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This document is a technical calculation report for feedwater pump sizing related to a temporary boiler system for the Miami VA Medical Center HVAC System Upgrade & Expansion B44 project (VA Project Number 546-22-110, Above Group Project Number 0122008). Prepared by Geoff Chenoweth on April 29, 2026, the calculations establish the steam plant requirements for a 90 PSIG (pounds per square inch gauge) system operating at 100 PSIG with a boiler capacity of 500 HP and actual output of 16,830 PPH (pounds per hour).

The report presents two design scenarios: an 80% maximum condensate return scenario and a 0% minimum condensate return scenario. In the maximum condensate return case, the system requires softwater at 3,300 PPH (6.6 GPM), returned condensate of 12,733 PPH (26.1 GPM), and feedwater discharge of 17,335 PPH (36.4 GPM). Pump specifications include a condensate pump rated at 130 TDH (total dynamic head) with 2 HP, a 90 feedwater pump at 480 TDH with 10 HP, and a 250 feedwater pump at 820 TDH with 25 HP. In the minimum condensate return scenario, softwater requirements increase to 14,284 PPH (28.6 GPM) while condensate drops to 139 PPH (0.3 GPM), with feedwater remaining constant at 17,335 PPH. The calculations apply conservation of mass and energy equations, with feedwater temperature maintained at 227°F and steam enthalpy at 1,190 BTU/LB, supporting a deaerator operating at 5 PSIG.

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FEEDWATER PUMP SIZING (90 PSIG SYSTEM)

PLANT CALCULATIONS FOR:

MIAMI VA MEDICAL CENTER

HVAC SYSTEM UPGRADE & EXP. B44

No. Revision Date

1 4/29/2026

April 29, 2026

Prepared By: Geoff Chenoweth

Reviewed By: Geoff Chenoweth

Approved By: Geoff Chenoweth

Requested Change by VA

Calculations/Steam Plant

Project: HVAC System Upgrade & Exp. B44

VA Project Number: 546-22-110

Above Group Project Number: 0122008

Current Phase: Temporary Boiler Sizing

TITLE Page 1

FEEDWATER PUMP SIZING (90 PSIG SYSTEM)

PROJECT SUMMARY

SYSTEM FLOWS:

PPH GPM Cond. Return Rate Notes:

Softwater Required SWr 22,984 46 0% Maximum Softwater Demand

Returned Condensate COND 25,213 52 100% Maximum Condensate Return

Steam to Deaerator STEAM 4,674 --- 0% Low Pressure Steam To The Deaerator

Steam to Campus StC 25,213 --- 100% Maximum Steam to Campus

Feedwater FEED 27,658 58 0% Deaerator Discharge

Recirc Total Flow Head Motor Power

% GPM TDH HP

Condensate Pump 30 130 2

90 Feedwater Pump 40 480 10

250 Feedwater Pump 80 820 25

Feedwater Temp 227 °F

Enthalpy of Water 195 BTU/LB

Steam Operating Pressure 100 PSIG

Enthalpy of Steam 1190 BTU/LB

Boiler Capacity 33475 BTUH/HP

Boiler Rating 500 HP

Nom. Boiler Cap. @ 212°F 16738 PPH

Actual Boiler Cap. @ Pressure 16830 PPH

Qty. of Boilers Running 1

Total Capacity 16830 PPH

Calculations/Steam Plant

Project: HVAC System Upgrade & Exp. B44

VA Project Number: 546-22-110

Above Group Project Number: 0122008

SUMMARY Page 2

80 % CONDENSATE RETURN

170° F CONDENSATE

Design Condition for Condensate System

INPUT DATA:

DATA SYMBOLS VALUE UNITS SOURCE NOTES

Boiler Steam Output SO 16,830 PPH GIVEN

Continuous Blowdown Rate CBD 3% % ASSUMED

Campus Condensate Return Rate CCrr 82% % GIVEN

Average Condensate Temperature CDt 170 ºF GIVEN

Average Softwater Temperature SWt 70 ºF GIVEN

Deaerator Pressure Dap 5 PSIG KNOWN

Parasitic Steam Load PAR 2,000 PPH ASSUMED

Desuperheating Flow DeSup 0 PPH ASSUMED

EQUATIONS:

Steam to Campus StC SO - STEAM - PAR

Feedwater Flow FEED DeSup + SO + (SO*CBD)

Returned Condensate COND StC * CCrr

Conservation of Mass Equation:

Conservation of Energy Equation:

CALCULATIONS:

MASS TEMP ENTHALPY ENERGY

SYMBOL m T h mh

CONDENSATE COND 12,733 170 138 1,756,965

SOFTWATER SOFT 3,300 70 38 125,652

PUMPED CONDENSATE MU 16,032 149 117 1,882,618

STEAM STEAM 1,302 227 1,156 1,505,164

FEEDWATER FEED 17,335 227 195 3,387,782

0 -

RESULTS:

Steam to Campus StC 15,528 PPH CALCULATED

PPH GPM

Softwater Required SOFT 3,300 6.6

Returned Condensate COND 12,733 26.1

Returned to the Deaerator MU 16,032 32.7

Feedwater FEED 17,335 36.4

* - Calculated on different sheet.

Assumptions:

Deaerator vent losses not accounted for.

Deaerator Steam is assumed to be saturated.

FEEDSTEAMSOFTCOND

mmmm &&&& =++

FEEDSTEAMSOFTCOND

hmhmhmhm &&&& =++

Calculations/Steam Plant

Project: HVAC System Upgrade & Exp. B44 VA Project Number: 546-22-110

Above Group Project Number: 0122008

DA - Max Cond Return Page 3

0 % CONDENSATE RETURN

170° F CONDENSATE

Design Condition for Softwater System

INPUT DATA:

DATA SYMBOLS VALUE UNITS SOURCE NOTES

Boiler Steam Output SO 16,830 PPH GIVEN

Continuous Blowdown Rate CBD 3% % ASSUMED

Campus Condensate Return Rate CCrr 1% % GIVEN

Average Condensate Temperature CDt 170 ºF GIVEN

Average Softwater Temperature SWt 70 ºF GIVEN

Deaerator Pressure Dap 5 PSIG KNOWN

Parasitic Steam Load PAR 0 PPH ASSUMED

Desuperheating Flow DeSup 0 PPH KNOWN*

EQUATIONS:

Steam to Campus StC SO - STEAM - PAR

Feedwater Flow FEED DeSup + SO + (SO*CBD)

Returned Condensate COND StC * CCrr

Conservation of Mass Equation:

Conservation of Energy Equation:

CALCULATIONS:

MASS TEMP ENTHALPY ENERGY

SYMBOL m T h mh

CONDENSATE COND 139 170 138 19,205

SOFTWATER SOFT 14,284 70 38 2,665

PUMPED CONDENSATE MU 14,423 71 39 21,871

STEAM STEAM 2,912 227 1,156 3,365,912

FEEDWATER FEED 17,335 227 195 3,387,782

0 0

RESULTS:

Steam to Campus StC 13,918 PPH CALCULATED

PPH GPM

Softwater Required SOFT 14,284 28.6 CALCULATED

Returned Condensate COND 139 0.3 CALCULATED

Returned to the Deaerator MU 14,423 28.9 CALCULATED

Feedwater FEED 17,335 36.4 CALCULATED

* - Calculated on different sheet.

Assumptions:

Deaerator vent losses not accounted for.

Deaerator Steam is assumed to be saturated.

FEEDSTEAMSOFTCOND

mmmm &&&& =++

FEEDSTEAMSOFTCOND

hmhmhmhm &&&& =++

Calculations/Steam Plant

Project: HVAC System Upgrade & Exp. B44 VA Project Number: 546-22-110

Above Group Project Number: 0122008

DA - Min Cond Return Page 4

DA - Min Cond Return Page 5

DA - Min Cond Return Page 6

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