纳滤膜分离浓缩煤化工高盐废水
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X703.1

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中国博士后基金(2019M662816);国家自然科学基金(42007314)


Separation of coal-chemical brine using nanofiltration membranes
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    摘要:

    利用NF-HF和NF-HS纳滤膜对煤化工废水二级反渗透浓水进行处理,重点考察其对Cl-与SO42-的分离效果、结垢离子的截留率以及膜抗污染性能,并采用STRO (卷式高压反渗透膜)对纳滤产水进行浓缩处理。实验结果表明,与NF-HS相比,NF-HF具有更优的Cl-/SO42-分离效果及钙、镁、硅离子截留效果和抗污染性能;NF-HF对Cl-截留率为3.38%~6.03%,对SO42-的截留率为91.18%~97.16%;对钙、镁、硅离子的最大截留率分别为90%、80%和40%;连续运行336 h,NF-HF的运行压力从初始的3.2 MPa升高至4.5 MPa,膜通量降低11%;经碱洗后恢复初始膜通量;STRO浓缩处理NF-HF透过液时表现出良好的浓缩效果和脱除COD效果,但其耐污染性能较差。NF-HF+DTRO (碟式高压反渗透)组合工艺使煤化工废水膜浓缩液进一步分离浓缩具备良好的可行性。

    Abstract:

    NF-HF and NF-HS nanofiltration membranes were employed to separate SO42- from Cl-in secondary reverse osmosis concentrate discharged from coal-chemical wastewater treatment plant. The separation of SO42- from Cl-, rejection of scaling ions and anti-fouling performance of the two types membrane were investigated. Spiral Tube Reverse Osmosis (STRO) was used to concentrate permeate of NF-HF. The results showed that NF-HF membrane had better separation Cl- from SO42- and rejection of scaling ions than NF-HS membrane, whose rejection were 3.38%-16.03% for Cl-, 91.18%-97.16% for SO42-, 90% for Ca2+, 80% for Mg2+ and 40% for SiO2, respectively. Moreover, NF-HF showed excellent antifouling property. The operating pressure rose slowly from 3.2 MPa to 4.5 MPa after continuously running 336 h and the membrane flux reduced by 11%, which was recovered completely after alkaline washing. STRO could effectively concentrate the NF-HF permeate and reject organic matter, but the anti-fouling performance was poor. Therefore, separating and concentrating coal chemical wastewater with NF-DTRO (Disc Tube Reverse Osmosis) combination process is practicable.

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陈发源,田小军,范飞,蒋林煜,王舒东,王樟新,何頔.纳滤膜分离浓缩煤化工高盐废水[J].土木与环境工程学报(中英文),2022,44(3):126-132. CHEN Fayuan, TIAN Xiaojun, FAN Fei, JIANG Linyu, WANG Shudong, WANG Zhangxin, HE Di. Separation of coal-chemical brine using nanofiltration membranes[J]. JOURNAL OF CIVIL AND ENVIRONMENTAL ENGINEERING,2022,44(3):126-132.10.11835/j. issn.2096-6717.2021.123

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  • 收稿日期:2021-01-17
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  • 在线发布日期: 2022-02-16
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