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Btu/(h¡¤ft©÷¡¤¢µ)

Water

 Temperature of heating medium ...........
 Temperature of water .........................
 Water velocity, ft./sec ........................

Up to 240.

240¡Æ -400.

125. or less

Above 125.

¡Â3

3

¡Â3

3

 Distilled ...........................................
 Sea water ........................................
 Treated boiler feed water ...................
 Treated makeup for cooling tower .......
 City, well, Great Lakes ......................
 Brackish, clean river water ................
 River water, muddy, silty ...................
 Hard(over 15 g./gal.) ........................
 Chicago Sanitary Canal ....................

2000
2000
1000
1000
1000
 500
 330
 330
 125

2000
2000
2000
1000
1000
1000
 500
 330
 170

2000
1000
1000
 500
 500
 330
 250
 200
 100

2000
1000
1000
 500
 500
 500
 330
 200
 125

Chemicals

 Inorganic:

Gases(Oil-bearing or dirty)...........................................500
Liquids(heating or vaporization)....................................500
Refrigerant brines.......................................................1000
 Organic:
      Gases
Process....................................................................1000
Utility(Oil-bearing, refrigerant, etc.)................................500
Condensing vapors(condensers).................................1000
      Liquids
Vaproizing Liquids(reboilers)........................................500
Heat-transfer media....................................................1000
Refrigerant Liquids.....................................................1000
polymer-forming liquids................................................200
Oils(vegetable and heavy gas Oil).................................330
Asphalt and residuum..................................................100
    *Rearranged and reproduced, by permission, from standards of Tubular
    Exchanger Manufacturers Association, 5th ed., New York, 1968.
    NOTE:¡É=(¢µ-32)/1.8; to convert feed per second to meters per second, multiply by 0.3048;
    to convert British thermal units per hour-square foot-degrees Fahrenheit to joules per square
    meter-second-kelvins, multiply by 5.6783.




U=Btu/(¢µ¡¤ft©÷¡¤h)

Shell side

Tube side

Design U

Includes
total
dirt

Liquid-liquid media

Aroclor 1248
Cutback asphalt
Demineralized water
Ethanol amine(MEA or
 DEA)10-25% solutions
Fuel oil
Fuel oil
Gasoline
heavy oils
Heavy oils
Hydrgen-rich reformer
  stream
Kerosene or gas oil
Kerosene or gas oil
Kerosene or jet fuels
Jacket water
Lube oil (low viscosity)
Lube oil (high viscosity)
Lube oil
Naphtha
Naphtha
Organic solvents
Organic solvents
Organic solvents
Tall oil derivatives,veg-
  etable oil, etc.
Water

Water
Wax distillate
Wax distillate

Jet fuels
Water
Water
Water or DEA,
or MEA solutions
Water
Oil
Water
Heavy oils
Water
Hydrogen-rich
 &nbspreformer stream
Water
Oil
Trichlorethylene
Water
Water
Water
Oil
Water
Oil
Water
Brine
Organic solvents
Water

Causstic soda
  solutions (10-30%)
Water
Water
Oil

100-150
10-20
300-500
140-200

15-25
10-15
60-100
10-40
15-50
90-120

25-50
20-35
40-50
230-300
25-50
40-80
11-20
50-70
25-35
50-150
35-90
20-60
20-50

100-250

200-250
15-25
13-23

0.0015
.01
.001
.003

.007
.008
.003
.004
.005
.002

.005
.005
.0015
.002
.002
.003
.006
.005
.005
.003
.003
.002
.004

.003

.003
.005
.005

Condensing vapor-liquid media

Alcohol vapor
Asphalt(450¢µ)
Dowtherm vapor

Water
Dowtherm vapor
Tall oil and   derivatives

100-200
40-60
60-80

.002
.006
.004

Shell side

Tube sid

Design U

Includes
total
dirt

Dowtherm vapor
Gas-plant tar
High-boiling hydro-
  carbons V
Low-boiling hydrocar-
  bons A
Hydrocarbon vapors
  (partial condenser)
Organic solvents A
Organic solvents high
   NC, A
Organic solvents low
   NC, V
Kerosene
Kerosene
Naphtha
Naphtha
Stabilizer reflux vapors
Steam
Steam
Steam
Sulfur dioxide
Tal-oil derivatives, ve-
  getable oils(vapor)
Water

Dowtherm liquid
Steam
Water

Water

Oil

Water
Water or brine

Water or brine

Water
Oil
Water
Oil
Water
Feed water
No.6 fuel Oil
No.2 fuel Oil
Water
Water

Aromatic vapor stream azeotrope

80-120
40-50
20-50

80-200

25-40

100-200
20-60

50-120

30-65
20-30
50-75
20-30
80-120
400,1000
15-25
60-90
150-200
20-50

40-80

.0015
.0055
.003

.003

.004

.003
.003

.003

.004
.005
.005
.005
.003
.0005
.0055
.0025
.003
.004

.005

Gas-liquid media

Air,N©ü,etc.(compressed) Air,N©ü,etc.,A
Water or brine

Water or brine
water


Water or brine
Water or brine
Air,N©ü(compressed)
Air,N©ü, etc, A
Hydrogen cont-
  aining natural-
  gas mixtures

40-80
10-50
20-40

5-20
80-125


.005
.005
.005

.005
.003


Vaporizersv

Anhydrous ammonia
Chlorine
Chlorine

Propane, butane,etc.
Water

Steam condens-
Steam condens-
Light heat-tran-
  sfer oil
Steam condens-
Steam condens-

150-300
150-300
40-60

200-300
250-400

.0015
.0015
.0015

.0015
.0015

NC=noncondensable gas present.
V=vacuum.
A=atmospheric pressure.
Dirt(or fouling factor)units are(h¡¤ft2¡¤)Btu.
To convert British thermal units per hour-square foot-degrees Fashrenheit to joules per square meter-second-kelvins, multiply by 5.6783;to convert hours per square foot-degree Fahrenheit- British thermal units to square meters per second-kelvin-joules, multiply by 0.1761.



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