Published May 2017 | Version v1
Journal article

Removal of strontium ions from simulated radioactive wastewater by vacuum membrane distillation

  • 1. Collaborative Innovation Center for Advanced Nuclear Energy Technology, INET, Tsinghua University, Beijing 100084 (China)
  • 2. Beijing Key Laboratory of Radioactive Waste Treatment, Tsinghua University, Beijing 100084 (China)

Description

Highlights: • Vacuum membrane distillation was used to separate Sr2+ from wastewater. • Effect of operation factors on membrane flux was examined. • Pressure buildup effect would decrease membrane flux. • Dusty gas model could estimate membrane flux well. - Abstract: The removal of Sr2+ ions from simulated radioactive wastewater by vacuum membrane distillation (VMD) with hollow fiber membrane module was investigated. The removal efficiency of Sr2+ could maintain over 99.60%, and the membrane flux could maintain at 6.71 L·m−2·h−1 when Sr2+ in the feed solution was about 10 mg/L. The effect of operating parameters on the membrane flux was examined, including feed temperature (30–70 °C), permeate side vacuum (0.10–0.98 atm) and feed flow velocity (10.5–41.8 L/h). Pressure buildup effect was observed during the process, which could interfere with the membrane flux. Pressure buildup effect was more serious when permeate side vacuum degree was over 0.9 atm. Considering energy consumption efficiency, the permeate side vacuum degree should be maintained at the turning point (0.9 atm) of the membrane flux. Dusty gas model could simulate the mass transfer of VMD process well with ARE (average relative error) of 5.31%. VMD is potential for the removal of Sr2+ ions from aqueous solution.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.anucene.2017.02.003

Additional details

Identifiers

DOI
10.1016/j.anucene.2017.02.003;
PII
S0306-4549(16)31083-0;

Publishing Information

Journal Title
Annals of Nuclear Energy (Oxford)
Journal Volume
103
Journal Page Range
p. 363-368
ISSN
0306-4549
CODEN
ANENDJ

Optional Information

Copyright
Copyright (c) 2017 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.