For Both Wye and Delta (Balanced Loads) | Wye and Delta Equivalent |
---|---|
VP= Phase Voltage VL= Line Voltage IP= Phase Current IL= Line Current R = R1 = R2 = R3 = Resistance of each branch W = Wattage |
WDELTA= 3 WWYE WODELTA= ¾ WDELTA WOWYE= ½ WWYE |
Phase Wye (Balanced Load) | Phase Open Wye (No Neutral) |
---|---|
|
Phase Delta (Balanced Load) | 3-Phase Open Delta |
---|---|
|
To Convert To… | Multiply… | By… | |
---|---|---|---|
Atmospheres -- (atm) | Bar -- Inches Mercury (in Hg) Pounds/square inch (psi) Torr -- | 0.9869 0.03342 0.06805 0.001316 |
|
Bar | Atmospheres (atm) Pounds/square inch (psi) | 1.0133 0.06895 |
|
British Thermal Units | (Btu) | Joules (J) Kilowatt-hours (KWh) Watt-hours (Wh) |
0.000948 3412 3.412 |
British Thermal Units/hour | (Btu/h) | Kilocalories/hour (kcal/h)
Watts (W) |
3.969 3.412 |
British Thermal Units/inches hour-square foot---°F British Thermal Units/pound British Thermal Units/pound---°F |
(Btu---in) (h-ft2---°F) (Btu/lb) (Btu/lb---°F) |
Watts/meter---°C (W/m---°C) Kilojoules/kilogram (kJ/kg) Kilojoules/kilogram---°C (kJ/kg---°C) |
6.933 0.4299 0.2388 |
Calories | (cal) | Joules (J) | 0.2388 |
Centimeters | (cm) | Feet (ft) Inches (in) |
30.48 2.54 |
Centimeters/second | (cm/s) | Feet/minute (fpm) | 0.508 |
Cubic centimeters | (cm3or cc) | Cubic feet (ft3) Cubic inches (in3) Milli Liters (ml) |
28,320 16.39 1.0 |
Cubic feet | (ft3) | Cubic meters (m3) Gallons, U.S. (gal) Liters (l) |
35.32 0.1337 .03532 |
Cubic inches | (in3) | Cubic centimeters (cm3or cc) | 0.061 |
Cubic meters | (m3) | Gallons, U.S. (gal) Liters (l) Cubic feet (ft3) |
0.003785 0.001 0.02832 |
Cubic meters/hour | (m3/h) | Cubic feet/minute (cfm) Gallons/minute (gpm) |
1.699 0.2271 |
Cubic meters/second | (m3/s) | Cubic feet/minute (cfm) | 0.000472 |
Feet | (ft) | Centimeters (cm) Meters (m) |
0.03281 3.281 |
Feet/minute | (fpm) | Centimeters/second (cm/s) Meters/second (m/s) |
1.969 196.9 |
Gallons, Imperial | -- | Gallons, U.S. (gal) | 0.8327 |
Gallons, U.S. | (gal) | Cubic feet (ft3) Cubic meters (m3) Gallons, Imperial -- Liters (l) |
7.481 264.2 1.201 0.2642 |
Gallons/minute | (gpm) | Cubic meters/hour Liters/second (m3/h) (l/s) |
4.403 15.85 |
Grams | (g) | Ounces (oz) Pounds (lb) |
28.35 453.6 |
Grams/cubic centimeter | (g/cm3) | Kilograms/cubic meter (kg/m3) Pounds/cubic foot (lb/ft3) Pounds/cubic inch (lb/in3) |
0.001 0.01602 27.68 |
Inches | (in) | Centimeters (cm) Millimeters (mm) |
0.3937 0.03937 |
Joules | (J) | British Thermal Units (Btu) Calories (cal) Watt-hours (Wh) |
1055 4.187 3600 |
Joules/second | (J/s) | British Thermal Units/hour (Btu/h) Watts (W) |
0.2931 1 |
Kilocalories/hour | (kcal/h) | Btu/hour (Btu/h) |
Btu/hour (Btu/h) 0.252 |
Kilograms Kilograms/cubic meter Kilograms/cubic meter Kilograms/square centimeter |
(kg) (kg/m3) (kg/m3) (kg/cm2) |
Pounds (lb) Grams/cubic centimeter (g/cm3) Pounds/cubic foot (lb/ft3) Pounds/square inch (psi) |
0.4536 1000 16.02 0.07031 |
Kilojoules Kilojoules/kilogram Kilojoules/kilogram---ºC |
(kJ) (kJ/kg) (kJ/kg---ºC) |
Watt-hours (Wh) British Thermal Units/pound(Btu/lb) British Thermal Units/pound---ºF (Btu/lb---ºF) |
3.6 2.326 4.187 |
Kilometers/hour |
(kJ) (kJ/kg) (kJ/kg---ºC) |
Miles/hour (mph) |
1.609 |
Kilopascals |
(kPa) |
