Position:Home >> Abstract

The influence of pretreatment ofReverse Osmosisconcentrate on the performance of Air Gap Membrane Distillation process
Authors:
Units: 1.Building installation engineering of China CO., LTD Najing 210046 China;2. School of Chemical Engineering and Technology,Tianjin University,Tianjin 300072,China;3.Tianjin Key Laboratory of Membrane Science and Desalination Technology,Tianjin University
KeyWords:
ClassificationCode:TQ028.8
year,volume(issue):pagination: 2014,34(3):86-91

Abstract:
A novel pretreatment process for Reverse Osmosis concentrate was proposed which consisted of chemical removal of hard ions,coagulation and sedimentation,ions exchanges and ultrafiltration.Experiments were carried out to study the effects of pretreatment process onthe removal of Ca2+,Mg2+and SiO32-and to the performance of the air gap membrane distillation (AGMD).The results showed that the contents of Ca2+, Mg2+and SiO32-were all below 5 ppm.Moreover,the insoluble salts such as CaCO3and Mg(OH)2 were unsaturated in the AGMD process.As a result, CaCO3 and Mg(OH)2would not deposit on the surface of the membrane when the RO concentrate wasprocessed in the AGMD module.After pretreatment ,the main substance in the RO concentrate is NaCl which could be concentrated to crystalline form to obtain NaCl solid.When the concentrate factor reached 7,the novel pretreatment process could increase the permeate flux by 24.02%,the conductivity maintainedrelatively stableand the CODCr of the permeate was below 10mg/l.As results,the permeate of the process could be used as circulating cooling water and washing water in industry. Moreover, after absorbed by activated carbon, the permeate water could be used as boiler water. The pretreated RO concentratewas concentrated continuously for 168 hours via AGMD.During the process, the permeate flux decreased slowly, the conductivity of the permeate was below 5μS/cm and the CODCr of the permeate was below 10 mg/l.

Funds:

AuthorIntro:
徐义明(1962-),男,高级工程师,联系电话:025-85562005

Reference:
[1]秦英杰,王焕,刘立强,等.经反渗透处理后炼油废水浓水的多效膜蒸馏技术[J].化工进展,2011,30(增刊):844-646。
[2]赵春霞,顾平,张光辉.反渗透浓水处理现状与研究进展[J].中国给水排水,2009,25(18):1-5。
[3]M.S. El-Bourawi, Z. Ding, R.Ma,etal.A framework for better understanding membranedistillation separation process[J].J Membr Sei,2006,285:4-29。
[4]MarekGryta.Long term performance distillation process[J].J Membr Sei,2005,265:153-159。
[5]刘东,武春瑞,吕晓龙.反渗透浓水除硬方法及其对减压膜蒸馏过程的影响[J].工业水处理,2010,30(5):23-26。
[6]孙项城,王军,侯德印,等.膜蒸馏法浓缩反渗透浓水的实验研究[J].中国给水排水,2011,27(17):22-25。
[7]李凭力,耿洪鑫,吴浩赟等.一种膜蒸馏器[P].中国,发明专利,201310100389.2.2013-06-26。
[8]曲丹,王军,范彬,等.钙的沉积对中空纤维膜蒸馏过程的影响[J].水处理技术,2007,33(10):14-17。
[9]宋震宇,李保安,高晓飞.减压膜蒸馏过程中的钙镁污染研究[A].膜科学与技术编辑部.第四届膜科学与技术论文集[C].北京:膜科学与技术,2010,390-393。
[10]何涌.结晶化学[M].北京:化学工业出版社,2008,170-172。
 

Service:
Download】【Collect

《膜科学与技术》编辑部 Address: Bluestar building, 19 east beisanhuan road, chaoyang district, Beijing; 100029 Postal code; Telephone:010-80492417/010-80485372; Fax:010-80485372 ; Email:mkxyjs@163.com

京公网安备11011302000819号