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    • 2. 发明申请
    • METHOD FOR THE CONTINUOUS PRODUCTION OF NITROBENZENE
    • 连续生产硝基苯的方法
    • US20150336875A9
    • 2015-11-26
    • US14046068
    • 2013-10-04
    • Bayer MaterialScience AG
    • Thomas KnaufJurgen MunnigJoerg Schmiedler
    • C07C201/08
    • C07C201/08C07C201/16C07C205/06
    • The present invention relates to a method for producing nitrobenzene, in which the waste gas streams accruing in the process and containing benzene and (traces of) nitrobenzene, possibly low- and medium-boiling components, possibly non-condensable gases and possibly water, optionally after removal of nitrogen oxides, are scrubbed in an absorption column with nitrobenzene, which comprises only very small amounts (maximum 50 ppm) of benzene and is distributed by means of a liquid distributor at a rate of 50 to 200 drip points per square metre, preferably 60 to 120 drip points per square metre, wherein (i) a liquid stream containing benzene and nitrobenzene, possibly organic low- and medium-boiling components and additionally containing sulfuric acid if sulfuric acid is used as the scrubbing agent and (ii) waste gas depleted in benzene and possibly in organic low- and medium-boiling components are obtained. A waste gas purified by the method according to the invention is particularly suitable for burning in a thermal exhaust air treatment process.
    • 本发明涉及生产硝基苯的方法,其中在该方法中产生的含有苯和(痕量)硝基苯的废气流,可能是低沸点和中沸点组分,可能是不可冷凝气体和可能的水,任选地 在除去氮氧化物之后,用硝基苯洗涤吸收塔,硝基苯仅包含极少量(最大50ppm)的苯,并以50至200滴每平方米的液滴分配器分配, 优选60至120滴/平方米,其中(i)含有苯和硝基苯的液体流,可能是有机低沸点和中沸点组分,如果使用硫酸作为洗涤剂,另外含有硫酸,和(ii)废物 获得了在苯中以及可能在有机低沸点和中沸点组分中贫化的气体。 通过根据本发明的方法净化的废气特别适用于在热排气处理过程中燃烧。
    • 6. 发明授权
    • Method for producing nitrobenzene by adiabatic nitriding
    • 通过绝热氮化生产硝基苯的方法
    • US09260377B2
    • 2016-02-16
    • US14415788
    • 2013-07-23
    • Bayer MaterialScience AG
    • Thomas KnaufMichael MerkelAntoni Mairata
    • C07C201/06C07C201/08
    • C07C201/06C07C201/08C07C205/06
    • The invention provides a continuous adiabatic process for the preparation of nitrobenzene by nitrating benzene with mixtures of sulfuric and nitric acids using a stoichiometric excess of benzene, wherein the content of organic compounds in the circulating sulfuric acid, at least during the start-up period of the production plant, is always kept below 1.0 mass percent, based on the total mass of circulating sulfuric acid. This is preferably achieved by a procedure in which, either after the end or before the beginning of a production cycle, the circulating sulfuric acid is circulated at elevated temperature so that the organics contained in the sulfuric acid, preferably comprising nitrobenzene and traces of benzene, dinitrobenzene and nitrophenols, are separated off in the evaporation apparatus for concentrating the sulfuric acid.
    • 本发明提供了一种连续的绝热方法,用于通过使用化学计量过量的苯将硫与硝酸的混合物硝化苯来制备硝基苯,其中循环硫酸中有机化合物的含量至少在启动期间 基于循环硫酸的总质量,生产厂总是保持在1.0质量%以下。 这优选通过以下程序来实现,其中,在生产周期结束或开始之前循环硫酸在升高的温度下循环,使得包含在硫酸中的有机物,优选包含硝基苯和痕量的苯, 二硝基苯和硝基苯酚在用于浓缩硫酸的蒸发装置中分离出来。
    • 7. 发明申请
    • PROCESS FOR THE PRODUCTION OF NITROBENZENE BY ADIABATIC NITRATION
    • 通过ADIABATIC NITRATION生产硝基苯的方法
    • US20150166460A1
    • 2015-06-18
    • US14415794
    • 2013-07-23
    • Bayer MaterialScience AG
    • Thomas KnaufMichael Merkel
    • C07C201/08C07C201/16
    • C07C201/08C07C201/16C07C205/06
    • The present invention provides a continuous process for the production of nitrobenzene by nitration of benzene with mixtures of sulfuric and nitric acid using a stoichiometric excess of benzene, in which the content of aliphatic organic compounds in the feed benzene during the start-up period of the production plant is always maintained at less than 1.5 wt. %, based on the total mass of the feed benzene. This is achieved either by mixing the feed benzene comprising recycled unreacted benzene (recycled benzene) and benzene newly supplied to the reaction (fresh benzene) in appropriate quantitative ratios during the start-up period, depending on the purity of the two streams, or by completely omitting the recycling of unreacted benzene during the start-up period, i.e. the feed benzene consists only of benzene newly supplied to the reaction.
    • 本发明提供了一种使用化学计量过量的苯硝化苯与硫酸和硝酸的混合物来生产硝基苯的连续方法,其中在起始时期的进料苯中的脂族有机化合物的含量 生产厂总是维持在1.5重量%以下。 %,基于进料苯的总质量。 这可以通过在启动期间将包含再循环的未反应苯(再循环苯)和新提供给反应的苯(新鲜苯)的进料苯与合适的定量比例混合,取决于两个流的纯度,或者通过 在启动期间完全省略未反应苯的再循环,即进料苯仅由新提供给反应的苯组成。
    • 9. 发明申请
    • METHOD FOR PRODUCING NITROBENZENE BY ADIABATIC NITRIDING
    • 通过自制氮化生产硝基苯的方法
    • US20150175522A1
    • 2015-06-25
    • US14415788
    • 2013-07-23
    • Bayer MaterialScience AG
    • Thomas KnaufMichael MerkelAntoni Mairata
    • C07C201/06
    • C07C201/06C07C201/08C07C205/06
    • The invention provides a continuous adiabatic process for the preparation of nitrobenzene by nitrating benzene with mixtures of sulfuric and nitric acids using a stoichiometric excess of benzene, wherein the content of organic compounds in the circulating sulfuric acid, at least during the start-up period of the production plant, is always kept below 1.0 mass percent, based on the total mass of circulating sulfuric acid. This is preferably achieved by a procedure in which, either after the end or before the beginning of a production cycle, the circulating sulfuric acid is circulated at elevated temperature so that the organics contained in the sulfuric acid, preferably comprising nitrobenzene and traces of benzene, dinitrobenzene and nitrophenols, are separated off in the evaporation apparatus for concentrating the sulfuric acid.
    • 本发明提供了一种连续的绝热方法,用于通过使用化学计量过量的苯将硫与硝酸的混合物硝化苯来制备硝基苯,其中循环硫酸中有机化合物的含量至少在启动期间 基于循环硫酸的总质量,生产厂总是保持在1.0质量%以下。 这优选通过以下程序来实现,其中,在生产周期结束或开始之前循环硫酸在升高的温度下循环,使得包含在硫酸中的有机物,优选包含硝基苯和痕量的苯, 二硝基苯和硝基苯酚在用于浓缩硫酸的蒸发装置中分离出来。