Electrode For Photovoltaic Cells And Associated Preparation Process

    公开(公告)号:US20170162337A1

    公开(公告)日:2017-06-08

    申请号:US15129905

    申请日:2015-04-15

    申请人: ENI S.P.A

    IPC分类号: H01G9/20

    CPC分类号: H01G9/2022 Y02E10/542

    摘要: The present invention relates to an electrode comprising a conductive material and characterised by the fact of containing a porous crosslinked layer of metal particles, said metal particles being fused between them by a part of their outer surface, still leaving the remaining portion of the outer surface free, said particles being characterised in that they contain one or more metals selected from platinum, palladium, gold and mixtures thereof.

    Method for recovering intracellular components from fermented microorganisms
    35.
    发明授权
    Method for recovering intracellular components from fermented microorganisms 有权
    从发酵微生物中回收细胞内成分的方法

    公开(公告)号:US09593067B2

    公开(公告)日:2017-03-14

    申请号:US14442840

    申请日:2013-12-11

    申请人: ENI S.p.A.

    IPC分类号: C12P7/64 C07C67/48 C12N1/06

    摘要: The present invention relates to a method for the recovery of intracellular components of materials of a biological origin, such as yeasts, algae, bacteria and/or mildews, after fermentation/cultivation, which comprises a thermal lysing treatment via nebulization and the use of a nebulization solvent capable of extracting said intracellular components once the nebulization has been completed.

    摘要翻译: 本发明涉及在发酵/培养后回收生物来源物质如酵母,藻类,细菌和/或霉菌的细胞内组分的方法,其包括通过雾化的热裂解处理和使用 一旦雾化完成,能够提取所述细胞内组分的雾化溶剂。

    PROCESS FOR THE REFINING OF CRUDE OIL
    38.
    发明申请
    PROCESS FOR THE REFINING OF CRUDE OIL 审中-公开
    原油精炼工艺

    公开(公告)号:US20160369181A1

    公开(公告)日:2016-12-22

    申请号:US14902204

    申请日:2014-07-04

    申请人: ENI S.p.A.

    IPC分类号: C10G65/00

    摘要: Process for the refining of crude oil comprising at least one atmospheric distillation unit for separating the various fractions, a sub-atmospheric distillation unit, a conversion unit of the heavy fractions obtained, a unit for enhancing the quality of some of the fractions obtained by actions on the chemical composition of their constituents and a unit for the removal of undesired components, characterized in that the sub-atmospheric distillation residue is sent to one of the conversion units, said conversion unit comprises at least one hydroconversion reactor in slurry phase, into which hydrogen or a mixture of hydrogen and ¾ S, is fed, in the presence of a suitable dispersed hydrogenation catalyst with dimensions ranging from 1 nanometer to 30 microns.

    摘要翻译: 用于精炼原油的方法包括至少一个用于分离各种馏分的常压蒸馏装置,亚常压蒸馏装置,所得重馏分的转化装置,用于提高通过动作获得的一些馏分的质量的装置 关于其组分的化学组成和用于除去不期望的组分的单元,其特征在于,将所述次大气压蒸馏残余物送入一个转化单元,所述转化单元包含至少一个浆料相中的加氢转化反应器,其中 氢或氢和¾S的混合物在适当的分散氢化催化剂的存在下进料,其尺寸范围为1纳米至30微米。

    WASTE SLUDGE INCINERATOR USING PYROLYSIS AND GASIFICATION, AND RELATIVE PROCESS

    公开(公告)号:US20160245508A1

    公开(公告)日:2016-08-25

    申请号:US15025835

    申请日:2014-10-02

    申请人: ENI S.P.A.

    摘要: The present invention relates to reaction equipment for the treatment of organic and/or inorganic waste of refineries or petrochemical plants comprising: •—a drying and pyrolysis device (4) which rotates around its longitudinal, tilted rotation axis (A), •—a gasification device (6) which rotates around its longitudinal, horizontal rotation axis (B), •—a combustion device (14) comprising a burner (13) having a longitudinal horizontal axis (C), •—at least one settling chamber (15) for the collection of intermediate solid residues and the accumulation of intermediate gaseous reaction products, •—at least one outlet duct of the gaseous end-products (16), at least one outlet duct of the solid end-products (7), and at least one inlet duct of the feedstock (2) •—said combustion device (14), drying and pyrolysis device (4), gasification device (6) are physically separated and positioned on three different levels, •—the longitudinal rotation axis (A) of the drying and pyrolysis device (4) is tilted with respect to both the longitudinal rotation axis (B) of the gasification device (6) and also with respect to the longitudinal axis (C) of the combustion device (14), •—the longitudinal rotation axis (B) of the gasification device (6) is parallel to the longitudinal axis (C) of the combustion device (14), •—the combustion device (14) is in fluid communication with the drying and pyrolysis device (4), •—the drying and pyrolysis device (4) comprises, in its interior, a first indirect heat exchange device (3) in which the combustion fumes coming from the combustion device (14) flow, •—at least one settling chamber (15) in fluid communication with said drying and pyrolysis device (4) and with said gasification device (6) and with said combustion device (14), •—conveying means (5) are positioned in the settling chamber (15) and put the drying and pyrolysis device (4) in fluid communication with the gasification device, •—it comprises a second heat exchange device (12) in fluid communication with the first indirect heat exchange device (3) and the combustion device (14), •—it comprises means for the suction of the intermediate gaseous reaction products, said means being positioned in the settling chamber (15).