EP3267039A1 - System and method for controlling a pump station - Google Patents

Abstract

Method for regulating a pumping station (1) in a hydraulic network, in particular a pressure booster system, which pressurizes a medium to be conveyed to at least one consumer (3), the pressure depending on the volume flow (Q) through the pumping station (1) according to a control curve is set. The control curve is formed from a plurality of partial pressure curves (P soll, 1 (Q), ..., p soll, n (Q)), each for a volume flow interval ("Q 1, ...," Q n) a number (n) of seamlessly adjoining volume flow intervals ("Q 1, ...," Q n) corresponding to the plurality can be defined on the basis of pressure and volume flow values of the network that are determined and to be evaluated on an interval-related basis. This enables an optimal, needs-based adjustment of the outlet pressure of the pumping station (1), so that the operation is energy-efficient.

Description

The invention relates to a method for controlling a pumping station in a hydraulic network, which pressurizes a medium to be conveyed to at least one consumer, the pressure being adjusted in dependence on the volume flow through the pumping station according to a control curve. Furthermore, the invention relates to a system for carrying out the method.

If a medium is pumped from a pumping station to a consumer, there are pressure losses along the conveying path, which are caused by the pipe friction to the other by actuators within the line on the one hand. The longer the cable routes, the higher the losses. This is in closed systems such as heating or cooling systems as well as in open systems, for example in the case of a pressure booster system of drinking water supply. Regularly, it is the desire that the consumer, for example, a withdrawal point for the funded drinking water, a radiator or a cooling circuit, a sufficient pressure is present to provide the consumer with sufficient. For example, the shower should be sufficiently high pressure not to interfere with the showering pleasure.

The actual pressure at the consumer is usually not known, so that the pumping station is always chosen so oversized and exaggerated high that with almost certainly even at unfavorable System conditions, the worst-served consumer is always adequately supplied.

In pressure booster systems in the drinking water supply, it is known to regulate to a constant, predetermined output pressure. The outlet pressure of these pumping stations is thus adjusted according to a constant pressure control curve, i. regardless of the volume flow through the pumping station kept constant. If the supply pressure provided by the supplier varies, the pressure booster compensates for such pressure fluctuations. However, a constant pressure control leads to an energetically not optimal operation. The pressure losses increase with the volume flow, so that a proportional pressure curve, along which the pumping station is controlled, would be energetically more favorable. However, the actual pressure losses along the route to be conveyed are generally unknown and optimum adjustment of the pumping station is therefore difficult. In addition, especially at pressure booster systems, the removal at several taps simultaneously leads to enormous fluctuations in pressure in the system, which makes no practical setting of the pressure.

The object of the underlying invention is to provide a method and a system for controlling a pumping station in a hydraulic network which regulates the pressure of the pumping station as required and energy-efficiently as a function of the volume flow without loss of comfort.

This object is achieved by a method having the features of claim 1. In addition, the object is achieved by a system having the technical features of claim 18. Advantageous embodiments and modifications of the invention will become apparent from the dependent claims and the description below.

According to the invention, it is proposed to set the pressure of the pumping station as a function of the volume flow through the pumping station in accordance with a control curve, the control curve being formed from a plurality of partial pressure curves, each corresponding to a volume flow interval of a plurality of the plurality be defined gapless intervals adjacent to each other on the basis of determined and interval-related evaluated pressure and flow values of the network. The control curve is thus defined section by section without gaps, ie on the one hand for all possible load cases, on the other hand taking into account the pressure losses actually occurring in the system. The concrete knowledge of the hydraulic resistances in the network is not necessary.

According to the invention, a system for controlling a pumping station in a hydraulic network is also proposed, with which a medium to be conveyed to at least one consumer can be pressurized, the pressure being adjustable as a function of the volume flow through the pumping station according to a control curve, the system for this purpose is arranged to form the control curve of a plurality of partial pressure curves, and to define these partial pressure curves for a volume flow interval of the plurality of corresponding number seamlessly contiguous flow intervals on the basis of determined and interval-related pressure and flow values of the network.

The control curve is composed of the plurality of partial pressure curves that are each defined for a specific volume flow interval. The definition or determination of the respective partial pressure curve of a specific volume flow interval is preferably carried out dynamically during operation, for which purpose pressure and volume flow values are determined and those values are assigned which are assigned to the specific volume flow interval. In this way, a control curve is formed, the use of which the control of the pumping station is optimally adapted to the hydraulic network and the pumping station is operated energetically particularly favorable.

Figur 1

ein System zur Regelung einer Pumpstation in einem hydraulischen Netzwerk unter Verwendung von Druckwerten von nur einer Systemstelle,

Figur 2

ein System zur Regelung einer Pumpstation in einem hydraulischen Netzwerk unter Verwendung von Druckwerten von zwei Systemstellen,

Figur 3a, b

Ablaufdiagramme des erfindungsgemäßen Verfahrens,

Figur 4

eine Darstellung erfasster Druck- und Volumenstromwerte als Datentupel in einem p-Q Diagramms,

Figur 5

eine Zuordnung der Datentupel zu Volumenstromdatenintervallen im Δp-Q Diagramms,

Figur 6

eine Darstellung gebildeter Repräsentanzwerte zu den Volumenstromdatenintervallen im Δp-Q Diagramms,

Figur 7

eine aus einer Mehrzahl partieller Konstantdruck-Kurven gebildete Regelkurve im p-Q Diagramm aufgrund der Repräsentanzwerte in Figur 6,

Figur 8

eine Darstellung gebildeter Repräsentanzwerte zu den Volumenstromdatenintervallen im Δp-Q Diagramm mit linearer Verknüpfung,

Figur 9

eine aus einer Mehrzahl partieller Proportionaldruck-Kurven gebildete Regelkurve im p-Q Diagramm aufgrund der Repräsentanzwerte in Figur 8,

Figur 10

eine Darstellung gebildeter Repräsentanzwerte zu den Volumenstromdatenintervallen im Δp-Q Diagramm mit linearer Verknüpfung, wobei die Repräsentanzwerte den Mitten der Volumenstromdatenintervalle zugeordnet sind.

Figur 11

eine aus einer Mehrzahl partieller Proportionaldruck-Kurven gebildete Regelkurve im p-Q Diagramm aufgrund der Repräsentanzwerte in Figur 10.

