Exploration of polyepoxysuccinic acid as a novel draw solution in the forward osmosis process

被引:34
|
作者
Wang, Chen [1 ]
Gao, Baoyu [1 ]
Zhao, Pin [1 ]
Li, Ruihua [1 ]
Yue, Qinyan [1 ]
Shon, Ho Kyong [2 ]
机构
[1] Shandong Univ, Sch Environm Sci & Engn, Shandong Prov Key Lab Water Pollut Control & Reso, Jinan 250100, Peoples R China
[2] Univ Technol Sydney, Sch Civil & Environm Engn, Post Box 129, Broadway, NSW 2007, Australia
来源
RSC ADVANCES | 2017年 / 7卷 / 49期
关键词
AMMONIA-CARBON DIOXIDE; WASTE-WATER TREATMENT; HIGH NUTRIENT SLUDGE; FILM COMPOSITE TFC; SEAWATER DESALINATION; PROCESS PERFORMANCE; FEED SOLUTION; SODIUM-SALT; MEMBRANE; FLUX;
D O I
10.1039/c7ra04036a
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Polyepoxysuccinic acid (PESA) is a green corrosion scale inhibitor. When PESA is used for wastewater desalination in the forward osmosis (FO) process, the diluted PESA solution could be used for cooling systems. In our investigation, the effects of membrane orientation, temperature and flow rate on FO performance are studied using PESA as a draw solute. The results show that the effect of temperature on water flux is obvious, but the water flux increase is higher from 25 degrees C to 35 degrees C than that from 35 degrees C to 45 degrees C. Compared to the FO mode, the water flux increases faster in the pressure-retarded osmosis mode (PRO mode) at high flow rate due to the reduction of concentrative internal concentration polarization (CICP). Compared with polyaspartic acid (PASP) and NaCl, the water flux of PESA is the lowest under the same conditions. However, PESA has the lowest specific reverse solute flux (Js/Jw) at both membrane orientations. For example in the FO mode this value is 0.46 g L-1, whereas that of NaCl and PASP is 1.12 and 0.74 g L-1, respectively. This means that PESA has lower loss to the feed side than NaCl and PASP in the FO process, which greatly reduces the replenishment cost of the draw solute. The use of PESA as the draw solute in the FO process to treat dyeing water has the advantages of stable water flux (within 20 min), high dye rejection (nearly 1) and reversible membrane fouling (restored to 97%). The nanofiltration (NF) process indicates the good performance of PESA recovery with a high specific water flux (0.94 LMH per bar) and rejection rate (97.8%). Thus, the overall performance of PESA demonstrates that it is a promising draw solute.
引用
收藏
页码:30687 / 30698
页数:12
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