Toward scale-up of seawater reverse osmosis (SWRO) – pressure retarded osmosis (PRO) hybrid system: A case study of a 240 m3/day pilot plant

Desalination ◽  
2020 ◽  
Vol 491 ◽  
pp. 114429 ◽  
Author(s):  
Sangho Lee ◽  
Tae-shin Park ◽  
Yong-Gyun Park ◽  
Won-il Lee ◽  
Seung-Hyun Kim
2016 ◽  
Vol 3 (1) ◽  
Author(s):  
Yashwant Sawle ◽  
S.C. Gupta ◽  
Aashish Kumar Bohre
Keyword(s):  

2013 ◽  
Vol 291-294 ◽  
pp. 679-681
Author(s):  
Jin Zeng Chen ◽  
Yan Fei Li ◽  
Guang Hua Li ◽  
Dong Bo Wang

The present work describes the upgrade of one type seawater reverse osmosis (SWRO) unit by Work-Exchanger Energy-Recovery (WEER) system to increace the product flowrate. Before the upgrade, the unit operated at a capacity of 120t/d, and a specific electricity of 7.4kWh/m3. Tests conducted on the unit after the upgrade, when the plant operated at essentially the same pressure conditions, the capacity increase to 150t/d, and a 67.6% reduction in specific electricity to 2.4kWh/m3. This confirmed that the reduction in specific electricity was due to the WEER system. The operating experience with the plant of the first month is presented.


Desalination ◽  
2009 ◽  
Vol 238 (1-3) ◽  
pp. 1-9 ◽  
Author(s):  
Suhan Kim ◽  
Dongin Cho ◽  
Min-Soo Lee ◽  
Byung Soo Oh ◽  
Joon Ha Kim ◽  
...  

2004 ◽  
Vol 4 (1) ◽  
pp. 111-118 ◽  
Author(s):  
R. Lo ◽  
S.-L. Lo

Currently, most semi-conductor plants adopt the conventional chemical coagulation and sedimentation process to treat chemical mechanical polishing (CMP) wastewater. This treatment process consumes a large quantity of coagulants, and its optimum pH operation range is rather narrow. This treatment process produces huge amounts of sludge and is hard to operate due to the unstable characteristics of the abrasive slurry of CMP wastewater. The purpose of this research is to establish a pilot plant which consists of chemical pretreatment, ceramic membrane microfiltration, carbon filtration and reverse osmosis system, which will allow the reclamation of the CMP wastewater. Actual CMP wastewater was sampled and treated in the pilot plant. The results of the pilot tests demonstrated the viability of the treatment scheme and provided data for scale-up calculations. Cost per ton of CMP wastewater reclaimed was calculated using the operating data established, and compared with the conventional chemical coagulation and sedimentation process.


2014 ◽  
Vol 57 (9) ◽  
pp. 3793-3819 ◽  
Author(s):  
Mohamed A. Darwish ◽  
Hassan K. Abdulrahim ◽  
Ashraf S. Hassan ◽  
Adel O. Sharif

2012 ◽  
Vol 167 (6) ◽  
pp. 1716-1727 ◽  
Author(s):  
Sanghyun Jeong ◽  
Lan Hee Kim ◽  
Sung-Jo Kim ◽  
Tien Vinh Nguyen ◽  
Saravanamuthu Vigneswaran ◽  
...  

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