02 Design Analysis_Redacted - GLEN 12-1027.pdf

DESIGN ANALYSIS REPORT

REPAIR BY REPLACING DOMESTIC WATER

PUMPS AND PIPING, BUILDING 420

Final Submittal

Schriever Air Force Base

GLEN 12-1027

15 February 2019

ARCHITECTURE ° ENGINEERING CONSTRUCTION °

REPAIR BY REPLACING DOMESTIC WATER PUMPS AND PIPING, SAFB

SAFB Project Number: GLEN 12-1027

Contract Number: FA7000-16-D-0008

Delivery Order: FA700017F0506

AECOM Project Number: 60582516

Prepared For: Prepared By:

Schriever Air Force Base

AECOM

Mr. Casey Waughtel 2315 Briargate Parkway, Suite 150 SAFB PM, 50 CES/CENMP Colorado Springs, CO. 80920

(719) 567-4687 (719) 531-0001 i

AUTHORIZATION

AECOM Group, Inc. (AECOM) was retained by the Shriever Air Force Base’s 50 CONS/LGCA to complete a Design Analysis Report under Contract No. FA7000-16-D-0008. The project is to provide pump and piping replacement for Building 420 potable water pump station.

PROJECT PERSONNEL

Schriever Air Force Base:

• Contract Administrator Kenneth Helgeson

• 50 CES Project Engineer Andrew Keener

AECOM Group:

• Project Manager Frank Tyboroski, P.E.

• Professional in Charge (PIC) Nathan Walker, P.E.

• Process/ Mechanical Lead Nathan Walker, P.E.

• Instrumentation and Controls/ Electrical Lead Kevin Sparrow, P.E.

• Fire Protection Engineer Jennifer Walker, PE

• CAD Design Jim Healy

• Independent Technical Review

Scott Cole, P.E.

Engineer of Record Electrical Engineer Fire Protection Engineer

TABLE OF CONTENTS

ii

SUMMARY:

SITE LOCATION:

1. CRITERIA:

4. ANALYSIS BY DISCIPLINE:

4.1. PROCESS/ MECHANICAL ENGINEERING:

4.1.1. EXISTING SYSTEM ASSESSMENT:

4.1.2. IDENTIFIED IMPROVEMENTS:

4.1.3. CALCULATIONS

4.1.4. PRODUCT LITERATURE:

4.2. ELECTRICAL ENGINEERING:

4.2.1. CONFORM TO SAFB LIGHTING DESIGN STANDARDS:

4.2.2. POWER REQUIREMENTS:

TABLE OF CONTENTS

iii

4.2.3. ADEQUACY OF EXISTING POWER SUPPLY:

4.2.4. LIGHTING AND OUTLET LOAD:

4.2.5. GROUNDING:

4.2.6. OUTAGES REQUIRED AND OCCUPANT IMPACTS:

4.2.7. TEMPORARY POWER REQUIREMENTS:

4.2.8. MATERIALS AND METHODS:

4.2.9. LOADS FOR SPECIAL EQUIPMENT:

4.2.10. STATEMENT OF STANDARDS SUCH AS VOLTAGE DROP, LIGHTING:

4.2.11. ELECTRONICS SYSTEMS:

4.2.12. CORROSION CONTROL/CATHODIC PROTECTION:

4.2.13. MAINTAINABiLITY OF SYSTEMS AND EQUIPMENT:

4.2.14. FAULT CALCULATIONS:

4.2.15. LIGHTNING PROTECTION:

4.2.16. POWER QUALITY:

4.2.17. LEED CREDITS THAT ARE TO BE ACHIEVED:

4.2.18. COORDINATION WITH OTHER DISCIPLINES:

4.3. FIRE PROTECTION ENGINEERING:

4.3.1. CONFORM TO NFPA 20 and UFC:

4.4. ENVIRONMENTAL ENGINEERING:

4.4.1. LEAD-BASED PAINT SURVEY AND ANALYSIS:

4.4.2. ASBESTOS SURVEY AND ANALYSIS:

5. SPECIFICATIONS

APPENDIX D - CALCULATIONS ............................................................................................................ D

APPENDIX E – PRODUCT CUT SHEETS ................................................................................................ E

APPENDIX G – SPECIFICATIONS .......................................................................................................... G

SUMMARY

SITE LOCATION:

Building 420 is located as indicated in Figure 1.

Figure 1, Site Location Aerial Photo

SECTIONONE Criteria

1. CRITERIA:

The following codes were used to generate the design criteria, construction drawings, and the specifications used for this project:

Structural Design, Drawings, & Design Analysis Report:

• Unified Facilities Criteria (UFC):

o 1-200-01 DoD Building Code (General Building Requirements) o 3-201-01 Civil Engineering o 3-230-01 Water Storage, Distribution and Transmission o 3-230-02 Operation and Maintenance Water Systems o 3-430-09 Exterior Mechanical Utility Distribution o 3-501-01 Electrical Engineering o 3-530-01 Interior and Exterior Lighting Systems and Controls o 3-550-01 Exterior Electrical Power Distribution o 3-600-01 Fire Protection Engineering for Facilities, 8 August 2016, Change 2, 25

March 2018

• The Schriever AFB Engineering Design Guide, revised March, 2016.

• The Schriever AFB Facility Excellence Plan (FEP), dated February, 2010.

• International Building Code (IBC) latest edition and modifications as provided in UFC 1- 200-01, Design: General Building Requirements (www.wbdg.org/ccb/DOD/ufc_1_200_01.pdf)

• Pikes Peak Regional Building Code, 2011 Edition

• ASCE 7-10

• The 2015 edition of the International Mechanical Code (IMC) (as adopted by the Colorado State Buildings Program as follows: Chapters 2-15 and Appendix A)

• The 2015 edition of the International Energy Conservation Code (IECC) (as adopted by the Colorado State Buildings Program)

• The 2017 edition of the National Electrical Code (NEC) (National Fire Protection Association Standard 70) (as adopted by the Colorado State Electrical Board)

• The 2015 edition of the International Plumbing Code (IPC) (as adopted by the Colorado Examining Board of Plumbers as follows: Chapter 1 Section 101.2,102, 105, 107, Chapters 2-13 and Appendices B, D, E, F and G)

• The National Fire Protection Association Standards (NFPA) (as adopted by the Department of Public Safety/Division of Fire Prevention and Control as follows with editions shown in parentheses:

NFPA-1 (2006), 11 (2005), 12 (2005), 12A (2004), 13 (2002), 13D (2002), 13R (2002), 14 (2003), 15 (2001), 16 (2003), 17 (2002), 17A (2002), 20 (2003), 22 (2003), 24 (2002), 25 (2002), 72 (2002), 409 (2004), 423 (2004), 750 (2003) and 2001 (2004))

• NFPA 101 Life Safety Code (Latest Edition)

• American Water Works Association (AWWA) – all applicable standards

SECTIONONE Criteria

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SECTIONFOUR Analysis by Discipline

4. ANALYSIS BY DISCIPLINE:

4.1. PROCESS/ MECHANICAL ENGINEERING:

4.1.1. EXISTING SYSTEM ASSESSMENT:

Building 420 houses the domestic water pump system for SAFB. This facility is located inside the Restricted Area (RA).

There are currently two American Marsh domestic water pumps in service in Building 420. These pumps run on variable frequency drives (VFD), and are rated for 1,500 gpm at 90 psi. They are powered by 125 horsepower (HP) electric motors.

