会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 3. 发明申请
    • SYSTEMS AND METHODS FOR POWER GENERATION WITH CARBON DIOXIDE ISOLATION
    • 用二氧化碳分离发电的系统和方法
    • US20080104939A1
    • 2008-05-08
    • US11557254
    • 2006-11-07
    • STEPHANIE MARIE-NOELLE HOFFMANNMICHAEL BARTLETT
    • STEPHANIE MARIE-NOELLE HOFFMANNMICHAEL BARTLETT
    • B01D53/00F02C3/00F02C7/00
    • F02C3/10F02C3/02F02C6/18Y02E20/16
    • A power generation system includes at least one turbine system. The turbine system includes a compressor section comprising at least one stage, configured to supply a compressed oxidant and a combustion chamber configured to combust the compressed oxidant and a fuel stream comprising carbon-based fuels and to generate a hot flue gas. The turbine system further includes an expander section having an inlet for receiving the hot flue gas comprising at least two stages. The two stages include a high-pressure expander configured to generate an expanded exhaust gas rich in CO2. The high-pressure expander fluidly coupled to a low-pressure expander configured to generate a final exhaust and electrical energy. A CO2 separation system is fluidly coupled to the high-pressure expander for receiving the expanded exhaust gas from the high-pressure expander and providing a CO2 lean gas that is then fed to the low-pressure expander.
    • 发电系统包括至少一个涡轮机系统。 涡轮机系统包括包括至少一个级的压缩机部分,其构造成供应压缩的氧化剂和被配置为燃烧压缩的氧化剂的燃烧室和包含碳基燃料的燃料流并产生热的烟道气。 涡轮机系统还包括具有用于接收包括至少两个级的热烟道气的入口的膨胀器部分。 这两个阶段包括构造成产生富CO 2的膨胀废气的高压膨胀器。 流体耦合到低压膨胀器的高压膨胀器被配置成产生最终的排气和电能。 CO 2分离系统流体耦合到高压膨胀器,用于接收来自高压膨胀器的膨胀废气,并提供CO 2稀有气体 供给低压膨胀机。
    • 4. 发明申请
    • SYSTEMS AND METHODS FOR POWER GENERATION WITH CARBON DIOXIDE ISOLATION
    • US20080104938A1
    • 2008-05-08
    • US11557250
    • 2006-11-07
    • MATTHIAS FINKENRATHMICHAEL BARTLETT
    • MATTHIAS FINKENRATHMICHAEL BARTLETT
    • B01D53/00F02C3/00F02C7/00
    • F02C3/02F01K23/10F02C3/10F02C6/18Y02E20/326
    • A power generation system includes a first turbine system. The first turbine system includes a first compressor section comprising at least two stages. The two stages includes a first low pressure compressor fluidly coupled to a first high pressure compressor configured to supply a first portion of compressed oxidant and a second portion of compressed oxidant A first combustion chamber is configured to combust said first portion of compressed oxidant and a first fuel stream comprising carbon-based fuels and to generate a first hot flue gas. The first turbine system further includes a first expander section having an inlet for receiving said first hot flue gas and generating a first expanded exhaust gas rich in CO2. The first high-pressure expander is fluidly coupled to a first low-pressure expander configured to generate a first exhaust and electrical energy. A CO2 separation system is fluidly coupled to the high-pressure expander for receiving said first expanded exhaust gas from said first high-pressure expander and provide a CO2 lean gas that is then fed to said first low-pressure expander. The power generation system also includes a second turbine system including a second compressor section comprising at least two stages. The two stages includes a second low-pressure compressor fluidly coupled to a second high pressure compressor, wherein said high pressure compressor is configured to receive said second portion of compressed oxidant. A second combustion chamber is configured to combust a second fuel stream comprising carbon-based fuels and to generate a second hot flue gas and a second expander section is configured to receive said second hot flue gas and to generate a second final exhaust and electrical energy. The second compressor section is configured to receive said second final exhaust comprising carbon dioxide and to discharge a recycle stream from said second high pressure compressor to said second combustion chamber and a split stream from said second low-pressure compressor to said first high pressure compressor.