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Tanker Biofouling Management Guide

Biofouling exposure: High

Overview

Understanding tanker biofouling

Oil tankers carry crude oil and refined petroleum products in bulk. Crude tankers move unrefined crude from extraction points to refineries; product tankers, generally smaller, carry refined products to consuming markets.

Classes follow deadweight tonnage (DWT). Ultra large crude carriers (ULCC, above 320,000 DWT) are now mostly floating storage; very large crude carriers (VLCC, 200,000–320,000 DWT) carry 2 million barrels from the Middle East to Asia. Suezmax (120,000–200,000 DWT) and Aframax (80,000–120,000 DWT) run Mediterranean, North Sea, and Caribbean trades, above the Long Range, Medium Range, and General Purpose product classes.

Tankers run at 12 to 15 knots and slow steam routinely. Non-biocidal foul-release coatings depend on hydrodynamic shear and are effective across roughly 15 and above, according to the US EPA review of underwater ship husbandry, so much of the fleet operates below the speed at which these coatings work as designed.

Tankers also spend long periods stationary: ballast waiting at anchorage, demurrage at congested terminals, and floating storage during oversupply. AIS data for ships over 500 GT, analysed by UMAS and UCL in 2024, found commercial vessels spend 15 to 22 days per year at anchor; floating storage can add weeks or months in warm water.

Marine biofilm, the first stage of biofouling, forms on all submerged surfaces within hours of immersion regardless of coating or speed, as described in a 2022 review in Nature Reviews Microbiology. According to the 2024 GESAMP Working Group 44 report on marine biofouling, a thin biofilm covering 50 per cent of a hull can increase fuel consumption by approximately 25 per cent; heavy macrofouling can raise it by up to 50 per cent.

Given the very large wetted surface areas of VLCC and Suezmax hulls, the absolute fuel and emissions penalties from tanker fouling are among the largest of any vessel type .Under the Carbon Intensity Indicator (CII) framework, hull condition is a significant variable in a vessel's rating.

Crude flows run from the Arabian Gulf through the Strait of Hormuz (around 20.9 million barrels per day) and across the Indian Ocean to Asia via the Strait of Malacca (around 23.2 million), warm, biologically productive waters that sustain year-round fouling.

A growing share of the ageing crude fleet operates as the so-called shadow fleet in sanctioned trades, with deferred maintenance, extended drydocking intervals, and limited access to class-approved coating and cleaning services, so fouling and its fuel, emissions, and biosecurity consequences run higher.


Global fleet

The tanker fleet at a glance

Active tankers (oil, crude and product)

24 978

Total active oil tanker fleet (2026).

Significance

Tankers pair the largest wetted surface areas in commercial shipping with a low-speed, high-idle profile in the warm Arabian Gulf, Strait of Hormuz, and Strait of Malacca crude corridors, and transit the Suez Canal, Bab el-Mandeb, Panama Canal, Turkish Straits, and Danish Straits between biogeographically distinct waters.

CompanyVessels (approx.)
Sinokor Merchant152
COSCO Shpg Energy120
TORM A/S89
Frontline80
Scorpio Tankers72
Dynacom Tankers67
Intl Seaways63
Hafnia Limited63

High risk regions

Where tankers face the highest fouling pressure

A handful of high-volume crude corridors route the tanker fleet repeatedly through the warmest, most biologically productive waters in commercial shipping.

A 2022 study in Frontiers in Marine Science found that in the Arabian Gulf, macrofouler coverage exceeded 86 per cent after six months immersion in southwestern Omani waters, with biomass more than triple that at cooler Kuwaiti sites.

A 2026 Marine Pollution Bulletin assessment across 35 European locations found Mediterranean sites showed the highest fouling intensity, with salinity the dominant driver rather than temperature alone. Ten principal regions are profiled below.

Arabian Gulf

Exposure:

High

Water temperature

~18 to 34 °C (yearly range)

Common fouling species

Amphibalanus amphitrite, Balanus sp., Hydroides elegans, Perna viridis, Saccostrea cucullata, tunicates, hydroids

Red Sea and Bab el-Mandeb

Exposure:

High

Water temperature

~22 to 32 °C (yearly range)

Common fouling species

Amphibalanus amphitrite, Saccostrea cucullata, Hydroides elegans, serpulid tubeworms, encrusting bryozoans

West Africa

Exposure:

High

Water temperature

~24 to 29 °C (yearly range)

Gulf of Guinea crude-loading region; warm equatorial waters, year-round settlement.

