Atmospheric Water Generation System Using CO2-Based Vapor Compression Refrigeration

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Executive Summary

This paper presents a high-level technical and commercial investigation into a novel solar-powered atmospheric water generation (AWG) system designed for remote, off-grid agricultural applications in Australia. Addressing the critical issue of water scarcity in inland regions like Gunnedah, New South Wales, where rainfall variability, drought cycles, and rising water delivery costs threaten agricultural productivity. The proposed system uniquely employs a CO2-based vapor compression refrigeration (VCR) cycle as its core technology. While CO2 (R-744) is an established refrigerant in commercial refrigeration, its application in AWG is theoretical and believed to be the first of its kind. This investigation sought to determine if such a system could offer a viable, low-emissions, and energy-efficient solution for potable water generation from air.

The analysis, based on Gunnedah’s climate data, modeled water production capacities for 100 L/day for small-scale needs and as a proof of concept. Key technical findings indicate that to produce 100 L/day, approximately 2,284 m3 of air per hour would need to be processed, requiring an estimated electrical input of 11 kW, or 49.5 kWh/day, assuming a Coefficient of Performance (COP) of 2.0.

A preliminary financial analysis, benchmarking against the cost of trucked water, projects a negative Net Present Value (NPV) of -$61,292.80 over a 20-year lifespan for a 100 L/day system with an estimated capital cost of $57,900. Despite this, the system offers substantial non-monetary benefits, including enhanced water security and resilience against drought, reduced reliance on carbon-intensive trucking, and alignment with environmental and sustainability goals.

Significant risks include the system’s theoretical nature and lack of commercial availability, the complexity of high-pressure transcritical CO2 operation, and the need for specialised components and maintenance. Recommendations for future steps include; 

  • exploring funding opportunities to improve commercial viability and support its development as a critical resilience infrastructure investment.
  • scale sensitivity analysis, 
  • evaluating performance in varying ambient conditions, 
  • detailed costing, and 

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Table of Contents

Executive Summary

1. Introduction / Background 8

3. Technology Overview 9

3.1 Current Technology Maturity of the CO2 AWG System 9

3.1 Introduction to Atmospheric Water Generation (AWG) 9

3.2 Atmospheric Conditions and Water Yield 9

3.3 Active AWG Systems 11

a. Vapor Compression Refrigeration (VCR) 11

b. Thermoelectric Cooling (TEC) 12

3.4 Passive AWG Systems 12

a. Fog Nets 12

b. Absorbent-Based Systems (Desiccants) 13

c. Radiative Dew Collectors 14

d. Dew Water Harvesting Systems 15

3.5 Hybrid Approaches 15

4. Technical Assessment 17

4.1 Understanding the Transcritical CO2 Cycle (with P-h Diagram) 18

4.2 Results 20

Assumptions 20

Daily Throughput and Air Volume Required 20

Heat Removed per Hour 21

Estimated Electrical Input 21

5. Economic & Commercial Feasibility 22

5.1. Current Market Options 22

5.2 Comparison with Alternative Water Supply Technologies 23

5.3 Preliminary Financial Analysis 25

Assumptions 25

Outcome 25

5.4 Discussion 25

Resilience & Water Security 25

Environmental & Strategic Benefits 25

Scalability & Innovation 26

6. Risks & Considerations 27

Technology Availability and Maturity 27

System Design and Operational Complexity 27

Water Quality and Treatment 27

Economic Viability 27

Environmental and Climatic Sensitivity 28

Technical Integration and Maintenance 28

7. Recommendations & Next Steps 29

1. Scale Sensitivity Analysis 29

2. System Performance at Higher Ambient Conditions 29

Detailed Costing and Procurement Review 29

Power Supply Scenario Planning 29

Regulatory and Compliance Review 29

Site-Specific Feasibility 29

Stakeholder Engagement and Funding Opportunities 29

Hybrid system 29

7. Conclusion 30

Appendix 1 31

Electrical Demand Calculation 31

8. References