JP2008131881A - Apparatus and method for debittering yeast - Google Patents

Apparatus and method for debittering yeast Download PDF

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JP2008131881A
JP2008131881A JP2006320225A JP2006320225A JP2008131881A JP 2008131881 A JP2008131881 A JP 2008131881A JP 2006320225 A JP2006320225 A JP 2006320225A JP 2006320225 A JP2006320225 A JP 2006320225A JP 2008131881 A JP2008131881 A JP 2008131881A
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yeast
debittering
muddy
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sieve
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Tokuo Endo
徳雄 遠藤
Kunitoshi Sakuma
邦敏 佐久間
Toshio Shibata
敏生 柴田
Shiyouminoru Morita
將稔 森田
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Kirin Brewery Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus for debittering yeast having an improved debittering capability of yeast slurry collected after fermentation process. <P>SOLUTION: In the debittering apparatus 10 in which a bitter substance is removed from the yeast slurry collected after the fermentation process, a yeast slurry tank 11 for keeping the yeast slurry, debittering devices 12 and 13 in which the yeast slurry is debittered by mixing the yeast slurry took out from the yeast slurry tank 11 with alkaline aqueous solution, and a vibrational sieving machine 14 to be used to remove the decke of the debittered yeast as a decke-removing means are provided. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、発酵工程後に回収した泥状酵母の苦味物質を除去する酵母の脱苦味処理装置及び脱苦味処理方法に関する。   The present invention relates to a yeast de-bitter taste treatment apparatus and a de-bitter taste treatment method for removing muddy yeast bitter substances recovered after a fermentation process.

ビール・発泡酒等の発泡性麦芽飲料や雑酒等のビール様飲料の製造工程内での発酵工程後に回収された酵母は、余剰酵母として乾燥酵母や酵母エキスの原料にされ、その含有たんぱく質、ビタミン等の有価物に着目して、調味料・健康食品等の食品、医薬品、動物飼料等として利用されている。しかし、余剰酵母は発酵工程後に回収された酵母であるため、発泡性麦芽飲料やビール様飲料の原料であるホップ樹脂等が付着しており、苦味が強いという特徴がある。酵母から苦味物質を除去する方法としては、酵母をアルカリ水溶液で洗浄する方法が知られている(例えば特許文献1参照)。その他に、余剰酵母をエタノール溶液に接触させて脱苦味処理する方法、余剰酵母を水蒸気蒸留、又は水蒸気蒸留と有機溶剤処理とによって脱苦味処理する方法も知られている(例えば特許文献2、3参照)。   Yeast collected after the fermentation process in the production process of beer-like beverages such as beer and sparkling liquor, beer-like beverages such as miscellaneous liquor, is used as a raw material for dried yeast and yeast extract as surplus yeast, Focusing on valuables such as vitamins, they are used as foods such as seasonings and health foods, pharmaceuticals, animal feeds and the like. However, since the surplus yeast is yeast recovered after the fermentation step, hop resin or the like, which is a raw material for effervescent malt beverages or beer-like beverages, is attached and has a characteristic that it has a strong bitter taste. As a method for removing bitter substances from yeast, a method of washing yeast with an alkaline aqueous solution is known (see, for example, Patent Document 1). In addition, there are also known a method in which surplus yeast is brought into contact with an ethanol solution and subjected to debittering treatment, and a method in which surplus yeast is debittered by steam distillation or steam distillation and organic solvent treatment (for example, Patent Documents 2 and 3). reference).

特開昭55−162983号公報Japanese Patent Laid-Open No. 55-162983 特開昭61−31083号公報JP 61-31083 A 特開昭63−22177号公報Japanese Unexamined Patent Publication No. 63-22177

従来のアルカリ水溶液を用いた脱苦味処理方法では、発酵工程後に泥状状態で回収された酵母(泥状酵母)を振動式ふるい機にかけてデッケ分を除去し、その後にアルカリ水溶液を酵母に添加して脱苦味を行っている。この方法では、デッケ分の除去時の泥状酵母のろ過性が悪いため、振動式ふるい機のメッシュ径を細かく設定することができない。このため、細かいデッケ分を除去することが困難であった。   In the conventional debittering treatment method using an alkaline aqueous solution, the yeast (mud yeast) recovered in a muddy state after the fermentation process is passed through a vibrating sieve to remove the decke, and then an alkaline aqueous solution is added to the yeast. And debittering. In this method, since the filterability of the muddy yeast at the time of removal of the decke is poor, the mesh diameter of the vibrating sieve cannot be set finely. For this reason, it was difficult to remove the fine decke.

