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JP5856811B2 - Hydrogen gas production method using apple - Google Patents
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JP5856811B2 - Hydrogen gas production method using apple - Google Patents

Hydrogen gas production method using apple Download PDF

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JP5856811B2
JP5856811B2 JP2011241637A JP2011241637A JP5856811B2 JP 5856811 B2 JP5856811 B2 JP 5856811B2 JP 2011241637 A JP2011241637 A JP 2011241637A JP 2011241637 A JP2011241637 A JP 2011241637A JP 5856811 B2 JP5856811 B2 JP 5856811B2
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幸嗣 川村
幸嗣 川村
恵介 和泉
恵介 和泉
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Komyo Rikagaku Kogyo KK
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本発明は、バイオマスであるリンゴ搾り粕、リンゴジュース、また、それらの混合物を原料として、非病原性細菌を用いて発酵させ、水素を得る技術に関する。   The present invention relates to a technology for obtaining hydrogen by fermenting non-pathogenic bacteria using biomass such as apple pomace, apple juice, or a mixture thereof as raw materials.

石油などの化石燃料の消費は大気中の二酸化炭素量を増加させ、地球温暖化を引き起こすとされている。これにより、カーボンニュートラル効果が得られることから、石油代替エネルギー源としてバイオマスを利用する方法が注目されている。   It is said that the consumption of fossil fuels such as oil increases the amount of carbon dioxide in the atmosphere and causes global warming. Thereby, since the carbon neutral effect is obtained, a method of using biomass as an alternative energy source for oil has attracted attention.

なかでもバイオマス由来の水素は燃料電池の反応ガス等としても利用可能であり、発電時に生成する物質が水のみであるためクリーンなエネルギー物質とされ注目されている。   In particular, hydrogen derived from biomass can be used as a reaction gas for a fuel cell, and since it is only water that is generated at the time of power generation, it has been attracting attention as a clean energy material.

バイオマスからの水素産生は、水素発酵を行う微生物により行うことが可能である。水素産生に用いられる微生物としては、クロストリジウム属菌や、エンテロバクター属菌、大腸菌属等の嫌気性細菌がある。しかしながらこれらの菌の多くはバイオセーフティレベルが2と病原性を有しており、発酵工程時の安全性に注意を要するものがほとんどである。   Hydrogen production from biomass can be performed by microorganisms that perform hydrogen fermentation. Examples of microorganisms used for hydrogen production include anaerobic bacteria such as Clostridium, Enterobacter, and Escherichia. However, most of these bacteria have pathogenicity with a biosafety level of 2, and most of them require attention to safety during the fermentation process.

また光合成細菌も水素発酵を行うことが知られているが、発酵には光エネルギーの供給が必要であり、太陽光を利用した場合は日中の晴天時にしか効率的に発酵しないという問題点がある。また、シアノバクテリアやクロレラ等も水素を産生することで知られているが、水素発生速度が遅く、実用化が困難であるとされている。   It is also known that photosynthetic bacteria also perform hydrogen fermentation, but fermentation requires a supply of light energy, and when sunlight is used, there is a problem that fermentation is efficient only on sunny days. is there. Cyanobacteria and chlorella are also known to produce hydrogen, but the hydrogen generation rate is slow and it is said that it is difficult to put into practical use.

バイオマスの種類としては様々なものがあるが、未利用バイオマスの一つとしてジュース製造時のリンゴ搾り粕(加工残渣)や、規格外や売れ残り等で農業廃棄物であるリンゴの活用も重要であるとされている。しかしながら、一部飼料粕としての利用はあるものの、バイオマスエネルギーとしての利用はほとんど報告されていない。   There are various types of biomass, but as one of the unused biomass, it is also important to use apple pomace (processed residue) during juice production and apples that are agricultural waste due to non-standard or unsold items It is said that. However, there are few reports on its use as biomass energy, although there are some uses as feed straw.

電子とイオンと機能化学シリーズ,Vol.4,「固体高分子燃料電池のすべて」,第4節,バイオマス水素製造,p234,監修者 田村英雄,担当著者 谷生重晴,2003年10月1日,初版,(株)NTS発行Electron, ion and functional chemistry series, Vol. 4, “All about polymer electrolyte fuel cells”, Section 4, Biomass hydrogen production, p234, Supervisor Hideo Tamura, Author Author Shigeharu Tanio, October 1, 2003, first edition, published by NTS Corporation

本発明は上記従来技術の不都合を解決するために創作されたものであり、その目的は病原性微生物を使用せず、種菌や活性汚泥などの発酵スターターを用いる必要もなく、バイオマスであるリンゴからバイオ水素の生産を行うことができる方法を提供するものである。   The present invention was created in order to solve the above-mentioned disadvantages of the prior art, and its purpose is not to use pathogenic microorganisms, it is not necessary to use fermentation starters such as inoculum or activated sludge, and from biomass apples. A method capable of producing biohydrogen is provided.

上記課題を解決するために、本発明は、リンゴ果実を搾ったときの搾り粕とリンゴ汁のうち、前記搾り粕又は前記リンゴ汁のいずれか一方又は両方を含有し、pHが6.5以上8未満に調整た培養液を作製し、前記リンゴ果実に付着する病原性の無いロドスポリジウム トルロイド(Rhodosporidium toruloides)によって前記培養液を発酵させて水素ガスを放出させる水素ガス製造方法である
た、本発明は、前記培養液を30℃以上の温度に維持して発酵させる水素ガス製造方法である。
In order to solve the above-mentioned problems, the present invention contains either or both of the squeezed straw and the apple juice out of the squeezed straw and the apple juice when the apple fruit is squeezed, and the pH is 6.5 or more. 8 to prepare a culture adjusted to less than is the hydrogen gas producing method for releasing hydrogen gas by fermenting the broth with no pathogenic Rhodosporidium Toruroido (Rhodosporidium toruloides) adhering to the apple fruit .
Also, the present invention is a hydrogen gas producing method of Ru fermented by maintaining the culture in 30 ° C. or higher.

