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arxiv: 2604.25192 · v1 · submitted 2026-04-28 · 🧮 math.OC · cs.SY· eess.SY

Reconfiguring flexibility in renewable power-to-ammonia systems using molten-salt thermal energy storage in the ammonia synthesis loop: A coordinated electro-hydrogen-thermal scheduling approach

Pith reviewed 2026-05-07 15:59 UTC · model grok-4.3

classification 🧮 math.OC cs.SYeess.SY
keywords renewable power-to-ammoniamolten-salt thermal energy storageammonia synthesis reactorcoordinated schedulingmixed-integer linear programmingthermal stabilityflexibilityeconomic optimization
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The pith

Molten-salt thermal storage in the ammonia synthesis loop lets small battery and hydrogen storage match the performance of large-battery renewable power-to-ammonia systems at lower cost.

A machine-rendered reading of the paper's core claim, the machinery that carries it, and where it could break.

The paper establishes that placing molten-salt thermal energy storage inside the Haber-Bosch loop can buffer temperature swings caused by intermittent renewable hydrogen production and keep the reactor in hot standby or low-load operation without repeated start-ups. A state-space thermal model feeds into a mixed-integer linear program that coordinates electricity, hydrogen, and heat flows while using information gap decision theory to handle renewable uncertainty. Year-round simulations on an industrial-scale northern China project show the combined small-battery, hydrogen-storage, and molten-salt setup delivers near-equivalent flexibility, thermal stability, and net revenue compared with oversized battery-only designs while cutting investment. A sympathetic reader would care because renewable power-to-ammonia must solve both intermittency and the chemical plant's preference for steady thermal conditions if green ammonia is to scale.

Core claim

Integrating molten-salt thermal energy storage directly into the ammonia synthesis loop decouples hydrogen-supply fluctuations from reactor thermal dynamics, enabling sustained hot-standby and thermal-support modes. When this is embedded in a coordinated electro-hydrogen-thermal MILP schedule that includes information-gap uncertainty handling, a configuration of modest battery energy storage plus hydrogen storage plus molten-salt storage achieves performance close to that of much larger battery systems, lowers total capital outlay, avoids most start-up and shutdown events, and produces higher net revenue across variable renewable conditions.

What carries the argument

The molten-salt thermal energy storage unit inserted in the ammonia synthesis loop, whose thermal inertia and hot-standby capability are captured by a state-space model and then optimized inside a mixed-integer linear program with information-gap decision theory.

If this is right

  • Capital cost drops because far less battery capacity is required for the same level of system flexibility.
  • The ammonia synthesis reactor avoids most damaging temperature cycles and start-up or shutdown events, extending equipment life.
  • Net revenue stays higher throughout the year even when wind and solar output varies strongly.
  • The economic value of adding still more battery capacity falls once molten-salt storage is present.
  • Reactor thermal stability improves under both normal and low-hydrogen-supply conditions.

Where Pith is reading between the lines

These are editorial extensions of the paper, not claims the author makes directly.

  • The same thermal-storage placement could be tested in other exothermic synthesis loops that suffer from renewable-driven load swings.
  • Lower storage costs might allow smaller overall renewable generation capacity while still meeting a fixed annual ammonia target.
  • Faster project payback could accelerate deployment of power-to-ammonia plants in regions with high renewable variability.

Load-bearing premise

The state-space model correctly captures the coupled thermal dynamics of the reactor and storage, and the MILP-plus-IGDT formulation fully represents all operational limits and uncertainties without later fixes that change the reported gains.

What would settle it

Year-round operational data or a high-fidelity simulation in which the small-battery plus molten-salt configuration fails to match the revenue, flexibility, or reactor-temperature stability achieved by a large-battery baseline.