本発明は、発酵工程後に回収した泥状酵母の脱苦味処理能力を向上させることが可能な酵母の脱苦味処理装置及び脱苦味処理方法を提供することを目的とする。   An object of this invention is to provide the de-bitter taste processing apparatus and de-bitter taste processing method of yeast which can improve the de-bitter taste processing capability of the muddy yeast collect | recovered after the fermentation process.

本発明の酵母の脱苦味処理装置(10)は、発酵工程後に回収した泥状酵母から苦味物質を除去する酵母の脱苦味処理装置であって、前記泥状酵母を保管する保管タンク(11)と、前記保管タンクから取り出された泥状酵母とアルカリ水溶液とを混合することにより前記泥状酵母に対する脱苦味を行う脱苦味手段(12、13)と、前記脱苦味後の酵母のデッケ分を除去するデッケ除去手段(14)とを備えることにより、上述した課題を解決する。また、本発明の酵母の脱苦味処理方法は、発酵工程後に回収した泥状酵母から苦味物質を除去する酵母の脱苦味処理方法であって、前記泥状酵母とアルカリ水溶液とを混合することにより前記泥状酵母に対する脱苦味を行う脱苦味工程と、前記脱苦味後の酵母のデッケ分を除去するデッケ除去工程とを備えることにより、上述した課題を解決する。   The yeast de-bitter taste treatment apparatus (10) of the present invention is a yeast de-bitter taste treatment apparatus for removing bitter substances from muddy yeast recovered after the fermentation step, and a storage tank (11) for storing the muddy yeast. And a debittering means (12, 13) for debittering the muddy yeast by mixing the muddy yeast taken out of the storage tank and an aqueous alkaline solution, and a deke part of the yeast after the debittering taste. The above-described problem is solved by providing the deck removal means (14) for removal. Further, the yeast de-bitter taste treatment method of the present invention is a yeast de-bitter taste treatment method for removing bitter substances from the muddy yeast recovered after the fermentation step, by mixing the muddy yeast and an aqueous alkaline solution. By providing a debittering process for debittering the muddy yeast and a dekke removal process for removing the dekke content of the yeast after the debittering taste, the above-described problems are solved.

本発明の脱苦味処理装置及び脱苦味処理方法によれば、発酵工程後に回収した泥状酵母からデッケ分を除去する前に、その泥状酵母とアルカリ水溶液とを混合しているので、泥状酵母がアルカリ水溶液中に分散され、デッケ除去時における酵母とデッケ分との分離性あるいは濾過性が改善される。これにより、泥状酵母からデッケ分を効率よく除去して脱苦味処理能力を向上させることができる。   According to the debittering treatment apparatus and debittering treatment method of the present invention, the muddy yeast and the aqueous alkaline solution are mixed before removing the Decke content from the muddy yeast recovered after the fermentation step. Yeast is dispersed in an alkaline aqueous solution, so that the separability or filterability between the yeast and the deke is improved when the deke is removed. As a result, it is possible to efficiently remove the decke content from the muddy yeast and improve the debittering ability.

本発明の一形態においては、デッケ除去手段が振動式ふるい機(14)であってもよい。さらに、その振動式ふるい機のふるいのメッシュ径が#60又はそれよりも細かいものとしてもよい。これにより、デッケ分を酵母から効率よくかつ確実に分離して、脱苦味処理能力を顕著に高めることができる。   In one embodiment of the present invention, the decke removing means may be a vibrating sieve (14). Furthermore, the mesh diameter of the sieve of the vibration type sieve may be # 60 or smaller. Thereby, the Decke content can be separated from the yeast efficiently and reliably, and the debittering ability can be significantly enhanced.

さらに、前記デッケ分が除去された酵母の冷水による洗浄及び脱水を実施するアルカリ成分除去手段(15、16、17、18)を備えてもよい。この場合は、酵母に加えられたアルカリ成分を水洗して、酵母色の変色を抑えることができる。   Furthermore, you may provide the alkali component removal means (15, 16, 17, 18) which implements washing | cleaning and dehydration with the cold water of the yeast from which the said decke part was removed. In this case, the alkaline component added to the yeast can be washed with water to suppress the discoloration of the yeast color.

