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    Corrosion resistant bimetallic tube and application in its tube bundle unit
    2.
    发明专利
    Corrosion resistant bimetallic tube and application in its tube bundle unit 有权
    耐腐蚀双金属管及其管件组件应用

    公开(公告)号：JP2008045739A

    公开(公告)日：2008-02-28

    申请号：JP2007167748

    申请日：2007-06-26

    Applicant: Snamprogetti Spa ,  スナムプロゲッティ、ソシエタ、ペル、アチオニSnamprogetti S.P.A.

    Inventor： GIANAZZA ALESSANDRO ,  MAIRANO LUCA ,  MERELLI GUISEPPE ,  SANFILIPPO DOMENICO

    IPC: F16L9/02 ,  B21C37/06 ,  B23K9/00 ,  B23K101/06 ,  B23K101/14 ,  C07C269/00 ,  C07C271/02

    CPC classification number: F28F19/06 ,  B23P15/26 ,  F16L13/0236 ,  F28F9/18 ,  F28F21/081 ,  F28F21/084 ,  F28F21/086 ,  F28F2275/062 ,  F28F2275/068 ,  Y02P80/156 ,  Y10T29/49718

    Abstract: PROBLEM TO BE SOLVED: To provide a suitable bimetallic tube for the tube bundle unit of heat exchanger, the unit which is operated under the high pressure condition and the high aggressive condition of erosiveness and corrosiveness. SOLUTION: The unit consists of at least one tubular part of the first metal which is tolerant to the corrosive and/or erosive action of the treated fluid in contact, and the tubular component is a bimetallic tube having a near area to one covered end with the second metal layer at least or the distal end when the exterior is seal welded to the different support body from the first metal. Moreover, the tube bundle unit is used for handling the heat exchanger in high temperature and high pressure under the conditions of high aggressive treated fluid, and the tube bundle contains at least one tube having the above characteristics. The unit is used especially as a dissolution unit in a cycle of the heat exchanger mechanism and a urea composition process of high pressure, high temperature, and high aggressive condition of the treated fluid, and the tube bundle contains at least one tube having the above characteristics. COPYRIGHT: (C)2008,JPO&INPIT

    Abstract translation: 要解决的问题：为热交换器的管束单元提供合适的双金属管，在高压条件下运行的单元和腐蚀性和腐蚀性的高侵蚀性。 解决方案：该单元由第一金属的至少一个管状部分组成，其耐受经处理流体接触的腐蚀和/或腐蚀作用，并且管状部件是双金属管，其具有近一个 当外部与第一金属密封焊接到不同的支撑体时，至少或远端具有第二金属层的覆盖端。 此外，管束单元在高侵蚀性处理液的条件下用于处理高温高压的热交换器，管束包含至少一个具有上述特征的管。 该单元特别用作热交换器机构的循环中的溶解单元和被处理流体的高压，高温和高侵蚀性条件的尿素组合工艺，并且管束包含至少一个具有上述管的管 特点。 版权所有（C）2008，JPO＆INPIT

    Method for producing synthesis gas by partial oxidation of heavy charge, such as heavy crude oil, distillation residue and the like
    4.
    发明专利
    Method for producing synthesis gas by partial oxidation of heavy charge, such as heavy crude oil, distillation residue and the like 有权
    通过部分氧化重金属（如重油，石油渣等）生产合成气的方法

    公开(公告)号：JP2005002306A

    公开(公告)日：2005-01-06

    申请号：JP2003202524

    申请日：2003-07-28

    Applicant: Snamprogetti Spa ,  スナムプロゲッティ、ソシエタ、ペル、アチオニSnamprogetti S.P.A.

    Inventor： SANFILIPPO DOMENICO ,  MIRACCA IVANO

    IPC: B01J3/00 ,  B01J19/00 ,  C01B3/24 ,  C01B3/36 ,  C10K1/02 ,  C10K1/06

    CPC classification number: B01J19/0013 ,  B01J2219/00123 ,  B01J2219/00243 ,  C01B3/36 ,  C10K1/06

    Abstract: PROBLEM TO BE SOLVED: To provide a method for producing a synthetic gas from a heavy charge with stable function of the system, almost no problem in foaming and no difficulty in adjusting a water level, in a cooling separation process of a method for producing a synthesis gas by partially oxidizing the heavy charge such as heavy crude oil, distillation residue or the like.
    SOLUTION: The method for producing the synthesis gas includes a process in which the heavy charge is partially oxidized at ≥1,000°C and ≥20 atm. in the presence of steam using oxygen or a highly oxygen-containing air, the obtained synthetic gas 1 is cooled by directly pouring water 2 to the synthesis gas 1, subsequently cooled gas 4 and water 3 are separated through a ring formed between an adduction tube TA and a concentric tube TC installed around the adduction tube and having both open ends. The distance (L) between the lower end of the adduction tube and the lower end of the open concentric tube is equal to or larger than x [x is expressed by x=0.026F+0.15 and varies depending on a gas flow ratio (F)(expressed by kg/h/cm
    2 )] times of the diameter (D) of the lower end of the adduction pipe.
    COPYRIGHT: (C)2005,JPO&NCIPI

