Patent Application
20230244253
The invention is related to packaging technology. More particularly, it is related to controlling a regulating valve of a packaging machine.
Today it is commonly known to use roll-fed packaging machines for different types of food products, e.g. milk. The roll-fed packaging machines are configured to be connected to a processing line such that the food products may be fed from the processing line to the packaging machine. The roll-fed packaging machines, also referred to as filling machines, have several advantages. One is that a continuous production of packages makes it possible to achieve higher speed compared to blanks-fed packaging systems. Another advantage is that by continuously filling a tube of packaging material and forming packages in a lower end of the tube, a risk that unwanted microorganisms enter the packages can be lowered.
Even though the roll-fed packaging machines of today are efficient in terms of produced packages per hour, and that the packaging machines have different systems in place to assure that the packages produced fulfil set quality requirements, there is nevertheless room for improvement. For instance, due to that the packages are produced at high speeds, a deviation in one part of the packaging machine may result in that a relatively large quantity of packages are produced that do no fulfill set quality requirements if the deviation is not detected and taken care of. A result of this may be increased losses in terms of packaging material, food product as well as production time. Thus, to be able to provide more efficient packaging machines, both in terms of financial costs and environmental costs, packaging machines that are improved in terms of handling deviations are requested by food producers.
For this reason, there is a demand for a packaging machine that is capable of having a more stable production compared to packaging machines of today, and hence reduce the packaging material waste, product waste and production downtime. An example of a known control system may be found in Bill Bolton: “Instrumentation and Control Systems—chapter 13—Controllers”, 1 Jan. 2014 (2014-01-01), XP055737048, ISBN: 978-0-7506-6432-5. Also, documents JP S59 109918 A, US 2012/192969 A1 and US 2017/344032 A1 may be of interest for the present application.
It is an object of the invention to at least partly overcome one or more of the above-identified limitations of the prior art.
According to a first aspect it is provided a method for controlling a regulating valve of a packaging machine, wherein the packaging machine is a roll-fed packaging machine configured to receive a roll of a carton-based packaging material, wherein the packaging machine is configured to be connected to a processing line via the regulating valve, wherein the processing line is configured to feed a liquid food product to the packaging machine through the regulating valve, the method comprising:
determining a product flow, using a flow meter, of the liquid food product in the packaging machine;
determining an inlet pressure measurement, using a pressure sensor, of the liquid food product in the packaging machine; and
adjusting an inlet pressure to the packaging machine via the regulating valve, said regulating valve being configured to receive an output signal from a flow feed forward module in combination with an output signal from a flow proportional-integral-derivative (PID) module, wherein the flow feed forward module has the inlet pressure measurement and a flow set point as input signals, and wherein the flow PID module has the product flow and the flow set point as input signals.
By the term “inlet pressure” is here meant an inlet pressure of the liquid food product, wherein the inlet pressure is the pressure of the liquid food product before the regulating valve. Thus, the inlet pressure may be the pressure being used for adjusting the output signals from the flow feed forward module and the flow PID module.
By the term “product flow” is here meant the flow of the liquid food product determined by the flow meter. Thus, the product flow is the flow of the liquid food product, wherein the liquid food product is fed from the processing line to the packaging machine. The product flow may be an input signal to the flow feed forward module. The product flow may be an input signal to the flow PID module.
By the term “inlet pressure measurement” is here meant a measured value, also referred to as sample, of the inlet pressure of the liquid food product determined by the pressure sensor. Thus, the inlet pressure measurement is the inlet pressure of the liquid food product, wherein the liquid food product is fed from the processing line to the packaging machine before the regulating valve. The inlet pressure measurement may be an input signal to the flow feed forward module.
By the term “flow feed forward module” is here meant any feed forward control system known in the art. The flow feed forward module in the present disclosure may have the inlet pressure measurement and the flow set point as input signals. However, the flow feed forward module may have other input signals as well and is not limited to these examples.
By the term “flow proportional-integral-derivative (PID) module” is here meant any PID controller, wherein the PID controller is a control loop mechanism, known in the art. The flow PID module in the present disclosure may have the product flow and the flow set point as input signals. However, the flow PID module may have other input signals as well and is not limited to these examples.
By the term “flow set point” is here meant an input signal comprising a machine speed percentage, wherein the machine speed percentage is a value for how many packages that may be filled per time unit. The machine speed percentage may depend on the size of the packages and/or the product that may be filled in the packages. However, the flow set point may comprise other input values as well such that a start flow percentage and/or a nominal flow percentage. The start flow percentage may be used in the beginning of a start event, to ramp up the speed of the machine. The nominal flow percentage is a value used when the packaging machine is run at nominal speed.