なお、以上の説明では本発明の理解を容易にするために添付図面の参照符号を括弧書きにて付記したが、それにより本発明が図示の形態に限定されるものではない。   In addition, in the above description, in order to make an understanding of this invention easy, the reference sign of the accompanying drawing was attached in parenthesis, but this invention is not limited to the form of illustration by it.

以上に説明したように、本発明の脱苦味処理装置及び脱苦味処理方法によれば、泥状酵母からのデッケ除去に先立って、泥状酵母にアルカリ水溶液を添加するため、従来よりも細かいデッケ分を除去することが可能となり、泥状酵母の脱苦味処理能力を向上させることができる。   As described above, according to the debittering treatment apparatus and the debittering treatment method of the present invention, the alkaline aqueous solution is added to the muddy yeast prior to the removal of the deke from the muddy yeast. It becomes possible to remove a part, and the de-bitter taste processing capability of muddy yeast can be improved.

図1は本発明の一形態に係る酵母の脱苦味処理装置を示す。脱苦味処理装置10は、酵母の脱苦味処理の順序に従って、保管タンクとしての泥状酵母タンク11と、炭酸ナトリウム溶解タンク12と、第1の操作タンク13と、振動式ふるい機14と、第2の操作タンク15と、第1の遠心分離機16と、第3の操作タンク17と、第2の遠心分離機18と、脱苦味泥状酵母タンク19とを備えている。以下、これらの構成について、脱苦味処理の手順とともに説明する。   FIG. 1 shows a yeast de-bittering treatment apparatus according to one embodiment of the present invention. The de-bittering treatment apparatus 10 includes a muddy yeast tank 11 as a storage tank, a sodium carbonate dissolution tank 12, a first operation tank 13, a vibrating sieve 14 and a first according to the order of yeast de-bittering treatment. 2 operation tank 15, first centrifuge 16, third operation tank 17, second centrifuge 18, and debittered mud yeast tank 19. Hereinafter, these configurations will be described together with the procedure of the debittering process.

泥状酵母タンク11は、例えば、ビール・発泡酒等の発泡性麦芽飲料や雑酒等のビール様飲料の製造工程内での発酵工程後に回収された泥状酵母を保管する。脱苦味処理のために保管される酵母は、デッケ分が付着した酵母であれば、ビール酵母・発泡酒酵母といった発泡性麦芽飲料用酵母、雑酒等のビール様飲料用酵母に限定されるものではなく、ワイン酵母、パン酵母、清酒酵母、ウイスキー酵母、その他の醸造用酵母等いずれでもよい。ビール酵母としては、例えばサッカロマイセス・セレビシエ(Saccharomyces cerevisiae)等がある。泥状酵母は、できるだけ10°C前後で保管することが好ましい。一方、炭酸ナトリウム溶解タンク12は、アルカリ水溶液として所定濃度の炭酸ナトリウム水溶液を保管する。固形炭酸ナトリウムを水に溶解すると経時的に分解するため、炭酸ナトリウム溶解タンク12では、一日の処理で使用される量の固形炭酸ナトリウムが投入されて水による溶解作業が行われる。但し、炭酸ナトリウムは常温の水では溶解し難いため、炭酸ナトリウム溶解タンク12にはまず40°C程度の温水が導入されて固形炭酸ナトリウムが溶解され、その後に常温の水が炭酸ナトリウム溶解タンク12に導入されて溶液が所定濃度に希釈される。泥状酵母タンク11に投入される泥状酵母の量が一日辺り25KL(キロリットル)の場合、250gの固形炭酸ナトリウムが2.5mの水により溶解される。この場合、炭酸ナトリウム溶解タンク12の容量は3m程度でよい。 The muddy yeast tank 11 stores, for example, muddy yeast recovered after the fermentation process in the production process of beer-like beverages such as beer-like and miscellaneous liquors. Yeast stored for debittering treatment is limited to yeast for beer-like malt beverages such as brewer's yeast and happoshu yeast, and yeast for beer-like beverages such as miscellaneous liquors, as long as the yeast is attached to the decke. Instead, any of wine yeast, baker's yeast, sake yeast, whiskey yeast, and other brewing yeasts may be used. Examples of the brewer's yeast include Saccharomyces cerevisiae. It is preferable to store the muddy yeast at around 10 ° C as much as possible. On the other hand, the sodium carbonate dissolution tank 12 stores a sodium carbonate aqueous solution having a predetermined concentration as an alkaline aqueous solution. When solid sodium carbonate is dissolved in water, it decomposes with time, so that the sodium carbonate dissolution tank 12 is charged with the amount of solid sodium carbonate used in a day's treatment and dissolved with water. However, since sodium carbonate is difficult to dissolve in normal temperature water, first, warm water of about 40 ° C. is introduced into the sodium carbonate dissolution tank 12 to dissolve solid sodium carbonate, and then normal temperature water is dissolved in the sodium carbonate dissolution tank 12. And the solution is diluted to a predetermined concentration. When the amount of muddy yeast charged into the muddy yeast tank 11 is 25 KL (kiloliter) per day, 250 g of solid sodium carbonate is dissolved in 2.5 m 3 of water. In this case, the capacity of the sodium carbonate dissolution tank 12 may be about 3 m 3 .

