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1. H n i480lEN 203923 closed86426 H n fem 283388 open 864 Z5 sl m G S00 ft m MM ag a x 1 30 BS s 20 Za A 1400 3 10 10 Seel De 100 200 200 400 AML ron 200 eo 100 og p Veenmg p 4 mem hp kW hp kW 150 zen 110 1400 1200 0 D 1000 00 0 log n 190 zoo 300 400 aM o 100 200 300 400 oe Figure 6 An example of pump curves Left Pump with three different impeller diameters Right Pump with six different speeds For the variable speed application example above a motor selection can be made for 110 kW 1400 rpm Application guide No 2 Using variable speed drives VSDs in pump applications 13 Pumping system Motor and variable speed drive selection Motor and drive manufacturers have developed software tools for motor and drive selection ABB has a DriveSize tool which can be used for the pump case above The results are similar to manual selection The tool has a database of ABB motors drives and transformers so its output is an exact selection with type designations The DriveSize tool can be downloaded from the Internet at www abb com and then entering DriveSize in the search box Figure 7 shows an example of DriveSize 2 5 motor selection Because the pump loading torque is very low at lower speeds the maximum torque is critical for motor selection In this case we need to check that the m
2. In many clean water applications the level of the water is a re quired control function In a typical level control loop the level in the tank is controlled by throttling a control valve at the pump discharge The flow through the pump will be between 25 and 75 of capacity The significant hydraulic energy generated by the pump is dissipated across the control valve to regulate the level in the tank The pump must be also dimensioned to accommodate the pressure drop associated with the valve at maximum flow Application guide No 2 Using variable speed drives VSDs in pump applications 23 Applying ABB variable speed drives to pumping applications Applying a VSD in the loop will control the pump to generate only the hydraulic energy needed to discharge the required amount of liquid This approach reduces energy costs while lowering pump maintenance requirements The net result is a system that reduces operating and maintenance costs by eliminating the need for a control valve bypass piping and the associated energy losses The level of the water tank can be controlled using PI control to maintain smooth but accurate level control with one or several pumps running in parallel Temperature control Figure 12 illustrates a control loop in which flow into a tank is regulated by the temperature of the tank content Figure 12 Temperature control with variable speed drive VSD Temperature of the liquid is used to contr
3. Application guide No 2 Using variable speed drives VSDs in pump applications 29 Applying ABB variable speed drives to pumping applications Pump priority function This function balances the operating time of all the pumps in the system over the long term This facilitates maintenance planning and can boost energy efficiency by operating pumps closer to their best efficiency point In a system where the consumption rate is greater during the day for instance the drive can be programmed to operate higher capacity pumps during daytime and smaller units at night Sleep boost function The sleep boost function runs the pump to boost the pressure in the pipeline or water level in the tank prior to shutdown This extends the pump s sleep time and therefore saves energy It also avoids unnecessary starting and stopping and helps to flush the pipelines Adaptive programming A PI controller is a common way of controlling changing proc ess variables When the process PI control is activated a proc ess reference and actual value are compared The process PI control adjusts the drive speed in order to keep the measured process quantity at the desired level In a situation where the gap between reference and actual value is high such as fill ing an empty pipeline in an irrigation system the PI controller might be too aggressive when trying to stabilize the situation at the start With ABB industrial drives it is possible to utilize
4. causing no harmful effect to the power grid thereby avoiding penalties while ensuring maximum uptime for the pumping station Easy communication ABB drives can connect to all major automation systems This is achieved with a dedicated gate way concept between the fieldbus systems and ABB drives The Ethernet module gives simple access to the drive via the Application guide No 2 Using variable speed drives VSDs in pump applications 19 Variable speed drive benefits with pump applications Internet communicating via a standard web browser The user can set up a virtual monitoring room wherever there is a PC with an Internet connection or via a simple dial up modem connec tion This enables remote monitoring configuration diagnostics and when needed control Flexibility in pump selection Quite often it is difficult to esti mate the system parameters in advance and therefore the safety margins used are too high This causes additional operational costs if the required flow and head are lower than estimated By using VSDs these over dimensioning problems can be resolved by running the pump at a lower speed Reasonable investment cost VSDs have developed rapidly during the last 10 years The cost of manufacture and subse quent cost of purchase has also fallen dramatically in recent years Sometimes it can be less expensive to install a VSD than a control valve with a PLC system Natural part of the control loop One big adv
