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Phosphorus removal and recovery from fosfomycin pharmaceutical wastewater by the induced crystallization process

机译:诱导结晶法从磷霉素制药废水中除磷和回收

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The excessive release of phosphorus is a main cause of eutrophication, but phosphorus itself is an important non-renewable resource. If phosphorus could be recovered from wastewater, it can not only reduce the pollution, but also reach the aim of resource recycle. An induced crystallization process was combined with the schorl/H2O2 system to remove and recover phosphorus from the fosfomycin pharmaceutical wastewater. Firstly, in the schorl/H2O2 heterogeneous Fenton system, the organic phosphorus (OP) in fosfomycin pharmaceutical wastewater was transformed to the inorganic phosphorus (IP), and then IP was recovered by hydroxyapatite (HAP) induced crystallization process. In sequence batch reactors (SBR), the entire crystallization process went through 60 cycles, and each of the cycle lasted for 12 h, including 2 h for reaction and 10 h for sedimentation. The influence of different initial pH values, which were 8, 9, 10 and 11, on the induced crystallized product was investigated. The morphology and structure of the induced crystallized product were analysed. The results indicated that when the pH value was about 8, most of the recovery products was in the form of dicalcium phosphate anhydrous (DCP, CaHPO4). At pH 9 the recovery products were mainly DCP and HAP. As pH increased to 10 or 11, most of the recovery products would be HAP and calcium carbonate. Carbonate involved in the crystallization reaction, especially at pH 11.
机译:磷的过量释放是富营养化的主要原因,但是磷本身是重要的不可再生资源。如果能从废水中回收磷,不仅可以减少污染,而且可以达到资源循环利用的目的。诱导结晶过程与schorl / H2O2系统结合,从磷霉素制药废水中去除和回收磷。首先,在schorl / H2O2非均相Fenton系统中,将磷霉素制药废水中的有机磷(OP)转化为无机磷(IP),然后通过羟基磷灰石(HAP)诱导的结晶过程将IP回收。在顺序分批反应器(SBR)中,整个结晶过程进行了60个循环,每个循环持续12小时,包括2小时反应和10小时沉淀。研究了不同的初始pH值(分别为8、9、10和11)对诱导的结晶产物的影响。分析了诱导结晶产物的形态和结构。结果表明,当pH值约为8时,大多数回收产物为无水磷酸二钙(DCP,CaHPO4)形式。在pH 9时,回收产物主要是DCP和HAP。随着pH值增加到10或11,大多数回收产物将是HAP和碳酸钙。碳酸盐参与结晶反应,尤其是在pH 11时。

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