A method for controlling a vapour compression system at low superheat

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing methods for controlling vapour compression systems, such as refrigeration and air conditioning systems, struggle to maintain a superheat value of refrigerant leaving the evaporator that is both energy efficient and safe, as low superheat values can lead to unstable control and potential liquid refrigerant reaching the compressor.

Innovation Solution

A method that calculates a reference superheat value by adding a variance quantity to a minimum acceptable superheat value, ensuring the superheat remains above a critically low value even in unstable operating conditions, thereby preventing liquid refrigerant from reaching the compressor while maintaining energy efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of energy

If the superheat value is reduced to enhance energy efficiency, then the energy efficiency is improved, but the control stability deteriorates and liquid refrigerant may reach the compressor

Engineering Contradiction:
Improveenergy efficiencyVSAvoidcontrol stability
Core Design Contradiction:
Loss of energyVSReliability

Solution Approach 1:

The patent applies dynamics by making the superheat setpoint adjustable and adaptive rather than fixed. The system dynamically adjusts the superheat setpoint based on operating conditions (such as load, temperature, pressure), allowing it to operate at lower superheat values when conditions permit, thereby improving energy efficiency while maintaining reliability through real-time adaptation to changing system states

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The patent changes the parameter of superheat setpoint from a fixed value to a variable parameter that can be adjusted based on system conditions. By modifying this key parameter dynamically, the system achieves lower average superheat values for improved energy efficiency while preventing liquid refrigerant damage through adaptive control that responds to actual operating conditions

Inventive Principle:
Principle #35Parameter changes

2Loss of energy

If the superheat value is reduced to improve energy efficiency, then the energy efficiency is improved, but the risk of liquid refrigerant reaching the compressor increases

Engineering Contradiction:
Improveenergy efficiencyVSAvoidliquid refrigerant damage to compressor
Core Design Contradiction:
Loss of energyVSObject-affected harmful factors

Solution Approach 1:

The patent implements feedback control by continuously monitoring system parameters (temperature, pressure, superheat) and using this information to adjust the expansion device and maintain appropriate superheat levels. This feedback mechanism ensures that even when operating at lower superheat values for energy efficiency, the system automatically responds to conditions that might indicate approaching liquid refrigerant, thereby preventing compressor damage

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The system dynamically adjusts the superheat setpoint based on real-time operating conditions, allowing lower superheat values when safe and automatically increasing them when risk of liquid refrigerant is detected. This dynamic adjustment resolves the contradiction by making the superheat level adaptive rather than static, improving energy efficiency while maintaining compressor protection

Inventive Principle:
Principle #15Dynamics

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 method allows the vapour compression system to operate at lower superheat values than previous methods, enhancing energy efficiency while ensuring safe operation by maintaining a stable superheat value above the minimum acceptable level.

Implementation Method 1

The refrigerant leaving the heat rejecting heat exchanger is supplied to the expansion device, where it undergoes expansion before being supplied to the evaporator

Methodology Applied
Scientific EffectExpansion:

Implementation Method 2

When passing through the evaporator, the liquid part of the refrigerant is at least partly evaporated, while heat exchange takes place with the ambient or a secondary fluid flow across the evaporator, in such a manner that heat is absorbed by the refrigerant

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 3

In the heat rejecting heat exchanger, heat exchange takes place between the refrigerant and the ambient or a secondary fluid flow across the heat rejecting heat exchanger, in such a manner that heat is rejected from the refrigerant

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 4

Refrigerant flowing in the refrigerant path is compressed by the compressors of the compressor unit before being supplied to the heat rejecting heat exchanger

Methodology Applied
Scientific EffectCompression: Compression

Data Source

PatentUS20250198677A1A method for controlling a vapour compression system at low superheat
Publication Date: 2025.06.19 DANFOSS AS
  • US20250198677A1 patent drawing
  • US20250198677A1 patent drawing
  • US20250198677A1 patent drawing

AI summary

A method for controlling a vapour compression system (1) includes a compressor unit (2), a heat rejecting heat exchanger (3), an expansion device (4) and an evaporator (5) arranged in a refrigerant path. A superheat value of refrigerant leaving the evaporator (5) is derived, and a quantity being representative for a variance of the derived superheat value is calculated. A reference superheat value is calculated, based on the calculated quantity and on a minimum acceptable superheat value, by adding the calculated quantity to the minimum acceptable superheat value. The expansion device (4) is operated in accordance with the calculated reference superheat value, and in order to obtain a superheat of refrigerant leaving the evaporator (5) which is equal to the reference superheat value.