1. Introduction
Over the past several decades, compliance with increasingly stringent low NO
$_x$
emission regulations has driven manufacturers of gas turbine engines and aero-engines to develop highly tuned combustion systems. These systems operate on traditional hydrocarbon fuels under lean-premixed conditions for power generation (Macquisten & Dowling Reference Macquisten and Dowling1993; Lieuwen & Zinn Reference Lieuwen and Zinn1998; Hobson, Fackrell & Hewitt Reference Hobson, Fackrell and Hewitt2000). While this approach effectively reduces NO
$_x$
emissions, it increases the susceptibility of combustion systems to thermoacoustic instability. Such instabilities manifest as high-amplitude self-excited oscillations near the natural acoustic frequency of the system (Lieuwen & Yang Reference Lieuwen and Yang2005). These instabilities arise from a positive feedback between unsteady heat-release-rate oscillations and pressure fluctuations within the combustor, as described by the Rayleigh criterion (Rayleigh Reference Rayleigh1878; Culick & Kuentzmann Reference Culick and Kuentzmann2006). The strength of this feedback coupling is influenced by several factors, including hydrodynamic instabilities (Poinsot et al. Reference Poinsot, Trouvé, Veynante, Candel and Esposito1987), equivalence ratio fluctuations (Lieuwen & Zinn Reference Lieuwen and Zinn1998), entropy waves (Motheau, Nicoud & Poinsot Reference Motheau, Nicoud and Poinsot2014) and fuel composition variations (Karlis, Hardalupas & Taylor Reference Karlis, Hardalupas and Taylor2020; Piemsinlapakunchon & Paul Reference Piemsinlapakunchon and Paul2021). Thermoacoustic instability can also arise from a flame-intrinsic feedback mechanism that operates independently of the acoustic boundary conditions of the system (Hoeijmakers et al. Reference Hoeijmakers, Kornilov, Arteaga, de Goey and Nijmeijer2014; Bomberg, Emmert & Polifke Reference Bomberg, Emmert and Polifke2015; Emmert, Bomberg & Polifke Reference Emmert, Bomberg and Polifke2015).
In recent years, growing concerns over the rapid depletion of fossil fuel reserves and the accelerating impacts of greenhouse gas emissions, in particular
${\rm CO}_2$
, have prompted interest in renewable low-carbon or carbon-neutral fuels. Alternatives such as hydrogen (
${\rm H}_2$
), ammonia (
${\rm NH}_3$
) or hydrocarbon fuel blends enriched with
${\rm H}_2$
and/or
${\rm NH}_3$
are being explored for power generation due to their potential to reduce carbon emissions (Kobayashi et al. Reference Kobayashi, Hayakawa, Somarathne and Okafor2019; Jin & Kim Reference Jin and Kim2024; Liu et al. Reference Liu, Yang, Ruan, Yu, Nan, Li and Lu2024). However, direct use of
${\rm NH}_3$
and
${\rm H}_2$
as fuel poses challenges owing to their contrasting thermochemical properties:
${\rm NH}_3$
has low reactivity and a slow flame speed, while
${\rm H}_2$
is highly reactive with a fast flame speed compared with traditional hydrocarbon fuels. Studies have shown that co-firing
${\rm NH}_3$
with
${\rm CH}_4$
or
${\rm CH}_4{-}{\rm H}_2$
fuel blends can mitigate these limitations, offering a viable combustion strategy (Taamallah et al. Reference Taamallah, LaBry, Shanbhogue and Ghoniem2015; Shanbhogue et al. Reference Shanbhogue, Sanusi, Taamallah, Habib, Mokheimer and Ghoniem2016; Katoch et al. Reference Katoch, Guiberti, de Campos and Lacoste2022; Meti et al. Reference Meti, Kushwaha, Sakthivel and Murugesan2025). Nevertheless, such blended fuels can significantly alter flame behaviour and heat release distribution, leading to complex and intense thermoacoustic oscillations (Valera-Medina et al. Reference Valera-Medina, Xiao, Owen-Jones, David and Bowen2018; Kushwaha et al. Reference Kushwaha, Kasthuri, Pawar, Sujith, Chterev and Boxx2021; Meti et al. Reference Meti, Kushwaha, Sakthivel and Murugesan2025). If left uncontrolled, these oscillations can increase thermomechanical stress, causing structural damage or a substantial decline in the performance and lifespan of combustion systems (Lieuwen & Yang Reference Lieuwen and Yang2005; Poinsot Reference Poinsot2017). Therefore, it is critical to implement tailored control strategies to effectively suppress the thermoacoustic oscillations (Bellows, Hreiz & Lieuwen Reference Bellows, Hreiz and Lieuwen2008; Balusamy et al. Reference Balusamy, Li, Han, Juniper and Hochgreb2015; Mondal, Pawar & Sujith Reference Mondal, Pawar and Sujith2019; Guan et al. Reference Guan, Yin, Yang and Li2024). Such strategies necessitate an
