Two-Stage Compressor Hot Gas Bypass for Low-Load Surge Control

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Solution Overview

Problem

Existing vapor compression systems with two-stage centrifugal compressors face challenges in maintaining stable operation at low loads, particularly in controlling surge and ensuring efficient refrigerant flow, which is not adequately addressed by traditional hot gas bypass configurations.

Innovation Solution

The implementation of a dual hot gas bypass system with two non-overlapping bypass flowpaths, each controlled by a valve, that divert refrigerant from the compressor, with one bypass extending between the inlet and outlet of the compressor stages and the other from the discharge to upstream of the expansion device, allowing for dynamic control based on pressure parameters calculated by a controller.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a traditional single hot gas bypass is used, then the system can provide stable operation at low loads, but the control precision and surge prevention capability are insufficient

Engineering Contradiction:
Improvestable operation at low loadsVSAvoidbypass control system
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The single bypass flowpath is segmented into two separate bypass flowpaths (first bypass flowpath from interstage to downstream of first heat exchanger, second bypass flowpath from interstage to upstream of expansion device), each with independent valve control. This segmentation allows independent control of refrigerant flow to different locations, providing more precise surge control and stability at low loads without excessive system complexity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system uses dynamic valve control based on real-time pressure parameter calculations. The controller continuously monitors pressure differential across the compressor and dynamically adjusts the bypass valves to maintain optimal flow conditions. This dynamic adjustment capability enables the system to adapt to varying load conditions and prevent surge effectively.

Inventive Principle:
Principle #15Dynamics

2Stability of the object's composition

If the bypass valve is opened to increase compressor load for stable operation, then stability improves, but energy efficiency and system performance deteriorate

Engineering Contradiction:
Improvecompressor operation stabilityVSAvoidsystem efficiency
Core Design Contradiction:
Stability of the object's compositionVSLoss of energy

Solution Approach 1:

Different bypass flowpaths deliver refrigerant to different locations with different thermal conditions. The first bypass delivers to downstream of the first heat exchanger while the second bypass delivers to upstream of the expansion device. This local quality differentiation allows selective bypass control that can maintain stability while minimizing energy loss by directing bypass flow to the most appropriate location based on system conditions.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The controller calculates pressure parameters (such as pressure differential across the compressor) and uses these parameters to dynamically adjust bypass valve positions. By changing the bypass flow rate as a variable parameter based on real-time pressure conditions, the system can maintain stable operation only when necessary, rather than continuously bypassing, thereby reducing energy losses.

Inventive Principle:
Principle #35Parameter changes

3Adaptability or versatility

If bypass flowpath delivers refrigerant to multiple locations, then flow control flexibility increases, but system complexity and potential for harmful factors increase

Engineering Contradiction:
Improverefrigerant flow control flexibilityVSAvoidsurge risk and system instability
Core Design Contradiction:
Adaptability or versatilityVSObject-affected harmful factors

Solution Approach 1:

The controller acts as an intermediary that coordinates the two bypass valves based on calculated pressure parameters. Rather than allowing independent or conflicting bypass actions, the controller mediates the bypass flow distribution to ensure that the combined effect of both bypasses maintains system stability and prevents surge conditions.

Inventive Principle:
Principle #24Intermediary (Mediator)

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 configuration enhances stability and efficiency by allowing for precise control of refrigerant flow, reducing the risk of surge and optimizing compressor operation across varying loads, thereby improving the overall performance of the vapor compression system.

Implementation Method 1

A bypass flowpath is positioned to deliver refrigerant from the compressor bypassing the first heat exchanger

Methodology Applied
Scientific EffectPressure gradient: Pressure Gradient

Implementation Method 2

A valve is positioned to control flow through the bypass flowpath

Methodology Applied
Scientific EffectPressure control: Pressure Gradient

Data Source

PatentUS10267539B2Hot gas bypass for two-stage compressor
Publication Date: 2019.04.23 CARRIER CORP
  • US10267539B2 patent drawing
  • US10267539B2 patent drawing
  • US10267539B2 patent drawing

AI summary

A vapor compression system comprising a centrifugal compressor (22) having: an inlet (24); an outlet (26); a first impeller stage (28); a second impeller stage (30); and a motor (34) coupled to the first impeller stage and second impeller stage. A first heat exchanger (38) is downstream of the outlet along a refrigerant flowpath. An expansion device (56) and a second heat exchanger (64) are upstream of the inlet along the refrigerant flowpath. A bypass flowpath (120; 320) is positioned to deliver refrigerant from the compressor bypassing the first heat exchanger. A valve (128) is positioned to control flow through the bypass flowpath, wherein: the bypass flowpath extends from a first location (140) intermediate the inlet and outlet to a second location (142; 342) downstream of the first heat exchanger along the refrigerant flowpath.