Effects of Different Initial Conditions on Combustion Process of Ammonium Dinitramide-Based Energetic Propellant in Straight Nozzle

: As a new type of green propellant, ammonium dinitramide (ADN)-based energetic pro-pellants have wide application value and development potential in the field of space propulsion. This paper delves into the intricate impact of varying initial temperatures, pressures, and propellant component ratios on critical parameters, including temperature, combustion rate, and heat release, in the straight nozzle of an ADN-based propellant. The findings indicate that an elevation in both initial temperature and ADN ratio expedites the thermal decomposition rate of ADN, thereby elevating the average temperature in the nozzle. However, the elevation in initial temperature has a negative effect on the overall rise amplitude of average temperature. Furthermore, the initial pressure setting is crucial in determining whether the oxidation reaction of the fuel CH 3 OH occurs in ADN propellants. When the initial pressure is greater than 10 atm, CH 3 OH is completely consumed, and the final average temperature is about 2650 K, which increases by 558.89% compared with that at 1 atm. Our work aims to provide theoretical guidance and practical optimization strategies for enhancing propellant performance and optimizing thruster structure design.


Introduction
In recent years, ammonium dinitramide (ADN)-based liquid propellants have become a substitute for traditional propellants, such as hydrazine and ammonium perchlorate (AP), due to the characteristics of the high energy, green, and low characteristic signal [1,2], which has attracted extensive attention in the field of aerospace propulsion.In 1971, the former Soviet Union successfully synthesized solid ADN [3,4] with its molecular formula (NH 4 N(NO 2 ) 2 ) for the first time, which can be used as a high-energy oxidant in rocket propellants [5][6][7].Owing to the strong water absorption and high solubility characteristics of solid ADN [8], the Swedish Defense Research developed ADN-based liquid propellants [9] at the beginning of the 21st century, which was mainly composed of ADN, fuel, and water.Subsequently, they revealed that ADN-based liquid propellants have better performance when methanol (CH 3 OH) is used as fuel.After that, many researchers carried out a series of experimental and theoretical studies on ADN-based liquid propellants in the form of the ADN-CH 3 OH-H 2 O combination [10][11][12].Lei Li et al. successfully conducted ignition experiments on ADN-based propellant droplets using contact electric heating ignition, investigating the effects of ambient pressure, droplet size, and gas atmosphere [13][14][15] on ignition performance.Yangyang Hou et al. [16] employed non-contact microwave ignition to study the sequential evolution processes of swelling, micro-explosion, and combustion exhibited by ADN-based propellant droplets during microwave loading.Michele Negri et al. [17] utilized pulsed laser irradiation on ADN-based propellant droplets, observing explosive phenomena in the ADN droplets but lacking direct evidence of successful ignition.In another study, Michele Negri et al. [18] reported that ADN-based liquid propellants, upon undergoing vaporization treatment, become more susceptible to successful ignition.Within our research group, Baosheng Du et al. [19] applied high-energy pulsed laser ablation to ADN-based propellant droplets placed within micron-scale pits, achieving an impulse of 9.8 µN•s and a specific impulse of 234.9 s, thereby demonstrating the feasibility of generating micro-thrust through the pulsed laser ablation of micro-droplets.
Simultaneously, significant progress and new breakthroughs have been made in related theoretical modeling efforts.Gustavo F. Velardez et al. [20] performed molecular dynamics calculations on the melting point and liquid properties of ADN.Weihua Zhu et al. [21] employed the density functional theory to conduct a comparative analysis of the electronic structure, absorption spectra, and thermodynamic changes of crystalline AP and ADN, finding that ADN exhibits a greater number of vibrational frequency modes than AP across the low-to-high frequency range and that ADN is more prone to decomposition than AP as temperature increases.The Yusong Yu team from Beijing Jiaotong University [22] investigated the influence of catalyst bed length, diameter, and wall thickness on the thrust performance of ADN thrusters, revealing that wall thickness plays the most crucial role among these factors, with optimal parameters yielding a 5.9% increase in specific impulse.Researchers led by Xiaoqing You at Tsinghua University proposed a detailed reaction mechanism for the combustion process of ADN-based propellants, encompassing 48 species and 242 chemical reactions [23].Subsequently, the team simplified this intricate mechanism (comprising 18 components and 40 reactions) and, based on the simplified model, conducted a study on the catalytic combustion process of ADN-based propellants in space thrusters.They discovered that ADN does not directly react with CH 3 OH; rather, it is the interaction between N-containing small molecules resulting from ADN pyrolysis and C-bearing small molecules produced by the dehydrogenation of CH 3 OH that drives the reaction [24].The team led by Liu Xuhui [25] at the Beijing Institute of Control Engineering employed three-dimensional numerical simulations to investigate the flow and phase change characteristics of the propellant at the microscale of capillaries within the ADNbased micro thruster.In summary, prior research on ADN has primarily focused on its physicochemical properties and combustion behavior.However, the thermal decomposition and combustion mechanisms of ADN-based propellants at the microscale in nozzles remain in the early stages of investigation.Moreover, studies examining the influence of varying initial conditions on the combustion and flow dynamics of ADN-based propellants are scarce.To address these gaps, the present work focuses on gaseous ADN-based propellants, employing a two-dimensional numerical simulation approach utilizing the reactingFoam solver.This study investigates the effects of different initial temperatures, pressures, and component ratios within the propellant on the thermal decomposition and combustion processes in the straight nozzle.The aim is to provide theoretical guidance for enhancing thruster performance and optimizing operating conditions in the thruster design.

