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Studies on the operation of loop-seal in circulating fluidized bed boilers

机译:循环流化床锅炉回路密封的运行研究

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Loop-seal, considered heart of a circulating fluidized bed (CFB), returns solids captured by cyclone to the base of the riser while preventing direct flow of gas from high pressure riser to the low-pressure cyclone. This non-mechanical valve is used in thousands of CFB systems yet only a limited information is available on its working. Present research studies the flow of solids through a loop-seal and the effect of several design and operating parameters on it. This experimental study was conducted in a loop-seal 110 mm × 448 mm × 400 mm high connected to a riser 152 mm diameter and 5180 mm high. Majority of the experiments was done with 171 μm sand though several other size and type of solids were studied for their flowability. It was found that for the solids to flow through the loop-seal a minimum level of aeration, in excess of that required for minimum fluidization was required. The length of the horizontal passage connecting the supply and recycle chambers of the loop-seal had an important effect on the solids flow. For example, the minimum aeration for the onset of solids flow increases with increase in this length. The pressure drop per unit length across the passage also increased with the passage length. The air fed into the supply chamber is split such that the superficial air velocity in the supply chamber (or the standpipe) remained below the minimum fluidization velocity of the particles while the remaining air conveys solids through the horizontal passage. Present study showed that the solids flowing through the horizontal passage are neither fully fluidized nor moving packed or suspended solids. It moves as a segregated flow of solids driven by hydrostatic pressure and fluid drag.
机译:循环密封被视为循环流化床(CFB)的心脏,它将旋风分离器捕获的固体返回到立管的底部,同时防止气体从高压立管直接流向低压旋流器。这种非机械阀已在数千个CFB系统中使用,但有关其工作的信息非常有限。当前的研究研究了固体通过环封的流动以及几种设计和运行参数对其的影响。这项实验研究是在110毫米×448毫米×400毫米高的环形密封件上进行的,该密封件连接到直径152毫米,高5180毫米的冒口。大多数实验都是用171μm砂子进行的,尽管还研究了其他几种尺寸和类型的固体的流动性。已经发现,为了使固体流过环封,需要的最小通气水平超过最小流化所需的通气水平。连接环封的进料室和再循环室的水平通道的长度对固体流动有重要影响。例如,固体流开始的最小通气量随着该长度的增加而增加。贯穿通道的每单位长度的压降也随着通道长度而增加。送入供应室的空气被分开,以使供应室(或竖管)中的表观空气速度保持低于颗粒的最小流化速度,同时剩余的空气通过水平通道输送固体。目前的研究表明,流经水平通道的固体既没有完全流化,也没有移动堆积或悬浮的固体。它在静水压力和流体阻力的驱动下作为固体的分离流运动。

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