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    • 71. 发明申请
    • High power density combined cycle power plant system and method
    • 高功率密度联合循环发电厂系统及方法
    • US20040031256A1
    • 2004-02-19
    • US10642717
    • 2003-08-18
    • William S. Rollins III
    • F02C006/18
    • F01K23/106F01K23/105Y02E20/14Y02E20/16Y02P80/154
    • A process for increasing the specific output of a combined cycle power plant and providing flexibility in the power plant rating, both without a commensurate increase in the plant heat rate, is disclosed. The present invention demonstrates that the process of upgrading thermal efficiencies of combined cycles can often be accomplished through the strategic use of additional fuel and/or heat input. In particular, gas turbines that exhaust into HRSGs, can be supplementally fired to obtain much higher steam turbine outputs and greater overall plant ratings, but without a penalty on efficiency. This method by and large defines a high efficiency combined cycle power plant that is predominantly a Rankine (bottoming) cycle. Exemplary embodiments of the present invention include a load driven by a topping cycle engine, powered by a topping cycle fluid which exhausts into a heat recovery device.
    • 公开了一种增加联合循环发电厂的具体产量并提供发电厂额定值的灵活性的过程,两者都不会相应地增加设备热量。 本发明表明,提高联合循环热效率的过程通常可以通过战略性地使用额外的燃料和/或热输入来实现。 特别是,排放到HRSG中的燃气轮机可以被补充燃烧以获得更高的蒸汽涡轮机输出和更大的总体设备额定值,但是对效率没有惩罚。 这种方法大体上定义了一个主要是兰金(底部)循环的高效率联合循环发电厂。 本发明的示例性实施例包括由顶部循环发动机驱动的负载,其由排放到热回收装置中的顶部循环流体驱动。
    • 73. 发明申请
    • Semi-closed brayton cycle gas turbine power systems
    • US20020023423A1
    • 2002-02-28
    • US09855237
    • 2001-05-14
    • Fermin ViteriRoger E. Anderson
    • F02C006/18
    • F02C3/34F01K21/047F01K23/10F02C1/007F02C1/08F02C3/20F02C6/18F05D2220/72F23L7/005Y02E20/16Y02E20/326Y02E20/344Y02P80/154Y02T50/671
    • A semi-closed combined cycle power system 100 is provided which can also convert an open combined cycle gas turbine 10 into a non-polluting zero emissions power system. The prior art open combined cycle gas turbine 10 includes a compressor 20 which compresses air Anull and combusts the air Anull with a fuel, such as natural gas. The products of combustion and the remaining portions of the air form the exhaust Enull which is expanded through the turbine 40. The turbine 40 drives the compressor 20 and outputs power. The exhaust Enull exits the turbine 40 and then can optionally be routed through a heat recovery steam generator 50 to function as a combined cycle. According to this invention, the exhaust Enull is not emitted into the atmosphere, but rather is routed to a divider 110. The divider 110 includes two outlets for the exhaust Enull including a return duct 120 and a separation duct 130 which both receive a portion of the exhaust Enull. The return duct 120 routes a portion of the exhaust Enull back to the compressor 20. Before reaching the compressor 20, an oxygen duct 150 adds additional oxygen to the exhaust Enull to form a gas mixture C which includes CO2 and steam from the exhaust Enull and oxygen from the oxygen duct 150. This gas mixture C has characteristics which mimic those of air, so that the compressor 20 need not be modified to effectively compress the gas mixture C. The gas mixture C is compressed within the compressor 20 and routed to the combustor 30 where the fuel combusts with the oxygen of the gas mixture Cnull and produces exhaust Enull which is substantially entirely CO2 and steam. This exhaust Enull is routed through the turbine 40 and expanded to drive the compressor 20 and output power. The exhaust Enull exits the turbine 40 and is routed back to the divider 110, preferably by way of a heat recovery steam generator 50 or other heat removal device, so that the semi-closed cycle operates as a combined cycle power system 100. The divider 110 directs a portion of the exhaust Enull to a separation duct 130 which leads to a condenser 140. In the condenser 140 the exhaust Enull is separated by condensation of the steam/water portion of the exhaust and removal of the remaining CO2 as gas from the condenser 140. The only exhaust from the semi-closed power system 100 is water and CO2 from the condenser. The CO2 exhaust is substantially pure and ready for appropriate further handling and disposal. Hence, no pollutants are emitted from the semi-closed power system 100. The return duct 120 can include a partial condenser 210 to condense a portion of the steam within the exhaust Enull. This condensed steam is then routed back through the heat recovery steam generator 50, where it is converted to steam. This steam can be injected through a steam injection port 233 directly into the combustor 30 to enhance the power output and efficiency of a steam injection power system 200 variation of this invention.