Further advantages and features and characteristics of the method according to the invention and of the system according to the invention are explained below with reference to exemplary embodiments and the accompanying figures. Show it:

FIG. 1

a system for controlling a pump station in a hydraulic network using pressure values from only one system location,

FIG. 2

a system for controlling a pump station in a hydraulic network using pressure values from two system locations,

FIG. 3a, b

Flowcharts of the method according to the invention,

FIG. 4

a representation of recorded pressure and volume flow values as a data tuple in a pQ diagram,

FIG. 5

an assignment of the data tuples to volume flow data intervals in the Δp-Q diagram,

FIG. 6

a representation of formed representative values for the volume flow data intervals in the Δp-Q diagram,

FIG. 7

a control curve formed from a plurality of partial constant pressure curves in the pQ diagram on the basis of the representation values in FIG. 6 .

FIG. 8

a representation of formed representative values for the volume flow data intervals in the Δp-Q diagram with linear link,

FIG. 9

a control curve formed in the pQ diagram from a plurality of partial proportional pressure curves on the basis of the representation values in FIG. 8 .

FIG. 10

a representation of formed representation values for the volume flow data intervals in the Δp-Q diagram with linear association, wherein the representation values are assigned to the centers of the volume flow data intervals.

FIG. 11

a control curve formed in the pQ diagram from a plurality of partial proportional pressure curves on the basis of the representation values in FIG. 10 ,

FIG. 1 shows a building 10 with a drinking water supply, which is fed by a central supply line 9 of a municipal utility with pressurized drinking water. The drinking water system comprises a set up within the building 10 pumping station 1 in the manner of a pressure booster, the On the input side is connected via a supply line 16 to the central supply line 9, and the output side is connected to a hydraulic network 8, 2, which has a plurality of consumers 3, to which the drinking water is passed. The consumers 3 are formed here by withdrawal points for the removal of drinking water. For example, the consumers, water fittings such as sinks, bathtubs or shower fittings, toilets, washing machines or dishwashers, etc. are formed.

The network 8, 2 comprises a connected to the output of the pumping station 1 pressure line 8, depart from the two local supply lines 2, along which the consumer 3 are arranged. Viewed hydraulically, the consumers 3 thus all have a different distance to the pumping station 1, so that each line path from the pumping station 1 to one of the consumers 3 causes an individual pressure loss.

The pumping station 1 comprises two parallel arranged pumps 17, which can be operated alternatively or cumulatively. A control and regulation unit 7 is provided for controlling and / or regulating the pumps 17 and adjusts them accordingly in their power and / or speed.

It should be noted that the illustration in FIG. 1 purely by way of example, and the invention is by no means limited thereto. For example, the pumping station may also have only one pump 17 or more than two pumps, for example three or four pumps 17, which may be hydraulically parallel and / or in series. The control and regulation unit 7 may be structurally part of the pumping station 1, but it may alternatively be outside the pumping station, for example, be part of a central control and / or regulation of a building technology. Furthermore, according to an alternative embodiment variant, the hydraulic network can also have two or more pressure lines 8 and / or the pressure line 8 can supply three or more floors. Also, in one embodiment, three or more local supply lines 2 may depart from the pressure line 8. Finally, it is also possible that a local supply line is split into two or more further lines. Finally, you do not have to, as in FIG. 1 represented in the local supply lines 2 the same number of consumers 3 be present, the local supply lines 2 have the same length, or the spacing between the consumers be equidistant. So shows FIG. 2 an exemplary drinking water system in which the local supply line 2 extending in the second floor is shorter on the one hand than the local supply line 2 extending in the first floor and on the other hand has fewer consumers 3 than the local supply line 2 extending in the first floor ,

The pumping station 1 increases the pressure of the central supply line 9 and promotes the drinking water via the pressure line 8 and the local supply lines 2 to the consumers 3, if at least one of the removal points 3 opens. In this case, the pumping station 1 is controlled so that at its output a certain output pressure is present, which ensures that even at the worst sampling point 3 is a sufficient flow pressure. Here, the pressure losses must be considered, which are present between the pumping station 1 and the respective sampling point 3. The worst removal point 3, also called the worst point, is usually the removal point which, geographically speaking, is the highest and / or furthest away from the pumping station 1. Hydraulically, it is the removal point 3, to reach the water experiences the greatest hydraulic resistance.

Pressure fluctuations in the central supply line 9, which are responsible, for example due to feed or actuator dependent from the supplier or resulting from sampling fluctuations in the neighborhood must be compensated by the pumping station 1 as well as pressure changes within the hydraulic network resulting from the opening and closing of one or more exit points result. To compensate for these pressure fluctuations, the pressure of the pumping station 1 is set at the output according to the prior art to a constant value, that is regulated according to a constant pressure control curve. Thus, the pressure p _from the output of the pumping station above the flow rate Q is constant.

The inventive method is based on this mode of operation and adjusts the control curve so that the output pressure in dependence of the volume flow Q is set by the pumping station 1 according to a new control curve. This new control curve is formed from a plurality of partial pressure curves p _{soll, 1} (Q),..., P _{soll, n} (Q), each for a volume flow interval ΔQ ₁ ,..., ΔQ _{n of} a number corresponding to the number n gaps of adjacent flow .DELTA.Q intervals _1, ..., _n .DELTA.Q based on determined and be evaluated with respect interval pressure and flow values of the network are defined.

In order to form the partial pressure curves, the pressure and volume flow values can at least system pressure values p _sys (t _v ), p _{sys, k} (t _v ) of the system pressure p _sys , p _{sys, k present} at a system location 5, 5 a, 5 _b and volume flow values Q ( t _v ) of the flow or delivered volume flow Q at different times t _v include.

As in FIG. 1 can be selected as system point 5, the worst point, ie the location of the worst sampling point 3. This has the advantage that the maximum occurring pipe losses are taken into account for the formation of the control curve and thus ensures that even the worst removal point 3 is supplied with sufficient operating pressure when the pumping station 1 is controlled according to the partial pressure curves according to the invention. It is therefore preferably the system pressure p _sys this worst sampling point 3 determined. As a rule, this is a removal point 3, which is located at the end of one of the local supply lines 2, in particular that extraction point, which is located at the highest.

However, it is not always the case and not always clear that the highest located sampling point 3 at the end of a local supply line 8 is the Schlechtpuntk. For that reason shows FIG. 2 an embodiment in which the system pressure p _{sys, k is determined} at two system locations 5a, 5b, each representing a potential bad point because they are each located at the end of a branch of the hydraulic network. Subsequently, the index k indicates the location of the system location, so that at two system locations k = 1 for the first system location 5a or k = 2 for the second system location 5b.

