식품의 열에 의한 손상을 줄이고 안전성을 높이기 위한 비열살균기술로 유전체장벽방전 플라즈마(DBDP) 이용 가능성을 타진하기 위하여 E. coli에 대한 살균효과를 전류세기와 전극간격을 달리하여 조사하였다. DBDP 살균효과는 초기에는 크게 나타나다가 이후 감소하는 2 구간으로 구성된 1차 반응으로 나타났고, 전류세기에 따라 살균효과가 증가하였다. 전극간격에 따른 살균력은 2.65 mm에서 가장 높았으며, 3.33 mm, 1.85 mm 순으로 감소하였다. DBDP 살균패턴은 Singh-Heldman 모델에 적합하였으며, 시료를 고정하고 DBDP를 처리한 경우 곡선형상계수(n)는 0.545-0.783 범위의 값을, D'-value는 0.565-3.268min의 값을 보였다. 최소 D'-value는 전극간격 2.65mm, 전류 1.25 A에서 나타나 가장 우수한 살균력을 보이는 조건으로 확인되었다. DBDP 처리 시 시료를 이동시키면 고정하여 처리한 경우에 비하여 살균효과는 크게 향상되었으며, 양방향 이동식 처리가 단일방향 이동식 처리에 비하여 양호한 살균력을 보였다.

비열살균기술로서 저온플라즈마 활용 가능성을 탐색하고자 유전체장벽 방전 플라즈마(DBDP)생성장치를 제작하여 최적 플라즈마생성 조건을 도출하고 Staphylococcus aureus를 대상으로 살균성능을 조사하였다. DBDP생성장치는 전력공급장치, 변압기, 전극, 시료처리부 등 네 부분으로 구성하였다. 인가전압은 단상 200 V AC를 사용하고, 변압기를 통하여 10.0-50.0 kV로 변환하고 10.0-50.0 kHz의 주파수의 펄스 구형파를 유전체인 세라믹 블록 내에 장치한 전극에 투입함으로써 상압에서 플라즈마를 생성하였다. 주파수를 올림에 따라 높은 전류가 유입되었고, 이에 비례하여 전력소비량이 증가하였다. 전류세기 1.0-2.0 A, 주파수 32.0-35.3 kHz 범위에서 균일하고 안정적인 플라즈마 발생이 이루어졌으며 시료를 투입하지 않은 상태에서의 최적 전극간격은 1.85 mm 이었다. 전극간격을 높임에 따라 소비 전력이 증가하였으나 시료 처리에 적합한 전극간격은 2.65 mm였다. DBDP 처리에 의한 온도상승은 최대 20oC에 불과하여 열에 의한 생물학적 효과는 무시할 수 있었으며 따라서 비열기술임이 확인되었다. Staphylococcus aureus를 대상으로 DBDP 처리할 경우 초기 5분 동안은 살균치가 직선적인 증가를 보이다가 이후 다소 완만해지는 경향을 보였으며 1.25 A에서 10분간 처리 시 살균치는 5.0을 상회하였다.

Abstract Dielectric barrier discharge (DBD) in air, which has been established for the production of large quantities of ozone, is more recently being applied to a wider range of aftertreatment processes for HAPs (hazardous air pollutants). Although DBD has high electron density and energy, its potential use as precharging nano and submicron sized particles, is not known. In this work, we measured V‐I (voltage‐current) characteristics of DBD and estimated the collection efficiency of particles with bimodal distribution by DBD type 2‐stage ESP (electrostatic precipitator). To examine the particle collection with various applied voltage waveforms of DBD, nano size particles of NaCl (20∼100 nm) and DOS (50∼800 nm) were generated by an electrical tube furnace and an atomizer, respectively. Particle collection efficiencies of all the cases increased with increase of DBD electric power that the results corresponded to product of V by I whose magnitudes were the largest in triangular voltage waveform.

