公开(公告)号：US20040195153A1

公开(公告)日：2004-10-07

申请号：US10736743

申请日：2003-12-17

Applicant: ENI S.p.A. ,  ENITECNOLOGIE S.p.A.

Inventor： Felicia Massetti ,  Alessandro Nardella ,  Raffaele Tomaciello ,  Alberto Guarneri

IPC: B03B007/00 ,  C09K007/00

CPC classification number: E21B21/066 ,  B01D11/0219 ,  B01D11/0488 ,  B01D11/0492 ,  B08B7/0021

Abstract: Method for the removal and recovery of the oily component from cuttings coming from the drilling of oil wells by treatment of the cuttings with a solvent, which can be compressed to the liquid state, at a pressure value ranging from 45 to 80 bar and a temperature corresponding to the saturation value.

Abstract translation: 通过用压力为45至80巴的压力值和可压缩到液态的溶剂处理切屑，从油井的钻井中除去和回收油性组分的方法， 对应于饱和度值。

公开(公告)号：US20040030205A1

公开(公告)日：2004-02-12

申请号：US10443095

申请日：2003-05-22

Applicant: ENI S.p.A. ,  ENITECNOLOGIE S.p.A.

Inventor： Silvia Pavoni ,  Vincenzo Calemma

IPC: C10L001/16

CPC classification number: C10L1/08

Abstract: An essentially hydrocarbon composition comprising a refinery liquid fuel and from 1 to 25% by weight of a medium distillate essentially without alcoholic oxygen obtained starting from the product of a Fischer-Tropsch-type synthesis. This composition surprisingly has enhanced lubricating properties with respect to both of the original components and can advantageously be used as a fuel for Diesel or turbine engines, with an evident decrease in wear of the mobile parts in contact therewith.

Abstract translation: 基本上是烃组合物，其包含炼制液体燃料和1至25重量％的基本上不含由费 - 托合成产物获得的醇氧的中等馏出物。 该组合物令人惊讶地具有相对于两种原始组分的增强的润滑性能，并且可以有利地用作柴油或涡轮发动机的燃料，同时与其接触的可移动部件的磨损明显降低。

公开(公告)号：US20040266894A1

公开(公告)日：2004-12-30

申请号：US10845109

申请日：2004-05-14

Applicant: ENI S.p.A. ,  INSTITUT FRANCAIS DU PETROLE ,  ENITECNOLOGIE S.p.A.

Inventor： Giuseppe Belmonte ,  Vincenzo Calemma

IPC: C07C027/06

CPC classification number: C10G2/342

Abstract: Hydrocarbons are prepared, which are liquid at the reaction temperature, by feeding synthesis gas into three-phase turbulent reactors in which the solid phase, consisting of the catalyst in the form of particles, is kept in suspension in the liquid phase by the rising synthesis gas. The reaction product is extracted in continuous, together with the catalyst dispersed therein, and sent to a separation section which comprises a primary filtration unit and a micro/ultra-filtration unit.

Abstract translation: 制备在反应温度下为液体的烃，通过将合成气送入三相湍流反应器中，其中将由颗粒形式的催化剂组成的固相通过上升合成保持在液相中悬浮 加油站。 反应产物与分散在其中的催化剂一起连续萃取，并送到包含初级过滤单元和微/超滤单元的分离段。

公开(公告)号：US20040248726A1

公开(公告)日：2004-12-09

申请号：US10891069

申请日：2004-07-15

Applicant: AGIP PETROLI S.p.A. ,  ENITECNOLOGIE S.p.A.

Inventor： Laura Zanibelli ,  Marco Ferrari ,  Virginio Arrigoni

IPC: C10G045/04 ,  C10G045/12

CPC classification number: C10G45/12 ,  B01J29/7815 ,  B01J35/1042 ,  B01J37/033 ,  B01J37/036 ,  B01J2229/18 ,  B01J2229/20 ,  B01J2229/34 ,  B01J2229/42 ,  C10G45/08 ,  C10G45/64 ,  C10G49/08

Abstract: The present invention relates to a catalytic composition which comprises a beta zeolite, a metal of group VIII, a metal of group VI B and optionally one or more oxides as carrier. The catalytic system of the present invention can be used for the hydrotreating of hydrocarbon mixtures and more specifically in the upgrading of hydrocarbon mixtures having boiling ranges within the range of 35null to 250null C., containing sulfur impurities, i.e. in hydrodesulfuration with contemporaneous skeleton isomerization and a reduced hydrogenation degree of olefins contained in said hydrocarbon mixtures, the whole process being carried out in a single step.

