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1. 发明授权

US5783164A Process for the preparation of hydrogen peroxide 失效
标题翻译：过氧化氢的制备方法
公开(公告)号：US5783164A
公开(公告)日：1998-07-21
申请号：US844675
申请日：1997-04-21
申请人： Daniele Bianchi , Rossella Bortolo , Rino D'Aloisio , Marco Ricci , Sergio Soattini
发明人： Daniele Bianchi , Rossella Bortolo , Rino D'Aloisio , Marco Ricci , Sergio Soattini
IPC分类号： C01B15/00 , B01J31/22 , C01B15/027 , C01B15/01
CPC分类号： C01B15/0275
摘要： A process is described for the preparation of hydrogen peroxide by the reaction of carbon monoxide, oxygen and water in an organic solvent immiscible with water, in the presence of a catalytic complex soluble in the organic solvent, deriving from the combination of a palladium salt, a non-coordinating organic or inorganic acid and a ligand capable of binding itself to the palladium atom, characterized in that said ligand is a mono or polydentate nitrogenated compound.
摘要翻译：描述了一种通过一氧化碳，氧和水在与水不混溶的有机溶剂中在可溶于有机溶剂的催化剂络合物的存在下制备过氧化氢的方法，其衍生自钯盐，非配位的有机或无机酸和能够与钯原子结合的配体，其特征在于所述配位体是单或多齿氮化的化合物。

2. 发明申请

US20100210483A1 PROCESS FOR THE REMOVAL OF FILTERCAKES IN OIL WELLS 审中-公开
标题翻译：在油井中除去过滤器的方法
公开(公告)号：US20100210483A1
公开(公告)日：2010-08-19
申请号：US12063142
申请日：2006-07-28
申请人： Rino D'Aloisio , Daniele Bianchi , Marco Ricci , Rossella Bortolo , Roberto Tassinari , Cristina Tonini , Sandra Cobianco
发明人： Rino D'Aloisio , Daniele Bianchi , Marco Ricci , Rossella Bortolo , Roberto Tassinari , Cristina Tonini , Sandra Cobianco
IPC分类号： C09K8/035
CPC分类号： C09K8/62 , C09K8/52 , C09K8/68
摘要： Process for the solubilization of polymeric material deposited on a porous medium, which comprises putting said polymeric material in contact with an aqueous composition comprising: (a) a catalyst selected from: (a1) a complex having general formula (I), Fe++(L)n(Y)s, L being a binder selected from those having general formula (II), wherein X═CH, N, (a2) a hydrosoluble cobalt2+ salt, preferably cobalt acetate; (b) an oxidizing agent selected from: (b1) hydrogen peroxide, (b2) MHSO5, wherein M is an alkaline metal, preferably potassium; with the constraint that the catalyst (a1) can only be used in the presence of the oxidizing agent (b1) and the catalyst (a2) can only be used in the presence of the catalyst (b2).
摘要翻译：沉积在多孔介质上的聚合材料的溶解方法，其包括将所述聚合物材料与含水组合物接触，所述组合物包含：（a）选自以下的催化剂：（a1）具有通式（I）的络合物，Fe ++（L ）n（Y）s，L是选自具有通式（II）的那些的粘合剂，其中X = CH，N，（a2）水溶性钴2+盐，优选乙酸钴; （b）选自以下的氧化剂：（b1）过氧化氢，（b2）MHSO5，其中M是碱金属，优选钾; 催化剂（a1）只能在氧化剂（b1）的存在下使用，催化剂（a2）只能在催化剂（b2）的存在下使用。

