-
1.
公开(公告)号:US20250051157A1
公开(公告)日:2025-02-13
申请号:US18718092
申请日:2022-12-14
Applicant: BASF SE
Inventor: Elias Christopher FREI , Michael KRAEMER , Virginie LANVER , Nils BOTTKE
Abstract: The present invention relates to a specific process for the reforming of ammonia, wherein the process comprises (i) providing a reactor containing a catalyst comprising a metal M1 selected from the group consisting of Ni, Co, or Ni and Co; (ii) preparing a feed gas stream comprising NH3; (iii) feeding the feed gas stream prepared in (ii) into the reactor provided in (i) and contacting the feed gas stream with the catalyst, wherein contacting is performed at a pressure of 1 to 50 bara, and at a temperature of 400 to 1,100° C.; (iv) removing an effluent gas stream from the reactor, the effluent gas stream comprising H2 and N2.
-
公开(公告)号:US20210283583A1
公开(公告)日:2021-09-16
申请号:US16323828
申请日:2017-08-08
Applicant: BASF SE
Inventor: ANDREY KARPOV , Michael KRAEMER , Marco BOSCH , Christian BARTOSCH , Juergen ZUEHLKE , Carlos LIZANDARA PUEYO , Guido WASSERSCHAFF
Abstract: The present invention is directed to a shaped catalyst body for preparing ethylene oxide, which comprises at least silver, cesium and rhenium applied to an alumina support, wherein the alumina support comprises Si, Ca, and Mg in a defined amount. Furthermore, the present invention is directed to a process for preparing the catalyst according to the present invention and process for preparing ethylene oxide by gas-phase oxidation of ethylene by means of oxygen in the presence of a shaped catalyst body according to the present invention.
-
公开(公告)号:US20210046459A1
公开(公告)日:2021-02-18
申请号:US16968542
申请日:2019-02-06
Applicant: BASF SE
Inventor: Andrey KARPOV , Christian WALSDORFF , Michael KRAEMER , Armin LANGE DE OLIVEIRA , Gerhard KRENNRICH , Christian BARTOSCH , Juergen ZUEHLKE
Abstract: The present invention provides a catalyst effective in the oxidative conversion of ethylene to ethylene oxide, comprising an alumina support and 20 to 45%by weight of the catalyst, of silver applied to the support, the catalyst meeting the following limitations (i) to (v): (i) an amount of cesium c(Cs) in mmol per Kg of catalyst of at least 2; (ii) an amount of rhenium c(Re) in mmol per Kg of catalyst of at least 3.0; (iii) an amount of tungsten c(W) in mmol per Kg of catalyst of at least 1.6; (iv) a silicon to alkaline earth metal molar ratio x of not higher than 1.80; (v) c(Cs)−c(Re)−c(W)≤4·x−0.5.
-
-