JP2014155593A - Decontamination system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a decontamination system which does not require large-scape installations, e.g. a large-diameter duct or a heater for prevention of condensation, allows long-distance piping for each of a plurality of to-be-decontaminated chambers and supplies accurate amounts of a gas for decontamination to each of the chambers.SOLUTION: A decontamination system includes compression air generation means and decontamination liquid supply means and is provided with a mixing gas/liquid regulator and a gas generator for each of to-be-decontaminated chambers. The carrying distance of the mixing gas/liquid supply piping which communicates the mixing gas/liquid regulator with the gas generator is greater than the carrying distance of the decontamination liquid supply piping which communicates the decontamination supply means with the mixing gas/liquid regulator.

Description

  The present invention relates to a decontamination system that performs decontamination by generating a decontamination gas in a room such as an aseptic room, a clean room, or a hospital room.

  In a manufacturing site where pharmaceuticals or foods are manufactured, or in a medical site such as an operating room, it is important to maintain sterility in the room. In particular, in the decontamination of an aseptic room, which is a working room for pharmaceutical manufacturing, it is necessary to complete advanced decontamination validation in accordance with GMP (Good Manufacturing Practice).

  In recent years, hydrogen peroxide gas has been adopted for decontamination of a working room such as an aseptic room (hereinafter referred to as a decontamination target room) instead of formalin gas harmful to the human body. This hydrogen peroxide gas has a powerful sterilization effect, is inexpensive and easily available, and is effective as an environmentally friendly decontamination gas that eventually decomposes into oxygen and water. However, hydrogen peroxide gas has been conventionally used for decontamination of small spaces such as isolators and glove boxes. On the other hand, in order to use hydrogen peroxide gas for decontamination of a large space such as a decontamination target chamber, there is a problem that a large amount of hydrogen peroxide gas of a predetermined concentration must be stably supplied.

  Therefore, in the following Patent Document 1, as a decontamination gas generator, a sterilization liquid vaporizer that can easily control the concentration of sterilization gas (hydrogen peroxide gas) and can supply a large amount of sterilization gas (hydrogen peroxide gas). Proposed. This sterilizing liquid vaporizer sprays hydrogen peroxide water into air heated to a high temperature by a heating means to form hydrogen peroxide gas, and includes two temperature sensors on the downstream side of the spraying means. The heating means is controlled from the temperature difference between these temperature sensors to stabilize the hydrogen peroxide gas concentration.

JP 2003-339829 A

  A large amount of hydrogen peroxide gas generated by these decontamination gas generators is obtained by vaporizing hydrogen peroxide water and is in a mixed gas state of hydrogen peroxide and water vapor. This hydrogen peroxide gas has a low density and is supplied to the decontamination target chamber through a large-diameter duct. Therefore, in order to stably supply the hydrogen peroxide gas adjusted to a predetermined concentration by the decontamination gas generator to the decontamination target chamber, the duct is sufficiently warmed by a heater to prevent condensation in the duct. There is a need to. If the heat insulation by the heater is insufficient, the supplied hydrogen peroxide gas is condensed in the duct and the supply concentration and supply amount to the decontamination target chamber are insufficient. Further, the hydrogen peroxide solution generated by the condensation is heated, and there is a problem that the inside of the duct is corroded.

  In this way, in order to supply a large amount of hydrogen peroxide gas from the decontamination gas generator to the decontamination target chamber, large-diameter and large-scale duct work, heater equipment that keeps the duct warm, and corrosion-resistant materials There was a problem that a duct was necessary.

  Furthermore, in the pharmaceutical manufacturing site, the decontamination target room is not limited to one room, and it is necessary to decontaminate a plurality of decontamination target rooms at the same time. In this case, it is not efficient to provide a decontamination gas generator as in Patent Document 1 for each decontamination target chamber and to perform duct work for each decontamination gas generator. Therefore, a long-distance duct is arranged from a single decontamination gas generator to a plurality of decontamination target chambers, and branch ducts are arranged from this duct to each decontamination target chamber for simultaneous decontamination. Is called. In this case, condensation is likely to occur at the branching portion of the duct, and the distance from the decontamination gas generator to each decontamination target chamber is different, so how much hydrogen peroxide gas is supplied. There was a problem that it was not possible to grasp accurately.

  On the other hand, as a method of decontaminating each decontamination target chamber without using a large-diameter duct, high-density hydrogen peroxide solution before gasification is supplied to each decontamination target chamber through a small-diameter supply pipe. It is conceivable that gasification takes place in the vicinity of each decontamination target room or in the room. In this case, gasification in the vicinity of or in each decontamination target chamber can be performed by dropping the supplied hydrogen peroxide solution onto a small evaporator (a heating plate or the like).

  In addition, compared with a large-diameter duct for gas supply, construction of a small-diameter supply pipe for liquid supply is easy, and the cost can be reduced even if piping work is performed for each decontamination target room. Furthermore, since it is not necessary to heat the hydrogen peroxide solution to be supplied, it is not necessary to keep the supply pipe warm, and corrosion in the pipe is also reduced. However, in this method, the hydrogen peroxide solution always remains in the small-diameter supply pipe, and a large amount of dead liquid is generated in many long pipes arranged for each decontamination target chamber. For this reason, there was a problem that it was impossible to accurately grasp how much hydrogen peroxide solution was supplied to each decontamination target room.

  Therefore, the present invention addresses the above-mentioned problems, and does not require large-scale equipment such as a large-diameter duct or a condensation-preventing heater, and a long distance for each decontamination target room. It is an object of the present invention to provide a decontamination system that can supply a precise amount of decontamination gas for each chamber.

  In solving the above problems, the present inventors supply mixed mist obtained by mixing hydrogen peroxide water into compressed air using a small-diameter supply pipe to each decontamination target chamber using the supply pipe. The present invention was completed by vaporizing the mixed mist in the vicinity of the dyeing target room or in the room to generate hydrogen peroxide gas.

That is, according to the description of claim 1, the decontamination system according to the present invention is
A decontamination system (100) for decontaminating the inside of each decontamination target chamber using a decontamination gas for one or two or more decontamination target chambers (R1 to R4),
Compressed air generating means (10) for generating compressed air, and decontamination liquid supply means (20) for supplying a decontamination liquid that is a source of decontamination gas,
For each chamber to be decontaminated, a gas mixture liquid regulator (31 to 35) for adjusting a gas mixture liquid for decontamination obtained by mixing the compressed air and the decontamination liquid, and vaporizing the gas mixture liquid Gas generators (41 to 45) for generating decontamination gas, air supply pipes (11 to 15) communicating from the compressed air generating means to the gas-liquid regulator, and the decontamination A decontamination liquid supply pipe (21 to 25) communicating between the liquid supply means and the gas mixture liquid regulator, and a gas mixture liquid supply pipe communicating between the gas mixture liquid regulator and the gas generator (61-65)
The compressed air generation means, the decontamination liquid supply means, and the gas mixture liquid regulators are disposed at positions separated from the decontamination target chambers, and the gas generators are arranged in the corresponding decontamination target chambers. By arranging in the vicinity or indoors,
The conveyance distance of the gas-liquid supply pipe for each decontamination target chamber is longer than the conveyance distance of the corresponding decontamination liquid supply pipe.

