©Black & Veatch Holding Company 2017. All rights reserved.

FINAL

MASTER PLAN REPORT

Potable Water Master Plan

B&V PROJECT NO. 190020

PREPARED FOR

City of Tampa

1 OCTOBER 2018

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Signature and printed name of Amanda Schwerman, Professional Engineer, with license number 70751, State of Florida, dated 10/1/18.
Professional Engineer: Si Amanda Schwerman Printed Name 70751 License No. Datt, /

Professional Engineer: Si Amanda Schwerman Printed Name 70751 License No. Datt, /

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Table of Contents

LIST OF TABLES

List of Tables

LIST OF FIGURES

LIST OF APPENDICES

List of appendices and their corresponding technical memorandums and reports.
Appendix Title
Appendix A Population and Demand Projection Technical Memorandum
Appendix B Distribution System Improvements Technical Memorandum
Appendix C‐a Model Update and Calibration Technical Memorandum
Appendix C‐b Hydraulic Model Recalibration Technical Memorandum
Appendix D Distribution System Assessment Technical Memorandum
Appendix E TPA and TIA Master Meter Technical Memorandum
Appendix F ISO 55001 Assessment Report
Appendix G Asset Management Implementation Plan Technical Memorandum
Appendix H Risked Based Prioritization Technical Memorandum
Appendix I Water Main Data Quality Review and Survival Curve Development Technical Memorandum

LIST OF ABBREVIATIONS

List of abbreviations and their full definitions used in the document.
Abbreviation Definition
ADD Average Day Demand
AFB Air Force Base
AMD Average Month Demand
ASR Aquifer Storage and Recharge
AWWA American Water Works Association
BEBR Bureau of Economic and Business Research
CIP Capital Improvement Plan
COF Consequence of Failure
DLTWTF David L. Tippin Water Treatment Facility
EPS Extended Period Simulations
EST Elevated Storage Tanks
FDEP Florida Department of Environmental Protection
FF Fire Flow
GIS Geographic Information System
gpm Gallons per Minute
GST Ground Storage Tanks
HGL Hydraulic Grade Line
HL Head loss
HSPS High Service Pump Station
I‐75 Interstate 75
ISO International Organization for Standardization
LOF Likelihood of Failure
MDD Maximum Day Demand
MG Million Gallons
MGD Million Gallons per Day
mi Mile
MMD Maximum Month Demand
PF Peaking Factor
PHD Peak Hour Demand
R&R Rehabilitation and Replacement
RPS Repump Stations
SCADA Supervisory Controls and Data Acquisition
SOPs Standard Operating Procedures
SWFWMD Southwest Florida Water Management District
TBW Tampa Bay Water
THIC Tampa‐Hillsborough Interconnect
TM Technical Memorandum
TWD or Department Tampa Water Department’s
USF University of South Florida
VFD Variable Frequency Drives
VSP Variable Speed Pumps
WTF Water Treatment Facility

1.0 Introduction

1.1 PURPOSE

This report summarizes the methodology, findings and recommendations of the 2018 Potable Water Master Plan Update (Master Plan) for the City of Tampa (City). Black & Veatch worked closely with the Tampa Water Department (TWD) Staff to develop this Master Plan Update, which involved a comprehensive assessment of the TWD potable water distribution system and facilities, as well as targeted reviews of the strategies and procedures used to operate the distribution system. The results of the assessments were used to define a plan for capital improvements that are needed to allow the TWD to meet future conditions and continue providing a safe and reliable drinking water supply for its customers.

The primary purposes of the Master Plan are to:

2.0 Existing System Summary

2.1 SYSTEM OVERVIEW

The City of Tampa is a thriving community, with a service population of approximately 600,000 people. The Tampa Water Department (TWD) maintains and operates a potable water distribution system that includes over 2,200 miles of water mains in three pressure zones, five repump stations, 50,000 valves, 14,000 hydrants, and one water treatment facility. The TWD service area encompasses approximately 219 square miles, all within Hillsborough County, and includes the City of Tampa and some surrounding areas of unincorporated Hillsborough County. The boundaries of the TWD service area can be seen in Figure 2‐1.

The primary source of potable water supply for the distribution system is the Hillsborough River Reservoir, which is located at the David L. Tippin Water Treatment Facility (DLTWTF). The TWD also operates an aquifer storage and recharge (ASR) program which pumps water into the groundwater aquifer during wet periods and can withdraw the supply back out during dry periods. In addition, TWD has water supply interconnects with the regional wholesale water supply authority, Tampa Bay Water, at the Morris Bridge Repump Station (RPS) and US 301 Interconnect.

The DLTWTF is TWD’s only treatment facility and provides up to 120 MGD of treatment capacity. The DLTWTF has a system of clearwells for finished water storage with an effective capacity of 12.5 million gallons (MG). Following treatment, the DLTWTF’s high service pump station (HSPS) delivers water to the distribution system via eight pumps on two power services.

During the Master Planning process, the TWD modified the operating strategy of the distribution system by creating three separate pressure zones: the DLTWTF, South Tampa, and North Tampa pressure zones. The boundaries for these three pressure zones are currently established by closing system valves. The pressure zones are delineated and supplied as follows:

The locations of the DLTWTF, the system RPSs, transmission and distribution system piping, and pressure zone boundaries can be seen in Figure 2‐1. A flow diagram schematically depicting facility locations and flow directions can be seen in Figure 2‐2.

Map of Tampa's potable water master plan, showing existing water distribution networks and pressure zones with varying diameters.
Morris Bridge RPS & TBW Interconnect North Blvd Interconnect (THIC) Northwest RPS DLTWTF West Tampa RPS US301 Interconnect Palma Ceia RPS / 1 inch = 14,000 feet Interbay RPS 0 7,000 14,000 Feet MacDill AFB Q WTP Pressure_Zones CITY OF TAMPA 3 South Tampa Potable Water Master Plan Ú Pump_Stations New Tampa [ Diameter T Ground Storage Tank Figure 2-1 U Less than 12-inch 12 - 16-inch Elevated Storage Tank Existing System 16 - 24-inch Service Area Greater than 24-inch [Ú UUTT [Ú UT 3Q [Ú [Ú [Ú UT Sources: Esri, Garmin, USGS, NPS
Flow diagram illustrating the existing system, including connections between tanks, pressure zones, and key components like interconnects and valves.
Figure 2-2: Existing System Flow Diagram Northwest RPS North Boulevard Interconnect (THIC) Aquifer Storage & Recovery (ASR) North Tampa Pressure Zone North Tampa Distribution System Morris Bridge RPS TBW Supplemental Supply High Service PS #5&6 # 1,2,3& 4 3011nterconnect DLTWTF West Tampa Tank South Tampa Pressure Zone Interbay RPS Legend Distribution/ Consumption Piping Pump Station Piping Pressure Reducing Valve Check Valve Isolation Valve

2.2 SYSTEM DESCRIPTION

This section provides information regarding the existing system infrastructure and operations that were used to develop the updated hydraulic model of the City of Tampa potable water distribution system. This section also presents the capacities and capabilities of the components that make up the potable water distribution system, including storage, pump stations, distribution piping, and system controls. The system described was used in the modeling and calibration process explained later in this report.

2.2.1 Distribution Piping

The existing distribution system has over 2,130 miles of pipelines ranging from 2‐inches to 54‐inches in diameter. The distribution system is well looped and gridded, which helps to maintain low velocities and headlosses throughout the system. However, the DLTWTF pressure zone also contains a significant quantity of 2‐inch diameter piping, which can experience high headlosses during peak demand periods and restrict available fire flow in these areas.

A summary of the distribution system pipelines by diameter, according to the October 2015 GIS files provided by TWD, is presented in Table 2‐1.

Table 2‐1: Existing Pipeline Summary by Diameter

Summary of existing distribution system pipeline lengths by diameter in inches, showing total miles of pipe for each size range.
Pipeline diameter (inches) Total length (miles) Pipeline diameter (inches) Total length (miles)
2&3 384 18 0.5
4 74 20 33
6 664 24 75
8 578 30 25
10 10 36 35
12 318 42 14
14 1 48 5
16 102 54 0.4
Total 2,327

Pipelines below 2‐inches omitted. 2‐inch and 3‐inch combined

2.2.2 Storage

After treatment at the DLTWTF, finished water is initially stored on site in five separate clearwell structures connected by piping with a total of 20 million gallons (MG) of storage capacity and an effective volume of 12.5 MG due to limitation on drawdown to limit pump cavitation and buoyancy of the tanks.

Within the distribution system there are six storage tanks: one each at Interbay, Palma Ceia, West Tampa and Northwest RPSs and two at Morris Bridge RPS. The Interbay, Northwest and Morris Bridge RPSs contain above grade ground storage tanks (GST), while the other two stations contain

elevated storage tanks (EST). However, the system normally operates at a hydraulic grade line (HGL) above the top elevation of the two ESTs. Due to this condition, these elevated tanks function more like ground storage tanks, and pumps have been installed to pump water from the tanks back into the distribution, similar to the RPSs. GST and EST data, including tank bottom elevation and tank total and effective volumes are presented in Table 2‐2.

Table 2‐2: Existing Tank Capacities

Existing tank locations with corresponding total and effective storage volumes and explanatory notes.
LOCATION TANK TOTAL VOLUME TANK EFFECTIVE VOLUME NOTES
DLTWTF Clearwell 20.0 12.5 Effective volume per TWD due to pump suction cavitation and tank buoyancy
Interbay GST 5.0 5.0 Tank effluent pipe located at the bottom of tank allowing for full usage of storage
Morris Bridge GST 10.0 7.5 Tank effluent pipe located four feet above the bottom of the tank
Northwest GST 3.0 3.0 Tank effluent pipe located at the bottom of tank allowing for full usage of storage
Palma Ceia EST 1.5 1.5 Tank effluent pipe located at the bottom of tank allowing for full usage of storage
West Tampa EST 1.5 1.5 Tank effluent pipe located at the bottom of tank allowing for full usage of storage

2.2.3 Pumping

Finished water is pumped from the clearwells by the high service pump station (HSPS) located at the DLTWTF. The target discharge pressure from the HSPS is currently 65 psi, which is set to maintain a minimum distribution system pressure of 40 psi. The distribution system contains three RPSs in the DLTWTF pressure zone. The RPSs are located relatively remote to the DLTWTF and provide the system with the ability to boost pressures during peak periods. Pumping capacity from the HSPS combined with the capacities from the Northwest, West Tampa, and Palma Ceia RPSs yield a pressure zone firm capacity of 160 MGD within the DLTWTF pressure zone.

The North Tampa pressure zone is supplied by the Morris Bridge RPS, which has a total of six pumps in two sets; Pumps 1‐4 and Pumps 5&6. The firm pumping capacity of the Morris Bridge RPS is 66 MGD based on the modeled capacity of pumps #1‐4 alone because the two sets of pumps cannot discharge to the same location simultaneously. However, the Morris Bridge RPS pumps are setup to allow multiple pumping configurations, including allowing pumps #5 and 6 to serve the North Tampa Zone while allowing Pumps 1‐4 to discharge into the DLTWTF zone when purchasing water from Tampa Bay Water.

The South Tampa pressure zone is fed by the Interbay RPS, which also has a total of six pumps; two jockey pumps and four standard pumps. The firm pumping capacity of the Interbay RPS is 15 MGD, which is supplied by pumps #1‐4 alone, because the two pump groups cannot be run concurrently.

The pumping capacity and characteristics of each pump and each RPS in the distribution system are summarized in Table 2‐3.

Table 2‐3: Existing Pump Capacities

Existing pump station capacities, including individual pump characteristics, motor power capability, and total pump station maximum, rated, and firm capacities.
Pump Station (Pump Type/ Install Year) # Maximum Capacity (gpm) Maximum Capacity (MGD) Rated Capacity (gpm) Rated Capacity (MGD) Rated TDH (ft) Motor (Type) Typical & Standby Power Capability Total Pump Station Capacity Max (MGD) Total Pump Station Capacity Rated (MGD) Total Pump Station Capacity Rated (MGD) Total Pump Station Capacity Modeled
Pump Station (Pump Type/ Install Year) # (gpm) (MGD) (gpm) (MGD) (ft) (Type) Typical & Standby Power Capability (MGD) (MGD) Rated Modeled
D.L. Tippin WTP‐ High Service Pump Station1 1 NA NA 13,900 20 NA Constant 2 Utility Feeds & Generators NA 164 134 134
D.L. Tippin WTP‐ High Service Pump Station1 2 NA NA 8,150 12 NA Constant 2 Utility Feeds & Generators NA 164 134 134
D.L. Tippin WTP‐ High Service Pump Station1 3 NA NA 7,850 11 NA Constant 2 Utility Feeds & Generators NA 164 134 134
D.L. Tippin WTP‐ High Service Pump Station1 4 NA NA 11,200 16 NA Constant 2 Utility Feeds & Generators NA 164 134 134
D.L. Tippin WTP‐ High Service Pump Station1 5 NA NA 15,800 23 NA VFD 2 Utility Feeds & Generators NA 164 134 134
D.L. Tippin WTP‐ High Service Pump Station1 6 NA NA 18,125 26 NA Constant 2 Utility Feeds & Generators NA 164 134 134
D.L. Tippin WTP‐ High Service Pump Station1 7 NA NA 18,350 26 NA VFD 2 Utility Feeds & Generators NA 164 134 134
D.L. Tippin WTP‐ High Service Pump Station1 8 NA NA 20,750 30 NA VFD 2 Utility Feeds & Generators NA 164 134 134
Morris Bridge Repump Station 1 14,000 20 11,100 16 152 VFD 2 Utility Feeds & Generators 101 78 62 66
Morris Bridge Repump Station 2 14,000 20 11,100 16 152 VFD 2 Utility Feeds & Generators 101 78 62 66
Morris Bridge Repump Station 3 14,000 20 11,100 16 152 VFD 2 Utility Feeds & Generators 101 78 62 66
Morris Bridge Repump Station 4 14,000 20 11,100 16 152 VFD 2 Utility Feeds & Generators 101 78 62 66
Morris Bridge Repump Station 5 4,161 6 2,200 3 150 VFD 2 Utility Feeds & Generators 101 78 62 66
Morris Bridge Repump Station 6 7,000 10 5,850 8 188 VFD 2 Utility Feeds & Generators 101 78 62 66
Morris Bridge Repump Station 7 4,200 6 1,500 2 79 VFD 2 Utility Feeds & Generators 101 78 62 66
Northwest Repump Station 1 2,600 4 2,100 3 150 Constant 1 Utility Feed & Generator 15 12 6 8
Northwest Repump Station 2 2,600 4 2,100 3 150 Constant 1 Utility Feed & Generator 15 12 6 8
Northwest Repump Station 3 5,000 7 4,000 6 150 Constant 1 Utility Feed & Generator 15 12 6 8
Interbay Repump Station 1 5,000 7 3,000 4 150 VFD 1 Utility Feed & Generator 30 16 12 15
Interbay Repump Station 2 5,000 7 3,000 4 150 VFD 1 Utility Feed & Generator 30 16 12 15
Interbay Repump Station 3 5,000 7 3,000 4 150 VFD 1 Utility Feed & Generator 30 16 12 15
Interbay Repump Station 4 5,000 7 3,000 4 150 VFD 1 Utility Feed & Generator 30 16 12 15
Interbay Repump Station 5 1,000 1 1,000 1 35 VFD 1 Utility Feed & Generator 30 16 12 15
Interbay Repump Station 6 1,000 1 1,000 1 35 VFD 1 Utility Feed & Generator 30 16 12 15
West Tampa Repump 1 7,000 10 5000 7.2 50 Constant 1 Utility Feed 10 7 0 0
Palma Ceia Repump 1 6,500 9 5000 7.2 45 Constant 1 Utility Feed 9 7 0 0
Footnote 1. Rated capacity of the DLTWTF pumps are unclear on the pump curves and are assumed values in this table.

