Cargando…
Economic Design of Solar-Driven Membrane Distillation Systems for Desalination
Solar-driven membrane distillation (SDMD) for desalination is a feasible method to solve water and energy resource issues. The design and operation of SDMD is different from continuous and steady state processes, such as common chemical plants, due to the intermittent and unpredictive characteristic...
Autores principales: | , , , |
---|---|
Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2020
|
Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7824013/ https://www.ncbi.nlm.nih.gov/pubmed/33374287 http://dx.doi.org/10.3390/membranes11010015 |
_version_ | 1783639973750112256 |
---|---|
author | Chen, Yih-Hang Hung, Hwo-Gan Ho, Chii-Dong Chang, Hsuan |
author_facet | Chen, Yih-Hang Hung, Hwo-Gan Ho, Chii-Dong Chang, Hsuan |
author_sort | Chen, Yih-Hang |
collection | PubMed |
description | Solar-driven membrane distillation (SDMD) for desalination is a feasible method to solve water and energy resource issues. The design and operation of SDMD is different from continuous and steady state processes, such as common chemical plants, due to the intermittent and unpredictive characteristics of solar radiation. Employing the steady state and dynamic simulation models developed on the platform of Aspen Custom Modeler(®), this paper presents a two-stage design approach for the SDMD systems using different types of membrane distillation configurations, including AGMD (air gap MD), DCMD (direct contract MD) and VMD (vacuum MD). The first design stage uses the steady state simulation model and determines equipment sizes for different constant-value solar radiation intensities with the objective of minimizing total annual cost. The second design stage is implemented on the SDMD systems with process control to automatically adjust the operating flow rates using the dynamic simulation model. Operated with the yearly solar radiation intensity of Taiwan, the unit production costs (UPCs) of the optimal SDMD systems using AGMD, DCMD, and VMD are $2.71, 5.38, and 10.41 per m(3) of water produced, respectively. When the membrane unit cost is decreased from $90/m(2) to $36/m(2), the UPC of the optimal solar-driven AGMD system can be reduced from $2.71/m(3) to $2.04/m(3). |
format | Online Article Text |
id | pubmed-7824013 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2020 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
spelling | pubmed-78240132021-01-24 Economic Design of Solar-Driven Membrane Distillation Systems for Desalination Chen, Yih-Hang Hung, Hwo-Gan Ho, Chii-Dong Chang, Hsuan Membranes (Basel) Article Solar-driven membrane distillation (SDMD) for desalination is a feasible method to solve water and energy resource issues. The design and operation of SDMD is different from continuous and steady state processes, such as common chemical plants, due to the intermittent and unpredictive characteristics of solar radiation. Employing the steady state and dynamic simulation models developed on the platform of Aspen Custom Modeler(®), this paper presents a two-stage design approach for the SDMD systems using different types of membrane distillation configurations, including AGMD (air gap MD), DCMD (direct contract MD) and VMD (vacuum MD). The first design stage uses the steady state simulation model and determines equipment sizes for different constant-value solar radiation intensities with the objective of minimizing total annual cost. The second design stage is implemented on the SDMD systems with process control to automatically adjust the operating flow rates using the dynamic simulation model. Operated with the yearly solar radiation intensity of Taiwan, the unit production costs (UPCs) of the optimal SDMD systems using AGMD, DCMD, and VMD are $2.71, 5.38, and 10.41 per m(3) of water produced, respectively. When the membrane unit cost is decreased from $90/m(2) to $36/m(2), the UPC of the optimal solar-driven AGMD system can be reduced from $2.71/m(3) to $2.04/m(3). MDPI 2020-12-24 /pmc/articles/PMC7824013/ /pubmed/33374287 http://dx.doi.org/10.3390/membranes11010015 Text en © 2020 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 (CC BY) license (http://creativecommons.org/licenses/by/4.0/). |
spellingShingle | Article Chen, Yih-Hang Hung, Hwo-Gan Ho, Chii-Dong Chang, Hsuan Economic Design of Solar-Driven Membrane Distillation Systems for Desalination |
title | Economic Design of Solar-Driven Membrane Distillation Systems for Desalination |
title_full | Economic Design of Solar-Driven Membrane Distillation Systems for Desalination |
title_fullStr | Economic Design of Solar-Driven Membrane Distillation Systems for Desalination |
title_full_unstemmed | Economic Design of Solar-Driven Membrane Distillation Systems for Desalination |
title_short | Economic Design of Solar-Driven Membrane Distillation Systems for Desalination |
title_sort | economic design of solar-driven membrane distillation systems for desalination |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7824013/ https://www.ncbi.nlm.nih.gov/pubmed/33374287 http://dx.doi.org/10.3390/membranes11010015 |
work_keys_str_mv | AT chenyihhang economicdesignofsolardrivenmembranedistillationsystemsfordesalination AT hunghwogan economicdesignofsolardrivenmembranedistillationsystemsfordesalination AT hochiidong economicdesignofsolardrivenmembranedistillationsystemsfordesalination AT changhsuan economicdesignofsolardrivenmembranedistillationsystemsfordesalination |