CONTROL DEVICE FOR REGULATING THE PRESSURE OF A FLUID

Abstract

A control device for controlling the pressure of a fluid, and a porometer that includes the control device. A regulating unit includes a pipe system for conveying a fluid and a regulating device associated with the pipe system. The regulating unit includes a first pressure regulator and a second pressure regulator, and the first and second pressure regulators each generate a regulating variable for an actuator for configuring the flow of the fluid in the pipe system; and a controller. The first pressure regulator is arranged on the inlet side in the pipe system. The second pressure regulator is arranged in series downstream of the first pressure regulator with respect to the direction of flow of the fluid in the pipe system. The controller is configured to specify a pressure setpoint value as a reference variable for the first pressure regulator and the second pressure regulator.

Claims

1. A control device for controlling a pressure of a fluid, comprising: a pipe system for conveying a fluid, the pipe system having an inlet and an outlet and the fluid flowing in the pipe system from the inlet to the outlet, a regulating unit associated with the pipe system, which comprises: at least two pressure regulators, which comprise a first pressure regulator and a second pressure regulator, the first and second pressure regulators each generating a regulating variable for an actuator to configure the flow of the fluid in the pipe system, and a controller, wherein the first pressure regulator is arranged on the inlet side of the pipe system, the second pressure regulator is arranged in series downstream of the first pressure regulator with respect to the direction of flow of the fluid in the pipe system, and the controller is configured to specify a respective pressure setpoint value as a reference variable for the first pressure regulator and the second pressure regulator.

2. The control device according to claim 1, wherein the pipe system forms a compensation volume in the region between the first pressure regulator and the second pressure regulator.

3. The control device according to claim 2, wherein the volume of the compensation volume is greater than the volume of the pipe system between the first pressure regulator and the second pressure regulator.

4. The control device according to claim 2, wherein the pipe system forms a further compensation volume downstream of the second pressure regulator.

5. The control device according to claim 4, wherein the volume of the further compensation volume is greater than the volume of the pipes between the second pressure regulator and the outlet of the pipe system.

6. The control device according to claim 1, wherein the pipe system runs linearly without forming branches.

7. The control device according to one of claim 1, wherein the pipe system forms two parallel pipe paths between the inlet and the outlet, wherein the at least two pressure regulators comprise the first pressure regulator, the second pressure regulator and a third pressure regulator, the first pressure regulator is arranged on the inlet side of the pipe system before the pipe system branches into two parallel pipe paths, the second pressure regulator is arranged along the one pipe path, and the third pressure regulator is arranged along the other pipe path.

8. The control device according to claim 7, wherein one pipe path forms a high-pressure region of the control device, through which the fluid flows when the pressure is above a threshold pressure, and the other pipe path forms a low-pressure region, through which the fluid flows when the pressure is below the threshold pressure.

9. The control device according to claim 8, wherein the pipe system comprises protection valves controllable by the controller, wherein the pipe path for the high-pressure region or the pipe path for the low-pressure region is activated by controlling the protection valves.

10. The control device according to claim 1, wherein the regulating unit further comprises an inlet pressure sensor at the beginning of the pipe system, which measures an actual pressure value on the inlet side and feeds the actual pressure value to the controller.

11. The control device according to claim 1, wherein the regulating unit further comprises an outlet pressure sensor at the outlet of the pipe system, which measures an actual pressure value at the outlet of the pipe system as a controlled variable, the controller detecting the actual pressure value measured by the outlet pressure sensor.

12. The control device according to claim 1, wherein the first pressure regulator is configured to carry out a pre-regulation of the pressure in the pipeline, the first pressure regulator receiving a first pressure setpoint value from the controller.

13. The control device according to claim 12, wherein the second pressure regulator is configured to carry out a fine regulation of the pressure in the pipeline, the second pressure regulator receiving a second pressure setpoint value from the controller.

14. The control device according to claim 1, wherein the first and second pressure regulators are configured as PI or PID regulators, one of the first and second pressure regulators being configured in such a way that the I component of the regulation in that pressure regulator that is so configured is switched off or reduced, and the controller interacts with that pressure regulator in such a way that the I component of the regulation is carried out by the controller.

