期刊文献+

单极层状冷冻法处理苦咸水 被引量:4

Treatment of Brackish Water with Unipolar Layered Freezing Method
在线阅读 下载PDF
导出
摘要 采用单极层状冷冻方法淡化苦咸水,可以获得回收率高、质量好的冰晶.分别取500、1.000、2.000、3.000、5.000.mg/L苦咸水在-2、-4、-6、-8、-10、-12、-14、-16、-18、-20.℃的条件下冷冻,观察分析脱盐率、冷冻温度、冷冻速率、成冰率和苦咸水浓度之间的关系,结果表明:随着冷冻速率增大或者溶液浓度增加脱盐率下降,冷冻速率主要受冷冻温度影响,成冰率主要受冷冻速率和冷冻时间的影响,而溶液浓度对冷冻速率没有明显影响.随水样浓度由低到高,其最佳冷冻温度范围分别为:-6~-10.℃、-4~-8.℃、-6~-10.℃、-2~-6.℃和-2~-8.℃.在成冰率分别为9.5%、9.3%、7.0%、7.8%和8.5%时,各水样的脱盐率达到最高值,分别为94.3%、80.6%、64.8%、68.1%和59.2%. Ice crystals of highquality can be obtained with high recovery rate in the process of brackish water desalination with unipolar layered freezing method.Brackish water with different concentrations of salt(500 mg/L,1 000 mg/L,2 000 mg/L,3 000 mg/L,5 000 mg/L)has been frozen at temperatures from-2 ℃ to-20 ℃ at a regular interval of 2 ℃ and relationships between the factors including desalination rate,freezing temperature,freezing rate,ice growth rate,and concentration of brackish water have been analyzed.Analysis results show that desalination rate declines with the increase of freezing rate and concentration of the samples.Freezing rate mainly depends on freezing temperature.Ice growth rate is mainly determined by freezing rate and freezing time,while the solution concentration has no effect on freezing rate.The optimum freezing temperature ranges for the samples with concentrations of 500 mg/L,1 000 mg/L,2 000 mg/L,3 000 mg/L,5 000 mg/L are-6—-10 ℃,-4—-8 ℃,-6—-10 ℃,-2—-6 ℃ and-2—-8 ℃,respectively.At the optimum freezing temperature,with the ice growth rates of 9.5%,9.3%,7.0%,7.8% and 8.5%,the desalination rates for the brackish water samples reach the maximums of 94.3%,80.6%,64.8%,68.1% and 59.2%,respectively.
出处 《天津大学学报》 EI CAS CSCD 北大核心 2010年第5期429-434,共6页 Journal of Tianjin University(Science and Technology)
基金 科技部"十一五"科技支撑计划资助项目(2006BAK30B02)
关键词 冷冻法 苦咸水 脱盐率 冷冻速率 成冰率 freezing method brackish water desalination rate freezing rate ice growth rate
  • 相关文献

参考文献6

二级参考文献33

共引文献64

同被引文献67

  • 1许映军,李宁,顾卫,史培军,崔维佳.控温法海冰冻融固态脱盐技术研究[J].应用基础与工程科学学报,2006,14(4):470-478. 被引量:20
  • 2许映军,顾卫,陈伟斌,徐学仁,张国明,史培军,李宁,崔维佳.重力法海冰固态自脱盐的姿态效应[J].海洋环境科学,2007,26(1):28-32. 被引量:20
  • 3马敬环,周军,孙宝红,常芙蓉.从淡化后的海水制取纳米级氢氧化镁的工艺[J].化学工业与工程,2007,24(5):428-432. 被引量:10
  • 4Hashim A, Hajjaj M. Impact of desalination plants fluid effluents on the integrity of seawater, with the Arabian Gulf in perspective[J].Desalination, 2005, 182 (1-3) : 373-393.
  • 5Alatiqi Imad, Ettouney Hisham, El-Dessouky Hishamet, et al. Measurements of dynamic behavior of a multistage flash water desalination system[J].Desalination, 2004, 160 (3) : 233-251.
  • 6刘彦华,李保安,张利.用膜蒸馏技术处理反渗透浓盐水工艺介绍[C]//2012青岛国际脱盐大会,青岛,2012.
  • 7Hoepner Thomas, Lattemann Sabine. Chemical impacts from seawater desalination plants - A case study of the northern Red Sea[J]. Desalination, 2003, 152 (1-3): 133-140.
  • 8Rautenbach R, Linn T, AI-Gobaisi D M K. Present and future pretreatment concepts -Strategies for reliable and low-maintenance reverse osmosis seawater desalination[J]. Desalination, 1997, 110 (1-2) : 97-106.
  • 9Cheng L H, Wu P C, Chen J. Numerical simulation and optimal design of AGMD-based hollow fiber modules for desalination[J]. Industrial & Engineering Chemistry Research, 2009, 48 (10) : 4948-4959.
  • 10Oriard T L, Haggerty P D. Forward osmosis utilizing a controllable osmotic agent: US, 2007/0278153 AI [P]. 2006.

引证文献4

二级引证文献24

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部