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    • 1. 发明申请
    • METHOD OF PROCESSING OF LIGNOCELLULOSE MATERIALS BY CONTINUOUS PRESSURE HYDROLYSIS AND CORRESPONDING EQUIPMENT
    • 连续压力水解和相关设备处理纤维素材料的方法
    • WO1996025553A1
    • 1996-08-22
    • PCT/CZ1996000005
    • 1996-02-01
    • F + S MARKET, SPOL. S.R.O.KRATOCHVIL, Zdenek, Sr.ROUS¿AR, IvoMACHEK, Frantis¿ekKRATOCHVIL, Zdenek, Jr.
    • F + S MARKET, SPOL. S.R.O.
    • D21C11/00
    • D21C11/0007C07D307/50D21C3/04
    • The invention relates to a method and an equipment for the processing of lignocellulose materials by continuous pressure hydrolysis, optionally in the presence of inorganic acid, by consequent expansion and separation of the hydrolysate and gaseous phase, wherein disintegrated raw material is wetted (50, 52, 67, 69) by pressure water of the temperature 170 to 200 DEG C at the ratio water to dry matter 0.5 to 1:1, from the mixture obtained excessive water is removed by pressing (51) to the ratio of dry matter to water 1:0.3 to 0.5, consequently with simultaneous feed of pressure water of the temperature 170 to 200 DEG C in the ratio to dry matter 1:2.5 to 4 it is hydrolysed at the temperature 160 to 230 DEG C and pressure 0.6 to 2.8 MPa for 3 to 18 minutes, while hydrolysis proceeds with simultaneous uniform advancement (54) of solid and liquid phases, after termination of hydrolysis the material is expanded in two stages (56, 57) giving rise to gaseous phase (2, 3) and hydrolysate (62), gaseous phase contains furfural, methanol and acetic acid, hydrolysate contains cellulose, lignin and water, gaseous phase is rectified (59) and separated to furfural (7) mixture and mixture of acetic acid, formic acid and water (8), water is removed from hydrolysate by pressing (64) and solid remnant (11) is extracted (66) by solvent from group formed by ethanol or acetone, lignin is extracted to the solvent and after evaporation of the solvent reactive lignin is obtained, cellulose remains in solid phase, furfural obtained from the gaseous phase is purified by other distillation and pure furfural may be further treated to furane.
    • 本发明涉及一种用于通过连续压力水解,任选地在无机酸存在下处理木质纤维素材料的方法和设备,通过随后的水解产物和气相的膨胀和分离,其中分解的原料被润湿(50,52 ,67,69),通过温度为170〜200℃的压力水,水与干物质的比例为0.5〜1:1,从得到的混合物中通过按压(51)除去干物质与水的比例 1:0.3至0.5,因此,与干物质比1:2.5至4同时进料温度为170至200℃的压力水,在160-230℃和0.6至2.8MPa的温度下水解,压力为0.6至2.8MPa, 3至18分钟,同时水解进行同时均匀提前(54)固相和液相,水解终止后,材料在两个阶段(56,57)中膨胀,产生气相(2,3)和水解产物 62) ,气相含有糠醛,甲醇和乙酸,水解产物含有纤维素,木质素和水,气相精馏(59)并分离成糠醛(7)乙酸,甲酸和水(8)的混合物,水分为 通过压榨(64)从水解产物中除去固体残余物(11),由乙醇或丙酮形成的基团的溶剂提取(66),将木质素萃取到溶剂中,蒸发溶剂后,纤维素保留在固体中 从气相获得的相,糠醛通过其他蒸馏进行纯化,纯糠醛可进一步处理成呋喃。