NZ618063B2 - Method for controlling at least a part of a pump station - Google Patents

Abstract

Disclosed is a method for controlling at least a part of a pump station which comprises a number of speed controlled pumps. The method is arranged to minimize the specific energy consumption Espec of the at least a part of a pump station. The method comprises a sub method (Find V3) that comprises the steps of: The input data in the form of a set of parameters corresponding to a fictitious or elapsed first operating period t1 and a fictitious or elapsed second operating period t2 is obtained. The mutual relative relationship between a first value A1 of a quantity that corresponds to a first pump speed V1 and a second value A2 of the quantity that corresponds to a second pump speed V2 is determined based on the set of parameters. A1 is derived based on the set of parameters which first value A1 relates to the first operating period t1. A2 is derived from the set of parameters which second value A2 relates to the second operating period t2. The mutual relative relationship between a first specific energy consumption Espec1 that is derived based on the set of parameters and that relates to the first operating period t1 and a second specific energy consumption Espec2 that is derived from the set of parameters and that relates to the second operating period t2 is also determined. Output data in the form of a third value A3 of the quantity corresponding to a third pump speed V3 of a third operating period t3 is determined based on the determined mutual relative relationships and on parameters B3, B4, B5, and B6 of the quantity. The operating speed of the number of speed controlled pumps in the third operating period is controlled by the determined value V3. e steps of: The input data in the form of a set of parameters corresponding to a fictitious or elapsed first operating period t1 and a fictitious or elapsed second operating period t2 is obtained. The mutual relative relationship between a first value A1 of a quantity that corresponds to a first pump speed V1 and a second value A2 of the quantity that corresponds to a second pump speed V2 is determined based on the set of parameters. A1 is derived based on the set of parameters which first value A1 relates to the first operating period t1. A2 is derived from the set of parameters which second value A2 relates to the second operating period t2. The mutual relative relationship between a first specific energy consumption Espec1 that is derived based on the set of parameters and that relates to the first operating period t1 and a second specific energy consumption Espec2 that is derived from the set of parameters and that relates to the second operating period t2 is also determined. Output data in the form of a third value A3 of the quantity corresponding to a third pump speed V3 of a third operating period t3 is determined based on the determined mutual relative relationships and on parameters B3, B4, B5, and B6 of the quantity. The operating speed of the number of speed controlled pumps in the third operating period is controlled by the determined value V3.

Description

METHOD FOR CONTROLLING AT LEAST A PART OF A PUMP STATION Technical Field of the Invention The present invention relates lly to a method for controlling at least a part of a pump station. In particular, the present invention relates to a method for controlling at least a part of a pump station comprising a number of speed controlled pumps, the method being arranged to minimize the specific energy consumption Egmc of said at least a part of a pump station.

BackgrOund of the ion and Prior Art The cost of driving the pumps of a pump station intended for waste water, sewage, surface water, etc., is very large. Long way back in time, the pump of the pump station was started at highest speed when the liquid level of the pump n had risen to a predetermined pump start liquid level, and the pump was allowed to e until a predetermined pump stop liquid level had been reached, but it was realized that this way of controlling was very expensive. As a solution, speed controlled pumps were introduced, for instance frequency controlled pumps wherein the current feed frequency to the pump was selected to a, from an energy consumption point—of—view, more l value ined via, for instance, calculations and/or tests.

These calculations and/or tests resulted in miscellaneous, system dependent and/or pump dependent, curve charts from which the energy consumption per pumped volume in relation to, for instance, the current feed frequency or pump speed of the pump can be derived, said optimal value being a derived minimum point. The uction of speed controlled pumps and utilization of optimum current feed frequency/pump speed based on the nominal curve chart of the pump entailed significant cost savings, as well as spared the pumps since they rarely or never were operated at maximum speed. r, speed l based on the nominal curve chart of a pump is impaired by certain disadvantages. It is a disadvantage that the curve chart of a pump model is not necessarily exactly the same for each pump entity within this pump model; furthermore, the l curve chart of the pump model is static over time, which is not true for the real curve chart of the specific pump entity. More precisely, the real curve chart of the pump entity will be changed concurrently with the parts of the pump being worn, which entails that the m current feed ncy/pump speed of the pump entity does not coincide with the optimum current feed frequency/pump speed of the pump model. In addition, the design of the pump station and the surrounding pipe system will make effect on the real curve chart of the pump entity, which effect may be difficult or impossible to anticipate and/or calculate.

Today, there are devices that e pumped liquid volume and energy consumption at specific current feed frequencies/pump speeds, see, for instance, WOZOO9/053923. r, it is expensive and cated to measure pumped liquid volume and there is a need of extra equipment intended only for the purpose of measuring pumped liquid volume.