TMGa와 유전체 장벽방전에 기초한 질소함유 활성종을 이용하여 (0001) 사파이어 기판위에 GaN 박막을 저온에서 성장시켰다. III-V 질소화합물 반도체의 에피막 성장에 있어서 암모니아는 유기금속 화학증착법에서 지금까지 알려진 가장 보편적인 질소 공급원이며 충분한 질소공급을 위해 1000˚C 이상의 고온 성장이 필수적이다. GaN 박막을 비교적 저온에서 성장시키기 위하여 질소 공급원으로 암모니아 대신 유전체 장벽방전을 이용하였다. 유전체 장벽방전은 전극사이에 유전체 장벽을 설치하여 arc를 조절하는 방전이며 수 기압의 높은 공정압력보다 훨씬 높으므로 기판표면까지 전달하는데도 이점이 있다. GaN 박막의 결정성과 표면형상은 성장온도, 완충층에 따라 변화하였으며, 700˚C의 저온에서도 우수한 (0001) 배향성을 갖는 GaN 박막을 성장할 수 있었다.

This study was conducted to investigated the possibility of inactivating wilt germs (Fusarium oxysporum f. sp. radicis lycopersici) using Dielectric Barrier Discharge (DBD) plasma in a hydroponic system. Recirculating hydroponic cultivation system for inactivation was consisted of planting port, LED lamp, water tank, and circulating pump for hydroponic and DBD plasma reactor. Two experiments were conducted: batch and intermittent continuous process. The effect of plasma treatment on Total Residual Oxidants (TRO) concentration change, Fusarium inactivation and growth of lettuce were investigated. In the batch experiment, most of the Fusarium was inactivated at a TRO concentration of 0.15 mg/L or more at four-day intervals. There was no change in lettuce growth after two times of plasma treatment for one week. The intermittent continuous experiment consisted of 30-minute, 60-minute, and 90-minute plasma treatment in 2 day intervals and 30-minute treatment a one-day; most of the Fusarium was inactivated only by treatment for 30-minute every two days. However, if inactivation under 101 CFU/mL is required, it will be necessary to treat for 60 minutes in 2 day intervals. The plasma treatment caused no damage to the lettuce, except the 30 min plasma treatment ay the one-day interval. It was considered that the residual TRO concentration was higher than that of the other treatments.

Many chemically active species such as ·H, ·OH, O3, H2O2, hydrated e-, as well as ultraviolet rays, are produced by Dielectric Barrier Discharge (DBD) plasma in water and are widely use to remove non-biodegradable materials and deactivate microorganisms. As the plasma gas containing chemically active species that is generated from the plasma reaction has a short lifetime and low solubility in water, increasing the dissolution rate of this gas is an important challenge. To this end, the plasma gas and water within reactor were mixed using the air-automizing nozzle, and then, water-gas mixture was injected into water. The dissolving effect of plasma gas was indirectly confirmed by measuring the RNO (N-Dimethyl-4-nitrosoaniline, indicator of the formation of OH radical) solution. The plasma system consisted of an oxygen generator, a high-voltage power supply, a plasma generator and a liquid-gas mixing reactor. Experiments were conducted to examine the effects of location of air-automizing nozzle, flow rate of plasma gas, water circulation rate, and high-voltage on RNO degradation. The experimental results showed that the RNO removal efficiency of the air-automizing nozzle is 29.8% higher than the conventional diffuser. The nozzle position from water surface was not considered to be a major factor in the design and operation of the plasma reactor. The plasma gas flow rate and water circulation rate with the highest RNO removal rate were 3.5 L/min and 1.5 L/min, respectively. The ratio of the plasma gas flow rate to the water circulation rate for obtaining an RNO removal rate of over 95% was 1.67 ~ 4.00.

