austlii:cth/APO/2025/17
General information, not legal advice.
APO
2025-06-03
Original judgment source is linked above.
Patent attorney for the applicant: Allens Patent & Trade Mark Attorneys
The opposition is successful. Claims 1-11 are not inventive.
Subject to appeal, I provide a period of 2 months to file suitable amendments.
I award costs according to Schedule 8 of the Patents Regulations 1991 against the applicant.
Referring to FIG. 1, a fluid mixing system 10 can include a treated water tank 100 that is fluidly connected to a treated water source 80. Treated water 102 can flow from treated water source 80 into treated water tank 100. Treated water 102 can enter treated water tank 100 at approximately 17 degrees Celsius. A vacuum pump 110 can remove the air and gases from within treated water tank 100. In one aspect, vacuum pump 110 can create a deaeration pressure within treated water tank 100 of at least approximately 0.8 bar. In another aspect, the deaeration pressure within treated water tank 100 can be approximately 0.91 bar.
A treated water pump 104 can pump treated water 102 from within treated water tank 100 to the next stage of mixing system 10. In one aspect, treated water pump 102 (sic) can pump treated water 102 through a cooling system 160 to reduce the temperature of treated water 102. In one aspect, cooling system 160 can reduce the temperature of treated water 102 from approximately 17 degrees Celsius before treated water 102 enters cooling system 60 to approximately 7.6 degrees Celsius after treated water 102 exits cooling system 160. In another aspect, treated water 102 can be maintained at ambient temperature in mixing system 10.
Mixing system 10 can include concentrate 132 in a concentrate tank 130. Concentrate 132 can be a beverage flavor syrup. Treated water 102 can mix with concentrate 132 to form a fluid mixture.
A carbonized pump 140 can inject carbon dioxide into the fluid mixture in carbon dioxide dosing apparatus 142 to create a carbonized fluid mixture, i.e., product fluid 152. In one aspect, carbon dioxide injection in carbon dioxide dosing apparatus 142 can occur at a pressure in a range of approximately 3.2 bar to approximately 4.2 bar.
The fluid 152 can be stored in a carbonized tank 150 prior to traveling to a filling machine 300 for dispensing into a container 400 (FIG. 3). In one aspect, carbonized tank 150 can be pressurized at approximately 5.5 bar. In another aspect, carbonized tank 150 can be pressurized at approximately 0.5 bar higher than filling machine 300.
Fluid 152 can exit carbonized tank 150 through product supply conduit 200 and can enter product cooling conduit 202 to cool fluid 152 by passing fluid 152 through cooing system 160. In one aspect, fluid 152 can enter cooing system 160 at approximately 11.8 degrees Celsius and can exit cooling system 160 at approximately 6.8 degrees Celsius. In another aspect, carbonized tank 150 can be fluidly connected to filling machine 300 such that fluid 152 can be maintained at ambient temperature in carbonized tank 150 and in filling machine 300.
In one aspect of the invention, the treated water, fluid mixture, and product fluid 152 can have a laminar flow as they move through mixing system 10. This laminar flow can reduce foam formation in the fluid 152.


The filling machine 300 can include a support housing 302 having an upper surface 304 and a lower surface 306 defining an inner fluid chamber 310 for supplying the fluid 152 to be discharged into the corresponding container 400. The fluid 152, which is preferably a liquid beverage, can fill a portion of the fluid chamber 310 while leaving a headspace 320 above the fluid 152 for a pressurized inert gas such as carbon dioxide or nitrogen. The supply and return pipes for the fluid 152 and gas as well are not shown in these Figures.
A valve housing 330 can be mounted to the lower surface 306 of the support housing 302 for controlling the discharge of the fluid 152 into the container 400. The valve housing 330 is shown schematically in the Figures and may be of any suitable design or configuration. An annular container seal 332 can be provided within the valve housing 30 for sealingly engaging the container 400. In the embodiment shown in FIG. 3, the container seal 332 can be designed to seal against a bottle type container 400. In another aspect, the container seal 332 can be configured to accept a can. A control device 340 can be disposed adjacent the upper surface 304 of the support housing 302. The control device 340 will be discussed in greater detail below.
