1. Why Do Thermal Oil Boilers Form Carbon Deposits?
Thermal oil boilers (also known as organic heat carrier furnaces) rely on thermal oil circulating in a closed loop to transfer heat, with operating temperatures typically reaching 280-320°C. At these temperatures, the thermal oil undergoes continuous degradation — oil molecules experience thermal cracking and oxidative polymerization under the combined effects of heat and oxygen, gradually forming gums and asphaltenes that eventually harden into carbon deposits firmly adhered to the tube walls.
Carbon deposits have extremely poor thermal conductivity. Research shows that a 1mm carbon layer creates thermal resistance equivalent to a 40mm steel plate. In other words, that seemingly thin black crust inside the tubes acts like a thick "insulation blanket" — heat from the flame cannot transfer through efficiently, exhaust temperature rises, and fuel consumption increases while process-side temperature fails to reach the setpoint.
More critically, carbon deposits cause localized overheating. The metal wall temperature beneath a coke layer can exceed normal values by 100-150°C. Under prolonged overtemperature conditions, tube material undergoes creep and may eventually rupture — this is not alarmist; incidents of tube burnout due to severe coking occur every year in thermal oil boilers.
2. Carbon Deposit vs. Coke: Understanding the Difference
Many plant technicians use "carbon deposit" and "coke" interchangeably, but they represent different stages of the problem:
| Dimension | Carbon Deposit (Soft) | Coke (Hard) |
|---|---|---|
| Formation Stage | Early oil degradation | After prolonged high-temp sintering |
| Appearance | Black sludge, relatively loose | Hard chunks, glossy surface |
| Adhesion | Weak, soluble by chemicals | Extremely strong, requires physical breaking |
| Removal Difficulty | Chemical cleaning sufficient | Chemical + mechanical combined |
| Risk Level | Efficiency loss | Potential tube rupture |
Once you understand this distinction, the cleaning strategy becomes clear: soft carbon deposits can be dissolved through chemical circulation; hard coke requires high-pressure water jetting to physically strip it from the tube walls.
3. Cleaning Process: Chemical + Mechanical Combined
3.1 Step 1: Oil Drainage and System Flushing
First, shut down and cool the system to below 80°C, then drain all used thermal oil. This step is critical — residual oil dilutes the cleaning solution and significantly reduces effectiveness. After drainage, purge the piping with nitrogen or steam to expel remaining oil, then flush with clean water until the discharge shows no oil sheen.
3.2 Step 2: Chemical Cleaning for Carbon Removal
Use a specialized carbon-removal cleaning agent formulated for thermal oil deposits. The solution is alkaline-based with Surfactant penetrants and corrosion inhibitors. The alkaline component saponifies oily carbon deposits; the Surfactant reduces surface tension, allowing the solution to penetrate deep into the deposit layer; the inhibitor protects the base metal from alkaline corrosion.
Operating parameters: temperature 80-95°C, circulation velocity 0.5-1.0 m/s, cleaning duration 8-24 hours (adjusted based on deposit severity). Sample and test pH and carbon content every 2 hours — when carbon concentration stops rising, chemical dissolution has reached its limit.
3.3 Step 3: High-Pressure Water Jetting for Coke Removal
Hard coke that resists chemical cleaning must be tackled with high-pressure water. Using a high-pressure plunger pump delivering 500-1000 bar, specialized nozzles rotate and advance through the tubes, stripping coke layers from the walls.
Two practical considerations: first, nozzle selection — use self-rotating nozzles for tubes under 50mm diameter, 3D rotating nozzles for larger diameters. Second, pressure selection — start at medium-low pressure (300-500 bar), increase only if needed. Some older boilers have thinned tube walls; excessive pressure can cause damage.
3.4 Step 4: Passivation and System Restoration
After decoking, exposed metal surfaces are highly susceptible to flash rusting. Immediate passivation is essential: circulate a passivation solution containing Sodium Molybdate and Na₃PO₄ for 2-4 hours to form a dense protective film. Drain, dry with nitrogen, then refill with fresh thermal oil and resume normal operation.
4. When Should You Clean? How to Tell?
Many plants practice "run-to-failure" maintenance and only consider cleaning after problems emerge. Experienced technicians can spot the warning signs during routine inspections. If you notice any two of the following, it's time to schedule cleaning:
Exhaust temperature abnormally high. Under normal conditions, exhaust gas temperature should be 50-80°C above thermal oil outlet temperature. If this gap widens beyond 100°C, heat transfer has seriously deteriorated — carbon deposits are the likely culprit.
