JPH0591890A - Production of trehalose - Google Patents

Production of trehalose

Info

Publication number
JPH0591890A
JPH0591890A JP21547891A JP21547891A JPH0591890A JP H0591890 A JPH0591890 A JP H0591890A JP 21547891 A JP21547891 A JP 21547891A JP 21547891 A JP21547891 A JP 21547891A JP H0591890 A JPH0591890 A JP H0591890A
Authority
JP
Japan
Prior art keywords
trehalose
extraction
yeast
extracted
drying
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.)
Pending
Application number
JP21547891A
Other languages
Japanese (ja)
Inventor
Kanji Matsumoto
幹治 松本
Yumi Yoshikawa
ユミ 吉川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tonen General Sekiyu KK
Original Assignee
Tonen Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tonen Corp filed Critical Tonen Corp
Priority to JP21547891A priority Critical patent/JPH0591890A/en
Publication of JPH0591890A publication Critical patent/JPH0591890A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To easily obtain a large amount of trehalose in a short time by heating and drying microbial cell containing trehalose and extracting the denaturated cell with water or an organic solvent. CONSTITUTION:A trehalose-containing microbial cell (preferably cell of yeast of the genus Saccharomyces) is denaturated by heating and/or drying. The denaturated cell is extracted with water or an organic solvent (preferably ethanol) and trehalose is separated from the extracted liquid. The above heat- treatment is preferably carried out at 80-100 deg.C for 2hr and the drying is preferably performed at 90-110 deg.C for 5hr.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、甘味料、保存剤、保湿
剤、さらには制ガン剤の原料として食品、医薬品分野で
広く利用が期待されているトレハロースの製造方法に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing trehalose, which is expected to be widely used in the fields of foods and pharmaceuticals as a raw material for sweeteners, preservatives, humectants, and anticancer agents.

【0002】[0002]

【従来の技術】トレハロースは微生物による生産の他、
酵素法などによっても製造されるが、その収量はわずか
であるため生産コストがかかる。そこで、一般には多量
にトレハロースを含有するパン酵母などから得る方法が
用いられる。L. C. Stewart ら、J.Am.Chem.Soc., 20
59〜2061頁、1950には圧搾酵母を95%アル
コールで抽出してトレハロースを得る方法が記載されて
いる。また農化第27巻第7号、412〜419頁(昭
和28年)にはパン酵母を90%エタノールで煮沸抽出
してトレハロースを得る方法が記載されている。
BACKGROUND OF THE INVENTION Trehalose is produced by microorganisms,
It is also produced by an enzymatic method or the like, but the production amount is high because the yield is small. Therefore, generally, a method of obtaining from baker's yeast containing a large amount of trehalose is used. LC Stewart et al., J. Am. Chem. Soc., 20.
Pages 59 to 2061 and 1950 describe a method of extracting squeezed yeast with 95% alcohol to obtain trehalose. Further, Agricultural Vol. 27, No. 7, pp. 412 to 419 (Showa 28), a method for obtaining trehalose by boiling and extracting baker's yeast with 90% ethanol is described.

【0003】トレハロースのエタノール水溶液による抽
出においては、エタノール濃度が低い場合には菌体中の
蛋白質も多量に抽出され、抽出後のトレハロースの回収
・精製工程が複雑になる。蛋白質の抽出を抑制するため
には高濃度のエタノールを使用する必要があるが、高濃
度のエタノールを用いて生菌体からトレハロースを抽出
しようとする場合、抽出率が非常に低くなる。
In the extraction of trehalose with an aqueous ethanol solution, when the concentration of ethanol is low, a large amount of protein in the cells is also extracted, and the process of recovery and purification of trehalose after extraction becomes complicated. Although it is necessary to use high-concentration ethanol in order to suppress the extraction of protein, the extraction rate becomes very low when high-concentration ethanol is used to extract trehalose from living cells.

