south arm peninsula irrigation water pipeline - network ... · this report outlines the development...

South Arm Peninsula Irrigation Water Pipeline - Network Analysis Report

2018

SYSTEM NETWORK MODEL DEVELOPMENT ALLAN BOASE

IMPACT BLUE PTY LTD | 49 Blessington Street, South Arm, Tasmania, 7022

Mary Ann’s Island Pty Ltd (ACN 141 272 568)

ARM END RECREATION RESERVE South Arm Peninsula Irrigation Water Pipeline Network Analysis Report

Impact Blue Pty Ltd 1 | P a g e

Contents EXECUTIVE SUMMARY ......................................................................................................................................... 2

BACKGROUND ..................................................................................................................................................... 4

MODEL SELECTION .............................................................................................................................................. 5

SYSTEM CONFIGURATION ................................................................................................................................... 6

EXTENDED PERIOD SIMULATION ......................................................................................................................... 8

NODE DEMANDS & PATTERNS ............................................................................................................................ 8

RESULTS ............................................................................................................................................................... 9

DISCUSSION ....................................................................................................................................................... 16

CONCLUSIONS ................................................................................................................................................... 18

RECOMMENDATIONS ........................................................................................................................................ 19

Author Details .................................................................................................................................................... 19

References ......................................................................................................................................................... 19

APPENDICES ....................................................................................................................................................... 20

A. Typical Model Output Report ................................................................................................................ 20

B. Pipeline Locality Plan ............................................................................................................................. 20

C. Network Model Schematic .................................................................................................................... 20



EXECUTIVE SUMMARY The Proposal

MARY ANN'S ISLAND PTY LTD (ACN 141 272 568), acting as the development proponent and management entity for the pipeline and the Arm End Recreation Reserve, has requested a network analysis report for the proposed South Arm Peninsula Irrigation Water Pipeline. Impact Blue Pty Ltd (ACN 116 083 311) has developed a network model to help confirm the engineering feasibility of a new pipeline to supply a scheme to re-use effluent from the TasWater Blackman’s Bay Treatment Plant. Water availability is a key issue for both the Arm End Recreation Reserve and other potential irrigator’s on the South Arm Peninsula.

This report outlines the development and potential use of a dynamic network analysis model for the pipeline proposal and discusses key engineering findings. The focus of the Network Analysis Report is the hydraulic assessment of an area wide system to meet South Arm Peninsula to needs, in stages. The primary pipeline route from Blackman’s Bay to Arm End in fact passes directly by the properties of a number of potential major users. A southerly branch from the Half Moon Bay Pump Station could supply the balance of the users and can be staged. The provision of connections and the balancing storage capacity needed to optimise the system can also be implemented progressively. The South Arm Peninsula Irrigation Water Pipeline system layout is shown in Figure 1.

Method of Analysis

Steady State Hydraulic Modelling was based on the use of KYPIPE 2018 software from the University of Kentucky. KYPIPE software was chosen because of its wide usage for water network analysis and to undertake dynamic extended period simulations of a system where fluctuating demands and extensive water storage behaviour is important. By using an Extended Period Simulation of 72 hours for this report, we observed the time related behaviour of significant water storages in this system, including the Arm End Storage Tanks, and sequences of pump operations under time varying demand patterns. The maximum golf turf irrigation demand was assumed to be 56L/s for four hours, a peak day requirement of 800,000 litres, 0.8ML. The report also discusses the potential for Cavitation at Blatherwick Rise, Energy Recovery from the Pipeline Arm End Storage Tank Behaviour.

Climate Change and South Arm Peninsula

South Arm Peninsula agriculture and living is vulnerable to low rainfall compared to the Hobart Region and at present lacks any formal public water supply. Recent climate change research published in the 2018 book Sunburnt Country, by Dr. Joelle Gergis at the University of Melbourne (Gergis, 2018) notes that Hobart is part of a southern region where there has already been an observed long term drying trend, characterised by a 10-20 percent reduction in average cool season (April-September) rainfall. As the CSIRO expect the region to experience more drought periods in future, there will be less rainfall for agriculture and ecosystems services. In view of these risks and vulnerabilities, Gergis contends that transformational, rather than incremental, climate change adaptations will be required in the southern region of Australia. For the South Arm Peninsula, this project represents such a transformational initiative.

Engineering Findings

There is technically sustainable evidence that the proponent can construct an irrigation water pipeline system, in stages, that will provides extensive access to Class ‘B’ effluent for irrigation purposes to landowners, farmers and organisations across the South Arm Peninsula. Results show that there is capacity in the Half Moon Bay Pump Station to also support future expansion of the irrigation supply if warranted by additional irrigation user or community demand. Back-up fire water supply to tanks at South Arm and Opossum Bay could also be achieved, subject to point of use treatment to Class ‘A’, which allows for a wider ranges of uses. For example,



Clarence City Council could use this irrigation water supply for the establishment and long term maintenance of the landscaping associated with their adopted Master Plan for facilities at Calverton Oval / South Arm Community Centre. In addition, Council support for this infrastructure project would assist the initiation of a significant and potentially transformational climate change adaptation for the South Arm Peninsula.

A combination of two major booster station is required to meet the irrigation demands of the Arm End Recreation Reserve site during an extended dry period. However, short term peak requirements would usually be met from the Arm End storage tanks and less pumping required. Minor flows can be supplied to the South Arm Peninsula by gravity from the Blackman’s Bay Balance Tank. Full site water demands for Arm End Recreation Reserve and all other potential users can be met by this system.

Reduced From Blackmans Bay Treatment Plant Discharges to River Derwent

To the extent that South Arm Peninsula co-operative irrigation users participate, future River Derwent discharge volumes by TasWater can also be reduced relative to their current projections and thereby reduce the existing outfall’s marine environment impacts. The scheme proposed will reduce effluent discharge volumes by up to 20% in the immediate future with attendant short term environmental benefits on water quality and ecosystem health. Notwithstanding the permanent diversion of up to 350ML/annum away from river discharge, the percentage reduction in discharge will slowly decline over time, as the Blackman’s Bay Treatment Plant effluent volumes increase to the projected design capacity.

Overall Findings

The proposed SAP effluent irrigation water supply network is feasible from both hydraulic and engineering perspectives based on the network modelling of proposed full system development undertaken for this report. It addresses SAP climate change adaptation and reduces projected future river effluent discharge environmental impacts.

Modelling undertaken also demonstrates that by scheduling user supply delivery times and effective use of balancing water storages, an optimum conjunctive use scheme can be developed based on the anchor irrigation needs of the Arm End Recreation Reserve site and the South Arm RSL / Iron Pot Golf Club.

The modelling studies provide an advanced tool for the future management of a co-operative effluent re-use scheme based on the SAP Irrigation Water Pipeline. To maximise the potential planning and operational benefits of the conceptual network model, several specific model refinements are recommended to the proponent for both the detailed design and operations phases of the project.



BACKGROUND South Arm Peninsula Irrigation Water Pipeline

MARY ANN'S ISLAND PTY LTD (ACN 141 272 568), acting as the development proponent and management entity for the pipeline and the Arm End Recreation Reserve, has requested a network analysis report for the proposed South Arm Peninsula Irrigation Water Pipeline. Impact Blue Pty Ltd (ACN 116 083 311) has developed a network model to help confirm the engineering feasibility of a new pipeline to supply a scheme to re-use effluent from the TasWater Blackman’s Bay Treatment Plant. Water availability is a key issue for both the Arm End Recreation Reserve and other potential irrigator’s on the South Arm Peninsula. This report outlines the development and potential use of a dynamic network analysis model for the pipeline proposal and discusses key engineering findings.

This water option emerged from water source investigations for Arm End Recreation Reserve rehabilitation and development for public recreation as the most sustainable and environmentally and cost-effective way of bringing water to Arm End. Other water solutions, including a pipeline from Droughty Point, groundwater, desalination, solar/condensation and trucking in the water were considered. The water pipeline proposed will employ and use the valuable resource suited to various existing and future irrigation needs of South Arm Peninsula, and reduce the quantity of effluent disposed via submarine outfall to the River Derwent Estuary and the associated environmental impacts of such direct discharge at Blackman’s Bay.

A number of potential significant users of recycled effluent are identified on South Arm Peninsula and infrastructure that facilitates the conveyance of this resource to the Arm End site will also have the capacity to supply these users. In particular, it is envisaged that the following uses could be conjunctive users:

• Arm End site water demands, including turf irrigation; • Calverton Oval Master Plan landscaping and oval irrigation; • RSL Community Club and Iron Pot Golf Course water demands; • Specialist small scale market produce water needs; • Farmers: revegetation or replanting large areas with native or productive plantings to achieve

diversification and sustainability; • Land owners for landscaping. • Access to water adds value to land generally.

Separate hydraulic assessments of the primary water pipeline, to meet Arm End needs only, have also been undertaken by others to form part of the design studies. The focus of this Network Analysis Report is the assessment of an area wide system that could be engineered for South Arm Peninsula to meet all of the above needs, in stages. The primary pipeline route from Blackman’s Bay to Arm End in fact passes directly by the properties of potential major users. A southerly branch from the Half Moon Bay Pump Station could also supply the balance of the possible users and also be readily staged. The provision of the balancing storage capacity needed to optimise the system can also be implemented progressively.



MODEL SELECTION The method of analysis adopted for Steady State Hydraulic Modelling was based on the use of the KYPIPE 2018 software suite from the University of Kentucky. This was chosen because of its wide usage for public water network analysis and the potential for use of its graphical user interface to undertake dynamic extended period simulations of systems where fluctuating demands and extensive water storage behaviour is important.

KYPIPE software is based on solving the full set of mass continuity and energy equations, utilizing efficient linearization schemes to handle non-linear terms and a very powerful spare matrix routine developed by A.R. Curtis and J.K. Reid of the Theoretical Physics Division, UKAEA Research Group, Harwell, England. This approach accommodates elements such as closed lines, check valves, and regulating valves in a direct and very efficient manner. The approach also effectively handles data with widely varying parameter values. Extensive testing of various algorithms for pipe network analysis led to the conclusions that the approach used by KYPIPE is the most powerful and has the best convergence characteristic of the commonly used approaches.

References:

1. Wood, D. J. and Rayes, A.G. "Reliability of algorithms for pipe network analysis." J. Hydr. Div. ASCE, 107(10), 1145-1161. (1981)

2. Wood, D. J. KYPIPE Reference Manual, Civil Engineering Software Center, University of Kentucky (1985)

The KYPIPE software engine has been developed to calculate steady state flows and pressures for piped water distribution systems. The engine can be applied to any liquid, including effluent. The engine is written to accommodate any piping configuration and a wide variety of hydraulic components such as pumps, valves (including check valves and regulating valves), any component or fitting which produces significant head loss (such as elbows, orifices, etc.), flow meters and storage tanks. Computations can be carried out using SI units.

The most obvious simplification is to model a skeletonized distribution system comprised of fewer pipes than the actual system. The most common method of skeletonizing the distribution system is to only consider pipes above a certain minimum size. If this is done, flow demands for the regions not considered are shown at junctions in the vicinity of these regions. Also, it is often possible to eliminate tree type pipe regions from a system. Demands to these regions can be specified at junctions leading to the region eliminated.



SYSTEM CONFIGURATION Description of System

The South Arm Peninsula Irrigation Water Pipeline system is described by the input data shown in Appendix A and will ultimately comprise the following key elements (subject to final design confirmation):

• Balance Tank at Blackman’s Bay Treatment Plant; (R-1) • Blackmans Bay TP Effluent Pump Station; (PUMP-3) • River Derwent Submarine Pipe (225mm diameter); (P-2 to P-8) • Half Moon Bay Booster Pump Station; (PUMP-1) • Half Moon Bay to Arm End Pipe (225mm and 160mm, directional drilling) (P-10 to P-17) • Half Moon Bay to Iron Pot Pipe (160mm and 125mm, directional drilling) (P-19 to P-21) • Protea Farm Storage Tank; (T-19) • Arm End Storage Tanks (2 x 2ML each) (T-1) • Iron Pot Golf Course Storage Dam (J-1) • Various small diameter branch lines and small storages.

The model designations for each of these key elements are shown in brackets above and use the following type prefixes:

• R= Reservoir with a fixed grade; • T=Storage Tank with altitude valve; • P=Pipe, key system pipe links between nodes; • J=Junction, a node where user demands, branch connections or system elements are located; and • PUMP= Booster Pump Station.

The proposed layout of the primary SAP irrigation water pipeline is shown in Figure 1 and Appendix B.

Figure 1: SAP Irrigation Water Pipeline Route



The network model for the whole of South Arm Peninsula has been skeletonised and configured by diameter as shown in Figure 2. Details of the model, including pipe link and node identification are also shown in more detail in Appendix C.

Figure 2: Schematic Network Model Layout

Arm End Storage Tanks

South Arm RSL / Iron Pot GC

Blackman’s Bay TP

River Derwent

SAP / Clarence CC

Kingborough CC



EXTENDED PERIOD SIMULATION The KYPIPE engine is used to complete an extended period simulation (EPS) considering storage tank levels which vary over the simulation period. Storage tanks of any shape have upper and lower surface levels which define the range of operation of the tanks. Lines leading to storage tanks will close if the liquid surface levels reach these limits (altitude valve). As a feature of the extended period simulation the open-closed status of designated pipes may be controlled by the hydraulic grade line at a specified location in the network (pressure switch). This feature will allow, for example, bringing a booster pump on line if the pressure at a specified location drops below a specified switching value. This pump will then operate until the pressure is increased above a second specified value. The same feature can be employed to use the water level in a storage tank to control a pump.

NODE DEMANDS & PATTERNS The model developed can be executed with a variety of diurnal demand patterns and active demand nodes. The number of user nodes will vary over time, as this system develops in stages. In particular, it is assumed that the main demand node at Arm End will reflect a four hour off-peak irrigation pumping cycle (12am to 4am to allow drying out before play). This will be drawn mainly from the storage tanks on site by separate independent golf course booster pumps, with the tank being refilled throughout the day by the system and pipeline booster pump stations. Similar demand patterns are also applied to other irrigation user nodes and a diurnal residential pattern is applied to any village landscaping areas served. These patterns utilise both a base demand and time variable peaking factors, across each 24 hour cycle.

The maximum golf demand is assumed to be approximately 56L/s for four hours, corresponding to a peak day requirement of 800,000 litres, 0.8ML. Demand is estimated pro-rata for the smaller Iron Pot Golf course at South Arm and other allowances made for known potential irrigators. The full range of demands for a fully developed scheme are shown in the report and data input files included herein and in Appendix A.

A variety of indicative user demands have been allocated for modelling purposes to potential user connection nodes across the network. These allocations may be refined as specific requirements are confirmed in due course. It is noted that these demands are each subject to various seasonal and diurnal timing and hence the applied demands take such utilisation factors into account.

Current model demand settings, by node, in L/sec are: • J-9: 28; Arm End Irrigation Pump Station Offtake • J-1: 5; South Arm RSL and Iron Pot Golf Course • J-14: 2; Opossum Bay Farms • J-18: 0.14; Protea Farm • J-25: 0.24; South Arm Road, Fire Station • J-24: 1 ; Calverton Oval • J-27: 0.05 Fort Direction Road South • J-28: 0.24 Blessington Street South

By using EPS for at least 72 hours for the purpose of this report, to predict responses under a worst case simultaneous peak demand scenario, we observe the key time-related behaviour of significant water storages in this system, including the Arm End Storage Tanks, under time varying demand patterns. Such analysis also helps to verify the selection of elements and design parameters to confirm their engineering requirements.



RESULTS The full results file for a 72 hour simulation of the entire pipeline network is shown in Appendix A. Typical summary results and data are as follows:

Pipe Summary

P I P E L I N E D A T A The model includes 32 key pipes at this stage supplying the whole of South Arm Peninsula. This model has been based on the use of 160mm nominal diameter pipe north of the Blatherwick Rise. Pump curves were adjusted to offset this change from an earlier analysis with larger supply mains.

Node Summary

N O D E D A T A The model is configured with 30 nodes at this stage plus two booster pump stations, each with an inlet and outlet node. Node demands specified are internally subject to demand patterns and associated hourly peaking factors during the extended period analysis.

Pump Summary

P U M P/L O S S E L E M E N T D A T A THERE IS A DEVICE AT NODE Pump-1 DESCRIBED BY THE FOLLOWING PUMP CURVE DATA: (ID= 11) HEAD FLOWRATE EFFICIENCY (m) (l/s) (%) 75.00 0.00 75.00 (Default) 68.00 18.00 75.00 (Default) 63.00 27.00 75.00 (Default) 55.00 33.00 75.00 (Default) 50.00 37.00 75.00 (Default) 40.00 43.00 75.00 (Default) 35.00 45.00 75.00 (Default) 30.00 47.00 75.00 (Default) THERE IS A DEVICE AT NODE Pump-3 DESCRIBED BY THE FOLLOWING PUMP CURVE DATA: (ID= 33) HEAD FLOWRATE EFFICIENCY (m) (l/s) (%) 75.00 0.00 75.00 (Default) 65.00 25.00 75.00 (Default) 60.00 35.00 75.00 (Default) 55.00 40.00 75.00 (Default) 40.00 48.00 75.00 (Default) 25.00 50.00 75.00 (Default) P U M P / L O S S E L E M E N T R E S U L T S This table shows the model pumping solutions to meet the assumed demand scenario. The information in columns 2 and 5 show the pump duty points applicable for each booster pump station, at various times throughout the EPS. The model has assumed a single pump at each booster pump station run to satisfy the required duty points. Final selections should consider other equivalent combinations of pumps with VSD controllers to achieve the standby and duty requirements, while maximising flexibility and efficiency at the minimum operational cost.



INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 43.10 2.22 42.00 39.8 75.00 17. 0.0 0.0 ** ** 12.2 0.0001 Pump-3 43.10 2.62 52.56 49.9 75.00 21. 0.0 0.0 ** ** 12.7 0.0001 Pump-1 43.14 2.03 41.71 39.7 75.00 17. 0.3 0.3 ** ** 12.1 0.1410 Pump-3 43.14 2.62 52.48 49.9 75.00 21. 0.4 0.4 ** ** 12.7 0.1410 Pump-1 40.63 12.96 58.04 45.1 75.00 18. 0.0 0.3 ** ** 23.0 0.1412 Pump-3 40.63 2.66 56.72 54.1 75.00 22. 0.0 0.4 ** ** 12.7 0.1412 Pump-1 40.52 13.41 58.70 45.3 75.00 18. 0.2 0.6 ** ** 23.4 0.2464 Pump-3 40.52 2.66 56.89 54.2 75.00 22. 0.3 0.7 ** ** 12.7 0.2464 Pump-1 34.46 34.40 87.57 53.2 75.00 18. 0.0 0.6 ** ** 44.5 0.2466 Pump-3 34.46 2.76 63.21 60.5 75.00 20. 0.0 0.7 ** ** 12.8 0.2466 Pump-1 29.81 46.51 106.19 59.7 75.00 17. 0.2 25.8 ** ** 56.6 11.1015 Pump-3 29.81 2.82 65.45 62.6 75.00 18. 0.2 27.9 ** ** 12.9 11.1015 Pump-1 11.88 81.10 152.07 71.0 75.00 8. 0.0 25.8 ** ** 91.2 11.1017 Pump-3 11.88 2.97 73.89 70.9 75.00 8. 0.0 27.9 ** ** 13.1 11.1017 Pump-1 29.05 48.39 109.05 60.7 75.00 17. 2.2 65.2 ** ** 58.5 34.9472 Pump-3 29.05 2.83 65.84 63.0 75.00 18. 2.2 69.2 ** ** 12.9 34.9472 Pump-1 10.68 82.64 154.14 71.5 75.00 7. 0.0 65.2 ** ** 92.8 34.9474 Pump-3 10.68 2.98 74.39 71.4 75.00 7. 0.0 69.2 ** ** 13.1 34.9474 Pump-1 29.05 48.39 109.05 60.7 75.00 17. 2.2 103.5 ** ** 58.5 58.9472 Pump-3 29.05 2.83 65.84 63.0 75.00 18. 2.2 109.5 ** ** 12.9 58.9472 Pump-1 10.68 82.64 154.14 71.5 75.00 7. 0.0 103.5 ** ** 92.8 58.9474 Pump-3 10.68 2.98 74.39 71.4 75.00 7. 0.0 109.5 ** ** 13.1 58.9474 Pump-1 34.57 34.07 87.10 53.0 75.00 18. 1.0 116.4 ** ** 44.1 72.0000 Pump-3 34.57 2.75 63.12 60.4 75.00 20. 1.0 122.4 ** ** 12.8 72.0000

The EPS plot in Figure 3 shows time changes in pump duties over an extended period simulation cycle. A residential demand pattern is superimposed for certain nodes in the first twenty-four hours to represent the impact of other possible small users on the SAP.

Tank Summary

V A R I A B L E H E A D T A N K D A T A

TANK MAXIMUM MINIMUM TANK INITIAL EXTERNAL NAME ELEVATION ELEVATION CAPACITY VOLUME FLOW (*) m m lts lts lps ------------------------------------------------------------------------------ T-1(1) 13.00 7.00 1884960. 1884960. 0.00 T-2(1) 44.00 42.00 14137. 14137. 0.00 T-19(1) 25.00 22.00 21206. 7069. 0.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA

The detailed hour by hour status of each variable head tank is reported in an Extended Period Simulation. Tank water levels, remaining capacity and draining /filling status are included for each time step. These detailed results are included in Appendix A. A typical example of this output is included for T-1 (Arm End Storage Tanks) also in Figure 3 below.

The pipe link flows experienced for each simulation period time-step are shown in Appendix A. Key pipe link flow variations, over 72 hours for a peak demand period, are shown in Figure 4.



Figure 3: 72 Hr Behaviour of Key System Elements at Peak Demand Period

Half Moon Bay Booster Pump Station (72h) (Capacity is available to add other users)

Arm End Storage Tanks (72h) (Tanks re-fill during day, after golf irrigation )

Iron Pot Golf Club Dam (72h) (Drawn direct from mains – ignoring dam)

Arm End Irrigation Booster Pumps (72h) (4 Hour Golf Irrigation at Night)



Figure 4: 72h Flows (L/sec) for Key Pipe Links at Peak Demand Period

P-11 (72h) (Note capacity available in main northern pipeline after T-1 refills)

P-19 (72h)

P-10 (72h) Pump – 3 discharge at Half Moon Bay BPS

P-16 (72h)



Max/Min Summary

This table shows the range of operating pressures likely to be experienced at each node in the system under the given scenario.

******************************************* Summary of Max/Min Node Values ******************************************* Node MnPres MnHead MnHGL MnTime MxPres MxHead MxHGL MxTime Elevation -------------------------------------------------------------------------------- J-1 191.18 19.49 24.49 0.14 1509.29 153.90 158.90 23.00 5.00 J-3 677.86 69.12 69.12 0.14 905.08 92.29 92.29 23.00 0.00 J-4 746.54 76.13 66.13 0.14 1000.97 102.07 92.07 23.00 -10.00 J-5 777.15 79.25 53.25 0.14 1148.41 117.10 91.10 23.00 -26.00 J-6 676.29 68.96 43.96 0.14 1131.78 115.41 90.41 23.00 -25.00 J-7 275.72 28.12 13.12 0.14 1010.96 103.09 88.09 23.00 -15.00 J-8 86.02 8.77 8.77 0.14 860.69 87.77 87.77 23.00 0.00 J-9 111.96 11.42 11.42 3.00 1417.92 144.59 144.59 23.00 0.00 J-10 340.30 34.70 44.70 0.14 1461.15 149.00 159.00 23.00 10.00 J-11 -16.84 -1.72 43.28 0.14 1098.75 112.04 157.04 23.00 45.00 J-12 162.57 16.58 38.58 0.14 1307.29 133.31 155.31 23.00 22.00 J-13 212.98 21.72 35.72 0.14 1375.85 140.30 154.30 23.00 14.00 J-14 235.06 23.97 31.97 0.14 1421.70 144.97 152.97 23.00 8.00 J-15 123.15 12.56 27.56 0.14 1333.89 136.02 151.02 23.00 15.00 J-16 101.08 10.31 20.31 0.14 1351.39 137.80 147.80 23.00 10.00 J-17 55.78 5.69 11.69 4.00 1359.08 138.59 144.59 23.00 6.00 J-18 255.63 26.07 26.07 0.00 1559.21 158.99 158.99 23.00 0.00 J-20 93.34 9.52 29.52 0.14 1362.19 138.90 158.90 23.00 20.00 J-21 148.26 15.12 25.12 0.14 1460.26 148.90 158.90 23.00 10.00 J-23 158.61 16.17 28.17 0.14 1440.22 146.86 158.86 23.00 12.00 J-24 98.24 10.02 28.02 0.14 1381.21 140.84 158.84 23.00 18.00 J-25 127.79 13.03 28.03 0.14 1410.41 143.82 158.82 23.00 15.00 J-26 275.33 28.08 28.08 0.14 1557.62 158.83 158.83 23.00 0.00 J-27 -117.28 -11.96 28.04 0.14 1164.66 118.76 158.76 23.00 40.00 J-28 29.46 3.00 28.00 0.14 1311.83 133.77 158.77 23.00 25.00 J-2a 492.62 50.23 70.23 0.14 709.73 72.37 92.37 23.00 20.00 O-Pump-1 409.02 41.71 46.71 0.14 1511.63 154.14 159.14 23.00 5.00 O-Pump-3 514.69 52.48 70.48 0.14 729.50 74.39 92.39 23.00 18.00 R-1 19.61 2.00 21.00 0.00 19.61 2.00 21.00 0.00 19.00 T-1 54.07 5.51 11.51 4.00 1359.08 138.59 144.59 23.00 6.00 T-2 11.91 1.21 43.21 0.14 1127.24 114.95 156.95 23.00 42.00 T-19 9.81 1.00 23.00 0.00 1343.46 136.99 158.99 23.00 22.00 I-Pump-1 19.93 2.03 7.03 0.14 810.42 82.64 87.64 23.00 5.00 I-Pump-3 25.68 2.62 20.62 0.14 29.18 2.98 20.98 23.00 18.00 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- J-5 938.56 R-1 19.61 J-6 868.40 I-Pump-3 27.00 J-4 865.39 T-1 68.65 O-Pump-1 854.12 J-17 71.41 J-10 792.08 J-16 190.70 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-11 1.67 P-17 0.02 P-12 1.67 P-24 0.02 P-13 1.67 P-28 0.03 P-10 1.67 P-27 0.05 P-32 1.67 P-25 0.12



H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 60.76 P-17 0.00 P-1 24.63 P-24 0.01 P-12 19.75 P-28 0.05 P-13 19.40 P-27 0.05 P-11 19.19 P-25 0.28 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-11 18.34 P-17 0.00 P-12 18.34 P-24 0.01 P-13 18.34 P-28 0.05 P-10 18.34 P-27 0.05 P-32 18.34 P-25 0.27

These maximum pressure details will assist in confirming pipe class and wall thickness determinations for each pipe segment.

Hydraulic Grade Line

The following typical HGL profile (Figure 5) is for a single EPS time step. KYPIPE also allows an animated HGL profile over 72 hours to be produced giving maximum and minimum HGL envelopes for all results.

Figure 5: Snapshot of EPS HGL Profile for Peak Demand Scenario



A small storage tank at Blatherwick Rise helps avoid cavitation by controlling minimum grades. By adding a one-way discharge tank at the high point, it would be possible to initiate siphoning over the high point during a pumping cycle and effectively reduce the friction head generally reflected at the Half Moon Bay Pump Station, thereby reducing the daily pumping energy required. Energy recovery may not be attainable at peak pipe flow ti mes, but during reduced flow periods the recovery of energy from the residual head at Arm End is possible.



DISCUSSION Final Pipeline Design Details

The model code allows for the inclusion of actual pipe dimensional details and the specification of locations for fittings and appurtenances, once known, to allow total friction and minor head losses to be accurately estimated and final hydraulic profiles determined for design flow rates. Based on such additional information, final pipe pressure classes and wall thicknesses required at all locations can be confirmed.

Climate Change and South Arm Peninsula

South Arm Peninsula agriculture and living is subject to low rainfall compared to the Hobart Region. At present SAP lacks any formal public water supply. Recent national climate change research has been published in the 2018 book Sunburnt Country, by Dr. Joelle Gergis at the University of Melbourne (Gergis, 2018). The book notes that Hobart is part of a southern region where there has already been an observed long term drying trend, characterised by a 10-20 percent reduction in average cool season (April-September) rainfall. As the CSIRO expect the region to experience more drought periods in future, there will be less rainfall for agriculture and ecosystems services. Both Bureau of Meteorology and CSIRO projections for the region are reported to show a continuing decreases in winter/spring rainfall, potentially affecting agriculture and having a large impact on local rural communities. Gergis (2018) notes that Hobart region is expected to transition towards a climate like Adelaide, by later this century. In view of these risks and vulnerabilities, this book contends that transformational, rather than incremental, climate change adaptations will be required in the southern region of Australia. For the already low rainfall prone South Arm Peninsula, this project represents such a transformational adaptation initiative.

Cavitation at Blatherwick Rise

It was noted that certain combinations of pump curve at Half Moon Bay Pump Station and pipe nominal diameter from this station to the high point will lead to cavitation and unstable operations. It was also found that by maintaining a 225mm diameter pipe to the high point and a suitable breather pipe, that this cavitation can be avoided. This choice reduces the head loss where the adverse grade exists. However, for the design scenario used, the balance of the northern branch pipe to Arm End can be reduced to 160mm diameter. The original assumption of 200mm pipe was found to be conservative once storage tanks were included in the model. The southern branch is based on significantly smaller diameter pipes, reflecting the expected lower user demands. These conclusions assume that users can be scheduled to balance abstractions from this pipe seasonally and over the annual service period. The introduction of local balancing storage capacity will allow the effective reduction in pipe sizes and maintain scheme economic viability.

Energy recovery

A detailed design assessment will need to be separately made of the optimum design diameter for the northern branch, if energy recovery is also proposed. There will be a trade-off between the diameter selected and the associated pumping power required versus the net economic benefits from installing energy recovery equipment beyond the SAP pipeline high point at Blatherwick Rise.

Arm End Tank Behaviour

For a drought dry period, the Arm End Tanks proposed (2 x 2ML) would alone supply peak golf irrigation needs for approximately five (5) days. This is a reasonable safety margin should any pump station routine maintenance be required. With pump stations being used to top up tanks each day during such an event, the Arm End storage tanks net drawdown is restricted to less than 0.20 ML/day. This means a supply capacity sufficient for approximately twenty (20) days of peak irrigation would be available. Additional storage



throughout the system will allow other users to schedule draw-off from the main supply to complement the golf user needs. Cropping requirements are also likely to be seasonal and each user can plan and order ahead for their growing season water needs.

Half Moon Bay Pump Station

The output from this booster pumping station is shown in Figure 6. Protea Farm Tank 19 is always full due to the static or pump hydraulic grade (head) available at this location.

The low flow periods shown below indicate that future capacity remains in this system to support future requests for connections beyond those modelled.

Figure 6: Half Moon Bay PS Outlet Discharge to P-9



CONCLUSIONS The proposed irrigation water pipeline will use minimal impact construction methods, including trenchless technology (Horizontal Directional Drilling) for land based pipes and beach/inshore habitat crossings and float and sink construction for the River Derwent marine section, and thus have minimal environmental impacts. These aspects are further considered separately in the associated EMP.

There is technically sustainable evidence that the proponent can construct an irrigation water pipeline system, in stages, that will provides extensive access to Class ‘B’ effluent for irrigation purposes to landowners, farmers and organisations across the South Arm Peninsula.

Back-up fire water supply to tanks at South Arm and Opossum Bay could also be achieved, subject to point of use treatment to Class ‘A’, which allows for a wider ranges of uses.

Clarence City Council could use this irrigation water supply for the establishment and long term maintenance of the landscaping associated with their adopted Master Plan for facilities at Calverton Oval / South Arm Community Centre. In addition, Council support for this infrastructure project would assist the initiation of a significant and potentially transformational climate change adaptation for the South Arm Peninsula.

A combination of two major booster station is required to meet the irrigation demands of the Arm End Recreation Reserve site during an extended dry period. However, short term peak requirements would usually be met from the Arm End storage tanks and less pumping required. Minor flows can be supplied to the South Arm Peninsula by gravity from the Blackman’s Bay Balance Tank. Full site water demands for Arm End Recreation Reserve and all other potential users can be met by this system. To the extent that South Arm Peninsula co-operative irrigation users participate, future River Derwent discharge volumes by TasWater can also be reduced by up to 20 percent relative to their current projections and thereby reduce the existing outfall’s marine environment impacts. Up to 350 ML/annum of Blackman’s Bay effluent can be diverted from estuarine discharge in future.

The proposed SAP effluent irrigation water supply network is feasible from both hydraulic and engineering perspectives based on the network modelling of proposed full system development undertaken for this report.

Modelling undertaken demonstrates that by scheduling user supply delivery times and effective use of balancing water storages, an optimum conjunctive use scheme can be developed based on the anchor irrigation needs of the Arm End Recreation Reserve site and the South Arm RSL / Iron Pot Golf Club.



RECOMMENDATIONS The modelling studies have provided operational evidence for the future management of a co-operative effluent re-use scheme based on the SAP Irrigation Water Pipeline. To maximise the potential planning and operational benefits of the network model, the following further actions are recommended:

1. Update the model during the detail design process by adding actual pump characteristic curves for each pump station, confirming actual internal diameters for the proposed pipe supply, and adding the details of key valves, fittings and appurtenances plus actual power tariffs for cost projections by the model.

2. Add the pipeline controls proposed to turn automate pumps and tanks on/ off signals, to bring the model to an operational configuration.

3. Calibrate the model after pipeline commissioning, using real time flow and pressure data, to fine tune the pipe roughness coefficients used.

4. Establish supply scheduling rules for each potential user group and adjust demand patterns used accordingly.

5. Prepare a sub-model for each stage of network development, based on this base model, to guide design plans and remain useful as an ongoing management and operating tool.

Author Details Impact Blue Pty Ltd (ACN 116 083 311) is an independent Australian consulting company established in 2006, now based in South Arm, Tasmania. It continues to serve existing clients across Eastern Australia, with a primary focus on advisory services to Local Governments in the water and waste sectors.

Company Director and Senior Principal Consultant, Mr Allan Boase, has authored this report. He is a qualified Water Engineer with has over 40 years of water industry consulting experience, including 30 years with national and multi-national firms, and holds a Bachelor of Engineering (Honours) degree in Civil Engineering from Monash University. He is a Fellow of Engineers Australia and a Life Member / Fellow of the American Society of Civil Engineers and the Environmental Water Resources Institute. He is a Chartered Engineer, a registered Civil Engineer on the National Engineer’s Register and is a Registered Professional Engineer of Queensland.

Allan has undertaken numerous static and dynamic network analyses for major urban and industrial water supply systems, including the Tamar Region Water Supply Master Plan, Winnaleah Irrigation Scheme, George Town and Bell Bay Major Users Water Quality Investigations, Loy Yang ‘B’ Power Station Water Supply and international projects such as Port Moresby Water Supply, Ipoh Water Supply, Mandalay Water Supply, Rockhampton Water Supply and the network modelling of a multi-pump leachate collection system for a World Bank’s Shanghai Landfill Upgrade. He has specialised in all aspects of water, sewer, stormwater, sludge and leachate pipeline hydraulics, including the assessment of hydraulic transients and control measures and designed numerous long and/or submarine pipelines, outfalls and siphons.

References 1. Gergis, J. “Sunburnt Country: A History and Future of Climate Change in Australia”, Melbourne

University Press, Melbourne, Australia, 2018



APPENDICES A. Typical Model Output Report

This Appendix includes the full results of one particular typical extended period simulation of the South Arm Peninsula Irrigation Water Pipeline. Other sensitivity analyses were also undertaken and each scenario run provides a similar level of detail. Results are available in this MS Word document format and may also be viewed via the KYPIPE Graphical User Interface in tabular and graphical formats. A selection of these outputs are used in this report. Custom Powerpoint results presentation files (animated) may also be generated as required.

