Distillation Column Control via Feed-Forward Reflux Adjustment

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Solution Overview

Problem

Existing distillation column control systems are inefficient for separating mixtures with significantly different boiling points, as they lack a linear temperature profile and fail to maintain product quality and energy efficiency.

Innovation Solution

A closed-loop control system that varies the reflux ratio and proactively adjusts energy input based on the feed stream, while monitoring and adjusting the bottom temperature to maintain optimal operating conditions.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If conventional control systems are used for distillation columns separating mixtures with significantly different boiling points, then the control system is simple to implement, but the system fails to maintain product quality and energy efficiency

Engineering Contradiction:
Improveproduct qualityVSAvoidcontrol system complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The control system proactively adjusts the energy input (heat carrier medium flow rate) based on feed stream conditions before they affect the distillation process outcome. This feedforward control anticipates disturbances and compensates for them in advance, maintaining product quality without requiring complex reactive control mechanisms.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system implements closed-loop feedback control by continuously monitoring the bottom temperature and adjusting the heat carrier medium flow rate accordingly. This feedback mechanism ensures that product quality is maintained by correcting deviations from the desired temperature profile, resolving the contradiction between simple control implementation and effective quality maintenance.

Inventive Principle:
Principle #23Feedback

2Loss of energy

If the heat carrier medium flow rate is reduced to improve energy efficiency, then energy consumption decreases, but the bottom temperature falls too far affecting separation quality

Engineering Contradiction:
Improveenergy consumptionVSAvoidseparation quality
Core Design Contradiction:
Loss of energyVSManufacturing precision

Solution Approach 1:

The closed-loop feedback control system monitors the bottom temperature and adjusts the heat carrier medium flow rate to maintain the temperature within the optimal range. This ensures that energy efficiency is improved by reducing unnecessary heating while preventing the bottom temperature from falling too far, thereby maintaining separation quality.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system dynamically adjusts operational parameters (heat carrier medium flow rate, reflux ratio) based on feed conditions and temperature measurements. By changing these parameters in response to process conditions, the system optimizes energy consumption while maintaining adequate bottom temperature for quality separation.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If proactive feedforward control is implemented to adjust energy input based on feed stream, then energy efficiency improves, but the control system complexity increases

Engineering Contradiction:
Improveenergy efficiencyVSAvoidcontrol system structure
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The feedforward control component proactively adjusts the heat carrier medium flow rate based on measured feed stream conditions (flow rate, composition, temperature) before these conditions affect the distillation process. This preliminary action improves energy efficiency by optimizing energy input in advance, while the modular structure of adding feedforward to existing feedback control limits the increase in overall system complexity.

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 ensures efficient operation, maintains high product quality, and reduces the need for manual intervention by stabilizing the distillation column's temperature and mass flow rates, even under varying feed conditions.

Implementation Method 1

a circulation evaporator (200) for the heating of the column bottom by indirect heating of a first portion B11 of the liquid bottom product B1

Methodology Applied
Scientific EffectIndirect heating: Heat Exchanger

Implementation Method 2

a top condenser (300) for condensing the evaporated top product A1 to obtain a liquefied stream A2

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 3

a distillation column set up for separation of a substance mixture S comprising essentially a substance A and a substance B which is significantly higher-boiling than substance A

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS12076670B2Method for operating a distillation column
Publication Date: 2024.09.03 COVESTRO DEUTSCHLAND AG
  • US12076670B2 patent drawing
  • US12076670B2 patent drawing
  • US12076670B2 patent drawing

AI summary

The present invention relates to a method for continuously operating a distillation column, which is designed to separate a mixture S, which contains essentially a substance A and a substance B, which boils significantly higher than substance A. In the method according to the invention, the reflux ratio is changed according to the feed flow and, at the same time, the energy input by means of the heat-transfer medium is changed proactively (so-called feed-forward control) by accounting for the feed flow by means of feed-forward control. At the same time, the bottom temperature is observed and the control structure is changed if the bottom temperature falls too far when the heat-transfer medium is reduced by means of the feed flow.