Fuel consumption significantly increased. For the same output, fuel usage is 15%+ above baseline and burner adjustment doesn't help — the carbon layer is eating into thermal efficiency.
Hot spots on tube exteriors. Scanning with an infrared thermometer reveals localized high-temperature areas — there's likely a coke layer underneath.
Increased pressure differential. The pressure drop between pump outlet and return is noticeably higher than when the system was new, but flow rate hasn't increased — the effective tube diameter has been reduced by deposits.
Oil samples dark and viscous. Oil samples appear black with a burnt odor — this indicates severe oil degradation and imminent widespread coking.
5. Frequently Asked Questions
How often should a thermal oil boiler be cleaned?
There's no one-size-fits-all answer — it depends on oil quality, operating temperature, and runtime. For continuously operating thermal oil boilers in chemical plants, cleaning every 1-2 years is generally recommended. With high-quality synthetic thermal oil and good maintenance practices, this can extend to 3 years. The key is to watch for the warning signs above rather than rigidly following a fixed interval.
Can cleaning be done online without shutting down?
Carbon deposit cleaning is generally not recommended online. Chemical cleaning solutions need adequate circulation time to dissolve deposits, and thermal oil boilers usually serve as the heat source for production lines — you cannot afford a day or two of degraded performance. Additionally, online cleaning generates large amounts of loosened debris that can clog small-diameter piping. Online treatment is only suitable for very mild deposits, using dispersant additives to slow coking — this is maintenance, not cleaning.
Can the old thermal oil be reused after cleaning?
If the used oil has high acid number, high viscosity, or excessive carbon residue, it's best to replace it entirely. Refilling a clean system with degraded oil defeats the purpose. However, drained oil can be sent for regeneration — some plants recover and reuse regenerated oil as backup, which is a cost-effective approach.
Can we do the cleaning ourselves in-house?
Technically possible, but risky in practice. High-pressure water jetting equipment requires trained operators; chemical solution formulation, temperature control, and circulation management all need experience. Most critically, passivation — this step is often skipped or done incompletely by in-house teams, resulting in post-cleaning corrosion that's worse than before. If you have an experienced boiler maintenance crew, light carbon cleaning may be manageable; for heavy coking, professional cleaning services are the safer choice.
How to choose a cleaning service provider?
Look for three things: (1) documented experience with thermal oil boiler cleaning; (2) a customized solution tailored to your boiler type and deposit condition, not a generic template; (3) clear acceptance criteria (typically: descaling rate ≥95%, intact passivation film, exhaust temperature restored to normal range).
6. Engineering Case Study
A chemical fiber company's 12 million kcal/h thermal oil boiler had operated for 4 years without system cleaning. On-site inspection revealed: exhaust temperature reaching 380°C (normal ≤300°C), fuel consumption 22% above baseline, and maximum tube wall temperature differential of 130°C.
The cleaning plan used the chemical-mechanical combined process: first, alkaline carbon-removal cleaning agent circulated for 18 hours to dissolve most soft deposits; then 600-bar high-pressure water jetting cleaned each tube individually, removing approximately 120kg of hard coke; finally, Sodium Molybdate passivation solution circulated for 3 hours.
Results:
| Parameter | Before | After |
|---|---|---|
| Exhaust Temperature | 380°C | 285°C |
| Fuel Consumption | Baseline +22% | Restored to baseline |
| Tube Wall Temp Differential | Max 130°C | ≤40°C |
| Descaling Rate | — | ≥96% |
| Passivation Film | — | Dense, intact, no corrosion |
Three-month follow-up after cleaning confirmed all parameters remained normal, with estimated annual fuel cost savings of approximately CNY 180,000.
7. Summary
Carbon deposits and coking in thermal oil boilers are inevitable problems, but they can be effectively managed through regular cleaning. Chemical cleaning dissolves soft carbon deposits, high-pressure water jetting tackles hardened coke, and passivation provides a protective film for the cleaned metal — these three steps are interconnected and none can be omitted.
For plant managers, incorporating scheduled cleaning into annual maintenance plans is far more economical than waiting for efficiency to collapse and then performing emergency shutdown repairs. The production loss from a few days of cleaning downtime is negligible compared to the fuel wasted over a year and the very real risk of tube rupture.
All acceptance criteria follow GB/T 25146-2010 Quality acceptance specifications of chemical cleaning for industrial equipment.
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