Numerical Modeling
In this paper, the two-dimensional transient simulation of the combustion process of a gaseous ADN-based propellant in a straight nozzle is carried out.The nozzle with an ADN-based propellant is shown in Figure 1, with a length of 4 mm, a bottom width of 0.2 mm, and an expansion angle of 0 • .The propellant filling length is 0.2 mm, and the rest of the nozzle is filled with nitrogen.Considering the symmetry of geometry and flow, the upper part is taken for meshing and numerical calculation.
OpenFOAM is a mature CFD calculation software.As an open-source framework, it can successfully calculate the combustion reaction [26][27][28].In this paper, the reactingFoam solver of OpenFOAM (V.6) was used to carry out the numerical simulation of an ADNbased propellant.The relevant mass conservation, momentum conservation, component conservation, and energy conservation equations are shown in Equation ( 1) [29].The control equation is solved by the built-in finite volume method solver, and the pressure implicit operator splitting (PISO) algorithm [30] is used to correct the velocity field using the output of the pressure equation.
where τ ij is the viscous stress tensor; V k,i is the i-component of the diffusion velocity for the kth component; Y k is the mass fraction of the kth component; . ω k is the reaction rate of the kth component; . ω T is the heat release rate of the combustion process; q i is the heat flux, including the thermal diffusion term caused by the temperature gradient and the thermal diffusion term caused by the diffusion of components with different specific enthalpies; and σ ij is the deviatoric stress tensor [31].OpenFOAM is a mature CFD calculation software.As an open-source can successfully calculate the combustion reaction [26][27][28].In this paper, the r solver of OpenFOAM (V.6) was used to carry out the numerical simulation based propellant.The relevant mass conservation, momentum conservation conservation, and energy conservation equations are shown in Equation (1) trol equation is solved by the built-in finite volume method solver, and the plicit operator splitting (PISO) algorithm [30] is used to correct the velocity fi output of the pressure equation.
where ij τ is the viscous stress tensor; ,  The gaseous ADN-based propellant mainly involved an ADN decomposition reaction and a CH 3 OH oxidation reaction.In this paper, the simplified reaction mechanism in reference [24] is used for the calculation.The working conditions involved in the ADNbased propellant on the left side of the nozzle in the study are shown in Table 1.Case 1 is the control group; the control variable of cases 1-3 is the initial temperature T 0 ; the control variable of cases 1, 4, 5, and 6 is the initial pressure p 0 ; and the control variable of cases 1, 7, 8, and 9 is the initial component ratio of propellant: Y ADN :Y CH3OH :Y H2O .For the remaining part of the nozzle, the initial temperature is uniformly set at 300 K, and the initial pressure is maintained at 1 atm.In computational geometry, the symmetrical boundary condition is used at the axis of symmetry, the zero gradient boundary condition is used at the outlet, and the other boundaries are set as no-slip walls.In order to ensure the accuracy of the calculation results and improve the calculation efficiency, the grid independence test is carried out in case 1.The number of grids is 200 × 5, 400 × 10, and 600 × 15, respectively (corresponding to the X and Y directions, structured grid).The distribution of ADN mass fraction and X-direction velocity on the central axis at 5 ms is surveyed.The results are shown in Figure 2, and the corresponding maximum values of ADN mass fraction and X-direction velocity are shown in Table 2.It was found that the calculation results of the 200 × 5 grid are different from those of the latter two grids, while the calculation results of the 400 × 10 grid and 600 × 15 grid are consistent, indicating that few grid numbers can cause the loss of effective information.At the same time, considering the calculation efficiency, the calculation time of the 400 × 10 grid is faster than that of the 600 × 15 grid, so the 400 × 10 grid distribution is adopted for all subsequent calculations.In order to ensure the accuracy of the calculation and minimize the diffusion caused by time discretization, the initial time step is set to 1 × 10 −11 s, the maximum Courant-Friedrichs-Lewy (CFL) number is set to 0.2, and the maximum time step is set to 1 × 10 −6 s. case 1.The number of grids is 200 × 5, 400 × 10, and 600 × 15, respectively (corresponding to the X and Y directions, structured grid).The distribution of ADN mass fraction and Xdirection velocity on the central axis at 5 ms is surveyed.The results are shown in Figure 2, and the corresponding maximum values of ADN mass fraction and X-direction velocity are shown in Table 2.It was found that the calculation results of the 200 × 5 grid are different from those of the latter two grids, while the calculation results of the 400 × 10 grid and 600 × 15 grid are consistent, indicating that few grid numbers can cause the loss of effective information.At the same time, considering the calculation efficiency, the calculation time of the 400 × 10 grid is faster than that of the 600 × 15 grid, so the 400 × 10 grid distribution is adopted for all subsequent calculations.In order to ensure the accuracy of the calculation and minimize the diffusion caused by time discretization, the initial time step is set to 1 × 10 −11 s, the maximum Courant-Friedrichs-Lewy (CFL) number is set to 0.2, and the maximum time step is set to 1 × 10 −6 s.