5. Left to right throttling bypassing on off control and VSD control Application guide No 2 Using variable speed drives VSDs in pump applications 9 Pumping system Throttling Bypassing 10 The relative power consumption of the different control methods can be estimated from the area between the x and y axes and the operating point It is using the formula P Q x H In the following example Figure 4 the relative power consump tion on an average flow rate of 70 is calculated with differ ent control methods More detailed explanations on power consumption and energy savings relating to different pump applications are described in the following chapters Throttling Bypassing H P T127 80 H HeT AN ener 10 o Pade 10 S H 8 8 5 5 a a 0 5 ja Qn124 a ST 10 a Ge On off control VSD control H Pump runs 70 of the time 0 Figure 4 The power consumption of the four most common flow control methods for centrifugal pumps Throttle control is the most commonly used method The flow caused by the constant speed pump is reduced by increasing the losses in the system by closing the valve In the example in Figure 4 the operating point is moved from Q 10 H 10 to Q 7 H 12 7 The relative power consumption can be calculated by P 7 x 12 7 89 Although not commonly used bypassing is applied mainly to circulation pumps The flow output to the system is r
6. and redundancy to handle situations when one or more pumps are out of order The collection points have tanks from where the wastewater is pumped to the treatment process It is crucially important to have the right level in those tanks as well as control over the pumps in order to keep the system operational at all times It is important to have stable process conditions in the treatment plant However this guide does not examine the wastewater treatment process in detail Level control is typically used to control the filling or emptying of wastewater storage tanks Single pump or parallel pumps operate at a favorable point most of the time to minimize energy consumption Level control can be used with up to three pumps and drives in parallel Figure 14 shows a typical single pump wastewater pump station Figure 14 Level control set up in a wastewater pump station with a single pump 26 Application guide No 2 Using variable speed drives VSDs in pump applications Anti jam Applying ABB variable speed drives to pumping applications In applications where the pumped liquid contains small particles capable of jamming the pump there is a need to have an active cleaning procedure for the pump otherwise there is a risk of breaking the pump Pump manufacturers recommend cleaning cycles for systems where the pump is running between maxi mum and minimum speeds with aggressive ramps in between With an ABB industrial drive thi
7. interested parties the basic information for selecting the correct variable speed drive VSD system for pump installations in industrial public and domestic applications Pumps are one of the most common variable speed drive VSD system applications and special interest has focused on improv ing their energy efficiency by using variable speed control in stead of throttling or other less efficient flow control methods Pumps are the single largest user of electricity in industry in the European Union consuming 160 TWh per annum of electricity and accounting for 79 million tonnes of carbon dioxide CO emissions The content of this guide has been kept as practical as possible without going into too much theoretical depth The symbols and definitions used are explained at the end of this document Application guide No 2 Using variable speed drives VSDs in pump applications Chapter 2 The basic function of pumps The purpose of pumps is to transfer liquids from a source to a destination A common example is filling a high level reservoir or increasing liquid pressure Other examples are filling a pres surized tank or circulating liquid around a system as a means of heat transfer There are two main categories of pumps e Centrifugal rotodynamic pumps e Positive displacement pumps This Application guide focuses on centrifugal pumps These account for 80 of all industrial pumps Centrifugal pumps The centrifugal
8. pump Figure 1 is a mechanical device for in creasing the pressure of liquid In passing through the pump the liquid is accelerated in the impeller discharging into the casing at high velocity This energy used is converted into pressure of the liquid as effectively as possible Source Variable speed pumping Europump and Hydraulic Institute 2004 Discharge Volute Figure 1 Centrifugal pump the most common pump type in industry and public utilities 6 Application guide No 2 Using variable speed drives VSDs in pump applications The basic function of pumps Terminology in this section Common terms Pump curves pplication guide No Before describing how a pump operates it is useful to under stand some key terminology Head The net work done on a unit weight of water by the pump impeller It is the amount of energy added to the water between the suction and discharge sides of the pump Pump head is measured as pressure difference between the discharge and suction sides of the pump Static head The vertical distance from the water level at the source to the highest point where the water must be delivered It is the sum of static lift and static discharge Static head is independent of the system discharge and is constant for all values of discharge However it is possible that the static head may vary over time due to the changes in the system Operating point A centrifugal pump can operate at a