2.2.4 Interconnections

The City of Tampa has two water supply interconnections and several wholesale water delivery interconnections. The two water supply interconnections are with Tampa Bay Water (TBW); 40 MGD at the Morris Bridge RPS and 30 MGD at the US 301 emergency interconnect. The two largest wholesale water delivery connections are at the Tampa‐Hillsborough Interconnect (THIC) also known as the North Boulevard Interconnect supplying water to Hillsborough County, and at the MacDill Airforce Base (AFB). The other wholesale connections are with developments within Hillsborough County and are metered with a residential master meter read monthly rather than a flow meter connected to SCADA. Figure 2‐3 illustrates the location of the Interconnections and wholesale customers.

2.2.5 Planned Improvements

The TWD already has significant distribution system improvements planned for completion prior to the 2020 planning year. These improvements are assumed to be existing in the model for planning year 2020 and future planning years. These planned improvements include:

Map of Tampa's potable water master plan, showing wholesale and interconnections, including various streets and water infrastructure elements.
^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ TBW US301 TBW MBRPS HC Pebble Creek 4200 S. 78th St. 2424 S. 70th St. 2606 S. 82nd St. 5103 E. Kirby St. 70th & Kingston Dr 5398 Old US Hwy 41A 9135 Florida Mining Blvd. TBW North Boulevard (THIC) Sources: Esri, Garmin, USGS, NPS / 1 inch = 14,000 feet 0 7,000 14,000 Feet 3Q WTP Diameter South Tampa Less than 12-inch New Tampa [Ú Pump_Stations 12 -16-inch Service Area 16 -24-inch UT Ground Storage Tank ^ Interconnections Greater than 24-inch Elevated Storage Tank CITY OF TAMPA Potable Water Master Plan Figure 2-3 Wholesale & Interconnections

3.0 Population and Demand Projections

3.1 POPULATION PROJECTIONS

Population projections are a critical component of master plans. Updating the hydraulic model included loading new demand projections as well as the updating the spatial allocation of the demands. Black & Veatch compared multiple population projection estimates to reach consensus with the TWD on what to use for the Master Plan. Sources included the Southwest Florida Water Management District (SWFWMD) which uses the University of Florida Bureau of Economic and Business Research (BEBR) data from 2014 and included population spatially distributed across the service area based on parcels; the Exhibit K document prepared by the Tampa Water Department using the high and low Florida Demographic Estimations; and the TBW 2014 Demand projections which use forecasting models that also incorporate factors such as weather and socioeconomic projections.

The SWFWMD estimates were considered to be the “low” population estimate with the Florida Demographic Estimations population projection in Exhibit K considered to be the “high” population estimate. A comparison of the two population projections for planning years analyzed in this Master Plan Update are presented in Table 3‐1. Additional information regarding population projections is presented in Appendix A, Population & Demand Projections Technical Memorandum.

Table 3‐1: Population Projection Summary

Summary of projected population for selected planning years under low and high population projection scenarios.
PLANNING YEAR “LOW” PROJECTIONS “HIGH” PROJECTIONS
2015 598,720 608,747
2020 611,383 651,733
2025 623,894 691,240
2035 633,422 761,822

3.2 DEMAND PROJECTIONS

The same data sources used for the population projections were used to determine the demand projections; SWFWMD, TWD Exhibit K high, TWD Exhibit K low, and TBW 2014 Projections. The different demand forecasts are shown in Figure 3‐1 and summarized in Table 3‐2. The comparison of the four demand projection methodologies and sources provide a window of likely scenarios. The average of the scenarios was selected for use in the Potable Water Master Plan. The solid black line shown in Figure 3‐1 displays the average of all the projections and was selected by TWD for the Master Plan Update. The use of the average demand projections increases the confidence that the analysis will yield applicable results and support conservative, but defendable capital improvement projects.

Figure 3‐1: Demand Projection Comparison

Graph comparing historic and projected total water use from 2015 to 2035, showing multiple demand projections with specific values.
Figure 3‐1: Demand Projection Comparison

Table 3‐2: Summary of Projected Demands

Table 3‐2 summarizes projected water demands, in MGD, by year for TWD Exhibit K high, TBW, SWFWMD, TWD Exhibit K – LOW, and the average of these projections.
YEAR TWD EXHIBIT K ‐HIGH TBW SWFWMD TWD EXHIBIT K – LOW AVERAGE
2015 75.3 68.1 74.7 71.2 72.31
2020 80.1 78.2 78.0 72.8 77.3
2025 84.7 84.1 81.0 74.3 81.0
2030 89.4 90.1 83.2 75.5 84.5
2035 94.4 97.2 83.9 76.5 88.0

1. Actual 2015 demand was 68.9 MGD. The actual demands will be used for the existing system analysis, while the remaining projected demands will be used for future analysis

3.3 NON‐REVENUE WATER

Distribution system demands are comprised of several different uses and are either consumed by customers, referred to as consumption demand and are metered for billing purposes, or are “lost” through water quality flushing, leaks, main breaks, and meter inaccuracies. These “losses” are referred to as non‐revenue water.

Non‐revenue water (NRW) demands are quantities of water lost from the system which are comprised of several categories including: water quality flushing, leakage, main breaks, and meter inaccuracies (apparent losses). NRW is monitored monthly by TWD by comparing total water production and total water consumption. A detailed review of water consumption and production records found that NRW had a five‐year average (2011‐2015) of 11% of total water demand. The NRW was broken down into each source as shown in Table 3‐3.

Table 3‐3: NRW Category Average % Breakdown

Average percentage breakdown of non-revenue water (NRW) by category.
NRW CATEGORY PERCENT OF NRW
Water Quality Flushing 8%
Meter Inaccuracies (apparent losses) 17%
Main Breaks & Leaking 75%
Total 100%

NRW was then allocated to each planning year based on the 11% assumption. The adopted planning years demands and non‐revenue water losses are shown in Table 3‐4. Additional details on the calculation and breakdowns of non‐revenue water are available in Appendix A, Population & Demand Projections Technical Memorandum.

Table 3‐4: NRW per Planning Year

Projected total demand, consumption, and non-revenue water (NRW) components by planning year.
YEAR TOTAL PROJECTED DEMAND (MGD) CONSUMPTION DEMAND (MGD) NON‐REVENUE WATER DEMAND (MGD) WQ FLUSHING (MGD) METER INACCURACIES (MGD) MAIN BREAKS / LEAKAGE (MGD)
2015 (Base)* 68.9 64.4 4.5 0.4 0.8 3.4
2020 77.3 68.8 8.5 0.7 1.4 6.4
2025 81.0 72.0 8.9 0.7 1.5 6.7
2035 88.0 78.3 9.7 0.8 1.6 7.3
*NOTE: 2015 (Base) demands are based on the actual demands recorded (consumptive and NRW).

3.4 DEMAND RATIOS

The average day demand (ADD) for each planning year was based on the projected demands and NRW as described above. However, water utilities, including TWD, typically plan for several additional demand conditions including: maximum day demand (MDD) and peak hour demand (PHD). In addition to being used to size new facilities, these conditions are also used to determine the condition of the system utilizing a number of different criteria. For example, FDEP requires pumping capacity to meet or exceed the MDD or PHD plus fire flow depending on the type of storage available.

Demand ratios, often referred to as peaking factors, are useful for increasing or decreasing average system demands to match different demand scenarios. This process is used in hydraulic modeling for modifying applied ADD system demands. A summary of demand ratios for the system as one pressure zone was calculated from a 5‐year horizon (2011‐2015) and is presented below in Table 3‐5. The PHD:MDD peaking factors were determined on a per pressure zone basis as a result of the diurnal pattern calculation described further in the section.

Table 3‐5: System‐wide Demand Ratio Summary

System‐wide demand ratio summary showing peaking factors by pressure zone for MDD:ADD, PHD:MDD, and PHD:ADD.
PRESSURE ZONE MDD:ADD PHD:MDD PHD:ADD
DLTWTF 1.56 1.42 2.22
North Tampa 1.56 1.63 2.54
South Tampa 1.56 1.37 2.14

3.4.1 Demand Update and Spatial Allocation

Customer billing records are the most current and accurate way to assign real base consumption demands to the hydraulic model. The spatial allocation of demands is almost as important as the demand calculations themselves. To accurately model demands and their impacts on the distribution system, it is important to accurately locate those demands. To determine the location or spatial allocation of the consumption demands, a combination of geocoded customer billing records provided by TWD and population projections by parcel provided by SWFWMD were used. Geocoded records were imported and applied directly to the nearest pipe and node in the model. Non‐revenue water demands, which accounted for eleven percent of total demands, were typically allocated equally across the distribution system. The exception to this occurs where NRW demands are well known, such as at flushing program locations, or where data indicates significant NRW demands have existed, such as in older parts of the system where main breaks are common. Future planning year demand allocations build on the base year consumption allocation, assuming existing use will remain and augmenting with future use based on increases in use derived from the population projections. The base year demand allocation is shown in Figure 3‐2, and the NRW allocation is shown in Figure 3‐3. Table 3‐6 summarizes the demands used for the system analysis and subsequent improvement identifications.

Table 3‐6: Demand Projections

Demand projections by pressure zone and planning year (2015, 2020, 2025, 2035) showing ADD, MDD, and PHD in MGD.
PRESSURE ZONE DEMAND BY PLANNING YEAR (MGD)
2015 2020 2025 2035
ADD MDD PHD ADD MDD PHD ADD MDD PHD ADD MDD PHD
North Tampa 4.8 7.4 10.5 6.1 9.5 13.5 7.0 10.8 15.4 8.3 13.0 18.5
South Tampa 4.6 7.2 11.7 5.1 7.9 12.9 5.2 8.1 13.2 5.4 8.4 13.6
DLTWTF 59.6 93.0 127.4 66.1 103.2 141.3 68.8 107.3 147.0 74.3 115.9 158.8
Total 69.0 107.6 ‐  77.3 120.6 ‐  80.9 126.2 ‐  88.0 137.3 ‐ 
Map of Tampa's 2015 potable water master plan showing consumption demand and distribution of water treatment plants.
Figure 3-2 Service Area Base Year (2015) Consumption Allocation. Consumption Demand = 65.2 MGD. Demand density categories range from Low Density to High Density. Map sources: Esri, USGS, NOAA, Esri, Garmin, USGS, NPS. Scale: 1 inch = 14,000 feet (0, 7,000, 14,000 Feet).
Map of Tampa showing potable water master plan with colored density areas for water treatment plants, main breaks, and leakage allocation.
[Ú UUTT [Ú UT 3Q [Ú [Ú [Ú UT Sources: Esri, USGS, NOAA, Sources: Esri, Garmin, USGS, NPS / 1 inch = 14,000 feet 0 7,000 14,000 Feet CITY OF TAMPA Diameter Service Area 3Q WTP Potable Water Master Plan 16 - 24-inch Leaking NRW Extents [ Greater than 24-inch Main Break Density Ú Pump Stations Figure 3-3High : Density Main Breaks ('10-'14) T Ground Storage Tank U NRW Mai & Leakage A n Break ocation llLow : Density Elevated Storage Tank

3.4.2 Diurnal Pattern Update

In order to conduct a 24‐hour extended period simulation (EPS) analysis, it was necessary to define diurnal demand patterns for each pressure zone that represent the existing system demand patterns as close as possible. This was accomplished through a mass balance calculation using the available SCADA data to relate pump station flows and changes in tank levels to determine system, facility, and pressure zone demands.

The selected MDD analysis pattern for each of the three pressure zones (DLTWTF, North Tampa, and South Tampa) are illustrated in Figure 3‐4 through Figure 3‐6. An additional diurnal pattern was developed to represent the time‐specific pattern of demands from MacDill Air Force Base (AFB), which draws water from the TWD system to fill its reservoirs and operate its water system. Figure 3‐7 illustrates the selected MacDill AFB demand pattern. The date selection process for demand data and the data processing and aggregation to compile and combine multiple days of data into a single pattern for each pressure zone is detailed in Appendix B, Distribution System Improvements Technical Memorandum.

Graph showing peak factor over time from 8/7 to 8/21/2017, including average and selected patterns.
Figure 3‐4: DLTWTF MDD Diurnal Pattern
Figure 3‐5: North Tampa MDD Diurnal Pattern
Line graph showing the Posting Factors over time from 8/7/2017 to 8/16/2017, with average and 95th percentile highlighted.
Figure 3‐6: South Tampa MDD Diurnal Pattern
Line graph showing positive factor over time, with multiple colored lines for each date and a highlighted average and 95th percentile.
Line graph showing a steep rise and plateau in values around 400 to 500, with the rest near zero.
Figure 3‐7: MacDill MDD Diurnal Pattern
Line graph showing multiple curves with dates on the right, depicting variations over time from March 1 to March 31, 2015.
Figure 3‐8: System‐wide ADD Diurnal Pattern

4.0 Hydraulic Model Update and Calibration

The TWD maintains a hydraulic model (model) of its potable water distribution system to conduct various analyses on the capabilities and capacities of the system. Black & Veatch updated the City’s hydraulic model with 2015 water demand information and prepared the model for extended period simulations (EPS). A 24‐hour EPS is the preferred calibration methodology and provides a clear indication of the ability of the hydraulic model to simulate system operating conditions under a number of settings. In addition, Black & Veatch completed a model calibration process to compare and validate the updated hydraulic model results with actual system operating data that was collected by the City.

Since the previous 2009 master plan and during this 2018 Master Plan update, the TWD has made a significant operational change, switching from operating their system as one large pressure zone, to three pressure zones. In the new operating configuration, pressure zone boundaries were established and the Interbay and Morris Bridge RPSs are used to supply water to the two new pressure zones. There are two hydraulic model calibration technical memorandums included in Appendix C that reflect the change in the system configuration. The results provided in this section of the report are for the most recent calibration effort reflecting the three pressure zone configuration.

4.1 MODEL UPDATE

In order for the TWD to more fully use the capabilities of its hydraulic model in analyzing its distribution system, the model needed to be updated to allow for EPS. To be accurate, EPS simulations require significantly more information, and the update of the TWD’s model for EPS required a number of changes including: collecting and applying system customer demand information, selecting system monitoring data and using that data to calculate changes in system demands at regular intervals to produce diurnal patterns, and collecting information regarding controls and operations of tank fill valves and the system’s pump stations. The model also required the addition of new and updated facilities.

4.2 CALIBRATION FIELD DATA

The TWD records and maintains Supervisory Controls and Data Acquisition (SCADA) data at each of the major system facilities, including the five RPSs and several permanent pressure loggers throughout the distribution system. The availability of this data allowed Black & Veatch to conduct an EPS model calibration of the distribution system following the update of the model. Data from 28 permanent SCADA pressure loggers and nine temporary hydrant pressure loggers was also available for the calibration effort. Table 4‐1 summarizes the available SCADA data.

To calibrate the model for EPS, a date had to be selected for the required 24 hours of data. September 5, 2017 was selected from the available data range (August 23‐September 7, 2017) due to its data consistency, small amount of SCADA data gaps, and high water demand. Diurnal demand patterns for the specific calibration data period were generated following the same process used to generate the diurnal patterns for the pressure zones. Calibration field data and diurnal demand pattern development and application are explained in further detail in Appendix C‐b Recalibration Technical Memorandum.