Brief Description of Objects and Features of the Invention The present invention aims at obviating the above- mentioned disadvantages and failings of previously known methods for controlling at least a part of a pump station and at providing an improved method. A primary object of the invention is to provide an improved method for controlling at least a part of a pump station of the initially defined type, which does not require that the pumped liquid volume needs to be measured.

Another object of the present invention is to provide a method for controlling at least a part of a pump station, which is self—regulating concurrently with the parts of the pump being worn and replaced, as well as is self—regulating based on the design of the pump station and the surrounding pipes.

Another object of the present invention is to provide a method that in a preferred embodiment indirectly takes the size of the pumped volume into consideration without measuring the same.

Brief Description of the Features of the Invention According to the invention, there is provided a method for controlling at least a part of a pump station sing a number of speed controlled pumps, the method being arranged to minimize the specific energy consumption Eflmc of said at least a part of a pump n, wherein said method comprises a sub method comprising the steps of * obtaining input data in the form of a set of parameters corresponding to a fictitious or d first operating period t1 and a fictitious or elapsed second operating period t2, * determining, based on said set of parameters, the mutual relative relationship between a first value A1 of a quantity that corresponds to a first pump speed V1 and that is derived based on said set of parameters, which first value Al relates to said first operating period t1, and a second value A2 of said quantity that corresponds to a second pump speed V2 and that this derived from said set of parameters, which second value A2 relates to said second operating period t2, and between a first specific energy consumption Egmcl that is derived based on said set of parameters and that relates to said first ing period t1, and a second ic energy consumption Eflmcz that is derived from said set of parameters and that relates to said second operating period t2, * determining, based on said determined mutual ve relationships and on parameters B3, B4, B5, and 36 of said ty, output data in the form of a third value A3 of said quantity corresponding to a third pump speed V3 of a third operating period t3, wherein A3 is set equal to A2—B3 if the ions A2<A1 and Esmm2<E$mcl are satisfied, A3 is set equal to A2+B4 if the conditions A2>Al and Eflmc2<Eqmcl are satisfied, A3 is set equal to A2+B5 if the ions A2<A1 and Efimc2>E$mcl are satisfied, and A3 is set equal to A2—B6 if the conditions A2>Al and Esmm2>Eflmcl are satisfied, and * using the determined value V3 as the operating speed of the number of speed controlled pumps in said third operating period.

Accordingly, the present ion is based on the understanding that the sum of the pumped liquid volume during a n period of time, for instance 24 h or a multiple of 24 h, is more or less constant as seen over a longer period of time.

Preferred embodiments of the present invention are furthermore defined in the dependent claims.

Preferably, the set of parameters comprises said first value A1 of said quantity and the associated first specific energy ption Eswml, as well as said second value A2 of said quantity and the associated second specific energy consumption ESMmZ.

Preferably, the first value A1 of said quantity consists of the pump speed V1 or a first current feed frequency F1, and the second value A2 of said quantity consists of the pump speed V2 or a second current feed frequency F2, and the third value A3 of said quantity consists of the pump speed V3 or a third current feed frequency F3.

Additional advantages and features of the invention are seen in the other ent claims as well as in the following, detailed description of preferred embodiments.

Brief Description of the gs A more complete understanding of the above—mentioned and other features and advantages of the present invention will be clear from the following, detailed description of preferred embodiments, reference being made to the accompanying drawings, wherein: Fig. 1 is a schematic illustration of a pump n, Fig. 2 is a flow chart showing a preferred embodiment of the method according to the invention, Fig. 3 is a flow chart showing an alternative embodiment of the method according to the invention, Fig. 4 is a flow chart showing the sub method "Find V3", Fig. 5 is a diagram that shows schematically the relationship between specific energy consumption Fame and pump speed memr and Fig. 6 is a diagram that shows schematically how the pump station liquid level h is changed over time T.

Detailed Description of Preferred Embodiments Initially, it should be pointed out that the term "specific energy consumption E‘.Spec VI as used in the claims as well as in the ption relates to and is a measure of energy consumption per unit of time of one or more pumps, or of one or more pump stations, etc. Herein, specific energy consumption is calculated ing to Fame = k * E, wherein E is real energy consumption during a certain elapsed period of time and k is a time parameter that is a measure of said elapsed period of time, preferred ments of the determination of the time ter k is bed later in the context of ent embodiment. In the simplest embodiment, k is equal to 1.

In Figure 1, a pump station is shown, generally designated 1, comprising a number of speed controlled pumps 2, i.e., one or more and y two, arranged to pump liquid from a sump 3 included in the pump station 1 to an outlet pipe 4 and further away from the pump station 1.