9. the user to gradually ramp the acceleration at a safe rate to avoid hammering Reduced stress on electrical supply VSDs always start the pump motor softly with much lower peak current than direct on line starting that is used with other flow control methods Reduced risk for cavitation Cavitation is a phenomenon that occurs whenever the static pressure drops below the liquid va pour pressure causing bubbles to collapse with a very high im pact force This force causes surface damage inside the pump With a VSD it is possible to monitor the pressure of the incoming pipeline and take steps if the risk of cavitation is high Redundancy With parallel pumps each controlled with a VSD there are two possibilities to minimize maintenance and repair costs Parallel connection means that if one pump fails the re maining pumps can continue uninterrupted Another benefit is to control the running times of each pump to a predefined sched ule This enables the customer to optimize any service breaks ensuring that there is always pumping capacity available Additional benefits with VSDs The use of VSDs has many other advantages in process control applications These include Harmonics In some countries power companies set strict limits on the permissible harmonic content of current and voltage in order to prevent damage to equipment in the same environment In these situations ABB low harmonic drives minimize offend ing harmonics
10. ABB drives Using variable speed drives VSDs in pump applications Application guide No 2 Using variable speed drives VSDs in pump applications Contents Chapter 1 Introduction nnnannnnneenannennensnanennnnnansnenvennnnenevennnnnenvennn 5 Chapter 2 The basic function of PUMPS nanne vennen enen ae nennen 6 Gentrifugall PUMPS 2e eres nutte intentie 6 Terminology in this section annen nennen ven eneenne nennen eeneenneenne eenen 7 Reuler H PUMP Reif a CDI Ia lenten rendeert edere dSeEE ELSE 8 Chapter 3 PUMPING system nnnnnunnannennnnanneensennnsenenennnnenenennnnneneennn 9 Pump as a part of the process a aa EnEn Aaa aA aa Kea Eaa nennen 9 Different flow Control methods AAA 9 TOOTING DT 10 BYPASSING EE 10 Onoff Conto EE 11 tree dee eebe ee ege ec 11 Parallel and serial PUMPS nanne vern veneneen eenen eneen evene venen 12 Selection of pump motor and variable speed drive VSD eceeeeee 12 Nu Bt EE 12 Motor and variable speed drive selection nnen eenen 14 Chapter 4 Variable speed drive benefits with pump applications 15 Life cycle cost LOC narren sen eis sie ad Gites aardi ved dede 15 VE SAVING RTE 16 Software for energy savings calculation nnen envennenreneenenennn 18 Low maintenance and repair COST nanne nennen eneeneneennerennveneneenn 19 Additional benefits with VSDS nnen eenen nennen nenvenveneenneenvenvennn 19 Chapter 5 Applying variable spe
11. Oh at 20 flow 5 100 AE CC nm FLOW mh tt Figure 8 A typical operating profile of a pumping system as presented in PumpSave ABB s energy saving calculation tool The earlier energy saving calculation example see page 13 is below calculated with PumpSave ABB s energy saving calcula tion tool The following conditions exsist Pump data Nominal flow 1000m 2 h 300I s Efficiency 85 Static head 10m Nominal head 30m Max head 45m Motor data Motor power 110 kW Motor voltage 400V Nominal efficiency 96 Drive data Nominal efficiency 95 Economic data Energy price 0 05 EUR kWh Application guide No 2 Using variable speed drives VSDs in pump applications 17 Variable speed drive benefits with pump applications The energy consumed with throttling and VSD is illustrated below on Figure 9 Energy Consumed Throttling Figure 9 Energy consumption of a pump system controlled with throttling and VSD control as presented in PumpSave ABB s energy saving calculation tool The total energy saving with the VSD compared to throttling is 202 MWh 46 The financial savings amount to 10 100 EUR every year This calculation clearly shows the benefit of VSD control with regard to energy savings for a single pump Software for energy savings calculation ABB has developed a calculation tool called PumpSave which estimates the energy savings when applying electric speed control to pump a
12. a more efficient solution Several paral lel pumps can be controlled with one VSD controlling the master pump and contactors switching the other pumps on and off Figure 10 shows a set up with parallel pumps using one ABB drive to control three pumps Figure 10 Pressure control of a pumping system with one variable speed drive VSD 22 Application guide No 2 Using variable speed drives VSDs in pump applications Applying ABB variable speed drives to pumping applications To guarantee pump operation even when a fault occurs the pump system needs redundancy In pump stations this means that a failure of one pump motor or drive in a parallel installa tion does not cause a process interruption but the operation will continue with a limited capacity In order to have a replacement for a failed unit a parallel system is needed This means that each pump is controlled by an ABB industrial drive for pump control Drives share information such as status of the drive priority running time process feedback etc through a fiber optic link In a ring connection implemented with fiber optics it is possible to define the actions for the drives in the event of failure of the optical link in order to achieve 100 redundancy No PLC is needed Figure 11 shows a system loop with three ABB industrial drives in ring connection controlling three pumps Figure 11 Pressure control with three ABB industrial drives Level control
13. adaptive programming to fine tune specific conditions of this kind in different pump stations Remote data access and monitoring via the Internet Internet Internet Figure 18 Different remote control methods for a pump station With a separate computer left or with an ABB industrial drive and an intelligent ethernet module right 30 Application guide No 2 Using variable speed drives VSDs in pump applications Applying ABB variable speed drives to pumping applications Pump stations are often located at a distance from the central controlling station In this case the pump station can be equipped with the intelligent ethernet module that gives simple access to the drive via the internet communicating via a standard web browser The user can set up a virtual monitor wherever there is a PC with an internet connection or via dial up modem con nection This enables remote monitoring of the drives and the process configuration diagnostic and when needed control The intelligent ethernet module also includes an alarm func tion which can provide additional confidence that the pumping station is operating correctly Further continuous process data monitoring can be set up Up to nine drives can be connected to the ethernet adapter mod ule supporting parallel connected pumps via fiber optic links Application guide No 2 Using variable speed drives VSDs in pump applications 31 Chapter 6 Bibliography Variable speed pu
