Production of low sulfur/low aromatics distillates
    1.
    发明授权
    Production of low sulfur/low aromatics distillates 有权
    生产低硫/低芳烃馏分

    公开(公告)号:US06824673B1

    公开(公告)日:2004-11-30

    申请号:US09553374

    申请日:2000-04-20

    CPC classification number: C10G65/12

    Abstract: A process for producing distillate boiling range streams that are low in both sulfur and aromatics. A distillate feedstock is treated in a first hydrodesulfurization stage in the presence of a hydrogen-containing treat gas and a hydrodesulfurization catalyst, thereby resulting in partial desufurization of the stream. The partially desulfurized distillate stream is then treated in a second hydrodesulfurization stage, also in the presence of a hydrogen-containing treat gas and a hydrodesulfurization catalyst. The hydrogen-containing treat gas is cascaded from the next downstream reaction stage, which is an aromatics hydrogenation stage.

    Abstract translation: 一种生产硫和芳烃含量低的馏出物沸腾物流的方法。 在含氢处理气体和加氢脱硫催化剂的存在下,在第一加氢脱硫阶段处理馏出物原料,从而导致料流的部分脱硫。 然后在第二加氢脱硫阶段,在含氢处理气体和加氢脱硫催化剂的存在下处理部分脱硫的馏出物物流。 含氢处理气体从下一个下游反应阶段级联,其是芳族化合物氢化反应阶段。

    Process for treatment of petroleum acids
    2.
    发明授权
    Process for treatment of petroleum acids 失效
    石油酸处理工艺

    公开(公告)号:US06767452B1

    公开(公告)日:2004-07-27

    申请号:US09958436

    申请日:2001-10-09

    CPC classification number: C10G29/22

    Abstract: The invention is a process for decreasing the acidity of an organic acid containing petroleum oil, comprising contacting said petroleum oil containing organic acids with an effective amount of an alcohol and an effective trace amount of a base selected from Group IA and IIA metal carbonates, hydroxides, phosphates, biphosphates and mixtures of a hydroxide and phosphate and/or biphosphates at a temperature and under conditions sufficient to form the corresponding ester of said alcohol.

    Abstract translation: 本发明是降低含有机酸的石油的酸度的方法,包括将含有机酸的石油与有效量的醇和有效微量的选自IAA和IIA族金属碳酸盐的碱,氢氧化物 ,磷酸盐,二磷酸盐以及氢氧化物和磷酸盐和/或二磷酸盐的混合物,在足以形成所述醇的相应酯的温度和条件下。

    High performance monolith treater for gasoline upgrade
    3.
    发明授权
    High performance monolith treater for gasoline upgrade 失效
    用于汽油升级的高性能整料处理器

    公开(公告)号:US06673237B2

    公开(公告)日:2004-01-06

    申请号:US09996499

    申请日:2001-11-28

    Abstract: A method of increasing the selective desulfurization of naphtha feed streams that includes: combining a naphtha feed stream with a hydrogen containing gas to form a combined feed stream and reacting the combined feed stream over a monolithic honeycomb catalyst bed containing hydrodesulfurization catalyst components to give a desulfurized naphtha. In conducting such an illustrative embodiment, the percent desulfurization of the naphtha is preferably greater than about 50% and the percent olefin hydrogenation of the naphtha is preferably less than about 50%. The monolithic honeycomb catalyst bed of one alternative and illustrative embodiment preferably has a channel density of about 25 to 1600 cells per square inch; a channel size from about 0.1 to 10 mm; and a channel wall thickness of about 0.01 to about 2.0 mm. The illustrative method should be carried out such that the octane number (R+M/2) of the naphtha feed stream is reduced by no more than 3.0 at 95% desulfurization and preferably no more than 1.5. The hydrodesulfurization catalyst components include a powdered refractory oxide and transition metal catalyst compounds. Alternatively the hydrodesulfurization catalyst components may be impregnated into the monolithic honeycomb catalyst bed itself. Preferable hydrodesulfurization catalyst components include a Group VIII metal containing compound and a Group VIB metal containing compound. Alternatively the hydrodesulfurization catalyst components may further include a phosphorous promoter.