売れ残りのリンゴ果実や、リンゴ果実の搾り粕等のリンゴの農業廃棄物から水素ガスが得られる。
リンゴ果実の常在菌であるRhodosporidium属の酵母を利用して発酵するので、活性汚泥や種菌など外部から細菌を投与する工程が必要ない。
Rhodosporidium属の至適であるpH7以上又はpH7付近で発酵させると水素ガス集率が高い。
Hydrogen gas is obtained from unsold apple fruits and apple agricultural waste such as apple fruit squeezed straw.
Since fermentation is carried out using yeast belonging to the genus Rhodosporidium, which is a resident bacteria of apple fruits, there is no need for a step of administering bacteria from the outside, such as activated sludge and inoculum.
When fermented at pH 7 or higher, or near pH 7, which is optimal for the genus Rhodosporidium, hydrogen gas collection is high.

本発明の水素ガス製造方法を実施できる水素収集装置の一例An example of a hydrogen collecting apparatus capable of carrying out the hydrogen gas production method of the present invention リンゴ培養液の種類による培養日数と気体発生量の積算値との関係を示すグラフA graph showing the relationship between the number of days of cultivation and the integrated value of gas generation by the type of apple broth 光と気体発生量の積算値との関係を示すグラフGraph showing the relationship between the integrated value of light and gas generation amount pHと気体発生量の積算値との関係を示すグラフGraph showing the relationship between pH and integrated value of gas generation 滅菌処理と発酵との関係を示すグラフGraph showing the relationship between sterilization and fermentation ブドウ、桃の培養日数と気体発生量の積算値との関係を示すグラフGraph showing the relationship between the number of days of cultivation of grapes and peaches and the integrated value of gas generation サン津軽(長野産)のpHと気体発生量の関係を示すグラフGraph showing the relationship between the pH of San Tsugaru (from Nagano) and the amount of gas generated 高pHでの水素ガス発生状況を示すグラフGraph showing hydrogen gas generation status at high pH 低pHで水素ガスが発生する場合の例を示すグラフGraph showing an example when hydrogen gas is generated at low pH

天然のリンゴには常在菌として、酵母であるRhodosporidium toruloidesがリンゴ果実に付着しており、常在菌を利用するため、バイオマス材料であるリンゴには消毒や加熱・殺菌・滅菌処理を施さず、その天然リンゴの常在菌を利用して水素発酵を行わせる。   Natural apples have yeast, Rhodosporidium toruloides, which adheres to the fruit of the apple. Since apples are biomass, they are not subjected to disinfection, heating, sterilization, or sterilization. Then, hydrogen fermentation is performed using the resident bacteria of the natural apple.

リンゴ搾り粕およびリンゴジュース、もしくはそれらの混合物から成る培養液は通常pHが4〜5程度の範囲であるが、このpHを7付近に調整することで、Rhodosporidium属の酵母が水素発酵できるような環境とし、発酵に供する。
本発明では、リンゴ搾り粕には、リンゴの皮の部分が含まれており、リンゴジュース(リンゴ搾り汁)は、リンゴ果実の皮を含む粉砕物を搾って取得している。
The culture solution consisting of apple pomace and apple juice, or a mixture thereof, usually has a pH in the range of about 4-5. By adjusting this pH to around 7, it is possible for yeasts of the genus Rhodosporidium to undergo hydrogen fermentation. Use as an environment for fermentation.
In the present invention, the apple pomace contains a portion of the apple skin, and the apple juice (apple juice) is obtained by squeezing the pulverized material containing the apple fruit skin.

リンゴ搾り粕およびリンゴジュース、もしくはそれらの混合物を、水とともに容器に入れる(以下、発酵溶液)。このリンゴ搾り粕およびリンゴジュース、もしくはそれらの混合物中には常在菌であるRhodosporidium toruloidesが含まれており、種菌や活性汚泥等の発酵スターターを添加する必要性がない。発酵溶液のpHは、未調整の場合は4〜5程度である。   Apple pomace and apple juice, or a mixture thereof are put in a container together with water (hereinafter referred to as fermentation solution). The apple pomace and apple juice, or a mixture thereof contains Rhodosporidium toruloides, which are resident bacteria, and there is no need to add a fermentation starter such as an inoculum or activated sludge. The pH of the fermentation solution is about 4 to 5 when not adjusted.

この条件では水素発酵が行われないため、pHをRhodosporidium toruloidesが水素発酵を行う条件であるpH7付近に調整して30℃程度の温度を維持しながら、24〜200時間程度放置すると、この発酵溶液から気体が発生する。発生した気体の中には水素と二酸化炭素とが含まれており、水素ガス(H2)濃度は30〜80%程度である。この水素濃度は、燃料電池を駆動させるのに十分な濃度であり、この発酵溶液から得られる気体を利用した発電、すなわちバイオマスエネルギーの利用が可能となる。発酵を行う際には、水素収集速度の観点からは、発酵液の温度は10℃以上40℃以下の範囲に維持することが望ましく、20℃以上35℃以下の範囲に維持することが、一層望ましい。 Since hydrogen fermentation is not performed under these conditions, the fermentation solution is left to stand for about 24 to 200 hours while maintaining a temperature of about 30 ° C. while adjusting the pH to around pH 7 where Rhodosporidium toruloides performs hydrogen fermentation. Gas is generated from The generated gas contains hydrogen and carbon dioxide, and the hydrogen gas (H 2 ) concentration is about 30 to 80%. This hydrogen concentration is a concentration sufficient to drive the fuel cell, and power generation using the gas obtained from the fermentation solution, that is, utilization of biomass energy becomes possible. When performing the fermentation, from the viewpoint of the hydrogen collection rate, it is desirable to maintain the temperature of the fermentation broth in the range of 10 ° C. or higher and 40 ° C. or lower. desirable.

