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REDUCTION OF DIOXIN EMISSIONS FROM WAELZ PROCESS OPERATED IN ACIDIC OR BASIC MODE

机译:从酸性或基本模式下操作的Waelz工艺减少二恶英排放

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Polychlorinated dibenzo-p-dioxin and dibenzofuran (PCDD/F) concentration measured in stack gas of the Waelz plant investigated was as high as 150 ng-TEQ/Nm3 in 2005 due to its relatively high dioxin formation potential and low PCDD/F removal efficiency (<70%) achieved with the bag filter (BF). In 2006, activated carbon injection (ACI) technology was adopted in the Waelz plant investigated to reduce PCDD/F emission. Flue gases samplings were conducted at different sampling points to evaluate the removal efficiency and the partitioning of PCDD/Fs between vapor/solid phases in this facility. By applying ACI + BF, the PCDD/F concentrations of stack gas was dramatically decreased to 3.38 ng-TEQ/Nm3 as the activated carbon injection rate was controlled at 40 kg/h. With adsorbent injection + dual baghouse filter (DBF) system being adopted in 2007, the PCDD/F concentration in stack gas was significantly reduced to 0.235 ng-I-TEQ/Nm3 with the adsorbent injection rate at 16 kg/h. In practice, the carbon-type adsorbent is mixed with part of the fly ash collected by cyclone and then injected into the flue gas. In 2008, Ca(OH)2 was applied to replace SiO2 as part of the input material of this facility and its operation was converted from acidic mode to basic mode. In the meantime, the PCDD/F concentration measured at stack gas was further reduced to 0.123 ng-TEQ/Nm3. With this operation mode, the total PCDD/F emission flow on the basis of treating one kg of EAF dust in this facility was dramatically decreased from 1,925 to 269 ng-I-TEQ/kg EAF-dust treated.
机译:由沃思司植物堆气堆气体测量的多氯二苯甲苯-P-二恶英和二苯并呋喃(PCDD / F)浓度在2005年,2005年高达150 ng-TEQ / NM3,由于其相对高的二恶英形成电位和低PCDD / F去除效率用袋式过滤器(BF)实现(<70%)。 2006年,沃尔斯工厂采用活性炭注射(ACI)技术,以减少PCDD / F排放。在不同的采样点进行烟道气体采样,以评估该设施中蒸气/固相之间PCDD / FS的去除效率和分配。通过施加ACI + BF,堆叠气体的PCDD / F浓度显着降低至3.38ng-TEQ / NM3,因为活性炭注射率被控制在40kg / h。采用吸附注射+双袋式过滤器(DBF)系统于2007年采用,堆垛气体的PCDD / F浓度明显降低至0.235ng-I-TEQ / NM3,吸附剂注射率为16 kg / h。实际上,碳型吸附剂与由旋风分离器收集的粉煤灰的一部分混合,然后注入烟道气中。 2008年,将Ca(OH)2施加以替换SiO2作为该设施的输入材料的一部分,其操作从酸性模式转换为基本模式。同时,在堆气中测量的PCDD / F浓度进一步降低至0.123ng-TEQ / NM3。利用这种操作模式,基于在该设施中处理一千克EAF灰尘的基础上的总PCDD / F排放流量从1,925到269 ng-I-TEQ / kg EAF粉末处理得显着降低。

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