$\textit {a priori}$
understanding of the nonlinear dynamics exhibited by the combustion system. In this study, we adopt a dynamical-systems approach to examine how variations in fuel blend composition influence the nonlinear dynamics of thermoacoustic systems. We place particular emphasis on the mechanisms driving mode transitions and instability. Before presenting our experimental methodologies (§ 2) and results (§ 3), we review relevant literature on the impact of hydrogen and ammonia on thermoacoustics (§ 1.2), highlighting examples of mode switching (§ 1.3) and transitions between nonlinear dynamical states (§ 1.1).
1.1. Nonlinear dynamical states in thermoacoustic systems
In combustion systems, thermoacoustic instability manifests as high-amplitude, self-excited limit cycle oscillations, typically occurring at frequencies close to the natural acoustic modes of the system (Dowling Reference Dowling1997; Juniper & Sujith Reference Juniper and Sujith2018). Researchers have demonstrated that thermoacoustic instability characterised by period-1 oscillations arises in various types of combustion systems. These range from laminar (Kashinath, Waugh & Juniper Reference Kashinath, Waugh and Juniper2014; Guan, Murugesan & Li Reference Guan, Murugesan and Li2018, Reference Guan, Gupta, Wan and Li2019b
) to turbulent combustors (Nair, Thampi & Sujith Reference Nair, Thampi and Sujith2014; Balusamy et al. Reference Balusamy, Li, Han, Juniper and Hochgreb2015; Murugesan & Sujith Reference Murugesan and Sujith2015) and from premixed (Bellows et al. Reference Bellows, Hreiz and Lieuwen2008; Kabiraj et al. Reference Kabiraj, Saurabh, Karimi, Sailor, Mastorakos, Dowling and Paschereit2015) to non-premixed combustion systems (Li & Juniper Reference Li and Juniper2013; Guan et al. Reference Guan, Li, Ahn and Kim2019d
). Under certain operating conditions, such systems can transition from periodic to quasiperiodic states, which involve two or more incommensurate frequencies (Jahnke & Culick Reference Jahnke and Culick1994; Kashinath et al. Reference Kashinath, Waugh and Juniper2014; Guan et al. Reference Guan, Gupta, Kashinath and Li2019a
,
Reference Guan, Gupta, Wan and Lib
). In nonlinear dynamics, quasiperiodic states emerge from the interaction of multiple incommensurate frequencies, producing aperiodic oscillations with an infinite period (Pikovsky, Rosenblum & Kurths Reference Pikovsky, Rosenblum and Kurths2003; Balanov et al. Reference Balanov, Janson, Postnov and Sosnovtseva2009). During such states, the phase trajectories do not repeat, but instead spiral aperiodically on the surface of a stable ergodic two-dimensional torus attractor,
$\mathbb{T}^2$
(Thompson & Stewart Reference Thompson and Stewart2002; Kushwaha et al. Reference Kushwaha, Worth, Dawson, Gupta and Li2022). Quasiperiodic behaviour has been observed in both laminar (Kabiraj et al. Reference Kabiraj, Saurabh, Wahi and Sujith2012; Kabiraj & Sujith Reference Kabiraj and Suijith2012) and turbulent combustion systems (Gotoda et al. Reference Gotoda, Nikimoto, Miyano and Tachibana2011; Balusamy et al. Reference Balusamy, Li, Han, Juniper and Hochgreb2015). Beyond periodic and quasiperiodic states, thermoacoustic systems can undergo a series of nonlinear bifurcations, giving rise to a rich spectrum of dynamical states, including period-
$k$
oscillations, intermittency, frequency-locked states, as well as strange non-chaotic and chaotic oscillations (Kabiraj et al. Reference Kabiraj, Saurabh, Wahi and Sujith2012; Guan et al. Reference Guan, Murugesan and Li2018, Reference Guan, He, Murugesan, Li, Liu and Li2019c
).
