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Thermal Fluid & Hot Oil U-Tube Exchangers

High Temperature at Low System Pressure

Thermal fluids carry heat at high temperature and low pressure. That combination is why they exist: reaching the same process temperature with steam would require a pressure system heavy enough to change the economics of the whole plant.

This is the duty the U-tube was made for. Large differential temperature between the hot oil and the process, abrupt startup transients, and constant cycling would all require an expansion joint in a fixed tubesheet exchanger. In a U-tube bundle they require nothing at all, because each tube is anchored at one end and free at the bend. Tubes can even sit at different temperatures from one another without consequence.

Film temperature is the governing limit. Degradation happens at the tube wall, where the fluid is hottest and moving slowest, not in the bulk. A system can run entirely within its bulk temperature rating and still crack the oil if tube-side velocity is too low or heat flux too high. What follows is coke: a hard carbonaceous deposit bonded to the tube wall that insulates, raises wall temperature further, and accelerates the process that created it.

Coke cannot be cleaned off a U-bundle. Chemical cleaning barely touches it, and mechanical cleaning cannot pass a 180 degree bend. This makes film temperature control a design requirement rather than an operating preference, and it is why we ask for the fluid supplier's data sheet rather than just the operating temperature.

Oxidation and the expansion tank. Thermal oil oxidises rapidly wherever hot oil meets air, and the expansion tank is precisely where that contact happens. A nitrogen blanket is standard practice and inexpensive insurance. Oxidised fluid turns acidic and forms sludge, which fouls surfaces and attacks the system, and routine fluid analysis catches it long before the exchanger does.

Support design at temperature. A hot shell grows measurably. One saddle fixed and one sliding, with slots sized for the calculated growth, keeps that movement out of the nozzles and the connected piping. We state the expected growth and the required support arrangement on the drawing rather than leaving it to be inferred on site.

Related pages: high-temperature U-tube exchangers, tank and suction heating, horizontal mounting and supports and carbon steel construction.



thermal fluid hot oil u-tube heat exchanger process diagram with heater, expansion tank and nitrogen blanket

Degradation happens at the tube wall rather than in the bulk. Velocity and heat flux are selected together to keep film temperature inside the fluid supplier's limit.

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high temperature u-tube heat exchanger for thermal fluid and hot oil service
High Temperature:
Free Expansion
  • No expansion joint
  • Handles thermal shock
  • Cycling tolerant
carbon steel industrial u-tube heat exchanger with saddle supports and davit arm
Industrial:
ASME Code Stamped
  • TEMA R, B or C
  • Carbon steel to alloy
  • Shells to 48 inches
custom engineered u-tube heat exchanger built to specified process conditions
Custom Build:
Rated To Your Duty
  • Any alloy or code
  • Applied nozzle loads
  • Accessories designed in

Thermal Fluid & Hot Oil Heating

Common FAQs

It is the fluid temperature at the tube wall, which is higher than the bulk because that layer is hottest and slowest moving. Thermal fluids degrade on film temperature, so a system operating within its bulk rating can still crack the oil if velocity is too low or heat flux too high.

Because these systems cycle hard. Batch heating, startup and trip produce large abrupt temperature swings, and every cycle fatigues an expansion joint in a fixed tubesheet unit. A U-tube bundle expands freely and has no such joint to fatigue.

Not usefully. Coke is a hard deposit bonded to the tube wall that chemical cleaning barely affects, and mechanical cleaning cannot pass the U-bend. Prevention through velocity and flux control is the only practical approach, which is why those are set conservatively.

It is strongly recommended. Hot oil in contact with air oxidises quickly, turning acidic and forming sludge that fouls surfaces and attacks the system. The blanket is inexpensive and it substantially extends fluid life.

Routine fluid analysis. Rising acid number, changes in viscosity and the appearance of low boilers or insolubles all indicate degradation well before the exchanger shows a performance loss. By the time the exchanger tells you, coke is usually already on the wall.

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