Durán A, Monteagudo J M, Sanmartín I, García-Peña F, Coca P
Department of Chemical Engineering, Escuela Técnica Superior de Ingenieros Industriales, University of Castilla-La Mancha, Avda. Camilo José Cela 3, 13071 Ciudad Real, Spain.
J Environ Manage. 2009 Mar;90(3):1370-6. doi: 10.1016/j.jenvman.2008.08.002. Epub 2008 Sep 17.
The aim of this work was to improve the quality of aqueous effluents coming from the Gasification Unit in an Integrated Gasification Combined Cycle (IGCC) Thermoelectric Power Station, with the purpose of fulfilling the future more demanding normative. To this end, an integral wastewater treatment including coagulation, flocculation, neutralization, photocatalytic oxidation, and ion-exchange has been studied. A final scheme has been proposed to remove pollutants. All the parameters of the treated wastewater are below pouring specifications. In the first stage, the wastewater was treated with CaCl2 (optimal dose=11 g CaCl2/g F-) as coagulant and a commercial anionic polyelectrolyte (optimal dose=0.02 g/g F-) as flocculant to remove fluoride ions (99%) and suspended solids (92%). The water was then neutralized, improving the degree of transmission of ultraviolet light, allowing the faster photo-degradation of pollutants. The photochemical study included different systems (H2O2, UV/H2O2, Fenton, Fenton-like, UV/Fenton, UV/Fenton-like and UV/H2O2/O2). In the Fenton-like system, the influence of two parameters (initial concentration of H2O2 and amount of Cu(II)) on the degradation of cyanide and formate (taken as the reference of the process) was studied. Experimental results were fit using neural networks (NNs). Results showed that the photocatalytic process was effective for total cyanide destruction after 60 min, while 180 min was needed to remove 80% of formates. However, a more simple system with UV/H2O2/O2 yields similar results and is preferred for industrial application due to fewer complications. Finally, an ion-exchange process with Amberlite IRA-420 was proposed to remove the excess of chlorides added as a consequence of the initial coagulation process.
这项工作的目的是提高整体煤气化联合循环(IGCC)热电厂气化单元排出的废水质量,以满足未来更严格的规范要求。为此,研究了包括混凝、絮凝、中和、光催化氧化和离子交换在内的一体化废水处理方法。已提出了一个去除污染物的最终方案。处理后废水的所有参数均低于排放标准。在第一阶段,使用CaCl2(最佳剂量 = 11 g CaCl2/g F-)作为混凝剂和一种商业阴离子聚电解质(最佳剂量 = 0.02 g/g F-)作为絮凝剂处理废水,以去除氟离子(99%)和悬浮固体(92%)。然后将水进行中和,提高紫外线的透射程度,使污染物更快地光降解。光化学研究包括不同的体系(H2O2、UV/H2O2、芬顿、类芬顿、UV/芬顿、UV/类芬顿和UV/H2O2/O2)。在类芬顿体系中,研究了两个参数(H2O2的初始浓度和Cu(II)的量)对氰化物和甲酸盐(作为该过程的参考)降解的影响。实验结果采用神经网络(NNs)进行拟合。结果表明,光催化过程在60分钟后对总氰化物的破坏有效,而去除80%的甲酸盐需要180分钟。然而,UV/H2O2/O2这种更简单的体系能产生类似的结果,并且由于并发症较少而更适合工业应用。最后,提出了用Amberlite IRA - 420进行离子交换的过程,以去除由于初始混凝过程而添加的过量氯化物。