read the original abstract

In renewable power-to-ammonia (ReP2A) systems, the intermittency of wind and solar generation propagates through electrolytic hydrogen production and induces thermal instability in the ammonia synthesis reactor (ASR). The resulting temperature cycling accelerates fatigue and shortens service life, while reactor thermal inertia limits flexible start-up, shutdown, and load adjustment. To address this issue, this study integrates molten-salt thermal energy storage (MS-TES) into the Haber-Bosch synthesis loop and develops a coordinated electro-hydrogen-thermal scheduling framework. MS-TES decouples hydrogen supply fluctuations from reactor thermal dynamics by enabling hot standby operation and sustained thermal support during start-up and low-load conditions. A state-space model is established to capture the thermal dynamics of the ASR and MS-TES. Based on this model, an optimal scheduling program coordinates ammonia synthesis operation with hydrogen production, battery energy storage (BES), and hydrogen storage (HS). The problem is formulated as a mixed-integer linear program (MILP) and extended with information gap decision theory (IGDT) to address renewable uncertainty. Case studies based on an industrial-scale project in northern China show that MS-TES enhances reactor thermal stability and system-level flexibility, while diminishing the marginal benefit of large BES capacity. As a result, a configuration combining small BES, HS, and MS-TES achieves near-equivalent performance to large-BES systems, with lower investment and improved economic returns. Year-round simulations further show that MS-TES avoids ASR start-up and shutdown and delivers consistently higher net revenue under variable renewable conditions.

Editorial analysis

A structured set of objections, weighed in public.

Desk editor's note, referee report, simulated authors' rebuttal, and a circularity audit. Tearing a paper down is the easy half of reading it; the pith above is the substance, this is the friction.

Referee Report

2 major / 2 minor

Summary. The paper proposes integrating molten-salt thermal energy storage (MS-TES) into the Haber-Bosch ammonia synthesis loop of renewable power-to-ammonia (ReP2A) systems. It develops a state-space model of the coupled ASR and MS-TES thermal dynamics, formulates a MILP-based coordinated electro-hydrogen-thermal scheduling problem, and augments it with IGDT to handle renewable uncertainty. Case studies on an industrial-scale project in northern China claim that a configuration with small BES, HS, and MS-TES achieves near-equivalent performance to large-BES systems at lower investment cost, avoids ASR start-up/shutdown cycles, and yields higher year-round net revenue under variable wind/solar conditions.

Significance. If the state-space model and resulting schedules are accurate, the work demonstrates a practical way to reduce electrical storage requirements in green ammonia production by exploiting thermal inertia and hot-standby operation. This could lower capital costs and improve reactor longevity, addressing a recognized barrier to flexible ReP2A operation. The application of standard MILP+IGDT tools to a new thermal-coupling configuration is a modest but useful contribution; the strength lies in the system-level economic comparison rather than methodological novelty.

major comments (2)
  1. [Model-development section (state-space equations for ASR and MS-TES)] The central claim that small-BES + HS + MS-TES matches large-BES performance and avoids ASR cycling rests on the accuracy of the linear state-space model for ASR-MS-TES thermal coupling (described in the model-development section following the abstract). Linearised dynamics may omit nonlinear reaction kinetics, variable heat losses, and valve/transient effects during start-up; without explicit validation against a nonlinear reference model or plant data, the MILP schedules and IGDT robustness margins may overstate stability and economic gains.
  2. [Case-study and year-round simulation results] Year-round simulation results showing consistently higher net revenue and elimination of start-up/shutdown events (case-study section) depend on the MILP correctly enforcing thermal constraints derived from the state-space model. If the linear approximation underestimates required thermal support during low-load or ramping conditions, the reported reduction in BES sizing and investment cost would not hold.
minor comments (2)
  1. The abstract is dense and would benefit from one or two quantitative metrics (e.g., percentage reduction in BES capacity or revenue improvement) to support the 'near-equivalent performance' and 'consistently higher net revenue' statements.
  2. Notation for the state-space matrices (A, B, C, etc.) and the mapping from continuous dynamics to the MILP constraints should be clarified to allow readers to reproduce the thermal-support formulation.

Simulated Author's Rebuttal

2 responses · 0 unresolved

We thank the referee for the constructive comments on our manuscript. We address each major point below and commit to revisions that strengthen the presentation of the model and results.

read point-by-point responses
  1. Referee: [Model-development section (state-space equations for ASR and MS-TES)] The central claim that small-BES + HS + MS-TES matches large-BES performance and avoids ASR cycling rests on the accuracy of the linear state-space model for ASR-MS-TES thermal coupling (described in the model-development section following the abstract). Linearised dynamics may omit nonlinear reaction kinetics, variable heat losses, and valve/transient effects during start-up; without explicit validation against a nonlinear reference model or plant data, the MILP schedules and IGDT robustness margins may overstate stability and economic gains.

