首页> 外文会议>International Conference on Fluidized Bed Combustion; 20050522-25; Toronto(CA) >THE KINETICS OF OXIDATION OF CHARS FROM THREE DIFFERENT COALS, AS MEASURED IN FLUIDIZED BEDS
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THE KINETICS OF OXIDATION OF CHARS FROM THREE DIFFERENT COALS, AS MEASURED IN FLUIDIZED BEDS

机译:从流化床中测得的三种不同煤中焦炭氧化的动力学

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摘要

There is substantial disagreement over the order of the reaction between a coal char and O_2. This is chiefly because of the difficulties of making good measurements when burning is kinetically controlled; thus heat and mass transfer can often obscure the true kinetics of the reaction. Consequently, a fluidized bed is an attractive reactor in which to measure the rate of this reaction. Chars from three different coals (of high, medium and low ranks) were prepared. The rate of oxidation of a char was measured by adding a small mass ( ~ 3 mg) of tiny particles (sieved to 106 - 150 μm) of the char to a fluidized bed of silica sand (90 - 126 μm), which was electrically heated to a fixed temperature between 700 and 950℃. The fluidizing gas was a mixture of O_2 and N_2 at 1 bar; its composition varied between 0 and 100% O_2. The concentrations of CO and CO_2 were continuously measured in the off-gases from the bed, using i.r. analysers, thus enabling the rate of oxidation of the added batch of char to be measured. Interestingly, it was found necessary to modify the quartz cylinder housing the fluidized bed to prevent backmixing of ambient air into the freeboard. The char particles were sufficiently small that mass transfer to their exteriors did not control the rate of reaction. Furthermore, the rapid rates of heat transfer from the bed to the particles of char ensured that the char burned at the temperature of the bed. Likewise, the mass of added char was small enough for the rate of burning not to be controlled by inter-phase mass transfer. The maximum rate of oxidation was taken to be the initial rate, which could, at least in principle, be correlated with the initial properties of a char, such as its BET area, pore diameters, etc. The char of the low-rank coal burned with kinetics which were zeroth order in O_2 and with a negligible activation energy. The other two coals had orders of reaction which were 0.7 - 0.8 at 700℃, but 0.2 -0.25 at 950℃. These orders are discussed in detail.
机译:煤焦和O_2之间的反应顺序存在很大分歧。这主要是因为在动力学控制燃烧时难以进行良好的测量;因此,传热和传质通常会掩盖反应的真实动力学。因此,流化床是吸引人的反应器,在其中测量该反应的速率。从三种不同的煤(高,中,低等级)制备了焦炭。炭的氧化速率是通过将少量(约3 mg)细小颗粒(筛分为106-150μm的炭)加到硅砂的流化床(90-126μm)中进行测量的,加热到700至950℃的固定温度。流化气体为1 bar的O_2和N_2的混合物;它的组成在0至100%O_2之间变化。使用红外光谱仪连续测量床层废气中的CO和CO_2浓度。分析仪,从而能够测量添加的焦炭批次的氧化速率。有趣的是,发现有必要对容纳流化床的石英缸进行改造,以防止周围空气混入干舷。炭颗粒足够小,以至于质量转移到其外部无法控制反应速率。此外,从床到焦炭颗粒的快速热传递速率确保了焦炭在床的温度下燃烧。同样,加入的焦炭的质量足够小,以致燃烧速率不受相间传质的控制。最大氧化速率取为初始速率,至少在原则上可以与炭的初始特性(例如其BET面积,孔径等)相关。低阶煤的炭燃烧时的动力学在O_2中为零级,活化能可忽略不计。另外两种煤的反应级数在700℃为0.7-0.8,在950℃为0.2-0.25。这些订单将详细讨论。

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