to (5), wherein 100 ppm to 200,000 ppm of a yeast soluble fraction is added.
(7) The food or drink according to (5) or (6), further containing carbon dioxide gas.

本発明により、飲食品に起泡性を付与し、ビールなどの発泡性飲料については発泡性飲料の液面に形成される泡を安定化させ、泡品質(泡付き、泡持ちなど)を向上させることができる。   According to the present invention, foamability is imparted to foods and drinks, and for foaming beverages such as beer, foam formed on the liquid surface of the foaming beverage is stabilized, and foam quality (foaming, foam retention, etc.) is improved. Can be made.

本発明における酵母細胞壁由来可溶性画分とは、酵母細胞の表層を形成する多糖類から得られる可溶性画分である。酵母細胞の表層を形成する可溶性画分は主にマンナンと呼ばれるマンノース含有多糖類であり、酵母菌体から菌体内可溶性成分である酵母エキスを抽出した残渣である酵母細胞壁を熱水抽出法(希アルカリ含む)抽出、自己消化法、細胞壁溶解酵素による消化などの方法により抽出されることが知られており、これらの細胞壁抽出多糖類は酵母マンナンとも呼ばれている。酵母マンナンの抽出に用いられる酵母は、酵母細胞壁由来可溶性画分の原料となりうる酵母細胞壁であれば特に限定されないが、例えばビール酵母細胞壁、発泡酒酵母細胞壁、雑酒酵母細胞壁、清酒酵母細胞壁、ワイン酵母細胞壁、ウィスキー酵母細胞壁等の醸造用酵母細胞壁、パン酵母細胞壁、トルラ酵母細胞壁等を挙げることができる。   The yeast cell wall-derived soluble fraction in the present invention is a soluble fraction obtained from a polysaccharide that forms the surface layer of a yeast cell. The soluble fraction that forms the surface layer of yeast cells is mainly a mannose-containing polysaccharide called mannan, and the yeast cell wall, which is a residue obtained by extracting yeast extract, which is a soluble component in the cells from yeast cells, is extracted with hot water (rare) It is known to be extracted by methods such as extraction (including alkali), autolysis, digestion with cell wall lytic enzymes, and these cell wall extracted polysaccharides are also called yeast mannan. The yeast used for the extraction of yeast mannan is not particularly limited as long as it is a yeast cell wall that can be a raw material for the soluble fraction derived from the yeast cell wall. For example, beer yeast cell wall, sparkling liquor yeast cell wall, sake yeast cell wall, sake yeast cell wall, wine Examples include yeast cell walls for brewing such as yeast cell walls and whiskey yeast cell walls, baker's yeast cell walls, and torula yeast cell walls.

酵母細胞壁を得る方法としては酵母菌体を5〜20時間45〜65℃に加温して自己消化させた後、遠心分離機で上清(酵母エキス)を除去する方法や、酵母菌体を80℃以上に昇温殺菌した後、そのまま遠心分離で上清(酵母エキス)を除去する方法や、酵素を添加、反応後に遠心分離して上清(酵母エキス)を除去する方法等がある。   The yeast cell wall can be obtained by heating the yeast cells to 45-65 ° C. for 5-20 hours and self-digesting, and then removing the supernatant (yeast extract) with a centrifuge. There are a method of removing the supernatant (yeast extract) by centrifuging as it is after sterilization by heating to 80 ° C. or higher, and a method of removing the supernatant (yeast extract) by adding an enzyme and centrifuging after the reaction.

次いで、得られた酵母細胞壁をアルカリ条件下で洗浄する。酵母細胞壁に残留したタンパク質やアミノ酸が洗浄により除去できれば、その洗浄方法は限定されない。洗浄方法はイーストセパレーターにより加水しながら行う方法などがあるが、洗浄後の固液分離した液が無色〜淡色、透明になればよい。洗浄温度は4〜95℃、好ましくは20℃〜50℃とする。   The resulting yeast cell wall is then washed under alkaline conditions. If the protein and amino acid remaining on the yeast cell wall can be removed by washing, the washing method is not limited. The washing method includes a method of adding water with a yeast separator, but it is sufficient that the solid-liquid separated liquid after washing is colorless to light color and transparent. The washing temperature is 4 to 95 ° C, preferably 20 to 50 ° C.

