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    MICROWAVE-PROMOTED DESULFURIZATION OF CRUDE OIL
    1.
    发明申请
    MICROWAVE-PROMOTED DESULFURIZATION OF CRUDE OIL 有权
    微波促进原油的脱硫

    公开(公告)号：US20130341247A1

    公开(公告)日：2013-12-26

    申请号：US13849429

    申请日：2013-03-22

    申请人： M. Rashid Khan ,  Emad Naji Al-Shafei

    发明人： M. Rashid Khan ,  Emad Naji Al-Shafei

    IPC分类号： C10G45/02 ,  E21B43/38

    CPC分类号： C10G45/02 ,  C10G29/02 ,  C10G29/20 ,  C10G32/02 ,  C10G45/04 ,  E21B43/38

    摘要： Heavy crude oils having high sulfur content and viscosities are upgraded by a hydrodesulfurization (HDS) process that includes microwave irradiation of a mixture of the sour heavy crude oil with at least one catalyst and optionally, one or more sensitizers, and irradiation in the presence of hydrogen. The process is also adapted to microwave treatment of hard to break emulsions, either above ground or below ground where water-in-oil emulsions are initially formed, followed by the catalytic hydrodesulfurization promoted by application of further microwave energy to the demulsified crude oil stream.

    摘要翻译： 具有高硫含量和粘度的重质原油通过加氢脱硫（HDS）方法提高，其包括将酸重质原油与至少一种催化剂和任选的一种或多种敏化剂的混合物的微波照射和在 氢。 该方法还适用于微波处理难以破碎的乳液，其在最初形成油包水乳液的地面或地下，接着通过向破乳原油流施加进一步的微波能促进催化加氢脱硫。

    DYNAMIC DEMULSIFICATION SYSTEM FOR USE IN A GAS-OIL SEPARATION PLANT
    2.
    发明申请
    DYNAMIC DEMULSIFICATION SYSTEM FOR USE IN A GAS-OIL SEPARATION PLANT 有权
    用于气油分离装置的动态解析系统

    公开(公告)号：US20130026082A1

    公开(公告)日：2013-01-31

    申请号：US13495599

    申请日：2012-06-13

    申请人： Emad Naji AL-SHAFEI ,  M. Rashid Khan

    发明人： Emad Naji AL-SHAFEI ,  M. Rashid Khan

    IPC分类号： B01D17/04

    CPC分类号： B01D17/12 ,  B01D17/04 ,  B01D17/042 ,  B01D17/06 ,  B01D2201/54 ,  B01D2221/04 ,  C10G31/08 ,  C10G33/02 ,  C10G33/08

    摘要： A dynamic water/oil demulsification system for a gas-oil separation plant (GOSP) includes: an in-line microwave treatment subsystem upstream of one or more of each of a dehydrator vessel, desalter vessel and/or water/oil separator vessel, each of which vessels receives a water-oil emulsion; sensors that monitor and transmit data corresponding to properties of the water-oil emulsion in or downstream of the respective vessel(s); and a processor/controller associated with the in-line microwave treatment subsystem that initiates the application of microwave energy to the emulsion(s) based on the data from the sensors.

    摘要翻译： 用于瓦斯油分离设备（GOSP）的动态水/油破乳系统包括：在脱水器容器，脱盐器容器和/或水/油分离器容器中的一个或多个上游的在线微波处理子系统，每个 其中船只接收水油乳液; 传感器，其监测和传输对应于相应容器内或下游的水 - 油乳液的性质的数据; 以及与在线微波处理子系统相关联的处理器/控制器，其基于来自传感器的数据启动对乳剂的微波能量的应用。

    Dynamic demulsification system for use in a gas-oil separation plant
    3.
    发明授权
    Dynamic demulsification system for use in a gas-oil separation plant 有权
    用于瓦斯油分离设备的动态破乳系统

    公开(公告)号：US09555345B2

    公开(公告)日：2017-01-31

    申请号：US13495599

    申请日：2012-06-13

    申请人： Emad Naji Al-Shafei ,  M. Rashid Khan

    发明人： Emad Naji Al-Shafei ,  M. Rashid Khan

    IPC分类号： B01D17/04 ,  B01D17/12 ,  C10G33/02 ,  C10G33/08 ,  B01D17/06

    CPC分类号： B01D17/12 ,  B01D17/04 ,  B01D17/042 ,  B01D17/06 ,  B01D2201/54 ,  B01D2221/04 ,  C10G31/08 ,  C10G33/02 ,  C10G33/08

    摘要： A dynamic water/oil demulsification system for a gas-oil separation plant (GOSP) includes: an in-line microwave treatment subsystem upstream of one or more of each of a dehydrator vessel, desalter vessel and/or water/oil separator vessel, each of which vessels receives a water-oil emulsion; sensors that monitor and transmit data corresponding to properties of the water-oil emulsion in or downstream of the respective vessel(s); and a processor/controller associated with the in-line microwave treatment subsystem that initiates the application of microwave energy to the emulsion(s) based on the data from the sensors.