14. antage in con sidering a VSD in comparison to a control valve is the elimi nation of deadband that a control valve introduces into loop performance 20 Application guide No 2 Using variable speed drives VSDs in pump applications Chapter 5 Applying variable speed drives to pumping applications The majority of pumping applications need to be controlled Changing the rotation speed of a centrifugal pump has an ef fect on the pump s volume flow generated head and power consumption The design of a pumping system with VSDs requires knowledge about the process control parameters Process control parameters The parameters to be considered in clean water applications include Inputs heads and pressure required flow and its variations required level of the liquid e Outputs pressure generated flow generated e External influences temperature change change in flow change of the liquid s properties floating breaking or jam ming of the pipeline change in the water consumption rate The parameters to be considered in waste water applications include accordingly Inputs level of the water temperature pH flow e Outputs flow optimum filling emptying time adjustement of pH or temperature S External influences temperature change change in flow change of the liquid s properties floating breaking or jam ming of the pipeline Knowing the above requirements makes it easy to find the right parameter
15. applications Chapter 3 Pumping system Pump as a part of the process When in use the pumps are always part of a pumping system A pumping system is usually a network of pipes tanks valves and other system parts The receiver is usually at a higher geo graphic level than the supply of the system These parts can be also on the same level as in the case of a closed circuit heat transfer system Pumping systems nearly always require a variation of flow rate Examples include the daily cycle in the consumption of drink ing water the varying process demand for a liquid or seasonal heating demand However the variation required may be in the pump head such as for cyclical changes in process pressure or pumping to tanks with a variable liquid level In spite of the variations the pump capacity is selected accord ing to the maximum flow and head or even to the future needs perhaps with a certain safety margin The average pumping capacity may be only a fraction of the maximum capacity and this will require some kind of control Different flow control methods There are several different methods to match the flow to the system requirements The most common flow control methods of pumps are throttling bypassing on off control and VSD control These are illustrated in Figure 3 D G a A E e Kal HON i YQ N i SS Ee 45 Di 3 en A ei d 7 af S 8 e 4 Figure 3 Illustrations of pump flow control methods
16. combina tion of head and discharge points given by its pump curve see below The particular combination of head and discharge at which a pump is operating is called the pump s operating point Once this point is determined brake power efficiency and net positive suction head required for the pump can be obtained from the set of pump curves The pump curves in Figure 2 show the technical performance of the pump The horizontal axis shows the flow rate and the vertical axis shows the head and power generated A system curve normally plotted together with the pump curve describes the static head and resistance of the pipeline The operating point of the pump is at the intersection of the system curve and the pump curve Pump curve System curve Power curve Figure 2 Pump performance curves Using Variable spi IVES Is in pump applications The basic function of pumps Affinity laws As stated before pumps are mechanical devices for increasing the pressure of liquid The affinity laws Table 1 below describe the relation between the rotational speed of the pump n flow rate Q head gener ated H and power absorbed P Speed and flow are directly proportional Flow Head is proportional to the square of the speed Head Power is proportional to the speed or flow cubed Power Table 1 Affinity laws Application guide No 2 Using variable speed drives VSDs in pump
17. e speed control method is the most energy efficient for pumping applications The exam ples discussed were calculated for one flow rate only 70 but the relative power consumption with different control methods depends on the flow rate This relationship is shown in Figure 5 In these curves the pump motor and drive efficiencies are also taken into account and for that reason the results differ somewhat to those in Figure 4 Throttling Bypassing On off control VSD control 20 40 eo 80 100 Flow Figure 5 Power consumption with different pump control methods as a function of flow rate The percentage values of flow and power are related to the nominal values of the pump Throttling control leads to high loss in the pump and in the valve when the system is running at a reduced flow rate The loss in the motor remains relatively constant over the whole flow range In VSD control the operating point follows the system Application guide No 2 Using variable speed drives VSDs in pump applications 11 Pumping system curve which is optimal for pump efficiency In general based on affinity laws the energy consumption drops dramatically when speed is reduced The energy savings with VSD control are significant Parallel and serial pumps If the available flow capacity with a single pump is not sufficient parallel connection of two or more pumps is possible It is im portant to install back pressu