Table 4‐1: Available SCADA Data

Available SCADA data for each pump station, tank, or logger, indicating availability of pump status, pump speed, total flow, individual pump flow, discharge pressure, and tank level.
PUMP STATION, TANK OR LOGGER PUMP STATUS PUMP SPEED TOTAL FLOW INDIVIDUAL PUMP FLOW DISCHARGE PRESSURE TANK LEVEL
D.L. Tippin WTF Limited (missing data on 6, 7, & 8) Limited (missing data on 5, 7, & 8) Yes ‐  Yes N/A
Interbay RPS Limited (lots of “Bad” readings) Limited (lots of “Bad” readings, missing jockey pumps) Yes (had a few “Bad” reading which were assumed to be zero) ‐   Yes Yes
Morris Bridge RPS Yes (looks like there is an error with 3 & 4, assumed off) No Yes No Yes Yes
Northwest RPS No N/A Yes No Yes Yes
Palma Ceia RPS No N/A No No Yes Yes
West Tampa RPS Yes N/A No No Yes Yes
North Boulevard Connection Yes No Yes No Yes N/A
Aquifer Storage Recovery (ASR) Recharge Flow No N/A No Yes No N/A

4.3 CALIBRATION GOALS

The calibration of the system hydraulic model included a total of 10 facility points of calibration (flow & tank levels) and 35 points of calibration at the permanent and temporary pressure loggers conducted over 288 different time steps. To determine the accuracy of the calibration, Black & Veatch set a number of goals and limits that are consistent with best practices for calibrating hydraulic models for water distribution systems. The calibration goals are summarized in Table 4‐2. Refer to Appendix C‐a, Model Update and Calibration Technical Memorandum, for a description of recommended calibration goals.

Table 4‐2: Calibration Goals

Calibration goals for different calibration point types, including tank levels, flows, and pressures, with associated locations and acceptable error ranges.
CALIBRATION POINT TYPE LOCATION CALIBRATION GOAL
Tank Level Interbay, Morris Bridge, Northwest, Palma Ceia and West Tampa +/‐ 3 ft.
Flow DLTWTF, Interbay, Morris Bridge, Northwest, ASR Recharge +/‐ 10%
Pressures Various locations +/‐ 3 psi

4.4 CALIBRATION RESULTS AND CONCLUSIONS

The results of calibration show a well calibrated model with a very high correlation between the field SCADA data, the tank levels, and pumped flows. One hundred percent of the 2880 data points covering all the facility locations were within the calibration goals. Likewise, the calibration results of the pressure points also had a good correlation with closely matching daily patterns and 95% of the 12,427 data points were within the calibration goal. Time series plots for pump station, tank level, and pressure point calibration data are included in Attachment 1 of Appendix C‐b, Hydraulic Model Recalibration TM. Figure 4‐1 and Figure 4‐2 illustrate the accuracy of the calibration results.

The following steps might be helpful in increasing the percent of goal met: surveying the elevation of each SCADA points and installing AMR/AMI for better demand allocation.

Figure 4‐1: Pressure Logger % of Goal Results
Bar chart showing percentage of goal met for various locations in Tampa, with a threshold line at 75%.
Map of Tampa showing points related to water master plan recalibration results, with varying percentages indicating goal achievement.
CITY OF TAMPA Potable Water Master Plan Figure 4-2 Recalibration Results Summary. Map showing service area recalibration results, percent of points that met goal, and pipe diameter categories removed from calibration.

1 1 1 1 1 1 1 1 0 1 1 1 0.9 0.99 0.92 0.97 0.82 0.94 0.99 0.92 0.91 0.91 0.85 0.99 0.97 0.99 0.97 0.98 0.98 0.91 0.94 0.95 0.81 0.84 0.94 0.99 0.94 0.98 0.99 0.99 0.95 0.91 2869168 1678275 1679506 2814356 1678943 1679899 1673512 1683316 FS6 SNST FS11 FS10 FS16 RIGA CSWY MDSN FS17 DREW FS19 CNTRL WB_RD BRK_ST CTY_HL PLM_RVR FWLR_AVE WRCHM_DR INTERBAY NRTH_BLVD NORTHWEST GRND_HMTN LCKWD_RDG PRKLDG_DR FRMNT_AVE Rocky Point CROSS_CREEK Busch Gardens MORRIS-BRIDGE Sources: Esri, Garmin, USGS, NPS / 1 inch = 14,000 feet 0 7,000 14,000 Feet % of Points that Met Goal Diameter Removed from Calibration Less than 12-inch Less the 50% 12 -24-inch 50% to 75% Greater than 24-inch Service Area 80% to 90% 90% to 100% 75% to 80% CITY OF TAMPA Potable Water Master Plan Figure 4-2 Recalibration Results Summary

5.0 Distribution System Assessment

Using the calibrated hydraulic model, Black & Veatch performed a comprehensive distribution system analysis. The analysis includes assessments of the system’s performance under a variety of scenarios including: MDD, PHD, Fire Flow (FF) and Asset Failures. These scenarios were run primarily for the base year (2015) and final future planning year (2035), with consideration of phasing of improvements for the two interims planning years (2020 and 2025). Scenarios were developed and analyzed based on the existing system configuration as well as a variety of proposed configurations. However, only the performances of the existing system scenarios are presented here.

The system analysis evaluates the adequacy of the existing distribution system and highlights areas requiring improvements (presented in Section 6) to meet the system performance criteria established by the TWD. The results of the distribution system assessment are summarized in the remainder of this section of the report. Additional details regarding the assessment of the distribution system are also provided in Appendix D, Distribution System Assessment Technical Memorandum.

5.1 PERFORMANCE CRITERIA

Black & Veatch worked with the TWD to establish the desired system performance criteria, which were used as the basis for determining if improvements are needed to meet the projected increases in system demands over the planning horizon. The criteria are based on various water system design guidelines and consider references such as existing and proposed regulations (e.g. FDEP regulations). Table 5‐1 summarizes the performance criteria on which the system was evaluated.

5.2 DISTRIBUTION SYSTEM ASSESSMENT RESULTS

Black & Veatch analyzed the existing distribution system for the purpose of identifying system capacity, operational, resiliency, and reliability needs across various planning years. More than twenty‐five scenarios were selected to analyze the existing and planned distribution systems. Discussions of the analysis approach, observations and conclusions of the system analysis are presented in the following sub‐sections.

5.2.1 Pumping Facilities

The capacities of the pumping facilities were analyzed using an Excel‐based desktop model for each planning year to evaluate the adequacy of the existing facilities and to identify any deficiencies in capacity based on regulations and the performance criteria. The results of the desktop pumping facilities capacity analyses are presented in Table 5‐2.

Table 5‐1: Distribution System Performance Criteria

Distribution system performance criteria summarizing parameters, criteria or descriptions, performance goals, and related comments.
Parameter Criteria / Description Performance Goal Comments
1. Demand Peaking Factor MDD: ADD 95th confidence interval (only exceeded 1 year out of 20 years) [B&V] ‐ Ratio to be calculated based on actual system data from 2004 ‐ 2015. th ‐ PHD: MDD data is not available for the period and will be based on 95 Percentile of 5 years (2011‐2015)
# Years of Historic Data 12 ‐ 12 years were selected to include the last drought conditions in 2007.
2. Pump Station Capacity Supply + Remote Pump Stations (w/out elevated storage) Firm Capacity > PHD + Fire Flow (per service area) [F.A.C 62‐555.320(15)(a)] ‐ Firm Capacity > PHD + Fire Demand, unless elevated finished drinking water storage is provided [F.A.C. 62‐555.320 (15)(a)] ‐ Firm Capacity + useful elevated storage capacity > greater of PHD for 4 hours or MDD+FF [F.A.C 62‐555.320(15)(b)] ‐ Firm capacity per pressure zone is the capacity with the largest pump out of service per pressure zone. • North Tampa Zone, South Tampa (Interbay) and DLT Zone
Supply + Remote Pump Stations (w/elevated storage) Firm Capacity > MDD + Fire Flow (per service area) [F.A.C 62‐555.320(16)(b)] ‐ Existing Elevated tanks cannot be counted for F.A.C 62‐555.320(15)(a) as they do not float on the system. ‐ If elevated tank improvements were made to allow the tanks to float on the system, the criterion may be reduced to meet F.A.C. 62‐555.320(15)(b). This can be evaluated as a potential improvement option.
3. Storage Volume Total Storage (per pressure zone) > 25% of the System’s MDD + Fire Flow (Reserve) [F.A.C. 62‐555.320 (19)(a)] ‐ Unless a demonstration showing that the useful finished water storage capacity (minus fire protection) is sufficient for operational equalization [F.A.C. 62‐555.320(19)(b)1] ‐ Unless a demonstration showing that the water system’s total useful finished water storage capacity (minus fire protection) is sufficient to meet the water systems PHD for 4 consecutive hours [F.A.C. 62‐555.320(19)(b)2] ‐ Equalization storage should be 15‐20% of max daily use. [Lindeburg] ‐ Per discussion with the City, total storage does not include additional emergency storage due to existing WQ concerns.
Fire Reserve 3,500 gpm for 3 hours (per service area) ‐ Minimum fire flow = 1,000 gpm for 1 hour [Florida Fire Code, Table 18.4.5.1.2] ‐ Fire Flow between 1,500 gpm & 2,750 gpm = a duration of 2 hours; 3,000 & 3,750 gpm = a duration of 3 hours [Florida Fire Code]
4. Pressure Minimum Pressure – Peak hour demand conditions. (Non‐Fire, Non‐Emergency) > 50 psi Transmission > 40 psi Distribution > 25 psi Metered Discharge [TWD Tech Manual, 3.2.A.2] ‐ > 20 psi [F.A.C. 62‐555.320 (15)(b)] ‐ Minimum pressure at the tap should be 25 psi. Minimum pressures at fire hydrants should be 60 psi, possibly higher in commercial and industrial districts [Lindeburg] ‐ Metered discharge pressure is on the private side of the customer meter and is not represented in the model
Maximum Pressure < 75 psi ‐ Florida 2010 Plumbing Code requires a service line PRV if the pressures within the building exceeds 80 psi.
5. Fire Flow System Demand/Supply MDD ‐ If fire protection is being provided the design capacity should be fire flow plus maximum day demand. MDD+FF [F.A.C. 62‐555.320(15)(a)] ‐ PHD+FF was not selected due to existing WQ concerns which would increase with oversized water mains.
Minimum Flow 1,000 gpm (residential) 3,500 gpm for 3 hours (commercial & Industrial) [exceeds TWD Tech Manual, 3.2.A.3.c] ‐ Residential fire flow can be reduced to 500 gpm if building has automatic sprinkler systems and greater than 30ft separation between buildings [18.4.5.1.23, Florida Fire Code] ‐ 1,000 gpm for 1 hour (residential) & 3,000 gpm for 3 hours (commercial & industrial) [TWD Tech Manual, 3.2.A.3.c]
Maximum Flow 3,500gpm for 3 hours [ISO & AWWA M31] The maximum flow is the maximum fire flow required from the TWD system. For system customers with fire flow requirements greater than what can be provided by the TWD system, it is assumed that those customers will construct private fire protection systems as needed to meet their own fire service needs.
Minimum Residual Pressure > 25 psi [TWD Tech Manual, 3.2] Minimum residual pressures = 20 psi. [F.A.C. 62‐555.320 (15)(a)]
6. Pipe Capacity Maximum Velocity < 5 ft./sec at peak hour demands (normal, non‐fire conditions) < 10 ft./sec at MDD+FF demands [TWD Tech Manual, 3.2] ‐ This parameter is used to identify pipes that may be contributing to pressure and/or flow deficiencies. ‐ Considered a secondary criterion to trigger consideration for improvement, but not automatically triggering an improvement
7. Headloss Gradient Maximum Head loss (HL) per 1,000 Feet < 3ft (Mains >=16‐inch diameter) < 5ft (Mains <16‐inch diameter) ‐ This parameter is used to identify pipes that may be contributing to pressure and/or flow deficiencies. ‐ Considered a secondary criterion to trigger consideration for improvement, but not automatically triggering an improvement

Table 5‐2: Pump Station Regulatory Capacity Assessment

Assessment of pump station capacities by pressure zone and pumping facility compared to performance criteria (PHD + Fire Flow) for multiple planning years, including indication of whether criteria are met and the year improvements are required.
PRESSURE ZONE PUMPING FACILITY CAPACITY PERFORMANCE CRITERIA (MGD) PHD + Fire Flow(4)(5) MEETS CRITERIA (Y/N) DEFICIENT CAPACITY (MGD) YEAR IMPROVEMENT REQUIRED
MAX (MGD) M. FIRM CAPACITY (MGD) 2015 2020 2025 2035 2015 2020 2025 2035
New Tampa(1) Morris Bridge RPS Pumps #1‐4 102 66.0 15.6 18.6 20.4 23.5 Y Y Y Y N/A N/A
South Tampa Interbay RPS(2) 28 15.0 16.8 17.9 18.2 18.7 N N N N 3.7 2015
DLTWTF(3) DLTWTF Total 198.5 160.2 137.8 163.8 170.9 185.2 Y N N N 25.0 2020
High Service 164 134 137.8 163.8 170.9 185.2 Y N N N 25.0 2020
Northwest 15 12 137.8 163.8 170.9 185.2 Y N N N 25.0 2020
West Tampa 10 7 137.8 163.8 170.9 185.2 Y N N N 25.0 2020
Palma Ceia 9 7 137.8 163.8 170.9 185.2 Y N N N 25.0 2020
  1. 1. Total Firm Capacity 62 MGD; Pumps #1 4 and Pumps #5&6 cannot operate at the same time and the firm capacity of Pumps #1 4 48 MGD. Pumps #1 4 are required to meet regulations
  2. 2. Interbay firm capacity exclude the two small jockey pumps due to pump station configuration
  3. 3. DLTWTF firm capacity is based upon the largest pump at the DLTWTF being out of service. The remainder of the pumps within this pressure zone ar operational.
  4. 4. The demand on the DLTWTF inlcudes the MDD of North Tampa and South Tampa due to the constant filling of the tanks
  5. 5. PHD + Fire Flow for each Plan Year is the PHD in MGD plus the Fire Flow of 3,500 gpm converted to MGD or 5.0 MGD

The Morris Bridge RPS, which supplies the North Tampa pressure zone, currently has 66 MGD of firm capacity. This capacity is well in excess of the PHD plus FF of the North Tampa pressure zone.

The Interbay RPS, which supplies the South Tampa pressure zone, currently has 15 MGD of firm capacity. This capacity is deficient under the 2015 planning year scenario by nearly 2 MGD and the deficiency increases to nearly 4 MGD in the 2035 planning year. Additional pump capacity or other augmentations to the South Tampa pressure zone are required to meet the pumping capacity criteria.

The DLTWTF pressure zone is served by four pump stations. The primary source of pumping capacity is the DLTWTF HSPS (HSPS). The HSPS is supplemented by the Northwest, West Tampa and Palma Ceia RPSs located throughout the distribution system. The combined firm pumping capacity of these facilities is 160.2 MGD. This capacity meets criteria under the 2015 planning year but is deficient from 2020 through the remainder of the planning horizon. The pumping capacity deficiency for the DLTWTF pressure zone reaches as high as 25 MGD by 2035 under the static capacity analysis. However, the EPS hydraulic model analysis showed that in order to supply the system under PHD conditions, flow from the DLTWTF HSPS could reached as high as 175 MGD without changes to the operating scheme for the RPSs. The existing firm capacity of the HSPS is 134 MGD, resulting in a capacity deficiency of 41 MGD by 2035 if no other improvements are made. The TWD currently has plans to expand the DLTWTF to a firm capacity of 153 MGD. However, the hydraulic modeling analysis of future system conditions indicates that an expansion of the HSPS to a firm capacity of 153 MGD alone will not be sufficient to address the pumping capacity requirements projected through year 2035. Additional HSPS pumping capacity and other potential improvements to the DLTWTF pressure zone were evaluated and are described in Section 6 of this report.