B. Pipeline Locality Plan C. Network Model Schematic

* * * * * * * * * * * * K Y P I P E * * * * * * * * * * * * * * * Pipe Network Modeling Software * * * * CopyRighted by KYPIPE LLC (www.kypipe.com) * * Version: 9.006 12/15/2017 * * Company: ImpactBlue Serial #: 591230 * * Interface: KYnetic * * Licensed for Pipe2018 * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * Date & Time: Thu Jun 28 14:38:20 2018 Master File : c:\users\public\documents\kypipe docs\kypipe (water)\copy 1 of full model arm end with brtank.KYP\copy 1 of full model arm end with brtank.P2K ************************************************ S U M M A R Y O F O R I G I N A L D A T A ************************************************ U N I T S S P E C I F I E D FLOWRATE ............ = liters/second HEAD (HGL) .......... = meters PRESSURE ............ = kpa METERED FLOW ........ = liters POWER COST .......... = 0.099 $/kW-Hr P I P E L I N E D A T A STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NAMES LENGTH DIAMETER ROUGHNESS MINOR N A M E #1 #2 (m) (mm) COEFF. LOSS COEFF. ------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 10.00 220.00 140.0000 5.00 P-2 J-2a J-3 90.00 197.80 140.0000 3.00 P-3 J-3 J-4 300.00 197.80 140.0000 3.00 P-4 J-4 J-5 1400.00 197.80 140.0000 3.00 P-5 J-5 J-6 1000.00 197.80 140.0000 3.00 P-6 J-6 J-7 3400.00 197.80 140.0000 3.00 P-7 J-7 J-8 450.00 197.80 140.0000 3.00 P-8 J-8 I-Pump-1 160.00 197.80 140.0000 3.00 P-9 O-Pump-1 J-10 190.00 197.80 140.0000 3.00 P-10 T-2 J-11 10.00 140.70 140.0000 3.00 P-11 T-2 J-12 500.00 140.70 140.0000 3.00 P-12 J-12 J-13 300.00 140.70 140.0000 3.00 P-13 J-13 J-14 400.00 140.70 140.0000 3.00 P-14 J-14 J-15 600.00 140.70 140.0000 3.00 P-15 J-15 J-16 1000.00 140.70 140.0000 3.00 P-16 J-16 J-17 1000.00 140.70 140.0000 3.00 P-17 J-18 J-10 250.00 109.90 140.0000 3.00 P-18 J-18 T-19 25.00 109.90 140.0000 3.00 P-19 J-10 J-20 2000.00 109.90 140.0000 3.00 P-20 J-20 J-21 1500.00 109.90 140.0000 3.00 P-21 J-21 J-1 200.00 109.90 140.0000 3.00 P-22 J-20 J-23 500.00 96.50 140.0000 3.00 P-23 J-23 J-24 300.00 79.00 140.0000 3.00 P-24 J-24 J-25 400.00 79.00 140.0000 3.00 P-25 J-25 J-26 200.00 79.00 140.0000 3.00 P-26 J-26 J-23 400.00 79.00 140.0000 3.00 P-27 J-25 J-28 1000.00 79.00 140.0000 3.00 P-28 J-26 J-27 1500.00 43.90 140.0000 3.00



P-29 J-17 T-1 25.00 175.80 140.0000 3.00 P-30 O-Pump-3 J-2a 10.00 220.00 140.0000 3.00 P-31 T-1 J-9 50.00 246.30 140.0000 3.00 P-32 J-10 J-11 600.00 140.70 140.0000 3.00 P U M P/L O S S E L E M E N T D A T A THERE IS A DEVICE AT NODE Pump-1 DESCRIBED BY THE FOLLOWING DATA: (ID= 11) HEAD FLOWRATE EFFICIENCY (m) (l/s) (%) 75.00 0.00 75.00 (Default) 68.00 18.00 75.00 (Default) 63.00 27.00 75.00 (Default) 55.00 33.00 75.00 (Default) 50.00 37.00 75.00 (Default) 40.00 43.00 75.00 (Default) 35.00 45.00 75.00 (Default) 30.00 47.00 75.00 (Default) THERE IS A DEVICE AT NODE Pump-3 DESCRIBED BY THE FOLLOWING DATA: (ID= 33) HEAD FLOWRATE EFFICIENCY (m) (l/s) (%) 75.00 0.00 75.00 (Default) 65.00 25.00 75.00 (Default) 60.00 35.00 75.00 (Default) 55.00 40.00 75.00 (Default) 40.00 48.00 75.00 (Default) 25.00 50.00 75.00 (Default) N O D E D A T A NODE NODE EXTERNAL JUNCTION EXTERNAL NAME TITLE DEMAND ELEVATION GRADE (l/s) (m) (m) -------------------------------------------------------------- J-1 Iron Pot Dam 0.50 5.00 J-3 0.00 0.00 J-4 0.00 -10.00 J-5 0.00 -26.00 J-6 0.00 -25.00 J-7 0.00 -15.00 J-8 0.00 0.00 J-9 5.60 0.00 J-10 0.00 10.00 J-11 0.00 45.00 J-12 Northern Far 0.00 22.00 J-13 0.00 14.00 J-14 0.20 8.00 J-15 0.00 15.00 J-16 0.00 10.00 J-17 Arm End Rese 1.00 6.00 J-18 0.30 0.00 J-20 Southern Far 0.00 20.00 J-21 South Arm Ro 0.00 10.00 J-23 Calverton Ov 0.20 12.00 J-24 South Arm Fi 0.10 18.00 J-25 Blessington 0.50 15.00 J-26 Fort Directi 0.00 0.00 J-27 Fort Directi 0.10 40.00 J-28 Shoecraft Ba 0.50 25.00 J-2a 0.00 20.00 O-Pump-1 Half Moon Ba 0.00 5.00 O-Pump-3 Blackmans Ba 0.00 18.00 R-1 ---- 19.00 21.00 T-1 ---- 6.00 13.00 T-2 Breather Pip ---- 42.00 44.00 T-19 ---- 22.00 23.00



I-Pump-1 Half Moon Ba 0.00 5.00 I-Pump-3 Blackmans Ba 0.00 18.00 O U T P U T O P T I O N D A T A OUTPUT SELECTION: ALL RESULTS ARE INCLUDED IN THE TABULATED OUTPUT MAXIMUM AND MINIMUM PRESSURES = 5 MAXIMUM AND MINIMUM VELOCITIES = 5 MAXIMUM AND MINIMUM HEAD LOSS/1000 = 5 E P S D A T A TOTAL TIME FOR SIMULATION = 72.000 NORMAL TIME PERIOD FOR CALCULATIONS = 1.000 NORMAL TIME PERIOD FOR TABULATED OUTPUT = 72.000 NORMAL TIME PERIOD FOR POSTPROCESSING FILE = 1.000 EPS OUTPUT SELECTION: THE ABOVE TABULATED OUTPUT OPTIONS ARE INCLUDED WITH THE FOLLOWING EXTENDED PERIOD PRINT OPTIONS INTERMEDIATE REPORTS (tank status, flow meter, regulating valve, etc.) TABULATED FOR ALL INTERMEDIATE TIME PERIODS TABULATED FOR ALL STATUS CHANGES (tanks, pressure switches, etc.) V A R I A B L E H E A D T A N K D A T A TANK MAXIMUM MINIMUM TANK INITIAL EXTERNAL NAME ELEVATION ELEVATION CAPACITY VOLUME FLOW (*) m m lts lts lps ------------------------------------------------------------------------------ T-1(1) 13.00 7.00 1884960. 1884960. 0.00 T-2(1) 44.00 42.00 14137. 14137. 0.00 T-19(1) 25.00 22.00 21206. 7069. 0.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA S Y S T E M C O N F I G U R A T I O N NUMBER OF PIPES ...................(P) = 32 NUMBER OF END NODES ...............(J) = 28 NUMBER OF PRIMARY LOOPS ...........(L) = 1 NUMBER OF SUPPLY NODES ............(F) = 4 NUMBER OF SUPPLY ZONES ............(Z) = 1 ================================================================================ Time: 0.000 TIME FROM INITIATION OF EPS = 0.0000 HOURS (0000 HOURS, DAY: 1) RESULTS OBTAINED AFTER 6 TRIALS: ACCURACY = 0.86964E-03 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 41.88 T-19 -32.88



NET SYSTEM INFLOW = 41.88 NET SYSTEM OUTFLOW = -32.88 NET SYSTEM DEMAND = 9.00 Time: 0.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 0.0001 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 0.000 TIME FROM INITIATION OF EPS = 0.0001 HOURS (0000 HOURS, DAY: 1) RESULTS OBTAINED AFTER 6 TRIALS: ACCURACY = 0.41678E-03 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 43.10 0.05 0.33 1.13 38.10 5.34 P-2 J-2a J-3 43.10 0.81 0.30 1.40 12.31 8.97 P-3 J-3 J-4 43.10 2.69 0.30 1.40 9.97 8.97 P-4 J-4 J-5 43.10 12.56 0.30 1.40 9.18 8.97 P-5 J-5 J-6 43.10 8.97 0.30 1.40 9.27 8.97 P-6 J-6 J-7 43.10 30.49 0.30 1.40 9.06 8.97 P-7 J-7 J-8 43.10 4.04 0.30 1.40 9.64 8.97 P-8 J-8 I-Pump-1 43.10 1.43 0.30 1.40 10.85 8.97 P-9 O-Pump-1 J-10 43.10 1.70 0.30 1.40 10.55 8.97 P-10 T-2 J-11 -6.78 0.02 0.03 0.44 4.44 1.53 P-11 T-2 J-12 17.72 4.54 0.20 1.14 9.48 9.08 P-12 J-12 J-13 17.72 2.72 0.20 1.14 9.74 9.08 P-13 J-13 J-14 17.72 3.63 0.20 1.14 9.58 9.08 P-14 J-14 J-15 15.72 4.36 0.16 1.01 7.53 7.27 P-15 J-15 J-16 15.72 7.27 0.16 1.01 7.43 7.27 P-16 J-16 J-17 15.72 7.27 0.16 1.01 7.43 7.27 P-17 J-18 J-10 -27.95 17.60 1.33 2.95 75.70 70.39 P-18 J-18 T-19 27.86 1.75 1.32 2.94 122.68 69.93 P-19 J-10 J-20 8.36 15.06 0.12 0.88 7.59 7.53 P-20 J-20 J-21 5.00 4.36 0.04 0.53 2.93 2.91 P-21 J-21 J-1 5.00 0.58 0.04 0.53 3.12 2.91 P-22 J-20 J-23 3.36 1.31 0.03 0.46 2.69 2.63 P-23 J-23 J-24 0.82 0.15 0.00 0.17 0.52 0.51 P-24 J-24 J-25 -0.18 0.01 0.00 0.04 0.03 0.03 P-25 J-25 J-26 -0.51 0.04 0.00 0.10 0.22 0.21 P-26 J-26 J-23 -0.55 0.10 0.00 0.11 0.25 0.24 P-27 J-25 J-28 0.17 0.03 0.00 0.03 0.03 0.03 P-28 J-26 J-27 0.03 0.03 0.00 0.02 0.02 0.02 P-29 J-17 T-1 15.72 0.06 0.06 0.65 5.02 2.46 P-30 O-Pump-3 J-2a 43.10 0.05 0.20 1.13 25.00 5.34 P-31 T-1 J-9 56.00 0.25 0.21 1.18 9.23 5.01 P-32 J-10 J-11 6.78 0.92 0.03 0.44 1.58 1.53 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs



lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 43.10 2.22 42.00 39.8 75.00 17. 0.0 0.0 ** ** 12.2 0.0001 Pump-3 43.10 2.62 52.56 49.9 75.00 21. 0.0 0.0 ** ** 12.7 0.0001 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 5.00( ** ) 24.79 5.00 19.79 194.04 J-3 0.00 69.20 J-4 0.00 66.21 -10.00 76.21 747.37 J-5 0.00 53.35 -26.00 79.35 778.20 J-6 0.00 44.09 -25.00 69.09 677.50 J-7 0.00 13.29 -15.00 28.29 277.47 J-8 0.00 8.96 J-9 56.00( ** ) 12.54 J-10 0.00 44.99 10.00 34.99 343.16 J-11 0.00 44.04 45.00 -0.96 -9.37 J-12 Northern Far 0.00 39.26 22.00 17.26 169.27 J-13 0.00 36.34 14.00 22.34 219.06 J-14 2.00( ** ) 32.51 8.00 24.51 240.33 J-15 0.00 27.99 15.00 12.99 127.35 J-16 0.00 20.56 10.00 10.56 103.52 J-17 Arm End Rese 0.00(0.00) 13.13 6.00 7.13 69.88 J-18 0.10(0.33) 26.07 J-20 Southern Far 0.00 29.81 20.00 9.81 96.21 J-21 South Arm Ro 0.00 25.41 10.00 15.41 151.13 J-23 Calverton Ov 2.00( ** ) 28.47 12.00 16.47 161.48 J-24 South Arm Fi 1.00( ** ) 28.31 18.00 10.31 101.11 J-25 Blessington 0.17(0.33) 28.32 15.00 13.32 130.66 J-26 Fort Directi 0.00 28.37 J-27 Fort Directi 0.03(0.33) 28.33 40.00 -11.67 -114.41 J-28 Shoecraft Ba 0.17(0.33) 28.30 25.00 3.30 32.33 J-2a 0.00 70.31 20.00 50.31 493.37 O-Pump-1 Half Moon Ba 0.00 47.00 5.00 42.00 411.86 O-Pump-3 Blackmans Ba 0.00 70.56 18.00 52.56 515.43 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 13.00 6.00 7.00 68.65 T-2 Breather Pip ---- 44.00 42.00 2.00 19.61 T-19 ---- 23.00 22.00 1.00 9.81 I-Pump-1 Half Moon Ba 0.00 7.22 5.00 2.22 21.79 I-Pump-3 Blackmans Ba 0.00 20.62 18.00 2.62 25.68 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- J-5 778.20 J-27 -114.41 J-4 747.37 J-11 -9.37 J-6 677.50 T-19 9.81 O-Pump-3 515.43 R-1 19.61 J-2a 493.37 T-2 19.61 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-17 2.95 P-28 0.02 P-18 2.94 P-27 0.03



P-2 1.40 P-24 0.04 P-3 1.40 P-25 0.10 P-4 1.40 P-26 0.11 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-18 122.68 P-28 0.02 P-17 75.70 P-27 0.03 P-1 38.10 P-24 0.03 P-30 25.00 P-25 0.22 P-2 12.31 P-26 0.25 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-17 70.39 P-28 0.02 P-18 69.93 P-27 0.03 P-12 9.08 P-24 0.03 P-11 9.08 P-25 0.21 P-13 9.08 P-26 0.24 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 43.10 T-1 40.28 T-2 10.94 Breather Pip T-19 -27.86 NET SYSTEM INFLOW = 94.32 NET SYSTEM OUTFLOW = -27.86 NET SYSTEM DEMAND = 66.46 T A N K S T A T U S R E P O R T (time = 0.0001 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -40.28 13.00 6.00 1884960. 100.0 DRAINING 5.93 T-2(1) -10.94 44.00 2.00 14137. 100.0 DRAINING 1.22 T-19(1) 27.86 23.00 1.00 7069. 33.3 FILLING 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 0.141 TIME FROM INITIATION OF EPS = 0.1410 HOURS (0014 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.39602E-03 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/



N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 43.14 0.05 0.33 1.13 38.18 5.35 P-2 J-2a J-3 43.14 0.81 0.30 1.40 12.33 8.98 P-3 J-3 J-4 43.14 2.70 0.30 1.40 9.99 8.98 P-4 J-4 J-5 43.14 12.58 0.30 1.40 9.20 8.98 P-5 J-5 J-6 43.14 8.98 0.30 1.40 9.29 8.98 P-6 J-6 J-7 43.14 30.55 0.30 1.40 9.07 8.98 P-7 J-7 J-8 43.14 4.04 0.30 1.40 9.65 8.98 P-8 J-8 I-Pump-1 43.14 1.44 0.30 1.40 10.87 8.98 P-9 O-Pump-1 J-10 43.14 1.71 0.30 1.40 10.57 8.98 P-10 T-2 J-11 -8.42 0.02 0.04 0.54 6.77 2.29 P-11 T-2 J-12 17.51 4.44 0.19 1.13 9.27 8.89 P-12 J-12 J-13 17.51 2.67 0.19 1.13 9.53 8.89 P-13 J-13 J-14 17.51 3.55 0.19 1.13 9.37 8.89 P-14 J-14 J-15 15.51 4.26 0.15 1.00 7.35 7.10 P-15 J-15 J-16 15.51 7.10 0.15 1.00 7.25 7.10 P-16 J-16 J-17 15.51 7.10 0.15 1.00 7.25 7.10 P-17 J-18 J-10 -26.36 15.78 1.18 2.78 67.85 63.13 P-18 J-18 T-19 26.26 1.57 1.17 2.77 109.57 62.69 P-19 J-10 J-20 8.36 15.06 0.12 0.88 7.59 7.53 P-20 J-20 J-21 5.00 4.36 0.04 0.53 2.93 2.91 P-21 J-21 J-1 5.00 0.58 0.04 0.53 3.12 2.91 P-22 J-20 J-23 3.36 1.31 0.03 0.46 2.69 2.63 P-23 J-23 J-24 0.82 0.15 0.00 0.17 0.52 0.51 P-24 J-24 J-25 -0.18 0.01 0.00 0.04 0.03 0.03 P-25 J-25 J-26 -0.51 0.04 0.00 0.10 0.22 0.21 P-26 J-26 J-23 -0.55 0.10 0.00 0.11 0.25 0.24 P-27 J-25 J-28 0.17 0.03 0.00 0.03 0.03 0.03 P-28 J-26 J-27 0.03 0.03 0.00 0.02 0.02 0.02 P-29 J-17 T-1 15.51 0.06 0.06 0.64 4.90 2.40 P-30 O-Pump-3 J-2a 43.14 0.05 0.20 1.13 25.05 5.35 P-31 T-1 J-9 56.00 0.25 0.21 1.18 9.23 5.01 P-32 J-10 J-11 8.42 1.37 0.04 0.54 2.36 2.29 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 43.14 2.03 41.71 39.7 75.00 17. 0.3 0.3 ** ** 12.1 0.1410 Pump-3 43.14 2.62 52.48 49.9 75.00 21. 0.4 0.4 ** ** 12.7 0.1410 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 5.00( ** ) 24.49 5.00 19.49 191.18 J-3 0.00 69.12 J-4 0.00 66.13 -10.00 76.13 746.54 J-5 0.00 53.25 -26.00 79.25 777.15 J-6 0.00 43.96 -25.00 68.96 676.29 J-7 0.00 13.12 -15.00 28.12 275.72 J-8 0.00 8.77 J-9 56.00( ** ) 12.47 J-10 0.00 44.70 10.00 34.70 340.30 J-11 0.00 43.28 45.00 -1.72 -16.84 J-12 Northern Far 0.00 38.58 22.00 16.58 162.58 J-13 0.00 35.72 14.00 21.72 212.98 J-14 2.00( ** ) 31.97 8.00 23.97 235.06 J-15 0.00 27.56 15.00 12.56 123.16