A vent tube 312 can have a first end 313a and a second end 313b with the second end 313b at least partially extending through the valve housing 330. Vent tube 312 can have a height less than approximately 4.5 mm. Vent tube 312 can have an umbellate ring 316 (FIG. 4) positioned adjacent second end 313b. Umbellate ring 316 can have a diameter 317.
The vent tube 312 can move along a predetermined stroke between a filling position and a non-use position. The second end 313b of the vent tube 312 and umbellate ring 316 can be disposed within the container 400 while in the filling position and the second end 313b of the vent tube 312 can be raised above the container 400 while in the non-use position. When vent tube 312 is in the filling position, umbellate ring 316 can be centered in the X direction and in the Y direction with respect to container 400...
...A fluid sealing mechanism 322 including a spring 318 can be movably mounted with respect to the support tube 314 for controlling the discharge of the fluid 152 from the inner fluid chamber 310 to the container 400. The length of spring 318 can be decreased
for slower valve movement. In one aspect, the spring strength can be optimized for laminar flow of fluid 152 from filling machine 300 into container 400. Valve fixing surface angle adjustments can also be made.
A cold fill system can dispense a fluid at approximately 8 degrees Celsius into a container. In one aspect of the invention, fluid 152 can be dispensed into container 400 at approximately 15 degrees Celsius resulting in significant energy savings. The filling system according to the present invention that fills containers 400 with a fluid at approximately 15 degrees Celsius can result in a reduction in system energy required to cool the fluid of approximately 60%, as compared to a cold fill system that fills at approximately 8 degrees Celsius.
A method of producing a container filled with a carbonated fluid product, the method comprising:
mixing the treated water with a concentrate to create a fluid mixture;
injecting the fluid mixture with carbon dioxide to create the carbonated fluid product;
storing the carbonated fluid product in a carbonized tank that is fluidly connected to a filling machine;
operating the filling machine to fill the container with the carbonated fluid product,
wherein the treated water, fluid mixture, and carbonated fluid product are maintained at an ambient temperature.
A method of producing a container filled with a carbonated fluid product, the method comprising:
retaining treated water at an ambient temperature in a water tank;
deaerating the water tank using a vacuum pump to create a negative pressure of at least 0.8 bar;
mixing the treated water with a concentrate to create a fluid mixture;
injecting the fluid mixture with carbon dioxide at a pressure in a range of approximately 3.2 bar to approximately 4.2 bar to create the carbonated fluid product;
storing the carbonated fluid product in a carbonized tank that is fluidly connected to a filling machine, the carbonized tank having an interior pressure of approximately 5.5 bar;
operating the filling machine to fill the container with the carbonated fluid product, the filling machine having an interior pressure of approximately 5 bar, and the carbonated fluid product being at the ambient temperature.
THE PERSON SKILLED IN THE ART AND THE EXPERTS
"In Catnic Lord Diplock said (at 242) that skilled addressees are "those likely to have a practical interest in the subject matter of [the] invention". A variety of people may have that interest. There are those who might wish to make or construct the invention, those who may wish to compound the invention and those who may wish to use the invention."
One aspect of the invention permits a filing system that utilizes an increase in filling temperature, for example, ambient temperature. To achieve the increased filling temperature, the mixer and blower operating parameters can be modified along with a new filing system ventile design. The present invention permits filing of a container with a carbonated fluid at ambient temperatures.
"...specific experience in the processes and equipment for mixing and filling of carbonated beverages into containers, and in particular in the design and working of multi-component mix processors and fillers."