Common fouling species

Amphibalanus amphitrite, Crassostrea spp., Balanus spp., serpulid tubeworms, hydroids

Mediterranean

Exposure:

High

Water temperature

~14 to 29 °C (yearly range)

Highest fouling intensity among European regions, salinity the dominant driver (Kim et al., 2026); Aframax and Suezmax regional crude trades.

Common fouling species

Mytilus galloprovincialis, Amphibalanus amphitrite, Ciona intestinalis, bryozoans, Ulva spp.

North Sea and Baltic

Exposure:

Medium

Water temperature

~5 to 18 °C (yearly range)

Common fouling species

Semibalanus balanoides, Mytilus edulis, Ulva spp., diatom films

Strait of Malacca and SE Asia

Exposure:

High

Water temperature

~27 to 31 °C (yearly range)

Around 23.2 million barrels per day; principal gateway for Gulf crude to Asian refineries, concentrating traffic and anchorage.

Common fouling species

Amphibalanus amphitrite, Perna viridis, Hydroides elegans, colonial tunicates, hydroids

East Asia refining hubs

Exposure:

High

Water temperature

~15 to 30 °C (yearly range)

Primary discharge destination for long-haul crude; heavy anchorage queuing at import terminals.

Common fouling species

Amphibalanus amphitrite, Balanus reticulatus, Hydroides elegans, Perna viridis, bryozoans

US Gulf Coast

Exposure:

High

Water temperature

~18 to 31 °C (yearly range)

Major crude and product export region; warm, nutrient-rich coastal waters.

Common fouling species

Amphibalanus amphitrite, Crassostrea virginica, Hydroides elegans, hydroids, tropical algae

Caribbean and Latin America

Exposure:

High

Water temperature

~24 to 30 °C (yearly range)

Warm year-round waters serving Latin American crude exports; relevant to Brazilian terminal calls.

Common fouling species

Amphibalanus amphitrite, Hydroides elegans, calcareous algae, hydroids, colonial tunicates

US West Coast and North Pacific

Exposure:

High

Water temperature

~10 to 22 °C (yearly range)

Los Angeles, San Francisco, and Long Beach crude and product terminals operate under California's mandatory biofouling rules.

Common fouling species

Mytilus galloprovincialis, Balanus glandula, bryozoans, Ciona intestinalis

Vessel risk areas

High biofouling risk areas on tankers

Oil tankers have a simple appendage profile: a niche-area-to-wetted-surface-area ratio of approximately 8 per cent, among the lowest of the vessel types assessed in a 2017 Biological Invasions study of the global fleet.

On hulls this large, even that low proportion is a substantial absolute niche area, and the high-idle profile means the flat bottom and seawater systems foul readily.

For tankers, sea chests, the propeller and shaft, the rudder, and the extensive flat bottom matter most; stabiliser fins are not fitted and thrusters are uncommon.

Sea chests & gratings

Risk:

High

Why this area fouls

Sea chests feed raw seawater to the tanker's cooling, ballast, firefighting, and inert gas systems. Their interior surfaces see near-zero flow at any vessel speed, so fouling settles and develops undisturbed.

During ballast waiting and floating storage in warm anchorages, the seawater systems keep drawing water through the sea chests while the vessel is stationary. Angular grating geometry limits coating film thickness at edges, creating localised coating-failure points; the IMO Biofouling Guidelines single out corners, edges and grating bars for particular attention during coating application.

Mitigation

  • Specialised coatings: biocidal formulations suited to near-zero flow; attend to film thickness at angular grating edges.
  • MGPS: Marine Growth Prevention System; copper and aluminium ion dosing protects continuously regardless of vessel speed, essential during long stationary periods.
  • Inspection and documentation: record sea-chest condition in the biofouling record book.

Flat bottom

Risk:

High

Why this area fouls

A crude tanker's flat bottom is an exceptionally large horizontal surface; on a VLCC it spans a 60-metre beam for much of the vessel's length, one of the largest continuous settlement surfaces of any vessel type.