    Authors: The state-space model captures the dominant thermal energy balances of the ASR and MS-TES, linearized around nominal operating points to enable tractable MILP scheduling over annual horizons. Reaction kinetics are treated as steady-state within the synthesis loop, consistent with the paper's focus on thermal stability rather than detailed chemistry. We agree that explicit validation would strengthen the claims. In the revised manuscript we will add a new subsection that compares linear-model trajectories against a nonlinear dynamic simulation (using the same energy-balance structure with temperature-dependent heat capacities and losses) for representative start-up, shutdown, and ramping events, and we will report the maximum temperature deviation and its effect on constraint satisfaction. revision: yes

  2. Referee: [Case-study and year-round simulation results] Year-round simulation results showing consistently higher net revenue and elimination of start-up/shutdown events (case-study section) depend on the MILP correctly enforcing thermal constraints derived from the state-space model. If the linear approximation underestimates required thermal support during low-load or ramping conditions, the reported reduction in BES sizing and investment cost would not hold.

    Authors: The MILP enforces the linear state-space constraints at every time step, which by construction prevents temperature excursions outside the allowable band and thereby eliminates start-up/shutdown cycles. To quantify the impact of linearization error we will include, in the revised case-study section, a sensitivity study that perturbs the linear coefficients (heat-loss factors and thermal capacities) within physically plausible ranges and re-solves the scheduling problem. The resulting changes in optimal BES size, investment cost, and net revenue will be reported, demonstrating that the economic advantage of the MS-TES configuration remains robust. revision: yes

Circularity Check

0 steps flagged

No circularity: standard state-space modeling and MILP/IGDT scheduling applied to new TES configuration.

full rationale

The derivation proceeds from a state-space model of ASR and MS-TES thermal dynamics to an MILP scheduling formulation extended by IGDT for renewable uncertainty, with performance claims evaluated on year-round simulations of an industrial-scale project. No quoted equations or steps show a performance metric, prediction, or flexibility benefit reducing to a fitted parameter by construction, nor does any load-bearing premise rest on self-citation chains or imported uniqueness theorems. The approach uses established optimization techniques on a novel hardware integration, remaining self-contained against external benchmarks.

Axiom & Free-Parameter Ledger

0 free parameters · 0 axioms · 0 invented entities

Abstract-only review provides no explicit free parameters, axioms, or invented entities; the state-space model and MILP are presumed to rely on standard engineering assumptions whose details are unavailable.

pith-pipeline@v0.9.0 · 5682 in / 1176 out tokens · 36122 ms · 2026-05-07T15:59:04.726684+00:00 · methodology

discussion (0)

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Reference graph

Works this paper leans on

58 extracted references · 58 canonical work pages

  1. [1]

    Ammonia as a renewable energy carrier from synthesis to utilization

    Wen Z, Huang B, Wang Y , et al. Ammonia as a renewable energy carrier from synthesis to utilization. Nature Reviews Clean Technology, 2025, 1(11): 755-770

  2. [2]

    Redesigning electrification of Chin a’s ammonia and methanol industry to balance decarbonization with power system security

    Li J, Lin J, Wang J, et al. Redesigning electrification of Chin a’s ammonia and methanol industry to balance decarbonization with power system security. Nature Energy, 2025, 10: 762-773

  3. [3]

    Optimal operation of the hydrogen-based energy management system with P2X demand response and ammonia plant

    Klyapovskiy S, Zheng Y , You S, et al. Optimal operation of the hydrogen-based energy management system with P2X demand response and ammonia plant. Applied Energy, 2021, 304: 117559

  4. [4]

    Experimental studies and modeling o f a 250-kW alkaline water electrolyzer for hydrogen 26 production

    Ren Z, Wang J, Yu Z, et al. Experimental studies and modeling o f a 250-kW alkaline water electrolyzer for hydrogen 26 production. Journal of Power Sources, 2022, 544: 231886

  5. [5]

    Extended load flexibility of utili ty-scale P2H plants: Optimal production scheduling considering dynamic thermal and HTO impurity effects

    Qiu Y , Zhou B, Zang T et al. Extended load flexibility of utili ty-scale P2H plants: Optimal production scheduling considering dynamic thermal and HTO impurity effects. Renewable Energy, 2023, 217: 119198

