WO2018124339A1 - Sterilizing device and method for measuring hydrogen peroxide concentration of sterilizing device - Google Patents
Sterilizing device and method for measuring hydrogen peroxide concentration of sterilizing device Download PDFInfo
- Publication number
- WO2018124339A1 WO2018124339A1 PCT/KR2016/015521 KR2016015521W WO2018124339A1 WO 2018124339 A1 WO2018124339 A1 WO 2018124339A1 KR 2016015521 W KR2016015521 W KR 2016015521W WO 2018124339 A1 WO2018124339 A1 WO 2018124339A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- hydrogen peroxide
- humidity sensor
- concentration
- humidity
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Images
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
- A61L2/20—Gaseous substances, e.g. vapours
- A61L2/208—Hydrogen peroxide
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
- A61L2/20—Gaseous substances, e.g. vapours
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/26—Accessories or devices or components used for biocidal treatment
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/10—Apparatus features
- A61L2202/12—Apparatus for isolating biocidal substances from the environment
- A61L2202/122—Chambers for sterilisation
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/10—Apparatus features
- A61L2202/14—Means for controlling sterilisation processes, data processing, presentation and storage means, e.g. sensors, controllers, programs
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/20—Targets to be treated
- A61L2202/24—Medical instruments, e.g. endoscopes, catheters, sharps
Definitions
- the present invention relates to a sterilization apparatus and a method for measuring hydrogen peroxide concentration of the sterilization apparatus, and more particularly, a sterilization apparatus capable of accurately detecting the concentration of hydrogen peroxide in hydrogen peroxide by a simple method and the measurement of hydrogen peroxide concentration of the sterilization apparatus. It is about a method.
- Medical instruments are usually sterilized by high pressure steam sterilization using saturated steam under high pressure, or by ethylene oxide gas sterilization using chemicals such as ethylene oxide that does not damage heat-affected instruments or materials.
- high pressure steam sterilizer sterilizes at a high temperature of more than 120 degrees
- medical instruments made of synthetic resins that have been recently developed are deformed, and medical instruments made of steel are dulled with fine blades, which are much shorter than the conventional lifespan.
- high-pressure steam sterilization may be an unsuitable sterilization method because expensive medical devices, instruments, and devices that are increasing due to the development of the latest surgical technology may be damaged during sterilization reprocessing because they are sensitive to heat or moisture.
- the ethylene oxide gas sterilizer can minimize the damage to the device, it can be sterilized at low temperature, but the ethylene oxide remains in the sterilized product or the reaction product may cause carcinogenic and toxic substances to be generated. Time is required.
- ethylene oxide gas itself is a high explosion risk, it has been reported that it can act as a genetic toxic substance that can cause mutations, and it is prescribed as a carcinogen, which requires much attention to its use.
- the sterilization method using hydrogen peroxide steam is a short sterilization time within 30 to 60 minutes at a temperature of 40 to 50 degrees, and the substances discharged to the atmosphere after sterilization are harmless to humans or the environment, so the disadvantages of the high pressure steam sterilizer and ethylene oxide gas Various disadvantages of the sterilizer can be compensated for.
- the hydrogen peroxide aqueous solution used to generate the hydrogen peroxide vapor makes it difficult to sufficiently diffuse hydrogen peroxide by evaporating and diffusing water before hydrogen peroxide during the vaporization process. This is because water is evaporated more quickly because of the higher vapor pressure than hydrogen peroxide, and because the molecular weight of water is lower than hydrogen peroxide, water vapor diffuses more rapidly into the gas phase than hydrogen peroxide vapor.
- Water vapor diffuses more quickly into diffusion-limiting spaces, such as smaller crevices or long narrow lumens, to suppress the permeation of hydrogen peroxide vapor. In other words, water reaches the sterilized product before hydrogen peroxide, so that sterilization is not performed properly.
- a hydrogen peroxide aqueous solution having a handleable concentration of 60 wt% or less through each step of concentration, for example, to a high concentration of hydrogen peroxide solution of 95 wt% or more and use it as a sterilizing agent. It can improve sterilization effect.
- the problem to be solved by the present invention is that the present invention was developed in order to solve the above problems, it is possible to accurately detect the concentration of hydrogen peroxide in the hydrogen peroxide by a simple method, avoiding the enlargement or complexity of the sterilization apparatus It is to provide a sterilization apparatus and a method for measuring the hydrogen peroxide concentration of the sterilization apparatus.
- the present invention is a sterilization apparatus including a sterilization chamber, the sterilization chamber, the first humidity sensor and a second humidity located adjacent to the first humidity sensor located in a predetermined region inside And a sensor, wherein the first humidity sensor detects the first relative humidity by the amount of hydrogen peroxide and the amount of water vapor, and the second humidity sensor detects the second relative humidity by the amount of water vapor. to provide.
- the present invention is characterized in that the first humidity sensor is a humidity sensor of a moisture absorption method, a humidity sensor of a saturation method or a humidity sensor of an absorption method, and the second humidity sensor is a humidity sensor of a spectroscopic method. It provides a sterilization apparatus.
- the present invention also provides a sterilization apparatus for calculating the concentration of the hydrogen peroxide by calculating a difference between the first relative humidity detected by the first humidity sensor and the second relative humidity detected by the second humidity sensor. do.
- the present invention comprises the steps of detecting the first relative humidity by the first humidity sensor; Detecting a second relative humidity by a second humidity sensor; Deriving a difference value between the first relative humidity and the second relative humidity; And it provides a hydrogen peroxide concentration measuring method comprising the step of calculating the concentration of hydrogen peroxide through the difference value.
- the present invention also provides a method for measuring hydrogen peroxide concentration in which the first humidity sensor determines relative humidity by the amount of water vapor and the amount of hydrogen peroxide, and the second humidity sensor determines the relative humidity by the amount of water vapor.
- the present invention is characterized in that the first humidity sensor is a humidity sensor of a moisture absorption method, a humidity sensor of a saturation method or a humidity sensor of an absorption method, and the second humidity sensor is a humidity sensor of a spectroscopic method. It provides a method for measuring the hydrogen peroxide concentration.
- the present invention is a target space for measuring the concentration of hydrogen peroxide, wherein the target space includes a first humidity sensor located in a predetermined internal area and a second humidity sensor located adjacent to the first humidity sensor; The first humidity sensor detects a first relative humidity by the amount of hydrogen peroxide and the amount of water vapor, and the second humidity sensor provides a target space for detecting the second relative humidity by the amount of water vapor.
- the present invention is characterized in that the first humidity sensor is a humidity sensor of a moisture absorption method, a humidity sensor of a saturation method or a humidity sensor of an absorption method, and the second humidity sensor is a humidity sensor of a spectroscopic method. Provide the target space.
- the present invention provides a target space, characterized in that the temperature of the first humidity sensor and the second humidity sensor is controlled higher than the temperature of the target space.
- the relative humidity is detected by each of these sensors, the concentration of hydrogen peroxide by the difference in these relative humidity It can be measured easily.
- FIG. 1 is a schematic perspective view showing a sterilizer using an aqueous solution of a sterilant according to the present invention
- Figure 2 is a schematic configuration diagram showing a sterilizer using an aqueous solution of a sterilant according to the present invention.
- Figure 3 is a flow chart illustrating a sterilization method of the sterilization apparatus using a sterilant aqueous solution according to the present invention.
- Figure 4 is a graph showing the response of the capacitive humidity sensor in the sterilization apparatus.
- FIG. 5 is a flowchart illustrating a method for measuring hydrogen peroxide concentration according to the present invention.
- first, second, etc. are used to describe various components, these components are of course not limited by these terms. These terms are only used to distinguish one component from another. Therefore, of course, the first component mentioned below may be a second component within the technical spirit of the present invention.
- spatially relative terms below “, “ beneath “, “ lower”, “ above “, “ upper” It can be used to easily describe a component's correlation with other components. Spatially relative terms are to be understood as including terms in different directions of components in use or operation in addition to the directions shown in the figures. For example, when flipping a component shown in the drawing, a component described as “below” or “beneath” of another component may be placed “above” the other component. Can be. Thus, the exemplary term “below” can encompass both an orientation of above and below. The components can be oriented in other directions as well, so that spatially relative terms can be interpreted according to the orientation.
- FIG. 1 is a schematic perspective view showing a sterilizer using an aqueous solution of a sterilant according to the present invention
- Figure 2 is a schematic configuration diagram showing a sterilizer using an aqueous solution of a sterilant according to the present invention.
- the sterilizing agent may be hydrogen peroxide
- the sterilizing agent aqueous solution may be hydrogen peroxide
- the sterilizing agent is hydrogen peroxide
- the sterilizing agent aqueous solution will be described in correspondence with hydrogen peroxide. do.
- the sterilization apparatus 100 using hydrogen peroxide according to the present invention includes a sterilization chamber (110).
- the sterilization chamber 110 represents a container into which sterilized substances, such as medical instruments or surgical instruments, to be sterilized are put. At this time, one side of the sterilization chamber 110 may include a door for access to the sterilized material.
- the vacuum pump 120 may draw a gas inside the sterilization chamber 110 to form a vacuum state.
- a vacuum valve 121 for controlling the operation of the vacuum pump 120 is connected.
- the sterilization apparatus 100 using hydrogen peroxide water according to the present invention is connected to the other side of the sterilization chamber 110 to supply hydrogen peroxide vapor to the sterilization chamber 110.
- the sterilization chamber 110 and the vaporizer 130 may include a vaporization valve 131.
- the sterilization apparatus 100 using hydrogen peroxide one side is connected to the vaporizer 130, the other side is connected to the sterilization chamber 110, the vaporizer 130 A collector 140 (or may be termed a collector vaporizer) for concentrating the supplied hydrogen peroxide.
- the sterilization chamber 110 and the collector 140 may include a vaporization valve 131.
- the sterilization chamber 110 and the collector 140 may include a collection valve 141.
- the vaporization valve 131 and the collection valve 141 may be connected in parallel between the sterilization chamber 110 and the collector 140.
- between the sterilization chamber 110 and the vaporizer 130 may include a vaporization valve 131, that is, one side of the vaporization valve 130 and the sterilization chamber 110 and The other side may be connected in parallel with the vaporizer 130 and the collector 140.
- the sterilization apparatus 100 using hydrogen peroxide includes a first connection pipe 142 and the vaporization connecting the collector 140 and the vaporization valve 131. It may include a second connecting pipe 133 connecting the valve 131 and the sterilization chamber 110.
- a third connecting pipe 143 connecting the collector 140 and the collection valve 141 and a fourth connecting pipe 144 connecting the collection valve 141 and the sterilization chamber 110. can do.
- the fourth connection pipe 144 is connected to the second connection pipe 133, and the vaporization valve 131 and the collection valve 141 are disposed between the sterilization chamber 110 and the collector 140.
- the fourth connection pipe 144 is connected directly to the sterilization chamber 110, the vaporization valve 131 between the sterilization chamber 110 and the collector 140, in contrast.
- the collection valve 141 may be connected in parallel.
- the vaporizer 130 may include a fifth connection pipe 132 connecting the vaporization valve 131, in this case, the fifth connection pipe 132 is the first connection pipe 142 in the drawing Is connected to the vaporization valve 130 and the vaporizer 130 and the collector 140, but in contrast, the fifth connection pipe 132 is directly connected to the vaporization valve 131
- the vaporization valve 130 may be connected in parallel with the vaporizer 130 and the collector 140.
- the vaporization valve 131 and the collection valve 141 may control the flow of the fluid of the first connection pipe 142 to the fifth connection pipe 132 by the open / close operation,
- the open / close operation of the vaporization valve 131 and the collection valve 141 may be controlled by a separate controller.
- the first connection pipe 142 for connecting the collector 140 and the vaporization valve 131 and the second connection pipe 133 for connecting the sterilization chamber 110 and the vaporization valve 131. May have a larger inner diameter than other connection pipes, that is, the third connection pipes 143 to the fifth connection pipes 132, for example, the third connection pipes 143 to the fifth connection pipes 132.
- the first connection pipe 142 and the second connection pipe 133 may be 1 inch pipe. This will be described later.
- the temperature control means may be a heater, which Since it is obvious in the art, a detailed description thereof will be omitted.
- the collector 140 may further include a cooling means as a temperature control means, and the cooling means may use a suitable means such as direct cooling using cooling water or a thermoelectric element or air cooling by blowing a heat exchanger. .
- Figure 3 is a flow chart illustrating a sterilization method of the sterilization apparatus using a sterilant aqueous solution according to the present invention.
- the sterilizing agent may be hydrogen peroxide
- the sterilizing agent aqueous solution may be hydrogen peroxide
- the sterilizing agent is hydrogen peroxide
- the sterilizing agent aqueous solution will be described in correspondence with hydrogen peroxide. do.
- the sterilization method of the sterilization apparatus using hydrogen peroxide includes the step of evacuating the sterilization chamber 110 (or, may be named sterilization chamber) and the vaporizer 130 ( S110).
- Evacuating the sterilization chamber 110 and the vaporizer 130 may be evacuated by operating the vacuum pump 120 (on) and opening the vacuum valve 121.
- step S110 that is, the step of evacuating the sterilization chamber and the vaporizer may be continued until step S160 to be described later, when the sterilization chamber reaches a predetermined set pressure, and the hydrogen peroxide liquid from which the water is removed is collected in the collector This step can be completed.
- the vaporization valve 131 between the sterilization chamber 110 and the vaporizer 130, or between the sterilization chamber 110 and the collector 140 is in an open state, is in communication with the sterilization chamber in the vacuum exhaust to be a pressure below atmospheric pressure and closed in the next step.
- the sterilization chamber and the vaporizer may be maintained at a temperature set by the above-described temperature control means.
- the hydrogen peroxide solution may be introduced through a hydrogen peroxide supply device 150 for storing hydrogen peroxide water at a first concentration. Meanwhile, although not shown in FIGS. 1 and 2, the vaporizer 130 and the hydrogen peroxide supply are provided. A hydrogen peroxide water supply control valve (not shown) may be provided between the devices 150 to supply an appropriate amount of hydrogen peroxide water.
- the first concentration of the hydrogen peroxide solution may be 60% by weight or less.
- the concentration of hydrogen peroxide is limited to 60% by weight or less in the handling of hydrogen peroxide solution, i.e., hydrogen peroxide water, so it is practically difficult to use a higher concentration of hydrogen peroxide as a sterilant.
- the first concentration of the hydrogen peroxide water indicates the concentration of the hydrogen peroxide water that can be handled and does not have an important meaning in understanding the meaning of the present invention.
- the first temperature may be 60 to 70 °C
- the first pressure may be 800 mb (pre-bar) to atmospheric pressure.
- step S120 while the hydrogen peroxide water of the first concentration is introduced into the vaporizer 130, the vaporization valve 131 and the collection valve 141 may correspond to a close state, but, depending on the supply device open It may be a state.
- step S120 the pressure of the sterilization chamber 110 is 600 mb to atmospheric pressure, the temperature may be 45 to 55 °C, the pressure of the collector 140 is 800 mb to atmospheric pressure, the temperature is 38 to May be 42 ° C.
- the first temperature in the present invention is characterized in that higher than the temperature of the sterilization chamber.
- the first temperature corresponds to the temperature of the vaporizer in the process of vaporizing more water vapor from the hydrogen peroxide water, the vaporization process of the water vapor very strong endothermic reaction occurs to suppress the vaporization rate very strongly.
- the first temperature is at least higher than the temperature of the sterilization chamber.
- the hydrogen peroxide water of the first concentration injected into the vaporizer 130 is vaporized (ie, water is removed) to form hydrogen peroxide water of the second concentration.
- the second concentration of the hydrogen peroxide solution may be 75% by weight to 85% by weight, and step S130 may be performed by vaporizing water in 60% by weight or less of hydrogen peroxide, thereby forming hydrogen peroxide water at a concentration of 75% by weight to 85% by weight. It may be a first concentration step.
- water ie, moisture
- water in the hydrogen peroxide water is evaporated / diffused before hydrogen peroxide, and thus a second concentration of hydrogen peroxide water may be formed.
- the evaporated water is evacuated through the vacuum pump via the sterilization chamber 110, and thus, in step S130 to operate (on) the vacuum pump 120, the vacuum valve 121 and the vaporization valve 131 corresponds to an open state.
- step S130 the temperature of the vaporizer 130 is temporarily lowered by the endothermic reaction of the vaporization process, the temperature is in the range of 55 to 65 °C, the pressure can be 30 to 800 mb (pre-bar) have.
- the pressure of the sterilization chamber 110 is in the range of 10 to 600 mb, the temperature may be 45 to 55 °C In addition, the pressure of the collector 140 is in the range of 20 to 500 mb, the temperature may be 35 to 40 °C.
- the vacuum pump 120 In order to inject the hydrogen peroxide solution of the second concentration into the collector 140 of the second temperature and the second pressure, the vacuum pump 120 is operated (on), and the vacuum valve 121 is opened, The vaporization valve 131 may be controlled in a close state, and the collection valve 141 may be controlled in an on state.
- the second temperature may be 35 to 42 °C
- the second pressure may be 8 to 50 mb.
- the pressure of the vaporizer 130 may be 10 to 60 mb
- the temperature may be 55 to 60 °C
- the second The concentration of hydrogen peroxide solution may move from the vaporizer 130 to the collector 140 via the fifth connection pipe 132 and the first connection pipe 142.
- step S140 the sterilization chamber 110 is continuously evacuated, the pressure of the sterilization chamber 110 is 1 to 10 mb, the temperature may be 45 to 55 °C.
- the second temperature in the present invention is characterized in that lower than the temperature of the sterilization chamber.
- the second temperature corresponds to the temperature of the collector in which the hydrogen peroxide water of the second concentration is collected, and if the saturated hydrogen peroxide vapor from the vaporizer is higher than the temperature of the chamber in the course of passing through the collector, the hydrogen peroxide vapor cannot be condensed in the collector. May be exhausted through the chamber.
- the second temperature is preferably at least lower than the temperature of the sterilization chamber.
- step S140 that is, the second temperature and the second Injecting the second concentration of hydrogen peroxide water into the collector of 2 pressure.
- the first concentration of hydrogen peroxide water directly into the collector it may be considered that the first concentration of hydrogen peroxide water directly into the collector, but is not preferable for the following reasons.
- Table 1 below shows an example of the vaporization rate of hydrogen peroxide vapor by the concentration of hydrogen peroxide water.
- the vaporization rate of hydrogen peroxide vapor in a 60% by weight hydrogen peroxide solution is 13%, which means that the remaining 87% is water vapor, and the vaporization rate of hydrogen peroxide vapor in an 80% by weight hydrogen peroxide solution. Is 40%, which means that the remaining 60% is water vapor.
- performing step S140 without step S130 may mean, for example, adding 60% by weight of hydrogen peroxide to a collector, and performing step S140 after performing step S130 is performed by 80% by weight. This could mean adding hydrogen peroxide to the collector.
- the ratio of the water vapor passing through the collector in the initial stage is relatively higher than when the step S140 is performed after the step S130 is performed.
- the collector is introduced into the collector when the pressure of the collector is high (saturated water vapor pressure is 75mb when the collector temperature is 40 ° C). It can also be condensed in the collector.
- the condensation of water vapor into the collector means that there is a limit to the concentration of hydrogen peroxide that is concentrated by the amount of water vapor that is condensed.
- step S130 that is, the hydrogen peroxide water of the second concentration by vaporizing the first concentration of hydrogen peroxide water
- step S140 that is, the step of introducing the hydrogen peroxide water of the second concentration to the collector of the second temperature and the second pressure.
- the hydrogen peroxide vapor in the second concentration of hydrogen peroxide water is condensed in the collector, and the step of evacuating the water vapor from the collector (S150).