5.2.2 Potable Water Storage

The capacities of the storage facilities were analyzed using an Excel‐based desktop model for each planning year to evaluate the adequacy of the existing facilities and to identify any deficiencies in capacity based on the performance criteria. The results of the initial storage facilities capacity analyses are presented in Table 5‐3.

Table 5‐3: Potable Water Storage Regulatory Capacity Assessment

Regulatory capacity assessment of potable water storage facilities by pressure zone, including total and effective storage volumes, minimum required storage, compliance with criteria, deficient volumes, and year improvements are required.
PRESSURE ZONE STORAGE FACILITY TOTAL VOLUME (MG) EFFECTIVE VOLUME (MG) 2015 Minimum Storage Volume (MG) 25% of MDD + Fire Reserve(1) 2020 Minimum Storage Volume (MG) 25% of MDD + Fire Reserve(1) 2025 Minimum Storage Volume (MG) 25% of MDD + Fire Reserve(1) 2035 Minimum Storage Volume (MG) 25% of MDD + Fire Reserve(1) 2015 MEETS CRITERIA (Y/N) 2020 MEETS CRITERIA (Y/N) 2025 MEETS CRITERIA (Y/N) 2035 MEETS CRITERIA (Y/N) DEFICIENT VOLUME (MG) YEAR IMPROVEMENT REQUIRED
New Tampa Morris Bridge RPS 10.0 7.5 2.5 3.0 3.3 3.9 Y Y Y Y N/A N/A
South Tampa Interbay RPS 5.0 5.0 2.4 2.6 2.7 2.7 Y Y Y Y N/A N/A
DLTWTF DLTWTF Total 26.0 18.5 23.9 26.4 27.4 29.6 No per FAC 62‐555.320(19)(a). See detailed storage analysis for further explantion of minimum criteria. 11.1 2016
DLTWTF Clearwell 20.0 12.5
DLTWTF Northwest 3.0 3.0
DLTWTF West Tampa 1.5 1.5
DLTWTF Palma Ceia 1.5 1.5
DLTWTF Deficient Storage without considering the Morris Bridge excess volume (MG) 5.4 7.9 8.9 11.1
DLTWTF Deficient Storage considering the Morris Bridge excess volume (MG) 0.4 3.4 4.8 7.5
Note 1. Fire Reserve storage required is 3500 gpm for 3 hours or 0.63 MG

5.2.3 Distribution System Capacity and Operation

The hydraulic capacity of the distribution system piping network was analyzed for each planning year based on the performance criteria. This analysis identifies undersized pipelines that may be impacting the system’s ability to deliver required flow or pressure under MDD conditions. The analysis showed that most of the distribution system maintains adequate minimum pressures during a MDD EPS simulation and does not significantly exceed maximum pressure criteria. The largest collection of low pressures in the system existed within the southern portion of the DLTWTF zone in the 2015 planning year. However, the modeling analysis predicts that the addition of the planned CIAC improvements will effectively address the low pressure issues in the southern portion of the DLTWTF zone. Additional locations of low pressures include the eastern boundary of

the service area near the University of South Florida (USF) and the western boundary of the service area north of the Northwest RPS. An assessment of these areas indicates that the ground elevations in these two areas are higher than other portions of the service area, and that distribution system pipe improvements are unlikely to sufficiently address the low pressure in these two areas. Table 5‐4 presents the results for compliance with the minimum and maximum pressure criteria at all model junctions for each planning year during a MDD scenario.

Table 5‐4: Percent of the System Meeting Pressure Criteria

Percent of model junctions in the system meeting specified minimum and maximum pressure criteria for each MDD analysis scenario.
# SCENARIO NAME MINIMUM PRESSURES > 30 psi MINIMUM PRESSURES > 40 psi MINIMUM PRESSURES > 50 psi MAX. PRESSURES > 75 psi MAX. PRESSURES > 85 psi
1 Base MDD Analysis 98.6% 91.5% 67.7% 15.6% 0.0%
2 2020 MDD Analysis 99.6% 94.3% 69.8% 17.6% 0.0%
3 2025 MDD Analysis 99.5% 93.2% 65.0% 16.4% 0.0%
4 2035 MDD Analysis 98.5% 88.9% 52.3% 9.8% 0.0%

The system capacity analysis also reviewed pipe velocity and headloss results for each planning year. High velocities in pipelines can lead to high headlosses and lower system pressures. The performance criteria for velocity and headloss were established to help identify existing and potential causes of pressure problems throughout the system. The results of this assessment show that the large majority of the distribution system operates well within the performance criteria and that outside of the planned improvements, the system does not require significant distribution or transmission capacity improvements. Table 5‐5 presents the results for compliance with the maximum velocity and headloss criteria for all modeled pipes 4‐inches and larger for each planning year during a MDD scenario.

Table 5‐5: Percent of the System Meeting Velocity and Headloss Criteria

Percent of modeled pipes 4-inches and larger meeting maximum velocity and headloss criteria for each MDD analysis scenario.
# Scenario Name Max. Velocity < 5 fps Max. Headloss1 < 3 ft / 1000ft Max. Headloss1 < 5 ft / 1000ft
1 Base MDD Analysis 99.8% 97.2% 95.2%
2 2020 MDD Analysis 99.7% 97.7% 96.0%
3 2025 MDD Analysis 99.8% 97.2% 95.7%
4 2035 MDD Analysis 99.7% 95.7% 94.7%
1 <3 ft/1000 ft criteria applies to pipes >= 16 inch. <5 ft/1000 ft criteria applies to pipes <16 inch

5.2.4 Fire Flow

In addition to meeting the MDD demands and pressures, the water distribution system must also be able to provide large volumes of water in a concentrated area during a fire event, while still maintaining minimum pressure requirements throughout the distribution system. This is known as fire flow (FF) demand. The amount of fire flow required varies based on the Florida Fire Code guidelines, which consider the structure’s size, use, and building materials. The fire flow analysis used MDD plus FF of 1,000 gpm for residential areas and 3,500 gpm for commercial areas while maintaining a minimum residual pressure of 25 psi in the system. Table 5‐6 summarizes the extent

of the distribution system that met the fire flow goals for water mains 6‐inches and larger. The City has a program to replace 2‐inch diameter pipes, which should continue to be administered to provide improved fire flow supply coverage.

Table 5‐6: Percent of the System Meeting Fire Flow Goals

Percent of the distribution system meeting residential and commercial/industrial fire flow goals under different MDD+FF analysis scenarios.
# SCENARIO NAME RESIDENTIAL (1,000 GPM) COMMERCIAL / INDUSTRAL (3,500 GPM)
1 Base MDD+FF Analysis 95% 61%
2 2020 MDD+FF Analysis 97% 62%
3 2025 MDD+FF Analysis 91% 51%
4 2035 MDD+FF Analysis 87% 50%
NOTE: increased coverage is due to the addition of the planned CIAC & KBar pipelines.

There are some residential fire flow deficiencies which exist sporadically throughout the system, and a variety of improvements discussed in Section 6 were identified to provide complete residential fire flow coverage. However, to be sensitive not to oversize the distribution system piping and avoid increasing water age within the system, Black & Veatch recommends that a separate analysis of the required commercial fire flow be conducted and commercial fire flow corridors be identified before significant fire flow improvements are planned.

5.2.5 Water Age

A water age analysis for the base year (2015) was performed as part of the distribution system analyses to set a baseline for comparing water ages in future year analyses. Generally, the model results show that the water age of the system is less than 5 days with small pockets around the tanks that have ages up to 10 days. Additionally, the water age in each of the small pressure zones is in the 5 to 10‐day range. This is attributed to all of the supply to these small zones going through the ground storage tanks. Additional information related to water age is available in Appendix B, Distribution System Improvements Technical Memorandum.

5.2.6 Resilience and Redundancy

Several scenarios exploring the system’s redundancy and resilience to key asset was to failures were also analyzed. The assets reviewed included the DLTWTF HSPS, all of the RPSs, and critical transmission pipelines. The results showed that, in general, the system has a good level of resiliency, with most key facilities covered by some or complete redundancy. A summary of the results of the resilience analyses are presented below.

HSPS, additional storage and/or pumping capacity, as well as emergency water supply sources, would need to be established.

6.0 Distribution System Improvements

The assessment of the distribution system revealed that the system contains some deficiencies due to projected growth over the planning horizon. The distribution capacity improvements are divided into three categories: Operational Improvements, Capacity Improvements (which includes fire flow improvements), and Resilience / Redundancy Improvements.

6.1 OPERATIONAL IMPROVMENTS

6.1.1 DLTWTF HSPS Discharge Pressure

The DLTWTF HSPS currently operates with a discharge pressure of 65 psi, which results in multiple areas within the DLTWTF pressure zone having a residual pressure below or just above the minimum pressure criteria of 40 psi. Increasing the HSPS discharge pressure would increase pressures throughout the zone and result in a much larger percentage of the zone meeting the TWD’s defined pressure criteria under all demand scenarios.

Increasing the HSPS discharge pressure by 5 psi brings the vast majority of the system pressures into compliance with the system pressure criteria under all demand scenarios. However, increasing the system pressures is not without risks. A 5‐psi increase in the distribution system pressures should be well within the original design pressure ratings of the piping throughout the system, however, the City’s system is aging, and increasing the system pressures by 5 psi could result in an increased frequency of pipe breaks. To minimize the potential risk for an increased amount of pipe breaks in the system, Black & Veatch recommends that any potential increases in system pressures are undertaken incrementally to allow the TWD to observe how the distribution system reacts to small increases in pressure. Minimum system pressures and conformance with minimum pressure criteria based on this change in operations is illustrated in Figure 6‐1 and described in more detail in Appendix B, Distribution System Improvements Technical Memorandum.

6.1.2 DLTWTF Pressure Zone Repump Station Controls

The system assessment identified that the DLTWTF HSPS capacity will be deficient within the short‐term planning horizon, and that previously planned capacity expansions from the current firm capacity of 134 MGD to 153 MGD will not be sufficient over the long‐term planning horizon (through 2035) without other pumping and storage improvements in the pressure zone. As part of the improvements development process, the entire DLTWTF zone was reviewed for its impact on demands on the HSPS. The current operating strategy for the system involves the HSPS maintaining a pressure set point and the discharge flowrate increasing or decreasing automatically to maintain the pressure set point as the demands in the pressure zone increase or decrease. The other RPSs in the DLTWTF pressure zone operate at full speed on their pump curves and do not automatically ramp up and down in speed in order to maintain a target pressure set‐point. This results in the HSPS experiencing a wide range of discharge flowrate conditions to meet the diurnal fluctuations in system demands. Additional review of the DLTWTF pressure zone indicates that the operating strategy for the Northwest, West Tampa, and Palma Ceia pump stations can be modified in the future to handle some of the diurnal demand fluctuations in the system to limit the amount of variance in the discharge flowrates from the HSPS, and reduce the maximum firm capacity needs for the DLTWTF HSPS.

CITY OF TAMPA Potable Water Master Plan - Figure 6-1

Map showing potable water master plan for 2015, highlighting existing and proposed water system pressures and infrastructure in blue and green.
Figure 6-1 D Proposed HSPS Discharge Pressure Changes. Planning Year 2035 Existing System Assessment -65 psi HSPS Discharge Pressure Minimum Pressures and Proposed Planning Year 2035 MDD with 24Hr EPS -70 psi HSPS Discharge Pressure Minimum Pressures. The figure includes a legend for minimum pressures (Below 20 psi; 20 -25 psi; 25 -30 psi; 30 -40 psi; 40 -50 psi; 50 -75 psi; 75 -85 psi; Greater than 85 psi), water main diameters (wMain Diameter < 12-inch; 12 -16-inch; 16 -24-inch; > 24-inch), and facility types (WTP, Pump Stations, Ground Storage Tank, Elevated Storage Tank). Scale: 1 inch = 17,000 feet; 0, 8,500, 17,000 Feet.

The TWD can use the Northwest, Palma Ceia, and West Tampa RPS’s to decrease the reliance on the DTWLTF HSPS to handle system peak hour demands by updating the operating and control strategies for these facilities. Black & Veatch recommends that the TWD implement a monitoring and controls system that will activate the RPS’s based on the output flow of the DLTWTF HSPS and/or local pressure settings. The recommended system would be automated and would activate the RPS’s to minimize the peak flow at the HSPS, as well as rotate which RPSs are being used to ensure even run time on pumps and cycling of the storage tanks.

Should the City not wish to install an automated system, a system that monitors the HSPS flow and provides operators with pre‐set indicators and a defined control strategy for operators to follow could be similarly effective. The modeling analysis indicates that modifying the RPS pump controls can reduce the required additional capacity of the DLTWTF HSPS for planning year 2035 by 13 MGD.

6.1.3 Distribution System Monitoring

For TWD operators and engineers to better understand system operations and to document and memorialize operational data, Black & Veatch recommends that the TWD install flow meters at the Palma Ceia and West Tamps RPSs. in addition, the TWD could perform field pump tests to generate accurate pump curves, document pump efficiencies and improve the understanding of pump flows at different tank levels and system pressure conditions.

Black & Veatch also recommends that power monitors be installed at all RPSs to begin the collection and monitoring of data on the power consumption and pump efficiencies at each facility.

6.2 CAPACITY IMPROVEMENTS

6.2.1 Pumping Capacity Improvements

As discussed in previous sections and presented in Appendix B, Distribution System Improvements Technical Memorandum, the DLTWTF and South Tampa pressure zones both require augmentations to the system to correct deficiencies in available pumping capacity.

Interbay Repump Station

The results indicate that the South Tampa pressure zone pumping capacity is currently deficient and additional pumping capacity, approximately 4 MGD, is required to provide 3,500 gpm for fire flow. There are two options available to remedy the deficient pumping capacity; 1) install an additional pump at the Interbay RPS with a capacity of 4 MGD; 2) Install check valves along the pressure zone boundary (Gandy Blvd.) to allow flow from the neighboring DLTWTF zone to supply the South Tampa pressure zone during low pressures and supplement the pump capacity in the event of reduced pressures from fire demands during a peak demand period. Black & Veatch recommends the second option of installing check valves along the pressure zone boundary to address fire flow and resilience concerns. The resilience impacts are discussed further in subsequent sections.

High Service Pump Station

Black & Veatch recommends that the planned DLTWTF HSPS expansion to a firm capacity of 140 MGD identified in the DL Tippin WTF Master plan be increased to 153 MGD. In addition, it is also recommended that the HSPS expansion design consider provisions to easily expand the firm capacity to the recommended 2035 firm capacity requirement of 167 MGD. This recommendation is one of several recommendations that alter and augment the operation of the DLTWTF pressure zone. An additional recommendation includes increasing the available storage in the DLTWTF pressure zone with elevated storage tanks, which will reduce the demand on the HSPS during peak demand periods. These recommendations are detailed later in this section. Should the recommended elevated storage tank improvements within the DLTWTF pressure zone not be implemented, the required capacity at the DLTWTF HSPS would increase. Details of the potential for additional required capacity are included in Appendix B, Distribution System Improvements Technical Memorandum.

6.2.2 Storage Capacity Improvements

Clearwell Storage

The DLTWTF was initially constructed in the 1920s and has been expanded over the years to accommodate the City’s growth. As such, there are currently five separate clearwell structures connected with piping, which supply eight pumps at three various locations that discharge into the distribution system. According to the 2017 David L. Tippin Water Treatment Facility Master Plan, the changes in design, system demands, and configuration have resulted in a clearwell and pump combination that only allow for 12.5 MG of the 20.0 MG storage capacity to be available without causing cavitation in a few of the pumps and potential buoyancy problems with the below grade clearwell tanks. In addition, the blending chamber which feeds the clearwell was designed for lower flows, and at high flows the chamber pressurizes and starts to leak into the filter gallery.