また、発酵を行うために培養液の濃度は所望の値に調整できるが、1gの搾り粕を330mLの水に分散・溶解した培養液(0.3%)から、リンゴジュースを希釈しない培養液(100%)まで、任意の濃度の培養液を発酵させて水素産生を行うことが可能である。
但し、効率を考えた場合、10gの搾り粕を300mLの水に溶解した濃度(3%)以上の濃度の培養液が望ましい。
In addition, the concentration of the culture solution can be adjusted to a desired value for fermentation, but the culture solution in which apple juice is not diluted from the culture solution (0.3%) in which 1 g of squeezed rice cake is dispersed and dissolved in 330 mL of water It is possible to produce hydrogen by fermenting a culture solution of any concentration up to (100%).
However, in view of efficiency, a culture solution having a concentration of 3% or more obtained by dissolving 10 g of pomace in 300 mL of water is desirable.

水素貯蔵には、例えば、図1に記載した水素収集装置10を用いることができる。
この水素収集装置10は、発酵槽12と捕集槽22を有しており、発酵槽12には、天井となる部分は蓋13によって閉塞されている。
蓋13には、捕集配管32の一端が接続され、捕集配管32の他端は、捕集槽22の内部に導入され、他端の先端の開口18が捕集槽22の底面の略中心の上方に配置されている。
発酵槽12内に、pH調整された培養液15が配置され、発酵して水素が発生すると、捕集配管32を通って、開口18から捕集槽22内に放出される。
For hydrogen storage, for example, the hydrogen collection device 10 described in FIG. 1 can be used.
This hydrogen collection device 10 has a fermenter 12 and a collection tank 22, and the fermenter 12 is closed with a lid 13 at a ceiling.
One end of a collection pipe 32 is connected to the lid 13, the other end of the collection pipe 32 is introduced into the collection tank 22, and the opening 18 at the tip of the other end is an abbreviation of the bottom surface of the collection tank 22. It is arranged above the center.
When the pH-adjusted culture solution 15 is disposed in the fermenter 12 and fermented to generate hydrogen, the fermenter 12 is discharged through the collection pipe 32 into the collection tank 22 through the collection pipe 32.

開口18の上方には、下端が捕集槽22の上端よりも下方に配置された貯蔵塔23が配置されている。貯蔵塔23の下端は開放され、容器状にされており、予め捕集槽22に捕集水16を注入し、貯蔵塔23の下端を、注入した捕集水16の水面化の位置に浸漬させておくと、開口18から放出された水素は、捕集水16内を泡となって上昇し、水上置換によって、貯蔵塔23内に捕集される。水素が捕集されると、その体積に応じて生じた浮力によって、貯蔵塔23が上昇する。   Above the opening 18, a storage tower 23 having a lower end disposed below the upper end of the collection tank 22 is disposed. The lower end of the storage tower 23 is opened and formed into a container shape, and the collected water 16 is poured into the collection tank 22 in advance, and the lower end of the storage tower 23 is immersed in the water leveling position of the collected collected water 16. If this is done, the hydrogen released from the opening 18 rises as bubbles in the collected water 16 and is collected in the storage tower 23 by water replacement. When hydrogen is collected, the storage tower 23 rises due to the buoyancy generated according to the volume.

貯蔵塔23の上方に向けられた底面には、サンプル管34の一端が接続され、貯蔵塔23に貯蔵された水素は、サンプル管34内を流れて燃料電池26の内部に導入されるようになっている。
サンプル管34の途中には、コック33が設けられており、開口18から放出された水素を貯蔵塔23の内部に貯蔵するときには、コック33を閉じておき、貯蔵された水素で燃料電池26を動作させるときには、コック33を開け、貯蔵塔23が重力で下降するときの圧力が貯蔵塔23内部の水素に印加され、その圧力で水素が燃料電池26に導入される。
One end of the sample tube 34 is connected to the bottom surface directed upward of the storage tower 23 so that the hydrogen stored in the storage tower 23 flows through the sample tube 34 and is introduced into the fuel cell 26. It has become.
A cock 33 is provided in the middle of the sample tube 34. When the hydrogen released from the opening 18 is stored in the storage tower 23, the cock 33 is closed and the fuel cell 26 is stored with the stored hydrogen. When operating, the cock 33 is opened, and the pressure at which the storage tower 23 descends due to gravity is applied to the hydrogen inside the storage tower 23, and hydrogen is introduced into the fuel cell 26 at that pressure.

燃料電池26の燃料極36と酸素極37とには、ファンモータ27が接続されており、燃料電池26に水素が供給されて発電され、ファンモータ27に電圧が印加されると、ファンモータ27に接続されたプロペラが回転するようになっている。   A fan motor 27 is connected to the fuel electrode 36 and the oxygen electrode 37 of the fuel cell 26. When the hydrogen is supplied to the fuel cell 26 to generate electric power and a voltage is applied to the fan motor 27, the fan motor 27. The propeller connected to is designed to rotate.

