公开(公告)号：WO2007057151A3

公开(公告)日：2007-07-26

申请号：PCT/EP2006010893

申请日：2006-11-13

Applicant: SNAM PROGETTI ,  DI GIROLAMO MARCO ,  SANFILIPPO DOMENICO ,  CONTE MASSIMO

Inventor： DI GIROLAMO MARCO ,  SANFILIPPO DOMENICO ,  CONTE MASSIMO

IPC: C07C2/08 ,  C10G50/00

CPC classification number: C07C2/28 ,  C07C7/06 ,  C07C9/21 ,  C07C2531/10 ,  C10G50/00 ,  C10G2400/22

Abstract: A process is described for the separation of C 5 hydrocarbons present, in a quantity ranging from 0.2 to 20 % by weight, in streams prevalently containing C 4 products used for the production of high-octane hydrocarbon compounds, by the selective dimerization of isobutene, characterized in that the dimerization reaction is carried out in the presence of linear and branched alcohols and alkyl ethers in a quantity which is such as to have a molar ratio alcohols/alkyl ethers/isobutene in the feeding higher than 0.01.

Abstract translation: 描述了用于分离存在的C 5 -C 5烃的方法，其量为0.2至20重量％，流体中普遍含有用于生产的C 4 S 3产物 的高辛烷烃化合物，通过选择性二聚异丁烯，其特征在于二聚反应在直链和支链醇和烷基醚的存在下进行，其量可以使醇/烷基醚的摩尔比 /异丁烯在饲料中高于0.01。

公开(公告)号：WO03053567A3

公开(公告)日：2003-10-02

申请号：PCT/EP0214816

申请日：2002-12-18

Applicant: SNAM PROGETTI ,  BARTOLINI ANDREA ,  SANFILIPPO DOMENICO ,  IEZZI RODOLFO

Inventor： BARTOLINI ANDREA ,  SANFILIPPO DOMENICO ,  IEZZI RODOLFO

IPC: B01J23/62 ,  B01J23/34 ,  B01J23/656 ,  B01J23/92 ,  B01J23/96 ,  B01J38/12 ,  C07B61/00 ,  C07C5/333 ,  C07C11/04 ,  C07C15/46

CPC classification number: B01J23/96 ,  B01J23/34 ,  B01J23/6562 ,  C07C5/3332 ,  C07C2521/04 ,  C07C2523/04 ,  C07C2523/08 ,  C07C2523/34 ,  C07C2523/42 ,  Y02P20/584 ,  C07C15/46

Abstract: Process for the catalytic dehydrogenation of alkylaromatic hydrocarbons optionally mixed with ethane which comprises: A) dehydrogenating the hydrocarbon stream, optionally mixed with an inert gas, in a fluid bed reactor in the pres­ence of a catalytic composition based on gallium and manganese supported on alumina modified with silica, at a temperature ranging from 400 to 700°C, at a total pressure ranging from 0.1 to 3 ata and with a GHSV (Gas Hourly Space Velocity) ranging from 50 to 10,000 h ; and B) regenerating and heating the catalyst, by means of the catalytic oxidation of a fuel, in a fluid bed regenera­tor at a temperature higher than 400°C.

Abstract translation: 用于任选与乙烷混合的烷基芳烃的催化脱氢方法，该方法包括：A）在流化床反应器中在基于负载在氧化铝上的镓和锰的催化组合物存在下，将任选与惰性气体混合的烃流脱氢改性 二氧化硅，温度范围为400-700℃，总压力为0.1至3ata，GHSV（气时空速）为50至10,000h -1; 和B）在温度高于400℃的流化床再生器中，通过催化氧化燃料来再生和加热催化剂。

公开(公告)号：WO2003053567A2

公开(公告)日：2003-07-03

申请号：PCT/EP2002/014816

申请日：2002-12-18

Applicant: SNAMPROGETTI S.p.A. ,  BARTOLINI, Andrea ,  SANFILIPPO, Domenico ,  IEZZI, Rodolfo

Inventor： BARTOLINI, Andrea ,  SANFILIPPO, Domenico ,  IEZZI, Rodolfo

IPC: B01J23/34

CPC classification number: B01J23/96 ,  B01J23/34 ,  B01J23/6562 ,  C07C5/3332 ,  C07C2521/04 ,  C07C2523/04 ,  C07C2523/08 ,  C07C2523/34 ,  C07C2523/42 ,  Y02P20/584 ,  C07C15/46

Abstract: Process for the catalytic dehydrogenation of alkylaromatic hydrocarbons optionally mixed with ethane which comprises: A) dehydrogenating the hydrocarbon stream, optionally mixed with an inert gas, in a fluid bed reactor in the pres­ence of a catalytic composition based on gallium and manganese supported on alumina modified with silica, at a temperature ranging from 400 to 700°C, at a total pressure ranging from 0.1 to 3 ata and with a GHSV (Gas Hourly Space Velocity) ranging from 50 to 10,000 h -1 ; and B) regenerating and heating the catalyst, by means of the catalytic oxidation of a fuel, in a fluid bed regenera­tor at a temperature higher than 400°C.

