Method for reducing foam in a primary fractionator
    2.
    发明授权
    Method for reducing foam in a primary fractionator 有权
    降低主分馏器泡沫的方法

    公开(公告)号:US07906012B2

    公开(公告)日:2011-03-15

    申请号:US10196725

    申请日:2002-07-16

    IPC分类号: C10G9/12 C10G9/16

    摘要: The present invention includes methods for improving the operational parameters in primary fractionators which are experiencing diminished operation efficiencies due to deposits of polymerized hydrocarbon species. The invention comprises the step of adding a foam reducing amount of a foam reducing composition at the primary fractionator. A reduction in foaming is achieved whereby the operational efficiency of the process is improved based upon operation parameters including, but not limited to, liquid-gas contact ratio, product top temperature, pressure differentials, gasoline end point or combinations thereof.

    摘要翻译: 本发明包括用于改进主要分馏器中的操作参数的方法,其由于聚合的烃类物质的沉积而经历降低的操作效率。 本发明包括在初级分馏器中加入泡沫减少量的泡沫减少组合物的步骤。 实现发泡减少,由此基于包括但不限于液 - 气接触比,产物顶部温度,压力差,汽油终点或其组合的操作参数来改进工艺的操作效率。

    Method for reducing oil fouling in heat transfer equipment
    4.
    发明申请
    Method for reducing oil fouling in heat transfer equipment 有权
    减少传热设备油污的方法

    公开(公告)号:US20090038995A1

    公开(公告)日:2009-02-12

    申请号:US12219180

    申请日:2008-07-17

    IPC分类号: C10G9/12

    CPC分类号: C10G75/04 C10G75/00

    摘要: A method of reducing asphaltene and particulate induced fouling during the thermal processing of petroleum oils utilizes resin extracts from HSDP crude oils to disperse and solubilize asphaltenes and disperse inorganic particulate contaminants such as salts and iron oxide. The extracts are essentially maltene fractions which may be separated from the HSDP crude by a process of extraction from a precipitated asphalt fraction using light paraffinic solvents such as n-heptane.

    摘要翻译: 在石油的热加工过程中减少沥青质和颗粒物引起的结垢的方法利用HSDP原油的树脂提取物来分散和溶解沥青质并分散无机微粒污染物如盐和氧化铁。 提取物基本上是麦芽酮馏分,其可以通过使用轻链烷烃溶剂如正庚烷从沉淀的沥青馏分中提取的方法与HSDP原料分离。

    Process for the at least partial elimination of carbon deposits in a heat exchanger
    5.
    发明授权
    Process for the at least partial elimination of carbon deposits in a heat exchanger 有权
    在热交换器中至少部分消除碳沉积物的方法

    公开(公告)号:US06929015B2

    公开(公告)日:2005-08-16

    申请号:US10388228

    申请日:2003-03-14

    CPC分类号: F28G13/00

    摘要: The invention proposes a process and device for the at least partial elimination of carbon deposits in a heat exchanger in which an oxidation treatment is carried out comprising at least one controlled-oxidation stage at a conventional temperature between 400 and about 500° C. for a period of at least 4 hours, by means of an oxidizing fluid comprising for the greater part an inert gas, and a lesser quantity of oxygen, under conditions such that the temperatures of the fluids feeding or leaving the heat exchanger remain below about 520° C. throughout the oxidation treatment, and in that the hot approach of the exchanger remains below about 120° C. throughout the oxidation treatment. The invention also relates to a hydrotreatment system for the implementation of this process and this device.