- the water is faster than the hydrogen peroxide because of the higher vapor pressure
- Water is diffused into the gas phase more quickly than hydrogen peroxide because the molecular weight of water is lower than hydrogen peroxide, and therefore, at the same temperature and pressure conditions, water (i.e., moisture) evaporates and diffuses faster than hydrogen peroxide. Since water of evaporates / diffuses before hydrogen peroxide, hydrogen peroxide vapor is condensed in the collector, and water vapor is exhausted from the collector, so that a third concentration of hydrogen peroxide water can be formed.
- the hydrogen peroxide water condensed in the collector may include hydrogen peroxide at a concentration higher than the concentration of the hydrogen peroxide water at the second concentration.
- the hydrogen peroxide vapor and steam passing through the pipe at step S140 is moved in the order of the fifth connection pipe, the first connection pipe, the third connection pipe, the fourth connection pipe, in this case, the smaller inner diameter of these connection pipes
- the temperature of must be higher than the temperature of the collector 140.
- the gaseous hydrogen peroxide vapor and water vapor differ in temperature at which they can condense at the same pressure. For example, at 35 degrees, hydrogen peroxide condenses above 5 mb and water vapor condenses above 55 mb.
- this difference is, for example, when the collector temperature being evacuated through the collecting valve is 35, the hydrogen peroxide vapor is condensed when the pressure is in the range of 5 mb to 55 mb, and the steam can be exhausted from the collector.
- the third concentration of the hydrogen peroxide solution may be 90% by weight to 95% by weight, and step S150 by vaporizing water in 75% by weight to 85% by weight of hydrogen peroxide, 90% by weight to 95% by weight of hydrogen peroxide It may be a second concentration step of hydrogen peroxide solution to form water.
- the hydrogen peroxide vapor in the second concentration of hydrogen peroxide in the step and the second concentration of hydrogen peroxide in the collector of the second temperature and the second pressure of step S140 and condensed in the collector The exhaust gas from the collector is described as being sequentially performed, but, alternatively, the steps S140 and S150 may be performed at the same time.
- the evaporated water is evacuated through the vacuum pump, and thus, in operation S150, the vacuum pump 120 may be operated (on), and the vacuum may be evacuated by opening the vacuum valve 121.
- the collection valve 141 corresponds to an open state.
- the method includes lowering the sterilization chamber to a predetermined pressure and concentrating the third concentration of hydrogen peroxide water to a fourth concentration of hydrogen peroxide water (S160).
- the predetermined pressure should be a set pressure for sterilization in the sterilization chamber, and, if the sterilant is hydrogen peroxide vapor, it should be easy to diffuse vacuum degree.
- the set pressure may be 0.5 to 1.3 mb
- the temperature of the sterilization chamber may be 45 to 55 °C.
- the fourth concentration of the hydrogen peroxide solution may be greater than or equal to 95% by weight, the third concentration of hydrogen peroxide to form more than 95% by weight of hydrogen peroxide by evaporating water in the hydrogen peroxide solution of the concentration of 90% to 95% by weight in step S160 It may be a step.
- the evaporated water is evacuated through the vacuum pump, and thus, in step S160, the vacuum pump 120 may be operated (on) and vacuumed by opening the vacuum valve 121.
- step S160 the collection valve 141 may repeat the open state and the close state.
- hydrogen peroxide evaporates at a pressure of about 20mb or less in 80% by weight hydrogen peroxide solution, but hydrogen peroxide does not evaporate at a pressure of about 11mb or less in 90% by weight hydrogen peroxide solution. Done.
- the high concentration of hydrogen peroxide can continue the decomposition reaction, the water generated during the decomposition will lower the concentration of hydrogen peroxide.
- This water removal method takes a very long time in the low concentration step, but is effective to remove a small amount of water in the high concentration step, it can be said to be effective to maintain at least a high concentration.
- the pressure of the collector 140 containing a third concentration of hydrogen peroxide is continuously lowered to prevent the hydrogen peroxide from evaporating at a lower pressure, the collection
- the valve 141 may prevent the pressure of the collector 140 from continuously lowering by repeating the open state and the close state.
- the pressure of the collector 140 is 5 to 10 mb
- the temperature may be 35 to 40 °C
- the pressure of the vaporizer 130 may be 7 to 10 mb
- the temperature may be 60 to 70 °C.
- step S160 since the aqueous solution of the vaporizer is completely exhausted, the temperature is restored in a vacuum state, and the collector is concentrated with high concentration of hydrogen peroxide, and a small amount of water is removed, or stays in the collector while maintaining an appropriate pressure.
- the collector can then be lowered to a lower temperature by temperature control means to prevent excessive exhaustion of hydrogen peroxide.
- the hydrogen peroxide vapor of the hydrogen peroxide solution of the fourth concentration is put into a sterilization chamber, and the step of sterilizing the object to be treated (S170).
- step S170 in order to inject the hydrogen peroxide vapor of the hydrogen peroxide solution of the fourth concentration located in the collector 140 to the sterilization chamber 110, the vaporization valve 131 is open, the collection valve corresponds to the open or close state. .
- the hydrogen peroxide vapor from the collector 140 to the sterilization chamber 110 may move through the first connection pipe 142 and the second connection pipe 133.
- the first connection pipe 142 connecting the collector 140 and the vaporization valve 131 and the second connection pipe connecting the vaporization valve 131 and the sterilization chamber 110 may have a larger inner diameter than other connection pipes, that is, the third connection pipe 143 to the fifth connection pipe 132, for example, the third connection pipe 143 to the fifth connection pipe 132.
- the first connection pipe 142 and the second connection pipe 133 may be a 1 inch pipe.
- hydrogen peroxide vapor flows into the sterilization chamber 110 from the collector 140 through the first connection pipe 142 and the second connection pipe 133, and the hydrogen peroxide vapor flows into the fifth connection pipe 132.
- hydrogen peroxide vapor may be introduced into the first connection pipe 142 having a relatively large inner diameter, and hydrogen peroxide vapor may not be introduced into the fifth connection pipe 132 having a relatively small inner diameter.
- the hydrogen peroxide vapor is added to the sterilization chamber, the sterilization treatment target, it is preferable that the hydrogen peroxide vapor is added in a state where the temperature of the hydrogen peroxide vapor is not high.
- the sterilization chamber enters the sterilization chamber at a temperature higher than the temperature of the sterilization chamber before the hydrogen peroxide vapor is sufficiently saturated in the sterilization chamber, the density of the hydrogen peroxide vapor in the entry path becomes excessive and easily condensed.
- the gas phase reduces the absolute amount of diffusion into the sterilization chamber and can adversely affect the diffusion effect for sterilization.
- the pipe of the path between the collector 140 and the sterilization chamber 110 may have an inner diameter larger than that of other paths, and the large inner diameter of the pipe means that a large amount of gas is moved. If the inner diameter is large, the gaseous driving force increases by the degree of vacuum as the amount of gas moving increases, thereby preventing the temperature rise of the gaseous hydrogen peroxide vapor.
- the pipe of the path between the collector 140 and the sterilization chamber 110 has a larger inner diameter than the pipe of the other path, so that the temperature of the hydrogen peroxide vapor can be added to the sterilization chamber in accordance with the temperature, Since the decomposition reaction is minimized and the hydrogen peroxide vapor easily accesses the sterilized product through sufficient diffusion into the gas phase, a good sterilization effect can be obtained.
- the hydrogen peroxide vapor of the fourth concentration of hydrogen peroxide into the sterilization chamber hydrogen peroxide is evaporated and diffused into the sterilization chamber, the vaporization of the hydrogen peroxide before the temperature of the collector 140 reaches the temperature of the sterilization chamber
- the temperature increase rate of the collector 140 may be controlled to be completed.
- the collector 140 may be heated by a temperature control means, wherein heating the collector is such that vaporization of hydrogen peroxide before the temperature of the collector reaches the temperature of the sterilization chamber
- the temperature increase rate can be controlled to complete more than 80%.
- the pressure of the sterilization chamber 110 may be 0.5 to 15 mb, the temperature may be 45 to 55 °C.
- the pressure of the collector 140 is 0.5 to 15 mb
- the temperature may be 30 to 70 °C
- the pressure of the vaporizer 130 may be 0.5 to 15 mb
- the temperature may be 60 to 70 °C or more.
- the concentration of the hydrogen peroxide solution in handling the hydrogen peroxide solution is 60% by weight or less. There is a difficulty in using a high concentration of hydrogen peroxide as a sterilizing agent.
- the water is brought into contact with the collector by proceeding with steps S140 and S150 described above. Can reduce the likelihood of doing so.
- the saturated steam pressure of the water according to the collector pressure of the hydrogen peroxide collector and the temperature of the collector, that is, the vaporization / condensation boundary pressure is lowered, so that even if the water contacts the collector, it cannot condense. This can be done.
- the above sterilization apparatus and the sterilization method using the same it is possible to sterilize the object, the above sterilization apparatus and the sterilization method using the same is just one example, in the present invention the configuration of the basic sterilization apparatus and the same It does not limit the sterilization method used.
- the concentration of the hydrogen peroxide solution in handling the hydrogen peroxide solution is 60% by weight or less. There is a difficulty in using a high concentration of hydrogen peroxide as a sterilizing agent.
- the sterilization apparatus is a sterilization chamber; A vacuum pump connected to one side of the sterilization chamber; A vaporizer connected to the other side of the sterilization chamber; And one side is connected to the carburetor, the other side comprises a collector connected to the sterilization chamber.
- the sterilization apparatus is the first humidity sensor 111 and the second humidity sensor 112 located adjacent to the first humidity sensor 111 located in a predetermined region of the sterilization chamber 110. It includes.
- the concentration of hydrogen peroxide in the sterilization chamber 110 is measured through the first humidity sensor 111 and the second humidity sensor 112.
- the sterilization chamber corresponds to the target space for measuring the concentration of hydrogen peroxide
- the target space may be a sterilization chamber as described above, alternatively, may be an operating room or a sterile room requiring aseptic breeding. have.
- the object space may be a chamber or an operating room or a sterile room, but the type of the object space is not limited in the present invention.
- the first humidity sensor 111 is a sensor in which the relative humidity is determined by the amount of water vapor and the amount of hydrogen peroxide, and the second humidity sensor 112 is determined only by the amount of water vapor. Corresponds to the sensor.
- the relative humidity is determined only by the amount of water vapor in the second humidity sensor 112, or the second humidity sensor directly measures the relative humidity with respect to the amount of water vapor, or the second humidity. This includes the case where the sensor measures absolute humidity with respect to the amount of water vapor and converts the absolute humidity into relative humidity.
- the first humidity sensor may be a humidity sensor of a moisture adsorption method, a humidity sensor of a saturation method, or a humidity sensor of an absorption method.
- the moisture sensor of the moisture adsorption method is a capacitance type.
- Humidity sensor, resistance change type humidity sensor, hair hygrometer, carbon film hygrometer, electric hygrometer, color hygrometer, the humidity sensor according to the saturation method may be dew point hygrometer, lithium chloride dew point hygrometer, and also by absorption method
- the humidity sensor may be a volumetric hygrometer, an electrolytic hygrometer, a weight hygrometer.
- the first humidity sensor 111 is a sensor in which the relative humidity is determined by the amount of water vapor and the amount of hydrogen peroxide.
- the principle of measuring the hydrogen peroxide concentration using a sensor for measuring the relative humidity of water such as the first humidity sensor described above
- the VHP (highly concentrated hydrogen peroxide vapor) vapor pressure is measured on the measuring sensor as the principle of measuring the relative humidity of water It is measured by the degree of humidity reduction.
- a capacitive humidity sensor corresponds to a very important principle that the relative dielectric constant of water and hydrogen peroxide can be directly substituted and used.
- the first humidity sensor such as a capacitive humidity sensor
- the relative humidity can be determined by the amount of water vapor and the amount of hydrogen peroxide will be.
- the second humidity sensor 112 is a humidity sensor according to a spectroscopic method
- the humidity sensor according to the spectroscopic method may be a non-dispersive infrared (NDIR) hygrometer or a near infrared hygrometer.
- NDIR non-dispersive infrared
- the relative humidity may be determined by the amount of water vapor and the amount of hydrogen peroxide.
- the spectroscopic second humidity sensor corresponds to a sensor whose relative humidity is determined only by the amount of water vapor.
- the non-dispersive infrared hygrometer is a method of calculating the absorbance of the selective IR of 6.1um, which is an absorption spectrum region of water in the IR region, so that hydrogen peroxide (H 2 O 2 ) having absorption bands of different regions ( 2.93um) corresponds to a hygrometer with a very high selectivity.
- the humidity sensor is a sensor for detecting the humidity in the object, the concept of the humidity is well known relative humidity and absolute humidity.
- absolute humidity is the mass of the actual water vapor contained in 1 liter of air
- relative humidity is the percentage of the actual water vapor contained in the air divided by the maximum amount of water the air can contain at a given temperature and pressure. to be.
- 1 liter of air at 37 ° C at 1 atmosphere can contain as much as 44 grams of steam. If an air with the same pressure and temperature now has 11 grams of steam, the relative humidity is 25% (11 grams / minute). 44 g ⁇ 100).
- such a humidity sensor is well known as a sensor for detecting the amount of water vapor contained in the air.
- the representative types of humidity sensors include a capacitive humidity sensor and a resistance-type humidity sensor.
- the resistance change type humidity sensor uses a characteristic in which the resistance changes according to the moisture content in the moisture sensitive film in response to the humidity change, and obtains a change signal by applying an alternating current to the polymer type and the ceramic type according to the material of the moisture sensitive material. Can be classified.
- the moisture sensitive material is a polymer
- moisture and polymer are combined to form ions in air, and electrical conductivity is generated.
- moisture adsorbed on the porous surface of the moisture sensitive material is used. The pores are separated to form ions, which cause electrical conductivity.
- the concentration of ions is changed according to the change of relative humidity, which is measured by the change of impedance of the sensor element to detect the relative humidity, and the conversion circuit for obtaining the electrical signal from the sensor is simple, which has the advantages of miniaturization and cost. .
- the resistance change type humidity sensor may be formed by sputtering and depositing a platinum (Pt) thin film on the upper surface of the sintered alumina substrate to form a pattern in the shape of an electrode, and applying a moisture-sensitive polymer on the upper surface of the platinum thin film pattern.
- Pt platinum
- the capacitive humidity sensor has a lower electrode on a substrate, the upper electrode having a property to uniformly apply a polymer dampener to the upper portion of the lower electrode, the humidity can be injected into the upper portion of the damper. It is composed.
- Au electrodes and moisture resistant materials are used for glass or ceramic substrates, and the moisture-sensitive material applied to the sensor may be a cellulose ester compound such as cellulose acetone, or a polymer material such as polyvinyl alcohol, polyacryl, or polyvinyl pyride. Used.
- the principle of detecting humidity in the capacitive humidity sensor is as follows.
- the relative dielectric constant of the polymer material is about 3 in a dry state, while the relative dielectric constant is changed while absorbing water molecules (relative dielectric constant 80) in the air, and through the change of the relative dielectric constant, the amount of water vapor in the air is changed. Can be detected.
- the capacitive humidity sensor may include a lower electrode formed on a substrate; A moisture sensitive layer applied on the lower electrode to absorb and desorb moisture; And a plurality of upper electrodes formed on the moisture sensitive layer.
- the humidity sensor that is, the capacitance type humidity sensor and the resistance change type humidity sensor are well known as a sensor for detecting the amount of water vapor contained in the air.
- the Applicant has confirmed that the value detected by the amount of water vapor, as well as the amount of hydrogen peroxide, in the case of the capacitive humidity sensor is changed, and in view of this, the first humidity sensor 111 and the second Through the humidity sensor 112, a method of measuring the concentration of hydrogen peroxide in the interior of the sterilization chamber 110 was developed.
- the detected value is changed not only by the amount of water vapor but also by the amount of hydrogen peroxide.
- Figure 4 is a graph showing the response of the capacitive humidity sensor in the sterilization apparatus.
- the reaction of the capacitive humidity sensor in the process of sterilization in the sterilization apparatus is measured.
- the relative humidity of the capacitive humidity sensor when the temperature of the sterilization chamber is 50 ° C, the value of the pressure inside the sterilization chamber must exceed 120 mb even by the pressure of steam alone. However, in reality, only 12 ⁇ 15mb of the sterilization chamber.
- the capacitance-type humidity sensor can be seen that the relative humidity is determined not only by the amount of water vapor but also by the amount of hydrogen peroxide.
- the relative humidity detected by the capacitive humidity sensor is determined by the amount of water vapor and the amount of hydrogen peroxide.
- the humidity sensor based on the spectroscopic method determines relative humidity only according to the amount of water vapor.
- the relative humidity is determined by the amount of water vapor and the amount of hydrogen peroxide, but in the case of the humidity sensor according to the spectroscopic method that is the second humidity sensor, only the water vapor The relative humidity is determined by the amount.
- the ratio of the relative humidity determined by the amount of hydrogen peroxide can be calculated.
- the relative humidity is determined only by the amount of water vapor in the second humidity sensor 112, or the second humidity sensor directly measures the relative humidity relative to the amount of water vapor
- the second humidity sensor measures an absolute humidity with respect to the amount of water vapor and converts the absolute humidity into a relative humidity.
- the absolute humidity of the target space may be measured through the second humidity sensor, and the absolute humidity may be converted into a relative humidity to detect the second relative humidity of the target space through the second humidity sensor.
- Method for measuring the concentration of hydrogen peroxide according to the present invention is as follows.
- FIG. 5 is a flowchart illustrating a method for measuring hydrogen peroxide concentration according to the present invention.
- the method for measuring hydrogen peroxide concentration according to the present invention includes detecting a first relative humidity by a first humidity sensor (S210).
- the first humidity sensor may typically be a capacitive humidity sensor.
- the capacitive humidity sensor may determine relative humidity according to the amount of water vapor and the amount of hydrogen peroxide. 1 Relative humidity corresponds to relative humidity depending on the amount of water vapor and the amount of hydrogen peroxide.
- the hydrogen peroxide concentration measuring method includes the step of detecting the second relative humidity by the second humidity sensor (S220).
- the second humidity sensor may typically be a non-dispersion infrared humidity sensor, as described above, the non-dispersion infrared humidity sensor is determined relative humidity only by the amount of water vapor, and thus, the second relative humidity is Corresponds to relative humidity depending on the amount of water vapor.
- the method for measuring hydrogen peroxide concentration according to the present invention includes deriving a difference value between the first relative humidity and the second relative humidity (S230).
- the relative humidity is determined by the amount of water vapor and the amount of hydrogen peroxide, but in the case of the second humidity sensor, the relative humidity is determined only by the amount of water vapor.
- the ratio of the relative humidity determined by the amount of hydrogen peroxide can be calculated.
- the hydrogen peroxide concentration measuring method includes the step of calculating the concentration of hydrogen peroxide through the difference value (S240).
- measuring the concentration of hydrogen peroxide vapor in the present invention corresponds to the principle of measuring the ratio of the saturated steam pressure, therefore, when the supersaturated hydrogen peroxide vapor is introduced into the chamber of the sterilization apparatus, etc.
- the temperature of the humidity sensor is present at a temperature lower than the measurement target space, the supersaturated hydrogen peroxide vapor may be condensed on the humidity sensor and measured to be lower than the concentration actually present.
- the temperature of the first humidity sensor and the second humidity sensor is preferably controlled higher than the measurement target space, that is, a chamber, an operating room or a clean room.
- Table 4 shows the saturated steam pressure with temperature.
- Table 4 shows examples of saturated steam pressure and hydrogen peroxide saturated steam pressure according to respective temperatures.
- the first relative humidity detected by the first humidity sensor is 80%
- the second relative humidity detected by the second humidity sensor is 30%.
- the second relative humidity detected by the second humidity sensor is 30%
- the humidity sensor measures absolute humidity with respect to the amount of water vapor and converts the absolute humidity into relative humidity.
