WO2016060284A1 - Chlorine dioxide gas fumigation apparatus - Google Patents
Chlorine dioxide gas fumigation apparatus Download PDFInfo
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- WO2016060284A1 WO2016060284A1 PCT/KR2014/009604 KR2014009604W WO2016060284A1 WO 2016060284 A1 WO2016060284 A1 WO 2016060284A1 KR 2014009604 W KR2014009604 W KR 2014009604W WO 2016060284 A1 WO2016060284 A1 WO 2016060284A1
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- chlorine dioxide
- dioxide gas
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B7/00—Preservation of fruit or vegetables; Chemical ripening of fruit or vegetables
- A23B7/14—Preserving or ripening with chemicals not covered by group A23B7/08 or A23B7/10
- A23B7/144—Preserving or ripening with chemicals not covered by group A23B7/08 or A23B7/10 in the form of gases, e.g. fumigation; Compositions or apparatus therefor
- A23B7/152—Preserving or ripening with chemicals not covered by group A23B7/08 or A23B7/10 in the form of gases, e.g. fumigation; Compositions or apparatus therefor in a controlled atmosphere comprising other gases in addition to CO2, N2, O2 or H2O ; Elimination of such other gases
Definitions
- the present invention relates to a chlorine dioxide gas fumigation apparatus.
- the cold chain method has been mainly used to date, and the modified atmosphere (CA) and modified atmosphere (MA) which reduce oxygen and increase carbon dioxide by changing the air composition of the sealed storage space ) Storage is also used.
- CA modified atmosphere
- MA modified atmosphere
- ethylene which acts as an aging hormone in plants
- there are techniques for maintaining freshness by applying various methods such as temperature control and vacuum packaging.
- Chlorine dioxide has a wide range of effects as an oxidizing fungicide from fungi to bacteria and viruses, and microbial sterilization mechanisms are known to kill microorganisms by penetrating the protective membrane of microorganisms and interfering with the enzyme's action of cells by oxidative power.
- This bactericidal power is effective in a wide pH range and is more than 2.5 times stronger than chlorine and does not produce carcinogens such as THM (trihalomethane), so it has been spotlighted as an environmentally friendly green fungicide in Europe or the United States.
- THM trihalomethane
- Chlorine dioxide gas fumigation apparatus is to remove by-products generated when generating chlorine dioxide gas by using electrolysis.
- a body having a first space in which the raw material solution for the generation of chlorine dioxide gas is injected, and a second space partitioned from the first space; A first electrode in contact with the raw material solution in the first space; A second electrode exposed to the second space; Chlorine dioxide gas fumigation apparatus including a washing unit for spraying the cleaning material toward the by-product attached to the surface of the second electrode in the process of the electrolysis of the raw material solution as the voltage applied to the first electrode and the second electrode Is provided.
- the raw material solution may include sodium chlorite, and the by-product may include sodium hydroxide.
- the cleaning material may include H 2 O or a material having an acidic group.
- the substance having an acidic group may be citric acid solution or acetic acid solution.
- the washing unit may include a nozzle unit provided in the second space to spray the washing material toward the second electrode, a washing material flow passage communicating with the nozzle unit to transfer the washing material to the nozzle unit, and the washing material.
- the cleaning material may include a pump for cleaning material installed in the cleaning material flow path so that the cleaning material is transferred.
- the chlorine dioxide gas fumigation apparatus further includes a discharge unit, the discharge unit is a discharge pump which is provided in the discharge flow path for transporting the cleaning material in the second space, and the cleaning material in the second space; It may include.
- the chlorine dioxide gas may be generated through electrolysis of the raw material solution containing no sodium chloride.
- the object exposed to the chlorine dioxide gas is exposed to the chlorine dioxide gas of the second concentration band lower than the first concentration band after being exposed to the chlorine dioxide gas of the first concentration band for a first time in the target space where the object is placed.
- the cleaning strength for the by-product when the object is exposed to chlorine dioxide gas in the first concentration band is such that the object is exposed to chlorine dioxide gas in the second concentration band.
- the lower limit concentration of the first concentration band is 5 ppm or more
- the upper limit concentration is 300 ppm or less
- the upper limit concentration of the second concentration band is 0.3 ppm or less
- the lower limit concentration of the second concentration band may be 0.03 ppm or more.
- the washing strength of the by-product of the washing part may increase.
- the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention can increase the efficiency of the fumigation apparatus by washing the by-products of the electrode surface generated during the electrolysis process.
- FIG. 1 shows a chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention.
- FIG. 2 shows an embodiment of the chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention.
- FIG. 3 shows the object density after a predetermined time after the object A is exposed to chlorine dioxide gas satisfying the first concentration band.
- FIG. 4 shows the uniform density of objects after a predetermined time after the exposure of the object A, the object B, and the object C to the chlorine dioxide gas satisfying the second concentration band lower than the first concentration band.
- FIG. 5 shows the uniform density of the object A when the object A is exposed to the chlorine dioxide gas satisfying the second concentration band for a predetermined time after exposure to the chlorine dioxide gas satisfying the first concentration band.
- the chlorine dioxide gas fumigation apparatus includes a body 110, a first electrode 120, a second electrode 130, and a washing unit 140.
- the body 110 has a first space S1 into which a raw material solution for generating chlorine dioxide gas is injected, and a second space S2 partitioned from the first space S1.
- the raw material solution may be stored in the first tank 150 and may be injected into the first space S1 of the body 110 through the raw material solution pump 161 and the raw material solution valve 162.
- the raw material solution pump 161 and the raw material solution valve 162 may be provided in the raw material solution passage 163 through which the raw material solution is transferred.
- the first electrode 120 is in contact with the raw material solution of the first space S1, and the second electrode 130 is exposed to the second space S2.
- the washing unit 140 may cleanse the cleaning material toward the by-product attached to the surface of the second electrode 130 in the process of electrolyzing the raw material solution. Spray.
- FIG. 2 shows an embodiment of the chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention.
- One side of the body 110 may be provided with an electrolyte injection port 111 into which a raw material solution containing sodium chlorite (NaClO 2 ) is injected and a first outlet 112 through which chlorine dioxide (ClO 2 ) gas is discharged.
- the second outlet 113 may be formed on the other side of the body 110 and the other side. By-products generated in the process of generating chlorine dioxide gas may be discharged through the outlets. By-products are described in detail later.
- the conductive film 145 may be provided inside the body 110.
- the first space S1 and the second space S2 of the body 110 may be partitioned by the conductive film 145.
- the conductive film 145 may be provided in hydrocarbon and fluorocarbon type as a proton conductive material, wherein the fluorocarbon type resin may have excellent oxidation resistance against halogen, strong acid and base.
- the first electrode 120 corresponds to an anode layer, is connectable to a power source (not shown), and may be in contact with one side of the conductive layer 145.
- the second electrode 130 may correspond to a cathode layer and may be connected to a power source and may be in contact with the other side of the conductive film 145 opposite to one side.
- the first electrode 120 causes an oxidation reaction with sodium chlorite, which is an electrolyte, and the second electrode 130 causes a reduction reaction. Since the connection between the power source and the first electrode 120 and the second electrode 130 is a general technique to those skilled in the art, a detailed description thereof will be omitted.
- the first electrode 120 and the second electrode 130 may further include an electrochemical catalyst to maximize the efficiency of the redox reaction.
- the electrochemical catalyst may be platinum, palladium, rhodium, iridium, ruthenium, osmium, carbon, gold, tantalum, tin, indium, nickel, tungsten, manganese, or mixtures comprising at least one of them, oxides, alloys, or combinations thereof Can be.
- Sodium chlorite (NaClO 2) injected through the electrolyte injection port 111 may be composed of sodium chlorite (NaClO 2) salt and water (H 2 O).
- Sodium chlorite (NaClO 2) salt is converted into chlorine dioxide (ClO 2) gas, sodium ions (Na +) and electrons (e ⁇ ) by an oxidation reaction of the first electrode 120, and water is transferred to the first electrode 120.
- Oxidation reaction converts oxygen (O2) gas, hydrogen ions (H +) and electrons (e-).
- Chlorine dioxide (ClO2) gas and oxygen (O2) gas formed by the oxidation reaction of the first electrode 120 is discharged to the outside through the first outlet 112, sodium ions (Na +) and hydrogen ions (H +) It moves to the second electrode 130 through the conductive film 145 by electrical attraction.
- water (H 2 O) together with sodium ions (Na +) and hydrogen ions (H +) may move together.
- the hydrogen ions (H +) moved to the second electrode 130 become hydrogen by a reduction reaction by the second electrode 130, and the sodium ions (Na +) are combined with OH ⁇ of water (H 2 O) to form sodium hydroxide ( NaOH). That is, by-products are generated during the electrolysis process, and the by-products may include hydrogen and sodium hydroxide.
- Sodium hydroxide is a by-product generated in the process of generating chlorine dioxide gas through electrolysis, and when sodium hydroxide is attached to the second electrode 130, it may act as a resistance that interrupts the flow of current. When the amount of sodium hydroxide attached to the second electrode 130 increases, the amount of current required to generate chlorine dioxide gas increases, so that the efficiency of electrolysis may decrease.
- the chlorine dioxide gas fumigation apparatus includes a washing unit 140 capable of removing sodium hydroxide attached to the second electrode 130.
- the operation and structure of the cleaning unit 140 will be described in detail later with reference to the drawings.
- the electrochemical catalyst of the first electrode 120 and the second electrode 130 promotes the oxidation reaction of the first electrode 120 and the reduction reaction of the second electrode 130, as described above.
- the conductive layer 145 may contact the first electrode 120 and the second electrode 130 without a gap between the 145 and the first electrode 120 and a gap between the conductive layer 145 and the second electrode 130. have.