These issues, combined with the projected increase in HSPS flows described above (140 – 167 MGD), have led to a recommendation in the 2017 David L. Tippin Water Treatment Facility Master Plan to abandon the two oldest clearwell structures (2.0 and 0.5 MG tanks), the existing blending chamber, and pumps 1‐6; repurpose the existing 7.5 MG clearwell to be a blending chamber; construct a new 5.0 MG clearwell; and add pumping capacity to reach 140 MGD firm capacity to be completed before 2025. Based on the system analysis, additional storage capacity beyond the proposed new 5.0 MG clearwell should be considered as part of this proposed project.

Accounting for the proposed modifications to the existing clearwell structures, a new 13 MG tank would increase the total storage capacity of the DLTWTF pressure zone to 31.5 MG, exceeding the FAC requirements in 62‐555.320(19)(a) and allowing for 4.5 to 5 hours of supply capacity should the treatment system be out of service. Therefore, Black & Veatch recommends increasing the proposed additional storage at the DLTWTF site from 5.0 MG to 13.0 MG. NOTE: this accounts for the reduction in volume from the proposed demolition of the 2.0 and 0.5 MG clearwells.

Figure 6‐2 illustrates the potential location for the additional clearwell storage. Additional assessments should be completed to confirm appropriate locations, dimensions and features of the recommended clearwell capacity expansions.

Map of the DLTWTF zone, showing existing capacity, improvements, detention time, and proposed changes in Clearwater storage.
Source: Esri, DigitalGlobe, GeoEye, Earthstar Geographics, CNES/Airbus DS, USDA, USGS, AeroGRID, IGN, and the GIS User Community HSP 1-4 HSP 7-8 HSP 5-6 Clearwell1=7.5MG RetrofittoBlendingChamber EffectiveVolume=5.0 (min5-ftdepth) Dim:333'x287'x12' Clearwell3=5.0MG Ef fectiveVolume=4.3;(min5-ftdepth) Dim:542'x109'x14'9" Clearwell 2 = 5.0 MG Effective Volume = 3.2 (min 5-ft depth) Dim: 197' x 287' x 12'8" Proposed Clearwell = 13 MG Actual Deminsions TBD Effective Volume = 11.0 (min 2-ft depth) Dim: 0.5 (535' x 478') x 17' Existing DLTWTF Zone Storage = 18.5 MG DLTWTF Zone Deficient Capacity = 11.1 MG (2035) DLTWTF Zone Storage after Improvements = 29.6 MG Detention time @ 153 MGD = 4 hours Clearwell 4 = 2.0 MG Effective Volume = 0.8 (min 5-ft depth) Dim: 180' x 120' x 10' Clearwell 5 = 0.5 MG Effective Volume = 0.3 (min 5-ft depth) Dim: 92' x 92' x 10' wMain Clearwell Status Diameter Demolish Less than 12-inch Existing 12 -24-inch Proposed Greater than 24-inch CITY OF TAMPA Potable Water Master Plan Figure 6-2 DLTWTF Clearwell Storage Improvements

Black & Veatch also recommends beginning the collection of data related to the groundwater level on the site in anticipation of the design of a new clearwell structure and the current buoyancy issues that limit the drawdown levels and useable storage capacity of the existing clearwells.

Distribution System Storage

Black & Veatch also recommends that two new elevated storages tanks be added (Broadway; 2.0‐MG and Nebraska; 3.5‐MG) to improve system resiliency, which is discussed further in the section and in Appendix B, Distribution System Improvements Technical Memorandum. These tanks are not required based on State regulations, but they provide additional benefits of protecting the system from transient pressures, reducing the capacity requirements for the DLTWTF HSPS, and allowing the Northwest, West Tampa and Palma Ceia RPSs to be taken out of service for maintenance as demands increase in the future.

6.2.3 Water Main Capacity Improvements

The assessment of the distribution system revealed that the hydraulic capacity of the existing distribution system piping is predominantly satisfactory based on the demands projected through the planning year 2035. Transmission and distribution mains appear to be properly sized and well distributed throughout the system.

TPA and TIA Master Meters

Black & Veatch completed an investigation of the potential to install master meters at the Tampa Port Authority (TPA) and the Tampa International Airport (TIA) to isolate the onsite water mains and transfer ownership of those mains to the respective customers as described in Appendix E, TPA and TIA Master Meter Technical Memorandum. This is an effort to simplify maintenance of the water mains, which is complicated due to access restrictions at these locations. The investigation showed that the water mains in the TPA and TIA sites could be isolated from the system without significant impacts to the surrounding distribution system. Therefore, installation of the master meters is assumed to be installed as part of the system analysis and identification of improvements.

Water Main Capacity Improvements

Due to the overall strong performance of the distribution system based on the velocity and headloss criteria, the system assessment resulted in the identification of a limited number of improvements to address areas within the system exhibiting high headloss, some of which contribute to areas of low pressure. Table 6‐1 summarizes the improvements. These improvements are not impacted by the installation of additional storage within the DLTWTF zone and are independent of pipeline projects recommended later in this chapter to improve available fire flow within the distribution system. Refer to Appendix B for more detailed descriptions of each project.

Table 6‐1: Water Main Capacity Improvement Summary

Summary of water main capacity improvement projects including project ID, whether the project is a replacement or new pipeline, proposed diameter, length, planned year, and comments on hydraulic benefits.
PROJECT ID REPLACE / NEW PROPSOED DIAMETER LENGTH PLAN YEAR PROPOSED COMMENTS
CP003 Replacement 12‐inch
16‐inch
1 mile
200 feet
2020 Reduces 2020 peak hour headloss gradient (headloss/1,000 ft.) in the pipelines from 5.4 to 1.3
CP004 New 12‐inch 1 mile 2025 >2.5 psi pressure increase
CP005 New 8‐inch
12‐inch
800 feet
2 miles
2035 Reduces 2035 peak hour headloss gradient from 15.1 to 4.9 in 2035

6.2.4 Fire Flow Capacity Improvements

Thirty‐three fire flow improvements were identified to ensure that residential area fire flow requirements were met through the planning year 2035. An additional six fire flow improvements were identified to improve available fire flow conditions in commercial zones through the planning year 2035. Fire flow improvements are described in further detail in Appendix B, Distribution System Improvements Technical Memorandum.

As mentioned above, only pipelines 6‐inches and larger, which were not dead ends, were reviewed for available fire flow since hydrants are not installed on lines smaller than 6‐inches. The TWD distribution system contains a significant number of 2‐inch pipelines, which are incapable of delivering adequate fire flows. The TWD has a program in place to replace smaller diameter pipe, and it is recommended that the TWD continue to execute this program to provide residential fire flow to their entire service area.

Table 6‐2: Fire Flow Improvement Summary

Summary of fire flow improvement projects including project ID, whether the project is a replacement or new pipeline, proposed diameter, length, expected fire flow increase, and comments describing changes in available fire flow.
PROJECT ID REPLACE / NEW PROPSOED DIAMETER LENGTH FF INCREASE (GPM) COMMENTS
FF0‐01 Replacement 12‐inch 2,100 ft. 2,500 Increases FF from 1,100 to 3,500 gpm
FF0‐02 Replacement 12‐inch 4,600 ft. 1,100 Increases FF from 1,200 to 2,300 gpm
FF0‐03 Replacement 8‐inch 1,250 ft. 640 Increases FF from 600 to 1,240 gpm
FF0‐04 Replacement 12‐inch 4,600 ft. 330 Increases FF from 670 to 1,000 gpm
FF0‐05 New 12‐inch 1,200 ft. 1,140 Increases FF from 1,400 to 2,540 gpm
FF0‐06 Replacement 16‐inch 1 mile 1,250 Increases FF from 1,900 to 2,750 gpm
FF0‐07 Replacement 12‐inch 3,300 ft. 450 Increases FF from 800 to 1,250 gpm
FF0‐08 Replacement 8‐inch 800 ft. 400 Increases FF from 810 to 1,210 gpm
FF0‐09 Replacement 12‐inch 1,400 ft. 330 Increases FF from 800 to 1,130 gpm
FF0‐10 New 12‐inch 1,100 ft. 830 Increases FF from 860 to 1,690 gpm
FF0‐11 Replacement 8‐inch 800 ft. 480 Increases FF from 870 to 1,350 gpm
FF0‐12 Replacement 8‐inch 800 ft. 580 Increases FF from 910 to 1,490 gpm
Fire flow improvement projects (FF0, FF1, FF2 series) including type, pipe size, length, fire flow increase, and description.
FF0‐13 Replacement 12‐inch 900 ft. 220 Increases FF from 780 to 1,000 gpm
FF0‐14 Replacement 8‐inch 1,900 ft. 890 Increases FF from 920 to 1,810 gpm
FF0‐15 Replacement 12‐inch 2,800 ft. 630 Increases FF from 920 to 1,550 gpm
FF0‐16 Replacement 12‐inch 600 ft. 270 Increases FF from 980 to 1,150 gpm
FF1‐00 New 8‐inch 50 ft. 2,070 Increases FF from 380 to 2,450 gpm
FF1‐01 New 16‐inch 120 ft. 510 Increases FF from 690 to 1,200 gpm
FF1‐02 New 12‐inch 10 ft. 4,170 Increases FF from 1,030 to 5,200 gpm
FF1‐03 New 16‐inch 10 ft. 1,430 Increases FF from 1,100 to 2,530 gpm
FF1‐04 New 6‐inch 10 ft. 2,900 Connect 6‐inch dead ends for improvement of neighborhood FF
FF1‐05 New 8‐inch 20 ft. 590 Increases FF from 930 to 1,510 gpm
FF1‐06 New 20‐inch 60 ft. 250 Connect 20‐inch and 16‐inch dead ends for improvement of neighborhood FF
FF1‐07 New 6‐inch 10 ft. 1,600 Connect 6‐inch dead ends for improvement of neighborhood FF
FF2‐00 Replacement 12‐inch 600 ft. 3,780 Increases FF from 90 to 3,870 gpm
FF2‐01 Replacement 8‐inch 2,500 ft. 2,360 Increases FF from 120 to 2,480 gpm
FF2‐02 Replacement 8‐inch 1,000 ft. 1,510 Increases FF from 380 to 1,890 gpm
FF2‐03 Replacement 8‐inch 300 ft. 4,190 Increases FF from 430 to 4,620 gpm
FF2‐04 Replacement 8‐inch 50 ft. 2,280 Increases FF from 420 to 2,700 gpm
FF2‐05 Replacement 6‐inch 2,200 ft. 1,750 Increases FF from 410 to 2,160 gpm
FF2‐06 Replacement 12‐inch 20 ft. 3,110 Increases FF from 500 to 3,610 gpm
FF2‐07 Replacement 8‐inch 20 ft. 1,450 Increases FF from 480 to 1,930 gpm
FF2‐08 Replacement 8‐inch 2,300 ft. 3,940 Increases FF from 640 to 4,580 gpm
FF2‐09 Replacement 8‐inch 1,100 ft. 4,350 Increases FF from 550 to 4,900 gpm
FF2‐91 Replacement 6‐inch 700 ft. 770 Increases FF from 980 to 1,750 gpm
‐ General (FF0 ##) projects to increase available fire flow resulting from long dead ends, under sized or limited transmission capacity, or a long distance from existing transmission capacity
‐ Disconnects / New Connections (FF1 ##) projects to increase available fire flow, primarily on dead end pipelines, by connecting to nearby pipes, and/or increasing looping in the direct vicinity of the project.
‐ Pipe Size Flow Restrictions (FF2 ##) projects to increase available fire flow caused by connections to or being in the immediate proximity of 2 inch and 3 inch diameter pipe within the distribution network

6.3 RESILIENCE AND REDUNDANCY IMPROVEMENTS

Resilience is the capacity to recover quickly from a negative event. In the case of water utilities, a negative event can come in many forms due to both acute shocks and chronic stresses from anything from security threats to storm surges from hurricanes to power outages.

Resilience needs were assessed from the acute shock perspective of losing one of the TWD major facilities. Several scenarios were analyzed to determine if the distribution system has sufficient

redundancy to be resilient to single asset failures within the distribution system and the results of those analyses are presented in assessment section of this report. The proposed improvements are presented below and discussed in more detail in Appendix B, Distribution System Improvements Technical Memorandum. Improvements were identified with the goal of creating complete redundancy for each facility as well as ensuring the system was resilient to each failure by being able to maintain the ability to meet system performance criteria.

6.3.1 Interbay RPS

The Interbay RPS is the sole source of water for the South Tampa pressure zone, however, that is a recent development due to the closing of several valves along the Gandy Blvd. to create a pressure zone boundary. Should the Interbay RPS experience an unexpected outage, those same valves could be opened and the zone could be absorbed into the DLTWTF zone and supplied by the DLTWTF and other RPSs. To make that transition process much quicker and less manually intensive, Black & Veatch recommends installing check valves at select locations along the pressure zone boundary, which would automatically open if the pressures within the South Tampa pressure zone were less than the pressures within the DLTWTF zone along the boundary area. These valves could be equipped with sensors to alert the operations staff when they open. The TWD may also wish to include features that would provide the ability to bypass and isolate the check valves to provide increased operational flexibility.

6.3.2 Morris Bridge RPS and 54‐inch Transmission Main

With the addition of the planned improvements at the Morris Bridge RPS and the TBW interconnect, the Morris Bridge RPS is now completely redundant, and no new improvements are recommended. If the RPS fails, the bypass for the TBW interconnect can then supply the North Tampa pressure zone with up to 40 MGD directly or the valves isolating the North Tampa zone can be opened and supplied by the DLTWTF zone.

Similarly, if the 48‐inch/54‐inch transmission main, which normally supplies flow to the Morris Bridge RPS, fails, the TBW interconnect can be activated and used to supply the pressure zone. Depending on where the break occurs, Pumps 1‐4 can also discharge south to absorb the portion of the DLTWTF zone isolated from supply.

If TWD did not want to rely upon the TBW interconnect to provide redundancy for the North Tampa pressure zone in the event of a failure of the 48‐inch/54‐inch transmission main or Morris Bridge RPS, Black & Veatch would recommend installing a new water main parallel to the 48‐inch/54‐inch water main that supplies the Morris Bridge RPS. This project has been included in the CIP and could be implemented to further improve the reliability of supply to the North Tampa pressure zone.

6.3.3 Northwest, West Tampa and Palma Ceia RPSs

The Northwest, West Tampa, and Palma Ceia RPSs have complete redundancy under the existing system demands. However, with the increased demands in 2035, the RPSs become more critical. Losing any of the three RPS’s during a MDD can result in the distribution system not meeting the City’s minimum system pressure criteria; however, the system remains in compliance with minimum regulatory pressures. Additional elevated storage or a new RPS would allow for complete

redundancy for 24‐hours for the West Tampa and Palma Ceia RPS’s and would increase the resiliency of the distribution system.

In addition to the new storage, one additional water main improvement project is needed to increase east‐west transmission capacity for complete redundancy of the Northwest RPS. The water main improvement project consists of a combined 7,900‐ft of 16‐inch and 20‐inch pipe along Hillsborough Ave.