- the assumption that the second relative humidity is 30% may be a case where it is converted from the absolute humidity measured by the second humidity sensor.
- the temperature in the sterilization chamber is 45 °C
- the air pressure is 1000mb
- the volume of the sterilization chamber is 1000L.
- the difference between the first relative humidity and the second relative humidity is 50%, and thus, 50%, the difference between the first relative humidity and the second relative humidity, corresponds to the ratio of relative humidity determined by the amount of hydrogen peroxide. do.
- the relative humidity reacted by the hydrogen peroxide vapor in the air in the sterilization chamber corresponds to 50%.
- the saturated steam pressure of hydrogen peroxide at a temperature of 45 °C corresponds to 9.8mb.
- the molecular weight of hydrogen peroxide is 34g / mol, it may be represented by a concentration of 6.4mg / L.
- the hydrogen peroxide concentration can be measured by the first humidity sensor and the second humidity sensor.
- the first humidity sensor and the second humidity sensor are included in a target space such as a sterilization chamber, and the relative humidity is detected by each of these sensors, and the concentration of hydrogen peroxide is determined by the difference in these relative humidity. Can be measured easily.
Landscapes
- Health & Medical Sciences (AREA)
- Epidemiology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
Description
본 발명은 멸균장치 및 상기 멸균장치의 과산화수소 농도 측정방법에 관한 것으로서, 더욱 상세하게는 간단한 방법에 의하여, 과산화수소수에서의 과산화수소의 농도를 정확하게 검출할 수 있는 멸균장치 및 상기 멸균장치의 과산화수소 농도 측정방법에 관한 것이다.The present invention relates to a sterilization apparatus and a method for measuring hydrogen peroxide concentration of the sterilization apparatus, and more particularly, a sterilization apparatus capable of accurately detecting the concentration of hydrogen peroxide in hydrogen peroxide by a simple method and the measurement of hydrogen peroxide concentration of the sterilization apparatus. It is about a method.
의료 기구는 통상 높은 압력 하에서 포화된 수증기를 이용하는 고압 증기 멸균법을 이용하거나, 열에 약한 기구나 재료에 손상을 주지 않는 에틸렌 옥사이드와 같은 화학 물질을 이용하는 에틸렌 옥사이드 가스 멸균법 등에 의해 멸균되고 있다.Medical instruments are usually sterilized by high pressure steam sterilization using saturated steam under high pressure, or by ethylene oxide gas sterilization using chemicals such as ethylene oxide that does not damage heat-affected instruments or materials.
그러나, 고압 증기 멸균기는 120도 이상의 고온으로 멸균을 하기 때문에 최근에 개발되고 있는 합성수지로 만든 의료 기구들은 변형이 발생하게 되고, 스틸로 만들어진 의료 기구들은 섬세한 날이 무뎌져 기존의 수명보다 많이 줄어들게 된다. 특히, 최신 수술기술의 발달로 증가하고 있는 고가의 의료 기기, 기구 및 장치들은 열이나 습기에 민감하여 멸균 재처리 과정에서 손상될 수 있으므로 고압 증기 멸균법은 적합하지 않은 멸균 방법일 수 있다.However, since the high pressure steam sterilizer sterilizes at a high temperature of more than 120 degrees, medical instruments made of synthetic resins that have been recently developed are deformed, and medical instruments made of steel are dulled with fine blades, which are much shorter than the conventional lifespan. . In particular, high-pressure steam sterilization may be an unsuitable sterilization method because expensive medical devices, instruments, and devices that are increasing due to the development of the latest surgical technology may be damaged during sterilization reprocessing because they are sensitive to heat or moisture.
이러한 기기손상을 최소화할 수 있는 에틸렌 옥사이드 가스 멸균기는 저온에서 멸균이 가능하지만 피멸균물에 에틸렌 옥사이드가 잔류하거나 이로 인한 반응 생성물로 인해 발암 및 독성 물질이 생성될 수 있어서 멸균 후 대략 12시간 이상의 환기 시간이 요구된다. 또한, 에틸렌 옥사이드 가스는 그 자체로 폭발 위험성이 높고 돌연변이를 일으킬 수 있는 유전적 독성 물질로 작용할 수 있다는 보고가 있으며 발암물질로 규정하고 있어 그 사용에 많은 주의를 요하게 된다.Although the ethylene oxide gas sterilizer can minimize the damage to the device, it can be sterilized at low temperature, but the ethylene oxide remains in the sterilized product or the reaction product may cause carcinogenic and toxic substances to be generated. Time is required. In addition, ethylene oxide gas itself is a high explosion risk, it has been reported that it can act as a genetic toxic substance that can cause mutations, and it is prescribed as a carcinogen, which requires much attention to its use.
반면, 과산화수소 증기를 사용한 멸균법은 40~50도의 온도에서 30~60분 내의 짧은 멸균 시간과 인체나 환경에 무해하도록 멸균 후 대기에 배출되는 물질이 물과 산소이므로 고압 증기 멸균기의 단점과 에틸렌 옥사이드 가스 멸균기의 다양한 단점을 보완할 수 있다. On the other hand, the sterilization method using hydrogen peroxide steam is a short sterilization time within 30 to 60 minutes at a temperature of 40 to 50 degrees, and the substances discharged to the atmosphere after sterilization are harmless to humans or the environment, so the disadvantages of the high pressure steam sterilizer and ethylene oxide gas Various disadvantages of the sterilizer can be compensated for.
그러나, 과산화수소 증기를 생성시키기 위해 사용되는 과산화수소 수용액은 기화과정에서 과산화수소 보다 물이 먼저 기화 확산하여 과산화수소의 충분한 확산을 곤란하게 한다. 물은 과산화수소보다 증기압이 높기 때문에 보다 신속하게 증발되고, 물의 분자량은 과산화수소보다 낮기 때문에 수증기가 과산화수소 증기보다 신속하게 기상으로 확산되기 때문이다.However, the hydrogen peroxide aqueous solution used to generate the hydrogen peroxide vapor makes it difficult to sufficiently diffuse hydrogen peroxide by evaporating and diffusing water before hydrogen peroxide during the vaporization process. This is because water is evaporated more quickly because of the higher vapor pressure than hydrogen peroxide, and because the molecular weight of water is lower than hydrogen peroxide, water vapor diffuses more rapidly into the gas phase than hydrogen peroxide vapor.
이러한 특성 때문에 과산화수소 수용액이 멸균시키고자 하는 제품을 둘러싸고 있는 공간 속에서 증발되는 경우, 물이 과산화수소보다 먼저 높은 농도로 멸균시키고자 하는 제품에 도달하게 된다. Because of this property, when the aqueous hydrogen peroxide solution is evaporated in the space surrounding the product to be sterilized, the water reaches the product to be sterilized at a higher concentration than the hydrogen peroxide.
수증기는 보다 신속하게 작은 틈(crevice)이나 길고 좁은 루멘과 같은 확산 제한 공간 속으로 신속하게 확산되어 과산화수소 증기의 투과를 억제한다. 즉, 물이 과산화수소보다 먼저 피멸균 제품에 도달하게 되어 멸균이 제대로 이루어지지 않게 된다.Water vapor diffuses more quickly into diffusion-limiting spaces, such as smaller crevices or long narrow lumens, to suppress the permeation of hydrogen peroxide vapor. In other words, water reaches the sterilized product before hydrogen peroxide, so that sterilization is not performed properly.
효과적인 멸균을 위해서는 보다 농축된 과산화수소 수용액을 사용하는 것이 바람직하지만, 과산화수소 수용액의 농도가 60중량% 이상인 경우에는 운송, 보관 등 취급하는 것이 현실적으로 곤란하다.In order to effectively sterilize, it is preferable to use a more concentrated aqueous hydrogen peroxide solution, but when the concentration of the aqueous hydrogen peroxide solution is 60% by weight or more, it is practically difficult to handle such as transportation and storage.
이러한 이유로, 취급이 가능한 농도가 60중량% 이하인 과산화수소 수용액을 각 단계별 농축과정을 통하여, 예를 들면, 95중량% 이상의 고농도의 과산화수소수로 농축하여 멸균제로 사용하는 것이 일반적이며, 이를 통해 멸균장치의 멸균효과를 향상시킬 수 있다.For this reason, it is common to use a hydrogen peroxide aqueous solution having a handleable concentration of 60 wt% or less through each step of concentration, for example, to a high concentration of hydrogen peroxide solution of 95 wt% or more and use it as a sterilizing agent. It can improve sterilization effect.
이때, 상기 과산화수소수를 고농도의 과산화수소수로 농축하여 멸균제로 사용함에 있어서, 멸균장치의 멸균챔버 내에서 상기 과산화수소의 농도를 측정하는 것은 용이하지 않다.At this time, in concentrating the hydrogen peroxide water to a high concentration of hydrogen peroxide water to use as a sterilizing agent, it is not easy to measure the concentration of hydrogen peroxide in the sterilization chamber of the sterilization apparatus.
특히, 고농도의 과산화수소 가스는 용이하게 응축이 발생하기 때문에, 직접 농도를 측정하는 수단은 일반적이지 않고, 통상은 흡수병법에 의해 가스 농도를 측정하고 있다.In particular, since a high concentration of hydrogen peroxide gas easily condenses, a means for directly measuring the concentration is not common, and the gas concentration is usually measured by an absorption bottle method.
그러나 이 경우, 단시간의 가스 농도 변화를 파악하는 것이나 연속적으로 가스 농도를 감시하는 수단이 될 수 없다고 하는 문제가 있었다. In this case, however, there has been a problem that it is not possible to grasp the gas concentration change in a short time or to be a means for continuously monitoring the gas concentration.
또한, 많은 경우, 살균 장치의 가스 품질을 연속 감시하는 수단으로서는 가스를 생성하기 위한 열풍과 과산화수소수의 공급 상태(온도, 양 , 압력 등)를 복합적으로 감시해, 가스 품질의 양부 판정을 하는 것이 일반적이나, 이러한 방법 역시 복잡하고 신뢰성이 부족한 실정이다.In many cases, as a means of continuously monitoring the gas quality of the sterilizing apparatus, it is necessary to monitor the supply status (temperature, quantity, pressure, etc.) of the hot air for generating gas and the hydrogen peroxide water in combination, and to judge the quality of the gas. In general, however, these methods are also complex and lack reliability.
본 발명이 해결하고자 하는 과제는 본 발명은 상기와 같은 문제점을 해결하기 위하여 개발된 것으로서, 멸균장치의 대형화나 복잡화를 지양하고 간단한 방법에 의하여, 과산화수소수에서의 과산화수소의 농도를 정확하게 검출할 수 있는 멸균장치 및 상기 멸균장치의 과산화수소 농도 측정방법을 제공하는 데 있다.The problem to be solved by the present invention is that the present invention was developed in order to solve the above problems, it is possible to accurately detect the concentration of hydrogen peroxide in the hydrogen peroxide by a simple method, avoiding the enlargement or complexity of the sterilization apparatus It is to provide a sterilization apparatus and a method for measuring the hydrogen peroxide concentration of the sterilization apparatus.
본 발명의 목적들은 이상에서 언급한 목적으로 제한되지 않으며, 언급되지 않은 또 다른 목적들은 아래의 기재로부터 당업자에게 명확하게 이해될 수 있을 것이다.The objects of the present invention are not limited to the above-mentioned objects, and other objects which are not mentioned will be clearly understood by those skilled in the art from the following description.
상기 지적된 문제점을 해결하기 위해서 본 발명은 멸균챔버를 포함하는 멸균장치에 있어서, 상기 멸균챔버는, 내부 일정 영역에 위치하는 제1습도센서 및 상기 제1습도센서와 인접하여 위치하는 제2습도센서를 포함하고, 상기 제1습도센서는 과산화수소수의 양 및 수증기의 양에 의해 제1상대습도를 검출하고, 상기 제2습도센서는 수증기의 양에 의해 제2상대습도를 검출하는 멸균장치를 제공한다.In order to solve the above-mentioned problems, the present invention is a sterilization apparatus including a sterilization chamber, the sterilization chamber, the first humidity sensor and a second humidity located adjacent to the first humidity sensor located in a predetermined region inside And a sensor, wherein the first humidity sensor detects the first relative humidity by the amount of hydrogen peroxide and the amount of water vapor, and the second humidity sensor detects the second relative humidity by the amount of water vapor. to provide.
또한, 본 발명은 상기 제1습도센서는, 수분흡착 방식의 습도센서, 포화방식에 의한 습도센서 또는 흡수 방식에 의한 습도센서이고, 상기 제2습도센서는 분광학적 방식에 의한 습도센서인 것을 특징으로 하는 멸균장치를 제공한다.In addition, the present invention is characterized in that the first humidity sensor is a humidity sensor of a moisture absorption method, a humidity sensor of a saturation method or a humidity sensor of an absorption method, and the second humidity sensor is a humidity sensor of a spectroscopic method. It provides a sterilization apparatus.
또한, 본 발명은 상기 제1습도센서에 의해 검출된 상기 제1상대습도와 상기 제2습도센서에 의해 검출된 제2상대습도의 차이를 계산하여, 상기 과산화수소의 농도를 계산하는 멸균장치를 제공한다.The present invention also provides a sterilization apparatus for calculating the concentration of the hydrogen peroxide by calculating a difference between the first relative humidity detected by the first humidity sensor and the second relative humidity detected by the second humidity sensor. do.
또한, 본 발명은 제1습도센서에 의해 제1상대습도를 검출하는 단계; 제2습도센서에 의해 제2상대습도를 검출하는 단계; 상기 제1상대습도와 상기 제2상대습도의 차이값을 도출하는 단계; 및 상기 차이값을 통해 과산화수소의 농도를 계산하는 단계를 포함하는 과산화수소 농도 측정방법을 제공한다.In addition, the present invention comprises the steps of detecting the first relative humidity by the first humidity sensor; Detecting a second relative humidity by a second humidity sensor; Deriving a difference value between the first relative humidity and the second relative humidity; And it provides a hydrogen peroxide concentration measuring method comprising the step of calculating the concentration of hydrogen peroxide through the difference value.
또한, 본 발명은 상기 제1습도센서는 수증기의 양 및 과산화수소의 양에 의해 상대습도가 결정되고, 상기 제2습도센서는 수증기의 양에 따라 상대습도가 결정되는 과산화수소 농도 측정방법을 제공한다.The present invention also provides a method for measuring hydrogen peroxide concentration in which the first humidity sensor determines relative humidity by the amount of water vapor and the amount of hydrogen peroxide, and the second humidity sensor determines the relative humidity by the amount of water vapor.
또한, 본 발명은 상기 제1습도센서는, 수분흡착 방식의 습도센서, 포화방식에 의한 습도센서 또는 흡수 방식에 의한 습도센서이고, 상기 제2습도센서는 분광학적 방식에 의한 습도센서인 것을 특징으로 하는 과산화수소 농도 측정방법을 제공한다.In addition, the present invention is characterized in that the first humidity sensor is a humidity sensor of a moisture absorption method, a humidity sensor of a saturation method or a humidity sensor of an absorption method, and the second humidity sensor is a humidity sensor of a spectroscopic method. It provides a method for measuring the hydrogen peroxide concentration.
또한, 본 발명은 과산화수소의 농도를 측정하기 위한 대상공간에 있어서, 상기 대상 공간은, 내부 일정 영역에 위치하는 제1습도센서 및 상기 제1습도센서와 인접하여 위치하는 제2습도센서를 포함하고, 상기 제1습도센서는 과산화수소수의 양 및 수증기의 양에 의해 제1상대습도를 검출하고, 상기 제2습도센서는 수증기의 양에 의해 제2상대습도를 검출하는 대상공간을 제공한다.In addition, the present invention is a target space for measuring the concentration of hydrogen peroxide, wherein the target space includes a first humidity sensor located in a predetermined internal area and a second humidity sensor located adjacent to the first humidity sensor; The first humidity sensor detects a first relative humidity by the amount of hydrogen peroxide and the amount of water vapor, and the second humidity sensor provides a target space for detecting the second relative humidity by the amount of water vapor.
또한, 본 발명은 상기 제1습도센서는, 수분흡착 방식의 습도센서, 포화방식에 의한 습도센서 또는 흡수 방식에 의한 습도센서이고, 상기 제2습도센서는 분광학적 방식에 의한 습도센서인 것을 특징으로 하는 대상공간을 제공한다.In addition, the present invention is characterized in that the first humidity sensor is a humidity sensor of a moisture absorption method, a humidity sensor of a saturation method or a humidity sensor of an absorption method, and the second humidity sensor is a humidity sensor of a spectroscopic method. Provide the target space.
또한, 본 발명은 상기 제1습도센서 및 상기 제2습도센서의 온도는 상기 대상 공간의 온도보다 높게 제어되는 것을 특징으로 하는 대상공간을 제공한다.In addition, the present invention provides a target space, characterized in that the temperature of the first humidity sensor and the second humidity sensor is controlled higher than the temperature of the target space.
(발명의 효과)(Effects of the Invention)
상기한 바와 같은 본 발명에 따르면, 멸균챔버 내에, 제1습도센서 및 제2습도센서를 포함시켜, 이들 각각의 센서들에 의해 상대습도를 검출하고, 이들 상대습도의 차이에 의해 과산화수소의 농도를 용이하게 측정할 수 있다.According to the present invention as described above, in the sterilization chamber, by including a first humidity sensor and a second humidity sensor, the relative humidity is detected by each of these sensors, the concentration of hydrogen peroxide by the difference in these relative humidity It can be measured easily.
도 1은 본 발명에 따른 멸균제 수용액을 이용한 멸균장치를 도시한 개략적인 사시도이며, 도 2는 본 발명에 따른 멸균제 수용액을 이용한 멸균장치를 도시한 개략적인 구성도이다.1 is a schematic perspective view showing a sterilizer using an aqueous solution of a sterilant according to the present invention, Figure 2 is a schematic configuration diagram showing a sterilizer using an aqueous solution of a sterilant according to the present invention.
도 3은 본 발명에 따른 멸균제 수용액을 이용한 멸균장치의 멸균방법을 도시한 순서도이다.Figure 3 is a flow chart illustrating a sterilization method of the sterilization apparatus using a sterilant aqueous solution according to the present invention.
도 4는 멸균장치에서의 정전용량형 습도센서의 반응을 도시한 그래프이다.Figure 4 is a graph showing the response of the capacitive humidity sensor in the sterilization apparatus.
도 5는 본 발명에 따른 과산화수소 농도 측정 방법을 설명하기 위한 순서도이다.5 is a flowchart illustrating a method for measuring hydrogen peroxide concentration according to the present invention.
본 발명의 이점 및 특징, 그리고 그것들을 달성하는 방법은 첨부되는 도면과 함께 상세하게 후술되어 있는 실시예들을 참조하면 명확해질 것이다. 그러나 본 발명은 이하에서 개시되는 실시예들에 한정되는 것이 아니라 서로 다른 다양한 형태로 구현될 것이며, 단지 본 실시예들은 본 발명의 개시가 완전하도록 하며, 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자에게 발명의 범주를 완전하게 알려주기 위해 제공되는 것이며, 본 발명은 청구항의 범주에 의해 정의될 뿐이다.Advantages and features of the present invention and methods for achieving them will be apparent with reference to the embodiments described below in detail with the accompanying drawings. However, the present invention is not limited to the embodiments disclosed below, but will be implemented in various forms, and only the present embodiments are intended to complete the disclosure of the present invention, and the general knowledge in the art to which the present invention pertains. It is provided to fully convey the scope of the invention to those skilled in the art, and the present invention is defined only by the scope of the claims.