- Such a gap serves as a resistance that interrupts the flow of current.
- the current flows. This improvement can increase the generation efficiency of chlorine dioxide gas through electrolysis.
- sodium chloride NaCl
- sodium chlorite sodium chlorite
- chlorine dioxide gas may be generated through electrolysis of a raw material solution containing no sodium chloride. That is, since there is no gap between the conductive film 145 and the first electrode 120 and between the conductive film 145 and the second electrode 130, the input of sodium chloride is not necessary, so damage due to chlorine can be prevented. In addition, since there is no gap between the conductive layer 145 and the first and second electrodes 130, resistance due to the gap does not occur, and thus the generation efficiency of chlorine dioxide gas may be improved.
- the cleaning material sprayed by the cleaning unit 140 may include a material having H 2 O or an acidic group.
- Sodium hydroxide is soluble in water, so water can be used as a cleaning material.
- the acidic group combines smoothly with OH- of sodium hydroxide, a substance having an acidic group may also be used as a washing material.
- the substance with acidic groups may be citric acid solution or acetic acid solution.
- Citric acid solution or acetic acid solution is diluted with citric acid or acetic acid in water, inexpensive, harmless to the human body and easy to obtain.
- the cleaning unit 140 may include a nozzle unit 141, a cleaning material flow path 142, and a cleaning material pump 143.
- the nozzle unit 141 may be provided in the second space S2 of the body 110 to spray the cleaning material toward the second electrode 130.
- a nozzle passage 144 communicating with the washing material passage 142 may be formed in the nozzle unit 141.
- the cleaning material flow path 142 communicates with the nozzle unit 141 to transfer the cleaning material to the nozzle unit 141.
- the cleaning material pump 143 may be installed in the cleaning material flow path 142 so that the cleaning material is transferred to the cleaning material flow path 142.
- the cleaning material may be stored in the second tank 155 of FIG. 1, and a cleaning material valve 146 may be provided in the cleaning material flow path 142 to control the flow of the cleaning material.
- the chlorine dioxide gas fumigation apparatus may further include a discharge unit (170).
- the discharge unit 170 is a discharge pump 172 provided in the discharge passage 171 communicated with the second space (S2), and the discharge passage 171 to transfer the cleaning material of the second space (S2). It may include.
- the discharge valve 173 for controlling the flow of the cleaning material may be provided in the discharge passage (171). Since the sodium hydroxide attached to the second electrode 130 is washed by the cleaning material, the discharged cleaning material may include sodium hydroxide as a by-product.
- the raw material solution pump 161, the cleaning material pump 143, the discharge pump 172, the raw material solution valve 162, the cleaning material valve 146 and the discharge valve 173 are described above.
- the controller 180 may be controlled, and the controller 180 may output a valve control signal and a pump control signal.
- the raw material solution valve 162, the cleaning material valve 146, and the discharge valve 173 are the raw material solution, the cleaning material flowing into the second space S2, and the second space S2. It is possible to control the amount of the washing material discharged from the) and to open and close the raw material solution flow path 163, the cleaning material flow path 142 and the discharge flow path (171).
- the operation of the raw material solution pump 161, the pump for cleaning material 143 and the discharge pump 172, the operation stop, and the pumping amount of the raw material solution and the washing material can be controlled. have.
- the chlorine dioxide gas fumigation apparatus may supply chlorine dioxide gas to a target space through a gas supply valve 191 and a gas supply pump 192.
- the gas supply valve 191 and the gas supply pump 192 may also be controlled by the controller 180 described above.
- the gas supply valve 191 may control the amount of chlorine dioxide gas flowing and open and close the gas supply flow passage 193.
- the operation of the gas supply pump 192, the operation stop, and the pumping amount of chlorine dioxide gas can be controlled.
- the target space may be a space to which chlorine dioxide gas is supplied.
- the target space may be a warehouse, a container box, a pig farm, or a poultry farm in which the agricultural products are stored or grown, but is not limited thereto.
- 3 to 5 show the effect of using different concentration bands for the same object.
- the object placed in the object space may be exposed to the chlorine dioxide gas supplied by the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention.
- FIG. 3 shows the average density of object A when object A is 10 days after being exposed to chlorine dioxide gas satisfying the first concentration band for 30 minutes.
- the upper limit offset of the first concentration band may be 10% of the reference concentration k, and the lower limit offset may be ⁇ 10% of the reference concentration k. Accordingly, the concentration of chlorine dioxide gas in the target space may vary between 1.1k and 0.9k.
- the reference concentration, the upper limit offset and the lower limit offset may vary depending on the type of the object or the internal volume of the object space.
- FIG. 4 shows the uniform density in object A, object B and object C when exposed to chlorine dioxide gas for a second concentration band lower than the first concentration band for 10 days.
- the reference concentration, the upper limit concentration, and the lower limit concentration of the second concentration band may be 0.05 ppm, 0.1 ppm, and 0.03 ppm, respectively.
- the microbial density does not decrease until 10 days and the change in the microbial density is small.
- FIG. 5 shows the average density of the object A when the object A is exposed to the chlorine dioxide gas satisfying the low concentration second concentration band for 10 days after being exposed to the chlorine dioxide gas satisfying the high concentration first concentration band for 30 minutes. .
- the bacterial density decreases rapidly until two days or three days. Since the object A is exposed to the chlorine dioxide gas of the second concentration band of low concentration, the reduced density can be maintained continuously.
- the object exposed to the chlorine dioxide gas is lower than the first concentration band after being exposed to the chlorine dioxide gas of the first concentration band for a first time in the target space in which the object is placed.
- the chlorine dioxide gas may be supplied to the target space to be exposed to the chlorine dioxide gas in the two concentration bands for a second time longer than the first time.
- the chlorine dioxide gas fumigation apparatus when the internal volume of the target space is large, the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention supplies a high concentration of chlorine dioxide gas corresponding to the first concentration band to the target space in a short time, the chlorine dioxide gas in the target space.
- the concentration can be reached to the target concentration.
- a high concentration of chlorine dioxide gas is supplied to the target space for a short time, the possibility of high concentration of chlorine dioxide gas affecting the human body can be lowered.
- the chlorine dioxide gas fumigation apparatus can maintain a uniform density of the object by supplying a low concentration of chlorine dioxide gas corresponding to the second concentration band to the target space for a long time.
- the chlorine dioxide gas satisfying the first concentration band is supplied during the first time period and the chlorine dioxide gas satisfying the second concentration band is supplied during the second time period through the gas supply valve 191 of the controller 180. It can be made through the control for the gas supply pump 192.
- the washing strength for the by-product when the object is exposed to the chlorine dioxide gas in the first concentration band may be greater than the washing strength for the by-product when the object is exposed to the chlorine dioxide gas in the second concentration band.
- the chlorine dioxide gas fumigation apparatus supplies a high concentration of chlorine dioxide gas corresponding to the first concentration band
- the amount of chlorine dioxide gas generated through electrolysis may increase.
- by-products such as sodium hydroxide generated during the electrolysis process for generating chlorine dioxide gas may also increase, and the washing strength of the washing unit 140 to remove the by-products may also increase.
- the washing strength may include at least one of the spraying speed of the washing material or the number of spraying per unit time.
- the injection speed may be defined as the amount of cleaning material sprayed per unit time.
- the chlorine dioxide gas fumigation apparatus As described above, supplying the chlorine dioxide gas so that the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention satisfies the first concentration band and the second concentration band, in order for the target space to store or grow the agricultural products.
- the volume of the target space should be large because it is difficult to maintain the concentration of chlorine dioxide uniformly throughout the target space as the volume of the target space increases.
- the chlorine dioxide fumigation apparatus controls the concentration of chlorine dioxide gas in the target space by supplying chlorine dioxide gas so that the chlorine dioxide concentration of the target space is in the set first and second concentration bands. It can be done easily.
- a concentration sensor may be installed in the target space.
- the controller 180 may receive the sensing signal of the concentration sensor and output a valve control signal and a pump control signal such that the concentration of chlorine dioxide gas in the target space satisfies the first concentration band and the second concentration band.
- the lower limit concentration of the first concentration band may be 5 ppm or more and the upper limit concentration may be 300 ppm or less.
- the upper limit concentration may be 300 ppm or less.
- the upper limit concentration of the second concentration band may be 0.3 ppm or less and the lower limit concentration of the second concentration band may be 0.03 ppm or more. Human exposure to 0.3 ppm of chlorine dioxide for 15 minutes is harmless to humans. In addition, sterilization of the concentrated product may be performed when the concentration of chlorine dioxide is 0.03 ppm or more.
- the washing strength of the by-product of the washing unit 140 may increase.
- the washing unit 140 may increase the washing strength for the by-products such as sodium hydroxide. Since the washing strength has been described above, a description thereof will be omitted.
- time information such as a first time and a second time may be input from the timer 200 to the controller 180.
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Abstract
A chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention comprises: a body having a first space into which source material solution for generating chlorine dioxide gas is injected, and a second space that is separated from the first space; a first electrode that contacts the source material solution in the first space; a second electrode that is exposed in the second space; a cleaning part for spraying cleaning material toward by-products attached to the surface of the second electrode during electrolysis of the source material solution as a voltage is applied to the first electrode and the second electrode.
Description
본 발명은 이산화염소가스 훈증장치에 관한 것이다.The present invention relates to a chlorine dioxide gas fumigation apparatus.
농축산물은 저장 및 유통을 통하여 소비자에게 전달되는 과정 중에 부패 미생물이나 생리적 작용 또는 온도 조건 등이 복합적으로 작용하여 썩거나 상품으로서의 가치가 훼손된다. 손실 비율은 전체 농축산물의 20% 내지 30%에 이르러 이를 경제적 손실규모로 환산하면 수 조원에 이른다. In agricultural and livestock products, decaying microorganisms, physiological effects, or temperature conditions act in combination during storage and distribution to consumers. The loss rate ranges from 20% to 30% of the total agricultural product, which translates into trillions of dollars in economic losses.