  6. [6]

    Dynamic modeling of a pressurized alkaline water electrolyzer: a multiphysics approach

    Iribarren Á, Elizondo D, Barrios E L, et al. Dynamic modeling of a pressurized alkaline water electrolyzer: a multiphysics approach. IEEE Transactions on Industry Applications, 2023, 59(3): 3741-3753

  7. [7]

    On the future relevance of green hydrogen in Europe

    Ajanovic A, Sayer M, Haas R. On the future relevance of green hydrogen in Europe. Applied Energy, 2024, 358: 122586

  8. [8]

    Utilization of excess water accumulation for green hydrogen production in a run-of-river hydropower plant

    Jovan D J, Dolanc G, Pregelj B. Utilization of excess water accumulation for green hydrogen production in a run-of-river hydropower plant. Renewable Energy, 2022, 195: 780-794

  9. [9]

    Co-planning of regional wind resources-based ammonia industry and the electric network: A case study of Inner Mongolia

    Li J, Lin J, Heuser P M, et al. Co-planning of regional wind resources-based ammonia industry and the electric network: A case study of Inner Mongolia. IEEE Transactions on Power Systems, 2021, 37(1): 65-80

  10. [10]

    Comparing green hydrogen and green ammonia as energy carriers in utility-scale transport and subsurface storage

    Menefee A H, Schwartz B A. Comparing green hydrogen and green ammonia as energy carriers in utility-scale transport and subsurface storage. Energy and Climate Change, 2024, 5: 100163

  11. [11]

    A review of structure configuration, integration, operation and key technologies of renewable energy power to hydrogen system

    Lin J, Cheng X, Qiu Y , et al. A review of structure configuration, integration, operation and key technologies of renewable energy power to hydrogen system. High V oltage Engineering, 2025,51(05): 2078-2095

  12. [12]

    Design and operat ion of Power-to-Ammonia sy stems: A review

    Narciso D A C, Pires J M, Fortunato J, et al. Design and operat ion of Power-to-Ammonia sy stems: A review. Energy Conversion and Management, 2025, 327: 119494

  13. [13]

    Operating envelope of Haber-Bosch process design for power-to-ammonia

    Cheema I I, Krewer U. Operating envelope of Haber-Bosch process design for power-to-ammonia. RSC Advances, 2018, 8(61): 34926-34936

  14. [14]

    The importance of dynamic operati on and renewable energy source on the economic feasibility of green ammonia

    Smith C, Torrente-Murciano L. The importance of dynamic operati on and renewable energy source on the economic feasibility of green ammonia. Joule, 2024, 8(1): 157-174

  15. [15]

    Dynamic simulation of a highly load-flexible Haber-Bosch plant

    Fahr S, Kender R, Bohn J P , et al. Dynamic simulation of a highly load-flexible Haber-Bosch plant. International Journal of Hydrogen Energy, 2025, 102: 1231-1242

  16. [16]

    Finney E E, Finke R G. Catalyst sintering kinetics data: Is the re a minimal chemical mechanism underlying kinetics previously fit by empirical power-law expressions and if so, what are its implications? Industrial & Engineering Chemistry Research, 2017, 56(37): 10271-10286

  17. [17]

    Techno-economic analyses of power-to-ammonia-to-power and biomass-to-ammonia-to-power pathways for carbon neutrality scenario

    Wen D, Aziz M. Techno-economic analyses of power-to-ammonia-to-power and biomass-to-ammonia-to-power pathways for carbon neutrality scenario. Applied Energy, 2022, 319: 119272

  18. [18]

    A comprehensive review on renewable power-to-green hydrogen-to-power systems: Green hydrogen production, transportation, storage, re-electrification and safety

    Dong H, Deng Q, Li C, et al. A comprehensive review on renewable power-to-green hydrogen-to-power systems: Green hydrogen production, transportation, storage, re-electrification and safety. Applied Energy, 2025, 390: 125821

  19. [19]

    Integrated battery and hydrogen energy storage for enhanced grid power savings and green hydrogen utilization

    Kwon K, Lee H B, Kim N, et al. Integrated battery and hydrogen energy storage for enhanced grid power savings and green hydrogen utilization. Applied Sciences, 2024, 14(17): 7631