【0004】また、生菌体からのトレハロースの抽出に
おいては抽出温度が低い場合には菌体内に存在する酵素
トレハラーゼによるトレハロースの分解等のためトレハ
ロースの抽出量が少なくなり、この傾向は特に低濃度ア
ルコール又は水を用いて抽出する場合に顕しい。このた
め生菌体からの抽出においては高温抽出を行わなければ
ならない。
Further, in the extraction of trehalose from live cells, when the extraction temperature is low, the amount of trehalose extracted decreases due to decomposition of trehalose by the enzyme trehalase existing in the cells, and this tendency is particularly low. Remarkable when extracting with alcohol or water. For this reason, high-temperature extraction must be performed when extracting from live cells.

【0005】また、生菌体からのトレハロースの抽出に
は比較的長時間を要する。
Further, it takes a relatively long time to extract trehalose from living cells.

【0006】[0006]

【発明が解決しようとする課題】従って本発明は上記の
種々の問題点を解決しようとするものである。
Therefore, the present invention is intended to solve the above-mentioned various problems.

【0007】[0007]

【課題を解決するための手段】本発明者らは上記の種々
の課題を解決すべく鋭意検討した結果、菌体を加熱及び
/又は乾燥により変性処理することにより上記の種々の
課題が解決されることを見出し、本発明を完成した。従
って、本発明はトレハロースを含有する菌体を加熱及び
/又は乾燥することによって該菌体を変性処理し、次に
水又は有機溶剤水溶液によりトレハロースを抽出し、そ
して該抽出液からトレハロースを採取することを特徴と
するトレハロースの製造方法を提供するものである。
Means for Solving the Problems As a result of intensive studies to solve the above-mentioned various problems, the present inventors have solved the above-mentioned various problems by denaturing the cells by heating and / or drying. It was found that the present invention was completed. Therefore, in the present invention, the bacterium containing trehalose is subjected to a denaturing treatment by heating and / or drying, and then trehalose is extracted with water or an aqueous solution of an organic solvent, and trehalose is collected from the extract. The present invention provides a method for producing trehalose, which is characterized by the above.

【0008】[0008]

【具体的な説明】本発明においてはトレハロースを含有
する任意の微生物の菌体、例えばリゾクトニア属、スク
レロナウム属、アースロバクター属、ノカルディア属等
の微生物の菌体を用いることができるが、実用上酵母の
菌体が好ましく、特にサッカロミセス(Sacchar
omyces)属酵母の菌体が好ましい。酵母菌体とし
てはトレハロースの製造のために特に培養したものを用
いることができるが、パン酵母等、他の目的で製造され
た酵母、ビールの製造等において副生する酵母等も用い
ることができる。
DETAILED DESCRIPTION In the present invention, microbial cells of any microorganism containing trehalose, for example, microbial cells of the genus Rhizoctonia, the genus Scleronium, the genus Arthrobacter, the genus Nocardia, etc. can be used. Upper yeast cells are preferred, and particularly Saccharomyces ( Sacchar
Oomyces ) yeast cells are preferred. As the yeast cells, those that have been particularly cultured for the production of trehalose can be used, but yeasts produced for other purposes such as baker's yeast, yeasts that are a by-product in the production of beer, etc. can also be used. ..

【0009】本発明において菌体を加熱及び/又は乾燥
処理するのは、トレハロース分解酵素であるトレハラー
ゼを失活させ、蛋白質を変性凝固せしめ、細胞壁を破壊
する、等のためである。従って、これらの目的を達成す
る加熱又は乾燥方法であればいずれの方法も用いること
ができる。例えば、加熱処理は、湿生菌体、菌体懸濁液
等を70℃〜110℃、好ましくは80℃〜100℃、
例えば95℃にて0.5〜12時間、好ましくは2時間
程度、水分の蒸発を抑えながら処理することにより行う
ことができる。また、乾燥処理は菌体を70℃〜110
℃、好ましくは90℃〜110℃、例えば100℃にて
2〜12時間、好ましくは5時間程度、水分を蒸発させ
ながら処理することにより行うことができる。なお、市
販の乾燥状態のパン製造用酵母は乾燥菌体ではあるが、
菌体の死滅又は損傷を最小限に留める特定の条件下で製
造されたものであるから、追加の加熱又は乾燥処理が施
されていない限り本発明の乾燥菌体には該当しない。
In the present invention, the cells are heated and / or dried to inactivate trehalase, which is a trehalose-degrading enzyme, denature and coagulate proteins, and destroy cell walls. Therefore, any heating or drying method that achieves these objects can be used. For example, the heat treatment may be performed on a wet cell, a cell suspension or the like at 70 ° C to 110 ° C, preferably 80 ° C to 100 ° C.
For example, the treatment can be performed at 95 ° C. for 0.5 to 12 hours, preferably about 2 hours while suppressing the evaporation of water. In addition, the drying treatment is performed on the cells at 70 ° C to 110 ° C.
C., preferably 90.degree. C. to 110.degree. C., for example, 100.degree. C. for 2 to 12 hours, preferably about 5 hours, while performing the treatment while evaporating water. Although commercially available yeast for bread making is a dry cell,
Since it was produced under specific conditions that kill or damage the cells to a minimum, it does not correspond to the dried cells of the present invention unless it is subjected to additional heating or drying treatment.