농축산물의 저장 및 유통 중 손실을 줄이기 위해 현재까지 저온 유지(cold chain) 방법이 주로 사용되며, 밀폐 저장 공간의 공기 조성 성분을 변경하여 산소는 줄이고 이산화탄소는 높이는 CA(Controlled Atmosphere), MA(Modified Atmosphere) 저장법이 활용되기도 한다. 또한 식물의 노화 호르몬으로 작용하는 에틸렌을 조절하는 방법이 부상되고 있다. 축산물의 경우에는 온도조절과 진공 포장 등 여러 방법의 적용으로 신선도를 유지하는 기술이 존재하고 있다. To reduce losses during the storage and distribution of agricultural and livestock products, the cold chain method has been mainly used to date, and the modified atmosphere (CA) and modified atmosphere (MA) which reduce oxygen and increase carbon dioxide by changing the air composition of the sealed storage space ) Storage is also used. In addition, a method of controlling ethylene, which acts as an aging hormone in plants, is emerging. In the case of livestock products, there are techniques for maintaining freshness by applying various methods such as temperature control and vacuum packaging.
그러나 농축산물의 표면에 부착된 미생물의 밀도를 낮추지 않고서는 미생물에 의한 농축산물의 부패 가속화를 제어하기 힘들다. 미생물의 제거를 위해 작물에 따라 농산물을 살균 용액으로 세척하여 미생물을 제거하기도 하지만 딸기, 포도, 복숭아를 포함하여 대부분의 과수 작물들과 약초는 수용액 접촉이 원천적으로 불가하고 축산물 역시 마땅한 대안이 없는 실정이다. However, it is difficult to control the accelerated decay of the concentrate by the microorganisms without lowering the density of the microorganisms attached to the surface of the concentrate. In order to remove microorganisms, some crops are washed with a disinfectant solution to remove microorganisms, but most fruit crops and herbs, including strawberries, grapes and peaches, are inherently incapable of contact with aqueous solutions, and livestock products do not have an alternative. to be.
용액의 접촉이 허용된다고 하더라도 농축산물의 갈라지거나 상처가 난 틈새 부위에 서식하는 미생물에 대한 살균 효과는 가스 살균이 용액에 의한 세척 살균보다 월등히 높은 것으로 실험결과들이 보고되고 있다. Even if the contact of the solution is allowed, the results of the experiment show that the sterilization effect on the microorganisms living in the cracked or injured crevices of the concentrated product is much higher than that of the solution sterilization.
용액 세척 살균과 비교하여 가스 훈증법을 적용하면 상품 포장이 이뤄진 후 아주 미세한 공기 구멍을 통해서도 가스와 작물의 접촉이 이루어져 살균효과가 발휘될 수 있다. Compared to solution wash sterilization, the application of gas fumigation can result in the sterilization effect due to the contact of gas and crops through very fine air holes after product packaging.
이와 같은 가스 훈증법에 사용되는 물질은 여러 가지가 있다. 유황 훈증 방법의 경우 인체 유해 가능성이 문제시 되고, MB(메틸브로마이드) 훈증의 경우는 오존파괴물질로 사용이 금지되어 가고 있는 반면, 이산화염소는 식약청에 등록된 식품첨가물이며 농수산식품부에서 식품 표면의 세척, 소독 목적으로 등록된 유기적 취급물질로 친환경적이다.There are many materials used in such a method of gas fumigation. In the case of the sulfur fumigation method, the possibility of harm to humans is a problem, and MB (methyl bromide) fumigation is being banned as an ozone depleting substance, while chlorine dioxide is a food additive registered with the KFDA. It is an environmentally friendly organic handling material registered for cleaning and disinfection.
이산화염소는 곰팡이에서 세균, 바이러스에 이르기까지 산화 살균제로서 광범위한 효력을 갖고 있으며, 미생물 살균 메커니즘은 미생물의 보호막을 뚫고 들어가 산화력에 의한 세포의 효소작용을 방해하여 미생물을 죽이는 것으로 알려져 있다. Chlorine dioxide has a wide range of effects as an oxidizing fungicide from fungi to bacteria and viruses, and microbial sterilization mechanisms are known to kill microorganisms by penetrating the protective membrane of microorganisms and interfering with the enzyme's action of cells by oxidative power.
이같은 살균력은 넓은 PH범위에서 유효하며 염소에 비해 2.5배 이상 살균력이 강하고 THM(trihalomethane)과 같은 발암물질을 생성하지 않으므로 유럽이나 미국에서 환경 친화적 그린(Green) 살균제로 각광 받고 있다. UN 산하 세계보건기구(WHO) 및 식량농업기구(FAO)는 이산화염소를 살균제로 추천하고 있다. This bactericidal power is effective in a wide pH range and is more than 2.5 times stronger than chlorine and does not produce carcinogens such as THM (trihalomethane), so it has been spotlighted as an environmentally friendly green fungicide in Europe or the United States. The United Nations World Health Organization (WHO) and the Food and Agriculture Organization (FAO) recommend chlorine dioxide as a disinfectant.
이와 같은 이산화염소를 발생시킬 수 있는 다양한 장치에 대한 연구가 진행되고 있다. Research on various devices capable of generating such chlorine dioxide is underway.
본 발명의 실시예에 따른 이산화염소가스 훈증장치는 전기분해를 이용하여 이산화염소가스를 생성할 때 발생하는 부산물을 제거하기 위한 것이다.Chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention is to remove by-products generated when generating chlorine dioxide gas by using electrolysis.
본 발명의 일측면에 따르면, 이산화염소가스 생성을 위한 원료 용액이 주입되는 제1 공간과, 상기 제1 공간과 구획된 제2 공간을 갖는 바디; 상기 제1 공간의 상기 원료 용액과 접촉하는 제1 전극; 상기 제2 공간에 노출되는 제2 전극; 상기 제1 전극 및 상기 제2 전극에 전압이 인가됨에 따라 상기 원료 용액이 전기분해되는 과정에서 상기 제2 전극의 표면에 부착되는 부산물을 향하여 세척물질을 분사하는 세척부를 포함하는 이산화염소가스 훈증장치가 제공된다.According to an aspect of the present invention, a body having a first space in which the raw material solution for the generation of chlorine dioxide gas is injected, and a second space partitioned from the first space; A first electrode in contact with the raw material solution in the first space; A second electrode exposed to the second space; Chlorine dioxide gas fumigation apparatus including a washing unit for spraying the cleaning material toward the by-product attached to the surface of the second electrode in the process of the electrolysis of the raw material solution as the voltage applied to the first electrode and the second electrode Is provided.
상기 원료용액은 아염소산나트륨을 포함하고, 상기 부산물은 수산화나트륨을 포함할 수 있다.The raw material solution may include sodium chlorite, and the by-product may include sodium hydroxide.
상기 세척물질은 H2O이거나 산성기를 지닌 물질을 포함할 수 있다.The cleaning material may include H 2 O or a material having an acidic group.
상기 산성기를 지닌 물질은 구연산 용액 또는 초산 용액일 수 있다.The substance having an acidic group may be citric acid solution or acetic acid solution.
상기 세척부는, 상기 제2 공간에 구비되어 상기 세척물질을 상기 제2 전극을 향하여 분사하는 노즐부, 상기 노즐부에 연통되어 상기 세척물질을 상기 노즐부로 이송하는 세척물질용 유로, 및 상기 세척물질용 유로에 상기 세척물질이 이송되도록 상기 세척물질용 유로에 설치되는 세척물질용 펌프를 포함할 수 있다.The washing unit may include a nozzle unit provided in the second space to spray the washing material toward the second electrode, a washing material flow passage communicating with the nozzle unit to transfer the washing material to the nozzle unit, and the washing material. The cleaning material may include a pump for cleaning material installed in the cleaning material flow path so that the cleaning material is transferred.
상기 이산화염소가스 훈증장치는 배출부를 더 포함하며, 상기 배출부는 상기 제2 공간과 연통된 배출용 유로와, 상기 제2 공간의 상기 세척물질이 이송되도록 상기 배출용 유로에 구비되는 배출용 펌프를 포함할 수 있다.The chlorine dioxide gas fumigation apparatus further includes a discharge unit, the discharge unit is a discharge pump which is provided in the discharge flow path for transporting the cleaning material in the second space, and the cleaning material in the second space; It may include.
상기 제1 전극 및 상기 제2 전극에 전압이 인가됨에 따라 염화나트륨이 미포함된 상기 원료 용액의 전기분해를 통하여 상기 이산화염소가스가 발생될 수 있다. As voltage is applied to the first electrode and the second electrode, the chlorine dioxide gas may be generated through electrolysis of the raw material solution containing no sodium chloride.
상기 이산화염소가스에 노출되는 대상물은 상기 대상물이 놓인 대상 공간에서 제1 농도밴드의 이산화염소가스에 제1 시간동안 노출된 후 상기 제1 농도밴드보다 낮은 제2 농도밴드의 이산화염소가스에 상기 제1 시간보다 긴 제2 시간동안 노출되며, 상기 대상물이 상기 제1 농도밴드의 이산화염소가스에 노출될 때의 상기 부산물에 대한 세척 강도는 상기 대상물이 상기 제2 농도밴드의 이산화염소가스에 노출될 때의 상기 부산물에 대한 세척 강도에 비해 클 수 있다. The object exposed to the chlorine dioxide gas is exposed to the chlorine dioxide gas of the second concentration band lower than the first concentration band after being exposed to the chlorine dioxide gas of the first concentration band for a first time in the target space where the object is placed. Exposed for a second time longer than 1 hour, the cleaning strength for the by-product when the object is exposed to chlorine dioxide gas in the first concentration band is such that the object is exposed to chlorine dioxide gas in the second concentration band. When compared to the wash strength for the by-products of the time.
