140–180 °C · Thermal Oil · API 650

Design and fabrication of
bitumen tanks for industry!

An engineering guide to insulation and shop fabrication of industrial bitumen storage tanks

A bitumen tank combines structure, heat and control; the bitumen must stay at 140 to 180 °C so it can be pumped, without solidifying or oxidising.

Bitumen storage tank built by Behineh Ab
Operating temperature
Usually 140 to 180 °C
Vertical capacity
Several hundred to 10,000+ m³
Horizontal/mobile capacity
Usually 10 to 100 m³
Shell standard
API 650 · sometimes ASME VIII
Bitumen held at 140–180 °C without solidifying or oxidising
Vertical refinery tanks or horizontal/mobile asphalt-plant tanks
Heating: thermal oil · fire tube · electric/trace
Designed to API 650 / ASME VIII · A36/A516 steel
Rockwool insulation + aluminium cladding
Coil pressure test · vacuum box · MDR and as-built

Design and fabrication of

industrial bitumen storage tanks · Behineh Ab Engineering

A bitumen storage tank is a carbon steel vessel that keeps bitumen at a controlled temperature and away from moisture. Unlike tanks for light products, structure, heat and control are integrated here, because bitumen's rheology depends strongly on temperature.

At 140–180 °C (grades such as 60/70 or 85/100 and polymer-modified bitumen) it can be pumped; a drop in temperature means solidifying and pumping stopping, and too much heat means oxidation and loss of penetration. Applications: refineries (blowing unit), export terminals and asphalt plants. This article covers the path from tank types to heating, insulation, fabrication, safety and a shop guide.

2. Tank types by structure

2.1. Vertical vs. horizontal

Vertical: several hundred to 10,000+ m³, optimal footprint, ring coils; the vertical temperature gradient needs an agitator or careful coil layout. Horizontal: usually 10–100 m³, elliptical/hemispherical heads, saddles and Zick analysis; a higher surface-to-volume ratio means more heat loss but simpler temperature control.

Fixed vs. mobile
ParameterFixed (plant)Mobile / skid
Typical capacity500 to 10,000+ m³10 to 100 m³
FoundationConcrete, API 650 Annex BSteel skid
Main heatingCentral thermal oilElectric or independent burner
Start-up from coldSeveral daysA few hours
UseRefinery · terminalAsphalt · temporary project

3. Heating systems

3.1. Thermal oil

The dominant standard for large tanks. The fluid is heated to ≈300 °C in a central heater; seamless 2–4 in coils, serpentine or parallel, on the bottom. Precise control with no direct flame → minimal coking. Needs an expansion tank and an oil network.

3.2. Direct fire tube

Tube surface up to 350–450 °C; controlling heat flux and circulation/agitation is essential to prevent coking. Lower capital cost but poorer control and efficiency — for medium capacities or where thermal oil is not available.

3.3. Electric

Immersion heaters or trace heating with PID and independent zoning. No fuel on site; electricity cost and infrastructure limit it on very large tanks. Suits small terminals and mobile tanks.

4.1. Shell thickness API 650

For a vertical atmospheric tank, course thickness is calculated by the one-foot or variable-point method:

Design thickness
t_d = [4.9 × D × (H − 0.3) × G] / S_d + C.A.
G of bitumen
Usually ≈ 1.0 to 1.05
Common steels
A36 · A283-C · A516-70 (S_d at design temperature)
Radial heat loss
Q/L = 2π(T_i−T_o) / Σ(ln(r_{i+1}/r_i)/k_i + 1/(h_o r_o))
Design temperature and pressure

Allowable stress must be read at the design temperature (not ambient); above ≈150 °C steel strength drops. Annex S has thermo-mechanical requirements above 93 °C. If vapour pressure or transfer with compressed air pressurises the tank, ASME VIII Div 1 governs. Rockwool of 100–150 kg/m³, usually 80–150 mm on the shell and 100–200 mm on the roof; corrugated aluminium cladding 0.6–0.8 mm.