Further, the pump station 1 comprises at least one level instrument 5 arranged to determine the pump station liquid level h; it should be pointed out that the level instrument may be an individual device that is ively ted to an external control unit 6, be operatively connected to one of said number of speed controlled pumps 2, be built—in in one of said number of speed controlled pumps 2, etc. Said number of speed controlled pumps 2 are preferably operatively connected to the external control unit 6 with the purpose of allowing regulation of the pump speed, alternatively at least one of said number of speed controlled pumps 2 may comprise a built-in control unit (not shown).

With the wording "speed controlled", all feasible ways to change the speed of a pump are embraced, above all current feed frequency control is intended, by means of a ncy converter, VFD, that is built-in in a pump or that is external, the al VFD preferably being arranged at the external control unit 6. However, also ally or externally controlled supply voltage control is intended, internal ical brake that preferably acts on the drive shaft of the pump, etc. Accordingly, on an overall level of the invention, it is not of central importance how the speed of the pump is controlled, only that the speed of the pump can be ted/controlled.

The method according to the ion is aimed at controlling at least a part of such a pump station 1 that comprises a number of speed controlled pumps 2, with the purpose of minimizing the specific energy ption Eamc of said at least a part of a pump station 1. Pump station 1 should in this connection be seen as a defined installation to which incoming liquid arrives and from which outgoing liquid is pumped. The pump station should, as regards the present invention, be regarded irrespective of the type of liquid and irrespective from where the liquid comes and where the liquid should be pumped. With the wording "a number of variable—speed controlled pumps", an integral number of pumps 2 is intended where the speed of the WO 73552 2012/050581 individual pump can be controlled, preferably by the fact that the current feed frequency F to each pump can be controlled with the purpose of changing the speed of the specific pump, the speed being tionate to the current feed ncy. Accordingly, such a pump station 1 may comprise one or more pumps, at least one pump 2 of which is speed controlled. In the case when the pump station comprises a plurality of speed controlled pumps 2, suitable alternation between them may be done, which is not handled herein.

Fundamental to the present invention is that the pumped liquid volume is not measured or employed in connection with the determination of specific energy consumption Eqmc. The invention is instead based on the sum of the pumped liquid volume during a certain period of time, usually 24 h, being more or less constant as seen over a longer time. In this patent application, said period of time is henceforth denominated operating period and has ably the time length n*24 h, wherein n is a positive integer. It should be realized that the operating period also may have another time length without the general idea of the present invention being deviated from, and/or that the time length of the operating period varies over the year. For instance, an operating period may be equal to one pump cycle, which comprises a period wherein the pump is active, i.e., pumps out liquid from a start level to a stop level, and a period in which the pump is inactive, i.e., when the liquid level rises from the stop level to the start level. The mutual order of the period in which the pump is active and the period in which the pump is inactive, respectively, is arbitrary.

It should be pointed out that the method according to the invention can be implemented for one or more complete pump stations, which directly or indirectly communicate with each other, for one pump or for several pumps, which directly or ctly communicate with each other. The 2012/050581 method may, for ce, be implemented in a built—in control unit in a pump 2 or in the external control unit 6 of a control cabinet, the external control unit 6 being operatively connected to the pump 2. Henceforth, the invention will be described implemented in a pump 2 of a pump station 1 if nothing else is stated, but the corresponding s when the invention is implemented in an external control unit 6.

The pump station 1 has a pump station liquid level, which is designated h and which in the present patent application is the distance between the liquid level in the sump 3 and the inlet of the pump 2 (see Figure 1), the pump n liquid level h is directly coupled to the real lifting height of the pump 2, which increases with falling pump station liquid level h. When the sump 3 is refilled with liquid, the pump station liquid level h rises, and when the pump 2 is active and pumps out liquid, the pump station liquid level h falls. It should be pointed out that the sump 3 can be ed with liquid at the same time as the pump 2 is active and pumps out liquid. hout this publication, the operating period in progress is also denominated the third operating period t3, which has been preceded by a fictitious or d first operating period t1 and a fictitious or elapsed second operating period t2. Fictitious operating periods are used when elapsed/actual operating periods have not yet occurred, for instance upon up or restart of the pump, the pump station, the register of the pump station, etc. The first operating period t1, the second operating period t2 and the 3O third operating period t3 do not necessarily need to be in immediate succession, but may be separated by one or more operating periods for which parameters have not been registered. Accordingly, when the third operating period t3 has been completed and parameters have been registered, the same will accordingly be regarded as a second operating period t2 and a new operating period is g, possibly a new third operating period t3, the previous second ing period will constitute the first operating period t1, and the previous first operating period will fall out of the register and/or possibly be filed in order to allow analysis of the progress of the pump station 1.