아래 첨부된 도면을 참조하여 본 발명의 실시를 위한 구체적인 내용을 상세히 설명한다. 도면에 관계없이 동일한 부재번호는 동일한 구성요소를 지칭하며, "및/또는"은 언급된 아이템들의 각각 및 하나 이상의 모든 조합을 포함한다.DETAILED DESCRIPTION Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. Regardless of the drawings, the same reference numbers refer to the same components, and “and / or” includes each and every combination of one or more of the items mentioned.
비록 제1, 제2 등이 다양한 구성요소들을 서술하기 위해서 사용되나, 이들 구성요소들은 이들 용어에 의해 제한되지 않음은 물론이다. 이들 용어들은 단지 하나의 구성요소를 다른 구성요소와 구별하기 위하여 사용하는 것이다. 따라서, 이하에서 언급되는 제1 구성요소는 본 발명의 기술적 사상 내에서 제2 구성요소일 수도 있음은 물론이다.Although the first, second, etc. are used to describe various components, these components are of course not limited by these terms. These terms are only used to distinguish one component from another. Therefore, of course, the first component mentioned below may be a second component within the technical spirit of the present invention.
본 명세서에서 사용된 용어는 실시예들을 설명하기 위한 것이며 본 발명을 제한하고자 하는 것은 아니다. 본 명세서에서, 단수형은 문구에서 특별히 언급하지 않는 한 복수형도 포함한다. 명세서에서 사용되는 "포함한다(comprises)" 및/또는 "포함하는(comprising)"은 언급된 구성요소 외에 하나 이상의 다른 구성요소의 존재 또는 추가를 배제하지 않는다.The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. In this specification, the singular also includes the plural unless specifically stated otherwise in the phrase. As used herein, "comprises" and / or "comprising" does not exclude the presence or addition of one or more other components in addition to the mentioned components.
다른 정의가 없다면, 본 명세서에서 사용되는 모든 용어(기술 및 과학적 용어를 포함)는 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자에게 공통적으로 이해될 수 있는 의미로 사용될 수 있을 것이다. 또 일반적으로 사용되는 사전에 정의되어 있는 용어들은 명백하게 특별히 정의되어 있지 않는 한 이상적으로 또는 과도하게 해석되지 않는다.Unless otherwise defined, all terms (including technical and scientific terms) used in the present specification may be used in a sense that can be commonly understood by those skilled in the art. In addition, the terms defined in the commonly used dictionaries are not ideally or excessively interpreted unless they are specifically defined clearly.
공간적으로 상대적인 용어인 "아래(below)", "아래(beneath)", "하부(lower)", "위(above)", "상부(upper)" 등은 도면에 도시되어 있는 바와 같이 하나의 구성 요소와 다른 구성 요소들과의 상관관계를 용이하게 기술하기 위해 사용될 수 있다. 공간적으로 상대적인 용어는 도면에 도시되어 있는 방향에 더하여 사용시 또는 동작시 구성요소들의 서로 다른 방향을 포함하는 용어로 이해되어야 한다. 예를 들면, 도면에 도시되어 있는 구성요소를 뒤집을 경우, 다른 구성요소의 "아래(below)" 또는 "아래(beneath)"로 기술된 구성요소는 다른 구성요소의 "위(above)"에 놓여질 수 있다. 따라서, 예시적인 용어인 "아래"는 아래와 위의 방향을 모두 포함할 수 있다. 구성요소는 다른 방향으로도 배향될 수 있고, 이에 따라 공간적으로 상대적인 용어들은 배향에 따라 해석될 수 있다. The spatially relative terms " below ", " beneath ", " lower ", " above ", " upper " It can be used to easily describe a component's correlation with other components. Spatially relative terms are to be understood as including terms in different directions of components in use or operation in addition to the directions shown in the figures. For example, when flipping a component shown in the drawing, a component described as "below" or "beneath" of another component may be placed "above" the other component. Can be. Thus, the exemplary term "below" can encompass both an orientation of above and below. The components can be oriented in other directions as well, so that spatially relative terms can be interpreted according to the orientation.
이하, 첨부된 도면을 참조하여 본 발명의 바람직한 실시예를 상세히 설명하기로 한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명에 따른 멸균제 수용액을 이용한 멸균장치를 도시한 개략적인 사시도이며, 도 2는 본 발명에 따른 멸균제 수용액을 이용한 멸균장치를 도시한 개략적인 구성도이다.1 is a schematic perspective view showing a sterilizer using an aqueous solution of a sterilant according to the present invention, Figure 2 is a schematic configuration diagram showing a sterilizer using an aqueous solution of a sterilant according to the present invention.
다만, 본 발명에서 상기 멸균제는 과산화수소일 수 있고, 상기 멸균제 수용액은 과산화수소수일 수 있으며, 이하에서는 설명의 편의를 위하여, 멸균제는 과산화수소로, 멸균제 수용액은 과산화수소수로 대응시켜 설명하기로 한다.However, in the present invention, the sterilizing agent may be hydrogen peroxide, the sterilizing agent aqueous solution may be hydrogen peroxide, and for the sake of convenience of explanation, the sterilizing agent is hydrogen peroxide, and the sterilizing agent aqueous solution will be described in correspondence with hydrogen peroxide. do.
도 1 및 도 2를 참조하면, 본 발명에 따른 과산화수소수를 이용한 멸균장치(100)는 멸균챔버(110)를 포함한다.1 and 2, the
상기 멸균챔버(110)는 멸균시키고자 하는 의료 기구나 수술용 도구와 같은 피멸균물을 넣을 수 있는 용기를 나타낸다. 이때, 상기 멸균챔버(110)의 일측에는 상기 피멸균물의 출입을 위한 도어를 포함할 수 있다.The
또한, 상기 멸균챔버(110)의 일측에 연결되는 진공펌프(120)을 포함하며, 상기 진공펌프(120)는 상기 멸균챔버(110) 내부의 기체를 뽑아내어 진공 상태를 형성시킬 수 있다. 이때, 상기 멸균챔버(110)와 상기 진공펌프(120)의 사이에는 상기 진공펌프(120)의 동작을 제어할 수 있는 진공밸브(121)가 연결되어 있다.In addition, it includes a
계속해서 도 1 및 도 2를 참조하면, 본 발명에 따른 과산화수소수를 이용한 멸균장치(100)는 상기 멸균챔버(110)의 다른 일측에 연결되어, 상기 멸균챔버(110)에 과산화수소 증기를 공급하기 위한 기화기(130)(또는, 증발기로 명칭될 수 있음) 및 상기 기화기(130)에 과산화수소를 공급하기 위한 과산화수소 공급장치(150)를 포함한다.1 and 2, the
이때, 상기 멸균챔버(110)와 상기 기화기(130)의 사이에는 기화밸브(131)를 포함할 수 있다.At this time, between the
또한, 본 발명의 제1실시예에 따른 과산화수소수를 이용한 멸균장치(100)는 일측은 상기 기화기(130)과 연결되고, 타측은 상기 멸균챔버(110)와 연결되어, 상기 기화기(130)에 공급된 과산화수소를 농축시키기 위한 수집기(140)(또는, 수집기화기로 명칭될 수 있음)를 포함한다.In addition, the
이때, 상기 멸균챔버(110)와 상기 수집기(140)의 사이에는 기화밸브(131)를 포함할 수 있다.At this time, between the
또한, 상기 멸균챔버(110)와 상기 수집기(140)의 사이에는 수집밸브(141)를 포함할 수 있다.In addition, between the
즉, 상기 멸균챔버(110)와 상기 수집기(140)의 사이에는 기화밸브(131)와 수집밸브(141)가 병렬로 연결될 수 있다.That is, the
한편, 상술한 바와 같이, 상기 멸균챔버(110)와 상기 기화기(130)의 사이에는 기화밸브(131)를 포함할 수 있으며, 즉, 상기 기화밸브(130)는 일측은 멸균 챔버(110)와 연결되고, 타측은 기화기(130) 및 수집기(140)와 병렬 연결될 수 있다.On the other hand, as described above, between the
계속해서 도 1 및 도 2를 참조하면, 본 발명에 따른 과산화수소수를 이용한 멸균장치(100)는 상기 수집기(140)와 상기 기화밸브(131)를 연결하는 제1연결배관(142) 및 상기 기화밸브(131)와 상기 멸균챔버(110)를 연결하는 제2연결배관(133)을 포함할 수 있다.1 and 2, the
또한, 상기 수집기(140)와 상기 수집밸브(141)를 연결하는 제3연결배관(143) 및 상기 수집밸브(141)와 상기 멸균챔버(110)를 연결하는 제4연결배관(144)를 포함할 수 있다.In addition, a third connecting
이때, 도면에서는 상기 제4연결배관(144)이 상기 제2연결배관(133)과 연결되어, 멸균챔버(110)와 수집기(140)의 사이에서 기화밸브(131)와 수집밸브(141)가 병렬로 연결되는 것을 도시하고 있으나, 이와는 달리, 상기 제4연결배관(144)는 상기 멸균챔버(110)와 직접 연결되어, 멸균챔버(110)와 수집기(140)의 사이에서 기화밸브(131)와 수집밸브(141)가 병렬로 연결될 수 있다.In this case, in the drawing, the
또한, 상기 기화기(130)와 상기 기화밸브(131)를 연결하는 제5연결배관(132)을 포함할 수 있으며, 이때, 도면에서는 상기 제5연결배관(132)이 상기 제1연결배관(142)과 연결되어, 기화밸브(130)가 기화기(130) 및 수집기(140)와 병렬 연결되는 것을 도시하고 있으나, 이와는 달리, 상기 제5연결배관(132)이 상기 기화밸브(131)와 직접 연결되어, 기화밸브(130)가 기화기(130) 및 수집기(140)와 병렬 연결될 수 있다.In addition, the
이때, 상기 기화밸브(131) 및 상기 수집밸브(141)는 open/close 동작에 의해 상기 제1연결배관(142) 내지 상기 제5연결배관(132)의 유체의 흐름을 제어할 수 있으며, 또한, 상기 기화밸브(131) 및 상기 수집밸브(141)는 별도의 제어부에 의해 open/close 동작이 제어될 수 있다.At this time, the
또한, 도면에 도시된 바와 같이, 수집기(140)와 기화밸브(131)를 연결하는 제1연결배관(142) 및 기화밸브(131)와 멸균챔버(110)를 연결하는 제2연결배관(133)은 다른 연결배관, 즉, 제3연결배관(143) 내지 제5연결배관(132)보다 내경이 클 수 있으며, 예를 들어, 제3연결배관(143) 내지 제5연결배관(132)이 1/4 inch 배관인 경우, 상기 제1연결배관(142) 및 제2연결배관(133)은 1 inch 배관일 수 있다. 이에 대해서는 후술하기로 한다.In addition, as shown in the figure, the
한편, 도면에는 도시하지 않았으나, 상기 멸균챔버(110), 기화기(130) 및 수집기(140)의 온도를 제어하기 위한 온도제어수단을 포함할 수 있고, 상기 온도제어수단은 히터일 수 있으며, 이는 당업계에서 자명한 사항이므로, 이에 대한 구체적인 설명은 생략하기로 한다.On the other hand, although not shown in the figure, it may include a temperature control means for controlling the temperature of the
또한, 상기 수집기(140)의 경우, 온도제어수단으로 냉각수단을 더 포함할 수 있으며, 상기 냉각수단은 냉각수나 열전소자를 이용한 직접 냉각 또는 열교환기의 송풍을 통한 공냉식 등 적절한 수단을 사용할 수 있다.In addition, the
이하에서는, 본 발명에 따른 멸균장치를 이용한 멸균방법에 대해 설명하기로 한다.Hereinafter, a sterilization method using a sterilization apparatus according to the present invention will be described.
도 3은 본 발명에 따른 멸균제 수용액을 이용한 멸균장치의 멸균방법을 도시한 순서도이다.Figure 3 is a flow chart illustrating a sterilization method of the sterilization apparatus using a sterilant aqueous solution according to the present invention.
다만, 본 발명에서 상기 멸균제는 과산화수소일 수 있고, 상기 멸균제 수용액은 과산화수소수일 수 있으며, 이하에서는 설명의 편의를 위하여, 멸균제는 과산화수소로, 멸균제 수용액은 과산화수소수로 대응시켜 설명하기로 한다.However, in the present invention, the sterilizing agent may be hydrogen peroxide, the sterilizing agent aqueous solution may be hydrogen peroxide, and for the sake of convenience of explanation, the sterilizing agent is hydrogen peroxide, and the sterilizing agent aqueous solution will be described in correspondence with hydrogen peroxide. do.
한편, 이하에서 설명하는 멸균방법은 상술한 도 1 및 도 2의 멸균장치의 도면부호를 병기하여 설명하기로 한다.On the other hand, the sterilization method described below will be described with reference to the reference numerals of the sterilization apparatus of FIGS. 1 and 2 described above.
도 3을 참조하면, 본 발명에 따른 과산화수소수를 이용한 멸균장치의 멸균방법은 멸균챔버(110)(또는, 살균챔버로 명칭될 수 있음) 및 기화기(130)를 진공배기하는 단계를 포함한다(S110).Referring to Figure 3, the sterilization method of the sterilization apparatus using hydrogen peroxide according to the present invention includes the step of evacuating the sterilization chamber 110 (or, may be named sterilization chamber) and the vaporizer 130 ( S110).
상기 멸균챔버(110) 및 상기 기화기(130)를 진공배기하는 단계는, 상기 진공펌프(120)를 작동(on 상태)시키고, 상기 진공밸브(121)를 open 시킴으로써 진공배기할 수 있다.Evacuating the
한편, S110 단계, 즉, 멸균챔버 및 기화기를 진공배기하는 단계는 후술하는 S160 단계까지 지속될 수 있으며, 멸균챔버가 소정의 설정압력에 도달되고, 수분이 제거된 과산화수소 액체가 수집기에 수집이 완료되면 본 단계는 완료될 수 있다.On the other hand, step S110, that is, the step of evacuating the sterilization chamber and the vaporizer may be continued until step S160 to be described later, when the sterilization chamber reaches a predetermined set pressure, and the hydrogen peroxide liquid from which the water is removed is collected in the collector This step can be completed.
또한, 상기 기화기(130)를 진공배기하기 위하여, 상기 멸균챔버(110)와 상기 기화기(130)의 사이의 기화밸브(131), 또는 상기 멸균챔버(110)와 상기 수집기(140)의 사이의 수집밸브(141)는 open 상태로, 진공배기 중인 멸균챔버와 연통되어 대기압 이하의 압력이 되도록 하고 다음 단계에서 닫힌다.In addition, in order to evacuate the
한편, 상기 멸균챔버(110) 및 상기 기화기(130)를 진공배기하는 단계와 동시에, 상기 멸균챔버 및 상기 기화기를 상술한 온도제어수단에 의해 설정된 온도로 유지될 수 있다.On the other hand, at the same time as the step of evacuating the
다음으로, 제1온도 및 제1압력의 기화기(130)에 제1농도의 과산화수소수를 투입하는 단계를 포함한다(S120).Next, a step of injecting hydrogen peroxide water of the first concentration into the
상기 과산화수소수를 투입시키는 것은 제1농도의 과산화수소수를 저장하는 과산화수소 공급장치(150)를 통해 투입될 수 있으며, 한편, 도 1 및 도 2에는 도시하지 않았으나, 상기 기화기(130) 및 상기 과산화수소 공급장치(150)의 사이에 과산화수소수 공급조절 밸브(미도시)를 포함하여, 적절한 양의 과산화수소수를 공급할 수 있다.The hydrogen peroxide solution may be introduced through a hydrogen
이때, 상기 과산화수소수의 제1농도는 60중량% 이하일 수 있다. In this case, the first concentration of the hydrogen peroxide solution may be 60% by weight or less.
상술한 바와 같이, 과산화수소 용액, 즉, 과산화수소수를 취급하는 데 있어서 과산화수소수의 농도가 60중량% 이하로 제한되어 있어서 그 이상의 높은 농도의 과산화수소를 멸균제로 쓰는 것은 현실적으로 어려운 일이다.As described above, the concentration of hydrogen peroxide is limited to 60% by weight or less in the handling of hydrogen peroxide solution, i.e., hydrogen peroxide water, so it is practically difficult to use a higher concentration of hydrogen peroxide as a sterilant.
즉, 본 발명에서 상기 과산화수소수의 제1농도는 취급이 가능한 과산화수소수의 농도를 표시한 것으로, 본 발명의 취지를 이해하는데 있어서, 중요한 의미를 가지지 않는다.That is, in the present invention, the first concentration of the hydrogen peroxide water indicates the concentration of the hydrogen peroxide water that can be handled and does not have an important meaning in understanding the meaning of the present invention.
또한, 상기 제1온도는 60 내지 70℃일 수 있으며, 상기 제1압력은 800 mb(미리바) 내지 대기압일 수 있다.In addition, the first temperature may be 60 to 70 ℃, the first pressure may be 800 mb (pre-bar) to atmospheric pressure.
이때, S120 단계에서는 제1농도의 과산화수소수가 상기 기화기(130)에 투입되는 동안, 상기 기화밸브(131) 및 상기 수집밸브(141)는 close 상태에 해당할 수 있으며, 다만, 공급장치에 따라 open 상태 일 수 있다.At this time, in step S120, while the hydrogen peroxide water of the first concentration is introduced into the
한편, S120 단계에서 상기 멸균챔버(110)의 압력은 600 mb 내지 대기압이고, 온도는 45 내지 55℃일 수 있으며, 또한, 상기 수집기(140)의 압력은 800 mb 내지 대기압이고, 온도는 38 내지 42℃일 수 있다.On the other hand, in step S120 the pressure of the
이때, 본 발명에서 상기 제1온도는 상기 멸균챔버의 온도보다 높은 것을 특징으로 한다.At this time, the first temperature in the present invention is characterized in that higher than the temperature of the sterilization chamber.
상기 제1온도의 경우, 과산화수소수로부터 수증기를 더 많이 기화시키는 과정에서 기화기의 온도에 해당하며, 수증기의 기화과정은 매우 강한 흡열 반응이 일어나서 기화 속도를 매우 강하게 억제하게 된다.In the case of the first temperature, it corresponds to the temperature of the vaporizer in the process of vaporizing more water vapor from the hydrogen peroxide water, the vaporization process of the water vapor very strong endothermic reaction occurs to suppress the vaporization rate very strongly.
이때, 기화속도를 높이려면 기화기의 압력을 낮추어 진공도를 높이는 방법도 있지만, 과산화수소의 기화비율도 높아질 수 있게 되어 과산화수소의 소모가 증가하게 되는 단점이 있고, 또한 온도가 낮은 상태에서는 기화에 필요한 열량이 원할하게 공급되기 어렵기 때문에, 따라서, 제1온도는 적어도 멸균챔버의 온도보다 높은 것이 바람직하다.At this time, in order to increase the vaporization rate, there is also a method of increasing the vacuum degree by lowering the pressure of the vaporizer, but there is a disadvantage that the vaporization rate of hydrogen peroxide can be increased, and the consumption of hydrogen peroxide increases, and the amount of heat required for vaporization in a low temperature state Since it is difficult to supply smoothly, therefore, it is preferable that the first temperature is at least higher than the temperature of the sterilization chamber.
다음으로, 상기 제1농도의 과산화수소수를 기화시켜 제2농도의 과산화수소수를 형성하는 단계를 포함한다(S130).Next, the step of vaporizing the hydrogen peroxide water of the first concentration to form a hydrogen peroxide water of a second concentration (S130).
즉, 상기 기화기(130)에 투입된 제1농도의 과산화수소수가 기화(즉, 수분제거)되어 제2농도의 과산화수소수가 형성된다.That is, the hydrogen peroxide water of the first concentration injected into the
상기 과산화수소수의 제2농도는 75중량% 내지 85중량%일 수 있으며, S130 단계는 60중량% 이하의 과산화수소수 중 수분을 기화시킴으로써, 75중량% 내지 85중량% 농도의 과산화수소수를 형성하는 과산화수소수 제1농축 단계일 수 있다.The second concentration of the hydrogen peroxide solution may be 75% by weight to 85% by weight, and step S130 may be performed by vaporizing water in 60% by weight or less of hydrogen peroxide, thereby forming hydrogen peroxide water at a concentration of 75% by weight to 85% by weight. It may be a first concentration step.
