Osmotic concentration of succinic acid by forward osmosis: Influence of feed solution pH and evaluation of seawater as draw solution
Separation Science and Engineering|Updated:2026-01-06
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Osmotic concentration of succinic acid by forward osmosis: Influence of feed solution pH and evaluation of seawater as draw solution
Chinese Journal of Chemical EngineeringVol. 26, Issue 5, Pages: 976-983(2018)
Affiliations:
2 Section of Chemical Engineering Technology, Universiti Kuala Lumpur, Malaysian Institute of Chemical & Bioengineering Technology, Lot 1988, Kawasan Perindustrian Bandar Vendor, Taboh Naning,, Melaka,Alor Gajah,Malaysia,78000
Jeng Yih Law, Abdul Wahab Mohammad. Osmotic concentration of succinic acid by forward osmosis: Influence of feed solution pH and evaluation of seawater as draw solution[J]. Chin.J.Chem.Eng., 2018, 26(5): 976-983.
DOI:
Jeng Yih Law, Abdul Wahab Mohammad. Osmotic concentration of succinic acid by forward osmosis: Influence of feed solution pH and evaluation of seawater as draw solution[J]. Chin.J.Chem.Eng., 2018, 26(5): 976-983.DOI: 10.1016/j.cjche.2017.10.003.
Osmotic concentration of succinic acid by forward osmosis: Influence of feed solution pH and evaluation of seawater as draw solution
we investigated the essential role of feed solution pH so as to gain insights into the transport mechanisms of succinic acid concentration by osmotically-driven forward osmosis (FO) process. FO performances including water flux and bidirectional transport of succinate and chloride anions were systematically examined using cellulose triacetate-based FO membrane. Additionally
real seawater was explored as draw solution. Experimental results revealed that the pH-dependent speciation of succinic acid can affect the FO performances. Ionization of succinic acid at higher solution pH enhanced the osmotic pressure of feed solution
thus leading to lower water flux performance. A strong effect was pointed out on the succinate rejection for which nearly 100% rejections were achieved at pH above its pK
a2
value. The rejection of succinate increased in the following order of chemical form:C
2
H
4
C
2
O
4
H
2
C
2
H
4
C
2
O
4
H
-
C
2
H
4
C
2
O
4
2-
. With real seawater as the draw solution
low to moderate wat
er fluxes (4 L·m
-2
·h
-1
) were observed. The divalent succinate anion was highly retained in the feed side despite differences in the succinic acid feed concentration at pH of approximately 6.90.
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Investigation on removing recalcitrant toxic organic polluters in coking wastewater by forward osmosis
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