In Figures 2 and 3, preferred embodiments of a method are shown, lly designated 7, for controlling at least a part of a pump station 1 comprising a number of frequency controlled pumps 2. It should be pointed out that the method 7 according to the invention may be expanded with one or more sub methods, and/or be run in parallel/sequentially with other control methods. In connection with the description below, also Figure 5 should be taken into consideration, but it should be appreciated that the curve drawn into Figure 5 not necessarily is registered and is not needed for the method according to the invention.

Reference is now made to Figures 2 and 3 and to the method steps that are common to the preferred embodiments.

The method 7 starts and then a check is made if the pump station 1 is in the middle of a third operating period t3 in progress or if the third operating period t3 precisely has been completed, i.e., whether the ion T2t3 is satisfied, wherein T is an elapsed time of the operating period in progress. In connection with an operating period being completed and r one being ted, the measurement of elapsed time T of the operating period in progress is set to zero. It should be pointed out that T also may be actual or te time and in that case, instead the relationship n actual time and a multiple of the third operating period is checked, i.e., for instance, every time the actual time strikes 00:00, a new operating period starts.

When an ing period precisely has been completed, the method 7 proceeds to a sub method, called "Find V3", which aims at finding optimum pump speed V3 of the third operating period t3 that just has been started or that will be started later, with the purpose of zing the specific energy consumption Eqmc of said at least a part of a pump station 1. The sub method "Find V3" will be described more in detail below after the overall method 7 has been described.

After the sub method "Find V3" or if the pump station 1 is in the middle of the third operating period t3 in progress, i.e., if the condition T2t3 is not satisfied, the method 7 continues to the next method step "Retrieve pump station liquid level, h".

The pump station liquid level h is determined by means of some form of customary level instrument arrangement, which may comprise one or more co—operating level instruments 5, for instance uous and/or discrete level instruments. When the pump station liquid level h has been ved, a check is made if the pump station liquid level h in the sump 3 is lower than the liquid level that corresponds to a pump stop liquid level hsum, i.e., whether the condition h<h5top is ied. If the condition h<hStop is satisfied, the pump speed mep is set equal to zero and the possibly activated pump 2 is switched off, and the method 7 is terminated and returns to start. If the condition h<hsum is not satisfied, a check is made if the liquid level in the sump 3 is higher than the liquid level that corresponds to a pump start liquid level baa“, i.e., whether the condition h>hmam is satisfied. If the condition h>hstart is ied, the pump 2 is ted at a pump speed mep that is equal to the present pump speed V3 of the third operating period t3 in progress, which earlier has 3O been determined by means of the sub method "Find V3". If the condition h>hflam is not satisfied or after the pump 2 has been activated at the pump speed V3, the method 7 is terminated and returns to start according to the preferred embodiment according to Figure 2.

According to the alternative embodiment according to Figure 3, a check is made if the pump station liquid level h 2012/050581 in the sump 3 falls/decreases if the condition h>hfiam is not satisfied or after the pump 2 has been activated at the pump speed V3. If the pump station liquid level h falls, it shows that the pump 2 is active and pumps out liquid and that the liquid level in the sump 3 falls but that the pump stop liquid level hsum has not yet been reached. The method 7 is terminated and returns to start. It should be d out that the steps of checking the conditions h<hst0p and h>huam, together with the respective associated subsequent method step, can interchange place without the method in other respects being affected.

If the pump station liquid level h does not fall, a check is made if the pump is active, i.e., whether the speed prp of the pump is different from zero. If the speed mep of the pump is equal to zero, it indicates that the pump station liquid level h is between pump stop liquid level lgtw and pump start liquid level huam and that the pump station is in a refill state in the operating period, after which the method 7 is terminated and returns to start. If the speed mep of the pump is ent from zero, normally it shows that the pump 2 is active and pumps out liquid but that the instantaneous liquid inflow to the pump n 1 is equal to or greater than the liquid outflow, alternatively it is an indication of the pump 2 not at all being active, for instance as a consequence of the same being , alternatively it is an indication of the pump speed being less than a smallest possible pump speed Vmfi the pump 2 can have and still manage to pump liquid. When the pump station liquid level h does not fall, the pump speed 3O mem is increased by a parameter B1, preferably corresponding to a current feed frequency increase of 1*5 Hz, and in addition the t pump speed V3 of the third operating period t3 in ss is increased by a parameter B2, preferably corresponding to a current feed frequency increase of O,l-O,5 Hz. Next, the method 7 is terminated and returns to start.

It should be pointed out that during one and the same operating period, under normal operation, the pump 2 may be active several times. It should furthermore be d out that the pump station 1 may have a maximally allowed pump station liquid level hm”, and if this is reached, preferably the pump speed of the pump 2 is increased to a higher pump speed or to a maximally d pump speed me to prevent the sump 3 from being flooded, and if this does not help, one or more further pumps are started, preferably at said maximally allowable pump speed me, at the present pump speed V3 of the third operating period t3 in ss, or at another suitable pump speed. If the pump station 1 ses several pumps, the alternating ones may be active during one and the same operating period.