従って、プロペラの回転により、発酵槽12内での発酵による水素の発生から、貯蔵塔23による捕集を経て燃料電池26にて発電するまでの結果を視認することができるので、水素収集装置10は、リンゴの廃棄物を再利用するための教材としても用いることができるし、水素収集装置10を大型化すれば、廃棄物リサイクルによるエネルギーの多様化に寄与することもできる。   Therefore, since the rotation of the propeller allows visual recognition of the results from the generation of hydrogen by fermentation in the fermenter 12 through the collection by the storage tower 23 to the generation of power by the fuel cell 26, the hydrogen collection device 10 Can be used as teaching materials for reusing apple waste, and if the hydrogen collecting device 10 is enlarged, it can also contribute to diversification of energy by waste recycling.

リンゴ1個を水で軽く洗ってから4つに包丁で切断し、食品用のすりおろし器ですり下ろした。すり下ろしたリンゴは300mL容のガラスビーカー内にてプラスチック製ネット(台所用水切りネット)を用いて搾りとり、この搾り粕を試験に供した。なお、すり下ろしの作業は手の常在菌からのコンタミネーションを防ぐ目的で、ゴム手袋をはめて実施した。   One apple was lightly washed with water, then cut into four with a knife, and then grated with a food grinder. The apple that was grated was squeezed out in a 300 mL glass beaker using a plastic net (draining net for kitchens), and the pomace was subjected to the test. In addition, the glove work was carried out with rubber gloves in order to prevent contamination from resident bacteria.

調製した搾り粕10gを容積300mLのガラス製三角フラスコ内に入れて脱イオン水を330mL投入した。これにKH2PO4を0.28g、K2HPO4を0.24g、HNaCO3を0.49g(割合はKH2PO40.85g、K2HPO40.75g、HNaCO31.5g/1Lとなる)投入し、pHを7付近に調製された培養液を作製した(上記試薬を投入するだけで、pH7付近となる)。また、培養前後の液体のpHはpHメーター((株)堀場製作所「B−212」)にて測定した。 10 g of the prepared pomace was placed in a 300 mL glass Erlenmeyer flask and 330 mL of deionized water was added. To this, 0.28 g of KH 2 PO 4 , 0.24 g of K 2 HPO 4 , 0.49 g of HNaCO 3 (ratio is 0.85 g of KH 2 PO 4 , 0.75 g of K 2 HPO 4 , 1.5 g of HNaCO 3 To 1 L), and a culture solution having a pH adjusted to around 7 was prepared (by just adding the reagent, the pH was around 7). The pH of the liquid before and after the culture was measured with a pH meter (Horiba, Ltd. “B-212”).

この溶液の入った三角フラスコにテフロンチューブ(テフロンは登録商標)を接続したシリコン栓を差し込み、三角フラスコを照明によって30℃付近(実測温度31℃)の温度に昇温させ、調整した恒温槽(水槽を利用、水は使用せず)内にフラスコを置き、培養液中の微生物を培養し、発酵させた。またテフロンチューブ(テフロンは登録商標)の先端を水の入れた水槽内に沈め、チューブ先端から発生した気体をガラス製メスシリンダー内に水上置換することで、発生気体の捕集を行った。   A conical flask containing a Teflon tube (Teflon is a registered trademark) was inserted into the Erlenmeyer flask containing this solution, and the Erlenmeyer flask was heated to a temperature of around 30 ° C. (measured temperature: 31 ° C.) by illumination, and an adjusted thermostat ( The flask was placed in a water tank (without using water), and the microorganisms in the culture were cultured and fermented. The tip of a Teflon tube (Teflon is a registered trademark) was submerged in a water tank containing water, and the gas generated from the tip of the tube was replaced with water in a glass graduated cylinder to collect the generated gas.

培養日数と気体発生量の積算値との関係を図2に示す。サンフジのリンゴを使用した培養液と、フジのリンゴを使用した培養液とを、滅菌せずに別々に発酵させて発生気体を捕集した。
培養液からは1〜2日後から気体の発生が確認できた。
The relationship between the number of days of culture and the integrated value of gas generation is shown in FIG. The culture solution using the Sanfuji apple and the culture solution using the Fuji apple were separately fermented without sterilization to collect the generated gas.
From the culture solution, generation of gas could be confirmed after 1-2 days.

メスシリンダー内に捕集した気体は、プラスチック製シリンジにて回収し、その後ガラスシリンジで空気によって100倍希釈してから、水素濃度を検知管法(水素検知管 U型 光明理化学工業(株)社製)にて水素濃度を測定した。測定した発生気体中の水素濃度を希釈前の濃度に換算すると、50%であった。   The gas collected in the graduated cylinder is collected with a plastic syringe and then diluted 100-fold with air with a glass syringe, and then the hydrogen concentration is detected by the detector tube method (hydrogen detector tube U-type Komyo Chemical Co., Ltd.) The hydrogen concentration was measured. The measured hydrogen concentration in the generated gas was 50% when converted to the concentration before dilution.