Fouling intensity across the flat bottom correlates with time spent stationary, and slow steaming plus ballast waiting and floating storage maximise that exposure. Barnacle adhesion force increases exponentially with organism base diameter, so fouling left to establish during long waiting periods becomes progressively harder to remove.

Mitigation

  • Antifouling coatings: the primary drydock focus; on a VLCC flat bottom, specification and application quality translate into very large absolute fuel savings.
  • Ultrasonic antifouling: transducers bonded to the inside of the hull plating, with no hull penetration, carry ultrasonic energy along the plates to discourage settlement across the flat bottom while the vessel is stationary or slow steaming; it runs continuously and supplements the coating rather than replacing it.
  • Proactive grooming: hull-crawling robots suit the large flat expanse; in a 54-month Florida Institute of Technology trial, weekly grooming sustained a fouling rating of zero with no non-indigenous species on groomed surfaces.
  • Reactive in-water cleaning: brush and cavitation jet systems for established fouling; must conform to local capture and containment requirements.

Propeller & shaft

Risk:

High

Why this area fouls

The propeller and shaft are performance-critical despite low service speed: the very large power demand of crude carriers converts any efficiency loss into significant absolute fuel and emissions penalties. During slow steaming, ballast waiting, and floating storage the propeller sits stationary in warm water and fouls.

AA 2023 CFD study in Polish Maritime Research found that at medium calcareous fouling, thrust can fall 26 per cent and torque rise 7 per cent, cutting propeller efficiency 30.9 per cent; an unpainted propeller may need 57.8 per cent more power after four years versus 2.7 per cent with foul-release coating. The greatest proportional loss occurs from clean surface to light slime.

Mitigation

  • Propeller coating: foul-release coating limits degradation: 2.7% versus 57.8% additional power over four years (Zinati et al., 2023).
  • Propeller polishing: scheduled in-water polishing restores surface smoothness between drydockings.
  • Ultrasonic antifouling: transducer positions at the stern can extend coverage to the propeller area in line with the system design, limiting biofilm on the blades during port calls and anchorage; it complements propeller coating and polishing.
  • Performance monitoring: ISO 19030 metrics and slip-ratio tracking flag propeller fouling before penalties compound.

Rudder

Risk:

Medium

Why this area fouls

Crude tanker rudders sit in the turbulent propeller slipstream in transit, which accelerates coating erosion on leading and trailing edges.

During long stationary periods the rudder, its fittings, and recesses offer sheltered surfaces where fouling establishes, and its position in the propeller wash makes coating condition hard to inspect during underwater surveys.

Mitigation

  • Coating specification: abrasion-resistant formulations suit leading edges better than soft self-polishing systems.
  • Drydock inspection: inspect the rudder and fittings specifically at drydock, where failures hidden by propeller wash in-water can be identified.

Internal seawater systems

Risk:

High

Why this area fouls

Tankers run extensive seawater circuits for engine cooling, ballast, firefighting, and inert gas generation: continuously wetted internal surfaces invisible to hull inspection and unprotected by hull coatings.

These systems keep drawing warm seawater during ballast waiting and floating storage, sustaining internal fouling pressure while the vessel is stationary. The IMO Biofouling Guidelines (MEPC.378(80)) identify MGPS downtime as a risk parameter to log in the biofouling record book.

Mitigation

  • MGPS: copper and aluminium ion dosing is the primary proactive tool; anode sizing and positioning relative to circuit flow govern effectiveness.
  • Monitoring and logging: anode consumption and strainer inspection records evidence biosecurity compliance; log MGPS downtime in the biofouling record book.

Risk profile

Summary of biofouling risk for tankers

How hull geometry, operating profile, niche-area share, regional trading, the shadow fleet, and biosecurity exposure shape tanker biofouling risk: a qualitative rating anchored in performance exposure, recognising compliance and biosecurity implications too.