J-16 0.00 20.31 10.00 10.31 101.09 J-17 Arm End Rese 0.00(0.00) 13.06 6.00 7.06 69.21 J-18 0.10(0.33) 27.74 J-20 Southern Far 0.00 29.52 20.00 9.52 93.34 J-21 South Arm Ro 0.00 25.12 10.00 15.12 148.26 J-23 Calverton Ov 2.00( ** ) 28.17 12.00 16.17 158.61 J-24 South Arm Fi 1.00( ** ) 28.02 18.00 10.02 98.24 J-25 Blessington 0.17(0.33) 28.03 15.00 13.03 127.79 J-26 Fort Directi 0.00 28.08 J-27 Fort Directi 0.03(0.33) 28.04 40.00 -11.96 -117.28 J-28 Shoecraft Ba 0.17(0.33) 28.00 25.00 3.00 29.46 J-2a 0.00 70.23 20.00 50.23 492.62 O-Pump-1 Half Moon Ba 0.00 46.71 5.00 41.71 409.02 O-Pump-3 Blackmans Ba 0.00 70.48 18.00 52.48 514.69 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 12.93 6.00 6.93 68.01 T-2 Breather Pip ---- 43.22 42.00 1.22 11.92 T-19 ---- 25.00 22.00 3.00 29.41 I-Pump-1 Half Moon Ba 0.00 7.03 5.00 2.03 19.93 I-Pump-3 Blackmans Ba 0.00 20.62 18.00 2.62 25.68 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- J-5 777.15 J-27 -117.28 J-4 746.54 J-11 -16.84 J-6 676.29 T-2 11.92 O-Pump-3 514.69 R-1 19.61 J-2a 492.62 I-Pump-1 19.93 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-17 2.78 P-28 0.02 P-18 2.77 P-27 0.03 P-2 1.40 P-24 0.04 P-3 1.40 P-25 0.10 P-4 1.40 P-26 0.11 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-18 109.57 P-28 0.02 P-17 67.85 P-27 0.03 P-1 38.18 P-24 0.03 P-30 25.05 P-25 0.22 P-2 12.33 P-26 0.25 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-17 63.13 P-28 0.02 P-18 62.69 P-27 0.03 P-2 8.98 P-24 0.03 P-3 8.98 P-25 0.21 P-4 8.98 P-26 0.24



S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 43.14 T-1 40.49 T-2 9.09 Breather Pip T-19 -26.26 NET SYSTEM INFLOW = 92.72 NET SYSTEM OUTFLOW = -26.26 NET SYSTEM DEMAND = 66.46 T A N K S T A T U S R E P O R T (time = 0.1410 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -40.49 12.93 5.93 1864530. 98.9 DRAINING 5.93 T-2(1) -9.09 43.22 1.22 8590. 60.8 DRAINING 1.21 T-19(1) 26.26 25.00 3.00 21196. 100.0 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Tank Filled/Emptied TIME FROM INITIATION OF EPS = 0.1412 HOURS (0014 HOURS, DAY: 1) RESULTS OBTAINED AFTER 5 TRIALS: ACCURACY = 0.82706E-05 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 40.63 0.05 0.29 1.07 33.91 4.79 P-2 J-2a J-3 40.63 0.72 0.27 1.32 11.01 8.04 P-3 J-3 J-4 40.63 2.41 0.27 1.32 8.93 8.04 P-4 J-4 J-5 40.63 11.26 0.27 1.32 8.23 8.04 P-5 J-5 J-6 40.63 8.04 0.27 1.32 8.31 8.04 P-6 J-6 J-7 40.63 27.34 0.27 1.32 8.12 8.04 P-7 J-7 J-8 40.63 3.62 0.27 1.32 8.63 8.04 P-8 J-8 I-Pump-1 40.63 1.29 0.27 1.32 9.71 8.04 P-9 O-Pump-1 J-10 40.63 1.53 0.27 1.32 9.45 8.04 P-10 T-2 J-11 -32.17 0.27 0.65 2.07 92.87 27.41 P-11 T-2 J-12 17.51 4.44 0.19 1.13 9.27 8.89 P-12 J-12 J-13 17.51 2.67 0.19 1.13 9.53 8.89 P-13 J-13 J-14 17.51 3.55 0.19 1.13 9.37 8.89 P-14 J-14 J-15 15.51 4.26 0.15 1.00 7.35 7.10 P-15 J-15 J-16 15.51 7.10 0.15 1.00 7.25 7.10 P-16 J-16 J-17 15.51 7.10 0.15 1.00 7.25 7.10 P-17 J-18 J-10 -0.10 0.00 0.00 0.01 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 8.36 15.06 0.12 0.88 7.59 7.53 P-20 J-20 J-21 5.00 4.36 0.04 0.53 2.93 2.91 P-21 J-21 J-1 5.00 0.58 0.04 0.53 3.12 2.91 P-22 J-20 J-23 3.36 1.31 0.03 0.46 2.69 2.63 P-23 J-23 J-24 0.82 0.15 0.00 0.17 0.52 0.51 P-24 J-24 J-25 -0.18 0.01 0.00 0.04 0.03 0.03 P-25 J-25 J-26 -0.51 0.04 0.00 0.10 0.22 0.21 P-26 J-26 J-23 -0.55 0.10 0.00 0.11 0.25 0.24 P-27 J-25 J-28 0.17 0.03 0.00 0.03 0.03 0.03



P-28 J-26 J-27 0.03 0.03 0.00 0.02 0.02 0.02 P-29 J-17 T-1 15.51 0.06 0.06 0.64 4.90 2.40 P-30 O-Pump-3 J-2a 40.63 0.05 0.17 1.07 22.26 4.79 P-31 T-1 J-9 56.00 0.25 0.21 1.18 9.23 5.01 P-32 J-10 J-11 32.17 16.44 0.65 2.07 28.50 27.41 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 40.63 12.96 58.04 45.1 75.00 18. 0.0 0.3 ** ** 23.0 0.1412 Pump-3 40.63 2.66 56.72 54.1 75.00 22. 0.0 0.4 ** ** 12.7 0.1412 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 5.00( ** ) 41.03 5.00 36.03 353.38 J-3 0.00 73.51 J-4 0.00 70.83 -10.00 80.83 792.69 J-5 0.00 59.31 -26.00 85.31 836.59 J-6 0.00 51.00 -25.00 76.00 745.31 J-7 0.00 23.40 -15.00 38.40 376.54 J-8 0.00 19.51 J-9 56.00( ** ) 12.47 J-10 0.00 61.24 10.00 51.24 502.51 J-11 0.00 44.14 45.00 -0.86 -8.41 J-12 Northern Far 0.00 38.58 22.00 16.58 162.57 J-13 0.00 35.72 14.00 21.72 212.98 J-14 2.00( ** ) 31.97 8.00 23.97 235.06 J-15 0.00 27.56 15.00 12.56 123.15 J-16 0.00 20.31 10.00 10.31 101.08 J-17 Arm End Rese 0.00(0.00) 13.06 6.00 7.06 69.21 J-18 0.10(0.33) 61.24 J-20 Southern Far 0.00 46.06 20.00 26.06 255.55 J-21 South Arm Ro 0.00 41.66 10.00 31.66 310.46 J-23 Calverton Ov 2.00( ** ) 44.71 12.00 32.71 320.81 J-24 South Arm Fi 1.00( ** ) 44.56 18.00 26.56 260.44 J-25 Blessington 0.17(0.33) 44.57 15.00 29.57 289.99 J-26 Fort Directi 0.00 44.62 J-27 Fort Directi 0.03(0.33) 44.58 40.00 4.58 44.92 J-28 Shoecraft Ba 0.17(0.33) 44.54 25.00 19.54 191.67 J-2a 0.00 74.50 20.00 54.50 534.48 O-Pump-1 Half Moon Ba 0.00 63.04 5.00 58.04 569.14 O-Pump-3 Blackmans Ba 0.00 74.72 18.00 56.72 556.28 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 12.93 6.00 6.93 68.01 T-2 Breather Pip ---- 43.21 42.00 1.21 11.91 T-19 ---- 61.24 22.00 39.24 384.82 I-Pump-1 Half Moon Ba 0.00 17.96 5.00 12.96 127.07 I-Pump-3 Blackmans Ba 0.00 20.66 18.00 2.66 26.09 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES



kPa kPa --------------------- --------------------- J-5 836.59 J-11 -8.41 J-4 792.69 T-2 11.91 J-6 745.31 R-1 19.61 O-Pump-1 569.14 I-Pump-3 26.09 O-Pump-3 556.28 J-27 44.92 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-10 2.07 P-17 0.01 P-32 2.07 P-28 0.02 P-9 1.32 P-27 0.03 P-2 1.32 P-24 0.04 P-3 1.32 P-25 0.10 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 92.87 P-17 0.00 P-1 33.91 P-28 0.02 P-32 28.50 P-27 0.03 P-30 22.26 P-24 0.03 P-2 11.01 P-25 0.22 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-10 27.41 P-17 0.00 P-32 27.41 P-28 0.02 P-11 8.89 P-27 0.03 P-12 8.89 P-24 0.03 P-13 8.89 P-25 0.21 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 40.63 T-1 40.49 T-2 -14.66 Breather Pip NET SYSTEM INFLOW = 81.12 NET SYSTEM OUTFLOW = -14.66 NET SYSTEM DEMAND = 66.46 T A N K S T A T U S R E P O R T (time = 0.1412 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -40.49 12.93 5.93 1864500. 98.9 DRAINING 5.89 T-2(1) 14.66 43.21 1.21 8583. 60.7 FILLING 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA



================================================================================ Time: 0.246 TIME FROM INITIATION OF EPS = 0.2464 HOURS (0024 HOURS, DAY: 1) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.14924E-04 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 40.52 0.05 0.29 1.07 33.73 4.77 P-2 J-2a J-3 40.52 0.72 0.27 1.32 10.95 8.00 P-3 J-3 J-4 40.52 2.40 0.27 1.32 8.89 8.00 P-4 J-4 J-5 40.52 11.20 0.27 1.32 8.19 8.00 P-5 J-5 J-6 40.52 8.00 0.27 1.32 8.27 8.00 P-6 J-6 J-7 40.52 27.20 0.27 1.32 8.08 8.00 P-7 J-7 J-8 40.52 3.60 0.27 1.32 8.59 8.00 P-8 J-8 I-Pump-1 40.52 1.28 0.27 1.32 9.66 8.00 P-9 O-Pump-1 J-10 40.52 1.52 0.27 1.32 9.40 8.00 P-10 T-2 J-11 -32.06 0.27 0.65 2.06 92.25 27.23 P-11 T-2 J-12 17.75 4.56 0.20 1.14 9.51 9.11 P-12 J-12 J-13 17.75 2.73 0.20 1.14 9.78 9.11 P-13 J-13 J-14 17.75 3.64 0.20 1.14 9.61 9.11 P-14 J-14 J-15 15.75 4.38 0.16 1.01 7.56 7.30 P-15 J-15 J-16 15.75 7.30 0.16 1.01 7.46 7.30 P-16 J-16 J-17 15.75 7.30 0.16 1.01 7.46 7.30 P-17 J-18 J-10 -0.10 0.00 0.00 0.01 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 8.36 15.06 0.12 0.88 7.59 7.53 P-20 J-20 J-21 5.00 4.36 0.04 0.53 2.93 2.91 P-21 J-21 J-1 5.00 0.58 0.04 0.53 3.12 2.91 P-22 J-20 J-23 3.36 1.31 0.03 0.46 2.69 2.63 P-23 J-23 J-24 0.82 0.15 0.00 0.17 0.52 0.51 P-24 J-24 J-25 -0.18 0.01 0.00 0.04 0.03 0.03 P-25 J-25 J-26 -0.51 0.04 0.00 0.10 0.22 0.21 P-26 J-26 J-23 -0.55 0.10 0.00 0.11 0.25 0.24 P-27 J-25 J-28 0.17 0.03 0.00 0.03 0.03 0.03 P-28 J-26 J-27 0.03 0.03 0.00 0.02 0.02 0.02 P-29 J-17 T-1 15.75 0.06 0.06 0.65 5.04 2.47 P-30 O-Pump-3 J-2a 40.52 0.05 0.17 1.07 22.14 4.77 P-31 T-1 J-9 56.00 0.25 0.21 1.18 9.23 5.01 P-32 J-10 J-11 32.06 16.34 0.65 2.06 28.32 27.23 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 40.52 13.41 58.70 45.3 75.00 18. 0.2 0.6 ** ** 23.4 0.2464 Pump-3 40.52 2.66 56.89 54.2 75.00 22. 0.3 0.7 ** ** 12.7 0.2464 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa



------------------------------------------------------------------------------ J-1 Iron Pot Dam 5.00( ** ) 41.71 5.00 36.71 359.96 J-3 0.00 73.69 J-4 0.00 71.02 -10.00 81.02 794.54 J-5 0.00 59.55 -26.00 85.55 839.00 J-6 0.00 51.29 -25.00 76.29 748.13 J-7 0.00 23.82 -15.00 38.82 380.72 J-8 0.00 19.96 J-9 56.00( ** ) 12.42 J-10 0.00 61.91 10.00 51.91 509.08 J-11 0.00 44.92 45.00 -0.08 -0.77 J-12 Northern Far 0.00 39.24 22.00 17.24 169.11 J-13 0.00 36.31 14.00 22.31 218.80 J-14 2.00( ** ) 32.47 8.00 24.47 239.94 J-15 0.00 27.93 15.00 12.93 126.80 J-16 0.00 20.47 10.00 10.47 102.68 J-17 Arm End Rese 0.00(0.00) 13.01 6.00 7.01 68.77 J-18 0.10(0.33) 61.91 J-20 Southern Far 0.00 46.73 20.00 26.73 262.13 J-21 South Arm Ro 0.00 42.33 10.00 32.33 317.04 J-23 Calverton Ov 2.00( ** ) 45.38 12.00 33.38 327.39 J-24 South Arm Fi 1.00( ** ) 45.23 18.00 27.23 267.02 J-25 Blessington 0.17(0.33) 45.24 15.00 30.24 296.57 J-26 Fort Directi 0.00 45.29 J-27 Fort Directi 0.03(0.33) 45.25 40.00 5.25 51.50 J-28 Shoecraft Ba 0.17(0.33) 45.22 25.00 20.22 198.24 J-2a 0.00 74.67 20.00 54.67 536.15 O-Pump-1 Half Moon Ba 0.00 63.70 5.00 58.70 575.63 O-Pump-3 Blackmans Ba 0.00 74.89 18.00 56.89 557.94 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 12.89 6.00 6.89 67.53 T-2 Breather Pip ---- 44.00 42.00 2.00 19.61 T-19 ---- 61.91 22.00 39.91 391.40 I-Pump-1 Half Moon Ba 0.00 18.41 5.00 13.41 131.51 I-Pump-3 Blackmans Ba 0.00 20.66 18.00 2.66 26.11 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- J-5 839.00 J-11 -0.77 J-4 794.54 T-2 19.61 J-6 748.13 R-1 19.61 O-Pump-1 575.63 I-Pump-3 26.11 O-Pump-3 557.94 J-27 51.50 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-10 2.06 P-17 0.01 P-32 2.06 P-28 0.02 P-2 1.32 P-27 0.03 P-3 1.32 P-24 0.04 P-4 1.32 P-25 0.10 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 92.25 P-17 0.00 P-1 33.73 P-28 0.02 P-32 28.32 P-27 0.03 P-30 22.14 P-24 0.03 P-2 10.95 P-25 0.22



H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-10 27.23 P-17 0.00 P-32 27.23 P-28 0.02 P-11 9.11 P-27 0.03 P-12 9.11 P-24 0.03 P-13 9.11 P-25 0.21 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 40.52 T-1 40.25 T-2 -14.31 Breather Pip NET SYSTEM INFLOW = 80.77 NET SYSTEM OUTFLOW = -14.31 NET SYSTEM DEMAND = 66.46 T A N K S T A T U S R E P O R T (time = 0.2464 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -40.25 12.89 5.89 1849169. 98.1 DRAINING 5.89 T-2(1) 14.31 44.00 2.00 14132. 100.0 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Tank Filled/Emptied TIME FROM INITIATION OF EPS = 0.2466 HOURS (0024 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.67408E-03 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 34.46 0.04 0.21 0.91 24.47 3.53 P-2 J-2a J-3 34.46 0.53 0.19 1.12 8.06 5.93 P-3 J-3 J-4 34.46 1.78 0.19 1.12 6.57 5.93 P-4 J-4 J-5 34.46 8.30 0.19 1.12 6.06 5.93 P-5 J-5 J-6 34.46 5.93 0.19 1.12 6.12 5.93 P-6 J-6 J-7 34.46 20.15 0.19 1.12 5.98 5.93 P-7 J-7 J-8 34.46 2.67 0.19 1.12 6.35 5.93 P-8 J-8 I-Pump-1 34.46 0.95 0.19 1.12 7.13 5.93 P-9 O-Pump-1 J-10 34.46 1.13 0.19 1.12 6.94 5.93 P-10 T-2 J-11 -26.00 0.18 0.43 1.67 61.23 18.47 P-11 T-2 J-12 26.00 9.24 0.43 1.67 19.33 18.47 P-12 J-12 J-13 26.00 5.54 0.43 1.67 19.90 18.47 P-13 J-13 J-14 26.00 7.39 0.43 1.67 19.54 18.47



P-14 J-14 J-15 24.00 9.56 0.36 1.54 16.53 15.93 P-15 J-15 J-16 24.00 15.93 0.36 1.54 16.29 15.93 P-16 J-16 J-17 24.00 15.93 0.36 1.54 16.29 15.93 P-17 J-18 J-10 -0.10 0.00 0.00 0.01 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 8.36 15.06 0.12 0.88 7.59 7.53 P-20 J-20 J-21 5.00 4.36 0.04 0.53 2.93 2.91 P-21 J-21 J-1 5.00 0.58 0.04 0.53 3.12 2.91 P-22 J-20 J-23 3.36 1.31 0.03 0.46 2.69 2.63 P-23 J-23 J-24 0.82 0.15 0.00 0.17 0.52 0.51 P-24 J-24 J-25 -0.18 0.01 0.00 0.04 0.03 0.03 P-25 J-25 J-26 -0.51 0.04 0.00 0.10 0.22 0.21 P-26 J-26 J-23 -0.55 0.10 0.00 0.11 0.25 0.24 P-27 J-25 J-28 0.17 0.03 0.00 0.03 0.03 0.03 P-28 J-26 J-27 0.03 0.03 0.00 0.02 0.02 0.02 P-29 J-17 T-1 24.00 0.13 0.15 0.99 11.37 5.39 P-30 O-Pump-3 J-2a 34.46 0.04 0.13 0.91 16.10 3.53 P-31 T-1 J-9 56.00 0.25 0.21 1.18 9.23 5.01 P-32 J-10 J-11 26.00 11.08 0.43 1.67 19.19 18.47 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 34.46 34.40 87.57 53.2 75.00 18. 0.0 0.6 ** ** 44.5 0.2466 Pump-3 34.46 2.76 63.21 60.5 75.00 20. 0.0 0.7 ** ** 12.8 0.2466 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 5.00( ** ) 71.04 5.00 66.04 647.66 J-3 0.00 80.32 J-4 0.00 78.35 -10.00 88.35 866.45 J-5 0.00 69.86 -26.00 95.86 940.11 J-6 0.00 63.75 -25.00 88.75 870.30 J-7 0.00 43.40 -15.00 58.40 572.75 J-8 0.00 40.55 J-9 56.00( ** ) 12.42 J-10 0.00 91.25 10.00 81.25 796.79 J-11 0.00 79.74 45.00 34.74 340.66 J-12 Northern Far 0.00 69.46 22.00 47.46 465.44 J-13 0.00 63.49 14.00 49.49 485.35 J-14 2.00( ** ) 55.68 8.00 47.68 467.53 J-15 0.00 45.75 15.00 30.75 301.60 J-16 0.00 29.46 10.00 19.46 190.86 J-17 Arm End Rese 0.00(0.00) 13.17 6.00 7.17 70.31 J-18 0.10(0.33) 91.25 J-20 Southern Far 0.00 76.07 20.00 56.07 549.83 J-21 South Arm Ro 0.00 71.67 10.00 61.67 604.74 J-23 Calverton Ov 2.00( ** ) 74.72 12.00 62.72 615.09 J-24 South Arm Fi 1.00( ** ) 74.57 18.00 56.57 554.72 J-25 Blessington 0.17(0.33) 74.58 15.00 59.58 584.27 J-26 Fort Directi 0.00 74.62 J-27 Fort Directi 0.03(0.33) 74.59 40.00 34.59 339.20 J-28 Shoecraft Ba 0.17(0.33) 74.55 25.00 49.55 485.95 J-2a 0.00 81.05 20.00 61.05 598.69 O-Pump-1 Half Moon Ba 0.00 92.57 5.00 87.57 858.75 O-Pump-3 Blackmans Ba 0.00 81.21 18.00 63.21 619.88 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 12.89 6.00 6.89 67.53



