会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明公开
    • PROCESS FOR THE PRODUCTION OF SYNTHESIS GAS AND HYDROGEN STARTING FROM LIQUID OR GASEOUS HYDROCARBONS
    • 工艺生产合成气和氢气起价液态或气态碳氢化合物
    • EP2238073A1
    • 2010-10-13
    • EP08852817.9
    • 2008-11-17
    • ENI S.p.A.
    • BASINI, LucaGUARINONI, AlessandraLAINATI, Andrea
    • C01B3/38C01B3/48B01J8/04B01J19/26
    • C01B3/386B01J4/002B01J8/0453B01J8/0492B01J8/0496B01J2208/00495B01J2219/185B01J2219/1946C01B3/48C01B2203/0233C01B2203/0238C01B2203/0261C01B2203/0283C01B2203/085C01B2203/0872C01B2203/1023C01B2203/1029C01B2203/1035C01B2203/1047C01B2203/1052C01B2203/1058C01B2203/1064C01B2203/107C01B2203/1247C01B2203/1252C01B2203/1276C01B2203/1288C01B2203/143C01B2203/82Y02P20/142
    • A process is described for producing synthesis gas and hydrogen starting from liquid hydrocarbon feedstocks, possibly also mixed with gaseous hydrocarbon streams, comprising at least the following operations: 1) nebulizing/vaporizing a stream of a liquid hydrocarbon feedstock consisting of one or more of the following hydrocarbons: naphthas, various kinds of gas oils, such as LCO, HCO and VGO, other products of refining cycles and oil up-grading, such as DAO, other heavy residues, at a N temperature ranging from 50 to 500° C. and a pressure of 2 to 50 atm, the nebulization also being effected with the help of a gaseous propellant, possibly with the addition of CO2, selected from vapour and/or a gaseous hydrocarbon and resulting in the formation of a nebulized/vaporized liquid hydrocarbon stream; 2) mixing the nebulized/vaporized liquid hydrocarbon stream coming from phase 1) with: a) an oxidizing stream, possibly mixed with vapour, b) possibly a gaseous hydrocarbon stream at a temperature ranging from 50 to 500° C. and a pressure of 2 to 50 atm, with the formation of a possibly biphasic liquid-gas reaction mixture; 3) passing the reaction mixture coming from phase 2) through at least a first structured catalytic bed with the formation of a mixture of reaction products comprising H2 and CO, said structured catalytic bed comprising a catalytic partial oxidation catalyst, arranged on one or more layers, the reaction mixture flowing through each of the layers with a contact time varying from 0.01 to 100 ms, preferably from 0.1 to 10 ms; 4) cooling the mixture of reaction products coming from phase 3). The relative equipment for effecting said process is also described.
    • 的方法描述了一种用于生产合成气和氢气从液体烃原料,因此可能与气态烃料流混合开始,包括至少以下操作:1)雾化/蒸发液体烃原料的由一个或多个的流 以下烃:石脑油,各种类型的瓦斯油,:如LCO,HCO和VGO,精炼周期和油向上分级,颜色等产品的:如DAO,其它重质残渣,在N个温度范围为50至500℃ 和的2〜50个大气压的压力下,雾化因此被实现与气态推进剂的帮助下,可能添加的CO 2,从蒸汽和/或气体烃和在雾化/蒸发的液体烃的形成而产生选择 流; 2)混合的雾化/蒸发的液体烃从阶段1来)与物流:a)至氧化流,可能与蒸汽混合,b)中可能在范围从50至500℃的温度下的气态烃料流和压力 2至50个大气压,具有可能的双相液气的反应混合物的形成; 3)通过至少一个第一结构化催化床使从第2阶段来)的反应混合物与反应产物包括H 2和CO的混合物的形成,所述结构化催化床包括布置在一个或多个层的催化部分氧化的催化剂 中,流过每一个与接触时间从0点01至100毫秒,最好为0.1至10毫秒变化的层的反应混合物; 4)冷却的反应产物从阶段3推出)的混合物中。 因此描述了用于实现所述方法的相对设备。