DimensionTanker characteristicWhy it matters
Hull geometryVery large wetted surface area, particularly on VLCC and Suezmax hulls; exceptionally large flat bottom.The absolute fuel and emissions penalties from tanker fouling are among the largest of any vessel type; biofilm on 50% of a hull can raise fuel use ~25%, heavy macrofouling up to 50% (GESAMP, 2024).
Operating profileLow service speeds (12–15 knots) with routine slow steaming; extended ballast waiting, demurrage, and floating storage leave the hull stationary for long periods.Foul-release coatings effective at 15–30 knots (US EPA, 2011) often operate outside their designed envelope; commercial vessels average 15–22 days/year at anchor, higher for tankers in floating storage (UMAS, 2024).
Niche areas8% niche-area-to-WSA ratio (Moser et al., 2017), but very large absolute niche area; sea chests and propeller are highest-consequence areasPropeller fouling at medium calcareous condition can cut efficiency 30.9%; an unpainted propeller may need 57.8% more power after four years vs 2.7% with foul-release coating (Zinati et al., 2023).
Regional tradingCrude corridors route the fleet repeatedly through the Arabian Gulf, Strait of Hormuz, and Strait of Malacca, among the highest fouling-pressure waters in commercial shipping.Arabian Gulf macrofouler coverage exceeded 86% after six months in Omani waters (Muthukrishnan et al., 2022); the Mediterranean shows the highest fouling intensity in European waters (Kim et al., 2026).
Shadow fleet dimensionA significant proportion of the ageing crude fleet operates as the sanctioned shadow fleet with deferred maintenance and extended drydock intervals.Deferred hull husbandry on ageing tonnage is associated with higher fouling accumulation and correspondingly higher fuel, emissions, and biosecurity consequences.
Biosecurity exposureCalls at New Zealand, Australian, and California ports on Pacific crude and product trades.Between 56% and 70% of established coastal non-indigenous species are attributed to transport via biofouling (GESAMP, 2024); non-compliant hulls can face denied port entry.
Performance & complianceHull condition is a significant variable in CII calculations; steady speeds on defined routes support meaningful performance normalisation.Thin biofilm covering 50% of a hull can increase fuel consumption by ~25%; heavy macrofouling can raise fuel use by up to 50% (GESAMP, 2024), impacting CII ratings.

Management practices

Recommended biofouling management for tankers

Antifouling coatings (SPC, CDP, hybrid, foul-release, silicone-hydrogel, biocide-containing foul-release), ultrasonic and MGPS systems, in-water cleaning and ROV (remotely operated vehicle) hull grooming, drydock cleaning, and performance and condition monitoring for the low-speed, high-idle tanker profile.

  • Ultrasonic and MGPS systems

    Tankers spend long periods stationary in warm anchorage and floating storage waters, where coatings protect least and fouling takes hold fastest. Active systems add a layer of defence proportional to idle time.

    • Ultrasonic antifouling — complementary layer that disrupts settlement during ballast waiting and floating storage.
    • MGPS for sea chests and strainers — copper and aluminium ion dosing to suppress accumulation in continuously running seawater circuits.

    Technical detail by system type

    Ultrasonic antifouling

    Ultrasound keeps working while a tanker sits still, which is why it suits vessels that spend weeks in ballast waiting or floating storage. In DHI's controlled exposure tests, protected panels showed a clear reduction in fouling, though results from systems installed on ships have been more variable (DHI, PortPIC 2026). It is used in addition to the hull coating, not instead of it, and should run from before immersion through every idle period.

    MGPS for sea chests and strainers

    Marine Growth Prevention Systems dose copper and aluminium ions into the seawater circuits that run continuously during ballast waiting and floating storage. Internal fouling restricts flow and degrades cooling, so for tankers idling in warm waters consistent MGPS operation is a high priority.

  • Tankers combine 12 to 15 knot service speeds with long stationary periods in warm anchorages and floating storage, a duty cycle largely below the speed envelope at which conventional foul-release systems work.

    • Self-polishing copolymers (SPC) — flow-driven biocide release; polishing rate slows at low tanker speeds.
    • Controlled depletion polymers (CDP) — passive depletion less speed-dependent; limited in warm tropical anchorages.
    • Hybrid coatings (SPC/CDP blends) — well matched to the slow-steaming, high-idle tanker profile.
    • Silicone foul-release — depends on 15–30 knot shear; a poor match for most tankers.
    • Fluoropolymer foul-release — same speed-dependent limitation; potential durability advantage for longer dockings.
    • Silicone-hydrogel hybrids — hydration layer resists settlement during low-speed and stationary conditions.
    • Biocide-containing foul-release — adds low-level biocide for the stationary periods that dominate the tanker profile.

