Dividing Wall Distillation Column Vapor Split Control for Sidecut Bias

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Solution Overview

Problem

Dividing wall fractional distillation columns lack operational and control parameter development, particularly in terms of flexibility to adjust sidecut product composition, which limits their ability to respond effectively to changes in feed composition.

Innovation Solution

Varying the vapor flow rates from the undivided portion of the column below the dividing wall to the feed and product sections, in conjunction with controlling liquid flow rates, allows for greater flexibility in achieving desired sidecut compositions by adjusting the Vp/Vf and Lp/Lf ratios, enabling better management of feedstock changes.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Use of energy by moving object

If dividing wall fractional distillation columns are used to separate hydrocarbon mixtures, then energy efficiency is improved through sharing reboiler and condenser duties, but operational flexibility to adjust sidecut product composition is insufficient

Engineering Contradiction:
Improveenergy efficiencyVSAvoidoperational flexibility
Core Design Contradiction:
Use of energy by moving objectVSAdaptability or versatility

Solution Approach 1:

The patent applies dynamics by making the vapor flow distribution adjustable rather than fixed. Variable flow control devices are installed in the vapor conduits connecting the lower undivided section to the upper divided sections, allowing operators to dynamically adjust vapor flow rates to each side according to changing feed composition and desired product specifications. This dynamic control capability resolves the contradiction by enabling operational flexibility while maintaining the energy-efficient dividing wall configuration.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent changes the operational parameters by introducing independent control of vapor flow rates to different column sections. By varying the vapor flow distribution ratio between sections and controlling liquid reflux ratios, the system can adjust sidecut product composition across a broader range. This parameter change approach allows the column to adapt to different operating conditions while preserving the energy efficiency benefits of the dividing wall design.

Inventive Principle:
Principle #35Parameter changes

2Adaptability or versatility

If conventional fractional distillation columns are used, then operational flexibility is maintained, but energy efficiency deteriorates due to separate reboiler and condenser duties for each column

Engineering Contradiction:
Improveoperational flexibilityVSAvoidenergy efficiency
Core Design Contradiction:
Adaptability or versatilityVSUse of energy by moving object

Solution Approach 1:

The patent merges multiple distillation functions into a single integrated column structure with a dividing wall. The dividing wall configuration allows two separate distillation sections to share common reboiler and condenser systems, eliminating duplicate energy-consuming equipment. This merging approach achieves energy efficiency while the patent simultaneously introduces vapor flow control mechanisms to maintain operational flexibility, thus resolving the contradiction between energy efficiency and adaptability.

Inventive Principle:
Principle #5Merging (Combining)

3Adaptability or versatility

If vapor flow rates to feed and product sections are varied, then the range of achievable sidecut compositions is enhanced, but device complexity increases due to additional flow control systems

Engineering Contradiction:
Improverange of sidecut compositionsVSAvoidflow control system complexity
Core Design Contradiction:
Adaptability or versatilityVSDevice complexity

Solution Approach 1:

The patent segments the vapor flow control into separate controllable sections. Variable flow control devices are installed in individual vapor conduits connecting the lower undivided section to specific upper sections, allowing independent adjustment of vapor flow to each section. This segmentation enables precise control over sidecut composition while keeping each control element relatively simple and modular, thus managing device complexity while enhancing adaptability.

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

This approach significantly enhances the range of achievable sidecut compositions, improving the column's ability to favor higher or lower molecular weight components and maintaining desired product compositions despite changes in feedstock, thereby increasing operational flexibility and energy efficiency.

Implementation Method 1

Distillation is a separation process that exploits differences (sometimes minor) in component relative volatilities or boiling points

Methodology Applied
Scientific EffectDistillation: Distillation

Implementation Method 2

a sufficient number of theoretical stages of vapor-liquid equilibrium contacting

Methodology Applied
Scientific EffectVapor-liquid equilibrium:

Data Source

PatentUS20120103013A1Vapor and liquid flow control in a dividing wall fractional distillation column
Publication Date: 2012.05.03 UOP LLC
  • US20120103013A1 patent drawing
  • US20120103013A1 patent drawing
  • US20120103013A1 patent drawing

AI summary

Dividing wall fractional distillation columns and methods of operating these columns with greater flexibility, especially in terms of the ability to adjust the composition of the heartcut, intermediate or sidecut product fraction, are described. In particular, this composition may be advantageously “biased” toward higher or lower molecular weight components, depending on operating needs. Changes in feedstock composition may also be managed more effectively. These benefits are obtained by varying the flow rate of vapor and liquid to each side of the dividing wall. The vapor flowrate rising from an undivided portion of the column interior below the dividing wall is varied to the feed and/or product sections on opposite sides of the dividing wall. Also, the liquid flowrate falling from an undivided portion of the column interior above the dividing wall is varied to the feed and/or product sections on opposite sides of the dividing wall.