Patent Application
20190039891
The present invention concerns a process for generating vaporous hydrogen peroxide, particularly by using a simple, small-scale device that does not require pressurization. The generated hydrogen peroxide can be used, for example, for decontamination.
Certain industries, such as the food and medical industries require a high degree of microbial purity in their products. Likewise, facilities, such as hospitals, and vehicles, such as ambulances, have similar requirements. Microbial disinfection is an important part of the used contamination control procedures. The word decontamination is used here to describe the process of reducing microbial contamination to a safe level.
Decontamination can be divided into physical, chemical and biological decontamination.
Physical methods include washing, treatment by hot air or steam, natural degradation, radiation, the use of UV light and cold plasma treatment.
Chemical methods include oxidation by chlorine compounds or hydrogen peroxide, alkaline hydrolysis and ozone treatment. As an example, JPH09272515 A describes the combined use of two different sterilization methods, one using steam and the other using hydrogen peroxide.
Biological methods include the use of bacteria, synthetic bacteria or enzymes.
The use of gaseous products is preferred over other alternatives, since the gaseous products make it possible to disinfect targets and spaces of different sizes, including large areas and facilities, and are capable of providing and maintaining an even concentration of gaseous components in the entire space to be decontaminated, they can be used at room temperature, they eliminate the human factor (compared to manual purification), and they are efficient and relatively gentle.
Several different gases have been used for decontamination. A few of the most common ones are chlorine dioxide (ClO2), aldehydes (particularly formaldehyde) and hydrogen peroxide (H2O2). Of these alternatives, hydrogen peroxide is, in addition to being the safest one, also the most convenient one, as chlorine dioxide corrodes metals and formaldehyde, a suspected carcinogen, leaves a layer on the decontaminated surfaces.
Vapour generating systems are described in, e.g., US 20120277662, where the system generates free radical rich effluent from a free radical electrical generator and/or a vaporizer, equipped with a closed loop circulating system. A similar system is described in U.S. Pat. No. 5792435, where the generator includes one or more vaporizers that inject a combination of a carrier gas and a vaporized decontaminant into an isolation chamber.
Both of these include the use of complex devices with a closed circulation of gas.
US2011176959 A1 also describes a method for sterilizing objects using hydrogen peroxide. Since the method requires the use of a vacuum, the objects to be sterilized must be of a limited size. Similarly, WO9715333 A1 describes a process for sterilizing medical instruments using hydrogen peroxide vapour.
US20140079597 describes a device for vaporizing a liquid from a wick. However, the surface area available for evaporation is small (evaporation occurs only from the end of the wick), and the formed vapour can travel out from the vaporization vessel, along the wick, only through a small outlet in a lid, through which the wick has been guided, whereby the rate of vapour generation remains low.
Although it is known that hydrogen peroxide vapour can be used for decontamination or sterilization purposes in a relatively safe and efficient method, there is still a need for a safe, reliable and robust method of generating the required hydrogen peroxide vapour at sufficiently high rates.
Currently it is typically done by evaporating H2O2 from liquid solutions. However, pressurized systems have been used for this purpose (commonly, a pressure of 4 bars is required), to ensure safe boiling of hydrogen peroxide.
The present invention is defined by the features of the independent claims. Some specific embodiments are defined in the dependent claims.
According to a first aspect of the present invention, there is provided a device suitable for generating vaporous hydrogen peroxide (H2O2).
According to a second aspect of the present invention, there is provided a process for generating vaporous hydrogen peroxide (H2O2).
According to a third aspect of the present invention, there is provided a use of said device or said process in hospitals, in the food industry, or in transport vehicles or pods, or defense or security sectors.
The general idea of the invention is to vaporize hydrogen peroxide into the air from a container using a capillary conveyer and a temperature controlled carrier gas supply. The capillary conveyer consists of a large number of thin non-absorbing solid fibres (e.g glass fibres) forming totally a large area for evaporation. Typically, a fabric system is comprised of many tows, each of which consists of numerous individual fibers; therefore, there are capillary gaps between fibers in a tow, as well as larger gaps between tows in a fabric.