15. The control device according to claim 1, wherein the first and second pressure regulators are configured as PI, PD or PID regulators, wherein one of the first and second pressure regulators is configured such that the P component and/or the D component of the regulation in that pressure regulator that is so configured is switched off or reduced, and the controller interacts with that pressure regulator such that the P component and/or D component of the regulation is carried out by the controller.

16. The control device according to claim 1, wherein all the logical controller components of one of the first and second pressure regulators are integrated into the control device, and that pressure regulator, that is integrated into the control device, itself comprising only one actuator, in particular, a valve operable to configure the flow of the fluid in the pipe system, and the controller being configured to provide a regulating variable for the actuator.

17. A control device for controlling a pressure of a fluid, comprising: a pipe system for conveying a fluid, the pipe system having an inlet and an outlet and the fluid flowing in the pipe system from the inlet to the outlet, a regulating unit associated with the pipe system, which comprises: a pressure regulator, wherein, in operation, the pressure regulator generates a regulating variable for an actuator to configure the flow of the fluid in the pipe system, a controller which is configured to preset a pressure setpoint value as a reference variable for the pressure regulator, and a compensation volume, which is arranged in the pipe system downstream of the at least one pressure regulator.

18. A porometer, that comprises: a device for holding a sample to be measured; and a control device according to claim 1, which is arranged upstream of the sample to be measured and pressurizes the sample to be measured with a fluid under defined pressure conditions.

19. The porometer according to claim 18, wherein in an operating state in which the control device applies a pressure to the sample to be measured in such a way that the sample in any case is partially flowed through by the fluid, the controller is configured such that: the first and second pressure regulators are controlled via the controller in such a way that valves obtained in the first and second pressure regulators for the configuration of the flow of the fluid in the pipe system are opened to such an extent that the flow through the first and second pressure regulators is equal to the flow through the sample through which the fluid flows.

20. The porometer according to claim 18, wherein in an operating state in which the control device applies a pressure to the sample to be measured in such a way that the fluid flows at least partially through the sample, the controller is configured in such a way that: the first and second pressure regulators are controlled via the controller in such a way that valves obtained in the first and second pressure regulators for the configuration of the flow of the fluid in the pipe system are opened to such an extent that the flow through the first and second pressure regulators deviates from the flow through the sample through which the fluid flows on average at most to such an extent that the change in pressure close to the sample does not exceed a predefined level.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0058] The invention will be explained in more detail on the basis of a plurality of exemplary embodiments, with reference being made to the figures, in which:

[0059] FIG. 1 is an embodiment of a control device for regulating a pressure in a pipe system, wherein the control device comprises a control device with two pressure regulators connected in series;

[0060] FIG. 2 is a schematic and exemplary pressure curve at point A of the control device of FIG. 1;

[0061] FIG. 3 is a schematic and exemplary pressure curve at point B of the control device of FIG. 1;

[0062] FIG. 4 is a schematic and exemplary pressure curve at point C of the control device of FIG. 1;

[0063] FIG. 5 is a schematic of a porometer with a sample to be measured and a control device;

[0064] FIG. 6 is a flowchart of a method for performing a porometric measurement with a porometer as shown in FIG. 5; and

[0065] FIG. 7 is a further embodiment of a control device for regulating a pressure in a pipe system, wherein the control device comprises a control device with a pressure regulator and a compensation volume arranged behind it.

DETAILED DESCRIPTION

[0066] FIG. 1 shows an embodiment of a control device 1 for controlling the pressure of a fluid. The regulating unit comprises a regulating section and a regulating device.

[0067] The regulating section is formed by a pipe system 2 in which the fluid is conveyed. The pipe system 2 can be formed from pipes and/or hoses. It comprises an inlet path 21, which branches into two parallel pipe paths 22, 23, which reunite at the end of the pipe system 2 to form an outlet path 24. The beginning of the inlet path 21 forms an inlet 201 of the pipe system 2 and the outlet of the outlet path 24 forms an outlet 202 of the pipe system 2. Further sensors and/or a sample 8 of a porometric measurement can be connected to the outlet 202 of the pipe system 2, as explained with reference to FIG. 5.

