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Degradation of the azo dye Orange G in a fluidized bed reactor using iron oxide as a heterogeneous photo-Fenton catalyst

机译:使用氧化铁作为非均相光芬顿催化剂在流化床反应器中降解偶氮染料Orange G

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The heterogeneous Fenton process was employed to degrade Orange G (OG) using waste iron oxide as the catalyst in a three-phase fluidized bed reactor (3P-FBR). The morphology and the FTIR spectra of the used BT4 were compared with the fresh catalyst to illustrate the catalyst stability. The catalyst reusability was evaluated by measuring the colour removal in four successive cycles. The effects of major parameters, including pH, H2O2 concentration and catalyst addition on the decolourization of OG were investigated. A satisfactory decolourization efficiency (>92%) could be obtained under the conditions tested, and 78.9% of TOC removal was achieved at a 50 mg L-1 initial OG concentration, 25 mg L-1 H2O2 concentration, pH = 3 and 6 g L-1 BT4 addition. The decolourization of OG was mainly attributed to the homogeneous photo-Fenton reaction, while the heterogeneous catalytic process played an important role in TOC removal. The main intermediates were identified by the GC/MS technique and the degradation pathway of OG was proposed.
机译:在三相流化床反应器(3P-FBR)中,使用废氧化铁作为催化剂,采用非均相Fenton工艺降解橙G(OG)。将用过的BT4与新鲜催化剂的形态和FTIR光谱进行比较,以说明催化剂的稳定性。通过在四个连续循环中测量脱色性来评估催化剂的可重复使用性。研究了pH,H2O2浓度和催化剂添加等主要参数对OG脱色的影响。在测试条件下可获得令人满意的脱色效率(> 92%),在50 mg L-1初始OG浓度,25 mg L-1 H2O2浓度,pH = 3和6 g的条件下,TOC去除率为78.9% L-1 BT4加成。 OG的脱色主要归因于均相光芬顿反应,而异相催化过程在TOC去除中起重要作用。通过GC / MS技术鉴定了主要中间体,并提出了OG的降解途径。

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