Packed Manifold Heat Exchanger for Stable Two-Phase Refrigerant Flow

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Solution Overview

Problem

Current heat exchangers, particularly in refrigeration systems, face inefficiencies in two-phase flow environments, leading to poor heat transfer coefficients, increased pressure drop, and freeze-out conditions, especially at ultra-low and cryogenic temperatures, due to inadequate phase distribution and surface area-to-volume ratios.

Innovation Solution

A heat exchanger design incorporating a packed distributor within the manifold, featuring packing elements such as spherical or cylindrical elements, which improves fluid distribution and reduces pressure drop across the exchanger, while maintaining a high heat transfer coefficient, even at low temperatures.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Volume of moving object

If plate type heat exchangers are used to increase surface area to volume ratio, then compactness is improved, but two-phase flow distribution deteriorates leading to poor heat transfer coefficients and increased pressure drop

Engineering Contradiction:
Improveheat exchanger compactnessVSAvoidtwo-phase flow distribution stability
Core Design Contradiction:
Volume of moving objectVSReliability

Solution Approach 1:

A packed distributor is introduced as an intermediary component within the manifold of the plate type heat exchanger. This packing material (such as random packing elements or structured elements) acts as a mediator to improve two-phase flow distribution before the fluid enters the heat transfer channels, thereby maintaining compactness while resolving the flow distribution issues

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The invention utilizes porous packing materials within the manifold to enhance two-phase flow distribution. The porous structure of the packing elements creates capillary forces and surface tension effects that promote uniform distribution of liquid and vapor phases across all channels, solving the distribution problems inherent in plate type heat exchangers

Inventive Principle:
Principle #31Porous materials

2Reliability

If typical two-phase flow distributors are used in plate-type heat exchangers to improve flow distribution, then phase distribution is improved, but pressure drop increases by more than 18 psi

Engineering Contradiction:
Improvephase distribution uniformityVSAvoidpressure drop
Core Design Contradiction:
ReliabilityVSStress or pressure

Solution Approach 1:

The invention changes the physical parameters of the distribution system by using packing material with specific properties (porosity, particle size, shape) that allow effective flow distribution at lower pressure drops. The packing is designed to create appropriate flow resistance through capillary effects rather than through high-velocity pressure drops, achieving distribution with pressure drop of no more than 5 psi

Inventive Principle:
Principle #35Parameter changes

3Area of stationary object

If tubular heat exchangers are used to achieve desired heat transfer surface area, then heat transfer area is improved, but device complexity and cost increase due to wrapping and contortion in confined spaces

Engineering Contradiction:
Improveheat transfer surface areaVSAvoidtubing configuration complexity
Core Design Contradiction:
Area of stationary objectVSDevice complexity

Solution Approach 1:

The invention transitions from one-dimensional tubular heat exchangers to a two-dimensional plate structure with distributed channels. This dimensional change allows the heat exchanger to achieve high surface area in a compact footprint without requiring complex three-dimensional tubing arrangements, thereby reducing device complexity and installation difficulty in confined spaces

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

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 solution achieves a pressure drop of no more than 5 psi and enhances the overall heat transfer coefficient by at least 2%, improving system efficiency and stability across various operating modes, including cool, standby, and defrost modes.

Implementation Method 1

A fluid entering the fluid inlet manifold may comprise at least two phases, which may be vapor and liquid

Methodology Applied
Scientific EffectTwo-phase flow: Two-Phase Flow

Implementation Method 2

a plurality of heat transfer channels configured to communicate with the fluid inlet manifold and the fluid outlet manifold

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 3

The heat exchanger may be a plate-type heat exchanger, such as a counter-flow heat exchanger

Methodology Applied
Scientific EffectConvection: Convection

Data Source

PatentUS7490483B2Efficient heat exchanger for refrigeration process
Publication Date: 2009.02.17 EDWARDS VACUUM LLC
  • US7490483B2 patent drawing
  • US7490483B2 patent drawing
  • US7490483B2 patent drawing

AI summary

Aspects of the invention are found in a heat exchanger. The heat exchanger includes a fluid inlet manifold, a fluid outlet manifold, a plurality of heat transfer channels configured to communicate with the fluid inlet manifold and the fluid outlet manifold, and packing located within the fluid inlet manifold. Further aspects of the invention are found in a refrigeration system. The refrigeration system includes a compressor and at least one heat exchanger coupled to the compressor. The at least one heat exchanger includes a header, packing located in the header, and a heat transfer channel. The heat transfer channel is configured to receive fluid passing through the header and the packing.