De-entrainment Device for Distillation Columns
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Solution Overview
Problem
In vapor-liquid contacting devices, particularly in high capacity distillation columns, the entrainment of liquid in vapor streams leads to reduced capacity and efficiency due to compositional mismatch and increased liquid traffic, which complicates effective separation, especially in sections near reboiler returns or feed introductions.
Innovation Solution
The implementation of de-entrainment devices with modular construction, featuring non-parallel alignment and bypass conduits that direct liquid from downcomers to avoid co-current flow channels, allowing efficient separation of entrained liquid from vapor, thus maintaining high capacity and efficiency while minimizing pressure drop.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Productivity
If conventional fractionation trays are used for high capacity vapor-liquid contacting, then vapor and liquid handling capacity is increased, but liquid entrainment in vapor streams increases causing compositional mismatch and reduced efficiency
Solution Approach 1:
The tray is divided into multiple functional zones: a high-capacity contacting section for vapor-liquid mass transfer, and a separate de-entrainment section with coalescing elements. This segmentation allows the tray to simultaneously handle high vapor/liquid traffic while effectively separating entrained liquid from vapor streams through the dedicated de-entrainment zone.
Solution Approach 2:
The de-entrainment function is extracted as a separate functional element within the tray structure. Coalescing elements are positioned in the vapor path to specifically address liquid entrainment removal, separating this function from the main contacting function and allowing optimized performance of both.
2Productivity
If tray spacing is reduced to increase column capacity, then more trays can be installed, but vapor velocity increases causing greater liquid entrainment
Solution Approach 1:
Coalescing elements serve as intermediary structures in the vapor path that capture and coalesce entrained liquid droplets. These elements provide a mechanism for liquid removal without requiring increased tray spacing, allowing high vapor velocities to be maintained while still achieving effective de-entrainment.
3Reliability
If de-entrainment devices are added to separate entrained liquid, then separation efficiency is improved, but device complexity and space requirements increase
Solution Approach 1:
The de-entrainment function is merged with the existing tray structure rather than being implemented as a separate device. Coalescing elements are integrated into the tray deck or positioned within the vapor path in a space-efficient manner, combining multiple functions (contacting, separation, and de-entrainment) in a single integrated structure.
4Reliability
If conventional de-entrainment methods are used, then liquid separation is achieved, but pressure drop increases reducing overall column efficiency
Solution Approach 1:
Coalescing elements with porous or mesh structures are used to provide large surface area for liquid-vapor separation. These porous structures allow vapor to pass through with minimal resistance while effectively capturing and coalescing liquid droplets, achieving good separation efficiency with low pressure drop.
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 de-entrainment devices effectively separate entrained liquid from vapor streams, enhancing column performance by preventing compositional mismatch and maintaining high vapor and liquid handling capabilities with minimal space occupation.
Implementation Method 1
de-entrainment devices for separating liquid that is entrained in a vapor stream
Implementation Method 2
allowing efficient separation of entrained liquid from vapor
Data Source
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AI summary
De-entrainment devices for effectively removing entrained liquid from a vapor stream are disclosed. These de-entrainment devices are effective in distillation columns and other apparatuses comprising vapor-liquid contacting devices. Particular representative applications for these de-entrainment devices are in distillation (or fractionation) columns having co-current contacting modules, in which liquid and vapor enter into co-current flow channels of the modules. The de-entrainment devices can be used, for example, with non-parallel contacting stages or other types of high capacity trays.