Secondary recovery of oil
    1.
    发明授权
    Secondary recovery of oil 失效
    二次恢复油

    公开(公告)号:US3685581A

    公开(公告)日:1972-08-22

    申请号:US3685581D

    申请日:1971-03-24

    Applicant: TEXACO INC

    CPC classification number: E21B43/24 E21B43/16

    Abstract: Promoting secondary recovery of crude petroleum from a subsurface reservoir by flooding the reservoir with a continuous phase liquid admixture of hydrocarbon oil and water under high temperatures and pressures at which the oil dissolves water.

    Abstract translation: 通过在石油溶解水的高温和高压下,用烃油和水的连续相液体混合物浸渍储层,促进从地下储层中二次回收原油。

    Production of low sulfur fuel oil
    2.
    发明授权
    Production of low sulfur fuel oil 失效
    生产低硫燃油

    公开(公告)号:US3658681A

    公开(公告)日:1972-04-25

    申请号:US3658681D

    申请日:1970-02-24

    Applicant: TEXACO INC

    CPC classification number: C10G65/16 C10G45/02

    Abstract: Low sulfur fuel oil is prepared by distilling an asphaltcontaining petroleum fraction to obtain a vacuum gas oil and vacuum residuum. The vacuum gas oil is passed downwardly with hydrogen through an upper bed of desulfurization catalyst; the residuum fraction is passed upwardly through one or more lower beds of desulfurization catalyst, and the desulfurized effluents are combined. It is found advantageous to pass the distilled fraction down through the desulfurization zone with less residence time and the residual fraction up through the zone to subject it to more back-mixing and turbulence and thereby effecting a longer residence time.

    Abstract translation: 通过蒸馏含沥青的石油馏分制备低硫燃料油,以获得真空瓦斯油和真空渣油。 真空瓦斯油通过氢气通过上层脱硫催化剂; 残渣馏分向上通过一个或多个下层脱硫催化剂,并将脱硫流出物合并。 发现有利的是将蒸馏的馏分向下通过脱硫区,停留时间较短,残余馏分向上通过该区域以使其进行更多的回混和湍流,从而实现更长的停留时间。

    Split flow hydrocracking process
    3.
    发明授权
    Split flow hydrocracking process 失效
    分流流水解工艺

    公开(公告)号:US3607723A

    公开(公告)日:1971-09-21

    申请号:US3607723D

    申请日:1969-03-28

    Applicant: TEXACO INC

    CPC classification number: C10G65/18

    Abstract: A hydrocracking process for the substantially complete hydrocracking of a heavy hydrocarbon charge stock by introducing a heavy hydrocarbon charge stock into a catalyst zone comprising a first catalyst zone below and a second catalyst zone above the point of entry of the charge stock, in the presence of hydrogen which is introduced in countercurrent relationship to said charge stock in first catalyst zone and maintained at a rate sufficient to provide for lower boiling liquid contact of the second catalyst zone followed by recycling the remaining hydrocarbon material from the first catalyst zone to the charge stock.

    Catalytic hydrogen contact process
    7.
    发明授权
    Catalytic hydrogen contact process 失效
    催化氢接触过程

    公开(公告)号:US3595779A

    公开(公告)日:1971-07-27

    申请号:US3595779D

    申请日:1969-03-28

    Applicant: TEXACO INC

    CPC classification number: C10G65/00

    Abstract: A CATALYTIC HYDROGEN CONTACT PROCESS FOR THE HYDROSULFURIZATION OF HEAVY HYDROCARBON MATERIALS BY INTRODUCING A HEAVY HYDROCARBON MATERIAL INTO A CATALYST ZONE COMPRISING A FIRST CATALYST ZONE BELOW AND A SECOND CATALYST ZONE ABOVE THE POINT OF ENTRY OF THE HEAVY HYDROCARBON MATERIAL, IN MTHE PRESENCE OF HYDROGEN WHEREIN THE HYDROGEN IS INTRODUCED IN COUNTERCURRENT RELATIONSHIP TO SAID HEAVY HYDROCARBON MATERIAL AND MAINTAINED AT A RATE SUFFICIENT TO PROVIDE FOR LIQUID CONTACT OF THE SECOND CATALYST ZONE AND RECOVERING AN INCREASED PROPORTION OF LOWER BOILING HYDROCARBONS AND/OR HYDROCARBONS OF REREDUCED SULFUR CONTENT.

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