There is room for one additional domestic water supply standby pump which can be added for redundancy. The pumps are set at a pre-set pressure of approximately 84 psi. These domestic water pumps are oversized for the wide range of flows at SAFB.

Night time flows are below 100 gpm. Even with the VFD’s, these low flows operate substantially outside the recommended range for these pumps.

There are also three fire pumps housed in Building 420. Two of the fire pumps are 125 HP electric fire pumps, each rated for 1,000 gpm at 125 psi. The third fire pump is a 2012 diesel driven single stage fire pump rated for 1,500 gpm at 125 psi. The third diesel fire pump provides approximately 24 hours of backup water at full engine power. Table 1 summarizes the existing pump system.

4.1.2. IDENTIFIED IMPROVEMENTS:

Instead of having two large domestic pumps, a combination of small and medium domestic pumps operating on VFDs would cover a wider flow range. During normal operation, one to three pumps would cover a range of flow between about 100 gpm and 600 gpm. The MDD plus fire flow demand would be met with three medium pumps running in parallel. To provide a reliable water supply, a fourth identical medium pump can be installed as a standby pump or the existing diesel fire pump could be kept as a backup for firm capacity. Since the diesel fire pump is new as of 2012, this pump could remain in service as is. Table 1 lists the major pump and VFD equipment. The fourth Medium Pump is in included in the design since it was listed in the statement of work, but this pump is not required for firm capacity if the existing diesel fire pump remains in service.

The proposed pump configuration would provide SAFB more operational flexibility, and the pumps would operate at much higher efficiencies than the existing pumping equipment.

Additionally, all steel piping infrastructure in and around Building 420 requires replacement, with pipes resized for the flows from the new pumps, and equipped with new valves and fittings to provide simplicity of maintenance and repairs.

Table 1: Major Equipment List

Equipment Description Equipment ID Equipment Purpose

(2) Small Pumps with VFDs SP-1, SP-2 Covers ADD flow condition

(1) Running, (1) Standby

(4) Medium Pumps with VFDs MP-1, MP-2, MP-3, MP-4 Cover MDD, PHD, and MDD+FF conditions

(1-3) Running, (1) Standby

(1) Jockey Pump FP-4 Low flow conditions

(1) Running

(2) Existing Circulation Pumps P-WS4, P-WS3 Tank Water Recirculation

(1) Existing Diesel Fire Pump FP-WS3 Fire Flow backup

4.1.3. CALCULATIONS

HYDRAULIC ANALYSIS:

The water distribution system must be able to supply water demands with sufficient service pressure and water quality over a range of fluctuating conditions that vary throughout the day and over the course of a year. AECOM created a hydraulic model using AFT Fathom software to verify and complete the final hydraulics. This included calculating the required head and pump turndown for each of the three pump types (Medium Pump, Small Pump, and Jockey Pump) at the required flow conditions, taking into account the frictional losses in the pipe system due to the recommended change in pipe sizes within the building. AECOM targeted a distribution pressure of 84 psi for normal water flow and 110 psi for fire flow.

Per the report “Potable Water System Analysis and Modeling, URS 2016”, the required flow demands for the SAFB potable water supply pumps are as follows:

Table 2: Demand Conditions

Demand Condition Total Demand (gpm)

Nightly flows < 40 gpm

Average Daily Demand (ADD) 156 gpm

Maximum Day Demand (MDD) 381 gpm

Peak Hour Demand (PHD) 225 gpm

Fire Flow Demand 1,500 gpm

Firm Pumping Capacity Required (MDD + Fire Flow)

1881 gpm

Where the terms used are defined as follows:

• Average Day Demand (ADD) is the total water usage over the course of the year divided by the total number of days in the year.

• Maximum Day Demand (MDD) is the maximum volume of water used in a single day during the year. For SAFB, this likely occurs on a day in the month of July.

• Peak Hour Demand (PHD) is the maximum volume of water used in any one hour throughout the year.

Based on these flow requirements, the following operating points were determined.

Table 3: Medium Pump Operating Points

Medium Pump Flow (gpm) Head (ft) Design Point 381 198 Min Flow 200 197 Max Flow 750 261

Minimum turndown (% of full speed) 83.2% NPSHR (ft) < 21.7

Table 4: Small Pump Operating Points

Small Pump Flow (gpm) Head (ft) Design Point 156 198 Min Flow 40 197 Max Flow 200 198

Minimum turndown (% of full speed) 94.8% NPSHR (ft) < 22.0

Table 5: Jockey Pump Operating Points

Jockey Pump Flow (gpm) Head (ft) Design Point 40 197.9 NPSHR (ft) < 22.3

The figure below shows the representative pump curves for the various operating points running at full speed and reduced speed, calculated using affinity laws. Actual pump curves will depend on the final pumps selected.

Figure 1: Representative Pump Curves

MATERIAL SELECTION:

Piping material is selected to be AWWA C200 steel pipe. Piping 4” and greater will be cement-mortar-lined per AWWA C205 with lining thickness as specified in the table below.

Table 6: Cement-mortar-lining thickness per AWWA C205

Nominal Pipe Size (in.) Lining Thickness (in.) Tolerance (in.)

4-10 1/2 -1/16, +1/8

11-23 5/16 -1/16, +1/8

Piping less than 4” will be galvanized steel. AECOM calculated the required minimum wall thickness of the pipe by pipe size per AWWA M11 guidelines (see Appendix D for calculation results). If the calculated required wall thickness is less than industry standards, than the minimum wall thickness per typical vendor standards may be used.

For external protection of underground pipe outside of Building 420, both tape wrap coating (in accordance with AWWA standard C214) or epoxy coating (in accordance with AWWA standard C210, C213, C215, C218 or C222) are acceptable. Indoor pipe shall be painted per industry standards.

NPSHA CONSIDERATIONS:

The potable water storage for diurnal equalization, fire flows, and emergency supply is provided by two tanks (Tk-1 and Tk-2). The two tanks are identical and located adjacent to the booster pumping station in Building 420. These identical, below grade, concrete, square storage tanks are located northwest of Building 420. Per Potable Water System Analysis and Modeling, URS 2016, the maximum water level is 23 feet and the normal minimum water level in the tanks is 18 feet. The water level in the tanks is controlled by level sensors. For conservatism, the NPSHA calculation of the pumps within AFT Fathom assumes that the tanks will need to be pumped all of the way down in the event of a fire, and that no tank level will be available.

LINE SIZING ANALYSIS:

A line sizing calculation was performed to determine the appropriate line sizes for the pump station’s new pumps. See Appendix D for calculation results.

COMBINATION AIR/ VACUUM VALVE SIZING ANALYSIS:

A Combination Air/ Vacuum Valve (CAV) is required on the discharge side of each of the pumps to protect against vacuum conditions from occurring during potential pump trips, as well as to release air from typical pump filling and draining operations. A CAV will also be installed at the highpoint of the piping to automatically release entrained air. CAVs are placed at high points to exhaust large volumes of air during pump start-up and pipeline filling. These valves will also admit large volumes of air into the pipeline to protect against internal vacuum conditions during pipeline draining and other conditions. CAVs combine the function of both air/vacuum and air release valves. CAV valves were sized per AWWA M51. A 2-inch CAV with a 1/16-inch orifice is required for the FP-3 fire flows, and a 1.5-inch CAV with a 1/16-inch orifice is required for the medium pumps.

