TY - JOUR
T1 - Pervaporation of ammonia solution with c-alumina supported organosilica membranes
AU - Yang, Xing
AU - Ding, Lining
AU - Wolf, Martin
AU - Velterop, Frans
AU - Bouwmeester, Henny J.M.
AU - Smart, Simon
AU - Diniz da Costa, João C.
AU - Liubinas, Audra
AU - Li, Jun-De
AU - Zhang, Jianhua
AU - Duke, Mikel
PY - 2016
Y1 - 2016
N2 - In this work, pervaporation of ammonia-solution using c-alumina supported organosilica membrane (HybSi , Pervatech) was explored to understand ammonia removal performance and material stability in this unique high pH environment. During the testing of synthetic ammonia solution of 50 mg/L at 45 C (pH 10), the hybrid silica membrane showed a preference towards ammonia transport over water, with an ammonia separation factor up to 12 and flux of 4.3 kg m 2 h 1 stable in a continuous testing period of 7 h. At an ammonia concentration of 1000 mg/L (pH 11), the membrane initially exhibited separation preference towards ammonia at 45 C, then gradually reversed to water selective after increasing to 70 C, where a significant flux decline was observed. The membrane degradation was investigated by FTIR, porosimetry, SEM and XRD. Only slight change in organosilica chemistry and structure was evident, however more significant degradation was observed in the supporting c-alumina layer. The changes in crystalline alumina structure, porous properties and physical structure undermined the functional silica separation layer. Therefore while the organosilica membrane appeared stable in the high pH aqueous ammonia environment, membranes for ammonia pervaporation applications should consider alternative supporting layers to c-alumina.
AB - In this work, pervaporation of ammonia-solution using c-alumina supported organosilica membrane (HybSi , Pervatech) was explored to understand ammonia removal performance and material stability in this unique high pH environment. During the testing of synthetic ammonia solution of 50 mg/L at 45 C (pH 10), the hybrid silica membrane showed a preference towards ammonia transport over water, with an ammonia separation factor up to 12 and flux of 4.3 kg m 2 h 1 stable in a continuous testing period of 7 h. At an ammonia concentration of 1000 mg/L (pH 11), the membrane initially exhibited separation preference towards ammonia at 45 C, then gradually reversed to water selective after increasing to 70 C, where a significant flux decline was observed. The membrane degradation was investigated by FTIR, porosimetry, SEM and XRD. Only slight change in organosilica chemistry and structure was evident, however more significant degradation was observed in the supporting c-alumina layer. The changes in crystalline alumina structure, porous properties and physical structure undermined the functional silica separation layer. Therefore while the organosilica membrane appeared stable in the high pH aqueous ammonia environment, membranes for ammonia pervaporation applications should consider alternative supporting layers to c-alumina.
KW - 2023 OA procedure
U2 - 10.1016/j.seppur.2016.05.017
DO - 10.1016/j.seppur.2016.05.017
M3 - Article
SN - 1383-5866
VL - 168
SP - 141
EP - 151
JO - Separation and purification technology
JF - Separation and purification technology
ER -