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HomeMy WebLinkAbout09 - Design Report - Norton Ranch - Lift Station 'l SANDERSON v-' STEWART LIFT STATION DESIGN REPORT FOR NORTON RANCH SUBDIVISION BOZEMAN, MONTANA PREPARED FOR NORTON PROPERTIES, LLC 63020 LOWER MEADOW ROAD BEND, OR 97701 FEBRUARY 2009 REVISED MARCH 17, 2009 BOZ-07004.04 • 6, SAN D E RSO N 40 STEWART March 22, 2010 Project No. BOZ-07004.04 NORTON RANCH LIFT STATION ENGINEERING REPORT 1. INTRODUCTION Norton Ranch Subdivision is a planned residential subdivision located in Bozeman, Montana. Wastewater generated from the subdivision will flow via new gravity sanitary sewers to a lift station located at Laurel Parkway and Norton Street. The wastewater will be pumped from the lift station and travel through force mains routed north on Laurel Parkway to Durston Road, and east on Durston Road to the tie-in with the existing City of Bozeman sanitary sewer collection system at Durston Road and Cottonwood Road. 2. PHASE I Phase I of the Norton Ranch Subdivision will consist of the development of 40 acres of the 242-acre site. For the first phase, the City of Bozeman has placed a limitation on the rate at which the Phase I wastewater may be pumped into the existing collection system based on the available and unreserved capacity in the receiving sewer. This rate is 175,000 gallons per day (121.5 gpm), which is below the design rate for the first phase. As such, equalizing storage will be incorporated into the lift station design to address the deficit pumping capacity as discussed in Section 4.3.1 below. Wastewater flows for subsequent phases of the Norton Ranch development will be able to be pumped at a rate equal to the future design rate as new sewerage collection system infrastructure will be constructed to increase the capacity of the collection system at and downstream of the collection system tie-in location. The design flow for the lift station is equal to the estimated peak hourly flow as defined in the Department of Environmental Quality (DEQ) design Circular-2. Peak hour flow is based on estimated population and determined as a ratio with the estimated average daily flow according to the following formula:: Qwk borrrly/Qnve.day= (18+0.5)1(4+1' S), whereeq. 1.0 P =population in thousands 1300 North Transtech Way Billings,Montana 59102 Phone 406.656.5255 Fax 406.656.0967 www.sandersonstewart.com The number of proposed dwelling units for the first phase conforms to the proposed R-4 Zoning as per the City of Bozeman zoning regulations. The dwelling unit density is 314. At 2.11 persons per dwelling unit, the estimate first phase population equals 663 persons. As per City of Bozeman design standards, the average day per capita wastewater flow equals 89 gallons per day (gpd). Therefore, the first phase average day wastewater flow for the estimated 663 persons equals 58,966 gpd (40.9 gallons per minute — gpm). Using equation 1.0 above, the peak hour to average day wastewater flow ratio for the first phase equals 3.92. Therefore, the peak hour domestic flow equals 161 gpm. Infiltration inflow (I/I) must also be included in the estimate of design flow and be equal to 150 gpd per acre. With a first phase area of 39.84 acres, the I/I equals 5,976 gpd (4.1 gpm). The total initial lift station design flow for the first phase when summing domestic wastewater flow and I/I equals 165 gpm. A scaled-back version of Phase I (Phase IA) could also be implemented. Under this scenario, Phase IA would consist of the development of 113 units. Consistent with what was presented above for Phase I, the estimated population under this scenario would be approximately 238 persons; the average day wastewater flow would equal 21,220 gpd (14.7 gpm); the peak hour to average day flow ratio would equal 4.12; and the peak hour wastewater flow would equal 60.6 gpm. Phase IA would occupy 15.76 acres, therefore the design infiltration inflow would equal 1.64 gpm. The total design flow for Phase IA would equal 62.2 gpm. Changes in the wet well sizing and pump cycling corresponding to this development scenario are addressed in the following sections. 