GB2554099A

GB2554099A - Use of gas mixtures comprising oxygen for the production of ozone

Info

Publication number: GB2554099A
Application number: GB1615996.4A
Authority: GB
Inventors: Barton David; Potts Hugh
Original assignee: Anacail Ltd
Current assignee: Anacail Ltd
Priority date: 2016-09-20
Filing date: 2016-09-20
Publication date: 2018-03-28
Also published as: CN109790023A; US20210290803A1; GB201615996D0; EP3515860A1; WO2018055358A1; JP2019534229A; KR20190062435A

Abstract

A method of preparing ozone (O3) comprising: providing a gas mixture comprising: a) 5 vol.% to 50 vol.% oxygen; b) 50 vol.% to 95 vol.% of an oxide gas. The gas mixture is then subjected to an ozone generating process to produce ozone. The use of such a composition as a feedstock for an O3 generating process is also described. The O3 generating process may be dielectric barrier discharge, corona discharge ionizing radiation or cold plasma. The oxide gas may be one or a mixture of carbon dioxide (CO2) carbon monoxide (CO) nitric oxide (NO) nitrogen dioxide (NO2). The gas may comprise 15-25 vol % oxygen and 75-85 vol % oxide gas. The so produced O3 can be used in sterilization of medical devices.

Description

(71) Applicant(s):

Anacail Limited

The Thompson Building, University of Glasgow, Strathclyde, GLASGOW, G12 8QQ, United Kingdom (56) Documents Cited:

US 5810978 A US 3214364 A

US 2850446 A US 20040223893 A1 (58) Field of Search:

INT CL C01B, C25B

Other: WPI, EPODOC, XPESP, XSPRUNG, TXTE (72) Inventor(s):

David Barton Hugh Potts (74) Agent and/or Address for Service:

HGF Limited

Document Handling - HGF - (Glasgow), 1 City Walk, LEEDS, LS11 9DX, United Kingdom (54) Title of the Invention: Use of gas mixtures comprising oxygen for the production of ozone Abstract Title: A method of preparing ozone with a mixed gas feed (57) A method of preparing ozone (O₃) comprising: providing a gas mixture comprising: a) 5 vol.% to 50 vol.% oxygen; b) 50 vol.% to 95 vol.% of an oxide gas. The gas mixture is then subjected to an ozone generating process to produce ozone. The use of such a composition as a feedstock for an O₃ generating process is also described. The O₃ generating process may be dielectric barrier discharge, corona discharge ionizing radiation or cold plasma. The oxide gas may be one or a mixture of carbon dioxide (CO₂) carbon monoxide (CO) nitric oxide (NO) nitrogen dioxide (NO₂). The gas may comprise 15-25 vol % oxygen and 75-85 vol % oxide gas. The so produced O₃ can be used in sterilization of medical devices.

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Use of gas mixtures comprising oxygen for the production of ozone

Field of the Invention

The present invention relates to a method of producing ozone. More particularly, the present invention relates to method of producing ozone using a gas mixture comprising oxygen and oxide gases and the use of specific gas mixtures as feedstock in an ozone generating process to convert oxygen to ozone.

Background

Ozone has been used in order to reduce the bioburden in foodstuff, medical devices and water sanitization for many years. As a strong oxidizing agent, ozone is capable of inactivating a wide range of microorganisms and has been found difficult for microorganisms to build up resistance to.

A key advantage of ozone is that it is created from oxygen gas and decays naturally back to oxygen leaving no other residues. This renders ozone environmentally benign compared to other compounds or technologies used alternatively. However, this natural decay of ozone prevents remote facility production with transport of ozone to the point of use. Consequently, ozone is typically generated on demand and in situ.

Most applications for ozone require volumetric concentrations of ozone gas of above 10,000 ppm to provide sufficient amounts of ozone to obtain the desired effect. For example, a medical device sterilizer may use an ozone exposure at 30,000 to 40,000 ppm for 4 hours to sufficiently sterilize reusable medical devices. However, there are also applications which allow for lower ozone concentrations. Ozone generators used for water sanitization use pure oxygen and generate similar concentrations in the gas phase before the resulting ozone is introduced into the water.

