JPH0216101A - Hydrolysis of hemicellulose with solid acid - Google Patents
Hydrolysis of hemicellulose with solid acidInfo
- Publication number
- JPH0216101A JPH0216101A JP16727488A JP16727488A JPH0216101A JP H0216101 A JPH0216101 A JP H0216101A JP 16727488 A JP16727488 A JP 16727488A JP 16727488 A JP16727488 A JP 16727488A JP H0216101 A JPH0216101 A JP H0216101A
- Authority
- JP
- Japan
- Prior art keywords
- solid acid
- hydrolysis
- hemicellulose
- hemicelluloses
- waste liquor
- 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.)
- Granted
Links
- 229920002488 Hemicellulose Polymers 0.000 title claims abstract description 21
- 239000011973 solid acid Substances 0.000 title claims abstract description 16
- 230000007062 hydrolysis Effects 0.000 title abstract description 11
- 238000006460 hydrolysis reaction Methods 0.000 title abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 17
- 238000004537 pulping Methods 0.000 claims abstract description 12
- 150000002772 monosaccharides Chemical class 0.000 claims abstract description 11
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 7
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000003729 cation exchange resin Substances 0.000 claims abstract description 5
- 206010061592 cardiac fibrillation Diseases 0.000 claims abstract description 4
- 230000002600 fibrillogenic effect Effects 0.000 claims abstract description 4
- 239000000126 substance Substances 0.000 claims abstract description 4
- 239000002023 wood Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000002699 waste material Substances 0.000 abstract description 24
- 238000011084 recovery Methods 0.000 abstract description 4
- 230000002378 acidificating effect Effects 0.000 abstract description 3
- 229920000172 poly(styrenesulfonic acid) Polymers 0.000 abstract description 3
- 229940005642 polystyrene sulfonic acid Drugs 0.000 abstract description 3
- 238000000354 decomposition reaction Methods 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 19
- 239000011347 resin Substances 0.000 description 12
- 229920005989 resin Polymers 0.000 description 12
- SRBFZHDQGSBBOR-IOVATXLUSA-N D-xylopyranose Chemical compound O[C@@H]1COC(O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-IOVATXLUSA-N 0.000 description 10
- PYMYPHUHKUWMLA-UHFFFAOYSA-N arabinose Natural products OCC(O)C(O)C(O)C=O PYMYPHUHKUWMLA-UHFFFAOYSA-N 0.000 description 5
- SRBFZHDQGSBBOR-UHFFFAOYSA-N beta-D-Pyranose-Lyxose Natural products OC1COC(O)C(O)C1O SRBFZHDQGSBBOR-UHFFFAOYSA-N 0.000 description 5
- 238000000605 extraction Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- WQZGKKKJIJFFOK-QTVWNMPRSA-N D-mannopyranose Chemical compound OC[C@H]1OC(O)[C@@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-QTVWNMPRSA-N 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000011122 softwood Substances 0.000 description 3
- 238000003797 solvolysis reaction Methods 0.000 description 3
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000010411 cooking Methods 0.000 description 2
- 229930003836 cresol Natural products 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 229920000057 Mannan Polymers 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011121 hardwood Substances 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 229910001410 inorganic ion Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229920001221 xylan Polymers 0.000 description 1
- 150000004823 xylans Chemical class 0.000 description 1
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はW複塩類の少ない廃液中に含まれる水溶性ヘミ
セルロースを固体酸によって加水分解し@糖を得る方法
に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for obtaining @sugar by hydrolyzing water-soluble hemicellulose contained in a waste liquid containing few W double salts with a solid acid.
更に詳しく言えば、木材の解繊あるいはオルガノソルブ
パルブ化の際に生じる木材成分抽出廃液に含まれる水溶
性ヘミセルロースを固体酸によって経済的に単糖化する
方法に関するものである。More specifically, the present invention relates to a method for economically converting water-soluble hemicellulose contained in wood component extraction waste liquid produced during wood fibrillation or organosolv pulpization into monosaccharides using a solid acid.