An advantage by having the flow feed forward module arranged in combination with the flow PID module is that it is possible to quickly identify the correct real-time working point of the regulating valve. The faster response of the regulating valve allows the achievement of filling parameters stability, namely the stability of the product level and product flow. Consequently, a stable packaging machine with a higher robustness may be achieved. Put differently, by being able to control the regulating valve with improved response time, a product level of a packaging tube formed within the roll-fed packaging machine may fluctuate less, which in turn provides for less quality issues of packages being produced.
A further advantage obtained with the disclosed method may be that the packaging material waste and the product waste may be reduced. Thus, by the disclosed method, it is possible to make use of the inlet pressure of the liquid food product being fed to the packaging machine for adjusting the regulating valve through the output signals from the flow feed forward module and the flow PID module.
By adjusting the regulating valve, it may be possible to control the product flow, the product pressure and the product level of the liquid food product fed from the processing line to the packaging machine. By the present disclosure, the inlet pressure of the liquid food product may be controlled compared to conventional packaging machines wherein the inlet pressure may be unknown. For instance, conventional packaging machine and control systems may be blind to the inlet product pressure, and assume a fixed inlet pressure value as flow feed-forward input.
A further advantage may be that by determining the inlet pressure in the disclosed way may provide for an increased speed in reaction to pressure disturbances occurring in the inlet product line.
A further advantage is that the pressure sensor may be configured to be integrated within connections of already existing packaging machines and processing lines. Thus, it is possible to integrate the pressure sensor into conventional lines comprising packaging machines and processing lines.
Yet a further advantage may be that the package weight accuracy may be improved. In other words, having the level of the packaging tube controlled with high precision does not only reduce quality issues of the packages being produced, but also result in that the package weight accuracy can be improved. A consequence of having a consistent amount of product placed above a transversal sealing system of the packaging machine namely provides for that the packages formed with the help of the transversal sealing system, possibly in combination with forming flaps, consistent packages can be produced.
Overall, by using the present disclosure, a more controllable and thus, a stable packaging machine may be achieved.
The method may further comprises determining a product level, using a level detector, of the liquid food product held in a vertical tube of the packaging material formed by the packaging machine, and using the product level for adjusting the regulating valve.
To improve the controlling the level in the packaging tube may be directly determined by using a level detector. This may be a light-based sensor that is used for determining a distance between the sensor and the level, and by having a set reference the level may be determined.
The step of adjusting the regulating valve may further be controlled using a level PID module configured to determine the flow set point, wherein the level PID module has the product level and a level set point as input signals.
By the term “level PID module” is here meant any PID controller, wherein the PID controller is control loop mechanism, known in the art. The level PID module in the present disclosure may have the product level and the level set point as input signals. However, the flow PID module may have other input signals as well and is not limited to these examples.
By the term “level set point” is here meant an input signal that is either manually set or automatically determined by an external device.
The flow PID module may further have the product level as input signal.
Upon the method comprising the level PID module configured to determine the flow set point, the flow set point may have the output from the level PID module as an input signal in combination with one or more of the input signals discussed above.
The flow PID module may further have a machine speed percentage as input signal.
The pressure sensor may comprise a metallic membrane.
The step of adjusting the regulating valve may further be based on real-time pressure measurements from the processing line.
An advantage with having the real-time pressure measurements in this way is that the regulating valve can quickly adapt to changes in the processing line. For instance, in case there is a pressure drop in the processing line this may be detected and transferred via a data communications network to the regulating valve, which may be adjusted to compensate for this pressure drop. Further, having several different real-time pressures measurements from the processing line as input provide for that reliable control of the regulating valve can be achieved.
Put differently, critical aspects of filling control systems on packaging machines mainly concerns transitions (start/stop events) and product line disturbances, which are not measurable in real-time as of today. Due to the lack of pressure sensor, a drawback with conventional packaging machines is thus that they show a slow reaction to disturbances. Therefore, an advantage by determining pressure measurements in the processing line may be that real-time pressure information may be exchanged between the packaging machine and the processing line. By exchanging information between the packaging machine and the processing line, a stable packaging machine may be provided. Hence, this may provide for even more reduced packaging materiel waste and product waste.
