This section presents a comprehensive analysis of the optimization outcomes and their subsequent validation. It begins by detailing the specific parameter optimization results achieved through the genetic algorithm, followed by the design of a comparative scheme to benchmark and verify the simulation data experimentally. Additionally, detailed simulation results regarding flow, pressure, concentration, and temperature fields are analyzed, culminating in a comprehensive performance index comparison.
4.2. Comparative Scheme Design
To verify the authenticity and reliability of the relevant simulation data of the combustion chamber, a micro turbojet engine test bench (as shown in
Figure 7) was built to carry out the actual measurement and verification of the outlet thermodynamic parameters of the combustion chamber matched with the optimized evaporator tube. The test adopted a high-precision pressure sensor (measurement range 0–500 kPa, accuracy ± 0.5% FS) and a thermocouple temperature sensor (measurement range 0–1200 °C, accuracy ± 1 °C). Under the rated working conditions of the engine (inlet air temperature 300 K, pressure 300 kPa, flow velocity 250 m/s, fuel flow rate 0.02 kg/s), the combustion chamber outlet pressure and temperature were tested repeatedly for many times. To properly quantify the variability of the measurements and ensure statistical rigor, standard deviations were calculated for all experimental readings.
The comparative data show (as shown in
Figure 8) that the simulation result of the combustion chamber outlet pressure is 192 kPa, the experimental result is 187 kPa (standard deviation
1.5 kPa), and the relative error is only 2.67%; the simulation result of the outlet temperature is 1098.26 °C, the experimental result is 1015.87 °C (standard deviation
5.2 °C), and the relative error between the corrected experimental result and the simulation value is 8.11%. The errors of the two key thermodynamic parameters are both controlled within the 10% error threshold, and the consistency of the pressure parameter is particularly prominent. This result shows that the CFD numerical simulation model adopted in this paper (including the RNG k-ε turbulence model, Lagrangian framework discrete phase model and PDF combustion model) can accurately capture the coupling process of flow, atomization and combustion inside the combustion chamber, and the simulation data has high credibility, providing a reliable numerical support for the structural optimization design of the evaporator tube.
To comprehensively verify the effectiveness of the multi-objective optimization scheme based on the genetic algorithm, in addition to the benchmark scheme of traditional empirical design, three additional groups of representative traditional single-objective design schemes (focusing on atomization effect, combustion efficiency and structural reliability, respectively) were selected as comparison objects to conduct multi-dimensional performance benchmarking with the genetic algorithm optimized structure, and the results are shown in
Table 1. Through the cross-comparison and visual analysis of multiple groups of schemes, it not only avoids the contingency of single benchmark comparison but also intuitively highlights the core advantage of the genetic algorithm in balancing multi-objective conflicts and achieving the optimal comprehensive performance.
The comprehensive performance score is calculated by weighting the normalized objective functions (the weights are the same as in
Section 2.4: atomization particle size 0.35, combustion efficiency 0.4, wall temperature 0.25). A higher score indicates better comprehensive performance, with a full score of 1.0.
It can be clearly seen from the multiple groups of comparative charts that the traditional single-objective design schemes generally have the performance shortcoming of “trading off one for another”, while the genetic algorithm optimization scheme realizes the coordinated improvement of the three core indicators through the global optimal matching of design variables.
The evaporation tubes of the 5 design schemes are shown in
Figure 9 and
Figure 10. For the convenience of calculation, an eighth of the model was taken for the simulation experiment, as shown in
Figure 11, where the x-plane is the evaporator tube section, the y-plane is the fuel hole section, the a-plane is the main combustion zone section, the b-plane is the secondary combustion zone section, and the c-plane is the auxiliary combustion zone section.
