08pp-wet

WETSIDE DESIGNWETSIDE DESIGN

© Copyright 2008 HVAC Design Solutions 1

Essential Design Programs with Accurate Sizing Calculations help to “Streamline Your Design”

HHVAC VAC DDESIGN ESIGN SSOLUTIONSOLUTIONS ENGINEERING SOFTWAREENGINEERING SOFTWARE

“Wetside Design” from HVAC Design Solutions is a package of software programs for many of the HVAC Designer’s sizing tasks:

Hydronic System Sizing -“Optimum Sizes” Pump Head Calcs (Primary, Secondary, &

Condenser Water Pumps) Heating Water Expansion Tank Sizing Chilled Water Expansion Tank Sizing Coil Psychrometrics & Coil GPM Calcs Extensive Help Files, and “Extras”


OverviewOverview

Reduce your dependence on Reference Books, Charts, Graphs, and “Rules of Thumb”.

Eliminate many of the usual HVAC Design Tasks

Reduce common errors and mistakes Create an easy-to-follow, step-by-

step “Procedure for Wetside Design” for all projects.


““Streamline Your Design”Streamline Your Design”

Software Package contains most of the sizing calculations and procedures for typical projects


Extensive Calculation ProgramsExtensive Calculation Programs

INDEX2C.xls#'PUMP-CHW-SEC.'!F15

INDEX2H.xls#'PUMP-HHW-PRIM.'!F15

INDEX2H.xls#'PUMP-HHW-SEC.'!F15

PRIMARY PUMP HEAD CALCULATIONS - HEATING WATER

INDEX2C.xls#'EXPTANK-CHW'!B9CHILLED WATER EXPANSION TANK CALCULATIONS

SECONDARY PUMP HEAD CALCULATIONS - HEATING WATER

AIR HANDLING UNIT - PRELIM. COOLING COIL CALCS

PUMP PRESSURE DROP CALCS - COOLING WATER

CONTENTS

INDEX2W.xls#'AHU-HTG.COIL'!H6

CEILING SPACE INFORMATION REQUEST FORMHEAT/COOL LOAD DESIGN CRITERIA

AIR HANDLING UNIT - PRELIM. HEATING COIL CALCS

BASIC PROJECT INPUT SHEETBUILDING INFORMATION REQUEST LETTER #1BUILDING INFORMATION REQUEST LETTER #2

PIPE SIZING - OPTIMUM ECONOMIC SIZES - SINGLE PIPESPIPE SIZING SCHEDULE - HYDRONIC PIPE SYSTEMSPRELIMINARY PUMP HEAD CALCULATIONSVAV - REHEAT COIL LOAD CALCULATIONS

PUMP HEAD CALCULATIONS DIAGRAM HEATING WATER EXPANSION TANK CALCULATIONS

PRIMARY PUMP HEAD CALCULATIONS - CHILLED WATER

PUMP PRESSURE DROP CALCS - HEATING WATER

SECONDARY PUMP HEAD CALCULATIONS - CHILLED WATERPUMP HEAD CALCULATIONS DIAGRAM - CHILLED WATERCONDENSER WATER PUMP HEAD CALCS - COOLING TOWER

INDEX2W.xls#PIPECALC!H10

INDEX2W.xls#PIPESIZE!A13

INDEX2W.xls#'PUMP-HD.-PRELIM.'!C3

INDEX2W.xls#'VAV REHEAT'!C6

INDEX2W.xls#'AHU-COOL. COIL'!H6

INDEX2H.xls#'PUMP-DIAG.'!B2

INDEX2H.xls#INDEX!C9

JUMP TO FILE

INDEX2W.xls#INDEX!C10

Bldginfo.xls#'Bldg. Info.'!E11

Bldginfo.xls#'Bldg. Info. 2'!D11

Bldginfo.xls#'Ceiling Space'!D11

LOADCAL.XLS#'Design Criteria'!C5

INDEXP.xls

INDEXP.xls#PROJ.INFO!D2

PROJECT INFORMATION

WET SIDE DESIGN

INDEX2C.xls#INDEX!C9

INDEX2C.xls#'PUMP-CHW-PRIM.'!F15

INDEX2H.xls#'EXPTANK-HHW'!B9

INDEX2C.xls#'PUMP-DIAG.'!C2

INDEX2C.xls#'PUMP-COOL.TOWER'!F15

“Any One of these programs is worth the cost of the Entire Package!”

Quick Links to all calculation programs


HELP

BASIC PROJECT INFORMATION

PROJECT NAME :PROJECT NUMBER :PROJECT LOCATION :DATE :TYPE OF BUILDING :SUMMER OUTDOOR DESIGN DRY BULB TEMP. (DEG. F):WINTER OUTDOOR DESIGN DRY BULB TEMP. (DEG. F):INDOOR DESIGN TEMP. - SUMMER (DEG. F) :INDOOR DESIGN TEMP. - WINTER (DEG. F) :PROJECT ELEVATION (FEET) :PROJECT MANAGER :PROJECT ENGINEER :CLIENT :CLIENT CONTACT NAME:

75.0-6.0

OAKPARK OFFICE BLDG. 3134-08CHICAGO, IL05/06/08

JOHN GOREMANN

"YOUR COMPANY NAME"

