CLC number: X703.3
On-line Access: 2024-08-27
Received: 2023-10-17
Revision Accepted: 2024-05-08
Crosschecked: 2009-02-26
Cited: 3
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Wei-hai PANG, Nai-yun GAO, Yang DENG, Yu-lin TANG. Novel photocatalytic reactor for degradation of DDT in water and its optimization model[J]. Journal of Zhejiang University Science A, 2009, 10(5): 732-738.
@article{title="Novel photocatalytic reactor for degradation of DDT in water and its optimization model",
author="Wei-hai PANG, Nai-yun GAO, Yang DENG, Yu-lin TANG",
journal="Journal of Zhejiang University Science A",
volume="10",
number="5",
pages="732-738",
year="2009",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.A0820501"
}
%0 Journal Article
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%A Nai-yun GAO
%A Yang DENG
%A Yu-lin TANG
%J Journal of Zhejiang University SCIENCE A
%V 10
%N 5
%P 732-738
%@ 1673-565X
%D 2009
%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.A0820501
TY - JOUR
T1 - Novel photocatalytic reactor for degradation of DDT in water and its optimization model
A1 - Wei-hai PANG
A1 - Nai-yun GAO
A1 - Yang DENG
A1 - Yu-lin TANG
J0 - Journal of Zhejiang University Science A
VL - 10
IS - 5
SP - 732
EP - 738
%@ 1673-565X
Y1 - 2009
PB - Zhejiang University Press & Springer
ER -
DOI - 10.1631/jzus.A0820501
Abstract: A novel photocatalytic reactor was developed to remove (1,1-bis(4-chlorophenyl)-2,2,2-trichloroethane) (DDT) from water. In the reactor, a cenosphere was used to support TiO2 film made by means of sol-gel. Because the cenospheres were coated with TiO2, their specific gravity was slightly increased from the original 0.6~0.8 to 0.8~0.9, so that they were able to be suspended in water. With the mixed operation of a bubbler, the water in the reactor was in a well-fluidized state. The bottom of the reactor is a sand filter bed, which can be used to prevent the photocatalyst from being lost. A mathematical model of the reactor has been developed in the two primary influential factors: ultraviolet (UV) light intensity and photocatalyst concentration. With such a model, the reactor can be designed more reasonably.
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Open peer comments: Debate/Discuss/Question/Opinion
<1>
Anonymous@No address<No mail>
2011-06-26 22:56:49
1. Introduction
Photocatalytic reactors can be employed to eliminate pollutants
from water and air streams. Different photocatalytic reactor configurations
have been proposed for such applications. One of the most
promising alternatives is the fluidized bed photocatalytic reactor
(FBPR) (Dibble and Raupp 1992; Haarstrick et al. 1996; Chiovetta
et al. 2001; Kumazawa et al. 2003; Lee et al. 2004 2006; Lim and
Kim 2004 2005; Pozzo et al. 1999 2000 2005; Nelson et al. 2007).
Among the advantages offered by FBPRs are the efficient contact between
the catalyst and the pollutants the low mass transfer resistances
the low pressure drop and the high TiO2 surface exposure
to UV-radiation. Besides FBPRs with an annular-type configuration
could enable a more efficient use of the radiation emitted by UV
lamps.
For design and optimization purposes modeling of the radiation
distribution inside photocatalytic reactors is essential because