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The Research On Forward Osmosis In Treating High-salinity Wastewater Containing Heavy Metal Zn2+and Ni2+

Posted on:2018-01-03Degree:MasterType:Thesis
Country:ChinaCandidate:H F TengFull Text:PDF
GTID:2311330512490889Subject:Environmental engineering
Abstract/Summary:PDF Full Text Request
High-salinity wastewater containing heavy metal is one of sewages that are most difficult to be treated,and receives more and more attention with the acceleration of the industrialization process in China.Traditional processing methods tend to have small range of processing,serious secondary pollution,low recycling rate of heavy metal and so on.It is urgent to find a novel method to treat this kind of wastewater.FO can be an alternative method due to the high resistance to various pollutants,relatively low pollution tendency and high pollution reversibility.Therefore,in this study,the performance of forward osmosis(FO)in treating the high-salinity feed waters was investigated by using NaCl as the driving solute and high concentration of NaCl solution as high-salinity wastewater.The performance of FO in treating high-salinity wastewater containing heavy metals was studied by adding heavy metal ions Zn2+,Ni2+,mixed ions Zn2+and Ni2+to high concentration of NaCl solution.The effects of temperature,membrane orientation,salinity of feed solution(FS)on FO performance in treating high-salinity wastewater were first to be investigated,the performance index was water flux.The optimal operating conditions were determined through the study.Results showed that water flux decreases with the increase of FS salinity.When FS salinity is low,the effect of temperature and membrane orientation on water flux is greater:the water flux in the pressure retarded osmosis(PRO)mode is greater than that in the forward osmosis(FO)mode.And water flux obtained at 35℃ is greater than at 25℃ and slightly less than at 45℃.When FS salinity is high,the effect of temperature and membrane orientation on water flux is small.Considering the efficiency of treatment and energy consumption,35℃ was selected as the best treatment temperature.Then the water flux and the removal efficiency of Zn2+ were investigated at different temperature and membrane orientation by adding heavy metal ions Zn2+ to high concentration of NaCl solution.Results showed that the effect of Zn2+ on water flux is relatively small.The removal efficiency of Zn2+ was higher than 95%,and tend to be increased with higher FS salinity and lower initial concentration of Zn2+in FS.Furthermore,the removal efficiency of Zn2+ in FO mode was higher than that in PRO mode in low salinity FS,while the two modes had a similar removal efficiency of Zn2+ in high salinity FS.By the study of water flux and removal efficiency of Zn2+ in long-term mode,it can be seen that FO technology has a relatively optimal time for the treatment of high-salinity wastewater containing Zn2+ generally this time is 10-11 h.By adding heavy metal ions Ni2+ to high concentration of NaCl solution,the water flux and the removal efficiency of Ni2+ were investigated at different temperature and membrane orientation.The results showed that the addition of Ni2+lowered the water flux in low salinity FS,while slightly increased in high salinity FS.The removal efficiency of Ni2+ of the FO membrane was higher than 98%,and increased with the FS salinity.Furthermore,the removal efficiency of Ni2+ in FO mode was lower than that in PRO mode in low salinity FS while the situation was opposite in high salinity FS.But when the salinity of FS was higher,both models have a high rejection rate for Ni2+.The above results showed that FO applied in the treatment of high-salinity wastewater containing Ni2+ is feasible.In the feasibility study of using FO technology to treat high-salinity wastewater containing Zn2+ and Ni2+,the water flux and the removal efficiency of Zn2+ and Ni2+ were investigated by using NaCl solution containing Zn2+ and Ni2+ as FS.The driving effect was compared with that of the treatment of high-salinity wastewater(baseline),high-salinity wastewater containing Zn2+ and high-salinity wastewater containing Ni2+.The water fluxes gained by four solutions were in sequence of:In low salinity FS,baseline>high-salinity wastewater containing Zn2+>high-salinity wastewater containing Zn2+ and Ni2+>high-salinity wastewater containing Ni2+.In high salinity FS,water flux gained by high-salinity wastewater containing Ni2+was slightly higher than baseline,while water fluxes gained by the rest three kinds of solutions were close.But in higher salinity FS,water fluxes gained by four different types of wastewater were relatively close.The removal efficiency of heavy metal ions in mixed solution higher than that in single solution.Studies on FO membrane scaling have shown that membrane fouling can be effectively removed by simple physical cleaning,and FO mode<PRO mode,low salinity<high salinity.The above results indicated that FO technology could be used to treat high-salinity wastewater and high-salinity wastewater containing Zn2+ and Ni2+,and the study results of different factors on water flux and the retention rate of heavy metals are helpful to the large-scale treatment of high-salinity wastewater in industrial production,thereby realizes the reduction and reutilization of high-salinity wastewater.
Keywords/Search Tags:Forward osmosis, High-salinity wastewater, Removal efficiency, Water flux, Membrane fouling
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