일반적으로, 동일한 온도와 압력에서, 물은 과산화수소보다 증기압이 높기 때문에 보다 신속하게 증발되고, 물의 분자량은 과산화수소보다 낮기 때문에 물이 과산화수소보다 신속하게 기상으로 확산된다.In general, at the same temperature and pressure, water evaporates faster because of its higher vapor pressure than hydrogen peroxide, and because water has a lower molecular weight than hydrogen peroxide, water diffuses more rapidly into the gas phase than hydrogen peroxide.
따라서, 동일한 온도 및 압력조건에서 물(즉, 수분)은 과산화수소보다 신속하게 증발하여 확산되기 때문에, 과산화수소수에서의 물은 과산화수소보다 먼저 증발/확산되므로, 제2농도의 과산화수소수가 형성될 수 있다.Accordingly, since water (ie, moisture) evaporates and diffuses faster than hydrogen peroxide at the same temperature and pressure conditions, water in the hydrogen peroxide water is evaporated / diffused before hydrogen peroxide, and thus a second concentration of hydrogen peroxide water may be formed.
이때, 증발된 물은 멸균챔버(110)를 경유하여 진공펌프를 통해 진공배기되며, 따라서, S130 단계에서 상기 진공펌프(120)를 작동(on 상태)시키고, 상기 진공밸브(121) 및 기화밸브(131)는 open 상태에 해당한다.At this time, the evaporated water is evacuated through the vacuum pump via the
한편, S130 단계에서, 상기 기화기(130)의 온도는 기화과정의 흡열반응에 의해 일시적으로 온도가 낮아지게 되어, 55 내지 65℃의 범위에 있으며, 압력은 30 내지 800 mb(미리바)일 수 있다.On the other hand, in step S130, the temperature of the
또한, 증발된 물이 멸균챔버(110)를 경유하여, 진공펌프를 통해 진공배기되는 동안, 상기 멸균챔버(110)의 압력은 10 내지 600 mb의 범위이고, 온도는 45 내지 55℃일 수 있으며, 또한, 상기 수집기(140)의 압력은 20 내지 500 mb의 범위이고, 온도는 35 내지 40℃일 수 있다.In addition, while the evaporated water is evacuated through the
다음으로, 제2온도 및 제2압력의 수집기에 상기 제2농도의 과산화수소수를 투입하는 단계를 포함한다(S140).Next, the step of injecting the hydrogen peroxide water of the second concentration into the collector of the second temperature and the second pressure (S140).
상기 제2농도의 과산화수소수를 제2온도 및 제2압력의 수집기(140)에 투입하기 위하여, 상기 진공펌프(120)를 작동(on 상태)로, 상기 진공밸브(121)를 open 상태로, 상기 기화밸브(131)는 close 상태로, 상기 수집밸브(141)는 on 상태로 제어할 수 있다.In order to inject the hydrogen peroxide solution of the second concentration into the
이때, 상기 제2온도는 35 내지 42℃일 수 있으며, 상기 제2압력은 8 내지 50 mb일 수 있다.At this time, the second temperature may be 35 to 42 ℃, the second pressure may be 8 to 50 mb.
또한, 상기 제2농도의 과산화수소수가 기화기(130)로부터 수집기(140)로 이동하는 동안, 상기 기화기(130)의 압력은 10 내지 60 mb이고, 온도는 55 내지 60℃일 수 있으며, 상기 제2농도의 과산화수소수는 제5연결배관(132) 및 제1연결배관(142)을 경유하여, 기화기(130)로부터 수집기(140)로 이동할 수 있다.In addition, while the hydrogen peroxide of the second concentration is moved from the
한편, S140 단계에서도 상기 멸균챔버(110)는 계속적으로 진공배기되어, 상기 멸균챔버(110)의 압력은 1 내지 10 mb이고, 온도는 45 내지 55℃일 수 있다.On the other hand, in step S140 the
이때, 본 발명에서 상기 제2온도는 상기 멸균챔버의 온도보다 낮은 것을 특징으로 한다.At this time, the second temperature in the present invention is characterized in that lower than the temperature of the sterilization chamber.
상기 제2온도의 경우, 제2농도의 과산화수소수가 수집되는 수집기의 온도에 해당하며, 기화기로부터 포화된 과산화수소 증기가 수집기를 경유하는 과정에서 챔버의 온도보다 높으면, 과산화수소 증기가 수집기에 응축되지 못하고 모두 챔버를 통해 배기될 수 있다.The second temperature corresponds to the temperature of the collector in which the hydrogen peroxide water of the second concentration is collected, and if the saturated hydrogen peroxide vapor from the vaporizer is higher than the temperature of the chamber in the course of passing through the collector, the hydrogen peroxide vapor cannot be condensed in the collector. May be exhausted through the chamber.
압력이 다소 높은 S140/S150단계 초기에 과산화수소 증기가 일부 응축되더라도, 배기되는 챔버로 진공압력이 지속적으로 부과되는 단계에서 수집기가 챔버의 온도보다 높으면, 과산화수소 증발열은 수증기에 비해서는 낮기 때문에 쉽게 재기화되어 수집기에 남지 못하게 되어, 결국, 후술하는 S170단계를 수행할 수 없게 되므로, 따라서, 제2온도는 적어도 멸균챔버의 온도보다 낮은 것이 바람직하다.Even if the hydrogen peroxide vapor is partially condensed in the early stage of the S140 / S150, where the pressure is rather high, if the collector is higher than the chamber temperature in the stage where the vacuum pressure is continuously applied to the evacuated chamber, the heat of evaporation of hydrogen peroxide is low compared to water vapor, so it is easily regasified. It is not possible to remain in the collector, and eventually, the step S170 to be described later can not be performed, therefore, the second temperature is preferably at least lower than the temperature of the sterilization chamber.
이상에서 알 수 있는 바와 같이, 본 발명에서는 S130 단계, 즉, 상기 제1농도의 과산화수소수를 기화시켜 제2농도의 과산화수소수를 형성하는 단계를 거친 후에, S140 단계, 즉, 제2온도 및 제2압력의 수집기에 상기 제2농도의 과산화수소수를 투입하는 단계를 수행한다.As can be seen above, in the present invention, after the step S130, that is, the step of evaporating the hydrogen peroxide water of the first concentration to form a hydrogen peroxide water of the second concentration, step S140, that is, the second temperature and the second Injecting the second concentration of hydrogen peroxide water into the collector of 2 pressure.
예를 들어, S130 단계없이 S140 단계를 수행하는 것, 제1농도의 과산화수소수를 수집기에 곧바로 투입하는 것을 고려해 볼 수 있으나, 다음과 같은 이유로 바람직하지 않다.For example, to perform the step S140 without the step S130, it may be considered that the first concentration of hydrogen peroxide water directly into the collector, but is not preferable for the following reasons.
하기 표 1은 과산화수소수의 농도별 과산화수소 증기의 기화비율의 예시를 나타낸다.Table 1 below shows an example of the vaporization rate of hydrogen peroxide vapor by the concentration of hydrogen peroxide water.
표 1
상기 표 1을 참조하면, 과산화수소수의 농도가 높아질수록, 또한, 설정온도가 높을수록, 과산화수소 증기의 기화비율이 수증기에 비하여 상대적으로 점점 높아지는 것을 알 수 있다.Referring to Table 1, it can be seen that the higher the concentration of hydrogen peroxide, and the higher the set temperature, the higher the vaporization rate of the hydrogen peroxide vapor than the water vapor.
예를 들어, 50℃에서, 60중량% 농도의 과산화수소수에서의 과산화수소 증기의 기화비율은 13%이므로, 나머지 87%는 수증기임을 의미하고, 80중량% 농도의 과산화수소수에서의 과산화수소 증기의 기화비율은 40%이므로, 나머지 60%가 수증기임을 의미한다.For example, at 50 ° C., the vaporization rate of hydrogen peroxide vapor in a 60% by weight hydrogen peroxide solution is 13%, which means that the remaining 87% is water vapor, and the vaporization rate of hydrogen peroxide vapor in an 80% by weight hydrogen peroxide solution. Is 40%, which means that the remaining 60% is water vapor.
즉, S130 단계 없이 S140 단계를 수행한다 함은 예를 들어, 60중량% 농도의 과산화수소수를 수집기에 투입하는 의미가 될 수 있으며, S130 단계를 수행 후 S140 단계를 수행한다 함은 80중량% 농도의 과산화수소수를 수집기에 투입하는 의미가 될 수 있다.That is, performing step S140 without step S130 may mean, for example, adding 60% by weight of hydrogen peroxide to a collector, and performing step S140 after performing step S130 is performed by 80% by weight. This could mean adding hydrogen peroxide to the collector.
이때, S130 단계 없이 S140 단계를 수행하는 경우는, S130 단계를 수행 후 S140 단계를 수행하는 경우에 비해, 초기단계에서 수집기를 통과하는 수증기의 비율이 상대적으로 높게 된다.In this case, when the step S140 is performed without the step S130, the ratio of the water vapor passing through the collector in the initial stage is relatively higher than when the step S140 is performed after the step S130 is performed.
수증기의 비율이 과산화수소 증기보다 상대적으로 높은 상태에서 수집기에 투입되면, 수집기의 압력이 높은 상태(수집기의 온도가 40도일 경우 포화수증기압은 75mb이므로 이보다 높은 압력)에서 수증기가 수집기에 진입되게 되므로, 수증기도 수집기에 응축될 수 있다. If the proportion of water vapor is higher than the hydrogen peroxide vapor, the collector is introduced into the collector when the pressure of the collector is high (saturated water vapor pressure is 75mb when the collector temperature is 40 ° C). It can also be condensed in the collector.
수증기도 수집기에 응축된다 함은, 응축되는 수증기의 양 만큼, 농축되는 과산화수소수의 농도에 한계가 있음을 의미한다.The condensation of water vapor into the collector means that there is a limit to the concentration of hydrogen peroxide that is concentrated by the amount of water vapor that is condensed.
따라서, 본 발명에서는 수증기가 수집기에 먼저 응축되어, 농축되는 과산화수소수의 농도에 한계가 발생하는 것을 방지하기 위해, S130 단계, 즉, 상기 제1농도의 과산화수소수를 기화시켜 제2농도의 과산화수소수를 형성하는 단계를 거친 후에, S140 단계, 즉, 제2온도 및 제2압력의 수집기에 상기 제2농도의 과산화수소수를 투입하는 단계를 수행한다.Therefore, in the present invention, in order to prevent the water vapor is condensed in the collector first, the limit occurs in the concentration of the hydrogen peroxide solution to be concentrated, step S130, that is, the hydrogen peroxide water of the second concentration by vaporizing the first concentration of hydrogen peroxide water After the step of forming the step, step S140, that is, the step of introducing the hydrogen peroxide water of the second concentration to the collector of the second temperature and the second pressure.
다음으로, 상기 제2농도의 과산화수소수 중 과산화수소 증기는 상기 수집기에 응축되고, 수증기는 상기 수집기로부터 배기시키는 단계를 포함한다(S150).상술한 바와 같이, 물은 과산화수소보다 증기압이 높기 때문에 보다 신속하게 증발되고, 물의 분자량은 과산화수소보다 낮기 때문에 물이 과산화수소보다 신속하게 기상으로 확산되므로, 따라서, 동일한 온도 및 압력조건에서 물(즉, 수분)은 과산화수소보다 신속하게 증발하여 확산되기 때문에, 과산화수소수에서의 물은 과산화수소보다 먼저 증발/확산되므로, 과산화수소 증기는 상기 수집기에 응축되고, 수증기는 상기 수집기로부터 배기되어, 제3농도의 과산화수소수가 형성될 수 있다.Next, the hydrogen peroxide vapor in the second concentration of hydrogen peroxide water is condensed in the collector, and the step of evacuating the water vapor from the collector (S150). As described above, the water is faster than the hydrogen peroxide because of the higher vapor pressure Water is diffused into the gas phase more quickly than hydrogen peroxide because the molecular weight of water is lower than hydrogen peroxide, and therefore, at the same temperature and pressure conditions, water (i.e., moisture) evaporates and diffuses faster than hydrogen peroxide. Since water of evaporates / diffuses before hydrogen peroxide, hydrogen peroxide vapor is condensed in the collector, and water vapor is exhausted from the collector, so that a third concentration of hydrogen peroxide water can be formed.
즉, 물은 과산화수소보다 더 높은 증기압을 갖고, 따라서, 증기상태에서 과산화수소는 물보다 더 쉽게 응축된다. 따라서, 상기 수집기에 응축되는 과산화수소수는 투입된 제2농도의 과산화수소수의 농도보다 더 높은 농도의 과산화수소를 포함할 수 있게 된다.That is, water has a higher vapor pressure than hydrogen peroxide, and therefore hydrogen peroxide condenses more easily than water in the vapor state. Accordingly, the hydrogen peroxide water condensed in the collector may include hydrogen peroxide at a concentration higher than the concentration of the hydrogen peroxide water at the second concentration.
한편, S140단계에서 과산화수소 증기와 수증기가 통과하는 배관은 제 5연결배관, 제1연결배관, 제3연결배관, 제4연결배관의 순으로 이동하며, 이때, 이들 연결배관들 중 내경이 작은 배관의 온도는 수집기(140)의 온도보다 높아야 한다.On the other hand, the hydrogen peroxide vapor and steam passing through the pipe at step S140 is moved in the order of the fifth connection pipe, the first connection pipe, the third connection pipe, the fourth connection pipe, in this case, the smaller inner diameter of these connection pipes The temperature of must be higher than the temperature of the
이는 과산화수소 증기가 수집기에 도달되기 전후 단계의 배관 온도가 수집기보다 낮으면 먼저 배관에 응축된 상태로 잔존할 수 있고, 내경이 작은 배관에 응축된 과산화수소 증기는 S170단계에서 기화될 때 보다 높은 온도에 노출되어 챔버로 진입하는 단계에서 분해에 의한 수증기 함량이 높아질 수 있기 때문이다.This means that if the pipe temperature in the stage before and after the hydrogen peroxide vapor reaches the collector is lower than the collector, it may remain condensed in the pipe first, and the hydrogen peroxide vapor condensed in the pipe having a small inner diameter may be at a higher temperature when vaporized in step S170. This is because the water vapor content due to decomposition may be increased in the step of being exposed to the chamber.
또한, 상기 표 1에서 도시한 바와 같이, 일단 농도가 높아진 상태(85중량% 미만)에서 물과 과산화수소의 증기비율은 비슷해지며, 기화비율에 의한 농축은 농축효율을 저하시키게 된다.In addition, as shown in Table 1, once the concentration is high (less than 85% by weight), the vapor ratio of water and hydrogen peroxide is similar, the concentration by the vaporization ratio is to reduce the concentration efficiency.
기체상태의 과산화수소 증기와 수증기는 같은 압력에서 응축할 수 있는 온도가 차이가 나는데, 예를 들어, 35도일 경우, 과산화수소는 5mb이상에서 응축되고, 수증기는 55mb이상에서 응축된다. The gaseous hydrogen peroxide vapor and water vapor differ in temperature at which they can condense at the same pressure. For example, at 35 degrees, hydrogen peroxide condenses above 5 mb and water vapor condenses above 55 mb.
따라서, 이러한 차이는 예를 들어, 수집밸브를 통해 진공 배기 중인 수집기 온도가 35일 때, 그 압력이 5mb 내지 55mb의 범위에 있을 경우 과산화수소 증기는 응축되고, 수증기는 수집기로부터 배기될 수 있다.Thus, this difference is, for example, when the collector temperature being evacuated through the collecting valve is 35, the hydrogen peroxide vapor is condensed when the pressure is in the range of 5 mb to 55 mb, and the steam can be exhausted from the collector.
이때, 상기 과산화수소수의 제3농도는 90중량% 내지 95중량%일 수 있으며, S150 단계는 75중량% 내지 85중량%의 과산화수소수 중 수분을 기화시킴으로써, 90중량% 내지 95중량% 농도의 과산화수소수를 형성하는 과산화수소수 제2농축 단계일 수 있다.At this time, the third concentration of the hydrogen peroxide solution may be 90% by weight to 95% by weight, and step S150 by vaporizing water in 75% by weight to 85% by weight of hydrogen peroxide, 90% by weight to 95% by weight of hydrogen peroxide It may be a second concentration step of hydrogen peroxide solution to form water.
한편, 상기에서는 S140 단계의 제2온도 및 제2압력의 수집기에 상기 제2농도의 과산화수소수를 투입하는 단계 및 S150 단계의 상기 제2농도의 과산화수소수 중 과산화수소 증기는 상기 수집기에 응축되고, 수증기는 상기 수집기로부터 배기시키는 단계가 순차적으로 이루어지는 것으로 설명하였으나, 이와는 달리, S140 및 S150 단계는 동시에 일어나는 단계일 수 있다.On the other hand, the hydrogen peroxide vapor in the second concentration of hydrogen peroxide in the step and the second concentration of hydrogen peroxide in the collector of the second temperature and the second pressure of step S140 and condensed in the collector, The exhaust gas from the collector is described as being sequentially performed, but, alternatively, the steps S140 and S150 may be performed at the same time.
즉, 제2온도 및 제2압력의 수집기에 상기 제2농도의 과산화수소수를 투입하면서, 이와 동시에, 상기 제2농도의 과산화수소수 중 과산화수소 증기는 상기 수집기에 응축되고, 수증기는 상기 수집기로부터 배기될 수 있다.That is, while injecting the second concentration of hydrogen peroxide water into a collector at a second temperature and a second pressure, at the same time, hydrogen peroxide vapor in the second concentration of hydrogen peroxide water is condensed into the collector, and water vapor is exhausted from the collector. Can be.
이때, 증발된 물은 진공펌프를 통해 진공배기되며, 따라서, S150 단계에서는 상기 진공펌프(120)를 작동(on 상태)시키고, 상기 진공밸브(121)를 open 시킴으로써 진공배기할 수 있으며, 또한, 증발된 물이 진공펌프를 통해 진공배기되기 위하여, 상기 수집밸브(141)는 open 상태에 해당한다.At this time, the evaporated water is evacuated through the vacuum pump, and thus, in operation S150, the
다음으로, 상기 멸균챔버의 일정 압력까지 낮추는 단계 및 상기 제3농도의 과산화수소수를 제4농도의 과산화수소수로 농축하는 단계를 포함한다(S160).Next, the method includes lowering the sterilization chamber to a predetermined pressure and concentrating the third concentration of hydrogen peroxide water to a fourth concentration of hydrogen peroxide water (S160).
이때, 상기 일정 압력이라 함은 멸균챔버에서 멸균을 하기 위한 설정압력이어야 하며, 또한, 멸균제가 과산화수소 증기인 경우, 확산이 용이한 진공도이어야 한다.At this time, the predetermined pressure should be a set pressure for sterilization in the sterilization chamber, and, if the sterilant is hydrogen peroxide vapor, it should be easy to diffuse vacuum degree.
따라서, 상기 설정압력은 0.5 내지 1.3 mb일 수 있으며, 또한, 상기 멸균챔버의 온도는 45 내지 55℃일 수 있다.Therefore, the set pressure may be 0.5 to 1.3 mb, the temperature of the sterilization chamber may be 45 to 55 ℃.
또한, 상기 과산화수소수의 제4농도는 95중량% 이상일 수 있으며, S160 단계 90중량% 내지 95중량% 농도의 과산화수소수 중 수분을 기화시킴으로써, 95중량% 이상의 과산화수소수를 형성하는 과산화수소수 제3농축 단계일 수 있다.In addition, the fourth concentration of the hydrogen peroxide solution may be greater than or equal to 95% by weight, the third concentration of hydrogen peroxide to form more than 95% by weight of hydrogen peroxide by evaporating water in the hydrogen peroxide solution of the concentration of 90% to 95% by weight in step S160 It may be a step.