上述のアルカリ条件は、酵母細胞壁スラリーに25%NaOH溶液を添加し、pHを8.0〜14.0好ましくは9.5〜12.0とする。添加方法はバッチ式でも連続式でもよい。   As for the above alkaline conditions, a 25% NaOH solution is added to the yeast cell wall slurry to adjust the pH to 8.0 to 14.0, preferably 9.5 to 12.0. The addition method may be batch or continuous.

次にアルカリ条件下で洗浄した酵母細胞壁のpHを8.0〜14.0、好ましくは10.0〜12.0に調整し、60〜120℃、好ましくは85〜95℃で3〜24時間、好ましくは12〜20時間加水分解する。加水分解の際、攪拌はしてもしなくてもよい。   Next, the pH of the yeast cell wall washed under alkaline conditions is adjusted to 8.0 to 14.0, preferably 10.0 to 12.0, and water is added at 60 to 120 ° C, preferably 85 to 95 ° C for 3 to 24 hours, preferably 12 to 20 hours. Decompose. During the hydrolysis, stirring may or may not be performed.

上記加水分解後、酵母水溶性多糖類を得るため、固液分離を行う。酵母水溶性多糖類は上清溶液に含まれる。固液分離の方法は、イーストセパレーターによる遠心分離や、珪藻土濾過、限外濾過膜を用いる方法等があるが特に限定されない。   After the hydrolysis, solid-liquid separation is performed to obtain a yeast water-soluble polysaccharide. Yeast water-soluble polysaccharide is contained in the supernatant solution. Solid-liquid separation methods include, but are not limited to, centrifugation using a yeast separator, diatomaceous earth filtration, and a method using an ultrafiltration membrane.

次に固液分離した上清溶液に塩酸を添加し、pH2.5〜5.0、好ましくは3.5〜4.5に調整後、90〜140℃、好ましくは115〜125℃で15〜120秒、好ましくは30〜60秒加熱し、熱凝固物を発生させる。pH調整はバッチ式でも連続式でもよい。また加熱の方法はプレート式の熱交換機による方法等があるが特に限定されない。発生した熱凝固物はイーストセパレーターによる遠心分離や、珪藻土濾過、限外濾過膜を用いる除去するが、その方法は特に限定されない。   Next, hydrochloric acid is added to the supernatant solution obtained by solid-liquid separation, and after adjusting to pH 2.5 to 5.0, preferably 3.5 to 4.5, 90 to 140 ° C., preferably 115 to 125 ° C. for 15 to 120 seconds, preferably 30 Heat for ~ 60 seconds to generate hot coagulum. The pH adjustment may be batch or continuous. The heating method includes a plate type heat exchanger, but is not particularly limited. The generated heat coagulated material is removed by centrifugation using a yeast separator, diatomaceous earth filtration, or ultrafiltration membrane, but the method is not particularly limited.

上記の方法で熱凝固物を除去した溶液を分画分子量3,000~200,000カット、好ましくは6,000〜100,000カットのUF膜で限外濾過をすることにより、溶液中の塩濃度が低下する。限外濾過後の溶液はそのままアセプティック充填するか、スプレードライヤーで乾燥してもよい。   By subjecting the solution from which the heat coagulated material has been removed by the above method to ultrafiltration with a UF membrane having a molecular weight cut off of 3,000 to 200,000, preferably 6,000 to 100,000, the salt concentration in the solution decreases. The solution after ultrafiltration may be filled aseptically as it is or may be dried with a spray dryer.