3. 发明授权

US07038093B2 Integrated process for the preparation of phenol from benzene with recycling of the by-products 有权
标题翻译：从苯中制备苯酚的副产物回收综合工艺
公开(公告)号：US07038093B2
公开(公告)日：2006-05-02
申请号：US10716460
申请日：2003-11-20
申请人： Daniele Bianchi , Rossella Bortolo , Roberto Buzzoni , Alberto Cesana , Leonardo Dalloro , Rino D'Aloisio
发明人： Daniele Bianchi , Rossella Bortolo , Roberto Buzzoni , Alberto Cesana , Leonardo Dalloro , Rino D'Aloisio
IPC分类号： C07C37/00
CPC分类号： C07C37/60 , B01J29/89 , B01J2229/30 , Y02P20/125 , Y02P20/52 , C07C39/04
摘要： The invention relates to a process for the preparation of phenol comprising the following phases: 1) preparation in continuous of phenol by means of the direct oxidation of benzene with hydrogen peroxide operating with an H2O2/benzene ratio ranging from 10 to 70%, in a three-phase reaction system comprising a first liquid phase consisting of benzene and an organic solvent, a second liquid phase consisting of water, a solid phase consisting of an activated catalyst based on titanium silicalite TS-1; 2) separation of the phenol and non-reacted benzene from the reaction mixture of the oxidation section (1), by means of fractionated distillation; 3) separation of the solvent and by-products from the mixture coming from the distillation tail (2), by means of basic extraction; 4) transformation of the by-products obtain in section (3) to phenol by means of hydrodeoxygenation with hydrogen operating in continuous, in aqueous solution, at a temperature ranging from 250 to 500° C., at pressures of 1-100 bar and in the presence of a catalyst based on elements of group VIB or their mixtures or group VIII of the periodic table or their mixtures; 5) recycling of the phenol obtained in section (4) to the distillation section (2).
摘要翻译：本发明涉及一种制备苯酚的方法，包括以下阶段：1）通过苯与氧化氢的直接氧化制备苯酚连续操作，所述过氧化氢用H 2 O 2 在含有由苯和有机溶剂组成的第一液相的三相反应体系中，第二液相由水组成，固相由活化的基于钛硅沸石TS-1的催化剂; 2）通过分级蒸馏从氧化段（1）的反应混合物中分离苯酚和未反应的苯; 3）通过碱性萃取法从蒸馏尾料（2）中分离出溶剂和副产物与混合物; 4）将第（3）部分获得的副产物转化为苯酚，通过加氢脱氧，氢气在连续的水溶液中，在250-500℃的温度，1-100巴的压力和在基于元素周期表VIB族元素或它们的混合物或VIII族元素或其混合物的催化剂的存在下; 5）将第（4）节中得到的酚再循环至蒸馏段（2）。

4. 发明授权

US08563461B2 Method to activate a catalyst for a continuous process for the preparation of phenol from benzene in a fixed bed reactor 有权
标题翻译：在固定床反应器中活化用于从苯制备苯酚的连续方法的催化剂的方法
公开(公告)号：US08563461B2
公开(公告)日：2013-10-22
申请号：US12725823
申请日：2010-03-17
申请人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
发明人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
IPC分类号： B01J21/00 , C07C29/14
CPC分类号： B01J37/12 , B01J29/89 , B01J37/0009 , B01J2229/30 , B01J2229/42 , C07C37/60 , Y02P20/52 , C07C39/04
摘要： A process to activate a titanium silicalite catalyst for the oxidation of benzene to phenol is provided. The catalyst is activated in the reactor for the oxidation by feeding to a reactor containing the titanium silicalite catalyst, during a time of from 2 to 6 hours, at a temperature ranging from 20 to 120° C., an aqueous solution of ammonium acid fluoride in a concentration ranging from 0.1% to 1% by weight; and hydrogen peroxide in a concentration ranging from 3% to 10% by weight; feeding water to the reactor at the end of the reaction; and drying or calcining the catalyst contained in the reactor to obtain the activated catalyst. The catalyst is represented by the formula: xTiO2.(1−x)SiO2 wherein x is from 0.0001 to 0.04.
摘要翻译：提供了一种活化用于将苯氧化成苯酚的钛硅沸石催化剂的方法。催化剂在反应器中通过在20至120℃的温度范围内进料至包含钛硅沸石催化剂的反应器2至6小时的反应器中活化，将酰基铵水溶液浓度范围为0.1％至1％; 和浓度为3重量％至10重量％的过氧化氢; 在反应结束时向反应器供水; 并干燥或煅烧反应器中所含的催化剂以获得活化的催化剂。催化剂由下式表示：xTiO 2（1-x）SiO 2，其中x为0.0001至0.04。