18. ed drives to pumping applications 21 Process control parameters AAA 21 Clean water applications nnn annen venvennvenenneeeevenvenerenvenevenen nennen 22 Ne te 22 Level Control nerian reinii ies Weyer eee 23 Temperature Control 24 Case example pressure boosting Station nnen ennen ennnensenn 24 Wastewater applications nennen venenenee eneen eneveneeneneereneennenenenn 26 Level controls entente dend eae Nn 26 Antifa ee reer a iter cerca treated raakte enke 27 Prevention of tank wall sedimentation nnn annen eene eennenennenenneenn 27 FIUSM EEE 28 Application guide No 2 Using variable speed drives VSDs in pump applications Case example Storm water pumping station nnn ennennennen eneen 28 Additional functions 29 Flow calculation function a eeeneeenenenenenenenvervee nennen nennen 29 Pump priority function nnee wiati eneen eenen eneen enen 30 Sleep boost function nano ia ie aeia ai ieie 30 Adaptive programming 30 Remote data access and monitoring via the Internet nennen 30 Chapter 6 Bibliography nnn senannenerenannnenennnnnnennnnnnneenvennnnennnenenn 32 Chapter 7 Symbols and definitions nn ansssnensnnnnerenennnenennnnnnenenn 33 RI Un ue In EE 33 Te E EE 35 Application guide No 2 Using variable speed drives VSDs in pump applications Chapter 1 Introduction The purpose of this Application guide is to give design and project engineers and any other
19. educed by bypassing part of the pump discharge flow to the pump suction This means that the total flow increases from 10 to 12 4 but the head decreases from 10 to 6 6 The relative power consump tion is P 12 4 x 6 6 82 Application guide No 2 Using variable speed drives VSDs in pump applications Pumping system On off control On off control is often used where stepless control is not nec essary such as keeping the pressure in a tank between preset limits The pump is either running or stopped The average flow is the relationship between the on time and the total time on off The relative power consumption can be easily calcu lated by P 0 7 x 100 70 VSD control To understand the benefits of VSD control consider to the pump curves in Figure 4 With low static head systems the optimal efficiency of the pump follows the system curve With VSD con trol the duty point of the pump follows the unchanged system curve Changing the speed of the pump moves the pump curves in accordance with the affinity laws If the pump impeller speed is reduced the pump curve moves downwards If the speed is increased it moves upwards This means that the pumping capacity is exactly matched to the process requirements Ac cording to our earlier example both flow rate from 10 to 7 and head from 10 to 6 4 are reduced The relative power consump tion can be calculated by P 7 x 6 4 45 This example shows that the variabl
20. ge points given by its pump curve The particular combination of head and discharge at which a pump is operating is called the pump s operating point Once this point is determined brake power efficiency and net posi tive suction head required for the pump can be obtained from the set of pump curves Redundancy Serving as a duplicate for preventing failure of an entire system upon failure of a single component Application guide No 2 Using variable speed drives VSDs in pump applications Symbols and definitions Deadband Also known as hysteresis The amount of a meas ured variable pressure temperature etc between the point where a switch closes and then re opens i e an area of a signal range where no action occurs the system is dead Deadband is used in voltage regulators thermostats and alarms The pur pose is to prevent oscillation or repeated activation deactivation cycles Often the deadband of a switch is fixed and cannot be adjusted 34 Application guide No 2 Using variable speed drives VSDs in pump applications Index Application guide No 2 Using variable speed drives VSDs in pump applications 35
21. hods especially with low flow speeds and when shutting down the pump With a traditional VSD control almost all pump speeds are accepted and changes in pump speed are smooth With the ABB industrial drive only efficient speed and maximum speed are allowed in this kind of application with a level control mode Rapid changes between these stages and in starting give a powerful flush effect in the pipelines and in the pump itself keeping them both clean Case example Storm water pumping station Pietarsaari Finland is a low lying town the centre of which can be prone to flooding during rainy weather This was because the storm water removal system consisting of pipes feeding into an open channel draining into the sea did not have sufficient capacity for very rainy periods The local water utility Pietarsaaren Vesi decided to tackle these problems by increasing the capacity of the channel with an underground holding tank A pumping station Figure16 was constructed to empty the tank Water is allowed to run into the tank until it reaches a trigger level and is then pumped out into the lower part of the channel where it continues to the sea The pumping station has two 80 kW pumps operated by two ABB industrial drives Figure 16 The Pietarsaari storm water pumping station Application guide No 2 Using variable speed drives VSDs in pump applications Applying ABB variable speed drives to pumping applications Additiona