상기 제1 농도밴드의 하한 농도는 5 ppm 이상이고 상한 농도는 300 ppm 이하이고, 상기 제2 농도밴드의 상한농도는 0.3 ppm 이하이고 상기 제2 농도밴드의 하한농도는 0.03 ppm 이상일 수 있다. The lower limit concentration of the first concentration band is 5 ppm or more, the upper limit concentration is 300 ppm or less, the upper limit concentration of the second concentration band is 0.3 ppm or less, and the lower limit concentration of the second concentration band may be 0.03 ppm or more.
상기 제1 전극 및 상기 제2 전극에 공급되는 전류의 크기가 증가함에 따라 상기 세척부의 상기 부산물에 대한 세척강도가 증가할 수 있다. As the magnitude of the current supplied to the first electrode and the second electrode increases, the washing strength of the by-product of the washing part may increase.
본 발명의 실시예에 따른 이산화염소가스 훈증장치는 전기분해과정에서 생성된 전극 표면의 부산물을 세척함으로써 훈증장치의 효율을 높일 수 있다.The chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention can increase the efficiency of the fumigation apparatus by washing the by-products of the electrode surface generated during the electrolysis process.
도 1은 본 발명의 실시예에 따른 이산화염소가스 훈증장치를 나타낸다.1 shows a chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention.
도 2는 본 발명의 실시예에 따른 이산화염소가스 훈증장치의 구현예를 나타낸다.Figure 2 shows an embodiment of the chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention.
도 3은 대상물 A가 제1 농도밴드를 만족하는 이산화염소가스에 노출된 후 소정 시간 경과 후의 대상물 균밀도를 나타낸다.FIG. 3 shows the object density after a predetermined time after the object A is exposed to chlorine dioxide gas satisfying the first concentration band.
도 4는 대상물 A, 대상물 B 및 대상물 C가 제1 농도밴드보다 낮은 제2 농도밴드를 만족하는 이산화염소가스에 노출된 후 소정 시간 경과 후의 대상물들의 균밀도를 나타낸다.FIG. 4 shows the uniform density of objects after a predetermined time after the exposure of the object A, the object B, and the object C to the chlorine dioxide gas satisfying the second concentration band lower than the first concentration band.
도 5는 대상물 A가 제1 농도밴드를 만족하는 이산화염소가스에 노출된 후 소정 시간 동안 제2 농도밴드를 만족하는 이산화염소가스에 노출되었을 때 대상물 A의 균밀도를 나타낸다.FIG. 5 shows the uniform density of the object A when the object A is exposed to the chlorine dioxide gas satisfying the second concentration band for a predetermined time after exposure to the chlorine dioxide gas satisfying the first concentration band.
이하 본 발명의 목적이 구체적으로 실현될 수 있는 본 발명의 실시예를 첨부된 도면을 참조하여 설명한다. 본 실시예를 설명함에 있어서, 동일 구성에 대해서는 동일 명칭 및 동일 부호가 사용되며 이에 따른 부가적인 설명은 생략하기로 한다.DETAILED DESCRIPTION Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the description of this embodiment, the same name and the same reference numerals are used for the same configuration and additional description thereof will be omitted.
도 1은 본 발명의 실시예에 따른 이산화염소가스 훈증장치를 나타낸다. 도 1에 도시된 바와 같이, 본 발명의 실시예에 따른 이산화염소가스 훈증장치는 바디(110), 제1 전극(120), 제2 전극(130) 및 세척부(140)를 포함한다. 1 shows a chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention. As shown in FIG. 1, the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention includes a body 110, a first electrode 120, a second electrode 130, and a washing unit 140.
바디(110)는 이산화염소가스 생성을 위한 원료 용액이 주입되는 제1 공간(S1)과, 제1 공간(S1)과 구획된 제2 공간(S2)을 갖는다. 원료 용액은 제1 탱크(150)에 저장될 수 있으며, 원료용액용 펌프(161) 및 원료용액용 밸브(162)를 통하여 바디(110)의 제1 공간(S1)에 주입될 수 있다. 이와 같은 원료용액용 펌프(161) 및 원료용액용 밸브(162)는 원료용액이 이송되는 원료용액용 유로(163)에 구비될 수 있다. The body 110 has a first space S1 into which a raw material solution for generating chlorine dioxide gas is injected, and a second space S2 partitioned from the first space S1. The raw material solution may be stored in the first tank 150 and may be injected into the first space S1 of the body 110 through the raw material solution pump 161 and the raw material solution valve 162. The raw material solution pump 161 and the raw material solution valve 162 may be provided in the raw material solution passage 163 through which the raw material solution is transferred.
제1 전극(120)은 제1 공간(S1)의 원료 용액과 접촉하고, 제2 전극(130)은 제2 공간(S2)에 노출된다. The first electrode 120 is in contact with the raw material solution of the first space S1, and the second electrode 130 is exposed to the second space S2.
세척부(140)는 제1 전극(120) 및 제2 전극(130)에 전압이 인가됨에 따라 원료 용액이 전기분해되는 과정에서 제2 전극(130)의 표면에 부착되는 부산물을 향하여 세척물질을 분사한다. As the voltage is applied to the first electrode 120 and the second electrode 130, the washing unit 140 may cleanse the cleaning material toward the by-product attached to the surface of the second electrode 130 in the process of electrolyzing the raw material solution. Spray.
도 2는 본 발명의 실시예에 따른 이산화염소가스 훈증장치의 구현예를 나타낸다. Figure 2 shows an embodiment of the chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention.
바디(110)의 일측에는 아염소산나트륨(NaClO2)을 포함하는 원료용액이 주입되는 전해질 주입구(111) 및 이산화염소(ClO2)가스가 배출되는 제1 배출구(112)가 구비될 수 있다. 또한 바디(110)의 일측과 다른 타측에 제2 배출구(113)가 형성될 수 있다. 배출구를 통하여 이산화염소가스의 생성 과정에서 발생하는 부산물이 배출될 수 있다. 부산물에 대해서는 이후에 상세히 설명된다.One side of the body 110 may be provided with an electrolyte injection port 111 into which a raw material solution containing sodium chlorite (NaClO 2 ) is injected and a first outlet 112 through which chlorine dioxide (ClO 2 ) gas is discharged. In addition, the second outlet 113 may be formed on the other side of the body 110 and the other side. By-products generated in the process of generating chlorine dioxide gas may be discharged through the outlets. By-products are described in detail later.
전도성막(145)은 바디(110)의 내부에 구비될 수 있다. 바디(110)의 제1 공간(S1) 및 제2 공간(S2)은 전도성막(145)에 의하여 구획될 수 있다. 전도성막(145)은 양성자 전도성 물질로서 탄화수소 및 플루오로카본 타입으로 구비될 수 있으며, 여기서 플루오로카본 타입 수지는 할로겐, 강산 및 염기에 대해 뛰어난 내산화성을 가질 수 있다.The conductive film 145 may be provided inside the body 110. The first space S1 and the second space S2 of the body 110 may be partitioned by the conductive film 145. The conductive film 145 may be provided in hydrocarbon and fluorocarbon type as a proton conductive material, wherein the fluorocarbon type resin may have excellent oxidation resistance against halogen, strong acid and base.
제1 전극(120)은 양극층에 해당되며 전원(미도시)과 연결가능하고 전도성막(145) 일측에 접촉할 수 있다. 제2 전극(130)은 음극층에 해당되며 전원과 연결가능하며 일측 맞은 편의 전도성막(145) 타측에 접촉할 수 있다. 제1 전극(120)은 전해질인 아염소산나트륨과 산화반응을 일으키고, 제2 전극(130)은 환원반응을 일으킨다. 전원과, 제1 전극(120) 및 제2 전극(130)의 연결은 통상의 기술자에게 일반적인 기술이므로 이에 대한 상세한 설명은 생략된다. The first electrode 120 corresponds to an anode layer, is connectable to a power source (not shown), and may be in contact with one side of the conductive layer 145. The second electrode 130 may correspond to a cathode layer and may be connected to a power source and may be in contact with the other side of the conductive film 145 opposite to one side. The first electrode 120 causes an oxidation reaction with sodium chlorite, which is an electrolyte, and the second electrode 130 causes a reduction reaction. Since the connection between the power source and the first electrode 120 and the second electrode 130 is a general technique to those skilled in the art, a detailed description thereof will be omitted.
제1 전극(120) 및 제2 전극(130)은 산화환원반응의 효율을 극대화하기 위해 전기화학적 촉매를 더 포함할 수 있다. 전기화학적 촉매는 백금, 팔라듐, 로듐, 이리듐, 루테늄, 오스뮴, 탄소, 금, 탄탈륨, 주석, 인듐, 니켈, 텅스텐, 망간 등과 이들 중 적어도 하나를 포함하는 혼합물, 산화물, 합금 또는 이들이 조합된 물질일 수 있다.The first electrode 120 and the second electrode 130 may further include an electrochemical catalyst to maximize the efficiency of the redox reaction. The electrochemical catalyst may be platinum, palladium, rhodium, iridium, ruthenium, osmium, carbon, gold, tantalum, tin, indium, nickel, tungsten, manganese, or mixtures comprising at least one of them, oxides, alloys, or combinations thereof Can be.