In connection with the third operating period t3 having been completed, in a preferred embodiment, the present pump speed V3 of the third operating period t3 and the present specific energy consumption Eqmc3 of the third ing period t3 are registered. In an alternative embodiment, it is registered whether the pump speed V3 is greater or smaller than the pump speed V2 of the second operating period t2 and whether the specific energy consumption Eqmc3 is greater or smaller than the ic energy consumption EQECZ of the second operating period t2. Instead of the third pump speed V3, the corresponding third value A3 of an equivalent quantity may be used in registration. The equivalent quantity may be current feed ncy, supply voltage, mechanical brake power of the drive shaft of the pump, or another corresponding equivalent quantity. It should be pointed out that if the method 7 according to the invention during a third operating period t3 in ss needs to set the pump speed mep to any value that differs from, for instance, zero and V3, preferably the parameters of this operating period should not be ered.

The sub method "Find V3" is shown in Figure 4 and begins with the step of obtaining/retrieving input data in the form of a set of parameters, this set of parameters may be set parameters corresponding to two fictitious operating periods, registered parameters corresponding to two d operating periods, or a combination of set parameters corresponding to a fictitious operating period and registered parameters corresponding to an elapsed operating period. Parameters set by operator/pump manufacturers/programmers are, for instance, used in the initial actual operating periods of the pump station 1, until ered parameters are available.

Based on said set of parameters, the mutual relative relationship is then determined n a first value A1 of said quantity that corresponds to a first pump speed V1 and that is derived based on said set of parameters, which first value A1 relates to a ious or elapsed first operating period t1, and a second value A2 of said quantity that corresponds to a second pump speed V2 and that is derived from said set of parameters, which second value A2 relates to a fictitious or d second operating period t2, and between a first specific energy consumption Efimcl that is derived based on said set of parameters and that relates to said first ing period t1, and a second specific energy ption Eqmc2 that is derived from said set of parameters and that relates to said second operating period t2.

Based on said determined mutual relative relationships, output data is then determined in the form of a third value A3 of said quantity corresponding to a third pump speed V3 of a third operating period t3, which may be the operating period directly following the second operating period t2 or may be a coming operating period. The third value A3 of the quantity is set equal to A2—B3 if the conditions A2<A1 and Eflwc2<Eflmcl are satisfied, equal to A2+B4 if the conditions A2>Al and Eflmc2<Eqmcl are satisfied, equal to A2+B5 if the ions A2<Al and Eqmc2>Eflmcl are satisfied, and equal to A2—B6 if the conditions A2>A1 and Exmcl are satisfied, wherein B3, B4, B5, and B6 are parameters of said quantity.

Next, the sub method "Find V3" returns to the method 7.

The parameters B3, B4, B5, and B6, each of which constitutes the difference n the third value A3 and the second value A2, are preferably predetermined , alternatively variables that, for instance, depend on the value of A2, the relationship n A1 and A2, and/or the relationship between Eflmcl and Eqmc2, etc. The parameters B3, B4, B5, and B6 have preferably the same value, but it is feasible that the parameters B3, B4, B5, and B6 have ent values with the purpose of preventing the sub method "Find V3" from jumping to and fro between two values around an optimum pump speed. In an alternative embodiment, the ter B3 is equal to B5, which is different from B4, which in turn is equal to B6. Each of the parameters B3, B4, BS, and B6 corresponds preferably to a current feed frequency change that is r than 0,5 Hz, and smaller than 5 Hz, preferably smaller than 2 Hz, and most preferably 1 Hz. Preferably, a current feed frequency change of 1 Hz corresponds to approximately a change of the pump speed of 2—5 percentage units, where the lly allowable pump speed me is used as the reference point 100 %. It is furthermore preferred that the parameters B3, B4, BS, and B6 are reduced, for instance halved or divided into three, if it turns out that the sub method "Find V3" jumps to and fro around an optimum pump speed. It should be d out that the above—mentioned parameter B2, when it is shown in the same quantity as the parameters BB, B4, BS, and B6, should be small in relation to B3, B4, B5, and B6, for instance in the order of less than 15 % of B3, B4, B5, and/or B6.

In preferred embodiments, the first value A1 of said quantity consists of the pump speed V1, a first current feed frequency F1, or a first supply voltage 81, and the second value A2 of said quantity consists of the pump speed V2, a second current feed frequency F2, or a second supply voltage 82, and the third value A3 of said quantity consists of the pump speed V3, a third current feed frequency F3, or a third supply voltage $3.