スプレードライヤーで乾燥した場合、白色で無味無臭の粉末が得られる。水によく溶け(30g/水100ml以上)、粘度も低く(15.0cp/20%以下、25℃)、糖質として70~95%を含有し、多糖類中のマンノースとグルコースの構成比は75〜95:5〜25で、食物繊維含有率は70〜95%である。またその粉末の収率は、原料として使用した酵母細胞壁の乾燥物量対比8〜20%である。   When dried with a spray dryer, a white, tasteless and odorless powder is obtained. It dissolves well in water (30g / 100ml or more), has low viscosity (15.0cp / 20% or less, 25 ℃), contains 70-95% saccharides, and the composition ratio of mannose and glucose in the polysaccharide is 75 ~ 95: 5-25, dietary fiber content is 70-95%. Moreover, the yield of the powder is 8 to 20% relative to the dry matter amount of the yeast cell wall used as a raw material.

また酵母細胞の細胞壁画分放出能を有する酵母も知られており、これらの酵母が培地中に放出する酵母細胞壁画分(マンナンタンパク質)も本発明における酵母可溶性画分として用いることができる。酵母細胞壁画分放出能を有する酵母とは、酵母をエチルメタンスルホネート(EMS)等の変異処理、UV照射、放射線照射などにより変異誘発し、マンナンタンパク質を細胞壁にとどまらせることができなくなった酵母株を選抜することにより得ることができる。この変異処理する酵母は特に限定されないが、サッカロミセス・セレビジアエ(Saccharomyces cerevisiae)、シゾサッカロミセス・ポンベ(Schizosaccharomyces pombe)、サッカロマイセス・パラドキサス(Saccharomyces paradouxus)、サッカロミセス・ミカタエ(Saccharomyces mikatae)、サッカロマイセス・ウチリス(Saccharomyces utilis)、カンジダ・アリビカンス(Candida alibicans)などを用いることができる。   Yeast having the ability to release the cell wall fraction of yeast cells is also known, and the yeast cell wall fraction (mannan protein) released by these yeasts into the medium can also be used as the yeast soluble fraction in the present invention. Yeast with the ability to release the yeast cell wall fraction is a yeast strain that has been unable to retain mannan protein on the cell wall by mutagenizing the yeast with mutation treatment such as ethylmethanesulfonate (EMS), UV irradiation, radiation irradiation, etc. Can be obtained by selecting. The yeast to be treated with this mutation is not particularly limited. utilis), Candida alibicans, etc. can be used.

酵母細胞壁から得られるマンナン及びマンナンタンパク質は、マンノースがα(1→6)結合した主鎖からα(1→2)結合によって分枝した側鎖構造をもつ。この酵母由来のマンナンは低温溶解性が高く、粘性も低く、発泡性飲料の持つ本来の泡品質を改善し、泡を安定化させる効果がある。   Mannan and mannan protein obtained from the yeast cell wall have a side chain structure branched from the main chain in which mannose is α (1 → 6) -linked by α (1 → 2) bond. This mannan derived from yeast has a low-temperature solubility and low viscosity, and has the effect of improving the original foam quality of the sparkling beverage and stabilizing the foam.

添加する酵母細胞壁由来可溶性画分は酵母細胞を熱水抽出や酵素分解法などの方法により調製し、100ppm〜200000ppm、好適には2000〜100000ppm添加することが望ましい。   The yeast cell wall-derived soluble fraction to be added is preferably prepared by adding yeast cells by a method such as hot water extraction or enzymatic degradation, and adding 100 ppm to 200,000 ppm, preferably 2000 to 100,000 ppm.

本発明における起泡剤とは、飲食品に溶解し、飲食品をかき混ぜたり(ホイップしたり)あるいは別容器に移しかえたときに空気を巻き込んで形成される泡の状態を保持する性質を持つ素材のことを示す。   The foaming agent in the present invention has a property of dissolving in food and drink, and holding the state of foam formed by entraining air when the food or drink is agitated (whipped) or transferred to another container. Indicates a material.

本発明における飲食品とは、果汁飲料、酒類、炭酸飲料などの液状飲料、ソース、スープ、ルー、シチューなどの液状調味料、ホイップクリーム、メレンゲなどの混練により起泡する食品である。   The food and drink in the present invention is a food that foams by kneading liquid drinks such as fruit juice drinks, alcoholic beverages, carbonated drinks, liquid seasonings such as sauces, soups, roux, stews, whipped cream, and meringues.

