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    • 1. 发明授权
    • Hot fluid recovery of heavy oil with steam and carbon dioxide
    • 重油与蒸汽和二氧化碳的热流体回收
    • US08561702B2
    • 2013-10-22
    • US12526392
    • 2008-02-11
    • Ian WylieL. Allan McGuireDavid L. HagenGary D. Ginter
    • Ian WylieL. Allan McGuireDavid L. HagenGary D. Ginter
    • E21B36/00
    • E21B43/24
    • Combustion gases with relatively high levels of carbon dioxide (CO2), steam, and/or hot water, may be used to improve recovery of heavy hydrocarbons from geologic formations and/or from surface mined materials. These gases reduce the viscosity and/or increase hydrocarbon extraction rates through improvements in thermal efficiency and/or higher rates of heat delivery for a given combustor an capital investment. Such high water/CO2 content combustion gases can be formed by adding water to combustion gases formed by burning fuel. The pressure to inject the combustion gases and extract heavy hydrocarbons may be provided by diverting high pressure expanded gases from wet combustion in a gas turbine, or by reducing the pressure drop across a turbine and using the expanded hot gases for extraction.
    • 可以使用具有相对高水平的二氧化碳(CO 2),蒸汽和/或热水的燃烧气体来改善地质构造和/或来自表面开采材料的重质烃的回收。 这些气体通过改善热效率和/或给定燃烧器的热输送速率来降低粘度和/或提高碳氢化合物的提取率。 这种高水/二氧化碳含量的燃烧气体可以通过向燃烧燃料形成的燃烧气体中加入水而形成。 注入燃烧气体并提取重质烃的压力可以通过将高压膨胀气体从燃气轮机中的湿式燃烧转移,或者通过减小涡轮机两端的压降和使用膨胀的热气体进行提取而提供。
    • 2. 发明申请
    • HOT FLUID RECOVERY OF HEAVY OIL WITH STEAM AND CARBON DIOXIDE
    • 重油与蒸汽和二氧化碳的热流体回收
    • US20100276148A1
    • 2010-11-04
    • US12526392
    • 2008-02-11
    • Ian WylieL. Allan McGuireDavid L. HagenGary D. Ginter
    • Ian WylieL. Allan McGuireDavid L. HagenGary D. Ginter
    • E21B43/24E21B43/16
    • E21B43/24
    • Combustion gases with relatively high levels of carbon dioxide (CO2), steam, and/or hot water, may be used to improve recovery of heavy hydrocarbons from geologic formations and/or from surface mined materials. These gases reduce the viscosity and/or increase hydrocarbon extraction rates through improvements in thermal efficiency and/or higher rates of heat delivery for a given combustor an capital investment. Such high water/CO2 content combustion gases can be formed by adding water to combustion gases formed by burning fuel. The pressure to inject the combustion gases and extract heavy hydrocarbons may be provided by diverting high pressure expanded gases from wet combustion in a gas turbine, or by reducing the pressure drop across a turbine and using the expanded hot gases for extraction.
    • 可以使用具有相对高水平的二氧化碳(CO 2),蒸汽和/或热水的燃烧气体来改善地质构造和/或来自表面开采材料的重质烃的回收。 这些气体通过改善热效率和/或给定燃烧器的热输送速率来降低粘度和/或提高碳氢化合物的提取率。 这种高水/二氧化碳含量的燃烧气体可以通过向燃烧燃料形成的燃烧气体中加入水而形成。 注入燃烧气体并提取重质烃的压力可以通过将高压膨胀气体从燃气轮机中的湿式燃烧转移,或者通过减小涡轮机两端的压降和使用膨胀的热气体进行提取而提供。
    • 3. 发明授权
    • Heavy oil recovery with fluid water and carbon dioxide
    • 用流体水和二氧化碳重油回收
    • US07814975B2
    • 2010-10-19
    • US12233503
    • 2008-09-18
    • David L. HagenIan WylieL. Allan McGuireGary Ginter
    • David L. HagenIan WylieL. Allan McGuireGary Ginter
    • E21B43/243
    • E21B43/24
    • Diluted wet combustion forms a hot process fluid or VASTgas including carbon dioxide (CO2) and fluid water which is delivered to geologic formations and/or to surface mined materials to reduce the viscosity and/or increase hydrocarbon extraction. High water and/or CO2 content is achieved by reducing non-aqueous diluent and/or adding or recycling CO2. Power recovered from expanding the VASTgas may be used to pressurize the VASTgas for delivery by partial expansion through a Direct VAST cycle, and/or by diverting compressed oxidant through a parallel thermogenerator in a Diverted VAST cycle. Pressurized VASTgas may be injected into a well within the hydrocarbon formation or with mined material into a heavy hydrocarbon separator vessel to heat, mobilize, solubilize and/or extract heavy hydrocarbons. Light hydrocarbons may be mixed in with the hot process fluid to enhance hydrocarbon mobilization and recovery. Microwaves may further heat the VASTgas and/or hydrocarbon. Sulfur oxidation, calcining limestone and/or recycling may increase CO2. Oxygen enrichment may increase the specific power. VASTgas may be delivered through and back injection wells and/or production wells, and/or between sequential injection wells in alternating and/or paired zigzag formations with multiple wells per VAST combined heat and power recovery system.