In a preferred embodiment, the above—mentioned set of parameters comprises said first value A1 of said quantity and the associated first specific energy consumption Eflmcl, as well as said second value A2 of said quantity and the associated second specific energy consumption Eqmc2. In an alternative embodiment, the set of parameters comprises, for instance, said second value A2 as well as the function of the curve segment that extends between the second value A2 and the first value Al, after which the mentioned mutual relative relationships can be determined. In an additional alternative embodiment, the set of ters comprises the second value A2 and the first value A1, as well as the slope of the curve segment that extends between the two values of the ty, after which the above— mentioned mutual relative relationships can be determined.

It should be pointed out that there are further sets of parameters from which it is possible to determine the above— mentioned mutual relative relationships, even if not more embodiment examples are shown here. It should be pointed out that values from additional ious or elapsed operating s may be used to check if the sub method "Find V3" jumps to and fro around an optimum pump speed.

Below, different ways to calculate the specific energy consumption Espec will be presented, more precisely how the time parameter k of the above-mentioned sion of the specific energy consumption Eflmc=k*E is calculated. ESpec is essentially equal to consumed energy divided by pumped volume during a n elapsed time, or equal to taneous power consumption divided by instantaneous flow. According to the invention, a time parameter k is used instead of instantaneous flow or pumped volume, and this time parameter may be equal to 1 or make allowance for the time length of the operating period, the vertical height between the pump start liquid level hflam and the pump stop liquid level hgmp, the number of starts during an operating period, the time the pump has been active during an operating period, the time the pump has been inactive during an operating period, the speed of the liquid level, etc.

Below, some examples will be shown, but the invention is not limited thereto.

According to a first variant, the length of an operating period is n*24 h and the time parameter k is calculated according to k=1/(n*24). This t is used when the inflow is predictable and almost constant for an ing period as seen over a longer period of time.

According to a second variant, the length of an operating period is n*24 h and the time parameter k is calculated according to k=1/(c*(n*24)), wherein c is an equalization parameter. This variant is used when the inflow is less table and more irregular for an operating period as seen over a longer period of time.

Preferably, the equalization parameter c may be calculated according to c=xm/Ztmu wherein xm,is the number of times a pump has been ted during an elapsed operating period, and Ztmxis the cumulative time for which the pump has been active in the d operating period.

Alternatively, the equalization parameter c may be calculated according to c=ZL/2tm, wherein L is the vertical height between the pump start liquid level hfla“ and the pump stop liquid level hsmp and EL is the cumulative height that has been pumped out during an elapsed operating period, regardless the inflow when the pump 2 has been active. 2ton is the cumulative time for which the pump has been active in the d operating period.

According to a third variant, the length of an operating period is 5 seconds, wherein s is a ve r and the time parameter k is calculated according to k=l/(c*s), n c is the equalization parameter. See Figure 6, wherein Atmlis equal to Atofi, each of which is equal to the length of the operating period, 5 seconds.

WO 73552 Preferably, the length 5 seconds of the operating period is in the range of 60—120 s.

The equalization parameter c is preferably calculated according to c=(Ahw1+ Ahofi), wherein Ahmxis the pump station liquid level change during an elapsed operating period, which elapsed operating period takes place in connection with the end of an active period during which one of said number of speed controlled pumps 2 is active and which directly is followed by an inactive period during which said pump is inactive, and Ahofi is the pump station liquid level change during a following operating period, which following ing period takes place in connection with the beginning of the ly following inactive period. In this variant, it is assumed that the inflow in the ing of an inactive period is the same as the inflow in the end of the preceding active period. By adding Ahm,and Ahofi, eration is given to how large the inflow probably was when the pump 2 was active. Atmland Atofi should be positioned as near as possible the instant of time when the pump n liquid level h reaches the pump stop liquid level hsmp, however Atmlshould be sufficiently far from the instant of time when the pump station liquid level h reaches the pump stop liquid level hsmp in order not to be influenced by so—called snooring effects of the pump 2, i.e., that the pump 2 sucks air, and Atofi should be sufficiently far from the instant of time when the pump station liquid level h reaches the pump stop liquid level hsup in order not to be influenced by so—called siphon effects of the outlet pipe 4, i.e., that liquid is pulled along in the outlet pipe 4 because of the inertia of the pumped liquid in spite of the pump 2 having been shut off, or reflux effect from the outlet pipe 4 when the pump 2 has been shut off.

According to a fourth t, which is a mixture of several of the above variants, an operating period comprises a period when the pump is active, i.e., tm” and a period in WO 73552 which the pump is inactive, i.e., ton; note, the mutual order is unimportant. hm1is the pump station liquid level change during the period when the pump is active and hofi is the pump station liquid level change during the period when the pump is inactive. In this fourth variant, it is assumed that the inflow during the inactive period of the pump is the same as the inflow during the active period of the pump.

