Pumps for Petrochemical and FuelsTechnical Guide for Distribution Bases and Terminals

1. The seven central products of the sector

From a pumping standpoint, the Brazilian petrochemical and fuels sector is dominated by a restricted set of products with specifications well defined by ANP, ABNT and international ASTM standards. The table below summarizes the seven main ones, with the physical-chemical properties most relevant for pump selection: density, viscosity at operating temperature, flash point, vapor pressure at 38 °C (critical for NPSH calculation) and hazard class per NBR 17.505.

2. Where FB Bombas serves and where it does not

Honesty about scope is a differentiator in a sector where exaggerated promises cause catastrophic failures. FB Bombas is CRCC Petrobras-qualified for supply to a specific series of applications within the petrochemical and fuels chain — but it is not a manufacturer of refinery hot pump service, and that is a territory where international API 610 is mandatory and normalized process pump manufacturers should not compete.

Being clear about this boundary is what enables delivering a technically correct solution where the FBCN line actually excels.

The correct applications for the FBCN and FBE lines in the sector are: transferring diesel, gasoline C, QAV-1 and anhydrous ethanol in distribution bases; truck-tank and rail-car loading and unloading operations; tank-to-tank transfer in terminals and TRR; refinery utilities (process water, cooling water, firewater in booster and jockey pumps, cooler lube oil circuits, demineralized water); industrial boiler feed with heated BPF (typical service for FBE 1.1/2" to 2"); feeding furnaces, emergency diesel generators and associated thermal oil systems.

Out-of-scope applications — which must be served by specialized API 610 manufacturers — are: hot pump service with charge pumps on atmospheric and vacuum distillation units, hydrotreatment and catalytic reforming charge pumps, FCC slurry, high-H₂S streams, and any continuous service above 40 bar with hot fluid.

3. NPSH in volatile products: concrete calculation for gasoline C

The real challenge of pumping gasoline, QAV-1 and naphtha lies in vapor pressure, not viscosity. Gasoline C at 38 °C has vapor pressure of about 50 kPa — roughly half an atmosphere. Any error in the available NPSH calculation leads to immediate suction cavitation and accelerated impeller degradation. The example below demonstrates the calculation applied to a typical tank-to-tank transfer system in a distribution base.

Consider a system with an atmospheric tank, minimum level two meters above the pump axis (flooded suction), DN100 suction line, 30-meter total length with two 90° bends and a Y-strainer. Ambient temperature 30 °C. Local atmospheric pressure is 101.3 kPa and gasoline vapor pressure at 30 °C is about 50 kPa. Density is 745 kg/m³.

The NPSHa calculation becomes: first, (Patm − Pv) / (ρ × g) = (101,300 − 50,000) / (745 × 9.81) = 7.02 meters; adding a static column of +2.00 m, subtracting friction loss of approximately 0.8 m at 80 m³/h flow, and deducting a 0.3 m safety margin for a partially dirty strainer, arrives at NPSHa near 7.9 meters.

Typical NPSHr of an FBCN 80-200 (DN80 suction, 80 m³/h rated flow, 1,750 rpm) is between 3.0 and 3.5 meters. The available margin of approximately 4.4 meters is comfortable. Hydraulic Institute best practice recommends a minimum margin of 1.0 m above NPSHr, or 1.3 times NPSHr for volatile hydrocarbons.

In a negative-suction configuration (buried tank, for example 2 meters below the pump axis), the calculation drops to about 3.0 meters — marginal, requiring a vertical-shaft pump, reduced rotation, or installation of a dedicated booster pump.

4. ATEX, INMETRO and Zone 1 classified areas

All pump islands and volatile fuel handling areas in Brazilian distribution bases and terminals operate in Zone 1 (probable presence of explosive atmosphere) or Zone 2 (improbable, short-duration presence), per ABNT NBR IEC 60079-10-1 classification. The electrical design standard in classified areas in Brazil also follows Petrobras N-2708 for installations contracted by that company, and complementary practice API RP 500/505.

An important compliance note: in Brazil, the certification equivalent to the European ATEX seal is issued by INMETRO per Ordinance 179/2010 — ATEX and INMETRO are equivalent from the technical standpoint but not the legal standpoint, and the Brazilian customer must require INMETRO certification, not just ATEX marking.

