NIST B226 Replace HVAC 100 Submission BOD.pdf

CUSTOMER: NIST Laboratories

E&W PROJECT NUMBER: 20-0538

QUANTITY: 1

MATERIAL:

BASE: SST

PANELS: SST

POWER SUPPLY: 460V/3PH/60 HZ

PERFORMANCE:

CAPACITY: 8,000 BTU/Hr

AIRFLOW: 5,500 CFM @ 2" WG

ENTERING AIR TEMPERATURE 0˚F WB / -1.5˚F DB

FLUID DYNALENE HF-LO

FLUID FLOW RATE 5 GPM

ENTERING FLUID TEMPERATURE -15˚F

COIL: CARBON STEEL FINS AND TUBES

FAN MOTOR: 3 HP

NOTES:

1. Drawing is for proposal purposes only. Actual design and dimensions may vary from that shown.

SECTION A-A

A A

B B

C C

D D

DWG NO SH REV

1 0

THIS DRAWING IS CONFIDENTIAL AND IS THE PROPERTY OF

ELLIS & WATTS GLOBAL INDUSTRIES, INC. IT CONTAINS

INFORMATION WHICH IS PROPRIETARY. IT SHALL NOT BE USED,

DISCLOSED, DUPLICATED, REPRODUCED, OR TRANSFERRED

WITHOUT PRIOR WRITTEN PERMISSION OF ELLIS & WATTS

GLOBAL INDUSTRIES, INC.

20-0538-01

TITLE

SIZE CAGE CODE DWG NO REV

SCALE: UNIT WT: SHEET OF

UNLESS OTHERWISE SPECIFIED

DIMENSIONS ARE IN INCHES.

TOLERANCES ARE:

FRACTIONS DECIMALS ANGLES

±1/16 .XX=±.015 2°

.XXX=±.005

DO NOT SCALE DRAWING

INTERPRET DIM AND TOL PER ASME

Y14.5M-1994

CONTRACT INFORMATION

QUALITY ASSURANCE APPROVED

ENGINEERING APPROVED

CHECKED

DRAWN DATE

APPROVED

D 20-0538-01 0

NONE 1

AHU-12

GLW

APPLICATION

NEXT ASSY USED ON

PMIC

9/22/2020

FILE: 20-0538-01.idw

767R6

A A

AIR DISCHARGE

AIR INLET

49 1/2

28 1/2

43 5/16

111 5/16

86 5/81 1/4 1 1/4

3643 3/16

107 13/16

109 9/16

4X n13/16 THRU

123 1/8

31 1/2

QUANTITY: 1

MATERIAL:

BASE: SST

PANELS: SST

POWER SUPPLY: 460V/3PH/60 HZ

PERFORMANCE:

CAPACITY: 11,270 BTU/Hr

AIRFLOW: 4,750 CFM @ 2" WG

ENTERING AIR TEMPERATURE 0˚F WB / -1.5˚F DB

FLUID DYNALENE HF-LO

FLUID FLOW RATE 7.5 GPM

ENTERING FLUID TEMPERATURE -15˚F

COIL: CARBON STEEL FINS AND TUBES

FAN MOTOR: 3 HP

NOTES:

1. Drawing is for proposal purposes only. Actual design and dimensions may vary from that shown.

SECTION A-A

A A

B B

C C

D D

DWG NO SH REV

1 0

THIS DRAWING IS CONFIDENTIAL AND IS THE PROPERTY OF

ELLIS & WATTS GLOBAL INDUSTRIES, INC. IT CONTAINS

INFORMATION WHICH IS PROPRIETARY. IT SHALL NOT BE USED,

DISCLOSED, DUPLICATED, REPRODUCED, OR TRANSFERRED

WITHOUT PRIOR WRITTEN PERMISSION OF ELLIS & WATTS

GLOBAL INDUSTRIES, INC.

20-0538-02

TITLE

SIZE CAGE CODE DWG NO REV

SCALE: UNIT WT: SHEET OF

UNLESS OTHERWISE SPECIFIED

CONTRACT INFORMATION

QUALITY ASSURANCE APPROVED

ENGINEERING APPROVED

CHECKED

DRAWN DATE

APPROVED

D 20-0538-02 0

NONE 1

AHU-13

PMIC

9/28/2020

FILE: 20-0538-02.idw

767R6

A A

AIR DISCHARGE

AIR INLET

80 5/16

55 5/81 1/4 1 1/4

3643 3/16

76 13/16

4X n13/16 THRU

84 9/16

78 9/16

43 3/16

31 1/2

28 1/2

49 1/2

17 3/4 3 1/2

17 3/4

QUANTITY: 1

MATERIAL:

BASE: SST

PANELS: SST

POWER SUPPLY: 460V/3PH/60 HZ

PERFORMANCE:

CAPACITY: 13,929 BTU/Hr

AIRFLOW: 4,750 CFM @ 2" WG

ENTERING AIR TEMPERATURE 0˚F WB / -1.5˚F DB

FLUID DYNALENE HF-LO

FLUID FLOW RATE 9.5 GPM

ENTERING FLUID TEMPERATURE -15˚F

COIL: CARBON STEEL FINS AND TUBES

FAN MOTOR: 3 HP

NOTES:

1. Drawing is for proposal purposes only. Actual design and dimensions may vary from that shown.

SECTION A-A

A A

B B

C C

D D

DWG NO SH REV

1 0

THIS DRAWING IS CONFIDENTIAL AND IS THE PROPERTY OF

ELLIS & WATTS GLOBAL INDUSTRIES, INC. IT CONTAINS

INFORMATION WHICH IS PROPRIETARY. IT SHALL NOT BE USED,

DISCLOSED, DUPLICATED, REPRODUCED, OR TRANSFERRED

WITHOUT PRIOR WRITTEN PERMISSION OF ELLIS & WATTS

GLOBAL INDUSTRIES, INC.

20-0538-03

TITLE

SIZE CAGE CODE DWG NO REV

SCALE: UNIT WT: SHEET OF

UNLESS OTHERWISE SPECIFIED

CONTRACT INFORMATION

QUALITY ASSURANCE APPROVED

ENGINEERING APPROVED

CHECKED

DRAWN DATE

APPROVED

D 20-0538-03 0

NONE 1

AHU-14

PMIC

9/28/2020

FILE: 20-0538-03.idw

767R6

A A

AIR DISCHARGE

AIR INLET

49 1/2

28 1/2

43 5/16

80 5/16

55 5/81 1/4 1 1/4

3643 3/16

76 13/16

4X n13/16 THRU

92 1/8

40 1/2

78 9/16

Unit: AHU 12 3/4" Tube Z:\UserFiles\AdamHorntvedt\Customers\Ellis and Watts\20200504-00-Low Temp Coils\AHU 12 0.625 Tube.htri

Output Summary Page 1

Released to the following HTRI Member Company:

SUPER RADIATOR COILS

ADAM HORNTVEDT

Xace 8.2 12/16/2020 15:17 SN: 00207-889033604 US Units

-10F inlet Temp, 5500CFM : AHU 12 3/4" Tube Rating-Horizontal economizer countercurrent to crossflow

See Data Check Messages Report for Warning Messages.

See Runtime Message Report for Warning Messages.

