Drying compressed gas

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Solution Overview

Problem

Existing compressed air drying systems face inefficiencies due to high pressure drops and energy consumption, which can lead to increased operational costs and capital expenditures, while also failing to effectively manage moisture and condensate, causing corrosion and equipment breakdowns.

Innovation Solution

A system comprising a cooler, refrigeration cycle, and multiple adsorption dryers in parallel configuration, where the cooler cools compressed air using a refrigerant, and adsorption dryers using desiccants like silica gel or molecular sieves further reduce moisture to a dew point of -40°C, with a pre-cooler and heaters for efficient operation and flexibility.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional refrigeration-based dryers are used to remove water vapor from compressed air, then water content is reduced, but pressure drop increases and system efficiency decreases

Engineering Contradiction:
Improvewater content removalVSAvoidsystem efficiency
Core Design Contradiction:
ReliabilityVSLoss of energy

Solution Approach 1:

The drying system is segmented into two distinct functional units: a refrigeration-based dryer for initial condensation removal and an adsorption dryer for final moisture removal. This segmentation allows each unit to operate optimally in its designated range, reducing overall pressure drop and energy consumption while achieving the required dew point.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The refrigeration-based dryer acts as an intermediary that pre-cools and pre-dries the compressed air before it enters the adsorption dryer. This intermediate step reduces the moisture load on the adsorption dryer, allowing it to operate more efficiently with lower pressure drop and reduced energy consumption.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Productivity

If high capacity dryers are installed to handle multiple compressors, then moisture removal capability increases, but capital costs increase

Engineering Contradiction:
Improvemoisture removal capabilityVSAvoidcapital costs
Core Design Contradiction:
ProductivityVSEase of manufacture

Solution Approach 1:

The drying capacity is segmented across multiple independent dryer units that can be configured in parallel. Each unit handles a portion of the total compressed air flow, allowing the system to scale with multiple compressors without requiring a single oversized expensive dryer. The modular approach reduces capital costs while maintaining adequate moisture removal capability.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The dryer system is designed with universal components that can serve multiple compressors. The refrigeration-based dryer and adsorption dryer units are configured to handle aggregate flow from multiple compressors, providing a cost-effective solution that avoids the need for individual dryers for each compressor.

Inventive Principle:
Principle #6Universality (Multi-functionality)

3Reliability

If adsorption dryers are used to achieve low dew point, then moisture removal effectiveness increases, but pressure drop and energy consumption increase

Engineering Contradiction:
Improvedew point achievementVSAvoidenergy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The refrigeration-based dryer performs preliminary cooling and condensation removal before the air enters the adsorption dryer. This preliminary action significantly reduces the moisture content and temperature of the incoming air to the adsorption dryer, allowing the desiccant to achieve the target dew point with lower pressure drop and reduced energy consumption for regenerating the desiccant.

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 configuration reduces pressure drops and energy consumption, enhances system efficiency, supports multiple compressors and dryer units, and lowers capital and operational costs by effectively managing moisture and condensate, thus minimizing equipment damage and energy usage.

Implementation Method 1

The cooler is configured to cool compressed air received from multiple compressors by exchange with a refrigerant

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Implementation Method 2

When air is cooled to a temperature less than the dew point, the water vapor condenses

Methodology Applied
Scientific EffectCondensation: Condensation

Implementation Method 3

The refrigeration cycle includes a refrigerant chiller configured to re-cool the refrigerant received from the cooler

Methodology Applied
Scientific EffectHeat removal: Cooling

Implementation Method 4

The adsorption dryers are configured to remove moisture from the cooled compressed air to form dried compressed air with a dew point of approximately -40°C (-40°F) or below

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentEP3829749B1Drying compressed gas
Publication Date: 2024.05.15 SAUDI ARABIAN OIL CO
  • EP3829749B1 patent drawingFigure 1A
  • EP3829749B1 patent drawingFigure 1B
  • EP3829749B1 patent drawingFigure 2

AI summary

A system includes a cooler, a refrigeration cycle, one or more receivers, and multiple adsorption dryers. The cooler is configured to cool compressed air received from multiple compressors by exchange with a refrigerant. The refrigeration cycle is in fluid communication with the cooler. The refrigeration cycle includes the refrigerant circulating in the refrigeration cycle. The refrigeration cycle includes a refrigerant chiller configured to re-cool the refrigerant received from the cooler. The one or more receivers are downstream of the cooler and are configured to collect condensate from the cooled compressed air. The adsorption dryers are in parallel downstream of the one or more receivers. The adsorption dryers are configured to remove moisture from the cooled compressed air to form dried compressed air with a dew point of approximately -40°F or below.