Title of Invention


Abstract An apparatus for producing a spray of ozonated water for disinfecting a surface comprising a reservoir (12) for water, means (24) for supplying ozone to the water to produce ozonated water, a nozzle (39) for spraying ozonated water onto a surface to be treated, a supply conduit (37) for delivering said ozonated water from the reservoir to the nozzle, the nozzle comprising a spray head (39) having a number of orifices for delivering jets of ozonated water, a shroud (40) encircling the nozzle and extending from the nozzle along the conduit to contain ozonated gas liberated at the nozzle and means for creating a negative pressure at the end of the shroud remote from the nozzle to extract ozone gas liberated at the nozzle, and the shroud comprising an outer conduit (38) encircling the supply conduit (37) and having an enlarged head (40) encircling the nozzle at one end and a suction device (32) connected to the outer conduit at the other end thereof to extract ozone gas from within said enlarged head through the outer conduit away from the nozzle.
Full Text Apparatus for Disinfecting a Surface
This invention relates to apparatus for use in the disinfection of surfaces
and in particular to disinfect wounds using a high concentration aqueous ozone
and also to methods and apparatus for producing a high concentration aqueous
solution of ozone.
Wounds can be divided into two basic categories, acute and chronic.
Acute wounds are caused when damage occurs to external intact skin tissue.
This includes surgical wounds, bites, burns, cuts, abrasions, lacerations and
more traumatic crush or gunshot wounds. Chronic wounds are associated with
endogenous mechanisms connected to a predisposed condition that eventually
damages the dermal tissue. Chronic wounds often result when the supply of
oxygen and nutrients (perfusion) to tissues is impaired. Reduced arterial supply,
venous drainage or metabolic diseases can cause chronic wound. Leg ulcers,
foot ulcers and pressure sores are all examples of chronic wounds.
Hunt et al (Hunt, T.K. And Hopt, H.W. 1997, Wound healing and
infection - what surgeons and anaesthesiologists can do, Surg. Clin. North
America. Vol.77, p587-606) state that acute wounds will heal rapidly if
blood perfusion is maximised, thus providing the cells of the immune
system the oxygen and nutrients necessary to ward off infection. Oxygen
is an integral requirement for cell growth, division and wound healing
Grief et al (Grief R., Akca, O., Horn, E., Kurz, A., and Sessler, D.J. 2000.
Supplemental perioperative oxygen to reduce the incidence of
surgical wound infection. The New England Journal o f Medicine. Vol
342, pl61-167). It is also critical for the respiratory
burst of Polymorphonuclear leukocytes (PMNs), which produce
potent anti-microbial compounds. As well as providing the
energy for metabolic reactions and hence infection defence
mechanisms, oxygen also plays a major role in determining
the oxidation - reduction potential of tissues. Bakker
(Bakker, D.J. 1998. Severe trauma and infections.
Anaesthesia. Vol 53, p65-67). Wound microbiology and
associated approaches) identifies that a low redox potential
favours the growth of anaerobic bacteria. Bowler et al
(Bowler, P.G. Duerden, D.I., and Armstrong, D.G. 2001.
Wound microbiology and associated approaches to wound
management. Clinical Microbiology Reviews. Vol 14, No 2,
p244-269) state that a low redox potential will facilitate
the development of synergistic aerobic/anaerobic
Wounds often have a diverse array of microflora. The
primary pathogens involved in the infection of chronic and
acute wounds are thought to be Staphylococcus aureus,
Pseudomonas aeruginosa and beta-hemolytic streptococci.
These pathogens are aerobic or facultative. However,
anaerobic pathogens are often overlooked in wound infection
investigations, because they reside deep within the dermal
tissue. Anaerobic micro-organism isolation, identification
and collection are time consuming and labour intensive.
Bowler et al (referred to above) investigated and conclude
that there is correlation between the incidence of anaerobic
pathogens and the prevalence of infection. Bascom (Bascom,
J.U. 1996. Pilonidal care: anerobes as visible villans.
European Journal of Surgery. Vol 162, p351)reports that
anaerobic bacteria are the true causative micro-organisms of
wound infection and that improved oxygenation of wounds is
required to minimise infection.
The polymicrobial nature of wounds has been widely
published, however Staphylococcus aureus is considered to be
the most problematic bacterium in traumatic, surgical and
burn wound infections Bowler et al (referred to above),
Tengrove et al (Tengrove, N.J., Stacey, M.C. McGechie, D.F.
and Mata, S. 1996. Qualitative bacteriology and leg ulcer
healing. Journal of wound care. Vol 5, p277-280) report
that when four or more bacterial groups are present within a
leg ulcer, the likelihood of healing is significantly
reduced. This finding promotes the hypothesis that microbial
synergy occurs within wounds increasing the net pathogenic
effect and severity of the infection. Oxygen consumption by
aerobic bacteria induces tissue hypoxia and lowers the redox
potential, which provides a more favourable habitat for
anaerobic organisms. Nutrients produced by one micro-
organism may encourage the growth of potentially pathogenic
co-habiting micro-organisms. Some anaerobes are able to
