• 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:
    METHOD FOR OBTAINING FURFUROL by hydrolyzing pentosan-containing plant raw materials in the presence of concentrated strong mineral acid followed by dehydration of the resulting solution of pentose by steam treatment in the presence of strong mineral acid in the second reactor, characterized in that, in order to simplify the process and increase the yield of the target product , volatile acid is used as a strong mineral acid, and hydrolysis of pentosan-containing plant materials is carried out at 60 ° C and atmospheric pressure. and, the dehydration of the resulting solution of pentose is carried out at 100-110 ° C and atmospheric pressure, the solution of pentose is supplied from above and the steam is fed from below with subsequent condensation of steam containing furfural, decantation and separation of liquid furfural, concentrated ( L volatile strong mineral acid is recycled to the first reactor 2. POP method 1, characterized in that 5-6 hours of saline acid azeotropic concentration of 20% is used.
    公开号:SU1176840A3
    申请号:SU813273771
    申请日:1981-04-02
    公开日:1985-08-30
    发明作者:Пьер Мари Раймон Бернар
    申请人:Бертен Э Ко (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to methods for producing furfural from a pentosan-containing raw material, which can be used in the production of synthetic textile fibers, plastic, synthetic rubber.
    The purpose of the invention is to simplify the process and increase the yield of the target product.
    Example. To produce 5,000 tons per year of furfural, 35,000 tons per year of corn cobs with a moisture content of 30% (or substances with a high content of pentosans and lower humidity), i.e., are needed. dry matter weight 25,000 tons per year, of the following composition,%: pentosans 32; cellulose 50; lignin 18.
    The 40-meter hydroliser was loaded with corn cobs at the rate of 3.12 tons / h of dry matter and 20% hydrochloric acid with a temperature of 60 ° C at the rate of 9.36 m / h. The feed rate of the hydrolyzate solution at the outlet of the hydrolyzer is 6.55 n 1 h, the concentration of pentoses in the hydrolyzate is 150 g / l.
    The hydrolyzate solution containing 150 g / l of pentose enters the furfural formation column with a volume of 14 m at a speed of 6.55. Steam at 110 ° and a pressure of 1.3 bar is served at a rate of 1.5 t / h. The vapor with furfural that leaves the column is condensed in a condenser, and a water-furfural mixture is obtained with 95% by weight of furfural (8 g / l pennant content. Under these conditions, the recirculation pump delivers the solution to the boiler at a rate of 27 m / h
    Acid hydrolysis regeneration, i.e. Hydrochloric acid, at the exit from the column, the formation of furfural and before its return to the hydrolyzer are carried out in a distillation column, for example a plate-shaped one. The column receives a solution of hydrochloric acid, obtained after extraction of plant residues after leaving the hydrolyzer at a rate of 3.46 t / h of P3% hydrochloric acid) and after the formation of furfural at a rate of 8.56 t / h (l7% by hydrochloric acid). on acid), i.e. on average, 15.8% of NSV at a speed of 12 t / h. From the bottom of the column, the regenerated 20% azeotropic hydrochloric acid is withdrawn at a rate of 9.3 t / h.
    The rate of release of residual water from the top of the column is 2.42 t / h, and the rate of contaminants from the bottom of the column is 0.3 t / h.
    The loss of hydrochloric acid is 1% with respect to the acid loaded, or based on a plant with a capacity of 5000 tons per year at a furfural formation level of 0.014. t / h, and at the level of removal of contaminants 0.06 t / h, i.e. 0.4 t / h furfural.
    A mixture containing 95% by weight of furfural is sent after decantation in a settling tank and neutralized in a reactor with a loading rate of 0.67 t / h in a dehydration column under a pressure of 100 mm Hg. to obtain, on the exit from the column, after separation of approximately 0.04 ton / h of furfural water of purity 99% by weight at a yield rate of 0.65 ton / h. Get 99% furfural in the amount of 625 kg / h. Yield 85%.