4.3. Simulation Result Analysis
The flow field visualization cloud map is the core means to reveal the internal flow-combustion-heat transfer coupling mechanism of the micro turbojet combustion chamber. Based on the CFD numerical simulation results, combined with the theories of fluid mechanics and combustion, this paper systematically analyzes the distribution law, physical essence, and engineering significance of the velocity, pressure, concentration, and temperature cloud maps, providing theoretical and data support for the effectiveness of the evaporator tube structural optimization.
4.3.1. Analysis of Static Temperature, Velocity, and Pressure Field
Combined with the color gradient and flow field structural characteristics of the static temperature, velocity, and pressure cloud maps of Schemes 1–5 arranged longitudinally in
Figure 12 and
Figure 13, the analysis is carried out through multi-dimensional quantitative comparison and flow mechanism.
From the gradient change in the longitudinal velocity cloud map, the core flow field characteristics of the 5 groups of schemes show an evolutionary trend of high-velocity zone contraction and focusing, and low-velocity zone boundary regularization. The high-velocity zone (200~280 m/s) of Scheme 1 is distributed in a “diffuse” shape; the beam shape from the evaporator tube outlet to the core flow channel of the main combustion zone is not obvious, and the high-velocity flow core diffuses to the wall, resulting in an excessively short distance from the wall cavity. The low-velocity recirculation zone ( m/s) has an excessively large range, and the tail recirculation zone is interconnected with the cavity recirculation zone, forming a local eddy dead zone. It can be judged from the continuity of the dark red tone in the cloud map that the Reynolds stress is prone to local surge here, and the aerodynamic loss is relatively high. The high-velocity flow core of Scheme 2 begins to shrink, but the focusing effect is insufficient, and the range of the core velocity interval with cyan-green tone is still wide, and the symmetry of the swirling flow shape is poor. The wall cavity recirculation zone is reduced, but the “tail” phenomenon still exists in the tail recirculation zone, the residence time shows local unevenness, and the residence time in some areas ms, which is difficult to fully meet the flame stabilization requirements. The focusing effect of the high-velocity flow core of Scheme 3 is significantly improved, but the upper limit of the high-velocity zone (about 260 m/s) does not reach the design peak, and the kinetic energy foundation of “air vortex wrapping liquid” is insufficient. The boundary of the low-velocity recirculation zone tends to be clear, but the closure of the cavity recirculation zone is general, and there is slight fragmentation at the shear interface between the cavity recirculation zone and the high-velocity flow in the main combustion zone. Irregular variegated colors appear in the color transition zone of the cloud map, indicating a high turbulent pulsation intensity. The shape and velocity interval of the high-velocity flow core of Scheme 4 are close to the design target, but the residence time distribution of the low-velocity recirculation zone is uneven, ms at the cavity, and drops to 8 ms at the tail area, resulting in local “insufficient residence”, and the Reynolds stress at the shear interface is close to the critical value of 500 m2/s2, and the aerodynamic loss control is in a critical state.
The velocity cloud map of Scheme 5 presents extreme structural regularity and quantitative adaptability: the high-velocity zone is presented in a pure cyan-green tone, strictly focused on the core flow channel of the main combustion zone without any wall diffusion, and the flow velocity is accurately and stably in the peak interval of 240~280 m/s, providing the maximum kinetic energy for the “air vortex wrapping liquid” effect. The boundary of the low-velocity recirculation zone is a perfect closed ring, and the cavity and tail recirculation zones are completely independent with accurate ranges. Calculated from the cloud map size and flow velocity, the global residence time is stably at 12~15 ms without local insufficiency or overlong phenomenon. At the same time, the color transition of the medium-velocity shear zone is smooth without variegated colors, and combined with the Reynolds stress monitoring ( m2/s2), the aerodynamic loss is further reduced by 20% compared with Scheme 4, realizing the optimal dynamic balance between high-velocity swirling flow and low-velocity recirculation flow.