Abstract translation: 用于任选与乙烷混合的烷基芳烃的催化脱氢方法，其包括：在流化床反应器中，在基于负载在氧化铝上的载体上的载体上的镓和锰的催化组合物存在下，将烃流任选地与惰性气体混合， 二氧化硅，温度范围为400-700℃，总压力为0.1至3ata，GHSV气体小时空速为50至10,000h-1，B为催化剂再生和加热，借助于 在高于400℃的温度下在流化床再生器中催化氧化燃料。

公开(公告)号：WO2010006757A1

公开(公告)日：2010-01-21

申请号：PCT/EP2009/005103

申请日：2009-07-13

Applicant: SAIPEM S.p.A. ,  SANFILIPPO, Domenico ,  MAIRANO, Luca ,  GIANAZZA, Alessandro ,  CARLESSI, Lino

Inventor： SANFILIPPO, Domenico ,  MAIRANO, Luca ,  GIANAZZA, Alessandro ,  CARLESSI, Lino

IPC: F28F19/06 ,  F28D7/16

CPC classification number: F28F19/06 ,  B01J19/02 ,  B01J19/2425 ,  B01J2219/0236 ,  F28D7/16 ,  F28F9/02 ,  F28F9/0229 ,  F28F2265/16 ,  Y10T29/49391 ,  Y10T29/49393

Abstract: Tube-bundle equipment for heat exchange operations at high pressures and temperatures, under conditions of high aggressiveness of the process fluids, comprising a titanium lining (11) and a series of tubes (1) consisting of at least one layer of zirconium (2), positioned in contact with said fluids, wherein the tube plate on which said tubes are inserted comprises an outer layer (S) of zirconium or an alloy thereof and an underlying layer (5) of titanium welded to the lining of the equipment. Said equipment is particularly used as a heat exchanger, for example as a stripper, in the high-pressure cycle of urea syntheses processes.

Abstract translation: 包括钛衬里（11）和由至少一层锆（2）组成的一系列管（1）的管道束设备，用于在高压和高温下进行的热交换操作， 定位成与所述流体接触，其中所述管被插入其上的管板包括锆或其合金的外层（S）和焊接到设备衬里的钛的下层（5）。 在尿素合成工艺的高压循环中，所述设备特别用作热交换器，例如作为汽提塔。

公开(公告)号：WO2007057153A1

公开(公告)日：2007-05-24

申请号：PCT/EP2006/010895

申请日：2006-11-14

Applicant: SNAMPROGETTI S.p.A. ,  DI GIROLAMO, Marco ,  SANFILIPPO, Domenico ,  CONTE, Massimo

Inventor： DI GIROLAMO, Marco ,  SANFILIPPO, Domenico ,  CONTE, Massimo

IPC: C07C2/08 ,  C10G50/00 ,  C10L1/06

CPC classification number: C07C9/21 ,  C10G50/00 ,  C10G2300/1088 ,  C10G2300/4018 ,  C10G2300/4081 ,  C10G2300/4087 ,  C10G2300/805 ,  C10G2400/02 ,  C10L1/06 ,  Y02P20/127

Abstract: A process is described for the production of high-octane hydrocarbon compounds by means of the selective dimerization of isobutene, in the presence of C 5 hydrocarbons and oxygenated compounds (branched alcohols or alternatively blends of linear or branched alcohols and alkyl ethers) characterized in that it utilizes a catalytic distillation as second reaction step.

