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Thermal

E-800Heat Exchanger Duty and Area

Two streams, one wall, and a temperature difference doing the work. The duty is set by the process; the area is set by how small a temperature difference you are willing to design around.

Cutaway — Heat Exchanger Duty and Area
Hot streamCold stream

How it works

  1. The duty — Start with what the process needs: mass flow times specific heat times the temperature change. That is the duty, in kilowatts, and it is fixed by the process — no amount of clever exchanger design changes it.
  2. Counter-current — Run the streams in opposite directions and the temperature difference stays roughly constant along the whole length. Run them in parallel and it collapses at the outlet end. Counter-current is why the cold stream can leave hotter than the hot stream does.
  3. LMTD and area — The driving force is the log-mean temperature difference. Area follows as duty over U times LMTD. Halve the approach temperature and you roughly double the area — the last few degrees are the expensive ones.
  4. The temperature cross — Push the hot outlet below the cold outlet and, in a single counter-current pass, you have asked for heat to flow uphill. LMTD goes imaginary, area goes infinite, and no exchanger exists. Drag the hot outlet down and watch the design fail.
  5. What governs it — Duty, U and approach. U you mostly inherit from the equipment type; duty the process gives you; approach is the only real design choice, and it trades capital area against operating temperature every time.
  6. Plate-and-frame — Corrugated plates give true counter-current flow and very high turbulence at low velocity, so the overall coefficient reaches several thousand W/m²·K. That is what lets it hold a 1 °C approach — the closest of anything here. It is also the only one you can uprate by simply adding plates, and the gaskets set the temperature and pressure ceiling.

Design parameters

The panel opposite runs the same correlations as the E-800 design sheet, so the animation and the calculator cannot disagree. Every parameter below is live — drag one and the picture responds.

ParameterUnitDefaultRange
Exchanger type
TypePlate-and-frame4 options
Type caps the overall coefficient and the closest approach you can hold. You cannot buy a 1 °C approach on a shell-and-tube at any area.
Duty
Hot flowm³/h302 – 200
Hot inlet°C8025 – 160
Cold flowm³/h362 – 200
Cold inlet°C202 – 90
Hot outlet target°C4010 – 150
Overall UW/m²·K3,20020 – 7,000

Open the full E-800 design sheet for the other five inputs, all twenty-seven results with their envelopes, the five equations printed beside the numbers they produce, and a calculation record you can export and put in a design file.

Live parameters

Six of the eleven inputs the E-800 design sheet takes.

Exchanger type

Type caps the overall coefficient and the closest approach you can hold. You cannot buy a 1 °C approach on a shell-and-tube at any area.

Duty

You have an estimate. The design sheet is the justification.

This page sizes the unit on six variables and tells you whether the headline numbers land in range. That is enough to sketch with, and it stays free. What it will not do is survive a design review: it does not show you the equation behind any number, it checks the obvious limits rather than all of them, and there is nothing to file.

The E-800 design sheet runs the same physics on eleven inputs, reports twenty-seven results against their envelopes, prints the five governing equations beside the numbers they produce, and exports the lot as a calculation record for the design file.

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