JPS5858077B2 - Pretreatment method for enzymatic hydrolysis of cellulosic materials - Google Patents

Pretreatment method for enzymatic hydrolysis of cellulosic materials

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Publication number
JPS5858077B2
JPS5858077B2 JP18167181A JP18167181A JPS5858077B2 JP S5858077 B2 JPS5858077 B2 JP S5858077B2 JP 18167181 A JP18167181 A JP 18167181A JP 18167181 A JP18167181 A JP 18167181A JP S5858077 B2 JPS5858077 B2 JP S5858077B2
Authority
JP
Japan
Prior art keywords
enzymatic hydrolysis
cellulose
lignin
irradiation
rad
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.)
Expired
Application number
JP18167181A
Other languages
Japanese (ja)
Other versions
JPS5886095A (en
Inventor
伸一 三宅
慶一 小島
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.)
SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI
Original Assignee
SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI
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 SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI filed Critical SHINNENRYOYU KAIHATSU GIJUTSU KENKYU KUMIAI
Priority to JP18167181A priority Critical patent/JPS5858077B2/en
Publication of JPS5886095A publication Critical patent/JPS5886095A/en
Publication of JPS5858077B2 publication Critical patent/JPS5858077B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はセルロース質材酵素加水分解の前処理方法に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a pretreatment method for enzymatic hydrolysis of cellulosic materials.

従来、セルロースをグルコースに分解する方法として、
酸加水分解及び酵素加水分解がある。
Conventionally, as a method to decompose cellulose into glucose,
There are acid hydrolysis and enzymatic hydrolysis.

このうち酵素加水分解法は、穏やかな圧力・温度条件下
で反応が進行し、特異的で二次分解も起こらないという
利点をもつ。
Among these, the enzymatic hydrolysis method has the advantage that the reaction proceeds under mild pressure and temperature conditions, is specific, and does not cause secondary decomposition.

しかし、木材、稲わら、小麦わら、トウモロコシの茎、
葉、バガス及び紙類などに含まれるセルロースは一般に
結晶性が高く、またリグニン、灰分などと混在している
ため酵素加水分解に対して強い抵抗性を示し、反応速度
は遅く、分解率は低いという欠点がある。
However, wood, rice straw, wheat straw, corn stalks,
Cellulose contained in leaves, bagasse, paper, etc. is generally highly crystalline, and because it is mixed with lignin, ash, etc., it exhibits strong resistance to enzymatic hydrolysis, the reaction rate is slow, and the decomposition rate is low. There is a drawback.

この欠点を取り除くため、酵素加水分解を行う前に、ボ
ールミルなどによる機械的粉砕、高温加熱粉砕、γ線照
射による破壊など、セルロースの非品性と反応表面積を
増大させる物理的前処理や、H3PO4,H2SO4゜
ZrC1□、カドキセン及びNaOHなどの試薬により
セルロースの結晶構造を破壊したり、リグニンを除去す
る化学的前処理を行って、天然のセルロース質材を加水
分解酵素が分解しやすい構造に変えることが行われてい
る。
In order to eliminate this drawback, prior to enzymatic hydrolysis, physical pretreatments such as mechanical pulverization using a ball mill, high-temperature heating pulverization, destruction by γ-ray irradiation, etc. that increase the quality of cellulose and the reaction surface area, and H3PO4 , H2SO4゜ZrC1□, cadoxene, NaOH, and other reagents are used to destroy the crystalline structure of cellulose and perform chemical pretreatment to remove lignin, changing the natural cellulosic material into a structure that is easy to be broken down by hydrolytic enzymes. things are being done.

しかし、従来行われている前処理方法により十分な効果
を期待すれば、長時間の運転や高濃度、高温、高圧など
が必要となり、エネルギー消費量が大きくなってしまう
という欠点をもつ。
However, if conventional pretreatment methods are expected to be sufficiently effective, they require long-time operation, high concentration, high temperature, and high pressure, resulting in high energy consumption.

本発明は、か\る従来技術における欠点を改善し、緩和
な条件、少ないエネルギーで十分であり、セルロース質
材の酵素加水分解反応に対して速い反応速度と高い分解
率を与える前処理方法を提供するものである。
The present invention improves the drawbacks of the prior art, and provides a pretreatment method that requires mild conditions and less energy, and provides a fast reaction rate and high decomposition rate for the enzymatic hydrolysis reaction of cellulosic materials. This is what we provide.

すなわち本発明は酵素加水分解の前処理として、予め電
子線またはγ線を10’rad以上L 08rad以下
照射することにより、アルカリ水溶液処理を容易にする
というものである。
That is, the present invention facilitates alkaline aqueous solution treatment by irradiating electron beams or gamma rays at 10'rad or more and L08rad or less as a pretreatment for enzymatic hydrolysis.

