TruHeat - 800.879.6199 - Electrical Heating Elements
 
Over-The-Side Immersion heating element
Cooking Elements
Defrost Elements
Custom Designed Elements

>> Custom Designs


TruHeat not only has the ability to mass produce heating elements through means of computer controlled technology and/or efficient cellular groups, but they also have the capability to custom design/engineer as little as one element to precision standards. They are proud to proclaim, Made in USA.

Steadfast engineering is TruHeat’s foundation, and manufacturing integration allows an unsurpassed knowledge base in the heating element industry.

There are three basic considerations in the designing of custom heating elements; desired final temperature, required sheath material, and allowable watt density.

Desired final temperature:

Tubular heating elements typically operate from ambient to 1500 degrees Fahrenheit. Principal aspects to consider are starting temperature, maximum temperature, and element temperature when media is at maximum temperature (See Graph TH4).

Required sheath material:

While Copper is a common sheath material for process water, cold rolled steel for oils, and higher grade stainless steel alloys for higher temperature air elements & corrosive immersion applications (see Table TH1), final sheath selection should include precise exposure conditions (i.e. media flow rates) , corrosion specifications, and TruHeat testing and evaluation.

Allowable Watt Density:

Watt density (measure in watts per square inch) is simply the power emanating from each square inch of the heating element. See Table TH1 for recommended watt densities on various materials. As watt density is directly tied to heater life numerous factors are to be considered for optimal engineering.

  • Operating temperature
  • Insulation material and/or temperature limits
  • Quality of either convection/conduction path (i.e. clamping, cast-in, immersion)
  • Immersion
  • Boiling point
  • Viscosity
  • Sheath corrosion rate
  • Temperature of material composition

View more detailed information and a listing of affiliated companies at the TruHeat Download Directory


Table TH1: Recommended Watt Densities on Various Materials.
 
* Maximum
 
 
Heated
Operating
**Maximum
Sheath
Material
Temperature
Watt Density
Material
Acetic Acid 180 40 SS316
Boric Acid 257 40 TITAN.
Carbonic Acid 180 40 I600
Chromic Acid 180 40 TITAN.
Citric Acid 180 23 I800
Fatty Acid 150 20 SS316
Lactic Acid 122 10 SS316
Levulinic Acid 180 40 I600
Malic Acid 122 10 SS316
Nitric Acid 167 20 SS316
Phosphoric Acid 180 23 I800
Proponic Acid 180 40 COPPER
Tannic Acid 180 40 SS304
Tartaric Acid 180 40 SS316
Acetaldehyde 180 10 COPPER
Acetone 130 10 SS304
Air *** *** I800
Alkyl Alcohol 200 10 COPPER
Alkaline Solution 212 40 CRS
Aluminum Acetate 122 10 SS316
Aluminum Potassium Sulfate 212 40 COPPER
Ammonia Gas *** *** CRS
Ammonium Acetate 167 23 I800
Amyl Acetate 240 23 I800
Amyl Alcohol 212 20 SS304
Aniline 350 23 SS304
Asphalt 200-500 4-10 CRS
Barium Hydroxide 212 10 SS316
Benzene (liquid) 150 10 COPPER
Butyl Acetate 225 10 SS316
Calcium Bisulfate 400 20 SS316
Calcium Chloride 200 5-8 I600
Carbon Monoxide *** 23 I800
Carbon Tetrachloride 160 23 I800
Caustic Soda 2% 210 48 I800
Caustic Soda 10% 210 25 I800
Caustic Soda 75% 180 25 I800
Citrus Juice 185 23 I800
Degreasing Solutions 275 23 CRS
Dextrose 212 20 SS304
Electroplating Cadmium Bath 180 40 SS304
Electroplating Copper Bath 180 40 SS316
Electroplating Dilute Cyanide Bath 180 40 SS316
Electroplating Rochelle Cyanide Bath 180 40 SS316
Electroplating Sodium Cyanide Bath 180 40 SS316
Electroplating Potassium Cyanide Bath 180 40 SS316
Ethylene Glycol 300 30 CRS
Formaldehyde 180 10 SS304
Freon (gas) 300 2-5 CRS
Fuel Oil (Grades 1&2,distilate) 200 23 CRS
Fuel Oil (Grades 3&4,residual) 200 13 CRS
Fuel Oil (Grade 6 & bunker C, residual) 160 8 CRS
Gasoline 300 23 CRS
Gelatin (liquid) 150 23 SS304
Gelatin (solid) 150 5 SS304
Glycerin 500 10 I800
Glycerol 212 23 I800
Grease (liquid) *** 23 CRS
Grease (solid) *** 5 CRS
Heat transfer Oil (static) 500 16 CRS
Heat transfer Oil (circulating) 500 23 CRS
Hydrazine 212 16 SS304
Hydrogen *** *** I800
Hydrogen Chloride *** *** I600
Hydrogen Sulfide *** *** SS316
Linseed oil 150 50 CRS
SAE 10, 90-100-SSU @ 130' F 250 23 CRS
SAE 20 120-185-SSU @ 130' F 250 23 CRS
SAE 30, 120-185-SSU @ 130' F 250 23 CRS
SAE 40, 80-SSU @ 210' F 250 13 CRS
SAE 50, 80-105-SSU @ 210' F 250 13 CRS
Magnesium Chloride 212 40 I600
Magnesium Sulfate 212 40 SS304
Manganese Sulfate 212 40 SS316
Methanol Gas *** *** SS304
Methylamine 180 20 I600
Methyl chloride 180 20 COPPER
Mineral Oil 200 23 CRS
Molasses 100 4-5 SS304
Molten Salt Bath 800-900 25-30 MONEL
Naphtha 212 10 CRS
Oil Drawn bath 600 23 CRS
Paraffin (Wax) 150 16 CRS
Perchloroethylene 200 23 CRS
Potassium Chlorate 212 40 SS316
Potassium Chloride 212 40 SS316
Potassium Hydroxide 160 23 MONEL
Soap (liquid) 212 20 SS304
Sodium Acetate 212 40 CRS
Sodium Cyanide 140 40 I800
Sodium Hydride 720 28 I800
Sodium Phosphate 212 40 COPPER
Steam 700 5 I800
Sulphur (Molten) 600 10 I800
Therminols 500 23 CRS
Toluene 212 23 CRS
Trichloroethylene 150 23 CRS
Turpentine 300 20 SS304
Vegetable Oil 400 30 SS304
Water (process) 212 60 I800

