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首页> 外文期刊>Applied thermal engineering: Design, processes, equipment, economics >Reducing the unburned combustible in the fly ash from a 45,000 Nm(3)/h Ende Pulverized-Coal Gasifier by applying steam-solid ejector
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Reducing the unburned combustible in the fly ash from a 45,000 Nm(3)/h Ende Pulverized-Coal Gasifier by applying steam-solid ejector

机译:通过施加蒸汽固体喷射器减少45,000nm(3)/ h末端粉碎 - 煤气化器中的粉煤灰中的未燃烧的燃烧

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摘要

Ejector is widely used in Industry areas. Ende pulverized-coal gasifiers (EPCG) as a type of atmospheric-pressure circulating fluidized bed (CFB) gasifier have been widely used in Gasification field; however, in these, the return conduit of the reactor was generally not equipped with a feedback control device, which led to a part of the flue gas flowing directly from the reactor to the cyclone separator through the return conduit. Such a structure reduced the efficiency of the cyclone separator and increased the unburned combustible in the fly ash and fly ash discharge, which reduced the economic efficiency of the EPCG and increased the generated environmental pollution. This paper presents a method of using steam-solid ejectors as the feedback device to provide a stable pressure barrier. The steam-solid ejector was installed on the return conduit of a 45,000 Nm(3)/h EPCG. The steam mass flow rate was varied, and the corresponding pressure barrier of the ejector, the temperature and pressure of the reactor, the effective syngas concentration (CO, H-2), and the amount of unburned combustible in the fly ash were measured. For a steam pressure of 0.5 MPa and mass flow rate greater than 383 kg/h, the outlet pressure of the Ejector was higher than that at the bottom part of the reactor. In this manner, the pressure sealing of the flue gas flowing directly from the reactor to the cyclone separator through the return conduit could be realized. With an increase in the steam mass flow rate, the pressure barrier and the outlet pressure of the ejector continuously increased; the steam mass flow rate had a linear relationship with the pressure barrier. Compared with the original EPCG, when the steam pressure was 0.5 MPa, the mass flow rate was 617 kg/h, effective syngas concentration increased from 73.3% to 74.5%, and the unburned combustible content in the fly ash decreased from 26.9% to 19.9%.
机译:喷射器广泛用于工业领域。 Ende粉碎 - 煤气化器(EPCG)作为一种大气压循环流化床(CFB)气化器已广泛用于气化领域;然而,在这些中,反应器的返回导管通常没有配备有反馈控制装置,其通过返回管道直接从反应器流到旋风分离器的一部分流动。这种结构降低了旋风分离器的效率,并增加了粉煤灰和粉煤灰放电中的不燃烧,这降低了EPCG的经济效率并增加了产生的环境污染。本文呈现了一种使用蒸汽固体喷射器作为反馈装置提供稳定的压力屏障的方法。蒸汽固体喷射器安装在45,000nm(3)/ h EPCG的返回管道上。测量蒸汽质量流量变化,并且反应器的相应压力屏障,反应器的有效合成气浓度(CO,H-2),以及粉煤灰中的不燃烧的燃烧量。对于0.5MPa的蒸汽压力和大于383kg / h的质量流速,喷射器的出口压力高于反应器的底部的出口。以这种方式,可以实现通过返回导管直接流过反应器流过旋风分离器的烟道气的压力密封。随着蒸汽质量流量的增加,喷射器的压力屏障和出口压力连续增加;蒸汽质量流量与压力屏障具有线性关系。与原始EPCG相比,当蒸汽压力为0.5MPa时,质量流量为617千克/小时,有效的合成气浓度从73.3%增加到74.5%,粉煤灰中未燃烧的可燃含量从26.9%下降到19.9 %。

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