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    METHOD, SERVER, COMPUTER-READABLE COMMAND, AND RECORDING MEDIUM FOR PROVIDING RECOMMENDED OPERATION CONDITION FOR PLANT
    1.
    发明公开
    METHOD, SERVER, COMPUTER-READABLE COMMAND, AND RECORDING MEDIUM FOR PROVIDING RECOMMENDED OPERATION CONDITION FOR PLANT 审中-公开

    公开(公告)号：EP3633591A1

    公开(公告)日：2020-04-08

    申请号：EP18806072.7

    申请日：2018-05-23

    申请人： Cosmo Oil Co., Ltd.

    发明人： NAKAJIMA Nobumasa ,  KIKUCHI Susumu ,  IDEI Kazuo

    IPC分类号： G06Q50/04 ,  C10G45/00 ,  G05B23/02

    摘要： Provided is a method for providing a recommended operating condition with which an oil refinery device can be operated more efficiently. A server 20: acquires past operational data for a device, a scheduled operating condition which is an operation condition for the device scheduled by a user, and plant information including at least a usage expiry time of the device; creates a user-specific catalyst deterioration function from the past operational data; calculates, on the basis of the catalyst deterioration function, the plant information, and the schedule operating condition, a recommended operating condition that achieves a catalyst lifetime which is later than the usage expiry time of the device and is earlier than the catalyst lifetime when the device is operated under a scheduled operating condition calculated on the basis of the scheduled operating condition and the catalyst deterioration function; and transmits the recommended operating condition to a user terminal.

    SERVER, METHOD, AND PROGRAM FOR SUPPLYING DESULFURIZATION CATALYST-RELATED INFORMATION, AND COMPUTER-READABLE RECORDING MEDIUM RECORDING SAME
    2.
    发明公开
    SERVER, METHOD, AND PROGRAM FOR SUPPLYING DESULFURIZATION CATALYST-RELATED INFORMATION, AND COMPUTER-READABLE RECORDING MEDIUM RECORDING SAME 审中-公开

    公开(公告)号：EP3561759A1

    公开(公告)日：2019-10-30

    申请号：EP17882586.5

    申请日：2017-12-20

    申请人： Cosmo Oil Co., Ltd.

    发明人： NAKAJIMA Nobumasa ,  KIKUCHI Susumu ,  IDEI Kazuo

    IPC分类号： G06Q50/04 ,  C10G45/72

    摘要： Provided are a desulfurization catalyst performance prediction system and a desulfurization catalyst performance prediction program with which the performance of a desulfurization catalyst is predicted with high accuracy, without performing a complicated process such as a plant simulation. A server, which is connected to a user terminal via a network, and which supplies a desulfurization catalyst lifetime of a user plant to a user on the basis of desulfurization catalyst bench plant data and a desulfurization catalyst lifetime function, is equipped with a processor and a storage means that stores computer-readable command. When a computer-readable command is executed by the processor, the server receives user plant-related data and a user desulfurization catalyst performance prediction condition from the user terminal to the user plant on the basis of a comparison between the desulfurization catalyst bench plant data and the obtained user plant-related data, calculates a catalyst lifetime for the user's desulfurization catalyst on the basis of the obtained user desulfurization catalyst performance prediction condition and the user desulfurization catalyst lifetime function, and transmits the calculated catalyst lifetime to the user terminal.

    HYDROGENATION CATALYST FOR HEAVY HYDROCARBON OIL AND HYDROGENATION METHOD FOR HEAVY HYDROCARBON OIL
    4.
    发明公开
    HYDROGENATION CATALYST FOR HEAVY HYDROCARBON OIL AND HYDROGENATION METHOD FOR HEAVY HYDROCARBON OIL 审中-公开
    FOR重烃油加氢催化剂的重烃油和加氢

    公开(公告)号：EP3050622A1

    公开(公告)日：2016-08-03

    申请号：EP14847966.0

    申请日：2014-09-25

    申请人： Cosmo Oil Co., Ltd.

    发明人： OSAKI, Takayuki ,  NAKAJIMA, Nobumasa

    IPC分类号： B01J23/88 ,  B01J35/10 ,  C10G45/04

    CPC分类号： B01J23/8873 ,  B01J21/04 ,  B01J23/06 ,  B01J23/883 ,  B01J35/0006 ,  B01J35/006 ,  B01J35/023 ,  B01J35/026 ,  B01J35/1014 ,  B01J35/1019 ,  B01J35/1061 ,  B01J37/0009 ,  B01J37/0201 ,  B01J37/0207 ,  B01J37/033 ,  B01J37/04 ,  B01J37/06 ,  B01J37/08 ,  B01J2523/00 ,  C10G45/04 ,  C10G45/08 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  B01J2523/27 ,  B01J2523/31 ,  B01J2523/68 ,  B01J2523/847