According to a second aspect, it is provided a filling control system configured to adjust an inlet pressure of a packaging machine. The packaging machine is a roll-fed packaging machine configured to receive a roll of carton-based packaging material, wherein the packaging machine is configured to be connected to a processing line via a regulating valve, wherein the processing line is configured to feed a liquid food product to the packaging machine through the regulating valve. The filling control system comprising:
a flow feed forward module configured to control the regulating valve, and having the inlet pressure measurement and a flow set point as input signals; and
a flow proportional-integral-derivative (PID) module configured to control the regulating valve together with the flow feed forward module, and having the product flow and the flow set point as input signals,
wherein the flow feed forward module is in parallel with the flow PID module.
An advantage with the disclosed control system may be that faster reactivity of the control system to inlet product pressure disturbances may be achieved.
The filling control system may further comprise a level PID module configured to feed into the flow feed forward module and the flow PID module and having the product level and a level set point as input signals.
The filling control system may further be configured to receive real-time pressure measurements from the processing line.
According to a third aspect, it is provided a filling line configured to control product pressure and flow in the paper tube of a packaging machine. The packaging machine is a roll-fed packaging machine configured to receive a roll of carton-based packaging material, wherein the packaging machine is configured to be connected to a processing line via a regulating valve, wherein the processing line is configured to feed a liquid food product to the packaging machine through the regulating valve, the filling line further comprising:
a flow meter configured to determine a product flow of the liquid food product;
a pressure sensor configured to determine an inlet pressure measurement of the liquid food product of the packaging machine;
a flow feed forward module configured to control the regulating valve, and having the inlet pressure measurement and a flow set point as input signals; and
a flow proportional-integral-derivative (PID) module configured to control the regulating valve together with the flow feed forward module, and having the product flow and the flow set point as input signals,
wherein the flow feed forward module is in parallel with the flow PID module.
The filling line may further comprise a level detector configured to determine a product flow of the liquid food product of the packaging machine, wherein the level detector is located after the flow meter in the filling line direction.
The filling line may further comprise a level PID module configured to feed into the flow feed forward module and the flow PID module and having the product level and a level set point as input signals.
Still other objectives, features, aspects and advantages of the invention will appear from the following detailed description as well as from the drawings.
Effects and features of the second and third aspects are largely analogous to those described above in connection with the first aspect. Embodiments mentioned in relation to the first aspect are largely compatible with the second and third aspect. It is further noted that the inventive concepts relate to all possible combinations of features unless explicitly stated otherwise. A further scope of applicability of the present invention will become apparent from the detailed description given below. However, it should be understood that the detailed description and specific examples, while indicating preferred embodiments of the invention, are given by way of illustration only, since various changes and modifications within the scope of the invention will become apparent to those skilled in the art from this detailed description.
Hence, it is to be understood that this invention is not limited to the particular component parts of the device described or steps of the methods described as such device and method may vary. It is also to be understood that the terminology used herein is for purpose of describing particular embodiments only and is not intended to be limiting. It must be noted that, as used in the specification and the appended claim, the articles “a”, “an”, “the”, and “said” are intended to mean that there are one or more of the elements unless the context clearly dictates otherwise. Thus, for example, reference to “a unit” or “the unit” may include several devices, and the like. Furthermore, the words “comprising”, “including”, “containing” and similar wordings does not exclude other elements or steps.
Embodiments of the invention will now be described, by way of example, with reference to the accompanying schematic drawings, in which
With reference to
Today, packaging material is often printed and prepared in packaging material production centers, also referred to as converting factories, and is shipped to a site where the packaging machine 100 is placed, e.g. a dairy. Usually the packaging material is loaded onto a reel before being transported. After arriving at the site, the reel is placed in the packaging machine as illustrated in
During production a web 102 of packaging material can be fed from the reel through the packaging machine in a web feeding direction A. Before providing the liquid food product, a paper tube can be formed from the web 102 by forming a longitudinal sealing. The food product can be fed into the tube via a pipe 104 and a regulating valve 206 may be used for regulating a flow through the pipe 104. A lower end 108 of the tube can be fed into a folding device 110 in which a transversal sealing can be made, the tube can be folded according to folding lines, also referred to as weakening lines, and cut off such that packages 112 can be formed. Even though the folding device 110 is illustrated as one single device, the folding device 110 may comprise a number of different devices.
With reference to
The food handling system 304 can comprise a processing line 202 and the packaging machine 100, wherein the processing line 202 can be connected to the packaging machine 100 via the regulating valve 206. The processing line 202 and the filling machine 100 can be connected such that the liquid food product may be fed therebetween through the regulating valve 206. The processing line 202 may be any processing line 202 known in the art.