Process Conditions Outside Tubeside Fluid name Air Dyanlene HFLO Fluid condition Sens. Gas Sens. Liquid Total flow rate (1000-lb/hr) 29.150 20.726 Weight fraction vapor, In/Out 1.0000 1.0000 0.0000 0.0000

Temperature, In/Out (Deg F) -10.00 -12.00 -15.00 -13.53

Skin temperature, Min/Max (Deg F) -12.92 -10.71 -12.93 -10.72

Pressure, Inlet/Outlet (psia) 14.700 14.693 0.000 0.000

Pressure drop, Total/Allow (psi) (psi) 7.12e-3 0.000 1.310 0.000

Midpoint velocity (ft/sec) 10.56 2.39

- In/Out (ft/sec) 2.39 2.39 Heat transfer safety factor (--) 1.0000 1.0000 Fouling (ft2-hr-F/Btu) 0.00000 0.00000

Exchanger Performance Outside film coef (Btu/ft2-hr-F) 7.53 Actual U (Btu/ft2-hr-F) 1.645

Tubeside film coef (Btu/ft2-hr-F) 22.30 Required U (Btu/ft2-hr-F) 2.900

Clean coef (Btu/ft2-hr-F) 1.645 Area (ft2) 1488.6 Hot regime Sens. Gas Overdesign (%) -43.28

Cold regime Sens. Liquid Tube Geometry

EMTD (Deg F) 3.2 Tube type High-finned Duty (MM Btu/hr) 0.014 Tube OD (inch) 0.6250

Unit Geometry Tube ID (inch) 0.5270

Bays in parallel per unit 1 Length (ft) 8.250

Bundles parallel per bay 1 Area ratio(out/in) (--) 10.564

Extended area (ft2) 1488.6 Layout Staggered

Bare area (ft2) 167.12 Trans pitch (inch) 1.5000

Bundle width (ft) 2.121 Long pitch (inch) 1.2990

Nozzle Inlet Outlet Number of passes (--) 4

Number (--) 1 1 Number of rows (--) 8

Diameter (inch) 3.0680 3.0680 Tubecount (--) 128

Velocity (ft/sec) 2.26 2.26 Tubecount Odd/Even (--) 16 / 16 R-V-SQ (lb/ft-sec2) 253.17 253.36 Material Carbon steel

Pressure drop (psi) 0.027 0.013 Fin Geometry

Fan Geometry Type Rectangular

No/bay (--) 0 Fins/length (fin/inch) 5.0

Fan ring type Fin root (inch) 0.6450

Diameter (ft) 0.000 Height (inch) 0.4025 Ratio, Fan/bundle face area (--) 0.0000 Base thickness (inch) 0.0100 Driver (design/min. ambient) (hp) - / - Over fin (inch) 1.5372 Tip clearance (inch) 0.0000 Efficiency (%) 66.7 Efficiency (%) 0.0000 Area ratio (fin/bare) (--) 8.9 Fans turned-off (--) No Fans Material Carbon steel Airside Velocities Actual Standard Thermal Resistance, % Face (ft/min) 314.35 Air 21.85 Maximum (ft/sec) 10.58 Tube 77.93 Flow (1000 ft3/min) 5.500 Fouling 0.00 Velocity pressure (inH2O) 0.000 Metal 0.22 Bundle pressure drop (inH2O) 0.197 Bond 0.00 Bundle flow fraction (--) 1.000 Bundle 100.00 Airside Pressure Drop, % Louvers 0.00 Ground clearance 0.00 Fan guard 0.00 Hail screen 0.00 Fan ring 0.00 Fan area blockage 0.00 Steam coil 0.00

Super R adia to r C oils

Super Radiator Coils - www.SuperRadiatorCoils.com

104 Peavey Road Chaska, MN 55318-2324 - (800) 394-2645

Firm:

To:

Phone:

Fax:

Email:

Project:

Ellis & Watts

Cathy Roundtree

513-752-4983 eroundtree@elliswatts.com

EW 20200504 Dynalene AHUs

Company:

From:

Phone:

Fax:

Email:

Date:

Super Radiator Coils

Adam Horntvedt

952-556-3308 adam.horntvedt@superradiatorcoils.com

2/16/2021

Version: 4.5.1.0

Super Radiator Coils - Coil Schedule

Other Fluid Coil

Job Qty Coil Type Air Flow

[ACFM]

Capacity [Btu/Hr]

Entering Air DB

[°F]

Entering Air WB

[°F]

Leaving Air DB

[°F]

Leaving Air WB

[°F] Fluid Type

Sensible Capacity [Btu/Hr]

Flow Rate

[GPM]

Entering Fluid

Temp.

[°F]

Leaving Fluid Temp.

[°F]

Fin Side Pressure

Drop [In.H2O]

Tube Side Pressure

Drop [Ft.H2O]

AHU 12 1

DYNALENE HF-LO Coil

24x99 - 8R - 0.625/60 5,685 30,081 0 N/A -4.2 N/A N/A 30,081 52.2 -15 -11.8 0.18 2.4

AHU 13 1

DYNALENE HF-LO Coil

24x68 - 8R - 0.625/72 4,750 22,027 0 N/A -3.7 N/A N/A 22,027 35 -15 -11.5 0.29 1.3

AHU 14 1

DYNALENE HF-LO Coil

24x68 - 12R - 0.625/60 4,750 35,526 0 N/A -6 N/A N/A 35,526 75 -15 -12.4 0.38 3.8

S u p e r

R a d ia to r C o il s

Version: 4.5.1.0 © 2021

Customer:

Project:

Item:

Ellis & Watts

EW 20200504 Dynalene AHUs

AHU 12

Date:

By:

Units:

2/16/2021

Adam Horntvedt

English

Other Fluid Coil Coil Qty: 1 Model: 24x99 - 8R - 0.625/60

104 Peavey Road Chaska, MN 55318-2324 - (800) 394-2645

Super Radiator Coils - www.SuperRadiatorCoils.com

Airside Requirements:

Input

Coil Application: Cooling

Air Flow: ACFM 5,685

Capacity: Btu/Hr. 40,000

Entering Air Dry-Bulb: °F 0.0

Leaving Air Dry-Bulb: °F -5.6

Air Pressure: PSIA 14.696

Coil Hand: Left Hand

Tubeside Requirements:

Tubeside Fluid: DYNALENE HF-LO

Flow Rate: GPM 52.2

Entering Fluid Temperature: °F -15.0

Specific Heat: Btu/(lb·F) 0.4580

Specific Gravity: 0.7949

Viscosity: (cP) 5.0560

Thermal Conductivity: Btu/(hr·ft·F) 0.0690

Reference Temperature: °F 0.0

Output Coil Selection:

Model Number: 24x99 - 8R - 0.625/60

Tube Size: In. 0.625

Arrangement: 1.5 x 1.299 Staggered

Fin Surface: Flat

Face Area / Coil: ft² 16.5

Face Velocity / Coil: Ft/Min. (STD) 397.0

Number Of Circuits: Qty 32

Tube Velocity: Ft/Second 2.1

Reynolds Number: 1,440

Circuitry Flow: Thermal Counter Flow

Tube Material: Carbon Steel

Tube Wall: In. 0.049

Fin Material: Carbon Steel

Fin Thickness: In. 0.0100

Header Material: Sche.40 Carbon Steel

Header NPS: In. 3

Connection Material: Sche.40 Carbon Steel

Connection NPS: In. 3

Casing Material: 12 Ga. Carbon Steel

Casing Depth: In. 21.500

Dry Weight: Lbs./Coil 975

Standard Options:

Hot Dipped Galv.