Moreover, according to the description of claim 2, the present invention provides the decontamination system according to claim 1,
About one or more or all decontamination target rooms among one or more decontamination target rooms,
When the transport distance of the gas-liquid supply pipe included in each decontamination target chamber is Ax, and the transport distance of the corresponding decontamination liquid supply pipe is Bx,
Ax / Bx ≧ 3 (1)
(X is an integer of 1 to n and corresponds to each decontamination target room of n decontamination target rooms)
It is characterized by satisfying.

According to the description of claim 3, the present invention provides the decontamination system according to claim 1 or 2,
The compressed air supplied from the compressed air generating means to the gas-liquid regulator through the air supply pipe has a discharge pressure of 0.05 MPa and an air flow rate with respect to each gas-liquid regulator. 5 NL / min to 70 NL / min,
The decontamination liquid supplied from the decontamination liquid supply means to the gas mixture liquid regulator via the decontamination liquid supply pipe has a flow rate of 0.3 mL / min with respect to each gas mixture liquid regulator. It is ˜30 mL / min.

According to the description of claim 4, the present invention provides the decontamination system according to any one of claims 1 to 3,
Water supply means (70) for supplying water for conditioning each decontamination target chamber (R1 to R4),
For each decontamination target chamber, water supply piping (71 to 75) communicating between the water supply means and the gas-liquid regulator is provided,
Supplying water via the water supply pipe and supplying the decontamination liquid via the decontamination liquid supply pipe (21-25) to the gas-liquid regulator (31-35). Like switching
When water is supplied to the gas-liquid regulator, the gas-liquid regulator adjusts the humidified gas-liquid mixture obtained by mixing the compressed air and water, The gas mixture (41 to 45) is supplied to the gas generator (41 to 45) through the gas mixture supply pipe (61 to 65) to vaporize the humidified gas mixture to generate a humidifying gas composed of water vapor.
When the decontamination liquid is supplied to the gas mixture liquid regulator, the gas mixture liquid regulator adjusts a decontamination gas mixture liquid in which the compressed air and the decontamination liquid are mixed. A gas mixture for decontamination is supplied to the gas generator via the gas mixture liquid supply pipe to vaporize the gas mixture for humidification to generate a gas for decontamination.

According to the description of claim 5, the decontamination method according to the present invention is
Using the decontamination system according to any one of claims 1 to 3,
By supplying the decontamination liquid to the gas mixture liquid regulator, the inside of each decontamination target chamber is decontaminated with the decontamination gas vaporized by the gas generator.

Moreover, according to the description of claim 6, the decontamination method according to the present invention includes
Using the decontamination system according to claim 4,
First, by supplying water to the gas-liquid regulator, the humidity in each decontamination target chamber is adjusted to a preset value with the humidifying gas vaporized by the gas generator,
Next, by supplying the decontamination liquid to the gas-liquid mixture regulator, the inside of each decontamination target chamber after dehumidification is decontaminated with the decontamination gas vaporized by the gas generator. It is characterized by that.

  According to the structure of the said Claim 1, the decontamination liquid used as the generation source of decontamination gas is mixed with the compressed air which generate | occur | produced with the compressed air generation means by the gas-liquid regulator, and turns into a gas-liquid mixture. This mixed gas / liquid is supplied to the gas generator via the mixed gas / liquid supply pipe and gasified to become a decontamination gas. Here, the gas-liquid mixture is a mixture of compressed air and liquid, is in a high density state, and has a high transport speed. Therefore, a small-diameter pipe can be used as the gas-liquid supply pipe. Accordingly, even when there are a plurality of decontamination target chambers and the arrangement distance of the gas-liquid supply pipe to each decontamination target chamber is different, it is an appropriate distance for each decontamination target chamber and a long distance is supplied. Piping can be provided. This eliminates the need for large-scale equipment such as a large-diameter duct.

  Further, since the hydrogen peroxide solution in the gas mixture is in a liquid state, it is not necessary to keep the temperature of the gas mixture liquid supply pipe in order to prevent condensation. Therefore, even when there are a plurality of decontamination target chambers and a long distance supply pipe is provided for each decontamination target chamber, a large facility such as a condensation prevention heater is not required.

  If there are multiple decontamination target chambers, the compressed air generating means and the decontamination liquid supply means are common to the respective decontamination target chambers, while the mixed gas-liquid regulator and gas generator and the mixture connecting them are used. A gas-liquid supply pipe (hereinafter referred to as “decontamination unit”) is arranged for each decontamination target room. Accordingly, the compressed air generation means, the decontamination liquid supply means, and the gas mixture liquid regulators can be disposed at positions separated from the respective decontamination target chambers. On the other hand, each gas generator is disposed in the vicinity or in the corresponding decontamination target chamber. In this way, a separate decontamination unit is provided for each decontamination target chamber, the transport distance of the decontamination liquid supply pipe is shortened, and the transport distance of the gas mixture liquid supply pipe is lengthened.

  Thus, by shortening the transport distance of the decontamination liquid supply pipe, it is possible to accurately grasp the supply amount of the decontamination liquid to the gas-liquid mixture regulator. This makes it possible to accurately grasp the amount of decontamination liquid supplied to the gas generator for each decontamination target chamber, and to clarify the amount of decontamination gas released to the decontamination target chamber. . On the other hand, since the hydrogen peroxide solution in the gas-liquid mixture is in a liquid state and does not condense, the decontamination liquid can be accurately conveyed far by increasing the conveyance distance of the gas-liquid supply pipe. Furthermore, since the hydrogen peroxide solution in the pipe can be completely transported by the compressed air, no dead liquid remains in the pipe.

  Therefore, according to the present invention, it is not necessary to use large-scale equipment such as a large-diameter duct or a condensation-preventing heater, and a long-distance pipe is possible for each decontamination target chamber, and In addition, it is possible to provide a decontamination system capable of supplying an accurate amount of decontamination gas for each chamber.

  Moreover, according to the structure of the said Claim 2, in each decontamination object chamber, the conveyance distance Ax of mixed gas liquid supply piping is the distance of 3 times or more of the conveyance distance Bx of decontamination liquid supply piping. Also good. As a result, the transport distance of the gas-liquid supply pipe can be increased and the decontamination liquid can be transported accurately far. Therefore, also in the structure of the said Claim 2, the effect similar to Claim 1 can be achieved further.

