• 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 method for continuous saccharification of plant raw material by feeding the raw material as such or prehydrolyzed and a dilute sulphuric acid solution into a flow reactor in order to hydrolyze the raw material under pressure and at a high temperature, discharging dry solids and liquid from the reactor by expansion and separating liquid and solids, wherein the raw material and sulfuric acid solution are led through the reactor at equal rate, which is the same as required by the more easily hydrolyzable particles of the raw material, the solids and liquid together are discharged into the same blow tank and at least part of the separated coarse solid is returned into the reactor.
    公开号:SU1410867A3
    申请号:SU803217964
    申请日:1980-12-17
    公开日:1988-07-15
    发明作者:Илмари Нуутипила Антти；Йюхани Похела Вейко
    申请人:Ой Тампелла Аб. (Фирма)；
    IPC主号:
    专利说明:

    sc
    Od


    s
    The invention relates to chemical technology, specifically to a method for the hydrolysis of cellulose-containing materials, and can be used to produce monosaccharides.
    The purpose of the invention is to simplify the process of hydrolysis of cellulose-containing materials.
    Example 1. Pre-untreated starting material — sawdust obtained from soft wood species — is hydrolyzed in a tubular reactor with a solution of sulfuric acid at a concentration of 0.25 wt.% With simultaneous feeding of sawdust and acid at one rate and with a ratio between liquid and solid. material 2.5, and the highest yield of glucose is obtained when the reaction time is 20 minutes. The yield of glucose is 38% of the cellulose contained in the starting material, taking into account losses due to washing once with water the residue after hydrolysis. The glucose concentration is 100 g / l.
    In the case of sawdust derived from soft wood species, pre-hydrolyzed, the glucose yield is 46.4% of the cellulose contained in the starting material.
    PRI mme R 2. Pre-hydrolyzed wheat straw is continuously hydrolyzed in accordance with Example 1 by recycling the mass of the unloaded unreacted residue. The yield of glucose increases with increasing recycle rate. The parameters for maximizing glucose yield are shown in Table 1.
    Temperature, from 170 180 190 200 210 220 Sulfuric acid, weight
    2.0 1.0 0.5 0.25 0.15 0.1
    Example 5. Pre-hydrolyzed sawdust wood
    Table 1
    five
    0
    0
    five
    0 5
    With respect to the pulp contained in the starting material. Example 3 Coniferous wood sawdust is hydrolyzed in the tubular reactor of Example 1. The reaction mixture is discharged after 5 minutes with continuous purging. The residue is subjected to similar processing (5 min hydrolysis h purge). The operation is repeated for each new residue. After each cycle, the particle size is determined. The average particle size of the material has been found to decrease with an increase in the number of treatments.
    Example 4. Pre-hydrolyzed softwood sawdust is hydrolyzed in a tubular reactor at a ratio of solids and liquid 2.5 and simultaneous feeding of reactants at the same rate by changing the reaction time and the concentration of sulfuric acid at a constant reaction time of 17 min It has been established that a glucose yield of 45% by weight is achieved when the temperature rises by 10 ° C is accompanied by a decrease in the concentration of sulfuric acid to half. . The results are presented in table 2.
    table 2
    softwoods are hydrolyzed in a tubular reactor while being fed. reagents with. same speed. The ratio of the liquid to the intermediate particles at the inlet of the reactor varies from 1 to 5. The rate of hydrolysis does not depend on the ratio of solid particles and the liquid when the ratio is above 1.5. These dependences of the rate of hydrolysis on the ratio of liquid and solid particles are presented in Table 3.
    Table3
    The ratio of liquid - the rate of hydro and solid particles of lysis, min

    0.063
    0.077
    0.0871
    0.082
    0.082
    0.083
    0.082
    When the hydrolysis process is carried out in a known manner, the source material is treated with a countercurrent method in several stages without separating the solid particles into fractions, which requires the use of sophisticated equipment and makes it difficult to control the process.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    The method of pvdrolizatsiya cellulose containing; their materials, including the processing of the source material with a dilute solution of sulfuric acid and the isolation of the products of hydrolysis of unhydrogenated material, characterized in that, in order to simplify the process, the source material and the solution of sulfuric acid are fed to the hydrolysis simultaneously at different rates and the treatment is carried out at 170-220 With a 0.1-2.0% solution of sulfuric acid for 6-20 minutes with a ratio of a solution of sulfuric acid and the starting material 1.0-5.0, and the unhydrogenated material in an amount of 58 -88% return to the stage of hydrolysis.
    类似技术:
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    同族专利:
    公开号 | 公开日
    IT1147074B|1986-11-19|
    US4432805A|1984-02-21|
    FI58346B|1980-09-30|
    PH16318A|1983-09-05|
    CH645131A5|1984-09-14|
    AU6469380A|1981-06-25|
    HU182261B|1983-12-28|
    NO803781L|1981-06-19|
    ZA807403B|1981-11-25|
    PL131403B1|1984-11-30|
    NZ195602A|1983-06-14|
    DE3047049C2|1986-06-26|
    PL228532A1|1981-08-07|
    CA1173825A|1984-09-04|
    FI58346C|1981-01-12|
    DE3047049A1|1981-09-03|
    JPS5692800A|1981-07-27|
    JPS6144479B2|1986-10-02|
    NO154605C|1986-11-12|
    DD155430A1|1982-06-09|
    AT373282B|1984-01-10|
    BR8008207A|1981-06-30|
    FR2472016B1|1984-10-05|
    AR223084A1|1981-07-15|
    CS226726B2|1984-04-16|
    YU317680A|1984-02-29|
    SE451331B|1987-09-28|
    IT8050392D0|1980-12-17|
    ATA616280A|1983-05-15|
    DK534880A|1981-06-19|
    SE8008673L|1981-06-19|
    NO154605B|1986-08-04|
    FR2472016A1|1981-06-26|
    AU542966B2|1985-03-28|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI793963A|FI58346C|1979-12-18|1979-12-18|FOERFARANDE FOER KONTINUERLIG FOERSOCKRING AV CELLULOSA AV VAEXTMATERIAL|
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