Pounds/square inch (psi)
|
6.895 |
Kilowatts |
(KW) |
British Thermal Units/hour (Btu/h) Watts (W) |
0.0002931
0.001
|
Kilowatt-hours |
(KWh) |
British Thermal Units Btu) Watt-hours (Wh) |
0.0002931 0.001 |
Liters |
(l) |
Cubic Feet (ft3) Cubic Meters (m3) Gallons, U.S. (gal) |
28.32 1000 3.785 |
Liters/second |
(l/s) |
Cubic feet/minute (cfm) Gallons/minute (gpm) |
0.4719 0.06309 |
Meters Meters/second |
(m) (m/s) |
Feet (ft) Feet/minute (fpm) |
0.3048 0.00508 |
(mph) | Kilometers/hour (km/h)
|
0.6215
|
|
Miles/hour | (mph) | KKilometers/hour (km/h)
|
0.6215
|
Millimeters | (mm) | Inches (in)
|
25.4
|
Newtons/square meter | (N/m2) | Pounds/square inch (psi)
|
6,895
|
Ounces | (oz) | Grams (g)
|
0.035274 |
Pounds | (lb) | Grams (g) Kilograms (kg) |
0.002205 2.205 |
Pounds/cubic foot | (lb/ft3) | Grams/cubic centimeter (g/cm3) Kilograms/cubic meter (kg/m3) |
62.43 0.06243 |
Pounds/cubic inch | (lb/in3) | Grams/cubic centimeter (g/cm3)
|
0.03613 |
Pounds/square inch | (psi) | Bar -
Kilograms/square centimeter (kg/cm2) Kilopascals (kPa) Newtons/square meter (N/m2) |
14.504 14.22 0.145 0.000145 |
Square centimeters | (cm2) | Square feet (ft2) Square inches (in2) |
929 6.452 |
Square feet | (ft2) | Square centimeters (cm2) Square meters (m2) |
0.001076 10.76 |
Square inches | (in2) | Square centimeters (cm2) |
0.155 |
Square meters | (m2) | Square feet (ft2) |
0.0929 |
Torr | Inches Mercury (in. Hg) Pounds/square inch (psi) |
0.03937 51.71 |
0.Watts |
Watts | Watts (W) | British Thermal Units/hour (Btu/h) Joules/second (J/s) |
0.2931
1 |
Watt-hours | (Wh) | British Thermal Units (Btu) Joules (J) Kilojoules (kJ) |
0.2931 0.0002778 0.2778 |
Watts/meter---ºC Watts/square centimeter Watts/square inch |
(W/m---ºC) (W/cm2) (W/in2) |
Watts/square inch (W/in2) Watts/square centimeter (W/cm2) |
0.1442 0.155 6.452 |
Watts/meter---ºC Watts/square centimeter Watts/square inch |
(W/m---ºC) (W/cm2) (W/in2) |
Watts/square inch (W/in2) Watts/square centimeter (W/cm2) |
0.1442 0.155 6.452 |
Temperature Scale | Convert to by… |
---|---|
Fahrenheit | °F = 1.8°C + 32° |
Celsius | °C =5/9(°F-32°) |
Rankine | °R = 1.8K + 0.6° °R = °F + 460° |
Kelvin | K =5/9(°R-0.6°) K = °C + 273° |
Criteria | Thermocouple | RTD | Thermistor |
---|---|---|---|
Temperature Range | Very wide -450°F +4200°F | Wide -400°F +1200°F | Narrow -100°F +500°F |
Interchangeability | Good | Excellent | Poor to fair |
Long-term Stability | Poor to fair | Good | Poor |
Accuracy | Medium | High | Medium |
Repeatability | Fair | Excellent | Fair to good |
Sensitivity (output) | Low | Medium | Very high |
Response | Medium to fast | Medium | Medium to fast |
Linearity | Fair | Good | Poor |
Point (end) Sensitive | Excellent | Fair | Good |
Lead Effect | High | Medium | Low |
Size/Packaging | Small to large | Medium to small | Small to medium |
Sensor | Advantages | Disadvantages |
---|---|---|
Thermocouple |
|
|
RTD |
|
|
Thermistor |
|
|
Many plant engineers do not give much thought to the heaters operating within their processes and applications - unless those heaters fail, require significant maintenance or cause other problems. Unfortunately, heaters play an integral role in many applications. Therefore, heater problems can easily snowball and lead to much larger headaches.