    摘要翻译: 本发明提出了一种在热交换器中至少部分消除碳沉积物的方法和装置,其中进行氧化处理,其包括在常规温度为400至约500℃之间的至少一个受控氧化阶段, 在至少4小时的时间内,通过氧化流体,在大多数情况下,包括惰性气体和较少量的氧气,使得进料或离开热交换器的流体的温度保持低于约520℃ 在整个氧化处理过程中,并且在整个氧化处理过程中交换器的热接近保持低于约120℃。 本发明还涉及一种用于实施该方法和该装置的加氢处理系统。

    Processes for reacting bastnaesite with alkaline-earth metals
    9.
    发明授权
    Processes for reacting bastnaesite with alkaline-earth metals 失效
    酿酒酵母与碱土金属反应的方法

    公开(公告)号:US5618406A

    公开(公告)日:1997-04-08

    申请号:US579926

    申请日:1995-12-28

    申请人: Edward J. Demmel

    发明人: Edward J. Demmel

    摘要: Bastnaesite and magnesium-containing materials can be chemically reacted by use of reactions wherein alumina is made into a sol by use of a mono-protonic acid and then reacted with a magnesium-containing ingredient (e.g., magnesium acetate) and a bastnaesite ingredient such that, upon spray drying and calcination of the resulting composition, the bastnaesite is chemically reacted with magnesia to form a bastnaesite/magnesia/alumina compound having SO.sub.x activity.

    摘要翻译: 硼砂矿和含镁材料可以通过使用其中氧化铝通过使用单质子酸制成溶胶然后与含镁成分(例如,乙酸镁)和熔体矿物成分反应的反应进行化学反应,使得 在对所得组合物进行喷雾干燥和煅烧后,将该矿渣与氧化镁化学反应形成具有SO x活性的熔体/氧化镁/氧化铝化合物。

    Hydrocracking of heavy hydrocarbon oils with heavy hydrocarbon recycle
    10.
    发明授权
    Hydrocracking of heavy hydrocarbon oils with heavy hydrocarbon recycle 失效
    重质烃油与重质烃再循环的加氢裂化

    公开(公告)号:US5374348A

    公开(公告)日:1994-12-20

    申请号:US133616

    申请日:1993-09-13

    CPC分类号: C10G49/22 C10G47/26

    摘要: A heavy hydrocarbon oil, a substantial portion of which boils above 524.degree. C., is subjected to hydrocracking with a fractionated heavy oil recycle stream containing active additive particles. In the process, a slurry feed of (1) fresh heavy hydrocarbon oil feedstock and a heavy hydrocarbon recycle and (2) from about 0.01-4% by weight (based on fresh feedstock) of iron sulphate additive particles having sizes less than 45 .mu.m, is passed upwardly through a confined vertical hydrocracking zone. A mixed effluent is removed from the top of the hydrocracking zone, which is then passed through a hot separator vessel. From the bottom of the separator is withdrawn a liquid heavy hydrocarbon stream comprising heavy hydrocarbons and particles of the iron sulphate additive converted mainly to an iron sulphide phase. This separated liquid heavy hydrocarbon stream is fractionated to obtain a heavy oil which boils above 450.degree. C., containing the additive particles. The fractionated heavy oil containing the additive particles is then recycled to and mixing with the hydrocracking zone feed slurry in an amount up to 40% by weight of the combined feed slurry.

    摘要翻译: 其中大部分沸点高于524℃的重质烃油用含有活性添加剂颗粒的分馏重油循环流进行加氢裂化。 在该方法中,(1)新鲜重质烃油原料和重质烃循环的浆料进料和(2)约0.01-4重量%(基于新鲜原料)的尺寸小于45μm的硫酸铁添加剂颗粒 m向上通过一个受限制的垂直加氢裂化区。 混合流出物从加氢裂化区的顶部除去,然后通过热分离器容器。 从分离器的底部取出包含重质烃的液体重质烃流和主要转化为硫化铁相的硫酸铁添加剂颗粒。 将分离的液体重质烃流分馏,得到含有添加剂颗粒的高于450℃的重油。 然后将含有添加剂颗粒的分馏的重油再循环至加氢裂化区进料浆料,并以与组合的进料浆料重量计最多40重量的量混合。