    Technical detail by coating type

    Self-polishing copolymers (SPC)

    SPC coatings release biocide through flow-driven hydrolysis; at low speeds and during idle periods polishing slows and release may fall short of warm anchorage fouling pressure. Specify against the actual speed profile, not nominal service speed. Governed by the IMO Antifouling Systems Convention (in force January 2008 after the tributyltin ban) (Dafforn et al., 2011) and the EU Biocidal Products Regulation.

    Controlled depletion polymers (CDP)

    CDP coatings deplete passively and are less speed-dependent than SPC, a reasonable fit for low tanker speeds. Lower activity in warm, high-pressure waters limits them as a sole solution for vessels idling long in tropical anchorages.

    Hybrid coatings (SPC/CDP blends)

    Hybrid coatings combine self-polishing in transit with passive depletion during slow steaming and stationary periods when conventional SPC underperforms, the most reliable response for vessels with significant floating storage or ballast waiting.

    Silicone foul-release

    Silicone foul-release depends on hydrodynamic shear and is effective across roughly 15 to 30 knots (US EPA, 2011), above the typical 12 to 15 knot tanker service speed. With no flow to self-clean during ballast waiting and floating storage, fouling establishes on hull and flat bottom; suited only to the few tankers on faster schedules with little idle time.

    Fluoropolymer foul-release

    Fluoropolymer systems share the same speed-dependent mechanism and the same limitation for low-speed tankers. Their durability may suit longer drydock cycles, but the operating-profile mismatch applies equally.

    Silicone-hydrogel hybrids

    Silicone-hydrogel systems add a hydration layer that resists settlement during low-speed and stationary conditions, addressing the central weakness of foul-release for tankers. Experience across the full range of tanker operating conditions is still accumulating.

    Biocide-containing foul-release

    Biocide-containing foul-release adds low-level biocide to maintain resistance during the stationary periods that dominate the tanker profile, a pragmatic fix for the gap that makes conventional foul-release a poor fit.


    "Tankers spend so much of their life slow steaming or sitting stationary in warm water that coating choice, niche-area protection, and proactive grooming have to be planned around idle time, not nominal service speed."

    Cathelco · Evac Group editorial
  • In-water cleaning, grooming, and drydock

    Tankers call at a defined set of terminals and idle at nearby anchorages, where in-water cleaning access varies: in GloFouling’s 2022 review of 138 biofouling provisions, 14 per cent did not allow in-water cleaning at all, 37 per cent required prior permission, and 28 per cent required or recommended debris capture.

    In-water cleaning is 35–65% less expensive than drydocking (US EPA, 2011), and the stationary periods that drive tanker fouling are also windows for scheduled grooming.

    • Proactive grooming — particularly well matched to the tanker profile; ballast-waiting and floating-storage periods are grooming windows.
    • Brush-based hull-crawling — suits the extensive flat bottom and vertical sides; tankers are strong candidates for efficient robotic coverage.
    • Cavitation waterjet — 50–250 m²/h coverage; effective on harder calcareous macrofouling.
    • High-pressure waterjet — effective on established fouling; risk of coating removal where paint is already breaking down.
    • Drydock cleaning — five-year class survey cycle with intermediate dockings; full hull preparation and coating renewal.

    Technical detail by cleaning method

    Proactive grooming

    Proactive grooming suits tankers because the stationary periods that drive fouling risk are also windows for scheduled intervention; in a 54-month Florida Institute of Technology trial it maintained a fouling rating of zero with no non-indigenous species on groomed surfaces. ISO 20679, the first international standard for testing in-water cleaning systems, was published in early 2025.

    Brush-based hull-crawling

    Brush-based hull-crawlers suit the tanker's extensive flat bottom and vertical sides, with large uninterrupted areas and limited niche complexity. Divers or ROVs cover sea chests, propeller, and rudder.

    Cavitation waterjet

    Cavitation systems cover 50–250 m²/hour (Kim et al., 2024) and remove harder calcareous fouling established during long stationary periods. Check coating integrity first on paint nearing the end of a drydock cycle; degraded coatings may not withstand the energy.

    High-pressure waterjet

    High-pressure waterjet removes established macrofouling but risks stripping coating at paint-breakdown sites. Document pre- and post-clean condition to support compliance at biosecurity-sensitive ports.