In most studies, these bifurcation cascades and the resulting complex nonlinear states arise because of changes in control parameters, such as the flame position, Reynolds number (Kabiraj et al. Reference Kabiraj, Saurabh, Wahi and Sujith2012; Kabiraj & Sujith Reference Kabiraj and Suijith2012), or from the application of external forcing to hydrodynamic (Kushwaha et al. Reference Kushwaha, Worth, Dawson, Gupta and Li2022, Reference Kushwaha, Worth, Dawson, Gupta and Li2026) and combustion systems (Balusamy et al. Reference Balusamy, Li, Han, Juniper and Hochgreb2015; Guan et al. Reference Guan, He, Murugesan, Li, Liu and Li2019c
). However, growing evidence indicates that similar nonlinear states can emerge when fuel composition is varied, particularly through different blend ratios of
${\rm H}_2$
,
${\rm NH}_3$
and
${\rm CH}_4$
(Lubrano Lavadera et al. Reference Lubrano Lavadera, Song, Sabia, Herbinet, Pelucchi, Stagni, Faravelli, Battin-Leclerc and de Joannon2018; Liu et al. Reference Liu, Yang, Ruan, Yu, Nan, Li and Lu2024; Meti et al. Reference Meti, Kushwaha, Sakthivel and Murugesan2025). These complex nonlinear states, even with brief excursions into high-amplitude oscillation regimes, can become detrimental to the combustion system and adversely affect the structural integrity and operational stability of the combustion system. Understanding the mechanisms by which fuel composition drives these nonlinear transitions is therefore critical for developing resilient combustion systems capable of operating with alternative fuel blends, as well as effective control strategies. Motivated by this need, the present study investigates the characteristics of thermoacoustic instability in a turbulent combustor operating with varying
${\rm NH}_3{-}{\rm H}_2{-}{\rm CH}_4$
fuel blends.
1.2. Ammonia and hydrogen-enriched methane–air combustion
In recent years, several studies have focused on the thermoacoustic behaviour of combustion systems operating with various blend ratios of partially premixed and premixed
${\rm NH}_3{-}{\rm H}_2{-}{\rm CH}_4$
fuel blends (Valera-Medina et al. Reference Valera-Medina, Morris, Runyon, Pugh, Marsh, Beasley and Hughes2015, Reference Valera-Medina, Pugh, Marsh, Bulat and Bowen2017; Kurata et al. Reference Kurata, Iki, Matsunuma, Inoue, Tsujimura, Furutani, Kobayashi and Hayakawa2017; Ramos et al. Reference Ramos, Rocha, Oliveira, Costa and Bai2019; Okafor et al. Reference Okafor, Somarathne, Ratthanan, Hayakawa, Kudo, Kurata, Iki, Tsujimura, Furutani and Kobayashi2020; Tang et al. Reference Tang, Jin, Bao, Chai and Zhou2021; Katoch et al. Reference Katoch, Guiberti, de Campos and Lacoste2022; Wei, Fang & Zhou Reference Wei, Li and Zhou2024c
). These studies have underscored the inherent limitations of
${\rm NH}_3$
as a fuel, specifically its low reactivity and slow flame speed, which pose significant challenges to flame stabilisation. When
${\rm NH}_3$
is used as a direct substitute for conventional hydrocarbons, it leads to significantly elevated NO
$_x$
emissions (Verkamp, Hardin & Williams Reference Verkamp, Hardin and Williams1967; Valera-Medina et al. Reference Valera-Medina, Pugh, Marsh, Bulat and Bowen2017; Kobayashi et al. Reference Kobayashi, Hayakawa, Somarathne and Okafor2019; Khateeb et al. Reference Khateeb, Guiberti, Wang, Boyette, Younes, Jamal and Roberts2021). However, co-firing
${\rm NH}_3$
with
${\rm H}_2$
,
${\rm CH}_4$
