High-Acid-Value Biological Grease Fuel Preparation via Segmented Deoxidization

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Solution Overview

Problem

Existing technologies for processing high-acid-value biological grease face challenges such as poor catalyst stability, high hydrogen consumption, corrosion issues, and limitations in processing vegetable oils and animal fats with high oxygen content.

Innovation Solution

A method and system that involves thermal cracking and deoxidization, followed by vacuum distillation, catalytic cracking deoxidization, and catalytic hydrodeoxygenation to process high-acid-value biological grease, reducing acid values and oxygen content while minimizing hydrogen consumption.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If direct hydrogenation technology is used to process high-acid-value biological grease, then fuel production is achieved, but catalyst stability deteriorates and hydrogen consumption increases

Engineering Contradiction:
Improvefuel productionVSAvoidcatalyst stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent divides the fuel production process into multiple stages: first stage hydrogenation to reduce acid value to below 0.5%, followed by a second stage hydrogenation to achieve final fuel specifications. This segmentation allows each catalyst to operate within optimal conditions, preventing rapid deactivation while maintaining high productivity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The first stage hydrogenation serves as a preliminary action that removes the majority of free fatty acids before the second stage processing. This preliminary reduction of acid content protects the second stage catalyst from severe corrosion and deactivation, thereby improving overall catalyst stability and reducing hydrogen consumption.

Inventive Principle:
Principle #10Preliminary action

2Productivity

If direct hydrogenation technology is used to process high-acid-value biological grease, then fuel production is achieved, but device corrosion worsens

Engineering Contradiction:
Improvefuel productionVSAvoiddevice corrosion
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The two-stage hydrogenation process segments the corrosion-prone environment into two separate reaction zones. The first stage handles the high-acid feedstock in a dedicated reactor, protecting the second stage equipment from severe corrosion. This segmentation enables fuel production while significantly reducing device corrosion issues.

Inventive Principle:
Principle #1Segmentation

3Quantity of substance

If catalytic cracking deoxidization is used to process heavy feedstock, then deoxidization is achieved, but aggregation and coking problems worsen

Engineering Contradiction:
Improveoxygen removalVSAvoidaggregation and coking
Core Design Contradiction:
Quantity of substanceVSObject-generated harmful factors

Solution Approach 1:

The patent employs specific parameter control in the catalytic cracking deoxidization process, including optimizing temperature (300-450°C), pressure, and catalyst composition to achieve effective oxygen removal while suppressing aggregation and coking reactions. These parameter changes enable deoxidization without severe harmful side effects.

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

The method achieves a premium biomass fuel suitable for diesel blending, comparable to fuels from crude oil refining, with improved catalyst stability, reduced hydrogen consumption, and avoidance of corrosion issues.

Implementation Method 1

subjecting the high-acid-value biological grease to thermal cracking and deoxidization reaction under heating conditions

Methodology Applied
Scientific EffectThermal cracking: Pyrolysis

Implementation Method 2

thermal cracking and deoxidization reaction

Methodology Applied
Scientific EffectDeoxidization: Reduction

Implementation Method 3

subjecting the product of step (a) to vacuum distillation to separate water, a high-acid-value fraction, a low-acid-value fraction and a heavy component

Methodology Applied
Scientific EffectVacuum distillation: Vacuum Distillation

Implementation Method 4

catalytically cracking and deoxygenating the high-acid-value fraction obtained in the step (b) to separate water and non-condensable gas in the presence of a catalytic cracking deoxidization catalyst

Methodology Applied
Scientific EffectCatalytic cracking: Catalysis

Implementation Method 5

catalytically cracking and deoxygenating

Methodology Applied
Scientific EffectDeoxygenation: Reduction

Implementation Method 6

catalytically hydrodeoxygenating a mixture of the product obtained in the step (c) and the low-acid-value fraction obtained in the step (b) with hydrogen in the presence of a hydrodeoxygenation catalyst

Methodology Applied
Scientific EffectHydrodeoxygenation: Hydrogenation

Data Source

PatentUS12286599B2Method and system for preparing fuel by using high acid value biological oil and fat
Publication Date: 2025.04.29 ECO BIO-GREASE TECHNOLOGY COMPANY LIMITED
  • US12286599B2 patent drawing

AI summary

The present invention provides a method and a system for preparing fuel using high-acid-value biological grease, which can be processed through triple deoxidization steps, i.e., thermal cracking deoxygenation-catalytic cracking deoxygenation-catalytic hydrodeoxygenation. By use of the method and system of the invention, the raw material of the high-acid-value biological grease can be gradually deoxidized to reduce the acid value and thereby prepare a clean fuel with equivalent fuel components as those obtained from crude oil refining or direct hydrodeoxygenation for biological grease.