Abstract translation: 描述了在C 5 C 5烃和含氧化合物（支链醇或可选择的直链或支链醇的共混物）的存在下，通过异丁烯的选择性二聚制备高辛烷烃化合物的方法 和烷基醚），其特征在于它利用催化蒸馏作为第二反应步骤。

公开(公告)号：WO2005075063A2

公开(公告)日：2005-08-18

申请号：PCT/EP2005/001258

申请日：2005-02-07

Applicant: SNAMPROGETTI S.p.A. ,  SANFILIPPO, Domenico ,  MIRACCA, Ivano ,  CAPONE, Guido ,  FANTINUOLI, Vincenzino

Inventor： SANFILIPPO, Domenico ,  MIRACCA, Ivano ,  CAPONE, Guido ,  FANTINUOLI, Vincenzino

IPC: B01J

CPC classification number: B01J8/0055 ,  B01J8/26 ,  B01J8/388 ,  C07C5/321 ,  C07C5/324 ,  Y02P20/52 ,  Y02P20/584 ,  C07C11/04 ,  C07C15/46

Abstract: Reactor-regenerator device, comprising at least one reactor for catalytic dehydrogenation reactions of hydrocarbons and at least one regenerator of the catalyst o the "fast riser" type wherein the regenerator-riser is a substan­tially tubular apparatus for chemical reactions which com­prise a gaseous phase in close contact with a solid phase, wherein gas phase and solid particles move upwards in co­current flow.

Abstract translation: 反应器 - 再生器装置，包括至少一个用于烃和至少一种催化剂的“快速提升管”类型的再生器的催化脱氢反应的反应器，其中再生器 - 提升管是用于化学反应的基本上管状的装置，其包括气相 与固相紧密接触，其中气相和固体颗粒以并流流动向上移动。

公开(公告)号：WO2007057151A2

公开(公告)日：2007-05-24

申请号：PCT/EP2006/010893

申请日：2006-11-13

Applicant: SNAMPROGETTI S.p.A. ,  DI GIROLAMO, Marco ,  SANFILIPPO, Domenico ,  CONTE, Massimo

Inventor： DI GIROLAMO, Marco ,  SANFILIPPO, Domenico ,  CONTE, Massimo

CPC classification number: C07C2/28 ,  C07C7/06 ,  C07C9/21 ,  C07C2531/10 ,  C10G50/00 ,  C10G2400/22

Abstract: A process is described for the separation of C 5 hydrocarbons present, in a quantity ranging from 0.2 to 20 % by weight, in streams prevalently containing C 4 products used for the production of high-octane hydrocarbon compounds, by the selective dimerization of isobutene, characterized in that the dimerization reaction is carried out in the presence of linear and branched alcohols and alkyl ethers in a quantity which is such as to have a molar ratio alcohols/alkyl ethers/isobutene in the feeding higher than 0.01.

Abstract translation: 描述了一种用于分离存在的C 5烃的方法，所述烃以0.2至20重量％的量存在于主要含有C 4， 通过异丁烯的选择性二聚作用用于生产高辛烷烃化合物的产物，其特征在于二聚反应在直链和支链醇和烷基醚的存在下进行，其量为 在进料中醇/烷基醚/异丁烯的摩尔比高于0.01。

公开(公告)号：WO2005075063A3

公开(公告)日：2007-04-26

申请号：PCT/EP2005001258

申请日：2005-02-07

Applicant: SNAM PROGETTI ,  SANFILIPPO DOMENICO ,  MIRACCA IVANO ,  CAPONE GUIDO ,  FANTINUOLI VINCENZINO

Inventor： SANFILIPPO DOMENICO ,  MIRACCA IVANO ,  CAPONE GUIDO ,  FANTINUOLI VINCENZINO

IPC: B01J8/00 ,  B01J8/26 ,  B01J8/38 ,  B01J23/656 ,  B01J38/30 ,  C07C5/32 ,  C07C5/333

CPC classification number: B01J8/0055 ,  B01J8/26 ,  B01J8/388 ,  C07C5/321 ,  C07C5/324 ,  Y02P20/52 ,  Y02P20/584 ,  C07C11/04 ,  C07C15/46

Abstract: Reactor-regenerator device, comprising at least one reactor for catalytic dehydrogenation reactions of hydrocarbons and at least one regenerator of the catalyst o the "fast riser" type wherein the regenerator-riser is a substan­tially tubular apparatus for chemical reactions which com­prise a gaseous phase in close contact with a solid phase, wherein gas phase and solid particles move upwards in co­current flow.

Abstract translation: 反应器 - 再生器装置，包括至少一个用于烃和至少一种催化剂的“快速提升管”类型的再生器的催化脱氢反应的反应器，其中再生器 - 提升管是用于化学反应的基本上管状的装置，其包括气相 与固相紧密接触，其中气相和固体颗粒以并流流动向上移动。