"...was responsible for maintaining all engineering facets in a manufacturing plant, including the beverage base and concentrate for Coca-Cola products; and co-ordinating and supervising the installation of plant equipment and machinery during plant expansions and upgrades for the Coca-Cola Export Corporation between January 1990 and May 1997, and provided technical support to various departments such as QA (Quality Assurance), bottlers and suppliers, including conducting bottling line trials/audits, for Coca-Cola South Pacific between May 1997 and November 2005. From April 2006 to December 2006, he managed installation, commissioning, training and acceptance of machinery sales, including food and beverage manufacturing equipment, for Carter Holt Harvey. From December 2008 to April 2013, he worked for Visy Plastics, where he was responsible for liaising with key technical partners (including the Opponent) in developing and validating new materials and designs, including hot-fill technologies."
"The notion of common general knowledge itself involves the use of that which is known or used by those in the relevant trade. It forms the background knowledge and experience which is available to all in the trade in considering the making of new products, or the making of improvements in old, and it must be treated as being used by an individual as a general body of knowledge."
a) sourcing and de-aeration of treated water to be used to make the drink; > > b) mixing of the water with a syrup containing a flavour concentrated, sugar and acid to make a liquid mixture (called final syrup); > > c) carbonation of the liquid mixture through the injection of carbon dioxide (COs); > > d) storing the carbonated fluid in a pressurized tank in preparation for transfer to the filling machine."[34]
"As a first step, water is treated in accordance with a manufacturing specification to remove any impurities in accordance with the product specification (e.g., chloride, fluoride ions). Depending on the location of the manufacturing site, the water may be sourced from mains water or spring water.
The water treatment step typically includes sterilisation and/or filtration steps. The water is also typically deaerated. Deaeration facilitates in reducing the amount of air within the water, which helps to prepare a more uniform mixture with concentrates (syrups).
The treated water is then mixed at a predefined ratio with a prepared syrup. The mixing can take place as the fluid moves through pipework, in a mixing tank, or through a 'Paramix' system.
The water/syrup mixture is then blended with CO2 at a predefined ratio to produce a carbonated beverage. The specific mechanism for the CO2 blending step may differ depending on the specific equipment of the manufacturing site.
The cooling of the beverage can take place at different stages of the product line. For example, the treated water may be cooled before mixing with the syrup, or the water/syrup mixture may be cooled before blending with CO2. Cooling the beverage helps by increasing CO2 absorption (reducing the amount of CO2 required to carbonate the beverage) and reducing foaming.
The carbonated beverage fluid is then provided to a filler bowl for filling in a product container (e.g., a PET bottle, glass bottle or an aluminium can) via filling heads, after which the container is sealed."
Temperature of operation of soft drink mixing systems
In the carbonation process, CO2 is injected into the beverage in an enclosed carbonation tank pressurised with the gas. Equilibrium between the gases in the liquid and the corresponding pressure in the tank will exist after a certain time. CO2 will be absorbed into the beverage and will remain in a dissolved state while the beverage is maintained under pressure. The higher the CO2 content required, the higher the saturation pressure required at a given temperature. Conversely, the lower the temperature for a given content, the lower the saturation pressure required.
"Before the priority date in November 2016, whether or not a cooling system was incorporated in a bottler's plant was strongly influenced by the cost of energy and the bottler's economic approach to running their plant. Taking into account all factors required to run a carbonated beverage plant, including age, type and size of: tanks, lines, pumps, fillers and any heat exchanges, the cost of energy required to run the plant was, and still is, a major consideration. The cost of CO2 was also an important factor... All these factors needed to be weighed up against each other, which resulted in some manufacturers choosing to cool the fluid in their carbonated beverage production, and other manufacturers choosing to leave their fluid un-cooled."
"The decision as to the temperature to use in the process depends on the geographical location, the systems available and an economic assessment of competing costs.
Mixing systems (whether tank-based or inline) and filling machines to make carbonated drink and fill containers were typically performed at ambient temperature in Europe, Australia and other countries with similar temperatures from well before the Priority Date. For example, in Germany all Coca-Cola bottlers fill their bottles at ambient temperature for many years."
"The cooling of the beverage can take place at different stages of the product line. For example, the treated water may be cooled before mixing with the syrup, or the water/syrup mixture may be cooled before blending with CO2. Cooling the beverage helps by increasing CO2 absorption (reducing the amount of CO2 required to carbonate the beverage) and reducing foaming."
