

Asphalt Pump
The FBE line with Heating Chamber (CA) is the Brazilian asphalt industry standard since the 1950s. Designed to transfer CAP, bitumen, pitch and polymer-modified asphalt at 120 °C to 180 °C, with saturated-steam or thermal-oil jacket integrated into the casing — API 676 3rd edition compliance and active Petrobras CRCC.
What pump to use for asphalt, CAP and bitumen?
The standard pump for asphalt, CAP, bitumen and asphalt emulsion is the external gear pump with Heating Chamber (FBE CA). The integrated jacket with saturated steam or thermal oil maintains fluid between 120°C and 180°C. FB Bombas has been the Brazilian asphalt-plant standard since the 1950s — API 676 3rd edition compliant.
Why is a heating chamber needed?
CAP, bitumen and modified asphalt solidify below 80°C, clogging the pump and piping. The heating chamber (steam or thermal oil jacket) integrated into the FBE CA casing keeps the fluid flowing during operation and short stops. Without it, operating with asphalt without thermal blockage is impossible.
What is the maximum operating temperature?
The FBE CA operates with asphalt and CAP up to 350°C with special mechanical sealing. Typical applications: CAP 30/45 to 85/100 (155-175°C), blown bitumen (180°C), SBS/AMP modified asphalt (170-185°C) and asphalt emulsions (60-80°C). Flow up to 390 m³/h. CRCC Petrobras registered.
CAP, bitumen and pitch: three products, three requirements
Asphalt, bitumen and pitch are often treated as synonyms but require distinct pump configurations. CAP (Cimento Asfáltico de Petróleo) is classified by ANP into four standard penetrations: 30/45, 50/70, 85/100 and 150/200 — refined, clean product with Newtonian behavior between 150 °C and 180 °C, served by standard FBE with steam jacket. Blown (oxidized) bitumen undergoes controlled oxidation that raises viscosity three to five times over the original CAP. It requires higher torque, slightly enlarged clearances, and above 1,500 cSt sustained, switching to FBEI internal gear is technically more efficient. Polymer-modified asphalt (AMP with SBS or EVA) requires low shear to avoid degrading the polymer chain — typical FBEI application. Coal-tar pitch is a distinct product: distillation residue, thixotropic, abrasive, softening point between 40 °C and 120 °C. Requires reinforced casing, enlarged clearances and strict cold-start procedures. Asphalt emulsion (CAE) has acidic pH between 2 and 4 and mandates AISI 316 stainless casing — the only asphalt application where stainless is technically necessary.
- CAP 30/45 at 180 °C ≈ 230 cSt — jacketed FBE, cast iron
- CAP 50/70 at 165 °C ≈ 320 cSt — jacketed FBE, carbon steel or cast iron
- CAP 85/100 at 150 °C ≈ 380 cSt — jacketed FBE, cast iron
- Blown bitumen 85/25 at 150 °C ≈ 2,500 cSt — FBEI preferred
- Coal-tar pitch at 120 °C ≈ 1,500 cSt — FBEI with reinforced casing
- Asphalt emulsion (CAE) — FBEI in AISI 316 stainless, mandatory
- SBS/AMP modified CAP — FBEI to preserve polymer
Heating chamber: why it is mandatory
An asphalt pump without integrated heating fails sooner or later. Heat from product passing through the casing is not enough to keep the entire metal mass above the critical pumping temperature, especially at the mechanical seal, bearings and end covers, which lose heat to the environment more rapidly. The FBE CA (With Heating Chamber) variant solves this: the casing is cast with an integral jacket that circulates saturated steam at 6-10 bar (150-180 °C) or thermal oil up to 300 °C. Steam jacket is the classic standard for conventional asphalt plants with own steam generation. Heating is uniform, response is rapid and there are no cold spots — casing temperature tracks steam temperature with lag under 10 °C in regime. Thermal oil replaces steam when the plant already operates a thermal fluid loop (typical in refineries producing CAP and waterproofing factories), offering more stable temperature and no condensate. Electrical tracing is acceptable only for small pumps (DN50 or smaller) or auxiliary lines. On the main transfer pump it fails to deliver uniform heating on the lower casing and fails repeatedly on cold starts.
Cold start: the number-one error in asphalt plants
Every cold start is a slow-motion destructive test. Most asphalt pump failures in Brazilian plants do not happen in continuous regime but in start-up attempts without sufficient warm-up. Minimum practical temperature to start an FBE pump with CAP 50/70 is 130 °C measured at the pump casing — not the tank, not the line, not the jacket outlet. Below that, CAP 50/70 viscosity exceeds 1,500 cSt and start torque breaks keys, deforms gear teeth or trips the motor breaker. A 20 °C drop typically doubles CAP viscosity, doubling the torque required at the shaft. A motor sized to run CAP 50/70 at 165 °C (320 cSt) and actually running at 145 °C (where viscosity exceeds 550 cSt) enters mechanical overload and trips the thermal — one of the most common failure modes in poorly instrumented plants. The mature start-up procedure follows four steps: heat the jacket for 45 to 60 minutes before energizing the motor, confirming via local thermocouple on the casing that the specified minimum was reached; confirm the discharge valve is open (starting positive displacement against a closed valve is a guaranteed catastrophic failure); energize and run at minimum flow for 2 to 3 minutes before loading the system; monitor vibration and bearing temperature during the first 5 minutes.
