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    • 4. 发明申请
    • METHOD FOR SEPARATION OF REACTION PRODUCTS FROM CATALYSTS
    • 从催化剂分离反应产物的方法
    • WO02036527A1
    • 2002-05-10
    • PCT/JP2001/009407
    • 2001-10-25
    • B01J31/02B01J31/40B01J38/00B01J38/56C07B63/00C07C45/32C07C45/34C07C45/80C07C49/447C07C49/557
    • B01J31/0247B01J31/40B01J31/4015B01J2531/845C07C45/34C07C45/80Y02P20/584C07C49/653C07C49/637
    • A method for separating a reaction product and an imide catalyst of the general formula (1) or a degenerate thereof from a reaction mixture obtained by a reaction with the imide catalyst, which comprises extracting the reaction mixture with two organic solvents which are separable from each other to thereby distribute the reaction product and the catalyst or the degenerate to the two organic solvent layers respectively: (1) [wherein R and R are each hydrogen, alkyl, or the like, or alternatively R and R may be united to form a double bond, or an aromatic or non-aromatic ring; and X is oxygen or hydroxyl]. According to this method, an imide catalyst such as N-hydroxyphthalimide and/or a degenerate thereof and a reaction product can be efficiently separated by easy operation from a reaction mixture obtained by using the imide catalyst and a substrate of hydrocarbon or the like.
    • 从通过与酰亚胺催化剂反应获得的反应混合物中分离出通式(1)的反应产物和酰亚胺催化剂或其简并物的方法,该方法包括用两种可分离的有机溶剂萃取反应混合物 另外分别将反应产物和催化剂或简并物分配到两个有机溶剂层:(1)[其中R 1和R 2各自为氢,烷基等,或者R 1为 >和R 2可以一起形成双键,或芳族或非芳族环; 并且X是氧或羟基]。 根据该方法,通过使用酰亚胺催化剂和烃等的底物获得的反应混合物,可以容易地将酰亚胺催化剂如N-羟基邻苯二甲酰亚胺和/或其简并物和反应产物有效地分离。
    • 7. 发明申请
    • PROCESSES FOR REGENERATING CATALYSTS USEFUL IN FISCHER-TROPSCH PROCESSES
    • 再生催化剂 - 再循环工艺中使用的催化剂再生工艺
    • WO2017091400A1
    • 2017-06-01
    • PCT/US2016/062177
    • 2016-11-16
    • CLARIANT CORPORATION
    • KIM, Jae HyungHUELSMAN, DougBRADEN, Jeffery L.
    • B01J38/56B01J38/10C07C1/04C10G2/00
    • B01J38/12B01J23/75B01J23/94B01J38/02B01J38/04B01J38/10B01J38/48C10G2/33C10G2300/70
    • The present disclosure relates to processes for regenerating catalysts. In certain aspects, a process for regenerating a deactivated catalyst disposed in a first organic material includes removing a substantial portion of the first organic material from the catalyst to provide a dewaxed catalyst having less than about 40 wt% (e.g., less than about 20%) organic material disposed thereon. The dewaxed catalyst is then contacted with a flow of a substantially inert gas at a temperature of at least about 200 °C to provide an inert gas-treated catalyst having less than about 10 wt% organic material disposed thereon. The inert gas-treated catalyst is then contacted with an oxygen-containing gas at a temperature of at least about 200 °C to form an oxidized catalyst (e.g., having less than 2 wt% carbonaceous material disposed thereon). The oxidized catalyst is then contacted with a hydrogen-containing gas at a temperature of at least about 200 °C to form a regenerated catalyst. Finally, the regenerated catalyst can be disposed in a second organic material. The regenerated catalysts can be useful, for example, in Fischer-Tropsch processes.
    • 本公开涉及用于再生催化剂的方法。 在某些方面,用于再生布置在第一有机材料中的失活催化剂的方法包括从所述催化剂除去大部分第一有机材料以提供具有小于约40重量%(例如,小于约20重量% )布置在其上的有机材料。 然后将脱蜡的催化剂与至少约200℃的基本惰性气体流接触,以提供惰性气体处理的催化剂,其上布置有少于约10wt%的有机材料。 然后使惰性气体处理的催化剂与含氧气体在至少约200℃的温度下接触以形成氧化催化剂(例如其上布置小于2wt%的含碳材料)。 然后使氧化的催化剂与含氢气体在至少约200℃的温度下接触以形成再生催化剂。 最后,再生催化剂可以置于第二有机材料中。 再生的催化剂可用于例如费 - 托工艺中。