Coil Rating Capacity:

Capacity / Coil: Btu/Hr. 30,081

Leaving Air Dry-Bulb: °F -4.2

Air Friction: In.H2O/Coil 0.18

Surface Condition: Dry

Leaving Fluid Temperature: °F -11.8

Fluid Pressure Drop: Ft.H2O/Coil 2.38

Internal Volume: ft³ 2.06 p e r

R a d ia to r C o il s

Version: 4.5.1.0 © 2021

Customer:

Project:

Item:

Ellis & Watts

EW 20200504 Dynalene AHUs

AHU 13

Date:

By:

Units:

2/16/2021

Adam Horntvedt

English

Other Fluid Coil Coil Qty: 1 Model: 24x68 - 8R - 0.625/72

104 Peavey Road Chaska, MN 55318-2324 - (800) 394-2645

Super Radiator Coils - www.SuperRadiatorCoils.com

Airside Requirements:

Input

Coil Application: Cooling

Air Flow: ACFM 4,750

Capacity: Btu/Hr. 29,300

Entering Air Dry-Bulb: °F 0.0

Leaving Air Dry-Bulb: °F -4.9

Air Pressure: PSIA 14.696

Coil Hand: Left Hand

Tubeside Requirements:

Tubeside Fluid: DYNALENE HF-LO

Flow Rate: GPM 35.0

Entering Fluid Temperature: °F -15.0

Specific Heat: Btu/(lb·F) 0.4580

Specific Gravity: 0.7949

Viscosity: (cP) 5.5600

Thermal Conductivity: Btu/(hr·ft·F) 0.0690

Reference Temperature: °F 0.0

Output Coil Selection:

Model Number: 24x68 - 8R - 0.625/72

Tube Size: In. 0.625

Arrangement: 1.5 x 1.299 Staggered

Fin Surface: Flat

Face Area / Coil: ft² 11.3

Face Velocity / Coil: Ft/Min. (STD) 482.9

Number Of Circuits: Qty 32

Tube Velocity: Ft/Second 1.4

Reynolds Number: 878

Circuitry Flow: Thermal Counter Flow

Tube Material: Carbon Steel

Tube Wall: In. 0.049

Fin Material: Carbon Steel

Fin Thickness: In. 0.0100

Header Material: Sche.40 Carbon Steel

Header NPS: In. 3

Connection Material: Sche.40 Carbon Steel

Connection NPS: In. 3

Casing Material: 12 Ga. Carbon Steel

Casing Depth: In. 21.500

Dry Weight: Lbs./Coil 741

Standard Options:

Hot Dipped Galv.

Coil Rating Capacity:

Capacity / Coil: Btu/Hr. 22,027

Leaving Air Dry-Bulb: °F -3.7

Air Friction: In.H2O/Coil 0.29

Surface Condition: Dry

Leaving Fluid Temperature: °F -11.5

Fluid Pressure Drop: Ft.H2O/Coil 1.35

Internal Volume: ft³ 1.49 p e r

R a d ia to r C o il s

Version: 4.5.1.0 © 2021

Customer:

Project:

Item:

Ellis & Watts

EW 20200504 Dynalene AHUs

AHU 14

Date:

By:

Units:

2/16/2021

Adam Horntvedt

English

Other Fluid Coil Coil Qty: 1 Model: 24x68 - 12R - 0.625/60

104 Peavey Road Chaska, MN 55318-2324 - (800) 394-2645

Super Radiator Coils - www.SuperRadiatorCoils.com

Airside Requirements:

Input

Coil Application: Cooling

Air Flow: ACFM 4,750

Capacity: Btu/Hr. 47,200

Entering Air Dry-Bulb: °F 0.0

Leaving Air Dry-Bulb: °F -7.9

Air Pressure: PSIA 14.696

Coil Hand: Left Hand

Tubeside Requirements:

Tubeside Fluid: DYNALENE HF-LO

Flow Rate: GPM 75.0

Entering Fluid Temperature: °F -15.0

Specific Heat: Btu/(lb·F) 0.4580

Specific Gravity: 0.7949

Viscosity: (cP) 5.0560

Thermal Conductivity: Btu/(hr·ft·F) 0.0690

Reference Temperature: °F 0.0

Output Coil Selection:

Model Number: 24x68 - 12R - 0.625/60

Tube Size: In. 0.625

Arrangement: 1.5 x 1.299 Staggered

Fin Surface: Flat

Face Area / Coil: ft² 11.3

Face Velocity / Coil: Ft/Min. (STD) 482.9

Number Of Circuits: Qty 32

Tube Velocity: Ft/Second 3.0

Reynolds Number: 2,069

Circuitry Flow: Thermal Counter Flow

Tube Material: Carbon Steel

Tube Wall: In. 0.049

Fin Material: Carbon Steel

Fin Thickness: In. 0.0100

Header Material: Sche.40 Carbon Steel

Header NPS: In. 3

Connection Material: Sche.40 Carbon Steel

Connection NPS: In. 3

Casing Material: 12 Ga. Carbon Steel

Casing Depth: In. 31.000

Dry Weight: Lbs./Coil 1,002

Standard Options:

Hot Dipped Galv.

Coil Rating Capacity:

Capacity / Coil: Btu/Hr. 35,526

Leaving Air Dry-Bulb: °F -6.0

Air Friction: In.H2O/Coil 0.38

Surface Condition: Dry

Leaving Fluid Temperature: °F -12.4

Fluid Pressure Drop: Ft.H2O/Coil 3.75

Internal Volume: ft³ 2.14

Unit: AHU 13 - 5/8" TubeZ:\UserFiles\AdamHorntvedt\Customers\Ellis and Watts\20200504-00-Low Temp Coils\AHU 13 0.625 Tube.htri

Output Summary Page 1

Released to the following HTRI Member Company:

SUPER RADIATOR COILS

ADAM HORNTVEDT

Xace 8.2 12/23/2020 10:55 SN: 00207-889033604 US Units

5F inlet Temp, 4750CFM : AHU 13 - 5/8" Tube Rating-Horizontal economizer countercurrent to crossflow

See Data Check Messages Report for Warning Messages.

See Runtime Message Report for Warning Messages.

Process Conditions Outside Tubeside Fluid name Air Dyanlene HFLO Fluid condition Sens. Gas Sens. Liquid Total flow rate (1000-lb/hr) 24.359 13.897 Weight fraction vapor, In/Out 1.0000 1.0000 0.0000 0.0000

Temperature, In/Out (Deg F) 5.00 0.08 -15.00 -10.50

Skin temperature, Min/Max (Deg F) -4.36 1.74 -4.41 1.71

Pressure, Inlet/Outlet (psia) 14.700 14.690 0.000 0.000

Pressure drop, Total/Allow (psi) (psi) 0.010 0.000 0.500 0.000

Midpoint velocity (ft/sec) 13.26 1.61

- In/Out (ft/sec) 1.60 1.61 Heat transfer safety factor (--) 1.0000 1.0000 Fouling (ft2-hr-F/Btu) 0.00000 0.00000

Exchanger Performance Outside film coef (Btu/ft2-hr-F) 8.06 Actual U (Btu/ft2-hr-F) 1.828

Tubeside film coef (Btu/ft2-hr-F) 25.05 Required U (Btu/ft2-hr-F) 1.846

Clean coef (Btu/ft2-hr-F) 1.828 Area (ft2) 1021.0 Hot regime Sens. Gas Overdesign (%) -0.96

Cold regime Sens. Liquid Tube Geometry

EMTD (Deg F) 15.3 Tube type High-finned Duty (MM Btu/hr) 0.029 Tube OD (inch) 0.6250

Unit Geometry Tube ID (inch) 0.5270

Bays in parallel per unit 1 Length (ft) 5.660

Bundles parallel per bay 1 Area ratio(out/in) (--) 10.564

Extended area (ft2) 1021.0 Layout Staggered

Bare area (ft2) 114.62 Trans pitch (inch) 1.5000

Bundle width (ft) 2.121 Long pitch (inch) 1.2990

Nozzle Inlet Outlet Number of passes (--) 4

Number (--) 1 1 Number of rows (--) 8

Diameter (inch) 3.0680 3.0680 Tubecount (--) 128

Velocity (ft/sec) 1.51 1.52 Tubecount Odd/Even (--) 16 / 16 R-V-SQ (lb/ft-sec2) 113.82 114.08 Material Carbon steel