  Moreover, according to the structure of the said Claim 3, even if the compressed air supplied to each gas-liquid regulator is a discharge pressure of 0.05 Mpa or more and an air flow rate is 5 NL / min-70 NL / min. Good. Moreover, the decontamination liquid supplied to each gas-liquid regulator may have a flow rate of 0.3 mL / min to 30 mL / min. This makes it possible to adjust the gas / liquid mixture in each gas / liquid regulator and to convey the gas / liquid mixture via the gas / liquid supply pipe. Therefore, also in the structure of the said Claim 3, the effect similar to Claim 1 can be achieved further.

  Moreover, according to the structure of the said Claim 4, the water supply means and water supply piping are further provided, and water supply and decontamination via a water supply piping are provided with respect to each gas-liquid regulator. You may make it switch supply of the decontamination liquid via liquid supply piping. When water is supplied to the gas-liquid regulator, the humidified gas-liquid mixture in which compressed air and water are mixed is adjusted by the gas-liquid regulator. This humidified gas-liquid mixture is supplied to the gas generator via the gas-liquid supply pipe and is vaporized to generate water vapor to humidify the decontamination target chamber. By this humidification, the humidity state in the decontamination target room can be brought into an appropriate state by decontamination with the decontamination gas.

  On the other hand, when the decontamination liquid is supplied to the gas mixture / liquid regulator, the gas mixture / liquid regulator adjusts the gas mixture for decontamination by mixing the compressed air and the decontamination liquid. This decontamination gas mixture liquid decontaminates the decontamination target chamber after humidity control. Therefore, in the structure of the said Claim 4, since decontamination can be performed after performing humidity control of the decontamination object chamber, the effect similar to Claim 1 can be achieved further.

It is a schematic block diagram of the decontamination system which concerns on 1st Embodiment. It is a schematic diagram which shows the relationship between the decontamination effect by hydrogen peroxide gas (D value), and the indoor relative humidity at that time. It is a schematic block diagram of the decontamination system which concerns on 2nd Embodiment.

  Hereinafter, each embodiment of the decontamination system according to the present invention will be described. In addition, this invention is not limited to each embodiment shown below.

First embodiment:
First, a first embodiment of a decontamination system according to the present invention will be described with reference to the drawings. FIG. 1 is a schematic configuration diagram of a decontamination system 100 according to the first embodiment. In the first embodiment, as shown in FIG. 1, aseptic rooms (clean rooms) including four rooms having different sizes are used as the decontamination target rooms R1 to R4. Between each decontamination object room, a door is provided, respectively, and these doors may be decontaminated in a released state, or these doors may be decontaminated in a closed state. . In the first embodiment, decontamination is performed with these doors open at the time of decontamination.

  In FIG. 1, the decontamination system 100 includes a common air compressor 10 and a hydrogen peroxide tank 20 in each of the decontamination target chambers R1 to R4. The decontamination target chambers R1 to R4 include ejectors 31 to 35, evaporators 41 to 45, and circulation fans 51 to 55 corresponding to the respective chambers.

  The air compressor 10 acts as compressed air generating means for generating compressed air as a carrier gas for conveying hydrogen peroxide water. The air compressor 10 is disposed at a position away from the decontamination target chambers R1 to R4.

  The hydrogen peroxide water tank 20 functions as a decontamination liquid supply means for storing hydrogen peroxide water that is a generation source of hydrogen peroxide gas as a decontamination gas. The hydrogen peroxide tank 20 is disposed in the vicinity of the air compressor 10 at a position away from the decontamination target chambers R1 to R4. Here, the concentration of the hydrogen peroxide solution stored in the hydrogen peroxide solution tank 20 is not particularly limited, but generally, 30 to 35% by weight is used in consideration of handling of dangerous substances. Is preferred.

  The ejectors 31 to 35 act as a gas-liquid regulator for adjusting a mixed mist obtained by mixing hydrogen peroxide water in compressed air. The ejectors 31 to 35 are disposed in the vicinity of the air compressor 10 and the hydrogen peroxide solution tank 20 at positions away from the decontamination target chambers R1 to R4.

  The evaporators 41 to 45 vaporize the mixed mist containing the hydrogen peroxide solution conveyed from the ejectors 31 to 35 to form a mixed gas of hydrogen peroxide and water vapor (hereinafter referred to as “hydrogen peroxide gas”). Acts as a gas generator. The evaporators 41 to 45 have a heated evaporation plate and evaporate the supplied mixed mist. The temperature of the evaporation plate only needs to have a sufficient amount of heat for vaporization, but generally only about 110 to 200 ° C. The evaporators 41 to 45 are disposed outside the upper walls of the decontamination target chambers R1 to R4.

  The circulation fans 51 to 55 uniformly circulate the hydrogen peroxide gas released from the evaporators 41 to 45 to the decontamination target chambers R1 to R4. The circulation fans 51 to 55 are disposed in the respective decontamination target chambers below the evaporators 41 to 45. Hydrogen peroxide gas released from the discharge ports of the evaporators 41 to 45 is supplied to the outlets of the circulation fans 51 to 55 and circulates in the respective decontamination target chambers.

  In the widest decontamination target chamber R2, two sets of decontamination units (two ejectors 32 and 33, two evaporators 42 and 43, and two mixed mist pipes 62 and 63 described later) and two circulation fans are provided. 52 and 53 are arranged. This is because the volume of the decontamination target chamber R2 is large, and a large amount of hydrogen peroxide gas is supplied only from one set of decontamination units, so that hydrogen peroxide gas is divided into two sets of decontamination units from two locations. It is because decontamination efficiency becomes high by discharge | releasing. Depending on the size of the decontamination target room, more than two sets of decontamination units may be provided in one room. Even when a plurality of decontamination units are provided in one room in this way, the piping has a small diameter, and there is no problem in terms of equipment costs.

  In FIG. 1, the decontamination system 100 includes hydrogen pipes 11 to 15 that connect the air compressor 10 and ejectors 31 to 35, hydrogen peroxide water tank 20 and ejectors 31 to 35 that communicate with each other. Water pipes 21 to 25, and mixed mist pipes 61 to 65 communicating the ejectors 31 to 35 and the evaporators 41 to 45 are provided.

  The air pipes 11 to 15 communicate the discharge port of the air compressor 10 and the drive flow path (not shown) of the ejectors 31 to 35. Open / close valves 11a to 15a for controlling the supply of compressed air are provided in the pipes of the air pipes 11 to 15, respectively. Here, the material and the pipe diameter of the air pipes 11 to 15 are not particularly limited, but in general, a stainless steel pipe having an inner diameter of 1 to 10 mm is preferable. Although not shown in FIG. 1, an air dryer, an air regulator, an auto drain, an oil mist separator, other filters, and the like are provided in the pipe line between the air compressor 10 and the air pipes 11 to 15. Also good.

  The hydrogen peroxide water pipes 21 to 25 communicate the supply port of the hydrogen peroxide water tank 20 and the suction flow paths (not shown) of the ejectors 31 to 35. Tube pumps 21a to 25a for controlling the supply of the hydrogen peroxide solution are provided on the pipes of the hydrogen peroxide solution pipes 21 to 25, respectively. Here, the material and the pipe diameter of the hydrogen peroxide water pipes 21 to 25 are not particularly limited as long as they can be used for the hydrogen peroxide water, but are generally stainless steel pipes having an inner diameter of 1 to 10 mm. It is preferable.