(実施例)
(酵母マンナンの調製)
酵母細胞壁は酵母菌体を17時間55℃に加温して自己消化させた後、遠心分離機で上清を除去して得た。
(Example)
(Preparation of yeast mannan)
The yeast cell wall was obtained by heating the yeast cells to 55 ° C. for 17 hours for self-digestion and then removing the supernatant with a centrifuge.

次いで、得られた酵母細胞壁をアルカリ条件下で洗浄した。洗浄方法はイーストセパレーターにより加水しながら行った。洗浄後の固液分離した液が無色になるまで行った。洗浄温度は25℃で行った。   The resulting yeast cell wall was then washed under alkaline conditions. The washing method was performed while adding water with a yeast separator. The washing was performed until the liquid separated into solid and liquid after washing became colorless. The washing temperature was 25 ° C.

上述のアルカリ条件は、酵母細胞壁スラリーに25%NaOH溶液を添加し、pHを10.0とした。添加方法は連続式で行った。   The above alkaline conditions were such that a 25% NaOH solution was added to the yeast cell wall slurry to a pH of 10.0. The addition method was performed continuously.

次にアルカリ条件下で洗浄した酵母細胞壁のpHを11.0に調整し、90℃で17時間攪拌しながら加水分解した。   Next, the pH of the yeast cell wall washed under alkaline conditions was adjusted to 11.0 and hydrolyzed with stirring at 90 ° C. for 17 hours.

上記加水分解後、酵母水溶性多糖類を得るため、固液分離を行った。酵母水溶性多糖類は上清溶液に含まれる。   After the hydrolysis, solid-liquid separation was performed to obtain a yeast water-soluble polysaccharide. Yeast water-soluble polysaccharide is contained in the supernatant solution.

次に固液分離した上清溶液に塩酸を添加し、pH4.0に調整後、125℃で30秒加熱し、熱凝固物を発生させた。pH調整はバッチ式で行った。プレート式の熱交換機にて加熱した。発生した熱凝固物は珪藻土濾過で除去した。   Next, hydrochloric acid was added to the solid-liquid separated supernatant solution, adjusted to pH 4.0, and then heated at 125 ° C. for 30 seconds to generate a thermal coagulum. The pH was adjusted batchwise. It heated with the plate-type heat exchanger. The generated thermal coagulum was removed by diatomaceous earth filtration.

上記の方法で熱凝固物を除去した溶液を分画分子量50,000カットのUF膜で限外濾過し、溶液中の塩濃度を低下させた。限外濾過後の溶液は、スプレードライヤーで乾燥した。   The solution from which the heat coagulated material was removed by the above method was ultrafiltered through a UF membrane having a cut-off molecular weight of 50,000 cut to reduce the salt concentration in the solution. The solution after ultrafiltration was dried with a spray dryer.

スプレードライヤーで乾燥した結果、白色で無味無臭の粉末が得られた。水によく溶け(30g/水100ml以上)、粘度も低く(15.0cp/20%以下、25℃)、糖質として90%以上含有し、多糖類中のマンノースとグルコースの構成比は95:5で、食物繊維含有率は70%以上であった。またその粉末の収率は、原料として使用した酵母細胞壁の乾燥物量対比約10%であった。   As a result of drying with a spray dryer, a white, tasteless and odorless powder was obtained. It dissolves well in water (30 g / 100 ml or more), low viscosity (15.0 cp / 20% or less, 25 ° C), contains 90% or more of carbohydrates, and the composition ratio of mannose and glucose in the polysaccharide is 95: 5 The dietary fiber content was over 70%. Further, the yield of the powder was about 10% relative to the dry matter amount of the yeast cell wall used as a raw material.