OFFICE91.0

ADS ARCHITECTS

70.0670BILL REECEJIM EDMOND

Begin with Basic Project Information input

Typical Project StartupTypical Project Startup

Information automatically transfers to all programs

Design Conditions are used in many calculations

PROJECT NAME: * NORMAL PIPE SIZING BASED ON: PROJECT NUMBER: VELOCITY NOT EXCEEDING 4 FT/SEC. UP TO 2" PIPE DATE: VELOCITY NOT EXCEEDING 10 FT/SEC. FOR LARGER THAN 2" PIPE CAUTION: VELOCITY EXCEEDS 10 FT./SEC. - MAY CAUSE NOISE AND EROSION PRESSURE DROP BETWEEN 1 AND 5 FT/100 FT. CAUTION: VELOCITY IS LESS THAN 2 FT./SEC. - MAY CAUSE AIR TRAPPING 1/2" TO 3" SIZES ARE COPPER, 4" AND LARGER SIZES ARE STEEL CAUTION: EXCESSIVE PRESSURE DROP - MAY INCREASE PUMP HORSEPOWER

FROM TO

1 2 164.0 4 4.4 1.8 2 1/2 11.7 20.0 4 4.42 3 152.0 4 4.4 1.8 2 1/2 11.7 20.0 4 4.43 4 141.5 3 7.1 5.5 2 1/2 10.1 13.0 4 4.04 5 138.0 3 7.1 5.5 2 1/2 10.1 13.0 4 4.05 6 136.8 3 7.1 5.5 2 1/2 10.1 13.0 4 4.06 7 121.0 3 5.9 4.0 2 1/2 8.4 8.5 4 3.37 8 96.0 3 4.7 2.6 2 10.4 17.0 3 4.78 9 48.5 2 5.2 5.1 2 5.2 5.1 3 2.49 10 22.3 1 1/2 4.5 5.7 1 1/4 6.4 13.0 2 2.6

10 11 12.8 1 1/4 3.1 3.4 1 4.7 9.0 1 1/2 2.211 12 6.3 3/4 4.0 10.0 3/4 4.0 10.0 1 1/4 1.5

0 0.0 0.0 0 0.0 0.0 0 0.0

PIPE SECTIONNORMAL PRESS. DROP

(FT/100 FT)

LOW FIRST COST PD

(FT/100 FT)

LOW OPERATING COST VEL. (FT/SEC)

FLOW RATE (GPM)

NORMAL SIZE * (INCH)

NORMAL VELOCITY (FT/SEC)

LOW OPERATING COST SIZE

(INCH)

LOW FIRST COST SIZE

(INCH)

LOW FIRST COST VEL. (FT/SEC)

PIPE SIZING SCHEDULE - OPTIMUM ECONOMICAL SIZES TEST PROJECT #1

12/19/071444-07PRINT


Hydronic Pipe Sizing-Optimum SizesHydronic Pipe Sizing-Optimum Sizes

Warning Flags for Alternate Sizes

Alternate Pipe Sizes

Quick and Easy Input

Most “Economical” Pipe Sizes to meet Sizing Criteria (Velocity and Pressure Drop)

HELP

164 PROJECT NAME:

4.0 PROJECT NUMBER:

3 APPROX. HP: 5.4 DATE:

PIPE SIZE TOTAL PIPE LENGTH (ft.)

PRESS. DROP (ft./100 ft.)

PIPE PRESS. DROP (ft.)

FITTING OR VALVE TYPE

NO. OF FITTINGS UP TO 2"

NO. OF FITTINGS 2" TO 4"

NO. OF FITTINGS 4" to 10"

FITTING PRESS. DROP (ft)

1/2 0 4.0 0.0 ELL - 90 DEG. 12 18 0 10.3

3/4 30 4.0 1.2 ELL - 45 DEG. 0 0 0 0.0

1 0 4.0 0.0 THRU TEE 3 7 0 3.9

1 1/4 15 4.0 0.6 BRANCH TEE 1 1 0 1.1

1 1/2 25 4.0 1.0 GLOBE VALVE 0 2 0 6.6

2 25 4.0 1.0 GATE VALVE 2 0 0 0.2

2 1/2 0 3.0 0.0 ANGLE VALVE 0 0 0 0.0

3 130 3.0 3.9SWING CHECK

VALVE 0 2 0 2.3

4 62 3.0 1.9LIFT CHECK

VALVE 0 0 0 0.0

5 0 2.5 0.0CONTROL

VALVE 1 1 0 5.3

MAX. PRESSURE DROP (ft./100 ft.):

TEST PROJECT #1

1444-07

12/19/2007

PRELIMINARY PUMP HEAD CALCULATIONSPUMP CAPACITY (GPM):

MAIN PIPE SIZE (in.):

PRINT


““Preliminary” Pump Head CalcsPreliminary” Pump Head Calcs

Preliminary Pump Head Calcs, for preliminary Pump HP requirements

Quick and Easy Input“Approximate” Fitting and Valve counts

PRIMARY PUMPS


Primary Pump Head Calcs - #1Primary Pump Head Calcs - #1Typical Project Example for Primary Pump Head Calcs

HELP

* PRESSURE DROP BASED ON: PROJECT NAME: VELOCITY NOT EXCEEDING 5 FT/SEC. UP TO 2" PIPE PROJECT NUMBER: VELOCITY NOT EXCEEDING 10 FT/SEC. FOR LARGER THAN 2" PIPE DATE: PRESSURE DROP BETWEEN 1 AND 5 FT/100 FT.