5. 发明申请

US20100184593A1 METHOD TO ACTIVATE A CATALYST FOR A CONTINUOUS PROCESS FOR THE PREPARATION OF PHENOL FROM BENZENE IN A FIXED BED REACTOR 有权
标题翻译：用于在固定床反应器中从苄苯制备苯酚的连续方法的催化剂的方法
公开(公告)号：US20100184593A1
公开(公告)日：2010-07-22
申请号：US12725823
申请日：2010-03-17
申请人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
发明人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
IPC分类号： B01J21/06
CPC分类号： B01J37/12 , B01J29/89 , B01J37/0009 , B01J2229/30 , B01J2229/42 , C07C37/60 , Y02P20/52 , C07C39/04
摘要： A process to activate a titanium silicalite catalyst for the oxidation of benzene to phenol is provided. The catalyst is activated in the reactor for the oxidation by feeding to a reactor containing the titanium silicalite catalyst, during a time of from 2 to 6 hours, at a temperature ranging from 20 to 120° C., an aqueous solution of ammonium acid fluoride in a concentration ranging from 0.1% to 1% by weight; and hydrogen peroxide in a concentration ranging from 3% to 10% by weight; feeding water to the reactor at the end of the reaction; and drying or calcining the catalyst contained in the reactor to obtain the activated catalyst. The catalyst is represented by the formula: xTiO2.(1−x)SiO2 wherein x is from 0.0001 to 0.04.
摘要翻译：提供了一种活化用于将苯氧化成苯酚的钛硅沸石催化剂的方法。催化剂在反应器中通过在20至120℃的温度范围内进料至包含钛硅沸石催化剂的反应器2至6小时的反应器中活化，将酰基铵水溶液浓度范围为0.1％至1％; 和浓度范围为3重量％至10重量％的过氧化氢; 在反应结束时向反应器供水; 并干燥或煅烧反应器中所含的催化剂以获得活化的催化剂。催化剂由下式表示：xTiO 2（1-x）SiO 2，其中x为0.0001至0.04。

6. 发明授权

US6156939A Process for the hydroxylation of aromatic hydrocarbons 有权
标题翻译：芳烃羟基化方法
公开(公告)号：US6156939A
公开(公告)日：2000-12-05
申请号：US542457
申请日：2000-04-04
申请人： Rodolfo Vignola , Ezio Battistel , Daniele Bianchi , Rossella Bortolo , Roberto Tassinari
发明人： Rodolfo Vignola , Ezio Battistel , Daniele Bianchi , Rossella Bortolo , Roberto Tassinari
IPC分类号： B01J31/28 , B01J23/745 , B01J31/04 , C07B41/02 , C07B61/00 , C07C37/60 , C07C39/04 , C07C39/06 , C07C69/96 , C07C37/00
CPC分类号： B01J31/403 , B01J23/745 , B01J31/04 , B01J31/181 , B01J31/2208 , C07B41/02 , C07C37/60 , B01J2531/842 , Y02P20/52 , Y02P20/584
摘要： The invention relates to a process for the hydroxylation of aromatic hydrocarbons by direct oxidation with hydrogen peroxide. The process is carried out in the presence of a catalyst comprising:iron, administered as inorganic salt;iron ligand, consisting of carboxylic acids of ether-aromatic compounds containing nitrogen, in particular pyrazin-2-carboxylic acid and derivatives;acidifying agent, especially trifluoracetic acid, and a solvent system comprising an organic phase consisting of a substrate and acetonitrile and an aqueous phase containing the catalyst and hydrogen peroxide.
摘要翻译：本发明涉及通过用过氧化氢直接氧化来芳族烃的羟基化的方法。该方法在催化剂的存在下进行，所述催化剂包含：作为无机盐施用的铁; 铁配体，由含氮的醚 - 芳族化合物的羧酸组成，特别是吡嗪-2-羧酸及其衍生物; 酸化剂，特别是三氟乙酸，以及包含由底物和乙腈组成的有机相和含有催化剂和过氧化氢的水相的溶剂体系。