第1の操作タンク13は、泥状酵母タンク11から取り出された泥状酵母が投入される。その泥状酵母には、炭酸ナトリウム溶解タンク12に保管された炭酸ナトリウム水溶液が添加される。これにより、操作タンク13内において泥状酵母が炭酸ナトリウム水溶液中に分散され、後述するデッケ処理時における濾過性が改善される。添加する炭酸ナトリウム水溶液の量は適宜に設定してよいが、例えば泥状酵母10KLにつき炭酸ナトリウムを100kgを添加する。添加後は、泥状酵母と炭酸ナトリウム水溶液とを撹拌するとよい。   The first operation tank 13 is charged with the muddy yeast extracted from the muddy yeast tank 11. A sodium carbonate aqueous solution stored in the sodium carbonate dissolution tank 12 is added to the muddy yeast. Thereby, muddy yeast is disperse | distributed in sodium carbonate aqueous solution in the operation tank 13, and the filterability at the time of the decking process mentioned later is improved. The amount of the sodium carbonate aqueous solution to be added may be appropriately set. For example, 100 kg of sodium carbonate is added per 10 KL of muddy yeast. After the addition, the muddy yeast and the aqueous sodium carbonate solution may be stirred.

第1の操作タンク13にて所定時間(例えば1.5時間)洗浄された泥状酵母は、続いて振動式ふるい機14に供給される。振動式ふるい機14では、網目のメッシュ径が#60(目開250μm、線径φ0.173mm)のふるい上に泥状酵母が投入され、そのふるいに振動が与えられてデッケ分除去処理が行われる。これにより、泥状酵母のデッケ分(ホップ樹脂等)がふるいの網目上に捕捉され、デッケ分が除去された泥状酵母が網目を通過する。   The muddy yeast that has been washed in the first operation tank 13 for a predetermined time (for example, 1.5 hours) is then supplied to the vibratory sieve 14. In the vibration type sieve 14, mud yeast is put on a sieve having a mesh diameter of # 60 (mesh size 250 μm, wire diameter φ0.173 mm), and vibration is given to the sieve to perform a deke removal process. Is called. As a result, the mecked yeast decke (hop resin or the like) is captured on the sieve mesh, and the muddy yeast from which the decke has been removed passes through the mesh.

振動式ふるい機14にて濾過された泥状酵母は第2の操作タンク15に導入される。濾過後の泥状酵母には冷水が添加される。冷水は、振動式ふるい機14から第2の操作タンク15に泥状酵母を導く管路中で添加されてもよいし、あるいは、泥状酵母の導入に先行して、予め第2の操作タンク15に注入されてもよい。なお、冷水は滅菌処理されたものを用いる必要がある。第2の操作タンク15ではデッケ分が除去された泥状酵母と冷水とが撹拌されて泥状酵母が洗浄される。   Mud yeast filtered by the vibration sieve 14 is introduced into the second operation tank 15. Cold water is added to the muddy yeast after filtration. The cold water may be added in a conduit that leads the muddy yeast from the vibrating sieve 14 to the second operation tank 15, or prior to the introduction of the muddy yeast, the second operation tank is previously provided. 15 may be injected. It is necessary to use cold water that has been sterilized. In the second operation tank 15, the muddy yeast from which the decke has been removed and the cold water are agitated to wash the muddy yeast.

