The invention shows: at least one supply component filled with preferably bulk material for liquids and gases which is used for carbonation.
State-of-the-art is, for example, that liquids and gases are supplied to a, for example, carbonating vessel for carbonation. These are introduced in the carbonating vessel through two separate lines. In this case, a supply component is not used for simultaneously supplying gases and liquids into the carbonating vessel which is preferably used for carbonating. In the state-of-the-art, by inventions by Mrs. Margaret Spiegel, the following patent-application Serial No. 100 55 137.8 “Supply Component For Gas And Liquids” discloses a so-called supply component for gases and liquids, and proposes with reference to at least one mixer for gases and liquids or carbonator system, to also employ a supply component for liquids and, preferably, CO2. This is generally done by flowing liquids and gases in the supply component towards an inline-carbonator, and can therefore only viewed as state-of-the-art for an individual component of an inline-carbonator.
The entire application and description texts and claims do not suggest that the so-called component or components in the aforementioned applications, the so-called supply component can be used also simultaneously as an inline-carbonator for liquids and gases or pre-carbonator without a separate inline-carbonator, or that the aforementioned supply components are preferably filled with bulk material, secured by preferably sieve material.
It is also not suggested that the fill of the inline carbonator(s) or mixer(s), through the preferably tap water flows in a flow-through principle, is misted or nebulized by the fill for absorbing the preferably CO2 and to combine therewith, and through this principle a large surface is produced and carbonation, for example, is performed. This is preferably solved by the invention of a component for liquids and gases, which is preferably filled with for example bulk material, as described below.
By already filling the supply component with preferably bulk material. By this measure, the supply component alone can already be used for carbonation and pre-carbonation, for example, preferably also without bulk material fill and without preferably retainer sieves. By preferably introducing tap water and preferably CO2 into the aforementioned supply component.
In this process, the introduced liquid is directly incident on the introduced preferably CO2, or the introduced liquids is incident on the bulk material inside the supply component for liquids and gases.
As a result, the liquid is for example separated or more clearly expressed nebulized by the large surface produced by the for example bulk material or the large surface of the interior wall of the supply component. When the preferably nebulized liquid flows towards preferably at least one post-mix valve or dispensing location, then the preferably nebulized liquid can combine with preferably CO2 because at the same time preferably CO2 as well as the liquid is introduced into the supply component. By this measure, the CO2 can preferably mix with the nebulized liquid already in the supply component. This is viewed in the flow-through process as flow-through carbonation and is not used in stationary liquid carbonation processes, like, for example, in the carbonating vessel.
Or like the principle of inline-carbonators, where the carbonation process is performed only in the separate inline-carbonator. However, this takes place also in the flow-through carbonation process. This shows that the component, which is preferably filled with bulk material and used in the supply component for liquids and gases, which is preferably used for carbonation, is in itself inventive. Because with the invention, for example the carbonation vessel or the inline-carbonators are completely eliminated. Because the preferred liquid and gas introduction and the carbonation process take place in a single component.
Because injection molded components made of suitable plastic material can be used with the invention, cost-effective production can be easily implemented or existing components can be modified very inexpensively, for example pluggable connectors from the company John Guest, such as for example the T-connector from this company. These T-connectors can be modified so that they can be easily used, for example, without bulk material or filled with bulk material, as well as also provided with a sieve retainer material, such as for example hat sieves from the company Neoperl, for securing the solid maternal.
The off-the-shelf parts from the company John Guest can also be used to connect to the supply component, for example, tap water and gases via at least one screw connection.
The supply component can also be only partially filled with preferably bulk material, because the water flow presses the partially introduced bulk material against the retaining sieve, with the carbonated liquid flowing towards the outlet to at least one dispensing location, which is designed with at least one pump, which can preferably boost the pressure towards the dispensing location and is preferably designed as self-priming displacement pump or membrane pump.
The quantity of the flowing gas and liquid can depend on the size of the supply component for gases and liquids, preferably unfilled or filled with bulk material, depending on the respective through openings. This should preferably be taken into account when using at least one pump. The supply component for liquids and gases can also have a straight configuration with at least one inlet and outlet. This component can also be fabricated and applied as a Y-piece, for example for supplying carbonated liquid to two separate lines (not illustrated).
The employed backflow preventers (not illustrated) can preferably be secured by inserted lines.
The preferably retainer and impregnation sieves or sieve material can be arranged in any position inside or outside the supply component.
These advantages of the invention of at least one supply component, preferably carbonator, unfilled or filled with preferably bulk material, is not state-of-the-art according to our extensive searches and is therefore inventive in itself.
The following is an exact description of the invention, with the
The invention describes: supply components (1) (11) (12) unfilled or filled with preferably bulk material (5) for liquids and gases, which is preferably used for carbonating or impregnating without a separate carbonator principle or inline-carbonator principle as a separate component.