전해질 주입구(111)를 통해 주입되는 아염소산나트륨(NaClO2)은 아염소산나트륨(NaClO2)염과 물(H2O)로 구성될 수 있다. 아염소산나트륨(NaClO2)염은 제1 전극(120)의 산화반응에 의해 이산화염소(ClO2) 가스, 나트륨이온(Na+) 및 전자(e-)로 전환되고, 물은 제1 전극(120)의 산화반응에 의해 산소(O2) 가스, 수소이온(H+) 및 전자(e-)로 전환된다.Sodium chlorite (NaClO 2) injected through the electrolyte injection port 111 may be composed of sodium chlorite (NaClO 2) salt and water (H 2 O). Sodium chlorite (NaClO 2) salt is converted into chlorine dioxide (ClO 2) gas, sodium ions (Na +) and electrons (e −) by an oxidation reaction of the first electrode 120, and water is transferred to the first electrode 120. Oxidation reaction converts oxygen (O2) gas, hydrogen ions (H +) and electrons (e-).
제1 전극(120)의 산화반응에 의하여 형성된 이산화염소(ClO2) 가스와 산소(O2) 가스는 제1 배출구(112)를 통해 외부로 배출되고, 나트륨이온(Na+)과 수소이온(H+)은 전기적 인력에 의해 전도성막(145)을 통과하여 제2 전극(130)으로 이동한다.Chlorine dioxide (ClO2) gas and oxygen (O2) gas formed by the oxidation reaction of the first electrode 120 is discharged to the outside through the first outlet 112, sodium ions (Na +) and hydrogen ions (H +) It moves to the second electrode 130 through the conductive film 145 by electrical attraction.
이때, 나트륨이온(Na+), 수소이온(H+)과 함께 물(H2O)이 함께 이동할 수 있다. 제2 전극(130)으로 이동한 수소이온(H+)은 제2 전극(130)에 의한 환원반응에 의해 수소가 되며, 나트륨이온(Na+)은 물(H2O)의 OH-와 결합하여 수산화나트륨(NaOH)으로 변한다. 즉, 전기분해과정에서 부산물이 생성되며, 부산물은 수소와 수산화나트륨을 포함할 수 있다. At this time, water (H 2 O) together with sodium ions (Na +) and hydrogen ions (H +) may move together. The hydrogen ions (H +) moved to the second electrode 130 become hydrogen by a reduction reaction by the second electrode 130, and the sodium ions (Na +) are combined with OH − of water (H 2 O) to form sodium hydroxide ( NaOH). That is, by-products are generated during the electrolysis process, and the by-products may include hydrogen and sodium hydroxide.
수산화나트륨은 전기분해를 통하여 이산화염소가스가 생성되는 과정에서 발생하는 부산물로서 제2 전극(130)에 부착될 경우 전류의 흐름을 방해하는 저항으로 작용할 수 있다. 제2 전극(130)에 부착되는 수산화나트륨의 양이 증가하면 이산화염소가스를 생성하는데 필요한 전류의 크기가 증가하므로 전기분해의 효율이 떨어질 수 있다. Sodium hydroxide is a by-product generated in the process of generating chlorine dioxide gas through electrolysis, and when sodium hydroxide is attached to the second electrode 130, it may act as a resistance that interrupts the flow of current. When the amount of sodium hydroxide attached to the second electrode 130 increases, the amount of current required to generate chlorine dioxide gas increases, so that the efficiency of electrolysis may decrease.
본 발명의 실시예에 따른 이산화염소가스 훈증장치는 제2 전극(130)에 부착된 수산화나트륨를 제거할 수 있는 세척부(140)를 포함한다. 세척부(140)의 동작 및 구조에 대해서는 이후에 도면을 통하여 상세히 설명된다. The chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention includes a washing unit 140 capable of removing sodium hydroxide attached to the second electrode 130. The operation and structure of the cleaning unit 140 will be described in detail later with reference to the drawings.
한편, 제1 전극(120) 및 제2 전극(130)의 전기화학적 촉매는 제1 전극(120)의 산화반응 및 제2 전극(130)의 환원반응을 촉진하므로 앞서 설명된 바와 같이 전도성막(145)과 제1 전극(120)의 간격 및 전도성막(145)과 제2 전극(130)의 간격없이 전도성막(145)은 제1 전극(120) 및 제2 전극(130)과 접촉할 수 있다. On the other hand, the electrochemical catalyst of the first electrode 120 and the second electrode 130 promotes the oxidation reaction of the first electrode 120 and the reduction reaction of the second electrode 130, as described above. The conductive layer 145 may contact the first electrode 120 and the second electrode 130 without a gap between the 145 and the first electrode 120 and a gap between the conductive layer 145 and the second electrode 130. have.
이와 같은 간격은 전류의 흐름을 방해하는 저항의 역할을 하는데 본 발명의 실시예와 같이 전도성막(145)의 양측이 제1 전극(120) 및 제2 전극(130)과 접촉할 경우 전류의 흐름이 향상되어 전기분해를 통한 이산화염소가스의 생성효율이 증가할 수 있다. Such a gap serves as a resistance that interrupts the flow of current. When both sides of the conductive layer 145 are in contact with the first electrode 120 and the second electrode 130 as in the embodiment of the present invention, the current flows. This improvement can increase the generation efficiency of chlorine dioxide gas through electrolysis.
본 발명의 실시예에 따른 이산화염소가스 훈증장치와 다르게 제1 전극(120) 및 제2 전극(130)이 전도성막(145)으로부터 이격될 경우 전기분해의 효율 저하를 방지하기 위하여 염화나트륨(NaCl)이 아염소산나트륨과 함께 투입될 수 있다. 이 경우 염화나트륨의 전기분해로 인하여 염소가 발생하여 인체에 해를 끼칠 수 있다. Unlike the chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention, when the first electrode 120 and the second electrode 130 are spaced apart from the conductive film 145, sodium chloride (NaCl) to prevent the degradation of the electrolysis efficiency. This may be added together with sodium chlorite. In this case, chlorine is generated due to the electrolysis of sodium chloride, which may harm the human body.
반면에 본 발명의 실시예의 경우 제1 전극(120) 및 제2 전극(130)에 전압이 인가됨에 따라 염화나트륨이 미포함된 원료 용액의 전기분해를 통하여 이산화염소가스가 발생될 수 있다. 즉, 전도성막(145)과 제1 전극(120) 사이 그리고 전도성막(145)과 제2 전극(130) 사이에 간격이 없으므로 염화나트륨의 투입이 필요없게 되므로 염소로 인한 피해가 방지될 수 있다. 또한 전도성막(145)과 제1 및 제2 전극(130) 사이에 간격이 없으므로 간격으로 인한 저항이 발생하지 않아 이산화염소가스의 생성 효율이 향상될 수 있다.On the other hand, in the embodiment of the present invention, as voltage is applied to the first electrode 120 and the second electrode 130, chlorine dioxide gas may be generated through electrolysis of a raw material solution containing no sodium chloride. That is, since there is no gap between the conductive film 145 and the first electrode 120 and between the conductive film 145 and the second electrode 130, the input of sodium chloride is not necessary, so damage due to chlorine can be prevented. In addition, since there is no gap between the conductive layer 145 and the first and second electrodes 130, resistance due to the gap does not occur, and thus the generation efficiency of chlorine dioxide gas may be improved.
한편, 세척부(140)가 분사하는 세척물질은 H2O이거나 산성기를 지닌 물질을 포함할 수 있다. 수산화나트륨은 물에 잘 녹으므로 물이 세척물질로 사용될 수 있다. 또한 산성기는 수산화나트륨의 OH-와 원활하게 결합하므로 산성기를 지닌 물질 또한 세척물질로 사용될 수 있다.Meanwhile, the cleaning material sprayed by the cleaning unit 140 may include a material having H 2 O or an acidic group. Sodium hydroxide is soluble in water, so water can be used as a cleaning material. In addition, since the acidic group combines smoothly with OH- of sodium hydroxide, a substance having an acidic group may also be used as a washing material.
예를 들어, 산성기를 지닌 물질은 구연산 용액 또는 초산 용액일 수 있다. 구연산 용액 또는 초산 용액은 물에 구연산이나 초산이 희석된 것으로 값이 싸고 인체에 해가 적을 뿐만 아니라 구하기 쉽다. For example, the substance with acidic groups may be citric acid solution or acetic acid solution. Citric acid solution or acetic acid solution is diluted with citric acid or acetic acid in water, inexpensive, harmless to the human body and easy to obtain.
세척부(140)는 노즐부(141), 세척물질용 유로(142) 및 세척물질용 펌프(143)를 포함할 수 있다. 노즐부(141)는 바디(110)의 제2 공간(S2)에 구비되어 세척물질을 제2 전극(130)을 향하여 분사할 수 있다. 도 2에 도시된 바와 같이 노즐부(141) 내부에는 세척물질용 유로(142)와 연통되는 노즐용 유로(144)가 형성될 수 있다. The cleaning unit 140 may include a nozzle unit 141, a cleaning material flow path 142, and a cleaning material pump 143. The nozzle unit 141 may be provided in the second space S2 of the body 110 to spray the cleaning material toward the second electrode 130. As shown in FIG. 2, a nozzle passage 144 communicating with the washing material passage 142 may be formed in the nozzle unit 141.
세척물질용 유로(142)는 노즐부(141)에 연통되어 세척물질을 노즐부(141)로 이송한다. 세척물질용 펌프(143)는 세척물질용 유로(142)에 세척물질이 이송되도록 세척물질용 유로(142)에 설치될 수 있다. 이 때 세척물질은 도 1의 제2 탱크(155)에 저장될 수 있으며, 세척물질의 흐름을 제어하기 위한 세척물질용 밸브(146)가 세척물질용 유로(142)에 구비될 수 있다. The cleaning material flow path 142 communicates with the nozzle unit 141 to transfer the cleaning material to the nozzle unit 141. The cleaning material pump 143 may be installed in the cleaning material flow path 142 so that the cleaning material is transferred to the cleaning material flow path 142. In this case, the cleaning material may be stored in the second tank 155 of FIG. 1, and a cleaning material valve 146 may be provided in the cleaning material flow path 142 to control the flow of the cleaning material.