or their blends has proven effective in mitigating these limitations. Such co-firing increases both the laminar flame speed and the adiabatic flame temperature across a broad range of equivalence ratios (Valera-Medina et al. Reference Valera-Medina, Morris, Runyon, Pugh, Marsh, Beasley and Hughes2015; Mei et al. Reference Mei, Zhang, Shi, Xi and Li2021; Zhang & Ratner Reference Zhang and Ratner2021; Katoch et al. Reference Katoch, Guiberti, de Campos and Lacoste2022). While
${\rm NH}_3$
-enriched fuel blends offer a promising approach to carbon-neutral combustion, they result in markedly increased
$\mathrm{NO}_x$
emissions compared with traditional hydrocarbon fuels. The emission characteristics of
${\rm NH}_3{-}{\rm CH}_4$
blends differ fundamentally from those of conventional fuels. Unlike traditional hydrocarbon fuels,
${\rm NH}_3{-}{\rm CH}_4$
blends exhibit peak NO
$_x$
emissions near stoichiometric conditions, elevated emissions under lean conditions and lower emissions under fuel-rich conditions (Ramos et al. Reference Ramos, Rocha, Oliveira, Costa and Bai2019; Zhang & Ratner Reference Zhang and Ratner2021). This behaviour suggests that conventional lean-premixed combustion strategies designed for
$\mathrm{NO}_x$
emission minimisation are not well suited for ammonia-based fuels. Several studies have shown a nonlinear relationship between
$\mathrm{NO}_x$
emissions and
${\rm NH}_3$
concentration in fuel blends, with a peak occurring at approximately 50
$\%$
${\rm NH}_3$
by fuel blend ratio. Beyond this threshold, further
${\rm NH}_3$
enrichment leads to reduced NO
$_x$
emissions, albeit at the expense of increased unburned
${\rm NH}_3$
(Konnov, Dyakov & De Ruyck Reference Konnov, Dyakov and De Ruyck2006; Valera-Medina et al. Reference Valera-Medina, Morris, Runyon, Pugh, Marsh, Beasley and Hughes2015; Kurata et al. Reference Kurata, Iki, Matsunuma, Inoue, Tsujimura, Furutani, Kobayashi and Hayakawa2017; Ramos et al. Reference Ramos, Rocha, Oliveira, Costa and Bai2019).
Although the emission characteristics and flammability limits of ammonia-enriched blends have been well studied, their influence on combustion dynamics and thermoacoustic instabilities remains poorly understood. Recent work by Liu et al. (Reference Liu, Yang, Ruan, Yu, Nan, Li and Lu2024) demonstrated that
${\rm NH}_3$
enrichment alters instability characteristics, including oscillation amplitudes, frequencies and flame structures. The authors showed that increasing
${\rm NH}_3$
concentration in a
${\rm CH}_4{-}{\rm NH}_3$
fuel blend elongates the flame front and weakens heat release rate fluctuations in the flame root regions, consequently shifting the reaction zones downstream. At a higher
${\rm NH}_3$
concentration, both the pressure and the heat release rate oscillations are substantially reduced. These findings are consistent with those of Xiao et al. (Reference Xiao, Valera-Medina and Bowen2017a
,Reference Xiao, Valera-Medina, Marsh and Bowen
b
) and Fu et al. (Reference Fu, Rao, Hu, Yang, Wen and Wang2025), which also reported significant changes in combustion dynamics with
${\rm NH}_3$
enrichment. Furthermore, these studies indicate that changes in
${\rm NH}_3$
concentration can trigger bifurcations in the system behaviour. Specifically, Liu et al. (Reference Liu, Yang, Ruan, Yu, Nan, Li and Lu2024) observed subcritical Hopf bifurcations with hysteresis zones that widen under lean conditions and disappear under fuel-rich conditions.
