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Microbial desalination cell combined with capacitive deionization /membrane capacitive deionization to desalinate seawater

机译:微生物脱盐细胞与电容式去离子/膜电容去离子联合到白藜芦醇

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Microbial desalination cell (MDC) was considered inefficient to desalinate salt water with low salt concentration, therefore, the feasibility of using capacitive deionization (CDI) and membrane capacitive deionization (MCDI) as a post-processing technologies for MDC was investigated in this study, as well as the possibility of using MDC as the power supply for CDI and MCDI. The internal resistances of MDC with different salt concentration, the desalination rate and fresh water yield during a typical desalination cycle under initial salt concentration of 35 g/L were investigated in order to find out the deadline salt concentration for the MDC to desalinate effectively. The internal resistance increased from 21.7 to 602 Ω as the concentration of salt water decreased from 35 g/L to 0.1g/L. The salt water volume increased from 42 to 48 ml when the salt concentration decreased from 35 to 15 g/L, then decreased to 38 ml at the end of one desalination cycle when the salt concentration achieved 0.05 g/L due to the salt gradient (osmotic pressure). The maximum desalination rate during one typical desalination cycle in our experiment reached 5.65 mg/h when salt concentration decreased from 27.26 to 26.32 g/L, while the minimum desalination rate was 0.534 mg/h when salt concentration decreased from 0.38 to 0.05 g/L. It was concluded that MDC was not suitable to desalinate salt water with salt concentration less than 1 g/L. When CDI and MCDI were used as the post-processing technologies for MDC, a better performance in term of electrosorption capacity was obtained from MCDI with an influent salt concentration of 1 g/L. The experimental result also showed that the electrosorption capacity of MCDI with MDC as power supply was more than that with potentiostat as power supply at 0.8V, this suggests that MDC could be an alternative power supply for MCDI.
机译:微生物脱盐细胞(MDC)被​​认为是低于盐浓度的脱盐盐水效率低,因此,在本研究中研究了使用电容去离子(CDI)和膜电容去离子(MCDI)的可行性,作为MDC的后处理技术,除了使用MDC作为CDI和MCDI的电源的可能性。研究了MDC在初始盐浓度为35g / L的典型脱盐循环期间具有不同盐浓度,脱盐率和淡水产量的内部电阻,以便有效地发现MDC的截止日期盐浓度。由于盐水浓度从35g / l降低至0.1g / l,内阻从21.7增加到602Ω增加。当盐浓度从35〜15g / L降低时,盐水量从42〜48mL增加,然后在盐浓度由于盐梯度达到0.05g / L时,在一个脱盐周期结束时降至38ml(渗透压)。当盐浓度从27.26降至26.32g / L时,我们实验中一个典型的脱盐周期中的最大脱盐速率达到5.65mg / h,而最低脱盐率为0.534mg / h,盐浓度从0.38降低0.05克/小时。得出结论,MDC不适合盐浓度小于1g / L的盐水。当CDI和MCDI被用作MDC后处理技术时,从MCDI获得电吸收能力的更好的性能,其流入的盐浓度为1g / l。实验结果还表明,MCDI具有MDC作为电源的电机容量大于0.8V的电源,这表明MDC可以是MCDI的替代电源。

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