7. 发明授权

US07759529B2 Continuous process for the preparation of phenol from benzene in a fixed bed reactor 有权
标题翻译：在固定床反应器中从苯制备苯酚的连续方法
公开(公告)号：US07759529B2
公开(公告)日：2010-07-20
申请号：US11575579
申请日：2005-10-26
申请人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
发明人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
IPC分类号： C07C29/14
CPC分类号： B01J37/12 , B01J29/89 , B01J37/0009 , B01J2229/30 , B01J2229/42 , C07C37/60 , Y02P20/52 , C07C39/04
摘要： The invention relates to a continuous process for the preparation of phenol by means of the direct oxidation of benzene with hydrogen peroxide in the presence of a catalyst based on titanium silicalite TS-1 comprising: (a) running the process in a fixed bed reactor containing the catalyst based on TS-1 at a temperature ranging from 80-120° C. and at a pressure ranging from 3-15 atm; (b) feeding to the reactor a stream containing H2O2, benzene, sulfolane and water in a single or double phase, wherein the quantities of the single components are within the range of 0.2-6, 15-60, 30-80, 0.5-30 parts by weight, respectively, for every 100 units fed and whose total flow rate is calculated so that the residence time in the reactor (defined as the ratio between the quantity of catalyst by weight and the feeding flow rate) ranges from 0.3 to 2 min; (c) recovery of the products, by-products and solvent from the liquid stream leaving the reactor.
摘要翻译：本发明涉及一种通过在基于钛硅沸石TS-1的催化剂存在下用过氧化氢直接氧化苯的连续方法，其包括：（a）在含有催化剂基于TS-1，温度范围为80-120℃，压力范围为3-15atm; （b）在单相或双相中向反应器中加入含有H 2 O 2，苯，环丁砜和水的流，其中单一组分的量在0.2-6,15-60,30-80,0.5- 对于每100个单位进料，分别计算30重量份，并且其总流速被计算为使得在反应器中的停留时间（定义为催化剂的重量比和进料流量之间的比率）为0.3-2 分钟（c）从离开反应器的液体流中回收产物，副产物和溶剂。

8. 发明授权

US06071848A Process for the hydroxylation of aromatic hydrocarbons 失效
标题翻译：芳烃羟基化方法
公开(公告)号：US06071848A
公开(公告)日：2000-06-06
申请号：US21816
申请日：1998-02-11
申请人： Rodolfo Vignola , Ezio Battistel , Daniele Bianchi , Rossella Bortolo , Roberto Tassinari
发明人： Rodolfo Vignola , Ezio Battistel , Daniele Bianchi , Rossella Bortolo , Roberto Tassinari
IPC分类号： B01J31/28 , B01J23/745 , B01J31/04 , C07B41/02 , C07B61/00 , C07C37/60 , C07C39/04 , C07C39/06 , C07C69/96 , B01J31/00
CPC分类号： B01J31/403 , B01J23/745 , B01J31/04 , B01J31/181 , B01J31/2208 , C07B41/02 , C07C37/60 , B01J2531/842 , Y02P20/52 , Y02P20/584
摘要： The invention relates to a process for the hydroxylation of aromatic hydrocarbons by direct oxidation with hydrogen peroxide. The process is carried out in the presence of a catalyst comprising:iron, administered as an inorganic salt;a carboxylic acid of an aromatic compound containing nitrogen, in particular a pyrazin-2-carboxylic acid or derivative;acidifying agent, especially trifluoracetic acid, and a solvent system comprising an organic phase consisting of a substrate and acetonitrile and an aqueous phase containing the catalyst and hydrogen peroxide.
摘要翻译：本发明涉及通过用过氧化氢直接氧化来芳族烃的羟基化的方法。该方法在催化剂的存在下进行，所述催化剂包含：作为无机盐施用的铁; 含氮的芳族化合物的羧酸，特别是吡嗪-2-羧酸或其衍生物; 酸化剂，特别是三氟乙酸，以及包含由底物和乙腈组成的有机相和含有催化剂和过氧化氢的水相的溶剂体系。