22. ions Plant equipment operations are receiving particular attention as a source of cost savings especially minimizing energy consump tion and plant downtime Application guide No 2 Using variable speed drives VSDs in pump applications 15 Variable speed drive benefits with pump applications In addition to the economic reasons for using LCC many organizations are becoming increasingly aware of the environ mental impact of their businesses and are considering energy efficiency as one way to reduce emissions and preserve natural resources Source Pump Life Cycle Costs Hydraulic Institute Europump 2000 Life cycle analysis for pumping systems show that e 5 of industrial energy goes to pumps 90 of the total cost of owning a pump comes from energy consumption Pump energy consumption can generally be reduced up to 20 Good guidance for Pump Life Cycle Cost is available from www pumps org An LCC Analysis for Pumping Systems has been developed by the Hydraulic Institute HI Europump and the US Department of Energy s Office of Industrial Technolo gies OIT The website also includes information related to variable speed pumping and energy savings Energy saving The Hydraulic Institute and Europump have jointly published a book entitled Variable Speed Pumping A Guide to Successful Applications which details seven ways to save energy 1 Design systems with lower capacity and total head require ments Do
23. l functions The following useful functions are for clean water and waste water applications Some of these features are only available with ABB industrial drives Flow calculation function This function enables calculation of flow without the installation of a separate flow meter The flow calculation function can meas ure the flow rate using two pressure transmitters or solely ABB industrial drive operating data It helps to monitor the pumping process in single pump installation where the flow data is not required for invoicing purposes The flow measurement calculation is based on pump curves PQ and HQ pressure feedback from two sensors data about the pump installation and Direct Torque Control DTC motor data Sensorless flow measurement is also possible For more ac curate results pressure transmitters can be used to supply the necessary measurement data The connections are illustrated in Figure 17 An ABB industrial drive can then carry both actual and total flow information further to other automation systems The flow measurement function is also applicable for parallel pumps There are some technical limitations due to the calcu lation formula The pumps need to be the same size and they need to run at the same speed It is also important that the pumps are connected to the same source and that the systems curves are equal Flow calculation function is patented by ABB Figure17 Flow measurement connections
24. ment cost of the equipment needed variable speed drives motors and pumps is relatively low when compared to the total LCC Maintenance is the third main cost component Active control using a VSD works as a means of preventive main tenance limiting maintenance costs in many ways VSD control has several benefits in pumping systems The most important is energy saving Accurate control of the pump system is another benefit With VSDs running the pump system link ing to other automation systems is easy by means of common fieldbus gateways The following chapters give more detailed descriptions of these benefits Life cycle cost LCC LCC analysis is a method of calculating the cost of a system over its entire life span The analysis of a typical system includes initial costs installation and commissioning costs energy operation maintenance and repair costs as well as down time environmen tal decommissioning and disposal costs Many organizations only consider the initial purchase and instal lation cost of a system It is in the interest of the plant designer or manager to evaluate the LCC of different solutions before installing major new equipment or carrying out a major over haul This evaluation will identify the most financially attractive alternatives As national and global markets continue to become more competitive organizations must continually seek cost sav ings that will improve the profitability of their operat
25. mping Europump and Hydraulic Institute 2004 Pump Life Cycle Costs Hydraulic Institute Europump 2000 Application guide No 2 Using variable speed drives VSDs in pump applications Chapter 7 Symbols and definitions Definitions AC Alternating current or voltage CO Carbon dioxide gas DTC Direct torque control EUR Currency euro H Head m HQ Head Flow pump performance curve Hz Hertz equals 1 s VO Inputs and output LCC Life cycle cost n rotation speed rotations per minute rpm kWh Kilowatt hour P Power Watt W Pl Controller type PLC Programmable logic controller PQ Power Flow pump performance curve Q Flow I s m3 h rpm Rotations per minute TWh Terawatt hour Head The net work done on a unit weight of water by the pump impeller It is the amount of energy added to the water between the suction and discharge sides of the pump Pump head is measured as pressure difference between the discharge and suction sides of the pump Static head The vertical distance from the water level at the source to the highest point where the water must be delivered It is the sum of static lift and static discharge Static head is independent of the system discharge and is constant for all values of discharge However it is possible that the static head may vary with time due to the changes in the system Operating point A centrifugal pump can operate at a combi nation of head and dischar
26. not assume these requirements are fixed 2 Avoid allowing for an excessive margin of error in capacity and or total head It typically will be less expensive to add pumping capacity later if requirements increase 3 Despite the tendency to emphasize initial cost you will save in the long run by selecting the most efficient pump type and size at the onset 4 Use VSDs to avoid losses from throttle valves and bypass lines except when the system is designed with high static heads 5 Use two or more smaller pumps instead of one larger pump so that excess pump capacity can be turned off 6 Use pumps operating as turbines to recover pressure energy that would otherwise be wasted 16 Application guide No 2 Using variable speed drives VSDs in pump applications Variable speed drive benefits with pump applications 7 Maintain pumps and all system components in virtually new condition to avoid efficiency loss The energy efficiency of a pumping system depends on the control method used The VSD is especially efficient when the pump is running with partial flow A typical example of the duty cycles of a pumping application is shown in Figure 8 Operating Profile Annual running time 5000 jh bel sl 250h at nom flow mm kl ls 500h at90 flow W B 15 750h at80 flow kl aas 1000h at 70 flow B min 1000h at 60 flow EJ mila 750h at half flow Fy mie 500h at 40 flow s EJ ais 250h at 30 flow e kel Iw