PRESSURE RELEIF VALVE (PRV) CALCULATION:

The maximum recommended discharge pressure from Building 420 is 110 psi to prevent exceeding the pressure rating of Schedule 40 PVC pipe that is present within the system. The distribution system mainly consists of PVC Schedule 40 pipes with sizes that range from 6-inch to 12-inch. The pressure rating of the 12-inch Schedule 40 PVC pipe is 130 psi at 73 deg F. Since the pressure rating of the pipe increases as the pipe diameter decreases, pipe sizes smaller than 12-inch in diameter will have a pressure rating higher than 130 psi. The selected pumps will likely have a dead head pressure of greater than 130 psig (per preliminary vendor pump curves), therefore a PRV will be installed on the distribution water header to protect from over-pressuring the downstream piping. The PCV-01 and PCV-02 will also serve this function, however overpressure analysis requires that these are assumed to fail. A preliminary PSV sizing calculation in accordance with API 520/521 has determined that PRV with a 2.5 sq in area orifice is required, however the PRV size will need to be confirmed by the manufacturer to certify the valve capacity. Pump Control Valve

(PCV) PCV-01 and PCV-02 are recommended to be set at 115 psig. The recommended PRV set pressure is 120 psig.

4.1.4. PRODUCT LITERATURE:

Several pump vendors were contacted to assist with pump selection. Preliminary vendor provided pump cut sheets are provided in Appendix E.

4.2. ELECTRICAL ENGINEERING:

4.2.1. CONFORM TO SAFB LIGHTING DESIGN STANDARDS:

No lighting changes are within the scope of this project.

4.2.2. POWER REQUIREMENTS:

The power requirements for the proposed pump replacements are a net reduction of 75 horsepower. All building loads besides pump motors are to remain. Therefore, the total change in connected load is a reduction of approximately 70 kVA.

4.2.3. ADEQUACY OF EXISTING POWER SUPPLY:

The power supply and power distribution equipment are assumed, at this time, to be adequate for the replacement of pumps. Assuming that the existing equipment is adequately sized for the existing loads, the reduction in loads will be within the existing equipment capacity.

4.2.4. LIGHTING AND OUTLET LOAD:

No new lighting and outlet load is within the scope of this project.

4.2.5. GROUNDING:

New equipment grounding will be established at each new motor controller that is exterior to Motor Control Centers (MCCs). New equipment installed inside of MCCs will be connected to internal MCC grounding bus.

4.2.6. OUTAGES REQUIRED AND OCCUPANT IMPACTS:

The electrical work will require some downtime to change over from existing pumping to new pumping. The phasing described above in Section 2.3 will minimize the duration of outages, but will increase the number of outages.

4.2.7. TEMPORARY POWER REQUIREMENTS:

Temporary power is not anticipated to be required for this effort.

4.2.8. MATERIALS AND METHODS:

All work performed under this project will be covered under the standard specification, Section 26 00 00.00 20 Basic Electrical Materials and Methods.

4.2.9. LOADS FOR SPECIAL EQUIPMENT:

No special equipment is associated with this project.

4.2.10. STATEMENT OF STANDARDS SUCH AS VOLTAGE DROP, LIGHTING:

All electrical design will meet the requirements of the NEC or the local Authority Having Jurisdiction. There are no unique impacts associated with the electrical work not covered by the previously mentioned Code or local modifications to that Code.

4.2.11. ELECTRONICS SYSTEMS:

Control wiring information between the new pump VFDs and the ATCC panel is provided for the Base’s use in integrating the VFDs into the ATCC system.

Integration by the Base to consist of confirmation, and addition, if necessary, of available I/O counts and types required for the VFDs and any programming changes required to the ATCC system to perform the pump controls as described in the pump control sequence in the drawings.

4.2.12. CORROSION CONTROL/CATHODIC PROTECTION:

Cathodic protection is included for buried steel pipe outside of Building 420. The system uses three 9 lb high potential magnesium sacrificial anodes, two north of the building and one to the south. Each side of the building includes a common cathodic test station for the buried steel pipe exiting that side of the building.

4.2.13. MAINTAINABILITY OF SYSTEMS AND EQUIPMENT:

The new VFDs will have lockable disconnects (feeder breakers) at the power distribution equipment and lockable local disconnects on the VFD enclosure to provide isolation for maintenance. Furthermore, the control circuits will be isolated from the power circuits within the VFD to provide a safer working environment for controls commissioning, testing, and maintenance.

4.2.14. FAULT CALCULATIONS:

MCC work for this project will be new feeder breaker units (buckets) or new motor control units (units) within existing MCC sections. No new distribution equipment is being added; therefore, fault calculations are not applicable to this project.

4.2.15. LIGHTNING PROTECTION:

Not Applicable.

4.2.16. POWER QUALITY:

The VFDs to be provided for motor control will be low-harmonic drives, either via 18-pulse transformer or active-front-end technology.

4.2.17. LEED CREDITS THAT ARE TO BE ACHIEVED:

Not Applicable.

4.2.18. COORDINATION WITH OTHER DISCIPLINES:

Electrical connections to piping and pumping equipment will be coordinated with Process Mechanical. If applicable, seismic requirements will be coordinated with Structural. No other coordination is anticipated at this time.

4.3. FIRE PROTECTION ENGINEERING:

4.3.1. CONFORM TO NFPA 20 AND UFC:

NFPA 20 Standard for Installation of Stationary Pumps for Fire Protection is not applicable to the domestic pumps in Building 420. In accordance with explanatory material contained in NFPA 20 Article A.4.7.1, the domestic pumps in this pump station are not classified as fire pumps. Furthermore, not being classified as fire pumps, the article states that domestic pumps are not expected to meet the requirements of the NFPA 20 standard regarding fire pumps.

The existing fire pump is not being modified and is outside the scope of this project.

As such UFC 3-600-01 does not apply to this project and it does not require review by a fire protection engineer.

4.4. ENVIRONMENTAL ENGINEERING:

4.4.1. LEAD-BASED PAINT SURVEY AND ANALYSIS:

Not included in scope, to be completed by the contractor.

4.4.2. ASBESTOS SURVEY AND ANALYSIS:

Not included in scope, to be completed by the contractor.

SECTIONFIVE Specifications

5. SPECIFICATIONS

The unedited UFGS specifications that AECOM anticipates including in the final design package are attached in Appendix G as well as listed below in Table 7. Future submittals will include the edited version of these specifications specific to the project. Note that the closest specification for the pumps and pump motors was vertical turbine pumps and vertical turbine motors, respectively. These specifications are placeholders until it is determined if there is a replacement specification, or the specification needs to be modified. AECOM will provide these specifications in UFGS format, as both Word and PDF files to SAFB.