第2の操作タンク15で冷水により洗浄された泥状酵母は、続いて第1の遠心分離機16に供給される。遠心分離機16では、第2の操作タンク15にて洗浄された泥状酵母が遠心力を利用して脱水される。脱水後の酵母は第3の操作タンク17に導入される。第3の操作タンク17の酵母には冷水が添加される。冷水は、遠心分離機16から第3の操作タンク17に酵母を導く管路中で添加されてもよいし、あるいは、酵母の導入に先行して、予め第3の操作タンク17に注入されてもよい。第3の操作タンク17では脱水後の酵母が冷水と撹拌されて洗浄される。なお、冷水は滅菌処理されたものを用いる必要があり、その温度は10°C程度が望ましい。冷水の温度が高い(例えば30°C以上)であると、酵母重量の減少率が高くなるおそれがある。   The muddy yeast washed with cold water in the second operation tank 15 is then supplied to the first centrifuge 16. In the centrifuge 16, the muddy yeast washed in the second operation tank 15 is dehydrated using centrifugal force. The dehydrated yeast is introduced into the third operation tank 17. Cold water is added to the yeast in the third operation tank 17. The cold water may be added in a conduit that leads the yeast from the centrifuge 16 to the third operation tank 17, or is injected into the third operation tank 17 in advance prior to the introduction of the yeast. Also good. In the third operation tank 17, the dehydrated yeast is agitated with cold water and washed. In addition, it is necessary to use the sterilized cold water, and the temperature is preferably about 10 ° C. If the temperature of the cold water is high (for example, 30 ° C. or higher), the rate of decrease in yeast weight may be high.

第3の操作タンク17による洗浄後は、再び酵母が遠心分離機16へ戻されて脱水され、脱水後の酵母は再び第3の操作タンク17に導入されて冷水により洗浄される。遠心分離機16及び第3の操作タンク17による処理が所定回数(例えば3〜4回)繰り返された後、第3の操作タンク17から取り出された酵母は第2の遠心分離機18に供給される。その遠心分離機18にて酵母の最終的な水分調整のための脱水処理が行われる。脱水処理後は、酵母のpHが検査される。pHが8.0未満であれば脱アルカリの洗浄が完了したものとして、脱水処理された酵母が脱苦味泥状酵母タンク19に導入される。pHが8.0以上であれば、第3の操作タンク17による洗浄を再び実施し、遠心分離機18にて脱水処理を行って再度pHを検査する。なお、炭酸ナトリウムが添加された酵母は茶褐色に変色するので、第3の操作タンク17から遠心分離機18に酵母を受け入れる際には、酵母色を確認することが望ましい。   After washing by the third operation tank 17, the yeast is again returned to the centrifuge 16 and dehydrated, and the dehydrated yeast is again introduced into the third operation tank 17 and washed with cold water. After the processing by the centrifuge 16 and the third operation tank 17 is repeated a predetermined number of times (for example, 3 to 4 times), the yeast taken out from the third operation tank 17 is supplied to the second centrifuge 18. The The centrifuge 18 performs a dehydration process for final moisture adjustment of the yeast. After dehydration, the pH of the yeast is examined. If the pH is less than 8.0, it is determined that the dealkalization washing is completed, and the dehydrated yeast is introduced into the debittered mud yeast tank 19. If the pH is 8.0 or more, the cleaning by the third operation tank 17 is performed again, the dehydration process is performed by the centrifuge 18, and the pH is inspected again. In addition, since the yeast to which sodium carbonate is added turns brown, it is desirable to confirm the yeast color when the yeast is received from the third operation tank 17 into the centrifuge 18.

脱苦味泥状酵母タンク19に保管された酵母はその後適宜に取り出されて乾燥酵母製造設備、酵母エキス製造設備等へと送られる。   The yeast stored in the debittered mud yeast tank 19 is then appropriately taken out and sent to a dry yeast production facility, a yeast extract production facility, or the like.