이때, 증발된 물은 진공펌프를 통해 진공배기되며, 따라서, S160 단계에서는 상기 진공펌프(120)를 작동(on 상태)시키고, 상기 진공밸브(121)를 open 시킴으로써 진공배기할 수 있다.At this time, the evaporated water is evacuated through the vacuum pump, and thus, in step S160, the
한편, S160 단계에서 상기 수집밸브(141)는 open 상태 및 close 상태를 반복할 수 있다.On the other hand, in step S160 the
즉, 상기 제3농도의 과산화수소수를 제4농도의 과산화수소수로 농축함에 있어서, 고농도의 과산화수소수가 될수록, 액상의 과산화수소수가 증발될 수 있는 압력은 더 낮아진다.That is, in concentrating the third concentration of hydrogen peroxide water to the fourth concentration of hydrogen peroxide water, the higher the concentration of hydrogen peroxide water, the lower the pressure at which the liquid hydrogen peroxide water can evaporate.
예를 들면, 45 ℃의 동일한 온도조건에서, 80중량% 농도의 과산화수소수에서는 약 20mb 이하의 압력에서 과산화수소가 증발하게 되나, 90중량% 농도의 과산화수소수에서는 약 11mb 이하의 압력이 되어야 과산화수소가 증발하게 된다.For example, under the same temperature of 45 ° C, hydrogen peroxide evaporates at a pressure of about 20mb or less in 80% by weight hydrogen peroxide solution, but hydrogen peroxide does not evaporate at a pressure of about 11mb or less in 90% by weight hydrogen peroxide solution. Done.
이는 상기 제3농도의 과산화수소수를 제4농도의 과산화수소수로 농축함에 있어서, 수분만 기화되는 것이 아니라, 과산화수소도 기화되게 되므로, 소정의 농도까지 과산화수소수를 농축하는 것이 어려워질 수 있다.This is because in the concentration of the hydrogen peroxide water of the third concentration to the hydrogen peroxide water of the fourth concentration, not only vaporization of the water, but also hydrogen peroxide, it is difficult to concentrate the hydrogen peroxide water to a predetermined concentration.
즉, 고농도의 과산화수소는 분해반응이 지속될 수 있으며, 분해 과정에서 생성된 수분은 과산화수소의 농도를 낮추게 된다.That is, the high concentration of hydrogen peroxide can continue the decomposition reaction, the water generated during the decomposition will lower the concentration of hydrogen peroxide.
따라서, 이러한 소량의 불순물인 수분을 제거하기 위해서는, 0.1 내지 2mb의 변동범위에서 압력의 상승/하강을 반복하는 경우, 기화되는 과산화수소가 제거되는 것을 억제하면서, 수분을 효과적으로 제거할 수 있다.Therefore, in order to remove the water which is such a small amount of impurities, it is possible to effectively remove the water while suppressing the removal of the vaporized hydrogen peroxide when the pressure rise / fall is repeated in the fluctuation range of 0.1 to 2 mb.
이러한 수분 제거 방법은 농도가 낮은 단계에서는 매우 긴 시간이 소요되지만, 농도가 높은 단계에서는 소량의 수분을 제거하기 위해 효과적이며, 적어도 높은 농도를 유지하는데 효과적이라 할 수 있다.This water removal method takes a very long time in the low concentration step, but is effective to remove a small amount of water in the high concentration step, it can be said to be effective to maintain at least a high concentration.
따라서, 상기 멸균챔버의 일정 압력까지 낮추는 단계에 의하여, 제3농도의 과산화수소수를 포함하고 있는 상기 수집기(140)의 압력이 지속적으로 낮아져서 보다 낮은 압력에서 과산화수소가 증발하는 것을 방지하기 위하여, 상기 수집밸브(141)는 open 상태 및 close 상태를 반복함으로써, 상기 수집기(140)의 압력이 지속적으로 낮아지는 것을 방지할 수 있다.Therefore, by lowering to a predetermined pressure of the sterilization chamber, the pressure of the
이때, 상기 수집기(140)의 압력은 5 내지 10 mb이고, 온도는 35 내지 40℃일 수 있으며, 상기 기화기(130)의 압력은 7 내지 10 mb이고, 온도는 60 내지 70℃일 수 있다.At this time, the pressure of the
한편, 상기 S160 단계에서는 기화기의 수용액은 완전히 소진된 상태이므로 진공상태에서 온도가 회복되고, 수집기는 고농축 과산화수소가 수집되어 소량의 수분이 제거되고 있거나, 적정 압력을 유지하면서 수집기에 머물게 된다.On the other hand, in step S160, since the aqueous solution of the vaporizer is completely exhausted, the temperature is restored in a vacuum state, and the collector is concentrated with high concentration of hydrogen peroxide, and a small amount of water is removed, or stays in the collector while maintaining an appropriate pressure.
이때 수집기는 과산화수소의 과도한 소진을 방지하기 위해 온도제어 수단에 의해 더 낮은 온도로 하강할 수 있다.The collector can then be lowered to a lower temperature by temperature control means to prevent excessive exhaustion of hydrogen peroxide.
다음으로, 제4농도의 과산화수소수의 과산화수소 증기를 멸균챔버에 투입하여, 피처리물을 멸균처리하는 단계를 포함한다(S170).Next, the hydrogen peroxide vapor of the hydrogen peroxide solution of the fourth concentration is put into a sterilization chamber, and the step of sterilizing the object to be treated (S170).
S170 단계에서는 수집기(140)에 위치하는 제4농도의 과산화수소수의 과산화수소 증기를 멸균챔버(110)에 투입하기 위하여, 기화밸브(131)는 open 상태이고, 수집밸브는 open 또는 close 상태에 해당한다.In step S170, in order to inject the hydrogen peroxide vapor of the hydrogen peroxide solution of the fourth concentration located in the
즉, 수집기(140)로부터 멸균챔버(110)로 과산화수소 증기가 이동하는 것은 제1연결배관(142) 및 제2연결배관(133)을 통해 이동할 수 있다.That is, the hydrogen peroxide vapor from the
이때, 상술한 바와 같이, 본 발명에서 수집기(140)와 기화밸브(131)를 연결하는 제1연결배관(142) 및 기화밸브(131)와 멸균챔버(110)를 연결하는 제2연결배관(133)은 다른 연결배관, 즉, 제3연결배관(143) 내지 제5연결배관(132)보다 내경이 클 수 있으며, 예를 들어, 제3연결배관(143) 내지 제5연결배관(132)이 1/4 inch 배관인 경우, 상기 제1연결배관(142) 및 제2연결배관(133)은 1 inch 배관일 수 있다.At this time, as described above, in the present invention, the
이는 수집기(140)로부터 멸균챔버(110)로 과산화수소 증기가 제1연결배관(142) 및 제2연결배관(133)을 통해 이동함에 있어서, 제5연결배관(132)으로 과산화수소 증기가 유입되는 것을 방지하기 위함으로, 상대적으로 내경이 큰 제1연결배관(142)으로 과산화수소 증기가 유입되고, 상대적으로 내경이 작은 제5연결배관(132)으로는 과산화수소 증기가 유입되지 않을 수 있다.This means that the hydrogen peroxide vapor flows into the
또한, 본 발명에서는 과산화수소 증기가 멸균챔버에 투입되어, 피처리물을 멸균처리함에 있어서, 과산화수소 증기의 온도가 높지 않은 상태에서 투입되는 것이 바람직하다.In the present invention, the hydrogen peroxide vapor is added to the sterilization chamber, the sterilization treatment target, it is preferable that the hydrogen peroxide vapor is added in a state where the temperature of the hydrogen peroxide vapor is not high.
멸균 챔버에 과산화수소 증기가 충분히 포화되기 전에 수집기에서 기화된 과산화수소 증기의 온도가 멸균 챔버의 온도보다 높은 상태에서 멸균챔버에 진입하는 경우, 진입 경로에 과산화수소 증기의 밀도가 과도한 상태가 되어 응축되기 쉽고, 기체 상태로 멸균챔버에 확산하는 절대적인 양을 감소시키게 되며 멸균을 위한 확산 효과에 나쁜 영향을 줄 수 있게 된다.If the sterilization chamber enters the sterilization chamber at a temperature higher than the temperature of the sterilization chamber before the hydrogen peroxide vapor is sufficiently saturated in the sterilization chamber, the density of the hydrogen peroxide vapor in the entry path becomes excessive and easily condensed. The gas phase reduces the absolute amount of diffusion into the sterilization chamber and can adversely affect the diffusion effect for sterilization.
이때, 본 발명에서는 수집기(140)와 멸균챔버(110) 사이 경로의 배관이 다른 경로의 배관보다 내경이 클 수 있는데, 배관의 내경이 크다 함은 기체의 이동 양이 많음을 의미하고, 배관의 내경이 크면 기체의 이동 양이 많아지는 만큼 진공도에 의한 기화 구동력이 강하게 상승하여 기체 상태의 과산화수소 증기의 온도 상승을 방지할 수 있다.At this time, in the present invention, the pipe of the path between the
즉, 기체의 이동 양이 적은 경우, 과산화수소 증기가 수집기에 체류되는 시간이 그만큼 증가하게 되고, 과산화수소의 기화 및 이동을 위해 온도 상승이 필요한 수집기에서 과산화수소 증기의 분해반응속도는 증가하게 되어 분해 부산물인 수증기와 산소기체의 농도가 높아지게 된다. 이는 과산화수소 확산에 방해요소인 수증기 양을 최소화시키고자 하는 이전 단계의 목적이 기화단계에서 상실되어 멸균 성능을 약화시킬 수 있다.That is, when the amount of gas movement is small, the time for which hydrogen peroxide vapor stays in the collector increases accordingly, and the decomposition reaction rate of the hydrogen peroxide vapor increases in the collector which needs to rise in temperature for vaporization and movement of hydrogen peroxide. The concentration of water vapor and oxygen gas is increased. This can lead to a loss of sterilization performance as the purpose of the previous step to minimize the amount of water vapor which is a barrier to the diffusion of hydrogen peroxide is lost in the vaporization step.
따라서, 본 발명에서는 수집기(140)와 멸균챔버(110) 사이 경로의 배관이 다른 경로의 배관보다 내경을 크게 함으로써, 과산화수소 증기의 온도가 높지 않은 상태에서 멸균챔버에 투입될 수 있으며, 온도에 따른 분해 반응이 최소화되면서 기상으로 충분한 확산을 통해 과산화수소 증기가 피멸균물에 접근하는 것이 용이하므로, 양호한 멸균 효과를 얻을 수 있다.Therefore, in the present invention, the pipe of the path between the
한편, 제4농도의 과산화수소수의 과산화수소 증기를 멸균챔버에 투입함에 있어서, 과산화수소는 멸균챔버로 기화 확산되는데, 상기 수집기(140)의 온도가 상기 멸균챔버의 온도에 도달하기 전에 과산화수소의 기화가 대부분 완료되도록 상기 수집기(140)의 승온속도를 제어할 수 있다.On the other hand, in the hydrogen peroxide vapor of the fourth concentration of hydrogen peroxide into the sterilization chamber, hydrogen peroxide is evaporated and diffused into the sterilization chamber, the vaporization of the hydrogen peroxide before the temperature of the
즉, 과산화수소의 기화를 촉진하기 위해, 상기 수집기(140)를 온도제어수단에 의해 가열할 수 있는데, 상기 수집기를 가열하는 것은, 수집기의 온도가 상기 멸균챔버의 온도에 도달하기 전에 과산화수소의 기화가 80% 이상 완료되도록 승온속도를 제어할 수 있다.That is, in order to promote the vaporization of hydrogen peroxide, the
이때, 상기 멸균챔버(110)의 압력은 0.5 내지 15 mb일 수 있으며, 온도는 45 내지 55℃일 수 있다.At this time, the pressure of the
또한, 상기 수집기(140)의 압력은 0.5 내지 15 mb이고, 온도는 30 내지 70℃일 수 있으며, 상기 기화기(130)의 압력은 0.5 내지 15 mb이고, 온도는 60 내지 70℃ 이상일 수 있다.In addition, the pressure of the
상기 각 단계에서의 압력 및 온도 조건을 정리하면 하기 표 2와 같다.To summarize the pressure and temperature conditions in each step is shown in Table 2 below.
표 2
또한, 각 단계에서의 진공펌프 및 밸브의 상태를 정리하면 하기 표 3과 같다.In addition, the state of the vacuum pump and the valve in each step is summarized in Table 3 below.
표 3
상술한 바와 같이, 멸균 성능을 향상시키기 위해, 보다 농축된 과산화수소수를 사용하는 것이 바람직한데, 보다 농축된 과산화수소 용액을 사용하는 것은, 과산화수소 용액을 취급하는 데 있어서 과산화수소 용액의 농도가 60중량% 이하로 제한되어 있어서 높은 농도의 과산화수소를 멸균제로 쓰는 어려움이 있다.As described above, in order to improve sterilization performance, it is preferable to use more concentrated hydrogen peroxide solution, but using a more concentrated hydrogen peroxide solution, the concentration of the hydrogen peroxide solution in handling the hydrogen peroxide solution is 60% by weight or less. There is a difficulty in using a high concentration of hydrogen peroxide as a sterilizing agent.
하지만, 본 발명에서는 각 단계별 농축과정을 통하여, 95중량% 이상의 과산화수소수를 멸균제로 사용할 수 있으며, 따라서, 수증기에 의한 확산방해 요인이 줄어들면서 멸균효과를 크게 향상시킬 수 있다.However, in the present invention, through each step of the concentration process, more than 95% by weight of hydrogen peroxide water can be used as a sterilizing agent, thus, the sterilization effect can be greatly improved while reducing the diffusion barrier caused by water vapor.
또한, 상술한 S130 단계인, 최초에 공급된 제1농도의 과산화수소 수용액으로부터 수분을 제거하여 제2농도의 과산화수소 수용액을 준비한 이후에, 상술한 S140 단계 및 S150 단계를 진행함으로써, 수집기에 수분이 접촉할 수 있는 가능성을 감소시킬 수 있다.In addition, after removing the water from the aqueous solution of hydrogen peroxide at the first concentration supplied in step S130 described above to prepare a second solution of hydrogen peroxide solution, the water is brought into contact with the collector by proceeding with steps S140 and S150 described above. Can reduce the likelihood of doing so.
또한, 과산화수소수를 수집기에 투입함에 있어서, 과산화수소수의 수집기의 압력과 수집기의 온도에 따른 수분의 포화수증기압, 즉, 기화/응축 경계 압력을 낮추어 줌으로써 수분이 수집기에 접촉하더라도, 응축할 수 없는 조건이 되도록 할 수 있다.In addition, when the hydrogen peroxide water is introduced into the collector, the saturated steam pressure of the water according to the collector pressure of the hydrogen peroxide collector and the temperature of the collector, that is, the vaporization / condensation boundary pressure is lowered, so that even if the water contacts the collector, it cannot condense. This can be done.
본 발명에서는 이상과 같은 멸균장치 및 이를 이용한 멸균방법에 의하여, 대상물을 멸균할 수 있으며, 다만 상술한 멸균장치 및 이를 이용한 멸균방법은 일예에해당할 뿐, 본 발명에서는 기본적인 멸균장치의 구성 및 이를 이용한 멸균방법을 제한하는 것은 아니다.In the present invention, the above sterilization apparatus and the sterilization method using the same, it is possible to sterilize the object, the above sterilization apparatus and the sterilization method using the same is just one example, in the present invention the configuration of the basic sterilization apparatus and the same It does not limit the sterilization method used.
이하에서는, 본 발명에 따른 과산화수소 농도를 측정할 수 있는 멸균장치 및 상기 멸균장치의 과산화수소수 농도 측정방법에 대해 설명하기로 한다.Hereinafter, a sterilization apparatus capable of measuring the hydrogen peroxide concentration according to the present invention and a method of measuring the hydrogen peroxide concentration of the sterilization apparatus will be described.
상술한 바와 같이, 멸균 성능을 향상시키기 위해, 보다 농축된 과산화수소수를 사용하는 것이 바람직한데, 보다 농축된 과산화수소 용액을 사용하는 것은, 과산화수소 용액을 취급하는 데 있어서 과산화수소 용액의 농도가 60중량% 이하로 제한되어 있어서 높은 농도의 과산화수소를 멸균제로 쓰는 어려움이 있다.As described above, in order to improve sterilization performance, it is preferable to use more concentrated hydrogen peroxide solution, but using a more concentrated hydrogen peroxide solution, the concentration of the hydrogen peroxide solution in handling the hydrogen peroxide solution is 60% by weight or less. There is a difficulty in using a high concentration of hydrogen peroxide as a sterilizing agent.
이러한 이유로, 취급이 가능한 농도가 60중량% 이하인 과산화수소 수용액을 각 단계별 농축과정을 통하여, 예를 들면, 95중량% 이상의 고농도의 과산화수소수로 농축하여 멸균제로 사용하는 것이 일반적이나, 상기 과산화수소수를 고농도의 과산화수소수로 농축하여 멸균제로 사용함에 있어서, 멸균장치의 멸균챔버 내에서 상기 과산화수소의 농도를 측정하는 것은 용이하지 않다.For this reason, it is common to use an aqueous solution of hydrogen peroxide with a concentration of up to 60% by weight in each step, for example, to concentrate at a concentration of 95% by weight or more with high concentration of hydrogen peroxide and use it as a sterilizing agent. In concentrating with hydrogen peroxide solution to use as a sterilizing agent, it is not easy to measure the concentration of hydrogen peroxide in the sterilization chamber of the sterilization apparatus.
따라서, 본 발명에서는, 멸균장치의 대형화나 복잡화를 지양하고 간단한 방법에 의하여, 과산화수소수에서의 과산화수소의 농도를 정확하게 검출할 수 있는 멸균장치 및 상기 멸균장치의 과산화수소 농도 측정방법을 제공하고자 하며, 이는 다음과 같다.Therefore, in the present invention, to avoid the enlargement or complexity of the sterilization apparatus, and to provide a sterilization apparatus capable of accurately detecting the concentration of hydrogen peroxide in the hydrogen peroxide solution and a method for measuring the hydrogen peroxide concentration of the sterilization apparatus by a simple method, which As follows.
상술한 바와 같이, 도 1 및 도 2를 참조하면, 본 발명에 따른 멸균장치는 멸균챔버; 상기 멸균챔버의 일측에 연결되는 진공펌프; 상기 멸균챔버의 다른 일측에 연결되는 기화기; 및 일측은 상기 기화기와 연결되고, 타측은 상기 멸균챔버와 연결되는 수집기를 포함한다.As described above, referring to Figures 1 and 2, the sterilization apparatus according to the present invention is a sterilization chamber; A vacuum pump connected to one side of the sterilization chamber; A vaporizer connected to the other side of the sterilization chamber; And one side is connected to the carburetor, the other side comprises a collector connected to the sterilization chamber.
이때, 본 발명에 따른 멸균장치는 상기 멸균챔버(110)의 내부 일정 영역에 위치하는 제1습도센서(111) 및 상기 제1습도센서(111)와 인접하여 위치하는 제2습도센서(112)를 포함한다.At this time, the sterilization apparatus according to the present invention is the
즉, 본 발명에서는 상기 제1습도센서(111) 및 상기 제2습도센서(112)를 통해, 상기 멸균챔버(110)의 내부의 과산화수소의 농도를 측정하고자 한다.That is, in the present invention, the concentration of hydrogen peroxide in the
한편, 상기 멸균챔버는 과산화수소의 농도를 측정하기 위한 대상공간에 해당하는 것으로, 상기 대상공간은 상술한 바와 같은 멸균챔버일 수 있고, 이와는 달리, 무균상태가 필요한 수술실 또는 무균 사육이 필요한 무균실일 수 있다.On the other hand, the sterilization chamber corresponds to the target space for measuring the concentration of hydrogen peroxide, the target space may be a sterilization chamber as described above, alternatively, may be an operating room or a sterile room requiring aseptic breeding. have.