Table 7: Specification List

UFGS Specification Number Specification Title

00 01 15 List of Drawings

00 22 13.00 20 Supplementary Instructions to Offerers

01 11 00 Summary of Work

01 14 00 Work Restrictions

01 20 00.00 20 Price and Payment Procedures

01 30 00 Administrative Requirements

01 32 01.00 10 Project Schedule

01 33 00 Submittal Procedures

01 35 26 Governmental Safety Requirements

01 42 00 Sources for Reference Publications

01 45 00.00 10 Quality Control

01 45 35 Special Inspections

01 50 00 Temporary Construction Facilities and Controls

01 57 19 Temporary Environmental Controls

01 58 00 Project Identification

01 74 19 Construction and Demolition Waste Management

01 78 00 Closeout Submittals

01 78 23 Operation and Maintenance Data

01 91 00.15 Total Building Commissioning

02 41 00 Demolition and Deconstruction

03 11 13.00 10 Structural Cast-In-Place Concrete Forming

03 15 00.00 10 Concrete Accessories

03 20 00.00 10 Concrete Reinforcing

03 30 00 Cast-In-Place Concrete

SECTIONFIVE Specifications

UFGS Specification Number Specification Title

03 30 53 Miscellaneous Cast-In-Place Concrete

03 35 00.00 10 Concrete Finishing

03 39 00.00 10 Concrete Curing

09 06 00 Schedules for Finishes

09 97 13.00 40 Steel Coatings

26 00 00.00 20 Basic Electrical Materials and Methods

26 05 00.00 40 Common Work Results for Electrical

26 05 19.10 10 Insulated Wire and Cable

26 05 71.00 40 Low Voltage Overcurrent Protective Devices

26 29 01.00 10 Electric Motors, 3-Phase Vertical Induction Type

26 29 23 Variable Frequency Drive Systems Under 600 Volts

26 42 14.00 10 Cathodic Protection System (Sacrificial Anode)

31 00 00 Earthwork

31 11 00 Clearing and Grubbing

32 92 19 Seeding

32 92 23 Sodding

33 11 00 Water Utility Distribution Piping

33 12 34 Magnetic Flowmeters

33 33 00 Horizontal Centrifugal Pumps

40 05 13 Pipelines, Liquid Process Piping

40 95 00 Process Control

SECTIONSIX Construction Cost Estimate

SECTIONSEVEN Limitations

APPENDICES

D

APPENDIX D - CALCULATIONS

Filling Rate 1500 gpm Differential Pressure 2 psi Air flow 228 SCFM Large Orifice Size 2 inches

Draining Rate 1500 gpm Air flow 201 SCFM Large Orifice Size 2 inches

Percent Entrained Air 2% Flow 1500 gpm Entrained Air 30 gpm Entrained Air 4.0 SCFM Design Pressure 110 psi Small Orifice Size 1/16 inches

Pipe Filling

Pipe Draining

Air Release

Shriever Air Force Base Potable Water Project

CAV Sizing Calculation

Fathom 8 (Model) 9/25/2018 rebekah.adams

AFT Fathom Model

General

Title: AFT Fathom Model

Input File: M:\DCS\Projects\BDL\60582516_B420_Pump\400_Technical\432_Process\Hydraulics - Fathom Models\SAFB Model 9-24-18 v5.fth

Scenario: Base Scenario/MP Max Flow

Number Of Pipes= 28

Number Of Junctions= 23

Pressure/Head Tolerance= 0.0001 relative change

Flow Rate Tolerance= 0.0001 relative change

Temperature Tolerance= 0.0001 relative change Flow Relaxation= (Automatic)

Pressure Relaxation= (Automatic)

Constant Fluid Property Model

Fluid Database: AFT Standard

Fluid: Water at 1 atm Max Fluid Temperature Data= 212 deg. F

Min Fluid Temperature Data= 32 deg. F

Temperature= 77 deg. F Density= 62.2513 lbm/ft3

Viscosity= 2.14623 lbm/hr-ft

Vapor Pressure= 0.46108 psia

Viscosity Model= Newtonian Apply laminar and non-Newtonian correction to: Pipe Fittings & Losses, Junction K factors, Junction Special Losses, Junction Polynomials

Corrections applied to the following junctions: Branch, Reservoir, Assigned Flow, Assigned Pressure, Area Change, Bend, Tee or Wye, Control Valve, Spray Discharge, Relief Valve

Ambient Pressure (constant)= 1 atm

Gravitational Acceleration= 1 g

Turbulent Flow Above Reynolds Number= 4000

Laminar Flow Below Reynolds Number= 2300

Pipes rebekah.adams

AFT Fathom Model

Pipe Name Pipe Defined

Length Length Units

Hydraulic Diameter

Hydraulic Diam. Units

Friction Data Set

Roughness Roughness Units

1 Pipe Yes 69.33 feet 12 inches Standard 0.0018 inches

2 Pipe Yes 20 feet 7.981 inches Standard 0.0018 inches

3 Pipe Yes 12 feet 12 inches Standard 0.0018 inches

4 Pipe Yes 5 feet 7.981 inches Standard 0.0018 inches

5 Pipe Yes 4 feet 12 inches Standard 0.0018 inches

6 Pipe Yes 5 feet 7.981 inches Standard 0.0018 inches

7 Pipe Yes 47.66 feet 12 inches Standard 0.0018 inches

8 Pipe Yes 3.33 feet 2.067 inches Standard 0.0018 inches

9 Pipe Yes 16 feet 12 inches Standard 0.0018 inches

10 Pipe Yes 5 feet 6.065 inches Standard 0.0018 inches

11 Pipe Yes 9.75 feet 12 inches Standard 0.0018 inches

12 Pipe Yes 5 feet 6.065 inches Standard 0.0018 inches

Pipe Name Pipe Defined

Length Length Units

Hydraulic Diameter

Hydraulic Diam. Units

Friction Data Set

Roughness Roughness Units

13 Pipe Yes 9.5 feet 12 inches Standard 0.0018 inches

14 Pipe Yes 5 feet 12 inches Standard 0.0018 inches

15 Pipe Yes 5 feet 6.065 inches Standard 0.0018 inches

16 Pipe Yes 5 feet 6.065 inches Standard 0.0018 inches

17 Pipe Yes 5 feet 6.065 inches Standard 0.0018 inches

18 Pipe Yes 5 feet 4.026 inches Standard 0.0018 inches

19 Pipe Yes 5 feet 4.026 inches Standard 0.0018 inches

20 Pipe Yes 5 feet 4.026 inches Standard 0.0018 inches

21 Pipe Yes 5 feet 10.02 inches Standard 0.0018 inches

22 Pipe Yes 10.75 feet 10.02 inches Standard 0.0018 inches

23 Pipe Yes 3.5 feet 12 inches Standard 0.0018 inches

24 Pipe Yes 17 feet 6.065 inches Standard 0.0018 inches

25 Pipe Yes 10.5 feet 12 inches Standard 0.0018 inches

26 Pipe Yes 24.75 feet 12 inches Standard 0.0018 inches

27 Pipe Yes 11.75 feet 10.02 inches Standard 0.0018 inches

28 Pipe Yes 14 feet 10.02 inches Standard 0.0018 inches rebekah.adams

AFT Fathom Model

Pipe Losses (K) Initial Flow Initial Flow Units

Junctions (Up,Down)

Geometry Material Size

1 1.423 1, 11 Cylindrical Pipe Steel - ANSI 12 inch

2 2.120219 11, 2 Cylindrical Pipe Steel - ANSI 8 inch

3 0.182 11, 12 Cylindrical Pipe Steel - ANSI 12 inch

4 2.120219 12, 3 Cylindrical Pipe Steel - ANSI 8 inch

5 0.182 12, 13 Cylindrical Pipe Steel - ANSI 12 inch

6 2.120219 13, 4 Cylindrical Pipe Steel - ANSI 8 inch

7 0.364 13, 14 Cylindrical Pipe Steel - ANSI 12 inch

8 2.15907 14, 5 Cylindrical Pipe Steel - ANSI 2 inch

9 0 14, 15 Cylindrical Pipe Steel - ANSI 12 inch

10 2.127882 15, 6 Cylindrical Pipe Steel - ANSI 6 inch

11 0 15, 16 Cylindrical Pipe Steel - ANSI 12 inch

12 2.127882 16, 7 Cylindrical Pipe Steel - ANSI 6 inch

Pipe Losses (K) Initial Flow Initial Flow Units

Junctions (Up,Down)