Using this procedure, large amounts of vaporized hydrogen peroxide can be generated in a safe and simple way.
An efficient process requires control of the temperature and humidity. This might require drying, which on the other hand can be easily done using e.g. a condensing or absorbing dryer. Further, an even concentration should be obtained and maintained in the entire area to be decontaminated. After the decontamination, the area should be ventilated and the ventilated air should be filtered.
The invention solves the main shortcomings of current generation methods, namely the need for complex and expensive equipment for hydrogen peroxide vapor generation.
The device of the present invention is therefore simple, robust, affordable and safe to use. Moreover, it does not need pressurization. Without pressurization, heating hydrogen peroxide can cause it to dissolve violently which is a potential risk. Thus, the equipment needed for decontamination can be reduced to minimum.
The use of hydrogen peroxide vapor for decontamination, in general, has the advantage of not causing corrosion, whereas hydrogen peroxide in solution would.
It is to be understood that the embodiments of the invention disclosed are not limited to the particular structures, process steps, or materials disclosed herein, but are extended to equivalents thereof as would be recognized by those ordinarily skilled in the relevant arts. It should also be understood that terminology employed herein is used for the purpose of describing particular embodiments only and is not intended to be limiting.
Reference throughout this specification to one embodiment or an embodiment means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one embodiment of the present invention. Thus, appearances of the phrases “in one embodiment” or “in an embodiment” in various places throughout this specification are not necessarily all referring to the same embodiment. Where reference is made to a numerical value using a term such as, for example, about or substantially, the exact numerical value is also disclosed.
Furthermore, the described features, structures, or characteristics may be combined in any suitable manner in one or more embodiments. In this description, specific details are provided, such as examples of lengths, widths, etc., to provide a thorough understanding of embodiments of the invention. One skilled in the relevant art will recognize, however, that the invention can be practiced without one or more of the specific details, or with other similar details.
Accordingly, it is not intended that the invention be limited, except as by the claims set forth below.
According to one embodiment of the invention (see
According to a further embodiment, the device also includes one or more of means 4 for adjusting the temperature in the carrier gas supply 2 (see
The container 1 is typically shaped like a cylinder or a funnel (that is thinner at the open end), with one opening that fits one end of the capillary conveyer 3, and typically a separate opening suitable for use as a carrier gas inlet.
The carrier gas supply 2 is typically connected to the container 1, so that gas can be blown into the container 1 at a point below its opening, preferably at a point that is located ⅓ ⅛ of the distance from the opening of the container 1 to the bottom of the container 1.
The carrier gas is selected from any non-reactive (or inert) gas or gas mixture, such as nitrogen, argon or air, or a mixture of any of these. Typically, nitrogen or air is used.
The capillary conveyer 3 is preferably essentially flat, has a width smaller than the diameter of the opening of the container 1, for example a width of ¾-⅞ of the diameter of the opening of the container 1, and has a length extending from the opening of the container 1 to the bottom of the container 1, whereby one end of the capillary conveyer 3 can be immersed into the liquid, while the other end is held at the opening of the container 1. Most suitably, it consists of a large number of thin non-absorbing solid fibres (e.g glass fibres) forming totally a large area for evaporation.
According to an embodiment, the present process for generating vaporous hydrogen peroxide (H2O2) includes the steps of providing a container 1 holding a hydrogen peroxide solution, impregnating the capillary conveyer 3 (such as a glass fiber fabric) with hydrogen peroxide, and blowing carrier gas onto it, whereby the hydrogen peroxide is vaporized.
Thus, the method includes vaporizing a liquid solution of hydrogen peroxide to form hydrogen peroxide vapor. The liquid solution to be evaporated is typically an aqueous solution, preferably having a hydrogen peroxide concentration of 5-50 vol-%. more preferably 30-35 vol-%.