    • 稀释的湿式燃烧形成热过程流体或包含二氧化碳(CO2)和流体水的VAST气体,其被输送到地质层和/或表面开采的材料以降低粘度和/或增加烃提取。 通过减少非水稀释剂和/或添加或再循环CO 2来实现高水和/或CO 2含量。 通过膨胀VAST气体回收的功率可用于通过直接VAST循环的部分膨胀和/或通过在分流VAST循环中的平行热发生器转移压缩的氧化剂来对VAST气体进行加压以进行递送。 加压的VAST气体可以注入到烃地层内的井中或者被注入到重质烃分离器容器中以加热,动员,溶解和/或提取重质烃。 轻烃可以与热过程流体混合以增强烃的动员和回收。 微波可以进一步加热VAST气体和/或烃。 硫氧化,煅烧石灰石和/或回收可能会增加二氧化碳。 氧气浓缩可能会增加比功率。 VAST气体可以通过和注入井和/或生产井和/或在交替和/或配对的之字形地层中的顺序注入井之间通过每个VAST组合热和功率回收系统的多个井输送。
    • 4. 发明授权
    • Partial load combustion cycles
    • 部分负载燃烧循环
    • US09254729B2
    • 2016-02-09
    • US12202964
    • 2008-09-02
    • L. Allan McGuireIan WylieDavid L. Hagen
    • L. Allan McGuireIan WylieDavid L. Hagen
    • F02C3/30B60H1/03B60H1/32F01K13/02F01K21/04F02C7/143
    • B60H1/032B60H1/3223F01K13/02F01K21/047F02C3/30F02C3/305F02C7/1435
    • The part load method controls delivery of diluent fluid, fuel fluid, and oxidant fluid in thermodynamic cycles using diluent, to increase the Turbine Inlet Temperature (TIT) and thermal efficiency in part load operation above that obtained by relevant art part load operation of Brayton cycles, fogged Brayton cycles, or cycles operating with some steam delivery, or with maximum steam delivery. The part load method may control the TIT at the design level by controlling one or both of liquid and/or gaseous fluid water over a range from full load to less than 45% load. This extends operation to lower operating loads while providing higher efficiencies and lower operating costs using water, steam and/or CO2 as diluents, than in simple cycle operation.
    • 部件加载方法控制稀释液,燃料流体和氧化剂流体在使用稀释剂的热力循环中的输送,以增加部分负载运行中的涡轮进口温度(TIT)和热效率,高于通过相关的Brayton循环的相关部分负载运行获得的 ,雾化的布雷顿循环,或循环运行,一些蒸汽输送,或最大的蒸汽输送。 零件加载方法可以通过在满载到小于45%的负载的范围内控制液体和/或气态流体水中的一种或两种来控制设计级别的TIT。 与简单的循环操作相比,这可以延长操作以降低运行负载,同时提供更高的效率和降低使用水,蒸汽和/或二氧化碳作为稀释剂的运行成本。
    • 5. 发明申请
    • HEAVY OIL RECOVERY WITH FLUID WATER AND CARBON DIOXIDE
    • 用油和二氧化碳重油回收
    • US20090071648A1
    • 2009-03-19
    • US12233503
    • 2008-09-18
    • David L. HagenIan WylieL. Allan McGuireGary Ginter
    • David L. HagenIan WylieL. Allan McGuireGary Ginter
    • E21B43/24
    • E21B43/24
    • Diluted wet combustion forms a hot process fluid or VASTgas comprising carbon dioxide (CO2) and fluid water which is delivered geologic formations and/or from surface mined materials to reduce the viscosity and/or increase hydrocarbon extraction. This may improve thermal efficiency and/or increases heat delivery for a given combustor or per capital investment. High water and/or CO2 content is achieved by reducing non-aqueous diluent and/or adding or recycling CO2. Power recovered from expanding the VASTgas may be pressurize the VASTgas for delivery by partial expansion through a Direct VAST cycle, and/or by diverting compressed oxidant through a parallel thermogenerator in a Diverted VAST cycle. Pressurized VASTgas may be injected into well within the hydrocarbon formation or with mined material into a heavy hydrocarbon separator vessel to heat, mobilize, solubilize and/or extract heavy hydrocarbons. Light hydrocarbons may be mixed in with the hot process fluid to enhance hydrocarbon mobilization and recovery. Microwaves may further heat the VASTgas and/or hydrocarbon. Sulfur oxidation, calcining limestone and/or recycling may increase CO2. Oxygen enrichment may increase the specific power. VASTgas may be delivered through and back injection wells and/or production wells, and/or between sequential injection wells in alternating and/or paired zigzag formations with multiple wells per VAST combined heat and power recovery system.