本発明は無機塩類の少ないパルプ化廃液もしくは木材成
分抽出廃液に対して適用され、単糖の新しい製造法とし
て利用される。The present invention is applied to pulping waste liquid or wood component extraction waste liquid that is low in inorganic salts, and is utilized as a new method for producing monosaccharides.
[従来技術]
現在行われているセルロースやヘミセルロースの加水分
解法は、鉱酸または酵素を用いる方法が主体である。鉱
酸を用いる場合は中和処理が必要であり、経済的に単糖
のみを回収することは困這である。・また酵素を用いる
場合は酵素のコスト及び廃液中の微量成分による酵素の
失活が1題であり、廃液などに適用することは問題であ
る。また弗素樹脂系の固体強酸が近年開発され、炭水化
物の加水分解への適用も検討されたが、固体強酸のコス
トが非常に高く、廃液等に利用できるものではない。[Prior Art] Currently used methods for hydrolyzing cellulose and hemicellulose mainly use mineral acids or enzymes. When using mineral acids, neutralization treatment is required, and it is difficult to economically recover only monosaccharides.・Additionally, when enzymes are used, there are problems with the cost of the enzymes and the inactivation of the enzymes due to trace components in the waste liquids, which poses problems when applied to waste liquids. In addition, fluororesin-based solid strong acids have been developed in recent years, and their application to hydrolysis of carbohydrates has been considered, but the cost of solid strong acids is extremely high and they cannot be used for waste liquids.
[発明が解決しようとする問題点]
従来のパルプ化もしくは木材解繊法では、抽出廃液中に
多量の無機塩類が混入したり、既に糖成分は単糖となっ
て#在するのが通常であった。しかし新たなパルプ化や
解繊法では、物理的な方法や無機薬品を用いない方法が
検討され、この場合糖成分は単糖ではなく水溶性ヘミセ
ルロースとして廃液中に存在することが多い、このよう
な廃液中には無機塩類も少なく、高濃度のヘミセルロー
スが蓄積されている。[Problems to be solved by the invention] In conventional pulping or wood defibration methods, it is common for large amounts of inorganic salts to be mixed into the extraction waste liquid, or for sugar components to already be present in the form of monosaccharides. there were. However, new pulping and defibration methods are being considered that do not use physical methods or inorganic chemicals. There are few inorganic salts in the wastewater, and a high concentration of hemicellulose is accumulated.
本発明はこのような木材抽出廃液中のヘミセルロースを
固体酸を用いて加水分解することで、加水分解後の廃液
からの固体酸の回収を容易にし、:[た固体酸を再使用
して、加水分解プロセスの単純化、コストの低下を図る
ものである。The present invention hydrolyzes hemicellulose in such wood extraction waste liquid using a solid acid, thereby facilitating recovery of the solid acid from the waste liquid after hydrolysis. The aim is to simplify the hydrolysis process and reduce costs.
[問題点を解決するための手段]
本発明者らは有機溶媒によるパルプ化法(ソルボリシス
パルプ化法)で得られた廃液中のヘミセルロースの加水
分解法についてm意研究を行った結果、強酸性カチオン
交換樹脂を加水分解用固体酸触媒として用いる単糖類の
製造法を見い出し、本発明を完成させるに至った。[Means for Solving the Problems] The present inventors conducted research on a method for hydrolyzing hemicellulose in waste liquid obtained by pulping method using an organic solvent (solvolysis pulping method). We have discovered a method for producing monosaccharides using a cation exchange resin as a solid acid catalyst for hydrolysis, and have completed the present invention.
