BRINE INJECTION SYSTEM WITH A FILTER

Abstract

The present invention relates to a brine injection system with a plurality of needles, which are inserted into a product and through which brine is injected into the product, wherein brine which does not end up in the product is collected and recycled and wherein during recycling, the brine flows through a filter.

Claims

1. A brine injection system comprising: a plurality of needles, which are inserted into a product and through which brine is injected into the product, and a filter, wherein brine which does not end up in the product is collected and recycled, wherein during recycling of the brine, the brine flows through the filter wherein the filter comprises a filter element along which unfiltered brine flows and through which filtered brine passes and which holds back residues in the unfiltered brine, wherein the filter element is at least locally curved, and wherein a permeability of the filter element varies with a flow-length of the brine along the filter element.

2. The brine injection system according to claim 1, wherein the filter element is at least locally inclined relative to a vertical and/or horizontal plane.

3. (canceled)

4. The brine injection system according to claim 1, wherein the brine flows along and through the filter element by gravity.

5. (canceled)

6. The brine injection system according to claim 1, wherein the permeability of the filter element increases with the flow-length of the brine along the filter-element.

7. The brine injection system according to claim 1, wherein the system comprises a chiller for the brine.

8. The brine injection system according to claim 1, wherein the filter element is a screen.

9. The brine injection system according to claim 1, wherein the filter element vibrates.

10. The brine injection system according to claim 1, wherein the system comprises an extra filter upstream from the needles.

11. The brine injection system according to claim 1, wherein the system comprises a cleaning system.

12. The brine injection system according to claim 11, wherein the system comprises a moving device, which moves the cleaning system relative to the filter element of the filter.

13. The brine injection system according to claim 11, wherein the cleaning system operates continuously or intermittently.

14. The brine injection system according to claim 11, wherein the system comprises a sensor, which measures the flow of the brine through the filter element, and signal of the sensor is utilized to control the cleaning system.

15. The brine injection system according to claim 11, wherein the system comprises a recycle means to recycle the brine, which is sucked in by the cleaning system.

16. The brine injection system according to claim 1, wherein the filter element is a slotted screen.

17. The brine injection system according to claim 1, wherein the system comprises a vacuum cleaner.

18. The brine injection system according to claim 1, wherein an angle of inclination of the filter element relative to the horizontal plane decreases with increased flow-length.

19. The brine injection system according to claim 1, wherein a radius of curvature of the filter element is in a range from 1500 to 1800 mm.

20. The brine injection system according to claim 1, wherein the permeability of the filter is adjustable.

21. A system comprising: a plurality of needles, the needles are inserted into a product and through which brine is injected into the product; a filter comprising a filter element, the filter element is curved and inclined relative to a horizontal plane so that the brine flows along and through the filter element by gravity, a radius of curvature of the filter element is in a range from 1500 to 1800 mm, the filter element is a screen that vibrates to increase filter capacity of the filter element, the filter element is a slotted screen; an extra filter upstream from the needles; a chiller for the brine; a cleaning system; a moving device that moves the cleaning system relative to the filter element in one or two directions parallel to a surface of the filter element; a sensor that measures the flow of the brine through the filter element, wherein a signal from the sensor is used to activate or deactivate the cleaning system; a recycle means to recycle brine that is sucked in by the cleaning system; wherein brine which does not end up in the product is collected by the cleaning system and recycled in the recycle means; wherein during recycling of the brine, the brine that does not end up in the product flows through the filter; wherein unfiltered brine flows along the filter element and through which filtered brine passes and which holds back residues in the unfiltered brine; and wherein a permeability of the filter element increases with a flow-length of the brine along the filter element.

22. The system according to claim 21, wherein the permeability of the filter element is adjustable.

Description

[0026] The invention is now explained according to the Figures. These explanations do not limit the scope of protection.

[0027] FIG. 1 shows the inventive system.

[0028] FIG. 2 shows details of the filter.

[0029] FIG. 3 shows the cleaning device.

[0030] FIG. 1 shows the inventive system 16. The system comprises a needle-head 6 with a multitude of needles, which are reciprocated from a remote- to an injecting position. In the injection position, the needles stick in a product, for example meat, poultry, fish or vegetables and a brine is forced through the hollow needles into the product. Surplus brine is collected, for example underneath the belt of the injector which transports the product below the needles and away and the brine flows via out-flow 1 to segment A of a brine tank. In segment A the return brine can be polluted with proteins, fat particles, bone- and cartilage-fragments. As a first cleaning step, two optional plates 14, 15, one connected at the top of the tank and a small one connected at the bottom of the tank are positioned a distance from each other such that heavier material could descend and fat will float on top.

