heat xfer/radcon progress 20oct2006 by john tang benton white

11
Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

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Page 1: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Heat Xfer/RadCon Progress20Oct2006

By

John Tang

Benton White

Page 2: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Heat Xfer Requirements

• Max differential pressure:– Across Clinac=6psi– Across

chiller=4.1psi

• Flow rate across piping=4.3GPM

• 30kW heat dissapation req’d

Page 3: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Heat Xfer Constraints

• Flexible tubing for piping – Fit in confined spaces– Allows for flexible placement of heat xfer

components

• Maintenance considerations– Access to essential components (ie: pump,

reservoir tank) easier– Isolation valves

Page 4: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Vendor Candidates             

VendorContact

InfoDimesion (in)

Weight (lbs)

PowerRequirements

Cooling Capacity

(kW)

Temp range (deg C)

Pressure available

for piping

Liebert1050 Dearborn

DrW 77x H 69.25

x D 38.5 750 2.2 pump kW 25.2 10 to 25 50 psi

  PO Box 29186     460V 60 Hz 3 phase      

 Columbus, OH

43229     208/230V      

  800-877-9222            

ThermoNESLAB 800-258-0830

W 12.6 x H 23.5 x D 20.9 120

115V, 60Hz, 15 Amps 1.25 5 to 35  

 www.thermo.com

/   

or 230V, 50Hz, 8 Amps  

Ambient 13 to 35C  

            55 to 95F  

Page 5: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Pipe Flow Analysis2

( )2L

L vh f k

D g

_

/

_ _

Lh headloss

f friction factor

Llength diameter

Dk pipebend loss coefficients

Page 6: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Pipe Flow Analysis (cont.)

Page 7: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Pipe Flow Analysis (cont.)

• Use Moody Diagram to find friction factors• Find Reynold’s Number, Re

ReDv

D=DiameterV=fluid velocityρ= fluid densityμ= dynamic fluid

viscosity

Page 8: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Pipe Flow Analysis (cont.)

• Use of headloss calculations can be used to find differential pressure in piping

LhP

hL=headloss in piping

ν= specific volume of fluid

Page 9: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

Pipe Flow Analysis (cont.)

• Determine mass flow rate of fluid

m Av V _ _

_

_

m mass flow rate

A area

v fluid velocity

density

V volumetric flowrate

Page 10: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

RadCon Calcs

• See excel spreadsheet

Page 11: Heat Xfer/RadCon Progress 20Oct2006 By John Tang Benton White

RadCon

• Safe operating distance for x-ray dose rate is 9km.

2

1

1( ) ( )p x ray m x ray

mD D

r