In a complex hydraulic network with multiple or multiple branched pathways, even more than two potential penalty points are possible. It then makes sense to determine corresponding system pressure values at several different network system locations that represent these potential bottlenecks.

It is not necessary to determine the system pressure p _sys , p _{sys, k} exactly at the location of a sampling point. Rather, it can also be determined away from, before, or after, such as FIG. 2 shows. Consequently, the system location 5 or the first or second system location 5a, 5b can also be before or after a removal point 3, in particular before or after the bad point. The resulting inaccuracy in the value detection is low and thus does not affect the inventive method. However, the system point 5 is preferably located in the immediate vicinity of the removal point 3, since the installation of a measuring device is the simplest there.

The determination of the system pressure values preferably takes place by measuring by means of a measuring device such as a pressure sensor. The system pressure p _sys , p _{sys, k} can alternatively be calculated or estimated from other variables.

In addition to the system pressure p _sys , p _{sys, k} , the volume flow Q is determined. This can also be done by measuring by means of a measuring device such as a volume flow sensor 6, but alternatively also mathematically from other variables such as the power or the rotational speed of one or both pumps 17. The measuring device 6 can be arranged, for example, at the entrance of the pumping station 1. As an alternative, an estimation of the volumetric flow can take place, for example on the basis of mathematical, electro-mechanical and / or mechanical-hydraulic models of the pumping station 1.

As far as one or more measuring devices are present, they preferably form part of the system according to the invention for controlling the pumping station 1. In particular, the measuring device for the outlet pressure and / or for the volume flow can be structurally combined with the pumping station 1.

The existing measuring devices may be connected to the control and regulation unit 7, for example via a cable connection and / or via a radio link. A cable connection has the advantage of a reliable and substantially simultaneous detection of the system pressure or one of the system pressures, the outlet pressure and / or the volume flow. In contrast, a radio link has the advantage of easy installation or retrofitting of components to be connected by data technology, such as a measuring device for detecting the system pressure, since the laying of a data line is eliminated.

The system pressure p _sys , or respective system pressure p _{sys, k} , and the volume flow Q are suitably assigned to one another in terms of time, ie, preferably determined at the same or essentially the same time t _v . Because of this common temporal reference, they form a unit in the form of a data tuple. For the definition of the control curve, a multiplicity of data tuples is preferably determined at different times.

The determination of the pressure and volume flow values, in particular detection of the data tuples, can take place at intervals, for example either at certain times, such as on the hour, or always after a period of time, e.g. every 15 minutes. They can therefore be determined periodically. Alternatively or cumulatively, certain events can trigger the determination of pressure and volume flow values, for example the opening of a sampling point.

It should be noted that the pressure p _sys , p _{sys, k} at the system site 5, 5 a, 5 b identical or at least almost identical to the outlet pressure p _from the pumping station 1 when no sampling point is open, or no consumer 3 consumed something , In this case, furthermore, the volume flow Q is equal to zero and thus the corresponding data tuple is not usable.

According to one embodiment, these cases, regardless of the knowledge associated with them, can still be recorded initially as pressure and volume flow values, in which case a filtering of the data tuples can follow, in which such data tuples with volume flow zero and / or those with a system pressure essentially correspond to the outlet pressure p _from the pumping station 1 be removed. To avoid this, it can be ensured that the unusable data tuples are not detected at all. This can be achieved by determining when the flow rate Q is greater than zero during operation of the pumping station 1, wherein only in this case the pressure value or pressure values p _sys (t _v ), p _{sys, k} (t _v ) and Volume flow value Q (t _v ) are determined.

In addition, in order to obtain valid pressure and volume flow values, it is advantageous to hide transition effects from one system state "sampling point closed" to the other system state "sampling point open". Such transition effects are, for example, a transient, ie decaying periodic pressure fluctuations. According to a preferred development of the method, therefore, additionally or alternatively for determining when the volume flow is greater than zero, it can be determined during operation of the pumping station 1 when the time change of a non-zero volume flow Q is substantially constant, at least for a certain period of time. whereby only in this case the pressure value or values p _sys (t _v ), p _{sys, k} (t _v ) and the volume flow value Q (t _v ) are recorded. Because in this case, the transition effects have largely subsided.

The determination of the pressure and volume flow values, in particular the detection of the data tuples, takes place at least at the beginning of the method and at least for a certain period of time, since they form the basis for the definition of the partial pressure curves. The longer the period, the more values or data tuples are collected and the more precisely the control curve can be adapted in sections to the actual conditions. It is not necessary to limit data collection to this period. Rather, the method according to the invention can be applied continuously during operation of the pumping station 1, and in this way the control curve can be adapted dynamically over and over again. However, the end of the period may be determined by the beginning of the subsequent evaluation of the collected data tuples. At the end of the period, a new period can then follow within which the data collection takes place.

The evaluation of the determined pressure and volume flow values or data tuple can be carried out as described below.

According to an embodiment variant, the data tuples can first be assigned, on the basis of their respective volume flow value Q (t _v ), to a volume flow data interval ΔQd _i that correlates with one of the volume flow intervals ΔQ _i . The collected data are thus grouped together with regard to the partial pressure curves to be defined, with the groups also being sorted. The time reference of the pressure and volume flow values or the data tuple is no longer relevant.

Subsequently, for each data tuple, the pressure distribution Δp is calculated by the pumping station 1 to the corresponding system location 5, 5a, 5b. This can be done according to an embodiment in that the difference from an output pressure setpoint p _booster the pumping station 1 and the system pressure value p _sys (t _v ), p _{sys, k} (t _v ) of the respective data tuple is formed. The output _{pressure set} point p _{booster of} the pumping station 1 is known since it corresponds to the constant _{pressure to} which the pumping station 1 is regulated at least at the beginning of the method according to the invention. It defines the initial constant pressure control curve according to which the output pressure p _{out is set} by the control and regulation unit 7.

Naturally, however, it is so that the output pressure p _from the pumping station 1 in practice does not or at least not always the output pressure _setpoint p _booster corresponds because occur before and / or behind the pumping station dynamic pressure changes, which are adjusted accordingly. Thus, the pressure losses from the pumping station 1 to the corresponding system location 5, 5a, 5b can be calculated more accurately if, instead of the output pressure _setpoint p _booster, the pressure p _aus actually present at the outlet of the pumping station 1 is used. For this reason, it is advantageous if the determined and / or determined pressure and volume flow values also include the outlet pressure p _from the pumping station 1.

