• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A process for the production of glucose from cellulose containing raw material by steam treatment at a temperature from 160 DEG to 230 DEG C. for from 2 minutes to 4 hours followed by lixiviation with aqueous alkali and acid or enzymatic hydrolysis of fibrinous residue.
    公开号:SU1072816A3
    申请号:SU772506593
    申请日:1977-07-20
    公开日:1984-02-07
    发明作者:Дитрихс Ханс-Херманн；Зиннер Михаэль；Опдербек Фритц；Брахтхойзер Карл-Хайнц
    申请人:Проектирунг Хемише Ферфаренстехник Гмбх (Фирма)；
    IPC主号:
    专利说明:


    ND
    СХ5
    The invention relates to biotechnology, in particular to a method for producing glucose from cellulose-containing materials. A method for producing glucose from cellulosic material is known, which involves grinding the raw material before hydrolyzing IJ. There is also known a method for producing glucose from cellulose-containing materials, which involves grinding the raw material, pre-treating it with an alkali solution C. a subsequent enzymatic or acidic hydrol from om 2. . According to a known method, the treatment is carried out with a 1-4% alkali solution at a temperature of 100-120 ° C. The yield of sugars is 9.4-13.6%. The purpose of the invention is to increase your glucose yield. This goal is achieved by the fact that according to the method for producing glucose from cellulose-containing material. before the treatment with an alkali solution, the raw materials are exposed to a sharp vapor at a temperature of 160-210 C and a pressure of 6-20 bar for 5-240 w; In this case, the concentration of the alkali solution is 0.2-1.0%. The method is carried out as follows. As a raw material, various plant cellulose-containing materials are used, for example, hardwood, straw, bagasse, grain husks, corn cobs and maize straw, etc. Raw materials are treated with steam under pressure. The treatment is carried out for 5-240 minutes, the treatment time depending on the temperature. The treatment process is accompanied by the formation of acetic acid, which has a beneficial effect on the preparation of the raw material. If little acetic acid is formed in the process, it is advisable to add about .6% acid. After steaming the raw material, the treatment is carried out with an alkaline solution, which can be carried out in several stages. The leaching is carried out immediately after the steam treatment under pressure, since the hot raw material heats the alkaline solution. Leaching is advisable to carry out on the counter-current principle. The residue obtained after leaching, which is a fibrous substance, is washed with water and subjected to acid or enzymatic hydrolysis. Since the obtained fibrous substance practically contains, in addition to lignin, only co-cellulose, only glucose is formed during hydrolysis. Example. 400 g of oak wood in the form of air-dry wood chips are treated with steam in a laboratory refiner firm ("L. Defibrator A.G. 7 minutes at 190 ° C and under a pressure of 12 MPa, then crushed. The resulting wet fibrous substance is washed out with 4 liters of water and defibrator and washed on a sieve. Immediately after this, the washed and pressed fibrous material is suspended in 5 liters of 1% aqueous sodium hydroxide solution at room temperature. After 30 minutes, the material is filtered, washed with water, dilute acid, and again with water. is 66% calculated on the applied amount of wood.The material obtained after treatment is subjected to acid hydrolysis.To 300 mg of fibrous material is added with cooling 3 ml of concentrated sulfuric acid. The mixture is kept for 60 minutes, diluted with 84 ml of water and heated for 60 minutes at 120s After treatment, the solutions contain 1T 70% glucose based on the weight of the fibrous substance. Example 2. Birch wood is treated as described in Example 1, but the steaming time is 80 minutes and a 0.5% alkali solution is used. The material obtained after treatment is subjected to enzymatic hydrolysis. 25 mg of the product obtained by dialysis and subsequent freeze-drying from the enzyme preparation .Onozuka ss (All Japan. Biochemicals Co. Nishinomiya, Japan) are added to 200 mg of fibrous matter with 5 ml of fl, M sodium acetate buffer pH 4.8 and extract -. live in closed Erlenmeyer flasks with a shaking water bath. The yield of glucose is 81%. Example 3: The method is carried out according to Example 2, but wheat straw is used as a raw material. The output of glucose - 66% of the fibrous matter. The residue obtained after enzymatic treatment, after complete hydrolysis, contains less than 10% carbohydrates. based on the amount of fiber material used, this amount is xylose, and glucose is contained in a very small amount. . Consequently, the cellulose of the fibrous substance is almost completely converted into glucose by enzymatic hydrolysis. PRI me R 4. 200 g of birch wood in the form of chips are treated with steam under a pressure of 20 MPa and tempe310728164
    The treatment room 210 is 5 minutes, then the treatment profile is crushed to 160 (as in Example 1J and a pressure of 6 at is processed, the treatment time is 4 hours. 0.2% alkali solution. Yield After acid hydrolysis, the yield of fibrous matter is 69%. Glucose 56 , 6% (based on absolute-acid hydrolysis yield - after. Enzymatic hydrolysis of glucose is 53.4% in terms of glucose yield: 58.2% calculated on the basis of the weight of the fibrous substance or salt dry in a bright substance. 36.9% in calculated on absolutely Thus, the proposed used wood. producing glucose from tsellyuloeoPr and m e p5. Method osuschestv- 0 roderzhaschih material allows the floor out according to Example 4, but with the glucose temtse- uchat horolshm yield.