6.3.4 DLTWTF High Service Pump Station

An event that results in the inability to operate the DLTWTF and associated HSPS would have the greatest negative impacts to the operation of the system. It is assumed that TWD would communicate with customers to request reduced water consumption during this type of scenario to keep demands to ADD conditions or less, rather than MDD. Based on this assumption and a 24‐hour DLTWTF failure scenario, the TWD could make the following system configuration changes:

Under these conditions and without additional supply and/or storage in the DLTWTF zone, the system could meet the existing ADD for 24 hours, but would still need an additional 5.5 MGD by 2035. The additional supply can come in the form of additional storage or additional interconnections with neighboring utilities. Black & Veatch recommends a combination of additional storage, which will also increase redundancy of the RPSs, and an additional 6 MGD interconnect with Hillsborough County or Tampa Bay Water.

One such location could be with Hillsborough County just north of the Northwest RPS. The interconnection flow could discharge directly into the distribution system, if feasible based on the County’s operational pressures, or into the Northwest tank. Note that this option requires negotiations and cooperation with each utility.

6.4 IMPACTS TO WATER AGE

6.4.1 Impacts of Proposed Improvements on Water Age

Most of the proposed improvements have negligible impacts on water age, with the exception of the proposed Broadway EST. This improvement increases the water age in the southeast portion of the system to approximately 10 days, which is an increase of 5 days. The tank should be designed with a motorized isolation valve and pump to force turnover during low demand periods. The phasing of the tank should also coincide with increased demands throughout the DLTWTF zone and not be

constructed before the system conditions warrant it to avoid potential water age/water quality impacts.

6.5 SUMMARY OF RECOMMENDED IMPROVEMENTS

Table 6‐3 below summarizes the recommended and prioritized improvements for the distribution system and Figure 6‐3 illustrates their locations. Figure 6‐4 through Figure 6‐6 illustrate the pressures and velocities throughout the distribution system before and after improvements. The figures show an obvious increase in pressures across the system, a minor and almost unnoticeable increase in system velocities and a decrease in water age, except for the North Tampa Pressure zone where the two tanks at the MBRPS are now being used.

Table 6‐3: Recommended Improvements

Summary of recommended and prioritized distribution system improvements, including project descriptions, triggers, types, and anticipated design years.
CIP # PROJECT NAME PROJECT DESCRIPTION PROJECT TRIGGER PROJECT TYPE ANTICIPATED DESIGN YEAR
1 IB, NW and MB Tank Inlet Sleeve Valves Installation of sleeve valves with flow control functions at the inlet to the Interbay, Northwest and Morris Bridge Tanks Three Pressure Zone Configuration Capital: Operational flexibility 2019
2 DLTWTF Discharge Pressure Increase DLTWTF HSPS discharge pressure to 70 psi; slowly / incrementally Min pressures Operational / Controls 2018
3 RPS controls modifications Modify the NWRPS, WTRPS and PCRPS to operate during peak demand periods rather than time of day Increased reliance on DLTWTF HSPS Operational / Controls 2018
4 DLTWTF Blending Chamber, Clearwell and HSPS Upgrades Demo 2.0 MG and 0.5 MG clearwells, convert 7.5 MG clearwell to blending chamber, install new 13.0 MG clearwell, demo pumps 1‐6 and install new 153 MGD HSPS firm capacity Sum of the MDDs for each pressure zone greater than 140 MGD R&R and Expansion 2020
5 HSPS Expansion Install additional pumping capacity at the new HSPS building total new capacity = 167 MGD firm capacity DLTWTF Pressure Zone Demands greater than 153 MGD Performance Criteria: Pump Capacity Expansion 2030
6 Northeast (Nebraska) EST Installation of a new EST in the north portion of the DLTWTF DLTWTF Pressure Zone PHD greater than 153 MGD Resilience 2025
7 Southeast (Broadway) EST Installation of a new EST in the north portion of the DLTWTF DLTWTF Pressure Zone PHD greater than 160 MGD Resilience 2030
8 Commercial Fire Flow Study Perform an analysis of the required commercial fire flow needs be conducted and commercial fire flow corridors be identified Fire Flow Demands Study 2018
9 South Tampa Check Valves Install check valves along South Tampa Pressure Zone (along Gandy Blvd) Fire Flow Demands Resilience TBD
10 Hillsborough County Interconnect Interconnect with Hillsborough County in the northwest portion of the system DLTWTF Pressure Zone OHD greater than 167 MGD Resilience 2030
List of water system projects including IDs, descriptions, related programs, purposes, and target years.
ID Project Description Related Program or Driver Purpose Target Year
11 West Tampa and Palma Ceia Flow Meters Install flow monitors on the effluent side of the West Tampa and Palma Ceia RPS’s and connect to the data historian Data Collection Operational / Controls 2018
12 RPS Power Monitors Install power monitors on all RPS equipment and connect to the data historian Data Collection Operational / Controls 2018
13 DLTWTF Clearwell Groundwater Level Study Collection of data related to the groundwater level on the site in anticipation of the design of a new clearwell structure DLTWTF Blending Chamber, Clearwell and HSPS Upgrade Project Capacity 2018
14 Water Quality Model Calibration Study Collect water quality data throughout the system in order to conduct a calibration of the existing water quality model Water Quality Study 2018
15 R‐01 Hillsborough Ave WM 6,000‐ft of 12‐inch pipe along Hillsborough Ave. DLTWTF Pressure Zone Demands greater than 125 MGD Resilience 2025
16 CP003 12‐inch; 1 Mile
16‐inch; 200 feet
System Pressures Capacity 2020
17 CP004 12‐inch; 1 mile System Pressures Capacity 2025
18 CP005 8‐inch; 800 feet
12‐inch; 2 miles
System Pressures Capacity 2035
19 FF0‐01 12‐inch; 4,600 feet Opportunistic Fire Flow 2018
20 FF0‐02 8‐inch; 1,250 feet Opportunistic Fire Flow 2018
21 FF0‐03 12‐inch; 4,600 feet Opportunistic Fire Flow 2018
22 FF0‐04 12‐inch; 1,200 feet Opportunistic Fire Flow 2018
23 FF0‐05 16‐inch; 1 mile Opportunistic Fire Flow 2018
24 FF0‐06 12‐inch; 3,300 feet Opportunistic Fire Flow 2018
25 FF0‐07 8‐inch; 800 feet Opportunistic Fire Flow 2018
26 FF0‐08 12‐inch; 1,400 feet Opportunistic Fire Flow 2018
27 FF0‐09 12‐inch; 1,100 feet Opportunistic Fire Flow 2018
28 FF0‐10 8‐inch; 800 feet Opportunistic Fire Flow 2018
29 FF0‐11 8‐inch; 800 feet Opportunistic Fire Flow 2018
30 FF0‐12 12‐inch; 900 feet Opportunistic Fire Flow 2018
31 FF0‐13 8‐inch; 1,900 feet Opportunistic Fire Flow 2018
32 FF0‐14 12‐inch; 2,800 feet Opportunistic Fire Flow 2018
33 FF0‐15 12‐inch; 600 feet Opportunistic Fire Flow 2018
34 FF0‐16 8‐inch; 50 feet Opportunistic Fire Flow 2018
Fire Flow (FF) projects listing with ID, pipe size and length, implementation type, program, and year.
ID Project Pipe Size and Length Implementation Type Program Year
35 FF1‐00 16‐inch; 120 feet Opportunistic Fire Flow 2018
36 FF1‐01 12‐inch; 10 feet Opportunistic Fire Flow 2018
37 FF1‐02 16‐inch; 10 feet Opportunistic Fire Flow 2018
38 FF1‐03 6‐inch; 10 feet Opportunistic Fire Flow 2018
39 FF1‐04 8‐inch; 20 feet Opportunistic Fire Flow 2018
40 FF1‐05 20‐inch; 60 feet Opportunistic Fire Flow 2018
41 FF1‐06 6‐inch; 10 feet Opportunistic Fire Flow 2025
42 FF1‐07 12‐inch; 600 feet Opportunistic Fire Flow 2025
43 FF2‐00 8‐inch; 2,500 feet Opportunistic Fire Flow 2018
44 FF2‐01 8‐inch; 1,000 feet Opportunistic Fire Flow 2018
45 FF2‐02 8‐inch; 300 feet Opportunistic Fire Flow 2018
46 FF2‐03 8‐inch; 50 feet Opportunistic Fire Flow 2018
47 FF2‐04 6‐inch; 2,200 feet Opportunistic Fire Flow 2018
48 FF2‐05 12‐inch; 20 feet Opportunistic Fire Flow 2018
49 FF2‐06 8‐inch; 20 feet Opportunistic Fire Flow 2018
50 FF2‐07 8‐inch; 2,300 feet Opportunistic Fire Flow 2018
51 FF2‐08 8‐inch; 1,100 feet Opportunistic Fire Flow 2018
52 FF2‐09 6‐inch; 700 feet Opportunistic Fire Flow 2018
53 FF2‐91 12‐inch; 4,600 feet Opportunistic Fire Flow 2018
Map of proposed water system improvements in Tampa, showing pipelines, water treatment facilities, and expansion areas through 2035.
CP005 FF004 FF006 FF002 FF014 FF001 FF013 FF201 [Ú UT RR001 RR001 [Ú [Ú [Ú UT FF00009 CP 3 KBar [Ú UUTT Parallel TM HC Interconnect HSPS & Clearwell Expansions CIAC Boundary Check Valves / 1 inch = 14,000 feet 0 7,000 14,000 Feet KBar Improvements Diameter CITY OF TAMPA Q WTP 3 CIAC Improvements Less than 12-inch Potable Water Master Plan [ Capacity Improvements 12 - 16-inch Ú Pump_Stations Fire Flow Improvements 16 - 24-inch T Ground Storage Tank Resilience Improvements Greater than 24-inch Figure 6-3U South Tampa Proposed Improvements New TampaElevated Storage Tank Through 2035 Service Area Proposed_Tank_Areas 3Q Sources: Esri, Garmin, USGS, NPS

CITY OF TAMPA

Potable Water Master Plan

Figure 6-4 – Proposed Planning Year 2035 MDD with 24Hr EPS Minimum Pressures
Maps comparing existing system assessment minimum pressures and proposed planning year 2035 model, showing changes in water pressure distribution.
3 Q WTP
Green square with 'WTP' in white text.
Legend symbols for pump stations and storage tanks
Logos of the City of Tampa, Florida and Black & Veatch, with a slogan about making a difference.

Figure 6-4

Proposed Planning Year 2035 MDD with 24Hr EPS Minimum Pressures

Pump Stations and Storage Tanks

3 Q WTP

Ú[

Pump Stations

UT

Ground Storage Tank

Elevated Storage Tank

Minimum Pressures MIN_PRESSURE

  • Below 20 psi
  • 20 -25 psi
  • 25 -30 psi
  • 30 -40 psi
  • 40 -50 psi
  • 50 -75 psi
  • 75 -85 psi
  • Greater than 85 psi

wMain

Diameter

  • < 12-inch
  • 12 -16-inch
  • 16 -24-inch
  • > 24-inch

Proposed_Tank_Areas

  • South Tampa
  • New Tampa
  • Service Area

/ 1 inch = 17,000 feet 0 8,500 17,000 Feet UT UTUT [Ú [Ú [Ú [Ú 3Q / 1 inch = 17,000 feet 0 8,500 17,000 Feet UT [Ú Planning Year 2035 Existing System Assessment Minimum Pressures UT UT UTUT [Ú [Ú [Ú [Ú [Ú 3Q Proposed Planning Year 2035 MDD with 24Hr EPS Minimum Pressures

Potable Water Master Plan

Maps comparing existing and proposed planning for 2035, highlighting areas of maximum velocity and proposed modifications.

Figure 6-5

Proposed Planning Year 2035 MDD with 24Hr EPS Maximum Velocity

Q 3 WTP

Ú [

Pump Stations

UT Ground Storage Tank

Elevated Storage Tank

Max Velocity

Max. Velocity

  • Less than 2 fps
  • 2 -3 fps
  • 3 -5 fps
  • 5 -10 fps
  • Greater than 10 fps

Proposed_Tank_Areas

South Tampa

New Tampa

Service Area

/ 1 inch = 17,000 feet 0 8,500 17,000 Feet UT UTUT [Ú [Ú [Ú [Ú 3Q / 1 inch = 17,000 feet 0 8,500 17,000 Feet UT [Ú Planning Year 2035 Existing System Assessment Maximum Velocity UT UT UTUT [Ú [Ú [Ú [Ú [Ú 3Q Proposed Planning Year 2035 MDD with 24Hr EPS Maximum Velocity

Logos of the City of Tampa, Florida, and Black & Veatch, with the tagline 'Building a world of difference.'

CITY OF TAMPA Potable Water Master Plan - Figure 6-6

Map comparing existing and proposed water distribution systems, highlighting water age increases in different planning years and water treatment facilities.
CITY OF TAMPA Potable Water Master Plan Figure 6-6 Proposed Planning Year 2035 Proposed System Water Age Increase. Scale: 1 inch = 17,000 feet; 0, 8,500, and 17,000 feet distance markers. Map includes Planning Year 2015 Existing System Assessment Water Age, WTP, pump stations, ground storage tank, elevated storage tank, water age increase categories (Less than 1 day, 1 -5 days, 5 -10 days, 10 -20 days, Greater than 20 days), water main diameter categories (< 12-inch, 12 -16-inch, 16 -24-inch, > 24-inch), Proposed_Tank_Areas, South Tampa, New Tampa Service Area, and Proposed Planning Year 2035 Proposed System Water Age Increase.

7.0 Asset Management Program Development

7.1 INTRODUCTION

Black & Veatch has performed an asset management maturity assessment of the City of Tampa’s Water Department (the Department) as part of the potable water distribution master plan project. The assessment is based on the requirements of the international asset management standard ISO (International Organization for Standardization) 55001:2014 Asset Management – Management System Requirements and focuses on the Department’s water operations. To undertake this assessment, the Black & Veatch team reviewed documents and information provided by City staff, and facilitated six group interviews with City staff.

The assessment included the following activities:

7.2 ISO 5500X STANDARDS

The ISO 5500X standards were published in January 2014 following several key global meetings, working groups and sub‐project team meetings involving more than 30 participating and 10 observing members in its development and based on the globally recognized standard for best practice asset management, PAS 55.

The ISO 5500X series consists of three standards:

The objective of ISO 55001 is to guide and influence the design of an organization’s asset management activities by embedding a number of key concepts and fundamental principles within a framework (referred to by ISO 55001 as a management system) for asset management. According to ISO 55001 the fundamental principles of asset management are:

Value. Assets exist to provide value to the organization and to stakeholders.

Alignment. Asset management translates the organization’s strategic objectives into asset management decisions, plans and activities.

Leadership. Leadership and commitment from all levels of management is essential for establishing and improving asset management within the organization.

Assurance. Asset management gives assurance that assets will fulfil their required purpose through effective governance.

The asset management system described by ISO 55001 consists of an organization’s asset management policy, asset management strategy, asset management objectives, asset management plan(s) and the activities, processes and organizational structures necessary for their development, implementation and continual improvement. The asset management system includes organizational structure, roles and responsibilities, standards, information management systems, processes, and resources. Figure 7‐1 below provides an outline of an asset management system.

Diagram illustrating asset management framework, featuring strategic plan, policies, management plans, life cycle activities, and performance monitoring.
Figure 7‐1: Components of an Asset Management System

7.3 ASSESSMENT APPROACH

Black & Veatch’s overall assessment approach is shown in Figure 7‐2. To undertake this assessment, the Black & Veatch team reviewed documents and information provided by City staff, which included the 2012 strategic plan (status report 2015), organization chart, and samples of reports, communications, policies, and procedures. A list of the documents provided is included in Appendix E, ISO 55001 Assessment Report. A total of seven group interviews were held with City of Tampa’s Water Department staff:

 Group 7 – Finance and Accounting

Figure 7‐2: Overview of Assessment Approach
Flowchart illustrating the process of ISO 55001 gap analysis and asset management initiatives, including document review, interviews, workshops, and an improvement roadmap.

