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Pumps for Asphalt, Bitumen and Pitch: Technical Guide to Heated Transfer

FBE and FBEI selection for transferring CAP, bitumen, pitch and asphalt emulsions: product data, speed by viscosity, heating (chamber or jacket), start-up, materials and assembly documentation.

FB Bombas technical answer

To specify a pump for asphalt, bitumen or pitch, provide the product (grade and supplier), viscosity at pumping temperature and at start-up, flow, pressure and the available heating. At FB Bombas, the FBE (external gear) lists asphalt among the applications in its 2026 catalog, offers a heating chamber (CA execution) from 1.1/2" to 6" and a recommended speed that drops with viscosity — 300 to 150 rpm in the 50,000 to 100,000 SSU band. The FBEI (internal gear) is published with independent maximums of 136 m³/h, 14 bar differential, 140,000 cP and 340 °C; its jacket follows the manual: steam up to 185 °C and thermal fluid up to 232 °C, at 10 bar.

1. Identify the product: CAP, bitumen or pitch

CAP stands for Cimento Asfáltico de Petróleo, petroleum asphalt cement. Petrobras describes CAP as a high-viscosity petroleum derivative with binding properties and lists CAP 30/45 and CAP 50/70 as conventional grades — the latter with lower viscosity and higher penetration than 30/45. There are also CAP Pro products and modified asphalts. For your pump enquiry, identify the grade and supplier and attach the technical data sheet of the product used.

Terminology varies by market: bitumen may identify the binder called asphalt elsewhere. State whether the product is conventional, oxidized or modified, following supplier documentation.

Coal-tar pitch and petroleum pitch differ from bitumen. Identify product origin and composition and send its technical data sheet for duty assessment.

2. Viscosity by temperature: the central problem

Collect the product curve or test results, with the temperature associated with each viscosity value. Identify the method and unit so engineering can compare the data with pump selection.

Include expected starting and continuous operating conditions. If the supplier data sheet does not cover those conditions, request the missing data before confirming the model and drive.

FBE tables use SSU. The FBE 2026 catalog (p.5) includes a conversion table between viscosity units and states, above 300 SSU, the approximate conversion SSU = cSt × 4.635. Dynamic viscosity (cP) only converts to kinematic with the density at the same temperature; the FBEI, in turn, publishes its maximum in cP (140,000 cP).

DataHow to reportSource documentSelection use
Product identificationCommercial grade, supplier and declared compositionSupplier technical data sheetIdentify the liquid to assess
Kinematic viscositycSt (mm²/s) or SSU, with test temperature in °CProduct test report or curveChoose speed and model in the FBE tables
Dynamic viscosity, when availablemPa·s (cP), temperature and methodTest reportCompare with the FBEI maximum in cP; convert using density
Densitykg/m³ and reference temperatureTechnical data sheet or measurementComplete the liquid physical data
Starting and running conditionsTemperatures and corresponding viscositiesProcess and product dataCheck pump and drive at each condition
Product data for viscosity and temperature assessment

Warning

Send viscosity with its unit and reference temperature. Do not compare cP with SSU without the density, and attach the product data sheet to your enquiry.

3. Heating: pump configuration and available utilities

When specifying heating, distinguish product conditions from the conditions of the utility available at the plant. Provide heating-circuit temperature and pressure and identify the pump configuration to be supplied.

On the FBE, the heating chamber is the CA execution (nomenclature of manual MTEC-01/01), available from 1.1/2" to 6"; the 2026 catalog lists the heating chamber among the series accessories. Confirm the configuration in the quotation and assembly drawing.

On the FBEI, manual MAN001-10 limits the jacket to steam up to 185 °C and thermal fluid up to 232 °C, both up to 10 bar. These jacket limits are not replaced by the 340 °C maximum published for the series in the 2026 catalog.

If the project includes electrical tracing on the piping or another auxiliary system, send its documentation for FB assessment.

4. Starting conditions: confirm before operation

The starting procedure must match the pump, product and installation. For the FBEI, manual MAN001-10 lists explicit checks: feed the heating jackets gradually to avoid thermal shock; confirm that the fluid inside the pump is at adequate temperature and viscosity; turn the shaft by hand at least one full turn; open the valves and wait for the fluid to flow into the pump before starting; and never run the pump without fluid or with water.

Provide engineering with the expected starting temperature and viscosity, together with the product data sheet and pump identification. For the FBE, request the instructions applicable to the supplied configuration.

Confirm the capacity of the pump, motor and transmission assembly under starting conditions. For choosing the commercial motor, the FBE catalog recommends a reserve over shaft power: 50% up to 2 cv, 30% from 3 to 5 cv, 25% from 6 to 10 cv, 15% from 11 to 25 cv and 10% above 25 cv.

Request the starting procedure for the supplied assembly. Identify the product conditions, heating preparation and checks required before equipment release in that documentation.

5. Comparing gear and centrifugal pumps

Evaluate the centrifugal curve corrected for the stated viscosity and compare flow, head, power and suction conditions at the required duty point.

Compare alternatives using the product viscosity curve and installation conditions. The asphalt trade designation does not replace those data.