3. SUBSEQUENT PHASES Population estimates and corresponding flows from areas within the remaining 202 acres of the Norton Ranch development are based on the anticipated zoning of these areas and dwelling unit density duties as set forth in the City of Bozeman zoning regulations. Table 1 below summarizes the breakdown of the proposed zoning in subsequent phases of the development, the number of dwelling units, and population per dwelling unit duties for the particular zoning type. Average day wastewater flows per zoning area are also established by zoning code and listed in Table 1. P:BOZ_07004_05_Fng_Rprt 2 (03/22/10)CN/tsc Table 1—Norton Ranch Future Development Area, Zoning, Population, and Avers e Da Wastewater Flow Ave. Dav Ave. Dwelling Population I Day Area Dwelling Q,,,� Flaw Zoning Unit Duty Units Duty Population D Qww (ac) Duty(du/ac) (per./du) Flow (guty (gpd) B-P 24.63 5.2 128 2.11 270 960 23,645 R-0 1 63.59 5.2 331 2.11 698 980 62,318 R-3 52.84 6.5 343 2.11 725 1,220 64,465 R-2 21.00 5.2 109 2.11 230 980 20,580 R-4 39.97 10.4 416 2.11 877 1,950 77,942 Total 1 202.03 1 1 1,327 2,800 1 1 248,950 Based on a future phase population of 2,800 in combination with the estimated population from Phase I, the total population of the Norton Ranch Development at full build-out would equal 3,463. From Eq. 1.0 the peak hourly to average day wastewater flow ratio would equal: Q,.k owyllQaw. �y= (18+3.4630-5)1(4+3.4630-5) = 3.39 Therefore, the domestic peak hourly flow would equal: (248,950 + 58,966) *3.39 = 1,043,835&5d(725 gpm) The required allowance for infiltration inflow to be added to the design flow equals: (39.84 ac+ 202.03) * 150gbd/ac= 36,281 obd(250m) Therefore, the total design flow that the lift station capacity must satisfy at full build-out of the subdivision equals 750 gpm. 4. LIFT STATION CONFIGURATION 4.1 Pumping Units The lift station will consist of a wet well utilizing submersible wastewater pumping units with discharge piping running to a generator building that houses both the control valves of the discharge piping as well as a backup diesel-fired generator and transfer switch. The lift station wet well shall use a tri-plex pumping unit configuration (3 pumps). For the first phase, the firm pumping capacity (capacity with the largest pump out of service) needs to equal 121.5 gpm as discussed in Section 2 above. Therefore, two pumps rated at 121.5 gpm shall be installed. As subsequent areas are being proposed for development, a third 121.5 gpm pump may be added, or two or three new pumps P:BOZ_07004_05_I np Rprt 3 (03/22/10)CN/tsc of greater capacity may be added to satisfy the needed pumping capacity requirements. The actual firm pumping capacity for any particular set of pumping units is dependent upon the discharge conditions present,which changes total dynamic head conditions and the rate at which the pumps will operate. These discharge conditions; specifically, the use of dual force mains of different sizes as discussed below,provide for the option of producing several different station pumping capacities using the same pumping unit set as discussed further in Section 4.2. The future configuration of the lift station in terms of the pumping unit sets will be dependent upon the nature and size of subsequent phases of development. 