Pressure drop (psi) 0.012 6.07e-3 Fin Geometry

Fan Geometry Type Rectangular

No/bay (--) 0 Fins/length (fin/inch) 5.0

Fan ring type Fin root (inch) 0.6450

Diameter (ft) 0.000 Height (inch) 0.4025 Ratio, Fan/bundle face area (--) 0.0000 Base thickness (inch) 0.0100 Driver (design/min. ambient) (hp) - / - Over fin (inch) 1.5372 Tip clearance (inch) 0.0000 Efficiency (%) 64.6 Efficiency (%) 0.0000 Area ratio (fin/bare) (--) 8.9 Fans turned-off (--) No Fans Material Carbon steel Airside Velocities Actual Standard Thermal Resistance, % Face (ft/min) 395.72 Air 22.67 Maximum (ft/sec) 13.32 Tube 77.09 Flow (1000 ft3/min) 4.750 Fouling 0.00 Velocity pressure (inH2O) 0.000 Metal 0.24 Bundle pressure drop (inH2O) 0.287 Bond 0.00 Bundle flow fraction (--) 1.000 Bundle 100.00 Airside Pressure Drop, % Louvers 0.00 Ground clearance 0.00 Fan guard 0.00 Hail screen 0.00 Fan ring 0.00 Fan area blockage 0.00 Steam coil 0.00

Tag:

Fan information

Size/Model . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .Class

Volumetric Flow Speed (RPM)

Max Speed

Power

SP

Outlet Vel150/BAE-DW II

5500 1653

4213 RPM @ 70 °F

2.54

2(in WC)

(BHP)

(FPM)

(CFM) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0.0864Density (lb/ft³)

Adjusted for (2) fans operating in parallel;Inlet Dens: 0.0864 lb/ft3

Customer:

Job ID:

Job Name:

Date: March 29, 2021

All quotations per Twin City Fan Terms and Conditions found at www.twincityfan.com/TC_TCF.pdf

Ver 10.1 October 2018 - Created Updated Owner

INDIVIDUAL FAN SOUND POWER

LwA: The individual sound power level in dB re. 10 Watts, ‘A’ weighted.

dBA: Estimated sound pressure level (re:0.0002microbar) based on a single ducted installation at 5 ft., using a directivity factor of 1.

TOTAL PACKAGE SOUND POWER

-12

LwA: The overall (single value) fan sound power level in dB re. 10 Watts, ‘A’ weighted.

dBA: Estimated sound pressure level (re:0.0002microbar) based on a single ducted installation at 5 ft., using a directivity factor of 1.

-12

INDIVIDUAL FAN SOUND PRESSURE

dBA: Estimated sound pressure level (re:0.0002microbar) based on a single ducted installation at 5 ft., using a directivity factor of 1.

Sound

Level at Inlet Level at Outlet

Octave Bands

LwA

Level at Inlet Level at Outlet

Octave Bands

LwA

Distance in

677181 687282 dBA at Outlet dBA at inlet

FAN DETAILS

Customer:

Job ID:

Job Name:

March 29, 2021Date:

Tag: N/A

Customer:

Job ID:

Job Name:

Date: March 29, 2021

AMCA Statements

1. Twin City Fan certifies that the model BAE-DW is licensed to bear the AMCA Seal. The ratings shown are based on tests and procedures performed in accordance with AMCA Publication 211 and AMCA Publication 311 and comply with the requirements of the AMCA Certified Ratings Program.

2. Performance certified is for Installation Type B & D: Free or ducted inlet, Ducted outlet.

3. Power rating (KW) does not include transmission losses.

4. The sound power level ratings shown are in decibels, referred to 10 E-12 watts calculated per AMCA Standard 301.

5. Values shown are for inlet Lwi and LwiA, and outlet Lwo and LwoA sound power levels for Installation Type B: Free inlet, Ducted outlet.

6. Ratings do not include the effects of duct end correction.

7. The A-weighted sound ratings shown have been calculated per AMCA Standard 301.

8. dBA levels are not licensed by AMCA International.

Tag:

Tag:

Fan information

Size/Model . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .Class

Volumetric Flow Speed (RPM)

Max Speed

Power

SP

Outlet Vel150/BAE-DW II

4750 1554

4213 RPM @ 70 °F

2.16

2(in WC)

(BHP)

(FPM)

(CFM) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 0.0883Density (lb/ft³)

Adjusted for (2) fans operating in parallel;Inlet Dens: 0.0883 lb/ft3

Customer:

Job ID:

Job Name:

Date: March 29, 2021

INDIVIDUAL FAN SOUND POWER

LwA: The individual sound power level in dB re. 10 Watts, ‘A’ weighted.

dBA: Estimated sound pressure level (re:0.0002microbar) based on a single ducted installation at 5 ft., using a directivity factor of 1.

TOTAL PACKAGE SOUND POWER

-12

LwA: The overall (single value) fan sound power level in dB re. 10 Watts, ‘A’ weighted.

dBA: Estimated sound pressure level (re:0.0002microbar) based on a single ducted installation at 5 ft., using a directivity factor of 1.

-12

INDIVIDUAL FAN SOUND PRESSURE

dBA: Estimated sound pressure level (re:0.0002microbar) based on a single ducted installation at 5 ft., using a directivity factor of 1.

Sound

Level at Inlet Level at Outlet

Octave Bands

LwA

Level at Inlet Level at Outlet

Octave Bands

LwA

Distance in

667080 677181 dBA at Outlet dBA at inlet

FAN DETAILS

Customer:

Job ID:

Job Name:

March 29, 2021Date:

Tag: N/A

Customer:

Job ID:

Job Name:

Date: March 29, 2021

AMCA Statements

1. Twin City Fan certifies that the model BAE-DW is licensed to bear the AMCA Seal. The ratings shown are based on tests and procedures performed in accordance with AMCA Publication 211 and AMCA Publication 311 and comply with the requirements of the AMCA Certified Ratings Program.

2. Performance certified is for Installation Type B & D: Free or ducted inlet, Ducted outlet.

3. Power rating (KW) does not include transmission losses.

4. The sound power level ratings shown are in decibels, referred to 10 E-12 watts calculated per AMCA Standard 301.

5. Values shown are for inlet Lwi and LwiA, and outlet Lwo and LwoA sound power levels for Installation Type B: Free inlet, Ducted outlet.

6. Ratings do not include the effects of duct end correction.

7. The A-weighted sound ratings shown have been calculated per AMCA Standard 301.

8. dBA levels are not licensed by AMCA International.

Tag:

Copyright © 2014 Dynalene, Inc. All Rights Reserved. EG Engineering Guide | 0

Dynalene HF-LO engineering guide http://www.dynalene.com/terms.asp

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 1

Contents

Product Overview 2

Freezing & Melting Point 2

Flash Point 2

Vapor Pressure 2

General Properties 3

Packaging & Shipping 3

Shelf Life 4

Metals Compatibility 4

Gasket & Polymer Compatibility 4

General Installation Guidelines 4

Retrofitting for Dynalene HF-LO 6

Preparing New Systems Using Dynalene HF-LO 7

Ongoing Fluid Maintenance 7

Basic Heat Transfer Fluid System Design 8

Dynalene HF-LO Properties: SI Units 9

Dynalene HF-LO Properties: English Units 10

Toxicology Report 11

Product Disclaimer 11

Locations & Contact Information 11

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 2

Product Overview

Dynalene HF-LO is a high flash point, low odor, non-toxic heat transfer fluid. It was developed as an alternative to silicone oils for low temperature applications. Dynalene HF-LO heat transfer fluid is also biodegradable and CFC free. Dynalene HF-LO has a recommended use temperature range of –100°F to 400°F for closed systems. It is essential that all personnel handling this product review and understand this manual and the Dynalene HF-LO material safety data sheet (MSDS). Please contact Dynalene for more information.