Ozone concentrations in water and air, and resulting disinfective properties, were measured following generation by either an ozone generator or a low-temperature dielectric barrier discharge plasma generator. In freshwater, ozone concentrations of 0.81 and 0.48 mg/L O3 were observed after the ozone and plasma generators had been operated for five minutes, respectively. Higher levels of dissolved O3 were attained more easily with the ozone generator. In seawater, both systems were capable of creating concentrations greater than 3.00 mg/L O3 after 5minutes of operation. Higher ozone levels were attained more easily in seawater than in freshwater. Rates of bacterial sterilization in seawater after three minutes were 96% and 88%, using the plasma and ozone generators, respectively. In freshwater, higher concentrations of ozone were released into the atmosphere by the ozone generator than by the plasma generator. In creating equivalent levels of dissolved ozone in freshwater, the plasma generator released 4.5 times more ozone into the atmosphere than did the ozone generator. This shows that ozone generators are more effective than plasma generators for creating ozonated water. For the same concentration of dissolved ozone in seawater, more ozone was released into the atmosphere using the ozone generator than using the plasma generator. Therefore, with regard to air pollution, plasma generators seem to be less expensive than ozone generators.

Dielectric discharges are an emerging technique in environmental pollutant degradation, which that are characterized by the production of hydroxyl radicals as the primary degradation species. For practical application of the plasma reactor, reactor that can handle large amounts of water are needed. Plasma research to date has focused on small-scale water treatment. This study was carried out basic study for scale-up of a single DBD (dielectric barrier discharge) plasma reactor. The degradation of N, N-Dimethyl-4-nitrosoaniline (RNO, indicator of the generation of OH radical) was used as a performance indicator of multi-plasma reactor. The experiments is divided into two parts: design parameters [effect of distance of single plasma module (1~14 cm), arrangement of ground electrode (single and multi), rector number (1~5) and power number (1~5)]; operation parameter [effect of applied voltage (60~220 V), air flow rate (1~5 L/min), electric conductivity of solution (1.4 μS/cm, deionized water)~18.8 mS/cm (addition of NaCl 10 g/L) and pH (5~9)]. Considering the electric stability of the plasma reactor, optimum spacing between the single plasma module was 2 cm. Multi discharge electrodes - single ground electrode array was selected. Combination of power 3-plasma module 5 was the optimal combination for maximum RNO degradation. The optimum 1st voltage and air flow rate for RNO degradation were 180 V and 4 L/min, respectively. The pH and conductivity of the solution was not influencing the RNO degradation.

We studied the ozone concentrations generated by low-temperature dielectric barrier discharge plasma reactor after adding air and phytoplankton to control the ozone concentrations in seawater. We also examined the numbers of bacteria and Vibrio spp. after treatment using the plasma reactor. As the airflow rate was increased, more ozone was removed. Although marked variation in the ozone decrease was observed with and without airflow, the rate of ozone removal did not increase proportionately with the airflow rates. The ozone concentration decreased with increasing organic matter and time. The amount of organic matter seems to be an important factor decreasing the dissolved ozone concentration in liquid. The ozone concentration was 0.07, 0.32, 1.28, and 2.3 mg/L when operating the plasma reactor for 30, 60, 180, and 300 s, respectively; i.e., the ozone concentration increased with the reactor operating time. The initial numbers of bacteria and Vibrio spp. were 800 and 480 CFU/mL, respectively. After operating the plasma reactor at a flow rate of 6 L/min for 30 s, no bacteria or Vibrio spp. were detected. The disinfection effect of this plasma reactor seems to be superior to that of a conventional ozone generator.