"The entire product line between water treatment and filling is typically a closed system to prevent foreign matter from contaminating the beverage. The design of this closed system has an added benefit of limiting the influence of external temperature fluctuations on the product stream. This means that the treated water or beverage mixture can be cooled to the selected filling temperature by means of a single heat exchange process upstream of the filling step.
It is important that the temperature of the beverage is controlled within the product specification ranges throughout the mixing, carbonation and filling processes to ensure that the beverage product meets product specifications for flavour and carbonation content. Temperature instability while manufacturing beverage can cause poor quality and uncontrolled CO2 content which is unfavourable to maintaining flavour profiles."
"It is not clear how Mr Kalinowski can make sweeping statements in relation to Australia or other countries (since his experience in Australia seems to be limited to the commissioning of a single pre-mixer for Schweppes in 1999 [Kalinowski #1 at [8]-[10]), which he does not say bottled carbonated beverages at ambient temperature, and his experience elsewhere seems to be limited to plants in Tanzania which used a cooler [Kalinowski #1 at [8] and [10]] and plants in the United States, which also used a cooler [Kalinowski #1 at [12] and [73]]. Mr Kalinowski does not detail the specific ambient temperature values he is referring to. Mr Aloisio explains that at some stages, ambient temperatures may coincide with the temperature thresholds set for manufacturing at carbonated beverage... but that these temperature thresholds are managed with heat exchangers or cooling units because of environmental temperature fluctuations, which mean the set filling temperature would be unlikely to coincide with the ambient temperatures year round [Aloisio at [126]]."
"the words in a claim should be read through the eyes of the skilled addressee in the context in which they appear ... while the claims define the monopoly claimed in the words of the patentee's choosing, the specification should be read as a whole ... it is not permissible to read into a claim an additional integer or limitation to vary or qualify the claim by reference to the body of the specification ... terms in the claim which are unclear may be defined or clarified by reference to the body of the specification."
"Lack of precise definition in claims is not fatal to their validity, so long as they provide a workable standard suitable to their intended use. The consideration is whether, on any reasonable view, the claim has meaning. In determining this, the expression in question must be understood in a practical, common sense manner."
1. to keep in existence or continuance; preserve; retain: to maintain good relations with New Zealand.
2. to keep in due condition, operation, or force; keep unimpaired: to maintain order; maintain public highways.
3. to keep in a specified state, position, etc.
3. of or relating to the surrounding air, especially with regard to temperature, pressure, humidity, etc.
The method of claim 1, wherein the fluid product is not cooled before entering the filling machine.
"Claim 2 defines a method dependent on claim 1 where 'the fluid product is not cooled before entering the filling machine'. This suggests that claim 1 covers embodiments where fluid product is cooled before entering the filling machine which is inconsistent with claim 1 requiring the carbonated fluid product to be 'maintained at an ambient temperature'."
"For example, if the water was initially heated above ambient temperature for the purpose of being treated, it might need to be cooled. In that scenario, the treated water would be maintained at ambient temperature, but there would nonetheless be cooling. Claim 1 would be infringed, but claim 2 would not. Claim 2 is a narrower claim, and requires that the fluid is not cooled."
"The specification and claims are also unclear as to what the (sic) pressure carbon dioxide is injected into the fluid mixture. Paragraph [0022] and claims 4 and 10 describes a pressure range at the carbon dioxide dosing apparatus of approximately 3.2 bar to approximately 4.2 bar. However, Fig. 1 shows the pressure at the carbon dioxide dosing apparatus 142 as 4.0 bar/3.10 bar. This could mean the CO2-gas pressure in front of a injectors is 4.0 bar and after the injectors it drops because of the suction of the injectors to a pressure of 3.10 bar. However, the carbon dioxide pressures in Fig. 1 and paragraph [0022] are inconsistent with other pressures shown in Fig. 1. For example, to reach a buffer tank pressure of 5.5 bar and filling machine pressure of 5.0 bar, the carbon dioxide injecting pressure of 3.2 to 4.2 bar is too low. This is because there will be a 1.5- 3.0 bar drop across the carbon dioxide dosing apparatus 142 that must be accounted for before the dosing apparatus 142, which an injecting pressure of 3.2 to 4.2 bar does not achieve."