4.2 Force Mains Dual force mains will be utilized to convey wastewater from the lift station to the tie- in location with the City of Bozeman collection system. The use of dual force mains was necessitated by the wide range of design wastewater flows that may be present as Norton Ranch is developed. The rate of these design flows varies between the initial Phase IA design pumping rate of 62.2 gpm;the Phase I design pumping rate of 121.5 gpm; or the estimated design pumping rate of 750 gpm at full build-out. By using either, or both, of the 4-inch diameter and 6-inch diameter force mains, the minimum 2 feet per second (ft/s) wastewater flow velocity requirement and 10 ft/s maximum velocity guideline can be maintained in the force mains during any operating scenario except Scenario 3, and the wide range of design wastewater flows can also be potentially satisfied using a single set of pumping units. Since the minimum flushing velocity cannot be maintained in Scenario 3, utilization of this operating scenario is not recommended. As is summarized in Table 2 below, the variation in the total dynamic head created when pumping into the different combination of force mains effectively shifts the operating point of the pumping units and provides for a significant variation in discharge rates depending upon the pump and force main scenario. For example, a firm pumping capacity of up to 206 gpm can be provided by the initial set of pumping units when utilizing both the 4-inch and 6-inch diameter force mains. (see Scenario 2, Tble. 2). A pumping capacity of 206 gpm is equivalent to the design flows from approximately 411 dwelling units. (Table 3). P:BOZ_07004_05_Eng—Rprt 4 (03/22/10)CN/tsc Table 2—Lift Station Confi uration and C sponding Design Capacity FM FM Pumping FM FM Firm Pumps Velocity Velocity TDH Pumping Scenario Installed Status Status Rate 4" 6" (ft) Capacity 4" 6" (gPm) ft/s ft/s m 121.5 nPell . 6SCC J m 2G 1 121.5 Open Closed 12 1.5 3.08 NA 46 '121.5 2@ 2 121.5 Closed Open 206 NA 2.34 15 206 2@ 3 121.5 Open Open 223 1.46* 1.88* 9 223 m n 178/ca 2:33 6 2 @m75 gp Closed Open 498 NA 5.65 98 498 7 2 @ 1375 Open Open 586 3.83 4.94 79 586 3- 375 8 m Closed Open 305/ea NA 6.93 140 610 3 C 375 Open Open 382/ca 5.01 6.45 123 764 *Does not provide 2 ft/sec flushing velocity. Utilization of this operating scenario is not recommended. P:B0Z_07004_05_Eng_Rprt 5 (03/22/10)CN/tsc Table 3 estimates the number of dwelling units that could be serviced by the particular pumping unit and force main combinations presented in Table 2. Table 3 assumes a general dwelling unit population of 2.11 persons, a per capita wastewater flow of 89 gpm, and uses Equation 1.0 to determine the peak hourly to average day wastewater flow ratio. Table 3—Dwelling Unit Threshold per Lift Station Configuration Scenario Firm Pumping Capacity Approximate Approx. No. of Dwelling mr Po ulation Units Served 34 2 206 868 411 3 223 945 448 621) 5 7 41505 742 6 498 2,276 1,079 7 0 2,725 1,291 8 G 10 2,853 1135 (NOTE: In order to better estimate design flows for future phases of development, it will be extremely important to monitor the wastewater flows from the Phase I so that actual flowrate data is used as the basis of design. Some modification tQ the design flow at full build-out will likely be seen based on the flows actually occurring in the existing developed phases). 4.3 Wet Well The wet well is sized to allow the installation of a tri-plex pump configuration as shown in the project drawings. The configuration of the lift station discharge piping has also been configured with an external connection point for the discharge piping of a portable pumping unit that may be installed by the City of Bozeman during emergency conditions. The wet well is sized to allow the pumping units to remain submerged below the "pump off' level; to provide for the working pump on and off volume; to allow for an equalizing storage volume; and to allow for an emergency volume between the top of the equalizing volume and invert of the influent pipe. Given the anticipated high ground water conditions, special consideration must also be given to buoyancy forces and mitigation measures to offset these forces, as discussed in Section 4.3.3 below. 