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公开(公告)号：US20130060071A1
公开(公告)日：2013-03-07
申请号：US13636797
申请日：2011-03-17
Applicant: Daniele Delledonne , Roberto Buzzoni , Daniele Bianchi
Inventor： Daniele Delledonne , Roberto Buzzoni , Daniele Bianchi
IPC: C07C1/22
CPC classification number: C10G3/50 , C07C37/54 , C10G1/002 , C10G1/06 , C10G3/46 , C10G3/47 , C10G3/48 , C10G2300/1014 , C10G2300/4006 , C10G2300/4018 , C10G2300/44 , C10G2400/02 , C10G2400/06 , C10L1/04 , Y02P30/20 , C07C39/08 , C07C39/06
Abstract: Process for the conversion of lignin to liquid hydro-carbons comprising: subjecting the lignin to hydrogenolysis in the presence of at least one hydrogenolysis catalyst, at a temperature ranging from 250° C. to 350° C., preferably ranging from 290° C. to 320 ° C., so as to obtain depolymerized lignin; subjecting said depolymerized lignin to hydrotreating so as to obtain a mixture of liquid hydrocarbons. Said liquid hydrocarbons can be used as such (biofuels) for the production of reformulated gasolines, or they can be used for the production of gasolines or of gas oils through conventional refining processes.
Abstract translation: 将木质素转化为液态碳氢化合物的方法，包括：在至少一种氢解催化剂存在下，在250℃至350℃，优选290℃的温度下使木质素进行氢解。 至320℃，以获得解聚的木质素; 对所述解聚的木质素进行加氢处理以获得液体烃的混合物。 所述液态碳氢化合物可以原样使用（生物燃料）用于生产重整汽油，或者它们可以用于通过常规精制方法生产汽油或瓦斯油。
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公开(公告)号：US20080132735A1
公开(公告)日：2008-06-05
申请号：US11813874
申请日：2006-01-10
Applicant: Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni , Fausto Genoni , Guido Spano , Franco Rivetti
Inventor： Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni , Fausto Genoni , Guido Spano , Franco Rivetti
IPC: C07C37/64
CPC classification number: B01J23/002 , B01J23/31 , B01J23/8885 , B01J2523/00 , C07C37/00 , C07C37/58 , Y02P20/52 , B01J2523/17 , B01J2523/27 , B01J2523/69 , B01J2523/54 , B01J2523/55 , B01J2523/68 , B01J2523/842 , B01J2523/3712 , B01J2523/56 , C07C39/04
Abstract: A process is described for the preparation of phenol by the hydrodeoxygenation of polyhydroxylated benzene derivatives or by the selective hydroxylation of benzene under depletive conditions, characterized in that the above-mentioned reactions are carried out in the presence of a catalyst based on multi component metal oxides comprising at least one metal selected from the groups VB, VIB, VIII, IB, IIB, IVA, VA.
Abstract translation: 描述了通过多羟基化苯衍生物的加氢脱氧或通过在脱碱条件下苯的选择性羟基化制备苯酚的方法，其特征在于上述反应在基于多组分金属氧化物的催化剂存在下进行 包括选自组VB，VIB，VIII，IB，IIB，IVA，VA中的至少一种金属。
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公开(公告)号：US07122501B2
公开(公告)日：2006-10-17
申请号：US10396503
申请日：2003-03-26
Applicant: Giuseppe Paparatto , Rino D'Aloisio , Giordano De Alberti , Roberto Buzzoni
Inventor： Giuseppe Paparatto , Rino D'Aloisio , Giordano De Alberti , Roberto Buzzoni
CPC classification number: C01B15/029 , B01J23/44 , B01J37/031 , B01J37/16 , B01J37/18 , Y10S502/523
Abstract: A description follows of a bimetallic catalyst, obtained by dispersing in sequence and alternating the precursors of the single metal components of the catalyst on a carrier, and a process for the synthesis of hydrogen peroxide by the direct reaction of hydrogen with oxygen, in a solvent medium containing a halogenated promoter and an acid promoter, in the presence of said catalyst.
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公开(公告)号：US20050032630A1
公开(公告)日：2005-02-10
申请号：US10944802
申请日：2004-09-21
Applicant: Luigi Balducci , Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni
Inventor： Luigi Balducci , Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni
IPC: C07D201/04 , B01J29/035 , B01J29/40 , C01B37/02 , C10G11/05 , B01J29/06
CPC classification number: B01J29/035 , B01J29/40 , B01J37/0072 , B01J37/033 , B01J2229/42
Abstract: The present invention relates to a process for the preparation of zeolitic catalysts of the MFI type in spheroidal form. The process consists in emulsifying and consolidating in paraffinic hydrocarbons, in the presence of a non-ionic surface-active agent or a suitable combination of a non-ionic surface-active agent and a cationic surface-active agent, a dispersion of particles of zeolitic material of the MFI type in a silica sol.
