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Process for the catalytic oxidation of sulfur, nitrogen and unsaturated compounds from hydrocarbon streams.

机译:从烃流中催化氧化硫,氮和不饱和化合物的方法。

摘要

A process for the catalytic oxidation and extraction or removal of sulfur compounds, nitrogen and unsaturated hydrocarbon fossil streams contaminated with said compounds, the process comprising the following steps: a) providing an iron oxide pulverized raw; b) providing at least one acid; c) providing at least one peroxide; d) oxidizing unsaturated compounds as well as sulfur contaminants and nitrogen by mixing, at atmospheric pressure and a temperature equal to or higher than room temperature, with agitation, said acid and said hydrocarbon stream contaminated with sulfur compounds, nitrogen and unsaturated and said peroxide to obtain a peracid, the molar amount of peroxide and acid relative to the sum of contents of nitrogen and sulfur present in the hydrocarbon stream at least 3, 0, at pH 2, 0 and 6, 0, during the period required to obtain a hydrocarbon stream where sulfur and nitrogen contaminants have been partially oxidized insaturadosde; e) further oxidizing said unsaturated ao compounds and sulfur contaminants and nitrogen in the presence of oxidizing hydroxyl radicals generated by adding, at atmospheric pressure and a temperature greater than ambient temperature, giving rise to the temperature higher than the ambient temperature by itself process, with stirring, a catalytic amount of said pulverized iron oxide to obtain a slurry of iron oxide, hydrocarbon stream and unsaturated compounds, sulfur and nitrogen oxidized, reaction conditions being maintained for 1-2 hours and at a pH acid from 2 0 to 6, 0; f) after the end of the reaction, filter the reaction medium containing an aqueous phase and an oily hydrocarbon phase, and separating the catalyst from spent iron oxide; g) decanting to separate the aqueous phase rich in organic compounds.
机译:一种催化氧化和萃取或去除被所述化合物污染的硫化合物,氮和不饱和烃化石流的方法,该方法包括以下步骤:a)提供氧化铁粉状原料; b)提供至少一种酸; c)提供至少一种过氧化物; d)通过在大气压和等于或高于室温的温度下搅拌混合氧化所述不饱和化合物以及硫污染物和氮,所述酸和所述烃流被硫化合物,氮和不饱和污染物以及所述过氧化物污染。获得过酸,在获得烃所需的时间段内,过氧化物和酸的摩尔量相对于烃物流中存在的氮和硫的含量之和至少为3、0,pH为2、0和6、0硫和氮污染物被饱和氧化的部分氧化的物流; e)在存在氧化的羟基自由基的情况下,进一步氧化所述不饱和的ao化合物和硫污染物以及氮,所述氧化的羟基自由基是通过在大气压力和高于环境温度的温度下添加而产生的,该温度通过自身的方法升高到高于环境温度搅拌下,将催化量的所述粉碎的氧化铁制得氧化铁,烃物流和不饱和化合物的浆液,将硫和氮氧化,将反应条件保持1-2小时并在pH值为2 0至6、0、0的条件下进行。 ; f)反应结束后,过滤包含水相和油性烃相的反应介质,并将催化剂与废氧化铁分离; g)倾析以分离出富含有机化合物的水相。

著录项

  • 公开/公告号ES2274970T3

    专利类型

  • 公开/公告日2007-06-01

    原文格式PDF

  • 申请/专利权人 PETROLEO BRASILEIRO S.A. - PETROBRAS;

    申请/专利号ES20020721879T

  • 发明设计人 DE SOUZA WLADIMIR FERRAZ;

    申请日2002-05-03

  • 分类号B01J23/94;C10G1;B01J23/745;B01J38;C10G27;C10G27/04;C10G27/12;C10G53/14;

  • 国家 ES

  • 入库时间 2022-08-21 20:54:31

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