impair host immune cell function and hence provide an
advantage for themselves and other co-habiting micro-
organisms. Bowler (Bowler, P.G. 2002. Microbiology of acute
and chronic wounds. Facing the challenge of wound
management in the 21st Century. Master Misericordiae
University Hospital) states that micro-organisms are able to
aid each other within a wound. Micro-organisms (especially
in biofilms) use a communication mechanism called Quorum
sensing. This is a cell density dependent form of
communication, facilitating survival in a new harsh
environment. They release signalling molecules informing
each other of "survival tips" (i.e. produce a specific
morphological change or a specific defensive chemical).
Debridement is an integral part of wound healing. The
removal of dead and unhealthy tissue is essential to
minimise the habitat available for microbial colonisation
and allow new tissue formation. Debridement is achieved
through physical removal of tissue using a sharp instrument
or the application of saline or sterile water. The
management of bite wounds involves high pressure irrigation
to reduce microbial load.
Historically ozone has been used to disinfect wounds in
its gaseous form or dissolved within oil. Direct ozone gas
application, intravenous injection, rectal insufflation or
autohemo-ozonotherapy are all known methods of medical ozone
application. Reference should be made to the following
Patent Publications for details of such treatments: RU-
2178699, FR-2784388, US-6073627.
Aqueous Ozone Hypotheses
1. Disinfection
1.1. Ozone is highly reactive and decomposes through
the formation of free radicals to form molecular oxygen.
Free radicals have an unpaired electron in their outer
orbital making them highly unstable and reactive. These free
radicals comprise hydroxyl, superoxide or ozonide radicals.
Ozone micro-organism attack is primarily on the cellular
membrane, with damage subsequently occurring to other cell
sites. The proposed mechanism of action is thought, in large
part, to relate to the olefinic bonds within the micro-
organism cell membrane being attacked by ozone to form an
ozonide or other decomposition product. The ozonide reacts
with enzymes, sulfhydryl groups and aldehydes, releasing
peroxyl compounds. The peroxyl compounds further damage
proteins, DNA and other structures. The cell is lysed and
the cytoplasm dispersed. In essence, the aqueous ozone would
be used to reduce the microbiological organisms within the
1.2. Aqueous ozone will be particularly effective against
anaerobic bacteria due to their lack of anti-oxidants and
other oxidation defence systems. Aerobic bacteria produce
anti-oxidants such as superoxide dismutase to prevent
cellular damage caused through respiration using oxygen.
Anaerobic bacteria do not use oxygen to respire and hence
have not evolved advanced anti-oxidants. The removal of
anaerobic bacteria will reduce the likelihood of infection
Bowler (referred to above).
1.3. Free radical based oxidation is random and hence it
will be extremely difficult for a micro-organism to develop
resistance to aqueous ozone. Free radical based disinfection
does not involve target site specificity. Free radicals will
be effective against all micro-organisms, with the killing
rate being dependent on, among other things, the prevalence
of anti-oxidants within different microbial species.
1.4. A sufficiently long contact period will remove all
micro-organisms from a wound bed, creating a sterile
2. Debridement
2.1. Aqueous ozone is not cell specific and will attack the
wound tissue as well as the micro-organisms. Unhealthy or
dead tissue is less well perfused than healthy tissue and as
such does not contain as much anti-oxidant or enzymatic
agents (superoxide, dismutase, glutathione, macrophage,
etc). The unhealthy tissues will mount a far weaker defence
against the free radical attack than the healthy tissues and
hence will be more prone to damage/rupture/removal than
healthy tissues. Hence, the aqueous ozone will provide a
quasi-selective chemical debridement system, creating an
improved healing environment.
3. Moist healing environment
3.1. The application of aqueous ozone will provide a moist
healing environment (in conjunction with 1.4.). A moist
healing environment is. critical to wound healing Winter
(Winter, G.D. 1962. Formation of scab and the rate of
epithelization of superficial wounds in the skin. Nature.
Vol 193, p293-294).
4. Reactive Oxygen Species (ROS)
4.1. Aqueous ozone produces Reactive Oxygen Species (ROS) as
decomposition intermediaries. The ROS produced will
complement the bodies own natural defence system in which
polymorphonucleocytes (PMNs) produce ROS to remove micro-
organisms. The aqueous ozone healing system is biomimetic,
providing a "booster" when the bodies own PMNs have been
overwhelmed by infection.
4.2. Aqueous ozone will act as an ROS generator in poorly
perfused ischemic tissues. The lack of perfusion inhibits
the body's own production of ROS through a deficiency in
nutrient/oxygen/energy. The aqueous ozone artificially
creates the body's natural infection removal mechanism.
4.3. ROS will support the formation of blood vessels
(angiogenesis) and stimulate collagen production (Sen, C.K.,
Khanna, S., Babiar, B.M., Hunt, T.K., Ellison, E.C., and
Roy, S. 2002. Redox control of wound repair. JCB (paper in
press) Manuscript M203391200).
4.4. Micro-organisms communicate through quorum sensing,