As in the case of system location 5 or system locations 5a, 5b, output pressure p can also be determined or estimated _from measurements or computations, for example on the basis of a mathematical model of pumping station 1. The determination also preferably takes place by measurement, for example by means of a pressure sensor which is suitably arranged at the outlet of the pumping station 1.

In terms of process technology, it is simple for the pressure loss determination if the data tuples together with the respective system pressure value p _sys (t _v ), p _{sys, k} (t _v ) and volume flow value Q (t _v ) also have an output pressure value p _out (t _v ) of the output the pumping station 1 currently applied output pressure p _off . It is determined at the same or at least substantially the same time t _v as the other two values, so that a corresponding system pressure value p _sys (t _v ), p _{sys, k} (t _v ), an output pressure value p _out (t _v ) and a Volume flow value Q (t _v ) form a group due to the common determination time. Thus, in this embodiment, each data tuple then comprises three elements and thus forms a data triplet.

According to a further development of this embodiment with data triplets, and alternatively for the calculation of the pressure loss from the pumping station 1 to the corresponding system location 5, 5a, 5b on the basis of the initial pressure setpoint p _booster , the pressure loss Δp (t _v ) can be calculated from the system pressure value p _sys (t _v ), p _{sys, k} (t _v ) and the determined output pressure value p _out (t _v ) of each data tuple are determined by subtraction. This results in a pressure loss Δp (t _v ) from each data tuple.

A diagrammatic representation of the determined data tuples is in FIG. 4 shown. It shows in a pQ diagram for different data tuples formed at different times t _v the output pressure value p _out (t _v ), the system pressure value p _sys (t _v ), p _{sys, k} (t _v ), each formed by a small circle - And the present volume flow value Q (t _v ). Particularly emphasized are the data tuples of the four times t ₁ , t ₂ , t ₃ , t ₄ . The vertical distance of the circles corresponds to the pressure loss Δp (t _v ) at the respective time (t _v ). Recognizable is the output pressure value p _from (t _v) for all detected data tuples on a p the output pressure setpoint _booster corresponding line, demonstrating that p used instead of the actual output pressure values p _from (t _v) of the output pressure setpoint _booster without significant deviations and thus deterioration in the quality of the process.

By allocating the data tuple to one of the volume flow data intervals ΔQd ₁ ,... ΔQd _n , one obtains in the result for each volume flow data interval ΔQd _i a set m of pressure loss values Δp _{i, j} (with i = 1 ... n; j = 1). m), which can be used to calculate the respective partial pressure curve. This is in FIG. 5 illustrated. It should be noted that although in the case of using two or more system locations 5a, 5a, the location was differentiated beforehand, namely, by referencing this location at the corresponding system pressure p _{sys, k} , it ultimately on the place of capture does not arrive. After all, only the height of the pressure losses and their assignment to a volume flow data interval ΔQd _{i are of importance} . With two system locations 5a, 5b, only the amount of data tuples detected in the same time period doubles.

The same result as in FIG. 5 is reached when the steps of interval allocation and pressure loss calculation are reversed. Thus, according to another embodiment, initially from the system pressure value p _sys (t _v ), p _{sys, k} (t _v ) and the output _setpoint p _{booster of} the pumping station 1 or determine the output pressure value p _from (t _v ) of each data tuple by forming a difference in pressure difference Δp (t _v ) from the output of the pumping station 1 to the system location 5, 5a, 5b are determined, and then this determined pressure loss .DELTA.p (t _v ) based on the volume flow value Q (t _v ) of the respective data tuple a volume flow data interval .DELTA.Qd _{i be} assigned. The time reference is then no longer important. The pressure loss Δp can rather be stated as the jth value of the i-th volume flow data interval ΔQd _i .

The volume flow intervals ΔQ ₁ ,..., ΔQ _n are closed subregions of the volume flow range that can be conveyed by the pumping station 1. This volumetric flow range extends from Q = 0 to Q = Q _max , cf. FIG. 4 in the event that all pumps 17 of the pumping station 1 are simultaneously in operation. The intervals are thus each down by a minimum value or initial value and bounded above by a maximum value (final value), wherein the maximum value of a volume flow interval .DELTA.Q _i the minimum value of the next higher volume flow interval .DELTA.Q _{i + 1} or wherein the minimum value of a volume flow intervals AQ _i corresponds to the maximum value of the next lower volume flow interval .DELTA.Q _i-1 . The volume flow intervals ΔQ ₁ ,..., ΔQ _n thus lie without gaps. Of course, for a mathematically exact interval definition these values may only be assigned to one of the intervals.

.... .DELTA.Q _n partial pressure curve according to the invention for each flow intervals .DELTA.Q ₁ is fixed. The number n of volumetric flow intervals ΔQ ₁ ,..., ΔQ _n or the corresponding number of partial pressure curves can basically be chosen freely. In order to ensure a good adaptation of the outlet pressure of the pumping station 1 to the volume flow-dependent pressure losses of the hydraulic system, at least 6 or 8 volume flow intervals ΔQ ₁ ,..., ΔQ _n should be used. However, the method can also be executed if only 4 volume flow intervals ΔQ ₁ ,..., ΔQ _n are used. It goes without saying that the more volume flow intervals ΔQ ₁ ,..., ΔQ _n are used, the more accurate is the adaptation of the control curve to the volume flow-dependent pressure losses of the hydraulic system. Furthermore, in the case of larger pumping stations 1, ie those with more powerful pumps 17 or more than 2 pumps 17, which also correspondingly cover a larger volume flow range, the number n of volumetric flow intervals ΔQ ₁ ,..., ΔQ _n can be selected to be greater than in FIG the FIGS. 1 and 2 For example, 20 or 30 volume flow intervals ΔQ ₁ ,..., ΔQ _{n may also} make sense.

According to one embodiment variant, the volume flow intervals ΔQ ₁ ,... ΔQ _{n can} already be established before the method according to the invention is carried out. For example, the volume flow intervals have a width of 0.5 m ³ / h to 3 m ³ / h, in particular 1 m ³ / h. However, the definition can also be made by the definition of the number n, in which case, according to the volume flow range 0 ... Q _max which can be conveyed by the pumping station 1, is subdivided into this number n volume flow intervals ΔQ ₁ , ...., ΔQ _n . suitably The volume flow intervals ΔQ ₁ , ..., ΔQ _n then have a substantially equal width, whereby the subdivision is simplified.