The color gradient evolution of the pressure cloud map mainly reflects the optimization of the matching degree between the low-pressure core zone and the wall high-pressure zone. The low-pressure core zone of Scheme 1 is “flat”, with a spatial coincidence degree of only about 70% with the high-velocity flow core, and an excessively large radial pressure gradient, leading to unstable swirling flow intensity, and the swirl number S fluctuates between 0.45 and 0.55, failing to enter the optimal mixing interval. The wall high-pressure zone is unevenly distributed, and local high-pressure peaks appear outside the cavity, with the reddish-brown tone of the cloud map concentrated in dots, which is easy to cause excessive local load on the wall. The coincidence degree between the low-pressure core zone and the high-velocity flow core of Scheme 2 is increased to 85%, but the axial pressure gradient changes steeply, the characteristic of “slow rise” of pressure from the main combustion zone to the tail is missing, and the pressure driving force of the tail recirculation zone is insufficient, resulting in weak recirculation intensity. The axial distribution of the pressure gradient of Scheme 3 tends to be gentle, but the radial pressure gradient is still small, and the swirl number S is stable at 0.52, close to the lower limit of the optimal interval, the swirling flow driving force for oil–gas mixing is slightly insufficient, the “air vortex wrapping liquid” effect is limited, and the fuel SMD is difficult to drop below 30 μm. The swirl number S of Scheme 4 is stable at 0.58, entering the optimal interval, but the “spindle-shaped” shape of the low-pressure core zone has slight asymmetry, and the fitting degree between the wall high-pressure zone and the recirculation zone boundary is about 90%, and there are still a small number of high-pressure areas beyond the recirculation zone, causing invalid aerodynamic load.
The pressure cloud map of Scheme 5 shows perfect spatial coupling and gradient rationality: the low-pressure core zone is a standard “spindle shape”, with a 100% spatial coincidence degree with the high-velocity flow core of the velocity field, and the radial pressure gradient accurately matches the axial momentum flux, making the swirl number stable at the optimal core value of 0.6. The wall high-pressure zone is completely fitted with the boundary of the low-velocity recirculation zone without any local high-pressure peaks or invalid load areas, and the dark brown to reddish-brown tone of the cloud map is distributed in a continuous and uniform ring shape. The axial pressure changes smoothly along the law of “inlet high pressure—main combustion zone low pressure—tail slow rise”, which not only provides continuous and stable power for the maintenance of swirling flow, but also makes the wall aerodynamic load evenly distributed, completely avoiding the risk of local erosion and structural fatigue. Schemes 1–4 all have defects in varying degrees in swirling flow shape control, recirculation zone accuracy, and pressure gradient adaptability, and fail to meet the triple design objectives of oil–gas mixing, flame stabilization effect, and aerodynamic loss control at the same time. Scheme 5, through the final optimization of the evaporator tube structure, realizes the accurate focusing of high-velocity swirling flow and the global stable regulation of low-velocity recirculation flow in the velocity field, and achieves the perfect adaptation of gradient uniform distribution and wall load in the pressure field. The core quantitative indicators all reach the design limit and are completely in line with the “recirculation flame stabilization theory of swirling flow combustion chamber”, which is the optimal scheme balancing aerodynamic performance, combustion efficiency, and structural safety.
