JP2008237055A - Method for producing rice saccharified liquid - Google Patents
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Description
本発明は、米の糖化液の製造方法に関し、詳しくは、エタノールを生産する前段階の糖化液製造工程に際し糖化効率が高い米糖化液の製造方法に関する。 The present invention relates to a method for producing a saccharified solution of rice, and more particularly, to a method for producing a saccharified solution of rice having high saccharification efficiency in a saccharified solution manufacturing step prior to ethanol production.
近年、地球温暖化防止策の一環としてエタノール、特に生物由来のエタノールへの関心が高まっており、エタノールを燃料とする車が開発されたことや、原料となるトウモロコシやサトウキビの価格高騰などの現象は記憶に新しいところである。 In recent years, as part of measures to prevent global warming, there has been an increasing interest in ethanol, especially bio-derived ethanol, and the development of vehicles that use ethanol as fuel, as well as rising prices for raw corn and sugarcane. Is new to memory.
米は、日本酒の原料であり、発酵素材としてはなじみの深い素材であるが、トウモロコシやサトウキビに比べ価格が高い点、トウモロコシよりもたんぱく質の量が多い点、加熱すると糊化が強い澱粉の性質などから工業的なエタノール生産の原料としての活用は遅れていた。 Rice is a raw material for sake and is a familiar material for fermentation, but it is more expensive than corn and sugarcane, has a higher protein content than corn, and has a high gelatinization property when heated. As a result, its utilization as a raw material for industrial ethanol production was delayed.
エタノールの製造工程には、高分子の澱粉を含む原料を主にグルコースなどの分子量の小さい糖質に加水分解する糖化工程と、酵母によってグルコースからエタノールを生産する発酵工程がある。糖化工程には、酸を用いて加水分解する酸糖化法と、酵素を用いて加水分解する酵素糖化法が知られている。 The ethanol production process includes a saccharification process in which a raw material containing a high molecular weight starch is mainly hydrolyzed into a sugar having a low molecular weight such as glucose, and a fermentation process in which ethanol is produced from glucose by yeast. As the saccharification step, an acid saccharification method in which hydrolysis is performed using an acid and an enzyme saccharification method in which hydrolysis is performed using an enzyme are known.
米の糖化は、本発明のようなアルコールを生産する他に、水飴(主な成分をグルコースが2つ結合したマルトースとする)などの甘味料を生産するためにも行われており、さまざまな手法が開示されている。 In addition to producing alcohol as in the present invention, saccharification of rice is also performed to produce sweeteners such as starch syrup (the main ingredient is maltose in which two glucoses are combined). A technique is disclosed.
特許文献1では、新規な活性を持つ複合酵素剤による糖化反応促進でグルコースを高収量で得る技術が開示されている。 Patent Document 1 discloses a technique for obtaining glucose in a high yield by promoting a saccharification reaction with a complex enzyme agent having a novel activity.
また、特許文献2においては生米に水を加え、115〜125℃、1〜6分の高温高圧処理を行って澱粉をα化させ、その後にアミラーゼを加えてホモジナイズし、酵素の作用を高めて短時間で糖化させ、その後すぐに酵素を失活させて、糖液の生産を行う技術が開示されている。
しかし、特許文献1に記載の技術では、特別な複合酵素剤を生産又は購入する必要がある。複合酵素剤を生産するには窒素源、炭素源が必要となり、さらにその培養には温度管理、pH管理を2〜4日かけて行わなければならない。また、培養後は遠心分離、除菌等を行って回収作業も行わなければならず、手間及び費用がかかるという問題がある。 However, in the technique described in Patent Document 1, it is necessary to produce or purchase a special complex enzyme agent. In order to produce a complex enzyme agent, a nitrogen source and a carbon source are required, and further, temperature control and pH control must be performed for 2 to 4 days for the culture. Moreover, after culture | cultivation, centrifugation, disinfection, etc. must be performed and collection | recovery work must also be performed, and there exists a problem that an effort and expense start.
