scholarly journals Ceramic membrane ozonator for soluble organics removal from produced water

Author(s):  
U W R Siagian ◽  
A S Dwipramana ◽  
S B Perwira ◽  
Khoiruddin ◽  
I G Wenten
2018 ◽  
Vol 20 ◽  
pp. 16-33 ◽  
Author(s):  
J. Saraiva de Souza ◽  
S. José dos Santos Filho ◽  
Severino Rodrigues de Farias Neto ◽  
A.G. Barbosa de Lima ◽  
H.A. Luma Fernandes Magalhães

Innovative technologies are needed to attend the increasingly strict requirements for produced water treatment, since most of the separation processes are limited to particles larger than 10 μm. Separation processes using ceramic membranes are attracting great interest from academic and industrial community. Nevertheless, few studies, especially numerical, regarding the inorganic membrane’s application for the polluted water separation have been reported. In the present work, therefore, a study of fluid-flow dynamics for a laminar regime in porous tubes (tubular porous ceramic membrane) has been performed. The mass, momentum and mass transport conservation equations were solved with the aid of a structured mesh using ANSYS CFX commercial package. The velocity of local permeation was determined using the resistance in series model. The specific resistance of the polarized layer was obtained by Carman-Kozeny equation. The numerical results were evaluated and compared with the results available in the literature, where by a good agreement with each other was found. The numerical results, obtained by the proposed shell and tubular membrane separation module, indicate that there is facilitation of mass transfer and hence a reduction in the thickness of the polarized boundary layer occurs.


2017 ◽  
Vol 9 (3) ◽  
pp. 168781401668864 ◽  
Author(s):  
Hortência Luma Fernandes Magalhães ◽  
Antonio Gilson Barbosa de Lima ◽  
Severino Rodrigues de Farias Neto ◽  
Helton Gomes Alves ◽  
Josedite Saraiva de Souza

2014 ◽  
Vol 675-677 ◽  
pp. 592-595
Author(s):  
Bi Da Qin ◽  
Xuan Dong Dong ◽  
Jia Yu Wang ◽  
Cai Yu Sun ◽  
Dong Pu Guo ◽  
...  

The voltage is the critical electrochemical parameter in microbial fuel cells (MFCs).There are three major oilfield wastewaters including water flooding produced water, polymer flooding produced water and ASP flooding produced water. These three wastewaters were used as anode substrate of three MFCs in this study. The influence and the influencing factors of the output voltage of the three MFCs and the produced water main refractory organics removal effect were studied. The results show that During this reaction period, MFCs cathode potential stays relative stable, however, anode potential shows a remarkable increasing trend, thus, the anode contributes mostly to the change in output voltage. COD removal effect of Anode substrate and the coulombic efficiency are both influencing factors of the anode potential .The microbial fuel cell for wastewater of surfactant, remove the best effect;For different produced water, oil and polymer removal effect abide by the MFC output voltage and COD value changing law.


2011 ◽  
pp. 181-186
Author(s):  
Marcel V. Melo ◽  
O.A. Pereira Jr ◽  
A. Jacinto Jr ◽  
L.A. dos Santos

2016 ◽  
Vol 165 ◽  
pp. 214-221 ◽  
Author(s):  
T. Zsirai ◽  
A.K. Al-Jaml ◽  
H. Qiblawey ◽  
M. Al-Marri ◽  
A. Ahmed ◽  
...  

Membranes ◽  
2021 ◽  
Vol 11 (10) ◽  
pp. 739
Author(s):  
Mohamad Izrin Mohamad Esham ◽  
Abdul Latif Ahmad ◽  
Mohd Hafiz Dzarfan Othman

The main problem usually faced by commercial ceramic membranes in the treatment of produced water (PW) is low water flux even though ceramic membrane was well-known with their excellent mechanical, thermal, and chemical properties. In the process of minimizing the problem faced by commercial ceramic membranes, titanium dioxide (TiO2) nanocomposites, which synthesized via a sol-gel method, were deposited on the active layer of the hydrolysed bentonite membrane. This paper studied the influence of grafting time of TiO2 nanocomposite on the properties and performance of the coated bentonite membranes. Several characterizations, which are Fourier transform infrared (FTIR), scanning electron microscopy (SEM), energy-dispersive X-ray Spectroscopy (EDX), contact angle, porosity, and average pore size, were applied to both pristine and coated bentonite membranes to compare the properties of the membranes. The deposition of TiO2 nanoparticles on the surface of the coated bentonite membranes was successfully confirmed by the characterization results. The pure water flux performance showed an increment from 262.29 L h−1 m−² bar−1 (pristine bentonite membrane) to 337.05 L h−1 m−² bar−1 (Ti-Ben 30) and 438.33 L h−1 m−² bar−1 (Ti-Ben 60) as the grafting time increase but when the grafting time reached 90 min (Ti-Ben 90), the pure water flux was decreased to 214.22 L h−1 m−² bar−1 which is lower than the pristine membrane. The oil rejection performance also revealed an increase in the oil rejection performance from 95 to 99%. These findings can be a good example to further studies and exploit the advantages of modified ceramic membranes in PW treatment.


MEMBRANE ◽  
2019 ◽  
Vol 44 (4) ◽  
pp. 174-177
Author(s):  
Fuyuhiko Ishikawa ◽  
Satoru Mima ◽  
Arata Nakamura ◽  
Kazuyuki Kawamura

2011 ◽  
Author(s):  
Pierre Pedenaud ◽  
Evans Wayne ◽  
Heng Samuel ◽  
Bigeonneau Didier

2017 ◽  
Author(s):  
I. Dunsmuir ◽  
G. Guthrie ◽  
T. Cottrell ◽  
A. Nijmeijer ◽  
B. Gydesen Reck

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