"...need to specify the pressure at which carbon dioxide is injected into the fluid mixture (which will depend in any case on the CO2 concentration required, but the determination of which is well within the capacity of the skilled addressee)."
"In CSR Building Products Ltd v United States Gypsum Company [2015] APO 72, Dr S D Barker adopted the summary provided by Aldous J in Schering Biotech at 252 - 253, which has been often followed in the United Kingdom (emphasis added):
...to decide whether the claims are supported by the description it is necessary to ascertain what is the invention which is specified in the claims and then compare that with the invention which has been described in the specification. Thereafter the court's task is to decide whether the invention in the claims is supported by the description. I do not believe that the mere mention in the specification of features appearing in the claim will necessarily be a sufficient support. The word "support" means more than that and requires the description to be the base which can fairly entitle the patentee to a monopoly of the width claimed.
That approach encapsulates broadly the claim support obligation under s 40(3). To it may be added the requirement that the technical contribution to the art must be ascertained. Where it is a product, it is that which must be supported in the sense that the technical contribution to the art disclosed by the specification must justify the breadth of the monopoly claimed".
"Although discussion of s 40(3) is often focused on the breath of the claim, there may be some claims which lack support not because they are too broad, but because they define an invention that is materially different to what is described in the body of the specification. Hence, a claim that includes a feature not disclosed in the specification, or omits a feature that is disclosed, may lack support because the invention claimed is materially different from the invention disclosed. Whether or not the claim will lack support in such circumstances will depend on the proper characterisation of the invention disclosed in the body of the specification and the invention claimed."
In an aspect of the invention, method of producing a container filled with a carbonated fluid product can include retaining treated water in a water tank, deaerating the water tank using a vacuum pump, mixing the treated water with a concentrate to create a fluid mixture, injecting the fluid mixture with carbon dioxide to create the carbonated fluid product, storing the carbonated fluid product in a carbonized tank that is fluidly connected to a filling machine, and operating the filling machine to fill the container with the carbonated fluid product. The treated water, fluid mixture, and carbonated fluid product can be maintained at an ambient temperature.
A treated water pump 104 can pump treated water 102 from within treated water tank 100 to the next stage of mixing system 10. In one aspect, treated water pump 102 can pump treated water 102 through a cooling system 160 to reduce the temperature of treated water 102. In one aspect, cooling system 160 can reduce the temperature of treated water 102 from approximately 17 degrees Celsius before treated water 102 enters cooling system 160 to approximately 7.6 degrees Celsius after treated water 102 exits cooling system 160. In another aspect, treated water 102 can be maintained at ambient temperature in mixing system 10.
Fluid 152 can exit carbonized tank 150 through product supply conduit 200 and can enter product cooling conduit 202 to cool fluid 152 by passing fluid 152 through cooing system 160. In one aspect, fluid 152 can enter cooing system 160 at approximately 11.8 degrees Celsius and can exit cooling system 160 at approximately 6.8 degrees Celsius. In another aspect, carbonized tank 150 can be fluidly connected to filling machine 300 such that fluid 152 can be maintained at ambient temperature in carbonized tank 150 and in filling machine 300.
The general filling operation of the filling machine 300 is now discussed. Fluid 152 can have a laminar flow through filling machine 300. In another aspect, fluid 152 can be filled into containers 400 from filling machine 300 at ambient temperature, e.g., approximately 15 degrees Celsius. Ambient filling requires less cooling and can result in significant operating cost savings.