27. ol the motor speed that regulates the flow to the tank An on off valve must be installed for safety reasons Case example pressure boosting station The basic example of a clean water pump station is a pressure boosting station It feeds water directly into the distribution system and seeks to maintain a constant pressure in the pipes With smooth VSD control there are no pressure shocks causing noise erosion or leakage in the pipeline Figure 13 shows a three pump parallel system at pressure boosting station in Pietarsaari Finland A water tower which was the main storage facility before the construction of the tank 24 Application guide No 2 Using variable speed drives VSDs in pump applications Applying ABB variable speed drives to pumping applications and pressure boosting station now serves as a back up The pressure boosting station is equipped with 2 x 75 kW and 1 x 37 kW electric pumps The station was recently upgraded with ABB industrial drives to operate the pumps Parallel drives enable the system to run with 100 redundancy If a defect occurs in one of the pumps motors or drives the others will continue the operation without any interruption Pump stations are sometimes located remotely and service activities might take some time With redundancy the pump station op eration is trouble free with minimized downtime Figure 13 Pressure boosting station in Pietarsaari Finland The running time of the p
28. otor torque T at 1400 rpm is higher than the pump torque T 9550xP 9550x1 10kW hee E0 Nm n 1400rpm As a result the pump torque is 750 Nm In this case the selected motor M3BP 315 SMB 4 has 848 Nm torque Motor Inad m Selected motor data Selection Drive Size Load type Pump fan load H Tyne code M38P 315 SMB 4 Product code 3GEP 312 220 FI Overload type Simple cyclic sl mn base max Speed rem au Dan Tam Power bw 110 fuo bg Overload 100 100 Overload time 2 fio every s soo Specifications Name undefined Mators per inverter jl Mator tupe Auto selection Figure 7 The selection window of DriveSize 2 5 DriveSize also selected a suitable VSD for the pump which is ACS800 02 01 70 3 14 Application guide No 2 Using variable speed drives VSDs in pump applications Chapter 4 Variable speed drive benefits with pump applications Pumping applications represent a significant opportunity for ap plying VSDs in new as well as retrofit installations The majority of pumping applications need to be controlled It is unlikely that a pump will run continuously at a maximum speed VSDs are crucial when limiting the life cycle costs LCC of a pump station The three main costs are energy initial investment and maintenance Many analyses show that energy consumption is the dominating element of the LCC especially if pumps run more than 2 000 hours per year The invest
29. perature etc Suction conditions such as suction head suction pipe losses etc Pump construction material 12 Application guide No 2 Using variable speed drives VSDs in pump applications Pumping system System description e g single parallel or serial connection with some other pump e Special conditions in the mounting space The required capacity can often be achieved by several different pump types with the same or different speed The selection has to be made for instance between a higher speed pump with low initial cost and a lower speed pump with lower maintenance costs The use of pump curves as printed in a manufacturer s catalogue is shown in Figure 6 For example to select a pump for a before mentioned quote We need to pump water at 300 I s please quote for a pump the selection steps are the following 1 find the required flow 300 I s 2 move upwards to match the required head 30 m 3 the required performance is achieved with pump of 1400 rpm speed 4 to see the power needed move down to the lower curve set along with 300l s line 5 when crossing the 1400 rpm curve move to left to read the power needed at the operating point 110 kW The selected pump is the smallest capable for the operating point required If we know that there is no need for higher ca pacity either now or in the future there is no need to choose a bigger pump The bigger pump leads to higher initial and operating costs
30. pplications To estimate the energy savings a VSD can be compared to throttling control on off control and hydraulic coupling control The calculations are based on typical pump operating charac teristics The accuracy of the input data affects the accuracy of the results Results should only be used for estimating purposes The results of calculations can be printed out PumpSave carries out a simple dimensioning and recommends an appropriate ABB drive type The tool provides financial fig ures for assessing the profitability of purchasing an ABB drive PumpSave runs in Microsoft Excel The PumpSave tool can be downloaded from www abb com motors amp drives and then entering PumpSave in the search box There is also a detailed user s manual for the PumpSave tool 18 Application guide No 2 Using variable speed drives VSDs in pump applications Variable speed drive benefits with pump applications Low maintenance and repair cost Maintenance and repair costs are one of the main elements in the LCC analysis The cost of unexpected downtime and lost production is a very significant item in the total LCC and can rival the energy costs With VSDs lower maintenance and repair cost is achieved through the following Reduced water hammer effects Water hammer is caused by rapid changes in flow These flow changes are followed by rapid pressure transients that cause pipes pipe supports and valves to be damaged causing leakage VSDs allow