9 CAUTION : ABOVE OR BELOW NORMAL VELOCITYAPPROXIMATE PUMP BHP: 2.5 (CALCULATED DURING INPUT) AVERAGE EQUIVALENT PRESS. LOSS FOR TOTAL

SIZE NUMBER OF GPM VELOCITY LENGTH DROP -EACH SIZE LOSSITEM LENGTH (FT.) (IN.) FITTINGS (EACH SIZE) (FT./SEC.) (FT.) (FT/100 FT.) * (FT. HD.) (FT. HD.)PUMP ACCESSORIES:PUMP FLEX. CONNECTIONS 2 5 22 2.6 1.14

CHECK VALVE - LIFT CHECK 1 5 84 2.6 2.18

CHECK VALVE - SWING CHECK 0 0 0 0 0.00

CHECK VALVE - SILENT CHECK 0 0 N/A N/A 0.00

BALANCING VALVE (80% OPEN) 1 7 N/A N/A 4.00

SHUT-OFF VALVE - BUTTERFLY 2 7 N/A N/A 2.00

SHUT-OFF VALVE - GATE 0 0 0 0 0.00

PUMP HEAD CALCULATION - CHILLED WATER - PRIMARYTEST PROJECT #11444-062/19/2006

0 0

0

0

0

0

0

0

0

0

0

0

0

0

RESET/CLEAR


Primary Pump Head Calcs - #2Primary Pump Head Calcs - #2

Easy Input of System Components and GPM Quantities

Running Total of Approx. Pump BHP

BRANCH TEE - DIVERTING FLOW OR CONVERGING FLOW (FLOW TURNS 90 DEGREES) SIZE GPM VEL. EQ. LEN. FT/100 FT.

TEE #1 3 GPM "IN" 160 8 21.39 7 1.50TEE #1 GPM "OUT" 120TEE #2 3 GPM "IN" 120 6 16.91 4 0.68TEE #2 GPM "OUT" 160TEE #3 3 GPM "IN" 120 6 16.91 4 0.68TEE #3 GPM "OUT" 160TEE #4 3 GPM "IN" 120 6 16.91 4 0.68TEE #4 GPM "OUT" 120TEE #5 3 GPM "IN" 120 6 16.91 4 0.68TEE #5 GPM "OUT" 120TEE #6 0 GPM "IN" 0 0 0 0 0.00TEE #6 GPM "OUT" 0TEE #7 0 GPM "IN" 0 0 0 0 0.00TEE #7 GPM "OUT" 0TEE #8 0 GPM "IN" 0 0 0 0 0.00TEE #8 GPM "OUT" 0TEE #9 0 GPM "IN" 0 0 0 0 0.00TEE #9 GPM "OUT" 0TEE #10 0 GPM "IN" 0 0 0 0 0.00TEE #10 GPM "OUT" 0 4.20

THRU TEE - CONVERGING FLOW (FLOW STRAIGHT THRU) SIZE GPM VEL. EQ. LEN. FT/100 FT.

TEE #1 3 GPM "IN" 120 6 8.9 4 0.36TEE #1 GPM "OUT" 160TEE #2 3 GPM "IN" 120 6 8.9 4 0.36TEE #2 GPM "OUT" 160TEE #3 0 GPM "IN" 0 0 0 0 0.00TEE #3 GPM "OUT" 0TEE #4 0 GPM "IN" 0 0 0 0 0.00TEE #4 GPM "OUT" 0TEE #5 0 GPM "IN" 0 0 0 0 0.00TEE #5 GPM "OUT" 0

OutIn

Out

In

Out

In



Easy Input of System Components and GPM Quantities

Built-in Fitting Coefficients

CHILLER EQUIPMENT: VEL. EQ. LEN. FT/100 FT.

ISOLATION VALVE - BUTTERFLY 2 5 N/A N/A 0.60

ISOLATION VALVE - GATE 0 0 0 0 0.00

ISOLATION VALVE - GLOBE 0 0 0 0 0.00

ISOLATION VALVE - ANGLE 0 0 0 0 0.00

ISOLATION VALVE - BALL 0 0 0 0 0.00

Y-TYPE STRAINER 1 5 N/A N/A 0.80

CHILLER AUTOMATIC ISOLATION VALVE (AUTOMATIC GLOBE VALVE) 1 5 130.5 2.6 3.39

CHILLER FLEX. CONNECTION 2 5 22 2.6 1.145.94

CHILLER PRESSURE DROP (FROM MANUFACTURER, IF KNOWN) : 0

GENERIC CHILLER PRESSURE DROP (IF NOT AVAIL. FROM MFG'R.) : CHILLER TONS : 100 CHILLER GPM : 120 4.20

4.20AIR CONTROL AND FLOW METERS:AIR SEPARATOR PRESSURE DROP (FROM MANUFACTURER, IF KNOWN) : 0

GENERIC AIR SEPARATOR PRESSURE DROP - WITH STRAINER (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0 GPM : 160 11.05

