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Pursuing the oxy-fuel light-/heavy oil retrofit route in oil refineries - A small scale retrofit study

机译:挖掘炼油厂氧气燃烧/重油改造途径 - 一种小规模改造研究

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Two commercial, one light- and one heavy oil burner for a CEN 250 kW boiler was modified by simple means to allow for operation at controlled dry oxy-fuel conditions. The variables measured for both air- and oxy-firing were the flue gas components; CO_2, CO, O_2 and NO_x, the flue gas exit temperature and boiler water temperatures (in/out). Both burners were run on air based base cases for comparison. The light- and the heavy oil burners were fired at 90 kW and 130 kW, respectively. For the light oil burner an experimental matrix consisting of five runs on air with varying excess air, λ = 1.1-1.25, ratio was performed. For each of the air-fired runs five additional cases were run, with a mixture of O_2/CO_2 replacing the air as oxidizer, with constant X_(O_2) and increasing X_(CO_2). However, for the heavy oil burner only two base cases where run at =1.15 and 1.25 and compared to oxy-fuel conditions with fixed X_(O_2) and varying CO_2 dilution. The main reason for the low number of runs with heavy oil was the large amounts of soot formed, which made heat flux measurements rather difficult. The results for the light oil burner show that on the average, the flue gas volume when shifting to oxy-firing is about × 0.7 times the volume when firing with air. A mass based comparison show that shifting from air- to oxy-firing, on the average results in a reduction in NO formation, an increase in CO, CO_2 and O_2 in the flue gas of about 19, 2.4,4.1 and 4.3 times, respectively. For light fuel oil the flame temperature for air- vs. oxy-firing coincides at around 35-37% O_2 through the burner. Although radiation measurements with light fuel oil was only measured in a single point, it was noticed that the measured radiation flux tends to increase linearly with increasing O_2 concentration, on the average about ×1.5 higher than with air-firing. For heavy fuel oil firing it has been shown that close to air-firing conditions can be reached at oxy-fuel operation at around 30/70. However, peaks of around 1.4 × air firing were observed at certain positions. As with light fuel oil oxyfuel experiments, heavy fuel oil seemed to be just as adaptable to oxy-firing. Also here no operational problems were observed and it is possible to achieve stable oxy-fuel conditions similar to that of air-firing. The main conclusion so far, based on the current experience with simple oxidant switching burning light- to heavy oil on an existing burner/boiler geometry, indicates that operation similar to air-fired burner/boiler behavior is easily achievable. Besides the large amount of soot formed during heavy oil combustion no operating or technical difficulties were experienced with any of the retrofitted burners and combustion conditions comparable with air firing in terms of ignition, flame stability and flame shape was achieved in the oxy-firing mode.
机译:两个商业,一个轻和一条重油燃烧器要CEN 250千瓦锅炉是由简单的手段修饰以允许在受控的干氧 - 燃料条件操作。两个空气和氧燃烧所测量的变量是烟道气体组分; CO_2,CO,O_2和NO_x的,烟道气出口温度和锅炉水的温度(入/出)。这两个燃烧器用于比较基础上的空军基地的情况下运行。该轻型和重油燃烧器在90千瓦和130千瓦燃煤分别。对于轻油燃烧器上的空气由五次运行的具有变化的过量空气的实验矩阵,λ= 1.1-1.25,进行比。对于每个空气燃烧运行附加的5例运行的,具有O_2 / CO_2代替空气作为氧化剂,以恒定X_(O_2)和增加X_(CO_2)的混合物中。然而,对于重油燃烧器只有两个,其中在R = 1.15和1.25运行,并与用固定X_(O_2)氧 - 燃料的条件和不同稀释CO_2基例。对于低数目与重油运行的主要原因是大量烟灰的形成,这使热通量值相当困难的。结果为轻油燃烧器显示,平均而言,转移到氧燃烧当烟气体积为约0.7×倍体积与空气中烧成时。基于质量比较表明,分别从空气转换到氧燃烧,上的平均结果在NO形成的减少,在CO,CO_2和O_2增加了烟道气中的约19,2.4,4.1和4.3倍, 。对于轻质燃油在通过燃烧器周围35-37%O_2火焰温度的空气与氧燃烧一致。虽然与轻质燃油辐射测量在单个点才被测量,注意到的是,测得的辐射通量倾向于与约×1.5比用空气点火更高增加O_2浓度,平均线性增加。对于重油烧它已经表明,接近空气点火条件,可以在全氧燃烧运行在30/70左右即可到达。然而,在某些位置观察周围1.4×空气燃烧的峰值。与轻质燃油富氧燃烧实验,重质燃料油似乎只是为适应氧燃烧。还观察到在这里没有操作上的问题,并且能够实现类似于空气点火的稳定的氧 - 燃料的条件。主要结论到目前为止,基于与简单氧化剂开关轻烧重油在现有的燃烧器/锅炉几何目前的经验,表示类似于空气燃烧器/锅炉行为操作很容易实现。除了重油燃烧过程中形成的大量烟尘的无操作或技术上的困难,用任何改装的燃烧器和点火,火焰稳定性和火焰形状方面与空气燃烧可比燃烧条件中的氧燃烧模式下达到了丰富的经验。

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