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A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes
An innovative concept is proposed to recover ammonia from industrial wastewater using a molecular sieve silica membrane in pervaporation (PV), benchmarked against vacuum membrane distillation (VMD). Cobalt and iron doped molecular sieve silica-based ceramic membranes were evaluated based on the ammo...
Autores principales: | , , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2014
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4021959/ https://www.ncbi.nlm.nih.gov/pubmed/24957120 http://dx.doi.org/10.3390/membranes4010040 |
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author | Yang, Xing Fraser, Thomas Myat, Darli Smart, Simon Zhang, Jianhua Diniz da Costa, João C. Liubinas, Audra Duke, Mikel |
author_facet | Yang, Xing Fraser, Thomas Myat, Darli Smart, Simon Zhang, Jianhua Diniz da Costa, João C. Liubinas, Audra Duke, Mikel |
author_sort | Yang, Xing |
collection | PubMed |
description | An innovative concept is proposed to recover ammonia from industrial wastewater using a molecular sieve silica membrane in pervaporation (PV), benchmarked against vacuum membrane distillation (VMD). Cobalt and iron doped molecular sieve silica-based ceramic membranes were evaluated based on the ammonia concentration factor downstream and long-term performance. A modified low-temperature membrane evaluation system was utilized, featuring the ability to capture and measure ammonia in the permeate. It was found that the silica membrane with confirmed molecular sieving features had higher water selectivity over ammonia. This was due to a size selectivity mechanism that favoured water, but blocked ammonia. However, a cobalt doped silica membrane previously treated with high temperature water solutions demonstrated extraordinary preference towards ammonia by achieving up to a 50,000 mg/L ammonia concentration (a reusable concentration level) measured in the permeate when fed with 800 mg/L of ammonia solution. This exceeded the concentration factor expected by the benchmark VMD process by four-fold, suspected to be due to the competitive adsorption of ammonia over water into the silica structure with pores now large enough to accommodate ammonia. However, this membrane showed a gradual decline in selectivity, suspected to be due to the degradation of the silica material/pore structure after several hours of operation. |
format | Online Article Text |
id | pubmed-4021959 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2014 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
spelling | pubmed-40219592014-05-27 A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes Yang, Xing Fraser, Thomas Myat, Darli Smart, Simon Zhang, Jianhua Diniz da Costa, João C. Liubinas, Audra Duke, Mikel Membranes (Basel) Article An innovative concept is proposed to recover ammonia from industrial wastewater using a molecular sieve silica membrane in pervaporation (PV), benchmarked against vacuum membrane distillation (VMD). Cobalt and iron doped molecular sieve silica-based ceramic membranes were evaluated based on the ammonia concentration factor downstream and long-term performance. A modified low-temperature membrane evaluation system was utilized, featuring the ability to capture and measure ammonia in the permeate. It was found that the silica membrane with confirmed molecular sieving features had higher water selectivity over ammonia. This was due to a size selectivity mechanism that favoured water, but blocked ammonia. However, a cobalt doped silica membrane previously treated with high temperature water solutions demonstrated extraordinary preference towards ammonia by achieving up to a 50,000 mg/L ammonia concentration (a reusable concentration level) measured in the permeate when fed with 800 mg/L of ammonia solution. This exceeded the concentration factor expected by the benchmark VMD process by four-fold, suspected to be due to the competitive adsorption of ammonia over water into the silica structure with pores now large enough to accommodate ammonia. However, this membrane showed a gradual decline in selectivity, suspected to be due to the degradation of the silica material/pore structure after several hours of operation. MDPI 2014-02-17 /pmc/articles/PMC4021959/ /pubmed/24957120 http://dx.doi.org/10.3390/membranes4010040 Text en © 2014 by the authors; licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution license (http://creativecommons.org/licenses/by/3.0/). |
spellingShingle | Article Yang, Xing Fraser, Thomas Myat, Darli Smart, Simon Zhang, Jianhua Diniz da Costa, João C. Liubinas, Audra Duke, Mikel A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes |
title | A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes |
title_full | A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes |
title_fullStr | A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes |
title_full_unstemmed | A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes |
title_short | A Pervaporation Study of Ammonia Solutions Using Molecular Sieve Silica Membranes |
title_sort | pervaporation study of ammonia solutions using molecular sieve silica membranes |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4021959/ https://www.ncbi.nlm.nih.gov/pubmed/24957120 http://dx.doi.org/10.3390/membranes4010040 |
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