前処理方法としての、高結晶性でリグニン混在のセルロ
ース質材への放射線による処理は、(1)セルロースの
重合度の低下 (2)結晶量の減少 (3)還元糖の生成 (4)機械的劣化 の効果があることが知られているが、(1) 、 (2
) 、 (3)の効果が特に顕著に現われてくるのは、
照射線量カ108rad以上となった場合で、多大なエ
ネルギーを要し、酵素加水分解の前処理として行うこと
は困難である。
As a pretreatment method, treatment of highly crystalline and lignin-containing cellulosic materials with radiation can (1) decrease the degree of polymerization of cellulose, (2) decrease the amount of crystals, (3) produce reducing sugars, and (4) mechanical It is known that it has the effect of deteriorating the
), the effect of (3) becomes especially noticeable when
When the irradiation dose is 108 rad or more, it requires a large amount of energy and is difficult to perform as a pretreatment for enzymatic hydrolysis.

(4)の効果はl 06rad程度の照射量でも明らか
であるが、酵素加水分解反応の速度と分解率とを飛躍的
に高めるためには、30μ程度の微粉としなければなら
ないため、電子線またはγ線による照射と粉砕に要する
エネルギーはかなり太きい。
The effect of (4) is obvious even with an irradiation dose of about 106 rad, but in order to dramatically increase the rate and decomposition rate of the enzymatic hydrolysis reaction, it is necessary to make the powder into a fine powder of about 30μ, so electron beam or The energy required for irradiation and crushing with gamma rays is quite large.

このほか、照射および加熱の相乗効果として、酵素加水
分解反応の速度と分解率とが高められることが知られて
いるが、かなりの高温条件が必要であるなど、やはり十
分な効果を期待すれば大きなエネルギー消費量を必要と
する。
In addition, it is known that the synergistic effect of irradiation and heating increases the rate and decomposition rate of enzymatic hydrolysis reactions, but this requires considerably high temperature conditions, so it is difficult to expect a sufficient effect. Requires large energy consumption.

しかるに本発明法によれば、電子線またはγ線の照射量
は■06rad以上108rad以下であればよく、ま
たアルカリ水溶液処理の条件も、常温付近、短時間で十
分であり、少ないエネルギー消費量の前処理により、速
い反応速窒と高い分解率とを与えることりうできる。
However, according to the method of the present invention, the amount of irradiation of electron beams or gamma rays may be between 06 rad and 108 rad, and the alkaline aqueous solution treatment conditions are sufficient at room temperature for a short time, resulting in low energy consumption. Pretreatment can provide fast reaction rates and high decomposition rates.

106rad以上L 08rad以下の電子線またはγ
線を照射した高結晶性でリグニン混在のセルロース質材
をアルカリ水溶液により、セルロース質材中に含まれる
リグニンが全て可溶化する条件より緩和な条件により処
理を行ったとき、照射量が大きくなればなるほど、処理
後のセルロース質材の回収率は小さくなり、可溶分は増
大する。
Electron beam or γ of 106 rad or more L 08 rad or less
When a highly crystalline, lignin-containing cellulosic material that has been irradiated with radiation is treated with an alkaline aqueous solution under milder conditions than those in which all the lignin contained in the cellulosic material is solubilized, if the irradiation dose becomes large, Indeed, the recovery rate of the cellulosic material after treatment decreases and the soluble content increases.

セルロース質材のクラーソンリグニン量は106rad
以上の電子線またはγ線の照射により若干低減すること
が報告されているが、クラーソンリグニン量の低減は、
セルロース質材中に含まれるリグニンが電子線またはγ
線の照射により、その反応性が高められることを示して
いる。
The amount of Klason lignin in cellulose material is 106 rad.
It has been reported that the amount of Klason lignin is slightly reduced by irradiation with electron beams or γ-rays, but the reduction in Klason lignin content is
Lignin contained in cellulosic materials is exposed to electron beams or γ
This shows that irradiation with radiation increases its reactivity.

本発明は、この電子線またはγ線の照射によるリグニン
の反応性の向上を利用したものである。
The present invention utilizes this improvement in the reactivity of lignin by irradiation with electron beams or gamma rays.

電子線またはγ線を106rad以上108rad以下
照射したセルロース質材に含まれるリグニンはアルカリ
水溶液処理によっても容易に低分子化、可溶化するよう
になる。
Lignin contained in a cellulosic material irradiated with electron beams or gamma rays at 106 rad or more and 108 rad or less becomes easily reduced in molecular weight and becomes solubilized by treatment with an alkaline aqueous solution.

