加布瑞拉·王尔德美腿:请各位翻译高手帮忙

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Fig.1 Photochemical batch reactor employed in all irradiation
experiments
The amount of H2O2 added is the stoichiometric
amount of H2O2 required for the total oxidation
of phenol as calculated according to Eq.(5).
C6H6O + 14H2O2 --6CO2 + 17H2O (5)
Following standard experimentation practice,
one multiple of Qth means 1.32 ml H2O2 solution of
30% (W/W) concentration.
Analytical methods
Phenol concentration was measured by amino-
pyrine colorimetric method (Xi et al., 1989). The
degradation rate, η, of phenol was defined as:
η = 1 - C/Co (6)
where, C and Co were phenol concentration at time t
and time zero, respectively. PHS-25 type pH meter
was used to measure the pH value (Xi et al., 1989).
The metal ion concentrations were determined by
spectrophotometric method (Xi et al., 1989). Analy-
sis of the CODcr was carried out using a titrimetric
method (Xi et al., 1989).
RESULTS AND DISCUSSION
Ion-exchange isotherms of Fe2+, Cu2+ and Mn2+
with NaY zeoliteThe ion-exchange isotherms of Fe2+, Cu2+ and
Mn2+ with NaY zeolite were measured and the results
are given in Fig.2 and Table 1 showing that the
ion-exchangeability of three kinds of metal ions on
the NaY zeolite was in the order: Cu2+ > Fe2+ > Mn2+.
The isotherms were correlated with Langmuir’s
equation
q = qmaxC/ (b + C) (7)
where, q and qmax represent the amount and maximum
amount of ion exchange on the NaY zeolite,
respectively, and b is a constant. The simulated qmax
and b values are listed in Table 1.
Preparation and comparison of multi-component
metal-ion catalysts
Fig.2 The isotherms of Fe2+, Cu2+, Mn2+
Table 1 Comparative study on the isotherm of Fe2+, Cu2+,
Mn2+
1. Fe-Mn-Y catalyst
Fe2+ and Mn2+ concentration ratio was changed,
while keeping the concentration of total metal ions
at 900 mg/L. The obtained catalysts were evaluated
in the heterogeneous UV/Fenton process. The experimental
procedure was as follows: 0.2 g catalyst
and 1/4 Qth of H2O2 were added to 500 ml solution
with 250 mg/L phenol to start the reaction with results
as shown in Fig.3. It was obvious that the
CODcr removal capabilities with two-component
metal-ion catalysts were higher than that with single
metal-ion catalysts. The optimal Fe2+ to Mn2+ ratio
of 2:1 was obtained for CODcr removal. After 40
min reaction, the CODcr removal rate reached 76.7%,
which was 30.5% and 28.6% higher than that catalyzed
by single Fe2+ and Mn2+ catalysts, respectively.
It indicated that synergistic effect should exist between
Fe2+ and Mn2+ in heterogeneous UV/Fenton
reaction. The synergistic effect among these transition
metal ions may be due to their differing redox
potential, which may enhance the deoxidizing of
high valence ion to low valence ion and result in
production of peroxyl radicals.
Fig.3 CODcr removal rate vs time

图1 光化学的一届反应者在所有的发光中雇用
实验
被增加的大量的 H2O2 是 stoichiometric
H2O2 的数量为总计的氧化需要
依照计算的酚依照情绪商数。(5)。
C6H6 O+14H2O2--6CO2+17H2O(5)
下列的标准实验练习,
Qth 的一倍数意谓 1.32 毫升 H 2O2 解决
30%(W/W) 集中。
分析的方法
酚集中被测量被含氨基的-
pyrine 色度法方法.(Xi 及其研究同仁,1989) 那
降格率,η, 酚被定义当做:
η =1- C/Co(6)
哪里, C 和 Co 在时间 t 是酚集中
而且时间零, 分别地。 个人随身电话系统 -25 类型酸碱质公尺
用来测量酸碱值。 (Xi 及其研究同仁,1989)
金属制的离子集中被决定被
spectrophotometric 方法.(Xi 及其研究同仁,1989) 言论集-
CODcr 的 sis 被使用 titrimetric 实行
方法.(Xi 及其研究同仁,1989)
结果及讨论
Fe2 的离子交换等温线+, Cu2+ 和 Mn2+
藉由 Fe2 的拒绝 zeoliteThe 离子交换等温线+, Cu2+ 和
Mn2+ 与拒绝沸石被测量和结果
被屈服图2 和表 1 成绩哪一那
离子-金属制离子的三个类型的可交换性在
拒绝沸石在次序中: Cu2+>Fe2+> Mn2+.
等温线对朗缪尔感到有相互关系
相等
q=qmaxC/(b+ C)(7)
哪里, q 和 qmax 表现数量和最大值
在拒绝沸石上的离子交换的数量,
分别地, 和 b 是一个常数。 被模拟的 qmax
而且 b 价值在表 1 被列出.
准备和多成份的比较
金属-离子的催化剂