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FUEL FLEXIBLE RICH CATALYTIC LEAN BURN SYSTEM FOR LOW BTU FUELS

机译:低BTU燃料的富油柔性富油催化稀燃系统

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Limited fuel resources, increasing energy demand, and stringent emission regulations are drivers to evaluate process off-gases or process waste streams as fuels for power generation. Often these process waste streams have low energy content and their operability in gas turbines leads to issues such as unstable or incomplete combustion and changes in acoustic response. Due to above reasons, these fuels cannot be used directly without modifications or efficiency penalties in gas turbine engines. To enable the use of the wide variety of ultra-low and low Btu fuels in gas turbine engines, a rich catalytic lean burn (RCL~®) combustion system was developed and tested in a subscale high pressure (10 atm.) rig. Previous work has shown promise with fuels such as blast furnace gas (BFG) with Lower Heating Value (LHV) of 3.1 MJ/Nm~3 (85 Btu/scf). The current testing extends the limits of RCL~® operability to other weak fuels by further modifying and improving the injector to achieve enhanced flame stability. Fuels containing low methane content such as weak natural gas with an LHV of 6.5 MJ/Nm~3 (180 Btu/scf) to fuels containing higher methane content such as landfill gas with an LHV of 21.1 MJ/Nm~3 (580 Btu/scf) were tested. These fuels demonstrated improved combustion stability with an extended turndown (defined as the difference between catalytic and non-catalytic lean blow out) of 140°C-170°C (280℉-340℉) with CO and NO_x emissions lower than 5 ppm corrected to 15% O_2.
机译:有限的燃料资源,不断增长的能源需求以及严格的排放法规是评估过程废气或过程废物流作为发电燃料的动力。这些过程废料流通常具有较低的能量含量,它们在燃气轮机中的可操作性导致诸如不稳定或不完全燃烧以及声学响应变化的问题。由于上述原因,如果不对燃气涡轮发动机进行修改或降低效率,则无法直接使用这些燃料。为了能够在燃气轮机中使用各种超低和低Btu燃料,开发了一种富催化稀薄燃烧(RCL〜®)燃烧系统,并在低于10气压的小型规模试验台上进行了测试。以前的工作已经显示出对诸如低热值(LHV)为3.1 MJ / Nm〜3(85 Btu / scf)的高炉煤气(BFG)等燃料的希望。当前的测试通过进一步修改和改进喷油器以增强火焰稳定性,将RCL〜®可操作性的限制扩展到其他弱燃料。甲烷含量低的燃料,如LHV为6.5 MJ / Nm〜3(180 Btu / scf)的弱天然气,或甲烷含量较高的燃料,如LHV为21.1 MJ / Nm〜3(580 Btu / L)的垃圾填埋气scf)进行了测试。这些燃料表现出改善的燃烧稳定性,延长的调节比(定义为催化和非催化稀薄燃尽之间的差异)为140°C-170°C(280℉-340℉),且CO和NO_x排放低于5 ppm达到15%的O_2。

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