4.3.1 Equalizing Storage As was mentioned in Section 2 above, a 121.5 gpm pumping rate limitation will be in place through the first phase of development at Norton Ranch. P:B0Z_07004_05_Fng_Rprt 6 (03/22/10)CN/tsc The design rate for the first phase equals 165 gpm. Therefore, the initial pumping units will theoretically not be able to satisfy the peak hour flow conditions, and equalizing storage must be provided to store the volume of wastewater equivalent to the deficit pumping capacity. The peak hourly flow is defined as the peak sustained hourly flowrate occurring during a 24-hour period based on annual operating data (Metcalf& Eddy). It is unlikely that the diurnal wastewater flow curve is proportionate to this peak hourly flow. Rather, this once per year peak hourly flow would be seen as a spike at the apex of the typical diurnal flow pattern where normal flows that would typically occur over several hours in a day coincide within a single hour. As per the design calculations made in Section 2, the peak hourly domestic flow of 161 gpm represents 3.92 times the average day flow of 41 gpm. The flows seen either before or after the peak hourly spike are assumed equal to typical daily flows leading up to, or directing following, the maximum hourly flow. The typical maximum hour wastewater flow in a 24-hour period could conservatively be estimated as being between 150 to 225 percent of average flows; which, in this case, would be equal to 62 gpm to 92 gpm. Since our 134 gpm allowable pumping capacity is 327 percent of average daily flow, the 121.5 gpm pumping capacity will be greater than the flows leading up to or following the peak hourly flow, so a pumping unit with a 121.5 gpm pumping rate would "catch up" to the incoming sewage flow without the need to provide additional equalizing storage volume beyond the product of the deficit pumping capacity times the one-hour period of the peak hourly flow. The required equalizing storage volume then becomes: (1650m— 121.5gpm) *60 minutes= 2,610gallons 4.3.2 Working Volumes and Pump Cycling The working volume in the wet well between the pump on and off levels must be less than the average day flow times 30 minutes (as per DEQ design standards) to prevent septic conditions from occurring, but be large enough to allow the pumps enough run time to promote motor cooling and to limit the number of pump starts per hour. To fall within these parameters, a proposed working volume of 441 gallons is being proposed initially;which, in an 8.0 foot diameter wet well, is equivalent to 1.1 feet. A volume of 441 gallons will accommodate the Phase IA scenario and this volume is equal to the average day flow of 14.7 gpm times 30 minutes. With this working volume, and based on the initial 121.5 gpm firm pumping capacity minus the 14.7 gpm filling rate, the pump cycle time will equal the following: RBO7_07004_05_i ng—Rprt 7 (03/22/10)CN/tsc Pumping -441 gallons/(121.5-14.7)Om = 4.1 minutes +Filling -441 gallons/14.7gpm = 30 minutes Pump cycle time = 34.1 minutes A pumping time of 4.1 minutes will provide adequate motor cooling time based on typical industry recommendations, and a pump cycle time of 34.1 minutes translates to 1.76 pump starts per hour in a duplex pumping station with alternating first "pump on" call. Flygt recommends no more than 15 starts per hour. The volume provided the initial working volume and the required equalizing storage volume equals 3,051 gallons, which represents approximately 8.1 feet of separation in the proposed 8-foot diameter wet well. As was mentioned in Section 2 above, subsequent phases beyond the original Phase I of the Norton Ranch development will have new sewer collection system infrastructure in place to accommodate a lift station pumping rate equal to future design flows. Therefore, no equalizing storage will be needed in the future and the working volume can be set anywhere between the initial 441 gallons and the 