    • 稀释的湿式燃烧形成热过程流体或包含二氧化碳(CO2)和流体水的VAST气体,其被输送地质构造和/或从表面开采的材料中以降低粘度和/或增加烃提取。 这可以提高给定燃烧器的热效率和/或增加热输送或每个资本投资。 通过减少非水稀释剂和/或添加或再循环CO 2来实现高水和/或CO 2含量。 通过扩展VAST气体回收的功率可能会通过直接VAST循环的部分膨胀来加压VAST气体进行输送,和/或通过在Diverted VAST循环中通过平行热发生器转移压缩氧化剂。 可以将加压的VAST气体注入到烃地层内,或者用开采的材料注入到重质烃分离器容器中以加热,动员,溶解和/或提取重质烃。 轻烃可以与热过程流体混合以增强烃的动员和回收。 微波可以进一步加热VAST气体和/或烃。 硫氧化,煅烧石灰石和/或回收可能会增加二氧化碳。 氧气浓缩可能会增加比功率。 VAST气体可以通过和注入井和/或生产井和/或在交替和/或配对的之字形地层中的顺序注入井之间通过每个VAST组合热和功率回收系统的多个井输送。
    • 6. 发明申请
    • PARTIAL LOAD COMBUSTION CYCLES
    • 部分负荷燃烧循环
    • US20090064653A1
    • 2009-03-12
    • US12202964
    • 2008-09-02
    • David L. HagenIan WylieL. Allan McGuire
    • David L. HagenIan WylieL. Allan McGuire
    • F02C9/00F02C3/30
    • B60H1/032B60H1/3223F01K13/02F01K21/047F02C3/30F02C3/305F02C7/1435
    • The part load method controls delivery of diluent fluid, fuel fluid, and oxidant fluid in thermodynamic cycles using diluent, to increase the Turbine Inlet Temperature (TIT) and thermal efficiency in part load operation above that obtained by relevant art part load operation of Brayton cycles, fogged Brayton cycles, or cycles operating with some steam delivery, or with maximum steam delivery. The part load method may control the TIT at the design level by controlling one or both of liquid and/or gaseous fluid water over a range from full load to less than 45% load. This extends operation to lower operating loads while providing higher efficiencies and lower operating costs using water, steam and/or CO2 as diluents, than in simple cycle operation.
    • 部件加载方法控制稀释液,燃料流体和氧化剂流体在使用稀释剂的热力循环中的输送,以增加部分负载运行中的涡轮进口温度(TIT)和热效率,高于通过相关的Brayton循环的相关部分负载运行获得的 ,雾化的布雷顿循环,或循环运行,一些蒸汽输送,或最大的蒸汽输送。 零件加载方法可以通过在满载到小于45%的负载的范围内控制液体和/或气态流体水中的一种或两种来控制设计级别的TIT。 与简单的循环操作相比,这可以延长操作以降低运行负载,同时提供更高的效率和降低使用水,蒸汽和/或二氧化碳作为稀释剂的运行成本。
    • 9. 发明申请
    • CONTROLLING DIAMOND FILM SURFACES AND LAYERING
    • 控制金刚石薄膜表面和层
    • US20110186942A1
    • 2011-08-04
    • US13018252
    • 2011-01-31
    • Charles WestJohn CarlisleJames NetzelIan WylieNeil Kane
    • Charles WestJohn CarlisleJames NetzelIan WylieNeil Kane
    • H01L27/12H01L29/66B82Y15/00B82Y99/00
    • H01L29/1602B81C1/0015H01L21/02527H01L21/02595H01L21/30625H01L21/3105
    • A method comprising: providing at least one first diamond film comprising polycrystalline diamond, e.g., nanocrystalline or ultrananocrystalline diamond, disposed on a substrate, wherein the first diamond film comprises a surface comprising diamond asperities and having a first diamond film thickness, removing asperities from the first diamond film to form a second diamond film having a second diamond film thickness, wherein the second thickness is either substantially the same as the first thickness, or the second thickness is about 100 nm or less thinner than the first diamond film thickness, optionally patterning the second diamond film to expose substrate regions and, optionally, depositing semiconductor material on the exposed substrate regions, and depositing a solid layer on the second diamond film to form a first layered structure. Applications include for example dielectric isolation in the semiconductor industry, as well as surface acoustic wave devices, scanning probe microscope, and atomic force microscope devices.
    • 一种方法,包括:提供至少一个第一金刚石膜,其包括设置在基底上的多晶金刚石,例如纳米晶体或超微晶金刚石,其中所述第一金刚石膜包括包含金刚石凹凸并具有第一金刚石膜厚度的表面, 第一金刚石膜以形成具有第二金刚石膜厚度的第二金刚石膜,其中所述第二厚度或者与所述第一厚度基本相同,或者所述第二厚度比所述第一金刚石膜厚度薄约100nm或更薄, 所述第二金刚石膜暴露衬底区域和任选地在所述暴露的衬底区域上沉积半导体材料,以及在所述第二金刚石膜上沉积固体层以形成第一层状结构。 应用包括例如半导体工业中的介电隔离以及表面声波器件,扫描探针显微镜和原子力显微镜器件。