In gear pumps, delivered flow results from displacement and internal leakage, which varies with pressure and viscosity. The FBE selection table in the 2026 catalog (p.6) applies to viscosity below 1,000 SSU; above that, speed is reduced according to the viscosity table (p.5), with pulley or gear reducer from 7,500 SSU. Request an FBE/FBEI comparison at the same duty point, identifying model, speed and drive.

6. Documenting plant pumping points

Prepare a data sheet for each transfer, recirculation or equipment-feed duty to be assessed. Identify origin, destination and required conditions; different duties may require different models and drives.

If a pump is already installed, also send nameplate photos, its dimensional drawing and motor or gearbox data. This allows comparison of the existing installation with the proposed assembly.

Data itemRequired informationUnit or formatSuggested source
Origin and destinationIdentification of connected tanks and equipmentTags and flow diagramProcess flow diagram
Transfer flowRequired flow and expected variationsm³/h or L/minProcess data sheet
PressuresSuction and discharge; state absolute or gaugeValue, unit and referenceHydraulic calculation or identified measurement
PipingDiameters, lengths, elevations and fittingsDimensioned drawingInstallation isometric drawing
Product at each conditionTemperature, viscosity and densityUnits and reference temperaturesTechnical data sheet and operating data
Drive and heatingElectrical supply, transmission and available utilities (steam or thermal oil)Nameplates and data sheetsEquipment and installation documents
Data collection sheet for each pumping point

7. Documented selection: FBE model, drive and configuration

Use process data to consult the FBE 2026 catalog and manual MTEC-01/01. Size must be confirmed together with speed, required capacity and construction configuration.

Check units before comparing the product data sheet with the tables. The FBE selection table (2026 catalog, p.6) uses flow in L/min, discharge pressure in kgf/cm² and shaft power in CV, for viscosity below 1,000 SSU. The speed-by-viscosity table (p.5) gives, for example, 850 rpm with direct drive from 2,500 to 7,500 SSU (1/2" to 6") and 300 to 150 rpm with pulley or gear reducer from 50,000 to 100,000 SSU (3" to 6").

In Table 5 of MTEC-01/01, the "maximum suction pressure" row goes from 22 kgf/cm² on the smaller sizes to 6 kgf/cm² on the 4" M12: it is a suction limit, not the pump differential pressure. The same table gives a maximum speed of 1,750 rpm up to the 1" DA, 1,150 rpm from 1.1/2" to 4" M12 and a hydrostatic test pressure of 10 kgf/cm².

CriterionData to checkFBE referenceExpected quotation detail
Model and capacityFlow, viscosity, pressure and speed for the selected condition2026 catalog, p.5 and p.6; MTEC-01/01, Tables 1 to 3Identified model and duty point
DriveSpeed, transmission and power2026 catalog, p.4 (motor or geared motor on baseplate) and p.5 (power reserve)Specified motor and transmission
Heating chamberCA execution from 1.1/2" to 6"MTEC-01/01 nomenclature (p.4) and 2026 catalog accessories (p.3)Confirmed heating configuration and utility
Materials and sealingStated product composition, temperature and solids2026 catalog, p.3; MTEC-01/01, Table 6 and sections 2.3 to 2.7Materials and sealing defined for the duty
Connections and installationThread or flange, class and available spaceFBE 2026 catalog, p.6 (BSP from 1/8" to 1"; ANSI B16.5 150 lb flanges from 1.1/2" to 10")Flange standard and class of the quoted execution checked against the piping
Checking FBE selection in the 2026 catalog and manual MTEC-01/01

Engineering note

Ask the quotation to identify the model, speed, motor, transmission, materials, sealing and heating chamber where applicable. Attach the installation drawing for connection checks.

8. Materials and sealing: specify the assembly configuration

The FBE 2026 catalog (p.3) lists casing and covers in ASTM A48 CL30 cast iron, ASTM A536 60-40-18 ductile iron, ASTM A216 WCB carbon steel or ASTM A743 CF8M stainless steel; shafts and gears in SAE 1045 steel or AISI 316L stainless (special treatments on request); bushings in self-lubricating bronze, cast iron, PTFE, graphite or babbitt; and sealing by packing, mechanical seal or lip seal. Check the quoted execution of each component, related to the stated product and conditions.

In manual MTEC-01/01, the allowable temperature of the mechanical seal follows the seal manufacturer recommendation, and the standard seal described in section 2.5 is type 21, ceramic × graphite × Viton. For hot asphalt, sealing and its materials must be confirmed for the real product temperature; do not use the general catalog maximum as the limit of every execution.

Include operating hours, starting frequency and maintenance history when comparing alternatives. These data support discussion of replacement, service access and spare parts with FB; the FBE catalog (p.4) lists the replacement components of the series, from shafts and gears to bushings, sealing and relief valve.

Compare quotations for the same duty point and scope of supply. Check which materials, seals, drive and accessories each option includes.

For emulsions and modified products, send the declared composition, additives and compatibility data provided by the product manufacturer. Record required materials in the specification and ask FB to confirm the available configuration for that duty.