(マンナンタンパク質の調製)
特願2004-250129記載の方法により得られたマンナンタンパク質放出酵母株AB9を20Lの合成培地(Difco社 Yeast Nitrogen Base w/o Amino acid and Ammonium sulfate 0.17%,Glucose 2%,アミノ酸0.13%)で50Lジャーファメンターで培養し(30℃、pH5.5、通気量1vvm、攪拌600rpm)、培養開始後48時間後に、7000rpm、15分の遠心分離にて培養上清を回収した。上清をセラミック限外ろ過膜(Membralox社製)にてクロスフローろ過し、100kDa(膜面積:0.35m2、ポアサイズ50nm)の分子量で分画濃縮した。限外ろ過残留液に加水し、分画濃縮と同じ条件で限外ろ過を行うことで脱塩した。脱塩後の残留液をスプレードライヤーで乾燥し粉体とし、培養上清1Lあたり0.2gのマンナンタンパク質が回収された。
(Preparation of mannan protein)
50 L of mannan protein-releasing yeast strain AB9 obtained by the method described in Japanese Patent Application No. 2004-250129 in 20 L of synthetic medium (Difco Yeast Nitrogen Base w / o Amino acid and Ammonium sulfate 0.17%, Glucose 2%, amino acid 0.13%) Culturing was performed with a jar fermenter (30 ° C., pH 5.5, aeration rate 1 vvm, stirring 600 rpm), and 48 hours after the start of the culture, the culture supernatant was collected by centrifugation at 7000 rpm for 15 minutes. The supernatant was subjected to cross flow filtration with a ceramic ultrafiltration membrane (Membralox), and fractionated and concentrated at a molecular weight of 100 kDa (membrane area: 0.35 m 2, pore size 50 nm). Water was added to the ultrafiltration residual liquid, and desalting was performed by performing ultrafiltration under the same conditions as fractional concentration. The desalted residual liquid was dried with a spray dryer to obtain a powder, and 0.2 g of mannan protein was recovered per liter of culture supernatant.

スプレードライヤーで乾燥することにより得られたマンナンタンパク質の粉体は白色で無味無臭であり、主な構成単糖がマンノースである。粉体中のマンノース含量は80〜90%であった。   Mannan protein powder obtained by drying with a spray dryer is white, tasteless and odorless, and the main constituent monosaccharide is mannose. The mannose content in the powder was 80 to 90%.

95%醸造用アルコール60mL、5倍濃縮グレープフルーツ果汁 4g、果糖ブドウ糖液糖(Brix75)100g、クエン酸 2g、香料 1gの溶液に、酵母マンナンを0.5g、2g、4g、8g添加し、その溶液を500mLになるように水に溶解した。この175mLについて350mL容の缶に入れ、175mLの炭酸水と混合後、封缶してガス入り果汁低アルコール飲料(ガス圧は20℃において0.23Mpa)を調製した。   Add 0.5 g, 2 g, 4 g, and 8 g of yeast mannan to a solution of 60 ml of 95% alcohol for brewing, 4 g of 5 times concentrated grapefruit juice, 100 g of fructose glucose liquid sugar (Brix75), 2 g of citric acid, and 1 g of flavor. Was dissolved in water to 500 mL. This 175 mL was put into a 350 mL can, mixed with 175 mL of carbonated water, and sealed to prepare a gas-containing fruit juice low-alcoholic beverage (gas pressure was 0.23 Mpa at 20 ° C.).

それぞれを5℃で48時間冷却し、グラスに注いで起泡性と泡持ちを比較した(表1)。   Each was cooled at 5 ° C. for 48 hours and poured into a glass to compare foaming properties and foam retention (Table 1).

なお、起泡性は溶液をグラスに注いだ直後に液面に形成される泡量を指し、泡持ちとは溶液をグラスに注いだ後、1分後の液面に残った泡量を目視で確認した。   In addition, foaming property refers to the amount of foam formed on the liquid surface immediately after pouring the solution into the glass, and foam retention refers to the amount of foam remaining on the liquid surface after 1 minute after pouring the solution into the glass. Confirmed with.