さらに、シリンジで回収した発生気体は、10mLを燃料電池に投入し、接続したファンモーターが駆動するかどうかについても確認した。駆動時間は、サンフジの場合は6分2秒、フジの場合は7分11秒であった。
発生した気体を燃料電池に投入することで、ファンの駆動から発電が確認できた。これより、バイオマスであるリンゴから電気エネルギーを取り出せることが確認できた。
なお、燃料電池の水素投入口は2ヵ所あるが、投入に使用しない側の投入口には、投入した水素が燃料電池から拡散しないように、シリンジを別途接続しておいた。
Furthermore, 10 mL of the generated gas recovered by the syringe was put into the fuel cell, and it was confirmed whether or not the connected fan motor was driven. The driving time was 6 minutes 2 seconds for Sanfuji and 7 minutes 11 seconds for Fuji.
By introducing the generated gas into the fuel cell, power generation was confirmed from the drive of the fan. From this, it was confirmed that electric energy could be extracted from the apple which is biomass.
In addition, although there are two hydrogen inlets of the fuel cell, a syringe was separately connected to the inlet that is not used for charging so that the charged hydrogen would not diffuse from the fuel cell.

一方、比較対照として滅菌処理(高圧蒸気滅菌処理)したリンゴからも培養液を作成し、同じ条件で発酵を試みたが、気体は発生しなかった。これより、リンゴ中に含まれている微生物が水素発酵し、水素が産生されていることが確認できた。
また、リンゴバイオマスに加熱等の消毒・殺菌・滅菌処理等をおこなうと、常在菌が死滅するため、発酵が行われず水素産生が見られないことがわかった。
On the other hand, a culture broth was also prepared from apples sterilized (high-pressure steam sterilization) as a comparative control and fermentation was attempted under the same conditions, but no gas was generated. From this, it was confirmed that the microorganisms contained in the apple fermented with hydrogen and produced hydrogen.
It was also found that when apple biomass was subjected to sterilization, sterilization, sterilization, etc., such as heating, resident bacteria were killed, so that fermentation was not performed and hydrogen production was not observed.

<光試験>
フジのリンゴジュースで30%の濃度のものを用い、pHを6.5に調整して培養液を作製した。この培養液は、培養液を配置した発酵容器を遮光して発酵させたときと、光照射しながら発酵させたときとで、それぞれ気体発生量を測定した。培養液は30℃に維持して発酵させた。
<Optical test>
Using a Fuji apple juice having a concentration of 30%, the pH was adjusted to 6.5 to prepare a culture solution. The amount of gas generated in this culture solution was measured when the fermentation vessel in which the culture solution was arranged was shielded from light and when fermented while being irradiated with light. The culture solution was maintained at 30 ° C. for fermentation.

培養日数と気体発生量の積算値との関係を図3に示す。光照射の有無にかかわらず気体は発生している。この結果から、水素産生が光合成細菌によるものではないことがわかる。発生気体の水素濃度は、光照射したときには30%、光照射しなかったときには25%であった。
発生気体をシリンジで10mL抽出し、燃料電池に注入して動作させると、ファンモーターの回転時間は、光照射したときの発生気体の時と光非照射のときとで、10分以上であった。
The relationship between the number of days of culture and the integrated value of gas generation is shown in FIG. Gas is generated regardless of the presence or absence of light irradiation. This result indicates that hydrogen production is not caused by photosynthetic bacteria. The hydrogen concentration of the generated gas was 30% when irradiated with light and 25% when not irradiated with light.
When 10 mL of the generated gas was extracted with a syringe and injected into the fuel cell and operated, the rotation time of the fan motor was 10 minutes or more when the generated gas was irradiated with light and when the light was not irradiated. .

<pH試験(1)>
次に、フジのリンゴの搾り粕10gを脱イオン水330mLに投入し、pHを4.9、7.0、7.2にそれぞれ調整した培養液を作製し、各培養液を30℃で発酵させた。pH4.9はpH未調整である。
<PH test (1)>
Next, 10 g of Fuji squeezed straw was put into 330 mL of deionized water to prepare culture solutions adjusted to pH 4.9, 7.0, and 7.2, respectively, and each culture solution was fermented at 30 ° C. I let you. pH 4.9 is not adjusted for pH.

初発(発酵開始時)のpH値と気体発生量の積算値との関係を図4に示す。pH未調整の4.9では気体発生が確認されなかったが、pH7付近(pH調整)では気体が発生し、水素濃度はpH7.0の培養液では40%、pH7.2の培養液では45%であった。これより、リンゴバイオマスはpH未調整の場合は水素産生がみられないが、pHを中性域に調整することにより、水素を産生させることが可能であることがわかった。
得られた発生気体をシリンジで5mL抽出し、燃料電池に注入して動作させると、ファンモーターは10分以上回転した。
FIG. 4 shows the relationship between the initial pH value (at the start of fermentation) and the integrated value of the amount of gas generated. Gas generation was not confirmed at pH 4.9, but gas was generated around pH 7 (pH adjustment), and the hydrogen concentration was 40% in the culture solution at pH 7.0, and 45 in the culture solution at pH 7.2. %Met. This shows that apple biomass does not produce hydrogen when pH is not adjusted, but can produce hydrogen by adjusting the pH to a neutral range.
When 5 mL of the obtained generated gas was extracted with a syringe and injected into the fuel cell to operate, the fan motor rotated for 10 minutes or more.

<発酵微生物の同定>
気体発生中の発酵溶液(発酵後48時間)を一部採取し、これをリンゴ寒天培地(リンゴ果汁をpH6.7に調整してから滅菌して調整した寒天平板培地。寒天濃度は1.5%)に塗沫して、発酵溶液中の微生物の釣菌を試みた。その結果、塗沫72時間後には寒天培地上に多数の赤色コロニーおよび少量の白色コロニーが確認された。
<Identification of fermentation microorganisms>
A portion of a gas-producing fermentation solution (48 hours after fermentation) was collected, and this was agar-agar medium (agar plate medium prepared by sterilization after adjusting apple juice to pH 6.7. Agar concentration was 1.5). %)) And tried to catch microorganisms in the fermentation solution. As a result, a large number of red colonies and a small amount of white colonies were confirmed on the agar medium 72 hours after smearing.