Engineering note

Attach the product data sheet, duty point and material and sealing requirements to your enquiry. Availability and lead time of the requested configuration are confirmed at quotation.

9. Check before your sales enquiry

Organize equipment records and process requirements for technical and commercial comparison. The three points below help complete your enquiry.

  • Maintenance: record inspections, operating hours and equipment events. Request FB maintenance guidance and the parts list for the model and duty.
  • Specification: confirm model limits for the stated liquid — speed by viscosity on the FBE and jacket limits on the FBEI. Identify heating, materials and sealing in the quotation and assembly drawing.
  • Materials: attach the product data sheet and identify components whose material needs confirmation. Include sealing and leakage-containment requirements in the enquiry scope.

Ready to quote your gear pump?

Direct quote on FBE/FBEI from engineering in Cabreúva-SP — fluid, flow, viscosity and temperature. Reply after briefing analysis.

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Frequently asked questions

Technical answers about selection, installation and operation in this application.

Can I pump CAP 30/45 at 140 °C?

Temperature alone does not confirm selection. According to Petrobras, CAP 30/45 is more viscous (lower penetration) than CAP 50/70, and the real viscosity at 140 °C comes from your supplier data sheet. With that value in SSU or cSt, engineering chooses the speed in the FBE viscosity table and checks model, motor and heating. Also send the flow and pressure of the duty point.

What is the minimum jacket warm-up time before starting the pump?

There is no single published time; the criterion is the product condition inside the pump. FBEI manual MAN001-10 instructs feeding the jackets gradually, to avoid thermal shock, respecting the limits of steam up to 185 °C and thermal fluid up to 232 °C (10 bar), and starting only when the fluid inside is at adequate temperature and viscosity. For an FBE with CA chamber, request FB criteria for the supplied assembly.

Why did my mechanical seal fail in 3 months on a new asphalt pump?

To investigate the failure, send pump and seal identification, operating period, temperature and pressure records and photos of inspected parts. One point to check is whether the seal materials were chosen for the real product temperature: in the FBE manual, mechanical seal temperature follows the seal manufacturer recommendation, and the standard seal is ceramic × graphite × Viton. The technical assessment relates the observed damage to duty conditions and equipment history.

Can I use FBE for heavy blown bitumen?

It depends on viscosity at pumping temperature. The speed table in the FBE 2026 catalog goes up to 100,000 SSU, at 300 to 150 rpm with pulley or gear reducer on sizes 3" to 6"; beyond that, or if the range does not fit the FBE, compare with the FBEI, published with an independent maximum of 140,000 cP (a dynamic unit, which needs density for comparison). Send product, viscosity, flow and pressure for assessment.

Which is the right bitumen pump?

Selection starts with the bitumen data and the duty point. The comparison is usually between the FBE (external gear, CA chamber from 1.1/2" to 6") and the FBEI (internal gear with gear reducer), with heating defined by the available utility: chamber or jacket with steam or thermal oil. Send viscosity at pumping temperature, flow and pressure to confirm series, model and heating.

Can the pump run against a closed valve?

Not as a routine. Gear pumps are positive displacement pumps and need overpressure protection. FBEI manual MAN001-10 requires, for pumps without a relief valve, a protection system such as an in-line valve, pressure switch or torque limiter; states that the relief valve must not be used to control pressure or flow nor stay open for long periods; and instructs never to close the valves with the pump running. Confirm with FB the protection applicable to the installed assembly.

Mechanical seal or graphite packing for asphalt?

Both options exist in the series: the FBE lists packing, mechanical seal or lip seal (2026 catalog, p.3); and the FBEI, packing and single, double or cartridge mechanical seals. The choice depends on temperature, product composition and leakage-containment requirements. Send these data to confirm assembly sealing.

What is the ideal rotation for an FBE pumping CAP?

The one in the FBE 2026 catalog (p.5) for the real CAP viscosity at pumping temperature: 1,750 rpm from 30 to 250 SSU; 1,150 rpm from 250 to 2,500 SSU; 850 rpm from 2,500 to 7,500 SSU; 700 to 500 rpm from 7,500 to 10,000 SSU; 500 to 300 rpm from 10,000 to 50,000 SSU; and 300 to 150 rpm from 50,000 to 100,000 SSU — from 1,750 down to 850 rpm with direct drive and below 850 rpm with pulley or gear reducer, always within the sizes listed for each band. Confirm speed, motor and transmission with engineering.

Can I stop the pump full of hot asphalt between batches?

It depends on whether heating keeps the product pumpable during the stop. Send FB the expected stop duration and the product and heating conditions during that period. On restart, follow the FBEI manual criterion: start only when the fluid inside is at adequate temperature and viscosity, turning the shaft by hand before switching on. Confirm the shutdown and restart procedure for the installed assembly.

Next steps

Continue to product documentation, related applications or talk with our technical team.

Your process. The right specification.

Share the fluid, flow, pressure and operating temperature. Include suction conditions and details of the installed equipment, if any. This context helps the FB Bombas team assess your application.

Talk to engineering

To start the assessment

  • Fluid and operating conditions
  • Required flow and pressure
  • Installation and existing equipment