Analysis of the Combustion Process of a Gaseous ADN-Based Propellant
The evolution process of the combustion and flow of a gaseous ADN-based propellant in the nozzle in case 1 is analyzed.The distribution of the reactant ADN mass fraction, intermediate product N2O mass fraction, temperature, and velocity is shown in Figure 3.In general, the chromaticity bar of the ADN mass fraction (YADN) exhibited a color transition from dark cyan → orange → blue over time, indicating that the combustion pyrolysis reaction of reactant ADN occurred and content continued to decrease.Correspondingly, the mass fraction of the intermediate product N2O (YN2O) produced from the combustion pyrolysis reaction of ADN experienced a change from blue → dark red → cyan, respectively, representing the stages of N2O formation → increase → diffusion.In addition, the

Analysis of the Combustion Process of a Gaseous ADN-Based Propellant
The evolution process of the combustion and flow of a gaseous ADN-based propellant in the nozzle in case 1 is analyzed.The distribution of the reactant ADN mass fraction, intermediate product N 2 O mass fraction, temperature, and velocity is shown in Figure 3.In general, the chromaticity bar of the ADN mass fraction (Y ADN ) exhibited a color transition from dark cyan → orange → blue over time, indicating that the combustion pyrolysis reaction of reactant ADN occurred and content continued to decrease.Correspondingly, the mass fraction of the intermediate product N 2 O (Y N2O ) produced from the combustion pyrolysis reaction of ADN experienced a change from blue → dark red → cyan, respectively, representing the stages of N 2 O formation → increase → diffusion.In addition, the content of ADN in the nozzle showed an uneven distribution of high in the middle and low on both sides, indicating that, compared with the middle position of the nozzle, the closer to the bottom wall of the nozzle, the faster the reaction of ADN, and the less the residual content.The decrease in ADN away from the wall was due to the concentration difference between the right side of ADN and the ambient gas, which led to the right diffusion of ADN.Compared with the reactant ADN, the product N 2 O had a higher content near the bottom wall and a lower content far away from the bottom wall.
closer to the bottom wall of the nozzle, the faster the reaction of ADN, and the less residual content.The decrease in ADN away from the wall was due to the concentrat difference between the right side of ADN and the ambient gas, which led to the right d fusion of ADN.Compared with the reactant ADN, the product N2O had a higher cont near the bottom wall and a lower content far away from the bottom wall.The temperature in the nozzle rose rapidly due to the occurrence of the ADN pyr ysis reaction, and the temperature rise range reached 200 K in 0-0.5 ms.Under the c vection and diffusion caused by the temperature difference and concentration differen a large velocity was generated on the right side of ADN at 0.5 ms; the velocity inside reactant was low due to the limitation of the left wall; and a region with virtually z velocity appeared near the interface between high and low temperatures.Due to the fluence of wall viscosity, the closer the position was to the central axis, the higher the locity was, which led to the uneven distribution of ADN.The movement speed of ADN the upper wall was slower than that at the central axis.In contrast, due to the low veloc near the bottom wall, no similar uneven distribution of N2O could be observed from figure.Over time, the components diffused to the right, and the high temperature-l temperature interface moved to the right, but the movement speed gradually decreas After 5 ms, the maximum temperature was lower than the initial temperature (718 K). the one hand, the temperature was reduced due to convection and component diffusi On the other hand, the combustion pyrolysis reaction was slowed down and no more h was generated.At 10 ms, ADN was almost completely consumed, indicating that the p rolysis reaction of ADN almost stopped.However, because the local temperature was high enough, N2O could not react further and, hence, still maintained a high concent tion.The temperature in the nozzle rose rapidly due to the occurrence of the ADN pyrolysis reaction, and the temperature rise range reached 200 K in 0-0.5 ms.Under the convection and diffusion caused by the temperature difference and concentration difference, a large velocity was generated on the right side of ADN at 0.5 ms; the velocity inside the reactant was low due to the limitation of the left wall; and a region with virtually zero velocity appeared near the interface between high and low temperatures.Due to the influence of wall viscosity, the closer the position was to the central axis, the higher the velocity was, which led to the uneven distribution of ADN.The movement speed of ADN at the upper wall was slower than that at the central axis.In contrast, due to the low velocity near the bottom wall, no similar uneven distribution of N 2 O could be observed from the figure.Over time, the components diffused to the right, and the high temperature-low temperature interface moved to the right, but the movement speed gradually decreased.After 5 ms, the maximum temperature was lower than the initial temperature (718 K).On the one hand, the temperature was reduced due to convection and component diffusion.On the other hand, the combustion pyrolysis reaction was slowed down and no more heat was generated.At 10 ms, ADN was almost completely consumed, indicating that the pyrolysis reaction of ADN almost stopped.However, because the local temperature was not high enough, N 2 O could not react further and, hence, still maintained a high concentration.