0 0

0

0

0

0

0

0

0

0

0

0

0 0

0 0

0

0

2



Allowance for Items at Chiller or Boiler

Generic Values Built-in (Conservative) if Mfgr’s. Data Unknown

PIPE LOSSES (MEASURE "OUT & BACK" TO PUMP) : PRESS. LOSS FOR TOTALSIZE NUMBER GPM VELOCITY EQ. LEN. DROP SIZE LOSS

LENGTH (FT.) (IN.) (FT./SEC.) (FT/100 FT.) * (FT. HD.) (FT. HD.)COPPER PIPE : 0 1/2 N/A 0 0.0 0 0.0 0.00COPPER PIPE : 0 3/4 N/A 0 0.0 0 0.0 0.00COPPER PIPE : 0 1 N/A 0 0.0 0 0.0 0.00COPPER PIPE : 0 1 1/4 N/A 0 0.0 0 0.0 0.00COPPER PIPE : 0 1 1/2 N/A 0 0.0 0 0.0 0.00COPPER PIPE : 0 2 N/A 0 0.0 0 0.0 0.00COPPER PIPE : 0 2 1/2 N/A 0 0.0 0 0.0 0.00COPPER PIPE : 150 3 N/A 160 8.0 150 7.0 10.50COPPER PIPE : 0 4 N/A 0 0.0 0 0.0 0.00

0 10.50STEEL PIPE : 0 1/2 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 3/4 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 1 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 1 1/4 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 1 1/2 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 2 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 2 1/2 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 3 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 4 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 5 N/A 0 0.0 0 0.0 0.00STEEL PIPE : 0 6 N/A 0 0.0 0 0.0 0.00

SUB-TOTAL PRESSURE DROP (FT. HEAD) : 55.25

GLYCOL PRESSURE DROP CORRECTION (IF ANY) - BASED ON 50 DEGREE F WATER TEMPERATURE :

PERCENT GLYCOL, BY WEIGHT : GLYCOL CORRECTION FACTOR : 1

CORRECTED SUB-TOTAL PRESSURE DROP (FT. HEAD) : 55.25

PRESSURE DROP SAFETY FACTOR (IF ANY) - RECOMMEND 5% = 1.05

TOTAL PUMP PRESSURE DROP (FT. HEAD): 58.01

0

1.05



Adjustments for Glycol (if applicable) and/or Safety Factor

Imput Length of “Longest Run” Piping (Measured “Out & Back” to Pump)

Final, Totalized Primary Pump Head (Ft.) for the System

PUMP HEAD CALCULATION - CHILLED WATER - PRIMARY * PRESSURE DROP BASED ON: PROJECT NAME: VELOCITY NOT EXCEEDING 5 FT/SEC. UP TO 2" PIPE PROJECT NUMBER: VELOCITY NOT EXCEEDING 10 FT/SEC. FOR LARGER THAN 2" PIPE DATE: PRESSURE DROP BETWEEN 1 AND 5 FT/100 FT.

9 CAUTION: ABOVE OR BELOW NORMAL VELOCITYAPPROXIMATE PUMP BHP: 2.5 (CALCULATED DURING INPUT) AVERAGE EQUIVALENT PRESS. LOSS FOR LOSSITEM NAME LENGTH (FT.) (IN.) FITTINGS (EACH SIZE) (FT./SEC.) (FT.) (FT/100 FT.) (FT. HD.) TOTALPUMP FLEX. CONNECTIONS 3 2 120 5 22 2.6 1.14CHECK VALVE - LIFT CHECK 3 1 120 5 84 2.6 2.18BALANCING VALVE (80% OPEN) 3 1 160 7 N/A N/A 4.00SHUT-OFF VALVE - BUTTERFLY 3 2 160 7 N/A N/A 2.00TRIPLE DUTY VALVE -STRAIGHT 3 1 120 5 N/A N/A 1.20TRIPLE DUTY VALVE -ANGLE 0 0 0 0 N/A N/A 0.00 10.53STANDARD 90 DEG. ELBOW 3 5 160.0 8 9.3 7 3.26STANDARD 90 DEG. ELBOW 12 0 0.0 0 0 0 0.00 3.26THRU TEE - DIVERTING FLOW 3 GPM "IN" 160.0 8 1.86 7 0.13

TEE #2 3 GPM "IN" 160.0 8 1.86 7 0.13TEE #3 3 GPM "IN" 160.0 8 1.86 7 0.13TEE #4 3 GPM "IN" 120.0 6 0.89 4 0.04TEE #5 3 GPM "IN" 120.0 6 0.89 4 0.04TEE #10 0 GPM "OUT" 0.0 0 0 0 0.00 0.46

BRANCH TEE - DIVERTING FLOW OR CONVERGING FLOW3 GPM "IN" 160.0 8 21.39 7 1.50TEE #2 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #3 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #4 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #5 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #10 0 GPM "OUT" 0.0 0 0 0 0.00 4.20

THRU TEE - CONVERGING FLOW 3 GPM "IN" 120 6.0 8.90 4 0.36TEE #2 3 GPM "IN" 120 6.0 8.90 4 0.36

TEE #10 0 GPM "OUT" 0 0.0 0.00 0 0.00 0.71ISOLATION VALVE - BUTTERFLY 3 2 120 5.0 N/A N/A 0.60Y-TYPE STRAINER 3 1 120 5.0 N/A N/A 0.80 (AUTOMATIC GLOBE VALVE) 3 1 120 5.0 130.50 3 3.39CHILLER FLEX. CONNECTION 3 2 120 5.0 22.00 3 1.14 5.94GENERIC CHILLER PRESSURE DROP (IF NOT AVAIL. FROM MFG'R.) : CHILLER TONS :100.0 CHILLER GPM : 120 4.20 4.20GENERIC AIR SEPARATOR PRESSURE DROP - WITH STRAINER (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 160 11.05GENERIC AIR SEPARATOR PRESSURE DROP - WITHOUT STRAINER (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 0 0.00 11.05GENERIC FLOW METER PRESSURE DROP (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 160 3.50 3.50GENERIC SUCTION DIFFUSER PRESSURE DROP (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 120 0.90 0.90COPPER PIPE : 150 3 N/A 160.0 8.0 150 7.0 10.50COPPER PIPE : 0 4 N/A 0.0 0.0 0 0.0 0.00 10.50

