Energy-Saving Design of Urea Method for Hydrazine Hydrate Process DOI Open Access

Zhihao Wang,

Xiaojing Wang, Haibin Wu

et al.

Processes, Journal Year: 2025, Volume and Issue: 13(5), P. 1585 - 1585

Published: May 20, 2025

The conventional urea-based process for hydrazine hydrate production faces challenges including low product yield and high energy consumption. To overcome these limitations, we propose an innovative integrated approach combining jet reactor technology with membrane separation, further enhanced through heat network optimization. Through simulation sensitivity analysis, the following optimal distillation parameters were identified: nine theoretical stages, feed entry at fifth stage, a reflux ratio of 0.6, distillate flow rate 354 kg/h. Systematic optimization exchanger (HEN) using pinch achieved substantial savings, reducing hot utility consumption by 66.8% (to 1317 MJ/h) cold usage 62.7% 1503 MJ/h). redesigned HEN prioritized temperature-cascaded recovery, enabling 67% recuperation from exothermic reaction streams. Operational costs decreased 12%, underscoring economic viability coupling intensification thermal integration. This work establishes sustainable framework synthesis, balancing industrial feasibility reduced environmental impact in chemical manufacturing.

Language: Английский

Pinch Analysis for Energy Optimization in Floating Photovoltaic-Based Ammonia Production Systems Using Hint Software: A Contribution Toward Sustainable Development Goals (SDGs) DOI
Widayat Widayat,

Aprilia Susanti,

Faustina Alda Nurushofa

et al.

Journal of Lifestyle and SDGs Review, Journal Year: 2025, Volume and Issue: 5(5), P. e6680 - e6680

Published: May 14, 2025

Objective: The objective of this study is to investigate the optimization energy efficiency in a renewable energy-based ammonia production system, with aim enhancing sustainability by integrating floating photovoltaic (FPV) panels and utilizing pinch analysis for optimal heat integration. Theoretical Framework: This underpinned concepts related efficiency, integration, process optimization. Pinch serves as primary framework maximizing thermal recovery minimizing external utility consumption, contributing more sustainable process. Method: methodology adopted research involves application an system powered panels. evaluates exchanger networks (HEN) identify potential savings improve overall efficiency. Data collection includes balance assessments determine impact integration on consumption. Results Discussion: results reveal Maximum Energy Recovery (MER) 845,085 kW, leading 36.83% cooling utilities 56.31% heating utilities, average saving rate 46.57%. discussion contextualizes these findings within theoretical framework, emphasizing benefits reduced dependency lower greenhouse gas emissions, improved operational also acknowledges limitations implementation feasibility scalability. Research Implications: provides practical insights into sources techniques production. can influence industrial practices, policy development, future advancements hydrogen carriers storage solutions. Originality/Value: contributes literature demonstrating effectiveness optimizing system. highlights value technology minimize costs, reduce support Sustainable Development Goal 7 (Affordable Clean Energy).

Language: Английский

Citations

0

Energy-Saving Design of Urea Method for Hydrazine Hydrate Process DOI Open Access

Zhihao Wang,

Xiaojing Wang, Haibin Wu

et al.

Processes, Journal Year: 2025, Volume and Issue: 13(5), P. 1585 - 1585

Published: May 20, 2025

The conventional urea-based process for hydrazine hydrate production faces challenges including low product yield and high energy consumption. To overcome these limitations, we propose an innovative integrated approach combining jet reactor technology with membrane separation, further enhanced through heat network optimization. Through simulation sensitivity analysis, the following optimal distillation parameters were identified: nine theoretical stages, feed entry at fifth stage, a reflux ratio of 0.6, distillate flow rate 354 kg/h. Systematic optimization exchanger (HEN) using pinch achieved substantial savings, reducing hot utility consumption by 66.8% (to 1317 MJ/h) cold usage 62.7% 1503 MJ/h). redesigned HEN prioritized temperature-cascaded recovery, enabling 67% recuperation from exothermic reaction streams. Operational costs decreased 12%, underscoring economic viability coupling intensification thermal integration. This work establishes sustainable framework synthesis, balancing industrial feasibility reduced environmental impact in chemical manufacturing.

Language: Английский

Citations

0