On the pump skid, this has specific implications: the electric motor must be Ex d IIB T3 for gasoline and LPG, Ex d IIA T3 for diesel and BPF, and in Zone 2, Ex nA is acceptable. The pump-motor coupling must have anti-spark guarding, typically in bronze or non-metallic composite, per EN 13463-1. Equipotential grounding between pump, motor, base and skid must have total resistance below 10 ohms, periodically verified.

Instrumentation (pressure sensors, temperature transmitters, pressure switches) must be Ex ia (intrinsically safe) or Ex d, and all cables must be routed with INMETRO-certified Ex d cable glands. FB Bombas supplies complete skids with WEG or Siemens motorization already certified, directly meeting compliance requirements for distribution bases and terminals without requiring the customer to manage multi-vendor certification.

5. Sealing: API 682 plans applied by product

The mechanical seal is the most critical component of a pump in volatile fuel service — not because it is the most expensive, but because its failure means direct emission of flammable vapor to the atmosphere. API 682 standardizes sealing plans, and the choice among them depends on product, volatility, environmental compliance and the system's tolerance for additional complexity.

For low-volatility products like diesel S10 and S500, Plan 11 (discharge recirculation across the seal face) is typically sufficient. For gasoline, naphtha and LPG, the rule is a double mechanical seal with Plan 53A or 53B (pressurized barrier with clean fluid), required both by volatility and by fugitive emissions controlled by CONAMA 382.

QAV-1 and kerosene occupy an intermediate position: simple Plan 11 or 13 is acceptable at the regulatory minimum, but the double plan is preferable in modern installations and at airports where ANAC requires stricter control.

Heated BPF at 80-90 °C requires Plan 32 (external flush with clean fluid to keep the seal face free from coking) or Plan 62 (external quench) — and here the choice typically falls on the FB Bombas FBE line, which is a gear pump suited to the elevated viscosity of BPF at that temperature.

The standard FB Bombas FBCN comes from the factory with a cartridge-type mechanical seal per ISO 21049 / API 682, silicon carbide and carbon faces, and FKM (Viton) elastomers, covering most non-BPF fuel applications without additional configuration.

6. Diesel S10: the reduced lubricity problem

Diesel S10, with maximum sulfur content of 10 ppm, has reduced lubricity compared to S500 and higher-sulfur diesel. The HFRR test per ASTM D6079 / ABNT NBR 14.359 limits wear to 460 micrometers maximum, and lubricity additives are added by the distributor to meet this limit — but the safety margin relative to the pump is lower than in S500.

For centrifugal pumps like the FBCN, this reduction has no practical impact: hydrodynamic lubrication at external bearings is by grease or oil from the bearing itself, independent of the pumped fluid. The impact appears at two specific points: at mechanical seal faces during start-up, and in gear pumps that use the pumped fluid itself to lubricate the teeth.

At the seal faces, pure S10 can cause stick-slip (intermittent friction) in carbide-on-carbide face combinations. The recommended solution is specifying silicon carbide against carbon faces, or silicon carbide against silicon carbide with hydropad profile — configurations that maintain an adequate hydrodynamic film even at dry starts.

For FBE gear pumps applied to pure S10, the recommendation is to operate at reduced rotation (not above 1,150 rpm) and slightly enlarged clearances — but FBE is not the ideal choice for clean diesel, and FBCN is preferable whenever fluid viscosity allows (i.e., always for pure diesel).

7. Typical pumping points in a distribution base

A fuel distribution base has between eight and fifteen distinct pumping points, depending on size and number of products handled. The table below lists the ten most frequent points, with typical flow range and the applicable FB Bombas series.

Note that the boiler feed pump with heated BPF is the only base point where the FBE external gear series is typically chosen — all others are FBCN centrifugals in different material, sealing and certification configurations.

8. Material matrix by fuel product

Material selection in the fuels sector has different rules than in sugar-ethanol or petrochemical hot service. Most products are chemically inert over carbon steel and cast iron; important exceptions are hydrous ethanol (which requires AISI 316), gasoline C with 27% ethanol (which slowly corrodes cast iron through moisture absorption and galvanic corrosion), and petrochemical naphtha at elevated temperature.

The table below summarizes recommended combinations, reflecting consolidated practice for CRCC Petrobras qualification.