which is facilitated through the release of signalling
molecules. ROS may actively oxidise these signalling
molecules reducing synergistic survival effects. This
mechanism would be important in reducing any biofilm
5. Oxygenation
5.1. Aqueous ozone decomposes to water and oxygen. The
decomposition reaction takes place within the wound
providing surface application of oxygen to cells and
produces a hyperoxic environment. Anaerobic bacteria cannot
survive in a hyperoxic environment, reducing infection.
5.2. A hyperoxic environment produced through aqueous ozone
application can provide a source of oxygen to poorly
perfused tissues (ischemic), which may improve wound
5.3. Cytokines and growth factors show an improved
mechanistic action in a hyperoxic environment, which can be
facilitated through the use of aqueous ozone application
5.4. The aqueous ozone application equipment contains an
oxygen concentrator that can be used to provide high
pressure sterile oxygen to a wound. Oxygen is critical to
the wound healing process. The equipment allows the
application of oxygen to the wound via a high pressure jet
or through the use of a hyperbaric chamber around the wound
6. Acute wound response
6.1. Research has identified that inflicting an acute wound
within a chronic wound can induce a wound healing response.
The cellular oxidation caused by aqueous ozone application
may induce an acute wound type response within a non-healing
chronic wound.
Qzonated water
Ozonated water is widely used to kill bacteria and
other micro-organisms. However, when generating and
dissolving ozone in water it is usual to expect levels of
under 1ppm.
WO-A-0020343 discloses an apparatus for producing an
aqueous ozone solution to disinfect animal house feed water.
The process requires pressurisation of the contactor to
facilitate ozonation.
US-A-5834031 discloses an apparatus that utilises
aqueous ozone to treat foot fungi. A single "in-line"
ozonation process is used to produce aqueous ozone, whilst
completely submerging the appendage to be treated.
US-A-5098415 discloses an apparatus to treat foot
diseases using aqueous ozone utilising submersion of the
appendage into aqueous ozone solution.
WO-A-0172432 discloses a mobile spray apparatus for
providing an aqueous ozone stream. The aqueous ozone
production process uses an "in-line" method of production as
well as a de-gas unit.
US-A-6455017 discloses a mobile apparatus for washdown
and sanitising using aqueous ozone. The aqueous ozone
production process uses an "in-line" method of production.
US-A-2002139755 discloses a method for enhancing
dissolution of gasses in liquids. The method uses a
plurality of nozzles sized and sited to produce micro-fine
bubbles and initiate rotational flow.
RU-A-2175539 discloses a method of treating wounds with
ozone gas. The treatment is based upon the application of
gas to the wound.
US-A-4375812 discloses a method for treating burn
injuries with aqueous ozone involving submerging the
patients entire body in a bath of aqueous ozone.
It is an object of the present invention to produce a
high concentration ozone solution capable of rapid
disinfection and to provide a method and apparatus for
applying a high concentration ozone solution to a surface to
be disinfected and in particular to a human or animal wound.
This invention discloses an apparatus for disinfecting
surfaces and in particular human and animal wounds, although
described in the context of a wound surface the scope of the
invention covers all types of surfaces, comprising a
reservoir for accumulating ozonated water and means to
deliver ozonated water from the reservoir to a nozzle having
one or more jets for delivering a spray of ozonated water on
to the surface to be treated. The nozzle has an encircling
shroud and means are provided for withdrawing ozonated gas
liberated at the nozzle from around the nozzle. A
collection tray is provided which is located under the
surface/wound to be treated to receive ozonated water
flowing from the treatment region. The base of a catchment
tray can contain a number of holes through which used
solution is drawn out of the tray by a pump which causes the
solution to pass through a catalyst to break down any
residual ozone contained in the solution.
The following is a description of some specific
embodiments of the invention, reference being made to the
accompanying drawings in which:
Figure 1 is a diagrammatic illustration of a system for
generating and applying ozonated water to a wound;
Figure 2 illustrates a first modification to the
Figure 3 illustrates a second modification;
Figures 4 to 10 illustrate a spray head for the
apparatus; and
Figures 11 to 15 illustrate a catchment tray and limb
support for a patient to be treated.
Referring firstly to Figure 1 of the drawings, the
apparatus for performing the invention comprises three main
components: an apparatus for generating a concentrated
aqueous solution of ozone indicated at 10; an apparatus for
spraying the ozone solution onto a surface of a limb to be
treated indicated at 11; and an apparatus for supporting a
limb to be treated and for collecting solution which flows
off the treated limb for disposal indicated at 11a. A
control system (not shown) is provided for the whole
apparatus comprising a programmable logic computer which
interfaces with the controllable elements of the apparatus
to control the operation of the apparatus.
The aqueous ozone generator 10 comprises a contactor 12