The invention preferably uses the component (1) which is preferably implemented as a hollow T-member (1). For filling this component (1) preferably with bulk material (5). Before this is done, retainer sieves (3) are preferably applied on, for example, two sides of the openings (4), which are in turn attached to the component (1) with gas-tight connections (not illustrated), in order to retain the sieves (3) and to enable supply of liquids and gases or to preferably function as an outlet for carbonated liquid. The retained sieves (3) are used to prevent the preferred bulk material (5) from being flushed out if, for example, liquid is introduced into the component (1) and preferably carbonated liquid is withdrawn. The sieves (3) are retained so that they do not uncontrollably slide into the component (1), by designing the sealing and retaining ring (2) so that it preferably rests on the material wall (1) and is in turn held in place, for example, by the sieve retainer (7) which is gas-tight. For example, the side on the component (1) which has not yet been secured with the retaining sieve (3) for preferably bulk material (5) is now used to fill in the preferably bulk material (5). This can be done, for example, either by pouring or for example also by suction (not illustrated).
After having been filled with preferably bulk material (5), the introduced bulk material (5) is also secured by the bulk material retainer sieve (3), and is also secured by the, for example, component (7). The process steps and use of material necessitate, for example, additional operating steps, for example attaching the component (13), which is preferably a gas-tight pluggable connector (14) for the nozzle for preferably the CO2 introduction into the component (1), which is preferably filled with bulk material (5).
The component (13) is constructed so that a backfill preventer is inserted in the chamber (16) which seals gas-tight against the walls (14) and opens the gas or liquid flow in the direction (17) (not illustrated). The opening (17) is sized so that not too much or too little preferably CO2 can enter the supply component (1) or (11) (12), so as to ensure continuous carbonation inside the component (1) (11) (12). To supply the preferred component (13) with preferably CO2 (not illustrated), preferably the principle of the pluggable connector from the company John Guest for gases and liquids is applied, as seen in FIGS. (6) and (4). This has the advantage that mass-produced and proven components are used (not all embodiments are illustrated). Combinations of pluggable connections (8) (9) (7) and gas-tight screw connectors are also used (not illustrated). Preferably, the preferably stepped gas-tight peg (14) of the component (13) with the opening (17) is preferably inserted into the opening (4) of the component (12) and can be rendered gas-tight by way of the component (8) which is implemented as an elastic O-ring. The component (9), here implemented as a mounting element, ensures stable seating of the component (13) and prevents unintentional detachment, and can be adapted to any dimension (only partially illustrated).
The retaining element (9) is secured as an additional safety measure by a so-called retainer ring (not illustrated). Optionally, at least one component (13) can be attached gas-tight at each opening (4), which can be used for liquid and gas supply. The backflow preventers (at least 1) in the chamber (16) are used to prevent, for example, CO2 from flowing into the main supply of preferably tap water, or the preferred second backflow preventer prevents, for example, tap water from entering the gas supply (not illustrated), as shown for example in
The invention has the advantage that the preferably tap water is directly incident on the preferred bulk material (5) when entering the opening (4), in combination with preferably CO2, which can also enter at the same time through the opening (4) into the hollow body of the component (1) (11) (12). The flow of both media can be enabled in the direction of the dispensing location preferably by opening at least one dispensing location (not shown on the figures). Because the upstream backflow preventers open (not illustrated), which are inserted in the component 13) and these components (13) were attached gas-tight on the components (1) (11) (12). Consequently, the liquid and the gas enter the hollow body (1) (11) (12) via the openings (4). The liquid is nebulized or misted by the preferred supplied bulk material (5), so that the preferred
The gas flow for the preferably components (1) (11) (12) should preferably be occur through a pressure control valve, which is known from the invention and patent application by Mrs. Margaret Spiegel having the Application No.: 10055137.8 “Supply component for gases and liquids”, as well as from the German patent application of Aug. 11, 1998 with the Application No.: DEA 19851360 “Novel Mixer” because with this known invention the following is provided (not illustrated). If the supply components (1) (11) (12) are to be connected directly to the water mains, preferably city water, then pressure fluctuations can or occur in the supply component (1) (11) (12). If this occurs during carbonation, for example at least one dispensing operation, then a malfunction occurs during carbonation via the components (1) (11) (12), because constant carbonation is no longer possible due to a decrease, for example, in the water supply pressure, since a large quantity of liquid is withdrawn in the same building, resulting in an oversupply of gas inside the supply component (1) (11) (12), because the preset gas pressure must always be constant in relation to the respective liquid pressure, for example: 4 bar liquid pressure and 4 bar for example CO2 pressure, because the liquid pressure drops during the dispensing operation, for example to 3.5 bar. This also depends of the dispensing locations, the greater the dispensed quantity of carbonated liquid, the greater the pressure drop in the supply component (1) (11) (12). The liquid pressure can be kept constant below an upper limit by a pressure regulator or a limiter, and the gas pressure also by at least one pressure regulator, preferably for CO2. If the liquid pressure or the rest pressure of the liquid main supply occurs during carbonating, then the required liquid pressure can decrease, for example, from 3.5 bar to, for example, 2.8 bar. If the difference pressure of the fixed, preferably CO2, pressure is too high, then the existing liquid is displaced within the supply component (1) (11) (12), and carbonation can no longer take place as a result. The reason therefore is that the, for example, CO2 pressure does not significantly decrease even during the dispensing operation, as long as the gas reservoir and its pressure are applied, because for example a difference pressure of 0.5 bar with respect to the full pressure of the liquid is sufficient to ensure good continuous carbonation. This is an ensured because a certain pressure drop occurs during dispensing, but not in the gas flow. If during dispensing for example the pressure difference from the liquid flow decreases to for example 1.5 bar, then a massive malfunction occurs within the entire system during carbonation, up to the dispensing locations (not illustrated). All this can be prevented by a pressure regulator which is also employed in the context of the components (1) (11) (12) (not illustrated). The pressure regulator valve for liquids and gases operates according to the principle that the gas pressure above the actual liquid pressure, in the rest and flow pressure of the liquid depending on the main supply of the liquid or liquid reservoir, guarantees a constant difference pressure to the preferably CO2 pressure, assuming that the gas control valve is connected with at least one gas reservoir (not illustrated).