Several studies (Karlis et al. Reference Karlis, Liu, Hardalupas and Taylor2019; Tang et al. Reference Tang, Jin, Bao, Chai and Zhou2021; Guan & Zhao Reference Guan and Zhao2023) have shown that enriching
${\rm NH}_3{-}{\rm CH}_4$
fuel blends with
${\rm H}_2$
can overcome some of their inherent limitations of these blends and improve combustion performance by increasing the laminar burning velocity while maintaining relatively lower NO
$_x$
emissions. Additionally,
${\rm H}_2$
enrichment increases the extinction strain rate, which influences flame anchoring locations and flame interactions with coherent structures, consequently modifying the flame topology (Ren et al. Reference Ren, Qin, Egolfopoulos and Tsotsis2001; Karlis et al. Reference Karlis, Liu, Hardalupas and Taylor2019). Furthermore,
${\rm H}_2$
enrichment enables stable operation near the lean flammability limit, contributing to reduced carbon monoxide emissions (Gauducheau, Denet & Searby Reference Gauducheau, Denet and Searby1998; Ren et al. Reference Ren, Qin, Egolfopoulos and Tsotsis2001; Schefer, Wicksall & Agrawal Reference Schefer, Wicksall and Agrawal2002). However, higher
${\rm H}_2$
concentrations in fuel blends introduce new challenges. Owing to its high molecular diffusivity and fast flame speed,
${\rm H}_2$
enrichment increases the risk of flashback and makes the system more prone to large-amplitude thermoacoustic instabilities (Rieth et al. Reference Rieth, Gruber, Williams and Chen2022; Gaucherand et al. Reference Gaucherand, Laera, Schulze-Netzer and Poinsot2023). Taamallah et al. (Reference Taamallah, LaBry, Shanbhogue and Ghoniem2015) and Zhang & Ratner (Reference Zhang and Ratner2021) have explored the effects of
${\rm H}_2$
enrichment on thermoacoustic instabilities. They have reported that increasing the
${\rm H}_2$
fraction leads to transitions between various nonlinear states, including chaos, intermittency and limit cycle oscillations. These findings are supported by the experimental study of Kushwaha et al. (Reference Kushwaha, Kasthuri, Pawar, Sujith, Chterev and Boxx2021), who also observed the progression from period-1 to period-2 oscillations with increasing
${\rm H}_2$
levels. To address both NO
$_x$
emissions and thermoacoustic instability simultaneously, Katoch et al. (Reference Katoch, Guiberti, de Campos and Lacoste2022) and Jin & Kim (Reference Jin and Kim2024) have explored hybrid fuel staging strategies. Their studies demonstrated that employing a combination of
${\rm H}_2$
-enriched rich-premixed
${\rm NH}_3$
flames surrounded by lean-premixed pure
${\rm H}_2$
flames creates radially stratified, non-homogeneous reaction zones. These distinct reaction zones, characterised by different reaction time scales, disrupt synchronised oscillations across the entire flame ensemble, thereby preventing the onset of large-amplitude thermoacoustic oscillations.
