Inception of CaSO4 scaling on RO membranes at various water recovery levels

被引:118
作者
Hasson, D [1 ]
Drak, A [1 ]
Semiat, R [1 ]
机构
[1] Technion Israel Inst Technol, Dept Chem Engn, WRI Rabin Desalinat Lab, IL-32000 Haifa, Israel
关键词
scaling limits; CaSO4; scaling; induction time; scale deposition; antiscalants;
D O I
10.1016/S0011-9164(01)00296-X
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper describes laboratory techniques for characterizing the permissible water recovery fraction in RO desalination, which is limited by the need to avoid scale deposition on the membrane. The CaSO4 scaling system was adopted for the development of these techniques, An upper water recovery bound is determined by operating an RO laboratory module such that the feed concentration level is gradually increased through continuous withdrawal of permeate while the concentrate is recycled to the feed vessel. The maximum possible water recovery is indicated by the solution concentration at which the supersaturation level triggers an immediate copious precipitation process. The procedure for evaluating a lower scaling threshold limit, at which precipitation is prevented or at least delayed for a sufficiently long period of time, is based on induction time experiments. These are carried out by operating the RO system in a full recycle mode (both permeate and concentrate recycled to the feed vessel) and measuring the time required for the onset of scaling. Results of preliminary tests show that induction time data are well correlated with the supersaturation level according to a relationship based on nucleation theory. Surface energies for CaSO4 nucleation on RO membranes are found to conform with literature data, thus lending support to the proposed induction time technique.
引用
收藏
页码:73 / 81
页数:9
相关论文
共 20 条
[1]  
*ASTM, D432897 ASTM
[2]   The roles of gas bubbling, wall crystallization and particulate deposition in CaSO4 scale formation [J].
Bramson, D ;
Hasson, D ;
Semiat, R .
DESALINATION, 1995, 100 (1-3) :105-113
[3]   Laboratory technique for predicting the scaling propensity of RO feed waters [J].
Drak, A ;
Glucina, K ;
Busch, M ;
Hasson, D ;
Laîne, JM ;
Semiat, R .
DESALINATION, 2000, 132 (1-3) :233-242
[4]  
HARRIS A, 1981, S PROGR PREV FOUL U, P174
[5]   Suppression of CaCO3 scale deposition by anti-sealants [J].
Hasson, D ;
Semiat, R ;
Bramson, D ;
Busch, M ;
Limoni-Relis, B .
DESALINATION, 1998, 118 (1-3) :285-296
[6]  
Hasson D., 1981, FOULING HEAT TRANSFE, P527
[7]   THE NUCLEATION KINETICS OF CALCIUM-SULFATE DIHYDRATE IN NACL SOLUTIONS UP TO 6-M AND 90-DEGREES-C [J].
HE, SL ;
ODDO, JE ;
TOMSON, MB .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1994, 162 (02) :297-303
[8]   STUDIES ON NUCLEATION PHENOMENA OCCURRING IN AQUEOUS-SOLUTIONS SUPERSATURATED WITH CALCIUM-SULFATE [J].
KELLER, DM ;
MASSEY, RE ;
HILEMAN, OE .
CANADIAN JOURNAL OF CHEMISTRY-REVUE CANADIENNE DE CHIMIE, 1978, 56 (06) :831-838
[9]   Role of temperature in the spontaneous precipitation of calcium sulfate dihydrate [J].
Klepetsanis, PG ;
Dalas, E ;
Koutsoukos, PG .
LANGMUIR, 1999, 15 (04) :1534-1540
[10]   Investigation of the initial period of sulphate scale formation - Part 1. Kinetics and mechanism of calcium sulphate surface nucleation at its crystallization on a heat-exchange surface [J].
Linnikov, OD .
DESALINATION, 1999, 122 (01) :1-14