Freezing & Melting Point

Dynalene HF-LO has a freezing and melting point below -118°C (-180°F), allowing broader application to systems using cryogenic liquids or ultra-low temperature mechanical refrigeration equipment. This results in greater tolerance when lowering the surface film temperature.

Flash Point

Dynalene HF-LO heat transfer fluid has a closed cup flash point of >61°C (>141°F), and an open cup flash point of >68°C (>156°F). When the vapor of a hydrocarbon fluid becomes concentrated and heated above its flash point, the vapor has the potential to ignite if it is exposed to hot surfaces, sparks, open flames, or any other source of ignition.

Vapor Pressure

Vapor pressure is a critical property to be considered when calculating Net Positive Suction Head (NPSH), a major factor in the sizing of fluid handling equipment. “Air tight” containment is recommended to limit the escape of

Dynalene HF-LO vapors to the environment, and to prevent the exposure of the fluid to moisture and oxygen. See

Table 1 below for vapor pressures of Dynalene HF-LO at various temperatures.

Table 1. Vapor pressure of Dynalene HF-LO.

Temperature, °C (°F) Vapor Pressure, mmHG (psi)

0 (32) 0.12 (0.002)

25 (77) 0.71 (0.014)

100 (212) 1.80 (0.035)

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 3

General Properties General properties of Dynalene HF-LO can be found in Table 2.

Table 2. General properties of Dynalene HF-LO.

Property

Composition Aliphatic hydrocarbon blend

Appearance Translucent, clear

Odor Low hydrocarbon odor

Operating range, closed systems -73°C to 204°C (-100°F to 400°F)

Operating range, open systems -52°C to 58°C (-60°F to 135°F)

Max film temperature 232°C (450°F)

Freezing point <-118°C (<-180°F)

Boiling point >191°C (376°F)

Flash point (closed) >61°C (>141°F)

Flash point (open) >68°C (>156°F)

Fire point 72°C (162°F)

Autoignition temp. >337°C (>640°F)

Critical temp. 394°C (741°F)

Critical pressure 27 bar (26.7 atm)

Molecular weight 150 g/mol

Dielectric constant 2.1 to 2.2

Packaging & Shipping

Dynalene HF-LO heat transfer fluid is available in 5 gallon pails, 55 gallon drums, and bulk quantities.

The following is the transportation and shipping regulatory information for Dynalene HF-LO:

Land (DOT): Proper shipping name: PETROLEUM DISTILLATES, N.O.S.

Hazard Class and Division: COMBUSTIBLE LIQUID

UN Number: 1268

Packing Group: III

Land (TDG): Not regulated for land transport.

Sea (IMDG): Not regulated for sea transport according to IMDG-code.

Air (IATA): Not regulated for air transport.

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 4

Shelf Life

Dynalene HF-LO heat transfer fluid will remain stable for a period of at least one year if:

(1) It is stored in the original unopened pail or drum

(2) The storage area is a dry environment below 100°F.

Partially full pails and drums should be blanketed with an inert gas such as nitrogen to eliminate oxygen from the container head space.

Metals Compatibility

Dynalene HF-LO heat transfer fluid has an acceptable compatibility rating when installed in vapor tight systems constructed within the temperature, pressure, and structural limitations of the following metals:

• Aluminum

• Brass

• Bronze (All)

• Carbon Steel

• Cast Steel

• Copper

• Copper Nickel (All)

• Hastelloy (All)

• Inconel

• Incoloy 825

• Monel

• Nickel

• Stainless Steel (All)

• Stainless Steel Clad

• Tantalum

Gasket & Polymer Compatibility

Dynalene HF-LO heat transfer fluid has an acceptable compatibility when used within the temperature and pressure limitation of the following polymers or gasketing materials:

• Acetal

• Aramid Fiber

• Chemraz (FFKM)

• Epoxy

• Fluorocarbon (FILM)

• Fluoroelastomer

• Glass Fiber

• Gylon Style 3500, 3504, & 3510

• Kalrez

• PEEK

• Polytetrafluoro-ethylene

• Teflon (All)

• Teflon Encapsulated Silicone

• Teflon Encapsulated Viton

• Telfon Impregnated Fiberglass

• Kel-F (CTE)

Viton

• Resin Impregnated Carbon Graphite

General Installation Guidelines

The following recommendations are provided to assist the designer/user in achieving proper installation.

1 Understanding the engineering guide

Prior to purchasing any Dynalene HF-LO, review and understand all of the information contained in this manual—especially the sections titled ‘Retrofitting for Dynalene HF-LO’ and ‘Preparing New Systems Using

Dynalene HF-LO’. Only qualified personnel with expertise in safe handling of potentially hazardous liquids

(in compliance with local, state, and federal regulations) should be involved with work processes of this nature.

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 5

2 Moisture content

Moisture content within Dynalene HF-LO in system operation is recommended to be less than 100 parts per million (.01% H20 in Dynalene HF-LO). The freezing point, viscosity, and heat transfer coefficient of

Dynalene HF-LO may be adversely affected if moisture content is above recommended levels. Moisture is heavier than Dynalene HF-LO and will drop out of the solution at approximately 400 to 500 PPM, depending upon liquid temperature.

In low temperature applications, excessive moisture in Dynalene HF-LO will impair heat transfer; this may result in frozen heat exchangers, seized regulators, etc. Desiccating Dynalene HF-LO as shown in Figure 1

(page 8) is one recommended method of removing moisture from Dynalene HF-LO. If a moisture analysis is required for your Dynalene HF-LO, contact Dynalene at 1-877-244-5525 or email info@dynalene.com.

3 Presence of oxygen

Limit the presence of oxygen within the wetted areas of a piped system. An inert gas, such as nitrogen, is the favored substitute to air in the vapor space. A replenishable supply of air or oxygen in contact with

Dynalene HF-LO will promote premature fluid degradation. The basic fluid system sketch illustrated in

Figure 1 (page 8), is an example of a typical Dynalene HF-LO heat transfer fluid system using an inert gas purge as a method of excluding oxygen. The inert gas pressure regulator BPV set point should be approximately 50% higher than the maximum Dynalene HF-LO vapor pressure value anticipated with the system.

4 Maximum surface temperature

Surface temperature of heat source components should not exceed 450°F (232°C). Fluid velocity should maintain a minimum of 8 feet per second (2.44 meters per second).

5 Using electric resistance heaters

Electric resistance heaters used in Dynalene HF-LO heat transfer fluid applications are recommended to use a maximum watt density of 28 watts per square inch. If you require a review on the heating equipment you have considered, consult Dynalene.

6 Pump equipment

To eliminate cavitation when using Dynalene HF-LO near its boiling point, apply sufficient inert gas

(nitrogen, argon) pressure in the head space.

7 Available ancillary equipment

Dynalene desiccation canisters are available upon request.

8 Safety dos and don’ts

Handling Dynalene HF-LO in the drum: ensure drums containing Dynalene HF-LO are properly grounded and keep all drums away from sources of ignition, power tools, heat, smoking, and sparks.

Pumping Dynalene HF-LO into the system: only pump Dynalene HF-LO in well-ventilated areas and wear the required personnel protective equipment as recommended in the Dynalene HF-LO MSDS.

System maintenance: prior to cutting or welding systems that use Dynalene HF-LO, ensure all residual

Dynalene HF-LO and its vapor are removed from the system. This can be accomplished by fully purging and evacuating all fluid and vapors using the methods described in ‘Retrofitting for Dynalene

HF-LO.’

Draining Dynalene HF-LO from a system: when draining Dynalene HF-LO from a system, be sure to use sealed connections on all pipes, tubes, and containment to minimize leakage of vapor and mists.