以上に説明した酵母の脱苦味処理装置・方法によれば、振動式ふるい機14においてデッケ分を除去する前に、泥状酵母に炭酸ナトリウム水溶液を添加して酵母を分散させているので、振動式ふるい機14における目詰まりが生じ難く、ふるいのメッシュ径を#60の細かいサイズに設定することができる。炭酸ナトリウム水溶液を添加せずにデッケ分除去を先行させた場合には、ふるいのサイズが#32程度に制限される。これとの比較において、本形態によれば、デッケ除去量が約10倍、振動式ふるい機14のデッケ処理能力が約2倍に改善される。これにより、脱苦味処理能力を大幅に向上させることができる。   According to the yeast de-bittering treatment apparatus and method described above, since the sodium carbonate aqueous solution is added to the muddy yeast to disperse the yeast before the decke is removed by the vibration sieve 14, the yeast is vibrated. Clogging is unlikely to occur in the sieving machine 14, and the mesh diameter of the sieve can be set to a fine size of # 60. When the removal of the deck is preceded without adding the aqueous sodium carbonate solution, the size of the sieve is limited to about # 32. In comparison with this, according to the present embodiment, the deke removal amount is improved about 10 times, and the deke processing capacity of the vibration type sieve machine 14 is improved about twice. Thereby, the debitter taste processing capability can be improved significantly.

また、上記の形態では、デッケ分の除去後、冷水を加えつつ遠心分離機で酵母を水洗しているので、アルカリ成分を直ちに除去して酵母色の変色を抑えることができる。また、冷水温度を適切に設定することにより、酵母重量の減少を抑えることができる。   Further, in the above-described embodiment, since the yeast is washed with a centrifuge while adding cold water after removing the decke, the alkaline component can be immediately removed to suppress the color change of the yeast. In addition, a decrease in yeast weight can be suppressed by appropriately setting the cold water temperature.

以上の形態では、炭酸ナトリウム溶解タンク12及び第1の操作タンク13が脱苦味手段に、振動式ふるい機14がデッケ除去手段に、第2の操作タンク15、第1の遠心分離機16、第3の操作タンク17及び第2の遠心分離機18の組み合わせがアルカリ成分除去手段にそれぞれ相当する。但し、本発明は上記の形態に限ることなく、適宜の形態にて実施してよい。例えば、泥状酵母に添加するアルカリ水溶液は炭酸ナトリウム水溶液に限らず、水酸化ナトリウム水溶液、炭酸カリウム水溶液等でもよい。デッケ除去手段は振動式ふるい機に限らず、泥状酵母内に存在するデッケ分を除去できる限りにおいて適宜に変更可能である。振動式ふるい機14のふるいのメッシュ径は#60に限らず、これよりも小さい(細かい)ものでもよい。水洗手段は、泥状酵母の冷水による洗浄と脱水とを実施できる限り適宜の構成としてよい。第2の操作タンク15及び第3の操作タンク17は兼用されてもよい。   In the above embodiment, the sodium carbonate dissolution tank 12 and the first operation tank 13 are used as the debittering means, the vibration sieve 14 is used as the deke removal means, the second operation tank 15, the first centrifuge 16, The combination of the third operation tank 17 and the second centrifuge 18 corresponds to the alkali component removing means. However, the present invention is not limited to the above form, and may be implemented in an appropriate form. For example, the alkaline aqueous solution added to the muddy yeast is not limited to the sodium carbonate aqueous solution, but may be a sodium hydroxide aqueous solution, a potassium carbonate aqueous solution, or the like. The deck removal means is not limited to the vibration type sieve, but can be appropriately changed as long as the decke present in the muddy yeast can be removed. The mesh diameter of the sieve of the vibration type sieve machine 14 is not limited to # 60, and may be smaller (fine) than this. The water washing means may have an appropriate configuration as long as the muddy yeast can be washed with cold water and dehydrated. The second operation tank 15 and the third operation tank 17 may be combined.

本発明の一形態に係る酵母の脱苦味処理装置の概要を示す図。The figure which shows the outline | summary of the debitter taste processing apparatus of the yeast which concerns on one form of this invention.

