Mechanically pumped system for direct control of two-phase isothermal evaporation

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Solution Overview

Problem

Current methods for maintaining isothermal heat rejection in systems with large heat loads face challenges such as poor isothermality, low evaporator performance, and excessive equipment requirements, particularly due to issues with fluid distribution and cavitation in multi-channel evaporators.

Innovation Solution

A thermal system comprising a reservoir, a cooling loop, and a heat rejection loop with specific components like sub-coolers, pre-heaters, evaporators, pressure regulators, and vapor compressors, which manage fluid flow and pressure to achieve consistent temperature and efficient heat transfer by sub-cooling, pre-heating, and regulating pressure to maintain saturation conditions within the evaporator channels.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If standard heat rejection methods are used, then heat transfer occurs, but isothermal temperature control deteriorates

Engineering Contradiction:
Improveisothermal temperature controlVSAvoidtemperature consistency
Core Design Contradiction:
TemperatureVSReliability

Solution Approach 1:

The system changes the pressure parameter of the working fluid using a pressure regulator to maintain constant saturation temperature during evaporation, achieving isothermal heat rejection. By controlling pressure to correspond to a specific saturation temperature, the system ensures consistent temperature control throughout the evaporator channels.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The system performs preliminary sub-cooling of the working fluid before it enters the evaporator channels. This pre-cooling action ensures the fluid enters the evaporator at a controlled temperature and pressure state, enabling subsequent isothermal evaporation and improving temperature consistency during heat rejection.

Inventive Principle:
Principle #10Preliminary action

2Area of stationary object

If multi-channel evaporators are used, then heat transfer area increases, but fluid distribution uniformity deteriorates

Engineering Contradiction:
Improveheat transfer areaVSAvoidfluid distribution uniformity
Core Design Contradiction:
Area of stationary objectVSStability of the object's composition

Solution Approach 1:

The system applies local quality by providing sub-cooling specifically at the inlet regions of the evaporator channels before fluid distribution. This localized pre-cooling ensures uniform fluid properties across all channels at the point of distribution, improving flow uniformity while maintaining large heat transfer area through multi-channel configuration.

Inventive Principle:
Principle #3Local quality

3Productivity

If evaporation rate increases, then heat rejection efficiency improves, but cavitation risk increases

Engineering Contradiction:
Improveheat rejection efficiencyVSAvoidcavitation prevention
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The system performs preliminary sub-cooling of the working fluid before it reaches the evaporator and pump inlet. This pre-cooling action increases the margin between the fluid temperature and its saturation temperature, preventing cavitation during high-rate evaporation by ensuring liquid remains in a stable state throughout the system.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The sub-cooling process creates a temperature buffer or cushion before the fluid enters the evaporator channels. This buffer protects against cavitation by maintaining a larger temperature difference between the actual fluid temperature and saturation temperature, even during high evaporation rates, thereby preventing vapor bubble formation that would cause cavitation.

Inventive Principle:
Principle #11Beforehand cushioning (Prior cushioning)

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 ensures stable, consistent temperature maintenance for heat loads while optimizing evaporator performance and reducing the need for excessive space and equipment, thereby enhancing isothermal heat rejection and system efficiency.

Implementation Method 1

a liquid pump, a first side of a pre-heater

Methodology Applied
Scientific EffectPumping: Pump

Implementation Method 2

sub-cooling the fluid drawn from the reservoir

Methodology Applied
Scientific EffectSub-cooling: Supercooling

Implementation Method 3

pre-heating the pumped fluid prior to the inlet of the evaporator

Methodology Applied
Scientific EffectPre-heating: Heating

Implementation Method 4

evaporating a portion of the fluid in the evaporator

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 5

Two-Phase Isothermal Evaporation

Methodology Applied
Scientific EffectIsothermal evaporation: Phase Change

Implementation Method 6

regulating the pressure of the fluid at the outlet of the evaporator to thereby maintain a substantially constant fluid temperature

Methodology Applied
Scientific EffectPressure regulation:

Implementation Method 7

compressing the fluid drawn from the reservoir

Methodology Applied
Scientific EffectCompression: Compression

Implementation Method 8

condensing the compressed fluid

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 9

expanding the condensed fluid

Methodology Applied
Scientific EffectExpansion:

Data Source

PatentUS10906150B2Mechanically pumped system for direct control of two-phase isothermal evaporation
Publication Date: 2021.02.02 ROLLS ROYCE NORTH AMERICAN TECHNOLOGIES INC
  • US10906150B2 patent drawing
  • US10906150B2 patent drawing
  • US10906150B2 patent drawing

AI summary

A thermal system may comprise a reservoir, a first fluid flowpath, and a second fluid flowpath. The first fluid flowpath may start at the reservoir and return to the reservoir. The first fluid flowpath may comprise, in a direction of the fluid flow, a first side of a sub-cooler, a liquid pump, a first side of a pre-heater, and a first side of an evaporator. The second fluid flowpath may start at the reservoir and return to the reservoir. The second fluid flowpath may comprise, in a direction of a fluid flow, a pressure regulator, a vapor compressor, a first side of a condenser, and an expansion value.