[0068] Furthermore, the pipe system 2 comprises two compensation volumes 71, 72, as will be explained. The compensation volumes 71, 72 are formed, for example, by corresponding tanks with volumes V1, V2.

[0069] The pipe system 2 under consideration here is particularly suitable for conducting gases that are used for porometric measurement. In principle, however, the control device 1 can also be used to control the pressure in a liquid.

[0070] The regulating unit controls and regulates the volume flow in pipe system 2. It comprises several pressure regulators 41, 42, 43, an inlet pressure sensor 31, an outlet pressure sensor 32, several protection valves 61, 62, 63, several flow meters 75, 76, 77, and a controller 5.

[0071] The controller 5 communicates with the said components via schematically shown control lines 51-57, whereby it can receive data recorded by the components and/or transmit control commands to the components. For example, the controller 5 can transmit control commands to the pressure regulators 41, 42, 43, which relate to pressure setpoint values. The controller 5 can transmit control commands to the protection valves 61, 62, 63 that relate to the opening, closing or partial opening of the protection valves. The controller 5 can receive sensor signals from the inlet pressure sensor 31, the outlet pressure sensor 32 and the flow meters 75, 76, 77.

[0072] According to FIG. 1, the inlet pressure sensor 31 is arranged on the inlet side of the pipe system 2. The inlet pressure sensor 31 measures an actual pressure value on the inlet side and communicates this information to the controller 5.

[0073] Furthermore, a first pressure regulator 41 is arranged in the inlet path 21. A second pressure regulator 42 is arranged in the upper pipe path 22 and a third pressure regulator 43 is arranged in the lower pipe path 43. This means in each case that the corresponding pressure regulator 41, 42, 43 can influence the pressure in the corresponding path 21, 22, 23. This is done, for example, via a valve for flow control, which is a component of the respective pressure regulator. Such a valve represents an actuator of a regulation in the pressure regulator. Alternatively, a valve for flow control can be arranged in a separate component that is controlled by the respective pressure regulator.

[0074] It is provided that the valve for controlling the flow of the pressure regulator 41, 42, 43 can be moved quickly and precisely so that pressure values can be configured quickly and precisely. This is, for example, an electrically and/or pneumatically actuated valve, such as an electromagnetically actuated valve.

[0075] The one compensation volume 71 with the volume V1 is located both between the first pressure regulator 41 and the second pressure regulator 42 and between the first pressure regulator 41 and the third pressure regulator 43. The volume V1 is, for example, in the range between 200 ml and 400 ml.

[0076] The other compensation volume 42 with the volume (V2) is located downstream of the third pressure regulator 43 before the two paths 22, 23 rejoin. A further compensation volume may also be present downstream of the second pressure regulator 42 in a corresponding manner. The volume V2 is, for example, in the range between 50 ml and 200 ml.

[0077] Furthermore, a protection valve 61 is located downstream of the second pressure regulator 42. Two further protection valves 62, 63 are located upstream and downstream of the third pressure regulator 43. By controlling the protection valves 61-63 by the controller 5, either the upper pipe path 22 or the lower pipe path 23 can be switched or activated. It is intended that the upper pipe path 22 defines a high-pressure region of the control device, while the lower pipe path 23 defines a low-pressure region of the control device. The low-pressure region is indicated schematically in FIG. 1 by the box 101. Depending on which pressure is present in the pressure line 2, pressure control takes place either via the high-pressure region or the low-pressure region. However, these areas are not usually used in parallel.

[0078] One or more flow meters 75-77 can be provided on the output side, whereby the number of three flow meters shown is only to be understood as an example.

[0079] The outlet pressure sensor 32 measures the actual pressure value at the outlet of the pipe system 2 and provides this information to the controller 5 as a controlled variable.