【0010】本発明の方法に用いる抽出溶剤は水又は有
機溶剤の水溶液である。この場合の有機溶剤としては、
水混和性の有機溶剤、例えばメタノール、エタノール、
アセトン等を用いることができるが、無毒性、蛋白質凝
集力、トレハロース抽出力、脂質抽出力等、種々の観点
からエタノールが好ましい。有機溶剤の好ましい濃度は
その有機溶剤のトレハロース溶解力、蛋白質凝集力等に
より異なる。
The extraction solvent used in the method of the present invention is water or an aqueous solution of an organic solvent. As the organic solvent in this case,
Water-miscible organic solvents such as methanol, ethanol,
Acetone or the like can be used, but ethanol is preferable from various viewpoints such as nontoxicity, protein aggregating power, trehalose extraction power, lipid extraction power and the like. The preferred concentration of the organic solvent varies depending on the trehalose-dissolving power of the organic solvent, the protein cohesion, and the like.

【0011】例えばエタノールについて言えば、図1に
示すごとく、抽出溶剤の沸点において1時間抽出した場
合、0%(水)からおよそ80%までの範囲で効率よく
抽出することができる。これは、生酵母においてはエタ
ノール濃度が60%以上では濃度の上昇と共に抽出率が
急激に低下するのと対照的である。図2に示すごとく、
抽出溶剤の沸点にて1時間抽出した場合、エタノール濃
度が上昇するに従って、蛋白質の抽出(溶解)量が急激
に減少する。従って、エタノール濃度50%〜90%、
好ましくは60%〜80%、例えば65〜70%程度の
エタノール水溶液を用いて抽出すれば、トレハロースが
十分に抽出され、しかも抽出液の蛋白質の溶解量が少な
いから、トレハロースを抽出液から非常に簡単に採取す
ることができる。
As for ethanol, for example, as shown in FIG. 1, when extraction is carried out for 1 hour at the boiling point of the extraction solvent, it can be efficiently extracted in the range of 0% (water) to approximately 80%. This is in contrast to that in the live yeast, when the ethanol concentration is 60% or more, the extraction rate sharply decreases as the concentration increases. As shown in Figure 2,
When extraction is performed at the boiling point of the extraction solvent for 1 hour, the amount of protein extracted (dissolved) sharply decreases as the ethanol concentration increases. Therefore, the ethanol concentration is 50% to 90%,
Preferably, trehalose is sufficiently extracted by extraction with an aqueous ethanol solution of 60% to 80%, for example, about 65 to 70%, and the amount of protein dissolved in the extract is small. It can be collected easily.