한편, 본 발명의 실시예에 따른 이산화염소가스 훈증장치는 배출부(170)를 더 포함할 수 있다. 배출부(170)는 제2 공간(S2)과 연통된 배출용 유로(171)와, 제2 공간(S2)의 세척물질이 이송되도록 배출용 유로(171)에 구비되는 배출용 펌프(172)를 포함할 수 있다. 이 때 세척물질의 흐름을 제어하기 위한 배출용 밸브(173)가 배출용 유로(171)에 구비될 수 있다. 세척물질에 의하여 제2 전극(130)에 부착된 수산화나트륨이 세척되므로 배출되는 세척물질은 부산물인 수산화나트륨을 포함할 수 있다. On the other hand, the chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention may further include a discharge unit (170). The discharge unit 170 is a discharge pump 172 provided in the discharge passage 171 communicated with the second space (S2), and the discharge passage 171 to transfer the cleaning material of the second space (S2). It may include. At this time, the discharge valve 173 for controlling the flow of the cleaning material may be provided in the discharge passage (171). Since the sodium hydroxide attached to the second electrode 130 is washed by the cleaning material, the discharged cleaning material may include sodium hydroxide as a by-product.
이상에서 설명된 원료용액용 펌프(161), 세척물질용 펌프(143), 배출용 펌프(172), 원료용액용 밸브(162), 세척물질용 밸브(146) 및 배출용 밸브(173)는 콘트롤러(180)에 의하여 제어될 수 있으며, 콘트롤러(180)는 밸브제어신호와 펌프제어신호를 출력할 수 있다. The raw material solution pump 161, the cleaning material pump 143, the discharge pump 172, the raw material solution valve 162, the cleaning material valve 146 and the discharge valve 173 are described above. The controller 180 may be controlled, and the controller 180 may output a valve control signal and a pump control signal.
밸브제어신호의 입력에 따라 원료용액용 밸브(162), 세척물질용 밸브(146) 및 배출용 밸브(173)는 원료용액, 제2 공간(S2)으로 유입되는 세척물질 및 제2 공간(S2)에서 배출되는 세척물질이 흐르는 양을 제어할 수 있고, 원료용액용 유로(163), 세척물질용 유로(142) 및 배출용 유로(171)를 개폐할 수 있다. 또한 펌프제어신호의 입력에 따라 원료용액용 펌프(161), 세척물질용 펌프(143) 및 배출용 펌프(172)의 동작, 동작중지, 및 원료용액과 세척물질의 펌핑량 등이 제어될 수 있다. According to the input of the valve control signal, the raw material solution valve 162, the cleaning material valve 146, and the discharge valve 173 are the raw material solution, the cleaning material flowing into the second space S2, and the second space S2. It is possible to control the amount of the washing material discharged from the) and to open and close the raw material solution flow path 163, the cleaning material flow path 142 and the discharge flow path (171). In addition, according to the input of the pump control signal, the operation of the raw material solution pump 161, the pump for cleaning material 143 and the discharge pump 172, the operation stop, and the pumping amount of the raw material solution and the washing material can be controlled. have.
다음으로 도면을 참조하여 본 발명의 실시예에 따른 이산화염소가스 훈증장치의 농도밴드(band)와 세척 사이의 관계를 설명한다.Next, with reference to the drawings will be described the relationship between the concentration band (band) and washing of the chlorine dioxide gas fumigation apparatus according to an embodiment of the present invention.
도 1에 도시된 바와 같이, 본 발명의 실시예에 따른 이산화염소가스 훈증장치는 이산화염소가스를 가스공급용 밸브(191) 및 가스공급용 펌프(192)를 통하여 대상공간으로 공급할 수 있다. 가스공급용 밸브(191) 및 가스공급용 펌프(192) 역시 앞서 설명된 콘트롤러(180)의 제어를 받을 수 있다. As shown in FIG. 1, the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention may supply chlorine dioxide gas to a target space through a gas supply valve 191 and a gas supply pump 192. The gas supply valve 191 and the gas supply pump 192 may also be controlled by the controller 180 described above.
콘트롤러(180)의 제어에 따라 가스공급용 밸브(191)는 이산화염소가스가 흐르는 양을 제어할 수 있고, 가스공급용 유로(193)를 개폐할 수 있다. 또한 펌프제어신호의 입력에 따라 가스공급용 펌프(192)의 동작, 동작중지, 및 이산화염소가스의 펌핑량 등이 제어될 수 있다.According to the control of the controller 180, the gas supply valve 191 may control the amount of chlorine dioxide gas flowing and open and close the gas supply flow passage 193. In addition, according to the input of the pump control signal, the operation of the gas supply pump 192, the operation stop, and the pumping amount of chlorine dioxide gas can be controlled.
대상 공간은 이산화염소가스가 공급되는 공간일 수 있다. 예를 들어, 대상 공간은 농축산물이 보관 또는 생육되는 창고, 컨테이너 박스(container box), 양돈장 또는 양계장일 수 있으나, 이에 한정되는 것은 아니다.The target space may be a space to which chlorine dioxide gas is supplied. For example, the target space may be a warehouse, a container box, a pig farm, or a poultry farm in which the agricultural products are stored or grown, but is not limited thereto.
도 3 내지 도 5는 동일 대상물에 대하여 서로 다른 농도밴드의 사용에 대한 영향을 나타낸다. 대상공간에 놓인 대상물은 본 발명의 실시예에 따른 이산화염소가스 훈증장치가 공급한 이산화염소가스에 노출될 수 있다.3 to 5 show the effect of using different concentration bands for the same object. The object placed in the object space may be exposed to the chlorine dioxide gas supplied by the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention.
도 3은 대상물 A가 제1 농도밴드를 만족하는 이산화염소가스에 30분 노출된 후 10 일이 지났을 때 대상물 A의 균밀도를 나타낸다. 제1 농도밴드의 상한 오프셋(offset)은 기준농도 k의 10%이고, 하한 오프셋은 기준농도 k의 -10%일 수 있다. 이에 따라 대상 공간 안의 이산화염소가스의 농도는 1.1k와 0.9k 사이에서 변할 수 있다. FIG. 3 shows the average density of object A when object A is 10 days after being exposed to chlorine dioxide gas satisfying the first concentration band for 30 minutes. The upper limit offset of the first concentration band may be 10% of the reference concentration k, and the lower limit offset may be −10% of the reference concentration k. Accordingly, the concentration of chlorine dioxide gas in the target space may vary between 1.1k and 0.9k.
이 때 기준농도, 상한 오프셋 및 하한 오프셋은 대상물의 종류나 대상공간의 내부 부피에 따라 달라질 수 있다. In this case, the reference concentration, the upper limit offset and the lower limit offset may vary depending on the type of the object or the internal volume of the object space.
도 3에 도시된 바와 같이, 대상물이 고농도의 이산화염소가스에 노출되므로 2일 또는 3일까지는 균밀도가 급격하게 줄어드나 그 이후에는 균밀도가 서서히 증가함을 알 수 있다.As shown in FIG. 3, since the object is exposed to a high concentration of chlorine dioxide gas, the bacterial density decreases rapidly until two days or three days, after which the bacterial density gradually increases.
도 4는 제1 농도밴드보다 낮은 제2 농도밴드를 만족하는 이산화염소가스에 10 일 동안 노출될 때 대상물 A, 대상물 B 및 대상물 C에 있는 균밀도를 나타낸다. FIG. 4 shows the uniform density in object A, object B and object C when exposed to chlorine dioxide gas for a second concentration band lower than the first concentration band for 10 days.
이 때 제2 농도밴드의 기준 농도, 상한 농도 및 하한 농도는 각각 0.05 ppm, 0.1 ppm과 0.03 ppm일 수 있다. 도 4에 도시된 바와 같이, 저농도의 이산화염소가스에 대상물 A 대상물 B 및 대상물 C가 노출되므로 10일까지 균밀도가 감소하지 않으며 균밀도의 변화가 작음을 알 수 있다. In this case, the reference concentration, the upper limit concentration, and the lower limit concentration of the second concentration band may be 0.05 ppm, 0.1 ppm, and 0.03 ppm, respectively. As shown in FIG. 4, since the target A target B and the target C are exposed to the low concentration of chlorine dioxide gas, the microbial density does not decrease until 10 days and the change in the microbial density is small.
도 5는 대상물 A가 고농도의 제1 농도밴드를 만족하는 이산화염소가스에 30분 노출된 후 10 일 동안 저농도의 제2 농도밴드를 만족하는 이산화염소가스에 노출되었을 때 대상물 A의 균밀도를 나타낸다. FIG. 5 shows the average density of the object A when the object A is exposed to the chlorine dioxide gas satisfying the low concentration second concentration band for 10 days after being exposed to the chlorine dioxide gas satisfying the high concentration first concentration band for 30 minutes. .
제1 농도밴드 및 제2 농도밴드는 앞서 도 3 및 도 4를 참조하여 설명되었으므로 이에 대한 설명은 생략된다. Since the first concentration band and the second concentration band have been described above with reference to FIGS. 3 and 4, description thereof will be omitted.