It should be pointed out that tm1and tofi do not need to be equally large. ably, the length of an operating period according to this t is equal to one pump cycle, and L is the vertical height n the pump start liquid level hflau and the pump stop liquid level hymp_Accordingly, in this preferred embodiment, each of hmland hofi is equal to L, which implies that tog is the time it takes for the pump station liquid level h to rise from the pump stop liquid level hsmp to the pump start liquid level hflam, tm,is the time it takes for the pump station liquid level h to fall from the pump start liquid level hflafi to the pump stop liquid level hflmp.

The time parameter k is calculated according to k=1/(c*tm%s), wherein c is the equalization parameter and tmeals is a subset of the period when the pump is active and during which ed power is measured. Accordingly, tmeas should be equal to or less than tmh Furthermore, consumed energy E during the period am“ can be measured by taneous power being summed up during the period tmfis, alternatively, instantaneous power is measured some time during the period tmeas and then the measured instantaneous power is multiplied by the time tmws.

Generally, the equalization parameter c is calculated according to C=(hofi/tofi + hm/tmfl, and in the preferred embodiment, the equalization parameter c is consequently calculated according to c=(L/tofi + L/tmd, i.e., c is a measure of pumped out quantity of liquid during the period tmeas ' WO 73552 According to a fifth variant, which is a special variant of the above fourth variant, the length of an ing period is equal to one pump cycle and consumed energy is determined for the entire period in which the pump is active, i.e., tmeas is equal to twp After simplification of the mathematical expression ing to the fourth variant, the following is ed.

Accordingly, a pump cycle comprises a period when the pump is active, i.e., tm” and a period in which the pump is inactive, i.e., tofi, in other words, the length of the operating period is equal to (tm1+ tofi). The time parameter k is calculated according to k=l/(c*(tm1+ tofi)), wherein c is the equalization ter. The length of a pump cycle is ably in the range of 1—10 min, but may also amount to one or several hours. It should be pointed out that tmland tofi do not need to be equally large.

Preferably, the equalization parameter c is calculated according to c=L/tofi, wherein L is the vertical height between the pump start liquid level hfiafi and the pump stop liquid level hsmp. Furthermore, tofi is the time for which the pump has been inactive during the elapsed pump cycle. In this variant, it is assumed that the inflow during the inactive period of the pump is the same as the inflow during the active period of the pump. According to said fifth variant, consumed energy E during the operating period/pump cycle can be measured, or an instantaneous power can be measured some time during the period of the pump cycle in which the pump is active, i.e., during tm, and then the measured instantaneous power is multiplied by the time ton the pump has been active. According to a red embodiment, instantaneous power is measured at the end of the period of the pump cycle in which the pump is active.

The method 7 according to the invention may be implemented for controlling a pump, as described above.

Furthermore, the method 7 may be implemented in a pump station comprising several variable—speed controlled pumps 2, where registration and control preferably takes place in the al control unit 6. The l may either be effected for the entire pump station 1 independently of which pump that has been active, or for each pump tely. When control is effected for the entire pump station 1, eration is given to each registered operating period independently of which pump that has been active, which gives a faster nt toward the optimum speed for the individual pump than when the control is effected for each pump separately, as well as that the external control unit 6 does not need to know how many le~speed controlled pumps 2 that are connected. The advantage of the control being effected for each pump separately is that the characteristic of the individual pump entity does not affect other pump es, i.e., different types of pumps and differently old pumps can be used side by side. In an alternative implementation, registration and control are effected in a built—in control unit in each individual pump 2, preferably two such pumps may be operatively interconnected to interchange information about the latest known third pump speed V3. le Modifications of the Invention The invention is not limited only to the embodiments described above and shown in the drawings, which only have the purpose of illustrating and exemplifying. This patent application is intended to cover all adaptations and variants of the preferred embodiments described herein, and consequently the t invention is defined by the wording of the accompanying claims and the equivalents thereof.

Accordingly, the equipment can be modified in all feasible ways within the scope of the accompanying claims.

It should also be pointed out that although the terms "speed control" and "pump speed" for the sake of simplicity have been used in the claims as well as in the description, WO 73552 it will be appreciated that also other lent values are included, such as current feed frequency control, supply voltage control, etc., which all aim at changing the speed of the pump, and which all have a unambiguous relationship to pump speed.

It should be pointed out that even if it is not explicitly mentioned that features from one specific embodiment can be combined with the features of another embodiment, this should be regarded as evident when possible.