which is connected to a reservoir of water 13 via a pump 14
and solenoid controlled valve 15. Figure 2 shows an
alternative arrangement in which mains water is supplied via
a pressure restriction valve. The pump 14 is activated and
solenoid valve 15 is opened to transfer water from the
reservoir into the contactor 12 until a sufficient level is
reached to activate a water level sensor 16. The sensor
activates a relay sending a signal back to the PLC, which
turns off a pump 14 and closes a solenoid valve 15.
The contactor has a conduit 17 extending from an
upwardly facing inlet 18 adjacent the top of the contactor
through a pump 19 and a differential pressure injection 20
(such as a Mazzei injector as disclosed in US-A-5863128) and
thence to an outlet 21 into the contactor adjacent the
bottom of the contactor. The pump 19 is activated taking in
water through the inlet 18, circulating through the
differential pressure injector 20 and returning it to the
contactor via the nozzle outlet 21. The nozzle serves two
functions. Primarily it provides the back pressure required
by the differential injector and secondly, it increases the
gas/liquid mixing within the contactor.
An oxygen supply 22, preferentially using an oxygen
concentrator, supplies dry oxygen gas through a throttle
valve 23 and a pressure regulator 24 to an ozone generator
25. The valve and regulator can be located either before or
after the ozone generator. The ozone generator can utilise
ultra violet, proton exchange membrane or corona discharge
based production methods, but preferentially is an air
cooled corona based ozone generator.
The ozone generator is activated and a solenoid valve
26 is opened. Ozone is drawn through the differential
pressure injector 20 where it contacts the water. The
gas/liquid mixture stream is forced through the outlet
nozzle 21 and into the contactor 12. Ozone gas bubbles move
up through the contactor and exit at an outlet 27 into a
pipe 28.
The pipe 28 is angled downwardly towards the outlet so
that any condensation that occurs within the pipe runs back
down through the outlet and into the contactor 12.
Any ozone gas which reaches pipe 28 passes through a
destruct device 30, where it is broken down into oxygen. A
heating element 30a is activated heating ozone destruct unit
30. A temperature sensor 30b is linked back into the
programmable logic computer (PLC), which controls the
heating process and maintains the destruct unit 30 at a
constant temperature between 40 and 80°C, but preferentially
60°C. The destruct 30 is heated, which prevents moisture
forming within the destruct itself. The oxygen gas which
exits destruct 30 passes into manifold 31. The oxygen gas
is drawn from the manifold by a fan 32 and into a secondary
ozone destruct device 32a. The oxygen gas exits the
secondary ozone destruct device from where it is directed
onto the ozone generator 25 referred to earlier where it
aids in cooling the unit.
Returning to the ozonation process in the contactor,
inlet 18 to the re-circulation system has an upturned end
and is shaped to prevent ozone gas bubbles being sucked into
the re-circulation system. The agueous ozone concentration
is monitored by a dissolved ozone sensor 33 linked into the
PLC. When the dissolved ozone concentration reaches the
desired level, set by the operator, the PLC switches off the
oxygen concentrator and the ozone generator and closes
solenoid controlled valve 26. Pump 19 is switched off and a
pump 34 activated for delivering the aqueous solution of
ozone to the spray system 11. A solenoid valve 35 is opened
and the solution moves along the pipe where the pressure is
restricted to between 40 and 100 mbar, but preferentially 70
mbar, by a pressure and flow regulator 36.
The aqueous ozone solution is delivered to one end of
an inner conduit 37 of a pair of concentric conduits 37,38.
The other end of conduit 37 has a spray head 39 for delivery
of multiple jets of aqueous ozone.
The spray head is illustrated in Figures 4 to 10 and is
designed and constructed so as to produce a series of jets,
preferentially in an interlocking fan configuration. The
spray system although appearing simple has a number of
important features. When high concentration ozone solution
is forced through an aperture a pressure differential is
created and causes the ozone gas dissolved in the stream to
come out of solution into the atmosphere (due to ozone's
vapour pressure). The higher the pressure differential the
greater the amount of gas liberated to atmosphere. The
legal atmospheric limit for ozone is 0.1ppm, which is very
low. Hence the spray head has been developed to use "jet
holes" 41 (see Figures 7 and 10) that are sufficiently small
to use low quantities of solution (facilitating the small
size of the unit) and yet have a large enough diameter to
prevent an excessively high pressure differential being
created that liberates too much ozone gas from the solution.
The pressure at which the ozone solution is supplied to the
head is also a factor and tests have indicated that a level
around 70 mbar is the most suitable. Higher pressures mean
more ozone gas is liberated to atmosphere and also causes
the jets to be too powerful "drilling" bugs down into the
surface of the wound.
As the solution exits the spray head 39, the pressure
drop causes ozone gas to come out of solution. An
overlapping arrangement of the jets as can be seen in Figurs
