Renewable Fuel Blending via Isomerization and Selective Cracking

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Solution Overview

Problem

The increasing demand for aviation fuel and the need for sustainable alternatives to petroleum-based fuels have led to a challenge in developing efficient processes for producing fuels from renewable sources, particularly from triglycerides and free fatty acids in plant and animal oils, and biomass-derived pyrolysis oil, while meeting specific fuel specifications without requiring significant upgrades to existing engines.

Innovation Solution

A process that involves hydrogenating, deoxygenating, isomerizing, and selectively cracking triglycerides and free fatty acids from plant and animal oils to produce a paraffin-rich component, and deoxygenating biomass-derived pyrolysis oil to produce a cyclic-rich component, which are then blended to create a fuel meeting aviation, diesel, or gasoline specifications, with optional reforming steps to generate hydrogen and recycle hydrocarbons to optimize reaction conditions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Ease of manufacture

If simple deoxygenation of renewable feedstock is employed, then the process is simple, but the product fails to meet aviation fuel specifications requiring specific chain lengths and molecular structure

Engineering Contradiction:
Improveprocess simplicityVSAvoidfuel specification compliance
Core Design Contradiction:
Ease of manufactureVSManufacturing precision

Solution Approach 1:

The patent divides the fuel production process into multiple sequential steps: deoxygenation, isomerization, and selective cracking. Each step transforms the feedstock progressively, with deoxygenation removing oxygen, isomerization creating branched structures for better cold flow, and selective cracking optimizing chain lengths for aviation fuel specifications. This segmented approach resolves the contradiction by achieving precise fuel specifications through controlled multi-stage processing rather than simple single-step deoxygenation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent employs parameter changes by adjusting reaction conditions at each processing stage. Deoxygenation occurs under specific catalytic conditions, followed by isomerization at controlled temperatures and pressures, then selective cracking with optimized residence times and catalyst selections. These parameter changes enable precise control over molecular structure and chain length distribution, ensuring aviation fuel compliance while maintaining reasonable process complexity.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If non-selective cracking is used to reduce paraffin chain length, then light products are minimized, but selectivity to aviation fuel range paraffins is reduced

Engineering Contradiction:
Improvefuel yieldVSAvoidselectivity to aviation fuel range
Core Design Contradiction:
ProductivityVSManufacturing precision

Solution Approach 1:

The patent introduces an isomerization step as an intermediary between deoxygenation and selective cracking. This intermediate transformation converts linear paraffins into branched isomers, which then undergo selective cracking to produce aviation fuel-range paraffins with higher selectivity. The isomerization intermediary enables the subsequent cracking step to be more selective, resolving the contradiction between productivity and manufacturing precision by optimizing the molecular structure before the final cracking stage.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Quantity of substance

If high operating pressure is applied to increase hydrogen solubility in deoxygenation, then hydrogen availability improves, but equipment complexity and operating costs increase

Engineering Contradiction:
Improvehydrogen solubilityVSAvoidoperating pressure requirements
Core Design Contradiction:
Quantity of substanceVSDevice complexity

Solution Approach 1:

The patent optimizes the deoxygenation step by carefully selecting and adjusting parameters including catalyst composition, temperature, and moderate pressure conditions. By using effective catalysts and optimizing reaction conditions, the process achieves sufficient hydrogen solubility and reaction efficiency without requiring excessively high pressures. This parameter optimization resolves the contradiction by finding the optimal balance point where adequate hydrogen availability is achieved at reasonable operating pressures, reducing equipment complexity and operating costs.

Inventive Principle:
Principle #35Parameter changes

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

This process effectively produces blended fuels entirely from renewable sources, meeting stringent fuel specifications without the need for engine upgrades, reducing dependence on petroleum and enhancing the economic viability by minimizing hydrogen requirements and operating pressures.

Implementation Method 1

The process involves hydrogenation, decarboxylation, decarbonylation, and/or hydrodeoxygenation, hydroisomerization, and selective cracking in two or more steps

Methodology Applied
Scientific EffectHydrogenation: Hydrogenation

Implementation Method 2

deoxygenating biomass-derived pyrolysis oil to produce a cyclic-rich component

Methodology Applied
Scientific EffectDeoxygenation:

Implementation Method 3

isomerizing the n-paraffins to improve cold-flow properties

Methodology Applied
Scientific EffectIsomerization:

Implementation Method 4

The selective cracking step optimally provides one cracking event per molecule

Methodology Applied
Scientific EffectSelective cracking:

Data Source

PatentUS8324438B2Production of blended gasoline and blended aviation fuel from renewable feedstocks
Publication Date: 2012.12.04 UOP LLC
  • US8324438B2 patent drawing
  • US8324438B2 patent drawing
  • US8324438B2 patent drawing

AI summary

A process for producing at least one blended fuel from a paraffin rich component and a cyclic rich component, where each of the components are generated from a renewable feedstock, is presented. The paraffin rich component is generated from glycerides and free fatty acids in feedstocks such as plant and animal oils. The cyclic rich component is generated from biomass derived pyrolysis oil. The source of the animal or plant oil and the biomass may be the same renewable source.