Lignocellulosic Esterification via Two-Zone Acid Anhydride Vapor Treatment

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Solution Overview

Problem

Existing methods for preparing esterified lignocellulosic materials face challenges such as inefficient and uncontrolled esterification reactions, excessive particle size reduction, unpleasant odors, and high costs, making them unsuitable for large-scale commercial production.

Innovation Solution

A process involving a two-zone system where lignocellulosic materials are treated with acid anhydride vapors at controlled temperatures and pressures, followed by steam stripping to remove excess agents and by-products, optimizing the access of modification agents to reactive hydroxyl groups and improving the degree of modification.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If lignocellulosic material is treated with acid anhydride vapors in a two-zone system at controlled temperatures and pressures, then the degree of modification is improved and access to reactive sites is enhanced, but the process complexity and equipment requirements increase

Engineering Contradiction:
Improvedegree of modificationVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The treatment process is divided into two distinct zones: a first zone for initial modification and a second zone for further treatment. This segmentation allows each zone to operate under optimized conditions for its specific function, improving the overall degree of modification while maintaining manageable process complexity through modular design

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent employs controlled temperature and pressure parameters in the two-zone system to optimize the esterification reaction. By carefully adjusting these parameters, the process achieves high modification degrees without requiring excessive complexity in equipment design

Inventive Principle:
Principle #35Parameter changes

2Object-generated harmful factors

If steam stripping is used to remove excess modification agents and by-products, then odor problems and particle size issues are reduced, but energy consumption increases

Engineering Contradiction:
ImproveodorVSAvoidenergy consumption
Core Design Contradiction:
Object-generated harmful factorsVSUse of energy by moving object

Solution Approach 1:

The steam stripping process converts the harmful odors and excess chemicals into removable by-products. The steam facilitates the removal of unwanted substances while the energy input is justified by the elimination of harmful factors and improvement of product quality

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

Solution Approach 2:

The patent utilizes phase transition of water from liquid to vapor during steam stripping. This phase change enables efficient removal of excess modification agents and by-products from the lignocellulosic material, reducing odors and improving particle characteristics while managing energy consumption through the natural heat of vaporization

Inventive Principle:
Principle #36Phase transitions

3Manufacturing precision

If acid anhydride vapors are used to modify lignocellulosic materials, then the access to reactive hydroxyl groups is improved, but the risk of uncontrolled esterification reactions increases

Engineering Contradiction:
Improveaccess to reactive sitesVSAvoidreaction control
Core Design Contradiction:
Manufacturing precisionVSReliability

Solution Approach 1:

The two-zone system incorporates controlled conditions that provide feedback on reaction progress. By monitoring temperature, pressure, and residence time in each zone, the process ensures complete esterification while preventing uncontrolled reactions, achieving both high modification degrees and reliable reaction control

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The first zone performs preliminary modification under controlled conditions before the material enters the second zone. This preliminary action prepares the material for further treatment while maintaining reaction control, preventing uncontrolled esterification by staged processing

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

This approach results in a higher degree of modification with improved access of acid anhydrides to reactive sites, reducing particle size issues and odor problems, while being more cost-effective and suitable for industrial-scale production.

Implementation Method 1

The hydroxyl groups are reactive functional groups, which are readily chemically modified with such chemical species, which are known to react with hydroxyl groups. Thus, the hydroxyl groups are readily esterified with mono- or dicarboxylic anhydrides

Methodology Applied
Scientific EffectEsterification: Chemical Bonding

Implementation Method 2

stripping the modified lignocellulosic material to remove excess of modification agent and by-products

Methodology Applied
Scientific EffectEvaporation: Evaporation

Data Source

PatentUS9091022B2Process and apparatus for modification of lignocellulosic materials and products of modified lignocellulosic materials obtained by the process
Publication Date: 2015.07.28 DANISH PLANT FIBER TECH HLDG
  • US9091022B2 patent drawing
  • US9091022B2 patent drawing
  • US9091022B2 patent drawing

AI summary

A process and apparatus for the preparation of a modified lignocellulosic material bytreating the lignocellulosic material in a first activator zone having an atmosphere of one or more acid anhydrides in vapour form in a gas at a gauge pressure of 0-50 kPag and a temperature of 100-160° C., and thentreating the lignocellulosic material in a second reactor zone having an atmosphere of a gas at a gauge pressure of 0-50 kPag and a temperature of 120-190° C., thereafterstripping the lignocellulosic material with steam or water in a stripper zone, andoptionally further processing.The process is more efficient as compared with the prior art processes by providing a better access of the acid anhydrides to the sites of the reactive lignocellulosic hydroxyl groups (—OH), which are located on the internal surfaces of pores and capillary channels in the lignocellulose. Furthermore, the apparatus is relatively simple. This makes the inventive process and apparatus suitable for a cost-efficient preparation of modified lignocellulosic fibre in industrial scale.