【0012】例えば、上記の濃度のエタノール水溶液に
より、その沸点温度にて本発明の処理酵母を抽出し、抽
出液を濾過、遠心分離等にかけることにより酵母菌体、
凝固蛋白質等を除去した後、得られた濾液又は上清を冷
却すればトレハロースが粗結晶の形で得られる。抽出時
間は、15分間以上で十分であり、抽出時間の上限は特
に臨界的ではない。しかしながら抽出時間を長くしても
抽出率が向上することはないから、実用上15分間〜1
時間が適当である。抽出溶剤として水を用い沸点にて抽
出を行い、トレハロースの抽出量を経時的に測定した結
果を図3に示す。この図から明らかな通り、生酵母では
30分間の抽出処理ではトレハロースの抽出量は非常に
少なく、少なくとも1時間の抽出が必要である。最終的
な抽出量も本発明の処理酵母に比べてかなり低い。
[0012] For example, the treated yeast of the present invention is extracted at the boiling temperature thereof with an aqueous ethanol solution having the above-mentioned concentration, and the extract is subjected to filtration, centrifugation, etc. to obtain yeast cells,
After removing coagulated proteins and the like, trehalose is obtained in the form of crude crystals by cooling the obtained filtrate or supernatant. The extraction time of 15 minutes or more is sufficient, and the upper limit of the extraction time is not particularly critical. However, even if the extraction time is lengthened, the extraction rate does not improve, so in practice 15 minutes to 1
Time is appropriate. FIG. 3 shows the results of measuring the amount of trehalose extracted with time by performing extraction at the boiling point using water as the extraction solvent. As is clear from this figure, the amount of trehalose extracted by the live yeast for the extraction treatment for 30 minutes is very small, and extraction for at least 1 hour is required. The final extraction amount is also considerably lower than that of the treated yeast of the present invention.

【0013】次に、抽出温度は、35℃〜溶剤の沸点の
範囲において、いずれの温度においても十分に抽出する
ことができる。図4は抽出溶剤として水を用い種々の温
度で1時間抽出処理を行った場合のトレハロース抽出量
を測定した結果である。本発明の処理を施した酵母にお
いては35℃〜100℃の間でトレハロース抽出量に差
は見られないが、生酵母においてはおよそ30℃〜60
℃の間で抽出されるトレハロース量が非常に少ない。こ
の理由の1つは生菌体中に含まれるトレハラーゼにより
トレハロースが抽出中に分解されるためと考えられる。
70℃〜100℃においてはトレハラーゼの失活等のた
め生菌体からもかなりのトレハロースが抽出されるが、
本発明の処理を行った菌体からのトレハロース量よりか
なり少ない。
Next, the extraction temperature is in the range of 35 ° C. to the boiling point of the solvent, and sufficient extraction can be performed at any temperature. FIG. 4 shows the results of measuring the amount of trehalose extracted when water was used as the extraction solvent and the extraction treatment was carried out at various temperatures for 1 hour. There is no difference in the amount of trehalose extracted in the yeast treated with the present invention between 35 ° C and 100 ° C, but in the live yeast, it is approximately 30 ° C-60 ° C.
Very little amount of trehalose extracted between ° C. One of the reasons for this is considered to be that trehalose contained in living cells is decomposed during the extraction.
At 70 ° C to 100 ° C, a considerable amount of trehalose is extracted from live cells due to inactivation of trehalase, etc.,
It is considerably smaller than the amount of trehalose from the cells that have been treated according to the present invention.

【0014】図5は、図4と同様の実験をエタノール5
0%水溶液を用いて行った結果である。生酵母からの低
温におけるトレハロースの抽出量は水を用いた場合ほど
低くはないが本発明の処理を行った酵母からの抽出量に
比べてかなり少ない。また、全温度域において本発明の
処理を施された酵母からのトレハロース抽出量は生酵母
からのそれに比べて常に多い。
FIG. 5 shows the same experiment as in FIG.
This is the result obtained by using a 0% aqueous solution. Although the amount of trehalose extracted from live yeast at low temperature is not as low as when water is used, it is considerably smaller than the amount extracted from yeast treated with the present invention. In addition, the amount of trehalose extracted from yeast treated with the present invention in the entire temperature range is always higher than that from live yeast.