    Drydock cleaning

    In a 2018 Journal of Cleaner Production study of eight identical Aframax tankers, periodic hull cleaning cut daily fuel use 11 per cent on average, underwater cleaning saving ~9 per cent and drydocking ~17 per cent. Drydock wastewater has measured 9,110 µg/L copper and 22,600 µg/L zinc (Kim et al., 2024), driving debris-capture requirements. Full technical detail in our guide to biofouling management practices for commercial vessels.

  • Performance, documentation, and condition monitoring

    Tankers run steady speeds on defined routes, which supports meaningful normalisation of hull and propeller performance data. Monitor propeller fouling separately, given the non-linear sensitivity of propeller efficiency to early-stage fouling.

    • Biofouling record book — log ballast-waiting and floating-storage periods, water temperature, MGPS downtime; framework defined in MEPC.378(80).
    • Biofouling management plan (BFMP) — inspection and cleaning triggers tied to stationary duration; required by California rules.
    • Hull and propeller performance monitoring — ISO 19030 KPIs; directly feed CII calculations.
    • AI, machine learning, and in-situ sensing — emerging tools including CNNs, Gaussian splatting, and biosensors.

    Technical detail by monitoring practice

    Biofouling record book

    The MEPC.378(80) record book framework applies to tankers. Log each ballast-waiting and floating-storage period with anchorage name, duration, water temperature, and MGPS status; floating storage, which can hold a vessel in warm water for months, is the highest-risk exposure. These records evidence arrival compliance at New Zealand, Australian, and California ports.

    Biofouling management plan (BFMP)

    The BFMP structure is defined in MEPC.378(80); a tanker plan should treat ballast waiting and floating storage as elevated-risk periods, with cleaning triggers tied to stationary duration. California requires the BFMP to cover the hull and enumerated niche areas; its 45-day extended residency provision, which adds niche-area obligations, is routinely exceeded in floating storage.

    Hull and propeller performance monitoring (ISO 19030)

    ISO 19030 KPIs are the proven framework for hull and propeller condition tracking, and the steady-speed tanker pattern allows meaningful normalisation of fuel and CII impact. CII ratings are directly influenced by hull condition, a regulatory as well as commercial incentive to monitor.

Regulations

Compliance framework

IMO biofouling guidelines (MEPC.378(80)), New Zealand CRMS, Australian biosecurity requirements, US EPA Vessel General Permit and California State Lands Commission rules, and Brazil's NORMAM-401/DPC.

Between 56% and 70% of established coastal non-indigenous species are attributed to hull biofouling transport, according to the 2024 GESAMP Working Group 44 report, driving increasingly prescriptive mandatory frameworks where tankers call.

IMO Biofouling Guidelines

2023 guidelines (MEPC.378(80)) for managing ships' biofouling, with a 0 to 4 fouling rating scale and risk parameters including extended idle periods and MGPS downtime.

Voluntary today; at MEPC 83 (April 2025) IMO agreed to develop a legally binding framework for entry into force in 2029 at the earliest. The extended-idle parameter bears directly on floating storage.

IMO Biofouling Guidelines

New Zealand CRMS

Craft Risk Management Standard administered by MPI, one of the two most comprehensive mandatory frameworks in force globally. Build compliance into pre-arrival planning, especially after recent floating storage or extended anchorage.

New Zealand CRMS

Australian Requirements

Biosecurity Act 2015 and Biofouling Management Regulations 2021 (in force 15 June 2022). Comply via a BFMP and record book aligned to IMO guidance, cleaning all biofouling within 30 days before arrival, or a pre-approved alternative method.

Australian requirements

US EPA & California

EPA Vessel General Permit hull husbandry requirements, plus California SLC rules for vessels of 300 GRT or more able to carry ballast water: vessel-specific BFMP, annual record book, Annual Vessel Reporting Form 24 h before first California arrival, and management of seven enumerated niche areas.

The 45-day extended residency provision applies to tankers in floating storage off California.

US EPA VGP

California Article 4.8

Brazil NORMAM-401/DPC

Ordinance DPC/DGN/MB No. 180/25 (June 2025), full enforcement from 10 June 2026; applies to vessels >24 m in Brazilian jurisdictional waters.

BFMP and record book aligned to MEPC.378(80); arrival at IMO fouling rating 1 or below; extra requirements when transiting between Brazil's three marine biogeographic regions. Brazil is a significant crude exporter.

Brazil NORMAM-401/DPC

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