The advantage is here that the component (1) (11) (12) controllably transfers the required preferably CO2 pressure, even if the pressure of the liquids increases, to the CO2 outlet location, which is connected with the component (1) (11) (12) via a line (not illustrated). This can be attained within the body of the pressure control valve for liquids and gases with a membrane or a piston separating the chambers for liquids and gases (not illustrated).
If the volume flow of the pressure control valve flowing through the regulator is insufficient, because the flow quantity is not sufficient, which also cannot be attained with the regulator to which a high liquid pressure is applied, then a bypass can be provided and the regulator does not supply the major portion of the liquid supply to at least one supply component (1) (11) (12), but is only used to measure the liquid pressure and to transfer the existing pressure controllably to the set gas pressure, thus providing good carbonation matched to the gas pressure and gas flow in the direction of the supply module (1) (11) (12) liquids and gases (not illustrated).
The described pressure control valve (not illustrated) also operates as a preventive measure if, for example, following the carbonation process, at least one preferably displacement pump is used to, for example, maintain carbonated liquid in a recirculating flow loop and is used as add-on cooling for beverage additives (not illustrated) in a post-mix process (not illustrated).
It may happen, if the afore-described control valve for liquids and gases is not used, that for example a CO2 bubble remains in form of a deposit inside the pump, causing damage to the pump (not illustrated).
It is also a preventative measure if the for example CO2 flow is only enabled during the dispensing operation (not illustrated).
In a preferred application for a supply component (1) (11) (12),
preferably filled with bulk material (5), for gases and liquids, which is designed as supply carbonator (1) (11) (12), the inline-pre-carbonator (1) (11) (12) is configured as at least one component for preferably carbonating tap water with CO2.
According to preferred arrangements and components, at least one pressure controller for liquids (not illustrated) is supplied from at least one main liquid supply, as well as at least one pressure control valve which regulates the gas pressure via the liquid pressure and supplies this pressure control valve with liquid via the pressure controller for liquids (not illustrated).
Which supplies through at least one pressure control valve, which controls the gas pressure via the fluid pressure, at least one supply component (1) (11) (12) controllably with liquid and gases (not illustrated).
That the pressure control valve is connected with at least one gas reservoir, via lines or a direct connection to at least one gas reservoir container (not illustrated).
That the liquid, the supply component (1) (11) (12) can be pre-cooled before entering via the openings (4) (not illustrated).
That the preferably tap water which is preferably pre-carbonated or carbonated via the supply component (1) (11) (12) is introduced into a post-cool line to the preferably displacement pump for withdrawing the carbonated liquid preferably in at least one closed loop system, connected to for optional withdrawal of the carbonated liquid via at least one dispensing location (not illustrated). That the gas or liquid flow can be turned off before entering or after entering into the component (1) (11) (12), and can be opened via an electric valve connection or pressure drop switch so as to prevent a potentially undesirable incursion of gas into the supply component (1) (11) (12) if dispensing or carbonation does not takes place (not illustrated).
The supply component (1) (11) (12) is also used as an impulse carbonator with or without pump support (not illustrated).
Carbonation is provided without requiring an additional carbonator or inline carbonator, which is considered state-of-the-art. No components are known with a supply component which makes it possible to supply preferably tap water and CO2 and to preferably carbonate inside the supply component (1) (11) (12)
preferably filled with bulk material (5), preferably at the same time the two media enter. This is made possible only by the present invention.
Another design of the invention was attained, in order to simplify for example the bulk material (5) and the assembly, by not entirely filling, for example, the component (1) (11) (12) with preferably solid matter (5), which is illustrated in exemplary form in
The fact that the supply component (1) or (11) (12) is not entirely filled has no effect on the carbonation process, because when at least one dispensing location (not illustrated) is opened, the liquid and gas flow pushes the introduced preferably solid matter (5) against the retainer sieve (3), allowing for the misting end nebulizing process of the liquid to occur. The bulk material (5) will always adapt to the flow conditions of the two preferred media, if materials are employed for the preferably solid matter (5), which are lightweight and floatable, as for example granulate from polycarbonate (not illustrated).
Number | Date | Country | Kind |
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10 2005 019 410.9 | Apr 2005 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/DE2006/000715 | 4/21/2006 | WO | 00 | 6/9/2008 |