【0015】上記の結果を考慮して、本発明のトレハロ
ースの製造方法の好ましい態様は次の通りである。加熱
処理をした酵母では、処理した酵母に高濃度エタノール
水溶液を加え、常温あるいは加温状態において10〜2
0分間攪拌を行い、抽出する。加えるエタノール水溶液
の濃度は処理酵母中の水分量によって異なるが、好まし
くは酵母中の水分を考慮し、攪拌後のエタノール濃度が
65%以上になることが望ましい。これは除蛋白を行な
い、さらに結晶化の際のトレハロースの溶解度を下げる
ためである。抽出後、懸濁液を濾過し、この濾液を冷却
することにより粗結晶を得る。
Considering the above results, the preferred embodiment of the method for producing trehalose of the present invention is as follows. In the case of heat-treated yeast, a high-concentration ethanol aqueous solution is added to the treated yeast, and the yeast is heated to room temperature or heated for 10 to 2
Stir for 0 minutes and extract. Although the concentration of the aqueous ethanol solution to be added varies depending on the amount of water in the treated yeast, it is preferable that the concentration of ethanol after stirring be 65% or more in consideration of the water in the yeast. This is because deproteinization is performed and the solubility of trehalose during crystallization is further reduced. After extraction, the suspension is filtered and the filtrate is cooled to obtain crude crystals.

【0016】乾燥処理を行った酵母では処理した酵母に
エタノール水溶液を加え、約20分間攪拌する。この懸
濁液を濾過し、濾液を冷却し、粗結晶を得る。なお、濾
液中のトレハロース濃度が低い場合には、濾液を濃縮し
た後に結晶化を行う。
For the yeast which has been dried, an aqueous ethanol solution is added to the treated yeast and stirred for about 20 minutes. The suspension is filtered and the filtrate is cooled to give crude crystals. When the trehalose concentration in the filtrate is low, the filtrate is concentrated and then crystallized.

【0017】[0017]

【発明の効果】上記の結果、本発明の方法によれば、生
菌体を使用する抽出方法に比べて、(1)トレハロース
の抽出量が常に多く、(2)抽出速度が高いから短時間
で抽出することができ、(3)抽出温度が限定されない
から、必要に応じて自由に抽出温度を設定することがで
き、(4)蛋白質が凝固する高アルコール濃度において
もトレハロースの抽出量が多いから、蛋白質含量の少な
いトレハロース抽出液が得られ、この抽出液からのトレ
ハロースの回収が極めて容易であり、そして(5)トレ
ハロース抽出率についていえば低濃度のアルコール水溶
液により抽出可能であるから、エタノールの使用量が少
なくてすむ。
As a result of the above, according to the method of the present invention, (1) the extraction amount of trehalose is always large, and (2) the extraction rate is high, as compared with the extraction method using live cells, so that the extraction time is short. (3) The extraction temperature is not limited, so the extraction temperature can be freely set as needed, and (4) the amount of trehalose extracted is high even at high alcohol concentrations where proteins coagulate. From this, a trehalose extract containing a small amount of protein was obtained, and trehalose was extremely easily recovered from this extract, and (5) trehalose extraction ratio was low. Uses less amount of.

【0018】[0018]

【実施例】次に、実験例及び実施例により本発明をさら
に具体的に説明する。なお、以下の実験例においては次
の一般的手法を用いた。生酵母としてオリエンタル酵母
(株)製パン酵母を用いた。酵母の乾燥及び/又は加熱
処理は後記の通りとした。抽出は湿重量30gの酵母を
150mlの溶媒に懸濁して行った。抽出処理後の固液分
離は0.22μmのメングランフィルターを用いる濾過
により行った。トレハロースの定量は、高速液体クロマ
トグラフィー(島津製作所製CR−4A;カラム:Bi
o−Rad製アミネックスHPX−87C)により行
い、蛋白質の定量は色素結合法(Coomassie Burilliant
Blue G−250)により行った。また、トレハロース
の抽出率は、生パン酵母から100℃の水を用いて1時
間抽出した場合に抽出されたトレハロース量を1.0と
して算出した。
EXAMPLES Next, the present invention will be described more specifically by way of experimental examples and examples. The following general method was used in the following experimental examples. Baker's yeast manufactured by Oriental Yeast Co., Ltd. was used as the live yeast. The yeast drying and / or heat treatment was as described below. The extraction was carried out by suspending yeast having a wet weight of 30 g in a solvent of 150 ml. Solid-liquid separation after the extraction treatment was performed by filtration using a 0.22 μm Menglan filter. High-performance liquid chromatography (CR-4A manufactured by Shimadzu Corporation; column: Bi
Aminex HPX-87C manufactured by o-Rad), and the protein was quantified by a dye binding method (Coomassie Burilliant).
Blue G-250). The extraction rate of trehalose was calculated by setting the amount of trehalose extracted from raw baker's yeast extracted with water at 100 ° C. for 1 hour to 1.0.