その結果、アルカリ濃度、処理温度、処理時間などの条
件を緩和しても、容易にセルロースとリグニンとの微細
な接合を離すことができ、酵素加水分解反応に対しても
、セルロース加水分解酵素がリグニンに阻害されること
なしに細胞壁のセルロース層に到達できるようになり、
糖化速度および分解率は向上する。
As a result, even if conditions such as alkali concentration, treatment temperature, and treatment time are relaxed, the fine bonds between cellulose and lignin can be easily separated, and cellulose hydrolase can be easily separated from the cellulose and lignin. It can now reach the cellulose layer of the cell wall without being inhibited by lignin.
Saccharification rate and decomposition rate are improved.

アルカリ水溶液処理を行ったセルロース質材の不溶分を
P別し、これを基質として酵素加水分解反応を行っても
よいが、電子線またはγ線の照射によりセルロースの重
合度低下がおこり、処理条件によってはアルカリ水溶液
処理の際に可溶化するセルロース分があるので、セルロ
ース質材中のセルロースの全利用という点から、不溶分
の酵素加水分解とは別に、沢液に酢酸またはリン酸など
を加えて緩衝液とし、セルロース加水分解酵素を加えて
酵素加水分解を行うか、あるいは処理藩液を戸別せず、
酢酸またはリン酸などを加えPHを調節し、セルロース
加水分解酵素を加え糖化液とし、酵素加水分解を行うこ
とが好ましい。
The insoluble matter of the cellulosic material treated with aqueous alkali solution may be separated from P and used as a substrate for enzymatic hydrolysis reaction, but the degree of polymerization of cellulose will decrease due to irradiation with electron beams or gamma rays, and the treatment conditions may be In some cases, some cellulose content becomes solubilized during alkaline aqueous treatment, so in order to fully utilize the cellulose in the cellulosic material, it is necessary to add acetic acid or phosphoric acid to the sap, in addition to the enzymatic hydrolysis of the insoluble content. Either use it as a buffer solution, add cellulose hydrolase to perform enzymatic hydrolysis, or do not send the treated solution to each house.
It is preferable to add acetic acid or phosphoric acid to adjust the pH, add cellulose hydrolase to form a saccharification solution, and perform enzymatic hydrolysis.

可溶化しているセルロースの重合度は低く、セルロース
加水分解酵素によりグルコースが生成する速度は大きい
The degree of polymerization of solubilized cellulose is low, and the rate at which glucose is produced by cellulose hydrolase is high.

また可溶化しているリグニンは、固体リグニンと異なり
、セルロース加水分解酵素が吸着し活性を失うことがな
いなど、酵素加水分解に対して大きな阻害を及ぼさない
Furthermore, unlike solid lignin, solubilized lignin does not adsorb cellulose hydrolase and lose its activity, and does not significantly inhibit enzymatic hydrolysis.

以下実施例を詳述するが、本発明がこの実権例にのみ限
定されるものでないことはいうまでもない。
Examples will be described in detail below, but it goes without saying that the present invention is not limited only to these practical examples.

実権例 ■ セルロース質材として稲わら(セルロース分31%)を
ハンマーミルにより粉砕したもの\うち、42〜80メ
ツシユの試料に対し電子線加速機により照射を行い、こ
れを各温度に保った25倍量のl規定水酸化ナトリウム
水溶液中で■5分間攪拌し、戸別して水および酢酸水溶
液で洗浄後乾燥して回収率を求め、リグニン除去率を計
算した。
Actual Example ■ Rice straw (cellulose content: 31%) was crushed using a hammer mill as a cellulosic material. A sample of 42 to 80 meshes was irradiated with an electron beam accelerator and kept at various temperatures. The mixture was stirred for 5 minutes in twice the volume of 1N aqueous sodium hydroxide solution, washed separately with water and acetic acid aqueous solution, and dried to determine the recovery rate, and the lignin removal rate was calculated.

表1に各照射量の試料を各温度で処理したときのリグニ
ンの除去率を示した。
Table 1 shows the lignin removal rate when samples with various irradiation doses were treated at various temperatures.

この表の如く、照射を行うことにより、リグニンの除去
率が向上すること、特に常温付近での処理における照射
の効果が顕著であることが判った。
As shown in this table, it was found that the removal rate of lignin was improved by irradiation, and the effect of irradiation was particularly remarkable in treatment near room temperature.