  The mixed mist pipes 61 to 65 communicate the discharge flow paths of the ejectors 31 to 35 with the evaporators 41 to 45. The mixed mist pipes 61 to 65 have a long distance from the vicinity of the air compressor 10 and the hydrogen peroxide tank 20 to the positions of the evaporators 41 to 45 disposed outside the upper walls of the decontamination target chambers R1 to R4. Has been. Here, with respect to the material and pipe diameter of the mixed mist pipes 61 to 65, it is preferable that a necessary amount of hydrogen peroxide mist per unit time can be conveyed over a long distance, and generally the inner diameter is 1 to 10 mm. The stainless steel tube is preferable.

  In this manner, the decontamination target chambers R1 to R4 are provided with the air pipes 11 to 15, the hydrogen peroxide water pipes 21 to 25, and the mixed mist pipes 61 to 65, respectively. Each time, the hydrogen peroxide gas can be released separately, and accurate decontamination can be performed for each chamber.

  As can be seen from FIG. 1, the transport distance of the mixed mist pipes 61 to 65 is longer than the transport distance of the air pipes 11 to 15 or the transport distance of the hydrogen peroxide water pipes 21 to 25. Although the conveyance distance of the mixed mist by this mixed mist piping 61-65 is not specifically limited, Usually, about 3-100 m can be conveyed. On the other hand, the transport distance of the air pipes 11 to 15 or the transport distance of the hydrogen peroxide water pipes 21 to 25 can be shortened.

  In the present invention, the transport distance of the mixed mist pipes 61 to 65 is Ax, the transport distance of the hydrogen peroxide water pipes 21 to 25 is Bx (x is an integer of 1 to n, and there are n chambers to be decontaminated). (Ax / Bx) is 3 or more, and may be 5 or more, further 10 or more as necessary. In this manner, by increasing the transport distance of the mixed mist pipes 61 to 65 with respect to the transport distance of the hydrogen peroxide water pipes 21 to 25, the location of the hydrogen peroxide water tank 20 to each decontamination target chamber is increased. The hydrogen peroxide solution can be stably conveyed in a mixed mist state even at a long distance.

  In the first embodiment, the mixed mist is a mixture of compressed air and hydrogen peroxide water, is in a high density state, and has a high transport speed. Therefore, small-diameter pipes are used for the mixed mist pipes 61 to 65. Can do. Therefore, the long distance mixed mist pipes 61 to 65 can be provided for each decontamination target chamber. This eliminates the need for large-scale equipment such as a large-diameter duct.

  Further, since the hydrogen peroxide solution in the mixed mist is in a liquid state, it is not necessary to keep the mixed mist pipes 61 to 65 warm in order to prevent condensation. Therefore, even when a long distance pipe is provided for each decontamination target room, a large facility such as a condensation prevention heater is not required.

  Thus, the supply amount of the hydrogen peroxide solution to the ejectors 31 to 35 can be accurately grasped by shortening the transport distance of the hydrogen peroxide solution pipes 21 to 25. This makes it possible to accurately grasp the amount of the hydrogen peroxide solution supplied to the evaporators 41 to 45 for each decontamination target chamber, and the amount of the hydrogen peroxide gas released into the decontamination target chamber. Become clear. On the other hand, since the hydrogen peroxide solution in the mixed mist is in a liquid state and does not condense, the transport distance of the mixed mist pipes 61 to 65 can be lengthened to accurately convey the hydrogen peroxide solution far. . Furthermore, since the hydrogen peroxide solution in the mixed mist pipes 61 to 65 can be completely transported by the compressed air, no dead liquid remains in the pipe.

  Next, a decontamination method for decontaminating the decontamination target chambers R1 to R4 using the decontamination system 100 according to the first embodiment will be described.

  In the first embodiment, the four decontamination target chambers R1 to R4 are decontaminated with the same gas generation time. Since the size of each decontamination target room is different, the amount of hydrogen peroxide gas to be released per unit time is calculated for each decontamination target room. From these gas discharge amounts, the amount of the hydrogen peroxide solution supplied from the hydrogen peroxide solution tank 20 through the hydrogen peroxide solution pipes 21 to 25 to the ejectors 31 to 35 corresponding to the respective decontamination target chambers is determined. calculate. In addition, it is preferable to set each chamber before decontamination to a predetermined condition using a temperature controller and a humidity controller.

  Next, the decontamination operation is started. First, the on-off valves 11a to 15a of the air pipes 11 to 15 are opened, and compressed air is supplied from the air compressor 10 to the drive flow paths of the ejectors 31 to 35 through the air pipes 11 to 15. Here, it is preferable that the compressed air supplied to the ejectors 31 to 35 has a discharge pressure of 0.05 MPa or more and an air flow rate of 5 to 70 NL / min. This air flow rate may be appropriately set according to the concentration and amount of the hydrogen peroxide solution supplied to each decontamination target chamber and the distance to each decontamination target chamber.

  Next, the tube pumps 21a to 25a of the hydrogen peroxide water pipes 21 to 25 are operated, and the hydrogen peroxide water tank 20 is overoxidized to the suction passages of the ejectors 31 to 35 via the hydrogen peroxide water pipes 21 to 25. Supply hydrogen water. The supply amount of the hydrogen peroxide solution corresponds to the amount calculated as described above for the ejectors 31 to 35. Here, the concentration of the hydrogen peroxide solution supplied to the ejectors 31 to 35 is not particularly limited, but generally 30 to 35% by weight of commercially available water may be used, or these These may be used after being concentrated or diluted. The hydrogen peroxide solution supplied to the ejectors 31 to 35 may have a flow rate of 0.3 to 30 mL / min, or may be adjusted to 0.5 to 15 mL / min. .

  When the amount of the hydrogen peroxide solution is in the above range and the amount of the compressed air is in the above range, the mixed mist mixed with the hydrogen peroxide solution is long through the mixed mist pipes 61 to 65. It can be transported even at a distance.

  Through the above-described operation, the hydrogen peroxide solution and the compressed air are mixed and mist in the ejectors 31 to 35, and are supplied to the evaporators 41 to 45 from the discharge flow paths of the ejectors 31 to 35 via the mixed mist pipes 61 to 65.

  In the evaporators 41 to 45, the mixed mist evaporates to generate hydrogen peroxide gas. The hydrogen peroxide gas vaporized in the evaporators 41 to 45 is supplied from the discharge ports of the evaporators 41 to 45 to the blowout ports of the circulation fans 51 to 55 installed in the decontamination target chambers R1 to R4. As a result, hydrogen peroxide gas is released into each decontamination target chamber, and each decontamination target chamber is uniformly decontaminated.

