Control of pull-down in refrigeration systems

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Solution Overview

Problem

Refrigeration systems in cargo containers consume excessive energy during the pull-down phase to achieve target temperatures, leading to inefficient cooling and increased operational costs.

Innovation Solution

Operating the evaporator fan at reduced speed during the pull-down phase, while maintaining constant compressor power, increases the temperature difference between return and supply air, reducing energy consumption and accelerating the cooling process without degrading system performance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If the evaporator fan is operated at high speed during pull-down, then the refrigeration effect is maximized and cargo is refrigerated quickly, but the energy consumption increases significantly

Engineering Contradiction:
Improverefrigeration speedVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The evaporator fan speed is dynamically adjusted based on the refrigeration stage: high speed during pull-down to maximize cooling effect, then automatically reduced to low speed when target temperature is reached. This dynamic adjustment resolves the contradiction by matching fan speed to actual cooling needs, achieving fast refrigeration when required while minimizing energy consumption during maintenance phase.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The system changes the operating parameters of the evaporator fan from high speed to low speed based on temperature conditions. During pull-down, high fan speed provides maximum air circulation and heat exchange; when target temperature is reached, the parameter changes to low speed, maintaining adequate air flow while dramatically reducing energy consumption and friction heat generation.

Inventive Principle:
Principle #35Parameter changes

2Productivity

If the evaporator fan operates at high speed, then air circulation is maximized for efficient heat exchange, but friction heat generated in the container increases

Engineering Contradiction:
Improveheat exchange efficiencyVSAvoidfriction heat
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The system applies partial action by operating the evaporator fan at high speed only during the pull-down phase when maximum cooling is needed, rather than continuously. Once the target temperature is reached, the fan speed is reduced to low level, providing just enough air circulation for heat exchange while minimizing friction heat generation. This partial application of high speed action resolves the contradiction between heat exchange efficiency and friction heat.

Inventive Principle:
Principle #16Partial or excessive action

3Power

If the compressor operates at full capacity during pull-down, then the refrigeration effect is maximized, but the pull-down period still extends longer than desired

Engineering Contradiction:
Improverefrigeration powerVSAvoidpull-down duration
Core Design Contradiction:
PowerVSLoss of time

Solution Approach 1:

The system maintains continuous useful action by keeping the compressor operating at full capacity throughout the pull-down phase without interruption. Combined with high-speed evaporator fan operation, this ensures maximum refrigeration power is continuously applied to the cargo, achieving the shortest possible pull-down duration while maximizing refrigeration effectiveness.

Inventive Principle:
Principle #20Continuity of useful 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 significantly saves energy and shortens the pull-down period, maintaining the set-point temperature effectively and reducing energy consumption by optimizing air flow and refrigerant circulation.

Implementation Method 1

The extracted return air is blown past the evaporator to refrigerate the air, and the refrigerated supply air is blown as into the container where it circulates and exchanges heat with the cargo and/or with the walls of the container

Methodology Applied
Scientific EffectHeat transfer: Convection

Implementation Method 2

The vapor-compression cycle is used in most household refrigerators as well as in many large commercial and industrial refrigeration systems

Methodology Applied
Scientific EffectCompression: Compression

Implementation Method 3

The extracted return air is blown past the evaporator to refrigerate the air

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 4

The vapor-compression cycle is used in most household refrigerators as well as in many large commercial and industrial refrigeration systems

Methodology Applied
Scientific EffectCondensation: Condensation

Data Source

PatentEP2180278B1Control of pull-down in refrigeration systems
Publication Date: 2021.01.27 THERMO KING CORP
  • EP2180278B1 patent drawingFigure 1~2
  • EP2180278B1 patent drawingFigure 3

AI summary

A method for operating a refrigeration system (100) for a container to pull down the temperature of cargo from ambient to a predetermined set-point temperature, and a system employing the method. The method includes operating a compressor (110) at a first power to compress a refrigerant and direct the refrigerant through a condenser (120) and an evaporator (140) of the refrigeration system, initially operating an evaporator fan (150) at a first speed to supply refrigerated supply air from the evaporator to the cargo within the container, sensing the temperature of the supply air, comparing the temperature of the supply air with a predetermined set-point temperature, and increasing the speed of the evaporator fan (150) to a second speed faster than the first when the temperature of the supply air is lower than the predetermined set-point temperature to maintain the temperature of the supply air at the predetermined set-point temperature.