However, it is not absolutely necessary that the volume flow intervals ΔQ ₁ ,..., ΔQ _n all have a substantially equal width. For example, a division can be made every 1m ³ / h, with the last interval ending at Q _max and narrower than 1m ³ / h. Alternatively, it can be provided that there are more intervals in the partial load range than in the full load or low load range. The interval width is then correspondingly smaller in the partial load range, so that a more accurate adaptation to the actual duck losses in the hydraulic network is possible here. Thus, alternatively or in combination with the determination of the number n, also the limit values and thus the positions of the volume flow intervals ΔQ ₁ ,..., ΔQ _{n can} already be determined before the method according to the invention is carried out.

According to another embodiment variant, the volume flow intervals ΔQ ₁ ,..., ΔQ _{n can be defined} during the method according to the invention, ie dynamically during operation, as a function of the determined pressure and volumetric flow values. The definition may relate to the number n and / or the width of the volume flow intervals ΔQ ₁ ,..., ΔQ _n . Thus, the volumetric flow range 0... Q _max which can be conveyed by the pumping station 1 can be subdivided into the number n of volumetric flow intervals ΔQ ₁ ,..., ΔQ _{n as a} function of the determined pressure and volumetric flow values. This can be done, for example, on the basis of the volume-flow-related density of the data tuples, ie on the basis of the number of pressure values occurring in a certain volume flow range. Thus, for example, a volume flow range in which data tuples pile up, narrower volume flow intervals, ie more volume flow intervals, can be used than in another volume flow range of the same width, in which there are fewer data tuples. In this way, a demand-dependent fine adjustment of the control curve is automatically performed. It is particularly simple to choose the width of the volume flow intervals ΔQ ₁ ,..., ΔQ _n to include the same or substantially the same number of data tuples.

The volume flow data intervals ΔQd ₁ ,... ΔQd _n are likewise closed subregions of the volume flow range O... Q _max , which can be conveyed by the pumping station 1. With regard to their definition and width, what has previously been said about volume flow intervals ΔQ ₁ ,..., ΔQ _n applies. They are thus also limited in each case downward by a minimum value and upwards by a maximum value. The volume flow data intervals ΔQd ₁ ,..., ΔQd _n form a type of data container for the assignment of the data tuples or the calculated pressure losses Δp _{i, j} to a volume flow range. Each volume flow data interval ΔQd _i correlates with a volume flow interval ΔQ _i . This means that each volume flow data interval ΔQd _{i is assigned to} one of the volume flow intervals ΔQ _i . In the simplest case, the volume flow intervals ΔQ _i , .... ΔQ _{n are} congruent with the volume flow data intervals ΔQd ₁ ,..., ΔQd _n . This is in the examples in the FIGS. 5 to 9 the case. Alternatively, the volume flow intervals ΔQ ₁ ,..., ΔQ _n can also be offset from the volume flow data intervals ΔQd ₁ ,..., ΔQd _n . This is for example in the example in FIG. 11 the case which will be described later. Here, the partial pressure curves (the volume flow intervals ΔQ ₁ ,..., ΔQ _n ) are offset relative to the data containers (the volume flow data intervals ΔQd ₁ ,..., ΔQd _n ) so that the definition of the pressure curves does not take place for the same volume flow intervals the assignment of the data tuple or the pressure losses takes place.

Based on the calculated volumenstromdateninterverall-related pressure drop Dp _{i, j,} for each flow data interval ΔQd _i from the, in particular the totality of this flow data interval ΔQd _i associated pressure losses (n) Dp _{i, j} a representative value Dp _{rep, i} are determined that a Represents pressure loss for the respective volume flow data interval or for the volume flow range covering the volume flow data interval. The representative value Δp _{rep, i} combines the pressure losses directly or indirectly associated with a volume flow data interval into a representative value.

The representative value Δp _{rep, i} can be, for example, the maximum value of the pressure losses Δp _{i, j} assigned to the corresponding volume flow data interval ΔQd ₁ ,..., ΔQd _n . Accordingly _, the largest value is to be filtered out of the associated pressure losses Δp _{i, j} . Alternatively, the representative value Δp _{rep, i may be} the arithmetic mean or a quantile in the range from 75% to 95% of the total of the pressure losses Δp _{i, j} assigned to the corresponding volume flow data interval ΔQd ₁ ,..., ΔQd _n . The quantile ensures that outliers in the calculated pressure drops upwards are not taken into account when determining the representative value, so that too high pressures are avoided by the pumping station and energy is thus saved. The formation of the arithmetic mean of the associated pressure loss values of a volume flow interval results in both up and down deviations being compensated or averaged.

FIG. 6 FIG. 12 illustrates the result of determining a representation value Δp _{rep, 1} , Δp _{rep, 2} , Δp _{rep, 3} ,... Δp _{rep, n} for each of the volume flow data intervals ΔQd ₁ ,..., ΔQd _n , in which case the quantity of one respective volume flow data interval ΔQd _i associated pressure losses .DELTA.p _{i, j in} each case the maximum is taken. These representational values Δp _{rep, i} thus _mean that there is no higher pressure loss for the corresponding volume flow interval, or at least during the previous period of time, there was no detection of the pressure and volume flow values.

In an advantageous development, all the representative values Δp _{rep, 1} ... Δp _{rep, n} can then be added to a common default pressure value p _set . This default pressure value p _set can correspond to that pressure which one would like to have at least at a removal point 3, also called comfort pressure in jargon. Since the representation values Δp _{rep, i} indicate the maximum pressure loss in the respective volume flow data interval ΔQd ₁ ,..., ΔQd _n , this comfort pressure is also reached at all extraction points 3 at each flow rate. This addition results in an interval-related desired pressure for the pumping station 1, which must at least be achieved for the corresponding volume flow interval in order to ensure the comfort pressure.

Included in this basic idea is also a variant in which the determination of the representative values Δp _{rep, i} and the addition of the default pressure value p _{set are} temporally reversed. Thus, according to an alternative embodiment variant, first of all the pressure losses Ap _{i, j are added to} the common preset pressure value p _set and then the respective representative value Δp _{rep , i} can be determined.

By adding the default pressure value p _set , the representative values Δp _{rep, i} in FIG. 6 raised by p _set . The result of this increase can FIG. 7 be removed. The raised representative values Δp _{rep, i} can now be used to define the partial pressure curves.

According to one embodiment, the partial pressure curves p _{soll, 1} (Q), ... p _{soll, n} (Q) may be constant pressure curves. In this case, each pressure curve p _{soll, i} (Q) is determined by a constant target pressure. This variant is in FIG. 7 illustrated. Which _will from all of the partial pressure curves _{p, 1} (Q), ... _{p, is to} control curve formed p _n (Q) _to (Q) is then discontinuous. It has at the interval limits, ie in the transition from one partial pressure curve to the next one jump.