[0080] The control unit 5 generates a pressure setpoint value for the pressure regulator 41 and a pressure setpoint value for the pressure regulator 42 or the pressure regulator 43. Based on these setpoint values, the pressure regulators 41, 42, 43 each perform pressure control autonomously in a first embodiment. They are designed, for example, as PI controllers or PID controllers.

[0081] Alternatively, in an embodiment, it is provided that the I component of the regulation of at least one of the pressure regulators 41-43, in particular all the pressure regulators involved, is carried out by the controller 5. In this case, the I component of the regulation in the pressure regulator 41-43 itself is switched off. Alternatively or additionally, the controller 5 can take over the P component and/or the D component of the respective pressure regulator 41-43. In order to realize this, the controller 5 takes over parts of the tasks of the firmware of the pressure regulators 41-43.

[0082] The series connection of two pressure regulators 41, 42 or 41, 43 in the respective flow path 21, 22 or 21, 23 in conjunction with the provision of one or more compensation volumes 71, 72 results in a strong reduction of occurring pressure fluctuations and enables virtually trouble-free and highly accurate controllable pressure control. This is shown schematically as an example in FIG. 2-4.

[0083] FIG. 2 shows the pressure curve at point A of FIG. 1, i.e. downstream of the first pressure regulator 41. The amplitude of the pressure fluctuation is still comparatively large, although it is already significantly reduced by the compensation volume 71 provided compared to the situation in which no such compensation volume 71 is present.

[0084] FIG. 3 shows the pressure curve at point B of FIG. 1, i.e. downstream of the second pressure regulator 42 of the upper path. At this point, consecutive pressure regulation has already taken place, first by the pressure regulator 41 and then by the pressure regulator 42. The pressure regulator 41 has carried out a pre-regulation of the pressure. It provides the downstream pressure regulator 42 with an inlet pressure that is smoothed as shown in FIG. 2 andapart from the superimposed oscillationis essentially constant. Due to the further regulation by the pressure regulator 42, the pressure has been further smoothed in accordance with FIG. 2.

[0085] FIG. 4 shows the pressure curve at point C of FIG. 1, i.e. downstream of the second pressure regulator 43 of the lower path 23. The explanations for FIG. 2 apply accordingly. In addition, the pressure is further smoothed by the additional compensation volume 72. Accordingly, the pressure fluctuations in FIG. 4 are further reduced and have almost completely disappeared.

[0086] In this context, it is pointed out that due to the fact that the sizes of the pores that are currently opening at a certain pressure are inversely proportional to this same pressure (i.e. larger pores open at a comparatively low pressure), and further due to the fact that the opening of larger pores leads to greater pressure fluctuations, stable vibration-free pressure control is even more important in the low-pressure region than in the medium or high-pressure region. Accordingly, in FIG. 1, a further compensation volume V2 is only provided in the low-pressure region 101, although, as explained, this is only to be understood as an example.

[0087] The controller 5 is intended to realize a pressure increase in the pipe system 2 as part of a porometric measurement, for which purpose the controller 5 increases the pressure setpoint values at the pressure regulators 41-43. Such a pressure increase can take place several times as part of the porometric measurement, whereby after a pressure increase has taken place, a further pressure increase only takes place when the pressure of the last pressure increase has stabilized. It is intended that the current values of the actual pressure value and the associated volume flow (measured by the flow meters 75-77) are recorded as measuring points of the porometric measurement for a stabilized pressure.

[0088] Before such a method is explained by way of example with reference to FIG. 6, a porometer is considered schematically in FIG. 5. The porometer comprises a sample to be measured 8, which is arranged in a device 80. The sample contains areas 81 with sample material and pores 82 without sample material, which are sealed by a liquid. Gas 95 flows into the device 80 via a supply line 92. The gas 95 collects in the device 80 and, after reaching a corresponding pressure, pushes the liquid out of the pores 82, the gas 95 ejecting the liquid first from the pores 82 with the largest diameter and ejecting it last from the pores 82 with the smallest diameter. A measured value is recorded in each case when there is a change in the volume flow of the gas 95 due to the emptying of a pore (or a class of pores with the same diameter) (whereby in FIG. 5 all the pores are still closed). Such a porometric method is known to the skilled person, so that it will not be discussed further here.

