水环境

  • 于明泉,常青.高分子重金属絮凝剂的性能及作用机理研究[J].环境科学学报,2005,25(2):180-185

  • 高分子重金属絮凝剂的性能及作用机理研究
  • Study on characteristics and action mechanisms of macromolecule heavy metal flocculant
  • 基金项目:国家自然科学基金项目(批准号:20377020)
  • 作者
  • 单位
  • 于明泉
  • 兰州交通大学环境与市政工程学院, 兰州 730070
  • 常青
  • 兰州交通大学环境与市政工程学院, 兰州 730070
  • 摘要:以含Ni2+废水作为处理对象,主要研究了几个影响高分子重金属絮凝剂去除废水中Ni2+的因素,从而进一步了解高分子重金属絮凝剂的结构和性能.实验结果表明:(1)某些离子存在时,pH值对Ni2+的最高去除率影响不大;(2)水中某些二价阳离子的存在不仅不会消耗高分子重金属絮凝剂的用量,而且会促进Ni2+絮凝沉淀,Ni2+的去除率均在95%以上;(3)水中Fe3+会与Ni2+竞争高分子重金属絮凝剂分子中二硫代羧基上的配位基,若高分子重金属絮凝剂投加量不足,Fe3+的存在将影响螯合体MHMFNi2+的生成;(4)Ni2+和致浊物质会互相促进彼此的去除,浊度的去除率在97%以上.(5)高分子重金属絮凝剂对重金属离子具有选择性,可将部分重金属离子从其它离子中分离开、回收再利用.
  • Abstract:Anovel approach for metal sequestration by the chelating and flocculating capabilities of water-soluble Macromolecule Heavy Metal Flocculant was introduced by using Ni2+ in wastewater as the target metal ion. The basic principle of removing heavy metal ion and turbidity with Macromolecule Heavy Metal Flocculant was mainly discussed, some factors which affected the removal rates in wastewater were also studied. The experimental results showed that: (1) Though the tendency of influence on the removal of Ni2+ and turbidity was opposite with pHvalue changed, an optimum pHexisted, and removal rates of Ni2+ and turbidity were both above 95% when the pHvalue was at 5.5. The pHvalue had little effect on the maximum removal rate of Ni2+ when some other ions (such as Ca2+ mg2+ ) also existed; (2) The existence of some bivalent ions (such as Ca2+ ) in wastewater not only consumed none of Macromolecule Heavy Metal Flocculant, but also promoted the flocculation and sedimentation of Ni2+ . The existence of Ca2+ made the double electricity layer thinner, speeded up the flocculation-sedimentation and broadened the range of the optimum input of Macromolecule Heavy Metal Flocculant. Therefore a better removal result was obtained, which could be advantagous to practical application. It was determined by two characteristics of Ca2+ : firstly, Ca2+ was not easy to react with Macromolecule Heavy Metal Flocculant. Secondl, Ca2+ had a higher positive charge; (3) Fe3+ and Ni2+ in wastewater competed for the ligand dithioic acid of Macromolecule Heavy Metal Flocculant, so the chelate production of MHMF-Ni2+ was affected by the existence of Fe3+ if the Macromolecule Heavy Metal Flocculant was not enough. On the contrary, the maximum removal rate of Ni2+ was higher than that when Fe3+ was absent;(4) Some factors such as charge neutralization as well as metal bridging contributed to the subsequent precipitation and separation of the chelate of MHMF-Ni2+ when Ni2+ was present. At the same time the existence of turbidity-causing substance accelerated the sedimentation chelate of MHMF-Ni2+ . Some dissolved Ni2+ would be absorbed onto the surface of floc and removed further. So Ni2+ and turbidity-causing substance promoted the removal of each other. Then the removal rate of turbidity was above 97%; (5) Macromolecule Heavy Metal Flocculant had the selectivity on the different heavy metal ions. When various heavy metal ions appeared in the wastewater, some of them could be separated and scaveged by the Macromolecule heavy metal flocculant based on the different chelation sequence of Macromolecule Heavy Metal Flocculant and different heavy metal ions(for example Hg2+ Cu2+ >Ni2+ ). The following conclusions were made in accordance with the experiments: (1) Arelatively insoluble chelate forms between Macromolecule Heavy Metal Flocculant and Ni2+ . It spent less time in forming the chelate,and the dimension of chelate were nearly same and it is easy to be separated from the original solution; (2) The solution containing heavy metal of industrial wastewater was generally acidic. And if it was treated with conventional chemical sediment action, the pHvalue must be higher, in order to adjust pHto neutral state which had to consume a large amount of alkal. (3) Treatment of wastewater containing heavy metal ions with Macromolecule Heavy Metal Flocculant had wild range of the pHvalue. In this process turbidity was reduced while removing heavy metal ions. Moreover, the additional equipments and structures are not needed;a better removal result of Ni2+ and turbidity could be attained by less input of Macromolecule Heavy Metal Flocculant. And it is easier to operate and more convenient to manage.

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