1.3. Mode switching and flame macrostructures
Mode switching in thermoacoustic systems manifests as abrupt transitions between distinct unstable eigenmodes in response to variations in control parameters. These parameters include acoustic reflection boundary conditions (Murugesan et al. Reference Murugesan, Singaravelu, Kushwaha and Mariappan2018), equivalence ratio (Hong et al. Reference Hong, Shanbhogue, Speth and Ghoniem2013; Zhao et al. Reference Zhao, Li, Zhao, Zhang, Sun, Yang, Li, Lu and Zheng2017), combustor length (Ahn et al. Reference Ahn, Lee, Jung and Kim2018) and external forcing (Guan et al. Reference Guan, He, Murugesan, Li, Liu and Li2019c
). Such parametric changes fundamentally alter the coupling pathway between unsteady heat-release-rate fluctuations and acoustic pressure oscillations. This altered coupling mechanism can excite different thermoacoustic modes, leading to either amplification or suppression of oscillations. Guan et al. (Reference Guan, He, Murugesan, Li, Liu and Li2019c
) demonstrated that transient forcing can induce mode transitions that reduce oscillation amplitudes by up to 50 %, highlighting the potential of mode switching as an active control strategy. Fuel composition represents another key driver of mode switching, particularly through
${\rm H}_2$
or
${\rm NH}_3$
enrichment (Wicksall & Agrawal Reference Wicksall and Agrawal2007; Allison, Driscoll & Ihme Reference Allison, Driscoll and Ihme2013; Taamallah et al. Reference Taamallah, LaBry, Shanbhogue and Ghoniem2015; Park & Lee Reference Park and Lee2016b
; Shanbhogue et al. Reference Shanbhogue, Sanusi, Taamallah, Habib, Mokheimer and Ghoniem2016; Palies, Ilak & Cheng Reference Palies, Ilak and Cheng2017; Baraiya & Chakravarthy Reference Baraiya and Chakravarthy2019). Mode switching often coincides with transitions in flame macrostructure, typically between V-shaped and M-shaped configurations in swirl-stabilised flames. While some studies report M-shaped flames during unstable periodic oscillations that transition to V-shaped flames upon stabilisation (Tao & Zhou Reference Tao and Zhou2020; Wei et al. Reference Wei, Fang, Tang, Wang, Wei and Zhou2024a
,Reference Wei, Fang and Zhou
b
), others observe opposing trends where flames transition from V-shaped to M-shaped with increasing
${\rm NH}_3$
concentration (Liu et al. Reference Liu, Yang, Ruan, Yu, Nan, Li and Lu2024). These apparently contradictory observations reflect the complex dependence of flame morphology on specific operating conditions and fuel blend compositions. Hydrogen enrichment produces particularly pronounced morphological changes due to its high diffusivity and high extinction strain rates. Shanbhogue et al. (Reference Shanbhogue, Sanusi, Taamallah, Habib, Mokheimer and Ghoniem2016) demonstrated that
${\rm H}_2$
-enriched flames penetrate deeper into outer recirculation zones, producing flattened M-shaped configurations. The displacement of reaction zones at higher
${\rm H}_2$
fractions causes flames to become shorter and more compact while exhibiting more intense heat (Schefer et al. Reference Schefer, Wicksall and Agrawal2002; Davis et al. Reference Davis, Therkelsen, Littlejohn and Cheng2013). These morphological changes fundamentally alter heat-release–acoustic coupling by redistributing heat-release patterns within the combustor, leading to notable shifts in thermoacoustic frequency characteristics (Wicksall & Agrawal Reference Wicksall and Agrawal2007; Nam & Yoh Reference Nam and Yoh2020; Zhang & Ratner Reference Zhang and Ratner2021). The frequency response to hydrogen enrichment exhibits system-dependent behaviour. Wicksall & Agrawal (Reference Wicksall and Agrawal2007) reported mode switching from higher to lower frequencies with increasing
${\rm H}_2$
content, while Zhang & Ratner (Reference Zhang and Ratner2021) observed the opposite trend. At sufficiently high
${\rm H}_2$
concentration, these authors showed that instabilities can be suppressed entirely through inhibition of flame fluctuations, consistent with findings of the numerical study by Nam & Yoh (Reference Nam and Yoh2020). This
${\rm H}_2$
and
${\rm NH}_3$
enrichment reflects changes in effective time delays (
$\tau$
) between acoustic perturbations and heat release, governed by the different flame speeds and diffusivities of constituent fuels (Allison et al. Reference Allison, Driscoll and Ihme2013; Park & Lee Reference Park and Lee2016a
; Yoon et al. Reference Yoon, Joo, Kim, Lee, Lee and Yoon2017). These variations change flame structures and combustion dynamics, triggering multi-mode instabilities and exciting incommensurate frequencies and higher harmonics (Kushwaha et al. Reference Kushwaha, Kasthuri, Pawar, Sujith, Chterev and Boxx2021; Liu et al. Reference Liu, Yang, Ruan, Yu, Nan, Li and Lu2024; Wei et al. Reference Wei, Fang and Zhou2024b
). Similar hydrogen-driven mode switching has been documented in annular combustors, where increasing
${\rm H}_2$
content in a
${\rm CH}_4{-}{\rm H}_2$
fuel blend induces transitions from stable to unstable states characterised by high-amplitude oscillations and dominant spinning modes (Lantz et al. Reference Lantz, Collin, Aldén, Lindholm, Larfeldt and Lörstad2015; Indlekofer et al. Reference Indlekofer, Ahn, Kwah, Wiseman, Mazur, Dawson and Worth2021; Ahn et al. Reference Ahn, Indlekofer, Dawson and Worth2022).