発酵溶液中の赤色菌数は5×104個/mL程度、白色菌数は2×102個/mL程度であった。生えてきたコロニーの大半は赤色菌であったことから、水素産生に寄与している微生物は赤色菌と考え、この赤色菌の同定を試みた。 The number of red bacteria in the fermentation solution was about 5 × 10 4 / mL, and the number of white bacteria was about 2 × 10 2 / mL. Since most of the colonies that grew were red fungi, the microorganisms contributing to hydrogen production were considered red fungi, and an attempt was made to identify these red fungi.

赤色菌のDNAを抽出し、PCR法によりLarge subunit rRNAのD2領域のDNAを増幅した。増幅したDNAについてABI PRISM 310 Genetic Analyzer(Life technologies corporation)を用いて塩基配列を解析した。得られた配列を国際塩基配列データベース(DDBJ/EMBL/Genbank)に登録されている配列およびMicroseq ID Analysis Software Version 2.0(Life technologies corporation)のデータベースと相同性検索を行い、近縁種との系統樹を近隣結合法(NJ法)により作成した。   The DNA of S. cerevisiae was extracted and the DNA of the large subunit rRNA D2 region was amplified by PCR. The base sequence of the amplified DNA was analyzed using ABI PRISM 310 Genetic Analyzer (Life technologies corporation). Homology search of the obtained sequence with sequences registered in the international nucleotide sequence database (DDBJ / EMBL / Genbank) and the database of Microseq ID Analysis Software Version 2.0 (Life technologies corporation), and a phylogenetic tree with related species Was created by the neighbor join method (NJ method).

その結果、Rhodosporidium toruloidesともっとも相同性が高く、その相同性は99.44%であった。この結果から、発酵溶液中の主要微生物である赤色菌はRhodosporidium toruloidesであることがわかった。Rhodosporidium toruloidesは植物、土壌、空気、動物、海水等から分離され、その不完全時代はRhodotorula rubescensである。   As a result, the homology was highest with Rhodosporidium toruloides, and the homology was 99.44%. From this result, it was found that the red fungus, which is the main microorganism in the fermentation solution, is Rhodosporidium toruloides. Rhodosporidium toruloides is isolated from plants, soil, air, animals, seawater, etc., and its incomplete era is Rhodotorula rubescens.

滅菌リンゴの搾り汁の30%、pH6.7の培養液に、Rhodosporidium toruloidesのコロニーを3白金耳投入し、30℃で培養したところ、図5に示すとおり、気体が発生し水素も確認された。水素ガス濃度は30%であった。(図5のグラフでは、発酵開始3日目から8日目の間は、データを取得していない。)
発生気体をシリンジで5mL抽出し、燃料電池に注入して動作させると、ファンモーターの回転時間は2分30秒であった。
同じ培養液にコロニーを投入せずに30℃で培養した比較対象では、水素は発生しなかった。
Three platinum loops of Rhodosporidium toruloides colonies were added to a culture solution of 30% of sterilized apple juice and pH 6.7, and cultured at 30 ° C. As shown in FIG. 5, gas was generated and hydrogen was also confirmed. . The hydrogen gas concentration was 30%. (In the graph of FIG. 5, data is not acquired during the 3rd to 8th days from the start of fermentation.)
When 5 mL of the generated gas was extracted with a syringe and injected into the fuel cell and operated, the rotation time of the fan motor was 2 minutes 30 seconds.
Hydrogen was not generated in comparison subjects cultured at 30 ° C. without introducing colonies into the same culture solution.

以上の結果により、リンゴバイオマス由来の水素発生にはRhodosporidium toruloidesが寄与していることが確認できた。
Rhodosporidium toruloidesはバイオセーフティレベルが1であり病原性がないとされている。これから、本微生物を用いたバイオ水素の産生は、発酵・水素製造・後処理作業時において、安全性が高いと言える。
From the above results, it was confirmed that Rhodosporidium toruloides contributed to hydrogen generation from apple biomass.
Rhodosporidium toruloides has a biosafety level of 1 and is not pathogenic. From this, it can be said that the production of biohydrogen using this microorganism is highly safe during fermentation, hydrogen production and post-treatment operations.

<発生ガスの解析>
発生したガスを検知管法にて解析をおこなった。結果の例を下記表1に示す。検知管はいずれも光明理化学工業株式会社製である。
<Analysis of evolved gas>
The generated gas was analyzed by the detector tube method. An example of the results is shown in Table 1 below. All the detector tubes are manufactured by Komyo Chemical Co., Ltd.

Figure 0005856811
Figure 0005856811

表1の結果は、複数回測定したときの測定結果例を示している。測定のタイミングや使用したリンゴの試験ロットは同一ではない。
ただし、水素、二酸化炭素が主要な発生ガスであり、硫化水素、酢酸、エチレン、アルコール類、アンモニアはほとんど含まれていないことがわかる。
The results in Table 1 show examples of measurement results when measured multiple times. The timing of measurement and the test lot of apples used are not the same.
However, it is understood that hydrogen and carbon dioxide are the main generated gases, and hydrogen sulfide, acetic acid, ethylene, alcohols, and ammonia are hardly contained.

発生ガス中には燃料電池の触媒被毒原因物質である硫化水素が含まれていないことから、燃料電池への投入ガスとしては利点がある。アンモニア等の有害ガスも含まれていないことから、安全上も利点が高い。   Since the generated gas does not contain hydrogen sulfide, which is a catalyst poisoning substance of the fuel cell, there is an advantage as an input gas to the fuel cell. Since no harmful gas such as ammonia is contained, there is a high safety advantage.