"The pressure ranges provided in claim 10 are disclosed in the preferred embodiment in the context of using cooling devices not in the context of performing the process at ambient temperature. For example, the pressure range of 3.2 to 4.2 bar is described in the context of the embodiment shown in Fig. 1 where there are two cooling stages, i.e. not for ambient temperature. Since an increase in beverage temperature requires an increased carbonation pressure, the claimed pressure range in claim 10 for fluid mixture at ambient temperature is not supported by the description."
a) construe the claims to determine the scope of invention as claimed,
b) construe the description to determine what it discloses to the person skilled in the art, and
"...judged against the invention as claimed and, where appropriate, against its essence or core where that is understood to be related to the technical contribution the specification makes to the art and/or its inventive concept."
"...the Applicant's case is not that it was not known how to produce and fill carbonated beverages at ambient temperature. It is that was not known to produce and fill carbonated beverages at ambient temperature. In light of that significant distinction, it is apparent that the Opponent's case on an absence of disclosure fails at the threshold."
The method of any one of claims 1 to 7, wherein the treated water, fluid mixture, and carbonated fluid product have a laminar flow.
"Section 18(1)(c) of the Patents Act provides that an invention is a patentable invention for the purposes of a standard patent if the invention, so far as claimed in any claim, is useful. Until recently, the requirement that an invention so far as claimed be "useful" within s 18(1)(c) was defined solely by reference to the common law development of that concept. The words in Lane Fox v Kensington & Knightsbridge Electric Lighting Co [1892] UKLawRpCh 139; [1892] 3 Ch 424 at 431 ... of Lindley LJ (with whom Lopes LJ agreed) set the scene (emphasis added):
The utility of the alleged invention depends not on whether by following the directions in the complete specification all the results now necessary for commercial success can be obtained, but on whether by such directions the effects which the patentee professed to produce could be produced, and on the practical utility of those effects.
What the patentee "professed to produce" is to be ascertained by having regard to what is now routinely referred to as the "promise of the invention" being the promise that the specification is said to make of the invention claimed: Rehm Pty Ltd v Websters Security Systems (International) Pty Ltd (1988) 81 ALR 79 at 84 and 96-7; 11 IPR 289 at 292 at 305-6 (Gummow J); Décor Corporation Pty Ltd v Dart Industries Inc [1988] FCA 399; (1988) 13 IPR 385 at 394 (per Lockhart J). This is assessed as a matter of construction of the specification: see generally ESCO Corporation v Ronneby Road Pty Ltd [2018] FCAFC 46; (2018) 358 ALR 431...[2018] FCAFC 46 at [182]-[239]...
In each case it is necessary to consider the nature of the promise of the invention by reference to the specification and also whether that promise is met by that which is the subject of the claims. Often that enquiry gives rise to a question of claim construction: if a broad claim includes something that does not meet the promise of the invention, will it be invalid for want of utility? ...
There is no dispute that a promise may be implied from language used in the specification."
"As noted above in relation to s 40, the description of the preferred embodiments identifies various control parameters such as pressures in the context of cooling the process. The process would not work if all cooling in the system was simply bypassed and nothing else was adjusted. The filling pressure at the filler would need to be very high, well above the saturation pressure of the final carbonated beverage at 6.8°C and at 17°C.
Further, if the cooling was simply by-passed, the final product would not meet product specification, foaming would occur and the bottler would lose control of the entire process. In practice, adjustments would need to be made to the process to compensate for removing the entire cooling system or even part of it. If the cooling system was by-passed, the fluid temperature would rise and the fluid pressure would need to be increased to keep a pressure above the saturation pressure in order to maintain the CO₂ content. A larger filling machine may be required and/or the production speed would need to slow down to increase the pressure relief time period (snifting time). However, the Opposed Application does not explain any such compensation resulting from by-passing the cooling system 160."
"The basic test for anticipation or want of novelty is the same as that for infringement and generally one can properly ask oneself whether the alleged anticipation would, if the patent were valid, constitute an infringement."
"A signpost, however clear, upon the road to the patentee's invention will not suffice. The prior inventor must be clearly shown to have planted his flag at the precise destination before the patentee".