  20. [20]

    Flexible operatio n, optimisation and stabilising control of a quench cooled ammonia reactor for power-to-ammonia

    Rosbo J W, Ritschel T K S, Hørsholt S, et al. Flexible operatio n, optimisation and stabilising control of a quench cooled ammonia reactor for power-to-ammonia. Computers & Chemical Engineering, 2023, 176: 108316

  21. [21]

    Nonlinear model predictive control of flexible ammonia production

    Kong B, Zhang Q, Daoutidis P. Nonlinear model predictive control of flexible ammonia production. Control Engineering Practice, 2024, 148: 105946

  22. [22]

    Research on design and multi-frequency scheduling optimization method for flexible green ammonia system

    Wu Y , Zhao T, Tang S, et al. Research on design and multi-frequency scheduling optimization method for flexible green ammonia system. Energy Conversion and Management, 2024, 300: 117976

  23. [23]

    Optimal sizing of Power-to-Ammonia plants: A stochastic two-stage mixed-integer programming approach

    Wang S. Optimal sizing of Power-to-Ammonia plants: A stochastic two-stage mixed-integer programming approach. Energy, 2025, 318: 134838

  24. [24]

    Optimal scheduling of electricity-hydrogen-ammonia coupled integrated energy system based on uncertain renewable generations

    Shi X, Xing H, Wang H, et al. Optimal scheduling of electricity-hydrogen-ammonia coupled integrated energy system based on uncertain renewable generations. Journal of Renewable and Sustainable Energy, 2025, 17(3): 035501

  25. [25]

    Multistable-flexible ammonia process adapted to renewable energy

    Ji X, Lin J, Nie L. Multistable-flexible ammonia process adapted to renewable energy. Clean Coal Technology, 2024, 30(2): 23-35

  26. [26]

    Design and thermody namic analysis of a large- scale ammonia reactor for increased load flexibility

    Fahr S, Schiedeck M, Schwarzhuber J, et al. Design and thermody namic analysis of a large- scale ammonia reactor for increased load flexibility. Chemical Engineering Journal, 2023, 471: 144612

  27. [27]

    How does a resilient, flexible ammonia process look? Robust design optimization of a Haber-Bosch process with optimal dynamic control powered by wind

    Verleysen K, Parente A, Contino F. How does a resilient, flexible ammonia process look? Robust design optimization of a Haber-Bosch process with optimal dynamic control powered by wind. Proceedings of the Combustion Institute, 2023, 39(4): 5511-5520

  28. [28]

    The Shenneng Otog Banne r wind-solar-hydrogen integrated green ammonia project: Exemplary leadership, pioneering demonstration, strivi ng for project excellence, 2025

    The People’s Government of Otog Banner. The Shenneng Otog Banne r wind-solar-hydrogen integrated green ammonia project: Exemplary leadership, pioneering demonstration, strivi ng for project excellence, 2025. Available: http://www.eq.gov.cn/zwgk/zdxxgk/xzsf/202507/t20250725_3819737.html

  29. [29]

    Bridging new energy and chemical industries: An on-site report on the CEEC 27 Songyuan hydrogen park (green H2-NH3-methanol integration) proj ect, 2025

    The People’s Government of Jilin Province. Bridging new energy and chemical industries: An on-site report on the CEEC 27 Songyuan hydrogen park (green H2-NH3-methanol integration) proj ect, 2025. Available: https://www.jl.gov.cn/szfzt/tzcj/tzdt/202506/t20250609_3462654.html

  30. [30]

    Optimizing dispatch for a concentrated solar power tower

    Wagner M J, Hamilton W T, Newman A, et al. Optimizing dispatch for a concentrated solar power tower. Solar Energy, 2018, 174: 1198-1211

  31. [31]

    Thermodynamic analysis and operation strategy optimization of coupled molten salt energy storage system for coal-fired power plant

    Li B, Cao Y , He T, et al. Thermodynamic analysis and operation strategy optimization of coupled molten salt energy storage system for coal-fired power plant. Applied Thermal Engineering, 2024, 236: 121702

  32. [32]

    Design and performance analysis of dee p peak shaving scheme for thermal power units based on high-temperature molten salt heat storage system