Each of the elements of ISO 55001 was assessed based on the evidence provided by the document review and the interviews, with each element scored on a scale of 0 to 4. The scoring system is shown in Figure 7‐3 below, with a score of 3 being in compliance with the ISO 55001 requirements (following “good practice”). A score of 4 indicates that the organization’s asset management maturity is “beyond ISO 55001” requirements, where asset management practices are optimized and/or the organization is employing leading practice. To achieve full compliance with ISO 55001, an organization must score a 3 in each of the elements.

Figure 7‐3: ISO 55001 Asset Management Maturity Scale
ISO 55001 asset management maturity scale showing maturity levels 0 to 3 and beyond ISO 55001, with descriptive criteria for each level.
Maturity level 0 Maturity level 1 Maturity Level 2 Maturity Level 3 Beyond ISO 55001
The organization has not recognized the need for this requirement and/or there is no evidence of commitment to put it in place. The organization has identified the need for this requirement, and there is evidence of intent to progress it. The organization has identified the means of systematically and consistently achieving the requirements, and can demonstrate that these are being progresses with credible and resourced plans in place. The organization can demonstrate that it systematically and consistently achieves relevant requirements set out in ISO 55001. The organization can demonstrate that it is systematically and consistently optimizing its asset management practice, in line with the organization’s objectives and operating context. The organization can demonstrate that it employs the leading practices and achieves maximum value from the management of its assets, in line with the organization’s objectives and operating context.

7.4 ASSESSMENT RESULTS

Overall, the City of Tampa’s Water Department achieved an average asset management maturity score of 1.6, which is in the “Aware” zone of the maturity scale. This score is typical of a utility that has some elements of good practice asset management in place but has identified the need to improve its asset management approach. Information on individual element scores is shown in Appendix F, ISO 55001 Assessment Report. Figure 7‐4 illustrates the results of the maturity assessment.

The Department leadership has recognized the need to implement a formal asset management program, and has commenced the process with the Water Master Plan and this gap assessment. The 2012 Strategic Plan includes some goals and objectives specific to asset management, some of which have been implemented such as the Geographic Information System (GIS) conversion to ArcGIS and the recent implementation of the InfoMaster software to support the risk assessment and rehabilitation planning and budgeting for the distribution system.

The Department has a number of good foundational elements on which to build: a planning process is in place with the CIP and master plan, key performance indicators are reported to the public, training is well managed with a skills matrix to determine training needs, the Water Treatment Facility has well defined Standard Operating Procedures (SOPs) in place, and there are processes to respond to incidents. However, the Department lacks an overarching asset management framework, strategy and objectives, and asset management plans, that combined result in lower scores in a number of areas.

Having sufficient staffing levels and resources are critical for successfully implementing and maintaining a successful asset management program. The gap assessment identified that it takes significant effort to obtain additional resources and there is no formal process to determine resource needs for the Department. Support groups from other City departments need to be developed as well, and top management support is required from the Public Works and Utility Services Administrator and Mayor.

Improvement recommendations were made to close the identified gaps, and these are further developed into initiatives in the Asset Management Implementation Plan.

7.5 ASSET MANAGEMENT IMPLEMENTATION PLAN

To aid in the implementation of an asset management framework that is aligned with the ISO 55001 requirements, Black & Veatch has developed an asset management implementation plan. The Asset Management Implementation Plan consists of an action plan and schedule for implementing improvements to the City of Tampa Water Department’s approach to asset management.

The asset management initiatives consist of:

  1. Update Water Department Strategic Plan
  2. Form AM Steering Committee
  3. Develop AM Framework (including Policy, Strategy and Objectives)
  4. Develop Water Department Resourcing Plan
  1. Develop Water Department Communications Plan
  2. Develop Key Performance Indicators
  3. Data Needs Assessment
  4. Implement Data Management Processes
  5. Update Water Department Policies and SOPs
  6. Develop SOP for Incident Response, Investigation and Corrective Action
  7. Update technical specifications
  8. Implement Facilities Risk Management
  9. Emergency Response Improvements
  10. Develop Asset Management Plans
  11. Implement Utility Management System
  12. Contract Management Improvements
  13. Production CMMS Improvements
  14. Implement Cost Accounting

The action plan lists out each of the initiatives, with specific actions and recommendations, the timeframe for completion, and the priority of the action. A high‐level consideration of resources needed to implement the initiative is included, and a Department lead has been assigned to each action.

The action plan and schedule are included in the Asset Management Implementation Plan Technical Memorandum, which is included as Appendix G.

Figure 7‐4: ISO 55001 Maturity Assessment Results
Radar chart depicting the average maturity scores across various leadership and organizational factors, with scores ranging from 0 to 10.

8.0 Risk Based Pipeline Prioritization

8.1 INTRODUCTION

Black & Veatch incorporated a risk‐based prioritization approach to assign a risk score and classification to each water main within the TWD’s potable water service area. The resulting risk scores and classifications will be used to prioritize the City’s potable water main rehabilitation and replacement projects. As part of this effort, Black & Veatch also performed a data quality review and survival curve analysis, which are further described in this section.

8.2 RISK BASED PRIORITIZATION APPROACH

The City is leveraging Innovyze’s InfoMaster software to improve its risk‐based prioritization for potable water main rehabilitation and replacement projects. The risk‐based prioritization model incorporates the City’s available GIS information and selected risk factors. The risk factors include a variety of likelihood of failure (LOF) and consequence of failure (COF) criteria as listed in Table 8‐1. Black & Veatch participated in workshops with the TWD to develop and agree upon the relative importance and scoring scheme for each criterion considering level of service to customers, economics, public health, and public safety.

A scoring range of 1 to 5, where 5 is most likely to fail or has the greatest consequence of failure, was used for the LOF and COF factors to align with InfoMaster’s standard 5x5 risk matrix. A weighting factor was applied to each scoring criteria to determine the overall risk score of each individual pipe. A preliminary scoring scheme was used to accommodate the City’s CIP budget schedule. The final scoring scheme will be implemented by the City in future updates using results from the potable water system hydraulic model. Appendix H, Risked Based Prioritization Technical Memorandum, includes further details on the selected criteria.

Table 8‐1: Likelihood of Failure and Consequence of Failure Criteria

Table 8-1 summarizes the likelihood of failure (LOF) and consequence of failure (COF) criteria used in the risk-based prioritization model for potable water mains.
Category Selected Criteria Selected Criteria
Likelihood of Failure (LOF) Breaks on Individual Pipe Segments
Remaining Life
Aggressive Soil Area
Consequence of Failure (COF) Social / Health / Safety Economics
Critical Customer Impact Right-of-Way Ownership and Crossings
Population Density Water Demand
Repeatable Breaks on Individual Pipe Segments Diameter
Contaminated Soil Interconnect Location
Additional Fire Hydrants 2015 Planned Paving Projects
* Modeled Velocity/High Head Loss
* Available Fire Flow
* Service Main Replacements

* Future criteria based on availability of model data.

8.3 SURVIVAL CURVE DEVELOPMENT

Survival curves were developed for each pipe material to estimate the life expectancy for the TWD water mains. The estimated life expectancy was used to estimate the remaining life for each water main to support the risk‐based prioritization for the TWD water mains. To ensure the results from the survival curve analysis were as accurate as possible, a data quality review was performed on the material and installation dates. The 2012 AWWA Buried No Longer publication (2012 AWWA Report), which documents “historic production and use of water pipe by material”, was used as a guide to identify pipes where the material and installation data did not align with the general timeframe for use. Pipes identified outside the general timeframe for use and associated main breaks were excluded from the survival curve analysis. Appendix I, Water Main Data Quality Review and Survival Curve Development Technical Memorandum, provides further details on the data quality review and survival curve analysis.

8.3.1 Data Quality Review

Based on review of the installation date and material, Table 8‐2,

Table 8‐3, and

Table 8‐4 provide a summary of the total number of pipe segments that were identified for further review by TWD. Appendix I, Water Main Data Quality Review and Survival Curve Development Technical Memorandum, includes figures identifying the pipe segments for review.

Table 8‐2: Pipe Segments with TWD Assigned Installation Date Discrepancy

Summary of pipe segments with TWD assigned installation date discrepancy by material, including counts, lengths, and percentages of pipes identified for review relative to total pipes.
Material Pipes identified for review - pipe count Pipes identified for review - length (mi) Total pipe count Total length (mi) Percentage of pipes to be reviewed - % total count Percentage of pipes to be reviewed - % total length
Asbestos Cement 27 0.2 295 11.2 9% 2%
Cast Iron (1) (2) 1,210 20.2 33,034 930.0 4% 2%
Copper 22 0.3 116 1.2 19% 23%
Ductile Iron Pipe 669 13.9 39,562 904.8 2% 2%
Fiberglass Reinforced 1 0.2 1 0.2 100% 100%
Galvanized Pipe 6 0.1 108 1.6 6% 5%
High Density Polyethylene 35 0.8 1,868 33.8 2% 2%
Polyvinyl Chloride (1) 31 0.7 6,157 155.0 1% 0.5%
Unlined Cast Iron (1) 126 2.1 6,056 124.6 2% 2%
Total 2,127 38.5 87,197 2162.5 2% 2%
(1) Includes pipes not owned by the City of Tampa (6 pipe segments total, 1 CAS, 4 PVC, 1 UCI) (2) Includes 1 inactive pipe

Table 8‐3: Pipe Segments with Assumed Installation Date

Summary of pipe segments with assumed installation dates by material, including counts, lengths, and percentages of total system pipes identified for review.
MATERIAL PIPES IDENTIFIED FOR REVIEW TOTAL PIPE COUNT TOTAL LENGTH (MI) PERCENTAGE OF PIPES TO BE REVIEWED
PIPE COUNT (1) LENGTH (MI) % TOTAL COUNT % TOTAL LENGTH
Asbestos Cement 22 1.1 295 11.2 7% 10%
Cast Iron (1) (2) 6,523 165.7 33,034 930.0 20% 18%
Concrete Segments (Bolted) 1 0.001 2 0.001 50% 72%
Copper 20 0.1 116 1.2 17% 8%
Ductile Iron Pipe (1) (2) 6,186 126.2 39,562 904.8 16% 14%
Galvanized Pipe (1) 61 1.3 108 1.6 56% 77%
High Density Polyethylene (2) 441 7.5 1,868 33.8 24% 22%
Polyvinyl Chloride (1) (2) 259 8.4 6,157 155.0 4% 5%
Steel 1 0.1 3 0.2 33% 45%
Transite 3 0.1 3 0.1 100% 100%
Unlined Cast Iron (1) (2) 5,150 103.3 6,056 124.6 85% 83%
Total 18,667 413.9 87,204 2162.6 21% 19%

(1) Includes pipes not owned by the City of Tampa (283 pipe segments total, 8 CAS, 21 DIP, 2 GP, 28 PVC, 224 UCI)

(2) Includes inactive pipes (115 pipe segments total, 7 CAS, 79 DIP, 5 HDPE, 2 PVC, 22 UCI)

Table 8‐4: Minimal Remaining Active Pipe Segments

Minimal remaining active pipe segments by material, showing total counts and lengths for pipes identified for review.
MATERIAL PIPES IDENTIFIED FOR REVIEW
TOTAL COUNT (1) LENGTH (MI)
Clay Tile 2 0.0003
Concrete Segments (Bolted) 2 0.001
Fiberglass Reinforced 1 0.25
Polyethylene 5 0.13
Steel 3 0.17
Transite 3 0.13
Total 16 0.55

8.3.2 Data Improvement Recommendations

Black & Veatch recommends that TWD perform a detailed review to confirm and/or update the material type and/or installation date for the 23% of pipe segments that either (1) did not align with the 2012 AWWA Report timeframes, (2) are missing an installation date and an assumption was made, or (3) have a material type of clay tile, concrete segments (bolted), polyethylene, steel, and transite. Main breaks associated with any pipe identified for further review should also be reviewed for confirmation of the correct pipe and/or update of the identified break pipe material on the break record.

As part of continually improving the GIS data source used for reporting, modeling, and asset management, additional data quality reviews can be performed by TWD as described below to confirm and/or update the master data:

  1. Pipes with duplicate facility IDs: Renumber pipes with duplicate facility IDs to ensure each facility ID is unique.

  2. Pipe assigned to Main Breaks

    • Each main break record within FY2000‑FY2015 was assigned to a pipe as part of the main break analysis effort performed by Black & Veatch using multiple confidence level criteria. The assigned pipe should be confirmed for all main breaks.
  3. Water mains that may be included in the wLateral feature class

    • Water mains that are included in the wLateral feature class should be removed and added to the wMains feature class.
  4. Service lines that may be included in the wMains feature class

    • Service lines that are included in the wMains feature class should be removed and added to the wLaterals feature class.
  5. Splits in pipes where a node (valve, hydrant, or fitting) is not located

    • Determine if a valve, hydrant, or fitting is missing at two adjoining pipes or if the pipe segments should be merged as a single pipe.
  6. Pipes not split at a node (valve, hydrant, or fitting)

    • Determine if a pipe should be split at an existing node or if the pipe is a duplicate and should be removed.
  7. Multiple pipes in the same location

    • Review if overlapping pipe(s) should be inactive
    • Review for pipe duplication (individual pipe segments between nodes may have been added and the original pipe segment may have not been deleted)

8.3.3 Survival Curve Analysis

The survival curve analysis follows the Kaplan‑Meier methodology and incorporates the total observed population of water mains for each pipe material, the age of each water main as of year 2015, and the main break occurrences between years 2000 and 2015 to develop a hazard curve and survival curve. The average life expectancies are based on the 50th percentile of the Weibull estimated survival probability. The average life expectancies for pipe materials that did not have sufficient data to support the survival curve analysis are based on the 2012 AWWA Report or

assumed, as applicable. Table 8‐5 provides the estimated life expectancy results for each pipe material.

Table 8‐5: Average Life Expectancy

Average life expectancy in years for each pipe material, comparing Weibull survival probability estimates, AWWA 2012 Report values, and the selected values used in this study.
MATERIAL WEIBULL SURVIVAL PROBABILITY (1) AWWA 2012 REPORT (2) SELECTED
Asbestos Cement 46 90 46
Cast Iron 86 110 86
Copper 40 Not Available 40
Concrete Segments (Bolted) Not Available 105 (2) 105
Clay Tile (4) Not Available Not Available 100
Ductile Iron 88 80 88
Fiberglass Reinforced Not Available 55 (2) 77 (3)
Galvanized Pipe 101 Not Available 101
High Density Polyethylene 78 Not Available 78
Polyethylene Not Available 55 (2) 77 (3)
Polyvinyl Chloride 77 55 77
Steel Not Available 70 70
Transite Not Available 90 (2) 46 (3)
Unlined Cast Iron 80 Not Available 80

(1) Average life expectancies are based on the “Modified” pipe population for each pipe material and are estimated at the 50th percentile of the Weibull survival probability curve.

(2) The 2012 AWWA Report average life expectancy is assumed to be 50th percentile. The AWWA report does not include life expectancy for all pipe materials. The following assumptions were made to estimate the remaining life for each pipe material. Concrete Segments (Bolted) – Assumed similar to Conc & PCCP Fiberglass Reinforced – Assumed similar to PVC Polyethylene – Assumed similar to PVC Transite – Assumed similar to Asbestos

(3) Pipe materials that did not have break history were not included in the survival curve analysis. The following assumptions were made in order to estimate the remaining life for each pipe material based on the Weibull survival probability curve estimates. Fiberglass Reinforced – Assumed similar to PVC Polyethylene – Assumed similar to PVC Transite – Assumed similar to Asbestos

(4) Clay Tile was assumed to have an average life expectancy of 100 years.