For precautionary measures, all systems using Dynalene HF-LO should be properly grounded.

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 6

Retrofitting for Dynalene HF-LO

Dynalene HF-LO heat transfer fluid is an excellent replacement for the fluid chemistries listed below:

• CFC Refrigerant

• Chlorinated Solvent

• HFC Refrigerant

• Hydrocarbon Based

• Alcohols (methanol, ethanol, isopropanol)

• Perfluorocarbon

• Silicone

• d-Limonene

Once the original liquid is removed, systems may retain small amounts of residual liquid in low lying areas such as piping traps, inverted coils, pump housings, valve housings, drain pipes, etc. The residual liquids must be removed for Dynalene HF-LO to function properly as specified.

The following recommendations are provided by Dynalene to assist the installer or end user in achieving a successful retrofit:

To determine the actual volume of the heat transfer fluid needed in the retrofit, there are two methods that can be used:

1. If the system drawing is available, then perform a volume calculation based on size and length of piping, reservoirs, heat exchangers, pumps, and all other wetted components.

2. Drain the existing heat transfer fluid from the system and measure the volume removed. To account for the residual fluid left after draining, follow the steps in the next section.

To remove residual fluids, purge the existing system with compressed air or an inert gas such as nitrogen (for combustible liquids). For best results, purge intermittently with disruptions to zero pressure once every two minutes. For example, purge with pressure for one minute, and then disrupt purge to zero pressure in system for the next minute. Continue this process for several minutes until there is no more fluid leaving the system.

Measure the volume of the residual fluid and add to the volume of the drained fluid to determine the total heat transfer fluid volume. Combine the residual fluid and drained fluid into a vented container and dispose accordingly.

Other methods to remove residual liquid:

1 System evacuation

Systems evacuation is performed by creating a vacuum, usually more than 20" Hg, within the existing system containing the residual liquid at room temperature. As the vacuum within the system increases, the boiling point of the residual liquid will decrease and evaporate. The intent is to evaporate the residual liquid completely by lowering its boiling point to below the internal temperature of the system.

2 Air and inert gas evaporation

Liquid evaporation using air or an inert gas may be another feasible method of removing residual liquid from an existing piped system. This is performed by allowing an adequate volume of dry compressed air or inert gas, such as nitrogen, to enter the existing system and flow through the inner piped wetted areas, including low points. The intent is to evaporate the residual liquid and allow the effluent to exit the piped system at a point that is generally opposite the inlet air or inert gas connection. Compressed air or inert gas is recommended to have a dew point lower than –95°F, and sufficiently below the evaporation point of liquid being removed.

3 Dilution

Dilution of residual fluid can be performed in conjunction with the system evacuation or evaporation methods. Dilution of the residual fluid can be performed by selecting a dilution solvent that is miscible with the residual fluid and has a high vapor pressure.

After diluting the residual fluid with the solvent, drain and follow either step 1 or 2.

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 7

Preparing New Systems Using Dynalene HF-LO

The following recommendations are provided to assist the installer or end user in achieving a proper installation:

1 Flush the system

Systems intending to use Dynalene HF-LO heat transfer fluid should be properly flushed clean after installing components such as pipes, valves, pumps, etc. Materials from welding operations, excess pipe joint compound, oils, and other unwanted contaminants must be removed completely prior to installing

Dynalene HF-LO.

Using a dilution solvent that is completely miscible with the contaminants generated during an installation is one recommended method of flushing a system clean.

2 Perform a moisture analysis

After installing Dynalene HF-LO and circulating for at least one hour, Dynalene recommends removing a fluid sample for moisture analysis. A pre-labeled sample kit will be provided upon request. Dynalene will perform a moisture analysis and report the necessary actions or corrections that need to be taken. This is to ensure the moisture content is within the recommended level, especially when operating

Dynalene HF-LO below 35°F.

3 Install line filtration

Dynalene HF-LO should remain free of debris throughout the operational life of the liquid. An appropriately sized in-line strainer using a perforation size (1⁄32") or less, is recommended to be installed directly in the flow of fluid to allow the most effective particulate removal from the fluid. Providing filtration down to approximately 5 microns, combined with an in-line strainer as a prefilter, is the best method of keeping

Dynalene HF-LO particulate free. Use of bypass and slip-stream filtration is also acceptable.

Ongoing Fluid Maintenance

Dynalene can provide a pre-labeled sample kit upon request, which includes the sample bottle, an instruction page, and an MSDS sheet. Dynalene offers the first sample analysis free of charge.

For best results:

1. Take a fluid sample when the system is at room temperature to prevent moisture from contaminating the

Dynalene HF-LO.

2. Before filling up the sample bottle, allow the fluid to flow out for a few seconds into another container to clear any debris. Leave about one inch of airspace from the top of the sample bottle to minimize leakage.

After closing the cap, secure by wrapping electrical tape around it several times.

3. It is best to take a fluid sample while the fluid is circulating.

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 8

Basic heat transfer fluid system design

Figure 1. Basic Dynalene HF-LO heat transfer system.

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 9

Dynalene HF-LO Properties: SI Units

Properties of Dynalene HF-LO vs. temperature in SI units are given in Table 3.

Table 3. Properties of Dynalene HF-LO.

Temp Viscosity Thermal Cond. Specific Heat Density

°C mPa·s W/m·K kJ/kg·K kg/m3

-73 70.2 0.1272 1.742 833

-70 52.7 0.1266 1.753 831

-60 23.9 0.1246 1.791 823

-50 13.3 0.1226 1.829 816

-40 8.40 0.1206 1.867 808

-30 5.80 0.1186 1.905 800

-20 4.20 0.1166 1.943 793

-10 3.20 0.1146 1.981 785

0 2.50 0.1126 2.019 778

10 2.00 0.1106 2.057 770

20 1.60 0.1086 2.095 762

30 1.40 0.1066 2.133 755

40 1.20 0.1046 2.171 747

50 1.00 0.1026 2.209 740

60 0.87 0.1006 2.247 732

70 0.77 0.0986 2.285 724

80 0.68 0.0966 2.323 717

90 0.60 0.0946 2.361 709

100 0.54 0.0926 2.399 702

110 0.49 0.0906 2.437 694

120 0.44 0.0886 2.475 686

130 0.40 0.0866 2.513 679

140 0.37 0.0846 2.551 671

150 0.34 0.0826 2.589 664

160 0.31 0.0806 2.627 656

170 0.29 0.0786 2.665 649

177 0.27 0.0772 2.692 643

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 10

Dynalene HF-LO Properties: English Units

Properties of Dynalene HF-LO vs. temperature in English units are given in Table 4.

Table 4. Properties of Dynalene HF-LO.

Temp Viscosity Thermal Cond. Specific Heat Density

°F cP BTU/hr·ft·°F BTU/lb·°F lb/ft3

-100 72.5 0.0749 0.416 51.9

-80 28.0 0.0736 0.426 51.4

-60 14.1 0.0722 0.436 50.9

-40 8.40 0.0709 0.446 50.3

-20 5.50 0.0696 0.456 49.8

0 3.90 0.0683 0.466 49.3

20 2.90 0.0670 0.476 48.8

40 2.30 0.0657 0.487 48.2

60 1.80 0.0644 0.497 47.7

80 1.50 0.0631 0.507 47.2

100 1.20 0.0618 0.517 46.7

120 1.00 0.0605 0.527 46.1

140 0.87 0.0592 0.537 45.6

160 0.76 0.0579 0.547 45.1

180 0.66 0.0566 0.557 44.6

200 0.58 0.0553 0.567 44.0

220 0.52 0.0539 0.577 43.5

240 0.46 0.0526 0.587 43.0

260 0.41 0.0513 0.598 42.5

280 0.37 0.0500 0.608 41.9

300 0.34 0.0487 0.618 41.4

320 0.31 0.0474 0.628 40.9

340 0.28 0.0461 0.638 40.3

350 0.27 0.0455 0.643 40.1

Copyright © 2014 Dynalene, Inc. All Rights Reserved. HF-LO Engineering Guide | 11

Toxicological Report

For complete toxicological information regarding Dynalene HF-LO, consult the MSDS. The MSDS for Dynalene HF-

LO should be understood prior to use.

