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    • 4. 发明专利
    • PRODUCTION OF HEAVY OIL BASE MATERIAL
    • JPH09263775A
    • 1997-10-07
    • JP7662896
    • 1996-03-29
    • NIPPON OIL CO LTD
    • USHIO MASARUKUBOTA YASUHIROKAMIYA KOZOFUJIYAMA YUICHIRO
    • C10G45/08C10G49/04C10G65/04C10G65/12
    • PROBLEM TO BE SOLVED: To obtain a low sulfur heavy oil base material economically without causing the plugging of pipes downstream of a hydrogenation tower by hydrotreating a specified feedstock oil repeatedly under specified conditions to form a hydrotreated oil. SOLUTION: A feedstock oil (e.g. vacuum residue) having a dry sludge content of 0-5.0mass% and an S content of 1.0-10mass% is hydrotreated in the 1st-stage tower packed with a hydrogenation catalyst (e.g. a catalyst prepared by impregnating an alumina support with NiO and MoO3 ) under elevated pressure at a temperature (the maximum temperature in the catalyst bed) of 390-450 deg.C to obtain a hydrotreated oil having an S content which is at most 30% of that of the feedstock oil and a content (T) of toluene-insolubles of 10 mass ppm or above. This oil is hydrotreated in the 2nd-stage hydrotreatment tower packed with a hydrogenation catalyst under elevated pressure at a temperature (the maximum temperature in the catalyst bed) which is lower than that in the 1st-stage tower by at least 10 deg.C and is lower than 410 deg.C to obtain a hydrotreated oil having an S content of 30% or below and a T which is at most 50% of that of the hydrotreated oil obtained in the 1st stage.
    • 7. 发明专利
    • Method for catalytic reaction of heavy petroleum oil
    • 重油石油催化反应方法
    • JPS5730787A
    • 1982-02-19
    • JP10429480
    • 1980-07-31
    • Nippon Oil Co Ltd
    • USHIO MASARUMORITA TOORUISHII TAKESHIOOISHI YASUYUKI
    • C10G9/24C10G9/00C10G11/00C10G35/04C10G45/00C10G47/00
    • PURPOSE: To improve the utilization efficiency of solid medium in the catalytic reaction of heavy petroleum oil, by separating the magnetizable particulate solid medium coated with the metal deposited from the heavy petroleum oil by the catalytic reaction and the nonmagnetizable particulate solid medium using a magnetic separator, and then reusing the latter medium for the reaction.
      CONSTITUTION: Heavy petroleum oil consisting of petroleum oil containing fractions having boiling point of ≥190°C (or a product obtained therefrom by hydrogenative desulfurization) is made to react in a catalytic reactor containing particulate solid medium having particle diameter of ≤5cm (pref. 0.1W500μm). After the reaction, at least a part of the medium is extracted from the reactor, and passed through a magnetic separator having a magnetic field of usually 1,000W20,000 gauss or more to separate the magnetizable particles from the nonmagnetizable particles, which are then returned to the catalytic reactor and reused.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:为了提高固体介质在重质石油的催化反应中的利用效率,通过使用磁选机分离涂覆有重质石油油沉积的金属的可磁化颗粒固体介质和不可磁化颗粒固体介质 ,然后重新使用后一种反应介质。 构成:将含有沸点> = 190℃的馏分的石油油(或通过氢化脱硫得到的产物)组成的重质石油在包含粒径<= 5cm的颗粒状固体介质的催化反应器中反应 (优选0.1-500mum)。 反应后,将介质的至少一部分从反应器中取出,并通过具有通常为1,000〜20,000高斯或更高的磁场的磁选机,以将可磁化颗粒与不可磁化的颗粒分离,然后将其还原至 催化反应器并重新使用。