    Abstract translation: 一种增加石脑油进料流的选择性脱硫的方法,其包括:将石脑油进料流与含氢气体组合以形成组合的进料流,并将组合的进料流在含有加氢脱硫催化剂组分的整体式蜂窝催化剂床上反应,得到脱硫 石脑油 在进行这样的说明性实施例中,石脑油的脱硫百分比优选大于约50%,并且石脑油的烯烃氢化百分比优选小于约50%。 一个替代和说明性实施方案的整体蜂窝催化剂床优选具有约25至1600个细胞/平方英寸的通道密度; 通道尺寸约0.1至10mm; 并且通道壁厚度为约0.01至约2.0mm。 应进行说明性的方法,使得石脑油进料流的辛烷值(R + M / 2)在95%脱硫时减少不超过3.0,优选不超过1.5。 加氢脱硫催化剂组分包括粉末难熔氧化物和过渡金属催化剂化合物。 或者,加氢脱硫催化剂组分可以浸渍到整体蜂窝催化剂床本身中。 优选的加氢脱硫催化剂组分包括含Ⅷ族金属的化合物和含VIB族金属的化合物。 或者,加氢脱硫催化剂组分可以进一步包括磷促进剂。

    Process for converting petroleum fractions, comprising an ebullated bed hydroconversion step, a separation step, a hydrodesulphurization step and a cracking step
    4.
    发明授权
    Process for converting petroleum fractions, comprising an ebullated bed hydroconversion step, a separation step, a hydrodesulphurization step and a cracking step 有权
    用于转化石油馏分的方法,包括沸腾床加氢转化步骤,分离步骤,加氢脱硫步骤和裂化步骤

    公开(公告)号:US06620311B2

    公开(公告)日:2003-09-16

    申请号:US09757602

    申请日:2001-01-11

    CPC classification number: C10G69/00 C10G65/04 C10G65/12

    Abstract: For converting hydrocarbons: step a) treating a hydrocarbon feed with hydrogen in at least one three-phase reactor (1), containing ebullated bed hydroconversion catalyst; a step b) passing effluent from step a) to a separation zone (2) to recover a fraction F1 containing at least a portion of gas, gasoline and atmospheric gas oil contained in the effluent from step a), and a fraction F2 containing compounds with boiling points of more than that of the atmospheric gas oil; step c) hydrodesulphurizing at least a portion of fraction F1; and step d) passing at least a portion of fraction F2 to catalytic cracking section (6).

    Abstract translation: 用于转化烃:步骤a)在含有沸腾床加氢转化催化剂的至少一个三相反应器(1)中用氢处理烃进料; 步骤b)将来自步骤a)的流出物送入分离区(2)以回收含有至少一部分来自步骤a)的流出物中含有的气体,汽油和常压瓦斯油的馏分F1和含有化合物的馏分F2 沸点高于大气瓦斯油; 步骤c)加氢脱硫馏分F1的至少一部分; 和步骤d)将部分F2的至少一部分通入催化裂化段(6)。

    Process for the desulfurization of petroleum feeds
    5.
    发明授权
    Process for the desulfurization of petroleum feeds 有权
    石油进料脱硫工艺

    公开(公告)号:US06592750B2

    公开(公告)日:2003-07-15

    申请号:US09886542

    申请日:2001-06-21

    CPC classification number: C10G65/04 C10G2300/4087 C10G2400/02

    Abstract: A process for the hydrodesulfurization of a cracked naphtha stream is disclosed where very little of the valuable olefins are saturated. The process is a two staged process wherein the H2S is removed between the stages to prevent recombinant mercaptans formation. Because the H2S is removed between the stages milder conditions can be used in the second stage polishing reactor to achieve the same desulfurization levels with less olefin loss.