Geometry Material Size

13 0.2576847 16, 23 Cylindrical Pipe Steel - ANSI 12 inch

14 2.112143 23, 8 Cylindrical Pipe Steel - ANSI 12 inch

15 2.637536 2, 17 Cylindrical Pipe Steel - ANSI 6 inch

16 2.637536 3, 18 Cylindrical Pipe Steel - ANSI 6 inch

17 2.637536 4, 19 Cylindrical Pipe Steel - ANSI 6 inch

18 2.753913 5, 10 Cylindrical Pipe Steel - ANSI 4 inch

19 2.753913 6, 20 Cylindrical Pipe Steel - ANSI 4 inch

20 2.753913 7, 21 Cylindrical Pipe Steel - ANSI 4 inch

21 2.580841 8, 22 Cylindrical Pipe Steel - ANSI 10 inch

22 0.2773084 22, 21 Cylindrical Pipe Steel - ANSI 10 inch

23 0 10, 9 Cylindrical Pipe Steel - ANSI 12 inch

24 0.209545 17, 18 Cylindrical Pipe Steel - ANSI 6 inch

25 0.182 18, 19 Cylindrical Pipe Steel - ANSI 12 inch

26 0.182 19, 10 Cylindrical Pipe Steel - ANSI 12 inch

27 0.19586 21, 20 Cylindrical Pipe Steel - ANSI 10 inch

28 0.19586 20, 10 Cylindrical Pipe Steel - ANSI 10 inch rebekah.adams

AFT Fathom Model

Pipe Type Special Condition

1 STD None

2 STD (schedule 40) Closed

3 STD None

4 STD (schedule 40) Closed

5 STD None

6 STD (schedule 40) None

7 STD Closed

8 STD (schedule 40) Closed

9 STD None

10 STD (schedule 40) Closed

11 STD None

12 STD (schedule 40) Closed

Pipe Type Special Condition

13 STD None

14 STD None

15 STD (schedule 40) None

16 STD (schedule 40) None

17 STD (schedule 40) None

18 STD (schedule 40) None

19 STD (schedule 40) None

20 STD (schedule 40) None

21 STD (schedule 40) None

22 STD (schedule 40) None

23 STD None

24 STD (schedule 40) None

25 STD None

26 STD None

27 STD (schedule 40) None

28 STD (schedule 40) Closed

Pipe Detail Summary

Pipe 1 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD Inner Diameter= 12 inches rebekah.adams

AFT Fathom Model

Length= 69.33 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 1.423

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.18, Quantity= 2 Valve:

Butterfly, PO=100, K= 0.46, Quantity= 1

Gate, Wedge\Plug, PO=100, K= 0.10, Quantity= 1 Entrance/Exit:

Entrance, Sharp, K= 0.50, Quantity= 1

Pipe 2 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 8 inch STD (schedule 40) Inner Diameter= 7.981 inches

Length= 20 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 2.120219

Valve:

Gate, Wedge\Plug, PO=100, K= 0.11, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Contraction to Smaller Area, K= 0.91, Quantity= 1

Pipe 3 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD

Inner Diameter= 12 inches Length= 12 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 0.182

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.18, Quantity= 1

Pipe 4 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 8 inch STD (schedule 40) Inner Diameter= 7.981 inches

Length= 5 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 2.120219

Valve:

Gate, Wedge\Plug, PO=100, K= 0.11, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Contraction to Smaller Area, K= 0.91, Quantity= 1

Pipe 5 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD

Inner Diameter= 12 inches Length= 4 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 0.182 rebekah.adams

AFT Fathom Model

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.18, Quantity= 1

Pipe 6 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 8 inch STD (schedule 40)

Inner Diameter= 7.981 inches Length= 5 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.120219

Valve:

Gate, Wedge\Plug, PO=100, K= 0.11, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1 Area Change:

Contraction to Smaller Area, K= 0.91, Quantity= 1

Pipe 7 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD Inner Diameter= 12 inches

Length= 47.66 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 0.364

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.18, Quantity= 2

Pipe 8 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 2 inch STD (schedule 40)

Inner Diameter= 2.067 inches

Length= 3.33 feet Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.15907

Valve:

Gate, Wedge\Plug, PO=100, K= 0.15, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1 Area Change:

Contraction to Smaller Area, K= 0.91, Quantity= 1

Pipe 9 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD Inner Diameter= 12 inches

Length= 16 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 0

Pipe 10 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 6 inch STD (schedule 40) Inner Diameter= 6.065 inches

Length= 5 feet

Absolute Roughness= 0.0018 inches rebekah.adams

AFT Fathom Model

Fittings & Losses= 2.127882

Valve:

Gate, Wedge\Plug, PO=100, K= 0.12, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1 Area Change:

Contraction to Smaller Area, K= 0.91, Quantity= 1

Pipe 11 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD Inner Diameter= 12 inches

Length= 9.75 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 0

Pipe 12 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 6 inch STD (schedule 40)

Inner Diameter= 6.065 inches Length= 5 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.127882 Valve:

Gate, Wedge\Plug, PO=100, K= 0.12, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Contraction to Smaller Area, K= 0.91, Quantity= 1

Pipe 13 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe Material: Steel - ANSI 12 inch STD

Inner Diameter= 12 inches

Length= 9.5 feet Absolute Roughness= 0.0018 inches

Fittings & Losses= 0.2576847

Elbow/Bend:

Smooth Flanged, r/D=1.5, 45 deg., K= 0.13, Quantity= 2

Pipe 14 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD

Inner Diameter= 12 inches Length= 5 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.112143 Valve:

Gate, Wedge\Plug, PO=100, K= 0.10, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Contraction to Smaller Area, K= 0.91, Quantity= 1

Pipe 15 Detailed Input Data

Name: Pipe rebekah.adams

AFT Fathom Model

Geometry: Cylindrical Pipe

Material: Steel - ANSI 6 inch STD (schedule 40) Inner Diameter= 6.065 inches

Length= 5 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 2.637536

Valve:

Gate, Wedge\Plug, PO=100, K= 0.12, Quantity= 1 Check Valve:

Swing, 90 deg. seat, K= 0.75, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1 Area Change:

Expansion to Pipe Area, K= 0.67, Quantity= 1

Pipe 16 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe Material: Steel - ANSI 6 inch STD (schedule 40)

Inner Diameter= 6.065 inches

Length= 5 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 2.637536

Valve:

Gate, Wedge\Plug, PO=100, K= 0.12, Quantity= 1 Check Valve:

Swing, 90 deg. seat, K= 0.75, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Expansion to Pipe Area, K= 0.67, Quantity= 1

Pipe 17 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe Material: Steel - ANSI 6 inch STD (schedule 40)

Inner Diameter= 6.065 inches

Length= 5 feet Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.637536

Valve:

Gate, Wedge\Plug, PO=100, K= 0.12, Quantity= 1

Check Valve:

Swing, 90 deg. seat, K= 0.75, Quantity= 1 Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Expansion to Pipe Area, K= 0.67, Quantity= 1

Pipe 18 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 4 inch STD (schedule 40)

Inner Diameter= 4.026 inches Length= 5 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.753913 Valve:

Gate, Wedge\Plug, PO=100, K= 0.14, Quantity= 1

Check Valve:

rebekah.adams

AFT Fathom Model

Swing, 90 deg. seat, K= 0.85, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Expansion to Pipe Area, K= 0.67, Quantity= 1

Pipe 19 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 4 inch STD (schedule 40)

Inner Diameter= 4.026 inches

Length= 5 feet Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.753913

Valve:

Gate, Wedge\Plug, PO=100, K= 0.14, Quantity= 1

Check Valve:

Swing, 90 deg. seat, K= 0.85, Quantity= 1 Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Expansion to Pipe Area, K= 0.67, Quantity= 1

Pipe 20 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 4 inch STD (schedule 40)

Inner Diameter= 4.026 inches Length= 5 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.753913 Valve:

Gate, Wedge\Plug, PO=100, K= 0.14, Quantity= 1

Check Valve:

Swing, 90 deg. seat, K= 0.85, Quantity= 1 Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1

Area Change:

Expansion to Pipe Area, K= 0.67, Quantity= 1

Pipe 21 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 10 inch STD (schedule 40) Inner Diameter= 10.02 inches

Length= 5 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 2.580841 Valve:

Gate, Wedge\Plug, PO=100, K= 0.11, Quantity= 1

Check Valve:

Swing, 90 deg. seat, K= 0.70, Quantity= 1

Other:

Tee, Branch flow (dead run), K= 1.10, Quantity= 1 Area Change:

Expansion to Pipe Area, K= 0.67, Quantity= 1

Pipe 22 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe rebekah.adams

AFT Fathom Model

Material: Steel - ANSI 10 inch STD (schedule 40)

Inner Diameter= 10.02 inches Length= 10.75 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 0.2773084 Elbow/Bend:

Smooth Flanged, r/D=1.5, 45 deg., K= 0.14, Quantity= 2

Pipe 23 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD Inner Diameter= 12 inches

Length= 3.5 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 0

Pipe 24 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 6 inch STD (schedule 40)

Inner Diameter= 6.065 inches Length= 17 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 0.209545 Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.21, Quantity= 1

Pipe 25 Detailed Input Data

Name: Pipe

Geometry: Cylindrical Pipe Material: Steel - ANSI 12 inch STD

Inner Diameter= 12 inches

Length= 10.5 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 0.182

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.18, Quantity= 1

Pipe 26 Detailed Input Data

Name: Pipe Geometry: Cylindrical Pipe

Material: Steel - ANSI 12 inch STD

Inner Diameter= 12 inches Length= 24.75 feet

Absolute Roughness= 0.0018 inches

Fittings & Losses= 0.182

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.18, Quantity= 1

Pipe 27 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 10 inch STD (schedule 40) Inner Diameter= 10.02 inches

Length= 11.75 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 0.19586

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.20, Quantity= 1 rebekah.adams

AFT Fathom Model

Pipe 28 Detailed Input Data Name: Pipe

Geometry: Cylindrical Pipe

Material: Steel - ANSI 10 inch STD (schedule 40) Inner Diameter= 10.02 inches

Length= 14 feet

Absolute Roughness= 0.0018 inches Fittings & Losses= 0.19586

Elbow/Bend:

Smooth Flanged, r/D=1.5, 90 deg., K= 0.20, Quantity= 1

Assigned Pressure Table

Assigned Pressure Name Object Defined

Inlet Elevation

Elevation Units

Initial Pressure

9 Assigned Pressure Yes 2.666 feet 84.00

Assigned Pressure Initial Pressure Units

Database Source

Pressure Pressure Units

Pressure Type

Balance Energy

9 psig 84 psig Stagnation No

Assigned Pressure Balance Concentration

(Pipe #1) K In, K Out

(Pipe #2) K In, K Out

(Pipe #3) K In, K Out

(Pipe #4) K In, K Out

(Pipe #5) K In, K Out

9 No (P23) 0, 0

Assigned Pressure (Pipe #6) K In, K Out

(Pipe #7) K In, K Out

(Pipe #8) K In, K Out

(Pipe #9) K In, K Out

(Pipe #10) K In, K Out

(Pipe #11) K In, K Out

Assigned Pressure (Pipe #12) K In, K Out

(Pipe #13) K In, K Out

(Pipe #14) K In, K Out

(Pipe #15) K In, K Out

(Pipe #16) K In, K Out

(Pipe #17) K In, K Out

Assigned Pressure (Pipe #18) K In, K Out

(Pipe #19) K In, K Out

(Pipe #20) K In, K Out

(Pipe #21) K In, K Out

(Pipe #22) K In, K Out

(Pipe #23) K In, K Out

Assigned Pressure (Pipe #24) K In, K Out

(Pipe #25) K In, K Out

Branch Table

Branch Name Object Defined

Inlet Elevation

Elevation Units

Initial Pressure Initial Pressure Units

Database Source

10 Branch Yes 2.666 feet

11 Branch Yes 0 feet

12 Branch Yes 0 feet rebekah.adams

AFT Fathom Model

Branch Name Object Defined

Inlet Elevation

Elevation Units

Initial Pressure Initial Pressure Units

Database Source

13 Branch Yes 0 feet

14 Branch Yes 0 feet

15 Branch Yes 0 feet

16 Branch Yes 0 feet

17 Branch Yes 2.666 feet

18 Branch Yes 2.666 feet

19 Branch Yes 2.666 feet

20 Branch Yes 2.666 feet

21 Branch Yes 2.666 feet

22 Branch Yes 2.666 feet

23 Branch Yes 0 feet

Branch Special Condition

Boundary Flow (+ = in/- = out)

Boundary Flow Units

(Pipe #1) K In, K Out

(Pipe #2) K In, K Out

(Pipe #3) K In, K Out

10 None (P18) 0, 0 (P23) 0, 0 (P26) 0, 0

11 None (P1) 0, 0 (P2) 0, 0 (P3) 0, 0

12 None (P3) 0, 0 (P4) 0, 0 (P5) 0, 0

Branch Special Condition

Boundary Flow (+ = in/- = out)