【0019】実験例1.加熱・乾燥条件の検討 加熱処理は生パン酵母を非乾燥条件下、すなわちフィル
ムにより密閉した状態で室温〜100℃の間の種々の温
度において0〜12時間の間の種々の時間にわたって行
った。乾燥処理は生パン酵母を乾燥条件下(大気開放の
状態)で室温〜100℃の間の種々の温度において0〜
12時間の種々の時間にわたって行った。加熱・乾燥処
理結果の評価は、処理された酵母を抽出剤である純水に
より100℃にて1時間抽出処理した後のトレハロース
抽出量により評価した。
Experimental Example 1. Examination of heating and drying conditions The heat treatment was performed on raw baker's yeast under non-drying conditions, that is, in a state of being sealed with a film, at various temperatures between room temperature and 100 ° C for various times between 0 and 12 hours. The drying treatment is carried out by drying raw baker's yeast at various temperatures between room temperature and 100 ° C. under dry conditions (open to the atmosphere).
It was carried out for various times of 12 hours. The evaluation of the heating / drying treatment results was carried out by the amount of trehalose extracted after treating the treated yeast with pure water as an extractant at 100 ° C. for 1 hour.

【0020】その結果、乾燥、及び加熱の処理温度は抽
出率に大きく影響を及ぼし、12時間の処理において、
45℃付近ではほとんどトレハロースが抽出されなかっ
た。しかし、45℃以上では温度の上昇と共に抽出率は
増大し、70〜80℃以上でほぼ一定となった。次に処
理時間について検討を行った。100℃での加熱処理酵
母では2時間処理までは徐々に抽出率が増大したが、そ
れ以後はほぼ一定の値であった。したがって、加熱処理
は2時間で充分である。100℃における乾燥処理では
乾燥率(生酵母を105℃、5時間乾燥させた後の減少
質量に対する、所定時間乾燥させた後の減少質量の比で
表した。)の増大とともに抽出率が増大し、乾燥率10
0%となる5時間以降、一定になった。したがって加熱
時間は5時間で充分である。以記の結果から、加熱処理
酵母としては、生酵母を100℃にて12時間加熱した
ものを用い、そして乾燥酵母としては生酵母を100℃
にて12時間乾燥したものを用いた。
As a result, the treatment temperature of drying and heating has a great influence on the extraction rate, and in the treatment for 12 hours,
Almost no trehalose was extracted at around 45 ° C. However, the extraction rate increased as the temperature increased at 45 ° C or higher, and became almost constant at 70 to 80 ° C or higher. Next, the processing time was examined. In the heat-treated yeast at 100 ° C., the extraction rate gradually increased until the treatment for 2 hours, but after that, it was almost constant. Therefore, the heat treatment for 2 hours is sufficient. In the drying treatment at 100 ° C., the extraction rate increased as the drying rate (expressed by the ratio of the reduced mass after drying the live yeast for 105 hours at 105 ° C. for 5 hours to the reduced mass after drying for a predetermined time) increased. , Drying rate 10
It became constant after 5 hours when it became 0%. Therefore, a heating time of 5 hours is sufficient. From the results described below, as the heat-treated yeast, live yeast heated at 100 ° C. for 12 hours was used, and as dry yeast, live yeast was heated at 100 ° C.
The dried product was used for 12 hours.