[0031] In the embodiment according to FIG. 1, a GEA SuperChill 2 is used to pump the eventually pre-cleaned return brine from tank A into an integrated cooling block so that the brine temperature of preferably 2-4 C. will be maintained. In case the return brine temperature and environment temperature will not influence the preferred brine temperature range, the GEA SuperChill could also be replaced with a conventional pump and a control system to turn the pump on/off and manage the flow speed and level control in tank A to protect the pump for dry-pumping. The GEA SuperChill or the separate pump pumps the return brine towards the inlet connection at the back of main filter 3 as shown in FIG. 2. In the optional reservoir 7 of the filter 3 the pumped return brine collects and will start to over-flow over the filter element 8. A weir 10 can be provided to force the unfiltered brine towards the filter element 8.

[0032] Flow speed and amount of return brine is depending on the injection rate, e.g. injection mode, pump pressure and/or needle-head speed but also on belt load, product, brine type etc. but can be easily managed by the flow regulator of the pump 2. The filtrate will flow out of the filter 3 and will be collected in tank segment B. Here it will preferably be mixed with cold and fresh brine, which has a preferred temperature of 2-4 C. The brine is then pumped via injector pump 4 through one of the in-line filters 5, which are, however, only optional. In case any material is dropped in segment B accidentally, for example by human interference, the in-line filter(s) will catch this debris. Preferably these filters 5 are provided by-passable such that one filter can be taken out to inspect/clean without interrupting the production. Valves will control which filter is in use before the brine is consumed by the injector's manifold and needles 6.

[0033] Referring now to FIG. 2, the unfiltered or pre-filtered brine 11 is flowing along the filter element 8, indicated by the arrow X, which depicts the flow length of the brine along the filter element. As the brine flows along the filter element 8, a portion of filtered brine 12 will pass the filter element 8 and will be caught beneath the filter element 8. Here a sloped bottom 17 guides the filtered brine to an exit, which is connected to the tank in segment B. The residues accumulate at the top of the filter element 8 and will be washed out by the stream of unfiltered brine 11 and here due to gravity. At the end of the filter element 8, the residues are collected in a reservoir 9 and discharged. The filter element 8 is preferably a modular build-up screen deck. Depending on the brine viscosity, brine ingredients, pollution degree and used needles in the injector, optimization of the filter process can be desirable. This can be achieved in different ways, for example by adjusting the angle of inclination and or of screen 8 and/or varying the permeability, for example the mesh size when using a slotted screen, with the flow length X of the brine, by, for example, choosing a smaller permeability at location H, i.e. a smaller flow length and a larger permeability at location L, i.e. a larger flow length. The angle of inclination a is preferably smaller at the smaller flow length of the brine along the filter element and preferably increases at least locally with increasing flow length. This results in higher velocity of the unfiltered brine at the beginning of the filtering process, which decreases with increasing flow length. To improve the slide and/or roll down of residue, the filter element 8 is preferably curved as shown by reference sign R. In case an optimization of the filter process is not sufficient a filter element 8 with a different slope, for example curvature R can be used. The filter elements 8 are preferably provided as moduls and can be exchanged based on the desired application. Further optimization can be achieved by using a vibrating screen 8.

[0034] FIG. 3 shows the cleaning system 20, which is in the present case a nozzle 18 which is connected to a vacuum source to remove solid- and/or jellylike-particles from the surface of the filter element 8. This is done to avoid clogging of the filter element 8. The cleaning system is designed such that it preferably removes as little brine from the surface of the filter element as possible. The cleaning system 20, preferably the nozzle 18 is preferably connected to a moving device (not depicted), which moves the cleaning system 20 and/or the nozzle 18 relative to the surface of the filter element. The moving device can move the cleaning system 20 and/or the nozzle in one or two directions parallel to the surface of the filter element 8. The moving pattern preferably depends on the size of the cleaning device and/or the nozzle.

[0035] The surface of the filter element 8 can be cleaned partially or entirely. The cleaning can take place continuously or intermittently. The cleaning system may comprise a sensor which, for example, measures directly or indirectly, the flow through the filter element. Depending on the signal of the sensor, the cleaning system is either activated or deactivated.

[0036] Preferably, the cleaning system comprises a sensor which measures the amount of brine removed from the surface of the filter element 8. In case this amount is too large, the cleaning system is either adjusted and/or stopped.

[0037] Brine removed from the surface of the cleaning system is preferably recycled to the system and reused.

LIST OF REFERENCE SIGNS

[0038] 1 outflow [0039] 2 pump, chiller [0040] 3 main filter [0041] 4 pump [0042] 5 inline filter [0043] 6 needles, needle-head [0044] 7 reservoir [0045] 8 filter element [0046] 9 residues [0047] 10 weir [0048] 11 flow of unfiltered brine [0049] 12 flow of filtered brine [0050] 13 separation tank [0051] 14 separation plate [0052] 15 separation plate [0053] 16 brine injection system [0054] 17 sloped bottom [0055] 18 nozzle vacuum cleaner [0056] 19 connection to vacuum cleaner [0057] 20 cleaning system, vacuum cleaner [0058] A first segment tank [0059] B second segment tank [0060] H filter region with a first permeability [0061] L filter region with a second permeability [0062] R curvature of the filter element [0063] X flow direction of the brine, flow length [0064] angle of inclination, relative to a vertical plane [0065] angle of inclination, relative to a horizontal plane