Transcritical CO2 Compression Staging for Capacity Boost

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Solution Overview

Problem

Refrigerant vapor compression systems operating in transcritical cycles, particularly in transport refrigeration, face challenges in maintaining refrigeration capacity equivalent to subcritical cycles, especially under high-capacity operations, and struggle with energy efficiency across varying load conditions.

Innovation Solution

A refrigerant vapor compression system with a multi-stage compression device and an economizer circuit, allowing for selective operation of compression stages in series or parallel flow relationships, and utilizing flow control devices to manage refrigerant flow through various heat exchangers, enabling operation in economized, non-economized, and capacity-boosted modes to optimize cooling capacity and efficiency.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Object-affected harmful factors

If a refrigerant vapor compression system operates in transcritical cycle with carbon dioxide, then environmental capability is improved, but refrigeration capacity under high-demand conditions deteriorates compared to subcritical systems

Engineering Contradiction:
Improveenvironmental capabilityVSAvoidrefrigeration capacity
Core Design Contradiction:
Object-affected harmful factorsVSProductivity

Solution Approach 1:

The system dynamically switches between series and parallel compression stage configurations based on operating conditions. The compression stages can be selectively connected in series for normal operation or in parallel for capacity-boosted operation, allowing the system to adapt its refrigeration capacity to match demand while maintaining transcritical carbon dioxide operation for environmental benefits

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The system changes operational parameters by altering the flow relationship between compression stages. Flow control devices adjust refrigerant flow distribution to switch between series and parallel configurations, thereby changing the effective compression capacity and ratio to match varying load conditions while maintaining transcritical operation

Inventive Principle:
Principle #35Parameter changes

2Loss of energy

If compression stages operate in series configuration, then energy efficiency is improved, but refrigeration capacity under high-demand conditions deteriorates

Engineering Contradiction:
Improveenergy efficiencyVSAvoidrefrigeration capacity
Core Design Contradiction:
Loss of energyVSProductivity

Solution Approach 1:

The system provides dynamic configuration switching between series and parallel compression stage arrangements. During normal operation, stages operate in series for energy efficiency. During high-demand periods, the system switches to parallel configuration to boost refrigeration capacity, and during pull-down operations, it can operate in capacity-boosted mode with both stages compressing simultaneously

Inventive Principle:
Principle #15Dynamics

3Productivity

If compression stages operate in parallel configuration, then refrigeration capacity is boosted, but energy efficiency deteriorates

Engineering Contradiction:
Improverefrigeration capacityVSAvoidenergy efficiency
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The system dynamically selects parallel configuration only when high refrigeration capacity is required. Flow control devices enable switching between series and parallel modes based on real-time operating conditions, ensuring parallel operation is used strategically during capacity-boosted需求的 periods rather than continuously, thereby minimizing energy waste

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The system changes operational parameters by adjusting the flow relationship between compression stages. During pull-down operations or high-demand periods, the system switches to parallel configuration with adjusted refrigerant flow distribution to maximize capacity. During normal steady-state operation, it returns to series configuration for energy efficiency

Inventive Principle:
Principle #35Parameter changes

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 system achieves refrigeration capacity comparable to subcritical systems, enhances cooling performance during high-demand periods, and reduces energy consumption by adjusting compression stage configurations, resulting in improved efficiency and potential displacement volume reduction of up to 25-30%, leading to overall system efficiency gains of 5-10%.

Implementation Method 1

a compression device having a first compression stage and a second compression stage

Methodology Applied
Scientific EffectCompression: Compression

Implementation Method 2

a first refrigerant heat rejection heat exchanger and a second refrigerant heat rejection heat exchanger

Methodology Applied
Scientific EffectHeat transfer: Heat Exchanger

Implementation Method 3

a refrigerant heat absorption heat exchanger

Methodology Applied
Scientific EffectHeat transfer: Heat Exchanger

Implementation Method 4

a primary expansion device operatively associated with the evaporator

Methodology Applied
Scientific EffectThrottling expansion: Pressure Drop

Implementation Method 5

a refrigerant heat absorption heat exchanger, hereinafter referred to as an evaporator

Methodology Applied
Scientific EffectEvaporation: Evaporation

Data Source

PatentEP2699853B1Transcritical refrigerant vapor system with capacity boost
Publication Date: 2019.03.13 CARRIER CORP
  • EP2699853B1 patent drawingFigure 1
  • EP2699853B1 patent drawingFigure 2
  • EP2699853B1 patent drawingFigure 3

AI summary

A refrigerant vapor compression system and method of operation are disclosed wherein the first (30a) and second (30b) compression stages of a two stage compression device are selectively configurable in a first arrangement and a second arrangement. In the first arrangement, the first and second compression stages operate in a series refrigerant flow relationship. In the second arrangement, the first and second compression stages (30a), (30b) operate in a parallel refrigerant flow relationship.