特許文献2の技術は糊化が強いα澱粉に対して流動性を確保する必要があり、米の容量に対してバッチ式で2〜4倍、連続式では8〜12倍の水を添加しなければならない。 In the technology of Patent Document 2, it is necessary to ensure fluidity with respect to α starch having strong gelatinization, and 2 to 4 times as much water as batch type and 8 to 12 times as much water as continuous type is added to the rice capacity. There must be.
そこで、本発明の課題は、一般の酵素を用いて米糖化液を製造する際に、酸・高温高圧の前処理を行うことで、米の糖化効率を格段に向上させる米糖化液の製造方法を提供することにある。 Then, the subject of this invention is the manufacturing method of the rice saccharified liquid which improves the saccharification efficiency of rice remarkably by performing the pretreatment of an acid and high temperature / high pressure when manufacturing rice saccharified liquid using a general enzyme Is to provide.
また本発明の他の課題は、以下の記載によって明らかとなる。 Other problems of the present invention will become apparent from the following description.
上記課題は、以下の各発明によって解決される。 The above problems are solved by the following inventions.
(請求項1)
容器に米粉と水を所定の混合比で導入して混合・攪拌後、該容器内の混合液に塩酸を添加してpHを1.5〜2.5に調整し、次いで酸処理後の混合液を圧力容器内で、温度100〜130℃の範囲下で15〜25分加熱する前処理を行い、その後酵素による糖化を行うことを特徴とする米糖化液の製造方法。
(Claim 1)
After mixing and stirring rice flour and water in a container at a predetermined mixing ratio, hydrochloric acid is added to the mixture in the container to adjust the pH to 1.5 to 2.5, and then mixing after acid treatment A method for producing a rice saccharified solution, comprising pretreating the solution in a pressure vessel at a temperature of 100 to 130 ° C for 15 to 25 minutes, and then performing saccharification with an enzyme.
(請求項2)
前記前処理における加熱温度が、110〜125℃であることを特徴とする請求項1記載の米糖化液の製造方法。
(Claim 2)
The method for producing a rice saccharified solution according to claim 1, wherein the heating temperature in the pretreatment is 110 to 125 ° C.
(請求項3)
前記前処理における加熱時間が18〜22分であることを特徴とする請求項1又は2記載の米糖化液の製造方法。
(Claim 3)
The method for producing a rice saccharified solution according to claim 1 or 2, wherein the heating time in the pretreatment is 18 to 22 minutes.
(請求項4)
米粉と水の混合比(重量比)が、1:1.5〜2.5であることを特徴とする請求項1、2又は3記載の米糖化液の製造方法。
(Claim 4)
The method for producing a rice saccharified solution according to claim 1, 2, or 3, wherein the mixing ratio (weight ratio) of rice flour and water is 1: 1.5 to 2.5.
本発明によれば、一般の酵素を用いて米糖化液を製造する際に、酸・高温高圧の前処理を行うことで、米の糖化効率を格段に向上させる米糖化液の製造方法を提供することができる。 ADVANTAGE OF THE INVENTION According to this invention, when manufacturing rice saccharified liquid using a general enzyme, the manufacturing method of the rice saccharified liquid which improves the saccharification efficiency of rice markedly by performing pretreatment of acid and high temperature and pressure is provided. can do.
以下、本発明の好ましい実施形態を説明する。 Hereinafter, preferred embodiments of the present invention will be described.