Abstract translation: 本发明涉及一种催化剂组合物，其包含β-沸石，VIII族金属，VIB族金属和任选的一种或多种氧化物作为载体。 本发明的催化体系可用于烃混合物的加氢处理，更具体地，用于提高沸程在35℃至250℃范围内的含硫杂质的烃混合物，即与同时代骨架加氢脱硫 异构化和所述烃混合物中包含的烯烃的氢化度降低，整个过程在一个步骤中进行。

公开(公告)号：US20040195152A1

公开(公告)日：2004-10-07

申请号：US10736737

申请日：2003-12-17

Applicant: ENI S.p.A. ,  ENITECNOLOGIE S.p.A.

Inventor： Felicia Massetti ,  Alessandro Nardella ,  Raffaele Tomaciello ,  Paolo Pallado ,  Alberto Guarneri

IPC: C23G001/36 ,  B08B007/04

CPC classification number: E21B21/066 ,  B01D11/0219 ,  B01D11/0488 ,  B01D11/0492

Abstract: Method for the removal and recovery of the oily component from cuttings coming from the drilling of oil wells by treatment of the cuttings with a solvent, which can be compressed to the liquid state, at a pressure value ranging from 45 to 80 bar and a temperature corresponding to the saturation value.

Abstract translation: 通过用压力为45至80巴的压力值和可压缩到液态的溶剂处理切屑，从油井的钻井中除去和回收油性组分的方法， 对应于饱和度值。

公开(公告)号：US20040127762A1

公开(公告)日：2004-07-01

申请号：US10736594

申请日：2003-12-17

Applicant: POLIMERI EUROPA S.p.A. ,  ENITECNOLOGIE S.p.A.

Inventor： Leonardo Dalloro ,  Alberto Cesana ,  Roberto Buzzoni ,  Franco Rivetti ,  Caterina Rizzo ,  Virginio Arrigoni ,  Carlo Perego

IPC: C07C005/22 ,  C07C005/52

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 400null C., at a pressure ranging from 1 to 50 bar, with a weight space velocity ranging from 0.1 to 20 hoursnull1 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，而不使用任何进一步的化合物，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，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。

公开(公告)号：US20030096712A1

公开(公告)日：2003-05-22

申请号：US10277105

申请日：2002-10-22

Applicant: ENITECNOLOGIE S.p.A.

Inventor： Armando Marcotullio ,  Enrico Borgarello

IPC: C09K007/02

CPC classification number: F17D1/17

Abstract: Process for recovering and moving refinery tar by the formation of oil in water dispersions of the above tar, the above dispersions having a water content of at least 20% by weight, and the dispersing agent being selected from salts of alkaline metals and ammonium, and relative mixtures, of the condensates of naphthalenesulfonic acid with formaldehyde, which comprises: a) fluidification of the tar by heating to a temperature at least equal to its softening point; b) mixing the tar thus fluidified with the desired quantity of water and dispersing agent until an oil in water dispersion is formed; c) recovery and moving of the tar in the form of the oil in water dispersion formed in step (b).

Abstract translation: 通过在上述焦油的水分散体中形成油来回收和移动精炼焦油的方法，上述分散体的水含量为至少20重量％，分散剂选自碱金属和铵的盐，以及 萘磺酸与甲醛的缩合物的相对混合物，其包括：a）通过加热至至少等于其软化点的温度使焦油流化; b）将如此流化的焦油与所需量的水和分散剂混合，直到形成水分散体; c）以步骤（b）中形成的水​​分散体形式的焦油的回收和移动。

公开(公告)号：US20040225170A1

公开(公告)日：2004-11-11

申请号：US10786553

申请日：2004-02-26

Applicant: POLIMERI EUROPA S.p.A. ,  ENITECNOLOGIE S.p.A.

