Non-affiliation notice: Independent company. No affiliation with President Donald J. Trump, the Trump family, the Trump Organization, the U.S. government, or the Venezuelan government.

TRUMP OILIndependent Energy Infrastructure
Lake Maracaibo shoreline in Venezuela at duskLake Maracaibo, Zulia

Conceptual Plan

A Phased, Modular Refinery Development Concept

This is a planning framework, not a project. No site has been selected, no engineering has been commissioned, no permit has been sought and no financing has been raised. Each phase is gated by the successful, documented completion of the phase before it.

Abstract dark illustration of modular refinery skid units and storage tanks

Sequence

Six proposed phases

  1. Phase 01

    Feasibility & Compliance

    • Sanctions and OFAC authorization pathway analysis with U.S. counsel
    • Venezuelan legal, regulatory and licensing pathway review
    • Anti-corruption programme design and counterparty screening framework
    • Preliminary assay collection and technical screening
    • Order-of-magnitude economics with explicit uncertainty ranges
  2. Phase 02

    Site, FEED & Environmental / Social Studies

    • Site identification, geotechnical, hydrology and marine access review
    • Front-end engineering design against measured assay data
    • Environmental and social impact assessment by independent consultants
    • Community consultation and grievance mechanism design
    • Permit register and consent-condition mapping
  3. Phase 03

    Financing, EPC Selection & Enabling Works

    • Definitive financing structure, insurance and financial assurance
    • Competitive EPC tender with technical and integrity due diligence
    • Binding agreements — no reliance on letters of intent
    • Enabling works: access, power, water, drainage, laydown
    • Independent engineer appointment and stage-gate governance
  4. Phase 04

    Modular Construction, Utilities, Storage & Logistics

    • Fabrication of modular process skids off site where practical
    • Utilities: power, steam, cooling, instrument air, nitrogen
    • Crude, intermediate and product tankage with containment
    • Marine, pipeline and road logistics interfaces
    • HSE management system and construction assurance
  5. Phase 05

    Commissioning & Start-Up

    • Pre-commissioning, mechanical completion and system handover
    • Operator training, competency assurance and simulator work
    • Emissions, effluent and safety-system performance verification
    • Staged introduction of feedstock under permit conditions
    • Independent performance testing before any sustained operation
  6. Phase 06

    Staged Expansion

    • Expansion only after demonstrated safe, compliant operation
    • Re-assessment of assays, markets, permits and financing
    • Incremental modular additions rather than single-step scale-up
    • Continued environmental monitoring and community engagement

High-Level Units

Process blocks under conceptual consideration

These are illustrative process blocks common to heavy-crude processing. Inclusion here is not a design decision, a procurement commitment or a capacity statement.

Desalting

Removal of salts, water and solids to protect downstream metallurgy and catalysts.

Atmospheric & Vacuum Distillation

Primary separation into fractions, with vacuum service handling the heavy bottoms characteristic of extra-heavy crude.

Residue Conversion / Delayed Coking

Conversion of heavy residue into lighter products and petroleum coke; selection depends on residue yield and market access.

Hydrotreating / Hydrocracking

Sulfur, nitrogen and metals removal, plus conversion severity matched to product specifications.

Hydrogen Production

Hydrogen supply sized to hydroprocessing demand, with its own utility and emissions profile.

Sulfur Recovery

Recovery and handling of sulfur removed during hydroprocessing, with tail-gas treatment.

Utilities

Power, steam, cooling water, instrument air, nitrogen, flare and relief systems.

Wastewater & Emissions Control

Effluent treatment, stormwater management, vapour recovery, monitoring and reporting.

Configuration is not fixed. Final configuration, capacity, technology licensors and phasing would depend on measured crude assays, site conditions, permit conditions, project economics, utility availability and independent engineering review. Any of these could change the concept fundamentally or render it unviable.

Disclosures

Development-stage conditions apply