In order to achieve such high ozone concentrations, the ozone generators typically use high (kV) voltage corona, dielectric barrier (DBD), similar discharges or ionizing radiation which operate in pure oxygen. Generating a diffuse plasma state in oxygen, a proportion of the oxygen molecules are broken down to then recombine to yield the ozone.

The combination of high voltage sources, plasma but also pure oxygen itself present a fire and explosion hazard which has to be controlled by adopting suitable procedures and equipment. This poses a significant disadvantage which can prevent the use of ozone in certain applications or at certain plants where this fire risk is unacceptable.

It has been attempted to alleviate this problem by diluting oxygen with nitrogen or argon or even by using air. However, ozone concentrations resulting from these gas mixtures were reduced significantly due in part to side reactions of singlet oxygen with nitrogen to form NOx.

Another method for reducing the bioburden employs ionizing radiation sterilization, for example ultraviolet, gamma, electron beam or X ray irradiation. However, certain materials especially when frequent sterilisation is required can be damaged. Typically, ozone is created as a by-product in these processes. Increase in the ozone concentration may lead to an improved and accelerated sterilization and could reduce the frequency and intensity of irradiation treatment.

It is, therefore, an object of the present invention to obviate or mitigate at least one or more of the aforementioned problems.

It is a further object of the present invention to provide a safer method of producing ozone from oxygen comprising gas mixtures in which flammable material is less likely to combust than in pure oxygen while the ozone yields are comparable.

It is a further object of the present invention to provide an ionizing radiation method for sterilization that minimizes or even avoids damage to the materials that are being sterilized.

Detailed Description

Surprisingly it has been found that a method of preparing ozone comprising: providing a gas mixture comprising 5 vol% to 50 vol% oxygen, 50 vol% to 95 vol% of an oxide gas, and subjecting the gas mixture to an ozone generating process to produce ozone, alleviates the aforementioned problems.

Ozone generating processes

Methods useful for the production of ozone according to the present invention using the specific oxygen containing gas mixtures are among others dielectric barrier discharge, corona discharge; ionizing irradiation, for example in the form of ultraviolet light, gamma, electron beam or X ray irradiation; and cold plasma. The corona discharge method uses a power supply to produce an electrical discharge across a dielectric, and an air gap. The dielectric is used to diffuse the discharge across a large area. The oxygen molecules passing through the air gap are exposed to the electrical discharge and are split into ozone. For production of ozone using ultraviolet light, an oxygen containing carrier gas is passed over an ultraviolet light emitting lamp. In the cold plasma method, oxygen containing gas is exposed to a plasma created by dielectric barrier discharge. The oxygen molecules are split into single atoms which then recombine in triplets to form ozone. Ozone may further be formed from oxygen by electrical discharges and by action of high energy electromagnetic radiation.

In a preferred embodiment, the ozone generating process is dielectric barrier discharge.

In embodiments, the gas mixture used for the production of ozone in accordance with the present invention comprises oxygen in an amount of 5 to 50 vol%. The reduced oxygen content leads to a significant reduction in the flammability of the gas mixture and therefore allows for a wider use. In a preferred embodiment, the gas mixture comprises 10 to 30 vol% of oxygen and in a most preferred embodiment 15 to 25 vol%.

As a further component, the gas mixture used in the present invention comprises oxide gas. The oxide gas is preferably selected from the group consisting of carbon monoxide (CO), carbon dioxide (CO2), nitrous oxide (N2O), nitric oxide (NO), nitrogen dioxide (NO2) and any mixtures thereof. In a preferred embodiment, the gas mixture comprises carbon dioxide, nitrous oxide or any mixture thereof as the oxide gas.

These oxide gases contribute to the formation of ozone in the ozone generating process, as these gases readily give up oxygen atoms thus contributing to the ozone yield.

In embodiments, the gas mixture comprises 50 vol% to 95 vol% of oxide gas, in a preferred embodiment 70 vol% to 90 vol% and in a most preferred embodiment 75 vol% to 85 vol%.

In a preferred embodiment, the gas mixture consists of oxygen and oxide gas.