実施例 2 セルロース質材として稲わら(セルロース分31φ)を
電子線加速機で照射を行い、ハンマーミルにより粉砕し
たもの\うち、511L7ILの丸孔スクリーンを通る
ものを用い、処理濃度7饅となるように0.25規定水
酸化ナトリウム水溶液を加え30°C915分間攪拌す
る。
Example 2 As a cellulosic material, rice straw (cellulose content: 31φ) was irradiated with an electron beam accelerator and pulverized with a hammer mill. Of these, the material that passed through a 511L7IL round hole screen was used, resulting in a treatment concentration of 7 man Add 0.25N aqueous sodium hydroxide solution and stir at 30°C for 915 minutes.

IOφ酢酸水溶液および水を加えてP H4,9、基質
濃度5%となるように調節し、セルロース加水分解酵素
(商品名セルラーゼオノズ力、近畿ヤクルト■製)を全
量の0.2係になるよう加え、酵素加水分解を行った。
Add IOφ acetic acid aqueous solution and water to adjust pH to 4.9 and substrate concentration to 5%, and add cellulose hydrolase (trade name: Cellulase Onozu Chikara, manufactured by Kinki Yakult ■) to 0.2 part of the total amount. and enzymatic hydrolysis.

図1に加水分解時間対酵素加水分解によるセルロース分
解率を示した。
Figure 1 shows the hydrolysis time versus cellulose decomposition rate by enzymatic hydrolysis.

予め照射を行ったものは、リグニン除去率が向上してお
り、照射の効果が顕著にあられれている。
The lignin removal rate of the samples that had been irradiated in advance was improved, and the effect of irradiation was remarkable.

水酸化カリウム水溶液またはアンモニア水溶液などのア
ルカリ水溶液を用いた場合も同様の結果が得られている
Similar results have been obtained when an alkaline aqueous solution such as a potassium hydroxide aqueous solution or an ammonia aqueous solution is used.

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

図1は加水分解時間対酵素加水分解によるセルロース分
解率を示したものである。
FIG. 1 shows the hydrolysis time versus cellulose degradation rate by enzymatic hydrolysis.

Claims (1)

【特許請求の範囲】[Claims] 1 セルロース質材のアルカリ水溶液により脱リグニン
処理を行う前に、予め該セルロース質材に電子線または
γ線をl 06rad以上108rad以下照射するこ
とを特徴とするセルロース質材酵素加水分解の前処理方
法。
1. A pretreatment method for enzymatic hydrolysis of cellulosic material, which comprises irradiating the cellulosic material with electron beams or gamma rays at 106 rad or more and 108 rad or less before delignifying the cellulosic material with an alkaline aqueous solution. .
JP18167181A 1981-11-12 1981-11-12 Pretreatment method for enzymatic hydrolysis of cellulosic materials Expired JPS5858077B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18167181A JPS5858077B2 (en) 1981-11-12 1981-11-12 Pretreatment method for enzymatic hydrolysis of cellulosic materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18167181A JPS5858077B2 (en) 1981-11-12 1981-11-12 Pretreatment method for enzymatic hydrolysis of cellulosic materials

Publications (2)

Publication Number Publication Date
JPS5886095A JPS5886095A (en) 1983-05-23
JPS5858077B2 true JPS5858077B2 (en) 1983-12-23

Family

ID=16104829

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18167181A Expired JPS5858077B2 (en) 1981-11-12 1981-11-12 Pretreatment method for enzymatic hydrolysis of cellulosic materials

Country Status (1)

Country Link
JP (1) JPS5858077B2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60164494A (en) * 1984-02-07 1985-08-27 Res Assoc Petroleum Alternat Dev<Rapad> Method for pretreatment of enzymic hydrolysis of cellulosic wood
JPS60251897A (en) * 1984-05-29 1985-12-12 Res Assoc Petroleum Alternat Dev<Rapad> Method of pretreatment for enzymatic hydrolysis of cellulosic material
CA2857801C (en) * 2006-10-26 2014-12-30 Xyleco, Inc. Methods of processing biomass comprising electron-beam radiation
KR100873700B1 (en) * 2007-06-25 2008-12-12 사단법인 한국가속기 및 플라즈마 연구협회 Method of producing bio-fuel using electron beam
US7900857B2 (en) 2008-07-17 2011-03-08 Xyleco, Inc. Cooling and processing materials
DK3095512T3 (en) 2009-02-11 2018-12-10 Xyleco Inc CREATION OF BIOMASS BY IONIZING RADIATION
KR101170052B1 (en) 2010-12-17 2012-08-01 한국수력원자력 주식회사 The method for extracting of Lignin using irradiation of radioactive ray
NZ743055A (en) * 2013-03-08 2020-03-27 Xyleco Inc Equipment protecting enclosures

Also Published As

Publication number Publication date
JPS5886095A (en) 1983-05-23

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