Method for operating a chiller

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Solution Overview

Problem

Chilled liquid systems using centrifugal compressors often fail to operate efficiently due to limited environmental conditions that allow for energy savings, as they typically shut down the compressor during free cooling conditions, resulting in reduced cooling capacity and energy inefficiencies.

Innovation Solution

A method of continuously operating the compressor in various temperature ranges by comparing condenser and evaporator temperatures, utilizing a variable speed drive for rotational speed control and magnetic bearings, to maintain a compressor operational state even during free cooling conditions, thereby increasing the range of operational temperatures and load capacity while minimizing energy costs.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of energy

If the compressor is shut down during free cooling conditions, then energy savings are achieved, but the range of environmental conditions for energy savings is limited

Engineering Contradiction:
Improveenergy savingsVSAvoidrange of environmental conditions
Core Design Contradiction:
Loss of energyVSAdaptability or versatility

Solution Approach 1:

The system dynamically adjusts compressor operation based on real-time temperature comparisons between condenser and evaporator. The control system continuously monitors temperatures and modulates compressor activity to maintain efficiency across varying environmental conditions, transitioning from static on/off control to dynamic adaptive control.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The invention changes the operational parameters by allowing compressor operation across a broader temperature differential range. By modifying the control logic to permit compressor operation when evaporator exit temperature is below condenser entering temperature, the system expands the environmental conditions under which energy savings can be achieved.

Inventive Principle:
Principle #35Parameter changes

2Adaptability or versatility

If the compressor is continuously operated, then the range of operational temperatures and load capacity are increased, but energy consumption increases

Engineering Contradiction:
Improverange of operational temperaturesVSAvoidcompressor energy consumption
Core Design Contradiction:
Adaptability or versatilityVSUse of energy by moving object

Solution Approach 1:

The system implements feedback control by continuously comparing condenser and evaporator temperatures and using this information to make real-time decisions about compressor operation. This closed-loop control ensures the compressor operates only when thermodynamically beneficial, preventing unnecessary energy consumption while maintaining expanded operational range.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The control system applies partial action by selectively operating the compressor only during specific temperature conditions rather than continuous operation. This partial operation strategy maintains the expanded temperature range capability while avoiding excessive energy consumption during conditions where compression would be inefficient.

Inventive Principle:
Principle #16Partial or excessive action

3Loss of energy

If the compressor is shut down during free cooling, then energy costs are reduced, but cooling capacity is reduced

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

Solution Approach 1:

The system dynamically balances energy consumption and cooling capacity by continuously monitoring temperature differentials and adjusting compressor operation accordingly. This dynamic approach allows the system to maintain adequate cooling capacity during periods when energy savings are achievable, rather than using fixed on/off thresholds.

Inventive Principle:
Principle #15Dynamics

Solution Approach 2:

The control system takes preliminary action by pre-cooling the evaporator water when conditions are favorable, storing cooling capacity in the chilled water loop. This allows the system to meet future cooling demands without continuous compressor operation, effectively decoupling immediate energy consumption from future cooling capacity requirements.

Inventive Principle:
Principle #10Preliminary 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 expands the range of operational temperatures, enhances energy savings, and increases chiller load capacity by maintaining compressor operation across a broader range of conditions, achieving nearly twice the design cooling capacity compared to conventional systems during free cooling conditions.

Implementation Method 1

a condenser (for thermal communication with refrigerant in the condenser)

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 2

an evaporator (for thermal communication with refrigerant in the evaporator)

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Implementation Method 3

the refrigerant used in the loop defining a pressure-enthalpy curve representative of different phases (vapor, liquid and vapor, and liquid) of the refrigerant

Methodology Applied
Scientific EffectPhase change: Phase Change

Data Source

PatentUS10883749B2Method for operating a chiller
Publication Date: 2021.01.05 TYCO FIRE & SECURITY GMBH
  • US10883749B2 patent drawing
  • US10883749B2 patent drawing
  • US10883749B2 patent drawing

AI summary

A method of operating a chiller having a closed refrigerant loop including a compressor, a condenser and an evaporator. The refrigerant used in the loop defining a pressure-enthalpy curve representative of different phases (vapor, liquid and vapor, and liquid) of the refrigerant at different combinations of pressure and enthalpy. The loop defining a process cycle (compression, condensation, expansion, and evaporation) of the refrigerant during operation of the loop relative to the pressure-enthalpy curve of the refrigerant. The method including continuously operating the compressor when a segment of the process cycle corresponds to the refrigerant being in the liquid phase.