     but dry fibrous matter.
    权利要求:
    Claims (1)
    [1]
    METHOD FOR PRODUCING GLUCOSE FROM CELLULOSE-CONTAINING MATERIALS, which involves grinding the raw material, its preliminary treatment with an alkali solution followed by enzymatic or acid hydrolysis, characterized in that, in order to increase the glucose yield, the raw materials act with acute steam at a temperature of 160-210 ° C at a temperature of 160-210 ° C and a pressure of 6-20 atm for 5-240 min, while the concentration of the alkali solution is 0.2-1.0%.
    SU „1072816
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    类似技术:
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    同族专利:
    公开号 | 公开日
    IT1077402B|1985-05-04|
    PL110696B1|1980-07-31|
    FR2359206B1|1983-01-14|
    FI62140B|1982-07-30|
    FR2359206A1|1978-02-17|
    PL199762A1|1978-03-13|
    DE2732289C2|1988-10-20|
    FI772233A|1978-01-21|
    CH631210A5|1982-07-30|
    AT350986B|1979-06-25|
    JPS6052800B2|1985-11-21|
    ES460856A1|1978-04-16|
    SE439323B|1985-06-10|
    GB1582480A|1981-01-07|
    US4160695A|1979-07-10|
    SE7708301L|1978-01-21|
    CA1087122A|1980-10-07|
    ATA534576A|1978-11-15|
    DE2732289A1|1978-01-26|
    JPS5334935A|1978-03-31|
    引用文献:
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    FR896034A|1942-07-13|1945-02-09|Hermann Schubert|Process for obtaining polyoses of wood, from wood, straw and other plant starting materials|
    US2510668A|1945-10-08|1950-06-06|Alfred M Thomsen|Method of converting woody substances|
    GB934904A|1960-09-16|1963-08-21|Ledoga Spa|Improvements in or relating to pentose solutions|
    DE1567335C3|1967-10-17|1979-03-29|Rudolf Dipl.-Ing. 8000 Muenchen Eickemeyer|Process and device for the chemical digestion of cellulosic material|
    US3565687A|1968-02-26|1971-02-23|Okamura Oil Mill|Manufacturing method of xylose with cottonseed hulls as material|
    DE1950729A1|1968-10-24|1970-06-18|Forsch Die Gaerungsindustrie E|Enzymatic hydrolysis of cellulosic materials|
    CA933028A|1970-12-21|1973-09-04|Bender Frederick|Method of converting broad-leafed wood or bagasse into nutritious fodder and the nutritious fodder so produced|
    US4018620A|1975-05-19|1977-04-19|Biocel Corporation|Method of hydrolyzing cellulose to monosaccharides|DE2737118C2|1977-08-17|1989-06-15|Bau- Und Forschungsgesellschaft Thermoform Ag, Murten, Fribourg, Ch|
    DE2827388C2|1978-06-22|1982-11-11|Hans Dipl.-Ing. 7758 Meersburg Knauth|Process for the extraction of sugars from cellulose-containing raw materials|
    FR2433475B1|1978-08-16|1982-12-03|Prunet Achille|
    US4237226A|1979-02-23|1980-12-02|Trustees Of Dartmouth College|Process for pretreating cellulosic substrates and for producing sugar therefrom|
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    US4831127A|1983-07-12|1989-05-16|Sbp, Inc.|Parenchymal cell cellulose and related materials|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    AT534576A|AT350986B|1976-07-20|1976-07-20|PROCESS FOR OBTAINING GLUCOSE FROM CELLULOSIC VEGETABLE RAW MATERIALS|
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