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S. Horikoshi et al. / Ultrasonics Sonochemistry 18 (2011) 938–942
as shown in Fig. 1d, affects the ultrasonic vibrations and only
microwaves can be delivered to the aqueous medium. To prevent
microwave leakages from occurring through the antenna and the
ultrasonic transducer the metallic cone in the waveguide was mod-
ified and the tight fit was relaxed such that the node of the ultra-
sounds on the antenna was made to touch the cone through the
insert (see Fig. 1e). The position of the node was calculated by
the equation: k/2 = c/2f, where k/2 is the node length; c is the speed
of sound; and f is the frequency. The length of the node was esti-
mated at 129.9 mm for a speed of sound of the titanium alloy of
5068 m sÀ1 [13]. Note that the position of the node becomes an
important criterion for the metallic horn to touch the cone. As
such, the node was fine-tuned to the position of maximum cavita-
tion before the experiments.
simultaneous microwave irradiation (power, 220 W; ignition
power, 500 W) and ultrasonic cavitation (power, 90 W). Evidently,
a decrease in the temperature around the tip of the antenna ap-
pears to control the deterioration of the antenna.
Tsochatzidis et al. [14] measured the size of the ultrasonic cav-
itation bubbles under 20-kHz ultrasonic irradiations by the phase-
Doppler analytical technique and reported that such bubbles were
distributed in the range of ca. 5–10 lm. The ultrasonic cavitation
bubbles will become a positive factor in plasma generation as they
will define the domain where plasma is easily generated. Plasma
extended into the aqueous medium from the antenna tip by about
20 mm on irradiation for 10 s (Fig. 2b), and extended downward to
40 mm on irradiation for 30 s (Fig. 2c). By contrast, the microwave
discharge water plasma did not diffuse to 20 mm under microwave
irradiation alone, requiring simultaneous ultrasonic cavitation.
Accordingly, ultrasonic cavitation not only caused a decrease of
the microwave power needed for plasma generation but also
caused an increase of the diffusion length of the plasma so
generated.
2.2. Evaluation of the device by the degradation of perfluorooctanoic
acid (PFOA)
High-purity perfluorooctanoic acid (PFOA: C7F15COOH) was
purchased from Wako Pure Chemical Industries, Ltd. Aqueous
PFOA solutions (50 mL; 0.010 mM) were introduced into a Pyrex
glass cylindrical reactor (length: 60 mm; internal diameter:
55 mm); the length of the hybrid antenna tip bathing the aqueous
solution was 8 mm. The aqueous PFOA solution was oxygenated by
bubbling oxygen gas for 5 min prior to irradiation/cavitation. The
defluorination of PFOA was assayed by ion chromatography using
a JASCO LC-2000 Plus HPLC chromatograph equipped with a con-
ductivity detector and an I-524 anionic column. The intermediates
were identified in the negative ion mode with a mass spectral
detector of an Agilent Technologies 6100 LC–MS (ESI mode) sys-
tem. The eluent was a solution of acetonitrile/water (1:1 v/v).
The measured UV/vis spectrum of the light plasma in water
using simultaneous microwave irradiation (power, 220 W) and
ultrasonic cavitation (power, 90 W) is displayed in Fig. 3. Measure-
ment of the UV/vis spectral wavelengths was carried out with an
Opto Sirius Co. USB-Iss-UV–VIS spectrophotometer through the fi-
ber probe. The emitted wavelengths of the water plasma were
433 nm (OH), 486 nm (Hb), 456 nm (H ), 777 nm (O) and 845 nm
a
(O), each assigned according to the MIT database of wavelength
tables [15]. On the other hand, no wavelength due to nitrogen
(main peak: 411 nm) was observed, which is consistent with the
notion that the generated plasma is produced entirely by the
degradation of water. The spectrum of the water plasma under
microwave irradiation alone was similar in shape. Thus, no
changes in the spectrum occurred by ultrasonic cavitation.
3. Results and discussion
3.2. Evaluation of the novel device by the degradation of
perfluorooctanoic acid (PFOA)
3.1. Generation of the microwave discharge plasma under ultrasonic
cavitation in water
The degradation of the model pollutant PFOA in aqueous media
was examined to evaluate the liquid plasma method consisting of
the microwave discharge plasma and ultrasonic cavitation (MW
power, 220 W; power for cavitation, ca. 90 W). Fig. 4 displays the
degradation of PFOA by the liquid plasma method as % defluorina-
tion and compares it to the degradation of PFOA in water by ultra-
sonic cavitation alone. Note that the expected theoretical yield of
defluorination of PFOA (0.010 mM) was 0.15 mM. The concentra-
tion of fluoride ion increased with time of irradiation by the plas-
ma, reaching 59% defluorination for 90 s of plasma irradiation. On
the other hand, no defluorination occurred when the PFOA solution
was treated by ultrasonic cavitation alone. The temperature of the
PFOA aqueous solution reached 51 °C from an initial 23 °C after
irradiation for 90 s. However, in the vicinity where plasma was
generated the temperature was far greater, with the tungsten tip
of the antenna reaching temperatures over 1000 °C. Moreover,
the plasma generated in water produced such active species as
The microwave discharge water plasma was generated in
300 mL of water in a beaker under simultaneous microwave irradi-
ation and ultrasonic cavitation. Initially, we confirmed generation
of ultrasonic cavitation at a power level of ca. 90 W without micro-
wave irradiation and found that cavitation was generated most
efficiently near the top of the aqueous medium close to the micro-
wave antenna. Ultrasonic cavitation was not affected when the
metal cone was connected to the waveguide (Fig. 2a). The pink col-
ored light water plasma was continuously produced by microwave
irradiation alone at a power level of ca. 1000 W (power consump-
tion) for the ignition in water under normal atmospheric condi-
tions. However, under simultaneous microwave irradiation and
ultrasonic cavitation at a power level of ca. 90 W, the pink colored
water plasma could be generated at a microwave power level of
500 W (see Fig. 2b), i.e. at 50% power by simultaneous ultrasonic
cavitation. The microwave power was decreased to 700 W when
microwave irradiation alone was used and to 220 W for microwave
irradiation/ultrasonic cavitation while maintaining the plasma.
Thus, the microwave power could be decreased by 69% for contin-
ued plasma generation. Consequently, the decrease in microwave
power can lower the temperature around the tip of the titanium/
tungsten antenna. The generation of the water plasma became
unstable under microwave irradiation for ca. 20 s without ultra-
sonic cavitation. The tungsten tip of the hybrid antenna was worn
out (corroded) by the heat of the plasma at a microwave power le-
vel of 700 W; the photograph of the damaged hybrid antenna after
microwave irradiation for only 20 s is illustrated in Fig. 2d. How-
ever, the damage to the hybrid antenna could be minimized under
the ÅOH, ÅH, HO2 , and ÅO1(D) radicals [4,16]. It is these active radical
Å
species that likely promote the plasma pyrolytic decomposition of
PFOA. Note that water plasma produced by microwave irradiation
alone could not be sustained for a few minutes owing to the dete-
rioration of the antenna tip. Therefore, decomposition of PFOA was
rendered difficult under microwave irradiation alone. The degrada-
tion/defluorination of PFOA required simultaneous microwave
irradiation and ultrasonic cavitation.
Intermediates from the degradation of PFOA were identified by
electrospray mass spectral techniques in the negative (M–) ion
mode. The initial PFOA substrate was seen at m/z = 413. The LC–
MS spectral intermediates were seen at m/z = 363, 313, and 263