[0089] The sample 8 or device 80 is preceded by a control device 1 as shown in FIG. 1, which receives gas via a supply line 91, which has a pressure in the range between 10 bar and 50 bar, for example. The gas is nitrogen, for example.

[0090] For a porometric measurement, it is necessary to increase the pressure several times and keep it as constant as possible in between. By cascading two pressure regulators in the control device 1 in accordance with the disclosure and the additional provision of compensation volumes, the control device 1 makes it possible to control the pressure with high precision and almost interference-free.

[0091] At the start of a measurement, the operating pressure to be kept constant for the first pressure regulator 41 is first determined in accordance with step 601 of FIG. 6 by defining a pressure setpoint value for the pressure regulator. Further, according to step 602, either the low-pressure region or the high-pressure region is selected for the measurement to be performed and the protection valves 61-63 are switched accordingly. If, for example, a measurement is made over the high-pressure region, the protection valves 62, 63 are closed so that the pressure regulator 43 is protected from high pressure.

[0092] According to step 603, after the pressure values at the first pressure regulator 41 have stabilized, the pressure setpoint value for the gas 95 at the outlet of the control device 1 is increased. For this purpose, certain pressure targets and step widths for the porometric measurement may have been defined beforehand. The pressure setpoint value is increased by adjusting the pressure setpoints at the two pressure regulators 41, 42 and 41, 43 accordingly.

[0093] The pressure setpoint value is increased according to step 604 by realizing a predefined pressure increase rate at which the pressure setpoint value is increased. It is intended that the pressure increase rate is variable and that its value depends on the distance between the actual pressure value and the pressure setpoint value (the desired pressure increase). This means that initially, when this distance is still large, the pressure rises quickly, while shortly before the pressure setpoint value is reached, the pressure rises only slowly. This enables a rapid realization of a pressure increase while avoiding the risk of exceeding the desired pressure setpoint value.

[0094] According to step 605, the pressure regulation for the second pressure regulator 42, 43 is frozen until a stable pressure and associated volume flow is configured. During this time, the setpoint for the second pressure regulator 42, 43 is no longer changed.

[0095] If a stable pressure is present, it may be provided that the valves mentioned for configuring the flow in the pressure regulators 41-43 are opened just wide enough so that the flow through the pressure regulators is equal to the flow through the closed sample 8. The stable state is thus maintained. Alternatively, it may be provided that the aforementioned valves for configuring the flow in the pressure regulators are opened to such an extent that the flow through the pressure regulators deviates from the flow through the flowing sample at most to such an extent that the change in pressure close to the sample does not exceed a predefined level and is thus harmless for the measurement.

[0096] If a stable pressure and associated flow are present, a corresponding measured value of the porometric measurement is recorded according to step 606. The pressure setpoint value can then be increased again, with steps 603-605 being repeated. A series of measured values of the porometric measurement is obtained.

[0097] FIG. 7 shows a further embodiment which corresponds to the embodiment of FIG. 7 except for the fact that the control device does not have an input-side pressure sensor 71. Thus, only one pressure regulator 42, 43 is provided along each of the paths 22, 23. A compensation volume 73, 72 with a tank volume V3 or V2 is provided downstream of each of the pressure regulators 42, 43. The equalizing volumes 72, 73 are each provided, for example, by a separate tank which is connected to the pipeline downstream of the respective pressure regulator 42, 43.

[0098] With regard to FIG. 7, reference is also made to the explanation of FIG. 1.

[0099] It should be understood tht the above description is intended for illustrative purposes only and is not intended to limit the scope of the present disclosure in any way. Also, those skilled in the art will appreciate that other aspects of the disclosure can be obtained from a study of the drawings, the disclosure and the appended claims. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. Various features of the various embodiments disclosed herein can be combined in different combinations to create new embodiments within the scope of the present disclosure. In particular, the disclosure extends to and includes all combinations and sub-combinations of one or more features described herein. Any ranges given herein include any and all specific values within the range and any and all sub-ranges within the given range.