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Basic investigations on burner design for high pressure entrained flow gasifier: Influence of pressure and fluid viscosity on twin fluid atomization

机译:高压夹带流动气体燃烧器设计的基本研究:压力和流体粘度对双液雾化的影响

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The conversion of low-grade fossil and biogenic fuels to a high quality chemical energy carrier (syngas) in high pressure entrained flow gasification process opens a wide spectrum for energy efficient fuel conversion. The syngas can be converted to methane (SNG), liquid fuels (BtL/CtL) or it can be fired in a gas turbine of a combined cycle power plant (IGCC) to produce electricity and heat with high efficiency. This so called poly-generation gives maximum operational flexibility combined with fuel- and product flexibility at high energetic efficiency. Currently such a thermochemical process is being tested on a pilot scale at KIT. The so called bioliq process produces synthetic fuels out of residual biomass (BtL) [1]. The operation of a technical entrained flow gasifier aims for complete fuel conversion into a tar-free syngas at minimum oxygen consumption, i.e. maximum cold gas efficiency. Oxygen as the gasification agent also serves as atomization agent in the commonly applied twin fluid nozzles. Based on the required stoichiometry for the gasification reaction there is only a limited amount of atomization agent available (low gas to liquid ratio, GLR) for slurry fed and oxygen blown entrained flow gasifiers. As the droplet size distribution generated by the burner has a significant influence on the fuel conversion and the synthesis gas quality [2], a fine and homogenous spray of high viscous suspension fuel (slurry) has to be generated with minimum amount of atomization agent. For optimization of design and scale-up of the burner nozzle, fundamental knowledge concerning the atomization behavior of pumpable high viscous, non-Newtonian slurries at high process pressure is necessary. In this context, the present work focuses on the influence of the physical liquid properties (dynamic viscosity, Newtonian and non-Newtonian rheological behavior) and the operational parameters (reactor pressure, GLR, gas velocity) on the spray quality generated by a twin-fluid atomizer.
机译:低级化石和生物燃料转化为高压夹带流动气化过程中的高质量化学能源载体(合成气)开辟了广泛的节能燃料转换。合成气可以转化为甲烷(SNG),液体燃料(BTL / CTL),或者它可以在组合循环发电厂(IGCC)的燃气轮机中烧制,以高效地产生电力和热量。这所谓的多相产生最大的运行灵活性,以高能效率为燃料和产品的灵活性。目前,这种热化学过程正在试用套件的试验规模上进行测试。所谓的BIOLIQ工艺产生除残留生物质(BTL)中的合成燃料[1]。技术夹带流动气化器的操作旨在将燃料转化成最小耗氧性的焦油合成气,即最大冷气效率。作为气化剂的氧气也用作常用的双流体喷嘴中的雾化剂。基于用于气化反应的所需化学计量,仅有有限量的雾化剂(低气体与液体比,GLR)用于浆料供给和氧气吹入的流动气体。由于燃烧器产生的液滴尺寸分布对燃料转换和合成气质[2]具有显着影响[2],因此必须以最小量的雾化剂产生精细和均匀的高粘性悬浮燃料(浆料)的喷雾。为了优化燃烧器喷嘴的设计和扩展,需要有关泵送高粘性的雾化行为的基础知识,是在高过程压力下的泵送高粘性的非牛顿浆料的雾化行为。在这种情况下,本作的工作侧重于物理液体性质(动态粘度,牛顿和非牛顿流变学行为)和操作参数(反应器压力,GLR,气体速度)对双胞胎产生的喷雾质量的影响流体雾化器。

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