9. 发明申请

US20070255078A1 Continuous Process for the Preparation of Phenol from Benzene in a Fixed Bed Reactor 有权
标题翻译：在固定床反应器中由苯制备酚的连续方法
公开(公告)号：US20070255078A1
公开(公告)日：2007-11-01
申请号：US11575579
申请日：2005-10-26
申请人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
发明人： Daniele Bianchi , Rossella Bortolo , Chiara Busto , Carla Lazzari
IPC分类号： C07C37/00
CPC分类号： B01J37/12 , B01J29/89 , B01J37/0009 , B01J2229/30 , B01J2229/42 , C07C37/60 , Y02P20/52 , C07C39/04
摘要： The invention relates to a continuous process for the preparation of phenol by means of the direct oxidation of benzene with hydrogen peroxide in the presence of a catalyst based on titanium silicalite TS-1 comprising: (a) running the process in a fixed bed reactor containing the catalyst based on TS-1 at a temperature ranging from 80-120° C. and at a pressure ranging from 3-15 atm; (b) feeding to the reactor a stream containing H2O2, benzene, sulfolane and water in a single or double phase, wherein the quantities of the single components are within the range of 0.2-6, 15-60, 30-80, 0.5-30 parts by weight, respectively, for every 100 units fed and whose total flow rate is calculated so that the residence time in the reactor (defined as the ratio between the quantity of catalyst by weight and the feeding flow rate) ranges from 0.3 to 2 min; (c) recovery of the products, by-products and solvent from the liquid stream leaving the reactor.
摘要翻译：本发明涉及一种通过在基于钛硅沸石TS-1的催化剂存在下用过氧化氢直接氧化苯的连续方法，其包括：（a）在含有催化剂基于TS-1，温度范围为80-120℃，压力范围为3-15atm; （b）在单相或双相中向反应器中加入含有H 2 O 2 O 2，苯，环丁砜和水的流，其中单一组分的量在对于每供给的100个单位，分别为0.2-6,15-60,30-80,0.5-30重量份的范围，并且计算其总流速使得在反应器中的停留时间（定义为催化剂的重量和进料流量）为0.3〜2分钟; （c）从离开反应器的液体流中回收产物，副产物和溶剂。

10. 发明授权

US06680413B2 Process for the recovery of phenol and biphenols 有权
标题翻译：苯酚和联苯酚的回收方法
公开(公告)号：US06680413B2
公开(公告)日：2004-01-20
申请号：US10442089
申请日：2003-05-21
申请人： Rossella Bortolo , Lino Carnelli , Daniele Moscotti , Daniele Bianchi
发明人： Rossella Bortolo , Lino Carnelli , Daniele Moscotti , Daniele Bianchi
IPC分类号： C07C3768
CPC分类号： C07C37/74 , C07C37/685 , C07C37/72 , C07C37/78 , C07C37/86 , Y02P20/582 , C07C39/04 , C07C39/15 , C07C39/235
摘要： A process is described for the recovery of phenol and biphenols from their homogeneous mixtures containing benzene, sulfolane and water, which is based on the use of an alkaline solution and benzene for the separation of biphenols from sulfolane, after removing the benzene, H2O and phenol contained in the reaction effluent. The process allows the recovery of phenol and biphenol by-products dissolved in sulfolane, directly obtaining the purified solvent containing the benzene necessary for the feeding to the reactor for the direct oxidation of benzene, as well as the biphenols dissolved in water and pure phenol.
摘要翻译：描述了一种从含有苯，环丁砜和水的均匀混合物中回收苯酚和联苯酚的方法，其基于在除去苯，H 2 O和苯酚之后使用碱性溶液和苯来分离联苯酚与环丁砜分离反应流出物中含有的苯酚和联苯酚副产物的回收，直接得到含有苯进行反应器所需的苯的纯化溶剂直接氧化苯，以及溶解的联苯酚在水和纯苯酚中。

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