  In this way, hydrogen peroxide gas is released for a predetermined time. When a predetermined time has elapsed, the tube pumps 21a to 25a of the hydrogen peroxide solution pipes 21 to 25 are stopped, and the supply of the hydrogen peroxide solution is stopped. At this stage, the compressed air is supplied to the ejectors 31 to 35 through the air pipes 11 to 15, and all the remaining hydrogen peroxide solution in the mixed mist pipes 61 to 65 is sent to the evaporators 41 to 45. It is done. As a result, a predetermined amount of hydrogen peroxide gas is accurately discharged to the decontamination target chambers R1 to R4.

  Next, the on-off valves 11a to 15a of the air pipes 11 to 15 are closed, and the supply of compressed air is stopped. Thereafter, the hydrogen peroxide gas in the room is discharged, the room is aired, and the decontamination operation is completed. The above operations are preferably performed by automatic control by a microcomputer.

Second embodiment:
Next, a second embodiment of the decontamination system according to the present invention will be described. The second embodiment is a decontamination system that can control the humidity in each decontamination target chamber prior to decontamination with hydrogen peroxide gas. In the decontamination with hydrogen peroxide, the room temperature and humidity at the time of decontamination, especially humidity conditions are important. FIG. 2 is a schematic diagram showing the relationship between the decontamination effect (D value) by hydrogen peroxide gas and the relative humidity in the room at that time. As shown in FIG. 2, in the decontamination with hydrogen peroxide gas, it can be seen that the decontamination effect is high (D value is low) when the indoor relative humidity is 40 to 60%.

  Here, the D value (Decimal reduction value) means the time (minutes) required to reduce the initial number of bacteria to 1/10 (90% kill) under a certain decontamination condition. It can be said that decontamination can be performed in a short time as the D value is low, and the decontamination effect is high.

  A second embodiment of the decontamination system according to the present invention will be described with reference to the drawings. FIG. 3 is a schematic configuration diagram of a decontamination system 200 according to the second embodiment. In the second embodiment, as in the first embodiment, aseptic rooms (clean rooms) including four rooms having different sizes are used as the decontamination target rooms R1 to R4. Between each decontamination object room, a door is provided, respectively, and these doors may be decontaminated in a released state, or these doors may be decontaminated in a closed state. . In the second embodiment, humidification and decontamination were performed with all these doors closed.

  In FIG. 3, the decontamination system 200 includes an air compressor 10, a hydrogen peroxide tank 20, and a distilled water tank 70 that are common to the decontamination target chambers R1 to R4. The decontamination target chambers R1 to R4 include ejectors 31 to 35, evaporators 41 to 45, and circulation fans 51 to 55 corresponding to the respective chambers.

  In the second embodiment, the configuration of the air compressor 10 and the hydrogen peroxide tank 20 is the same as that of the first embodiment, and the description thereof is omitted.

  In the second embodiment, unlike the first embodiment, a distilled water tank 70 is provided. The distilled water tank 70 functions as distilled water supply means for storing distilled water that is a source of water vapor for conditioning the interior of the decontamination target chamber. The distilled water tank 70 is disposed in the vicinity of the air compressor 10 and the hydrogen peroxide water tank 20 at a position away from the decontamination target chambers R1 to R4.

  The ejectors 31 to 35 act as a gas-liquid adjuster for adjusting a mixed mist (mixed gas / liquid for decontamination) in which hydrogen peroxide is mixed in compressed air, as in the first embodiment. It also functions as a gas-liquid regulator for adjusting a mixed mist (mixed liquid for humidification) in which distilled water is mixed in compressed air. For this reason, in the second embodiment, a switching valve (not shown) is provided in the suction flow paths (not shown) of the ejectors 31 to 35 so that liquid can be supplied from two paths.

  One path is the same as that in the first embodiment, and communicates the suction flow paths of the ejectors 31 to 35 and the hydrogen peroxide tank 20. The other path connects the suction flow paths of the ejectors 31 to 35 and the distilled water tank 70. The ejectors 31 to 35 are disposed in the vicinity of the air compressor 10, the hydrogen peroxide tank 20, and the distilled water tank 70 at positions away from the decontamination target chambers R 1 to R 4.

  The evaporators 41 to 45 act as gas generators that vaporize the mixed mist containing distilled water or hydrogen peroxide solution conveyed from the ejectors 31 to 35 to form water vapor or hydrogen peroxide gas. In the second embodiment, evaporators 41 to 45 having the same evaporation plate as in the first embodiment are employed.

  The circulation fans 51 to 55 uniformly circulate water vapor or hydrogen peroxide gas discharged from the evaporators 41 to 45 to the decontamination target chambers R1 to R4. In the second embodiment, similarly to the first embodiment, the circulation fans 51 to 55 are disposed in the decontamination target chambers below the evaporators 41 to 45. Water vapor or hydrogen peroxide gas discharged from the discharge ports of the evaporators 41 to 45 is supplied to the outlets of the circulation fans 51 to 55 and circulates in the respective decontamination target chambers.

  Also in the second embodiment, the widest decontamination target chamber R2 includes two sets of decontamination units (two ejectors 32 and 33, two evaporators 42 and 43, and two mixed mist pipes 62 and 63. ) And two circulation fans 52 and 53 are disposed. This is because the volume of the decontamination target chamber R2 is large, and a large amount of water vapor or hydrogen peroxide gas is supplied from only one set of decontamination units, so that two sets of decontamination units divide the water vapor or excess water from two places. This is because the humidity control efficiency and the decontamination efficiency are increased by releasing the hydrogen oxide gas. Depending on the size of the decontamination target room, more than two sets of decontamination units may be provided in one room. Even when a plurality of decontamination units are provided in one room in this way, the piping has a small diameter, and there is no problem in terms of equipment costs.

  In FIG. 3, the decontamination system 200 includes hydrogen pipes 11 to 15 that communicate the air compressor 10 and the ejectors 31 to 35, hydrogen peroxide water that communicates the hydrogen peroxide tank 20 and the ejectors 31 to 35. Water pipes 21 to 25, distilled water pipes 71 to 75 that communicate the distilled water tank 70 and the ejectors 31 to 35, and mixed mist pipes 61 to 65 that communicate the ejectors 31 to 35 and the evaporators 41 to 45. I have.

  In this 2nd Embodiment, the structure of the air piping 11-15, the hydrogen peroxide solution piping 21-25, and the mixing mist piping 61-65 is the same as that of the said 1st Embodiment, The description is abbreviate | omitted.

  The distilled water pipes 71 to 75 communicate the supply port of the distilled water tank 70 and the suction flow paths (not shown) of the ejectors 31 to 35. As described above, the suction flow path is provided with a switching valve (not shown) and is provided with two paths. Tube pumps 71a to 75a for controlling the supply of hydrogen peroxide water are provided in the pipes of the distilled water pipes 71 to 75, respectively. Here, although the material and pipe diameter of the distilled water pipes 71 to 75 are not particularly limited, in general, a stainless steel pipe having an inner diameter of 1 to 10 mm is preferable.