If the representation values Δp _{rep, i have been determined} from the sum of the pressure losses Δp _{i, j} and the default value p _set , the constant desired pressure of the corresponding pressure curve p _{soll, i} (Q) can directly correspond to the representative value Δp _{rep, i} of the volume flow data interval ΔQd _i for which the corresponding partial pressure curve p _{soll, i} (Q) is at least partially defined. If the default value p _set is not yet taken into account in the representative values Δp _{rep, i} , the constant desired pressure of the corresponding pressure curve p _{soll, i} (Q) may alternatively be the sum of the default pressure value p _set and the representative value Δp _{rep, i} of the volume flow data interval ΔQd _i , for which the corresponding partial pressure curve p _{soll, i is} at least partially defined. Just this second possibility shows FIG. 7 in which the partial pressure curves p _{soll, 1} (Q), ... p _{soll, n} (Q) are defined by the sum of the common default value p _set and the corresponding representative value Δp _{rep, i of} the respective volume flow data interval ΔQd _i . Since the volume flow data intervals ΔQd ₁ ,..., ΔQd _n in FIG. 7 coincide with the volume flow intervals ΔQ ₁ , ..., ΔQ _n , the definition of the partial pressure curves p _{soll, 1} (Q), ... p set _{, n} (Q) takes place here not only partially for a respective volume flow data interval ΔQd _i Completely. If the volume flow data intervals ΔQd ₁ ,..., ΔQd _{n were} shifted to the volume flow intervals ΔQ ₁ ,..., ΔQ _n , this would not be the same as in FIG. 11 the case is.

According to another embodiment, the partial pressure curves p _{soll, 1} (Q), ... p _{soll, n} (Q) may be proportional pressure curves. In this case, each partial pressure curve p _{soll, i} (Q) is determined by a nominal pressure p _soll (Q) rising linearly with the volume flow Q. This variant is in FIGS. 8 and 9 illustrated. Which _will from all of the partial pressure curves _{p, 1} (Q), ... _{p, is to} control curve formed p _n (Q) _to (Q) is then steadily. However, it has a kink at the interval boundaries, a partial pressure curve p _{soll, i} (Q) to the next p _{soll, i + 1} (Q).

FIG. 8 shows that for a volume flow data interval ΔQd _i determined and fixed representative value Δp _{rep, i} compared to a partial constant pressure curve only the target pressure at the beginning of the determined for this volume flow data interval AQd _i partial pressure curve p _{soll, i} (Q) defined. In contrast, the representative value Δp _{rep, i + 1} determined and set for the next volume flow data interval ΔQd _{i + 1} determines the setpoint pressure at the end of this partial pressure curve p _{soll, i} (Q). The partial pressure curve p _{soll, i} (Q) is then defined by the line between the two representative values Δp _{rep, i} and Δp _{rep, i + 1} . There FIG. 8 on FIG. 5 However, it still lacks the added default pressure value p _set . This one is in FIG. 9 considered.

If, therefore, the representation values Δp _{rep, i have been determined} from the sum of the pressure losses Δp _{i, j} and the default value p _set , the desired linear pressure curve p _{soll, i} (Q) can be formed such that it differs from that represented by Representative value Δp _{rep, i} of the volume flow data interval ΔQd _i , for which the corresponding partial pressure curve p _{soll, i} (Q) is at least partially defined, formed first pressure value, by the representative value Δp _{rep, i + 1 of} the next volume flow data interval ΔQd _{i + 1} formed second pressure value increases or decreases. If the default value p _set but not yet in the Representative values Δp _{rep, i is} considered, as in FIG. 9 - The linear target pressure of the corresponding pressure curve p _{soll, i} (Q) may alternatively be formed so that of the by the sum of the default pressure value p _set and the representative value .DELTA.p _{rep, i} that volume flow data interval .DELTA.Qd _i , for which the corresponding partial pressure curve p _{should, i} (Q) is at least partially defined, formed first pressure value to the second pressure value formed by the sum of the default pressure value p _set and the representative value Δp _{i + 1 of} the next following flow data interval ΔQd _{i + 1} increases or decreases.

bestimmt werden oder sein, wobei
p_soll,i der volumenstromabhängige Druck-Sollwert für das i-te Volumenstromintervall,

Q

der Volumenstrom,

p_set

der Vorgabedruckwert,

Δ_prep,l

der Repräsentanzwert für das i-te Volumenstromdatenintervall,

Δp_rep,i+1

der Repräsentanzwert für das (i+1)-te Volumenstromdatenintervall,

ΔQ_i,max

der Maximalwert (Endwert) des Volumenstroms im i-ten Volumenstromintervall ist.

ΔQ_i,min

der Minimalwert (Anfangswert) des Volumenstroms im i-ten Volumenstromintervall ist.

Preferably, the partial proportional pressure curve for the i-th volume flow interval ΔQ _i according to the equation: $${\mathrm{p}}_{\mathrm{should}.\mathrm{i}}\left(\mathrm{Q}\right)={\mathrm{p}}_{\mathrm{set}}+{\mathrm{\Delta }}_{\mathrm{prep}.\mathrm{i}}+\left({\mathrm{Ap}}_{\mathrm{prep}.\mathrm{i}+\mathrm{1}}-{\mathrm{Ap}}_{\mathrm{rep}.\mathrm{i}}\right)/\left({\mathrm{.DELTA.Q}}_{\mathrm{i}.\mathrm{Max}}-{\mathrm{.DELTA.Q}}_{\mathrm{i}.\min }\right)\cdot \left(\mathrm{Q}-{\mathrm{Q}}_{\mathrm{i}.\min }\right)$$

be determined or be, where
p _{soll, i is} the volumetric flow-dependent pressure setpoint for the ith volumetric flow interval,

Q

the volume flow,

p _set

the default pressure value,

Δ _{prep, l}

the representation value for the ith volume flow data interval,

Δp _{rep, i + 1}

the representative value for the (i + 1) th volume flow data interval,

ΔQ _{i, max}

is the maximum value (end value) of the volume flow in the ith flow interval.

ΔQ _{i, min}

is the minimum value (initial value) of the volumetric flow in the ith volumetric flow interval.

Based on this mathematical relationship, the output pressure p _out = p _{soll, i} (Q) of the pump device 1 can be set for all volume flow intervals in a simple manner as a function of the volume flow Q.

