On a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit
This study investigates a novel cooling-desalination system having a single-double-effect absorption heat pump coupled with a humidification-dehumidification desalination unit. A waste-heat source drives the system in addition to natural gas. Using a waste-heat source lowers the cost of the desalina...
Guardado en:
Autores principales: | , , |
---|---|
Formato: | article |
Lenguaje: | EN |
Publicado: |
Elsevier
2021
|
Materias: | |
Acceso en línea: | https://doaj.org/article/f49887cf57fd4f22bfef7342d66b2c4c |
Etiquetas: |
Agregar Etiqueta
Sin Etiquetas, Sea el primero en etiquetar este registro!
|
id |
oai:doaj.org-article:f49887cf57fd4f22bfef7342d66b2c4c |
---|---|
record_format |
dspace |
spelling |
oai:doaj.org-article:f49887cf57fd4f22bfef7342d66b2c4c2021-11-14T04:35:27ZOn a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit2590-174510.1016/j.ecmx.2021.100128https://doaj.org/article/f49887cf57fd4f22bfef7342d66b2c4c2021-12-01T00:00:00Zhttp://www.sciencedirect.com/science/article/pii/S2590174521000532https://doaj.org/toc/2590-1745This study investigates a novel cooling-desalination system having a single-double-effect absorption heat pump coupled with a humidification-dehumidification desalination unit. A waste-heat source drives the system in addition to natural gas. Using a waste-heat source lowers the cost of the desalinated water and thus gives the proposed system considerable attention in the water market. The results reveal that the system can produce desalinated water of about 110 l per day for 0.0068 $/l with a gained output ratio of 4.15. When the air extraction technique is applied, the daily water production and the gained output ratio increase to 225 l and 8.5, respectively. The corresponding water cost drops to 0.0042 $/l. Besides, the system has a coefficient of performance and cooling capacity of 1.06 and 0.8 kW, respectively. The performance results show that for optimal performance, the absorber and the feed saline water temperatures should be around 45 °C and 30–35 °C, respectively. Further, compared with other absorption/humidification-dehumidification configurations, a promising performance of the proposed system is observed.Muhammad H. ElbassoussiM.A. AhmedSyed M. ZubairElsevierarticleAir extractionCoolingHumidification-dehumidificationThermodynamic balancingSingle-double-effect absorptionWater desalinationEngineering (General). Civil engineering (General)TA1-2040ENEnergy Conversion and Management: X, Vol 12, Iss , Pp 100128- (2021) |
institution |
DOAJ |
collection |
DOAJ |
language |
EN |
topic |
Air extraction Cooling Humidification-dehumidification Thermodynamic balancing Single-double-effect absorption Water desalination Engineering (General). Civil engineering (General) TA1-2040 |
spellingShingle |
Air extraction Cooling Humidification-dehumidification Thermodynamic balancing Single-double-effect absorption Water desalination Engineering (General). Civil engineering (General) TA1-2040 Muhammad H. Elbassoussi M.A. Ahmed Syed M. Zubair On a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit |
description |
This study investigates a novel cooling-desalination system having a single-double-effect absorption heat pump coupled with a humidification-dehumidification desalination unit. A waste-heat source drives the system in addition to natural gas. Using a waste-heat source lowers the cost of the desalinated water and thus gives the proposed system considerable attention in the water market. The results reveal that the system can produce desalinated water of about 110 l per day for 0.0068 $/l with a gained output ratio of 4.15. When the air extraction technique is applied, the daily water production and the gained output ratio increase to 225 l and 8.5, respectively. The corresponding water cost drops to 0.0042 $/l. Besides, the system has a coefficient of performance and cooling capacity of 1.06 and 0.8 kW, respectively. The performance results show that for optimal performance, the absorber and the feed saline water temperatures should be around 45 °C and 30–35 °C, respectively. Further, compared with other absorption/humidification-dehumidification configurations, a promising performance of the proposed system is observed. |
format |
article |
author |
Muhammad H. Elbassoussi M.A. Ahmed Syed M. Zubair |
author_facet |
Muhammad H. Elbassoussi M.A. Ahmed Syed M. Zubair |
author_sort |
Muhammad H. Elbassoussi |
title |
On a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit |
title_short |
On a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit |
title_full |
On a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit |
title_fullStr |
On a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit |
title_full_unstemmed |
On a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit |
title_sort |
on a novel integration of a multistage absorption heat pump with a balanced humidification-dehumidification desalination unit |
publisher |
Elsevier |
publishDate |
2021 |
url |
https://doaj.org/article/f49887cf57fd4f22bfef7342d66b2c4c |
work_keys_str_mv |
AT muhammadhelbassoussi onanovelintegrationofamultistageabsorptionheatpumpwithabalancedhumidificationdehumidificationdesalinationunit AT maahmed onanovelintegrationofamultistageabsorptionheatpumpwithabalancedhumidificationdehumidificationdesalinationunit AT syedmzubair onanovelintegrationofamultistageabsorptionheatpumpwithabalancedhumidificationdehumidificationdesalinationunit |
_version_ |
1718429934603468800 |