"In respect of the issue whether information was 'publicly available' before the priority
date, the following principles emerge from the cases:
D1: Fullmix" product brochure, obtained at Interbrau trade fair in Munich, Germany on 25 September 1993.

"There is no cooling (or heating) device in the diagrams or description of D1. Additionally, step 4) on page 4 states that "The deaeration process is performed at ambient temperatures and therefore requires no plates or other surface elements". The schematic diagrams on pages 4, 5 and 6 obviously follow on one after the other to show the entire mixing and carbonating process. Since the deaerated water is at ambient temperature and there is no indication of any cooling, the PSA would understand the entire process to the filler line is performed under ambient temperature. As discussed below, it would be very unlikely that the beverage is cooled at the filler. It would not make sense to cool at the final step at the filler as it would be much easier and more economical to cool earlier in the process. Accordingly, in the absence of any explicit teaching of such an unusual cooling step, the PSA would understand that D1 taught the production and filling of carbonated beverages at ambient temperature."
D6: Dissertation entitled "For the Optimization of High-Performance Filling Systems for Carbonated Beverages" by M. Rammert, published in 1993
"In 2009/2010, Krones installed and commissioned a "Contiflow mixer" (Krones machine number KB40204) and a filler "MECAFILL VKP-PET" (Krones machine number K129A55) at Vilsa's premises.
This mixing and filling system was designed to carry out the following steps 4) to 10), which procedure was carried out, among others, during commissioning in 2010 (with Vilsa employees) and during subsequent production in 2010 and thereafter for several carbonated drink products. Steps 1) to 3) were carried out using overall system components at Vilsa production site, i.e. that were not installed by Krones.
"During the entire process, i.e. during all of these 10 steps, neither the water nor the degassed water nor the mixture nor the carbonated soft drink was actively cooled or heated. Accordingly, throughout production there was no active influence on the temperature of the water, the degassed water, the mixture of concentrate (syrup) and water or the carbonated drink. Neither the water, the degassed water, the mixture, nor the carbonated soft drink flowed through a device (e.g. a heat exchanger) that actively influenced or changed the temperature until the product was bottled and the bottle was closed. As a result, the carbonated soft drink was bottled at nearly the same temperature as the water from the ground source in step 1).
The water temperature from the mineral water source was usually in the range of 15°C +/- 2°C throughout the year. This temperature did not change significantly during all the above mentioned steps 1) to 10). Apart from minor changes, the water temperature largely corresponded to the filling temperature. During longer production stops, the temperature of the water within the plant (tanks and pipelines) could reach values of 17°C or higher due to transferred heat from the production facility to the water. To avoid unnecessary water losses, this water was used in the beginning of the next production to produce carbonated soft drinks. Consequently, the first filled containers had a slightly higher temperature compared to the containers filled during normal operation."
"...in my experience each manufacturer has strict protocols around safety and security, including information security, security gates requiring personnel sign-in, and restricted areas secured by key passes. The beverage industry is highly competitive and the syrups for carbonated beverages are typically kept confidential, along with other sensitive manufacturing details. In my experience, personnel on site, whether employees or contractors, are informed or understand that confidentiality protocols are in place.
Throughout my career, including as an employee and in various consultancy roles, my access once on-site has generally been restricted to only the facilities related to my role - that is, access to the broader manufacturing site is not provided. It is also common general practice to sign nondisclosure agreements for certain major projects, often without an end date specified in the agreement.
The equipment used in carbonated beverage lines typically look like large stainless-steel units. There are no signs identifying what each piece of equipment is doing and equipment can include outer casings with inner mechanisms that are not visible. The specific parameters being used (e.g., flow rate, temperature, pressure) are also not apparent without close inspection or disassembly. Furthermore, as there are multiple tanks, fluid lines etc., it is difficult to understand where product is flowing without detailed schematics, particularly when equipment is located over various rooms and sections in a factory."
(b) a combination of any 2 or more pieces of prior art information that the skilled person mentioned in subsection (2) could, before the priority date of the relevant claim, be reasonably expected to have combined.