    Abstract translation: 解决问题：为了提供一种由系统功能稳定的重负荷生产合成气的方法，在方法的冷却分离过程中几乎没有发泡问题和调节水位难度 用于通过部分氧化重质原油，蒸馏残余物等重质装料来生产合成气。 解决方案：合成气的制备方法包括重荷在≥1000℃和≥20atm下部分氧化的方法。 在使用氧气或高含氧空气的蒸汽的存在下，通过将合成气1直接倒入合成气1中来冷却所得的合成气体1，随后将冷却气体4和水3分离通过形成在内装管 TA和同心管TC安装在内收管周围并且具有两个开口端。 内接管的下端与开放的同心管的下端之间的距离（L）等于或大于x [x由x = 0.026F + 0.15表示，并且根据气体流量比（F ）（以kg / h / cm 2表示）SP吸收管内壁直径（D）。 版权所有（C）2005，JPO＆NCIPI

    Catalytic system and process for the production of hydrogen
    5.
    发明申请
    Catalytic system and process for the production of hydrogen 审中-公开
    催化系统和生产氢气的方法

    公开(公告)号：US20040152790A1

    公开(公告)日：2004-08-05

    申请号：US10768103

    申请日：2004-02-02

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

    Inventor： Ugo Cornaro ,  Domenico Sanfilippo

    IPC: C07C027/06

    CPC classification number: B01J23/83 ,  B01J23/005 ,  B01J23/745 ,  B01J23/78 ,  B01J23/80 ,  B01J35/08 ,  C01B3/063 ,  Y02E60/36

    Abstract: Catalytic system for the production of hydrogen consisting of an active component based on iron and a micro-spheroidal carrier based on alumina and represented by the following formula nullFex1Mx2Qx3Dx4Alx5nullOy wherein xi with inull1.5 represent the atomic percentages assuming values which satisfy the equation nullxinull100. y is the value required by the oxidation number with which the components are present in the formulate, x1 is the atomic percentage with which Fe is present in the formulate and ranges from 5 to 80, preferably from 20 to 50, M is Cr and/or Mn, x2 ranges from 0 to 30, preferably from 0 to 10, Q is La, Lanthanides (with Ce particularly preferred), Zr or a combination thereof, x3 ranges from 0 to 30, preferably from 0 to 10, D is Mg, Ca, Ba, Co, Ni, Cu, Zn or combinations thereof, x4 ranges from 0 to 35, preferably from 5 to 25, x5 is the atomic percentage with which Al is present in the formulate and ranges from 20 to 95, preferably from 50 to 80.

    Abstract translation: 用于生产基于铁的活性组分和基于氧化铝的微球形载体的氢的催化体系，由下式[Fex1Mx2Qx3Dx4Alx5] Oy表示，其中i = 1.5的xi表示原子百分比，假定满足式 Sigmaxi = 100。 y是组分存在于配方中的氧化数所需的值，x1是配制物中Fe存在的原子百分数，范围为5至80，优选为20至50，M为Cr和/ 或Mn，x2为0〜30，优选为0〜10，Q为La，镧系元素（特别优选Ce），Zr或其组合，x3为0〜30，优选为0〜10，D为Mg ，Ca，Ba，Co，Ni，Cu，Zn或其组合，x4的范围为0至35，优选5至25，x5是配位体中Al存在的原子百分比，范围为20至95，优选 从50到80。

    Use of an oxygenated product as a substitute of gas oil in diesel engines
    10.
    发明申请
    Use of an oxygenated product as a substitute of gas oil in diesel engines 有权
    在柴油发动机中使用含氧产品作为瓦斯油的替代品

    公开(公告)号：US20040187380A1

    公开(公告)日：2004-09-30

    申请号：US10716501

    申请日：2003-11-20

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

    Inventor： Domenico Sanfilippo ,  Renata Patrini ,  Mario Marchionna

    IPC: C10L001/18

    CPC classification number: C10L1/1852 ,  C10L1/026 ,  C10L1/1985 ,  C10L10/02

    Abstract: Use of a liquid oxygenated product with a cetane number higher than 50, consisting of one or more compounds selected from dialkyl-polyformals represented by the formula RO(CH2O)mR wherein R is an alkyl chain CnH2nnull1, m is an integer equal to or higher than 2, n is an integer between 1 and 10, as a substitute of gas oil in diesel engines.

    Abstract translation: 使用十五烷值高于50的液体氧化产物，由一种或多种选自式RO（CH 2 O）m R表示的二烷基 - 聚异构体的化合物组成，其中R是烷基链C n H 2n + 1，m是等于 或高于2，n为1〜10的整数，作为柴油发动机中瓦斯油的替代品。

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