Non-thermal plasma processing using a dielectric barrier discharge (DBD) has been investigated as an alternative method for the degradation of non-biodegradable organic compounds in wastewater. The active species such as OH radical, produced by the electrical discharge may play an important role in degrading organic compound in water. The degradation of N, N-Dimethyl-4-nitrosoaniline (RNO) was investigated as an indicator of the generation of OH radical. The DBD plasma reactor of this study consisted of a plasma reactor, recycling pump, power supply and reservoir. The effect of diameter of external reactor (15 ∼ 40 mm), width of ground electrode (2.5 ∼ 30 cm), shape (pipe, spring) and material (copper, stainless steel and titanium) of ground electrode, water circulation rate (3.1 ∼ 54.8 cm/s), air flow rate (0.5 ∼ 3.0 L/min) and ratio of packing material (0 ∼ 100 %) were evaluated. The experimental results showed that shape and materials of ground were not influenced the RNO degradation. Optimum diameter of external reactor, water circulation rate and air flow rate for RNO degradation were 30 mm, 25.4 cm/s and 4 L/min, respectively. Ground electrode length to get the maximum RNO degradation was 30 cm, which was same as reactor length. Filling up of glass beads decreased the RNO degradation. Among the experimented parameters, air flow rate was most important parameters which are influenced the decomposition of RNO.

A Dielectric barrier discharge (DBD) plasma is shown in the present investigation to be effective of phenol degradation in the aqueous solutions in batch reactor with continuous air bubbling. Removal of phenol and effects of various parameters on the removal efficiency in the aqueous solution with high-voltage streamer discharge plasma are studied. The effect of 1st voltage (80 ~ 220 V), air flow rate (3 ~ 7 L/min), pH (3 ~ 11), electric conductivity of solution (4.16 μS/cm, deionized water) ~ 16.57 mS/cm (addition of NaCl 10 g/L) and initial phenol concentration (2.5 ~ 20.0 mg/L) were investigated. The observed results showed that phenol degradation was higher in the basic solution than that of the acidic. The optimum values on the 1st voltage and air flow rate for phenol degradation were 140 V and 6 L/min, respectively. It was considered that absorbance variation of UV254 of phenol solution can be use as an indirect indicator of change of the non-biodegradable organic compounds within the treated phenol solution. Electric conductivity was not influenced the phenol degradation. To obtain the removal efficiency of phenol and COD of phenol over 97 % (initial phenol concentration, 10.0 mg/L), 80 min and 120 min were need, respectively. Phenol and COD degradation showed a pseudo-first order kinetics.

This study investigated the degradation of N, N-Dimethyl-4-nitrosoaniline (RNO, indicator of the generation of OH radical) by using dielectric barrier discharge (DBD) plasma. The DBD plasma reactor of this study consisted of a quartz dielectric tube, titanium discharge (inner) and ground (outer) electrode. The effect of shape (rod, spring and pipe) of ground electrode, diameter (9 ～ 30 mm) of ground electrode of spring shape and inside diameter (4 ～ 13 mm) of quartz tube, electrode diameter (1 ～ 4 mm), electrode materials (SUS, Ti, iron, Cu and W), height difference of discharge and ground electrode (1 ～ 15.5 cm) and gas flow rate (1 ～ 7 L/min) were evaluated. The experimental results showed that shape of ground electrode and materials of ground and discharge electrode were not influenced the RNO degradation. The thinner the diameter of discharge and ground electrode, the higher RNO degradation rate observed. The effect of height gap of discharge between ground electrode on RNO degradation was not high within the experimented value. Among the experimented parameters, inside diameter of quartz tube and gas flow rate were most important parameters which are influenced the decomposition of RNO. Optimum inside diameter of quartz tube and gas flow rate were 7 mm and 4 L/min, respectively.

Removal of elemental mercury (Hg0) with the reactive species produced from dielectric barrier discharge (DBD) was studied. We investigated the effect of operating parameters such as the applied voltage, residence time, initial concentration and co-existence of other pollutants. The removal of Hg0 was significantly promoted by an increase in the applied voltage of the DBD reactor system. It is important to note that at the same input power, the removal efficiency of Hg0 was much higher than that of NO gas. These results imply that if the DBD system is used as a NOx treatment facility, it is capable of removing Hg0 simultaneously with NOx.