Figure 2008271820
Figure 2008271820

酵母マンナン無添加区(対照区)では起泡性がみられなかったが、酵母マンナンを添加した試料1〜試料4は良好な起泡性を示し、泡安定性(泡持ち)も良好であった。   Although no foaming property was observed in the yeast mannan-free group (control group), Samples 1 to 4 to which yeast mannan was added showed good foaming properties, and foam stability (foam retention) was also good. It was.

95%醸造用アルコール540mL、5倍濃縮グレープフルーツ果汁 36g、果糖ブドウ糖液糖(Brix75)900g、クエン酸 18g、香料 9gの溶液に、酵母マンナンを4.5g、18g、36g、72g添加し、その溶液を1.5Lになるように水に溶解した。この全量について図1に示すような10L容の樽缶61に入れ、7.5Lの炭酸水と混合後、封缶してガス入り果汁低アルコール飲料(ガス圧は20℃において0.23Mpa)を調製した。(即ちそれぞれの酵母マンナン添加量は0.5、2、4、8g/Lに相当する。)
各樽缶を図1に示すような生ビール用ディスペンサー1に接続し、炭酸ガスボンベ4から炭酸ガスを供給しながら常法により樽缶61から溶液をグラスに注いで実施例1と同様に起泡性と泡持ちを比較した(表2)。
95% brewing alcohol 540 mL, 5 times concentrated grapefruit juice 36 g, fructose glucose liquid sugar (Brix75) 900 g, citric acid 18 g, flavor 9 g added to a solution of 4.5 g, 18 g, 36 g and 72 g yeast mannan Was dissolved in water to 1.5 L. About this whole quantity, it puts in the barrel can 61 of 10L capacity as shown in FIG. 1, and after mixing with 7.5L carbonated water, it can seals, and gas-containing fruit juice low alcoholic beverage (gas pressure is 0.23 Mpa at 20 degreeC). Prepared. (That is, each yeast mannan added amount corresponds to 0.5, 2, 4, 8 g / L.)
Each barrel can is connected to a draft beer dispenser 1 as shown in FIG. 1, and a solution is poured from a barrel can 61 into a glass by a conventional method while supplying carbon dioxide gas from a carbon dioxide gas cylinder 4, and the foaming property is the same as in Example 1. And foam retention were compared (Table 2).

Figure 2008271820
Figure 2008271820

酵母マンナン無添加区(対照区)では起泡性がみられなかったが、酵母マンナンを添加した試料5〜試料8は良好な起泡性を示し、泡持ちも良好であった。   Although no foaming property was observed in the yeast mannan-free group (control group), Samples 5 to 8 to which yeast mannan was added showed good foaming properties and good foam retention.

料飲店で酎ハイを供する時には、焼酎等のベースアルコールに糖類やフルーツフレーバーの含有した濃縮シロップを加え、ソーダ水で希釈する場合が多い。   When offering strawberry high at a restaurant, a concentrated syrup containing sugars or fruit flavors is often added to base alcohol such as shochu and diluted with soda water.

95%醸造用アルコール60mL、5倍濃縮グレープフルーツ果汁 4g、果糖ブドウ糖液糖(Brix75)100g、クエン酸 2g、香料 1gの溶液に、マンナンタンパク質を2g、4g添加し、その溶液を500mLになるように水に溶解した。この175mLについて350mL容の缶に入れ、175mLの炭酸水と混合後、封缶してガス入り果汁低アルコール飲料(ガス圧は20℃において0.23Mpa)を調製した。   Add 2g and 4g of mannan protein to a solution of 60ml of 95% alcohol for brewing, 4g of 5 times concentrated grapefruit juice, 100g of fructose-glucose liquid sugar (Brix75), 2g of citric acid and 1g of fragrance so that the solution becomes 500ml. Dissolved in water. This 175 mL was put into a 350 mL can, mixed with 175 mL of carbonated water, and sealed to prepare a gas-containing fruit juice low-alcoholic beverage (gas pressure was 0.23 Mpa at 20 ° C.).

