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1. 发明公开

US20240050922A1 SILICON TRAPPING MASS 审中-公开
公开(公告)号：US20240050922A1
公开(公告)日：2024-02-15
申请号：US18267965
申请日：2021-12-09
申请人： IFP ENERGIES NOUVELLES
发明人： Nicolas LEGAGNEUX , Marie-Claire MARION , Karin BARTHELET , Patrick EUZEN , Joseph LOPEZ
IPC分类号： B01J20/08 , B01J20/32 , B01J20/28 , C10G25/05
CPC分类号： B01J20/08 , B01J20/3204 , B01J20/3236 , B01J20/28011 , B01J20/28061 , B01J20/28083 , B01J20/2809 , C10G25/05 , C10G2300/104 , C10G2400/02 , C10G2300/202
摘要： The present invention relates to a mass for trapping silicon compounds, comprising a porous alumina-based support and at least one metal chosen from the metals from groups VIB and VIIIB, and exhibiting a grain density of at least 1.20 g/ml, a specific surface of at least 300 m2/g and pores with a mean size of less than 6.5 nm, as determined by mercury porosimetry. The present invention also relates to a process for the preparation of said trapping mass and to a trapping process using said trapping mass.

2. 发明公开

US20240059981A1 METHOD FOR CAPTURING SILICON AT LOW HOURLY SPACE VELOCITY 审中-公开
公开(公告)号：US20240059981A1
公开(公告)日：2024-02-22
申请号：US18268174
申请日：2021-12-09
申请人： IFP ENERGIES NOUVELLES
发明人： Nicolas LEGAGNEUX , Marie-Claire MARION , Karin BARTHELET
IPC分类号： C10G25/00 , C10L3/10 , B01D53/82 , B01D53/46 , B01J20/08 , B01J20/28
CPC分类号： C10G25/003 , C10L3/101 , B01D53/82 , B01D53/46 , B01J20/08 , B01J20/28011 , B01J20/28061 , B01J20/28083 , B01J20/28071 , B01J20/28073 , B01J20/28076 , C10G2300/1003 , C10G2300/104 , C10G2300/1022 , C10G2300/1025 , C10G2300/202 , B01D2253/1124 , B01D2253/306 , B01D2253/311 , B01D2253/308 , B01D2253/25 , B01D2257/55 , B01J2220/56
摘要： The present invention relates to a process for trapping silicon compounds in a gaseous or liquid feedstock, comprising bringing the feedstock into contact with a trapping mass with a liquid hourly space velocity LHSV of less than 5 h−1 or a gas hourly space velocity GHSV of less than 500 h−1.

3. 发明申请

US20140374321A1 PROCESS FOR ELIMINATING ARSENIC FROM A HYDROCARBON FEED 审中-公开
标题翻译：从碳氢化合物排出砷的方法
公开(公告)号：US20140374321A1
公开(公告)日：2014-12-25
申请号：US14306308
申请日：2014-06-17
申请人： IFP ENERGIES NOUVELLES
发明人： Marie-Claire MARION , Philibert LEFLAIVE , Annick PUCCI
IPC分类号： C10G65/04
CPC分类号： C10G65/04 , B01J20/06 , B01J20/08 , B01J20/3204 , B01J20/3236 , B01J23/85 , B01J23/883 , B01J29/076 , B01J35/0006 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J37/0201 , B01J37/0205 , B01J37/04 , B01J37/20 , B01J37/28 , C10G45/08 , C10G2300/205
摘要： The invention concerns a process for eliminating arsenic from a hydrocarbon feed which is at least partially liquid, comprising at least the following steps: a) bringing the hydrocarbon feed and hydrogen into contact with a first capture mass comprising a support and at least one metal M1 from group VIB and at least two metals M2 and M3 from group VIII; b) bringing the hydrocarbon feed and hydrogen into contact with a second capture mass in the sulphide form comprising a support and nickel, the quantity of nickel being at least 5% by weight of NiO with respect to the total weight of the second capture mass, in which step a) is either carried out before step b) or carried out simultaneously with step b).
摘要翻译：本发明涉及一种从至少部分为液体的烃进料中消除砷的方法，该方法至少包括以下步骤：a）使烃进料和氢气与包含载体和至少一种金属M1的第一捕获物质接触来自VIB组和至少两种来自VIII族的金属M2和M3; b）使烃进料和氢气与包含载体和镍的硫化物形式的第二捕集物接触，镍的量相对于第二捕获质量的总重量为至少5重量％的NiO，其中步骤a）在步骤b）之前进行或者与步骤b）同时进行。

4. 发明申请

US20130158139A1 PROCESS FOR PRODUCTION OF HYDROCARBONS WITH CATALYST CONDITIONING 有权
标题翻译：用催化剂条件生产碳氢化合物的方法
公开(公告)号：US20130158139A1
公开(公告)日：2013-06-20
申请号：US13712232
申请日：2012-12-12
申请人： IFP ENERGIES NOUVELLES
发明人： Marie-Claire MARION , Fabrice DIEHL , Francois HUGUES
IPC分类号： C10G2/00
CPC分类号： C10G2/332 , B01J21/12 , B01J23/75 , B01J23/83 , B01J23/8892 , B01J23/8896 , B01J23/8913 , B01J37/0201 , B01J37/18
摘要： A method for continuous production of hydrocarbons from synthesis gas in the presence of a cobalt-based catalyst which comprises a step of providing synthesis gas from a source (1) of synthesis gas in a Fischer-Tropsch synthesis reactor (4). The method also includes the following steps: a) conditioning of the catalyst in reduced state in a conditioning reactor (2) by contact with a flow of reducing gas from a synthesis gas source supplying the synthesis reactor, the reducing conditioning gas comprising carbon monoxide (CO) or a mixture comprising hydrogen (H2) and carbon monoxide (CO), the H2/CO molar ratio of which is between 0.1 and 0.9, at a temperature between 200 and 500° C., and a total pressure between 0.1 and 5 MPa and under a gas flow between 1 and 20 NI/h/g of catalyst to be treated, b) supply of reduced catalyst conditioned in step a) to the synthesis reactor (4).
摘要翻译：一种在钴基催化剂存在下从合成气中连续生产烃的方法，该方法包括在费 - 托合成反应器（4）中从合成气源（1）提供合成气的步骤。该方法还包括以下步骤：a）通过与供应合成反应器的合成气源的还原气体流接触，调节反应器（2）中处于还原状态的催化剂，还原调节气体包括一氧化碳（ CO）或H 2 / CO摩尔比为0.1-0.9之间的氢（H 2）和一氧化碳（CO）的混合物，温度为200-500℃，总压力为0.1-5 MPa，并且在待处理催化剂的1至20Ni / h / g之间的气流下，b）将在步骤a）中调节的还原催化剂供应到合成反应器（4）。

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