<発酵前後の発酵溶液中の糖質・有機酸・エタノール濃度>
発酵前後の発酵溶液中の糖質・有機酸濃度を測定した。
測定結果は、下記表2に示す。
<Concentration of sugar, organic acid and ethanol in fermentation solution before and after fermentation>
The sugar and organic acid concentrations in the fermentation solution before and after fermentation were measured.
The measurement results are shown in Table 2 below.

Figure 0005856811
Figure 0005856811

本試験時には40%の水素を含む気体が65mL産生した。
各成分は酵素法(ロシュ社 F−kit)にて測定した。その結果、ショ糖、麦芽糖、グルコース、フルクトースの糖質およびリンゴ酸は発酵前には比較的高濃度で含まれていたが、発酵後には著しく減少していることが確認できた。一方、エタノール、L/D−乳酸、酢酸は発酵前にはほとんど含まれていなかったが、発酵後には著しく増加していることが確認できた。この結果から、発酵溶液中では糖質およびリンゴ酸を栄養源として微生物が利用し、それにより水素発酵、エタノール発酵、乳酸発酵、酢酸発酵が行われていることがわかる。
pHは、発酵前は7.1であったが、発酵後は5.8にまで低下していた。これは、発酵により酢酸、乳酸などの有機酸が生成したことによることがわかる。
At the time of this test, 65 mL of gas containing 40% hydrogen was produced.
Each component was measured by an enzyme method (Roche F-kit). As a result, it was confirmed that sucrose, maltose, glucose, fructose saccharides and malic acid were contained at a relatively high concentration before fermentation, but significantly decreased after fermentation. On the other hand, ethanol, L / D-lactic acid, and acetic acid were hardly contained before fermentation, but it was confirmed that they were remarkably increased after fermentation. From this result, it can be seen that microorganisms use carbohydrates and malic acid as nutrient sources in the fermentation solution, and thus hydrogen fermentation, ethanol fermentation, lactic acid fermentation, and acetic acid fermentation are performed.
The pH was 7.1 before fermentation, but decreased to 5.8 after fermentation. This shows that organic acids, such as acetic acid and lactic acid, produced | generated by fermentation.

<水素産生速度>
本発明における水素産生速度は、試験条件にも左右されるが、事例としては22mmol/L.h程度の結果が得られている。文献によると、非病原性である水素産生微生物の産生速度は、Oscillatoria sp.(ヨレモ)で0.4、Anabaena cylindrical(シアノバクテリア)で1.2、Rhdopseudomonas capslata(光合成細菌)で5.3mmol/L.hであった。これから、本発明による水素産生速度は非病原性微生物としては優れていることがわかる。また、病原性微生物においては、Clostridium beijerinkii(偏性嫌気性菌)で17、Enterobacter aerogenesで36mmol/L.hとなっており、本発明より早いケースはあるものの、本発明の方法は非病原性でありながらこれらの病原性微生物による産生速度とくらべても十分に比較可能なものであることがわかる。
<Hydrogen production rate>
The hydrogen production rate in the present invention depends on the test conditions, but as an example, it is 22 mmol / L. The result of about h is obtained. According to the literature, the production rate of non-pathogenic hydrogen-producing microorganisms is 0.4 for Oscillatoria sp. (Joremo), 1.2 for Anabaena cylindrical (Cyanobacteria), 5.3 mmol / Rhdopseudomonas capslata (Photosynthetic bacteria). L. h. This shows that the hydrogen production rate according to the present invention is excellent as a non-pathogenic microorganism. Among pathogenic microorganisms, Clostridium beijerinkii (obligate anaerobe) is 17 and Enterobacter aerogenes is 36 mmol / L. Although h, there are cases earlier than the present invention, it can be seen that the method of the present invention is sufficiently non-pathogenic but comparable to the production rate of these pathogenic microorganisms.

<比較例>
天然リンゴに替え、ブドウと桃についても、果実に付着している常在細菌によって発酵させた。その結果を図6に示す。
桃、ブドウについて気体が発生したが、桃の発生気体は75%の水素ガス濃度が検出されていたが、ブドウの発生気体には水素は検出されなかった。
ブドウについては、巨峰についての搾り粕40gを脱イオン水330mLに投入し、桃については白桃の搾り粕20gを脱イオン水330mLに投入し、pHを8.0にして培養液をそれぞれ作成し、30℃で発酵させた。
<Comparative example>
Instead of natural apples, grapes and peaches were also fermented by resident bacteria attached to the fruits. The result is shown in FIG.
Although gas was generated for peaches and grapes, 75% hydrogen gas concentration was detected in the peach gas, but no hydrogen was detected in the grape gas.
For grapes, 40 g of squeezed koji for Kyoho is added to 330 mL of deionized water, and for peaches, 20 g of squeezed koji of white peach is added to 330 mL of deionized water, and pH is set to 8.0 to prepare a culture solution Fermented at 30 ° C.

桃、ブドウの発生気体をシリンジで5mL抽出して燃料電池に注入して動作させたところ、ファンモーターの回転時間は桃の発生気体では10分以上であり、ブドウの発生気体では、回転しなかった。
なお、水素発生を確認した時点では、発酵に寄与した常在細菌の特定はできていない。
When 5 mL of peach and grape gas was extracted with a syringe and injected into the fuel cell, the operation time of the fan motor was 10 minutes or more with peach gas, and it did not rotate with grape gas. It was.
In addition, at the time of confirming hydrogen generation, the resident bacteria that contributed to fermentation have not been identified.