それぞれを5℃で48時間冷却し、グラスに注いで起泡性と泡持ちを比較した(表3)。   Each was cooled at 5 ° C. for 48 hours and poured into a glass to compare foaming properties and foam retention (Table 3).

なお、起泡性は溶液をグラスに注いだ直後に液面に形成される泡量を指し、泡持ちとは溶液をグラスに注いだ後、1分後の液面に残った泡量を目視で確認した。   In addition, foaming property refers to the amount of foam formed on the liquid surface immediately after pouring the solution into the glass, and foam retention refers to the amount of foam remaining on the liquid surface after 1 minute after pouring the solution into the glass. Confirmed with.

Figure 2008271820
Figure 2008271820

麦芽粉砕物70kg及びデンプン質副原料(コーンスターチ)150kgを仕込釜に入れた。これに、温水770リットルを加えて、これらの原料を混合して液化を行いマイシェを作った。この操作は、開始時の液温を55℃とし、徐々に昇温して、65〜70℃とした後、該温度で10分間保持し、さらに段階的に昇温して、90〜100℃まで液温を高め、この温度で30分保持した。一方、仕込槽では、別の麦芽粉砕物380kgに温水950リットルを加えて混合し、40〜50℃とし、20〜90分間保持してマイシェを作った。その後、仕込槽中のマイシェに、仕込釜で製造したマイシェと温水680リットルを加えた。次いで、このマイシェ混合物を仕込槽2中において、68〜75℃で10〜30分間保持して、糖化を行った。糖化工程終了後、これを麦汁濾過槽において濾過して、その濾液として透明な麦汁3100リットルを得た(糖度12.7%)。   70 kg of malt pulverized product and 150 kg of starchy auxiliary material (corn starch) were placed in a charging kettle. To this, 770 liters of warm water was added, and these raw materials were mixed and liquefied to make a miche. In this operation, the liquid temperature at the start was 55 ° C., the temperature was gradually raised to 65 to 70 ° C., held at the temperature for 10 minutes, and further heated stepwise to 90 to 100 ° C. The liquid temperature was raised to 30 minutes and maintained at this temperature for 30 minutes. On the other hand, in the charging tank, 950 liters of hot water was added to 380 kg of another malt pulverized product and mixed to obtain 40 to 50 ° C., which was held for 20 to 90 minutes to make a miche. Thereafter, the maiche produced in the brewing pot and 680 liters of hot water were added to the maiche in the brewing tank. Next, this mash mixture was held in the charging tank 2 at 68 to 75 ° C. for 10 to 30 minutes for saccharification. After completion of the saccharification step, this was filtered in a wort filtration tank to obtain 3100 liters of transparent wort as the filtrate (sugar content 12.7%).

得られた麦汁を煮沸釜に移し、これにホップ2.5kg、酵母マンナン0〜4kg/KLとなるように加えて、100℃で90分間煮沸した。煮沸した麦汁をワールプール槽5に入れて、沈殿により生じたタンパク質などの粕を除去した。この際、煮沸後麦汁2700リットル(糖度14.5%)に温水400リットルを加えて糖度12.7%に調整した。次いで、これをプレートクーラーにより、5℃まで冷却して、冷却した麦汁3000リットルを得た。   The obtained wort was transferred to a boiling kettle, added to this so as to be 2.5 kg of hops and yeast mannan 0-4 kg / KL, and boiled at 100 ° C. for 90 minutes. The boiled wort was placed in the whirlpool tank 5 to remove wrinkles such as protein produced by precipitation. At this time, after boiling, 2700 liters of wort (sugar content 14.5%) was added with 400 liters of warm water to adjust the sugar content to 12.7%. Subsequently, this was cooled to 5 degreeC with the plate cooler, and 3000 liters of cooled worts were obtained.