    摘要： The purpose of the present invention is to provide: a hydrogenation catalyst capable of improving the storage stability of hydrogenated heavy hydrocarbon oil without reducing desulfurization activity or demetallization activity; and a method for hydrogenation of heavy hydrocarbon oil by using the hydrogenation catalyst, the present invention provides a hydrogenation catalyst for heavy hydrocarbon oil is provided, characterized by: at least one of metals in Group 6 of the periodic table being held by a zinc-containing alumina carrier containing 1% by mass to 15% by mass of zinc oxide particles having an average particle diameter of 2 µm to 12 µm based on the carrier; the average pore diameter being 18 nm to 35 nm, and the specific surface area being 70 m 2 /g to 150 m 2 /g, and a hydrogenation method for heavy hydrocarbon oil is also provided, characterized by a catalytic reaction of heavy hydrocarbon oil in the presence of the hydrogenation catalyst, under the conditions of a temperature of 300 °C to 420°C, a pressure of 3 MPa to 20 MPa, a hydrogen/oil ratio of 400 m 3 /m 3 to 3,000 m 3 /m 3 , and a liquid space velocity of 0.1 h -1 to 3 h -1 .

    摘要翻译： 本发明的目的在于提供：能够提高氢化重质烃油的储存稳定性，而不会降低脱硫活性或脱金属活性的加氢催化剂; 并且通过使用氢化催化剂的重质烃油加氢方法中，本发明提供了一种重质烃油的加氢催化剂提供，其特点：金属中的至少一种在第6组被保持由一种锌元素周期表 含有氧化铝载体含有1质量％至15％的具有上的2微米至12基于载体微米平均粒径的氧化锌颗粒的质量; 因此，平均孔直径为18纳米至35纳米，且比表面积为70米2 /克至150米2 /克，而对于重质烃油的加氢方法被提供，由重质烃油的催化反应为特征的 在氢化催化剂的存在下，在300℃的温度的条件下，以420℃，3MPa的至20MPa，400米3 /米3至3000米3 / m的氢/油比的压力 3，和0.1小时-1至3小时-1的液时空速。

    HYDROCARBON PRODUCTION APPARATUS AND HYDROCARBON PRODUCTION METHOD
    6.
    发明公开
    HYDROCARBON PRODUCTION APPARATUS AND HYDROCARBON PRODUCTION METHOD 审中-公开
    烃生产装置和生产烃的方法

    公开(公告)号：EP2980188A1

    公开(公告)日：2016-02-03

    申请号：EP14772786.1

    申请日：2014-03-19

    申请人： Japan Oil, Gas and Metals National Corporation ,  INPEX Corporation ,  JX Nippon Oil & Energy Corporation ,  Japan Petroleum Exploration Co., Ltd. ,  Cosmo Oil Co., Ltd. ,  Nippon Steel & Sumikin Engineering Co., Ltd.

    发明人： ISHITO, Yukifumi ,  INOUE, Junichi ,  SHINGU, Masaki ,  NAGANO, Haruki ,  TASAKA, Kazuhiko

    IPC分类号： C10G2/00

    CPC分类号： C10G2/342 ,  B01J8/22 ,  C10G2/32

    摘要： In the hydrocarbon-producing apparatus of the present invention, a vapor-liquid separation tank of a second vapor-liquid separation unit is provided with a filling material layer. A vapor-liquid separation tank of the first vapor-liquid separation unit is provided with a first return line. The vapor-liquid separation tank of the second vapor-liquid separation unit is provided with a second return line. A light component of light oil discharged from a bottom of the vapor-liquid separation tank is returned to a portion between a top side above a return-location from the second return line within the vapor-liquid separation tank of the second vapor-liquid separation unit, and a line directly connected with a cooler installed on the first vapor-liquid separation unit through the first return line. A heavy component of light oil discharged from a bottom of the vapor-liquid separation tank of the second vapor-liquid separation unit is returned to the filling material layer through the second return line.

    摘要翻译： 在本发明的烃生产设备中，第二汽液分离单元的汽液分离罐设置有填充材料层。 第一汽液分离单元的汽液分离罐设有第一回流管路。 第二汽液分离单元的汽液分离罐设有第二返回管线。 从气液分离槽的底部排出的轻油的轻组分返回到第二汽液分离的气液分离槽内的来自第二返回线路的返回位置上方的顶侧之间的部分 单元以及与通过第一回流管线安装在第一汽液分离单元上的冷却器直接连接的管线。 从第二汽液分离单元的汽液分离罐的底部排出的轻油的重组分经过第二返回管线返回到填充材料层。