ソルボリシスパルプ化法とはクレゾール水溶液を木材の
パルプ化蒸解溶剤として用いる新しいパルプ化法であり
、クレゾールは蒸解後回収して再使用する。そのため廃
液中には無機イオンは少なく、ヘミセルロースが高濃度
で含まれる。このヘミセルロースは木材が広葉樹の場合
はキシラン、針葉樹の場合はマンナンが主体であるが、
これらからキシロース、マンノースを製造するにはヘミ
セルロースを加水分解する必要がある。The solvolysis pulping method is a new pulping method that uses an aqueous cresol solution as a cooking solvent for wood pulping, and the cresol is recovered and reused after cooking. Therefore, the waste liquid contains few inorganic ions and a high concentration of hemicellulose. This hemicellulose is mainly composed of xylan when the wood is hardwood, and mannan when the wood is softwood.
To produce xylose and mannose from these, it is necessary to hydrolyze hemicellulose.
本発明はこのような廃水中に含まれるヘミセルロースを
加水分解し、単糖類を得るに当たって、固体酸として例
えばポリスチレンスルホン酸等の強酸性カチオン交換樹
脂を用いることに特徴がある。これらの樹脂はイオン交
換容量すなわち触媒能が大きく、また水処理用として市
販されているので入手も容易である。The present invention is characterized in that in hydrolyzing hemicellulose contained in such wastewater to obtain monosaccharides, a strongly acidic cation exchange resin such as polystyrene sulfonic acid is used as the solid acid. These resins have a large ion exchange capacity, that is, catalytic ability, and are easily available as they are commercially available for water treatment.
この樹脂を耐圧性のカラムに充填し、加熱しなからヘミ
セルロースを含む廃液を通液することでl\ミセルロー
スは容易に単糖に加水分解され、単糖を含む廃液を流出
液として得ることができる。By filling this resin into a pressure-resistant column and passing the waste solution containing hemicellulose through it without heating, the microcellulose is easily hydrolyzed into monosaccharides, and the waste solution containing monosaccharides can be obtained as an effluent. I can do it.
E記のようにカラムを用いて通液する以外にもバッチ的
にオートクレーブ中で加熱する方法で加水分解すること
もできる。In addition to passing the solution through a column as described in E, hydrolysis can also be carried out in batches by heating in an autoclave.
[作用と実施例]
次に本発明の実施方法について実験結果を例にあげて説
明する。[Operations and Examples] Next, the method of carrying out the present invention will be explained using experimental results as examples.
実施例1
オートクレーブ内にソルボリシスパルプ化廃液100
m lに対しポリスチレンスルホン酸型の強酸性カチオ
ン交換梅脂を5g加え、攪はんしなから種々の温度で加
熱を行い、キシロースの生成濃度を調べた。Example 1 100 solvolysis pulping waste liquid in autoclave
5 g of strongly acidic cation-exchanged plum fat of the polystyrene sulfonic acid type was added to each ml, and the mixture was heated at various temperatures while stirring, and the concentration of xylose produced was examined.
第1mに示すように、加熱温度をこの樹脂の常用耐熱温
度である150℃にとフた場合、接触時間40分が最も
ヘミセルロースの加水分解効率が高く、これ以上の温度
ではキシロースの生成量はむしろ低下した。この最大値
では、キシロース生成量は鉱酸触媒の場合の約90%に
達した。温度が低いと接触時間を長くとる必要があるた
め、この樹脂を用いる場合、150℃では40分が好ま
しい。As shown in No. 1m, when the heating temperature is kept at 150°C, which is the usual heat-resistant temperature of this resin, the hemicellulose hydrolysis efficiency is highest when the contact time is 40 minutes, and at higher temperatures, the amount of xylose produced is In fact, it has declined. At this maximum value, xylose production reached approximately 90% of that for the mineral acid catalyst. Since it is necessary to take a long contact time when the temperature is low, when using this resin, 40 minutes at 150° C. is preferable.
実施例2
内径15mm長さ30 cmのステンレス製のカラムに
樹脂を充填し、オイルバス中で加熱したカラムに針葉樹
材のチップ解繊廃液を流速1〜10m l / m i
nで通液し、溶出液中のマンノース濃度を定量した。Example 2 A stainless steel column with an inner diameter of 15 mm and a length of 30 cm was filled with resin, and the waste liquid from softwood chip defibration was poured into the column heated in an oil bath at a flow rate of 1 to 10 ml/mi.