得られた麦汁3000リットルを、発酵タンクに移した。次いで、発酵タンクに、麦汁1mlあたり20×10個の酵母を添加し、10℃で7日間発酵を行った。その後−1℃で十分熟成させた後、珪藻土ろ過機によりろ過して、アルコール含量約5%のビールを得た。尚、アルコール含量の微調整は、脱気水を用いて希釈により行った。 The resulting 3000 liters of wort was transferred to a fermentation tank. Next, 20 × 10 6 yeasts per ml of wort were added to the fermentation tank, and fermentation was performed at 10 ° C. for 7 days. Thereafter, the mixture was sufficiently aged at -1 ° C and then filtered through a diatomaceous earth filter to obtain a beer having an alcohol content of about 5%. The alcohol content was finely adjusted by dilution with degassed water.

濾過後のビールについて泡分析を行った。それぞれの分析値を表4に示す。なお、泡分析はビールで一般的な測定法であるNIBEM泡に従った。   Foam analysis was performed on the filtered beer. Each analysis value is shown in Table 4. The foam analysis followed NIBEM foam, which is a common measurement method for beer.

Figure 2008271820
Figure 2008271820

酵母マンナンを添加した試料12〜試料14は無添加対照区よりも良好な起泡性を示し、泡持ちも良好であった。   Samples 12 to 14 to which yeast mannan was added exhibited better foaming properties and better foam retention than the non-added control group.

本発明により、飲食品に起泡性を付与し、発泡性炭酸飲料の泡持ちを改善することができる。   By this invention, foamability can be provided to food-drinks and the foam retention of a sparkling carbonated drink can be improved.

生ビール用ディスペンサーの説明図。Explanatory drawing of dispenser for draft beer.

符号の説明Explanation of symbols

1 ディスペンサー
2 ディスペンスヘッド
3 ホース
4 炭酸ガスボンベ
6 ガスホース
12 ディスペンスコック
61 樽缶
1 Dispenser 2 Dispensing Head 3 Hose 4 Carbon Dioxide Cylinder 6 Gas Hose
12 dispense cock
61 barrels

Claims (7)

酵母細胞壁由来可溶性画分からなることを特徴とする泡安定化剤。   A foam stabilizer comprising a soluble fraction derived from a yeast cell wall. 酵母細胞壁由来可溶性画分が、酵母細胞壁から抽出された酵母細胞壁由来可溶性画分であることを特徴とする請求項1記載の泡安定化剤。   The foam stabilizer according to claim 1, wherein the yeast cell wall-derived soluble fraction is a yeast cell wall-derived soluble fraction extracted from the yeast cell wall. 酵母由来可溶性画分が,酵母細胞壁画分放出能を有する酵母により産生された酵母細胞壁由来可溶性画分であることを特徴とする請求項1記載の泡安定化剤。   The foam stabilizer according to claim 1, wherein the yeast-derived soluble fraction is a yeast cell wall-derived soluble fraction produced by a yeast having a yeast cell wall fraction releasing ability. 酵母細胞壁由来可溶解性画分中のマンノース含量が乾物重量あたり75〜95%であることを特徴とする請求項1〜3のいずれか1項に記載の泡安定化剤。   The foam stabilizer according to any one of claims 1 to 3, wherein the mannose content in the soluble fraction derived from the yeast cell wall is 75 to 95% per dry matter weight. 酵母可溶解性画分を添加したことを特徴とする起泡性を付与されたまたは泡安定化された飲食品。   A food / beverage product imparted with foamability or foam-stabilized, characterized by adding a yeast soluble fraction. 酵母可溶解性画分を100ppm〜200000ppm添加したことを特徴とする請求項5記載の飲食品。   The food or drink according to claim 5, wherein the yeast soluble fraction is added in an amount of 100 ppm to 200,000 ppm. さらに炭酸ガスを含有することを特徴とする請求項5または6に記載の飲食品。   Furthermore, carbon dioxide gas is contained, The food-drinks of Claim 5 or 6 characterized by the above-mentioned.
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EP3132047A4 (en) * 2014-04-14 2017-10-04 Biothera, Inc. Yeast cell wall enriched in mannan oligosaccharide protein
WO2015160818A1 (en) 2014-04-14 2015-10-22 Biothera, Inc. Yeast cell wall enriched in mannan oligosaccharide protein
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