SUB-TOTAL PRESSURE DROP (FT. HEAD) : 55.25PERCENT GLYCOL, BY WEIGHT : 0 GLYCOL CORRECTION FACTOR : 1

CORRECTED SUB-TOTAL PRESSURE DROP (FT. HEAD) : 55.25PRESSURE DROP SAFETY FACTOR (IF ANY) - RECOMMEND 5% = 1.05 1.05 1.05TOTAL PUMP PRESSURE DROP (FT. HEAD): 58.01

© 2007 hvacdesignsolutions.com

1444-062/19/2006

TEST PROJECT #1



After Input is complete, press “Compile & Print” Button for full System Report


Coil Psychrometrics CalcsCoil Psychrometrics CalcsHELP

91 67074 1075

AHU COOLING SUPPLY MINIMUM SUPPLY AIR RETURN AIR OUTSIDE AIR RETURN AIR ENTERING AIR LEAVING AIR COOLING CHILLED FLOOR CFM PERNUMBER LOAD * AIR TEMP. OUTSIDE AIR QUANTITY TEMP. ENTHALPY ENTHALPY ENTHALPY ENTHALPY COIL LOAD WATER AREA SQ. FT.

(MBH) (°F) (CFM) (CFM) (°F) (BTU/LB.) (BTU/LB.) (BTU/LB.) (BTU/LB.) (MBH) (GPM) (SQ. FT)

1 12.5 54.0 150 590 78.0 37.7 30.2 32.1 21.7 26.1 5.2 400 1.52 18.2 54.0 320 859 78.0 37.7 30.2 33.0 21.7 41.1 8.2 650 1.33 46.3 54.0 1550 2186 78.0 37.7 30.2 35.5 21.7 126.6 25.3 2000 1.14 244.8 54.0 5500 11556 78.0 37.7 30.2 33.8 21.7 586.9 117.4 12950 0.95 42.0 54.0 1480 1983 78.0 37.7 30.2 35.8 21.7 117.2 23.4 1820 1.16 121.7 54.0 2640 5745 78.0 37.7 30.2 33.6 21.7 289.6 57.9 4800 1.27 24.5 54.0 450 1157 78.0 37.7 30.2 33.1 21.7 55.7 11.1 820 1.48 205.9 54.0 5120 9720 78.0 37.7 30.2 34.2 21.7 509.2 101.8 11200 0.99 105.5 54.0 2200 4980 78.0 37.7 30.2 33.5 21.7 248.2 49.6 4280 1.210 33.6 54.0 1250 1586 78.0 37.7 30.2 36.1 21.7 95.8 19.2 1500 1.111 19.5 54.0 250 921 78.0 37.7 30.2 32.2 21.7 41.2 8.2 700 1.312 150.3 54.0 2850 7095 78.0 37.7 30.2 33.2 21.7 344.7 68.9 6200 1.1

0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.00 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.00 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.00 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0

PROJECT ELEVATION =CHILLED WATER DELTA-T =

AIR HANDLING UNIT - PRELIMINARY COOLING COIL LOAD CALCULATIONS

TEST PROJECT #11456-0706/21/07

PROJECT NAME:PROJECT NUMBER:DATE:

OA DESIGN DB =OA DESIGN WB =DESIGN ROOM TEMP. =

PRINTRESET/CLEAR

Psychrometric Calculations Assist with Preliminary Equipment Selection, Preliminary Pump Sizing, Etc.

HELP

MINIMUM WATER TEMP. (DEG. F): 40

HEATING WATER TEMP. (DEG. F): 200

PROJECT ELEVATION (ft.) 670

PIPE SIZETOTAL PIPE LENGTH (ft.)

GALLONS PER FOOT PIPE GALLONS

1/2 0.0121 0.0

3/4 120 0.0251 3.0

1 60 0.0429 2.6

1 1/4 0.0653 0.0

1 1/2 75 0.0924 6.9

2 224 0.1610 36.1

DATE:

TEST PROJECT #1

1444-07

12/19/2007

PROJECT NAME:

PROJECT NUMBER:

EXPANSION TANK SIZING - HEATING WATER

PRINT

BOILER MBH 450 337.5COIL

GALLONS

# HEATING COILS 18 36.0 EXCHANGER GALLONS

# HEAT EXCHANGERS 1 15.0

TOTAL CONTENT (gal.) 490.2

GLYCOL % (IF APPLICABLE) 10

EXPANSION FACTOR 0.03510

EXPANDED WATER VOLUME (gal.) 20.8

HEIGHT OF SYSTEM (ft.) 45 24.6 30

RELIEF VALVE SETTING (psi) 30 27

ACCEPTANCE FACTOR 0.06 0.94

TANK VOLUME (gal.) 353.8

CAUTION: RELIEF VALVE SETTING MUST BE LARGER THAN REQUIRED SYSTEM PRESSURE

ACCEPTANCE VOLUME MUST EXCEED EXPANDED WATER VOLUME (gal.)