    Abstract translation: 公开了一种裂化石脑油流的加氢脱硫方法,其中很少有价值的烯烃是饱和的。 该方法是两阶段方法,其中在阶段之间除去H 2 S以防止重组硫醇形成。 由于H2S在两段之间被去除,较温和的条件可用于第二阶段抛光反应器,以达到与较少烯烃损失相同的脱硫水平。

    Process for the desulfurization of petroleum feeds
    6.
    发明授权
    Process for the desulfurization of petroleum feeds 有权
    石油进料脱硫工艺

    公开(公告)号:US06303020B1

    公开(公告)日:2001-10-16

    申请号:US09502509

    申请日:2000-02-11

    CPC classification number: C10G65/04 C10G2300/4087 C10G2400/02

    Abstract: A process for the hydrodesulfurization of a cracked naphtha stream is disclosed where very little of the valuable olefins are saturated. The process is a two staged process wherein the H2S is removed between the stages to prevent recombinant mercaptans formation. Because the H2S is removed between the stages milder conditions can be used in the second stage polishing reactor to achieve the same desulfurization levels with less olefin loss.

    Abstract translation: 公开了一种裂化石脑油流的加氢脱硫方法,其中很少有价值的烯烃是饱和的。 该方法是两阶段方法,其中在阶段之间除去H 2 S以防止重组硫醇形成。 由于H2S在两段之间被去除,较温和的条件可用于第二阶段抛光反应器,以达到与较少烯烃损失相同的脱硫水平。

    Process for treatment of petroleum acids (LAW824)
    8.
    发明授权
    Process for treatment of petroleum acids (LAW824) 有权
    石油酸处理方法(LAW824)

    公开(公告)号:US06190541B1

    公开(公告)日:2001-02-20

    申请号:US09309941

    申请日:1999-05-11

    CPC classification number: C10G29/22

    Abstract: The invention is a process for decreasing the acidity of an organic acid containing petroleum oil, comprising contacting said petroleum oil containing organic acids with an effective amount of an alcohol and an effective trace amount of a base selected from Group IA and IIA metal carbonates, hydroxides, phosphates, and mixtures of a hydroxide and phosphate at a temperature and under conditions sufficient to form the corresponding ester of said alcohol.

    Abstract translation: 本发明是降低含有机酸的石油的酸度的方法,包括将含有机酸的石油与有效量的醇和有效微量的选自IAA和IIA族金属碳酸盐的碱,氢氧化物 ,磷酸盐,以及氢氧化物和磷酸盐的混合物在足以形成所述醇的相应酯的温度和条件下进行。

    Process for softening fischer-tropsch wax with mild hydrotreating
    9.
    发明授权
    Process for softening fischer-tropsch wax with mild hydrotreating 有权
    用轻度加氢处理软化费 - 托蜡的方法

    公开(公告)号:US06776898B1

    公开(公告)日:2004-08-17

    申请号:US09542894

    申请日:2000-04-04

    CPC classification number: C10G73/44

    Abstract: A novel process for forming hydrocarbon waxes from synthesis gas is disclosed. This invention teaches a process whereby a Fischer-Tropsch wax can be formulated such that the wax softness as defined by ASTM Standard Test Method for Needle Penetration of waxes (ASTM D-1321) can be adjusted to within a region most preferred for end use applications while simultaneously removing undesirable impurities, such as oxygenates (e.g., primary alcohols), olefins, and trace levels of aromatics. In a Fischer-Tropsch reactor, Fischer-Tropsch wax is formed from synthesis gas in a catalyzed reaction. The Fischer Tropsch wax is then subjected to a relatively mild hydroprocessing over a hydroisomerization catalyst under conditions such that essentially no boiling point conversion is obtained, but yet chemical conversions (e.g., hydrogenation and mild isomerization) occur yielding a high purity, hydrocarbon wax product of reduced hardness.

    Abstract translation: 公开了一种从合成气中形成烃蜡的新方法。 本发明教导了一种方法,其中可以配制费 - 托蜡,使得ASTM标准测试方法针对蜡的渗透(ASTM D-1321)所定义的蜡柔软度可以调整到最适用于最终用途应用的区域内 同时除去不需要的杂质,例如含氧化合物(例如伯醇),烯烃和痕量芳族化合物。 在费 - 托反应器中,费 - 托蜡在催化反应中由合成气形成。 然后在基本上不获得沸点转化率的条件下,在加氢异构化催化剂上进行相对温和的加氢处理,但是仍然发生化学转化(例如氢化和轻度异构化),产生高纯度烃蜡产物 降低硬度。

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