Product Disclaimer

The information contained in this entire publication is presented in good faith at “no charge” and is believed to be correct as of the date indicated no representations or warranties are made as to its completeness or accuracy. The information listed is supplied upon the condition that the persons receiving it will make their own determination as to its suitability for their purposes prior to use. In no event will the seller be responsible for damages of any nature whatsoever resulting from the use of, or reliance upon, this information or the product to which this information refers. Nothing contained on this page is to be construed as a recommendation to use the product, process, equipment or formulation in conflict with any patent. No representation or warranty, expressed or implied, is made that the use of this product will not infringe any patent.

No representations or warranties, either expressed or implies, of merchantability, fitness for a particular purpose or for any other nature are made with respect to the information, or the product to which the information refers.

Locations & Contact Information

Corporate Headquarters

Dynalene, Inc.

5250 West Coplay Road

Whitehall, PA 18052

Phone: 610-262-9686 / 1-877-244-5525

Fax: 610-262-7437

Email: info@dynalene.com

Website: www.dynalene.com

Midwest Location

648 Bennett Road

Elk Grove Village, IL 60007

Phone: 1-855-216-7639

West Location

1701 S 5350 W

Salt Lake City, UT 84104

Phone: 1-877-244-5525

Pump size & type / Stages : 1E1.5x1SP-82RV / 1 Based on curve no. : MIII7044AV Impeller diameter : 7.88 in

Customer : - Item number : Sump Glycol Pump Service : - Flowserve reference : 3245447589 Date : March 23, 2021

Capacity : 25.0 USgpm Head : 25.00 ft Density / Specific gravity : - / 1.123 Pump speed : 1150 rpm Ns / Nss : 726 / 7930 (US units) Test tolerance : ANSI/HI 14.6 Grade 1B

CURVES ARE APPROXIMATE, PUMP IS GUARANTEED FOR ONE SET OF CONDITIONS; CAPACITY, HEAD, AND EFFICIENCY.

The customer must provide a minimum NPSHa of 1.1 ft.

Copyright © 2016 Flowserve. All rights reserved. Affinity v2.18.2

Hydraulic Datasheet

Customer : - Customer reference : NIST Brine Pump Item number : Sump Glycol Pump Service : -

Pump / Stages : 1E1.5x1SP-82RV / 1 Based on curve no. : MIII7044AV Flowserve reference : 3245447589 Date : March 23, 2021

Operating Conditions Capacity : 25.0 USgpm Water capacity (CQ=0.94) : 26.7 USgpm Normal capacity : - Rated head @ Discharge flange : 25.00 ft Water head (CH=0.96) : 26.06 ft NPSH available (NPSHa) @ Low liquid level : Ample NPSHa less NPSH margin @ Impeller eye : - Maximum suction pressure : 0.0 psig

Liquid Liquid type : Other Liquid description : - Temperature : 60 °F Specific gravity / Viscosity : 1.123 / 17.80 cSt

Materials / Specification / Construction Material column code : C Pump specification : - Pump construction : Standard, External Lube Pump length : 1.74 ft Tailpipe length : -

Other Requirements Hydraulic selection : No specification Construction : No specification Test tolerance : ANSI/HI 14.6 Grade 1B Driver Sizing : Max Power(MCSF to EOC) using SF Seal configuration : Lipseal

Performance Hydraulic power : 0.18 hp Pump speed : 1150 rpm Pump overall efficiency (CE=0.74) : 28.6 % NPSH required (NPSH3) @ Impeller eye : 1.1 ft Rated brake power : 0.62 hp Maximum brake power : 0.82 hp Driver power rating : 1.00 hp / 0.75 kW Casing working pressure : 13.6 psig (based on shut off @ cut dia/rated SG)

Maximum allowable : 250.0 psig Casing hydrotest : 375.0 psig Minimum submergence : 12.00 in Pump thrust at rated flow : 2.3 lbf

Impeller diameter Rated : 7.88 in Maximum : 8.19 in Minimum : 5.00 in

Ns / Nss : 726 / 7930 (US units) Minimum continuous flow : 4.8 USgpm Maximum head at rated diameter : 28.04 ft Flow at BEP : 41.6 USgpm Flow as % of BEP : 60.1 % Efficiency at normal flow : - Impeller diameter ratio (rated/max) : 96.2 % Head rise to shut off : 12.1 % Total head ratio (rated / max) / (max / rated) : 92.4 % / 108.2 %

CURVES ARE APPROXIMATE, PUMP IS GUARANTEED FOR ONE SET OF CONDITIONS; CAPACITY, HEAD, AND EFFICIENCY.

The customer must provide a minimum NPSHa of 1.1 ft.

Construction Datasheet

: March 23, 2021

Pump / Stages Based on curve no.

: 1E1.5x1SP-82RV

: 3245447589Flowserve reference Date

/ 1

: MIII7044AV

Pump / Stages

: March 23, 2021

Customer Customer reference

Service Item number

: Sump Glycol Pump : NIST Brine Pump

: Standard, External Lube : Reverse Vane : .25" Opening : Flanged : 1.66 ft : 1.74 ft

: ASTM A395 Gr60-40-18 : ASTM A536 Gr60-40-18

: 357.0 lb : 53.0 lb

: Flowserve Choice : 1.00 hp / 0.75 kW1.0/1.15

: 145TC

: Direct on line (DOL) : F : 80 °C

: 62.0 dBA

: No Seal or Packing : N/A

: Not Supplied : Not supplied : 2344 rpm

Piping below mounting plate:

Lubrication Lines - Polymer Braided Hose

: N/A : N/A

Pump construction

Impeller fastening Impeller type

Suction strainer Column construction Pit / sump depth Pump length

(mounting surface to flange/strainer) Tailpipe length

Casing Impeller Case wear ring Impeller wear ring Suction strainer Column Column hardware

Complete pump Pit cover Driver (net) Shipping gross weight/volume

Pump paint Support plate paint Shipment type

Manufacturer Power / SF (Req' / Act')

Motor Thrust rating down/up

Amps-full load/locked rotor Motor starting Insulation

Enclosure Hazardous area class Explosion 'T' rating Volts / Phase / Hz

Frame size / Base dia Driver type

Driver, expected Pump & driver, estimated

Arrangement Size

Material code (Man'f/API)

Seal flush construction

Float switch type Float switch rating Critical speed

Construction Driver Information

Materials

Weights (Approx.)