The temperature and flow rate of the carrier gas blowing onto the capillary conveyer 3 from the above mentioned carrier gas supply 2 can be adjusted, whereby the process can be modified for the intended end use.
The flow rate of the carrier gas is typically adjusted to a suitable level, based on parameters such as the size of the container 1, the size of the opening of the container 1, and the surface area of the capillary conveyer 3.
According to an embodiment, the flow rate is adjusted to a level of 120-200 l/min, although flow rates up to 480 l/min can be easily achieved when necessary.
Typically, the carrier gas supply is designed to be able to provide carrier gas having a temperature of up to 650° C., but according to an embodiment of the present invention, the temperature is maintained at <100° C., preferably 40-90° C. The pressure is not adjusted, whereby it remains at around ambient pressure.
The humidity of the air in the space to be decontaminated needs to be below the dew point of the mixture of water and hydrogen peroxide vapour, often requiring drying of the air in the space.
The space to be decontaminated using a single device of the embodiments of the present invention is typically <50 m3, although larger spaces can be treated by simultaneously using more than one device.
An effective concentration of H2O2 vapor, of about 300 to about 500 ppm, typically between 350 and 400 ppm, in the above mentioned room size of <50 m3, is typically achieved within 4 h, although 3.5 h is generally sufficient.
According to the above embodiments, hydrogen peroxide is generated using a gentle and efficient evaporation method. The hydrogen peroxide solution is drawn up by the capillary conveyer, having a large evaporation area, and is evaporated with the aid of the heated flow of carrier gas. While the H2O2 is evaporated, more solution can be drawn up by the capillary conveyer, whereby the method is continuous, and gives a steady and high yield of gaseous hydrogen peroxide.
The invention is useful particularly for disinfecting purposes (i.e. killing microbes) in, e.g., hospitals and the food industry.
The hydrogen peroxide vapour generated according to the present invention should not be allowed to condensate, as this could result in corrosion. Therefore, the atmosphere is kept sufficiently dry during the entire disinfecting procedure, and a suitable temperature is maintained.
Preferably the hydrogen peroxide concentration is 5-50% by weight, more preferably 30-35% by weight aqueous hydrogen peroxide. At this level, condensation of hydrogen peroxide is limited, while disinfection in a short period of time is achieved.
Further, the process conditions are adjusted based on the target to be decontaminated, such as its volume or surface area.
In the decontamination process, the space to be decontaminated is closed, possibly dried using a suitable dryer selected based on the space to be decontaminated, and filled with H2O2 vapour. A sufficient amount of hydrogen peroxide is constantly generated to maintain a steady concentration of gas in the space for a sufficient amount of time (e.g. 1-2 h). After the disinfection is considered complete, ventilation of the space is provided, and preferably equipped with filtering of the exhaust air.
The invention facilitates decontamination of a wide range of microbes in e.g. hospitals, food industry, transport vehicles and pods and in the security and defense sectors.
The most important application area of the invention, in one embodiment, is its use in microbe decontamination in infectious disease control.
The following non-limiting example is intended merely to illustrate the advantages obtained with the embodiments of the present invention.
A decontamination was carried out in a test room of 33 m3, by generating hydrogen peroxide from an aqueous 35 vol-% H2O2 solution using the device shown in
In about 200 minutes, a H2O2 vapor concentration of 400-450 ppm (the results of two identical measurements) was achieved, while only using up about 40 ml of the hydrogen peroxide solution.
The results of the decontamination are shown in
The present device and the present process can be used in generating hydrogen peroxide to decontaminate or disinfect spaces, such as hospital rooms, facilities of the food industry, or vehicles, such as ambulances or army vehicles, and generally for replacement of conventional complex vapour generators that utilize high pressures and sometimes high temperatures.
| Number | Date | Country | Kind |
|---|---|---|---|
| 20165089 | Feb 2016 | FI | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/FI2017/050075 | 2/9/2017 | WO | 00 |
