Performance evaluation of a continuous flow immobilized rotating tube photocatalytic reactor (IRTPR) immobilized with TiO2 catalyst for azo dye degradation

2008 ◽  
Vol 144 (1) ◽  
pp. 59-66 ◽  
Author(s):  
Rahul A. Damodar ◽  
T. Swaminathan
2014 ◽  
Vol 21 (21) ◽  
pp. 12505-12517 ◽  
Author(s):  
Mohammad Rezaei ◽  
Fariborz rashidi ◽  
Sayed Javid Royaee ◽  
Morteza Jafarikojour

Author(s):  
Suiyi Zhu ◽  
Xia Yang ◽  
Gu-Ning Wang ◽  
Lei-Lei Zhang ◽  
He-Feng Zhu ◽  
...  

A kind of P-25 TiO2 films coated nickel foam was synthesized by a facile dip-coating/calcination route, and used to fabricate a continuous-flow three-phase photocatalytic reactor. The morphology, crystal phase structure, surface composition and specific surface area of P-25 films coated nickel foam were investigated by field emission scanning electron microscope (FE-SEM), X-ray diffractometer (XRD), X-ray photoelectron spectroscopy (XPS) and nitrogen adsorption-desorption measurements, respectively. The results indicated that the coated/ calcined P-25 films had the porous surface structure fabricated by nano-sized titanium dioxide consisted of two crystal phases and incorporated with a NiO interlayer. The increase of P-25 contents enhanced the specific surface area; however, 20 percent of initial P-25 sol would result in visible large cracks because of too high P-25 content and consequently cause the peeling of films. The photocatalytic activities of nickel foam with different coating amounts of P-25 for the degradation of quinoline aqueous solutions were investigated with a continuous-flow three-phase photocatalytic reactor based on the P-25 films coated nickel foam. The results suggested that nickel foam coated with 10 percent of P-25 sol had an optimal photocatalytic activity for the degradation of quinoline aqueous solutions. The continuous-flow three-phase photocatalytic reactor fabricated with P-25 films coated nickel foam with an optimal P-25 coating amount shows high photocatalytic activity and stability for the degradation of quinoline aqueous solutions and industrial wastewater. The treated industrial wastewater meets the international discharge standard.


Author(s):  
Natalija Koprivanac ◽  
Dinko Vujevic

Organic synthetic dyes are widely produced and used today. Significant losses of organic and inorganic content occurs during the manufacturing and application of dyes and its discharge in the effluent presents a threat to the eco-systems due to general toxicity and resistance to destruction by biological treatment methods. Particularly azo dyes are of special environmental concern due to their degradation products such as aromatic amines, which are considered highly carcinogenic. So, dyes have to be removed from coloured wastewater before discharge. However, traditional treatment methods (adsorption, coagulation/flocculation) mainly transfer the contaminants from wastewater to secondary waste. Therefore, advanced oxidation processes seem to be sustainable and clean technology to decolorize and minimize organic dyes content from wastewater. In this paper, degradation of an azo dye C.I. Direct Orange 39 (DO39) using Fenton type processes (Fe2+/H2O2, Fe3+/H2O2and Fe0/H2O2) has been performed. The molar ratio of Fenton’s type reagents has been varied in the range of 1 : 5 up to 1 : 50 at 0.5 and 1.0 mM concentrations of iron salts and iron powder. Experiments have been conducted for two hours in a batch reactor with magnetic stirring, ambient conditions and pH 3. The process efficiency and formation of degradation by-products have been determined on the basis of results obtained by UV/VIS spectrophotometric, total organic carbon (TOC) and high performance liquid chromatography (HPLC) analyses. The optimal Fenton and Fenton ``like" processes parameters have been applied in the photo reactor, too. It has been observed that simultaneous utilization of UV irradiation with Fenton's and Fenton ``like" reagents increases the degradation of DO39 dye. Degradation of the dye in dilute aqueous solution follows pseudo-first order kinetics. The maximal decolourization of 20 mg L-1 DO39 in water of 93.2% and TOC degradation of 76.9% were obtained using Fe3+/H2O2= 1 : 5 molar ratio. The results indicate that the treatment of DO39 dye wastewater with UV/Fe3 +/H2O2 system was found to be the most efficient.


Author(s):  
Chetsada Khositanon ◽  
Siwada Deepracha ◽  
Suttichai Assabumrungrat ◽  
Makoto Ogawa ◽  
Nopphon Weeranoppanant

2013 ◽  
Vol 56 (5) ◽  
pp. 867-874 ◽  
Author(s):  
Marcus Vinicius Freire Andrade ◽  
Karla Mayara Lima da Silva ◽  
João Paulo da Silva Siqueira ◽  
Carlos Ronald Pessoa Wanderley ◽  
Rinaldo dos Santos Araújo ◽  
...  

Chemosphere ◽  
2017 ◽  
Vol 174 ◽  
pp. 76-81 ◽  
Author(s):  
Z. Deng ◽  
X.H. Zhang ◽  
K.C. Chan ◽  
L. Liu ◽  
T. Li

2007 ◽  
Vol 18 (4) ◽  
pp. 14-18 ◽  
Author(s):  
I.N. Itodo ◽  
G.E. Agyo ◽  
P. Yusuf

A biogas stove was designed, constructed and its performance evaluated using a 3 m3 continuous-flow Indian type biogas plant at the Teaching and Research Farm, University of Agriculture, Makurdi, Nigeria. The biogas plant was operated with cattle dung as feedstock in the ratio of 1 part of dung to 2 parts of water at a retention time of 30 days and daily loading rate of 100 kg of slurry. The perform-ance of the stove was evaluated by boiling water, cooking rice and beans and the time taken to per-form specific tasks determined from a stop watch. The amount of biogas used in boiling and cooking was determined from the operating pressure of the plant measured from a manometer that was placed between the stove and the plant. The results obtained showed that 0.14 l of water was boiled in 1 minute while 5.13 g of rice and 2.55 g of beans cooked in a minute. The biogas consumption for boiling water, cooking rice and beans was 0.69m3/min, 2.81m3/min and 4.87m3/min respec-tively. The efficiency of the stove in boiling water, cooking rice and beans was 20%, 56% and 53%respectively.


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