8.4 RISK ANALYSIS

Each individual water main segment was analyzed and ranked based on both a calculated risk score and risk classification. The overall risk score was calculated by multiplying the total LOF score and the total COF score. The total LOF and COF scores are determined by multiplying each individual factor score by the assigned weighting and then summing, respectfully. The weightings for each LOF and COF criteria are shown in Table 8‐6.

Table 8‐6: Criteria Weightings

Criteria and preliminary scoring weightings used to determine risk classification for each water main segment.
CRITERIA PRELIMINARY SCORING WEIGHT
Likelihood of Failure
Breaks on Individual Pipe Segments 45%
Remaining Life 45%
Aggressive Soil Area 10%
Consequence of Failure
Critical Customer Impact 15%
Population Density 10%
Repeatable Breaks on Individual Pipe Segments 5%
Contaminated Soil 10%
Additional Fire Hydrants 5%
Right‐of‐Way Ownership and Crossings 10%
Water Demand 15%
Diameter 15%
Interconnect Location 10%
2015 Planned Paving Projects 5%

To determine the risk classification for each water main segment, the bi‐directional distribution risk assessment method using a 5x5 risk matrix is utilized. The risk classifications range from negligible to extreme as shown in Figure 8‐1. The risk classification for each water main segment is based on where the LOF and COF scores intersect within the matrix.

Figure 8‐1: Overall Risk Score Classification Matrix

A color-coded risk assessment matrix showing levels of consequence of failure (COF) and likelihood of failure (LOF).
Figure 8‐1: Overall Risk Score Classification Matrix

8.5 ANALYSIS RESULTS

8.5.1 Overall Risk Scoring Results

The results of the COF and LOF analysis are shown in Figure 8‐2. Water main segments not active or owned by the TWD were not included in the results. Further detail regarding the overall risk scoring results is included in Appendix H, Risked Based Prioritization Technical Memorandum.

Figure 8‐2: Bi‐Directional Risk Matrix Results
A blank gray canvas with a subtle horizontal line across the middle, creating a minimalist design.

8.5.2 Linear Asset R&R Gap Analysis Results

To support the TWD in future decision making towards water distribution rehabilitation and replacement (R&R) system planning, a gap analysis was performed based on current funding versus total and annual replacement cost needs. Valve, fire line service, hydrant, and distribution main replacement needs were included in the analysis. Table 8‐7 and Figure 8‐3 through Figure 8‐5 provide a summary of the gap analysis results. Assumptions used to support the gap analysis are provided in Appendix H, Risked Based Prioritization Technical Memorandum.

Table 8‐7: Total and Annual Replacement Costs

Table 8‐7 summarizes total counts or lengths, total replacement costs, replacement or rehabilitation schedules, and resulting annual costs for valves, fire line services, hydrants, and distribution mains.
CATEGORY TYPE TOTAL COUNT/ LENGTH (MI) TOTAL REPLACEMENT COST REPLACEMENT / REHABILITATION SCHEDULE ANNUAL COST
Valve 49,704 $904,772,541 20‐year (Replace) $45,239,000
Fire Line Services 2,571 $40,880,323 86‐year (Replace) $475,000
Hydrant 14,094 $581,096 20‐year (Rehab) $29,000
Distribution Mains 2,146 mi $3,448,968,221 Varies (Replace) ‐‐

Assumptions:

  1. Base/Fee/Rate charges assumed to increase at a rate matching inflation. All dollar values shown in 2018 dollars.
  2. Developer funded pipeline R&R rate is reduced by 50% to account for pipes being taken out of service prior to the pipe being in service for its entire projected lifespan.
  3. Domestic & irrigation service replacements are included in the pipeline R&R $/ft. estimates
Line graph showing Distribution Main R&R backlog and funding from 2013 to 2018, indicating trends in replacement costs and annual requirements.
Figure 8‐3: Annual Replacement Cost (Years 2018‐ 2103) vs Current Funding Rate
Graph showing annual replacement cost (2018-2037) vs current funding rate, highlighting costs for distribution, fire hydrant assemblies, and backlog.
Figure 8‐4: Annual Replacement Cost (Years 2018 ‐ 2037) vs Current Funding Rate
Graph showing projected R&R backlog at two funding levels from 2018 to 2037, with values in millions of dollars.
Figure 8‐5: Projected R&R Backlog at Various Distribution Main Funding Levels

Note: Funding levels are based on distribution main replacement costs needed up to year 2037

8.5.3 Valve Replacement Decision Tool

Black & Veatch developed a spreadsheet tool to support the TWD in standardizing the decision‐making process for valve replacement. Two options were considered for evaluation:

Appendix H, Risked Based Prioritization Technical Memorandum provides further details on the set‐up and calculations used in the spreadsheet template. The spreadsheet tool was provided to the TWD separately in Microsoft Excel format. The cost for valve replacement has not been included in the list of CIP projects are part of this Master Plan. The TWD is investigating the true service life of the valves and methods to extend the service life.

9.0 Capital Improvement Planning

Once the recommended improvement projects were identified and preliminary implementation planning years established, Black & Veatch estimated the cost for each improvement project. Black & Veatch then adjusted the implementation date, in conjunction with the TWD through a series of workshops. The following section describes the unit costs established, the proposed capital improvement plan and the cash flow required to implement the improvements.

9.1 WATER MAIN UNIT COSTS

Black & Veatch worked with the TWD to prepare unit cost information and assumptions for the variety of types of water main improvements to be used to develop planning‐level opinions of probable project costs. The unit costs were based on the 2015 bid tab provided by the TWD on‐call contractor. Table 9‐1 summarizes the unit costs per diameter and items included in the unit cost are comprised of the following:

Table 9‐1: Water Main Unit Costs

Water main unit costs per pipe diameter, including restoration, pipe material, pipework additions, and markups.
Diameter (in) Unit Cost with Contingency ($/LF)
4 $201.00
6 $224.00
8 $238.00
12 $286.00
16 $465.00
20 $554.00
24 $794.00
30 $969.00
36 $1,169.00
42 $1,436.00
48 $1,970.00

9.2 CAPITAL IMPROVEMENT PLAN

The non‐rehabilitation and replacement (R&R) portion of the distribution system capital improvement plan through 2035 includes 55 separate improvement projects at a total project cost of $129M, including a 2.5% inflation rate beginning in 2024 outside of the short‐term CIP. Black & Veatch provided detailed cost estimate assumptions for each project to TWD in a CIP spreadsheet file. Table 9‐2 summarizes the CIP per planning year.

Table 9‐2: Capital Improvement Plan Summary

Summary of short term capital improvement projects through 2024, including CIP number, project name and description, project trigger and type, anticipated design year, and costs with inflation.
CIP # PROJECT NAME PROJECT DESCRIPTION PROJECT TRIGGER PROJECT TYPE ANTICIPATED DESIGN YEAR COSTS WITH INFLATION
Short Term Capital Improvement Projects through 2024 $65,980,530
2 DLTWTF Discharge Pressure Increase DLTWTF HSPS discharge pressure to 70 psi; slowly / incrementally Min pressures Operational / Controls 2018 $0
3 RPS controls modifications Modify the NWRPS, WTRPS and PCRPS to operate during peak demand periods rather than time of day Increased reliance on DLTWTF HSPS Operational / Controls 2018 $65,000
8 Commercial Fire Flow Study Perform an analysis of the required commercial fire flow needs be conducted and commercial fire flow corridors be identified Fire Flow Demands Study 2018 $50,000
11 West Tampa and Palma Ceia Flow Meters Install flow monitors on the effluent side of the West Tampa and Palma Ceia RPS’s and connect to the data historian Data Collection Operational / Controls 2018 $1,046,000
12 RPS Power Monitors Install power monitors on all RPS equipment and connect to the data historian Data Collection Operational / Controls 2018 $18,500
13 DLTWTF Clearwell Groundwater Level Study Collection of data related to the groundwater level on the site in anticipation of the design of a new clearwell structure DLTWTF Blending Chamber, Clearwell and HSPS Upgrade Project Capacity 2018 $50,000
14 Water Quality Model Calibration Study Collect water quality data throughout the system in order to conduct a calibration of the existing water quality model Water Quality Study 2018 $200,000
1 IB, NW and MB Tank Inlet Sleeve Valves Installation of sleeve valves with flow control functions at the inlet to the Interbay, Northwest and Morris Bridge Tanks Three Pressure Zone Configuration Capital: Operational flexibility 2019 $2,230,000
9 South Tampa Check Valves Install check valves along South Tampa Pressure Zone (along Gandy Blvd) Fire Flow Demands Resilience 2019 $957,000
4 DLTWTF Blending Chamber, Clearwell and HSPS Upgrades Demo 2.0 MG and 0.5 MG clearwells, convert 7.5 MG clearwell to blending chamber, install new 13.0 MG clearwell, demo pumps 1‐6 and install new 153 MGD HSPS Sum of the MDDs for each pressure zone greater than 140 MGD R&R and Expansion 2020 $59,500,000
16 CP003 12‐inch; 5,392 feet 16‐inch; 200 feet System Pressures Capacity 2020 $1,872,000

Mid Term Capital Improvement Projects 2025 2030

Mid Term Capital Improvement Projects 2025 2030 – project list with ID, name, description, driver, benefit category, year, and cost.
ID Project Description Driver Benefit Year Cost
6 Northeast (Nebraska) EST Installation of a new EST in the north portion of the DLTWTF DLTWTF Pressure Zone Demands greater than 130 MGD Resilience 2025 $12,273,267
15 R‐01 Hillsborough Ave WM 6,000‐ft of 12‐inch pipe along Hillsborough Ave. DLTWTF Pressure Zone Demands greater than 125 MGD Resilience 2025 $9,401,986
17 CP004 8‐inch; 3,546 feet 12‐inch; 4,219 feet System Pressures Capacity 2025 $2,651,842
19 FF0‐01 12‐inch; 2,900 feet Opportunistic Fire Flow 2025 $1,059,583
20 FF0‐02 12‐inch; 4,600 feet Opportunistic Fire Flow 2025 $1,720,452
22 FF0‐04 12‐inch; 4,650 feet Opportunistic Fire Flow 2025 $1,753,214
25 FF0‐07 12‐inch; 4,260 feet Opportunistic Fire Flow 2025 $1,588,942
26 FF0‐08 8‐inch; 800 feet Opportunistic Fire Flow 2025 $253,130
41 FF1‐06 6‐inch; 10 feet Opportunistic Fire Flow 2025 $2,194
42 FF1‐07 12‐inch; 600 feet Opportunistic Fire Flow 2025 $229,023
21 FF0‐03 12‐inch; 1,610 feet Opportunistic Fire Flow 2026 $617,162
23 FF0‐05 12‐inch; 1,200 Opportunistic Fire Flow 2027 $467,727
24 FF0‐06 16‐inch; 1 mile Opportunistic Fire Flow 2028 $3,495,922
27 FF0‐09 12‐inch; 1,850 feet Opportunistic Fire Flow 2029 $769,257
28 FF0‐10 12‐inch; 1,150 feet Opportunistic Fire Flow 2029 $477,470
29 FF0‐11 8‐inch; 800 feet Opportunistic Fire Flow 2029 $278,524
30 FF0‐12 8‐inch; 800 feet Opportunistic Fire Flow 2029 $278,524
Mid Term Capital Improvement Projects 2025 2030 subtotal $35,664,974
Long Term Capital Improvement Projects 2030 2035 – Fire Flow and related improvements with project IDs, descriptions, drivers, timing, and costs.
No. Project ID Description Driver / Condition Category Year Cost
31 FF0‐13 12‐inch; 900 feet Opportunistic Fire Flow 2029 $371,365
Long Term Capital Improvement Projects 2030 2035 $62,886,623
5 HSPS Expansion Install additional pumping capacity at the new HSPS building total new capacity = 167 MGD DLTWTF Pressure Zone Demands greater than 153 MGD Performance Criteria: Pump Capacity 2030 $4,891,280
10 Hillsborough County Interconnect Interconnect with Hillsborough County in the northwest portion of the system either directly into the distribution system or the Northwest Tank DLTWTF Pressure Zone Demands greater than 140 MGD Resilience 2030 $1,753,928
32 FF0‐14 12‐inch; 100 feet Opportunistic Fire Flow 2030 $54,365
33 FF0‐15 12‐inch; 2,800 feet Opportunistic Fire Flow 2030 $1,182,059
34 FF0‐16 12‐inch; 450 feet Opportunistic Fire Flow 2030 $190,216
35 FF1‐00 8‐inch; 310 feet Opportunistic Fire Flow 2030 $108,695
36 FF1‐01 16‐inch; 140 feet Opportunistic Fire Flow 2030 $96,345
37 FF1‐02 16‐inch; 10 feet Opportunistic Fire Flow 2030 $11,113
43 FF2‐00
8‐inch; 500 feet
12‐inch; 650 feet
Opportunistic Fire Flow 2031 $459,343
44 FF2‐01 8‐inch; 2,500 feet Opportunistic Fire Flow 2031 $904,767
45 FF2‐02 8‐inch; 1,300 feet Opportunistic Fire Flow 2031 $473,263
46 FF2‐03 8‐inch; 300 feet Opportunistic Fire Flow 2031 $108,822
47 FF2‐04 8‐inch; 50 feet Opportunistic Fire Flow 2031 $22,789
48 FF2‐05 6‐inch; 2,200 feet Opportunistic Fire Flow 2032 $770,092
49 FF2‐06 12‐inch; 20 feet Opportunistic Fire Flow 2032 $14,261
50 FF2‐07 8‐inch; 20 feet Opportunistic Fire Flow 2032 $12,963
51 FF2‐08 8‐inch; 2,300 feet Opportunistic Fire Flow 2032 $855,658
52 FF2‐09 8‐inch; 1,350 feet Opportunistic Fire Flow 2032 $499,134
53 FF2‐10 6‐inch; 700 feet Opportunistic Fire Flow 2033 $248,395
Project list with IDs, locations, descriptions, drivers, planning years, and estimated costs.
Project No. Project ID Project Description Project Driver Planning Year Estimated Cost
7 Southeast (Broadway) EST Installation of a new EST in the south portion of the DLTWTF DLTWTF Pressure Zone Demands greater than 135 MGD 2035 $9,918,429
18 CP005 12‐inch; 2 miles System Pressures 2035 $5,369,060
54 BBD Parallel Water Main 12‐inch; 1,650 feet
30‐inch; 14,106 feet
36‐inch; 8,949 feet
When the MB TBW Interconnect is used for normal daily water supply 2035 $33,598,658

9.3 CASH FLOW

The CIP for distribution system improvements involves a number of significant capital cost projects through the 2035 planning horizon. In addition, there are a number of distribution system pipeline R&R projects that have been prioritized for implementation throughout the planning horizon and beyond. Figure 9‐1 illustrates the required cash flow over the planning horizon assuming all design costs are encumbered at the beginning of the design period and all construction costs are encumbered at the beginning of the construction period. This method of encumbering costs increases the variable appearance of the graphs. Figure 9‐2 provides the same information but at a different scale, and without the R&R costs, to more clearly show the breakdown of the costs for each year.

Figure 9‐1: 2018 – 2035 Cash Flow
Bar graph showing various funding categories from 2015 to 2040, highlighting study, resilience, capital criteria, fire flow, and rehabilitation.
Figure 9‐2: 2018 – 2035 Cash Flow ($30M Scale) without R&R
Bar graph depicting financial data from 2015 to 2040, showing various categories like resilience, capital criteria, and fire flow.