4.3.2. Analysis of Static Temperature and Concentration Field
Combined with the color gradient, distribution shape, and spatial coverage characteristics of the fuel concentration cloud maps of Schemes 1–5 arranged longitudinally in
Figure 14, the analysis is carried out through multi-dimensional comparison of fuel atomization and diffusion, oil–gas mixing uniformity, and concentration adaptability of the core combustion zone:
The concentration cloud maps of the 5 groups of schemes show a clear longitudinal evolutionary trajectory: the high-concentration core zone gradually shrinks and focuses, the medium-concentration mixing zone expands evenly, and the boundary of the low-concentration diffusion zone is regularized. The high-concentration core zone in the concentration cloud map of Scheme 1 is distributed in a “cluster-like” diffuse shape; the extension trajectory from the evaporator tube outlet to the main combustion zone is messy without obvious directional diffusion characteristics. The range of the medium-concentration mixing zone is extremely small, and there is a sharp color mutation between the high and low-concentration intervals, indicating that the fuel has not formed effective mixing with air and still exists in the form of large droplet clusters. The low-concentration diffusion zone extends excessively to the flame tube wall, and an obvious high-concentration “wall adhesion” phenomenon appears in the wall area, which is very easy to cause wall carbon deposition and local high-temperature thermal erosion, completely failing to meet the design requirement of “no wall pollution” for the micro combustion chamber. The high-concentration core zone of Scheme 2 begins to shrink to the center of the flow channel, but still has the “bifurcation” characteristic, and the focusing of the fuel jet is insufficient. The range of the medium-concentration mixing zone is expanded, but the distribution is extremely uneven, and a mixing “blank zone” (concentration of light color system) appears at the core position of the main combustion zone, which means that there is a local fault in oil–gas mixing and cannot provide a uniform fuel foundation for stable combustion. The tail recirculation zone has no obvious characteristics of low-concentration hot flue gas mixing, and the concentration gradient is single, which is not conducive to the flame stabilization feedback at the flame root. The focusing effect of the high-concentration core zone of Scheme 3 is significantly improved, passing through the main combustion zone in a “beam shape”, but the core concentration is too high and the range of the dark color system is too large, indicating that the fuel atomization particle size is still too large and the crushing effect of “air vortex wrapping liquid” is limited. The uniformity of the medium-concentration mixing zone is improved, but the connection with the wall recirculation zone is insufficient, and the interior of the recirculation zone is still dominated by low concentration, which cannot accurately control the combustion intensity through fuel supplement. The boundary of the low-concentration diffusion zone still has slight irregularities, and a local concentration “wake” appears in some areas, indicating the existence of a weak eddy dead zone in the flow field. The concentration field distribution of Scheme 4 is close to the design target; the high-concentration core zone is focused on the center of the main combustion zone, and the medium-concentration mixing zone covers most of the core combustion area. However, there are two key defects: first, the distance between the boundary of the high-concentration core zone and the low-velocity recirculation zone is too close, which is easy to cause the fuel to directly enter the recirculation zone and cause local rich fuel combustion; second, the color gradient of the medium-concentration mixing zone has slight “striped” unevenness, indicating that the micro-uniformity of oil–gas mixing still has room for improvement, and the fuel SMD has not dropped to the optimal interval.
The concentration cloud map of Scheme 5 shows extreme spatial adaptability and mixing uniformity, and its color distribution and gradient change are completely in line with the fuel combustion requirements of the micro turbojet engine combustion chamber, with core advantages reflected in three dimensions:
- 1.
High-concentration core zone
Accurate focusing and optimal particle size. The high-concentration dark color area of Scheme 5 is a standard thin beam shape, strictly limited to the center position from the evaporator tube outlet to the core combustion zone of the main combustion zone without any diffusion or wall adhesion phenomenon. The range of the core zone is further reduced by 15% compared with Scheme 4, and the color saturation is uniform, indicating that under the driving of the optimal flow field with swirl number S = 0.6, the “air vortex wrapping liquid” effect is exerted to the extreme, the fuel SMD ≤ 28 μm, the droplet crushing is sufficient and the jet direction is accurate, laying the optimal particle size foundation for the micro mixing of oil and gas.
- 2.
Medium-concentration mixing zone
Global coverage and high uniformity. The medium-concentration transition color area in Scheme 5 presents a continuous, uniform, and dead-angle-free distribution characteristic, perfectly covering the connection area between the core flow channel of the main combustion zone and the wall recirculation zone. The color gradient transitions smoothly without any mutation, blank or striped unevenness, indicating that the fuel vapor and air have achieved molecular-level uniform mixing under the action of turbulence, and the mixing efficiency is increased by more than 10% compared with Scheme 4. This distribution characteristic ensures the uniform combustion intensity in the main combustion zone and completely avoids local rich or lean fuel phenomena.
