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