Steady-State Digital Twin Development for Heat and Shaft-Work Integration in a Dual-Stage Pressure Nitric Acid Plant Retrofit

This study focuses on enhancing heat and shaft power integration within existing nitric acid production processes to optimize waste heat recovery and identify opportunities to improve process efficiency. A digital twin of the operational plant is utilized, which features a dual-stage pressure nitric acid production process with a capacity of 50 tons/h of HNO3 (100% equivalent). The authors conducted a simultaneous analysis of the thermal energy potential and the expansion capacity of tail gases to effectively fulfil the primary process's heating, cooling, and power requirements while increasing steam generation through waste heat recovery, all without compromising plant throughput. The proposed process modifications lead to a 23.8% reduction in cooling water usage and a 35.6% decrease in CO2 equivalent emissions while achieving a 13.1% increase in steam generation. These utility savings culminate in a 10.2% enhancement in plant throughput.

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Publication Details

Journal
Systems and Control Transactions
Published
2025-06-30
DOI
https://doi.org/10.69997/sct.127061
Citations
1
Primary Topic
Flexible and Reconfigurable Manufacturing Systems
Type
article
Field-Weighted Citation Impact
1.24

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article

Steady-State Digital Twin Development for Heat and Shaft-Work Integration in a Dual-Stage Pressure Nitric Acid Plant Retrofit

Goran Krajačić, Stanislav Boldyryev
1 citations
Systems and Control Transactions
Flexible and Reconfigurable Manufacturing Systems
1.24
article

Steady-State Digital Twin Development for Heat and Shaft-Work Integration in a Dual-Stage Pressure Nitric Acid Plant Retrofit

Goran Krajačić, Stanislav Boldyryev
article en
1 citations

Abstract

This study focuses on enhancing heat and shaft power integration within existing nitric acid production processes to optimize waste heat recovery and identify opportunities to improve process efficiency. A digital twin of the operational plant is utilized, which features a dual-stage pressure nitric acid production process with a capacity of 50 tons/h of HNO3 (100% equivalent). The authors conducted a simultaneous analysis of the thermal energy potential and the expansion capacity of tail gases to effectively fulfil the primary process's heating, cooling, and power requirements while increasing steam generation through waste heat recovery, all without compromising plant throughput. The proposed process modifications lead to a 23.8% reduction in cooling water usage and a 35.6% decrease in CO2 equivalent emissions while achieving a 13.1% increase in steam generation. These utility savings culminate in a 10.2% enhancement in plant throughput.

Systems and Control TransactionsVol. 4
University of Zagreb (HR)
European Commission, HORIZON EUROPE Framework Programme
Openalex Percentile: Top 18%
Flexible and Reconfigurable Manufacturing Systems
1.24
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