(PERCENT BY VOLUME) ENTER 0 IF NO GLYCOL IN SYSTEM

(SYSTEM PRESSURE)

(BASED ON HEATING WATER TEMP. MINUS MINIMUM WATER TEMP.)


Heating Water Expansion TankHeating Water Expansion Tank

Heating Water and Chilled Water Expansion Tank Sizing Programs

Built-in Water Volumes, Expansion Factors, Acceptance Factors, and Expansion Formulas


Project Information Request LettersProject Information Request LettersHELP

PROJECT NAME: DATE: 06/21/07

PROJECT NUMBER:

REQUESTED BY:

1. All Offices

2. Conference Rooms

3. Photocopy machine rooms

4. Lounge and/or lunch rooms

5. Electrical equipment rooms

6. Computer Rooms

7. Procedure Rooms

8. Other specialty rooms

B. Please indicate any special HVAC requirements such as areas requiring:

1. 24 Hour Air Conditioning

2. Relative Humidity Controls

The above information should include: PC Stations, Laser Printers, Fax Machines, Photocopy Machines, Microwaves, Vending Machines, Refrigerators, Coffee Makers, Special Lighting, etc. If available, this information should contain: quantity, location, BTU/hr, wattage, amperage, voltage, heat output to the space, operating cycle time, etc.

Please provide the following information, to expedite our design of your project. It is very important that you respond as soon as possible, with as accurate information as you have available, so we can calculate the correct air conditioning requirements and make accurate equipment selections.

A. Please provide the number of people, heat output or amperage and voltage of equipment, and any other element that might effect the HVAC load in the following areas:

1456-07

TEST PROJECT #1

BUILDING MECHANICAL INFORMATION REQUESTHELP

PROJECT NAME: DATE: 06/21/07

PROJECT NUMBER:

REQUESTED BY:

ROOM NAME/NUMBER:

NUMBER OF PEOPLE

HEAT PRODUCING EQUIPMENT (Please Indicate Quantity Below)

PC Stations Laser Printers

Photocopy Machines Fax Machines

Microwaves TV Sets or Monitors

Refrigerators (Small – S, Large – L) Vending Machines

Coffee Makers

Special Lighting (Total Watts to Room)

Special Equipment (Total Watts to Room)

Exposed Motors in Room (Horsepower)

NO HEAT PRODUCING EQUIPMENT IN THIS ROOM

SPECIAL OPERATING CONDITIONS

24 Hour Air Conditioning Required

BUILDING MECHANICAL ROOM INFORMATION REQUEST FORM

PEOPLE ACTIVITY LEVEL: (S) - Seated Office; (M) - Moderate Office; (W) - Walking or Standing; (B) - Bench Work; (H) Heavy Work

TEST PROJECT #1

1456-07

“Programming” Information Request Forms for Owner or Architect Input


Extensive “Quality Control” Mechanical Checklists are available in a separate “Mechanical Peer Review” Software Package

Coordination Between DisciplinesContents: (Click on hyperlink to jump to the sheet checklist)

A Preliminary Review of Plans and SpecificationsB Demolition PlansC Architect and/or Owner CoordinationD Structural CoordinationE Mechanical CoordinationF Plumbing CoordinationG Civil Engineering CoordinationH Electrical Coordination

A Preliminary Review of Plans and Specifications1 Quickly review all Drawings in the Construction Document set, including Architectural,

Structural, Civil, Landscaping, Mechanical, Plumbing, Fire Protection, Electrical, FoodService, and any other discipline. Spend not more than one minute per sheet, average.

2 Make a list of any apparent discrepancies or questions while reviewing the set, and add‘flags’ to sheets where there are significant questions.

3 Quickly review the Specif ications by reading through the Table of Contents forMechanical and Plumbing work. Check the Table of Contents against the actualSpecification sections to verify all sections have been included. Make a list of questionsthat may come up during the cursory review.

4 Review Architectural T itle Sheet, or first sheet in the set, and make a list of the ProjectSquare Footage, Building Occupancy Type, Building Construction Type, GoverningCodes, Index of Drawings, and any other information that relates to Mechanical orPlumbing work.

5 Check for consistent appearance of Title Blocks, Drawing Scales, North Arrows,Professional Stamps, Company Logos, Sheet Numbers, Sheet Tit les, Issue Dates, andIssue Revisions on all sheets.

B Demolition Plans1 Verify that Demolition Symbols (cross-hatching, etc.) are clear and complete, and are

coordinated with other disciplines.2 Verify there are notes regarding potential hazardous materials (asbestos, lead paint,

etc.), and coordinate with Architect or other Prime Consultant and Owner.