Inventor： Leonardo Dalloro ,  Alberto Cesana ,  Roberto Buzzoni ,  Franco Rivetti ,  Giovanni Antonio Fois ,  Caterina Rizzo ,  Virginio Arrigoni

IPC: C07C002/64 ,  C07C004/06

CPC classification number: C07C5/2737 ,  C07C2529/40 ,  C07C15/02

Abstract: A process is described for the synthesis of mesitylene, characterized in that mesitylene is obtained starting exclusively from pseudocumene, without the use of any other chemical compound, operating in continuous, at a temperature ranging from 225 to 400null C., at a pressure ranging from 1 to 50 bar, at a weight space velocity ranging from 0.1 to 10 hoursnull1, and in the presence of a catalyst containing a zeolite selected from ZSM-5 zeolite having a crystal lattice based on silicon oxide and aluminum oxide, and ZSM-5 zeolite modified by the partial or total substitution of Si with a tetravalent element such as Ti or Ge and/or the partial or total substitution of Al with other trivalent elements, such as Fe, Ga or B.

Abstract translation: 描述了用于合成均三甲苯的方法，其特征在于，均匀地从假阳离子开始获得均三甲苯，而不使用在225-400℃的温度范围内连续操作的任何其它化合物，在压力范围 1至50巴，重量空间速度为0.1至10小时-1，并且在含有选自具有基于氧化硅和氧化铝的晶格的ZSM-5沸石的沸石的催化剂存在下， 和通过Si与四价元素如Ti或Ge的部分或全部取代和/或Al与其它三价元素如Fe，Ga或B的部分或全部取代而改性的ZSM-5沸石。

公开(公告)号：US20040104150A1

公开(公告)日：2004-06-03

申请号：US10722411

申请日：2003-11-28

Applicant: ENITECNOLOGIE S.p.A.

Inventor： Armando Marcotullio ,  Enrico Borgarello

IPC: F17D001/17 ,  F17D001/18

CPC classification number: F17D1/17

Abstract: Process for recovering and moving refinery tar by the formation of oil in water dispersions of the above tar, the above dispersions having a water content of at least 20% by weight, and the dispersing agent being selected from salts of alkaline metals and ammonium, and relative mixtures, of the condensates of naphthalenesulfonic acid with formaldehyde, which comprises: a) fluidification of the tar by heating to a temperature at least equal to its softening point; b) mixing the tar thus fluidified with the desired quantity of water and dispersing agent until an oil in water dispersion is formed; c) recovery and moving of the tar in the form of the oil in water dispersion formed in step (b).

Abstract translation: 通过在上述焦油的水分散体中形成油来回收和移动精炼焦油的方法，上述分散体的水含量为至少20重量％，分散剂选自碱金属和铵的盐，以及 萘磺酸与甲醛的缩合物的相对混合物，其包括：a）通过加热至至少等于其软化点的温度使焦油流化; b）将如此流化的焦油与所需量的水和分散剂混合，直到形成水分散体; c）以步骤（b）中形成的水​​分散体形式的焦油的回收和移动。

公开(公告)号：US20030109376A1

公开(公告)日：2003-06-12

申请号：US10309145

申请日：2002-12-04

Applicant: ENICHEM S.p.A ,  ENITECNOLOGIE S.p.A.

Inventor： Paolo Pollesel ,  Caterina Rizzo ,  Carlo Perego ,  Renato Paludetto ,  Gastone Del Piero

IPC: C10G011/04 ,  B01J021/16

CPC classification number: C10G11/04 ,  B01J23/002 ,  B01J23/02 ,  B01J2523/00 ,  C01F7/164 ,  C01P2002/70 ,  B01J2523/23 ,  B01J2523/31

Abstract: Catalyst for steam cracking reactions consisting of pure mayenite having the general formula:12CaO.7Al2O3having an X-ray diffraction spectrum as indicated in Table I, obtained with a preparation process comprising the following steps: dissolution of salts containing calcium and aluminum with water; completing of the dissolved salts by means of polyfunctional organic hydroxyacids; drying of the solution resulting from the completing in order to obtain a solid precursor product; calcination of the solid precursor product at a temperature ranging from 1300 to 1400null C. for at least two hours.

Abstract translation: 用于蒸汽裂解反应的催化剂，其由具有以下通式的纯钙铝石组成：具有表C所示的X射线衍射光谱的12CaO.7Al 2 O 3，其制备方法包括以下步骤：用水溶解含钙和铝的盐; 通过多官能有机羟基酸完成溶解的盐; 干燥由此完成的溶液，以获得固体前体产物; 在1300〜1400℃的温度下煅烧固体前体产物至少2小时。