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Washing Characteristics of Calcinated Washed-Fly-Ash from Municipal Solid Waste Incinerators

机译:生活垃圾焚烧炉煅烧粉煤灰的洗涤特性

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WCCB—Washing, Calcinating and Changing the treated fly ash into the raw material in cement industry— has been proposed to recycle fly ashes from municipal solid waste incinerator. We have studied the washing process and calcination process. Here we will discuss the post-washing step after the fly ash was washed and then calcinated. As we have studied the hierarchy of parameters and chlorides distribution in the washing step, and as most of the chlorides have been reduced in washing and calcination step, it is not so important to discuss the operation condition for post-washing here. So the purpose of this study is that one is to make sure that calcination is necessary to reduce chlorine besides the function of evaporation, and the other is to discuss the characteristics of chlorides in the residues. The operation condition of post-washing is once-washing (Liquid (ml)/ Solid (gram)=3, mixing time=10min, disturbing speed=150 rpm). We also studied three kinds of fly ashes: raw fly ash from the boiler or economizer of incineration system (RFA), fly ash collected in bag filter with the injection of Ca(OH)2 for acid removal (CaFA) and fly ash collected in bag filter with the injection of NaHCO3 for acid removal (NaFA). The residue we used is from the washing process and calcinated by several conditions we selected from the calcination process by checking the calcination results. It was found that the sequence of WCCB system is reasonable and can effectively reduce chlorine content in fly ash, and calcination can decompose some insoluble chlorides to soluble chlorides. As to CaFA-II# during calcination, some chlorides reacted with some other compounds in the residues and then be fixed. As to RFA-II# and NaFAIl#, higher temperature got better results, however, when the heating temperature is higher than 400 °C, the increasing portion of soluble chlorides did not go as fast as the rising of heating temperature.
机译:WCCB(洗涤,煅烧和将处理后的粉煤灰转变成水泥工业的原料)已被提议用于回收城市固体废物焚化炉中的粉煤灰。我们已经研究了洗涤过程和煅烧过程。在这里,我们将讨论粉煤灰被洗涤然后煅烧后的后洗涤步骤。由于我们研究了洗涤步骤中参数和氯化物分布的层次结构,并且由于大多数氯化物已在洗涤和煅烧步骤中还原,因此在此处讨论后洗涤的操作条件并不是很重要。因此,本研究的目的是:一方面确保除蒸发功能外还需要煅烧以减少氯,另一方面是讨论残渣中氯化物的特性。后洗涤的操作条件是一次洗涤(液体(ml)/固体(克)= 3,混合时间= 10min,干扰速度= 150 rpm)。我们还研究了三种粉煤灰:来自锅炉或焚化炉节能器(RFA)的原粉煤灰,袋式除尘器中收集的粉煤灰以及注入除酸的Ca(OH)2(CaFA)以及粉煤灰收集的粉煤灰。袋式除尘器,注入的碳酸氢钠用于除酸(NaFA)。我们使用的残留物来自洗涤过程,并通过检查煅烧结果从煅烧过程中选择的几种条件下进行煅烧。研究发现,WCCB体系的顺序合理,可以有效降低粉煤灰中的氯含量,煅烧可以将一些不溶性氯化物分解为可溶性氯化物。至于煅烧过程中的CaFA-II#,一些氯化物与残留物中的其他化合物反应,然后被固定。对于RFA-II#和NaFAIl#,较高的温度可获得更好的结果,但是,当加热温度高于400°C时,可溶性氯化物的增加部分的上升速度不如加热温度的上升快。

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