    摘要翻译： 用于瓦斯油分离设备（GOSP）的动态水/油破乳系统包括：在脱水器容器，脱盐器容器和/或水/油分离器容器中的一个或多个上游的在线微波处理子系统，每个 其中船只接收水油乳液; 传感器，其监测和传输对应于相应容器内或下游的水 - 油乳液的性质的数据; 以及与在线微波处理子系统相关联的处理器/控制器，其基于来自传感器的数据启动对乳剂的微波能量的应用。

    Flare stack combustion method and apparatus
    5.
    发明申请
    Flare stack combustion method and apparatus 有权
    火炬烟囱燃烧方法及装置

    公开(公告)号：US20080145807A1

    公开(公告)日：2008-06-19

    申请号：US12069348

    申请日：2008-02-07

    申请人： Mazen Mashhour ,  M. Rashid Khan

    发明人： Mazen Mashhour ,  M. Rashid Khan

    IPC分类号： F23D1/00

    CPC分类号： F23G7/08 ,  F23L17/16

    摘要： Apparatus for enhancing combustion of an undesired chemical to minimize the formation of smoke during operation of a flare stack for the discharge of a flare feedstream includes a plurality of high-pressure air nozzles spaced apart below and around the periphery of the stack outlet. Each nozzle is directed toward the stack outlet and in the direction of the feedstream's movement. High-pressure air from the nozzles forms a plurality of high-velocity air jets to produce a moving air mass that draws additional atmospheric air into the air mass moving toward the stack outlet to enhance combustion of the flare feedstream. Analytical means determine the stoichiometric oxygen requirements, and an air-flow valve controls the flow rate of the high-pressure air to the nozzles. Air flow control means adjust the mass flow-rate of high-pressure air based on minimum oxygen requirements determined by the analytical means, whereby the oxygen content of the air flow at the stack outlet meets or exceeds the requirement for the complete combustion of the feedstream.

    摘要翻译： 用于在用于排放火炬进料流的火炬塔的操作期间增强不需要的化学物质的燃烧以最小化烟雾形成的装置包括在堆叠出口周围间隔开的多个高压空气喷嘴。 每个喷嘴指向堆叠出口并沿着进料流运动的方向。 来自喷嘴的高压空气形成多个高速空气射流，以产生移动空气质量，其将额外的大气空气吸入空气质量物质中，朝着堆叠出口移动，以增强火炬进料流的燃烧。 分析方法确定化学计量氧的要求，并且空气流量阀控制高压空气到喷嘴的流量。 空气流量控制装置基于由分析装置确定的最小氧气需求来调节高压空气的质量流量，由此堆叠出口处的空气流的氧含量满足或超过进料流的完全燃烧的要求 的。

    AUTOMATION AND CONTROL OF ENERGY EFFICIENT FLUID CATALYTIC CRACKING PROCESSES FOR MAXIMIZING VALUE ADDED PRODUCTS
    7.
    发明申请
    AUTOMATION AND CONTROL OF ENERGY EFFICIENT FLUID CATALYTIC CRACKING PROCESSES FOR MAXIMIZING VALUE ADDED PRODUCTS 有权
    能量有效液体催化裂化过程的自动化和控制，用于最大限度地增加产品数量

    公开(公告)号：US20120193269A1

    公开(公告)日：2012-08-02

    申请号：US13429047

    申请日：2012-03-23

    申请人： Othman A. Taha ,  M. Rashid Khan

    发明人： Othman A. Taha ,  M. Rashid Khan

    IPC分类号： C10G11/02

    CPC分类号： C10G11/187 ,  C10G11/05 ,  C10G2300/1059 ,  C10G2300/107 ,  C10G2300/301 ,  C10G2400/20 ,  G05B13/027 ,  G05B17/02

    摘要： Petroleum oil is catalytically cracked by contacting oil with catalyst mixture consisting of a base cracking catalyst containing an stable Y-type zeolite and small amounts of rare-earth metal oxide, and an additive containing a shape-selective zeolite, in an FCC apparatus having a regeneration zone, a separation zone, and a stripping zone. Production of light-fraction olefins is maximized by applying appropriate process control, monitoring, and optimizing systems. Mathematical process models, including neural networks, statistical models and finite impulse models are used in conjunction with advanced controllers and optimizing routines to calculate optimal settings for various parameters. Process model and historical data to test a predictive system can provide early warning of potential performance degradation and equipment failure in the FCC unit, decreasing overall operating costs and increasing plant safety.