  As described above, the air pipes 11 to 15, the hydrogen peroxide pipes 21 to 25, the distilled water pipes 71 to 75, and the mixed mist pipes 61 to 65 are disposed for the decontamination target chambers R1 to R4, respectively. Thus, water vapor and hydrogen peroxide gas can be separately released for each decontamination target chamber, and accurate humidity control and decontamination can be performed for each chamber.

  As can be seen from FIG. 3, the transport distance of the mixed mist pipes 61 to 65 is the transport distance of the air pipes 11 to 15, the transport distance of the hydrogen peroxide water pipes 21 to 25, or the transport distance of the distilled water pipes 71 to 75. Longer distance. Although the conveyance distance of the mixed mist by this mixed mist piping 61-65 is not specifically limited, Usually, about 3-100 m can be conveyed. On the other hand, the conveyance distance of the air piping 11-15, the conveyance distance of the hydrogen peroxide water piping 21-25, or the conveyance distance of the distilled water piping 71-75 can be shortened.

  In the second embodiment, the mixed mist is a mixture of compressed air and distilled water or hydrogen peroxide water, is in a high density state, and has a high conveyance speed. Therefore, the mixed mist pipes 61 to 65 have small diameter pipes. Can be used. Therefore, the long distance mixed mist pipes 61 to 65 can be provided for each decontamination target chamber. This eliminates the need for large-scale equipment such as a large-diameter duct.

  Moreover, since distilled water or hydrogen peroxide solution in the mixed mist is in a liquid state, it is not necessary to keep the mixed mist pipes 61 to 65 warm in order to prevent condensation. Therefore, even when a long distance pipe is provided for each decontamination target room, a large facility such as a condensation prevention heater is not required.

  Thus, the supply amount of the hydrogen peroxide solution to the ejectors 31 to 35 can be accurately grasped by shortening the transport distance of the hydrogen peroxide solution pipes 21 to 25. This makes it possible to accurately grasp the amount of the hydrogen peroxide solution supplied to the evaporators 41 to 45 for each decontamination target chamber, and the amount of the hydrogen peroxide gas released into the decontamination target chamber. Become clear.

  On the other hand, since distilled water or hydrogen peroxide solution in the mixed mist is in a liquid state and does not condense, the transport distance of the mixed mist pipes 61 to 65 is increased to accurately transport the hydrogen peroxide solution far. be able to. Furthermore, since the distilled water or the hydrogen peroxide solution in the mixed mist pipes 61 to 65 can be completely conveyed by the compressed air, no dead liquid remains in the pipe.

  Next, a decontamination method for decontaminating the decontamination target chambers R1 to R4 using the decontamination system 200 according to the second embodiment will be described.

  In the second embodiment, first, the relative humidity of the decontamination target chambers R1 to R4 is adjusted to a predetermined value. As described above, the relative humidity in the room is preferably 40 to 60%. However, as described above, the hydrogen peroxide gas released into the room by decontamination contains water vapor, and the indoor humidity increases with the passage of the decontamination time. Therefore, the relative humidity at the start of decontamination may be set slightly lower than 40% so that the time during which the relative humidity is maintained at 40 to 60% is the longest from the start to the end of decontamination. Good.

  First, the humidity control operation is started. The on-off valves 11a to 15a of the air pipes 11 to 15 are opened, and compressed air is supplied from the air compressor 10 to the drive flow paths of the ejectors 31 to 35 via the air pipes 11 to 15. Here, the discharge pressure and the air flow rate of the compressed air supplied to the ejectors 31 to 35 are the same as the compressed air in the decontamination operation of the first embodiment.

  Next, the tube pumps 71a to 75a of the distilled water pipes 71 to 75 are operated, and distilled water is supplied from the distilled water tank 70 to the suction flow paths of the ejectors 31 to 35 via the distilled water pipes 71 to 75. At this time, the suction flow paths of the ejectors 31 to 35 need to be on the distilled water pipes 71 to 75 side by switching a switching valve (not shown). Here, the amount of distilled water supplied to the ejectors 31 to 35 may be approximately the same as the amount of hydrogen peroxide water in the decontamination operation of the first embodiment.

  By the above-described operation, distilled water and compressed air are gas-liquid mist in the ejectors 31 to 35, and are supplied from the discharge passages of the ejectors 31 to 35 to the evaporators 41 to 45 via the mixing mist pipes 61 to 65.

  In the evaporators 41 to 45, the mixed mist is evaporated to generate water vapor. The water vapor evaporated in the evaporators 41 to 45 is supplied from the outlets of the evaporators 41 to 45 to the outlets of the circulation fans 51 to 55 installed in the decontamination target chambers R1 to R4. As a result, water vapor is released into each decontamination target chamber, and each decontamination target chamber is uniformly conditioned.

  Here, a temperature sensor and a humidity sensor (both not shown) are installed in the decontamination target chambers R1 to R4. When the temperature and relative humidity of the decontamination target chambers R1 to R4 are within the set range with the progress of the humidity control operation, the tube pumps 71a to 75a of the distilled water pipes 71 to 75 are stopped, and the supply of distilled water is stopped. At this stage, the compressed air is supplied to the ejectors 31 to 35 via the air pipes 11 to 15, and all the remaining distilled water in the mixed mist pipes 61 to 65 is sent to the evaporators 41 to 45. .

  In order for the relative humidity of each decontamination target room to be within the set range, a time difference occurs for each room. Therefore, it is necessary to control each room individually. Once the relative humidity of the decontamination target room that has fallen within the set range has decreased, the supply of distilled water is started again, and humidity control is performed when the relative humidity of all rooms is within the set range. finish.

  Next, the decontamination operation is started. Also in the second embodiment, the four decontamination target chambers R1 to R4 are decontaminated with the same gas generation time. The amount of hydrogen peroxide gas to be released per unit time for each decontamination target room and the excess amount supplied from the hydrogen peroxide water tank 20 to the ejectors 31 to 35 via the hydrogen peroxide water pipes 21 to 25. Calculation of the amount of hydrogen oxide water is the same as in the first embodiment.

  Next, the decontamination operation is started. The on-off valves 11a to 15a of the air pipes 11 to 15 are opened, and compressed air is supplied from the air compressor 10 to the drive flow paths of the ejectors 31 to 35 via the air pipes 11 to 15. Here, the discharge pressure and the air flow rate of the compressed air supplied to the ejectors 31 to 35 are the same as the compressed air in the decontamination operation of the first embodiment.

  Next, the switching valves (not shown) of the suction flow paths of the ejectors 31 to 35 are switched to the hydrogen peroxide water pipes 21 to 25 side. Thereafter, the tube pumps 21a to 25a of the hydrogen peroxide water pipes 21 to 25 are operated, and the hydrogen peroxide is supplied from the hydrogen peroxide water tank 20 to the suction passages of the ejectors 31 to 35 via the hydrogen peroxide water pipes 21 to 25. Supply water. Here, the hydrogen peroxide solution supplied to the ejector 31 is the same as the amount of the hydrogen peroxide solution in the decontamination operation of the first embodiment. The supply amount of the hydrogen peroxide solution corresponds to the amount calculated as described above for the ejectors 31 to 35.