In an embodiment, the gas mixture comprises

a) 5 vol.% to 50 vol.% oxygen; and

b) 50 vol.% to 95 vol.% of an oxide gas;

with the proviso that these two percentages add up to 100 vol%.

In a further embodiment, the gas mixture comprises

a) 10 vol.% to 30 vol.% oxygen;

b) 70 vol.% to 90 vol.% of an oxide gas selected from the group consisting of carbon monoxide, carbon dioxide, nitrous oxide, nitric oxide, nitrogen dioxide and any mixtures thereof;

with the proviso that these two percentages add up to 100 vol%.

In a further embodiment, the gas mixture comprises

a) 15 vol.% to 25 vol.% oxygen;

b) 75 vol.% to 85 vol.% of an oxide gas;

with the proviso that these two percentages add up to 100 vol%.

In a further embodiment, the gas mixture comprises

a) 15 vol.% to 20 vol.% oxygen;

b) 75 vol.% to 85 vol.% of an oxide gas selected from carbon dioxide, nitrous oxide or any mixtures thereof;

with the proviso that these two percentages add up to 100 vol%.

In a further embodiment, the method of preparing ozone further comprises the step of sterilizing an article with the resulting ozone. The article may be a medical device such as endoscopes, sets of instruments, implantable devices, life science consumables and single use devices such as microtitre plates, syringes, dressings, disposable blades, disposable scissors, disposable needles; sample collection tubes, preparation vessels such as centrifuge cubes; cell culture equipment such as flasks, dishes and bioreactors; biological equipment such as all appliances for peptide and protein preparation including powdered media.

Further, the article may be a contaminated space such as fume cupboards, glove boxes and other equipment where contamination can be an issue. Contamination in the sense of the present invention relates to biological contamination by microorganisms such as bacteria, viruses, yeasts, moulds, spores, vegetative cells and parasites.

Further, the article may be a foodstuff in food processing to reduce the bioburden and to increase shelf life. For example, fruit and vegetables may be treated with ozone in food purifiers or washers to improve food surface hygiene. But also sanitation of food plant equipment, reuse of waste water, lowering of biological oxygen demand and chemical oxygen demand of food plant waste can be achieved with ozone generated according to the present invention. In this regard, waste water treatment is not restricted to such of the food industry.

Further, ozone generated according to the present invention can be used for disinfecting meat based foodstuffs and production plants and wastes such as recycled poultry chill water and disinfection of poultry carcasses

Further, the method of the present invention may be used for decontaminating semi enclosed drain systems. A cap may be placed over for example a semi enclosed drain with the cap comprising an ozone generator. The gas mixture or composition is pumped into the trapped volume between the cap and the water sump of the drains and the ozone is generated within this trapped volume between the cap and the water sump.

Sterilization may be carried out by placing the article directly into the reaction chamber where ozone is generated from the reactants/gas mixture or providing the article in a sealed pack which comprises the gas mixture before placing the sealed pack into the reaction chamber. This has the added benefit that no further packaging has to be done under sterile conditions.

A further aspect of the present invention is the use of a composition comprising 5 vol% to 50 vol% oxygen, 50 vol% to 95 vol% of an oxide gas as reactant in the preparation of ozone.

Reactant in the sense of the present invention is to be understood as the chemical material that undergoes chemical reaction to yield the ozone.

The composition can be provided to the reaction chamber as a feedstock, i.e. a premix of the different components which will form the gas mixture within the reaction chamber for preparation of the ozone. The composition may be provided as a premix in a cylinder that can easily be transported and stored. The composition may be stored and/or transported as a liquefied composition or in the gaseous state. Further, the different components of the composition can be added through different channels to be mixed only within the reaction chamber before being subjected to the ozone generating process.

The feedstock may further be provided directly within a medical device. For example, the feedstock may be located in an automated endoscope reprocessor. The ozone required for sterilisation of the endoscope can be produced directly within the reprocessor.

The composition may be the gas mixture as described with regard to the present invention. The feedstock can either be in the gaseous aggregation state or liquefied.

As ozone generating process any of the processes mentioned in the present application can be used.

