Vacuum Vessel U-Tube Heat Exchange Design

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Solution Overview

Problem

Existing vacuum vessels for oil deodorization lack efficiency in heat exchange between oil and heating/cooling medium, leading to suboptimal processing capacity and potential leakage issues due to complex machining requirements.

Innovation Solution

The vacuum vessel design features counter-current flow of oil and heating/cooling medium through U-tubes arranged in groups and rows, with channel plates and self-supporting structures to enhance stability and sealing, allowing for efficient heat exchange while minimizing vessel size and risk of leakage.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of energy

If U-tubes are arranged in groups and rows with counter-current flow to enhance heat exchange efficiency, then heat exchange efficiency is improved, but device complexity increases

Engineering Contradiction:
Improveheat exchange efficiencyVSAvoidU-tube arrangement complexity
Core Design Contradiction:
Loss of energyVSDevice complexity

Solution Approach 1:

The U-tubes are divided into multiple groups arranged in rows, with each group handling a specific section of the heat exchange process. This segmentation allows for optimized counter-current flow patterns while maintaining manageable complexity through modular arrangement

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The U-tubes are arranged in three-dimensional space with multiple rows and vertical positioning, creating a multi-layered heat exchange structure. This spatial arrangement maximizes heat transfer surface area and enables efficient counter-current flow without requiring excessive linear complexity

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Stability of the object's composition

If channel plates are firmly connected to both sides of the vessel to increase stability, then structural stability is improved, but manufacturing precision requirements increase

Engineering Contradiction:
Improvevessel structural stabilityVSAvoidchannel plate connection precision
Core Design Contradiction:
Stability of the object's compositionVSManufacturing precision

Solution Approach 1:

The channel plates are firmly connected to both sides of the vessel, merging the structural support function into the channel plate assembly itself. This integration provides inherent structural stability and positioning reference, reducing the need for high-precision separate mounting components

Inventive Principle:
Principle #5Merging (Combining)

3Volume of stationary object

If the vessel size is reduced to improve space utilization, then space efficiency is improved, but heat exchange efficiency may deteriorate

Engineering Contradiction:
Improvevessel sizeVSAvoidheat exchange efficiency
Core Design Contradiction:
Volume of stationary objectVSLoss of energy

Solution Approach 1:

The U-tubes are arranged in multiple rows and vertical layers within the vessel, utilizing three-dimensional space efficiently. This allows maximum heat transfer surface area to be packed into a compact volume, maintaining high heat exchange efficiency while minimizing vessel size

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

Solution Approach 2:

The heat exchange function is divided into multiple U-tube groups operating in parallel, allowing the total heat transfer capacity to be distributed across several smaller units that fit efficiently within the compact vessel volume

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 design significantly enhances heat exchange efficiency, reduces the risk of oil leakage, and maintains operational stability by optimizing the flow paths and structural integrity of the vessel.

Implementation Method 1

U-tubes for heating or cooling medium are arranged in such a way in said spaces that the flow of oil is counter-current to the flow of heating or cooling medium

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

the flow of oil is counter-current to the flow of heating or cooling medium all through the vessel

Methodology Applied
Scientific EffectCounter-current flow heat transfer: Convection

Implementation Method 3

The deodorization is carried through under vacuum 1-20 mbar and the removal of the volatiles is facilitated by adding stripping gas to the oil

Methodology Applied
Scientific EffectVacuum: Vacuum

Implementation Method 4

The stripping gas ensures agitation of the oil and promotes heat transfer and makes the removal of the unwanted substances easier

Methodology Applied
Scientific EffectGas sparging agitation: Sparging

Implementation Method 5

the flow of oil is counter-current to the flow of heating or cooling medium all through the vessel

Methodology Applied
Scientific EffectCounter-current flow: Convection

Data Source

PatentUS8070865B2Vacuum vessel for treatment of oils
Publication Date: 2011.12.06 ALFA LAVAL CORP AB
  • US8070865B2 patent drawing
  • US8070865B2 patent drawing
  • US8070865B2 patent drawing

AI summary

A vacuum vessel for continuous or semi-continuous treatment of oils in connection with deodorization comprises spaces (12, 121, 122) through which oil to be treated is brought to pass and means to heat or cool the oil in the form of U-tubes. There are perforated pipes (26) arranged at the bottom of said spaces to lead stripping gas into said oil. The vessel has a connection to a vacuum source (7). The spaces in the vessel are arranged such that the oil to be treated in the vessel flows through the same by gravity. The heating or cooling medium passing the U-tubes is arranged to be pumped therethrough. The U-tubes for heating or cooling medium are arranged in such a way in said spaces that the flow of oil is counter-current to the flow of heating or cooling medium all through the vessel and a number of U-tubes are arranged in groups (13), parallel and in rows above each other in said spaces.