- 3.
Low-concentration diffusion zone
Regular boundary and adapt to flame stabilization. The boundary of the low-concentration light color area is a regular closed ring, accurately fitting the outline of the flame tube wall and the tail recirculation zone, without wall pollution caused by excessive diffusion or mixing blank caused by insufficient contraction. The low-concentration distribution of the tail recirculation zone completely coincides with the hot flue gas residence area, realizing the optimal flame stabilization combination of “low-concentration fuel + high-temperature hot flue gas”—it not only provides an appropriate amount of fuel supplement for the flame root, but also maintains flame stability through the thermal feedback of hot flue gas.
Schemes 1–4 all have phased defects in fuel jet focusing, oil–gas mixing uniformity, and the adaptability of the concentration field to flow field/recirculation zone, and fail to meet the triple core requirements of fuel atomization and crushing, uniform mixing, and flame stabilization combustion at the same time. Through the final optimization of the evaporator tube structure, Scheme 5 realizes the accurate control of the concentration field with the help of the optimal flow field conditions: the high-concentration core zone is fully focused and crushed, the medium-concentration mixing zone is globally uniform, and the low-concentration diffusion zone has a regular boundary and is adapted to flame stabilization. Its fuel spatial distribution is completely in line with the combustion mechanism of the micro turbojet engine combustion chamber, which is the optimal scheme balancing atomization quality, mixing efficiency, and combustion stability.
4.3.3. Analysis of Combustion Temperature Field
Combined with the combustion temperature cloud maps of Schemes 1–5 arranged longitudinally in
Figure 15 and
Figure 16 (including the circumferential section temperature distribution of the main combustion zone, secondary combustion zone and auxiliary combustion zone), the analysis is carried out through multi-dimensional comparison of temperature field shape, peak control, radial/circumferential uniformity and coupling with flow field/concentration field:
The temperature cloud maps of the 5 groups of schemes show a clear longitudinal evolutionary trajectory: the high-temperature core zone gradually shrinks and focuses, the radial temperature gradient tends to be gentle, the circumferential uniformity is significantly improved, and the wall thermal load is continuously reduced. The high-temperature zone (>1800 K) of the x-plane of Scheme 1 is in a “diffuse cluster shape”, with no obvious boundary from the evaporator tube outlet to the main combustion zone, local ultra-high temperature peaks > 2000 K appear, and the high-temperature zone is directly attached to the flame tube wall, which is very easy to cause wall ablation and thermal fatigue. In addition, the high-temperature zone of the main combustion zone is eccentrically distributed, the circumferential temperature difference > 300 K, the temperature gradient of the secondary combustion zone and auxiliary combustion zone is sharp, and there is an obvious low-temperature “blank zone”, indicating that the oil–gas mixing is seriously uneven, local rich fuel leads to over-temperature, and local lean fuel leads to incomplete combustion. The high-temperature core zone of the x-plane of Scheme 2 begins to shrink to the center of the flow channel, but still has the “bifurcation” phenomenon; the ultra-high temperature peaks (>1950 K) are reduced, but there is still a high-temperature zone > 1700 K near the wall, and the wall adhesion risk is not completely eliminated. The circumferential temperature difference in the main combustion zone is reduced to about 250 K, but the temperature distribution of the secondary combustion zone is still “blocky” and uneven; the range of the low-temperature zone of the auxiliary combustion zone is too large, and the combustion heat release fails to effectively cover the entire flow channel. The high-temperature core zone of Scheme 3 passes through the main combustion zone in a “beam shape”, the over-temperature peaks basically disappear, but the core temperature is still too high (about 1900 K), the radial temperature gradient is large, the temperature difference from the center to the wall is >400 K, which is easy to cause thermal stress concentration. The circumferential temperature difference in the main combustion zone is further reduced to 200 K, the uniformity of the secondary combustion zone is improved, but there is still a local low-temperature zone in the auxiliary combustion zone, indicating that the mixing and combustion of fuel at the tail are still insufficient. The temperature field distribution of Scheme 4 is close to the design target, the high-temperature core zone is accurately focused on the center of the main combustion zone, the wall temperature is reduced to <1600 K, and the radial temperature difference < 300 K. Its circumferential temperature difference in the main combustion zone < 150 K, the uniformity of the secondary combustion zone is good, but there is still slight “striped” temperature unevenness in the auxiliary combustion zone, and the core temperature of the main combustion zone is still maintained at about 1850 K, failing to reach the optimal temperature control interval.