““Mechanical Peer Review” SoftwareMechanical Peer Review” Software

Over (110) Pages of Checklists and Spreadsheets for a thorough review of Mechanical Construction Documents


““Mechanical Peer Review” SoftwareMechanical Peer Review” SoftwareMechanical Plan Review ItemsContents: (Click on hyperlink to jump to the sheet checklist)

A Preliminary Review of Plans and SpecificationsB Legend and Symbols SheetC Schedule SheetsD Mechanical Demolition PlansE Mechanical Ductwork Floor PlansF Mechanical Piping PlansG Mechanical Roof PlansH Mechanical Central Plant PlansI Clean Room and Fabrication FacilitiesJ Mechanical Piping DiagramsK Mechanical Control DrawingsL Mechanical Detail Drawings

A Mechanical Piping Plans Return to Table of Contents1 Sum all Chilled Water Supply and Return quantities (GPM’s) from coils back to service

connection or pumps. Pencil in quantities adjacent to pipes. Verify flow rates are listedfor all coils or equipment, and that Schedules for each device are complete. Check flowdirection Arrows for completeness and correct direction.

2 Sum all Heating Water Supply and Return quantities (GPM’s) same as Chilled Water.Pencil in quantities. Verify Schedule information is complete. Check flow directionArrows.

3 Check for provisions for Water Balancing on plans or on details of coil connections.4 Check for Isolation Valves to allow servicing without shutting down and draining entire

systems.5 Verify whether Direct-return or Reverse-return piping. Suggest Reverse-return for better

water balancing, if appropriate.6 Check provisions for Condensate Drains. Coordinate with Plumbing drawings for piping

and Approved Disposal methods.7 Check on provisions for Air Venting and Drainage – on Coil Piping Details and plans.8 Check Thermostat locations (if thermostats are shown on Piping Plans) and verify all

heating and cooling elements have a corresponding Thermostat or Sensor Control.9 Spot-check pipe sizes against totalized water quantities. Use maximum of 4 ft. per 100 ft.

pipe friction, up to 5” pipe size, and maximum of 8 ft. per second Velocity for pipe 6” andlarger.

10 Check for provisions for Pipe Expansion – Pipe Loops, adequate turns (less than 50 feetof straight pipe), or expansion devices.

11 Check for restrictions to pipe movement – against columns, against solid walls, drops orrises to adjacent floors.

12 Verify that pipes are not run through Stairwells, Elevator Shafts, Columns, or ElectricalRooms.

13 Compare Totalized water quantities with associated Pumps, and analyze diversity if totalsare not equal.

14 Verify that all pipes are sized.15 Coordinate Pipe plans with Ductwork plans and identify any potential conflicts.

Example of Quality Control Check List Items

PUMP HEAD CALCULATION - CHILLED WATER - PRIMARY * PRESSURE DROP BASED ON: PROJECT NAME: VELOCITY NOT EXCEEDING 5 FT/SEC. UP TO 2" PIPE PROJECT NUMBER: VELOCITY NOT EXCEEDING 10 FT/SEC. FOR LARGER THAN 2" PIPE DATE: PRESSURE DROP BETWEEN 1 AND 5 FT/100 FT.

9 CAUTION: ABOVE OR BELOW NORMAL VELOCITYAPPROXIMATE PUMP BHP: 2.5 (CALCULATED DURING INPUT) AVERAGE EQUIVALENT PRESS. LOSS FOR LOSSITEM NAME LENGTH (FT.) (IN.) FITTINGS (EACH SIZE) (FT./SEC.) (FT.) (FT/100 FT.) (FT. HD.) TOTALPUMP FLEX. CONNECTIONS 3 2 120 5 22 2.6 1.14CHECK VALVE - LIFT CHECK 3 1 120 5 84 2.6 2.18BALANCING VALVE (80% OPEN) 3 1 160 7 N/A N/A 4.00SHUT-OFF VALVE - BUTTERFLY 3 2 160 7 N/A N/A 2.00TRIPLE DUTY VALVE -STRAIGHT 3 1 120 5 N/A N/A 1.20TRIPLE DUTY VALVE -ANGLE 0 0 0 0 N/A N/A 0.00 10.53STANDARD 90 DEG. ELBOW 3 5 160.0 8 9.3 7 3.26STANDARD 90 DEG. ELBOW 12 0 0.0 0 0 0 0.00 3.26THRU TEE - DIVERTING FLOW 3 GPM "IN" 160.0 8 1.86 7 0.13

TEE #2 3 GPM "IN" 160.0 8 1.86 7 0.13TEE #3 3 GPM "IN" 160.0 8 1.86 7 0.13TEE #4 3 GPM "IN" 120.0 6 0.89 4 0.04TEE #5 3 GPM "IN" 120.0 6 0.89 4 0.04TEE #10 0 GPM "OUT" 0.0 0 0 0 0.00 0.46

BRANCH TEE - DIVERTING FLOW OR CONVERGING FLOW3 GPM "IN" 160.0 8 21.39 7 1.50TEE #2 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #3 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #4 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #5 3 GPM "IN" 120.0 6 16.91 4 0.68TEE #10 0 GPM "OUT" 0.0 0 0 0 0.00 4.20

