INCREASING CONVERSION IN MEMBRANE FILTRATION SYSTEMS USING A DESUPERSATURATION UNIT TO PREVENT SCALING

Citation
I. Bremere et al., INCREASING CONVERSION IN MEMBRANE FILTRATION SYSTEMS USING A DESUPERSATURATION UNIT TO PREVENT SCALING, Desalination, 119(1-3), 1998, pp. 199-204
Citations number
10
Categorie Soggetti
Water Resources","Engineering, Chemical
Journal title
ISSN journal
00119164
Volume
119
Issue
1-3
Year of publication
1998
Pages
199 - 204
Database
ISI
SICI code
0011-9164(1998)119:1-3<199:ICIMFS>2.0.ZU;2-V
Abstract
A desupersaturation unit (DU), placed between the stages of either RO or NF systems is aimed at reducing the degree of supersaturation in th e concentrate stream thus preventing membrane scaling in the last stag e of a membrane filtration system while allowing conversion to be maxi mized up to design limits (>90%). Barium sulfate desupersaturation in an up-flow fixed bed reactor was demonstrated for ca. 200 h (Concentra te A). However, barium removal in the DU was shown to be source depend ent and early break-through of the DU occurred with Concentrate B afte r ca. 30 h. Calculations showed that barium sulfate deposition in the DU was affected by natural organic matter (NOM). Blocking of seed crys tal surface by rapid adsorption of certain NOM fractions hindered crys tal growth and was believed to be the main reason for break-through in the DU. Recycling of these naturally occurring organic molecules as ' 'natural antiscalants'' to maximize the conversion of RO (NF) systems may be possible if they can be isolated and characterized.