  By the above-described operation, the hydrogen peroxide solution and the compressed air are gas-liquid mist in the ejectors 31 to 35, and are supplied from the discharge passages of the ejectors 31 to 35 to the evaporators 41 to 45 through the mixing mist pipes 61 to 65. .

  In the evaporators 41 to 45, the mixed mist evaporates to generate hydrogen peroxide gas. The hydrogen peroxide gas vaporized in the evaporators 41 to 45 is supplied from the discharge ports of the evaporators 41 to 45 to the blowout ports of the circulation fans 51 to 55 installed in the decontamination target chambers R1 to R4. As a result, hydrogen peroxide gas is released into each decontamination target chamber, and each decontamination target chamber is uniformly decontaminated.

  In this way, hydrogen peroxide gas is released for a predetermined time. When a predetermined time has elapsed, the tube pumps 21a to 25a of the hydrogen peroxide solution pipes 21 to 25 are stopped, and the supply of the hydrogen peroxide solution is stopped. At this stage, the compressed air is supplied to the ejectors 31 to 35 through the air pipes 11 to 15, and all the remaining hydrogen peroxide solution in the mixed mist pipes 61 to 65 is sent to the evaporators 41 to 45. It is done. As a result, a predetermined amount of hydrogen peroxide gas is accurately released to the decontamination target chambers R1 to R4.

  Next, the on-off valves 11a to 15a of the air pipes 11 to 15 are closed, and the supply of compressed air is stopped. Thereafter, the hydrogen peroxide gas in the room is discharged, the room is aired, and the decontamination operation is completed. The above operations are preferably performed by automatic control by a microcomputer.

  Hereinafter, based on each said embodiment, the following decontamination operation of each Example was performed, respectively.

Example 1 was implemented based on the first embodiment. In Example 1, the decontamination target chamber having a volume different from that of the first embodiment described with reference to FIG. 1 was decontaminated. The decontamination target chamber of Example 1 is a clean room of a pharmaceutical production line consisting of four large and small chambers, and the volume of each chamber is shown in Table 1. In particular, the volume of the fourth chamber was very large at 258 m ³ . The decontamination system according to the first embodiment was applied to these decontamination target rooms. Table 1 shows the number of decontamination units arranged for each chamber. For the fourth chamber having a large volume, five sets of decontamination units were arranged.

  In Example 1, a stainless steel pipe (SUS304) having an inner diameter of 6 mm was used as the mixed mist pipe. As shown in Table 1, the value of (Ax / Bx) representing the ratio between the transport distance Ax of the mixed mist pipe and the transport distance Bx of the hydrogen peroxide solution pipe was 3.5 to 13. Thus, in the present Example 1, the conveyance distance of the mixing mist piping which conveys the mixed mist of hydrogen peroxide solution was long.

  Next, the 6 log reduction BI required for confirming the decontamination effect was set at a predetermined position in each chamber. In Example 1, all the doors between the rooms were opened. Moreover, although humidity control of each chamber was not performed, each chamber had a temperature of about 25 ° C. and a relative humidity of about 35%. From this state, a decontamination operation according to the first embodiment was performed, and all the rooms released a necessary amount of hydrogen peroxide gas over a predetermined time.

  The room temperature of each room after completion of the decontamination operation was about 30 ° C., and the relative humidity at that time was about 55%. After stopping the release of hydrogen peroxide gas, indoor aeration was performed to remove the hydrogen peroxide gas in each decontamination target chamber, and then all BIs were collected.

回収したＢＩは、所定の方法で培養し滅菌の程度を判定した。本実施例１においては、使用したＢＩが６対数減少用のものであり、回収した全てのＢＩの滅菌指標菌が全到死した条件を６対数減少が達成されたものとして判定した。表１の除染効果の欄には、６対数減少が達成されたものを「１０^-6」として表示した。表１から分かるように、全ての除染対象室において６対数減少が達成されており、混合ミスト配管の搬送距離が長い場合であっても高度な除染バリデーションが可能となる。

The recovered BI was cultured by a predetermined method to determine the degree of sterilization. In the present Example 1, the used BI was for 6 log reduction, and the conditions under which all the collected BI sterilization indicator bacteria were completely killed were determined to have achieved 6 log reduction. In the column of the decontamination effect in Table 1, those that achieved a 6 log reduction were displayed as “10 ⁻⁶ ”. As can be seen from Table 1, a 6 log reduction has been achieved in all the decontamination target chambers, and advanced decontamination validation is possible even when the transport distance of the mixed mist pipe is long.

Example 2 was implemented based on the second embodiment. In Example 2, decontamination target chambers having different numbers and volumes from those of the second embodiment described with reference to FIG. 2 were decontaminated. The decontamination target chamber of Example 2 is a clean room of a pharmaceutical production line consisting of five large and small chambers. Table 2 shows the volume of each chamber. In particular, the volume of the third chamber was very large at 313 m ³ . The decontamination system according to the second embodiment was applied to these decontamination target rooms. Table 2 shows the number of decontamination units arranged for each chamber. Six sets of decontamination units were arranged for the third chamber having a large volume.

  In Example 2, a stainless steel pipe (SUS304) having an inner diameter of 6 mm was used as the mixed mist pipe. As shown in Table 2, the value of (Ax / Bx) representing the ratio between the transport distance Ax of the mixed mist pipe and the transport distance Bx of the hydrogen peroxide water pipe was 3 to 18.5. Thus, in the present Example 2, the conveyance distance of the mixing mist piping which conveys the mixed mist of hydrogen peroxide solution was long.

  Next, the 6 log reduction BI required for confirming the decontamination effect was set at a predetermined position in each chamber. In Example 2, all the doors between the rooms were closed. Next, the humidity control operation was performed according to the second embodiment, and the relative humidity was adjusted to about 40% at 26 to 28 ° C. in each chamber. Next, the decontamination operation was performed according to the second embodiment, and a necessary amount of hydrogen peroxide gas was released from all the rooms over a predetermined time.

  The room temperature of each room after completion of the decontamination operation was 30 to 32 ° C., and the relative humidity at that time was 50 to 60%. After stopping the release of hydrogen peroxide gas, indoor aeration was performed to remove the hydrogen peroxide gas in each decontamination target chamber, and then all BIs were collected.