Pumping points in an asphalt plant
A conventional asphalt plant has between six and ten distinct pumping points. Truck unloading to the storage tank operates at ~150 °C with viscosity ~600 cSt, served by jacketed FBE 2" or 3". Tank-to-mixer transfer (drum mix) is the most critical point for continuity and operates at ~165 °C with ~320 cSt viscosity for CAP 50/70. Tank recirculation for homogenization can use standard FBE at 160 °C. Burner feed (when the plant uses asphalt itself as tank heater fuel) typically operates at 140 °C with viscosity ~800 cSt — a point where small FBE at 500 rpm is adequate. SBS-modified CAP blending at 175 °C (~1,200 cSt) and asphalt emulsion transfer at 60 °C (~200 cSt) are the two points where FBEI in 316 stainless becomes technically mandatory. Truck loading at the plant exit uses a pump identical to the unloading one — jacketed FBE 2" or 3". The unblocking return loop (line used to maintain minimum circulation when production pauses) operates on standard FBE. Properly sizing each point against actual process temperature is the difference between a plant running 7,000 hours/year and one stopping for maintenance every 90 days.
FB Bombas: 82+ years supplying the Brazilian asphalt industry
FB Bombas has manufactured gear pumps for asphalt transfer since the 1950s, when the first plants in inland São Paulo and Paraná began operation. Today the FBE line is supplied in twelve standard sizes from 1/8" to 6", with steam or thermal-fluid jacket option, in cast iron, carbon steel or 316 stainless — factory specification, not field adaptation. Served plants include federal highway concessionaires, CBIC System paving companies and asphalt emulsion manufacturers across the national territory. FB is registered in Petrobras CRCC Family 6 (Rotating Equipment), enabling direct supply to CAP-producing refineries and Petrobras asphalt terminals. Replacement of imported pumps (Viking, Netzsch, Maag, Edral) is done with direct dimensional compatibility and typical 20-35 calendar-day lead time against 4-8 months from foreign competitors. Spare parts — gears, shafts, bushings, seals, jacket covers — are manufactured in Cabreúva, Brazil, with standard stock available. For plants in critical production regime, FB offers field application-engineer technical support via +55 11 4898-9200.
Frequently Asked Questions
Can I pump CAP 30/45 at 140 °C?
Not safely. At 140 °C, CAP 30/45 exceeds 1,300 cSt, requiring excessive motor torque and accelerating tooth wear. Minimum practical operating temperature is 155 °C, and the start-up procedure recommends 160 °C measured at the pump casing.
Minimum jacket warm-up time before starting the pump?
45 minutes for FBE 2", 60 minutes for DN80 to DN100 models. Always measure temperature at the pump casing with a local thermocouple, not at the steam gauge — a jacket with 180 °C steam may have the casing at only 120 °C due to heat loss to the environment on cold or windy days.
Why did my mechanical seal fail in 3 months on a new asphalt pump?
The most common cause is repeated cold starts or partial loss of the steam jacket (clogged trap, closed condensate valve or jacket leak). In conventional CAP, the type 21 mechanical seal has typical life of 18-36 months. Early failures indicate operation outside the technical envelope — check the steam system, local thermocouple and operational start-up procedure before replacing the seal.
Can I use FBE for heavy blown bitumen or do I need FBEI?
Up to roughly 1,500 cSt sustained, jacketed FBE is sufficient. Above that, FBEI has superior volumetric efficiency and longer service life thanks to internal gear geometry that reduces shear and pulsation. For continuous production of high-viscosity blown bitumen, SBS-modified CAP or waterproofing asphalt, the correct technical choice is FBEI.
Is asphalt corrosive? Do I really need stainless steel?
No, in the vast majority of cases. Hot CAP (150-180 °C) is chemically inert over cast iron and carbon steel — the FBE standard configuration. Stainless is technically necessary only in two situations: asphalt emulsion (CAE) with pH 2-4 which attacks ferrous components, and polyphosphoric acid (PPA) modified CAP, aggressive to iron at 180 °C. For pure CAP, specifying stainless is a waste of capital — three to five times higher cost with no measurable technical gain.
Mechanical seal or graphite packing for asphalt?
Graphite packing is appropriate for simple conventional CAP transfer — more tolerant of cold starts, easier to maintain and lower cost. Cooled double mechanical seal is mandatory in SBS-modified CAP, pitch and asphalt emulsions, where environmental leakage is not acceptable (environmental and operational-safety requirements).
Ideal rotation for an FBE pumping CAP?
600 to 900 rpm for conventional CAP transfer — reduces tooth wear, minimizes pulsation and extends seal life. Rotations above 1,200 rpm accelerate tooth erosion and should be avoided in continuous operation. For blown bitumen and modified CAP, the ideal range drops to 400-700 rpm via reducer or pulley.
Talk to FB Bombas engineering
Send fluid data and operating conditions. Sizing direct from the manufacturer since 1944.
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