(前処理工程)
通常、米中澱粉を、酵素を使ってグルコースに変換すると、グルコースの回収効率が悪い。これは米中澱粉が運動性の低いβ澱粉として存在するためである。本発明では酵素処理を行う前処理として加熱処理を行うことでβ澱粉からα澱粉に変化させて、その運動性を高めることで米中の澱粉を酵素が分解しやすくなる。一方でα澱粉化した米は粘性が高く、糊状になると逆に酵素が作用しにくくなる。そのため、酸を加えて低pHで行うことで糊状になること(糊化)を防ぎ、α化澱粉の流動性を高めている。
(Pretreatment process)
Normally, when rice starch is converted to glucose using an enzyme, the efficiency of glucose recovery is poor. This is because starch in rice exists as β starch having low mobility. In this invention, it changes from beta starch to alpha starch by performing heat processing as pre-processing which performs enzyme treatment, and it becomes easy to decompose | disassemble the starch in rice by improving the motility. On the other hand, α-starch rice is highly viscous, and when it becomes pasty, the enzyme is less likely to act. Therefore, by adding an acid and carrying out at low pH, it is prevented from becoming pasty (gelatinization) and the fluidity of the pregelatinized starch is enhanced.
本発明の酸処理や加熱処理を行うと、澱粉がβ化しないよう60℃以上に保持したまま酵素処理を行うことで、グルコースの回収効率を高くし、米の糖化効率を向上させることができる。 When the acid treatment or the heat treatment of the present invention is performed, the enzyme treatment is performed while maintaining the starch at 60 ° C. or higher so that the starch is not β-ized, thereby increasing the glucose recovery efficiency and improving the rice saccharification efficiency. .
本発明の米糖化液の製造方法における最初の工程は、容器に米粉と水を所定の混合比で導入して混合・攪拌する工程である。 The first step in the method for producing a rice saccharified solution of the present invention is a step of introducing and mixing and stirring rice flour and water in a container at a predetermined mixing ratio.
米粉と水の混合比(重量比)は、1:1.5〜2.5であることが好ましく、より好ましくは1:1.2〜2.2である。混合比(重量比)が1:2.5より越えると、酵素反応効果が低下するので好ましくなく、また1:1.5より小さいと得られる糖液の濃度が低下するので好ましくない。 The mixing ratio (weight ratio) of rice flour and water is preferably 1: 1.5 to 2.5, more preferably 1: 1.2 to 2.2. When the mixing ratio (weight ratio) exceeds 1: 2.5, the enzyme reaction effect decreases, which is not preferable. When it is less than 1: 1.5, the concentration of the resulting sugar solution decreases, which is not preferable.
この工程で用いられる容器としては、耐酸性と耐熱性がある円筒形容器(約10L)等が挙げられる。 Examples of the container used in this step include a cylindrical container (about 10 L) having acid resistance and heat resistance.
次の工程は、前記容器内の混合液に塩酸を添加してpHを1.5〜2.5の範囲に調整する酸処理を行う工程である。 The next step is a step of performing an acid treatment for adjusting the pH to a range of 1.5 to 2.5 by adding hydrochloric acid to the mixed solution in the container.
酸処理に塩酸を用いるのは、糖化工程の後、アルコール発酵(エタノール生産)を行う上で好ましいからである。例えば硫酸を用いると、得られた糖化液に硫黄が含まれ、この硫黄がアルコール発酵を阻害するので好ましくない。 The reason for using hydrochloric acid for the acid treatment is that it is preferable for alcohol fermentation (ethanol production) after the saccharification step. For example, when sulfuric acid is used, sulfur is contained in the obtained saccharified solution, and this sulfur is not preferable because it inhibits alcohol fermentation.
本発明では、pHは1.5〜2.5の範囲に調整されるが、pHが1.5未満であると製造プロセスを耐強酸仕様にする必要があるために好ましくなく、またpHが2.5を越えるとα化した米の糊化を防ぐ効果が少ないので好ましくない。 In the present invention, the pH is adjusted to a range of 1.5 to 2.5, but if the pH is less than 1.5, it is not preferable because the production process needs to be resistant to strong acid, and the pH is 2 If it exceeds .5, the effect of preventing gelatinization of pregelatinized rice is small, which is not preferable.
本発明において好ましいpHは1.6〜2.4の範囲であり、より好ましいpHの範囲は1.8〜2.2の範囲である。 In the present invention, a preferred pH is in the range of 1.6 to 2.4, and a more preferred pH range is in the range of 1.8 to 2.2.