The mannose concentration in the eluate was determined.
第2図に示すように150℃におけるマンノース濃度は
流速が3ml/minで極大を示した。As shown in FIG. 2, the mannose concentration at 150° C. reached its maximum at a flow rate of 3 ml/min.
充填した樹脂は廃液中の微量の無機塩(カリウム、カル
シウム、マグネシウム等のカチオン)を吸着して触媒能
が徐々に低下してくるか、一定期閏毎ζご硫酸または塩
酸の希薄水ll液によって再生することにより、回復さ
せることができた。The filled resin will adsorb trace amounts of inorganic salts (cations such as potassium, calcium, magnesium, etc.) in the waste liquid, and the catalytic ability will gradually decrease, or the catalytic ability will gradually decrease, or it will be removed at regular intervals by dilute aqueous solution of sulfuric acid or hydrochloric acid. I was able to recover it by regenerating it.
また有機物による樹脂の汚染も長期間使用した場合に生
じたが、約5Nの水酸化ナトリウム溶液で樹脂を洗浄す
ることにより、約80%回復させることができた。Contamination of the resin with organic substances also occurred during long-term use, but by washing the resin with an approximately 5N sodium hydroxide solution, approximately 80% recovery was possible.
[発明の効果]
本発明の方法で木材抽出廃液中のヘミセルロースの加水
分解を行うと、触媒である固体酸の分離め、経済的に加
水分解を行うことができる。[Effects of the Invention] When the hemicellulose in the wood extraction waste liquid is hydrolyzed by the method of the present invention, the hydrolysis can be carried out economically due to the separation of the solid acid that is the catalyst.
第1図は本発明をバッチ法にて実施し、150℃加熱の
場合の樹脂への接触時間とキシロース生成潰との関係を
示すグラフである。樹脂はソルボノシスパルブ化廃液に
対して5%添加した。
第2図は本発明なカラム法で実施した場合である。針葉
樹材の解繊で生じる廃液を150℃に加熱した樹脂充填
カラム(15mmx30cm)に通7αした際の通液速
度とマンノース生成濃度との関係を示したグラフである
。
特許出願人 工業技術院長 飯塚幸三指定代理
人
工業技術院四国工業技術′J、験所長
菅壌和彦
箋1図
樹脂ヒの嶺J九時國(5)
連洟還II(祇7へ、1ル)FIG. 1 is a graph showing the relationship between the contact time to the resin and the production of xylose when the present invention is carried out by a batch method and heated at 150°C. The resin was added in an amount of 5% to the solvonosis pulping waste liquid. FIG. 2 shows the case where the column method according to the present invention is used. It is a graph showing the relationship between the liquid passage rate and the mannose production concentration when waste liquid generated from fibrillation of softwood material is passed through a resin-filled column (15 mm x 30 cm) heated to 150°C. Patent Applicant Kozo Iizuka, Director of the Agency of Industrial Science and Technology, Designated Representative of the Agency of Industrial Science and Technology, Shikoku Industrial Technology'J, Director of the Institute, Kazuhiko Sugayoshi, Figure 1, Resin Hi no Mine, J Kujikuni (5) Renshokan II (To G7, 1 Ru )
Claims (2)
繊する際に生じる水溶性ヘミセルロースの固体酸による
加水分解法。(1) A method of hydrolyzing water-soluble hemicellulose produced during pulping or fibrillation of wood using a solid acid without using inorganic chemicals.
