1 / 3Avelta genuine part · AVL-BPD
Tank Immersion Heating Coil Assembly
Welded steel heating coil providing efficient indirect thermal transfer to maintain bitumen at spraying temperature.
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At a glance
| Tube OD | 38 mm or 50 mm (1½ in / 2 in) — to order |
|---|---|
| Wall thickness | Schedule 40 (3.0–3.7 mm) |
| Material | Seamless carbon steel, ASTM A106 Gr. B |
| Working pressure (thermal oil) | Up to 10 bar (145 psi) |
| Temperature rating | Up to 260 °C (500 °F) |
| Heat-transfer area | 4–18 m² (43–194 ft²) — tank-capacity matched |
| External connection | DN32 or DN40 flanged, tank exterior |
| Hydrostatic test | 1.5× working pressure, as-built certificate supplied |
Overview
The immersion heating coil is a fabricated serpentine or U-bank tube assembly welded inside the bitumen tank, running the full usable length of the tank interior on the AVL-BPD. In thermal-oil heating systems the coil carries circulating heat-transfer oil at 200–250 °C (392–482 °F); in direct-fired hot-gas designs it acts as the primary heat exchanger between flue gases and the stored bitumen. The coil transfers heat uniformly into the bitumen without direct flame contact, preventing localised thermal degradation of the binder.
The heating coil determines both the heating rate and the temperature holding capacity of the tank. Adequate coil surface area is critical: insufficient area produces extended heat-up times from cold on remote site starts, and localised hot-gas systems with undersized coil sections can produce bitumen oxidation near the heat entry point.
Function
Bitumen must be held between 150 °C and 185 °C (302–365 °F) for effective spraying. The coil provides the thermal mass to raise a full cold charge from ambient to working temperature — typically 3–5 hours for a 6,000 L (1,585 gal) tank — and to compensate for heat loss to the ambient environment during extended site operations in cold weather. Damaged or scaled coil sections produce cold zones where bitumen viscosity rises, restricting pump suction, reducing delivery pressure and causing uneven spray application. A leaking coil section contaminates the bitumen charge with heat-transfer oil, which alters binder properties and requires full tank purge and clean-out.
Construction & quality
Tube: seamless carbon steel, 38 mm or 50 mm OD (1½ in or 2 in), schedule 40 wall, ASTM A106 Gr. B or equivalent. Bends: socket-welded or butt-welded, 1.5D radius to avoid stress concentration. Headers: heavy-wall carbon steel with flanged external connections. Tank wall penetration: reinforced by backing ring welds. Internal surface: bare carbon steel — bitumen provides cathodic protection against corrosion in service. Support brackets: carbon steel saddles welded to tank floor, allowing longitudinal thermal expansion. Each assembly is fully hydrostatically tested at 1.5× working pressure before despatch.
When to replace
- Heat-transfer oil visible in the bitumen charge — milky appearance or abnormal behaviour — indicating a coil tube leak
- Bitumen temperature fails to reach or hold the setpoint despite the burner running at full output
- A localised cold zone at one end of the tank detected with a surface contact thermometer
- Thermal oil circuit pressure drops consistently between pump cycles without a visible external leak
- Sludge or scale accumulation on coil outer surface reducing heat transfer, visible on internal tank inspection
Compatibility & fitment
Fabricated to tank-specific dimensions for the full AVL-BPD range from 1,000 L to 10,000 L; coil configuration — serpentine or U-bank — tube OD, header positions and penetration flange layout are all matched to the customer's tank serial number and drawings.
Why buy from Avelta
Each coil assembly is fully welded, hydrostatically tested and supplied with an as-built hydrostatic test certificate; dimensional drawings are included for plant maintenance records.
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