Effects of Different Initial Temperatures on the Combustion Process of an ADN-Based Propellant
Figure 4 shows the variation of average temperature, total mass of five components (ADN, N 2 O, HNO 3 , NH 3 , and CH 3 OH), and average heat release rate in the straight nozzle with time in case 1.As shown in Figure 4, the average heat release first increased within 0-2 ms, reached its peak at 0.1 ms, then rapidly decreased and approached 0. Correspond-ingly, the average temperature inside the nozzle first rose rapidly and then tended to flatten, rising from 323 K to 406 K.By analyzing the total mass curves of the five components, it can be seen that the total mass of ADN decreased rapidly from time 0, and the total mass of the ADN pyrolysis products, N 2 O, HNO 3 , and NH 3 , increased continuously before 0.25 ms, resulting in a rapid rise in the temperature inside the nozzle.After 0.25 ms, the mass of NH 3 began to decrease slowly, and HNO 3 decreased faster.This is because HNO 3 continued to decompose to produce N 2 O.Under the combined influence of ADN pyrolysis and HNO 3 decomposition, N 2 O kept an upward trend after 0.25 ms, but, due to the rapid reduction in ADN content, the upward trend of N 2 O also gradually slowed down.It is worth mentioning that, as one of the main components of propellants, the total mass of CH 3 OH had remained unchanged, indicating that its oxidation reaction did not start, which can be attributed to the CH 3 OH aggregation region not reaching its reaction temperature.
(ADN, N2O, HNO3, NH3, and CH3OH), and average heat release rate in the straight no with time in case 1.As shown in Figure 4, the average heat release first increased wi 0-2 ms, reached its peak at 0.1 ms, then rapidly decreased and approached 0. Correspo ingly, the average temperature inside the nozzle first rose rapidly and then tended to ten, rising from 323 K to 406 K.By analyzing the total mass curves of the five compone it can be seen that the total mass of ADN decreased rapidly from time 0, and the total m of the ADN pyrolysis products, N2O, HNO3, and NH3, increased continuously before ms, resulting in a rapid rise in the temperature inside the nozzle.After 0.25 ms, the m of NH3 began to decrease slowly, and HNO3 decreased faster.This is because HNO3 tinued to decompose to produce N2O.Under the combined influence of ADN pyro and HNO3 decomposition, N2O kept an upward trend after 0.25 ms, but, due to the r reduction in ADN content, the upward trend of N2O also gradually slowed down.worth mentioning that, as one of the main components of propellants, the total mas CH3OH had remained unchanged, indicating that its oxidation reaction did not s which can be attributed to the CH3OH aggregation region not reaching its reaction t perature.Figure 5 shows the velocity distribution in the x-direction along the central ax different times.Before 0.3 ms, the velocity exhibited a profile of initially increasing then decreasing along the x-direction.Under the action of the temperature gradient maximum velocity of 1.24 m/s appeared at x = 0.42 mm, i.e., in front of the ADN-ba propellant at 0.05 ms.With the pyrolysis of ADN, the temperature in this area increa and, hence, the flow velocity also gradually increased.At 0.1 ms, the peak velocity of m/s appeared at x = 0.535 mm, and the peak moving velocity was 2.3 m/s.Then, the p velocity continued to decrease, and the position of peak velocity also continued to m forward, but the moving velocity continued to decrease.After 0.3 ms, the velocity sented an "S" shape distribution along the x-direction.By investigating the density di bution at 0.3 ms, it can be concluded that the negative velocity near the bottom wall due to the negative flow caused by the density difference.Figure 5 shows the velocity distribution in the x-direction along central axis at different times.Before 0.3 ms, the velocity exhibited a profile of initially increasing and then decreasing along the x-direction.Under the action of the temperature gradient, the maximum velocity of 1.24 m/s appeared at x = 0.42 mm, i.e., in front of the ADN-based propellant at 0.05 ms.With the pyrolysis of ADN, the temperature in this area increased, and, hence, the flow velocity also gradually increased.At 0.1 ms, the peak velocity of 1.43 m/s appeared at x = 0.535 mm, and the peak moving velocity was 2.3 m/s.Then, the peak velocity continued to decrease, and the position of