THRU TEE - CONVERGING FLOW 3 GPM "IN" 120 6.0 8.90 4 0.36TEE #2 3 GPM "IN" 120 6.0 8.90 4 0.36

TEE #10 0 GPM "OUT" 0 0.0 0.00 0 0.00 0.71ISOLATION VALVE - BUTTERFLY 3 2 120 5.0 N/A N/A 0.60Y-TYPE STRAINER 3 1 120 5.0 N/A N/A 0.80 (AUTOMATIC GLOBE VALVE) 3 1 120 5.0 130.50 3 3.39CHILLER FLEX. CONNECTION 3 2 120 5.0 22.00 3 1.14 5.94GENERIC CHILLER PRESSURE DROP (IF NOT AVAIL. FROM MFG'R.) : CHILLER TONS :100.0 CHILLER GPM : 120 4.20 4.20GENERIC AIR SEPARATOR PRESSURE DROP - WITH STRAINER (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 160 11.05GENERIC AIR SEPARATOR PRESSURE DROP - WITHOUT STRAINER (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 0 0.00 11.05GENERIC FLOW METER PRESSURE DROP (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 160 3.50 3.50GENERIC SUCTION DIFFUSER PRESSURE DROP (IF NOT AVAIL. FROM MFG'R.) : SIZE : 0.0 GPM : 120 0.90 0.90COPPER PIPE : 150 3 N/A 160.0 8.0 150 7.0 10.50COPPER PIPE : 0 4 N/A 0.0 0.0 0 0.0 0.00 10.50

SUB-TOTAL PRESSURE DROP (FT. HEAD) : 55.25PERCENT GLYCOL, BY WEIGHT : 0 GLYCOL CORRECTION FACTOR : 1

CORRECTED SUB-TOTAL PRESSURE DROP (FT. HEAD) : 55.25PRESSURE DROP SAFETY FACTOR (IF ANY) - RECOMMEND 5% = 1.05 1.05 1.05TOTAL PUMP PRESSURE DROP (FT. HEAD): 58.01

© 2007 hvacdesignsolutions.com

1444-062/19/2006

TEST PROJECT #1


Calculation DocumentsCalculation Documents

After completing input and calculations, Output and Sizing Documents can be printed for submittal to building department officials and for addition to drawings and schedules

PUMP-DIAG.

EXPTANK-HHW

SECONDARY HEATING WATER PUMP HEAD CALCULATIONS

PUMP HEAD CALCULATIONS DIAGRAM

PUMP-HHW-PRIM.

PUMP-HHW-SEC.

PRIMARY HEATING WATER PUMP HEAD CALCULATIONS

HEATING WATER EXPANSION TANK CALCULATIONS

PUMP-DIAG.

PUMP-COOL.TOWER

EXPTANK-CHW

SECONDARY CHILLED WATER PUMP HEAD CALCULATIONS

CHILLED WATER EXPANSION TANK CALCULATIONS

PUMP HEAD CALCULATIONS DIAGRAM

PUMP-CHW-PRIM.

PUMP-CHW-SEC.

CONDENSER WATER (COOLING TOWER) PUMP HEAD CALCULATIONS

PRIMARY CHILLED WATER PUMP HEAD CALCULATIONS

Bldg. Info. 2

Ceiling Space

Bldg. Info.BUILDING MECHANICAL INFORMATION REQUEST FORM

BUILDING MECHANICAL ROOM INFORMATION REQUEST FORM

CEILING SPACE INFORMATION REQUEST FORM


Software ContentsSoftware Contents

Extensive Wetside Programs to help “Streamline” your Design Procedures

PIPESIZE

PUMP-HD.-PRELIM.

PIPECALCPIPE SIZING CALCULATOR- OPTIMAL ECONOMIC SIZING

PIPE SIZING SCHEDULE - OPTIMAL ECONOMIC SIZING

PRELIMINARY PUMP HEAD CALCULATIONS

VAV - REHEAT COIL LOAD CALCULATIONSVAV REHEAT

AHU-COOL. COIL

AHU-HTG.COIL

AHU - PRELIMINARY COOLING COIL LOAD CALCULATIONS

AHU - PRELIMINARY HEATING COIL LOAD CALCULATIONS

Straightforward takeoff and input allows easy calculation and sizing of Wetside Systems.

Extensive procedures, formulas, charts, and tables as prescribed by Mechanical Codes and as recommended by ASHRAE and Equipment Manufacturers have been included and have been used to establish the “Accurate” Wetside System Sizes.

Multiple Programs are included, covering most of the typical Wetside Design Tasks for most projects.


Features and BenefitsFeatures and Benefits

Significantly reduces “Reference Material Dependence” which can save a great deal of time and effort.

Output in the form of Compliance Documents or System Sizing Summaries for submittal to appropriate code enforcement officials or building departments.

Extensive “Help Files” that are hyperlinked to each program, form, or table.


Features and BenefitsFeatures and Benefits

Limited time “Special Pricing” available at our website www.hvacdesignsolutions.com

Wetside Design Package Original Price: $225 US, Special Price: $169 US

Mechanical Peer Review Package Original Price: $275 US, Special Price: $198 US


PricingPricing

Current Version: 2.12, with latest update (08/24/2008) Free updates, as available.

To purchase Wetside Design or Mechanical Peer Review, visit our website at www.hvacdesignsolutions.com and go to the Prices/Orders page

Software can be downloaded for immediate installation (with password) after purchase is confirmed


AvailabilityAvailability

OS: Windows® 98, 2000, XP, 2003, Vista Processor: Pentium® or equivalent Ram: 512MB (minimum recommended) Disk Space: 100 MB (recommended) Software: MS Word®, MS Excel®


System RequirementsSystem Requirements

Thank you for taking your time to review our Wetside Design software packages

If you have any questions or comments, you can e-mail to: steve”at”hvacdesignsolutions.com , or support”at”hvacdesignsolutions.com

We also have an interactive demo of our Wetside Design software that can be delivered, on request, via e-mail.


Thanks!Thanks!

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Documents

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