範囲第1項記載の水溶性ヘミセルロースと接触させなが
ら100〜150℃の間で加熱することによって、水溶
性ヘミセルロースを加水分解して、単糖を得る方法。(2) Using a cation exchange resin as a solid acid, the water-soluble hemicellulose is hydrolyzed by heating between 100 and 150°C while contacting with the water-soluble hemicellulose described in claim 1, and the monosaccharide How to get.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16727488A JPH0216101A (en) | 1988-07-04 | 1988-07-04 | Hydrolysis of hemicellulose with solid acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16727488A JPH0216101A (en) | 1988-07-04 | 1988-07-04 | Hydrolysis of hemicellulose with solid acid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0216101A true JPH0216101A (en) | 1990-01-19 |
| JPH0548762B2 JPH0548762B2 (en) | 1993-07-22 |
Family
ID=15846705
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16727488A Granted JPH0216101A (en) | 1988-07-04 | 1988-07-04 | Hydrolysis of hemicellulose with solid acid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0216101A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5342641A (en) * | 1991-07-02 | 1994-08-30 | Fuji Oil Co., Ltd. | Food additive comprising water-soluble hemicellulose |
| KR100682592B1 (en) * | 1999-05-14 | 2007-02-15 | 다카라 바이오 가부시키가이샤 | Manufacturing method of beverage containing liquid agar |
| JP2009296919A (en) * | 2008-06-12 | 2009-12-24 | Tokyo Univ Of Agriculture & Technology | Method for liquefying cellulose-based biomass |
| US20100113764A1 (en) * | 2008-11-05 | 2010-05-06 | Blair Richard G | Solid Acid Catalyzed Hydrolysis of Cellulosic Materials |
| WO2011037194A1 (en) * | 2009-09-24 | 2011-03-31 | 株式会社Ihi | System and method for treating biomass |
| CN101402659B (en) | 2008-11-18 | 2011-06-08 | 中国农业大学 | Method for removing hemicellulose from biomass raw material |
| JP2013144741A (en) * | 2012-01-13 | 2013-07-25 | Futamura Chemical Co Ltd | Method for producing chain-shortened polysaccharide |
-
1988
- 1988-07-04 JP JP16727488A patent/JPH0216101A/en active Granted
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5342641A (en) * | 1991-07-02 | 1994-08-30 | Fuji Oil Co., Ltd. | Food additive comprising water-soluble hemicellulose |
| KR100682592B1 (en) * | 1999-05-14 | 2007-02-15 | 다카라 바이오 가부시키가이샤 | Manufacturing method of beverage containing liquid agar |
| US7217817B1 (en) | 1999-05-14 | 2007-05-15 | Takara Bio Inc. | Agarobiose-containing composition |
| KR100816665B1 (en) * | 1999-05-14 | 2008-03-26 | 다카라 바이오 가부시키가이샤 | Agarobiose-containing composition |
| KR100857844B1 (en) * | 1999-05-14 | 2008-09-10 | 다카라 바이오 가부시키가이샤 | Agarobiose-containing composition |
| JP2009296919A (en) * | 2008-06-12 | 2009-12-24 | Tokyo Univ Of Agriculture & Technology | Method for liquefying cellulose-based biomass |
| US20100113764A1 (en) * | 2008-11-05 | 2010-05-06 | Blair Richard G | Solid Acid Catalyzed Hydrolysis of Cellulosic Materials |
| US8871739B2 (en) * | 2008-11-05 | 2014-10-28 | University Of Central Florida Research Foundation, Inc. | Solid acid catalyzed hydrolysis of cellulosic materials |
| CN101402659B (en) | 2008-11-18 | 2011-06-08 | 中国农业大学 | Method for removing hemicellulose from biomass raw material |
| WO2011037194A1 (en) * | 2009-09-24 | 2011-03-31 | 株式会社Ihi | System and method for treating biomass |
| CN102597273A (en) * | 2009-09-24 | 2012-07-18 | 株式会社Ihi | System and method for treating biomass |
| JP2013144741A (en) * | 2012-01-13 | 2013-07-25 | Futamura Chemical Co Ltd | Method for producing chain-shortened polysaccharide |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0548762B2 (en) | 1993-07-22 |
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