According to yet another embodiment variant, a part of the partial pressure curves p _{soll, 1} (Q), ... p _{soll, n} (Q) constant pressure curves and the remaining part Be proportional pressure curves. Such a mixed variant is in FIG. 11 in which the first and last partial pressure curves are pressure curves p _{soll, 1} (Q), p _{soll, n} (Q) constant pressure curves and the partial pressure curves P _{soll, 2} (Q), ..., P _{shall, n-1} (Q) are proportional pressure curves.

Optionally, the case may occur that the pump station 1 is operated over the period of detection of the pressure and flow values in all airflow ranges, so not present _n values for all volume flow data intervals ΔQd _1, .... ΔQd. Preferably, in the case that one of the flow rate data intervals ΔQd _i no data tuples or no pressure drop Ap (t _v), .DELTA.p _k (t _v) has been allocated as a representative value Ap _{rep, i} for this flow data interval ΔQd _i of representation value Dp _{rep, i -1} , Δp _{rep, i + 1 of} the preceding or succeeding volume flow data interval ΔQd _i-1 , ΔQd _{i + 1} . This ensures that the control curve for the entire volumetric flow range of the pumping station 1 can be defined.

FIG. 10 ₁ illustrates an embodiment variant in which the representative values Δp _{rep, 1} ,... Δp _{rep, n are} not assigned to the beginning of the volume flow data intervals ΔQd ₁ ,..., ΔQd _n , but approximately to the middle. This leads to the definition of the partial pressure curves p _{soll, 1} (Q),... P _{soll, n} (Q) overflowing the volume flow data intervals ΔQd ₁ ,..., ΔQd _n . They each run from the middle of one volume flow data interval AQd _i to the middle of the next volume flow data interval ΔQd _{i + 1} . The volume flow intervals ΔQ ₁ ,..., ΔQ _n thus have the same width as the volume flow data intervals ΔQd ₁ ,..., ΔQd _n , but they are offset by half their width. This is in FIG. 11 representing the course of the final partial pressure curves p _{soll, 1} (Q), ... p _{soll, n} (Q).

At the in FIG. 11 illustrated variant, the first volume flow interval .DELTA.Q _{1 has} only half the width of the other volume flow intervals .DELTA.Q ₂ , ..., .DELTA.Q _n . This shows that not all volumetric flow intervals ΔQ ₁ ,..., ΔQ _n must have the same width.

At the in FIG. 11 illustrated embodiment variant is further noted that for the first volume flow interval .DELTA.Q ₁ a partial constant pressure curve is defined whose setpoint is defined by the representation of the first volume flow interval .DELTA.Q _{1 representative} value .DELTA.p _{rep, 1} . In contrast, partial proportional pressure curves are defined for the other volume flow intervals ΔQ ₂ ,..., ΔQ _n . This shows that not all partial pressure curves need to have the same order.

It should also be noted that the maximum pump curve M limits the operating range of the pumping station 1. Thus, no operating points beyond this pump curve M can be achieved. The pump curve M thus superimposed on the control curve p _set (Q) in the or the last flow interval (s) such that the operating points on the .DELTA.Q to last or optionally also the penultimate flow interval _n formed partial pressure curve p _{soll, n} (Q), the other side the maximum pump curve M would be on the maximum pump curve M lie.

FIGS. 3a and 3b now show a graphic representation of a first and second process sequence according to the invention in its basic steps. In a first step 11, the determination of data tuples from pressure and volume flow values takes place in both variants. In the first procedure in FIG. 3a Then, in step 12a, the assignment of the data tuples to a volume flow data interval follows, followed by the calculation of a pressure loss for each data tuple in step 13a. These two steps are in the second procedure in FIG. 3b reversed, in which case in step 12a first the calculation of a pressure loss for each data tuple takes place and then in step 13a these pressure losses are each assigned to a volume flow data interval. The subsequent steps 14, 15, 16 are the same again for both variants. A representative value for each volume flow data interval is determined from the calculated pressure losses, step 14. From each representative value, a partial pressure curve is defined for each volume flow interval correlated with the corresponding volume flow data interval, step 15, followed by control of the pumping station along the line joins partial pressure curves formed, step 16. The process is then repeated. After step 16, it continues at step 11 and thus the defined Control curve dynamic, especially adapted again and again. The formation of the partial pressure curves can be described as before. The partial pressure curves may be constant pressure curves, or proportional pressure curves or, in part, constant pressure curves and, on the other hand, proportional pressure curves.

The method according to the invention can, according to a variant, be carried out as part of a commissioning procedure immediately after the installation of the pumping station 1. If the method is started, only one of the removal points 3 and / or two or more, in particular all removal points 3, has to be opened simultaneously one after the other. At least the bad points should be included. This has the advantage that pressure and volume flow values can be recorded in a short time for the entire volume flow range of pumping station 1 that can be conveyed. Subsequently, the data acquisition, step 11, can be ended and the evaluation, steps 12 to 15, started.

Alternatively, the method according to the invention can be carried out independently of the installation of the pumping station 1 as part of its intended operation. Although this requires a longer period of time, until a sufficient number of pressure and volume flow values are recorded. However, it eliminates the commissioning procedure for data collection. In both variants, the pumping station can first be regulated according to a constant over the entire volume flow pressure curve.

LIST OF REFERENCE NUMBERS

1

pump station

2

local supply line

3

Consumer, sampling point

4

Output of the pumping station with pressure sensor

5, 5a, 5b

System location with pressure sensor

6

Flow Sensor

7

Control and regulation unit

8th

pressure line

9

central supply line

10

building

11

Step in operating value recording

12a

Step Data tuple mapping

12b

Step pressure loss calculation

13a

Step pressure loss calculation

13b

Step pressure loss allocation

14

Step representation value determination

15

Step formation of the partial pressure curves

16

Step Control of the pumping station based on partial pressure curves

17

supply

18

pump

Claims (18)