Following a few simple guidelines will not only reduce the likelihood of heater-related issues, but can actually have a significant positive impact on the efficiency of systems and reduce maintenance requirements and costs. Below are 10 ways to maximize a heater's service life and performance.
Contamination is the most frequent cause of heater failure (see images). As heaters expand and contract during cycling, they often draw in organic or conductive materials. This can lead to an arcing failure between individual heater windings or between heater windings and the electrically grounded outer heater sheath. When allowed to collect at the lead end of a heater, contaminants can also cause electrical shorts between power pins or terminals. Therefore, it is important to keep lubricants, oils, low-temperature tapes or processing materials out of contact with the lead end of the heater. Employing seals will help.
Standard fiberglass-insulated lead wire may be used in applications with ambient temperatures up to approximately 260°C (500°F). If a lead is exposed to higher temperatures, high-temperature lead wire or ceramic bead insulation should be used. An unheated section of the heater, extending away from the heated region of the system, enables the leads to run at a beneficially cooler temperature. When heaters are mounted in moving machinery, it is essential to anchor the leads to prevent them from being damaged. A lead protection option should be specified and used for optimum protection against lead damage.
A heater's wattage should be matched as closely as possible to the application's actual load requirements to limit ON/OFF cycling (see tip 6). For fitted-part applications, specify the hole or an alternative application feature size to ensure an optimal fit between the heater and application feature. A tight fit minimizes air gaps and reduces the instances of hot spotting.
It is common sense and safe practice to electrically ground all equipment on which the heater is used. Grounding equipment helps protects plant and personnel in the event of an electrical failure in the heating system.
It is essential to ensure a heater's rated voltage matches the available voltage supply because wattage increases (or decreases) at the square of the change in voltage applied to a heater. For example, if a heater is rated for 120V/1000W and is connected to a 240V supply, it will generate four times the rated wattage output or 4000W. This will cause a heater to fail relatively quickly and can also cause significant damage the attached equipment.
Excessive temperature cycling is very detrimental to the life of a heater. The most detrimental is the cycle rate that allows full expansion and contraction of the heater resistance wire at a high rate (30 to 60 seconds' power ON and power OFF). This causes severe stress and oxidation of the resistance wires inside a heater. A bad temperature cycle is typically found when thermostats are used. Thermostats respond slowly to temperature changes and have large switch ON/OFF temperature differentials. An improvement, but a somewhat more expensive solution, is to use ON/OFF or PID controllers with mechanical relays. It is crucial to not switch the frequency or cycle time too rapidly (somewhere between 3 to 10 seconds), because the relay contacts can wear out quickly.
The most effective way to minimize heater element temperature cycling, and the most expensive solution, is to use solid state relays (SSRs) and SCR power controllers coupled to PID temperature controllers. This combination provides the best performance for both your thermal system as well as for the heater itself. Solid state switching devices cycle power to the heater very rapidly (from one second with a SSR, down to milliseconds with phase-angle fired SCRs). This fast-power cycling dramatically reduces heater element wire temperature excursions and substantially extends heater life.