<pH試験(2)>
リンゴの産地と種類を変え、水素発生の試験を行った。
試験結果を下記表3に示す。
<PH test (2)>
The production and type of apples were changed, and hydrogen generation was tested.
The test results are shown in Table 3 below.

Figure 0005856811
Figure 0005856811

上記表3から、発酵開始時のpHの値は、6pH以上8pH未満であれば、水素発生が可能なことが分かる。
次に、長野県産の「サン津軽」のリンゴの搾り粕10gを300mLの水に溶解し、濃度(3%)で、pH値が4.9、5.8、7.0、7.9の四種類の培養液を作成し、発酵させた。培養温度は30℃にした。
From Table 3 above, it can be seen that hydrogen generation is possible when the pH value at the start of fermentation is 6 pH or more and less than 8 pH.
Next, 10 g of apples of “Sun Tsugaru” produced in Nagano Prefecture are dissolved in 300 mL of water, and the pH value is 4.9, 5.8, 7.0, 7.9 at a concentration (3%). Were prepared and fermented. The culture temperature was 30 ° C.

各培養液についての培養日数と気体発生量積算値の関係を、図7に示す。図中の数値は、各培養液についての、発生ガス中の水素ガス濃度と、サンプル気体によるモータ回転時間とを示す値である(シリンジで5mL注入)。これらの試験結果から、pH5以上pH8未満の培養液について、水素発生が確認されている。   FIG. 7 shows the relationship between the number of culture days and the gas generation amount integrated value for each culture solution. The numerical values in the figure are values indicating the hydrogen gas concentration in the generated gas and the motor rotation time by the sample gas for each culture solution (injection of 5 mL with a syringe). From these test results, hydrogen generation was confirmed in the culture solution having a pH of 5 or more and less than pH 8.

次に、長野産に替え、会津産「サン津軽」のリンゴで、長野産と同じ濃度、体積で異なるpH値5.8、7.0、8.0、9.1の培養液を作成し、長野産と同じ条件で発酵させた。
その培養液の培養日数と気体発生量の積算値との関係を図8に示す。シリンジへの注入量は5mLである。pH7.0の培養液は水素ガス発生が確認できたが、pH5.8と、pH8〜9の培養液については水素ガス発生は確認できなかった。
Next, instead of Nagano products, Aizu “Sun Tsugaru” apples with different pH values of 5.8, 7.0, 8.0, 9.1 in the same concentration and volume as Nagano products were prepared. Fermented under the same conditions as in Nagano.
FIG. 8 shows the relationship between the number of days of culture and the integrated value of the amount of gas generated. The injection amount into the syringe is 5 mL. Hydrogen gas generation was confirmed in the culture solution of pH 7.0, but hydrogen gas generation was not confirmed in the culture solutions of pH 5.8 and pH 8-9.

次に、低pH値でも、大量の水素ガスが発生する例を示す。
図9は、青森産のリンゴ「フジ」の搾り汁30%、pH6.5の培養液を光を照射して発酵させたときと、遮光して発酵させたときの、培養日数と気体発生量の積算値との関係を示すグラフである。光照射したときの水素ガス濃度は30%、遮光したときの水素ガス濃度は25%であった。シリンジで10mL注入したときのモータ駆動時間は、それぞれ10分以上であった。
このグラフの例から分かるように、pH6.5のときでも、水素ガスが大量発生する場合はある。
以上のことにより、水素ガス発生には、培養液のpH値は6以上8未満、発生量を考慮すると、6.5以上8.0未満が望ましい。
Next, an example in which a large amount of hydrogen gas is generated even at a low pH value will be described.
Fig. 9 shows the number of days of cultivation and the amount of gas generated when fermenting the fermented juice of 30% of Aomori apple "Fuji", pH 6.5, and fermenting it with light. It is a graph which shows the relationship with the integrated value of. The hydrogen gas concentration when irradiated with light was 30%, and the hydrogen gas concentration when shielded from light was 25%. The motor driving time when 10 mL was injected with a syringe was 10 minutes or more, respectively.
As can be seen from the example of this graph, even when the pH is 6.5, a large amount of hydrogen gas may be generated.
From the above, for hydrogen gas generation, the pH value of the culture solution is preferably 6 or more and less than 8, and considering the generation amount, it is preferably 6.5 or more and less than 8.0.

10……水素収集装置
12……発酵槽
23……貯蔵塔
26……燃料電池
27……ファンモータ
DESCRIPTION OF SYMBOLS 10 ... Hydrogen collection device 12 ... Fermenter 23 ... Storage tower 26 ... Fuel cell 27 ... Fan motor

Claims (2)

リンゴ果実を搾ったときの搾り粕とリンゴ汁のうち、前記搾り粕又は前記リンゴ汁のいずれか一方又は両方を含有し、pHが6.5以上8未満に調整た培養液を作製し、前記リンゴ果実に付着する病原性の無いロドスポリジウム トルロイド(Rhodosporidium toruloides)によって前記培養液を発酵させて水素ガスを放出させる水素ガス製造方法。 Of lees and apple juice when squeezed apple fruit, it contains either one or both of the lees or the apple juice, to produce a pH was adjusted to 8 less than 6.5 or more cultures A method for producing hydrogen gas, wherein the culture solution is fermented by Rhodosporidium toruloides having no pathogenicity attached to the apple fruit to release hydrogen gas. 前記培養液を30℃以上の温度に維持して発酵させる請求項記載の水素ガス製造方法。 Claim 1 of hydrogen gas production method according to Ru fermented by maintaining the culture in 30 ° C. or higher.
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