Table TH2: Kilowatts to Heat (Water) in one hour.

 

Amount of Water by Gallons
Temperature Rise (F)
  20 40 60 80 100 120 140
5 0.3 0.5 0.8 1.1 1.3 1.6 1.9
10 0.5 1.1 1.6 2.2 2.7 3.2 3.8
15 0.8 1.6 2.4 3.2 4.0 4.8 5.6
20 1.1 2.2 3.2 4.3 5.4 6.5 7.5
25 1.3 2.7 4.0 5.4 6.7 8.1 9.4
30 1.6 3.2 4.8 6.5 8.1 9.7 11.3
40 2.2 4.3 6.5 8.6 10.8 12.9 15.1
50 2.7 5.4 8.1 1.8 13.5 16.1 18.8
60 3.2 6.5 9.7 12.9 16.1 19.4 22.6
70 3.8 7.5 11.3 15.1 18.8 22.6 26.4
80 4.3 8.6 12.9 17.2 21.5 25.8 30.1
90 4.8 9.7 14.5 19.4 24.2 2.1 33.9
100 5.4 10.8 16.1 21.5 26.9 32.3 37.7
125 6.7 13.5 20.2 26.9 33.6 40.4 47.1
150 8.1 16.1 24.2 32.3 40.4 48.4 56.5
175 9.4 18.8 28.2 37.7 47.1 56.5 65.9
200 10.8 21.5 32.3 43.0 53.8 64.6 75.3
250 13.5 26.9 40.4 53.8 67.3 80.7 94.2
300 16.1 32.3 48.4 64.6 80.7 96.9 113.0
400 21.5 43.0 64.6 86.1 107.6 129.1 150.7
500 26.9 53.8 80.7 107.6 134.5 161.4 188.3

Use equation 1 for heating flowing water.
Use equation 2 or table for heating water in tanks.

Equation 1: KW= GPM x Temperature rise (F) x .16
Equation 2: KW= Gallons x Temperature rise (F)
...........372 x Heat up time (hrs)

Table TH3: Kilowatts to Heat (Air) in one hour.

Temperature Rise (F)
 Amount of Air CFM
50 100 150 200 250 300 350 400 450 500 600
100 1.7 3.3 5.0 6.7 8.3 10.0 11.7 13.3 15.0 16.7 20.0
200 3.3 6.7 10.0 1.3 16.7 20.0 23.3 26.7 30.0 33.3 40.0
300 5.0 10.0 15.0 20.0 25.0 30.0 35.0 40.0 45.0 50.0 60.0
400 6.0 13.3 20.0 26.7 33.3 40.0 46.7 53.3 60.0 66.7 80.0
500 8.3 16.7 25.0 33.3 41.7 50.0 58.3 66.7 75.0 83.3 100.0
600 10.0 20.0 30.0 40.0 50.0 60.0 70.0 80.0 90.0 100.0 120.0
700 11.7 23.3 35.0 46.7 58.3 70.0 81.7 93.3 105.0 116.7 140.0
800 13.3 26.7 40.0 53.3 66.7 80.0 93.3 106.7 120.0 1333.3 160.0
900 15.0 30.0 45.0 60.0 75.0 90.0 105.0 120.0 135.0 150.0 180.0
1000 16.7 33.3 50.0 66.7 83.3 100.0 116.7 133.3 150.0 16.7 20.0
1100 18.3 36.7 55.0 73.3 91.7 110.0 128.3 146.7 165.0 183.3 220.0
1200 20.0 40.0 60.0 80.0 100.0 120.0 140.0 160.0 180.0 200.0 240.0

For Free Air: Use equation or table

Free Air: KW= CFM x Temperature rise
3000

Compressed Air: KW= CFM* x Density* (lbs. /cu.ft.) x Temperature rise
228

Table TH4: Kilowatts to Heat (Oil) in one hour.