Boundary Flow Units

(Pipe #1) K In, K Out

(Pipe #2) K In, K Out

(Pipe #3) K In, K Out

13 None (P5) 0, 0 (P6) 0, 0 (P7) 0, 0

14 None (P7) 0, 0 (P8) 0, 0 (P9) 0, 0

15 None (P9) 0, 0 (P10) 0, 0 (P11) 0, 0

16 None (P11) 0, 0 (P12) 0, 0 (P13) 0, 0

17 None (P15) 0, 0 (P24) 0, 0

18 None (P16) 0, 0 (P24) 0, 0 (P25) 0, 0

19 None (P17) 0, 0 (P25) 0, 0 (P26) 0, 0

20 None (P19) 0, 0 (P27) 0, 0 (P28) 0, 0

21 None (P20) 0, 0 (P22) 0, 0 (P27) 0, 0

22 None (P21) 0, 0 (P22) 0, 0

23 None (P13) 0, 0 (P14) 0, 0

Branch (Pipe #4) K In, K Out

(Pipe #5) K In, K Out

(Pipe #6) K In, K Out

(Pipe #7) K In, K Out

(Pipe #8) K In, K Out

(Pipe #9) K In, K Out

(Pipe #10) K In, K Out

10 (P28) 0, 0 rebekah.adams

AFT Fathom Model

Branch (Pipe #4) K In, K Out

(Pipe #5) K In, K Out

(Pipe #6) K In, K Out

(Pipe #7) K In, K Out

(Pipe #8) K In, K Out

(Pipe #9) K In, K Out

(Pipe #10) K In, K Out

Branch (Pipe #11) K In, K Out

(Pipe #12) K In, K Out

(Pipe #13) K In, K Out

(Pipe #14) K In, K Out

(Pipe #15) K In, K Out

(Pipe #16) K In, K Out

(Pipe #17) K In, K Out

Branch (Pipe #11) K In, K Out

(Pipe #12) K In, K Out

(Pipe #13) K In, K Out

(Pipe #14) K In, K Out

(Pipe #15) K In, K Out

(Pipe #16) K In, K Out

(Pipe #17) K In, K Out

Branch (Pipe #18) K In, K Out

(Pipe #19) K In, K Out

(Pipe #20) K In, K Out

(Pipe #21) K In, K Out

(Pipe #22) K In, K Out

(Pipe #23) K In, K Out

(Pipe #24) K In, K Out

(Pipe #25) K In, K Out rebekah.adams

AFT Fathom Model

Branch (Pipe #18) K In, K Out

(Pipe #19) K In, K Out

(Pipe #20) K In, K Out

(Pipe #21) K In, K Out

(Pipe #22) K In, K Out

(Pipe #23) K In, K Out

(Pipe #24) K In, K Out

(Pipe #25) K In, K Out

Pump Table

Pump Name Object Defined

Inlet Elevation

Elevation Units

Initial Pressure Initial Pressure Units

Database Source

2 MP-1 Yes 2.666 feet

3 MP-2 Yes 2.666 feet

4 MP-3 Yes 2.666 feet

5 JP-4 Yes 2.666 feet

6 SP-1 Yes 2.666 feet

7 SP-2 Yes 2.666 feet

8 FP-WS3 Yes 2.666 feet

Pump Special Condition

Pump Type

Design Flow Rate

Design Flow Rate Units

Current Configuration

Independent Variable

2 None Vol. Flow 750 gal/min N/A

3 None Vol. Flow 750 gal/min N/A

4 None Vol. Flow 750 gal/min N/A

5 None Vol. Flow 40 gal/min N/A

6 None Vol. Flow 200 gal/min N/A

7 None Vol. Flow 200 gal/min N/A

8 None Vol. Flow 1500 gal/min N/A rebekah.adams

AFT Fathom Model

Pump Ind. Variable Units

Dependent Variable

Dep. Variable Units

Pump Curve Constant a

Pump Curve Constant b

Pump Curve Constant c

Pump Pump Curve Constant d

Pump Curve Constant e

Runout Flow Rate

Runout Flow Rate Units

Speed Control When Exceeded Only

Pump Heat Added To Fluid

Heat Added Units

2 0 Percent

3 0 Percent

4 0 Percent

5 0 Percent

6 0 Percent

7 0 Percent

8 0 Percent

Reservoir Table

Reservoir Name Object Defined

Inlet Elevation

Elevation Units

Initial Pressure Initial Pressure Units

Database Source

1 Water Tk Yes

Reservoir Liquid Elev. Liquid Elev.

Units Surface

Pressure Surface

Pressure Units Balance Energy

Balance Concentration

1 0 feet 1 atm No No

Reservoir (Pipe #1)

K In, K Out (Pipe #2)

K In, K Out (Pipe #3)

K In, K Out (Pipe #4)

K In, K Out (Pipe #5)

K In, K Out (Pipe #6)

K In, K Out

1 (P1) 0, 0 rebekah.adams

AFT Fathom Model

Reservoir (Pipe #7)

K In, K Out (Pipe #8)

K In, K Out (Pipe #9)

K In, K Out (Pipe #10) K In, K Out

(Pipe #11) K In, K Out

(Pipe #12) K In, K Out

Reservoir (Pipe #13) K In, K Out

(Pipe #14) K In, K Out

(Pipe #15) K In, K Out

(Pipe #16) K In, K Out

(Pipe #17) K In, K Out

(Pipe #18) K In, K Out

Reservoir (Pipe #19) K In, K Out

(Pipe #20) K In, K Out

(Pipe #21) K In, K Out

(Pipe #22) K In, K Out

(Pipe #23) K In, K Out

(Pipe #24) K In, K Out

Reservoir (Pipe #25) K In, K Out

(Pipe #1) Depth

(Pipe #2) Depth

(Pipe #3) Depth

(Pipe #4) Depth

(Pipe #5) Depth

(Pipe #6) Depth

1 (P1) 0

Reservoir (Pipe #7)

Depth (Pipe #8)

Depth (Pipe #9)

Depth (Pipe #10)

Depth (Pipe #11)

Depth (Pipe #12)

Depth (Pipe #13)

Depth

Reservoir (Pipe #14)

Depth (Pipe #15)

Depth (Pipe #16)

Depth (Pipe #17)

Depth (Pipe #18)

Depth (Pipe #19)

Depth (Pipe #20)

Depth

Reservoir (Pipe #21)

Depth (Pipe #22)

Depth (Pipe #23)

Depth (Pipe #24)

Depth (Pipe #25)

Depth Pipe Depth

Units

1 feet

Fathom 8 (Workspace) 9/24/2018 rebekah.adams

AFT Fathom Model

X P28

P27

P26

P25

P24

P23

P22

P21

P20

P19

P18

P17

P16

P15

P14

P13

X P12

P11

X P10

P9

X P8

X P7

P6

P5

X P4

P3

X P2

P1

J1 Water Tk

J2

MP-1

J3

MP-2

J4

MP-3

J5

JP-4

J6

SP-1

J7

SP-2

J8

FP-WS3

J9

J10

J11

J12

J13

J14

J15

J16

J17

J18

J19

J20

J21

J22J23

Fathom 8 (Output) rebekah.adams

AFT Fathom Model

Model Reference Information

General

Title: AFT Fathom Model Analysis run on: 8/28/2018 1:12:48 PM

Application version: AFT Fathom Version 8 (2015.05.20)

Input File: M:\DCS\Projects\BDL\60582516_B420_Pump\400_Technical\432_Process\Hydraulics - Fathom Models\SAFB Model 9-24-18 v5.fth

Scenario: Base Scenario/MP Max Flow

Output File:

Execution Time= 0.50 seconds

Total Number Of Head/Pressure Iterations= 0

Total Number Of Flow Iterations= 2 Total Number Of Temperature Iterations= 0

Number Of Pipes= 28

Number Of Junctions= 23 Matrix Method= Gaussian Elimination

Pressure/Head Tolerance= 0.0001 relative change Flow Rate Tolerance= 0.0001 relative change

Temperature Tolerance= 0.0001 relative change

Flow Relaxation= (Automatic) Pressure Relaxation= (Automatic)

Constant Fluid Property Model

Fluid Database: AFT Standard Fluid: Water at 1 atm

Max Fluid Temperature Data= 212 deg. F

Min Fluid Temperature Data= 32 deg. F Temperature= 77 deg. F

Density= 62.2513 lbm/ft3

Viscosity= 2.14623 lbm/hr-ft Vapor Pressure= 0.46108 psia

Viscosity Model= Newtonian

Apply laminar and non-Newtonian correction to: Pipe Fittings & Losses, Junction K factors, Junction Special Losses, Junction Polynomials

Corrections applied to the following junctions: Branch, Reservoir, Assigned Flow, Assigned Pressure, Area Change, Bend, Tee or Wye, Control Valve, Spray Discharge, Relief Valve

Ambient Pressure (constant)= 1 atm

Gravitational Acceleration= 1 g Turbulent Flow Above Reynolds Number= 4000

Laminar Flow Below Reynolds Number= 2300

Total Inflow= 750.0 gal/min Total Outflow= 750.0 gal/min

Maximum Static Pressure is 99.55 psia at Pipe 17 Inlet

Minimum Static Pressure is 12.94 psia at Pipe 6 Outlet

Warnings

No Warnings

Pump Summary rebekah.adams

AFT Fathom Model

Jct Name Vol.