4 and 5 minimises the surface to Volume area of the outer
edges of the spray cone, thus reducing the amount of ozone
gas that is liberated from the solution. Ozone will rapidly
decompose in air and hence the reduced surface to volume -
ratio is critical in preventing the decomposition of the
ozone solution as it is travelling from the spray head to
the wounds surface. The jets operate at very low pressures
to minimise the amount of ozone gas that escapes from
solution and also to ensure that micro-organisms are not
driven down into the wound bed. The spray head is located
within a head attachment (further referred to as the "cone
head") 40, shaped to match the dimensions of the "jet cone"
produced by the spray head. The length of the cone head is
dependent upon the pressure of the jets, but is
preferentially 125mm. The inside of the cone head is
maintained at a negative pressure to the atmosphere by the
fan 32 connected to the manifold 31. Any ozone gas released
from solution in the spraying process is drawn back through
outer conduit 38 into the manifold and subsequently passed
through a secondary ozone destruct 32a, where it is
decomposed to oxygen.
In use the cone head 40 is positioned over a wound to
be decontaminated/healed. The distance from the wound
surface to the edge of the cone head is dependent on the
pressure of the jets but is preferentially 10mm.
The patient whose wound is to be disinfected/healed can
be bed-ridden or mobile. A collection tray 43 which will be
described in greater detail below is placed under the
patient's appendage on which the wound is located. The
catchment tray contains a jointed support mechanism (not
shown) that takes the weight of the patient's appendage
during the treatment. The support mechanism can be rigid or
flexible, but preferentially comprises of a removable padded
concave or convex support, located upon a knuckle joint to
facilitate horizontal rotation. This in turn is located on a
stem fixed to the collection device by means of a joint 47
that allows the stem to move in an arc in the vertical
plane. Preferentially this is a pin joint. The catchment
tray has a removable insert 48 that has holes 49 in it to
allow the used solution to drain to the base of the tray.
This insert 48 will preferentially be a 'Vee' with a series
of holes 49 that allow the solution to drain through but
retain any large biological material flushed off the wound
in the disinfection process. The catchment tray has side
flanges 50 upon which the spray head system is mounted.
The spray head 39 is fixed to a mounting and support
device (not shown) that securely holds the spray cone in
position above the wound. This mounting device can comprise
of a wide range of structures to retain the head in its
required position, typically either a mechanical or
electromagnetic device to provide attachment to a flexi-
rigid conduit upon which the spray head is clamped.
The base of the catchment tray 43 contains a number of
holes 51 through which the used solution is drawn out of the
tray. A pump 52 creates a negative pressure within vessel
53 coupled to the tray (see Figure 1) causing the liquid in
the collection tray to be drawn into the vessel 53. The gas
removed from vessel 53 by pump 52 is directed into manifold
31, where it passes through the secondary catalyst 32a. Any
residual ozone gas released by the used solution is
decomposed here.
The solution is applied to the wound for a period of
time determined by the operator and programmed into the PLC
at the start of the treatment. Once the required duration
has past, the PLC closes valve 35 and continues to operate
fan 32 and pump 52 for a defined period of time to clear the
catchment tray of solution. During this period valve 60 is
opened and the solution within the contactor is pumped into
vessel 53, until level, switch 61 in the contactor is
activated. Pump 34 is turned off and valve 60 is closed.
After this period has passed the pump 52 and fan 32 are
switched off.
The inlets and outlets of vessels comprise of quick
connect couplings to facilitate their ease of removal and
attachment. At the end of the treatment, vessel 53 is
disconnected and the water contained within it poured
straight to drain.
Figure 3 shows an alternative arrangement of the
apparatus, whereby vessel 53 is removed and the contents of
the catchment tray are pumped directly to drain via a pump.
The excess solution remaining in the contactor is pumped
directly to drain as opposed to vessel 53. This solution can
pass through a carbon filter 65 within the waste pipe line
to destroy any ozone that may remain.
The system is described operating with tap water taken
from a domestic or commercial supply. The invention does not
preclude the use of a filtered or conditioned water supply.
Such a water supply will have an effect of speeding up the
ozonation process, but is not the preferred water supply of
use due to the reduction in portability filtration systems
The ability to capture and destroy as much as possible
of any aqueous ozone gas released to atmosphere from any
aqueous ozone solution is paramount to the successful
operation of any unit. The following apparatus is directed
to that objective.
Figure 7 is an illustration of the nozzle 39 and
encircling shroud 40 for the nozzle for applying ozonated
water to a patient's wound or other surface; and Figures 11
to 15 illustrate the catchment tray supporting the area of