"The test is whether the hypothetical addressee faced with the same problem would have taken as a matter of routine whatever steps might have led from the prior art to the invention, whether they be the steps of the inventor or not."
"Would the notional research group at the relevant date in all the circumstances directly be led as a matter of course to try [the claimed invention] in the expectation that it might well produce a useful [desired result]?"
a support housing having an upper surface and a lower surface defining an inner fluid chamber for supplying the fluid material to be discharged into the container;
a valve housing mounted to the lower surface for controlling the discharge of the fluid material;
a vent tube having a first end and a second end, the second end at least partially extending through the valve housing;
an umbellate ring surrounding the vent tube and being positioned adjacent the second end of the vent tube;
a spring positioned about the first end of the vent tube; and
a fluid sealing mechanism positioned adjacent to the upper surface and operating with the spring to control fluid flow into the beverage container.
The opponent suggests that the claim recites well known components of filling machines at the priority date[97]. The applicant takes no contention with the opponent's position and their evidence does not address the claim. I accept the opponent's position and also find claim 11 obvious.
"D1 clearly teaches the production of carbonated drinks at ambient temperature. To the extent that D1 is said not to exclude the possibility of cooling at the filler, for the reasons detailed above, if the PSA wished to reduce energy usage the first thing they would consider would be to avoid any such cooling step. As noted, it was well within the ordinary skill of the PSA to determine the necessary operating conditions, including pressures, to produce and fill the specified carbonated beverage without cooling.
"...the Opponent should pay the Applicant's costs, given the Opponent's conduct, including the Opponent's filing evidence in German and not providing translation, raising grounds (such as manner of manufacture) which were misconceived and then dropping them on the eve of the hearing and including a vast quantity of prior art (including prior art introduced on amendment) and relying very little on it."
[3] Specification at [0032]-[0036] and [0039]
[31] [1980] HCA 9; (1980) 144 CLR 253 at page 292
[44] Carbonated Soft Drinks - Formulation and Manufacture: edited by P. Steen and Philip R. Ashurst, 2006.
[63] Monsanto Co v Commissioner of Patents (1974) 48 ALJR 59
[64] [2000] FCA 890 and cited with approval in Austal Ships Sales Pty Ltd v Stena Rederi Aktiebolag [2008] FCAFC 121
[65] The Macquarie Dictionary, https://www.macquariedictionary.com.au
[67] [2020] FCA 1477 (Merck) at [546]-[547]
[68] Calix Limited v Grenof Pty Ltd [2023] FCA 378 at [128]
[69] Kalinowski #1 at [106] and [108], Kalinowski #2 at [21]-[24]
[72] Cytec Industries Inc. v Nalco Company [2021] FCA 970
[73] Jusand Nominees Pty Ltd v Rattlejack Innovations Pty Ltd (Jusand) [2023] FCAFC 178 at [191], [217]
[76] Nicaro Holdings Pty Ltd v Martin Engineering Co [1990] FCA 40 at [19]
[77] The General Tire & Rubber Company v The Firestone Tyre and Rubber Company Limited [1972] RPC 457 at [486]
[79] Damorgold Pty Ltd v JAI Products Pty Ltd [2015] FCAFC 31 at [11]- [12], [48]-[49]
[80] Weippert at [4]-[6], corroborated by Stüttgen at [5]-[6]
[81] Weippert at [7]-[10], Stüttgen at [7]-[10]
[84] Kalinowski #2 at [19] and [20]
[86] [2002] HCA 59 at [51]- [53]
[87] [1970] RPC 157 at 187
[88] Specification at [0002]-[0005]
[93] Kalinowski #1 at [98] and Kalinowski #2 at [26]
Krones AG
PepsiCo, Inc. [2025] APO 17
(1988) 13 IPR 385
(1988) 81 ALR 79
(2018) 358 ALR 431
(1961) 180 CLR 98
(2006) 154 FCR 31
(1989) 25 FCR 565
(1980) 144 CLR 253
(1974) 48 ALJR 59