    Ma T, Li Z, Lv K, et al. Design and performance analysis of dee p peak shaving scheme for thermal power units based on high-temperature molten salt heat storage system. Energy, 2024, 288: 129557

  33. [33]

    Flexible design and operation of off-grid green ammonia systems with gravity energy storage under long-term renewable power uncertainty

    Zhou J, Tong B, Wang H, et al. Flexible design and operation of off-grid green ammonia systems with gravity energy storage under long-term renewable power uncertainty. Applied Energy, 2025, 388: 125629

  34. [34]

    Intelligent hydrogen-ammonia combined energy storage system with deep reinforcement learning

    Lan P, Chen S, Li Q, et al. Intelligent hydrogen-ammonia combined energy storage system with deep reinforcement learning. Renewable Energy, 2024, 237: 121725

  35. [35]

    Safety investigation of hydrogen energy storage systems using quantitative risk assessment

    Le S T, Nguyen T N, Linforth S, et al. Safety investigation of hydrogen energy storage systems using quantitative risk assessment. International Journal of Hydrogen Energy, 2023, 48(7): 2861-2875

  36. [36]

    Studying the effect of dynamic operation conditions on green ammonia production synthesis loop

    Patel R, Mehr A S, Valverde J I, et al. Studying the effect of dynamic operation conditions on green ammonia production synthesis loop. Journal of Process Control, 2025, 150: 103436

  37. [37]

    Optimal sizing and pricing of grid-connected renewable power to ammonia systems considering the limited flexibility of ammonia synthesis

    Y u Z, Lin J, Liu F, et al. Optimal sizing and pricing of grid-connected renewable power to ammonia systems considering the limited flexibility of ammonia synthesis. IEEE Transactions on Power Systems, 2023, 39(2): 3631-3648

  38. [38]

    Optimal capacity and multi-stable flexible operation strategy of green ammonia systems: Adapting to fluctuations in renewable energy

    Zhou J, Zhang Z, Zhang R, et al. Optimal capacity and multi-stable flexible operation strategy of green ammonia systems: Adapting to fluctuations in renewable energy. Energy Conversion and Management, 2024, 314: 118720

  39. [39]

    Multi-timescale trading strategy for renewable power to ammonia virtual power plant in the electricity, hydrogen, and ammonia markets

    Wu S, Lin J, Li J, et al. Multi-timescale trading strategy for renewable power to ammonia virtual power plant in the electricity, hydrogen, and ammonia markets. IEEE Transactions o n Energy Markets, Policy and Regulation, 2023, 1(4): 322-335

  40. [40]

    Optimal sizing of isolated renewable power systems with ammonia synthesis: Model and solution approach

    Yu Z, Lin J, Liu F, et al. Optimal sizing of isolated renewable power systems with ammonia synthesis: Model and solution approach. IEEE Transactions on Power Systems, 2024, 39(5): 6372-6385

  41. [41]

    Optimal sc heduling for wind-powered ammo nia generation: Effects of key design parameters

    Allman A, Daoutidis P. Optimal sc heduling for wind-powered ammo nia generation: Effects of key design parameters. Chemical Engineering Research and Design, 2018, 131: 5-15

  42. [42]

    Optimal dispatching of integrated en ergy system with hydrogen-to-ammonia and ammonia- mixed/oxygen-enriched thermal power

    Li W, Liu W, Lin Y , et al. Optimal dispatching of integrated en ergy system with hydrogen-to-ammonia and ammonia- mixed/oxygen-enriched thermal power. Energy, 2025, 316: 134514

  43. [43]

    A dispatchable region-guided adaptive mode-switching regulation for renewable power to ammonia virtual power plants

    Wu S, Li J, Lin J, et al. A dispatchable region-guided adaptive mode-switching regulation for renewable power to ammonia virtual power plants. IEEE Transactions on Sustainable Energy, 2024, 16(1): 32-44

  44. [44]

    Stochastic scheduling optimizati on of integrated energy system incorporating power and ammonia energy storages for cost-effective and flexible operati on

    Ding J, Wang J, Zhao N, et al. Stochastic scheduling optimizati on of integrated energy system incorporating power and ammonia energy storages for cost-effective and flexible operati on. International Journal of Hydrogen Energy, 2026, 197: 152626