In a preferred embodiment, the composition used as reactant in the preparation of ozone comprises 15 vol% to 25 vol% of oxygen and 75 vol% to 85 vol% of an oxide gas selected from carbon dioxide, nitrous oxide or any mixtures thereof, with the proviso that these two percentages add up to 100 vol%.

Examples

Example 1

Using a 60mm diameter electrode, a dielectric barrier discharge was generated at 100% duty cycle, 21kHz supply frequency and 3.80kV electrode voltage. A range of gas mixtures were prepared containing different ratios of oxygen and carbon dioxide gases. The gas mixtures were prepared in sealed polythene bags which were then subjected to the dielectric barrier discharge to generate the ozone within the bag.

A discharge was run for a fixed 60s period, after which the ozone concentration was measured using a 2B Technologies 106-MH ozone meter.

In Figure 1, the ozone concentration obtained from the different mixtures is depicted against the increasing amount of carbon dioxide or nitrogen in the gas mixture (reactant).

As shown in Figure 1 and as expected, the ozone concentration decreases with lower amounts of oxygen in the reaction chamber. However, as the oxide gases contribute to the ozone yield, even with lower oxygen concentrations sufficient amounts of ozone can be produced at lower oxygen content in the gas mixture as compared to gas mixtures comprising oxygen and nitrogen.

Claims

1. A method of preparing ozone comprising:

- providing a gas mixture comprising

a) 5 vol.% to 50 vol.% oxygen;

b) 50 vol.% to 95 vol.% of an oxide gas; and

- subjecting the gas mixture to an ozone generating process to produce ozone.

2. A method of preparing ozone according to claim 1, wherein the oxide gas is selected from the group consisting of carbon monoxide, carbon dioxide, nitrous oxide, nitric oxide, nitrogen dioxide and any mixtures thereof.

3. A method of preparing ozone according any one of claims 1 or 2, wherein the oxide gas is selected from carbon dioxide, nitrous oxide or any mixtures thereof.

4. A method of preparing ozone according to any one of claims 1 to 3, wherein the ozone generating process is selected from dielectric barrier discharge, corona discharge, ionizing irradiation or cold plasma.

5. A method of preparing ozone according to any one of claims 1 to 4, wherein the gas mixture comprises

a) 15 vol% to 25 vol% of oxygen; and

b) 75 vol% to 85 vol% of an oxide gas;

with the proviso that these two percentages add up to 100 vol%.

6. A method of preparing ozone according to any one of claims 1,4 to 5, wherein the gas mixture comprises

a) 15 vol% to 25 vol% of oxygen; and

b) 75 vol% to 85 vol% of an oxide gas selected from carbon dioxide, nitrous oxide and any mixtures thereof;

with the proviso that these two percentages add up to 100 vol%.

7. A method of preparing ozone according to any one of claims 1 to 6, further comprising the step of sterilizing an article with the resulting ozone.

8. A method of preparing ozone according to claim 7, wherein the article is a medical device.

9. Use of a composition comprising

a) 5 vol.% to 50 vol.% oxygen;

b) 50 vol.% to 95 vol.% of an oxide gas; as reactant in the preparation of ozone.

10. Use according to claim 9, wherein the composition is a feedstock.

11. Use according to claim 10, wherein the feedstock is located in an automated endoscope reprocessor.

12. Use according to any one of claims 9 to 11, wherein the oxide gas is selected from the group consisting of carbon monoxide, carbon dioxide, nitrous oxide, nitric oxide, nitrogen dioxide and any mixtures thereof.

13. Use according to any one of claims 9 to 11, wherein the oxide gas is selected from carbon dioxide, nitrous oxide or any mixtures thereof.

14. Use according to any one of claims 9 to 13, wherein ozone is prepared using an ozone generating process selected from dielectric barrier discharge, corona discharge, ionizing irradiation or cold plasma.

15. Use according to any one of claims 9 to 11, or 14, wherein the composition comprises

a) 15 vol% to 25 vol% of oxygen; and

b) 75 vol% to 85 vol% of an oxide gas selected from carbon dioxide, nitrous oxide or any mixtures thereof;

with the proviso that these two percentages add up to 100 vol%.

Intellectual

Property

Office

Application No: Claims searched:

GB1615996.4

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