peak velocity also continued to move forward, but the moving velocity continued to decrease.After 0.3 ms, the velocity presented an "S" shape distribution along the x-direction.By investigating the density distribution at 0.3 ms, it can be concluded that the negative velocity near the bottom wall was due to the negative flow caused by the density difference.Figure 6 shows the evolution of the influence of different initial temperatures (case 1/2/3) on the average temperature in the nozzle and the total mass of ADN.In the range of 0-0.3 ms, with the increase in initial temperature, the consumption rate of ADN in creased, and the heat release increased, which accelerated the rise rate of the average tem perature in the nozzle.After 0.5 ms, the average temperature of case 3 (the initial temper ature was 863 K) gradually stabilized, and the temperature in the nozzle gradually began to decrease after 1.5 ms.This is because the initial temperature of case 3 was higher than that of cases 1 and 2, which made ADN reach the average temperature peak in a shorte time.However, due to the lack of subsequent CH3OH participation in the reaction and the continuous outflow of substances in the nozzle, the average temperature in the nozzle decreased.Although the higher the initial temperature of the propellant the faster i reached the average temperature peak, the increase in average temperature became les due to the reduction in initial ADN mass, which in turn led to the reduction in heat release Specifically, the average temperature increments corresponding to the initial tempera tures of 718 K, 773 K, and 863 K are 86.38 K, 82.60 K, and 76.97 K, respectively, with in creases of 26.92%, 25.52%, and 23.46%.Figure 6 shows the evolution of the influence of different initial temperatures (cases 1/2/3) on the average temperature in the nozzle and the total mass of ADN.In the range of 0-0.3 ms, with the increase in initial temperature, the consumption rate of ADN increased, and the heat release increased, which accelerated the rise rate of the average temperature in the nozzle.After 0.5 ms, the average temperature of case 3 (the initial temperature was 863 K) gradually stabilized, and the temperature in the nozzle gradually began to decrease after 1.5 ms.This is because the initial temperature of case 3 was higher than that of cases 1 and 2, which made ADN reach the average temperature peak in a shorter time.However, due to the lack of subsequent CH 3 OH participation in the reaction and the continuous outflow of substances in the nozzle, the average temperature in the nozzle decreased.Although the higher the initial temperature of the propellant the faster it reached the average temperature peak, the increase in average temperature became less due to the reduction in initial ADN mass, which in turn led to the reduction in heat release.Specifically, the average temperature increments corresponding to the initial temperatures of 718 K, 773 K, and 863 K are 86.38 K, 82.60 K, and 76.97 K, respectively, with increases of 26.92%, 25.52%, and 23.46%.Figure 6 shows the evolution of the influence of different initial temperatures (cases 1/2/3) on the average temperature in the nozzle and the total mass of ADN.In the range of 0-0.3 ms, with the increase in initial temperature, the consumption rate of ADN increased, and the heat release increased, which accelerated the rise rate of the average temperature in the nozzle.After 0.5 ms, the average temperature of case 3 (the initial temperature was 863 K) gradually stabilized, and the temperature in the nozzle gradually began to decrease after 1.5 ms.This is because the initial temperature of case 3 was higher than that of cases 1 and 2, which made ADN reach the average temperature peak in a shorter time.However, due to the lack of subsequent CH3OH participation in the reaction and the continuous outflow of substances in the nozzle, the average temperature in the nozzle decreased.Although the higher the initial temperature of the propellant the faster it reached the average temperature peak, the increase in average temperature became less due to the reduction in initial ADN mass, which in turn led to the reduction in heat release.Specifically, the average temperature increments corresponding to the initial temperatures of 718 K, 773 K, and 863 K are 86.38 K, 82.60 K, and 76.97 K, respectively, with increases of 26.92%, 25.52%, and 23.46%.