  45. [45]

    A multi-time scale optimal dispatch strategy for green ammonia production using wind-solar hydrogen under renewable energy fluctuations

    Zheng Y , Zhu S, Yang D, et al. A multi-time scale optimal dispatch strategy for green ammonia production using wind-solar hydrogen under renewable energy fluctuations. Energies, 2025, 18(24): 6518

  46. [46]

    Planning of off-grid renewable power to ammonia systems with heterogeneous flexibility: A multistakeholder equilibrium perspective

    Zeng Y , Qiu Y , Zhu J, et al. Planning of off-grid renewable power to ammonia systems with heterogeneous flexibility: A multistakeholder equilibrium perspective. IEEE Transactions on Power Systems, 2025, 40(6): 4984-4999

  47. [47]

    Comparison, operation and cooling design of three general reactor types for Power-to-Ammonia processes

    Rosbo J W, Jensen A D, Jørgensen J B, et al. Comparison, operation and cooling design of three general reactor types for Power-to-Ammonia processes. Chemical Engineering Journal, 2024, 496: 153660

  48. [48]

    Hundred-megawatt molten salt heat s torage system for deep peak shaving of thermal power plant

    Wang H, Li J, Zhu P, et al. Hundred-megawatt molten salt heat s torage system for deep peak shaving of thermal power plant. Energy Storage Science and Technology, 2021, 10(05): 1760-1767

  49. [49]

    Linear programming and network flows

    Bazaraa M S, Jarvis J J, Sherali H D. Linear programming and network flows. John Wiley & Sons, 2011

  50. [50]

    Scheduling multiple industrial electrolyzers in renewable P2H systems: A coordinated active- reactive power management method

    Zeng Y , Qiu Y , Zhu J, et al. Scheduling multiple industrial electrolyzers in renewable P2H systems: A coordinated active- reactive power management method. IEEE Transactions on Sustainable Energy, 2025, 16(1): 201-215

  51. [51]

    Optimal investment portfolio of thyristor-and IGBT-based electrolysis rectifiers in utility-scale renewable P2H systems

    Zeng Y , Qiu Y , Xu L, et al. Optimal investment portfolio of thyristor-and IGBT-based electrolysis rectifiers in utility-scale renewable P2H systems. IEEE Transactions on Sustainable Energy, 2026, 17(2): 740-755

  52. [52]

    Assessing the effect iveness of weighted information gap decision theory integrated with energy management systems for isolated microgri ds

    Nasr M A, Nasr-Azadani E, Nafisi H, et al. Assessing the effect iveness of weighted information gap decision theory integrated with energy management systems for isolated microgri ds. IEEE Transactions on Industrial Informatics, 2020, 16(8): 5286-5299

  53. [53]

    Feasibility analysis of peak shaving for coal-fired units based on molten salt heat storage

    Peng J, Ni Y , Wang Y , et al. Feasibility analysis of peak shaving for coal-fired units based on molten salt heat storage. Thermal Power Generation, 2024, 53(01): 99-106. (in Chinese). 28

  54. [54]

    Heat Transfer[M]

    Zhu T, An Q. Heat Transfer[M]. Beijing: China Architecture & Building Press, 2020

  55. [55]

    Research on Vacuum Plume and Its Effects

    He B, Zhang J, Cai G. Research on Vacuum Plume and Its Effects. Chinese Journal of Aeronautics, 2013, 26(1): 27-36

  56. [56]

    Application of a new high-temper ature insulation material, high-silica fiber, in ammonia synthesis production

    Jiangsu Nantong Glass Factory. Application of a new high-temper ature insulation material, high-silica fiber, in ammonia synthesis production. Shanghai Chemical Industry, 1974(03): 42+3. (in Chinese)

  57. [57]

    Solar Power Tower Design Basis Document, Revision 0

    Zavoico A B. Solar Power Tower Design Basis Document, Revision 0. Albuquerque, NM: Sandia National Laboratories, 2001

  58. [58]

    Alleima® 321 Aerospace: Tube and pipe, seamless

    Alleima. Alleima® 321 Aerospace: Tube and pipe, seamless. https ://www.alleima.com/en/technical-center/material- datasheets/tube-and-pipe-seamless/alleima-321-aerospace/