Transportation of a Monomer Composition in a Transport Means or Pipe
    4.
    发明申请
    Transportation of a Monomer Composition in a Transport Means or Pipe 审中-公开
    在运输工具或管道中运输单体组合物

    公开(公告)号:US20100056739A1

    公开(公告)日:2010-03-04

    申请号:US12532502

    申请日:2008-03-20

    CPC classification number: C07C51/412 C07C51/50 C07C57/04

    Abstract: The invention relates to a method for the transportation of a monomer composition in which a composition comprising an aqueous solution of partially or entirely neutralized acrylic acid or overneutralized acrylic acid is placed in a transport means or sent through a pipe. The method according to the invention is characterized in that it has an increased level of safety during the transportation of acrylic acid monomers, an improved quality of the resulting product, and a high degree of efficiency. The method ensures safe transport of the highly reactive acrylic acid. The amount of polymerization inhibitors added to said acrylic acid may be reduced. An additional advantage is the minimization of the formation of dimeric acrylic acid. Tempering of containers, pipes, and pipelines may be omitted.

    Abstract translation: 本发明涉及一种运输单体组合物的方法,其中将包含部分或全部中和的丙烯酸或过度中和丙烯酸的水溶液的组合物置于运输装置中或通过管道送出。 根据本发明的方法的特征在于其在丙烯酸单体的输送过程中具有提高的安全性,所得产物的质量提高,效率高。 该方法确保高反应性丙烯酸的安全运输。 添加到所述丙烯酸中的聚合抑制剂的量可以减少。 另外的优点是最小化二聚丙烯酸的形成。 容器,管道和管道的回火可以省略。

    PROCESS FOR PREPARING AT LEAST ONE ORGANIC TARGET COMPOUND BY HETEROGENEOUSLY CATALYZED GAS PHASE PARTIAL OXIDATION
    5.
    发明申请
    PROCESS FOR PREPARING AT LEAST ONE ORGANIC TARGET COMPOUND BY HETEROGENEOUSLY CATALYZED GAS PHASE PARTIAL OXIDATION 有权
    通过异源催化气相部分氧化制备至少一种有机靶化合物的方法

    公开(公告)号:US20080260605A1

    公开(公告)日:2008-10-23

    申请号:US12146807

    申请日:2008-06-26

    CPC classification number: C07C51/252 C07C57/04

    Abstract: A process for preparing an organic target compound by heterogeneously catalyzed gas phase partial oxidation of an organic precursor compound with molecular oxygen in two oxidation reactor lines operated in parallel and removal of the target compound from the mixture of the product gas streams in a workup line, wherein the catalysts charge of one of the oxidation lines comprises a portion of catalyst over which the heterogeneously catalyzed gas phase partial oxidation has already been carried out for longer than over the portions of catalyst of the catalyst charge of the other oxidation reactor line.

    Abstract translation: 通过在两个平行操作的氧化反应器管线中的有机前体化合物与分子氧的非均相催化气相部分氧化来制备有机靶化合物的方法,并且从处理线中的产物气流的混合物中除去目标化合物, 其中氧化线之一的催化剂装料包括一部分催化剂,其上已经进行非均相催化的气相部分氧化比在另一个氧化反应器管线的催化剂装料的催化剂的部分长。

    PROCESS FOR PREPARING ACRYLIC ACID
    8.
    发明申请
    PROCESS FOR PREPARING ACRYLIC ACID 有权
    制备丙烯酸的方法

    公开(公告)号:US20080183014A1

    公开(公告)日:2008-07-31

    申请号:US12020264

    申请日:2008-01-25

    CPC classification number: C07C51/44 C07C51/48 C07C57/04

    Abstract: A process for preparing acrylic acid, in which an acrylic acid-comprising product gas mixture obtained by catalytic gas phase partial oxidation of a C3 precursor of acrylic acid is fractionally condensed in a condensation column provided with internals ascending into itself with side draw removal of crude acrylic acid and with liquid phase draw removal of acrylic acid-comprising acid water, and acrylic acid present in acid water is taken up into an extractant and then removed from the extractant and recycled into the condensation column, or taken up in aqueous metal hydroxide, or sent to further purification of the crude acrylic acid.

    Abstract translation: 制备丙烯酸的方法,其中通过丙烯酸C 3/3前体的催化气相部分氧化获得的含丙烯酸的产物气体混合物在具有内部升降的冷凝塔中分级冷凝 用丙烯酸粗抽出去除丙烯酸的酸性水,并将存在于酸性水中的丙烯酸吸收到萃取剂中,然后从萃取剂中除去并再循环到冷凝塔中, 或吸收在金属氢氧化物水溶液中,或者进一步纯化粗丙烯酸。

    Multi-tube fixed-bed reactor, especially for catalytic gas phase reactions
    9.
    发明授权
    Multi-tube fixed-bed reactor, especially for catalytic gas phase reactions 有权
    多管固定床反应器,特别适用于催化气相反应

    公开(公告)号:US07226567B1

    公开(公告)日:2007-06-05

    申请号:US09936354

    申请日:2000-03-15

    Abstract: A multitube fixed bed reactor and the use of such a reactor for carrying out catalytic gas-phase reactions, in particular for carrying out exothermic and endothermic catalytic gas-phase reactions such as the preparation of phthalic anhydride (PA), acrylic acid, methacrylic acid (MAA), acrolein, maleic anhydride (MA), glyoxal, phosgene, hydrocyanic acid or vinyl formamide (VFA). In a relatively large multitube reactor in which a large amount of heat of reaction is generated owing to the numerous catalyst tubes (17) and has to be removed, it is proposed that the ratio of tube spacing t to external tube diameter da be made dependent on the reactor diameter or on the external tube bundle diameter dRBa. At an external diameter of the catalyst tube bundle (18) of more than 4 meters, a ratio of tube spacing d to external tube diameter da of at least 1.3 is preferred.

    Abstract translation: 一种多管固定床反应器和这种反应器用于进行催化气相反应的用途,特别是用于进行放热和吸热催化气相反应,例如制备邻苯二甲酸酐(PA),丙烯酸,甲基丙烯酸 (MAA),丙烯醛,马来酸酐(MA),乙二醛,光气,氢氰酸或乙烯基甲酰胺(VFA)。 在由于多个催化剂管(17)而产生大量反应热并且必须被去除的相对大的多管反应器中,提出管间距t与外管直径d a取决于反应器直径或外管束直径d RBa。 在超过4米的催化剂管束(18)的外径处,管间距d与外管直径d的比例优选至少为1.3。

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