This is absolutely critical to ensure long heater life and healthy processing equipment. When heating solids, such as metals, the operating temperature and heater-to-part fit drive sheath material and watt density choices. Carbon steels, aluminum, silicone rubber sheath materials are fine for lower temperatures (a few hundred degrees). However, as temperatures increase beyond this point, sheath material choices become limited to galvanized or stainless steels and other higher temperature metal alloys. As temperature also increases, the watt density must decrease accordingly to prevent internal resistance wires from oxidizing quickly and failing prematurely. A good heater-to-part fit ensures proper heat transfer and does not force the resistance wires to overheat. When heating gases, the operating temperature and flow rates dictate what sheath material and watt density can be used. For example, you can run higher watt densities when heating hydrogen versus nitrogen, but hydrogen requires Alloy 800 sheaths, whereas 304 Stainless Steel will work for many nitrogen applications. Increasing flow and turbulence across the heater elements means better heat transfer, which raises watt density values. For liquid heating, the prime driver for materials and watt density selection is the fluid material and flow rate. Water can easily handle 42.52 to 70.87W/cm2 (60 to 100W/in2) using a copper sheath, whereas a 50/50-water/glycol mix can only handle 21.26 W/cm2 (30 W/in2) and must use a steel sheath.
Heaters should be placed horizontally and near tank bottoms to maximize convective circulation. Vertical mounting is only advisable when limitations, such as space restrictions, prohibit horizontal placement. Regardless of whether a heater is mounted horizontally or vertically, it is essential to place it high enough to avoid any sludge and debris buildup in the bottom of the tank. Likewise, for both mounting methods, the entire heated length of the heater must be immersed at all times - one reason vertical mounting is rarely recommended. It is also important to avoid placing heaters in restricted spaces that limit convective flow and/or where free boiling or steam traps can occur.
Scale, coking and sludge build-up on heater sheaths must be minimized. Any accumulation should be periodically removed or at least minimized, to avoid inhibiting heat transfer to the liquid. Periodic cleaning prevents heater elements being forced to operate at higher temperatures, which can lead to early heater failure. Extreme care should also be taken to avoid getting silicone lubricant on the heated section of a heater. Silicone will prevent the "wetting" of the sheath by the liquid, act as an insulator, and possibly cause the heater to fail.
Matching the appropriate temperature control system to the heater is imperative to strong heater performance and life. Each process application should, at the very least, include a process temperature sensor (to sense the material being heated) and a limit sensor (to sense the heater sheath temperature). The process sensor should be directly immersed into the material to be heated, or snugly inserted into a thermowell inside the fluid itself. For safety reasons, two separate control systems should be used - one for process temperature control and one for high limit control. PID type process temperature controllers offer more stable control and faster. problem. Some of this supporting information may not be readily available or apparent to you. You may find it necessary to consult the reference tables and charts in this reference data section, or reference a book that deals with the particular parameter you need to define. At the minimum, the thermal properties of both the material(s) being processed/heated and their containing vessel(s) will be required. Figuring a safety factor requires some intuition on your part. The list of possible influences can be great. From changing ambient operating temperatures, caused by seasonal changes, to a change in material or material temperature being processed, you must carefully examine all the influences. Generally speaking, the smaller the system with fewer variables and outside influences---the smaller the safety factor. Conversely, the larger the system and the greater the variables and outside influences — the greater the safety factor.
The safety factor should be higher for systems that have production operations that contain equipment cycles subjecting them to excessive heat dissipations, e.g.: opening doors on furnaces, introducing new batches of material that can be of varying temperatures, large radiant applications and the like.
Thermocouple Type | Useful/General Application Range | Notes |
---|---|---|
B | 1370-1700°C (2500-3100°F) | Easily contaminated, require protection. |
C* | 1650-2315°C (3000-4200°F) | No oxidation resistance. Vacuum, hydrogen or inert atmospheres. |
E** | 95-760°C (200-1400°F) | Reducing atmosphere recommended. Iron leg subject to oxidation a |
K** | 95-1260°C (200-2300°F) | Well suited for oxidizing atmospheres. |
N | 870-1450°C (1600-2640°F) | Oxidizing atmosphere recommended. Easily contaminated, require protection. |
S | 980-1450°C (1800-2640°F) | Laboratory standard, highly reproducible. Easily contaminated, require |
T** | -200-350°C (-330-660°F) | Most stable at cryogenic temperatures ranges. Excellent in oxidizing |