次の工程は、酸処理後の混合液を圧力容器内で、温度100〜130℃の範囲下で15〜25分加熱する工程である。 The next step is a step of heating the mixed solution after acid treatment in a pressure vessel at a temperature of 100 to 130 ° C. for 15 to 25 minutes.
加熱温度が100℃未満であると澱粉のα化が十分進行しないために好ましくなく、また加熱温度が130℃を越えると製造プロセスを耐圧仕様にしなければならないので好ましくない。加熱温度は好ましくは110〜125℃であり、さらに好ましくは120〜122℃である。 When the heating temperature is less than 100 ° C., it is not preferable since the pregelatinization of starch does not proceed sufficiently, and when the heating temperature exceeds 130 ° C., it is not preferable because the manufacturing process must be pressure resistant. The heating temperature is preferably 110 to 125 ° C, more preferably 120 to 122 ° C.
また加熱時間は15分未満であると澱粉のα化が十分進行しないために好ましくなく、また25分を越えても、それ以上の効果はなく、製造プロセスにおけるエネルギーを無駄に消費してしまうので好ましくない。加熱時間は好ましくは18〜22分である。 Also, if the heating time is less than 15 minutes, starch is not sufficiently converted to gelatin, and if it exceeds 25 minutes, there is no further effect, and energy in the production process is wasted. It is not preferable. The heating time is preferably 18 to 22 minutes.
加熱することにより、高温、高圧環境になり、米中澱粉をβ澱粉からα澱粉に変化させてその運動性を高めることができる。また、pHが1.5〜2.5の範囲に調整されているのでα化した米が強く糊化することを防ぐことができる。 By heating, it becomes a high temperature and high pressure environment, and the motility can be enhanced by changing the starch in rice from β starch to α starch. Moreover, since pH is adjusted to the range of 1.5-2.5, it can prevent that gelatinized rice gelatinizes strongly.
高温高圧処理を行う圧力容器としては、好ましくはオートクレーブが用いられる。 An autoclave is preferably used as the pressure vessel for performing the high-temperature and high-pressure treatment.
本発明では、反応終了後は米粉中の澱粉が再びβ化しないように60℃前後に温度を保持した状態で酵素糖化工程に供することが好ましい。 In this invention, after completion | finish of reaction, it is preferable to use for an enzyme saccharification process in the state which hold | maintained the temperature at about 60 degreeC so that the starch in rice flour may not be beta-ized again.
本発明では、前記の混合・攪拌工程、酸処理工程、加熱処理工程を前処理といい、この工程を通常の糖化工程の前処理として行うことで、澱粉のグルコースへの糖化効率を大幅に向上させることができる。 In the present invention, the mixing / stirring step, the acid treatment step, and the heat treatment step are referred to as pretreatment, and by performing this step as a pretreatment for a normal saccharification step, the saccharification efficiency of starch into glucose is greatly improved. Can be made.
(糖化工程)
前述のように前処理した米粉液のpHを中和し、第一次酵素反応に使用する酵素の最適pHにする。中和にはNaOH水溶液などを用いるのが好ましい。このとき温度が50〜60℃以下にならないように保つことが好ましい。
(Saccharification process)
As described above, the pH of the pretreated rice flour solution is neutralized to the optimum pH of the enzyme used for the primary enzyme reaction. For neutralization, an aqueous NaOH solution or the like is preferably used. At this time, it is preferable to keep the temperature from 50 to 60 ° C. or lower.
次いで液化酵素を添加し、大まかに混ぜた後、加熱、攪拌をしながら第一次酵素反応(澱粉の液化)を行う。 Next, a liquefied enzyme is added and mixed roughly, and then a primary enzyme reaction (starch liquefaction) is performed while heating and stirring.
澱粉の液化に用いる酵素としては、例えば、α−アミラーゼ、β−アミラーゼが挙げられるが、ここではα−アミラーゼを使用することが好ましい。 Examples of the enzyme used for liquefaction of starch include α-amylase and β-amylase. Here, α-amylase is preferably used.