The food handling system 304 can further comprise a pressure sensor 204 for determining an inlet pressure measurement of the liquid food product fed from the processing line 202 to the packaging machine 100. The inlet pressure measurement may be transmitted to the filling control system 302.
The packaging machine 100 can comprise a flow meter 106 for determining the product flow of the liquid food product fed from the processing line 202 to the packaging machine 100. The determined product flow may be transmitted to the filling control system 302. The packaging machine 100 can further comprise a level detector 208 for determining the product level of the liquid food product that may be fed from the processing line 202 to the packaging machine 100. The determined product level may be transmitted to the filling control system 302.
The inlet pressure measurement, the product flow and the product level may be referred to as filling parameters.
For a person skilled in the art, it is conceivable that the filling line 200 may comprise more than one pressure sensor 204, and/or more than one flow meter 106 and/or more than one level detector 208. It should also be noted that the packaging machine 100 may lack the flow meter 106 and/or the level detector 208.
The packaging machine 100 can further comprise a sterilization device 210, e.g. a hydrogen peroxide bath or an LVEB (Low-Voltage Electron Beam) station, for ensuring that the web 102 may be free from unwanted microorganisms. The packaging machine 100 can further comprise a longitudinal sealing station 212 for sealing the package along the longitudinal direction and a transversal sealing station 214, which may comprise two sealing jaws, for sealing the package transversally.
With reference to
As illustrated in
The filling control system 302 may comprise a flow feed forward module 308 and a flow proportional-integral-derivative (PID) module 310. The filling control system 302 may further comprise a plurality of summing junctions 314a-e for summing one or more signals within the filling control system 302. The filling control system 302 may further comprise a plurality of switches 316a-c for controlling the signals that are traveling within the filling control system 302.
The flow feed forward module 308 can be configured to control the regulating valve 206. The flow PID module 310 can be configured to control the regulating valve 206. The flow feed forward module 308 may be arranged in parallel with the flow PID module 310 such that both the flow feed forward module 308 and the flow PID module 310 can be configured to control the regulating valve 206. Upon the flow feed forward module 308 and the flow PID module 310 can be controlling the regulating valve 206, the inlet pressure of the liquid food product may also be controlled. A purpose of the present arrangement, wherein the flow feed forward module 308 is arranged in parallel with the flow PID module 310, is to provide for a faster reactivity of the filling control system 302 to inlet pressure disturbances as well as real-time pressure information exchange between the packaging machine 100 and the processing line 202.
The filling control system 302 may further comprise a level PID module 312 for controlling the regulating valve 206. The level PID module 312 and the flow PID module 310 may together form a double PID feedback control loop in the filling control system, wherein the output signal from the level PID module 312 may be input signals to the flow feed forward module 308 and the flow PID module 310. Thus, the flow feed forward module 308 may be arranged in parallel with the double PID feedback control loop. By introducing the level PID module 312 in the arrangement may provide for another parameter that may be tuned and hence, controlled in the filling control system 302 in order to provide for the faster reactivity of the filling control system 302 to inlet pressure disturbances as well as the real-time pressure information exchange between the packaging machine 100 and the processing line 202.
As illustrated in
The inlet pressure measurement 306 may be transmitted from the pressure sensor 204 to the flow feed forward module 308, thus the inlet pressure measurement 306 may be an input signal to the flow feed forward module 308. A further input signal to the flow feed forward module 308 may be a flow set point, wherein the flow set point can be based on a machine speed percentage. The machine speed percentage may pass a second summing junction 314b and a third summing junction 314c before entering the flow feed forward module 308. According to one example, the flow set point may further be based on a start flow percentage and/or a nominal flow percentage. If the flow set point may be further based on the start flow percentage, a first switch 316a may be set such that the start flow percentage may be transmitted to the second summing junction 314b. Alternatively, or in combination, if the flow set point may be further based on the nominal flow percentage, a second switch 316b may be set such that the nominal flow percentage may be transmitted to the second summing junction 314b. The second summing junction 314b may be configured to combine the machine speed percentage with the start flow percentage and/or the nominal flow percentage. For a person skilled in the art, it is conceivable that the first switch 316a and the second switch 316b may be set such that both the start flow percentage and the nominal flow percentage are combined with the machine speed percentage in the second summing junction 314b.