The temperature cloud map of Scheme 5 shows extreme uniformity, accurate temperature control ability, and perfect structural adaptability, and its color distribution and gradient change are completely in line with the combustion mechanism and thermal protection requirements of the micro turbojet engine combustion chamber, with core advantages reflected in three dimensions.
- 1.
Axial temperature field: Accurate core temperature control and the lowest wall thermal load.
In the axial temperature cloud map of Scheme 5, the high-temperature core zone (1750~1850 K) is a standard thin beam shape, strictly limited to the central flow channel of the main combustion zone without any diffusion or wall adhesion phenomenon. The core temperature is stably at about 1800 K, which not only ensures sufficient combustion heat release, but also avoids thermal decomposition and NOx generation caused by over-temperature. The wall temperature is uniformly controlled at 1400~1500 K, the radial temperature difference is <200 K, the thermal stress is significantly reduced, and the risk of wall ablation is completely avoided.
- 2.
Circumferential temperature field (main/secondary/auxiliary combustion zones): Global uniformity and no local imbalance.
The high-temperature zone of the main combustion zone is in a perfect centrosymmetric distribution, the circumferential temperature difference is <100 K, the color gradient transitions smoothly without any eccentricity or blocky unevenness, indicating that the oil–gas mixing reaches molecular-level uniformity and the combustion heat release is completely consistent in the circumferential direction. The temperature distribution of the secondary combustion zone is smoothly connected with the main combustion zone, and the medium-temperature zone (1500~1700 K) is evenly covered without obvious temperature faults, ensuring the continuous and stable combustion process. The boundary of the low-temperature zone (<1500 K) of the auxiliary combustion zone is regular, accurately fitting the tail recirculation zone, which not only ensures the sufficient afterburning of unburned fuel but also reduces the exhaust temperature through low-temperature flue gas, improving the safety of the turbine working environment.
- 3.
Global coupling: Perfect coordination with the flow field and concentration field.
The temperature field of Scheme 5 forms a perfect coupling with the aforementioned velocity field and concentration field: the high-temperature core zone is completely coincident with the high-velocity swirling flow core of 240~280 m/s and accurately matched with the high-concentration fuel zone, ensuring that “where the fuel is, the combustion is efficiently carried out there”; the medium-temperature zone corresponds to the medium-concentration mixing zone one by one, realizing the synchronization of heat release and mixing; the low-temperature zone accurately covers the wall recirculation zone, stabilizing the flame root through the recirculation of hot flue gas.
Schemes 1–4 all have phased defects in high-temperature core zone temperature control, circumferential/radial uniformity, wall thermal load control, and coupling with flow field/concentration field, and fail to meet the triple core requirements of high-efficiency combustion, low thermal stress, and high stability at the same time. Through the final optimization of the evaporator tube structure, Scheme 5 realizes the accurate control of the temperature field with the help of the optimal flow field and concentration field conditions: the high-temperature core zone has accurate temperature control, the circumferential/radial distribution is globally uniform, and the wall thermal load is the lowest. Its temperature field distribution is completely in line with the combustion mechanism and thermal protection requirements of the micro turbojet engine combustion chamber, which is the optimal scheme balancing combustion efficiency, thermal load distribution, and flame stability.