the patient's limb or body to be treated and for recovering
ozonated water which flows off the area of the patient being
Aqueous ozone is created by dissolving ozone gas into
liquid. The saturated, vapour pressure of ozone is >760mmHg
at 25 C, which means that ozone will actively diffuse out of
the liquid into the atmosphere. Ozone has a legal exposure
limit of 0.1 ppm and hence this poses a problem when a high
concentration aqueous ozone solution is exposed to the
atmosphere (the ozone teadily comes out of solution and the
concentration in the atmosphere rises above the 0.1ppm
The rate at which the ozone gas liberates from the
liquid is highly dependent on temperature and pressure. The
higher the temperature the more ozone comes out of solution
and the lower the pressure the more ozone comes out of
The aqueous ozone solution is produced at atmospheric
pressure. It is then placed under increased pressure as it
is pumped to the spray head. When it is under pressure
(i.e. in the pipe from the pump to the spray head) no ozone
comes out of solution, because of the fact that it has been
put under increased pressure. When it reaches the spray
head, it is suddenly exposed to normal atmospheric
conditions (i.e. a drop in pressure occurs) and hence a
proportion of the ozone contained in the liquid stream is
released to atmosphere. There is a pressure differential
created across the aperture(s) in the spray head. The size
of this pressure differential determines the amount of ozone
gas that is released from the liquid as it exits the spray
head. The release of ozone gas has two consequences, the
first has already been explained, ozone gas is toxic and
hence raises the atmospheric concentration above the legal
exposure limit. The second is that the concentration of the
aqueous ozone fluid drops. The purpose of the system is to
apply a high concentration solution to the wound, hence the
amount of concentration loss due to ozone gas liberation
needs to be minimised.
Experiments were conducted using spray heads with
varying sized apertures combined with alternating pressures
from the pump. It was found that a 0.5mm diameter aperture
is the most effective size, combined with a liquid pressure
of 70mbar. 0.2mm diameter apertures produced a pressure
differential that was too large and liberated a substantial
amount of ozone gas, dropping the solution concentration
from 20ppm down to 12ppm. A 0.75mm diameter aperture
allowed too much liquid through the head. Too much liquid
will cause a wound to macerate and hence would inhibit
rather than aid the healing process.
The 0.5mm diameter aperture still allows a proportion
of the ozone gas to escape from the liquid, due to the
change in pressure. The concentration drops from 20ppm to
17ppm. The ozone gas that escapes to the atmosphere has to
be dealt with; otherwise over a period of time the
cumulative effect would raise the ozone concentration above
0.1ppm. To that end the spray head is surrounded by an
extraction system 38,40, so that as the ozone gas is
liberated on exiting the spray head it is immediately taken
back into the machine in the extract air stream.
The use of an extract system dictates the design and
shape of the spray pattern exiting the spray head. The
implementation of an extract system means that ozone gas is
continually being stripped from the surface of the air borne
aqueous liquid from the spray head to the wound.
The amount of ozone gas being removed can be limited by
reducing the surface to volume ratio of the spray cone. The
optimal spray configuration is one that has a very small
surface area exposed to the extract air stream, whilst
providing a large surface impact area. The spray head has a
series of interlocked jets (see Figures 4 and 5) that
produce a dual fan effect. This may or may not be the most
optimal configuration for the spray pattern.
The extract "shroud" 40 is intended to be a consumable
item (i.e. it can be quickly replaced between patients).
As explained earlier, ozone gas actively diffuses out
of aqueous solution. When aqueous ozone is sprayed on to a
wound or other organic surface, a large proportion of the
ozone is broken down on the surface. However, the waste
run-off liquid still contains ozone, which, as previously
described, will actively enter into the atmosphere. The
catchment tray has two main "concepts" that allow it to
The first of these relates to the catchment tray 43
which is basically a tray that has a solid plastic insert
48, which is angled in an inverted V shape. A series of
holes 49 (e.g. four cm apart are drilled along the apex of
the V. The insert allows aqueous ozone solution to pass
through the holes, but capture any gas released in the gap
underneath the insert preventing it from escaping to
The second concept of the catchment tray is a catalyst
break down arrangement. A pair of six inch fans 70 are
mounted horizontally above the waste liquid collection area
71. Below each fan is a bed 72 of ruthenium pellets or
other catalytic material, through which the fans draws air.
As can be seen in Figure 11 the fans draws in air (and
hence any atmospheric ozone, as ozone is heavier than air)
through the holes in the V shaped insert. The air passes
over the aqueous ozone liquid drawing off any ozone gas that
may be coming out of the solution. This ozone air mix is
then drawn through a catalyst, which converts it into
oxygen. The oxygen is released into the atmosphere.
Thus the system takes a number of previous systems