The product flow may be transmitted from the flow meter 106 to a fourth summing junction 314d, wherein the product flow may be combined with the flow set point. The flow set point may be configured in the same way as discussed above. Thus, the flow set point may be the same flow set point arranged as the input signal to the flow feed forward module 308. The product flow in combination with the flow set point may be transmitted to the flow PID module 310, thus the product flow and the flow set point may be input signals to the flow PID module 310.
As discussed above, the flow feed forward module 308 may be arranged in parallel with the flow PID module 310. The output signal from the flow feed forward module 308 and from the flow PID module 310 may be combined in a fifth summing junction 314e. The output signal from the fifth summing junction 314e may be a control signal configured to control the regulating valve 206.
Thus, the regulating valve 206, may be controlled based on the inlet pressure measurement 306, the product flow and the flow set point.
An advantage with the present disclosure is that the pressure of the liquid food product in the paper tube may be known and controlled, compared to conventional packaging machines whose control systems have an inlet pressure normally set to a fixed value and hence, independent of other filling parameters in the system.
An advantage by controlling the regulating valve 206 based on determined values from both the flow meter and the pressure sensor is that a faster reaction of the regulating valve 206 is achieved. Thus, the regulating valve 206 may be controlled with higher feedback compared to conventional packaging machines and control systems due to the arrangement between the flow feed forward module 308 and the flow PID module 310. Thus, the flow feed forward module 308 may be configured to tune the filling parameter in a quicker way compared to conventional packaging machines and control systems.
According to one example, the product level may be transmitted from the level detector 208 to a first summing junction 314a, wherein the product level may be combined with a product set point. The product level in combination with the level set point may be transmitted to the level PID module 312, thus the product level and the level set point may be input signals to the level PID module 312. Upon a third switch 316c may be set, the output signal from the level PID module 312 may be transmitted to a third summing junction 314c. In the third summing junction 314c, the output signal from the level PID module 312 may be combined with the machine speed percentage and the start flow percentage and/or the nominal flow percentage. The output signal from the third summing junction 314c may be the flow set point. Thus, the flow set point may further be based on the output signal from the level PID module 312. In addition, the output signal from the third summing junction 314c may be transmitted to the fourth summing junction 314d and hence, combined with the product flow.
As discussed above, the flow feed forward module 308 may be arranged in parallel with the double PID feedback control loop. The output signal from the flow feed forward module 308 and from the double PID feedback control loop may be combined in a fifth summing junction 314e. The output signal from the fifth summing junction 314e may be the control signal configured to control the regulating valve 206.
An advantage by having the level PID module 312 in the filling control system is that the adjustment of the regulating valve 206 may be even more precise due to more filling parameters.
A further advantage by introducing the level PID module 312 in the arrangement is that, in combination with the switches 316a-c, it is possible to optimize the signals in the system and hence, adjust the regulating valve 206 in a more precise and efficient way.
Yet a further advantage, the filling parameters are used to tune the system for stability achievements through different phases in various configurations.
In
In a first step S402, a product flow of the liquid food product in the packaging machine 100 can be determined by using a flow meter 106. In a second step S404, an inlet pressure measurement 306 of the liquid food product in the packaging machine 100 can be determined by using a pressure sensor 204. Preferably, the pressure sensor 204 comprises a metallic membrane. In a third step S406, the regulating valve 206 can be adjusted by using a flow feed forward module 308 in parallel with a flow proportional-integral-derivative (PID) module 310. The flow feed forward module 308 has the inlet pressure measurement 306 and a flow set point as input signals. The flow PID module 310 has the product flow and the flow set point as input signals.
Optionally, the method 400 may further comprise the fourth step S408 of determining a product level, using a level detector 208, of the liquid food product 216 held in a vertical tube 308 of the packaging material 102 formed by the packaging machine 100. Upon that may be the case, the third step S406 may further comprise using the product level for adjusting the regulating valve 206.
Optionally, the third step S406 of adjusting the regulating valve may be further controlled using a level PID module 312 configured to determine the flow set point, wherein the level PID module has the product level and a level set point as input signals.
Optionally, the flow PID module 310 may further have the product flow and/or a machine speed percentage as input signal.
Optionally, the third step S406 of adjusting the regulating valve 206 may further be based on real-time pressure measurements from the processing line 202.