【0021】実験例2.抽出剤のエタノール濃度の検討
(図1及び図2) 生酵母及び各処理酵母から、種々の濃度のエタノール水
溶液を用いて、各溶媒の沸点において、トレハロースを
抽出した結果を図1に示す。トレハロース抽出率は生パ
ン酵母からの抽出の場合、最もエタノール濃度に依存
し、40vol %付近をピークとする曲線となった。それ
以上の濃度では急激に抽出率が低下した。一方、乾燥、
又は加熱を施した酵母では、生酵母の場合ほど顕著では
ないが依存性がみられた。しかし、何れのエタノール濃
度においてもトレハロースの抽出率は、処理酵母の方が
生酵母よりも大きく、加熱、あるいは乾燥処理により抽
出率が増大することがわかった。
Experimental Example 2. Examination of ethanol concentration of extractant
(FIGS. 1 and 2) The results of extracting trehalose from live yeast and each treated yeast using various concentrations of aqueous ethanol solutions at the boiling point of each solvent are shown in FIG. The extraction rate of trehalose was most dependent on the ethanol concentration in the case of extraction from raw baker's yeast, and the curve showed a peak at around 40 vol%. At higher concentrations, the extraction rate dropped sharply. On the other hand, dry,
Alternatively, in the yeast which was heated, the dependence was observed, though not as remarkable as in the case of the live yeast. However, it was found that the trehalose extraction rate was higher in the treated yeast than in the live yeast at any ethanol concentration, and the extraction rate was increased by heating or drying.

【0022】また、エタノール濃度と、固液分離後の蛋
白質残存率との関係を調べた。生酵母をエタノール抽出
液中で沸点にて1時間処理した後、4℃、6000rpm
にて遠心分離し、上清中の蛋白質の相対量を、水抽出の
場合を100として図2に示す。この図から明らかな通
り、抽出液中のアルコール濃度が60%以上となると、
残存蛋白質の量が著しく減少した。
Further, the relationship between the ethanol concentration and the protein residual rate after solid-liquid separation was investigated. After treating live yeast with boiling point for 1 hour in ethanol extract, 4 ℃, 6000rpm
It is centrifuged in FIG. 2 and the relative amount of protein in the supernatant is shown in FIG. As is clear from this figure, when the alcohol concentration in the extract exceeds 60%,
The amount of residual protein was significantly reduced.

【0023】実験例3.抽出時間の検討(図3) 各酵母からの抽出速度の比較を行った。図3に抽出率の
経時変化を示す。この図から明らかなように、加熱又は
乾燥処理した酵母からの抽出は未処理酵母からの抽出に
比べて著しく速く、15〜20分程度の抽出で充分であ
ることがわかった。
Experimental Example 3. Examination of extraction time (Fig. 3) The extraction rates from each yeast were compared. FIG. 3 shows the change over time in the extraction rate. As is clear from this figure, the extraction from the heat-treated or dried yeast was significantly faster than the extraction from the untreated yeast, and it was found that the extraction for about 15 to 20 minutes was sufficient.

【0024】実験例4.抽出温度の検討(図4及び図
5) 各酵母からの抽出に及ぼす抽出温度の影響を検討した。
純水での抽出結果を図4に、50vol %エタノール水溶
液での抽出を図5に示す。純水での抽出では、生パン酵
母からの抽出率は著しく温度に影響された。また、エタ
ノール水溶液でもわずかに影響が見られた。しかし乾
燥、加熱処理酵母ではまったく影響は見られず室温での
抽出も可能であることがわかった。
Experimental Example 4. Examination of extraction temperature (Fig. 4 and Fig.
5) The effect of extraction temperature on the extraction from each yeast was examined.
The extraction result with pure water is shown in FIG. 4, and the extraction with 50 vol% ethanol aqueous solution is shown in FIG. In extraction with pure water, the extraction rate from raw baker's yeast was significantly affected by temperature. In addition, the effect was slightly observed in the ethanol aqueous solution. However, it was found that the dried and heat-treated yeast had no effect at all, and extraction at room temperature was also possible.

【図面の簡単な説明】[Brief description of drawings]

【図1】図1は、抽出時間が1時間、抽出温度が抽出溶
剤の沸点での、抽出溶剤中のエタノール濃度とトレハロ
ースの相対抽出量との関係を示すグラフである。
FIG. 1 is a graph showing the relationship between the concentration of ethanol in the extraction solvent and the relative amount of trehalose extracted when the extraction time is 1 hour and the extraction temperature is the boiling point of the extraction solvent.

【図2】図2は、生酵母を種々のアルコール濃度の抽出
剤により沸点にて1時間抽出した場合の濾過した抽出液
中の蛋白質の量を示すグラフである。
[Fig. 2] Fig. 2 is a graph showing the amount of protein in the filtered extract when live yeast was extracted with boiling point for 1 hour with extractants having various alcohol concentrations.