Method for controlling a pumping station (1) in a hydraulic network which pressurizes a medium to be conveyed to at least one consumer (3), the pressure being adjusted in dependence on the volume flow (Q) by the pumping station (1) according to a control curve , characterized in that the control curve is formed of a plurality of partial pressure curves (p set _{, 1} (Q), ..., p set _{, n} (Q)), each for a volume flow interval (ΔQ ₁ , ..., ΔQ _n ) one of the plurality of corresponding number (s) of seamlessly adjacent volume flow intervals (ΔQ ₁ ,..., ΔQ _n ) are defined on the basis of determined pressure and volume flow values of the network to be evaluated at intervals. A method according to claim 1, characterized in that the pressure and volume flow values comprise data tuples having at least the following values associated with each other: a system pressure value (p _sys (t _v ), p _{sys, k} (t _v )) of the system pressure (p _sys, p _{sys, k} ) applied to a system location (5, 5 a, 5 _b ) and - A volume flow value (Q (t _v )) of the flowing volume flow (Q). A method according to claim 2, characterized in that the data tuples further comprise an output pressure (p _out (t _v)) of the output of the pump station (1) currently applied output pressure (p _out). Method according to Claim 2 or 3, characterized in that the data tuples are each assigned, based on their respective volume flow value (Q (t _v )), to a volume flow data interval (ΔQd _i ) which correlates with one of the volume flow intervals (ΔQ _i ) and from the system pressure value (p _sys (t _v ), p _{sys, k} (t _v )) and an output _{pressure set} point (p _booster ) of the pumping station (1) or the determined output pressure value (p _out (t _v )) of each data tuple Difference formation a pressure loss (Δp _{i, j} ) from the output of the pumping station (1) to the system location (5, 5a, 5b) is determined. A method according to claim 2 or 3, characterized in that from the system pressure value (p _sys (t _v ), p _{sys, k} (t _v )) and an output _setpoint (p _booster ) of the pumping station (1) or determine the output pressure value (p _out (t _v )) of each data tuple a difference in pressure (Δp _{i, j} ) from the output of the pumping station (1) to the system location (5, 5a, 5b) is determined, and that this pressure loss (.DELTA.P _{i, j} ) based Volume flow value (Q (t _v )) of the respective data tuple is associated with a volume flow data interval (ΔQd _i ), which correlates with one of the flow rate intervals (ΔQ _j ). A method according to claim 4 or 5, characterized in that for each volume flow data interval (ΔQd _i ) from the, in particular the entirety of the volume flow data interval (ΔQd _i ) associated pressure losses (Δp _{i, j} ), a representation value (Δp _{rep, i} ) is determined. A method according to claim 6, characterized in that all representative values (Δp _{rep, i} ) a common default pressure value (p _set ) is added or that the pressure losses (Δp (t _v ), Δp _k (t _v )) first a common default pressure value (p _set ) is added and then the respective representative value (Δp _{rep, i} ) is determined. The method of claim 6 or 7, characterized in that in the event that one of the flow rate data intervals (ΔQd _i) no data tuples or no pressure drop (.DELTA.p (t _v), .DELTA.p _k (t _v)) has been assigned, (as a representative value Ap _{rep, i} ) for this volume flow data interval (ΔQd _i ) the representative value (Δp _{rep, i-1} , Δp _{rep, i + 1} ) of the previous or subsequent volume flow data interval (ΔQd _i-1 , ΔQd _{i + 1} ) is used. Method according to claim 7 or 8, characterized in that one, several or all partial pressure curves (p set _{, 1} (Q), ... p set _{, n} (Q)) are constant-pressure curves, the setpoint pressure of which is in each case the representation value (Δp _{rep, i} ) or the sum of the default pressure value (p _set ) and the representative value (Δp _{rep, i} ) of the volume flow data interval (ΔQd _i ) for which the corresponding partial pressure curve (p _{soll, i} ) is at least partially defined. Method according to claim 7, 8 or 9, characterized in that one, several or all partial pressure curves (p set _{, 1} (Q), ... p set _{, n} (Q)) are proportional pressure curves, the target pressure of each of which by the representative value (Δp _i ) or the sum of the default pressure value (p _set ) and the representative value (Δp _{rep, i} ) of the volume flow data interval (ΔQd _i ) for which the corresponding partial pressure curve (p _{soll, i} (Q)) is at least partially is defined, formed first pressure value to which the representation value (Δp _{i + 1} ) or the sum of the default pressure value (p _set ) and the representative value (Δp _{i + 1} ) of the next volume flow data interval (ΔQd _i ) formed second pressure value increases or drops. Method according to one of Claims 6 to 10, characterized in that the representative value (Δp _{rep, i} ) is the maximum value, the arithmetic mean or a quantile in the range from 75% to 95% of the total of the corresponding volume flow data interval (ΔQd ₁ , .. ., ΔQd _n ) associated pressure losses (Δp _{i, j} ). Method according to one of the preceding claims, characterized in that the volume flow intervals (ΔQ ₁ , ..., ΔQ _n ) have a substantially equal width. Method according to one of the preceding claims, characterized in that the volumetric flow range (0 ... Q _max ) which can be conveyed by the pumping station (1) is converted into the number (n) of volume flow intervals (ΔQ ₁ , ΔQ _n ) as a function of the determined pressure and volumetric flow values ) is divided. Method according to one of claims 4 to 13, characterized in that the volume flow intervals (ΔQ ₁ , ..., ΔQ _n ) are congruent with the volume flow data intervals (ΔQd ₁ , ..., ΔQd _n ) or are offset therefrom. Method according to one of the preceding claims, characterized in that it is determined during operation of the pumping station (1) when the Volume flow (Q) is greater than zero, and that only in this case, the pressure value or values (p _sys (t _v ), p _{sys, k} (t _v ), p _from (t _v )) and the volume flow value (Q (t _v )) be determined. Method according to one of the preceding claims, characterized in that it is determined during operation of the pumping station (1), when the change of the volume flow (Q) for a period of time is substantially constant, and that only in this case, the pressure value or values (p _sys (t _v), p _{sys, k} (t _v), p _from (t _v)) and the flow rate value) are recorded (Q _(v t). Method according to one of claims 2 to 16, characterized in that the system pressure (p _sys (t _v ), p _{sys, k} (t _v )) at a hydraulically furthest from the pumping station (1) remote removal point (5, 5a, 5b) and / or at the end of a supply line (2) is determined. System for controlling a pumping station (1) in a hydraulic network, with which a medium to be conveyed to at least one consumer (3) can be pressurized, the pressure being adjustable in accordance with the volume flow through the pumping station (Q) according to a control curve, characterized in that the system is arranged to form the control curve from a plurality of partial pressure curves (p _{soll, 1} (Q), ... p _{soll, n} (Q)), and these partial pressure curves (p _{soll, 1} ( Q), ... p _{soll, n} (Q)) in each case for a volume flow interval (ΔQ ₁ ,..., ΔQ _n ) of one of the plurality of corresponding number (n) of seamlessly adjoining volume flow intervals (ΔQ ₁ ,..., ΔQ _n ) on the basis of determined and to be evaluated interval-related pressure and volume flow values of the network.

Images