Effects of Different Initial Pressures on the Combustion Process of an ADN-Based Propellant
Figure 7 shows the temporal evolution of average temperatures and average pressures in the nozzle at different initial pressures (cases 1/4/5/6).It can be seen from the figure that, when the initial pressure was 1 atm (case 1), because only the ADN pyrolysis reaction took effect and CH 3 OH did not participate in the subsequent reaction, the average temperature and average pressure increased only slightly before 0.5 ms, and then remained basically unchanged.At 10 ms, the average temperature and average pressure in the nozzle were 403.66K and 1.20 atm, respectively.When the initial pressure rose to 5 atm (case 4), according to the ideal gas equation, because the initial ADN concentration increased by 4 times and the heat released by the pyrolysis reaction also increased, the final average temperature was higher than that of the initial pressure 1 atm.The average temperature in the nozzle was 1166.64K at 10 ms.The average pressure decreased rapidly before 0.5 ms, which was due to pressure conduction from the high pressure zone to the low pressure zone, and, finally, the pressure was released at the nozzle outlet.After 0.5 ms, the average pressure gradually increased due to the heat release of the pyrolysis reaction of ADN.As observed in the temperature-pressure curve, there was no intense oxidation reaction of CH 3 OH at the initial pressure of 5 atm.When the initial pressure was increased to 10 atm (case 5), an obvious three-stage heat release could be observed.The variations in average temperature, average heat release rate, and total mass of ADN/N 2 O/HNO 3 /NH 3 /CH 3 OH/CO/CO 2 with time at the initial pressure is shown in Figure 8.The first stage occurred from 0 to 0.3 ms, during which the partial pyrolysis reaction of ADN took place, resulting in a slight increase in the average temperature inside the nozzle, which then stabilized at around 500 K.The second stage spanned from 1 to 3 ms, during which extensive decomposition of ADN occurred, yielding thermal decomposition products such as N 2 O, HNO 3 , and NH 3 .The average temperature rose to approximately 1300 K, remaining relatively constant from 3 to 7.5 ms.However, during this period, the total mass of CH 3 OH decreased steadily at a stable rate, indicating oxidation and dehydrogenation reactions with relatively low heat release, as inferred from the average heat release rate.The third exothermic stage spanned from 7.5 to 8.6 ms, during which other nitrogen-containing small molecules, like N 2 O, were extensively consumed, while CO 2 was generated in large quantities through the oxidation of CO.Although CO 2 was derived from CO oxidation, the total mass of CO remained relatively low throughout, suggesting rapid consumption upon generation, thus maintaining a low concentration.The average temperature ultimately rose to around 2650 K, with an increase of 558.89% compared to 1 atm.There was a noticeable decrease in average pressure before 1 ms due to the pressure release through conduction, followed by two distinct increases, corresponding to the rise in average temperature.Overall, the consumption of nitrogenous small molecules and the oxidation of CO contributed significantly to the high average heat release rate, playing a crucial role in the elevation of average temperature.It was noteworthy that, when the initial pressure was increased to 20 atm, compared to 10 atm, the secondary heating and pressurization processes occurred later at 7.5 ms and 9 ms, respectively.Although there was no difference in the temperature achieved at each stage, the initial pressure impacted the heat release of the reactions to some extent.This indicated that a higher initial pressure was not necessarily advantageous.When the initial pressure was excessively high, pressure transmission and release at the initial moment led to a lower mean pressure, thereby slowing down the progression of the reaction.
Figure 9 shows the temporal evolution of the total mass of ADN and CH 3 OH at different initial pressures.With the increase in initial pressure, the initial total mass of ADN and CH 3 OH also increased accordingly.Although high pressure was conducive to the reaction near t = 0, the rapid release of high initial pressure created a low-pressure environment in the nozzle, which would slow down the reaction rate after the low-pressure environment was generated.Therefore, the consumption rate of ADN and CH 3 OH did not increase proportionally with the increase in initial pressure.When the initial pressure was 1 atm, the time for ADN to decompose completely was 0.5 ms; when the initial pressure was 5 atm, the time for ADN to decompose completely was 4.5 ms; and when the initial pressure was 10 atm, the time for ADN to decompose completely was 2.5 ms, which was nearly twice as fast as 5 atm.At an initial pressure of 20 atm, the time for ADN to decompose completely was similar to that at 5 atm.Among the four cases mentioned above, only when the initial pressure was 10 atm or 20 atm, CH 3 OH was completely consumed, while at 5 atm, it was partially consumed.Based on the changes in average temperature at different initial pressures mentioned earlier, it can be speculated that CH 3 OH did not undergo a drastic oxidation reaction due to insufficient temperatures or reaction times.Figure 9 shows the temporal evolution of the total mass of ADN and CH ferent initial pressures.With the increase in initial pressure, the initial total ma  Figure 9 shows the temporal evolution of the total mass of ADN and CH ferent initial pressures.With the increase in initial pressure, the initial total m and CH3OH also increased accordingly.Although high pressure was conduciv

