Phenol Wastewater Treatment by High Voltage Pulse Discharge Combined with Nanometer Catalyst
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Phenol Wastewater Treatment by High Voltage Pulse Discharge Combined with Nanometer Catalyst
Vol. 43, Issue 8, Pages: 2645-2652(2017)
作者机构:
江西理工大学资源与环境工程学院
作者简介:
基金信息:
DOI:
CLC:
Published Online:31 August 2017,
Published:2017
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DONG Bingyan, DENG Wei, SUN Yu, et al. Phenol Wastewater Treatment by High Voltage Pulse Discharge Combined with Nanometer Catalyst[J]. 2017, 43(8): 2645-2652.
DOI:
DONG Bingyan, DENG Wei, SUN Yu, et al. Phenol Wastewater Treatment by High Voltage Pulse Discharge Combined with Nanometer Catalyst[J]. 2017, 43(8): 2645-2652.DOI:
Phenol Wastewater Treatment by High Voltage Pulse Discharge Combined with Nanometer Catalyst
The discharge of industrial waste water is increasing year by year. We adopted high-voltage pulse discharge combine with two types of nanometer catalyst TiO
2
and Fe-TiO
2
to degrade phenol to treat industrial waste water
investigated the degradation of the phenol affected by the catalyst calcination temperature and the additive amount
and analyzed the phenol intermediate products
the rate of mineralization
and total organic carbon(TOC). The results show that there is a certain influence on the phenol degradatio
n rate of the calcination temperature and additive amount
with the increase of temperature and adding dosage
the Phenol degradation rate would increase and then decrease; compared with single-high voltage pulse discharge
coordination catalyst discharge can effectively improve the degradation rate of phenol
particularly treated by high-voltage pulse discharge combined with Fe-TiO
2
degraded phenol best; when 0.05 g Fe-TiO
2
catalyst is added
the calcination temperature is 450 ℃
and discharged 140 min
degradation rate of solution is as high as 98.75%; the concentration of intermediate will increase then decrease as the time changes
compared with single pulse discharge
resorcinol no longer appears continuously when treated by high-voltage pulse discharge combined with TiO
2
; the peak concentration of the other three materials will increase and then decrease faster
compared with high-voltage pulse discharge combined with TiO
2
resorcinol decompose completely and the peak concentration of hydroquinone and benzoquinone decrease when treated by high voltage pulse discharge combined with Fe-TiO
2
; the mineralization rate is increased by a big margin when a catalyst is added
compared with single high-voltage pulse discharge
when treated by high-voltage pulse discharge combined with Fe-TiO
2
for 140 min
it increases over one time. The results can provide some theoretical supports for the treatment of phenol waste by pulsed discharge synergistic catalyst.