3,051 gallon wet well volume. For this application and as shown in Table 4, it is assumed that the working volume will equal 441 gallons for Phases I and IA; and then be increased to the product of 30 minutes times the average day flow for Scenarios 2-5; and to 3,051 gallons for the remaining phases. The cycle times shown in Table 4 are based on the pumping configuration scenarios presented in Tables 2 and 3. Table 4-Puni in Cycle Times per Lift Station PumpingCa acity Net Approx. Peak Ave. Pumping Pumping Firm No. of Pumping Filling Approx. Hr/Ave. Day Cycle Cycles Scenario Pumping Dwelling Duration Duration Pop. Day Flow Duration per Hour Capacity Units Ratio (gpm) (min) (min) (min) (duplex) m 1 Served 2** 152 868 411 3.84 54 10.6 30.0 40.6 1.5 3** 0357 945 448 3.82 58 10.6 30.0 40.6 1.5 1.5 1.5 6*** 2,276 1,079 3.54 141 6.4 16.3 22.7 2.6 7*** 2,725 1,291 3.48 168 5.5 13.7 19.2 3.1 8�** 434 2,853 1,352 3.46- .3 13.1 18.4 3.3 9*** _ 537 _lam 1 738 3.3 - = 4.2 1 Net firm pumping capacity equals firm pumping capacity minus filling rate. Filling rate equals average day flow. * Pumping cycle based on 441 gallon working volume. ** Pumping cycle based on 30 min.times ave.day flow. *** Pumping cycles based on 3,051 gallon working volume. P:BOZ_07004_05_Eng-Rprt 8 (03/22/10)CN/tsc Table 5 shows the wet well operating levels, and required working volume and equalizing storage volume for each scenario. All elevations are preceded by 47xx.xx. Table 5- Wet Well O eratina Levels &Re uired Working and Equa . 1.1 0 Storage Volumes Required Required Wet Well Normal Lead Lag High Influent Workin Equalizing Bottom "Pump "Pump "Pump Level Invert Scenario g Storage Off' On" On" Alarm Elevation Volume Elevation Volume Elevation Elevation Elevation Elevation De th (gal) al (Depth) (Depth) (Depth) (Depth) a th ( p ) ,G10 45'9A 47.98 49.15 5.6.30 56.60 56. 19, 2 1,620 0 45.93 47.98 52.29 56.30 56.60 56.87 19.76 17.71 (13.40) (9.39) (9.09) 8.82 3 1,740 0 45.93 47.98 52.61 56.30 56.60 56.87 19.76 17.71 13.08 9.39 9.09 8.82 4 2'400 1 1" 19.76) {17.71) (11.17)_ (9.39' (9.09) (8 45.93 47.9�i 55.72 56.3ti 56.Gt1 5: .9i. a.39 Lan- 6.$2 6 3,051 p 45.93 47.98 56.09 56.30 56.60 56.87 19.76 17.71 9.60 9.39 9.09) 8.82 7 3,051 0 45.93 47.98 56.09 56.30 56.60 56.87 19.76 17.71 (9.6f 1 9.39 9.09) 8.82 8- - - - 3,051 0 56.09 5 . 6.60 9] .76 17.71 9.60 9.39) 9.Q9 8.82) 9 3,051 MOW 45.93 47.98 56.09 56.30 56.60 56.87 .76 17.71) 9.G0 9.39 9.09 8.82 4.3.3 Buoyancy To be conservative, buoyancy force calculations were made assuming that the wet well would be submerged to the highest measured groundwater level. The buoyancy force was then compared to the weight of the wet well to determine if additional measures are needed to prevent vertical displacement of the wet well. As can be seen in the buoyancy calculation provided in the Appendix, the weight of the wet well is not, by itself, adequate to offset the buoyancy force. As such, the monolithic base of the wet well will be extended beyond the barrel outside diameter 6 inches. The additional force provided by the soil acting on this extended base section is great enough to offset the buoyancy force when combined with the weight of the wet well. P:BOZ-07004-05-Eng-Rprt 9 (03/22/10)CN/tsc APPENDIX P:BOZ_07004_05_Eng—Rprt 10 (03/22/10)CN/tsc SANDERSON t!•� STEWART lax 8 , gnu G� � rc l C- 47 6s•6 5 r r 6-w l sC z3q �l�l6 `may �r+a, � �+ 4u- 5�� ��� �� �C9,��J/� • e �7 Aso 3) V / ac , ,KS it 4c. / PROJECT /1���C+^ Gi GS JOB �o7,-D70W.a-7 DATE _S BY SHEET / OF L www.sandersonstewart.com IO�, SANDERSON t�•� STEWART �)bri%z n 17)L 360 7 3 7Ca 045 71 ✓� G✓�� �I c�" /�H.y/l�/ /J� 41 cIAVA�,.ca o, s �j�f�� �n ��r rat it r✓' ��SC �,,�v.,t t"./c./C�C.� u'a /�✓t a��`p�c^�" PROJECT A Co , ����l LS JOB 66e ' 670 DATE 1Z6/ia BY e-Ar SHEET Z OF z www.sandersonstewart.com 10 -kNDERSON 40 STEWART �= 2.4d4 ���� 5� Iv G✓P I DPI— a7i''�� hew" s 7./�,rQ qC l�o�S �LiaSe �lA ,� ore�v ) �.