Two-Stage Hydrodeoxygenation Process for Biomass Conversion

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Solution Overview

Problem

Existing biomass-to-biofuel conversion processes face inefficiencies in hydrodeoxygenation (HDO) due to high oxygen content in biomass, catalyst deactivation by metal salts and acids, and challenges in heat management, leading to low hydrocarbon yields and high CO+CO2 production.

Innovation Solution

A two-stage HDO process using a low-activity catalyst for initial cracking of triglycerides and a high-activity catalyst for subsequent hydrodeoxygenation, with separate stages to manage contaminants and reduce water partial pressure, achieving selective conversion and improved hydrocarbon yields.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional single-stage HDO process is used, then process simplicity is maintained, but HDO efficiency is low and hydrocarbon yields are reduced

Engineering Contradiction:
ImproveHDO efficiencyVSAvoidprocess complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The HDO process is divided into two distinct stages: first stage uses a non-noble metal catalyst (NiMo or CoMo) to perform initial hydrodeoxygenation, and second stage uses a noble metal catalyst (Pt, Pd, or Rh) to complete the reaction and maximize hydrocarbon yield. This segmentation allows each catalyst to be optimized for its specific function, resolving the contradiction between process simplicity and HDO efficiency.

Inventive Principle:
Principle #1Segmentation

2Productivity

If high metal chloride salt content feed is processed, then biomass utilization is improved, but catalyst deactivation occurs due to salt accumulation

Engineering Contradiction:
Improvebiomass utilizationVSAvoidcatalyst stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

A feed pretreatment step is implemented before the HDO process to remove metal chloride salts from the biomass feedstock. This preliminary action prevents salt accumulation that would otherwise deactivate the catalyst, allowing high biomass utilization to be achieved without compromising catalyst stability.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent introduces an intermediary pretreatment process that acts as a buffer between the high-salt biomass feed and the catalyst. This intermediary step removes harmful salts while preserving the biomass components needed for fuel production, resolving the contradiction between biomass utilization and catalyst stability.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If high temperature is used for exothermic HDO reaction, then reaction rate is improved, but heat management becomes difficult and side products increase

Engineering Contradiction:
Improvereaction rateVSAvoidheat management
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The exothermic HDO reaction is segmented into two stages with different temperature profiles. The first stage operates at moderate temperatures to control heat release, while the second stage optimizes temperature for maximum hydrocarbon yield. This segmentation allows the reaction rate to be maintained without excessive heat management problems.

Inventive Principle:
Principle #1Segmentation

4Temperature

If feed dilution is used to control reaction temperature, then heat management is improved, but reactor size and separation costs increase significantly

Engineering Contradiction:
Improvereaction temperature controlVSAvoidreactor size and separation costs
Core Design Contradiction:
TemperatureVSDevice complexity

Solution Approach 1:

Feed pretreatment is performed in advance to remove contaminants that would interfere with the HDO reaction. This preliminary action allows the reaction to proceed efficiently at optimized temperatures without requiring excessive dilution, thereby avoiding increased reactor size and separation costs while maintaining temperature control.

Inventive Principle:
Principle #10Preliminary action

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 two-stage process enhances HDO efficiency, reduces water partial pressure, prevents catalyst deactivation, and increases hydrocarbon yields, while minimizing CO+CO2 production and reactor size, thereby improving the overall biofuel production process.

Implementation Method 1

Removal of oxygen by catalytic reaction with hydrogen is referred to as hydrodeoxygenation (HDO). This reaction may be conducted with conventional fixed-bed bimetallic hydrotreating catalysts such as sulfided nickel-molybdenum (NiMo) or cobalt-molybdenum (CoMo)

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

the exothermic HDO reaction, which in turn reduces the heavy side products that are formed at high temperature

Methodology Applied
Scientific EffectExothermic reaction: Exothermic Reaction

Data Source

PatentUS8026401B2Hydrodeoxygenation process
Publication Date: 2011.09.27 REG SYNTHETIC FUELS LLC
  • US8026401B2 patent drawing
  • US8026401B2 patent drawing
  • US8026401B2 patent drawing

AI summary

A process for producing a hydrocarbon from biomass. A feed stream having free fatty acids, fatty acid esters or combinations thereof is provided. The feed stream is heated in the presence of a first catalyst to produce a partially hydrodeoxygenated stream. The partially hydrodeoxygenated stream is heated in the presence of a second catalyst to produce an effluent stream containing the hydrocarbon.