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    • 15. 发明授权
    • Process for the purification of high-melting organic products
    • 纯化高熔点有机产品的方法
    • US4141799A
    • 1979-02-27
    • US824198
    • 1977-08-12
    • Bernd ThelenHans-Walter BrandtWolfgang AugeKarl-Werner Thiem
    • Bernd ThelenHans-Walter BrandtWolfgang AugeKarl-Werner Thiem
    • C07C46/10B01D20060101B01D1/22B01D3/00B01D3/14C07B31/00C07B63/00C07C45/00C07C50/18C07C50/20C07C50/34C07C67/00C07C201/00C07C205/47C07C225/34
    • The purification of high-melting organic products, such an anthraquinone and substituted anthraquinones, which is substantially free from lower-boiling impurities, by melting the product to be purified by heating, while mechanically conveying the same along a path with a screw conveyer, as for example, in a melting screw; degassing the melt at a reduced pressure in a column, as for example, at a pressure of 50 to 400 mm Hg; passing the degassed melt through a thin film evaporator at a reduced pressure of, for example, 5 to 250 mm Hg to evaporate the high-melting organic product and discharging the remaining high-boiling impurities and such impurities which are not capable of being distilled from the evaporator through a conically tapering sump, while mechanically scraping residue from the sump wall, preferably with the use of a rotating helical screw in the sump; the discharge from the sump being effected into and through an enclosed path at a rate sufficient to prevent liquid accumulating in the sump, while maintaining the central portion of the enclosed discharge path at a lower temperature than its end portion to form a crystal sludge in the central portion, which acts as a pressure seal; and solidifying and recovering the product discharging from the enclosed path. The enclosed path is preferably established through a screw-type pump which feeds into a crystallizing screw where the solidification takes place, the crystallizing screw being preferably maintained above the screw-type pump and is maintained filled with an amount of sump product which approximately corresponds to the amount of product in the sump take-off screw. The vapors produced in the thin film evaporator are passed via a heated rectifying column into a condenser, and a portion of the condensate is passed to the column as a reflux and another portion taken off and solidified in a crystallizing screw.
    • 通过将通过加热净化的产品熔化,同时用螺旋输送机沿着路径机械地输送,从而净化基本上不含低沸点杂质的高熔点有机产物,例如蒽醌和取代的蒽醌,作为 例如,在熔化螺杆中; 例如在压力为50至400mm Hg的柱中,在减压下对熔体进行脱气; 将脱气的熔体通过薄膜蒸发器在例如5至250mm Hg的减压下通过,以蒸发高熔点有机产物并排出不能从蒸馏出的剩余的高沸点杂质和这些杂质 蒸发器通过锥形锥形槽,同时机械地刮擦来自贮槽壁的残留物,优选地使用在贮槽中的旋转螺旋螺杆; 从贮槽中的排放物以足以防止液体积聚在贮槽中的速率进入并通过封闭路径,同时将封闭排放路径的中心部分保持在比其端部部分更低的温度,以在其中形成结晶污泥 中心部分,用作压力密封; 并固化并回收从封闭路径排放的产品。 封闭路径优选通过螺旋式泵来建立,所述螺旋式泵进料到结晶螺杆中,其中发生固化,结晶螺杆优选地保持在螺旋式泵上方,并且保持充满一定量的贮槽产品,其大致对应于 产品的数量在油底壳起飞螺丝中。 在薄膜蒸发器中产生的蒸汽通过加热的精馏塔进入冷凝器,一部分冷凝物作为回流通入塔中,另一部分在结晶螺杆中脱去固化。
    • 16. 发明授权
    • Process for the preparation of mononitro-aromatic compounds
    • 制备单硝基芳族化合物的方法
    • US4112005A
    • 1978-09-05
    • US795249
    • 1977-05-09
    • Karl-Werner ThiemAdolf HamersJosef Heinen
    • Karl-Werner ThiemAdolf HamersJosef Heinen
    • C07C67/00C07C201/00C07C201/08C07C205/06C07C205/12C07C79/10C07C79/12
    • C07C201/08Y02P20/582
    • The present invention relates to an improved continuous process for the preparation of mononitro-aromatic compounds which comprises (1) nitrating a reactive aromatic compound in the absence of sulphuric acid until mono-nitration is essentially complete, said nitration being carried out in 40 to 68% strength by weight nitric acid, (2) separating mechanically the nitration reaction mixture into an inorganic phase and an organic phase, (3) washing of the organic phase with water and dilute alkali solution and subsequent separation of the unconverted starting material end of the adhering water by means of rectification (4) feeding the inorganic phase and, if necessary, the wash water of the first water wash of the organic phase, to a rectification column in which (a) water is withdrawn over the top (b) optionally a fraction which has a lower nitric acid content than the feed is withdrawn from a sidestream takeoff in the rectifying section of the column and (c) a fraction which has a higher nitric acid content than the feed is taken off from the sump, (5) recycling said material withdrawn from the sump of the column to the nitration reaction vessel with the addition of fresh concentrated nitric acid and (6) withdrawing from the system an amount of the top product from the column which corresponds to the water of reaction and that which enters with the nitric acid that is added.
    • 本发明涉及一种用于制备单硝基芳族化合物的改进的连续方法,其包括(1)在不存在硫酸的情况下硝化反应性芳族化合物直到单硝化基本上完成,所述硝化在40至68 硝酸重量%,(2)将硝化反应混合物机械分离成无机相和有机相,(3)用水和稀碱溶液洗涤有机相,随后将未转化的原料末端分离 通过精馏(4)将无机相和必要时将有机相的第一次水洗涤的洗涤水进料到精馏塔(1)将顶部(b)中的水排出任选地 硝酸含量低于进料的馏分从柱的精馏段的侧流起飞中取出,(c)馏分具有较高的馏分 硝酸含量比原料从油底壳中取出,(5)加入新鲜的浓硝酸使从塔的集油槽抽出的物料回收到硝化反应容器,(6)从系统中取出一定量的 对应于反应水的塔的顶部产物和加入的硝酸进入的顶部产物。