� IA — f-136.30 f�s�ac � 4710- 15 17. 7 -fo ✓1 CA Li JOB �ayD�oolr a7 DATE 3/zolio BY c� SHEET l OF PROJECT�iM ° fj vwvw.sandersonstewart.com AMD ,,. ANDERSON W49 STEWART jQaua� � Z C v1A) 47 0-4 ibz�f� ll �7��•g8 lVd a�A PROJECT i✓a✓ Li JOB So-7-0700'� 0'7 DATE 3/?Olio BY eAJ SHEET 1, OF 6 www.sandersonstewart.com All ANDERSON t_•,7 STEWART Tlr dU i4�14 7 ��J°� PROJECT 14 0' L JOB 6o7--o7a0t-o'7 DATE 3/?0ll o BY SHEET OF Fj www.sandersonstewart.com ,ANDERSON V,7 STEWART h177 7 � - !✓e7 ✓�-�gCJ�F/ �5 kC�v.�y .' 7, 4$C � lee�O�Hw s C PROJECT A✓ 0� Gi JOB 9o7--07oW- o'7 DATE 3/?Olio BY SHEET 4 OF 6 www.sandersonstewart.com kNDERSON t_•,7 STEWART ,Z/N`=` ��( 1�77 77��� � !✓�� �✓�-`� �/�Pl�� kCy.�.X y .� s,�Q$C Vas 40 y-755.-7z v PROJECT i✓u� �� �` G� JOB So7--D70� 0'7 DATE ;/zo))o BY cAJ SHEET OF 6 www.sandersonstewart.com SAN D E RSO N t # STEWART �v ' Ad C PROJECT A4- -4 0l Li JOB So7­07oW- 07 DATE 3/zo)i0 BY e-AJ SHEET (p OF www.sandersonstewart.com FLYGT Technical specification Submersible pump 6 3060, 60 Hz _ Flygt �& ITT Industries FLYGT BIRO 3060 VFD Application NSSHOU.J3E+St 3x2,5+3x2,5/3E+3x1,5 St :.� Monitoring equipment Thermal contacts opening temperature 125°C r / _ Material 4 Impeller Stainless sleet - Pump housing Stainless steel Stator housing Stainless steel 5 ,F Shaft Stainless steel 0-rings Fluorinated rubber '$ } Mechanical face seals 1. Alternative Inner seal Outer seal CarboNAluminlum Aluminlumoxlde/ to h, oxide Aluminium oxide 2 Silicon carbide/ Silicon carbide/ B I B O 3060 Silicon carbide Silicon carbide 3 Aluminium oxide/ Aluminium oxide/ Corrosion resistant Corrosion resistant cemented carbide cemented carbide Product Weight Submersible pump for use In highly corrosive industrial waste water. Sea dimensional drawing. Denomination Option Product code 3060.390 Other cables. Installation S Impeller characteristics IT Accessories Process data Discharge connections,adapters,hose connections and other mechanical accessories. Liquid temperature max+40`C Electrical accessories such as pump controller,control panels,starters, Depth of immersion max 20 m monitoring relays,cables. The pH of the pumped liquid pH 3-12 See separate booklet or www.flygi.com,for further Information Liquid density max.1100 kg/m3 Motor data Frequency 60 Hz Insulation class H(+180°C) Voltage variation continuously running max t b% Intermittent running max±10% Voltage imbalance between phases max 2% No.of starts/hour max 15 Strainer hole size(MT) 12 mm Cable Direct-on-line start SUSCAB® 401,5 mm2 4G1,5+2xl,5 mm2 4G2,5 mm2 4G2,5+2x1,5 mm2 3 FI4YGT B/BO 3060 Dimensional drawing All drawings are available as Acrobat documents(.pdf) and AutoCad drawings(.dwg).Download the drawings from www.flygt.com or contact your ITT Flygt representative for more information. All dimensions are in mm. LT, S-installation wesm run�.v wn,Y 410 ■ww+rwg 160 wx sa PJ I 10130 I i gal V .7 c4ii 'rig 4 gyp W_MRd CY�.7aA WT W H 4 1 PRODUCT TYPE PERFORMANCE CURVE CP3060.390 MT DATE PROJECT CURVE NO ISSUE 2010-03-12 63-226-00-0525 4 1/1-LOAD 314-LOAD 112-LOAD RATED IMPELLER DIAMETER POWER..... 3.6 hp 101 mm POWER FACTOR 0.93 0.91 0.87 STARTING EFFICIENCY 77.0% 79.0% 78.0% CURRENT... 25 A MOTOR# STATOR REV RATED 14-10-2AF 37YSER 11 MOTOR DATA -•- --- -- CURRENT... 4.7 A COMMENTS INLET/OUTLET RATED FREQ. 1PHASES1 VOLTAGE POLES -12.5 inch TO MOM.OF 3410 rpm T 60Hzj 3 1 460 V 2 IMP.THROUGHLET INERTIA... 0.0052 kgm2 GEARTYPI RATIO NO.OF --- BLADES 2 - - I --- [hp] ------- 3.0 - -- r 1 �_ Lu r O 2.0 CL I w w 1.5 J -' LL DUTY-POINT FLOWIUSgpm] HEAD[ft] POWER[hp] EFF.[%] NPSHrelfl] p 1 121 46.0 3.00(2.41) 46.7 (59.2) B.E.P. 132 42.1 2.99(2.36) 47.0 (59.6) IN - a (L LL w W 70• - _ _— - W m 60 EFF. 50 50 W = 40 — ---— - 40 30 --- / \ 30 20 / — 20 Co 10 10 Ln 0 <o cco)v M 0 0 0 40 80 120 160 200 [USgpm] FLOW LL FL G H I B C u rve Performance with clear water and ambient temp 40°C