Pre-hydrolysis Reactor Extraction Screens for Pseudolignin Removal

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Solution Overview

Problem

The buildup of pseudolignins and lignin fragments on wood chips and equipment during pre-hydrolysis and Kraft cooking processes interferes with the operation of reactors, blocking pores and disrupting the flow of cellulosic feed material, particularly in acidic environments.

Innovation Solution

A pulp cooking system with multiple extraction points and a pre-hydrolysis vessel that includes a center pipe for discharging wash liquids and extraction screens to remove pseudolignins, along with pH management using hydrolysate and bisulfite compounds to prevent deposition, ensuring controlled flow and efficient processing.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If pre-hydrolysis is performed in an acidic environment to dissolve pulp, then the hydrolysis reaction is enhanced, but pseudolignins and lignin fragments build up on wood chips and equipment surfaces

Engineering Contradiction:
Improvehydrolysis reaction rateVSAvoidpseudolignin and lignin fragment buildup
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent introduces a separate extraction zone that physically removes pseudolignins and lignin fragments from the hydrolyzed cellulosic fiber feed material as they are formed. This extraction system continuously extracts the harmful substances from the acidic hydrolysis environment, preventing their accumulation on chips and equipment while allowing the hydrolysis reaction to proceed efficiently.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent uses an intermediary extraction zone that acts as a buffer between the hydrolysis reaction zone and the downstream equipment. This intermediary zone captures and removes pseudolignins and lignin fragments before they can deposit on equipment surfaces, while still allowing the acidic hydrolysis environment to be maintained in the reaction zone for optimal productivity.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If pseudolignins and lignin fragments are allowed to form during hydrolysis, then pulp dissolution is achieved, but pores in wood chips are blocked preventing alkali penetration

Engineering Contradiction:
Improvepulp dissolution efficiencyVSAvoidalkali penetration to chips
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The extraction zone continuously removes pseudolignins and lignin fragments from the hydrolyzed material, preventing these substances from blocking the pores in wood chips. This ensures that when the material transitions to the Kraft cooking stage, the alkali can penetrate the chip pores effectively, maintaining reliable processing while still achieving thorough pulp dissolution during hydrolysis.

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If pseudolignins and dissolved lignins build up on equipment surfaces, then the hydrolysis process continues, but flow passages are blocked and equipment operation is interfered with

Engineering Contradiction:
Improvehydrolysis process continuityVSAvoidequipment flow passage operation
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The patent introduces a dedicated extraction zone that continuously removes pseudolignins and dissolved lignins from the hydrolysis stream before they can deposit on equipment flow passages. This extraction system maintains equipment operability by preventing buildup, while allowing the hydrolysis process to continue uninterrupted in the reaction zone.

Inventive Principle:
Principle #2Taking out (Extraction)

4Object-generated harmful factors

If multiple extraction points are added to remove pseudolignins, then buildup is reduced, but device complexity increases

Engineering Contradiction:
Improvepseudolignin depositionVSAvoidextraction system structure
Core Design Contradiction:
Object-generated harmful factorsVSDevice complexity

Solution Approach 1:

The patent divides the extraction function into multiple discrete extraction points distributed along the length of the reactor. Each extraction point handles a specific zone, allowing pseudolignins to be removed at multiple locations where they are most likely to form. This segmented approach reduces deposition effectively while keeping each individual extraction point relatively simple in design.

Inventive Principle:
Principle #1Segmentation

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 system effectively reduces the buildup of pseudolignins and lignin fragments, maintaining uniform pH levels and enhancing the flow of feed material through reactors, thereby improving the efficiency and operation of pre-hydrolysis and Kraft cooking processes.

Implementation Method 1

Hydrolysis of comminuted cellulosic fiber feed material, such as wood chips, before Kraft cooking

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Implementation Method 2

The pseudolignins and lignin fragments tend to build up on the surfaces of chips and equipment most when in an acidic environments

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentEP2678470B1Method and apparatus to produce pulp using pre- hydrolysis and kraft cooking
Publication Date: 2020.01.01 ANDRITZ INC
  • EP2678470B1 patent drawingFigure 1
  • EP2678470B1 patent drawingFigure 2

AI summary

A pulp cooking system including: a cellulosic material feed system, a pre-hydrolysis reactor vessel and a Kraft cooking reactor vessel. The feed material system includes a steaming chip bin (10) and a high pressure transfer device (12). The pre-hydrolysis reactor vessel maintains the feed material in a mildly acidic condition and allows hydrolysate to be extracted through screens (60) below a hydrolysis zone (56) in the vessel. A wash zone (66) is below the screens and allows wash liquid to flow through the feed material in a cross-current direction. The wash liquid and hydrolysate removed from the feed material is extracted from the wash zone through the screens (60). The feed material is maintained in a mildly acidic condition through the pre-hydrolysis reactor vessel until the material enters the Kraft cooking vessel where the feed material is treated with alkaline cooking liquors.