Effects of Different Initial Component Ratios on the Combustion Process of an ADN-Based Propellant
Figure 10 shows the changes in average temperature and total mass of ADN over time for different initial component ratios (cases 1/7/8/9), where the proportion of H2O remained constant and only the proportions of ADN and CH3OH were altered.It can be observed from the figure that, as the proportion of ADN increased, its total mass also increased, the consumption rate was faster, and the rate of increase in average temperature was also faster.The final stable temperature reached was higher as well.At 2.5 ms, the average temperatures corresponding to ADN proportions of 44.20%, 52.81%, 61.43%, and 73.67% in the propellant were 359.83K, 380.71 K, 406.92 K, and 456.48 K, respectively, with increases of 12.13%, 18.64%, 26.81%, and 42.25%.Inspection of the average temperature curve revealed that, regardless of whether ADN proportion was high or low, no intense oxidation of CH3OH occurred.Consequently, there was no secondary rise in temperature.

Effects of Different Initial Component Ratios on the Combustion Process of an ADN-Based Propellant
Figure 10 shows the changes in average temperature and total mass of ADN over time for different initial component ratios (cases 1/7/8/9), where the proportion of H 2 O remained constant and only the proportions of ADN and CH 3 OH were altered.It can be observed from the figure that, as the proportion of ADN increased, its total mass also increased, the consumption rate was faster, and the rate of increase in average temperature was also faster.The final stable temperature reached was higher as well.At 2.5 ms, the average temperatures corresponding to ADN proportions of 44.20%, 52.81%, 61.43%, and 73.67% in the propellant were 359.83K, 380.71 K, 406.92 K, and 456.48 K, respectively, with increases of 12.13%, 18.64%, 26.81%, and 42.25%.Inspection of the average temperature curve revealed that, regardless of whether ADN proportion was high or low, no intense oxidation of CH 3 OH occurred.Consequently, there was no secondary rise in temperature.

Effects of Different Initial Component Ratios on the Combustion Process of an ADN-Based Propellant
Figure 10 shows the changes in average temperature and total mass of ADN time for different initial component ratios (cases 1/7/8/9), where the proportion of remained constant and only the proportions of ADN and CH3OH were altered.It ca observed from the figure that, as the proportion of ADN increased, its total mass also creased, the consumption rate was faster, and the rate of increase in average tempera was also faster.The final stable temperature reached was higher as well.At 2.5 ms average temperatures corresponding to ADN proportions of 44.20%, 52.81%, 61.43%, 73.67% in the propellant were 359.83K, 380.71 K, 406.92 K, and 456.48 K, respectively, w increases of 12.13%, 18.64%, 26.81%, and 42.25%.Inspection of the average tempera curve revealed that, regardless of whether ADN proportion was high or low, no int oxidation of CH3OH occurred.Consequently, there was no secondary rise in temperat

Conclusions
In this paper, the combustion of gaseous ADN-based propellants in the nozzle at different initial temperatures, pressures, and propellant ratios was compared and analyzed.In all cases, ADN first decomposed and released heat to generate small nitrogen-containing molecules, such as N 2 O and NH 3 .In this process, the average temperature and pressure rose, and the flow in the nozzle accelerated.Through the comparison of different initial conditions, the main conclusions were as follows: 1.
Both the increase in initial temperature and the increase in the ADN component ratio had a positive effect on the pyrolysis of ADN, which led to the increase in average temperature in the nozzle, but the elevation in initial temperature had a negative effect on the overall rise amplitude of average temperature.