 

 
Amount of Oil by Gallons
 Temperature Rise (F)
  50 100 200 300 400 500  
5 0.3 0.7 1.4 2.1 2.8 3.5  
10 0.7 1.4 2.8 4.2 5.5/8 7.0  
15 1.0 2.1 4.2 6.3 8.4 10.5  
20 1.4 2.8 5.6 8.4 11.2 14.0  
25 1.7 3.5 7.0 10.5 14.0 17.4  
30 2.1 4.2 8.4 12.6 16.7 20.9  
40 2.8 5.6 11.0 16.7 22.3 27.9  
50 3.5 7.0 14.0 20.9 27.9 34.9  
60 4.2 8.4 17.0 25.1 33.5 41.9  
70 4.9 9.8 20.0 29.3 39.1 48.8  
80 5.6 11.0 22.0 33.5 44.7 55.8  
90 6.3 13.0 25.0 37.7 50.2 62.8  
100 7.0 14.0 28.0 41.9 55.8 69.8  
125 8.7 17.0 35.0 52.3 69.8 87.2  
150 10.0 21.0 42.0 62.8 83.7 105.0  
175 12.0 24.0 49.0 73.3 97.7 122.0  
200 14.0 28.0 56.0 83.7 112.0 140.0  
250 17.0 35.0 70.0 105.0 140.0 174.0  
300 21.0 42.0 84.0 126.0 167.0 209.0  
400 28.0 56.0 112.0 167.0 223.0 279.0  
500 35.0 70.0 140.0 209.0 279.0 349.0  

Use equation or table

Still Oil: KW= Gallons x Temperature rise (F)
860 x heat-up time (hrs.)

Table TH5: Amperage Conversion Table.

 

 
Watts
Volts Single Phase
   
Volts 3 Phase Balanced Load
   
Watts
120 240 480 240 480  Watts
100 0.83 0.42 0.21 0.24 0.13 100
150 1.25 0.63 0.31 0.36 0.18 150
200 1.67 0.83 0.42 0.49 0.25 200
300 2.5 1.25 0.63 0.73 0.37 300
350 2.92 1.46 0.73 0.85 0.43 350
400 3.33 1.67 0.84 0.97 0.49 400
450 3.75 1.88 0.93 1.1 0.55 450
500 4.17 2.08 1.04 1.2 0.6 500
600 5 2.5 1.25 1.45 0.73 600
700 5.83 2.92 1.46 1.7 0.85 700
750 6325 3.13 1.56 1.81 0.91 750
800 6.67 3.33 1.67 1.93 0.97 800
900 7.5 3.75 1.87 2.17 1.09 900
1000 8.33 4.17 2.1 2.41 1.21 1000
1100 9.17 4.58 2.3 2.65 1.33 1100
1200 10 5 2.51 2.9 1.45 1200
1250 10.4 5.21 2.61 3.1 1.55 1250
1300 10.8 5.42 2.71 3.13 1.57 1300
1400 11.7 5.83 2.91 3.38 1.69 1400
1500 12.5 6.25 3.12 3.62 1.82 1500
1600 13.3 6.67 3.34 3.86 1.93 1600
1700 14.2 7.08 3.54 4.1 2.05 1700
1750 14.6 7.29 3.65 4.22 2.1 1750
1800 1530 7.5 3.75 4.34 2.17 180
1900 15.8 7.92 3.96 4.58 2.29 1900
2000 16.7 8.33 4.17 4.82 2.41 2000
2200 18.3 9.17 4.59 5.3 2.65 2200
2500 20.8 10.4 5.21 6.1 3.05 2500
2750 23 11.5 5.73 6.63 3.32 2750
3000 25 12.5 6.25 7.23 3.62 3000
3500 29.2 14.6 7.3 8.45 4.23 3500
4000 33.3 16.7 8.33 9.64 4.82 4000
4500 37.5 18.8 9.38 10.84 5.42 4500
5000 41.7 20.8 10.42 12.1 6.1 5000
6000 50 25 12.5 14.5 7.25 6000
7000 58.3 29.2 14.59 16.9 8.5 7000
8000 66.7 33.3 16.67 19.3 9.65 8000
9000 75 37.5 18.75 21.7 10.85 9000
10000 83.3 41.7 20.85 24.1 12.1 10000

 

© 2004 Truheat, Inc. All rights reserved.