Biomass Pretreatment Reactor Venting for Stable Pressure Control

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Solution Overview

Problem

Pretreatment processes for lignocellulosic biomass in reactors face issues with unstable reaction conditions due to gas accumulation, leading to inefficient yields and deposits on reactor walls, particularly during high-temperature and high-pressure treatments like steam explosion.

Innovation Solution

A pretreatment arrangement with a reactor vessel equipped with a gas valve for controlled gas removal based on temperature and pressure measurements, using adjustable gas flow control to maintain stable conditions and prevent deposits.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high temperature and high pressure treatments are applied for pretreatment, then the pretreatment efficiency is improved, but gas accumulation occurs in the reactor leading to unstable reaction conditions

Engineering Contradiction:
Improvepretreatment efficiencyVSAvoidreaction condition stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent implements a feedback control system where gas pressure sensors continuously monitor the reactor interior pressure and automatically adjust the gas vent valve opening degree in response to pressure changes. This closed-loop feedback mechanism maintains stable reaction conditions while allowing efficient pretreatment by dynamically balancing gas removal with process requirements.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system transitions from static pressure management to dynamic control by continuously adjusting the gas vent valve opening based on real-time pressure measurements. The controller modulates the valve position dynamically throughout the pretreatment process, enabling the system to adapt to changing gas generation rates and maintain optimal reaction conditions.

Inventive Principle:
Principle #15Dynamics

2Reliability

If gas venting is increased to remove accumulated gas, then reaction condition stability is improved, but sugar yield decreases due to loss of volatile compounds

Engineering Contradiction:
Improvereaction condition stabilityVSAvoidsugar yield
Core Design Contradiction:
ReliabilityVSLoss of substance

Solution Approach 1:

The system optimizes the balance between gas removal and volatile retention by dynamically adjusting the gas vent valve opening degree as a controllable parameter. The controller modulates this parameter based on pressure feedback to achieve the optimal trade-off point where gas accumulation is prevented while minimizing loss of valuable volatile compounds that contribute to sugar yield.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The feedback control system enables precise regulation of gas venting by continuously monitoring reactor pressure and adjusting valve opening accordingly. This prevents both excessive gas accumulation and excessive volatile loss, maintaining the optimal balance for maximizing sugar yield while ensuring reaction stability.

Inventive Principle:
Principle #23Feedback

3Productivity

If steam and gaseous catalysts are added to catalyze the reaction, then the pretreatment process is enhanced, but excess gas accumulates in the reactor

Engineering Contradiction:
Improvepretreatment process enhancementVSAvoidgas accumulation
Core Design Contradiction:
ProductivityVSQuantity of substance

Solution Approach 1:

The feedback control system automatically compensates for gas accumulation from steam and gaseous catalysts by continuously monitoring reactor pressure and adjusting the gas vent valve opening. This enables the system to maintain the enhanced pretreatment process while dynamically balancing the removal of excess gas generated by catalyst addition.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system dynamically adjusts gas removal rates to match the gas generation rates from steam and catalyst addition. The controller modulates the valve opening in real-time, enabling the process to benefit from catalyst-enhanced pretreatment while preventing gas accumulation that would destabilize reaction conditions.

Inventive Principle:
Principle #15Dynamics

4Device complexity

If gas accumulation is allowed to occur, then equipment complexity is reduced, but deposits form on reactor walls and process efficiency decreases

Engineering Contradiction:
Improveequipment simplicityVSAvoidprocess efficiency
Core Design Contradiction:
Device complexityVSProductivity

Solution Approach 1:

The feedback control system provides automatic gas pressure management through the gas vent valve, eliminating the need for complex manual intervention or additional sophisticated gas management equipment. This relatively simple feedback mechanism effectively prevents deposit formation and maintains high process efficiency.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system achieves self-regulating gas pressure control where the feedback mechanism automatically adjusts gas venting based on reactor conditions. This self-service capability prevents deposit formation and maintains process efficiency without requiring complex external control systems or frequent manual intervention.

Inventive Principle:
Principle #25Self-service

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 solution ensures stable pretreatment conditions, reducing deposits and enhancing efficiency by maintaining a controlled gas flow, thereby improving sugar yields and reactor performance.

Implementation Method 1

Some pretreatment methods, such as steam explosion, involves deliberately increasing the pressure and temperature within the reactor. Steam and gaseous catalysts, such as sulfur dioxide (SO2) or carbon dioxide (CO2) may be added to catalyze the reaction. The addition of steam and gaseous catalysts may result in an excess amount of gas accumulating in the reactor.

Methodology Applied
Scientific EffectPressure control: Pressure Increase

Implementation Method 2

measuring means arranged for measuring a number of process parameters of the pretreatment in the reactor vessel, which process parameters include at least a temperature parameter and a pressure parameter

Methodology Applied
Scientific EffectTemperature measurement: Temperature Gradient

Implementation Method 3

measuring means arranged for measuring a number of process parameters of the pretreatment in the reactor vessel, which process parameters include at least a temperature parameter and a pressure parameter

Methodology Applied
Scientific EffectPressure measurement: Pressure Increase

Implementation Method 4

gas flow control means configured to adjust the outflow of gas from the gas valve in response to the measured process parameters, whereby a controlled flow of gas out from the reactor vessel is achieved

Methodology Applied
Scientific EffectGas flow control: Pressure Gradient

Implementation Method 5

Steam and gaseous catalysts, such as sulfur dioxide (SO2) or carbon dioxide (CO2) may be added to catalyze the reaction

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 6

The polysaccharides can be hydrolyzed to sugars and converted to various fermentation products, e.g. bioalcohols, by means of fermenting microorganisms

Methodology Applied
Scientific EffectHydrolysis: Hydrolysis

Data Source

PatentUS12516473B2Arrangement and method for pretreatment of biomass
Publication Date: 2026.01.06 SEKAB E TECHNOLOGY AB
  • US12516473B2 patent drawing
  • US12516473B2 patent drawing
  • US12516473B2 patent drawing

AI summary

The present disclosure generally relates to a pretreatment arrangement (100) for pretreatment of lignocellulosic biomass comprising a reactor vessel (101) having an upstream inlet (102) for receiving biomass and a downstream outlet (103) for discharging biomass. The pretreatment arrangement (100) further comprises a gas valve (104) and gas flow control means (106).