次いで無菌状態で冷却した後、第二次酵素反応(澱粉の糖化)の最適pHに調整し、酵素を加えて攪拌しながら、第二次酵素反応を行う。澱粉の糖化に使用する糖化酵素としてはグルクザイム、プロテアーゼ、リパーゼなどが挙げられる。 Next, after cooling in an aseptic state, the pH is adjusted to the optimum pH for the secondary enzyme reaction (starch saccharification), and the secondary enzyme reaction is performed while adding the enzyme and stirring. Examples of the saccharifying enzyme used for saccharification of starch include gluczyme, protease, lipase and the like.
所定時間酵素反応を行い、必要により酵素を失活させて、糖化工程を終了する。 The enzyme reaction is performed for a predetermined time, the enzyme is deactivated as necessary, and the saccharification step is completed.
以下、本発明を実施例に基づき説明するが、本発明はかかる実施例によって限定されない。 EXAMPLES Hereinafter, although this invention is demonstrated based on an Example, this invention is not limited by this Example.
(実施例1)
(前処理:酸処理・加熱処理)
米粉 1000g、水 2000g(米:水=1:2)を容器に入れ、攪拌した後、含米粉液をHCl(6mol/L)にてpHを2.0に調整し、オートクレーブで121℃、20分加熱した。
Example 1
(Pretreatment: acid treatment / heat treatment)
After 1000 g of rice flour and 2000 g of water (rice: water = 1: 2) were put in a container and stirred, the pH of the rice-containing flour solution was adjusted to 2.0 with HCl (6 mol / L), and the autoclave was 121 ° C., 20 Heated for minutes.
反応終了後、米粉中澱粉が再びβ化しないように60℃前後に温度を保持した状態で酵素糖化工程に供した。 After completion of the reaction, it was subjected to the enzymatic saccharification step while maintaining the temperature at around 60 ° C. so that the starch in the rice flour was not β-ized again.
(糖化工程)
前処理後、全容量が減少していた場合はイオン交換水を補充した。
(Saccharification process)
After the pretreatment, if the total volume was reduced, ion exchange water was replenished.
前処理した米粉液のpHを5.8にNaOH水溶液(10mol/L)で調整した。 The pH of the pretreated rice flour solution was adjusted to 5.8 with an aqueous NaOH solution (10 mol / L).
このとき温度が50〜60℃以下にならないようにし、大きな固まりは事前に滅菌したスプーンでほぐしてかき混ぜ、液化酵素(アミラーゼRG−IIG)を原料米粉に対して0.05wt%添加した。 At this time, the temperature was kept at 50 to 60 ° C. or less, and a large lump was loosened and stirred with a previously sterilized spoon, and 0.05 wt% of liquefying enzyme (amylase RG-IIG) was added to the raw rice flour.
攪拌翼、フタ(ともに滅菌済み)をセットし、加熱器に乗せ、攪拌機と攪拌翼の棒を固定し熱電対をセットした後データロガーの電源を入れ、温度測定しながら、200rpmにて攪拌しながら、95〜100℃まで加熱し、60分間保持した。 Set a stirring blade and lid (both sterilized), place on a heater, fix the stirrer and stirring rod, set a thermocouple, turn on the data logger, and stir at 200 rpm while measuring the temperature. However, it heated to 95-100 degreeC and hold | maintained for 60 minutes.
攪拌翼、フタを取り外し、無菌状態で60〜65℃まで冷却し、pHをHClにて4.5に調整して、グルクザイムAF−6(アマノ)、プロテアーゼN「アマノ」、リパーゼ「ワコー」をそれぞれ原料米粉に対して0.07wt%添加した。 Remove the stirring blade and lid, cool to 60-65 ° C under aseptic conditions, adjust the pH to 4.5 with HCl, add Gluczyme AF-6 (Amano), Protease N “Amano”, Lipase “Wako” 0.07 wt% was added with respect to each raw rice flour.