즉, 상기 대상공간은 챔버 또는 수술실 또는 무균실일 수 있으며, 다만, 본 발명에서 상기 대상공간의 종류를 제한하는 것은 아니다.That is, the object space may be a chamber or an operating room or a sterile room, but the type of the object space is not limited in the present invention.
이때, 본 발명에서 상기 제1습도센서(111)는 수증기의 양 및 과산화수소의 양에 의해 상대 습도가 결정되는 센서이고, 상기 제2습도센서(112)는 수증기의 양에 의해서만 상대 습도가 결정되는 센서에 해당한다.At this time, in the present invention, the
또한, 본 발명에서 상기 제2습도센서(112)가 수증기의 양에 의해서만 상대습도가 결정된다함은, 상기 제2습도센서가 수증기의 양에 대한 상대습도를 직접 측정하는 경우이거나, 상기 제2습도센서가 수증기의 양에 대한 절대습도를 측정하고, 상기 절대습도를 상대습도로 변환한 경우를 포함한다.In addition, in the present invention, the relative humidity is determined only by the amount of water vapor in the
수증기의 절대습도에서 상대습도로 변환하는 것은 당업계에서 자명한 사항이므로, 이하 구체적인 설명은 생략하기로 한다. Since the conversion from the absolute humidity to the relative humidity of the water vapor is obvious in the art, a detailed description thereof will be omitted below.
보다 구체적으로, 상기 제1습도센서는, 수분흡착 방식의 습도센서, 포화방식에 의한 습도센서 또는 흡수 방식에 의한 습도센서일 수 있으며, 보다 구체적으로, 상기 수분흡착 방식의 습도센서는 정전용량형 습도센서, 저항 변화형 습도센서, 모발습도계, 탄소피막습도계, 전기식 습도계, 색습도계일 수 있고, 상기 포화방식에 의한 습도센서는 노점 습도계, 염화리튬 노점 습도계일 수 있으며, 또한, 흡수 방식에 의한 습도센서는 부피식 습도계, 전기분해식 습도계, 중량식 습도계일 수 있다.More specifically, the first humidity sensor may be a humidity sensor of a moisture adsorption method, a humidity sensor of a saturation method, or a humidity sensor of an absorption method. More specifically, the moisture sensor of the moisture adsorption method is a capacitance type. Humidity sensor, resistance change type humidity sensor, hair hygrometer, carbon film hygrometer, electric hygrometer, color hygrometer, the humidity sensor according to the saturation method may be dew point hygrometer, lithium chloride dew point hygrometer, and also by absorption method The humidity sensor may be a volumetric hygrometer, an electrolytic hygrometer, a weight hygrometer.
한편, 상술한 바와 같이, 본 발명에서 상기 제1습도센서(111)는 수증기의 양 및 과산화수소의 양에 의해 상대 습도가 결정되는 센서이다.On the other hand, as described above, in the present invention, the
이때, 상술한 제1습도센서와 같은, 물의 상대습도를 측정하는 센서를 사용하여 과산화수소 농도를 측정하는 원리는, VHP(고농축된 과산화수소 증기) 증기압이 물의 상대습도를 측정하는 원리와 같이 측정센서에 감습되는 정도 등에 의해 측정된다는 것이다.At this time, the principle of measuring the hydrogen peroxide concentration using a sensor for measuring the relative humidity of water, such as the first humidity sensor described above, the VHP (highly concentrated hydrogen peroxide vapor) vapor pressure is measured on the measuring sensor as the principle of measuring the relative humidity of water It is measured by the degree of humidity reduction.
특히, 정전용량형 습도센서를 이용하는 것은 비유전율의 값이 물과 과산화수소가 거의 같아서 직접적으로 대입하여 사용할 수 있다는 점이 매우 중요한 원리에 해당한다.In particular, the use of a capacitive humidity sensor corresponds to a very important principle that the relative dielectric constant of water and hydrogen peroxide can be directly substituted and used.
즉, 물의 상대습도를 측정하는 방식과 VHP의 상대포화도를 측정하는 방식이 동일하기 때문에, 정전용량형 습도센서와 같은 제1습도센서는 수증기의 양 및 과산화수소의 양에 의해 상대 습도가 결정될 수 있는 것이다.That is, since the method of measuring the relative humidity of the water and the method of measuring the relative saturation of the VHP is the same, the first humidity sensor, such as a capacitive humidity sensor, the relative humidity can be determined by the amount of water vapor and the amount of hydrogen peroxide will be.
또한, 상기 제2습도센서(112)는 분광학적 방식에 의한 습도센서로, 상기 분광학적 방식에 의한 습도센서는 비분산적외선(NDIR, Non-dispersive Infrared) 습도계 또는 근적외선 습도계일 수 있다.In addition, the
상술한 바와 같이, 제1습도센서의 경우, 수증기의 양 및 과산화수소의 양에 의해 상대 습도가 결정될 수 있다.As described above, in the case of the first humidity sensor, the relative humidity may be determined by the amount of water vapor and the amount of hydrogen peroxide.
하지만, 분광학적 방식의 제2습도센서는 수증기의 양에 의해서만 상대 습도가 결정되는 센서에 해당한다.However, the spectroscopic second humidity sensor corresponds to a sensor whose relative humidity is determined only by the amount of water vapor.
예를 들어, 상기 비분산적외선 습도계는 IR영역에서 물의 흡수 스펙트럼 영역인 6.1um의 선택적 IR에 대한 흡광정도를 산정하는 방식이기 때문에, 서로 다른 영역의 흡수대역을 가진 과산화수소(H2O2)(2.93um)에 대한 선택성이 매우 높은 습도계에 해당한다.For example, the non-dispersive infrared hygrometer is a method of calculating the absorbance of the selective IR of 6.1um, which is an absorption spectrum region of water in the IR region, so that hydrogen peroxide (H 2 O 2 ) having absorption bands of different regions ( 2.93um) corresponds to a hygrometer with a very high selectivity.
한편, 일반적으로, 습도센서란 대상물에서의 습도를 검출하는 센서로써, 상기 습도의 개념으로는 잘 알려진 상대습도와 절대습도가 있다.On the other hand, in general, the humidity sensor is a sensor for detecting the humidity in the object, the concept of the humidity is well known relative humidity and absolute humidity.
보다 구체적으로, 절대 습도는 1ℓ의 공기에 포함된 실제 수증기의 질량을 의미하며, 상대 습도는 공기 중에 포함된 실제 수증기의 양을 주어진 기온과 기압하에서 공기가 포함할 수 있는 최대량의 수증기로 나눈 백분율이다. More specifically, absolute humidity is the mass of the actual water vapor contained in 1 liter of air, and relative humidity is the percentage of the actual water vapor contained in the air divided by the maximum amount of water the air can contain at a given temperature and pressure. to be.
예를 들어, 1기압에 기온이 37℃인 1ℓ의 공기는 44g 만큼의 수증기를 함유할 수 있는데, 현재 같은 기압과 기온을 가진 공기가 11g의 수증기를 가지고 있다면, 상대 습도는 25%(11g/44g×100)에 해당한다.For example, 1 liter of air at 37 ° C at 1 atmosphere can contain as much as 44 grams of steam. If an air with the same pressure and temperature now has 11 grams of steam, the relative humidity is 25% (11 grams / minute). 44 g × 100).
즉, 이러한 습도센서는 공기에 포함된 수증기의 양을 검출하는 센서로 잘 알려져 있다.That is, such a humidity sensor is well known as a sensor for detecting the amount of water vapor contained in the air.
이때, 이러한 대표적인 습도 센서의 종류로는 정전용량형 습도센서 및 저항변화형 습도센서가 있다.At this time, the representative types of humidity sensors include a capacitive humidity sensor and a resistance-type humidity sensor.
먼저, 상기 저항변화형 습도센서는 습도 변화에 대응해서 감습막에 있는 수분량에 따라 저항이 변화하는 특성을 이용한 것으로 교류를 인가하여 변화 신호를 얻는 것으로, 감습재의 재질에 따라 고분자형과 세라믹형으로 분류될 수 있다.First, the resistance change type humidity sensor uses a characteristic in which the resistance changes according to the moisture content in the moisture sensitive film in response to the humidity change, and obtains a change signal by applying an alternating current to the polymer type and the ceramic type according to the material of the moisture sensitive material. Can be classified.
예를 들어, 감습재가 고분자인 고분자형의 경우, 공기 중에 수분자와 고분자가 결합하여 이온을 만들고, 전기 전도도가 발생하며, 감습재가 세라믹인 세라믹형 의 경우, 감습재료의 다공질 표면에 흡착된 수분자를 분리시켜 이온을 만들고 이것이 전기 전도도를 발생시키게 된다.For example, in the case of a polymer type in which the moisture sensitive material is a polymer, moisture and polymer are combined to form ions in air, and electrical conductivity is generated. In the case of a ceramic type in which the moisture sensitive material is ceramic, moisture adsorbed on the porous surface of the moisture sensitive material is used. The pores are separated to form ions, which cause electrical conductivity.
즉, 상대습도의 변화에 따라 이온의 농도가 변화되고, 이는 센서 소자의 임피던스 변화로 측정되어 상대습도를 검출하는 방식으로, 센서에서 전기 신호를 얻는 변환 회로가 간단하여 소형화와 가격적인 이점이 있다.That is, the concentration of ions is changed according to the change of relative humidity, which is measured by the change of impedance of the sensor element to detect the relative humidity, and the conversion circuit for obtaining the electrical signal from the sensor is simple, which has the advantages of miniaturization and cost. .
이러한 저항변화형 습도센서는 일반적으로 잘 알려진 습도센서이므로, 이하 구체적인 설명은 생략하기로 하며, 예를 들어, 한국실용신안 출원 제20-1998-0026410호 및 한국특허출원 제10-2010-0000557호 등을 참조할 수 있다.Since the resistance-type humidity sensor is generally well known humidity sensor, the following detailed description will be omitted, for example, Korean Utility Model Application No. 20-1998-0026410 and Korean Patent Application No. 10-2010-0000557 And the like.
예를 들면, 저항변화형 습도센서는 소결 알루미나 기판의 상면에 백금(Pt)박막을 스퍼터링 증착하여 전극모양으로 패턴을 형성하고, 그 백금박막형 패턴의 상면에 감습폴리머를 도포하여 이루어질 수 있다.For example, the resistance change type humidity sensor may be formed by sputtering and depositing a platinum (Pt) thin film on the upper surface of the sintered alumina substrate to form a pattern in the shape of an electrode, and applying a moisture-sensitive polymer on the upper surface of the platinum thin film pattern.
다음으로, 상기 정전용량형 습도센서는 기판상에 하부 전극이 있고, 상기 하부 전극의 상부에 고분자의 감습재를 균일하게 도포하고, 상기 감습재의 상부에 습도가 투입할 수 있는 성질의 상부 전극으로 구성된다.Next, the capacitive humidity sensor has a lower electrode on a substrate, the upper electrode having a property to uniformly apply a polymer dampener to the upper portion of the lower electrode, the humidity can be injected into the upper portion of the damper. It is composed.
일반적으로 유리 또는 세라믹 기판에 Au 전극과 내습성의 재료가 사용되며, 센서에 도포되어 있는 감습재는 셀룰로스 아세톤 등의 셀롤로스에스텔 화합물 또는 폴리비닐알콜, 폴리아크릴, 폴리비닐피리드 등의 고분자 재료가 사용된다.In general, Au electrodes and moisture resistant materials are used for glass or ceramic substrates, and the moisture-sensitive material applied to the sensor may be a cellulose ester compound such as cellulose acetone, or a polymer material such as polyvinyl alcohol, polyacryl, or polyvinyl pyride. Used.
이러한 정전용량형 습도센서에서 습도를 검출하는 원리는 다음과 같다.The principle of detecting humidity in the capacitive humidity sensor is as follows.
즉, 상기 고분자 재료의 비유전율은 건조 상태에서 약 3 정도로, 공기 중의 물분자(비유전율 80)를 흡수하면서 비유전율은 높게 변화하게 되고, 이러한 비유전율의 변화를 통해, 공기 중의 수증기의 양을 검출할 수 있다.That is, the relative dielectric constant of the polymer material is about 3 in a dry state, while the relative dielectric constant is changed while absorbing water molecules (relative dielectric constant 80) in the air, and through the change of the relative dielectric constant, the amount of water vapor in the air is changed. Can be detected.
이러한 정전용량형 습도센서는 일반적으로 잘 알려진 습도센서이므로, 이하 구체적인 설명은 생략하기로 하며, 예를 들어, 한국특허출원 제10-2007-0135890호 및 한국특허출원 제10-2012-0027010호 등을 참조할 수 있다.Since the capacitive humidity sensor is a well-known humidity sensor in general, the following detailed description will be omitted, for example, Korean Patent Application No. 10-2007-0135890 and Korean Patent Application No. 10-2012-0027010 See.
예를 들면, 상기 정전용량형 습도센서는, 기판상에 형성된 하부 전극; 상기 하부 전극상에 도포되어 수분을 흡탈착하기 위한 감습층; 및 상기 감습층상에 형성된 복수의 상부 전극을 포함할 수 있다.For example, the capacitive humidity sensor may include a lower electrode formed on a substrate; A moisture sensitive layer applied on the lower electrode to absorb and desorb moisture; And a plurality of upper electrodes formed on the moisture sensitive layer.
상술한 바와 같이, 상기 습도센서, 즉, 정전용량형 습도센서 및 저항변화형 습도센서는 공기에 포함된 수증기의 양을 검출하는 센서로 잘 알려져 있다.As described above, the humidity sensor, that is, the capacitance type humidity sensor and the resistance change type humidity sensor are well known as a sensor for detecting the amount of water vapor contained in the air.
하지만, 본 출원인은 상기 정전용량형 습도센서의 경우, 수증기의 양 뿐만 아니라, 과산화수소의 양에 의해서도 검출되는 수치가 변화됨을 확인하였으며, 이에 착안하여, 상기 제1습도센서(111) 및 상기 제2습도센서(112)를 통해, 상기 멸균챔버(110)의 내부의 과산화수소의 농도를 측정하는 방법을 개발하였다.However, the Applicant has confirmed that the value detected by the amount of water vapor, as well as the amount of hydrogen peroxide, in the case of the capacitive humidity sensor is changed, and in view of this, the
상기 정전용량형 습도센서의 경우, 수증기의 양 뿐만 아니라, 과산화수소의 양에 의해서도 검출되는 수치가 변화됨은 다음과 같다.In the case of the capacitive humidity sensor, the detected value is changed not only by the amount of water vapor but also by the amount of hydrogen peroxide.
도 4는 멸균장치에서의 정전용량형 습도센서의 반응을 도시한 그래프이다.Figure 4 is a graph showing the response of the capacitive humidity sensor in the sterilization apparatus.
즉, 본 발명에서는 정전용량형 습도센서를 통해, 과산화수소의 농도를 측정할 수 있음을 확인하기 위해, 멸균장치에서의 멸균과정이 진행되는 공정에서의 정전용량형 습도센서의 반응을 측정하였다.That is, in the present invention, through the capacitive humidity sensor, in order to confirm that the concentration of hydrogen peroxide can be measured, the reaction of the capacitive humidity sensor in the process of sterilization in the sterilization apparatus is measured.
도 4를 참조하면, 챔버를 진공배기 하면서, 농축 모듈을 통해 과산화수소수를 증발시키면서 과산화수소수를 농축시키는 과정이 진행되었다. (50 sec 내지 300 sec)Referring to FIG. 4, a process of concentrating hydrogen peroxide water while evaporating the hydrogen peroxide water through the concentration module while evacuating the chamber was performed. (50 sec to 300 sec)
이후, 고농도로 농축된 과산화수소가 멸균챔버 내부로 확산하면서 멸균챔버 내의 압력이 증가하고 있으며, 여기에 비례하여 정전용량형 습도센서의 상대 습도가 100% 근처를 측정되고 있음을 확인할 수 있다. (300 sec 내지 450 sec)Thereafter, the hydrogen peroxide concentrated in a high concentration is diffused into the sterilization chamber, the pressure in the sterilization chamber is increasing, and it can be seen that the relative humidity of the capacitive humidity sensor is measured around 100% in proportion thereto. (300 sec to 450 sec)
이때, 진공화된 멸균챔버의 온도가 50℃일 때, 상대습도가 100%가 되려면, 수증기만의 압력으로도 120mb를 초과해야 하지만, 실제로 과산화수소 증기(VHP)로만 주입된 멸균챔버의 압력은 12 ~ 15mb에 해당하였다.At this time, when the temperature of the vacuum sterilization chamber is 50 ℃, in order to achieve a relative humidity of 100%, the pressure of the steam alone must exceed 120mb, but the pressure of the sterilization chamber injected only with hydrogen peroxide vapor (VHP) is 12 It corresponded to ~ 15mb.
즉, 예를 들어, 정전용량형 습도센서의 상대 습도가 100%가 되기 위해서는, 멸균챔버의 온도가 50℃인 상황에서, 멸균챔버 내부의 압력의 수치가 수증기만의 압력으로도 120mb를 초과해야 하나, 실제, 멸균챔버의 12 ~ 15mb에 불과하였다.That is, for example, in order for the relative humidity of the capacitive humidity sensor to be 100%, when the temperature of the sterilization chamber is 50 ° C, the value of the pressure inside the sterilization chamber must exceed 120 mb even by the pressure of steam alone. However, in reality, only 12 ~ 15mb of the sterilization chamber.
결국, 정전용량형 습도센서의 상대 습도가 100%가 됨에 있어서, 수증기의 양에 의해 상대 습도가 결정된 것이 아닌, 다른 인자, 즉, 과산화수소의 양이 상대 습도의 결정에 영향을 미쳤음을 확인할 수 있으며, 따라서, 정전용량형 습도센서는 수증기의 양 뿐만아니라, 과산화수소의 양에 의해서도 상대습도가 결정됨을 확인할 수 있다.As a result, when the relative humidity of the capacitive humidity sensor is 100%, it can be confirmed that the relative humidity is not determined by the amount of water vapor, but other factors, that is, the amount of hydrogen peroxide, influenced the determination of the relative humidity. Therefore, the capacitance-type humidity sensor can be seen that the relative humidity is determined not only by the amount of water vapor but also by the amount of hydrogen peroxide.
따라서, 상기 정전용량형 습도센서에 의해 검출된 상대 습도는 수증기의 양 및 과산화수소의 양에 의해 결정된 것을 확인할 수 있다.Therefore, it can be seen that the relative humidity detected by the capacitive humidity sensor is determined by the amount of water vapor and the amount of hydrogen peroxide.
이때, 상기 분광학적 방식에 의한 습도센서는 정전용량형 습도센서와는 달리, 오직 수증기의 양에 따라 상대습도가 결정되게 된다.In this case, unlike the capacitive humidity sensor, the humidity sensor based on the spectroscopic method determines relative humidity only according to the amount of water vapor.
즉, 제1습도센서인 상기 정전용량형 습도센서의 경우, 수증기의 양 및 과산화수소의 양에 의해 상대습도가 결정되나, 제2습도센서인 상기 분광학적 방식에 의한 습도센서의 경우, 오직 수증기의 양에 따라 상대습도가 결정되는 것이다.That is, in the case of the capacitive humidity sensor which is the first humidity sensor, the relative humidity is determined by the amount of water vapor and the amount of hydrogen peroxide, but in the case of the humidity sensor according to the spectroscopic method that is the second humidity sensor, only the water vapor The relative humidity is determined by the amount.
