Heavy Crude Upgrading via Ni-Mo Catalytic Hydrocracking

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Solution Overview

Problem

Current technologies face limitations in efficiently improving the physical and chemical properties of heavy and extra-heavy crude oils, such as high viscosity and sulfur content, which hinders their extraction and refining, particularly due to risks associated with combustion methods and limited applicability of existing processes.

Innovation Solution

A two-stage homogeneous catalytic process using a liquid phase ionic Ni—Mo catalyst is injected into the crude oil, controlling temperature, pressure, and time to transform heavy crude oils into lighter ones by reducing viscosity, increasing API gravity, and altering the SARA composition, thereby reducing sulfur and nitrogen content.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If combustion methods (steam injection, air injection, THAI) are used to improve heavy crude extraction, then recovery factor increases, but safety risks (explosion, fire) and operational complexity increase

Engineering Contradiction:
Improverecovery factorVSAvoidsafety risks
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent replaces thermal combustion methods with a chemical catalytic system. A nickel-molybdenum catalyst system is used to facilitate hydrocracking reactions that break down heavy crude components at lower temperatures, eliminating the need for high-temperature combustion and associated safety risks while maintaining improved recovery rates

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The invention changes the fundamental operating parameters from high-temperature combustion (thermal energy) to moderate-temperature catalytic reactions (chemical energy). The catalyst enables the process to proceed at temperatures below 400°C compared to combustion methods requiring temperatures above 700°C, thereby reducing safety hazards

Inventive Principle:
Principle #35Parameter changes

2Ease of operation

If steam injection or SAGD is used to reduce viscosity, then fluidity improves, but energy consumption and operational complexity increase

Engineering Contradiction:
ImprovefluidityVSAvoidenergy consumption
Core Design Contradiction:
Ease of operationVSUse of energy by moving object

Solution Approach 1:

The patent replaces thermal energy input (steam injection) with chemical catalysis. The nickel-molybdenum catalyst system facilitates bond breaking and reforming reactions that reduce viscosity through chemical transformation rather than thermal heating, significantly lowering energy requirements

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The invention changes the mechanism of viscosity reduction from thermal softening to chemical transformation. The catalyst enables hydrocracking reactions that break large hydrocarbon molecules into smaller, less viscous molecules, achieving fluidity improvement at lower energy input

Inventive Principle:
Principle #35Parameter changes

3Productivity

If heavy crude is extracted and refined conventionally, then production is maintained, but sulfur and metals content remain high, reducing commercial value

Engineering Contradiction:
ImproveproductionVSAvoidsulfur and metals content
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent replaces conventional physical separation and mechanical refining with chemical catalysis. The nickel-molybdenum catalyst system promotes hydrocracking and hydrodesulfurization reactions that chemically remove sulfur and metals from the crude, transforming them into removable byproducts while maintaining production rates

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

Solution Approach 2:

The invention introduces a catalyst system as an intermediary substance that facilitates the removal of harmful components. The nickel-molybdenum catalyst acts as a mediator that enables sulfur and metals to be transformed and separated from the crude oil through chemical reactions, rather than requiring complex physical separation processes

Inventive Principle:
Principle #24Intermediary (Mediator)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

The process effectively increases the yield of lighter, higher-value distillates with improved selectivity towards gasoline, diesel, and fuel oils, while minimizing coke formation and enhancing commercial value, with a high liquid yield exceeding 95% and sulfur removal.

Implementation Method 1

A process has been found for improving the properties of heavy and extra-heavy crude oils 'in-situ' by means of a catalytic reaction with a liquid phase ionic composition of a Ni—Mo catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

which intends to promote hydrocracking and hydrogenation type reactions

Methodology Applied
Scientific EffectHydrocracking:

Implementation Method 3

which intends to promote hydrocracking and hydrogenation type reactions

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 4

likewise, these procedures reduce the content of sulfur and nitrogen associated to those crudes

Methodology Applied
Scientific EffectHydrodesulfurization:

Implementation Method 5

by means of a catalytic reaction with a liquid phase ionic composition of a Ni—Mo catalyst

Methodology Applied
Scientific EffectChemical reaction: Reaction (physics)

Data Source

PatentUS9512373B2Procedure for the improvement of heavy and extra-heavy crudes
Publication Date: 2016.12.06 INST MEXICANO DEL GASOLINEEO
  • US9512373B2 patent drawing
  • US9512373B2 patent drawing

AI summary

The physical and chemical properties of heavy and extra-heavy crudes are improved by a procedure that uses a homogeneous type catalyst and involves the stages: 1. separation and removal of the water fraction that is contained in the hydrocarbons, 2. catalyst injection and activation of the reaction system, 3. elimination of gaseous hydrocarbons and recovery of the partial pressure of hydrogen at different times, 4. reaction and 5. recovery of distillated products.