再び反応容器を加熱器に乗せ、蓋をして攪拌機と攪拌翼の棒をしっかりと固定し熱電対をセットし、58℃、200rpmにて攪拌しながら、20時間保持して、糖化工程を終了させ、糖化液のグルコース濃度を測定した。 Place the reaction vessel on the heater again, close the lid and firmly fix the stirrer and stirrer blade, set the thermocouple, hold at 58 ° C and 200 rpm, hold for 20 hours, and complete the saccharification process And the glucose concentration of the saccharified solution was measured.
グルコース濃度の測定は高速液体クロマトグラフィー(HPLC LC−8010 東ソー製)により行い、回収率は(糖化液中のグルコース濃度)/(米粉澱粉中の全糖量)で表す。 The glucose concentration is measured by high performance liquid chromatography (HPLC LC-8010, manufactured by Tosoh Corporation), and the recovery rate is expressed as (glucose concentration in saccharified solution) / (total sugar amount in rice starch).
(比較例1)
実施例1において、前処理を行わず、実施例1と同じ酵素糖化工程を行った。
(Comparative Example 1)
In Example 1, the same enzymatic saccharification step as in Example 1 was performed without performing pretreatment.
(比較例2)
実施例1の条件で、塩酸によるpH調整を行わずに、加熱処理のみを行い、酵素糖化工程を行った。
(Comparative Example 2)
Under the conditions of Example 1, without performing pH adjustment with hydrochloric acid, only the heat treatment was performed to carry out the enzymatic saccharification step.
(比較例3)
実施例1の条件で、加熱時間を5分にして前処理を行い、酵素糖化工程を行った。
(Comparative Example 3)
Under the conditions of Example 1, a pretreatment was performed with a heating time of 5 minutes, and an enzymatic saccharification step was performed.
(比較例4)
実施例1の条件で、加熱温度を95℃にして前処理を行い、酵素糖化工程を行った。
(Comparative Example 4)
Under the conditions of Example 1, a pretreatment was performed at a heating temperature of 95 ° C., and an enzymatic saccharification step was performed.
以上の実験の結果を表1に示す。 The results of the above experiment are shown in Table 1.
表1より、実施例1は、比較例1、比較例2、比較例3、比較例4と比べ、糖回収量が高く、回収率が高いことが分かる。 From Table 1, it can be seen that Example 1 has a higher sugar recovery amount and higher recovery rate than Comparative Example 1, Comparative Example 2, Comparative Example 3, and Comparative Example 4.
Claims (4)
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JP5493042B1 (en) * | 2013-07-10 | 2014-05-14 | たかい食品株式会社 | Rice-derived amino acid-containing saccharified composition and method for producing the same |
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JPH11113600A (en) * | 1997-10-13 | 1999-04-27 | Shokuhin Sangyo Kankyo Hozen Gijutsu Kenkyu Kumiai | Production of water-soluble saccharide from grain hull |
JP2003250485A (en) * | 2002-02-26 | 2003-09-09 | Nagano Pref Gov Nouson Kogyo Kenkyusho | Method for producing saccharification liquid of rice |
JP2006169153A (en) * | 2004-12-15 | 2006-06-29 | Shinshu Univ | Rice syrup having antimicrobial activity |
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JPH11113600A (en) * | 1997-10-13 | 1999-04-27 | Shokuhin Sangyo Kankyo Hozen Gijutsu Kenkyu Kumiai | Production of water-soluble saccharide from grain hull |
JP2003250485A (en) * | 2002-02-26 | 2003-09-09 | Nagano Pref Gov Nouson Kogyo Kenkyusho | Method for producing saccharification liquid of rice |
JP2006169153A (en) * | 2004-12-15 | 2006-06-29 | Shinshu Univ | Rice syrup having antimicrobial activity |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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JP5493042B1 (en) * | 2013-07-10 | 2014-05-14 | たかい食品株式会社 | Rice-derived amino acid-containing saccharified composition and method for producing the same |
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