Heating duty divides into two questions. What is the medium, and does the thing being heated tolerate the surface temperature that medium produces? Almost every heating problem we are sent turns on the second one.
The second of those two questions is what separates the duties below. A utility stream tolerates a hot surface; a product stream burns onto it. That single distinction is why steam duty is mostly a control problem, glycol duty is a pumping problem, and product duty is a surface-temperature problem with a cleaning requirement attached to it.
The heating medium and its temperature, the flow and required outlet temperature of the heated stream, the allowable pressure drop, and whether the stream fouls. On product duty the surface temperature the medium produces matters more than its bulk temperature, because burn-on happens at the wall.
A plate pack gives a very close temperature approach, so a lower-temperature medium can still deliver the duty, which is exactly what protects a heat-sensitive product. Where the thing being heated is in a tank rather than a pipe, Temp-Plate puts the surface inside or outside the vessel instead.
Steam on one side, water on the other, and a temperature difference large enough that the exchanger selection...
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Closed loop, liquid to liquid, modest temperature difference. The design is undemanding until glycol enters...
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Heating the product itself is a different problem from heating a utility. The stream is valuable, often...
+ Learn MoreTell us which, because it reverses the design logic. When the plant sets the medium, we work out the wall temperature it will produce and add surface to keep that wall acceptable. When the outlet temperature is the hard number, we show what medium temperature it takes and what that means for fouling.
Viscosity at the inlet and outlet temperatures comes first, along with the temperature at which the product starts to scorch, set or denature. Specific heat and density are often close enough from a handbook, but viscosity on real product can be several times the textbook value. Lab data at two or more temperatures takes most of the guesswork out of the plate choice.
A plate pack sized for full flow can drop into laminar flow at low rates, and on steam the control valve then works near its seat and the outlet temperature hunts. Give us the lowest flow the heater will see as well as the highest. Knowing the range up front lets us split the duty, change the pass arrangement or size the valve for both ends.
State the fouling you actually see between cleans, and we size so the outlet temperature still holds at the end of a run. Piling on margin as a blanket percentage tends to backfire, since the oversized unit runs slow when clean and gathers deposit faster. On product duty, the cleaning interval you want is a better input than any fouling factor.