Flow (gal/min)

Mass Flow (lbm/sec) dP

(psid) dH

(feet)

Overall Efficiency (Percent)

Speed

(Percent)

Overall Power (hp)

BEP

(gal/min)

2 MP-1 0.0 0.0 No Solution No Solution N/A N/A 0.00 N/A

Jct Name Vol.

Flow (gal/min)

Mass Flow (lbm/sec) dP

(psid) dH

(feet)

Overall Efficiency (Percent)

Speed

(Percent)

Overall Power (hp)

BEP

(gal/min)

3 MP-2 0.0 0.0 No Solution No Solution N/A N/A 0.00 N/A

4 MP-3 750.0 104.0 86.92 201.1 100.0 N/A 38.02 N/A

5 JP-4 0.0 0.0 No Solution No Solution N/A N/A 0.00 N/A

6 SP-1 0.0 0.0 No Solution No Solution N/A N/A 0.00 N/A

7 SP-2 0.0 0.0 No Solution No Solution N/A N/A 0.00 N/A

8 FP-WS3 0.0 0.0 No Solution No Solution N/A N/A 0.00 N/A

Jct % of

BEP

(Percent)

NPSHA

(feet)

NPSHR

(feet)

2 N/A 227.28 N/A

Jct % of

BEP

(Percent)

NPSHA

(feet)

NPSHR

(feet)

3 N/A 227.28 N/A

4 N/A 29.23 N/A

5 N/A 227.24 N/A

6 N/A 128.16 N/A

7 N/A 129.44 N/A

8 N/A 127.96 N/A

Reservoir Summary

Jct Name Type Liq.

Height (feet)

Liq.

Elevation (feet)

Surface Pressure (psia)

Liquid Volume (feet3)

Liquid Mass (lbm)

Net Vol. Flow (gal/min)

Net Mass Flow (lbm/sec)

1 Water Tk Infinite N/A 0 14.70 N/A N/A -750.0 -104.0

Pipe Output Table rebekah.adams

AFT Fathom Model

Pipe

Name Vol.

Flow Rate (gal/min)

Velocity

(feet/sec)

P Static Max (psia)

P Static Min

(psia)

Elevation Inlet (feet)

Elevation Outlet (feet) dP Stag.

Total (psid)

1 Pipe 750.0 2.128 14.67 14.59 0.000 0.000 0.078089

X2 Pipe 0.0 0.000 14.62 14.62 0.000 2.666 1.152514

3 Pipe 750.0 2.128 14.59 14.58 0.000 0.000 0.011561

Pipe

Name Vol.

Flow Rate (gal/min)

Velocity

(feet/sec)

P Static Max (psia)

P Static Min

(psia)

Elevation Inlet (feet)

Elevation Outlet (feet) dP Stag.

Total (psid)

X4 Pipe 0.0 0.000 14.61 14.61 0.000 2.666 1.152514

5 Pipe 750.0 2.128 14.58 14.57 0.000 0.000 0.007543

6 Pipe 750.0 4.810 14.44 12.94 0.000 2.666 1.501046

X7 Pipe 0.0 0.000 14.60 14.60 0.000 0.000 0.000000

X8 Pipe 0.0 0.000 No Solution No Solution 0.000 2.666 1.152514

9 Pipe 0.0 0.000 No Solution No Solution 0.000 0.000 0.000000

X10 Pipe 0.0 0.000 No Solution No Solution 0.000 2.666 1.152514

11 Pipe 0.0 0.000 No Solution No Solution 0.000 0.000 0.000000

X12 Pipe 0.0 0.000 No Solution No Solution 0.000 2.666 1.152514

13 Pipe 0.0 0.000 No Solution No Solution 0.000 0.000 0.000000

14 Pipe 0.0 0.000 No Solution No Solution 0.000 2.666 1.152514

15 Pipe 0.0 0.000 98.72 98.72 2.666 2.666 0.000000

16 Pipe 0.0 0.000 98.72 98.72 2.666 2.666 0.000000

17 Pipe 750.0 8.329 99.55 98.25 2.666 2.666 1.304820

18 Pipe 0.0 0.000 98.70 98.70 2.666 2.666 0.000000

19 Pipe 0.0 0.000 No Solution No Solution 2.666 2.666 0.000000

20 Pipe 0.0 0.000 No Solution No Solution 2.666 2.666 0.000000

21 Pipe 0.0 0.000 No Solution No Solution 2.666 2.666 0.000000

22 Pipe 0.0 0.000 No Solution No Solution 2.666 2.666 0.000000

23 Pipe 750.0 2.128 98.67 98.67 2.666 2.666 0.001758

24 Pipe 0.0 0.000 98.72 98.72 2.666 2.666 0.000000

25 Pipe 0.0 0.000 98.72 98.72 2.666 2.666 0.000000

26 Pipe 750.0 2.128 98.69 98.67 2.666 2.666 0.017963

27 Pipe 0.0 0.000 No Solution No Solution 2.666 2.666 0.000000

X28 Pipe 0.0 0.000 98.70 98.70 2.666 2.666 0.000000 rebekah.adams

AFT Fathom Model

Pipe dP Static Total (psid) dP Gravity (psid) dH

(feet)

P Static In

(psia)

P Static Out

(psia)

P Stag. In

(psia)

P Stag. Out

(psia)

1 0.078089 0.000 0.180637 14.67 14.59 14.70 14.62

X2 1.152514 1.153 0.000000 14.62 No Solution 14.62 No Solution

3 0.011561 0.000 0.026742 14.59 14.58 14.62 14.61

Pipe dP Static Total (psid) dP Gravity (psid) dH

(feet)

P Static In

(psia)

P Static Out

(psia)

P Stag. In

(psia)

P Stag. Out

(psia)

X4 1.152514 1.153 0.000000 14.61 No Solution 14.61 No Solution

5 0.007543 0.000 0.017449 14.58 14.57 14.61 14.60

6 1.501046 1.153 0.806226 14.44 12.94 14.60 13.10

X7 0.000000 0.000 0.000000 14.60 No Solution 14.60 No Solution

X8 1.152514 1.153 0.000000 No Solution No Solution No Solution No Solution

9 0.000000 0.000 0.000000 No Solution No Solution No Solution No Solution

X10 1.152514 1.153 0.000000 No Solution No Solution No Solution No Solution

11 0.000000 0.000 0.000000 No Solution No Solution No Solution No Solution

X12 1.152514 1.153 0.000000 No Solution No Solution No Solution No Solution

13 0.000000 0.000 0.000000 No Solution No Solution No Solution No Solution

14 1.152514 1.153 0.000000 No Solution No Solution No Solution No Solution

15 0.000000 0.000 0.000000 98.72 98.72 98.72 98.72

16 0.000000 0.000 0.000000 98.72 98.72 98.72 98.72

17 1.304820 0.000 3.018316 99.