(ozone generator, oxygen concentrator, differential pressure
injector) and combines them in such a way as to produce a
portable and highly mobile unit that is able to produce very
high aqueous ozone concentrations (>20ppm).
Previous aqueous ozone based disinfection systems have
been based on large less-portable systems or on mobile
systems that can only produce low concentration aqueous
ozone solutions (5ppm). The concept of applying ozone to
wounds is not novel, however the theories developed based on
the inventors research and understanding of biological
systems and their modes of interaction with aqueous ozone is
novel. The development of an effective system to apply high
concentration aqueous ozone to a human (or animal) without
endangering the patient through exposure to ozone gas is
novel and inventive. The invention incorporates an aqueous
ozone delivery system that delivers the high concentration
solution to the wound surface whilst minimising the amount
of ozone gas released from that solution. The design of the
spray configuration, the pressure requirements and the spray
head enclosure design are all novel in regard to minimising
ozone gas release. The use of an extraction system to remove
ozone gas from the wound area is novel, as is the design,
which incorporates the aqueous ozone delivery conduit and
ozone gas extract into a single pipe system.
The catchment tray also incorporates other important
design features. The perforated insert tray is designed to
allow aqueous ozone solution to pass through to the bottom
of the tray. Ozone gas is heavier than air and hence will
remain at the bottom of the tray. The insert 48 functions to
trap the ozone gas in the bottom of the tray away from the
patient. Waste solution within the tray is removed by a
peristaltic pump and fan system, therefore removing the
ozone gas as well as the waste solution. The arrangement
has been designed so that all sources of ozone gas are
extracted back to a single manifold at the input to the
systems main fan, which forces the gas through a catalytic
destruct. The design of the system is novel and inventive in
that a single catalyst is used as a final destruct for gas
coming from three individual sources. Further, the
catalytically reacted gas is directed to and exhausted over
the surface of the ozone generator, which is preferentially
an air-cooled (as opposed to water-cooled) generator.
The primary catalytic destruct is novel and inventive.
Catalytic destructs are designed to operate with dry gas
supplies, as water poisons most catalysts. The design of the
system allows the catalyst to destroy wet ozone gas, without
damaging the catalyst.
The apparatus allows the user to determine the
concentration of the solution that is to be applied to the
surface (preferentially ranging from 1 - 21ppm). The user
is able to select the aqueous ozone concentration required
at the start of the cycle. The user is also able to select
the duration for which the solution is to be applied to the
1. An apparatus for producing a spray of ozonated water for disinfecting a
surface comprising a reservoir for water, means for supplying ozone to the water
to produce ozonated water, a nozzle for spraying ozonated water onto a surface
to be treated, a supply conduit for delivering said ozonated water from the
reservoir to the nozzle, the nozzle comprising a spray head having a number of
orifices for delivering jets of ozonated water, a shroud encircling the nozzle and
extending from the nozzle along the conduit to contain ozonated gas liberated at
the nozzle and means for creating a negative pressure at the end of the shroud
remote from the nozzle to extract ozone gas liberated at the nozzle, and the
shroud comprising an outer conduit encircling the supply conduit and having an
enlarged head encircling the nozzle at one end and a suction device connected
to the outer conduit at the other end thereof to extract ozone gas from within said
enlarged head through the outer conduit away from the nozzle.
2. An apparatus as claimed in claim 1, wherein the jets are located to
produce an overlapping spray pattern.
3. An apparatus as claimed in claim 1 or 2, wherein the spray head contains
a number of orifices between 0.2 mm and 1.5 mm in diameter, preferentially 0.5
4. An apparatus as claimed in claim 3, wherein the diameter of the orifices
is 0.5 mm.
5. An apparatus as claimed in any of the preceding claims, wherein the
means to deliver ozonated water to the nozzle comprise a pump means
arranged to pump the fluid to the spray head at a pressure of between 50 and
100 mbar.
6. An apparatus as claimed in claim 5, wherein the pump is arranged to
pump the fluid at a pressure of 70 mbar.
7. An apparatus as claimed in any of claims 1 to 6, wherein the enlarged
head of the shroud is pyramidal in shape and has an open end to encircle a
wound through which the spray is delivered.
8. An apparatus as claimed in claim 7, wherein the dimensions of the
shroud are such as to closely contain, yet not interfere with, the fluid spray
9. An apparatus as claimed in any of claims 1 to 8, wherein the spray head
is mounted on a support structure located at said one end of the outer conduit,
and wherein the other end of the conduit is connected to the suction device.
10. An apparatus as claimed in claim 9, wherein the support structure
consists of a switchable electromagnetic base and a variable position clamping