2.
The initial pressure of propellant was an important factor affecting whether CH 3 OH reacted.When the initial pressure was 1 atm, CH 3 OH did not react.When the initial pressure was 5 atm, part of CH 3 OH reacted, but there was no intense oxidation or heat release.When the initial pressure was 10 atm and 20 atm, CH 3 OH reacted violently, producing CO 2 with a large amount of heat release, resulting in an average temperature of approximately 2650 K, which increased by 558.89% compared with that at 1 atm.

3.
In the cases of this study, setting a higher initial pressure of the propellant did not necessarily result in faster reaction rates of ADN and CH 3 OH.In the cases where CH 3 OH was completely consumed, the reaction time at an initial pressure of 10 atm was shorter than at 20 atm.For situations with higher pressures, the influence of shock waves needs to be taken into consideration.

erospace 2024 ,Figure 1 .
Figure 1.Geometric model of the straight nozzle with an ammonium dinitramide (A propellant.

Figure 1 .
Figure 1.Geometric model of the straight nozzle with an ammonium dinitramide (ADN)-based propellant.

Figure 3 .
Figure 3. Distribution of the ADN mass fraction, N2O mass fraction, temperature, and velocity m nitude at different times.

Figure 3 .
Figure 3. Distribution of the ADN mass fraction, N 2 O mass fraction, temperature, and velocity magnitude at different times.

Figure 4 .
Figure 4. Time-varying curves of average temperature, total mass of ADN/N2O/HNO3/NH3/CH and average heat release rate in case 1.

Figure 4 .
Figure 4. Time-varying curves of average temperature, total mass of ADN/N 2 O/HNO 3 /NH 3 /CH 3 OH, and average heat release rate in case 1.

Aerospace 2024 , 1 Figure 5 .
Figure 5. Velocity distribution in the x-direction along the central axis and density distribution a 0.3 ms.

Figure 6 .
Figure 6.Temporal evolution of average temperatures and the total mass of ADN at different initia propellant temperatures.

Figure 5 .
Figure 5. Velocity distribution in the x-direction along the central axis and density distribution at 0.3 ms.

Aerospace 2024 , 12 Figure 5 .
Figure 5. Velocity distribution in the x-direction along the central axis and density distribution at 0.3 ms.

Figure 6 .
Figure 6.Temporal evolution of average temperatures and the total mass of ADN at different initial propellant temperatures.

Figure 6 .
Figure 6.Temporal evolution of average temperatures and the total mass of ADN at different initial propellant temperatures.

Aerospace 2024 ,Figure 7 .
Figure 7. Temporal evolution of average temperatures and average pressures at differen pellant pressures.

Figure 7 .Figure 7 .
Figure 7. Temporal evolution of average temperatures and average pressures at different initial propellant pressures.

Figure 8 .
Figure 8. Time-varying curves of average temperatures, average heat release rates, and the total mass of ADN/N 2 O/HNO 3 /NH 3 /CH 3 OH/CO/CO 2 at the initial propellant pressure of 10 atm.

Figure 9 .
Figure 9. Temporal evolution of the total mass of ADN and CH3OH at different initial propellant pressures.

Figure 10 .
Figure 10.Temporal evolution of average temperatures and total ADN mass at different initial propellant ratios.

Figure 9 .
Figure 9. Temporal evolution of the total mass of ADN and CH 3 OH at different initial pressures.

Figure 9 .
Figure 9. Temporal evolution of the total mass of ADN and CH3OH at different initial prope pressures.

Figure 10 .
Figure 10.Temporal evolution of average temperatures and total ADN mass at different initial pellant ratios.

Figure 10 .
Figure 10.Temporal evolution of average temperatures and total ADN mass at different initial propellant ratios.

Table 2 .
Maximum values of ADN mass fraction and axial velocity.

Table 2 .
Maximum values of ADN mass fraction and axial velocity.