    摘要翻译： 在含有稳定的Y型沸石和少量稀土金属氧化物的基础裂化催化剂和含有形状选择性沸石的添加剂组成的催化剂混合物中，油与催化剂混合物在具有 再生区，分离区和汽提区。 通过应用适当的过程控制，监测和优化系统，轻馏分烯烃的生产最大化。 数学过程模型，包括神经网络，统计模型和有限脉冲模型与高级控制器和优化程序结合使用，以计算各种参数的最佳设置。 用于测试预测系统的过程模型和历史数据可以提供对FCC单元潜在性能下降和设备故障的预警，降低总体运营成本并提高工厂安全性。

    Advanced control of severe fluid catalytic cracking process for maximizing propylene production from petroleum feedstock
    8.
    发明申请
    Advanced control of severe fluid catalytic cracking process for maximizing propylene production from petroleum feedstock 有权
    严格流化床催化裂化过程的先进控制，可最大限度地利用石油原料生产丙烯

    公开(公告)号：US20080128325A1

    公开(公告)日：2008-06-05

    申请号：US11983078

    申请日：2007-11-07

    申请人： M. Rashid Khan ,  Othman A. Taha

    发明人： M. Rashid Khan ,  Othman A. Taha

    IPC分类号： C10G51/04

    CPC分类号： C10G11/187 ,  B01J23/10 ,  B01J29/084 ,  B01J29/40 ,  B01J29/80 ,  C10G11/05 ,  C10G2300/1033 ,  C10G2300/1044 ,  C10G2300/1059 ,  C10G2300/1074 ,  C10G2300/4006 ,  C10G2300/4081 ,  C10G2400/20 ,  G05D21/02

    摘要： With an aim to optimize propylene production, petroleum oil such as gas oil is catalytically cracked by contacting the oil with catalyst mixture consisting of a base cracking catalyst containing an stable Y-type zeolite and small amounts of rare-earth metal oxide, and an additive containing a shape-selective zeolite, in a down-flow type fluid catalytic cracking apparatus having a regeneration zone, a separation zone, and a stripping zone, wherein conversion of hydrocarbon occurs under relatively severe conditions. According to this fluid catalytic cracking process, the production of light-fraction olefins such as propylene is maximized by applying appropriate process control, monitoring, and optimizing systems. Process model and historical data to test a predictive system can provide early warning of potential performance degradation and equipment failure in the FCC unit.

    摘要翻译： 为了优化丙烯生产，通过使油与由含有稳定的Y型沸石的基础裂化催化剂和少量的稀土金属氧化物组成的催化剂混合物和添加剂，催化裂化石油油，例如瓦斯油， 在具有再生区，分离区和汽提区的下流式流化催化裂化装置中含有形状选择性沸石，其中碳氢化合物在相对苛刻的条件下发生。 根据这种流化催化裂化方法，通过应用适当的过程控制，监测和优化系统，使轻馏分烯烃（如丙烯）的生产最大化。 用于测试预测系统的过程模型和历史数据可以提供FCC单元潜在性能下降和设备故障的预警。

    Low temperature pyrolysis of coal or oil shale in the presence of calcium compounds
    9.
    发明授权
    Low temperature pyrolysis of coal or oil shale in the presence of calcium compounds 失效
    在钙化合物存在下，煤或油页岩的低温热解

    公开(公告)号：US4747938A

    公开(公告)日：1988-05-31

    申请号：US853117

    申请日：1986-04-17

    申请人： M. Rashid Khan

    发明人： M. Rashid Khan

    IPC分类号： C10G1/02 ,  C10G1/04

    CPC分类号： C10G1/02

    摘要： A coal pyrolysis technique or process is described in which particulate coal is pyrolyzed in the presence of about 5 to 21 wt. % of a calcium compound selected from calcium oxide, calcined (hydrate) dolomite, or calcined calcium hydrate to produce a high quality hydrocarbon liquid and a combustible product gas which are characterized by low sulfur content. The pyrolysis is achieved by heating the coal-calcium compound mixture at a relatively slow rate at a temperature of about 450.degree. to 700.degree. C. over a duration of about 10 to 60 minutes in a fixed or moving bed reactor. The gas exhibits an increased yield in hydrogen and C.sub.1 -C.sub.8 hydrocarbons and a reduction in H.sub.2 S over gas obtainable by pyrolyzing cola without the calcium compound. The liquid product obtained is of a sufficient quality to permit its use directly as a fuel and has a reduced sulfur and oxygen content which inhibits polymerization during storage.

    摘要翻译： 描述了煤热解技术或方法，其中颗粒煤在约5至21重量％存在下热解。 选自氧化钙，煅烧（水合物）白云石或煅烧钙水合物的钙化合物的百分比，以产生以低硫含量为特征的高质量烃液体和可燃产物气体。 热解是通过在约450至700℃的温度下以固定或移动床反应器中约10至60分钟的持续时间内以相对较慢的速率加热煤 - 钙化合物混合物来实现的。 该气体在氢气和C1-C8烃中表现出增加的产率，并且通过在没有钙化合物的情况下热解可乐而可以减少H 2 S。 获得的液体产品具有足够的质量以允许其直接用作燃料，并且具有降低的硫和氧含量，其在储存期间抑制聚合。