T-2 Breather Pip ---- 79.13 42.00 37.13 364.08 T-19 ---- 91.25 22.00 69.25 679.10 I-Pump-1 Half Moon Ba 0.00 39.40 5.00 34.40 337.40 I-Pump-3 Blackmans Ba 0.00 20.76 18.00 2.76 27.02 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- J-5 940.11 R-1 19.61 J-6 870.30 I-Pump-3 27.02 J-4 866.45 T-1 67.53 O-Pump-1 858.75 J-17 70.31 J-10 796.79 J-16 190.86 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-11 1.67 P-17 0.01 P-12 1.67 P-28 0.02 P-13 1.67 P-27 0.03 P-10 1.67 P-24 0.04 P-32 1.67 P-25 0.10 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 61.23 P-17 0.00 P-1 24.47 P-28 0.02 P-12 19.90 P-27 0.03 P-13 19.54 P-24 0.03 P-11 19.33 P-25 0.22 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-12 18.47 P-17 0.00 P-11 18.47 P-28 0.02 P-13 18.47 P-27 0.03 P-32 18.47 P-24 0.03 P-10 18.47 P-25 0.21 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.46 T-1 32.00 NET SYSTEM INFLOW = 66.46 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.46



T A N K S T A T U S R E P O R T (time = 0.2466 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.00 12.89 5.89 1849139. 98.1 DRAINING 5.61 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 1.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 1.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 1.000 TIME FROM INITIATION OF EPS = 1.0000 HOURS (0100 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.86666E-05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.42 T-1 31.93 NET SYSTEM INFLOW = 66.35 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.35 T A N K S T A T U S R E P O R T (time = 1.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -31.93 12.61 5.61 1762337. 93.5 DRAINING 5.24 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 2.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 2.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr



JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 2.000 TIME FROM INITIATION OF EPS = 2.0000 HOURS (0200 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.36968E-05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.42 T-1 31.87 NET SYSTEM INFLOW = 66.30 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.30 T A N K S T A T U S R E P O R T (time = 2.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -31.87 12.24 5.24 1647389. 87.4 DRAINING 4.88 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 3.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 3.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 3.000 TIME FROM INITIATION OF EPS = 3.0000 HOURS (0300 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.53380E-05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.46 T-1 31.84 NET SYSTEM INFLOW = 66.30



NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.30 T A N K S T A T U S R E P O R T (time = 3.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -31.84 11.88 4.88 1532650. 81.3 DRAINING 4.51 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 4.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 4.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 4.000 TIME FROM INITIATION OF EPS = 4.0000 HOURS (0400 HOURS, DAY: 1) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.69036E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.00 T-1 -18.63 NET SYSTEM INFLOW = 29.00 NET SYSTEM OUTFLOW = -18.63 NET SYSTEM DEMAND = 10.37 T A N K S T A T U S R E P O R T (time = 4.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.63 11.51 4.51 1418040. 75.2 FILLING 4.73 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 5.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 5.0000 hours)



UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 5.000 TIME FROM INITIATION OF EPS = 5.0000 HOURS (0500 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.62090E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.07 T-1 -18.56 NET SYSTEM INFLOW = 29.07 NET SYSTEM OUTFLOW = -18.56 NET SYSTEM DEMAND = 10.51 T A N K S T A T U S R E P O R T (time = 5.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.56 11.73 4.73 1485102. 78.8 FILLING 4.94 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 6.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 6.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 6.000 TIME FROM INITIATION OF EPS = 6.0000 HOURS (0600 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.60877E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE --------------------------------------------



R-1 29.20 T-1 -18.45 NET SYSTEM INFLOW = 29.20 NET SYSTEM OUTFLOW = -18.45 NET SYSTEM DEMAND = 10.75 T A N K S T A T U S R E P O R T (time = 6.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.45 11.94 4.94 1551908. 82.3 FILLING 5.15 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 7.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 7.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 7.000 TIME FROM INITIATION OF EPS = 7.0000 HOURS (0700 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.63036E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.52 T-1 -18.24 NET SYSTEM INFLOW = 29.52 NET SYSTEM OUTFLOW = -18.24 NET SYSTEM DEMAND = 11.28 T A N K S T A T U S R E P O R T (time = 7.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.24 12.15 5.15 1618336. 85.9 FILLING 5.36 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 8.000



C H A N G E S F O R N E X T S I M U L A T I O N (time = 8.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 8.000 TIME FROM INITIATION OF EPS = 8.0000 HOURS (0800 HOURS, DAY: 1) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.16006E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.75 T-1 -18.06 NET SYSTEM INFLOW = 29.75 NET SYSTEM OUTFLOW = -18.06 NET SYSTEM DEMAND = 11.69 T A N K S T A T U S R E P O R T (time = 8.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.06 12.36 5.36 1683984. 89.3 FILLING 5.57 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 9.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 9.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 9.000 TIME FROM INITIATION OF EPS = 9.0000 HOURS (0900 HOURS, DAY: 1) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.16376E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES



NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.82 T-1 -17.99 NET SYSTEM INFLOW = 29.82 NET SYSTEM OUTFLOW = -17.99 NET SYSTEM DEMAND = 11.83 T A N K S T A T U S R E P O R T (time = 9.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 17.99 12.57 5.57 1749009. 92.8 FILLING 5.77 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 10.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 10.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 10.000 TIME FROM INITIATION OF EPS = 10.0000 HOURS (1000 HOURS, DAY: 1) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.30671E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.83 T-1 -17.95 NET SYSTEM INFLOW = 29.83 NET SYSTEM OUTFLOW = -17.95 NET SYSTEM DEMAND = 11.88 T A N K S T A T U S R E P O R T (time = 10.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 17.95 12.77 5.77 1813774. 96.2 FILLING 5.98 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA



================================================================================ Time: 11.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 11.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 11.000 TIME FROM INITIATION OF EPS = 11.0000 HOURS (1100 HOURS, DAY: 1) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.10104E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.81 T-1 -17.93 NET SYSTEM INFLOW = 29.81 NET SYSTEM OUTFLOW = -17.93 NET SYSTEM DEMAND = 11.88 T A N K S T A T U S R E P O R T (time = 11.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 17.93 12.98 5.98 1878398. 99.7 FILLING 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 11.102 TIME FROM INITIATION OF EPS = 11.1015 HOURS (1110 HOURS, DAY: 1) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.11121E-04 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 29.82 0.03 0.16 0.78 18.38 2.70 P-2 J-2a J-3 29.81 0.41 0.14 0.97 6.13 4.53 P-3 J-3 J-4 29.81 1.36 0.14 0.97 5.01 4.53 P-4 J-4 J-5 29.81 6.34 0.14 0.97 4.63 4.53 P-5 J-5 J-6 29.81 4.53 0.14 0.97 4.68 4.53



P-6 J-6 J-7 29.81 15.41 0.14 0.97 4.57 4.53 P-7 J-7 J-8 29.81 2.04 0.14 0.97 4.85 4.53 P-8 J-8 I-Pump-1 29.81 0.73 0.14 0.97 5.43 4.53 P-9 O-Pump-1 J-10 29.81 0.86 0.14 0.97 5.29 4.53 P-10 T-2 J-11 -27.93 0.21 0.49 1.80 70.48 21.11 P-11 T-2 J-12 27.93 10.55 0.49 1.80 22.09 21.11 P-12 J-12 J-13 27.93 6.33 0.49 1.80 22.75 21.11 P-13 J-13 J-14 27.93 8.44 0.49 1.80 22.34 21.11 P-14 J-14 J-15 27.93 12.66 0.49 1.80 21.93 21.11 P-15 J-15 J-16 27.93 21.11 0.49 1.80 21.60 21.11 P-16 J-16 J-17 27.93 21.11 0.49 1.80 21.60 21.11 P-17 J-18 J-10 -0.40 0.01 0.00 0.04 0.03 0.03 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 1.47 0.61 0.00 0.16 0.30 0.30 P-20 J-20 J-21 0.00 0.00 0.00 0.00 0.00 0.00 P-21 J-21 J-1 0.00 0.00 0.00 0.00 0.00 0.00 P-22 J-20 J-23 1.47 0.29 0.01 0.20 0.58 0.57 P-23 J-23 J-24 0.69 0.11 0.00 0.14 0.38 0.37 P-24 J-24 J-25 0.69 0.15 0.00 0.14 0.37 0.37 P-25 J-25 J-26 -0.65 0.07 0.00 0.13 0.35 0.33 P-26 J-26 J-23 -0.79 0.19 0.00 0.16 0.48 0.47 P-27 J-25 J-28 0.67 0.35 0.00 0.14 0.35 0.35 P-28 J-26 J-27 0.13 0.47 0.00 0.09 0.31 0.31 P-29 J-17 T-1 17.93 0.08 0.08 0.74 6.48 3.14 P-30 O-Pump-3 J-2a 29.81 0.03 0.09 0.78 12.11 2.70 P-31 T-1 J-9 0.01 0.00 0.00 0.00 0.00 0.00 P-32 J-10 J-11 27.93 12.66 0.49 1.80 21.93 21.11 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 29.81 46.51 106.19 59.7 75.00 17. 0.2 25.8 ** ** 56.6 11.1015 Pump-3 29.81 2.82 65.45 62.6 75.00 18. 0.2 27.9 ** ** 12.9 11.1015 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 0.00(0.00) 109.58 5.00 104.58 1025.58 J-3 0.00 82.78 J-4 0.00 81.28 -10.00 91.28 895.12 J-5 0.00 74.79 -26.00 100.79 988.40 J-6 0.00 70.11 -25.00 95.11 932.74 J-7 0.00 54.56 -15.00 69.56 682.15 J-8 0.00 52.38 J-9 0.01(0.00) 13.00 J-10 0.00 110.19 10.00 100.19 982.52 J-11 0.00 97.03 45.00 52.03 510.26 J-12 Northern Far 0.00 85.28 22.00 63.28 620.57 J-13 0.00 78.45 14.00 64.45 632.08 J-14 0.00(0.00) 69.52 8.00 61.52 603.29 J-15 0.00 56.36 15.00 41.36 405.61 J-16 0.00 34.76 10.00 24.76 242.83 J-17 Arm End Rese 10.00( ** ) 13.16 6.00 7.16 70.23 J-18 0.40(1.34) 110.18 J-20 Southern Far 0.00 109.58 20.00 89.58 878.48 J-21 South Arm Ro 0.00 109.58 10.00 99.58 976.54 J-23 Calverton Ov 0.00(0.00) 109.29 12.00 97.29 954.07 J-24 South Arm Fi 0.00(0.00) 109.18 18.00 91.18 894.12 J-25 Blessington 0.67(1.34) 109.03 15.00 94.03 922.08



J-26 Fort Directi 0.00 109.10 J-27 Fort Directi 0.13(1.34) 108.63 40.00 68.63 673.00 J-28 Shoecraft Ba 0.67(1.34) 108.67 25.00 83.67 820.54 J-2a 0.00 83.33 20.00 63.33 621.08 O-Pump-1 Half Moon Ba 0.00 111.19 5.00 106.19 1041.41 O-Pump-3 Blackmans Ba 0.00 83.45 18.00 65.45 641.88 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 13.00 6.00 7.00 68.65 T-2 Breather Pip ---- 96.33 42.00 54.33 532.76 T-19 ---- 110.18 22.00 88.18 864.77 I-Pump-1 Half Moon Ba 0.00 51.51 5.00 46.51 456.09 I-Pump-3 Blackmans Ba 0.00 20.82 18.00 2.82 27.62 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- O-Pump-1 1041.41 R-1 19.61 J-1 1025.58 I-Pump-3 27.62 J-5 988.40 T-1 68.65 J-10 982.52 J-17 70.23 J-21 976.54 J-16 242.83 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-10 1.80 P-20 0.00 P-11 1.80 P-21 0.00 P-12 1.80 P-31 0.00 P-13 1.80 P-17 0.04 P-32 1.80 P-28 0.09 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 70.48 P-20 0.00 P-12 22.75 P-21 0.00 P-13 22.34 P-31 0.00 P-11 22.09 P-17 0.03 P-32 21.93 P-19 0.30 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-10 21.11 P-20 0.00 P-11 21.11 P-21 0.00 P-12 21.11 P-31 0.00 P-13 21.11 P-17 0.03 P-32 21.11 P-19 0.30 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE --------------------------------------------



R-1 29.82 T-1 -17.93 NET SYSTEM INFLOW = 29.82 NET SYSTEM OUTFLOW = -17.93 NET SYSTEM DEMAND = 11.88 T A N K S T A T U S R E P O R T (time = 11.1015 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 17.93 13.00 6.00 1884954. 100.0 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Tank Filled/Emptied TIME FROM INITIATION OF EPS = 11.1017 HOURS (1110 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.52543E-07 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 11.88 0.00 0.02 0.31 2.98 0.49 P-2 J-2a J-3 11.88 0.07 0.02 0.39 1.08 0.83 P-3 J-3 J-4 11.88 0.25 0.02 0.39 0.90 0.83 P-4 J-4 J-5 11.88 1.16 0.02 0.39 0.84 0.83 P-5 J-5 J-6 11.88 0.83 0.02 0.39 0.85 0.83 P-6 J-6 J-7 11.88 2.81 0.02 0.39 0.83 0.83 P-7 J-7 J-8 11.88 0.37 0.02 0.39 0.88 0.83 P-8 J-8 I-Pump-1 11.88 0.13 0.02 0.39 0.97 0.83 P-9 O-Pump-1 J-10 11.88 0.16 0.02 0.39 0.95 0.83 P-10 T-2 J-11 -10.01 0.03 0.06 0.64 9.49 3.15 P-11 T-2 J-12 10.01 1.58 0.06 0.64 3.28 3.15 P-12 J-12 J-13 10.01 0.95 0.06 0.64 3.36 3.15 P-13 J-13 J-14 10.01 1.26 0.06 0.64 3.31 3.15 P-14 J-14 J-15 10.01 1.89 0.06 0.64 3.26 3.15 P-15 J-15 J-16 10.01 3.15 0.06 0.64 3.22 3.15 P-16 J-16 J-17 10.01 3.15 0.06 0.64 3.22 3.15 P-17 J-18 J-10 -0.40 0.01 0.00 0.04 0.03 0.03 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 1.47 0.61 0.00 0.16 0.30 0.30 P-20 J-20 J-21 0.00 0.00 0.00 0.00 0.00 0.00 P-21 J-21 J-1 0.00 0.00 0.00 0.00 0.00 0.00 P-22 J-20 J-23 1.47 0.29 0.01 0.20 0.58 0.57 P-23 J-23 J-24 0.69 0.11 0.00 0.14 0.38 0.37 P-24 J-24 J-25 0.69 0.15 0.00 0.14 0.37 0.37 P-25 J-25 J-26 -0.65 0.07 0.00 0.13 0.35 0.33 P-26 J-26 J-23 -0.79 0.19 0.00 0.16 0.48 0.47 P-27 J-25 J-28 0.67 0.35 0.00 0.14 0.35 0.35 P-28 J-26 J-27 0.13 0.47 0.00 0.09 0.31 0.31 P-29 J-17 T-1 0.01 0.00 0.00 0.00 0.00 0.00 P-30 O-Pump-3 J-2a 11.88 0.00 0.01 0.31 1.99 0.49 P-31 T-1 J-9 0.01 0.00 0.00 0.00 0.00 0.00 P-32 J-10 J-11 10.01 1.89 0.06 0.64 3.26 3.15 P U M P/L O S S E L E M E N T R E S U L T S



INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 11.88 81.10 152.07 71.0 75.00 8. 0.0 25.8 ** ** 91.2 11.1017 Pump-3 11.88 2.97 73.89 70.9 75.00 8. 0.0 27.9 ** ** 13.1 11.1017 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 0.00(0.00) 156.28 5.00 151.28 1483.55 J-3 0.00 91.77 J-4 0.00 91.50 -10.00 101.50 995.40 J-5 0.00 90.32 -26.00 116.32 1140.75 J-6 0.00 89.48 -25.00 114.48 1122.63 J-7 0.00 86.65 -15.00 101.65 996.83 J-8 0.00 86.25 J-9 0.01(0.00) 142.48 J-10 0.00 156.89 10.00 146.89 1440.49 J-11 0.00 154.93 45.00 109.93 1078.09 J-12 Northern Far 0.00 153.20 22.00 131.20 1286.64 J-13 0.00 152.19 14.00 138.19 1355.19 J-14 0.00(0.00) 150.87 8.00 142.87 1401.05 J-15 0.00 148.91 15.00 133.91 1313.23 J-16 0.00 145.70 10.00 135.70 1330.73 J-17 Arm End Rese 10.00( ** ) 142.48 6.00 136.48 1338.43 J-18 0.40(1.34) 156.88 J-20 Southern Far 0.00 156.28 20.00 136.28 1336.45 J-21 South Arm Ro 0.00 156.28 10.00 146.28 1434.52 J-23 Calverton Ov 0.00(0.00) 155.99 12.00 143.99 1412.05 J-24 South Arm Fi 0.00(0.00) 155.88 18.00 137.88 1352.10 J-25 Blessington 0.67(1.34) 155.73 15.00 140.73 1380.05 J-26 Fort Directi 0.00 155.80 J-27 Fort Directi 0.13(1.34) 155.33 40.00 115.33 1130.98 J-28 Shoecraft Ba 0.67(1.34) 155.37 25.00 130.37 1278.52 J-2a 0.00 91.87 20.00 71.87 704.80 O-Pump-1 Half Moon Ba 0.00 157.07 5.00 152.07 1491.29 O-Pump-3 Blackmans Ba 0.00 91.89 18.00 73.89 724.61 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 142.48 6.00 136.48 1338.43 T-2 Breather Pip ---- 154.84 42.00 112.84 1106.58 T-19 ---- 156.88 22.00 134.88 1322.74 I-Pump-1 Half Moon Ba 0.00 86.10 5.00 81.10 795.31 I-Pump-3 Blackmans Ba 0.00 20.97 18.00 2.97 29.13 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- O-Pump-1 1491.29 R-1 19.61 J-1 1483.55 I-Pump-3 29.13 J-10 1440.49 J-2a 704.80 J-21 1434.52 O-Pump-3 724.61 J-23 1412.05 I-Pump-1 795.31 V E L O C I T I E S



PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-10 0.64 P-20 0.00 P-11 0.64 P-21 0.00 P-12 0.64 P-31 0.00 P-13 0.64 P-29 0.00 P-32 0.64 P-17 0.04 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 9.49 P-20 0.00 P-12 3.36 P-21 0.00 P-13 3.31 P-31 0.00 P-11 3.28 P-29 0.00 P-32 3.26 P-17 0.03 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-10 3.15 P-20 0.00 P-11 3.15 P-21 0.00 P-12 3.15 P-31 0.00 P-32 3.15 P-29 0.00 P-13 3.15 P-17 0.03 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.88 NET SYSTEM INFLOW = 11.88 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.88 T A N K S T A T U S R E P O R T (time = 11.1017 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 12.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 12.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr



JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 12.000 TIME FROM INITIATION OF EPS = 12.0000 HOURS (1200 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.00000E+00 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.85 NET SYSTEM INFLOW = 11.85 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.85 T A N K S T A T U S R E P O R T (time = 12.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 13.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 13.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 13.000 TIME FROM INITIATION OF EPS = 13.0000 HOURS (1300 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.33974E-08 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.78 NET SYSTEM INFLOW = 11.78 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.78



T A N K S T A T U S R E P O R T (time = 13.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 14.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 14.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 14.000 TIME FROM INITIATION OF EPS = 14.0000 HOURS (1400 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.19452E-08 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.76 NET SYSTEM INFLOW = 11.76 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.76 T A N K S T A T U S R E P O R T (time = 14.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 15.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 15.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr



JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 15.000 TIME FROM INITIATION OF EPS = 15.0000 HOURS (1500 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.19452E-08 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.76 NET SYSTEM INFLOW = 11.76 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.76 T A N K S T A T U S R E P O R T (time = 15.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 16.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 16.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 16.000 TIME FROM INITIATION OF EPS = 16.0000 HOURS (1600 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.53820E-07 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.80 NET SYSTEM INFLOW = 11.80 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.80



T A N K S T A T U S R E P O R T (time = 16.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 17.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 17.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 17.000 TIME FROM INITIATION OF EPS = 17.0000 HOURS (1700 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.26436E-08 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.92 NET SYSTEM INFLOW = 11.92 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.92 T A N K S T A T U S R E P O R T (time = 17.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 18.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 18.0000 hours)



UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 18.000 TIME FROM INITIATION OF EPS = 18.0000 HOURS (1800 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.54248E-07 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 12.13 NET SYSTEM INFLOW = 12.13 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 12.13 T A N K S T A T U S R E P O R T (time = 18.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 19.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 19.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 19.000 TIME FROM INITIATION OF EPS = 19.0000 HOURS (1900 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.44251E-08 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 12.39 NET SYSTEM INFLOW = 12.39 NET SYSTEM OUTFLOW = 0.00



NET SYSTEM DEMAND = 12.39 T A N K S T A T U S R E P O R T (time = 19.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 20.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 20.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 20.000 TIME FROM INITIATION OF EPS = 20.0000 HOURS (2000 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.44045E-08 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 12.46 NET SYSTEM INFLOW = 12.46 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 12.46 T A N K S T A T U S R E P O R T (time = 20.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 21.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 21.0000 hours)



UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 21.000 TIME FROM INITIATION OF EPS = 21.0000 HOURS (2100 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.55586E-07 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 12.34 NET SYSTEM INFLOW = 12.34 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 12.34 T A N K S T A T U S R E P O R T (time = 21.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 22.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 22.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 22.000 TIME FROM INITIATION OF EPS = 22.0000 HOURS (2200 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.55890E-07 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 11.27 NET SYSTEM INFLOW = 11.27



NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 11.27 T A N K S T A T U S R E P O R T (time = 22.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 23.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 23.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 23.000 TIME FROM INITIATION OF EPS = 23.0000 HOURS (2300 HOURS, DAY: 1) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.13147E-08 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 23.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 24.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 24.0000 hours)



UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 24.000 TIME FROM INITIATION OF EPS = 24.0000 HOURS (2400 HOURS, DAY: 1) RESULTS OBTAINED AFTER 5 TRIALS: ACCURACY = 0.22734E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.57 T-1 32.11 NET SYSTEM INFLOW = 66.67 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 24.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.11 13.00 6.00 1884960. 100.0 DRAINING 5.63 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 25.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 25.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 25.000 TIME FROM INITIATION OF EPS = 25.0000 HOURS (0100 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.12162E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.61



T-1 32.07 NET SYSTEM INFLOW = 66.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 25.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.07 12.63 5.63 1769378. 93.9 DRAINING 5.26 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 26.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 26.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 26.000 TIME FROM INITIATION OF EPS = 26.0000 HOURS (0200 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.99071E-05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.64 T-1 32.04 NET SYSTEM INFLOW = 66.67 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 26.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.04 12.26 5.26 1653923. 87.7 DRAINING 4.90 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 27.000



C H A N G E S F O R N E X T S I M U L A T I O N (time = 27.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 27.000 TIME FROM INITIATION OF EPS = 27.0000 HOURS (0300 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.54266E-05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.67 T-1 32.00 NET SYSTEM INFLOW = 66.67 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 27.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.00 11.90 4.90 1538595. 81.6 DRAINING 4.53 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 28.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 28.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 28.000 TIME FROM INITIATION OF EPS = 28.0000 HOURS (0400 HOURS, DAY: 2) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.51789E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES



NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.20 T-1 -18.51 NET SYSTEM INFLOW = 29.20 NET SYSTEM OUTFLOW = -18.51 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 28.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.51 11.53 4.53 1423395. 75.5 FILLING 4.74 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 29.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 29.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 29.000 TIME FROM INITIATION OF EPS = 29.0000 HOURS (0500 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.60482E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.17 T-1 -18.49 NET SYSTEM INFLOW = 29.17 NET SYSTEM OUTFLOW = -18.49 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 29.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.49 11.74 4.74 1490043. 79.0 FILLING 4.95 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA



================================================================================ Time: 30.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 30.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 30.000 TIME FROM INITIATION OF EPS = 30.0000 HOURS (0600 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.63391E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.15 T-1 -18.48 NET SYSTEM INFLOW = 29.15 NET SYSTEM OUTFLOW = -18.48 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 30.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.48 11.95 4.95 1556622. 82.6 FILLING 5.17 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 31.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 31.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 31.000 TIME FROM INITIATION OF EPS = 31.0000 HOURS (0700 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.68054E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S



(+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.13 T-1 -18.46 NET SYSTEM INFLOW = 29.13 NET SYSTEM OUTFLOW = -18.46 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 31.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.46 12.17 5.17 1623136. 86.1 FILLING 5.38 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 32.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 32.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 32.000 TIME FROM INITIATION OF EPS = 32.0000 HOURS (0800 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.61389E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.11 T-1 -18.44 NET SYSTEM INFLOW = 29.11 NET SYSTEM OUTFLOW = -18.44 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 32.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.44 12.38 5.38 1689580. 89.6 FILLING 5.59 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00



T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 33.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 33.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 33.000 TIME FROM INITIATION OF EPS = 33.0000 HOURS (0900 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.78136E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.09 T-1 -18.41 NET SYSTEM INFLOW = 29.09 NET SYSTEM OUTFLOW = -18.41 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 33.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.41 12.59 5.59 1755956. 93.2 FILLING 5.80 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 34.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 34.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 34.000 TIME FROM INITIATION OF EPS = 34.0000 HOURS (1000 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.60115E-04



S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.07 T-1 -18.39 NET SYSTEM INFLOW = 29.07 NET SYSTEM OUTFLOW = -18.39 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 34.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.39 12.80 5.80 1822234. 96.7 FILLING 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 34.947 TIME FROM INITIATION OF EPS = 34.9472 HOURS (1094 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.66974E-04 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 29.05 0.03 0.15 0.76 17.46 2.57 P-2 J-2a J-3 29.05 0.39 0.14 0.95 5.84 4.32 P-3 J-3 J-4 29.05 1.30 0.14 0.95 4.78 4.32 P-4 J-4 J-5 29.05 6.05 0.14 0.95 4.42 4.32 P-5 J-5 J-6 29.05 4.32 0.14 0.95 4.46 4.32 P-6 J-6 J-7 29.05 14.69 0.14 0.95 4.36 4.32 P-7 J-7 J-8 29.05 1.94 0.14 0.95 4.62 4.32 P-8 J-8 I-Pump-1 29.05 0.69 0.14 0.95 5.18 4.32 P-9 O-Pump-1 J-10 29.05 0.82 0.14 0.95 5.04 4.32 P-10 T-2 J-11 -28.38 0.22 0.51 1.83 72.69 21.73 P-11 T-2 J-12 28.38 10.87 0.51 1.83 22.75 21.73 P-12 J-12 J-13 28.38 6.52 0.51 1.83 23.43 21.73 P-13 J-13 J-14 28.38 8.69 0.51 1.83 23.01 21.73 P-14 J-14 J-15 28.38 13.04 0.51 1.83 22.58 21.73 P-15 J-15 J-16 28.38 21.73 0.51 1.83 22.24 21.73 P-16 J-16 J-17 28.38 21.73 0.51 1.83 22.24 21.73 P-17 J-18 J-10 -0.14 0.00 0.00 0.02 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 0.53 0.09 0.00 0.06 0.05 0.05 P-20 J-20 J-21 0.00 0.00 0.00 0.00 0.00 0.00 P-21 J-21 J-1 0.00 0.00 0.00 0.00 0.00 0.00 P-22 J-20 J-23 0.53 0.04 0.00 0.07 0.09 0.09 P-23 J-23 J-24 0.25 0.02 0.00 0.05 0.06 0.05 P-24 J-24 J-25 0.25 0.02 0.00 0.05 0.06 0.05 P-25 J-25 J-26 -0.23 0.01 0.00 0.05 0.05 0.05 P-26 J-26 J-23 -0.28 0.03 0.00 0.06 0.07 0.07



P-27 J-25 J-28 0.24 0.05 0.00 0.05 0.05 0.05 P-28 J-26 J-27 0.05 0.07 0.00 0.03 0.05 0.05 P-29 J-17 T-1 18.38 0.08 0.09 0.76 6.79 3.29 P-30 O-Pump-3 J-2a 29.05 0.03 0.09 0.76 11.51 2.57 P-31 T-1 J-9 0.01 0.00 0.00 0.00 0.00 0.00 P-32 J-10 J-11 28.38 13.04 0.51 1.83 22.58 21.73 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 29.05 48.39 109.05 60.7 75.00 17. 2.2 65.2 ** ** 58.5 34.9472 Pump-3 29.05 2.83 65.84 63.0 75.00 18. 2.2 69.2 ** ** 12.9 34.9472 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 0.00(0.00) 113.00 5.00 108.00 1059.10 J-3 0.00 83.20 J-4 0.00 81.77 -10.00 91.77 899.93 J-5 0.00 75.58 -26.00 101.58 996.18 J-6 0.00 71.12 -25.00 96.12 942.66 J-7 0.00 56.30 -15.00 71.30 699.19 J-8 0.00 54.22 J-9 0.01(0.00) 13.00 J-10 0.00 113.09 10.00 103.09 1010.96 J-11 0.00 99.54 45.00 54.54 534.85 J-12 Northern Far 0.00 87.44 22.00 65.44 641.71 J-13 0.00 80.41 14.00 66.41 651.23 J-14 0.00(0.00) 71.20 8.00 63.20 619.82 J-15 0.00 57.65 15.00 42.65 418.30 J-16 0.00 35.41 10.00 25.41 249.21 J-17 Arm End Rese 10.00( ** ) 13.17 6.00 7.17 70.31 J-18 0.14(0.48) 113.09 J-20 Southern Far 0.00 113.00 20.00 93.00 912.00 J-21 South Arm Ro 0.00 113.00 10.00 103.00 1010.06 J-23 Calverton Ov 0.00(0.00) 112.95 12.00 100.95 990.02 J-24 South Arm Fi 0.00(0.00) 112.94 18.00 94.94 931.02 J-25 Blessington 0.24(0.48) 112.92 15.00 97.92 960.22 J-26 Fort Directi 0.00 112.93 J-27 Fort Directi 0.05(0.48) 112.86 40.00 72.86 714.47 J-28 Shoecraft Ba 0.24(0.48) 112.86 25.00 87.86 861.64 J-2a 0.00 83.73 20.00 63.73 624.94 O-Pump-1 Half Moon Ba 0.00 114.05 5.00 109.05 1069.38 O-Pump-3 Blackmans Ba 0.00 83.84 18.00 65.84 645.68 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 13.00 6.00 7.00 68.65 T-2 Breather Pip ---- 98.81 42.00 56.81 557.14 T-19 ---- 113.09 22.00 91.09 893.27 I-Pump-1 Half Moon Ba 0.00 53.39 5.00 48.39 474.53 I-Pump-3 Blackmans Ba 0.00 20.83 18.00 2.83 27.71 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM



NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- O-Pump-1 1069.38 R-1 19.61 J-1 1059.10 I-Pump-3 27.71 J-10 1010.96 T-1 68.65 J-21 1010.06 J-17 70.31 J-5 996.18 J-16 249.21 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-11 1.83 P-20 0.00 P-12 1.83 P-21 0.00 P-13 1.83 P-31 0.00 P-10 1.83 P-17 0.02 P-32 1.83 P-28 0.03 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 72.69 P-20 0.00 P-12 23.43 P-21 0.00 P-13 23.01 P-31 0.00 P-11 22.75 P-17 0.00 P-32 22.58 P-19 0.05 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-11 21.73 P-20 0.00 P-12 21.73 P-21 0.00 P-13 21.73 P-31 0.00 P-10 21.73 P-17 0.00 P-32 21.73 P-19 0.05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.05 T-1 -18.38 NET SYSTEM INFLOW = 29.05 NET SYSTEM OUTFLOW = -18.38 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 34.9472 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.38 13.00 6.00 1884953. 100.0 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA



================================================================================ Tank Filled/Emptied TIME FROM INITIATION OF EPS = 34.9474 HOURS (1094 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 10.68 0.00 0.02 0.28 2.41 0.40 P-2 J-2a J-3 10.68 0.06 0.02 0.35 0.88 0.68 P-3 J-3 J-4 10.68 0.20 0.02 0.35 0.74 0.68 P-4 J-4 J-5 10.68 0.95 0.02 0.35 0.69 0.68 P-5 J-5 J-6 10.68 0.68 0.02 0.35 0.70 0.68 P-6 J-6 J-7 10.68 2.30 0.02 0.35 0.68 0.68 P-7 J-7 J-8 10.68 0.30 0.02 0.35 0.72 0.68 P-8 J-8 I-Pump-1 10.68 0.11 0.02 0.35 0.79 0.68 P-9 O-Pump-1 J-10 10.68 0.13 0.02 0.35 0.77 0.68 P-10 T-2 J-11 -10.01 0.03 0.06 0.64 9.49 3.15 P-11 T-2 J-12 10.01 1.58 0.06 0.64 3.28 3.15 P-12 J-12 J-13 10.01 0.95 0.06 0.64 3.36 3.15 P-13 J-13 J-14 10.01 1.26 0.06 0.64 3.31 3.15 P-14 J-14 J-15 10.01 1.89 0.06 0.64 3.26 3.15 P-15 J-15 J-16 10.01 3.15 0.06 0.64 3.22 3.15 P-16 J-16 J-17 10.01 3.15 0.06 0.64 3.22 3.15 P-17 J-18 J-10 -0.14 0.00 0.00 0.02 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 0.53 0.09 0.00 0.06 0.05 0.05 P-20 J-20 J-21 0.00 0.00 0.00 0.00 0.00 0.00 P-21 J-21 J-1 0.00 0.00 0.00 0.00 0.00 0.00 P-22 J-20 J-23 0.53 0.04 0.00 0.07 0.09 0.09 P-23 J-23 J-24 0.25 0.02 0.00 0.05 0.06 0.05 P-24 J-24 J-25 0.25 0.02 0.00 0.05 0.06 0.05 P-25 J-25 J-26 -0.23 0.01 0.00 0.05 0.05 0.05 P-26 J-26 J-23 -0.28 0.03 0.00 0.06 0.07 0.07 P-27 J-25 J-28 0.24 0.05 0.00 0.05 0.05 0.05 P-28 J-26 J-27 0.05 0.07 0.00 0.03 0.05 0.05 P-29 J-17 T-1 0.01 0.00 0.00 0.00 0.00 0.00 P-30 O-Pump-3 J-2a 10.68 0.00 0.01 0.28 1.61 0.40 P-31 T-1 J-9 0.01 0.00 0.00 0.00 0.00 0.00 P-32 J-10 J-11 10.01 1.89 0.06 0.64 3.26 3.15 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 10.68 82.64 154.14 71.5 75.00 7. 0.0 65.2 ** ** 92.8 34.9474 Pump-3 10.68 2.98 74.39 71.4 75.00 7. 0.0 69.2 ** ** 13.1 34.9474 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa



------------------------------------------------------------------------------ J-1 Iron Pot Dam 0.00(0.00) 158.90 5.00 153.90 1509.29 J-3 0.00 92.29 J-4 0.00 92.07 -10.00 102.07 1000.97 J-5 0.00 91.10 -26.00 117.10 1148.41 J-6 0.00 90.41 -25.00 115.41 1131.78 J-7 0.00 88.09 -15.00 103.09 1010.96 J-8 0.00 87.77 J-9 0.01(0.00) 144.59 J-10 0.00 159.00 10.00 149.00 1461.15 J-11 0.00 157.04 45.00 112.04 1098.75 J-12 Northern Far 0.00 155.31 22.00 133.31 1307.29 J-13 0.00 154.30 14.00 140.30 1375.85 J-14 0.00(0.00) 152.97 8.00 144.97 1421.70 J-15 0.00 151.02 15.00 136.02 1333.89 J-16 0.00 147.80 10.00 137.80 1351.39 J-17 Arm End Rese 10.00( ** ) 144.59 6.00 138.59 1359.08 J-18 0.14(0.48) 158.99 J-20 Southern Far 0.00 158.90 20.00 138.90 1362.19 J-21 South Arm Ro 0.00 158.90 10.00 148.90 1460.26 J-23 Calverton Ov 0.00(0.00) 158.86 12.00 146.86 1440.22 J-24 South Arm Fi 0.00(0.00) 158.84 18.00 140.84 1381.21 J-25 Blessington 0.24(0.48) 158.82 15.00 143.82 1410.41 J-26 Fort Directi 0.00 158.83 J-27 Fort Directi 0.05(0.48) 158.76 40.00 118.76 1164.66 J-28 Shoecraft Ba 0.24(0.48) 158.77 25.00 133.77 1311.83 J-2a 0.00 92.37 20.00 72.37 709.73 O-Pump-1 Half Moon Ba 0.00 159.14 5.00 154.14 1511.63 O-Pump-3 Blackmans Ba 0.00 92.39 18.00 74.39 729.50 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 144.59 6.00 138.59 1359.08 T-2 Breather Pip ---- 156.95 42.00 114.95 1127.24 T-19 ---- 158.99 22.00 136.99 1343.46 I-Pump-1 Half Moon Ba 0.00 87.64 5.00 82.64 810.42 I-Pump-3 Blackmans Ba 0.00 20.98 18.00 2.98 29.18 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- O-Pump-1 1511.63 R-1 19.61 J-1 1509.29 I-Pump-3 29.18 J-10 1461.15 J-2a 709.73 J-21 1460.26 O-Pump-3 729.50 J-23 1440.22 I-Pump-1 810.42 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-10 0.64 P-20 0.00 P-11 0.64 P-21 0.00 P-12 0.64 P-31 0.00 P-13 0.64 P-29 0.00 P-32 0.64 P-17 0.02 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 9.49 P-20 0.00 P-12 3.36 P-21 0.00 P-13 3.31 P-31 0.00 P-11 3.28 P-29 0.00 P-32 3.26 P-17 0.00



H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-10 3.15 P-20 0.00 P-11 3.15 P-21 0.00 P-12 3.15 P-31 0.00 P-32 3.15 P-29 0.00 P-13 3.15 P-17 0.00 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 34.9474 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 35.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 35.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 35.000 TIME FROM INITIATION OF EPS = 35.0000 HOURS (1100 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68



NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 35.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 36.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 36.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 36.000 TIME FROM INITIATION OF EPS = 36.0000 HOURS (1200 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 36.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 37.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 37.0000 hours)



UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 37.000 TIME FROM INITIATION OF EPS = 37.0000 HOURS (1300 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 37.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 38.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 38.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 38.000 TIME FROM INITIATION OF EPS = 38.0000 HOURS (1400 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68



NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 38.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 39.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 39.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 39.000 TIME FROM INITIATION OF EPS = 39.0000 HOURS (1500 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 39.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 40.000



C H A N G E S F O R N E X T S I M U L A T I O N (time = 40.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 40.000 TIME FROM INITIATION OF EPS = 40.0000 HOURS (1600 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 40.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 41.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 41.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 41.000 TIME FROM INITIATION OF EPS = 41.0000 HOURS (1700 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE --------------------------------------------



R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 41.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 42.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 42.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 42.000 TIME FROM INITIATION OF EPS = 42.0000 HOURS (1800 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 42.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 43.000



C H A N G E S F O R N E X T S I M U L A T I O N (time = 43.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 43.000 TIME FROM INITIATION OF EPS = 43.0000 HOURS (1900 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 43.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 44.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 44.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 44.000 TIME FROM INITIATION OF EPS = 44.0000 HOURS (2000 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE



-------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 44.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 45.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 45.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 45.000 TIME FROM INITIATION OF EPS = 45.0000 HOURS (2100 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 45.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 46.000



C H A N G E S F O R N E X T S I M U L A T I O N (time = 46.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 46.000 TIME FROM INITIATION OF EPS = 46.0000 HOURS (2200 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 46.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 47.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 47.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 47.000 TIME FROM INITIATION OF EPS = 47.0000 HOURS (2300 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE



NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 47.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 48.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 48.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 48.000 TIME FROM INITIATION OF EPS = 48.0000 HOURS (2400 HOURS, DAY: 2) RESULTS OBTAINED AFTER 5 TRIALS: ACCURACY = 0.22734E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.57 T-1 32.11 NET SYSTEM INFLOW = 66.67 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 48.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.11 13.00 6.00 1884960. 100.0 DRAINING 5.63 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================



Time: 49.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 49.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 49.000 TIME FROM INITIATION OF EPS = 49.0000 HOURS (2500 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.12162E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.61 T-1 32.07 NET SYSTEM INFLOW = 66.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 49.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.07 12.63 5.63 1769378. 93.9 DRAINING 5.26 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 50.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 50.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 50.000 TIME FROM INITIATION OF EPS = 50.0000 HOURS (2600 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.99071E-05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES



(-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.64 T-1 32.04 NET SYSTEM INFLOW = 66.67 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 50.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.04 12.26 5.26 1653923. 87.7 DRAINING 4.90 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 51.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 51.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 51.000 TIME FROM INITIATION OF EPS = 51.0000 HOURS (2700 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.54266E-05 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.67 T-1 32.00 NET SYSTEM INFLOW = 66.67 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 51.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.00 11.90 4.90 1538595. 81.6 DRAINING 4.53 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00



* TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 52.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 52.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 52.000 TIME FROM INITIATION OF EPS = 52.0000 HOURS (2800 HOURS, DAY: 2) RESULTS OBTAINED AFTER 4 TRIALS: ACCURACY = 0.51789E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.20 T-1 -18.51 NET SYSTEM INFLOW = 29.20 NET SYSTEM OUTFLOW = -18.51 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 52.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.51 11.53 4.53 1423395. 75.5 FILLING 4.74 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 53.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 53.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 53.000 TIME FROM INITIATION OF EPS = 53.0000 HOURS (2900 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.60482E-04



S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.17 T-1 -18.49 NET SYSTEM INFLOW = 29.17 NET SYSTEM OUTFLOW = -18.49 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 53.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.49 11.74 4.74 1490043. 79.0 FILLING 4.95 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 54.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 54.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 54.000 TIME FROM INITIATION OF EPS = 54.0000 HOURS (3000 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.63391E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.15 T-1 -18.48 NET SYSTEM INFLOW = 29.15 NET SYSTEM OUTFLOW = -18.48 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 54.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m -------------------------------------------------------------------------------



T-1(1) 18.48 11.95 4.95 1556622. 82.6 FILLING 5.17 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 55.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 55.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 55.000 TIME FROM INITIATION OF EPS = 55.0000 HOURS (3100 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.68054E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.13 T-1 -18.46 NET SYSTEM INFLOW = 29.13 NET SYSTEM OUTFLOW = -18.46 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 55.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.46 12.17 5.17 1623136. 86.1 FILLING 5.38 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 56.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 56.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 56.000 TIME FROM INITIATION OF EPS = 56.0000 HOURS (3200 HOURS, DAY: 2)



RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.61389E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.11 T-1 -18.44 NET SYSTEM INFLOW = 29.11 NET SYSTEM OUTFLOW = -18.44 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 56.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.44 12.38 5.38 1689580. 89.6 FILLING 5.59 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 57.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 57.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 57.000 TIME FROM INITIATION OF EPS = 57.0000 HOURS (3300 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.78136E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.09 T-1 -18.41 NET SYSTEM INFLOW = 29.09 NET SYSTEM OUTFLOW = -18.41 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 57.0000 hours)



TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.41 12.59 5.59 1755956. 93.2 FILLING 5.80 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 58.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 58.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 58.000 TIME FROM INITIATION OF EPS = 58.0000 HOURS (3400 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.60115E-04 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.07 T-1 -18.39 NET SYSTEM INFLOW = 29.07 NET SYSTEM OUTFLOW = -18.39 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 58.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.39 12.80 5.80 1822234. 96.7 FILLING 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 58.947 TIME FROM INITIATION OF EPS = 58.9472 HOURS (3494 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.66974E-04 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE



P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 29.05 0.03 0.15 0.76 17.46 2.57 P-2 J-2a J-3 29.05 0.39 0.14 0.95 5.84 4.32 P-3 J-3 J-4 29.05 1.30 0.14 0.95 4.78 4.32 P-4 J-4 J-5 29.05 6.05 0.14 0.95 4.42 4.32 P-5 J-5 J-6 29.05 4.32 0.14 0.95 4.46 4.32 P-6 J-6 J-7 29.05 14.69 0.14 0.95 4.36 4.32 P-7 J-7 J-8 29.05 1.94 0.14 0.95 4.62 4.32 P-8 J-8 I-Pump-1 29.05 0.69 0.14 0.95 5.18 4.32 P-9 O-Pump-1 J-10 29.05 0.82 0.14 0.95 5.04 4.32 P-10 T-2 J-11 -28.38 0.22 0.51 1.83 72.69 21.73 P-11 T-2 J-12 28.38 10.87 0.51 1.83 22.75 21.73 P-12 J-12 J-13 28.38 6.52 0.51 1.83 23.43 21.73 P-13 J-13 J-14 28.38 8.69 0.51 1.83 23.01 21.73 P-14 J-14 J-15 28.38 13.04 0.51 1.83 22.58 21.73 P-15 J-15 J-16 28.38 21.73 0.51 1.83 22.24 21.73 P-16 J-16 J-17 28.38 21.73 0.51 1.83 22.24 21.73 P-17 J-18 J-10 -0.14 0.00 0.00 0.02 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 0.53 0.09 0.00 0.06 0.05 0.05 P-20 J-20 J-21 0.00 0.00 0.00 0.00 0.00 0.00 P-21 J-21 J-1 0.00 0.00 0.00 0.00 0.00 0.00 P-22 J-20 J-23 0.53 0.04 0.00 0.07 0.09 0.09 P-23 J-23 J-24 0.25 0.02 0.00 0.05 0.06 0.05 P-24 J-24 J-25 0.25 0.02 0.00 0.05 0.06 0.05 P-25 J-25 J-26 -0.23 0.01 0.00 0.05 0.05 0.05 P-26 J-26 J-23 -0.28 0.03 0.00 0.06 0.07 0.07 P-27 J-25 J-28 0.24 0.05 0.00 0.05 0.05 0.05 P-28 J-26 J-27 0.05 0.07 0.00 0.03 0.05 0.05 P-29 J-17 T-1 18.38 0.08 0.09 0.76 6.79 3.29 P-30 O-Pump-3 J-2a 29.05 0.03 0.09 0.76 11.51 2.57 P-31 T-1 J-9 0.01 0.00 0.00 0.00 0.00 0.00 P-32 J-10 J-11 28.38 13.04 0.51 1.83 22.58 21.73 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 29.05 48.39 109.05 60.7 75.00 17. 2.2 103.5 ** ** 58.5 58.9472 Pump-3 29.05 2.83 65.84 63.0 75.00 18. 2.2 109.5 ** ** 12.9 58.9472 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 0.00(0.00) 113.00 5.00 108.00 1059.10 J-3 0.00 83.20 J-4 0.00 81.77 -10.00 91.77 899.93 J-5 0.00 75.58 -26.00 101.58 996.18 J-6 0.00 71.12 -25.00 96.12 942.66 J-7 0.00 56.30 -15.00 71.30 699.19 J-8 0.00 54.22 J-9 0.01(0.00) 13.00 J-10 0.00 113.09 10.00 103.09 1010.96 J-11 0.00 99.54 45.00 54.54 534.85 J-12 Northern Far 0.00 87.44 22.00 65.44 641.71 J-13 0.00 80.41 14.00 66.41 651.23 J-14 0.00(0.00) 71.20 8.00 63.20 619.82



J-15 0.00 57.65 15.00 42.65 418.30 J-16 0.00 35.41 10.00 25.41 249.21 J-17 Arm End Rese 10.00( ** ) 13.17 6.00 7.17 70.31 J-18 0.14(0.48) 113.09 J-20 Southern Far 0.00 113.00 20.00 93.00 912.00 J-21 South Arm Ro 0.00 113.00 10.00 103.00 1010.06 J-23 Calverton Ov 0.00(0.00) 112.95 12.00 100.95 990.02 J-24 South Arm Fi 0.00(0.00) 112.94 18.00 94.94 931.02 J-25 Blessington 0.24(0.48) 112.92 15.00 97.92 960.22 J-26 Fort Directi 0.00 112.93 J-27 Fort Directi 0.05(0.48) 112.86 40.00 72.86 714.47 J-28 Shoecraft Ba 0.24(0.48) 112.86 25.00 87.86 861.64 J-2a 0.00 83.73 20.00 63.73 624.94 O-Pump-1 Half Moon Ba 0.00 114.05 5.00 109.05 1069.38 O-Pump-3 Blackmans Ba 0.00 83.84 18.00 65.84 645.68 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 13.00 6.00 7.00 68.65 T-2 Breather Pip ---- 98.81 42.00 56.81 557.14 T-19 ---- 113.09 22.00 91.09 893.27 I-Pump-1 Half Moon Ba 0.00 53.39 5.00 48.39 474.53 I-Pump-3 Blackmans Ba 0.00 20.83 18.00 2.83 27.71 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- O-Pump-1 1069.38 R-1 19.61 J-1 1059.10 I-Pump-3 27.71 J-10 1010.96 T-1 68.65 J-21 1010.06 J-17 70.31 J-5 996.18 J-16 249.21 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-11 1.83 P-20 0.00 P-12 1.83 P-21 0.00 P-13 1.83 P-31 0.00 P-10 1.83 P-17 0.02 P-32 1.83 P-28 0.03 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 72.69 P-20 0.00 P-12 23.43 P-21 0.00 P-13 23.01 P-31 0.00 P-11 22.75 P-17 0.00 P-32 22.58 P-19 0.05 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-11 21.73 P-20 0.00 P-12 21.73 P-21 0.00 P-13 21.73 P-31 0.00 P-10 21.73 P-17 0.00 P-32 21.73 P-19 0.05



S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 29.05 T-1 -18.38 NET SYSTEM INFLOW = 29.05 NET SYSTEM OUTFLOW = -18.38 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 58.9472 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 18.38 13.00 6.00 1884953. 100.0 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Tank Filled/Emptied TIME FROM INITIATION OF EPS = 58.9474 HOURS (3494 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 P I P E L I N E R E S U L T S STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 10.68 0.00 0.02 0.28 2.41 0.40 P-2 J-2a J-3 10.68 0.06 0.02 0.35 0.88 0.68 P-3 J-3 J-4 10.68 0.20 0.02 0.35 0.74 0.68 P-4 J-4 J-5 10.68 0.95 0.02 0.35 0.69 0.68 P-5 J-5 J-6 10.68 0.68 0.02 0.35 0.70 0.68 P-6 J-6 J-7 10.68 2.30 0.02 0.35 0.68 0.68 P-7 J-7 J-8 10.68 0.30 0.02 0.35 0.72 0.68 P-8 J-8 I-Pump-1 10.68 0.11 0.02 0.35 0.79 0.68 P-9 O-Pump-1 J-10 10.68 0.13 0.02 0.35 0.77 0.68 P-10 T-2 J-11 -10.01 0.03 0.06 0.64 9.49 3.15 P-11 T-2 J-12 10.01 1.58 0.06 0.64 3.28 3.15 P-12 J-12 J-13 10.01 0.95 0.06 0.64 3.36 3.15 P-13 J-13 J-14 10.01 1.26 0.06 0.64 3.31 3.15 P-14 J-14 J-15 10.01 1.89 0.06 0.64 3.26 3.15 P-15 J-15 J-16 10.01 3.15 0.06 0.64 3.22 3.15 P-16 J-16 J-17 10.01 3.15 0.06 0.64 3.22 3.15 P-17 J-18 J-10 -0.14 0.00 0.00 0.02 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 0.53 0.09 0.00 0.06 0.05 0.05 P-20 J-20 J-21 0.00 0.00 0.00 0.00 0.00 0.00 P-21 J-21 J-1 0.00 0.00 0.00 0.00 0.00 0.00 P-22 J-20 J-23 0.53 0.04 0.00 0.07 0.09 0.09 P-23 J-23 J-24 0.25 0.02 0.00 0.05 0.06 0.05 P-24 J-24 J-25 0.25 0.02 0.00 0.05 0.06 0.05 P-25 J-25 J-26 -0.23 0.01 0.00 0.05 0.05 0.05 P-26 J-26 J-23 -0.28 0.03 0.00 0.06 0.07 0.07 P-27 J-25 J-28 0.24 0.05 0.00 0.05 0.05 0.05 P-28 J-26 J-27 0.05 0.07 0.00 0.03 0.05 0.05



P-29 J-17 T-1 0.01 0.00 0.00 0.00 0.00 0.00 P-30 O-Pump-3 J-2a 10.68 0.00 0.01 0.28 1.61 0.40 P-31 T-1 J-9 0.01 0.00 0.00 0.00 0.00 0.00 P-32 J-10 J-11 10.01 1.89 0.06 0.64 3.26 3.15 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 10.68 82.64 154.14 71.5 75.00 7. 0.0 103.5 ** ** 92.8 58.9474 Pump-3 10.68 2.98 74.39 71.4 75.00 7. 0.0 109.5 ** ** 13.1 58.9474 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 0.00(0.00) 158.90 5.00 153.90 1509.29 J-3 0.00 92.29 J-4 0.00 92.07 -10.00 102.07 1000.97 J-5 0.00 91.10 -26.00 117.10 1148.41 J-6 0.00 90.41 -25.00 115.41 1131.78 J-7 0.00 88.09 -15.00 103.09 1010.96 J-8 0.00 87.77 J-9 0.01(0.00) 144.59 J-10 0.00 159.00 10.00 149.00 1461.15 J-11 0.00 157.04 45.00 112.04 1098.75 J-12 Northern Far 0.00 155.31 22.00 133.31 1307.29 J-13 0.00 154.30 14.00 140.30 1375.85 J-14 0.00(0.00) 152.97 8.00 144.97 1421.70 J-15 0.00 151.02 15.00 136.02 1333.89 J-16 0.00 147.80 10.00 137.80 1351.39 J-17 Arm End Rese 10.00( ** ) 144.59 6.00 138.59 1359.08 J-18 0.14(0.48) 158.99 J-20 Southern Far 0.00 158.90 20.00 138.90 1362.19 J-21 South Arm Ro 0.00 158.90 10.00 148.90 1460.26 J-23 Calverton Ov 0.00(0.00) 158.86 12.00 146.86 1440.22 J-24 South Arm Fi 0.00(0.00) 158.84 18.00 140.84 1381.21 J-25 Blessington 0.24(0.48) 158.82 15.00 143.82 1410.41 J-26 Fort Directi 0.00 158.83 J-27 Fort Directi 0.05(0.48) 158.76 40.00 118.76 1164.66 J-28 Shoecraft Ba 0.24(0.48) 158.77 25.00 133.77 1311.83 J-2a 0.00 92.37 20.00 72.37 709.73 O-Pump-1 Half Moon Ba 0.00 159.14 5.00 154.14 1511.63 O-Pump-3 Blackmans Ba 0.00 92.39 18.00 74.39 729.50 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 144.59 6.00 138.59 1359.08 T-2 Breather Pip ---- 156.95 42.00 114.95 1127.24 T-19 ---- 158.99 22.00 136.99 1343.46 I-Pump-1 Half Moon Ba 0.00 87.64 5.00 82.64 810.42 I-Pump-3 Blackmans Ba 0.00 20.98 18.00 2.98 29.18 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa



--------------------- --------------------- O-Pump-1 1511.63 R-1 19.61 J-1 1509.29 I-Pump-3 29.18 J-10 1461.15 J-2a 709.73 J-21 1460.26 O-Pump-3 729.50 J-23 1440.22 I-Pump-1 810.42 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-10 0.64 P-20 0.00 P-11 0.64 P-21 0.00 P-12 0.64 P-31 0.00 P-13 0.64 P-29 0.00 P-32 0.64 P-17 0.02 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 9.49 P-20 0.00 P-12 3.36 P-21 0.00 P-13 3.31 P-31 0.00 P-11 3.28 P-29 0.00 P-32 3.26 P-17 0.00 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-10 3.15 P-20 0.00 P-11 3.15 P-21 0.00 P-12 3.15 P-31 0.00 P-32 3.15 P-29 0.00 P-13 3.15 P-17 0.00 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 58.9474 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 59.000



C H A N G E S F O R N E X T S I M U L A T I O N (time = 59.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 59.000 TIME FROM INITIATION OF EPS = 59.0000 HOURS (3500 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 59.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 60.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 60.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 60.000 TIME FROM INITIATION OF EPS = 60.0000 HOURS (3600 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES



NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 60.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 61.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 61.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 61.000 TIME FROM INITIATION OF EPS = 61.0000 HOURS (3700 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 61.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================



Time: 62.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 62.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 62.000 TIME FROM INITIATION OF EPS = 62.0000 HOURS (3800 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 62.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 63.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 63.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 63.000 TIME FROM INITIATION OF EPS = 63.0000 HOURS (3900 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES



NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 63.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 64.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 64.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 64.000 TIME FROM INITIATION OF EPS = 64.0000 HOURS (4000 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 64.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA



================================================================================ Time: 65.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 65.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 65.000 TIME FROM INITIATION OF EPS = 65.0000 HOURS (4100 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 65.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 66.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 66.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 66.000 TIME FROM INITIATION OF EPS = 66.0000 HOURS (4200 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES



(-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 66.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 67.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 67.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 67.000 TIME FROM INITIATION OF EPS = 67.0000 HOURS (4300 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 67.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA



================================================================================ Time: 68.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 68.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 68.000 TIME FROM INITIATION OF EPS = 68.0000 HOURS (4400 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 68.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 69.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 69.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 69.000 TIME FROM INITIATION OF EPS = 69.0000 HOURS (4500 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S



(+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 69.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 70.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 70.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 70.000 TIME FROM INITIATION OF EPS = 70.0000 HOURS (4600 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 70.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA



================================================================================ Time: 71.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 71.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 71.000 TIME FROM INITIATION OF EPS = 71.0000 HOURS (4700 HOURS, DAY: 2) RESULTS OBTAINED AFTER 3 TRIALS: ACCURACY = 0.32867E-09 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 10.68 NET SYSTEM INFLOW = 10.68 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 10.68 T A N K S T A T U S R E P O R T (time = 71.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) 0.00 13.00 6.00 1884960. 100.0 FULL 6.00 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Time: 72.000 C H A N G E S F O R N E X T S I M U L A T I O N (time = 72.0000 hours) UNIT COST OF POWER FOR THIS SIMULATION PERIOD = 0.099 $/kW-Hr JUNCTION DEMANDS CHANGED - PLEASE SEE RESULTS TABLE Time: 72.000 TIME FROM INITIATION OF EPS = 72.0000 HOURS (4800 HOURS, DAY: 2) RESULTS OBTAINED AFTER 5 TRIALS: ACCURACY = 0.22734E-04 P I P E L I N E R E S U L T S



STATUS CODE: XX -CLOSED PIPE CV -CHECK VALVE P I P E NODE NUMBERS FLOWRATE HEAD MINOR LINE HL+ML/ HL/ N A M E #1 #2 LOSS LOSS VELO. 1000 1000 lps m m m/s m/m m/m ----------------------------------------------------------------------------------------- P-1 R-1 I-Pump-3 34.57 0.04 0.21 0.91 24.63 3.55 P-2 J-2a J-3 34.57 0.54 0.19 1.12 8.11 5.96 P-3 J-3 J-4 34.57 1.79 0.19 1.12 6.61 5.96 P-4 J-4 J-5 34.57 8.35 0.19 1.12 6.10 5.96 P-5 J-5 J-6 34.57 5.96 0.19 1.12 6.15 5.96 P-6 J-6 J-7 34.57 20.27 0.19 1.12 6.02 5.96 P-7 J-7 J-8 34.57 2.68 0.19 1.12 6.39 5.96 P-8 J-8 I-Pump-1 34.57 0.95 0.19 1.12 7.17 5.96 P-9 O-Pump-1 J-10 34.57 1.13 0.19 1.12 6.98 5.96 P-10 T-2 J-11 -25.89 0.18 0.42 1.67 60.76 18.34 P-11 T-2 J-12 25.89 9.17 0.42 1.67 19.19 18.34 P-12 J-12 J-13 25.89 5.50 0.42 1.67 19.75 18.34 P-13 J-13 J-14 25.89 7.34 0.42 1.67 19.40 18.34 P-14 J-14 J-15 23.89 9.48 0.36 1.54 16.41 15.80 P-15 J-15 J-16 23.89 15.80 0.36 1.54 16.16 15.80 P-16 J-16 J-17 23.89 15.80 0.36 1.54 16.16 15.80 P-17 J-18 J-10 -0.14 0.00 0.00 0.02 0.00 0.00 P-18 J-18 T-19 0.00 0.00 0.00 0.00 0.00 0.00 P-19 J-10 J-20 8.53 15.62 0.12 0.90 7.87 7.81 P-20 J-20 J-21 5.00 4.36 0.04 0.53 2.93 2.91 P-21 J-21 J-1 5.00 0.58 0.04 0.53 3.12 2.91 P-22 J-20 J-23 3.53 1.43 0.04 0.48 2.94 2.87 P-23 J-23 J-24 0.90 0.18 0.01 0.18 0.62 0.61 P-24 J-24 J-25 -0.10 0.00 0.00 0.02 0.01 0.01 P-25 J-25 J-26 -0.58 0.05 0.00 0.12 0.28 0.27 P-26 J-26 J-23 -0.63 0.12 0.00 0.13 0.32 0.31 P-27 J-25 J-28 0.24 0.05 0.00 0.05 0.05 0.05 P-28 J-26 J-27 0.05 0.07 0.00 0.03 0.05 0.05 P-29 J-17 T-1 23.89 0.13 0.15 0.98 11.27 5.34 P-30 O-Pump-3 J-2a 34.57 0.04 0.13 0.91 16.20 3.55 P-31 T-1 J-9 56.00 0.25 0.21 1.18 9.23 5.01 P-32 J-10 J-11 25.89 11.00 0.42 1.67 19.05 18.34 P U M P/L O S S E L E M E N T R E S U L T S INLET OUTLET PUMP EFFIC- USEFUL INCREMTL TOTAL #PUMPS #PUMPS NPSH Time NAME FLOWRATE HEAD HEAD HEAD ENCY POWER COST COST PARALLEL SERIES Avail. hrs lps m m m % kW $ $ m -------------------------------------------------------------------------------------------------------------- Pump-1 34.57 34.07 87.10 53.0 75.00 18. 1.0 116.4 ** ** 44.1 72.0000 Pump-3 34.57 2.75 63.12 60.4 75.00 20. 1.0 122.4 ** ** 12.8 72.0000 N O D E R E S U L T S NODE NODE EXTERNAL HYDRAULIC NODE PRESSURE NODE NAME TITLE DEMAND GRADE ELEVATION HEAD PRESSURE lps m m m kPa ------------------------------------------------------------------------------ J-1 Iron Pot Dam 5.00( ** ) 70.00 5.00 65.00 637.47 J-3 0.00 80.23 J-4 0.00 78.25 -10.00 88.25 865.39 J-5 0.00 69.71 -26.00 95.71 938.56 J-6 0.00 63.55 -25.00 88.55 868.40 J-7 0.00 43.09 -15.00 58.09 569.69 J-8 0.00 40.22 J-9 56.00( ** ) 12.54 J-10 0.00 90.77 10.00 80.77 792.08 J-11 0.00 79.34 45.00 34.34 336.78



J-12 Northern Far 0.00 69.14 22.00 47.14 462.29 J-13 0.00 63.21 14.00 49.21 482.62 J-14 2.00( ** ) 55.45 8.00 47.45 465.36 J-15 0.00 45.61 15.00 30.61 300.19 J-16 0.00 29.45 10.00 19.45 190.70 J-17 Arm End Rese 0.00(0.00) 13.28 6.00 7.28 71.41 J-18 0.14(0.48) 90.77 J-20 Southern Far 0.00 75.03 20.00 55.03 539.64 J-21 South Arm Ro 0.00 70.63 10.00 60.63 594.55 J-23 Calverton Ov 2.00( ** ) 73.56 12.00 61.56 603.67 J-24 South Arm Fi 1.00( ** ) 73.37 18.00 55.37 543.00 J-25 Blessington 0.24(0.48) 73.37 15.00 58.37 572.46 J-26 Fort Directi 0.00 73.43 J-27 Fort Directi 0.05(0.48) 73.36 40.00 33.36 327.16 J-28 Shoecraft Ba 0.24(0.48) 73.32 25.00 48.32 473.88 J-2a 0.00 80.96 20.00 60.96 597.78 O-Pump-1 Half Moon Ba 0.00 92.10 5.00 87.10 854.12 O-Pump-3 Blackmans Ba 0.00 81.12 18.00 63.12 618.98 R-1 ---- 21.00 19.00 2.00 19.61 T-1 ---- 13.00 6.00 7.00 68.65 T-2 Breather Pip ---- 78.73 42.00 36.73 360.24 T-19 ---- 90.77 22.00 68.77 674.39 I-Pump-1 Half Moon Ba 0.00 39.07 5.00 34.07 334.10 I-Pump-3 Blackmans Ba 0.00 20.75 18.00 2.75 27.00 M A X I M U M A N D M I N I M U M V A L U E S P R E S S U R E S JUNCTION MAXIMUM JUNCTION MINIMUM NUMBER PRESSURES NUMBER PRESSURES kPa kPa --------------------- --------------------- J-5 938.56 R-1 19.61 J-6 868.40 I-Pump-3 27.00 J-4 865.39 T-1 68.65 O-Pump-1 854.12 J-17 71.41 J-10 792.08 J-16 190.70 V E L O C I T I E S PIPE MAXIMUM PIPE MINIMUM NUMBER VELOCITY NUMBER VELOCITY (m/s) (m/s) --------------------- --------------------- P-11 1.67 P-17 0.02 P-12 1.67 P-24 0.02 P-13 1.67 P-28 0.03 P-10 1.67 P-27 0.05 P-32 1.67 P-25 0.12 H L + M L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL+ML/1000 NUMBER HL+ML/1000 (m/m) (m/m) --------------------- --------------------- P-10 60.76 P-17 0.00 P-1 24.63 P-24 0.01 P-12 19.75 P-28 0.05 P-13 19.40 P-27 0.05 P-11 19.19 P-25 0.28 H L / 1 0 0 0 PIPE MAXIMUM PIPE MINIMUM NUMBER HL/1000 NUMBER HL/1000 (m/m) (m/m) --------------------- --------------------- P-11 18.34 P-17 0.00 P-12 18.34 P-24 0.01 P-13 18.34 P-28 0.05 P-10 18.34 P-27 0.05



P-32 18.34 P-25 0.27 S U M M A R Y O F I N F L O W S A N D O U T F L O W S (+) INFLOWS INTO THE SYSTEM FROM SUPPLY NODES (-) OUTFLOWS FROM THE SYSTEM INTO SUPPLY NODES NODE FLOWRATE NODE NAME lps TITLE -------------------------------------------- R-1 34.57 T-1 32.11 NET SYSTEM INFLOW = 66.67 NET SYSTEM OUTFLOW = 0.00 NET SYSTEM DEMAND = 66.67 T A N K S T A T U S R E P O R T (time = 72.0000 hours) TANK NET WATER TANK TANK TANK TANK PROJECTED NAME FLOW ELEVATION DEPTH VOLUME VOLUME STATUS DEPTH (*) lps m m lts % m ------------------------------------------------------------------------------- T-1(1) -32.11 13.00 6.00 1884960. 100.0 DRAINING 5.63 T-2(1) 0.00 44.00 2.00 14137. 100.0 FULL 2.00 T-19(1) 0.00 25.00 3.00 21206. 100.0 FULL 3.00 * TANK TYPE: (1) - CONSTANT DIAMETER (2) - VARIABLE AREA ================================================================================ Total Power Cost *************************************************** TOTAL POWER COST($) FOR THIS SIMULATION = 238.80 *************************************************** ================================================================================ Max/Min Summary ******************************************* Summary of Max/Min Node Values ******************************************* Node MnPres MnHead MnHGL MnTime MxPres MxHead MxHGL MxTime Elevation -------------------------------------------------------------------------------- J-1 191.18 19.49 24.49 0.14 1509.29 153.90 158.90 23.00 5.00 J-3 677.86 69.12 69.12 0.14 905.08 92.29 92.29 23.00 0.00 J-4 746.54 76.13 66.13 0.14 1000.97 102.07 92.07 23.00 -10.00 J-5 777.15 79.25 53.25 0.14 1148.41 117.10 91.10 23.00 -26.00 J-6 676.29 68.96 43.96 0.14 1131.78 115.41 90.41 23.00 -25.00 J-7 275.72 28.12 13.12 0.14 1010.96 103.09 88.09 23.00 -15.00 J-8 86.02 8.77 8.77 0.14 860.69 87.77 87.77 23.00 0.00 J-9 111.96 11.42 11.42 3.00 1417.92 144.59 144.59 23.00 0.00 J-10 340.30 34.70 44.70 0.14 1461.15 149.00 159.00 23.00 10.00 J-11 -16.84 -1.72 43.28 0.14 1098.75 112.04 157.04 23.00 45.00 J-12 162.57 16.58 38.58 0.14 1307.29 133.31 155.31 23.00 22.00 J-13 212.98 21.72 35.72 0.14 1375.85 140.30 154.30 23.00 14.00 J-14 235.06 23.97 31.97 0.14 1421.70 144.97 152.97 23.00 8.00 J-15 123.15 12.56 27.56 0.14 1333.89 136.02 151.02 23.00 15.00 J-16 101.08 10.31 20.31 0.14 1351.39 137.80 147.80 23.00 10.00 J-17 55.78 5.69 11.69 4.00 1359.08 138.59 144.59 23.00 6.00 J-18 255.63 26.07 26.07 0.00 1559.21 158.99 158.99 23.00 0.00 J-20 93.34 9.52 29.52 0.14 1362.19 138.90 158.90 23.00 20.00 J-21 148.26 15.12 25.12 0.14 1460.26 148.90 158.90 23.00 10.00 J-23 158.61 16.17 28.17 0.14 1440.22 146.86 158.86 23.00 12.00



J-24 98.24 10.02 28.02 0.14 1381.21 140.84 158.84 23.00 18.00 J-25 127.79 13.03 28.03 0.14 1410.41 143.82 158.82 23.00 15.00 J-26 275.33 28.08 28.08 0.14 1557.62 158.83 158.83 23.00 0.00 J-27 -117.28 -11.96 28.04 0.14 1164.66 118.76 158.76 23.00 40.00 J-28 29.46 3.00 28.00 0.14 1311.83 133.77 158.77 23.00 25.00 J-2a 492.62 50.23 70.23 0.14 709.73 72.37 92.37 23.00 20.00 O-Pump-1 409.02 41.71 46.71 0.14 1511.63 154.14 159.14 23.00 5.00 O-Pump-3 514.69 52.48 70.48 0.14 729.50 74.39 92.39 23.00 18.00 R-1 19.61 2.00 21.00 0.00 19.61 2.00 21.00 0.00 19.00 T-1 54.07 5.51 11.51 4.00 1359.08 138.59 144.59 23.00 6.00 T-2 11.91 1.21 43.21 0.14 1127.24 114.95 156.95 23.00 42.00 T-19 9.81 1.00 23.00 0.00 1343.46 136.99 158.99 23.00 22.00 I-Pump-1 19.93 2.03 7.03 0.14 810.42 82.64 87.64 23.00 5.00 I-Pump-3 25.68 2.62 20.62 0.14 29.18 2.98 20.98 23.00 18.00 ***** HYDRAULIC ANALYSIS COMPLETED *****

APPENDIX B: LAYOUT PLAN FOR SOUTH ARM PENINSULA RECYCLED WATER PIPELINE with ENGINEERING MODEL POINTS

APPENDIX B: LAYOUT PLAN FOR SOUTH ARM PENINSULA RECYCLED WATER PIPELINE - DA APPLICATION PLAN.

APPENDIX C: NETWORK MODEL SCHEMATIC FOR SOUTH ARM PENINSULA RECYCLED WATER PIPELINE

R-1: BBTP OFFTAKE

PUMP-3: BBTP BPS

PUMP-1: BBTP BPS

J-11 T-19: PROTEA FARM TANK

T-1: ARM END STORAGE TANKS

J-1: IRON POT DAM

J-23

J-15

J-20 J-8

J-5

J-21

J-3

J-17

J-28

J-10

J-25

RIVER DERWENT

SOUTH ARM PENINSULA-CCC

BLACKMAN’S BAY-KCC

N

south arm peninsula irrigation water pipeline - network ... · this report outlines the development...

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