您的位置: 专家智库 > >

国家自然科学基金(21307149)

作品数:3 被引量:9H指数:2
相关作者:李洁王军李红岩更多>>
相关机构:中国科学院生态环境研究中心更多>>
发文基金:国家自然科学基金更多>>
相关领域:化学工程天文地球环境科学与工程更多>>

文献类型

  • 3篇期刊文章
  • 1篇会议论文

领域

  • 4篇化学工程
  • 2篇环境科学与工...
  • 1篇天文地球

主题

  • 2篇膜蒸馏
  • 1篇丁酯
  • 1篇对苯二甲酸
  • 1篇对苯二甲酸乙...
  • 1篇乙二醇酯
  • 1篇直接接触式
  • 1篇渗透膜
  • 1篇生活污水
  • 1篇疏水膜
  • 1篇添加剂
  • 1篇脱盐
  • 1篇污水
  • 1篇纤维素膜
  • 1篇邻苯二甲酸二...
  • 1篇聚对苯
  • 1篇聚对苯二甲酸
  • 1篇聚对苯二甲酸...
  • 1篇聚对苯二甲酸...
  • 1篇聚酯网
  • 1篇甲酸

机构

  • 2篇中国科学院生...

作者

  • 2篇王军
  • 1篇李红岩
  • 1篇侯得印
  • 1篇李洁
  • 1篇李国亮

传媒

  • 2篇Journa...
  • 1篇水处理技术

年份

  • 1篇2017
  • 3篇2016
3 条 记 录,以下是 1-4
排序方式:
醋酸纤维素正渗透膜的制备及脱盐研究
随着人口的增长和经济的发展,能源、资源和环境污染问题越来越突出,给生态文明建设构成了极大的威胁。其中,水资源短缺和水环境污染问题日益显著,促使人们开发各种水处理技术,解决日益严峻的水环境问题。膜分离技术具有分离效率高、设...
李国亮王军侯得印
文献传递
Fabrication and performance of PET mesh enhanced cellulose acetate membranes for forward osmosis被引量:2
2016年
Polyethylene terephthalate mesh(PET) enhanced cellulose acetate membranes were fabricated via a phase inversion process. The membrane fabrication parameters that may affect the membrane performance were systematically evaluated including the concentration and temperature of the casting polymer solution and the temperature and time of the evaporation, coagulation and annealing processes. The water permeability and reverse salt flux were measured in forward osmosis(FO) mode for determination of the optimal membrane fabrication conditions. The optimal FO membrane shows a typical asymmetric sandwich structure with a mean thickness of about 148.2 μm. The performance of the optimal FO membrane was tested using 0.2 mol/L Na Cl as the feed solution and 1.5 mol/L glucose as the draw solution. The membrane displayed a water flux of 3.47 L/(m2·hr) and salt rejection of95.48% in FO mode. While in pressure retarded osmosis(PRO) mode, the water flux was4.74 L/(m2·hr) and salt rejection 96.03%. The high ratio of water flux in FO mode to that in PRO mode indicates that the fabricated membrane has a lower degree of internal concentration polarization than comparable membranes.
Guoliang LiJun WangDeyin HouYu BaiHuijuan Liu
关键词:醋酸纤维素膜聚对苯二甲酸乙二醇酯聚酯网
Effect of non-solvent additives on the morphology,pore structure, and direct contact membrane distillation performance of PVDF-CTFE hydrophobic membranes被引量:4
2016年
Four common types of additives for polymer membrane preparation including organic macromolecule and micromolecule additives, inorganic salts and acids, and the strong non-solvent H2 O were used to prepare poly(vinylidene fluoride-co-chlorotrifluoroethylene)(PVDF-CTFE) hydrophobic flat-sheet membranes. Membrane properties including morphology, porosity, hydrophobicity, pore size and pore distribution were investigated, and the permeability was evaluated via direct contact membrane distillation(DCMD) of 3.5 g/L Na Cl solution in a DCMD configuration. Both inorganic and organic micromolecule additives were found to slightly influence membrane hydrophobicity. Polyethylene glycol(PEG),organic acids, Li Cl, Mg Cl2, and Li Cl/H2 O mixtures were proved to be effective additives to PVDF-CTFE membranes due to their pore-controlling effects and the capacity to improve the properties and performance of the resultant membranes. The occurrence of a pre-gelation process showed that when organic and inorganic micromolecules were added to PVDF-CTFE solution, the resultant membranes presented a high interconnectivity structure. The membrane prepared with dibutyl phthalate(DBP) showed a nonporous surface and symmetrical cross-section. When H2 O and Li Cl/H2 O mixtures were also used as additives, they were beneficial for solid–liquid demixing, especially when Li Cl/H2 O mixed additives were used. The membrane prepared with 5% Li Cl + 2% H2 O achieved a flux of24.53 kg/(m2·hr) with 99.98% salt rejection. This study is expected to offer a reference not only for PVDF-CTFE membrane preparation but also for other polymer membranes.
Libing ZhengZhenjun WuYong ZhangYuansong WeiJun Wang
关键词:非溶剂添加剂直接接触式膜蒸馏疏水膜邻苯二甲酸二丁酯
正渗透-膜蒸馏集成工艺处理海岸带城市生活污水应用研究被引量:3
2017年
为考察正渗透-膜蒸馏(FO-MD)集成工艺用于海岸带城市污水处理的可行性并提高工艺性能,系统研究了FO-MD集成工艺运行参数及影响规律,利用自制的FO-MD集成装置考察工艺通量性能及污染物去除效果。结果表明,MD过程能够实现FO汲取剂的高效回收,较高的汲取液温度有利于提高FO-MD集成工艺产水量,集成工艺对生活污水中大部分污染物具有较好的截留性能,去除率均达90%以上。该集成工艺将FO技术低污染倾向和MD技术高截留率的优势叠加,同时有效地缓解了FO过程驱动力下降及MD膜润湿潜在风险。
李洁李红岩王军
关键词:膜蒸馏
共1页<1>
聚类工具0