Claims (16)

WHAT WE CLAIM IS:

1. Method for controlling at least a part of a pump Station comprising C a number or speed controlled pumps, the method being arranged to minimize the ic energy consumption ESpec of said at least a part of a pump station, n said method comprises a sub method (Find V3) that comprises the steps of * obtaining input data in the form of a set of parameters corresponding to a fictitious or elapsed first operating 10 period tl and a fictitious or elapsed second operating period t2, * determining, based on said set of parameters, the mutual relative relationship between a first value A1 of a quantity that ponds to a 15 first pump speed V1 and that is derived based on said set of parameters, which first value A1 relates to said first operating period t1, and a second value A2 of said quantity that corresponds to a second pump speed V2 and that is derived from said set of 20 ters, which second value A2 relates to said second operating period t2, and between a first specific energy consumption Eqmcl that is derived based on said set of ters and that 25 relates to said first operating period t1, and a second specific energy consumption Eqmc2 that is derived from said set of parameters and that relates to said second operating period t2, * ining, based on said determined mutual relative 30 relationships and on parameters B3, B4, B5, and B6 of said quantity, output data in the form of a third value A3 .C said quantity corresponding to a third pump speed V3 0: a third operating period t3, wherein A3 is set equal to A2—33 if the conditions A2<Al ard 35 Efimc2<Eqmcl are satisfied, A3 is set equal to A2+B4 if the conditions A2>Al and Eqmc2<Eqmcl are satisfied, A3 is set equal to A2+BS if the conditions A2<Al and Eqmc2>Eqmcl are satisfied, and A3 is set equal to A2—B6 if the conditions A2>A1 and Eflmc2>Eqmcl are satisfied, and * using the determined value V3 as the operating speed of the number of speed controlled pumps in said third operating period. 10

2. Method according to claim 1, wherein the specific energy consumption of said at least a part of a pump n is given as a predetermined value Eflmc for a fictitious operating period or is calculated according to Espec = k*E for an elapsed operating period, where E is consumed energy 15 by at least one of said number of frequency controlled pumps during said elapsed operating period and k is a time parameter, and wherein the value A of said quantity is given as a predetermined value for the fictitious operating period or is registered for said elapsed operating period.

3. Method ing to claim 1 or 2, wherein the first value A1 of said quantity consists of the pump speed Vl, the second value A2 of said ty consists of the pump speed V2, and the third value A3 of said quantity consists of the 25 pump speed V3.

4. Method according to claim 1 or 2, wherein the first value A1 of said quantity consists of a first t feed frequency Fl, the second value A2 of said quantity consists 30 of a second current feed frequency F2, and the third value A3 of said quantity consists of a third current feed frequency F3.

5. Method according to claim 1 or 2, wherein the first value 35 A1 of said quantity consists o a 'irst supply voltage 81, the second value A2 of said ty consists of a second supply voltage 82, and the third value A3 of said quantity consists of a third supply voltage S3.

6. Method according to any one of the preceding , wherein the set of parameters ses said first value A1 of said quantity and the associated first specific energy consumption Eqmcl, as well as said second value A2 of said quantity and the associated second specific energy consumption Egmcz.

7. Method according to any one of the preceding claims, wherein the parameters B3, B4, B5, and B6 have predetermined values, each of which corresponds to a current feed frequency change that is r than 0,5 Hz, and smaller 15 than 5 Hz.

8. Method according to claim 7, wherein said current feed frequency change is smaller than 2 Hz. 20

9. Method according to claim 7 or claim 8, wherein each of the parameters B3, B4, B5, and 36 corresponds to a current feed frequency change of 1 Hz.

10. Method according to claim 7, 8 or 9, wherein the 25 parameter B3 is equal to the parameter B5, and the parameter B4 is equal to the parameter B6.

ll. Method according to claim 2, wherein the length of an operating period is n*24 h, where n is a ve integer, 3O and wherein the time parameter k is ated according to n*24

12. Method according to claim 2, wherein the length of an operating period is n*24 h, where n is a positive integer, and wherein the time parameter k is calculated according to k-————————, where . . . c is an equalization parameter. __c*(n*24)

13. Method according to claim 12, wherein the equalization parameter c is calculated according to where xmlis the number of times a pump has been activated during an elapsed operating period, and ZtMIis the cumulative time for which the pump has been active in the elapsed operating period.

14. Method according to claim 2, wherein the length of an ing period is 8 seconds, where s is a positive integer, and wherein the time parameter k is ated according to 20 k: where c is an equalization parameter.

15. Method according to claim 14, wherein the equalization parameter c is calculated according to 25 c:(AhM-+Ahw) where Ahmlis the pump n liquid level change during an elapsed operating period, which elapsed ing period takes place in connection with the end of an active period 30 during which one of said number of speed controlled pumps is active and which directly is followed by an ve period during which said pump is inactive, and Ahofi is the pump station liquid level change during a following operating period, which following operating period takes place in connection with the beginning of the directly following inactive period.

16. A method according to claim 1, substantially as herein described or exemplified with reference to the anying drawings. WO 73552 W0