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Concentrating aqueous hydrochloric acid by multiple-effect membrane distillation 被引量:7

Concentrating aqueous hydrochloric acid by multiple-effect membrane distillation
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摘要 Multiple-effect membrane distillation (MEMD) using a hollow fiber-based air-gap membrane distillation module was experimentally examined for concentrating dilute aqueous hydrochloric acid. The effects of the hot and cold feed-in temperatures, and the feed-in volumetric flow rates on the performance of the MEMD process were studied. The performance was evaluated using the performance ratio (PR), the average selectivity of water over HCl (βavg) and the permeation flux (N). Two types of porous fibers made from polypropylene were used to fabricate the MEMD modules. The experimental data indicated that hollow fibers with high porosity were preferred for the MEMD process. The PR, βavg and N all decreased as the feed concentration increased. When the feed concentration was below 12 wt-%, the PR was 6.0 - 9.6 and βavg was 10 190. When the concentration of HCl reached 18 wt-%, the PR and βavg were about 4.4 and 2.3, respectively. However, βavg sharply decreased to around 1.0 when the feed was further concentrated. During an operational stability test that lasted for 30 days, the performance of the MEMD modules remained good. Multiple-effect membrane distillation (MEMD) using a hollow fiber-based air-gap membrane distillation module was experimentally examined for concentrating dilute aqueous hydrochloric acid. The effects of the hot and cold feed-in temperatures, and the feed-in volumetric flow rates on the performance of the MEMD process were studied. The performance was evaluated using the performance ratio (PR), the average selectivity of water over HCl (βavg) and the permeation flux (N). Two types of porous fibers made from polypropylene were used to fabricate the MEMD modules. The experimental data indicated that hollow fibers with high porosity were preferred for the MEMD process. The PR, βavg and N all decreased as the feed concentration increased. When the feed concentration was below 12 wt-%, the PR was 6.0 - 9.6 and βavg was 10 190. When the concentration of HCl reached 18 wt-%, the PR and βavg were about 4.4 and 2.3, respectively. However, βavg sharply decreased to around 1.0 when the feed was further concentrated. During an operational stability test that lasted for 30 days, the performance of the MEMD modules remained good.
出处 《Frontiers of Chemical Science and Engineering》 CAS CSCD 2012年第3期311-321,共11页 化学科学与工程前沿(英文版)
关键词 multiple-effect membrane distillation performance ratio hydrochloric acid RECOVERY STABILITY multiple-effect membrane distillation, performance ratio, hydrochloric acid, recovery, stability
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  • 1唐建军,周康根,赵方辉,李荣光,张启修.Hydrochloric Acid Recovery from Rare Earth Chloride Solutions by Vacuum Membrane Distillation (1) Study on the Possibility[J].Journal of Rare Earths,2003,21(S1):78-82. 被引量:3
  • 2陈建秋,王铎,汪东.钢铁氧化层酸洗液配方的研制[J].表面技术,2005,34(2):69-70. 被引量:9
  • 3郑隆鳌,刘文夫.钢铁酸洗废液的处理技术及其评价[J].钢铁研究,1997,25(1):58-62. 被引量:25
  • 4Galvez J L, Dufour J, Negro C, et aL Selective separation of iron and chromium from stainless steel spent pickling[J]. Revista de Metalurgia (Madrid), 2005, supplement: 475-478. 被引量:1
  • 5Ozaki H, Sharma K, Saktaywin W. Performance of an ultra low pressure reverse osmosis membrane (ULPROM) for separating heavy metal: effect of interference parameters [J]. Desalination, 2002, 144(1-3) :287-294. 被引量:1
  • 6Anon, Pickling acid- recovery proeess by diffusion dialysis[J]. Transactions of the Iron and Steel Institute of Japan,1987,27(5): 386. 被引量:1
  • 7Negro C, Blanco M A,Lopez-matcos F, et al. Free acids and chemicals recovery from stainless steel pickling baths[J]. Separation Science and Technology, 2001, 6(7):1543-1556. 被引量:1
  • 8Kuppinger F F. Method for the production of hydrochloric acids with concentration above the concentration of the water/HCl azeotrope[P]. DE 19850398, 2000-05-04. 被引量:1
  • 9Dorefeev V Y, Korchagina M V, Naumenko A A. Porous ceramic membranes for regeneration of waste sulfate solutions[J]. Glass and Ceramics ,2002,59(3 -4) : 103-105. 被引量:1
  • 10Cadotte J E, Forester R, Kim M, et al. Nanofiltration membranes broaden the use of membrane separation technology[J]. Desalination, 1988,70(1-3) :77 -88. 被引量:1

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