符号の説明Explanation of symbols

10 脱苦味処理装置
11 泥状酵母タンク(保管タンク)
12 炭酸ナトリウム溶解タンク(脱苦味手段)
13 第1の操作タンク(脱苦味手段)
14 振動式ふるい機(デッケ除去手段)
15 第2の操作タンク(アルカリ成分除去手段)
16 第1の遠心分離機(アルカリ成分除去手段)
17 第3の洗浄タンク(アルカリ成分除去手段)
18 第2の遠心分離機(アルカリ成分除去手段)
19 脱苦味泥状酵母タンク
10 Debittering processing equipment 11 Mud yeast tank (storage tank)
12 Sodium carbonate dissolution tank (means to remove bitterness)
13 1st operation tank (debittering means)
14 Vibrating sieve (Decke removal means)
15 Second operation tank (alkali component removing means)
16 1st centrifuge (alkali component removing means)
17 Third cleaning tank (alkali component removing means)
18 Second centrifuge (alkali component removing means)
19 Debittering Muddy Yeast Tank

Claims (5)

発酵工程後に回収した泥状酵母から苦味物質を除去する酵母の脱苦味処理装置において、
前記泥状酵母を保管する保管タンクと、前記保管タンクから取り出された泥状酵母とアルカリ水溶液とを混合することにより前記泥状酵母に対する脱苦味を行う脱苦味手段と、前記脱苦味後の酵母のデッケ分を除去するデッケ除去手段と、を備えたことを特徴とする酵母の脱苦味処理装置。
In a debittering treatment apparatus for yeast that removes bitter substances from muddy yeast collected after the fermentation process,
A storage tank for storing the muddy yeast, a debittering means for debittering the muddy yeast by mixing the muddy yeast extracted from the storage tank and an alkaline aqueous solution, and the yeast after the debittering taste And a deke removal means for removing the dekke content of the yeast.
前記デッケ除去手段が振動式ふるい機であることを特徴とする請求項1に記載の酵母の脱苦味処理装置。   The yeast de-bittering treatment apparatus according to claim 1, wherein the decking removing means is a vibrating sieve. 前記振動式ふるい機のふるいのメッシュ径が#60又はそれよりも細かいことを特徴とする請求項2に記載の酵母の脱苦味処理装置。   The apparatus for de-bittering taste of yeast according to claim 2, wherein the mesh size of the sieve of the vibration type sieve is # 60 or finer. 前記デッケ分が除去された酵母の冷水による洗浄及び脱水を実施するアルカリ成分除去手段を備えたことを特徴とする請求項1〜3のいずれか一項に記載の酵母の脱苦味処理装置。   The yeast de-bittering treatment apparatus according to any one of claims 1 to 3, further comprising alkaline component removal means for performing washing and dehydration of the yeast from which the decke has been removed with cold water. 発酵工程後に回収した泥状酵母から苦味物質を除去する酵母の脱苦味処理方法において、
前記泥状酵母とアルカリ水溶液とを混合することにより前記泥状酵母に対する脱苦味を行う脱苦味工程と、前記脱苦味後の酵母のデッケ分を除去するデッケ除去工程とを備えたことを特徴とする酵母の脱苦味処理方法。
In the debittering treatment method for yeast that removes bitter substances from muddy yeast recovered after the fermentation process,
A debittering step for debittering the muddy yeast by mixing the muddy yeast and an aqueous alkaline solution, and a dekke removal step for removing the dekke content of the yeast after the debittering taste, Yeast bitterness treatment method.
JP2006320225A 2006-11-28 2006-11-28 Apparatus and method for debittering yeast Pending JP2008131881A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010057434A (en) * 2008-09-04 2010-03-18 Kirin Food-Tech Co Ltd Agent for enhancing milk feeling of milk-containing food
JP2010268713A (en) * 2009-05-20 2010-12-02 Kirin Kyowa Foods Co Ltd Sauce taste improver
JP2013507983A (en) * 2009-10-27 2013-03-07 ピュアバイオ アンド テック インコーポレイテッド Regenerative cell extraction system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010057434A (en) * 2008-09-04 2010-03-18 Kirin Food-Tech Co Ltd Agent for enhancing milk feeling of milk-containing food
JP2010268713A (en) * 2009-05-20 2010-12-02 Kirin Kyowa Foods Co Ltd Sauce taste improver
JP2013507983A (en) * 2009-10-27 2013-03-07 ピュアバイオ アンド テック インコーポレイテッド Regenerative cell extraction system

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