따라서, 상기 제1습도센서에 의해 검출된 상대습도와 상기 제2습도센서에 의해 검출된 상대습도의 차이를 계산한다면, 과산화수소의 양에 의해 결정된 상대습도의 비율을 계산할 수 있는 것이다.Therefore, if the difference between the relative humidity detected by the first humidity sensor and the relative humidity detected by the second humidity sensor is calculated, the ratio of the relative humidity determined by the amount of hydrogen peroxide can be calculated.
한편, 상술한 바와 같이, 본 발명에서 상기 제2습도센서(112)가 수증기의 양에 의해서만 상대습도가 결정된다함은, 상기 제2습도센서가 수증기의 양에 대한 상대습도를 직접 측정하는 경우이거나, 상기 제2습도센서가 수증기의 양에 대한 절대습도를 측정하고, 상기 절대습도를 상대습도로 변환한 경우를 포함한다.On the other hand, as described above, in the present invention, the relative humidity is determined only by the amount of water vapor in the
즉, 상기 제2습도센서를 통해 대상공간의 절대습도를 측정하고, 상기 절대습도를 상대습도로 변환하여 상기 제2습도센서를 통해 대상공간의 제2상대습도를 검출할 수 있다.That is, the absolute humidity of the target space may be measured through the second humidity sensor, and the absolute humidity may be converted into a relative humidity to detect the second relative humidity of the target space through the second humidity sensor.
본 발명에 따른 과산화수소의 농도 측정 방법은 다음과 같다.Method for measuring the concentration of hydrogen peroxide according to the present invention is as follows.
도 5는 본 발명에 따른 과산화수소 농도 측정 방법을 설명하기 위한 순서도이다.5 is a flowchart illustrating a method for measuring hydrogen peroxide concentration according to the present invention.
도 5를 참조하면, 본 발명에 따른 과산화수소 농도 측정 방법은 제1습도센서에 의해 제1상대습도를 검출하는 단계를 포함한다(S210).Referring to FIG. 5, the method for measuring hydrogen peroxide concentration according to the present invention includes detecting a first relative humidity by a first humidity sensor (S210).
이때, 상기 제1습도센서는 대표적으로 정전용량형 습도센서일 수 있으며, 상술한 바와 같이, 상기 정전용량형 습도센서는 수증기의 양 및 과산화수소의 양에 따라 상대습도가 결정되며, 따라서, 상기 제1상대습도는 수증기의 양 및 과산화수소의 양에 따른 상대습도에 해당한다.In this case, the first humidity sensor may typically be a capacitive humidity sensor. As described above, the capacitive humidity sensor may determine relative humidity according to the amount of water vapor and the amount of hydrogen peroxide. 1 Relative humidity corresponds to relative humidity depending on the amount of water vapor and the amount of hydrogen peroxide.
다음으로, 본 발명에 따른 과산화수소 농도 측정 방법은 제2습도센서에 의해 제2상대습도를 검출하는 단계를 포함한다(S220).Next, the hydrogen peroxide concentration measuring method according to the present invention includes the step of detecting the second relative humidity by the second humidity sensor (S220).
이때, 상기 제2습도센서는 대표적으로 비분산적외선 습도센서일 수 있으며, 상술한 바와 같이, 상기 비분산적외선 습도센서는 수증기의 양에 의해서만 상대습도가 결정되며, 따라서, 상기 제2상대습도는 수증기의 양에 따른 상대습도에 해당한다.In this case, the second humidity sensor may typically be a non-dispersion infrared humidity sensor, as described above, the non-dispersion infrared humidity sensor is determined relative humidity only by the amount of water vapor, and thus, the second relative humidity is Corresponds to relative humidity depending on the amount of water vapor.
다음으로, 본 발명에 따른 과산화수소 농도 측정 방법은 상기 제1상대습도와 상기 제2상대습도의 차이값을 도출하는 단계를 포함한다(S230).Next, the method for measuring hydrogen peroxide concentration according to the present invention includes deriving a difference value between the first relative humidity and the second relative humidity (S230).
상기 제1습도센서의 경우, 수증기의 양 및 과산화수소의 양에 의해 상대습도가 결정되나, 상기 제2습도센서의 경우, 오직 수증기의 양에 따라 상대습도가 결정되는 것이다.In the case of the first humidity sensor, the relative humidity is determined by the amount of water vapor and the amount of hydrogen peroxide, but in the case of the second humidity sensor, the relative humidity is determined only by the amount of water vapor.
따라서, 상기 제1습도센서에 의해 검출된 제1상대습도와 상기 제2습도센서에 의해 검출된 제2상대습도의 차이를 계산하여, 과산화수소의 양에 의해 결정된 상대습도의 비율을 계산할 수 있다.Therefore, by calculating the difference between the first relative humidity detected by the first humidity sensor and the second relative humidity detected by the second humidity sensor, the ratio of the relative humidity determined by the amount of hydrogen peroxide can be calculated.
다음으로, 본 발명에 따른 과산화수소 농도 측정 방법은 상기 차이값을 통해과산화수소의 농도를 계산하는 단계를 포함한다(S240).Next, the hydrogen peroxide concentration measuring method according to the present invention includes the step of calculating the concentration of hydrogen peroxide through the difference value (S240).
한편, 상술한 바와 같이, 본 발명에서 과산화수소 증기의 농도를 측정하는 것은 포화 수증기압의 비율로 측정하는 원리에 해당하며, 따라서, 과포화된 과산화수소 증기가 멸균장치의 챔버 등의 내부로 유입되는 경우, 상기 습도센서의 온도가 측정 대상 공간보다 낮은 온도로 존재할 경우, 상기 과포화된 과산화수소증기가 상기 습도센서에 응축되어 실제로 존재하는 농도보다 낮게 측정될 수가 있다.On the other hand, as described above, measuring the concentration of hydrogen peroxide vapor in the present invention corresponds to the principle of measuring the ratio of the saturated steam pressure, therefore, when the supersaturated hydrogen peroxide vapor is introduced into the chamber of the sterilization apparatus, etc. When the temperature of the humidity sensor is present at a temperature lower than the measurement target space, the supersaturated hydrogen peroxide vapor may be condensed on the humidity sensor and measured to be lower than the concentration actually present.
따라서, 본 발명에서 상기 제1습도센서 및 상기 제2습도센서의 온도는 상기 측정 대상 공간, 즉, 챔버, 수술실 또는 무균실 등 보다 높게 제어되는 것이 바람직하다.Therefore, in the present invention, the temperature of the first humidity sensor and the second humidity sensor is preferably controlled higher than the measurement target space, that is, a chamber, an operating room or a clean room.
이하에서는, 제1습도센서 및 제2습도센서에 의해 과산화수소 농도를 측정하는 방법을 설명하기로 한다.Hereinafter, a method of measuring hydrogen peroxide concentration by the first humidity sensor and the second humidity sensor will be described.
다만, 하기 방법은 일예에 해당할 뿐, 본 발명에서 하기 측정 방법을 제한하는 것은 아니다.However, the following method is only one example, it does not limit the following measurement method in the present invention.
하기 표 4는 온도에 따른 포화증기압을 도시하고 있다.Table 4 shows the saturated steam pressure with temperature.
표 4
즉, 상기 표 4는 각 온도에 따른 포화수증기압 및 과산화수소 포화수증기압의 예를 도시하고 있다.That is, Table 4 shows examples of saturated steam pressure and hydrogen peroxide saturated steam pressure according to respective temperatures.
먼저, 상기 제1습도센서에 의해 검출된 제1상대습도가 80%이고, 상기 제2습도센서에 의해 검출된 제2상대습도가 30%라고 가정한다.First, it is assumed that the first relative humidity detected by the first humidity sensor is 80%, and the second relative humidity detected by the second humidity sensor is 30%.
이때, 상술한 바와 같이, 상기 제2습도센서에 의해 검출된 제2상대습도가 30%라고 가정하는 것은, 상기 제2습도센서가 수증기의 양에 대한 상대습도를 직접 측정하는 경우이거나, 상기 제2습도센서가 수증기의 양에 대한 절대습도를 측정하고, 상기 절대습도를 상대습도로 변환한 경우를 포함한다.In this case, as described above, it is assumed that the second relative humidity detected by the second humidity sensor is 30%, when the second humidity sensor directly measures the relative humidity with respect to the amount of water vapor, 2 includes a case in which the humidity sensor measures absolute humidity with respect to the amount of water vapor and converts the absolute humidity into relative humidity.
따라서, 상기 제2상대습도가 30%라고 가정하는 것은, 상기 제2습도센서에 의해 측정된 절대습도로부터 변환된 경우일 수 있다.Therefore, the assumption that the second relative humidity is 30% may be a case where it is converted from the absolute humidity measured by the second humidity sensor.
또한, 멸균챔버 내의 온도는 45℃이고, 기압은 1000mb라고 가정하며, 멸균챔버의 부피는 1000L라고 가정한다.In addition, it is assumed that the temperature in the sterilization chamber is 45 ℃, the air pressure is 1000mb, the volume of the sterilization chamber is 1000L.
이때, 제1상대습도와 제2상대습도의 차이는 50%이고, 따라서, 상기 제1상대습도와 상기 제2상대습도의 차이값인 50%는 과산화수소의 양에 의해 결정된 상대습도의 비율에 해당한다.At this time, the difference between the first relative humidity and the second relative humidity is 50%, and thus, 50%, the difference between the first relative humidity and the second relative humidity, corresponds to the ratio of relative humidity determined by the amount of hydrogen peroxide. do.
즉, 멸균챔버 내의 공기 중의 과산화수소 증기에 의해 반응한 상대습도는 50%에 해당한다.That is, the relative humidity reacted by the hydrogen peroxide vapor in the air in the sterilization chamber corresponds to 50%.
이때, 멸균챔버 내의 온도는 45℃이므로, 상기 표 4를 참조하면, 45℃의 온도에서의 과산화수소의 포화증기압은 9.8mb에 해당한다.At this time, since the temperature in the sterilization chamber is 45 ℃, referring to Table 4, the saturated steam pressure of hydrogen peroxide at a temperature of 45 ℃ corresponds to 9.8mb.
한편, 일반적으로 상대습도(%)=(현재 수증기압/포화수증기압)×100에 해당하므로, 따라서, 멸균챔버 내의 과산화수소 증기압 x은 50% = (x mb/9.8mb)×100%에 해당하므로, 과산화수소 증기압 x = 4.9mb에 해당한다.On the other hand, since the relative humidity (%) = (current steam pressure / saturated steam pressure) × 100 generally corresponds to, the hydrogen peroxide vapor pressure x in the sterilization chamber corresponds to 50% = (x mb / 9.8mb) × 100%, hydrogen peroxide Corresponds to vapor pressure x = 4.9 mb.
이때, 멸균챔버 내의 기압이 1000mb이므로, 과산화수소 증기의 기체 농도는 (4.9mb/1000mb)×100%=0.49%에 해당한다.At this time, since the air pressure in the sterilization chamber is 1000mb, the gas concentration of the hydrogen peroxide vapor corresponds to (4.9mb / 1000mb) × 100% = 0.49%.
이를 부피당 무게로 환산하면, 45℃에서의 이상적인 기체 부피는 (22.4L/mol(at 273k)×(273+45))/273=26.09 L/mol에 해당한다.In terms of weight per volume, the ideal gas volume at 45 ° C. corresponds to (22.4 L / mol (at 273 k) × (273 + 45)) / 273 = 26.09 L / mol.
따라서, 과산화수소 증기의 기체 농도 0.49%를 해당온도에서의 이상적인 기체 부피로 나누면, 즉, 0.49% / 26.09 (L/mol) = 0.0188 mol%에 해당하며, 따라서, 1000L 부피의 멸균챔버 내에 과산화수소 증기는 0.000188mol/L로 존재한다.Thus, dividing the gas concentration 0.49% of the hydrogen peroxide vapor by the ideal gas volume at that temperature, ie 0.49% / 26.09 (L / mol) = 0.0188 mol%, thus the hydrogen peroxide vapor in the 1000L volume of the sterilization chamber Present at 0.000188 mol / L.
이때, 과산화수소의 분자량은 34g/mol이므로, 이는 6.4mg/L의 농도로 표시될 수 있다.In this case, since the molecular weight of hydrogen peroxide is 34g / mol, it may be represented by a concentration of 6.4mg / L.
이상과 같은 방법으로, 제1습도센서 및 제2습도센서에 의해 과산화수소 농도를 측정할 수 있다.By the above method, the hydrogen peroxide concentration can be measured by the first humidity sensor and the second humidity sensor.
상술한 바와 같이, 과산화수소수를 고농도의 과산화수소수로 농축하여 멸균제로 사용함에 있어서, 멸균장치의 멸균챔버 내에서 상기 과산화수소의 농도를 측정하는 것은 용이하지 않다.As described above, in concentrating hydrogen peroxide water to a high concentration of hydrogen peroxide water and using it as a sterilizing agent, it is not easy to measure the concentration of hydrogen peroxide in the sterilization chamber of the sterilization apparatus.
하지만, 본 발명에서는, 멸균챔버 등과 같은 대상공간 내에, 제1습도센서 및 제2습도센서를 포함시켜, 이들 각각의 센서들에 의해 상대습도를 검출하고, 이들 상대습도의 차이에 의해 과산화수소의 농도를 용이하게 측정할 수 있다.In the present invention, however, the first humidity sensor and the second humidity sensor are included in a target space such as a sterilization chamber, and the relative humidity is detected by each of these sensors, and the concentration of hydrogen peroxide is determined by the difference in these relative humidity. Can be measured easily.
이상과 첨부된 도면을 참조하여 본 발명의 실시예를 설명하였지만, 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자는 본 발명이 그 기술적 사상이나 필수적인 특징을 변경하지 않고서 다른 구체적인 형태로 실시될 수 있다는 것을 이해할 수 있을 것이다. 그러므로 이상에서 기술한 실시예들은 모든 면에서 예시적인 것이며 한정적이 아닌 것으로 이해해야만 한다.Although embodiments of the present invention have been described above with reference to the accompanying drawings, those skilled in the art to which the present invention pertains may implement the present invention in other specific forms without changing the technical spirit or essential features thereof. You will understand that. Therefore, it should be understood that the embodiments described above are exemplary in all respects and not restrictive.
Claims (8)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR10-2016-0182591 | 2016-12-29 | ||
| KR1020160182591A KR101931102B1 (en) | 2016-12-29 | 2016-12-29 | A sterilizing apparatus and a method for measuring concentration of hydrogen peroxide of the sterilizing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2018124339A1 true WO2018124339A1 (en) | 2018-07-05 |
Family
ID=62709490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/KR2016/015521 Ceased WO2018124339A1 (en) | 2016-12-29 | 2016-12-29 | Sterilizing device and method for measuring hydrogen peroxide concentration of sterilizing device |
Country Status (2)
| Country | Link |
|---|---|
| KR (1) | KR101931102B1 (en) |
| WO (1) | WO2018124339A1 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR102438554B1 (en) * | 2020-03-26 | 2022-08-31 | (주)씨엠테크 | Sterilization apparatus and method of measuring hydrogen peroxide concentration of the sterilization apparatus |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0774263B1 (en) * | 1995-11-20 | 2003-03-12 | Bioquell UK Limited | Method and apparatus for hydrogen peroxide vapor sterilization |
| KR101087306B1 (en) * | 2009-09-28 | 2011-11-25 | 유영종 | Medical sterilization apparatus and method |
| KR101111388B1 (en) * | 2010-04-13 | 2012-02-24 | (주)우정비에스씨 | A Portable Sterilizer Using Hydrogen Peroxide Vapor |
| KR20140049347A (en) * | 2012-10-17 | 2014-04-25 | 우병훈 | Sterilizing method |
| KR101653173B1 (en) * | 2015-02-03 | 2016-09-02 | (주) 씨엠테크 | Hydrogen peroxide supply device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6953549B2 (en) * | 2003-07-15 | 2005-10-11 | Steris Inc. | System and method for determining concentration of sterilant |
| JP2007202628A (en) * | 2006-01-31 | 2007-08-16 | Daikin Ind Ltd | Sterilizer and sterilization system |
-
2016
- 2016-12-29 KR KR1020160182591A patent/KR101931102B1/en active Active
- 2016-12-29 WO PCT/KR2016/015521 patent/WO2018124339A1/en not_active Ceased
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0774263B1 (en) * | 1995-11-20 | 2003-03-12 | Bioquell UK Limited | Method and apparatus for hydrogen peroxide vapor sterilization |
| KR101087306B1 (en) * | 2009-09-28 | 2011-11-25 | 유영종 | Medical sterilization apparatus and method |
| KR101111388B1 (en) * | 2010-04-13 | 2012-02-24 | (주)우정비에스씨 | A Portable Sterilizer Using Hydrogen Peroxide Vapor |
| KR20140049347A (en) * | 2012-10-17 | 2014-04-25 | 우병훈 | Sterilizing method |
| KR101653173B1 (en) * | 2015-02-03 | 2016-09-02 | (주) 씨엠테크 | Hydrogen peroxide supply device |
Also Published As
| Publication number | Publication date |
|---|---|
| KR20180077837A (en) | 2018-07-09 |
| KR101931102B1 (en) | 2018-12-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2015008947A1 (en) | Sterilization apparatus and sterilization method using same | |
| EP3186563A1 (en) | Appliance for dehumidification and multi-function appliance for dehumidificaton or humidification | |
| KR101817185B1 (en) | Active dew point sensing and load lock venting to prevent condensation of workpieces | |
| WO2018124339A1 (en) | Sterilizing device and method for measuring hydrogen peroxide concentration of sterilizing device | |
| WO2018080070A1 (en) | Sterilization apparatus and sterilization method | |
| WO2019194327A1 (en) | Wafer storage container | |
| WO2016140449A1 (en) | Sterilization method and apparatus using the same | |
| WO2020175743A1 (en) | Continuous activated carbon regeneration apparatus using hydrothermal pressurization, having structure connected with filter, and continuous activated carbon regeneration method using same | |
| WO2021177671A1 (en) | Laundry dryer and laundry dryer control method | |
| WO2016200155A1 (en) | Humid air forming device, inspection device comprising same, and inspection method | |
| WO2017034057A1 (en) | Substrate treatment device and substrate treatment method | |
| JP2009509336A (en) | Method and apparatus for isolating and processing substrate edge regions | |
| WO2018124392A1 (en) | Reduced pressure drying apparatus and reduced pressure drying method | |
| KR102258695B1 (en) | A sterilizing apparatus and a method for measuring concentration of hydrogen peroxide of the sterilizing apparatus | |
| WO2017188746A1 (en) | Apparatus for measuring moisture of solid sample, method for measuring moisture content of solid sample, and method for analyzing imidization ratio | |
| WO2025127480A1 (en) | Sterilization device | |
| KR101596778B1 (en) | Water-drying apparatus of substrate and drying process thereof | |
| WO2021177527A1 (en) | Implant storage container | |
| WO2019160339A1 (en) | Sterilizer and sterilization method thereof | |
| WO2020153587A1 (en) | Sterilization system comprising independent type pump module and sterilization method thereof | |
| JPH03137977A (en) | Washing apparatus | |
| JP6117061B2 (en) | Substrate processing method and apparatus | |
| TWI601851B (en) | Tungsten oxide film hydrogen sensor | |
| US6236023B1 (en) | Cleaning process for rapid thermal processing system | |
| JPH11287743A (en) | Thermal desorbing/analyzing chamber for wafer process monitor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 16925810 Country of ref document: EP Kind code of ref document: A1 |
|
| NENP | Non-entry into the national phase |
Ref country code: DE |
|
| 122 | Ep: pct application non-entry in european phase |
Ref document number: 16925810 Country of ref document: EP Kind code of ref document: A1 |