11. An apparatus as claimed in any of the preceding claims, wherein the
reservoir for ozonated water has a circuit extending from an upper level of the
reservoir and returning to the reservoir at a lower level, the circuit including a
pump for drawing off liquid at the upper level in the reservoir and returning the
liquid at the lower level, an ozbnating station and means to supply ozone to the
ozonating station to be dissolved in the flow of circulating liquid returning to the
reservoir to enable the ozone concentration in the water to be raised to a
requisite level prior to delivery of ozonated water to the spray nozzle for
application to the surface to be treated.
12. An apparatus as claimed in claim 11, wherein the circulation means has
an inlet in the reservoir which is upwardly open to minimise entry of bubbles of
ozone into the inlet.
13. An apparatus as claimed in claim 11 or 12, wherein the ozonating station
comprises a venturi through which the water in the circuit passes and to the
constriction of which the ozone gas is supplied to be entrained in the water flow.
14. An apparatus as claimed in any of claims 11 to 13, wherein the means for
supplying ozone gas into the water within the circuit is a differential pressure
15. An apparatus as claimed in any of the preceding claims, wherein the
reservoir has means for measuring the dissolved ozone concentration and/or the
oxidation reduction potential of the fluid, and means for applying said fluid.
16. An apparatus as claimed in any of the preceding claims, wherein the
reservoir has a common orifice for delivery of water to the reservoir and supply of
ozonated water from the reservoir.
17. An apparatus as claimed in any of the preceding claims, wherein any
undissolved gas in the reservoir is captured and passed through a destruct
18. An apparatus as claimed in claim 17, wherein the destruct device
comprises :
a) a gas decomposition unit for breaking down ozone gas ;
b) a heating element; and
c) a temperature sensor.
19. An apparatus as claimed in claim 18, wherein the destruct unit comprises
a manganese dioxide catalyst for breaking down the ozone gas.
20. An apparatus as claimed in claim 18 or 19, wherein the gas
decomposition unit is connected to the reservoir by a tube angled to the
horizontal to allow water resulting from the condensation of ozone to flow back to
the reservoir.
21. An apparatus as claimed in any of claims 18 to 20, wherein heating
element and temperature sensor keep the gas decomposition unit at a
temperature of between 40 and 80°C, although preferentially 60°C.
22. An apparatus as claimed in any of claims 18 to 21, wherein the
decomposed gas is directed through a secondary destruct unit.
23. An apparatus as claimed in claim 22, wherein the secondary destruct unit
is an activated carbon catalyst.
24. An apparatus as claimed in any of the preceding claims, wherein means
are provided to apply negative pressure around the region where the reaction
fluid is sprayed onto a surface.
25. An apparatus as claimed in any of the preceding claims, wherein a device
(11a) is provided for supporting a patient's appendage to be treated and
collecting fluid sprayed onto a wound on the appendage, the reaction fluid is
sprayed onto a wound and is subsequently collected in a device, onto or into
which the patient's appendage is placed.
26. An apparatus as claimed in any of the preceding claims, wherein the
equipment is portable.
An apparatus for producing a spray of ozonated water for disinfecting a
surface comprising a reservoir (12) for water, means (24) for supplying ozone to
the water to produce ozonated water, a nozzle (39) for spraying ozonated water
onto a surface to be treated, a supply conduit (37) for delivering said ozonated
water from the reservoir to the nozzle, the nozzle comprising a spray head (39)
having a number of orifices for delivering jets of ozonated water, a shroud (40)
encircling the nozzle and extending from the nozzle along the conduit to contain
ozonated gas liberated at the nozzle and means for creating a negative pressure
at the end of the shroud remote from the nozzle to extract ozone gas liberated at
the nozzle, and the shroud comprising an outer conduit (38) encircling the supply
conduit (37) and having an enlarged head (40) encircling the nozzle at one end
and a suction device (32) connected to the outer conduit at the other end thereof
to extract ozone gas from within said enlarged head through the outer conduit
away from the nozzle.


2393-KOLNP-2005-CLAIMS 1.1.pdf

2393-KOLNP-2005-CORRESPONDENCE 1.1.pdf


2393-KOLNP-2005-DRAWINGS 1.1.pdf

2393-KOLNP-2005-FORM 13.pdf

2393-KOLNP-2005-FORM 27 1.1.pdf

2393-KOLNP-2005-FORM 27.pdf






2393-kolnp-2005-granted-description (complete).pdf


2393-kolnp-2005-granted-examination report.pdf

2393-kolnp-2005-granted-form 1.pdf

2393-kolnp-2005-granted-form 18.pdf

2393-kolnp-2005-granted-form 3.pdf

2393-kolnp-2005-granted-form 5.pdf


2393-kolnp-2005-granted-reply to examination report.pdf



Patent Number 233796
Indian Patent Application Number 2393/KOLNP/2005
PG Journal Number 15/2099
Publication Date 10-Apr-2009
Grant Date 08-Apr-2009
Date of Filing 28-Nov-2005
# Inventor's Name Inventor's Address
PCT International Classification Number A61M 35/00, 27/00
PCT International Application Number PCT/GB2004/002212
PCT International Filing date 2004-05-24
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 0311958.3 2003-05-23 U.K.