【図3】図3は、抽出剤として水を用い、沸点にて抽出
を行った場合の抽出時間のトレハロースの相対抽出量と
の関係を示すグラフである。
FIG. 3 is a graph showing the relationship between the extraction time and the relative amount of trehalose extracted when water is used as the extractant and extraction is performed at the boiling point.

【図4】図4は抽出剤として水を用い、1時間抽出した
場合の抽出温度とトレハロースの相対抽出量の関係を示
すグラフである。
FIG. 4 is a graph showing the relationship between the extraction temperature and the relative amount of trehalose extracted when water is used as the extractant for 1 hour.

【図5】図5は抽出剤として50%エタノール水溶液を
用い1時間抽出した場合の抽出温度とトレハロース抽出
量との関係を示すグラフである。
FIG. 5 is a graph showing the relationship between the extraction temperature and the amount of trehalose extracted when an aqueous solution of 50% ethanol was used as an extractant for extraction for 1 hour.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 トレハロースを含有する菌体を加熱及び
/又は乾燥することによって該菌体を変性処理し、次に
水又は有機溶剤水溶液によりトレハロースを抽出し、そ
して該抽出液からトレハロースを採取することを特徴と
するトレハロースの製造方法。
1. A bacterium containing trehalose is subjected to a denaturation treatment by heating and / or drying, and then trehalose is extracted with water or an aqueous solution of an organic solvent, and trehalose is collected from the extract. A method for producing trehalose, comprising:
JP21547891A 1991-08-27 1991-08-27 Production of trehalose Pending JPH0591890A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21547891A JPH0591890A (en) 1991-08-27 1991-08-27 Production of trehalose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21547891A JPH0591890A (en) 1991-08-27 1991-08-27 Production of trehalose

Publications (1)

Publication Number Publication Date
JPH0591890A true JPH0591890A (en) 1993-04-16

Family

ID=16673046

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21547891A Pending JPH0591890A (en) 1991-08-27 1991-08-27 Production of trehalose

Country Status (1)

Country Link
JP (1) JPH0591890A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995009243A1 (en) * 1993-09-28 1995-04-06 Ústav Makromolekulární Chemie Akademie Ved C^¿Eské Republiky METHOD OF PRODUCING α,α-TREHALOSE
EP0707062A1 (en) 1994-09-16 1996-04-17 Nihon Shokuhin Kako Co., Ltd. Maltose phosphorylase, trehalose phosphorylase, plesiomonas strain and preparation process of trehalose
CN102504040A (en) * 2011-11-16 2012-06-20 华南理工大学 Method for extracting trehalose from waste yeast after sterol production
JP2013013424A (en) * 1993-06-03 2013-01-24 Hayashibara Co Ltd Trehalose-releasing enzyme, method for producing the same, and use thereof

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013013424A (en) * 1993-06-03 2013-01-24 Hayashibara Co Ltd Trehalose-releasing enzyme, method for producing the same, and use thereof
WO1995009243A1 (en) * 1993-09-28 1995-04-06 Ústav Makromolekulární Chemie Akademie Ved C^¿Eské Republiky METHOD OF PRODUCING α,α-TREHALOSE
EP0707062A1 (en) 1994-09-16 1996-04-17 Nihon Shokuhin Kako Co., Ltd. Maltose phosphorylase, trehalose phosphorylase, plesiomonas strain and preparation process of trehalose
US5705378A (en) * 1994-09-16 1998-01-06 Nihon Shokuhin Kako Co. Ltd. Maltose phosphorylase, trehalose phosphorylase, novel strain of genus plesiomonas capable of producing these enzymes and process for producing trehalose
US5935827A (en) * 1994-09-16 1999-08-10 Nihon Shokuhin Kako Co., Ltd. Maltose phosphorylase, trehalose phosphorylase, novel strain of genus plesiomonas capable of producing these enzymes and process for producing trehalose
CN102504040A (en) * 2011-11-16 2012-06-20 华南理工大学 Method for extracting trehalose from waste yeast after sterol production

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