Below follows an alternative way of describing a method for controlling the regulating valve:
A method 400 for controlling a regulating valve 206 of a packaging machine 100, wherein the packaging machine 100 is a roll-fed packaging machine configured to receive a roll of a carton-based packaging material 102. The packaging machine 100 is configured to be connected to a processing line 202 via the regulating valve 206, wherein the processing line 202 is configured to feed a liquid food product 216 to the packaging machine 100 through the regulating valve 206. The method 400 comprises determining S402 a product flow, using a flow meter 106, of the liquid food product in the packaging machine 100; determining S404 an inlet pressure-measurement 306, using a pressure sensor 204, of the liquid food product in the packaging machine 100; and making use of the inlet pressure measurement to the packaging machine 100 for adjusting the regulating valve 206, said regulating valve being configured to receive an output signal from a flow feed forward module 308 in combination with an output signal from a flow proportional-integral-derivative (PID) module 310, wherein the flow feed forward module (308) has the inlet pressure measurement 306 and a flow set point as input signals, and wherein the flow PID module 310 has the product flow and the flow set point as input signals.
The features and advantages described in the context of the first aspect in the summary are also applicable for the method described above.
From the description above follows that, although various embodiments of the invention have been described and shown, the invention is not restricted thereto, but may also be embodied in other ways within the scope of the subject-matter defined in the following claims.
As already discussed, one or more embodiments may relate to the filling line 200 comprising the filling control system 302 and the food handling system 304. The food handling system 304 may comprise the processing line 202 and the filling machine 100. The food handling system 304 may comprise the regulating valve 206. The regulating valve 206 may connect the processing line 202 and the filling machine 100. The filling line 200 may be configured to perform the method according to one or more embodiments as described above.
The filling line 200 may be configured to control product pressure and/or flow in the paper tube of the packaging machine 100, e.g. a roll-fed packaging machine configured to receive a roll of carton-based packaging material 102. The packaging machine 100 is configured to be connected to the processing line 202 via the regulating valve 206, wherein the processing line 202 is configured to feed a liquid food product 216 to the packaging machine 100 through the regulating valve 206.
The food handling system 304 may comprise the pressure sensor 204 for determining the inlet pressure measurement of the liquid food product fed from the processing line 202 to the packaging machine 100. The inlet pressure measurement may be transmitted to the filling control system 302. The pressure sensor 204 may be positioned upstream of the regulating valve 206 in a direction of flow of the liquid food product 216.
Preferably, the food handling system 304 may comprise the flow meter 106 for determining the product flow of the liquid food product fed from the processing line 202 to the packaging machine 100. The determined product flow may be transmitted to the filling control system 302. The flow meter 106 may be positioned upstream of the regulating valve 206 in the direction of flow of the liquid food product 216.
Preferably, the food handling system 304 can comprise the level detector 208 for determining the product level of the liquid food product that may be fed from the processing line 202 to the packaging machine 100. The determined product level may be transmitted to the filling control system 302. The level detector 208 may be positioned downstream of the regulating valve 206 in the direction of flow of the liquid food product 216.
The filling control system 302 may comprise the flow feed forward module 308, the flow proportional-integral-derivative (PID) module 310 and/or the level PID module 312.
The flow feed forward module 308 may receive as input the inlet pressure measurement 306 from the pressure sensor 204 and the flow set point. The flow feed forward module 308 may comprise as an output a control signal for adjusting the regulating valve 206 calculated as a function of the flow set point and inlet pressure measurement 306.
The flow proportional-integral-derivative (PID) module 310 may receive as input the flow set point and the product flow. An output of the flow PID module 310 may be indicative of a difference between a real flow, measured e.g. by means of the flow meter 106, and a desired flow, i.e. the flow set point.
The level PID module 312 may comprise as inputs the level set point and the product level. An output of the level PID module 312 may be indicative of a difference between a real product level, measured e.g. by means of the level detector 308, and a desired level, i.e. the level set point.
The outputs of the flow proportional-integral-derivative (PID) module 310 and the flow feed forward module 308 may be combined. The regulating valve 206 may be adjusted as a function of the combined outputs.
The flow set point may be indicative of a target flow of product through the regulating valve 206. The flow set point may be calculated as a function of one or more of a start flow percentage a nominal flow percentage, a machine speed percentage, a level set point and/or a product level.
The step of adjusting the regulating valve 206 may comprise adjusting a flow of liquid product passing therethrough. The step of adjusting the regulating valve 206 may comprise physically opening or closing the valve 206 to regulate the flow of liquid product therethrough. That is, by means of filling control system 302 and the regulating valve 206 it is possible to control a flow of the liquid product through the filling machine 100. Advantageously, this way it is possible to control a pressure and/or flow of the liquid product.
| Number | Date | Country | Kind |
|---|---|---|---|
| 20181962.0 | Jun 2020 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2021/066588 | 6/18/2021 | WO |
