Sugar Beet Drying Preventing Enzymatic Degradation

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Solution Overview

Problem

Existing methods for drying sugar beet material often cause degradation, especially when dealing with unstabilized material, as they fail to prevent enzymatically catalyzed reactions with atmospheric oxygen or electromagnetic radiation.

Innovation Solution

A method involving the disintegration of sugar beet material into particles with a surface area of at least 2.0 cm², followed by immediate exposure to a controlled flow of drying gas at temperatures between 25°C to 160°C, and a flow rate of 5 m·s⁻¹ to 40 m·s⁻¹, to rapidly remove free water and prevent degradation reactions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If fluid drying is used on unstabilized sugar beet material, then drying efficiency is improved, but material degradation occurs

Engineering Contradiction:
Improvedrying efficiencyVSAvoidmaterial degradation
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The material is pre-stabilized by thermal inactivation of polyphenol oxidases at temperatures above 80°C before the fluid drying process. This preliminary action prevents enzymatic degradation during the subsequent high-efficiency fluid drying, allowing the use of aggressive drying conditions without quality loss.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The invention changes the temperature parameter during processing - using temperatures above 80°C for stabilization and then controlling the fluid drying temperature to achieve rapid water removal. This parameter change transforms the material state from vulnerable to resistant against degradation.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If thermal inactivation at temperatures above 80°C is applied, then polyphenol oxidase destruction is improved, but energy consumption increases

Engineering Contradiction:
Improveenzyme inactivationVSAvoidenergy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The thermal stabilization step is integrated continuously with the fluid drying process. The material flows continuously through the stabilization zone and then into the fluid drying zone, eliminating idle time and maximizing the efficiency of energy usage throughout the entire processing chain.

Inventive Principle:
Principle #20Continuity of useful 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 method effectively prevents the degradation of sugar beet material by rapidly removing free water and reducing the moisture content below 30% by weight, thereby maintaining the quality and stability of the material.

Implementation Method 1

converting water into water vapour

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 2

exposure to a flow of drying gas at a temperature of 25° C. to 160° C.

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 3

exposure to a flow of drying gas/gases at a temperature of 25° C. to 160° C. and at a flow rate of 5 m·s⁻¹ to 40 m·s⁻¹

Methodology Applied
Scientific EffectConvection: Convection

Data Source

PatentUS12291755B2Method of disintegrating and fluid drying of sugar beet material preventing the degradation reaction of the material
Publication Date: 2025.05.06 ZITNY BORIS

AI summary

A method for the disintegration and fluid drying of sugar beet material which prevents the material's degradation reaction from taking place and which includes the steps of disintegrating the sugar beet material to particles with a particle surface area of at least 2.0 cm2, and subsequent immediate exposure of the disintegrated material to a drying gas(es) at a temperature of 25° C. to 160° C. and a flow rate of 5 m·s31 1 to 40 m·s−1, where the relative humidity of the drying gas(es) at the inlet to the drying space is at most 85%; and subsequent mixing of the disintegrated material with a flow of drying gas(es) until attaining a value of dry matter of at least 70% by weight.