31. re valves for all parallel pumps to avoid backwards flow through the pumps With parallel pump installation the redundancy of the system is much higher If one of the pumps is lost in the system other pumps can take its place and continue operation Downtime is very limited depending on how fast the replacement is carried out With ABB industrial drives the parallel connection of drives detects faulty units and makes any necessary corrections in the control loop in less than one second Serial connection of pumps can be used in high pressure system applications for example where one pump cannot produce the head required Selection of pump motor and variable speed drive VSD The selection of pumps motors and drives is based on the proc ess information Sometimes the information can be simply We need to pump water at 300 I s please quote for a pump Even though the pump is a simple machine proper pump selec tion calls for more input data There are many selection tools to support the dimensioning of pumps motors and drives The motor and VSD are dimensioned to run the pump under normal pump operation conditions Pump selection The general requirements for pump selection are Working conditions e Capacity suction and discharge pressures with variation ranges e Maximum differential pressure for the pump casing Exceptional starting stopping and other running condi tions Liquid specification with density tem
32. s kind of cleaning sequence can be activated during motor jam or during a specific run on or run off time This is also a good example of preventive mainte nance for the pump Anti jam is an easy way to guarantee continuous pump opera tion in harsh environments Prevention of tank wall sedimentation Application guide No 2 Using variable speed drives VSDs in pump applications In many pump applications there is a tank for liquid storage With liquids containing particles wall sedimentation Figure 15 left tank is acommon problem if fixed levels are used when filling and emptying the tank A special software feature of ABB industrial drive is designed to prevent sediment build up Varying randomly the surface level within a range of preset limits it is possible to avoid wall sedimentation Manual tank cleaning can then be performed at longer intervals Eliminating unnecessary stops for tank cleaning maximizes operating time Figure 15 Ways to avoid wall sedimentation in a tank Manual cleaning left and ABB industrial drive right Applying ABB variable speed drives to pumping applications Flush effect When a liquid contains particles it affects the tank and pump as described above Particles can also get jammed in pipelines and cause severe capacity problems and service breaks These problems are avoided if the liquid and the particles are moved rapidly Pump manufacturers advise avoiding very smooth control met
33. to be controlled and subsequently optimize the process VSD can handle several analogue and digital inputs and outputs to control and monitor the pumping process The large number of fieldbus options makes it easy to incorporate the drives seam lessly into any automation system Some basic control loops in industrial and public pump applica tions are described later in this chapter Application guide No 2 Using variable speed drives VSDs in pump applications 21 Applying ABB variable speed drives to pumping applications Clean water applications Clean water applications require pumps to carry fresh water from the source lake well etc to the users homes industry etc Clean water is often stored in tanks either before or after un dergoing different chemical cleaning processes Water is finally pumped to the users through pipelines with stable pressure Three different control examples for clean water applications are described below pressure level and temperature control Additional functions section describes additional useful VSD functions These functions are applicable for both clean and waste water applications Pressure control Using VSDs to control pressure reduces the electrical energy requirements by reducing the amount of hydraulic energy actu ally produced A basic pressure control pump station is equipped with one pump conirolled by one VSD In some pump stations pumps connected in parallel are
34. umps can be stabilized with the pump priority function to ensure that the wear and tear of all pumps is the same In some cases prioritization can use smaller pumps during light loading and bigger pumps during heavy loading thereby maximizing energy use In Pietarsaari the smaller 37 kW pump is used only at night time The flow calculation function enables the pumped volume to be monitored by the VSD without any additional components This is a very useful feature in systems where data about the total flow during a specific time period is needed However this is not deemed accurate enough for invoicing purposes In Pietarsaari the flow measurement result of the drive is compared with the flow meter The results are the same ABB industrial drives have enabled customers to reduce energy consumption by about 30 The pressure in the system is much more stable which has reduced leaks as well as maintenance needs Application guide No 2 Using variable speed drives VSDs in pump applications 25 Applying ABB variable speed drives to pumping applications Wastewater applications Level control In this application wastewater is transferred from the source houses drain wells and other collection points to the sewage treatment plant Wastewater and rainwater contains solid particles which have to be pumped Actual pumping time and pressure are not important issues but there must be sufficient capacity for special cases heavy rain

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