Abstract translation: 本发明涉及一种以球形形式制备MFI型沸石催化剂的方法。 该方法包括在非离子表面活性剂或非离子表面活性剂和阳离子表面活性剂的合适组合的存在下在链烷烃中乳化和固结，沸石颗粒的分散体 在硅溶胶中的MFI型材料。
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公开(公告)号：US09334450B2
公开(公告)日：2016-05-10
申请号：US13636797
申请日：2011-03-17
Applicant: Daniele Delledonne , Roberto Buzzoni , Daniele Bianchi
Inventor： Daniele Delledonne , Roberto Buzzoni , Daniele Bianchi
CPC classification number: C10G3/50 , C07C37/54 , C10G1/002 , C10G1/06 , C10G3/46 , C10G3/47 , C10G3/48 , C10G2300/1014 , C10G2300/4006 , C10G2300/4018 , C10G2300/44 , C10G2400/02 , C10G2400/06 , C10L1/04 , Y02P30/20 , C07C39/08 , C07C39/06
Abstract: A process for the conversion of lignin to liquid hydrocarbons comprising: (1) hydrogenolyzing a lignin in the presence of at least one hydrogenolysis catalyst, at a temperature ranging from 250° C. to 350° C., preferably ranging from 290° C. to 320° C., to obtain depolymerized lignin; and (2) hydrodeoxygenating said depolymerized lignin in the presence of a hydrodeoxygenating catalyst to obtain a mixture of liquid hydrocarbons. The resultant liquid hydrocarbons can be used as such (biofuels) for the production of reformulated gasolines, or they can be used for the production of gasolines or oils by conventional refining processes.
Abstract translation: 一种将木质素转化为液态烃的方法，包括：（1）在至少一种氢解催化剂的存在下，在250℃至350℃，优选290℃的温度下，使木质素氢解。 至320℃，以获得解聚的木质素; 和（2）在加氢脱氧催化剂存在下加氢脱氧所述解聚的木质素以获得液体烃的混合物。 所得到的液体烃可以原样使用（生物燃料）用于生产重整汽油，或者它们可以用于通过常规精制方法生产汽油或油。
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Patent Agency Ranking
公开(公告)号：US09193643B2
公开(公告)日：2015-11-24
申请号：US13518550
申请日：2010-12-23
Applicant: Maria Angela Mantegazza , Fabrizio Bordes , Roberto Buzzoni
Inventor： Maria Angela Mantegazza , Fabrizio Bordes , Roberto Buzzoni
CPC classification number: C07C2/864 , Y02E50/17 , Y02P20/52 , C07C15/073
Abstract: The invention relates to a process for the production of ethylbenzene which comprises: a reaction step in which benzene is reacted with ethanol, or a mixture of ethanol and ethylene, at a pressure higher than atmospheric pressure, preferably in gaseous phase or in mixed gas-liquid phase, in the presence of a catalytic system containing a zeolite belonging to the BEA family, and a separation step of the product obtained. According to a preferred aspect, ethanol deriving from biomasses is used, in particular ethanol obtained from the fermentation of sugars deriving from biomasses.
Abstract translation: 本发明涉及一种生产乙苯的方法，该方法包括：在高于大气压，优选气相或混合气体反应器中，苯与乙醇或乙醇和乙烯的混合物反应的反应步骤， 在含有属于BEA族的沸石的催化体系的存在下，所得的产物的分离步骤。 根据优选的方面，使用衍生自生物质的乙醇，特别是从衍生自生物质的糖的发酵得到的乙醇。
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公开(公告)号：US07868210B2
公开(公告)日：2011-01-11
申请号：US11813874
申请日：2006-01-10
Applicant: Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni , Fausto Genoni , Guido Spano′ , Franco Rivetti
Inventor： Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni , Fausto Genoni , Guido Spano′ , Franco Rivetti
CPC classification number: B01J23/002 , B01J23/31 , B01J23/8885 , B01J2523/00 , C07C37/00 , C07C37/58 , Y02P20/52 , B01J2523/17 , B01J2523/27 , B01J2523/69 , B01J2523/54 , B01J2523/55 , B01J2523/68 , B01J2523/842 , B01J2523/3712 , B01J2523/56 , C07C39/04
Abstract: A process is described for the preparation of phenol by the hydrodeoxygenation of polyhydroxylated benzene derivatives or by the selective hydroxylation of benzene under depletive conditions, characterized in that the above-mentioned reactions are carried out in the presence of a catalyst based on multi component metal oxides comprising at least one metal selected from the groups VB, VIB, VIII, IB, IIB, IVA, VA.