5. Fabrication and assembly in the shop and on site

5.1. Rolling and NDT

Plate rolling checked with a curvature template. Vertical seams: GTAW/SMAW root + SAW fill; course-by-course erection. WPS/PQR and ASME IX-qualified welders. Spot or full RT, UT of the bottom, MT/PT of fillets, vacuum box on the bottom.

5.2. Heating coil

Prefabricated spools on coil supports, held off the bottom. Hydrotest at 1.3–1.5× design for 30–60 min, then a pneumatic test with foaming agent. Full draining and drying of the coil is mandatory — residual moisture risks a steam explosion with hot bitumen.

6. Accessories and safety

Agitator, level, safety

Side- or top-entry agitators to prevent settling and even out temperature (especially for polymer bitumen). Multi-level RTDs + PLC/SCADA. Level: guided-wave radar preferred over floats. Emergency drain, P/V valve, foam/sprinkler fire protection, sometimes N₂ blanketing.

Guide: API 650 and shop drawings

The standard's role and the shop package

Joint efficiency 0.7–1.0 depending on RT level; Charpy at MDMT for cold start-up; Annex S for high temperature; Annex B for foundation and tolerances. Shop package: plate layout, weld details, WPS/PQR, coil layout, ITP with hold/witness points — TPI approval before cutting.

Guide: welding dense coils

Access, distortion, sequence

Tube spacing is often 150–300 mm. Do as much welding as possible in the open shop; only tie-ins inside the tank. Balanced/backstep sequence and temporary jigs. Coordinate coil installation with the shell courses before the roof goes on.

Guide: insulation and quality control

Insulation and cladding

After hydrotesting the shell/coil and painting (Sa 2.5 + heat-resistant primer). Multi-layer staggered rockwool with bands and pins. Cladding with ≥50 mm overlap in the rain direction; flashing and sealant at nozzles — more than half of insulation loss comes from water entering at exactly these points.

Tolerances and foundation

Vacuum box on the bottom; full hydrotest of the shell. Plumbness ≈1/200–1/300 of height, roundness, bottom flatness, nozzle positions. Foundation: level, concrete strength, anchor bolts, drainage slope — before the first course.

Summary

A successful bitumen tank is the result of an API 650 structure, a suitable heating system, economical insulation and strict quality control of the coil and shop work.

Behineh Ab Engineering designs, builds, tests and delivers fixed and mobile bitumen tanks to suit the capacity and site climate.

Technical specifications

Operating temperature
Usually 140 to 180 °C
Vertical capacity
Several hundred to 10,000+ m³
Horizontal/mobile capacity
Usually 10 to 100 m³
Shell standard
API 650 · sometimes ASME VIII
Main heating
Thermal oil coil
Insulation
Rockwool 80–150 mm + Al cladding

Why is thermal oil preferred over a fire tube?

Central control of the heat-transfer fluid's temperature, with no flame touching the bitumen, reduces the risk of coking and is the industry standard for large refinery tanks.

Why is drying the coil after the hydrotest critical?

Water left in the coil turns to steam on contact with hot oil and causes local pressure or a steam burst in contact with hot bitumen; this step must never be cut short.

Where is insulation weakest?

More than half of long-term performance loss comes from water getting in at nozzles and through poor flashing, not from too little rockwool thickness.

Applications and industries

Refineries, after the bitumen blowing unit
Refineries, after the bitumen blowing unit
Export terminals and ship/tanker loading
Export terminals and ship/tanker loading
Asphalt batch plants
Asphalt batch plants
Temporary road-building projects
Temporary road-building projects (mobile tank)
Homogenising and storing 60/70 and 85/100 grades
Homogenising and storing 60/70 and 85/100 grades
Polymer-modified bitumen
Polymer-modified bitumen

Frequently asked questions

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Bitumen tank design & fabrication

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