도 5에 도시된 바와 같이, 대상물 A가 고농도의 제1 농도밴드의 이산화염소가스에 노출되므로 2일 또는 3일까지는 균밀도가 급격하게 줄어든다. 이후 대상물 A가 저농도의 제2 농도밴드의 이산화염소가스에 노출되므로 줄어든 균밀도가 지속적으로 유지될 수 있다. As shown in FIG. 5, since the object A is exposed to the high concentration of chlorine dioxide gas in the first concentration band, the bacterial density decreases rapidly until two days or three days. Since the object A is exposed to the chlorine dioxide gas of the second concentration band of low concentration, the reduced density can be maintained continuously.
이와 같이 이산화염소가스에 노출되는 대상물이 대상 공간에서 고농도의 제1 농도밴드의 이산화염소가스에 노출된 후 저농도의 제2 농도밴드의 이산화염소가스에 노출될 때 살균 효율이 도 3 및 도 4의 살균 효율보다 높음을 알 수 있다. As described above, when the object exposed to chlorine dioxide gas is exposed to the high concentration of chlorine dioxide gas of the first concentration band in the target space and then to the low concentration of chlorine dioxide gas of the second concentration band, the sterilization efficiency is shown in FIGS. 3 and 4. It can be seen that higher than the sterilization efficiency.
본 발명의 실시예에 따른 이산화염소가스 훈증장치는 이산화염소가스에 노출되는 대상물이 대상물이 놓인 대상 공간에서 제1 농도밴드의 이산화염소기스에 제1 시간동안 노출된 후 제1 농도밴드보다 낮은 제2 농도밴드의 이산화염소가스에 상기 제1 시간보다 긴 제2 시간동안 노출되도록 이산화염소가스를 대상 공간에 공급할 수 있다. In the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention, the object exposed to the chlorine dioxide gas is lower than the first concentration band after being exposed to the chlorine dioxide gas of the first concentration band for a first time in the target space in which the object is placed. The chlorine dioxide gas may be supplied to the target space to be exposed to the chlorine dioxide gas in the two concentration bands for a second time longer than the first time.
즉, 대상 공간의 내부 부피가 클 경우 본 발명의 실시예에 따른 이산화염소가스 훈증장치는 제1 농도밴드에 해당되는 고농도의 이산화염소가스를 대상공간에 공급함으로써 짧은 시간 내에 대상 공간의 이산화염소가스 농도를 타겟 농도에 이르게 할 수 있다. 또한 고농도의 이산화염소가스가 대상공간에 단시간 동안 공급됨으로써 고농도의 이산화염소가스가 인체에 영향을 끼칠 가능성을 낮출 수 있다. That is, when the internal volume of the target space is large, the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention supplies a high concentration of chlorine dioxide gas corresponding to the first concentration band to the target space in a short time, the chlorine dioxide gas in the target space. The concentration can be reached to the target concentration. In addition, since a high concentration of chlorine dioxide gas is supplied to the target space for a short time, the possibility of high concentration of chlorine dioxide gas affecting the human body can be lowered.
이후 본 발명의 실시예에 따른 이산화염소가스 훈증장치는 제2 농도밴드에 해당되는 저농도의 이산화염소가스를 대상공간에 장시간 공급함으로써 대상물의 균밀도를 유지할 수 있다. Subsequently, the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention can maintain a uniform density of the object by supplying a low concentration of chlorine dioxide gas corresponding to the second concentration band to the target space for a long time.
이와 같이 제1 시간동안 제1 농도밴드를 만족하는 이산화염소가스가 공급되고 제2 시간동안 제2 농도밴드를 만족하는 이산화염소가스가 공급되는 것은 콘트롤러(180)의 가스공급용 밸브(191) 및 가스공급용 펌프(192)에 대한 제어를 통하여 이루어질 수 있다. In this way, the chlorine dioxide gas satisfying the first concentration band is supplied during the first time period and the chlorine dioxide gas satisfying the second concentration band is supplied during the second time period through the gas supply valve 191 of the controller 180. It can be made through the control for the gas supply pump 192.
이 때 대상물이 제1 농도밴드의 이산화염소가스에 노출될 때의 부산물에 대한 세척 강도는 대상물이 제2 농도밴드의 이산화염소가스에 노출될 때의 부산물에 대한 세척 강도에 비해 클 수 있다. At this time, the washing strength for the by-product when the object is exposed to the chlorine dioxide gas in the first concentration band may be greater than the washing strength for the by-product when the object is exposed to the chlorine dioxide gas in the second concentration band.
즉, 본 발명의 실시예에 따른 이산화염소가스 훈증장치가 제1 농도밴드에 해당되는 고농도의 이산화염소가스를 공급함에 따라 전기분해를 통한 이산화염소가스의 발생량이 증가할 수 있다. 이에 따라 이산화염소가스 의 생성을 위한 전기분해 과정에서 발생하는 수산화나트륨과 같은 부산물 역시 증가할 수 있으며, 세척부(140)가 부산물을 제거하는 세척강도 역시 증가할 수 있다. That is, as the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention supplies a high concentration of chlorine dioxide gas corresponding to the first concentration band, the amount of chlorine dioxide gas generated through electrolysis may increase. Accordingly, by-products such as sodium hydroxide generated during the electrolysis process for generating chlorine dioxide gas may also increase, and the washing strength of the washing unit 140 to remove the by-products may also increase.
본 발명의 실시예에서 세척강도는 상기 세척물질의 분사속도 또는 단위 시간당 분사 횟수 중 적어도 하나를 포함할 수 있다. 이 때 분사속도는 단위 시간당 분사되는 세척물질의 양으로 정의될 수 있다. In the embodiment of the present invention, the washing strength may include at least one of the spraying speed of the washing material or the number of spraying per unit time. In this case, the injection speed may be defined as the amount of cleaning material sprayed per unit time.
이상에서 설명된 바와 같이, 본 발명의 실시예에 따른 이산화염소가스 훈증장치가 제1 농드밴드 및 제2 농도밴드를 만족하도록 이산화염소가스를 공급하는 것은 대상 공간이 농축산물을 저장하거나 생육하기 위해서는 대상 공간의 부피가 커야 하는데, 대상 공간의 부피가 증가할수록 대상 공간 전체에서 균일하게 이산화염소의 농도를 일정한 값으로 유지하기 어렵기 때문이다.As described above, supplying the chlorine dioxide gas so that the chlorine dioxide gas fumigation apparatus according to the embodiment of the present invention satisfies the first concentration band and the second concentration band, in order for the target space to store or grow the agricultural products. The volume of the target space should be large because it is difficult to maintain the concentration of chlorine dioxide uniformly throughout the target space as the volume of the target space increases.
즉, 본 발명의 실시예에 따른 이산화염소 훈증장치는 대상공간의 이산화염소 농도가 설정된 제1 농도밴드 및 제2 농도밴드 안에 있도록 이산화염소가스를 공급함으로써 대상공간에서의 이산화염소가스의 농도 조절을 용이하게 수행할 수 있다. That is, the chlorine dioxide fumigation apparatus according to the embodiment of the present invention controls the concentration of chlorine dioxide gas in the target space by supplying chlorine dioxide gas so that the chlorine dioxide concentration of the target space is in the set first and second concentration bands. It can be done easily.
도 1에는 도시되어 있지 않으나 대상 공간에는 농도 센서가 설치될 수 있다. 콘트롤러(180)는 농도 센서의 센싱 신호를 입력받아 대상 공간의 이산화염소가스의 농도가 제1 농도밴드 및 제2 농도밴드를 만족하도록 밸브제어신호와 펌프제어신호를 출력할 수 있다. Although not shown in FIG. 1, a concentration sensor may be installed in the target space. The controller 180 may receive the sensing signal of the concentration sensor and output a valve control signal and a pump control signal such that the concentration of chlorine dioxide gas in the target space satisfies the first concentration band and the second concentration band.
한편, 제1 농도밴드의 하한 농도는 5 ppm 이상이고 상한 농도는 300 ppm 이하일 수 있다. 대상 공간에서 5 ppm 이상의 이산화염소가스가 투입될 경우 농축산물과 같은 대상물에 대한 살균이 짧은 시간 내에 충분히 이루어져 인체에 대한 피해를 방지하거나 최소화할 수 있다. 또한 대상 공간에 300 ppm 이하의 농도를 지닌 이산화염소가스가 공급될 경우 오렌지나 단호박과 같이 껍질 두께가 큰 농축산물에 대해서도 살균에 짧은 시간 내에 충분히 이루어질 수 있다.Meanwhile, the lower limit concentration of the first concentration band may be 5 ppm or more and the upper limit concentration may be 300 ppm or less. When more than 5 ppm of chlorine dioxide gas is injected in the target space, sterilization of the target such as concentrated agricultural products is sufficiently performed in a short time, thereby preventing or minimizing damage to the human body. In addition, when chlorine dioxide gas having a concentration of 300 ppm or less is supplied to the target space, it is possible to achieve sufficient sterilization within a short time even for a concentrated product having a large shell thickness such as orange or sweet pumpkin.
또한 제2 농도밴드의 상한농도는 0.3 ppm 이하이고 제2 농도밴드의 하한농도는 0.03 ppm 이상일 수 있다. 사람이 0.3 ppm의 이산화염소에 15분 정도 노출되어도 인체에 무해하다. 또한 농축산물에 대한 살균은 이산화염소의 농도가 0.03ppm 이상일 때부터 이루어질 수 있다.In addition, the upper limit concentration of the second concentration band may be 0.3 ppm or less and the lower limit concentration of the second concentration band may be 0.03 ppm or more. Human exposure to 0.3 ppm of chlorine dioxide for 15 minutes is harmless to humans. In addition, sterilization of the concentrated product may be performed when the concentration of chlorine dioxide is 0.03 ppm or more.