Abstract translation: 描述了通过多羟基化苯衍生物的加氢脱氧或通过在脱碱条件下苯的选择性羟基化制备苯酚的方法，其特征在于上述反应在基于多组分金属氧化物的催化剂存在下进行 包括选自组VB，VIB，VIII，IB，IIB，IVA，VA中的至少一种金属。
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公开(公告)号：US07101526B2
公开(公告)日：2006-09-05
申请号：US10485629
申请日：2002-07-30
Applicant: Giuseppe Paparatto , Giordano De Alberti , Rino D'Aloisio , Roberto Buzzoni
Inventor： Giuseppe Paparatto , Giordano De Alberti , Rino D'Aloisio , Roberto Buzzoni
IPC: C01B15/029 , B01J31/06
CPC classification number: C01B15/029 , B01J21/18 , B01J23/40 , B01J23/42 , B01J23/44 , B01J27/053 , B01J31/06
Abstract: The present invention relates to a catalyst consisting of: (a) one or more metals of the platinum group as active components; (b) one or more polyolefins; and (c) a carrier. The invention also relates to a process for the synthesis of hydrogen peroxide (H2O2) from hydrogen and oxygen which uses said catalyst and the use of the hydrogen peroxide solution in oxidation processes catalyzed by titanium silicalite. The process operates under high safety conditions with a high productivity and molar selectivity towards the formation of H2O2.
Abstract translation: 本发明涉及由以下组成的催化剂：（a）一种或多种铂族金属作为活性组分; （b）一种或多种聚烯烃; 和（c）承运人。 本发明还涉及使用所述催化剂和使用过氧化氢溶液的氢气和氧气合成过氧化氢（H 2 O 2 O 2）的方法 由钛硅沸石催化的氧化过程。 该方法在高安全性条件下以高生产率和摩尔选择性在H 2 O 2 O 2的形成中运行。
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公开(公告)号：US06949687B2
公开(公告)日：2005-09-27
申请号：US10736594
申请日：2003-12-17
Applicant: Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni , Franco Rivetti , Caterina Rizzo , Virginio Arrigoni , Carlo Perego
Inventor： Leonardo Dalloro , Alberto Cesana , Roberto Buzzoni , Franco Rivetti , Caterina Rizzo , Virginio Arrigoni , Carlo Perego
IPC: B01J29/08 , B01J29/18 , B01J29/70 , B01J29/90 , B01J38/02 , C07B61/00 , C07C2/70 , C07C5/27 , C07C6/12 , C07C15/02 , C07C5/22
CPC classification number: C07C6/123 , C07C5/2737 , C07C15/02
Abstract: A process is described for the contemporaneous preparation of mesitylene and durene, characterized in that mesitylene and durene are obtained exclusively starting from pseudo-cumene without the use of any further chemical compound, operating in continuous, at a temperature ranging from 210 to 400° C., at a pressure ranging from 1 to 50 bar, with a weight space velocity ranging from 0.1 to 20 hours−1 and in the presence of a catalyst based on crystalline metal-silicates in acid form. After the recovery of mesitylene and durene from the reaction raw product, some of the remaining components of the raw product itself are recycled and fed to the reactor together with the pseudo-cumene.
Abstract translation: 描述了同时制备均三甲苯和杜烯的方法，其特征在于，均三甲苯和杜烯仅从起始伪异丙苯开始获得，而不使用任何其它化学化合物，连续操作，温度范围为210-400℃ 在1至50巴的压力下，重量空间速度为0.1至20小时-1的范围内，并且在基于酸形式的结晶金属硅酸盐的催化剂存在下进行。 在从反应原料中回收均三甲苯和杜烯后，原料的其余部分本身被再循环并与假枯烯一起进料到反应器中。
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公开(公告)号：US20130011893A1
公开(公告)日：2013-01-10
申请号：US13518550
申请日：2010-12-23
Applicant: Maria Angela Mantegazza , Fabrizio Bordes , Roberto Buzzoni
Inventor： Maria Angela Mantegazza , Fabrizio Bordes , Roberto Buzzoni
CPC classification number: C07C2/864 , Y02E50/17 , Y02P20/52 , C07C15/073
Abstract: The invention relates to a process for the production of ethylbenzene which comprises: a reaction step in which benzene is reacted with ethanol, or a mixture of ethanol and ethylene, at a pressure higher than atmospheric pressure, preferably in gaseous phase or in mixed gas-liquid phase, in the presence of a catalytic system containing a zeolite belonging to the BEA family, and a separation step of the product obtained. According to a preferred aspect, ethanol deriving from biomasses is used, in particular ethanol obtained from the fermentation of sugars deriving from biomasses.
Abstract translation: 本发明涉及一种生产乙苯的方法，该方法包括：在高于大气压，优选气相或混合气体反应器中，苯与乙醇或乙醇和乙烯的混合物反应的反应步骤， 在含有属于BEA族的沸石的催化体系的存在下，所得的产物的分离步骤。 根据优选的方面，使用衍生自生物质的乙醇，特别是从衍生自生物质的糖的发酵得到的乙醇。
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