    The total consumption of water vapor is 7 t / h, the total consumption of water is 185 m / h.
    Burning 2.12 t / h (calculated on the dry matter of plant residues obtained from the hydrolyser, with a caloric content of 3400 kcal / kg, gives 7200 termi / h 7200-10. Cal / h) or 11 t / h of steam, therefore, steam much more is obtained than is required for installation (approximately 7 t / h.
    The effect of temperature on the reaction rate of the hydrolysis of pentosans to pentoses was established by studying the change in the concentration of pentose in a closed hydrolysis reactor depending on the duration at different temperatures.
    The conditions of the experiments are presented in the table ..
    The chemical equilibrium in the system of pentosan — pentose slows down the rate of hydrolysis and impedes the achievement of the maximum concentration of pentose in a closed reactor.
    At 60 ° C and a hydrolysis duration of about 5 hours, a decomposition reaction is observed. The enthalpy of the hydrolysis reaction is H 15.5 kcal / mol.
    Studies have shown that the yield of furfural increases depending on the length of stay of hydrolysis in the furfural formation column (the optimal time is
    11768404
    furfural formation rates, i.e. Thus, the proposed method, when too long, allows the process to be simplified. As a result, the hydrolyzate in the process column at atmospheres (for more than 2 hours) will decrease the yield of furfural and increase the yield of the target product from 68 to 85%.
    cure The temperature of dehydration pentoe 100-110 C. Used corn cobs, dried in the Mush: composeicin: II sec.Z moisture, density 160 kg / n, the content of pentosan 38 wt.%. .
    权利要求:
    Claims (2)
    [1]
    METHOD FOR PRODUCING FURFUROL by hydrolysis of a pentosan-containing plant material in the presence of concentrated strong mineral acid followed by dehydration, the resulting pentose solution by steam treatment in the presence of strong mineral acid in the second reactor, characterized in that, in order to simplify the process and increase the yield of the target product, as volatile acid using volatile acid and the hydrolysis of pentosan-containing plant materials is carried out at 60 ° C and atmospheric pressure, and hydration of the resulting solution · pentosis is carried out at 100-110 ° C and atmospheric pressure, and the pentosis solution is supplied from above, and the steam is supplied from below, followed by condensation of the steam containing furfural, decantation and separation of liquid furfural <0, concentrated volatile strong mineral acid recycle to the first reactor.
    [2]
    2. The method according to claim 1, characterized in that they use 5-6 hours. hydrochloric acid of an azeotropic concentration of 202.
    SU „, .1176840>
    类似技术:
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    同族专利:
    公开号 | 公开日
    BR8008782A|1981-05-26|
    DE3068793D1|1984-09-06|
    HU185421B|1985-02-28|
    JPS56501046A|1981-07-30|
    US4366322A|1982-12-28|
    FR2462433A1|1981-02-13|
    EP0033323A1|1981-08-12|
    WO1981000407A1|1981-02-19|
    EP0033323B1|1984-08-01|
    IN153609B|1984-07-28|
    引用文献:
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    AT387408B|1987-05-12|1989-01-25|Voest Alpine Ind Anlagen|COMBINED METHOD FOR THE THERMAL AND CHEMICAL TREATMENT OF BIOMASS CONTAINING LIGNOCELLULOSE AND FOR THE EXTRACTION OF FURFURAL|
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    US5559031A|1987-08-12|1996-09-24|Technipetrol S.P.A.|Apparatus for the continuous production of ethanol from cereals|
    DE19905655A1|1999-02-11|2000-08-17|Karl Zeitsch|Process for the production of furfural by delayed relaxation|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7919935A|FR2462433A1|1979-08-03|1979-08-03|IMPROVEMENTS IN PROCESSES AND EQUIPMENT FOR OBTAINING FURFURAL FROM PLANT MATERIALS|
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