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1. 发明申请

WO2013178375A1 PROCESS AND CATALYST FOR UPGRADING GASOLINE 审中-公开
标题翻译：加氢汽油的工艺和催化剂
公开(公告)号：WO2013178375A1
公开(公告)日：2013-12-05
申请号：PCT/EP2013/055758
申请日：2013-03-20
申请人： HALDOR TOPSØE A/S
发明人： HIDALGO VIVAS, Angelica , JOENSEN, Finn
IPC分类号： C10G45/64 , B01J23/755 , B01J29/46 , C07C15/02 , C10L1/06
CPC分类号： C07C5/2775 , B01J27/043 , B01J29/40 , B01J29/46 , B01J2229/186 , C07C5/2737 , C07C2529/46 , C10G45/64 , C10L1/06
摘要： Process and catalyst for upgrading gasoline comprising durene ( 1, 2, 4, 5-tetramethylbenzene) and pseudodocumene, the process comprises hydroisomerization of durene (1,2,4,5- tetramethylbenzene) and pseudocumene (1,2,4- trimethylbenzene) contained in the gasoline in presence of a catalyst comprising a sulfided base metal supported on an acidic carrier, thereby converting durene (1,2,4,5- tetramethylbenzene) to isodurene (1,2,4,5- tetramethylbenzene) and prehnitene (1,2,3,4- tetramethylbenzene) and converting pseudocumene (1,2,4- trimethylbenzene) to mesitylene (1, 3, 5-trimethylbenzene).
摘要翻译：包含杜烯（1,2,4,5-四甲基苯）和假花生烯烃的汽油升级方法和催化剂，该方法包括杜烯（1,2,5,5-四甲基苯）和假枯烯（1,2,4-三甲基苯）的加氢异构化，在包含负载在酸性载体上的硫化贱金属的催化剂存在下，汽油中含有，从而将杜烯（1,2,4,5-四甲基苯）转化为异戊烯（1,2,4,5-四甲基苯）和前亚硝基（ 1,2,3,4-四甲基苯），并将假枯烯（1,2,4-三甲基苯）转化为均三甲苯（1,3,5-三甲基苯）。

2. 发明申请

WO2017001539A1 DEMETALLIZATION OF HYDROCARBONS 审中-公开
标题翻译：碳氢化合物的去除
公开(公告)号：WO2017001539A1
公开(公告)日：2017-01-05
申请号：PCT/EP2016/065251
申请日：2016-06-30
申请人： HALDOR TOPSØE A/S
发明人： EGEBERG, Rasmus Gottschalck , HIDALGO VIVAS, Angelica , ENEVOLDSEN, Søren Selde
IPC分类号： C10J3/00 , C10B51/00 , C10K1/00 , C10G31/10 , C10G32/02 , C10G45/32 , C10G45/02 , C10G3/00 , C10G67/08 , C10G17/06 , C10B53/00
CPC分类号： C10C1/205 , C10B53/00 , C10C1/20 , C10G3/42 , C10G3/50 , C10G17/06 , C10G31/10 , C10G32/02 , C10G45/02 , C10G45/32 , C10G67/08 , C10G2300/203 , C10J3/00 , C10K1/004 , Y02P30/20
摘要： The present disclosure refers to a process and a process plant for extraction of metals from a hydrocarbon mixture obtained from a gasification or pyrolysis process, comprising the steps of combining said hydrocarbon mixture with an aqueous acid forming a mixture, mixing said mixture, separating said mixture in a contaminated aqueous phase and a purified hydrocarbon phase, with the associated benefit of said aqueous acid being able to release metals bound in such gasification and pyrolysis processes.
摘要翻译：本公开内容涉及从气化或热解过程获得的烃混合物中提取金属的方法和工艺装置，包括以下步骤：将所述烃混合物与形成混合物的含水酸混合，混合所述混合物，分离所述混合物在污染的水相和纯化的烃相中，所述含水酸的相关益处能够释放在这种气化和热解过程中结合的金属。

3. 发明申请

WO2019002028A1 DEMETALLIZATION OF HYDROCARBONS 审中-公开
公开(公告)号：WO2019002028A1
公开(公告)日：2019-01-03
申请号：PCT/EP2018/066269
申请日：2018-06-19
申请人： HALDOR TOPSØE A/S
发明人： ZEUTHEN, Jacob Hjerrild , HIDALGO VIVAS, Angelica , ALKILDE, Ole Frej
IPC分类号： C10G31/08 , C10G31/10 , C10G53/00 , C10G53/10 , C10G17/06
摘要： The present disclosure refers to a process plant and a process for production of a demetallized hydrocarbon from a contaminated hydrocarbon comprising a means for mixing having one or more inlets in fluid communication with a contaminated hydrocarbon inlet and with an acid inlet and having an outlet a settling tank having an inlet, an aqueous phase outlet, and a firsthydrocarbon phase outlet, a means for evaporative concentration having an inlet, a water outlet and a brine outlet, wherein the outlet of said means for mixing is in fluid communication with the inlet of said settling tank and characterized in the inlet of said means for evaporative concentration being in fluid communication with the aqueous phase outlet of said settling tank and the water outlet of said means for evaporative concentration is in fluid communication with the acid inlet and said hydrocarbon phase outlet providing a demetallized hydrocarbon for withdrawal with the associated benefit of such a process plant having a reduced water consumption, in that the acid feed may be a concentrated acid and be diluted by the water withdrawn from the means for evaporative concentration.

4. 发明申请

WO2021204621A1 SELECTIVE PRODUCTION OF LIGHT SYNTHETIC GASOLINE 审中-公开
公开(公告)号：WO2021204621A1
公开(公告)日：2021-10-14
申请号：PCT/EP2021/058423
申请日：2021-03-31
申请人： HALDOR TOPSØE A/S
发明人： HIDALGO VIVAS, Angelica , RASMUSSEN, Henrik Wolthers , MENJON, Ian , ALKILDE, Ole Frej , KNUDSEN, Arne
IPC分类号： C10G3/00 , C10G45/64 , C10G47/02 , C10G65/14
摘要： The present disclosure relates to a production plant and a method for production of a synthetized gasoline product from a synthetic hydrocarbon mixture produced from a mixture of reactive oxygenates comprising the steps ofa. separating the synthetic hydrocarbon mixture in at least a light hydrocarbon frac-tion, and a higher boiling hydrocarbon fraction, wherein the higher boiling fraction comprises at least 70% of the molecules comprising 10 or more carbon atoms pre-sent in the hydrocarbon mixture and less than 20% of the molecules comprising ex-actly 9 carbon atoms present in the synthetic hydrocarbon mixture,b. directing at least an amount of said higher boiling hydrocarbon fraction as a hy-drocracking feedstock to contact a material catalytically active in hydrocracking un-der effective hydrocracking conditions providing a hydrocracked hydrocarbon stream,wherein at least an amount of said hydrocracked hydrocarbon stream, optionally after further hydroprocessing, is combined with at least an amount of said light hydrocarbon fraction, to provide said synthetized gasoline product having a T90 according to ASTM D86 being below T90 according to ASTM D86 of said synthetic hydrocarbon mixture, such as 10°C or 20°C below, with the associated benefit of such a process reducing the upper boiling point of the synthetized gasoline product, by hydrocracking C10 and C11 hydrocarbons, especially two-ring aromatics, while minimizing the yield loss of gasoline product.

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