상기 제1 전극(120) 및 상기 제2 전극(130)에 공급되는 전류의 크기가 증가함에 따라 상기 세척부(140)의 상기 부산물에 대한 세척강도가 증가할 수 있다. 단위 시간당 이산화염소가스의 발생량이 증가하면 즉, 제1 전극(120) 및 상기 제2 전극(130)에 공급되는 전류의 크기가 증가함에 따라 부산물 생성량 역시 증가할 수 있다. 이에 따라 세척부(140)는 수산화나트륨과 같은 부산물에 대한 세척강도를 높일 수 있다. 세척강도에 대해서는 앞서 설명되었으므로 이에 대한 설명은 생략된다. As the magnitude of the current supplied to the first electrode 120 and the second electrode 130 increases, the washing strength of the by-product of the washing unit 140 may increase. As the amount of chlorine dioxide gas generated per unit time increases, that is, as the amount of current supplied to the first electrode 120 and the second electrode 130 increases, the amount of by-products may also increase. Accordingly, the washing unit 140 may increase the washing strength for the by-products such as sodium hydroxide. Since the washing strength has been described above, a description thereof will be omitted.
이상의 설명에서 제1 시간 및 제2 시간 등과 같은 시간 정보는 타이머(200)로부터 콘트롤러(180)로 입력될 수 있다. In the above description, time information such as a first time and a second time may be input from the timer 200 to the controller 180.
이상과 같이 본 발명에 따른 실시예를 살펴보았으며, 앞서 설명된 실시예 이외에도 본 발명이 그 취지나 범주에서 벗어남이 없이 다른 특정 형태로 구체화 될 수 있다는 사실은 해당 기술에 통상의 지식을 가진 이들에게는 자명한 것이다. 그러므로, 상술된 실시예는 제한적인 것이 아니라 예시적인 것으로 여겨져야 하고, 이에 따라 본 발명은 상술한 설명에 한정되지 않고 첨부된 청구항의 범주 및 그 동등 범위 내에서 변경될 수도 있다.As described above, the embodiments of the present invention have been described, and the fact that the present invention can be embodied in other specific forms without departing from the spirit or scope of the present invention can be embodied by those skilled in the art. It is self-evident to. Therefore, the above-described embodiments should be regarded as illustrative rather than restrictive, and thus, the present invention is not limited to the above description and may be modified within the scope of the appended claims and their equivalents.
Claims (10)
- 이산화염소가스 생성을 위한 원료 용액이 주입되는 제1 공간과, 상기 제1 공간과 구획된 제2 공간을 갖는 바디;A body having a first space into which a raw material solution for generating chlorine dioxide gas is injected and a second space partitioned from the first space;상기 제1 공간의 상기 원료 용액과 접촉하는 제1 전극;A first electrode in contact with the raw material solution in the first space;상기 제2 공간에 노출되는 제2 전극;A second electrode exposed to the second space;상기 제1 전극 및 상기 제2 전극에 전압이 인가됨에 따라 상기 원료 용액이 전기분해되는 과정에서 상기 제2 전극의 표면에 부착되는 부산물을 향하여 세척물질을 분사하는 세척부를 포함하는 이산화염소가스 훈증장치.Chlorine dioxide gas fumigation apparatus including a washing unit for spraying the cleaning material toward the by-product attached to the surface of the second electrode in the process of the electrolysis of the raw material solution as the voltage applied to the first electrode and the second electrode .
- 제1항에 있어서,The method of claim 1,상기 원료용액은 아염소산나트륨을 포함하고, 상기 부산물은 수산화나트륨을 포함하는 것을 특징으로 하는 이산화염소가스 훈증장치.The raw material solution comprises sodium chlorite, and the by-product chlorine dioxide gas fumigation apparatus, characterized in that containing sodium hydroxide.
- 제1항에 있어서,The method of claim 1,상기 세척물질은 H2O이거나 산성기를 지닌 물질을 포함하는 것을 특징으로 하는 이산화염소가스 훈증장치. The chlorine dioxide gas fumigation apparatus, characterized in that the cleaning material comprises a substance having H 2 O or acidic groups.
- 제1항 내지 제3항 중 어느 한 항에 있어서,The method according to any one of claims 1 to 3,상기 산성기를 지닌 물질은 구연산 용액 또는 초산 용액인 것을 특징으로 하는 이산화염소가스 훈증장치.The material having an acidic group is chlorine dioxide gas fumigation apparatus, characterized in that the citric acid solution or acetic acid solution.
- 제1항 내지 제3항 중 어느 한 항에 있어서,The method according to any one of claims 1 to 3,상기 세척부는 The washing unit상기 제2 공간에 구비되어 상기 세척물질을 상기 제2 전극을 향하여 분사하는 노즐부, 상기 노즐부에 연통되어 상기 세척물질을 상기 노즐부로 이송하는 세척물질용 유로, 및 상기 세척물질용 유로에 상기 세척물질이 이송되도록 상기 세척물질용 유로에 설치되는 세척물질용 펌프를 포함하는 것을 특징으로 하는 이산화염소가스 훈증장치.A nozzle unit provided in the second space to spray the cleaning material toward the second electrode, a cleaning material flow path communicating with the nozzle part to transfer the cleaning material to the nozzle part, and the cleaning material flow path; Chlorine dioxide gas fumigation apparatus comprising a pump for the cleaning material installed in the flow path for the cleaning material so that the cleaning material is transferred.
- 제1항 내지 제3항 중 어느 한 항에 있어서,The method according to any one of claims 1 to 3,상기 이산화염소가스 훈증장치는 배출부를 더 포함하며,The chlorine dioxide gas fumigation apparatus further comprises a discharge,상기 배출부는 상기 제2 공간과 연통된 배출용 유로와, 상기 제2 공간의 상기 세척물질이 이송되도록 상기 배출용 유로에 구비되는 배출용 펌프를 포함하는 하는 것을 특징으로 하는 이산화염소가스 훈증장치. The discharge unit chlorine dioxide gas fumigation apparatus, characterized in that it comprises a discharge passage provided in the discharge passage and the discharge passage communicating with the second space, the cleaning material of the second space.
- 제1항 내지 제3항 중 어느 한 항에 있어서,The method according to any one of claims 1 to 3,상기 제1 전극 및 상기 제2 전극에 전압이 인가됨에 따라 염화나트륨이 미포함된 상기 원료 용액의 전기분해를 통하여 상기 이산화염소가스가 발생되는 것을 특징으로 하는 이산화염소가스 훈증장치. Chlorine dioxide gas fumigation apparatus, characterized in that the chlorine dioxide gas is generated through the electrolysis of the raw material solution containing no sodium chloride as a voltage is applied to the first electrode and the second electrode.
- 제1항 내지 제3항 중 어느 한 항에 있어서,The method according to any one of claims 1 to 3,상기 이산화염소가스에 노출되는 대상물은 상기 대상물이 놓인 대상 공간에서 제1 농도밴드의 이산화염소가스에 제1 시간동안 노출된 후 상기 제1 농도밴드보다 낮은 제2 농도밴드의 이산화염소가스에 상기 제1 시간보다 긴 제2 시간동안 노출되며,The object exposed to the chlorine dioxide gas is exposed to the chlorine dioxide gas of the second concentration band lower than the first concentration band after being exposed to the chlorine dioxide gas of the first concentration band for a first time in the target space where the object is placed. Exposed for a second time period longer than 1 hour,상기 대상물이 상기 제1 농도밴드의 이산화염소가스에 노출될 때의 상기 부산물에 대한 세척 강도는 상기 대상물이 상기 제2 농도밴드의 이산화염소가스에 노출될 때의 상기 부산물에 대한 세척 강도에 비해 큰 것을 특징으로 하는 이산화염소가스 훈증장치. The wash strength for the byproduct when the object is exposed to chlorine dioxide gas in the first concentration band is greater than the wash strength for the byproduct when the object is exposed to chlorine dioxide gas in the second concentration band. Chlorine dioxide gas fumigation apparatus, characterized in that.
- 제8항에 있어서,The method of claim 8,상기 제1 농도밴드의 하한 농도는 5 ppm 이상이고 상한 농도는 300 ppm 이하이고,The lower limit concentration of the first concentration band is 5 ppm or more and the upper limit concentration is 300 ppm or less,상기 제2 농도밴드의 상한농도는 0.3 ppm 이하이고 상기 제2 농도밴드의 하한농도는 0.03 ppm 이상인 것을 특징으로 하는 이산화염소가스 훈증장치. The upper limit concentration of the second concentration band is 0.3 ppm or less and the lower limit concentration of the second concentration band is chlorine dioxide gas fumigation apparatus, characterized in that.
- 제1항 내지 제3항 중 어느 한 항에 있어서,The method according to any one of claims 1 to 3,상기 제1 전극 및 상기 제2 전극에 공급되는 전류의 크기가 증가함에 따라 상기 세척부의 상기 부산물에 대한 세척강도가 증가하는 것을 특징으로 하는 이산화염소가스 훈증장치. Chlorine dioxide gas fumigation apparatus, characterized in that the washing strength of the by-products of the washing unit increases as the magnitude of the current supplied to the first electrode and the second electrode increases.
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KR101024011B1 (en) * | 2010-06-24 | 2011-03-25 | (주)엠비티 | Apparatus producing chlorine dioxide and manufacturing method for chlorine dioxide using the same |
KR20120092056A (en) * | 2011-02-09 | 2012-08-20 | (주)엘켐텍 | The electrolytic apparatus for clo2 gas and sterilization system of room |
KR101455719B1 (en) * | 2013-05-23 | 2014-11-04 | (주)푸르고팜 | ClO2 GAS FUMIGATION APPARATUS |
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US4542008A (en) * | 1983-10-03 | 1985-09-17 | Olin Corporation | Electrochemical chlorine dioxide process |
US5041196A (en) * | 1989-12-26 | 1991-08-20 | Olin Corporation | Electrochemical method for producing chlorine dioxide solutions |
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