VERFAHREN ZUR HERSTELLUNG VON ACETYLEN UND SYNTHESEGAS

    公开(公告)号:EP2861527A1

    公开(公告)日:2015-04-22

    申请号:EP13728203.4

    申请日:2013-06-13

    申请人: BASF SE

    IPC分类号: C01B3/36 C07C2/78

    摘要: The invention relates to a method for producing acetylene and synthesis gas by partially oxidizing hydrocarbons by means of oxygen. In said method, a first input flow containing one or more hydrocarbons and a second input flow containing oxygen are preheated separately from each other, mixed at a ratio of the mass flow rate of the second input flow to the mass flow rate of the first input flow corresponding to an oxygen number λ less than or equal to 0.31, and fed via a burner block to a combustion chamber. The hydrocarbons are partially oxidized in the combustion chamber. A cracked gas is thereby obtained, which is quenched to 80 to 90 degrees Celsius downstream of the combustion chamber by injecting an aqueous quenching medium. A process water flow I
    liq and a product gas flow I
    g are obtained. The product gas flow is cooled down in a cooling column by means of direct heat exchange with cooling water in order to obtain a process water flow II
    liq as a bottom flow, a product gas flow II
    g as a top flow, and a side flow, which is depleted of soot in an electric filter. A process water flow III
    liq arises in the electric filter. The process water flows I
    liq , II
    liq , and III
    liq are merged and conducted via soot grooves having surface particle separators in order to obtain a merged process water flow IV
    liq . The method is characterized in that the merged process water flow IV
    liq is subjected to cleaning by means of partial evaporation in a single-stage flash tank, the merged process water flow IV
    liq being evaporated to a fraction of 0.01 wt% to 10 wt%, in relation to the total weight thereof, in order to obtain a cleaned process water flow V
    liq , which is recycled into the method.

    摘要翻译: 本发明涉及一种通过用氧气部分氧化烃来生产乙炔和合成气的方法。 在所述方法中,将含有一种或多种烃的第一输入流和含有氧的第二输入流彼此分开预热,以第二输入流的质量流量与第一输入的质量流量的比率 对应于小于或等于0.31的氧数λ的流动,并且经由燃烧器块供给到燃烧室。 烃在燃烧室中被部分氧化。 由此获得裂化气体,其通过注入含水淬火介质而在燃烧室的下游淬火至80至90摄氏度。 获得工艺水流I liq和产品气流I g。 产品气流在冷却塔中通过与冷却水的直接热交换而冷却,以获得作为底流的工艺水流II liq,作为顶流的产品气流II g和侧流 ,这是电除尘器中烟灰的消耗。 在电过滤器中产生工艺水流III liq。 工艺水流I liq,II liq和III liq通过具有表面颗粒分离器的烟灰槽合并并传导,以获得合并的工艺水流IV liq。 该方法的特征在于合并的工艺水流IV liq在单级闪蒸罐中通过部分蒸发进行清洁,合并的工艺水流IV liq被蒸发至0.01重量%至10重量%的分数, ,相对于其总重量,以获得再循环到该方法中的清洁的工艺水流V liq。