PROCESS FOR ADIABATIC PRODUCTION OF MONONITROTOLUENE
    152.
    发明申请
    PROCESS FOR ADIABATIC PRODUCTION OF MONONITROTOLUENE 有权
    用于生产单硝基苯的方法

    公开(公告)号:US20130253233A1

    公开(公告)日:2013-09-26

    申请号:US13427688

    申请日:2012-03-22

    Inventor: Michael Gattrell

    CPC classification number: C07C201/08 C07C205/06

    Abstract: A process for continuous adiabatic nitration of toluene to mononitrotoluene (MNT). The process yields a product quality of MNT that is comparable to that obtained by isothermal production. The process uses excess toluene, with the reaction rate being controlled to maintain a residual of 0.003-0.102 wt % nitric acid in the spent acid and an orange to red color of the spent acid. Further process conditions include re-concentrated sulfuric acid at 83 to 99 degrees C. with a concentration of sulfuric acid from 66 to 70.5 wt %. This is mixed with nitric acid to generate a mixed acid with 1.0 to 3.8 wt % nitric acid and toluene is added at a rate of 1.1 to 1.71 moles toluene/mole nitric acid. The reactants are mixed in a reactor with an overall average mixing intensity of 5.8 to 19 W/kg of contained solution.

    Abstract translation: 将甲苯连续绝热硝化成单硝基甲苯(MNT)的方法。 该方法产生与通过等温生产获得的MNT相当的MNT的产品质量。 该方法使用过量的甲苯,控制反应速率以维持废酸中的0.003-0.102重量%的硝酸残留量和废酸的橙色至红色。 进一步的工艺条件包括在83至99℃下的浓硫酸,浓度为66至70.5重量%的硫酸。 将其与硝酸混合以产生具有1.0至3.8重量%硝酸的混合酸,并以1.1至1.71摩尔甲苯/摩尔硝酸的速率加入甲苯。 反应物在反应器中混合,总体平均混合强度为5.8至19W / kg的所含溶液。

    REMOVAL OF NON-AROMATIC IMPURITIES FROM A NITRATION PROCESS
    154.
    发明申请
    REMOVAL OF NON-AROMATIC IMPURITIES FROM A NITRATION PROCESS 有权
    从硝化过程中去除非芳香污染物

    公开(公告)号:US20130018210A1

    公开(公告)日:2013-01-17

    申请号:US13636478

    申请日:2011-02-17

    CPC classification number: C07C201/16 Y02P20/582 C07C205/06 C07C205/12

    Abstract: A method and apparatus for removing non-aromatic impurities from non-nitrated aromatic reactant in a nitration production process, in which process an aromatic reactant is nitrated (100) to produce a nitrated aromatic product using a molar excess of the aromatic reactant, and non-nitrated aromatic reactant is recovered (102) from the produced nitrated aromatic product and is recycled (104) for use in the nitration production process. A portion of the removed excess non-nitrated aromatic reactant is diverted (106) and subjected to nitration (108). The nitrated stream may be further processed by separating out the spent acids (110) and the non-aromatic impurities (116). These streams may be sent (114, 118) to a suitable location in the nitration production train.

    Abstract translation: 一种用于在硝化生产过程中从非硝化芳族反应物除去非芳族杂质的方法和装置,其中芳族反应物被硝化(100)以产生使用摩尔过量的芳族反应物的硝化芳族产物, 硝酸芳香族反应物(102)从所生产的硝化芳香族产物中回收(102)并循环使用(104),用于硝化生产过程。 去除的过量非硝化芳族反应物的一部分被转移(106)并进行硝化(108)。 可以通过分离废酸(110)和非芳族杂质(116)来进一步处理硝化物流。 这些流可以被发送(114,118)到硝化生产列车中的合适位置。

    PROCESS FOR THE SYNTHESIS OF DIHALODINITROTOLUENE
    155.
    发明申请
    PROCESS FOR THE SYNTHESIS OF DIHALODINITROTOLUENE 失效
    二羟基二苯并呋喃合成方法

    公开(公告)号:US20100160695A1

    公开(公告)日:2010-06-24

    申请号:US12634772

    申请日:2009-12-10

    CPC classification number: C07C201/08 C07C205/12

    Abstract: An improved process is provided for the preparation of 2,6-dihalo-3,5-dinitrotoluene by the nitration of 2,6-dihalotoluene. The direct isolation of highly pure 2,6-dihalo-3,5-dinitrotoluene is accomplished without a water or ice quench, by providing at least one equivalent of SO3 during the reaction, slow crystallization, and isolation of product from a cold crystal slurry.

    Abstract translation: 提供了通过2,6-二卤代甲苯硝化制备2,6-二卤代-3,5-二硝基甲苯的改进方法。 通过在反应期间提供至少一当量的SO 3,缓慢结晶并从冷结晶浆中分离产物,直接分离高纯度的2,6-二卤代-3,5-二硝基甲苯,无需水或冰骤冷 。

    Process for producing 2,5-bis(trifluoromethyl)nitrobenzene
    156.
    发明授权
    Process for producing 2,5-bis(trifluoromethyl)nitrobenzene 有权
    制备2,5-双(三氟甲基)硝基苯的方法

    公开(公告)号:US06930214B2

    公开(公告)日:2005-08-16

    申请号:US10883820

    申请日:2004-07-06

    Applicant: Tamaki Shimizu

    Inventor: Tamaki Shimizu

    CPC classification number: C07J75/00 C07C201/08 C07J73/00 C07C205/11

    Abstract: A process to produce 2,5-bis(trifluoromethyl)nitrobenzene in a high yield from an industrially easily available material by using a substance with which the reaction operation is simple and handling is easy, with a small number of steps under moderate reaction conditions, is provided. 1,4-bis(trifluoromethyl)benzene is nitrated by means of nitric acid in a solvent comprising as an essential component an acid selected from sulfuric acid having a sulfuric acid concentration of from 91 to 100 mass % and fuming sulfuric acid having a sulfur trioxide concentration of higher than 0 mass % and at most 20 mass %.

    Abstract translation: 通过使用反应操作简单并且处理容易的物质,在中等反应条件下以少量的步骤从工业上容易获得的材料中以高产率制备2,5-双(三氟甲基)硝基苯的方法, 被提供。 1,4-二(三氟甲基)苯通过硝酸在含有选自硫酸浓度为91〜100质量%的硫酸和三氧化硫的发烟硫酸作为必需成分的溶剂中进行硝化 浓度高于0质量%,最多为20质量%。

    Continuous process for the dinitration of aromatic substrates
    160.
    发明授权
    Continuous process for the dinitration of aromatic substrates 失效
    芳香底物二硝化的连续工艺

    公开(公告)号:US5907062A

    公开(公告)日:1999-05-25

    申请号:US974104

    申请日:1997-11-19

    CPC classification number: C07C209/76

    Abstract: A continuous process for the dinitration of alkyl-substituted derivatives of phenol and aniline, using nitric acid substantially free of sulphuric acid, characterized in which the dinitration is conducted in a single step in a tubular reactor in the presence of a catalytically-effective amount of a catalyst capable of reacting with the nitric acid to form nitrous acid in situ.

    Abstract translation: 使用基本上不含硫酸的硝酸对苯酚和苯胺的烷基取代的衍生物进行二硝化的连续方法,其特征在于在催化有效量的条件下,在管式反应器中,在一个步骤中进行二硝化反应 能够与硝酸反应以在原位形成亚硝酸的催化剂。

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