回収したＢＩは、所定の方法で培養し滅菌の程度を判定した。本実施例２においては、使用したＢＩが６対数減少用のものであり、回収した全てのＢＩの滅菌指標菌が全到死した条件を６対数減少が達成されたものとして判定した。表２の除染効果の欄には、６対数減少が達成されたものを「１０^-6」として表示した。表２から分かるように、全ての除染対象室において６対数減少が達成されており、混合ミスト配管の搬送距離が長い場合であっても高度な除染バリデーションが可能となる。

The recovered BI was cultured by a predetermined method to determine the degree of sterilization. In this Example 2, the used BI was for 6 log reduction, and the conditions under which all the collected BI sterilization indicator bacteria died completely were judged as having achieved 6 log reduction. In the column of the decontamination effect in Table 2, “10 ⁻⁶ ” is displayed as the result of 6 log reduction. As can be seen from Table 2, a 6 log reduction is achieved in all the decontamination target chambers, and advanced decontamination validation is possible even when the transport distance of the mixed mist pipe is long.

  As described above, as is clear from the above embodiments, the present invention does not require large-scale equipment such as a large-diameter duct and a condensation prevention heater, and each chamber can be used for a plurality of decontamination target chambers. Therefore, it is possible to provide a decontamination system that can provide long-distance piping for each chamber and that can supply an accurate amount of decontamination gas for each chamber.

In carrying out the present invention, the following various modifications are not limited to the above embodiments.
(1) In each of the above embodiments, the decontamination target chamber consisting of four or five chambers is decontaminated, but the present invention is not limited to this, and only one chamber is targeted by the decontamination system of the present invention. You may make it dye, or you may make it make object 10 rooms or more.
(2) In Example 1 described above, humidity conditioning prior to decontamination is not performed, but dehumidification may be performed after humidity conditioning is performed by a humidity controller provided in each chamber.
(3) In each of the above embodiments, an air compressor is employed as the compressed air generating means. However, the present invention is not limited to this, and other means such as a high-pressure air cylinder may be employed.
(4) In each of the above embodiments, an ejector is employed as the gas-liquid mixer, but the present invention is not limited to this, and other gas-liquid mixing means such as a gas-liquid pump may be employed.
(5) In each of the above embodiments, a distilled water tank is employed as the water supply means, but is not limited thereto, and other means such as a water supply pipe may be employed.
(6) In each of the above embodiments, a tube pump is used for the pipe of the hydrogen peroxide pipe and the pipe of the distilled water pipe, but the present invention is not limited to this, and any other pump or supply You may make it employ | adopt a liquid means.
(7) In each of the above embodiments, an evaporator having an evaporation plate is adopted as a gas generator. However, the present invention is not limited to this, and other gas generators may be adopted as long as they can vaporize mixed mist. You may make it do.
(8) In each of the above embodiments, a circulation fan is adopted for each decontamination target room. However, the present invention is not limited to this. For example, the decontamination target room is a RABS (Restricted Access Barrier System) or LF (Laminer). In the case of having an original air flow mechanism such as Flow), the hydrogen peroxide gas in the room may be circulated by these mechanisms. Further, the hydrogen peroxide gas may be circulated by an air conditioner device already installed in the decontamination target chamber.

10 ... air compressor, 11-15 ... air piping, 20 ... hydrogen peroxide tank,
21-25 ... Hydrogen peroxide pipe, 31-35 ... Ejector, 41-45 ... Evaporator,
51-55 ... circulation fan, 61-65 ... mixed mist piping, 70 ... distilled water tank,
71-75 ... distilled water piping, 100, 200 ... decontamination system, R1-R4 ... decontamination target room.

Claims (6)

A decontamination system that decontaminates the interior of each decontamination target chamber using one or more decontamination target chambers using a decontamination gas,
Compressed air generating means for generating compressed air, and decontamination liquid supply means for supplying a decontamination liquid that is a source of decontamination gas,
For each decontamination target chamber, a mixture gas-liquid regulator that adjusts a mixture gas for decontamination that is a mixture of the compressed air and the decontamination solution, and for decontamination by vaporizing the mixture gas and liquid A gas generator that generates gas, an air supply pipe that communicates between the compressed air generation means and the gas-liquid controller, and a communication between the decontamination liquid supply means and the gas-liquid regulator. A decontamination liquid supply pipe, and a gas-liquid supply pipe communicating between the gas-liquid regulator and the gas generator,
The compressed air generation means, the decontamination liquid supply means, and the gas mixture liquid regulators are disposed at positions separated from the decontamination target chambers, and the gas generators are arranged in the corresponding decontamination target chambers. By arranging in the vicinity or indoors,
The decontamination system characterized in that the transport distance of the gas-liquid supply pipe for each decontamination target chamber is longer than the transport distance of the corresponding decontamination liquid supply pipe. About one or more or all decontamination target rooms among one or more decontamination target rooms,
When the transport distance of the gas-liquid supply pipe included in each decontamination target chamber is Ax, and the transport distance of the corresponding decontamination liquid supply pipe is Bx,
Ax / Bx ≧ 3 (1)
(X is an integer of 1 to n and corresponds to each decontamination target room of n decontamination target rooms)
The decontamination system according to claim 1, wherein: The compressed air supplied from the compressed air generating means to the gas-liquid regulator through the air supply pipe has a discharge pressure of 0.05 MPa and an air flow rate with respect to each gas-liquid regulator. 5 NL / min to 70 NL / min,
The decontamination liquid supplied from the decontamination liquid supply means to the gas mixture liquid regulator via the decontamination liquid supply pipe has a flow rate of 0.3 mL / min with respect to each gas mixture liquid regulator. The decontamination system according to claim 1, wherein the decontamination system is ˜30 mL / min. Water supply means for supplying water for conditioning each decontamination target chamber;
For each decontamination target chamber, each has a water supply pipe communicating between the water supply means and the gas-liquid regulator.
With respect to the gas-liquid regulator, the supply of water through the water supply pipe and the supply of the decontamination liquid through the decontamination liquid supply pipe are switched,
When water is supplied to the gas-liquid regulator, the gas-liquid regulator adjusts the humidified gas-liquid mixture obtained by mixing the compressed air and water, To supply the gas generator via a gas-liquid supply pipe to vaporize the humidified gas-liquid mixture to generate a humidifying gas composed of water vapor;
When the decontamination liquid is supplied to the gas mixture liquid regulator, the gas mixture liquid regulator adjusts a decontamination gas mixture liquid in which the compressed air and the decontamination liquid are mixed. 2. A decontamination gas mixture is supplied to the gas generator via the gas mixture liquid supply pipe to vaporize the decontamination gas mixture to generate a decontamination gas. The decontamination system as described in any one of -3. Using the decontamination system according to any one of claims 1 to 3,
The decontamination is characterized by decontaminating the interior of each decontamination target chamber with the decontamination gas vaporized by the gas generator by supplying the decontamination liquid to the gas-liquid mixture regulator. Method. Using the decontamination system according to claim 4,
First, by supplying water to the gas-liquid regulator, the humidity in each decontamination target chamber is adjusted to a preset value with the humidifying gas vaporized by the gas generator,
Next, by supplying the decontamination liquid to the gas-liquid mixture regulator, the inside of each decontamination target chamber after dehumidification is decontaminated with the decontamination gas vaporized by the gas generator. A decontamination method.

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