Paint and Package

Sound Pressure (dBA @ 1.0 m)

Seal Information

Additional information

Notes

: 492.0 lb / 14.15 cu.ft

: 460 / 3 / 60 Hz

: N/A / N/A : N/A / N/A

Manufacturer / Type

Lineshaft brg spacing Lineshaft bearings, qty

Bearing number (thrust) Disch size/rating/face Pump/driver coupling Support plate shape Pit cover type

: 48.00 in(maximum) : 1

: 7308BEGAM

: 2.00 / 150# ANSI / RF

: Woods Sureflex 5S : Round : No pit cover

Gland material Seal flush plan

: N/A : None : Not supplied

: Chesapeake System 1 : Chesapeake System 1 : Domestic

Testing Hydrostatic test Performance test NPSH test

: Non witnessed : None : None

Temperature rise Bearings / Lubrication Motor mounted by

: NEMA

: TEFC-SD

: Customer

Lineshaft Lineshaft bearing Lineshaft sleeve Lower bearing bush Lower bearing sleeve Shaft coating Pit cover Support plate

: Polypropylene

: ASTM A53 TYPE S/A105

: Alloy Steel

: AISI 1040

: Carbon graphite : N/A : Carbon graphite : N/A : None : N/A : Carbon Steel

: Ball / Grease

Lineshaft lubrication : External

Full Page GA Drawing

Customer : - Item number : Sump Glycol Pump Service : - Customer PO # : - Flowserve reference : 3245447589

Pump size & type : 1E1.5x1SP-82RV Pump speed / Stages : 1150 rpm / 1 Flow / Head : 25.0 USgpm / 25.00 ft Driver power / Frame : 1.00 hp / 0.75 kW / 145TC Volts / Phase / Hz : 460 / 3 / 60 Hz

Drawing number : - Date : March 23, 2021 Certified by / Date : : - Seal type : N/A Seal flush plan : None

Item number : Sump Glycol Pump Service : - Flowserve reference : 3245447589 Pump size & type / Stages : 1E1.5x1SP-82RV / 1 Based on curve no. : MIII7044AV Impeller diameter : 7.88 in

Capacity : 25.0 USgpm Head : 25.00 ft Density / Specific gravity : - / 1.123 Pump speed : 1150 rpm Ns / Nss : 726 / 7930 (US units) Pump WR² at 1150 rpm : -

Date : March 23, 2021 CURVES ARE APPROXIMATE, PUMP IS GUARANTEED FOR ONE SET OF CONDITIONS; CAPACITY, HEAD, AND EFFICIENCY.

Additional Details

Customer : - Pump / Stages : 1E1.5x1SP-82RV / 1 Customer reference : NIST Brine Pump Based on curve no. : MIII7044AV Item number : Sump Glycol Pump Flowserve reference : 3245447589 Service : - Date : March 23, 2021

Duty Conditions Quantity of pumps : 1 Liquid description : - Liquid type : Other Frequency : 60 Hz Flammable : No Toxic : No H2S : No Rated flow : 25.0 USgpm Rated head : 25.00 ft @ Discharge flange NPSHa : Ample @ Low liquid level Viscosity : 17.80 cSt Specific gravity : 1.123 Maximum suction pressure : 0.0 psig Rated suction pressure : 0.0 psig Maximum liquid temperature : 60 °F Vapor pressure : - Altitude : - Static head : - Pump length strategy used : Maximize length for sump depth

Performance Hydraulic power : 0.18 hp Pump overall efficiency : 28.6 % NPSH3 @ Impeller eye : 1.1 ft Rated brake power : 0.62 hp Maximum brake power : 0.82 hp Motor rating : 1.00 hp / 0.75 kW Ns / Nss : 726 / 7930 (US units) MCSF : 4.8 USgpm Rated impeller diameter : 7.88 in Maximum impeller diameter : 8.19 in Minimum impeller diameter : 5.00 in Maximum head : 28.04 ft Flow at BEP : 41.6 USgpm Flow as % of BEP : 60.1 % Rated/max diameter : 96.2 % Head rise to shut off : 12.1 % Rated/max head : 92.4 % Visc. capacity correction factor (CQ) : 0.94 Visc. head correction factor (CH) : 0.96 Visc. efficiency correction factor (CE) : 0.74

Selection status Product line : ESP3 Vertical Sump Pump speed : 1150 rpm

Business unit : Chesapeake Selection status : Acceptable

Working Pressure Limits Casing pressure : 13.6 psig (based on shut off @ cut dia/rated SG) Casing Assembly MAWP : 250.0 psig Pressure above liquid : 0.0 psig Max allowable pressure above liquid : 0.0

Orifice Plate Calculated diameter : -

Hydrostatic Test Pressures (when purchased) Casing hydrotest pressure : 375.0 psig Discharge region hydrotest pressure : 375.0 psig Suction region hydrotest pressure : 375.0 psig

Additional Performance Power rating (max/rated) : 0.07 hp/100 rpm / 0.05 hp/100 rpm Power limit impeller :

Power limit lineshaft :

Materials Requested pump material : C Selected pump material : C Casing material : ASTM A395 Gr60-40-18 Impeller material : - Lineshaft material : AISI 1040

Sump & Submergence User defined well / sump opening : - Required minimum well / sump opening : - User defined pit depth : 1.66 ft Min req. pit depth for pump length : - Combined bowl & column assembly length : 1.74 ft Clearance from strainer/bearing hub to sump bottom : - Available submergence above bell lip : - Req. min. submergence above bell lip : 12.00 in User defined NPSHa : Ample User defined mounting surf. to LLL : -0.01 ft Max allowed LLL for pump length : - NPSHa at eye of impeller : Ample NPSH3 @ Impeller eye : 1.1 ft

Copyright © 2016 Flowserve. All rights reserved. 1/2 Affinity v2.18.2

Customer : - Pump / Stages : 1E1.5x1SP-82RV / 1 Customer reference : NIST Brine Pump Based on curve no. : MIII7044AV Item number : Sump Glycol Pump Flowserve reference : 3245447589 Service : - Date : March 23, 2021

Performance Corrections Head Corrections

Rated head at discharge flange : 25.00 ft Discharge pressure at discharge flange : 12.2 psig Discharge flange face to mounting surface : 7.25 in Mounting surface to low liquid level : -0.01 ft Discharge pipe friction loss : 0.02 ft Elbow friction loss : 0.45 ft Increaser friction loss : 0.03 ft Tailpipe friction loss : - Rated head at casing : 26.09 ft

Efficiency Corrections Bowl efficiency after correction : 30.5 % Pump overall efficiency : 28.6 %

Capacity Corrections Rated flow at discharge flange : 25.0 USgpm Bearing flush loss : - Seal flush loss : - Separator loss : - Rated flow at casing : 26.7 USgpm

Power Corrections Casing horsepower : N/A Mechanical seal/packing horsepower loss : - Overall brake horsepower : 0.62 hp

Construction and Dimensions Casing Assembly Construction

Strainer supply : .25" Opening Tailpipe selection method : Automatic select

Casing Assembly Dimensions Casing assembly length : 8.31 in Strainer length : 4.88 in Casing discharge centerline to suction flange : 4.00 in Tailpipe length : -

Column Assembly Construction Separators : 0 Construction : Standard, External Lube Lineshaft lubrication : External Shaft sealing method : Lipseal Total no. of lineshaft bearings : 1

Column Assembly Dimensions Lineshaft diameter : 1.13 in Bearing span : 48" Column length : 0.68 ft

Discharge Head Assembly Construction Discharge pipe size : 2.00 in Discharge flange spec./rating : -

Discharge Head Assembly Dimensions Discharge pipe configuration (size) : Oversized discharge pipe Flange height above mounting plate : 7.25 in C/L casing discharge flange to mounting surface : 12.00 in Shaft diameter through stuffing box : 1.13 in

Mechanical Data Total net down thrust at rated conditions : 2.3 lbf Thrust bearing life limit (rated) : - Thrust bearing life limit (shut off) : - Thrust bearing life (rated) : - Thrust bearing life (shut off) : -

1st critical speed : 2316 rpm 2nd critical speed : 9262 rpm Bearing configuration : - Pump WR² at 1150 rpm : -

Additional Notes

Copyright © 2016 Flowserve. All rights reserved. 2/2 Affinity v2.18.2

Industrial Engineering and Equipment Company 425 Hanley Industrial Ct.

Saint Louis MO 63144 314-644-4305 Ext. 240 • Fax 314-644-5332

To Company: Boland Trane Date: March 29, 2021

Pages: 1 of 4

Attention: Kevin Chou

From: Mark Cornwell

Subject: INDEECO…