Mode switching can also occur between two fundamentally different thermoacoustic mechanisms: cavity acoustic modes and intrinsic thermoacoustic (ITA) modes (Bomberg et al. Reference Bomberg, Emmert and Polifke2015; Silva et al. Reference Silva, Merk, Komarek and Polifke2017; Murugesan et al. Reference Murugesan, Singaravelu, Kushwaha and Mariappan2018). Unlike the cavity acoustic mode, which arises from resonant coupling between unsteady heat release and the acoustic eigenmodes of the combustor geometry, the ITA mode originates from a flame-intrinsic feedback loop that operates independently of the combustor acoustic boundary conditions (Hoeijmakers et al. Reference Hoeijmakers, Kornilov, Arteaga, de Goey and Nijmeijer2014; Emmert et al. Reference Emmert, Bomberg and Polifke2015). This fundamental distinction manifests in their frequency characteristics: while cavity modes exhibit fixed frequencies determined by combustor geometry, ITA modes scale with mean flow velocity and convective time scales (Albayrak et al. Reference Albayrak, Steinbacher, Komarek and Polifke2018; Murugesan et al. Reference Murugesan, Singaravelu, Kushwaha and Mariappan2018). Recent investigations have revealed that
${\rm H}_2$
enrichment can trigger the emergence of the ITA mode in practical combustion systems (Katoch et al. Reference Katoch, Guiberti, de Campos and Lacoste2022; Kumar et al. Reference Kumar, Massey, Soundararajan, Boxx and Swaminathan2025). These
${\rm H}_2$
-enriched fuel blends modify convective transport mechanisms through altered flame speeds and diffusivities, fundamentally changing the thermoacoustic coupling pathway, which subsequently excites ITA instabilities (Kumar et al. Reference Kumar, Massey, Soundararajan, Boxx and Swaminathan2025). Despite extensive studies on hydrogen-induced mode switching, the specific mechanisms by which
${\rm H}_2$
enrichment modifies intrinsic thermoacoustic feedback and the associated nonlinear dynamics remain less well understood. The present study demonstrates that progressive
${\rm H}_2$
enrichment induces systematic transitions within the ITA mode family from fourth-harmonic ITA instability (179 Hz, pure methane operation) to first-harmonic ITA dominance (130–160 Hz range, at
$P_{\textrm{H}_2}$
= 0.50), accompanied by nonlinear dynamical transitions from limit-cycle oscillations through quasiperiodic states to period-3 behaviour. Through acoustic network modelling, we reveal that this harmonic switching reflects hydrogen-induced flame compaction and reduced characteristic time delays, representing a fundamental change in the dominant ITA mechanism rather than a simple frequency adjustment. The harmonic transition coincides with flame morphological changes from elongated structures to compact configurations, providing compelling evidence that hydrogen enrichment fundamentally alters the intrinsic thermoacoustic coupling pathway through modified convective time scales, which will be thoroughly explained in §§ 3.3.1 and 3.3.2.
1.4. Contributions of the present study
It is well known that co-firing carbon-neutral fuels such as ammonia and hydrogen with natural gas can reduce net carbon dioxide emissions in many modern gas turbines and industrial burners. However, such combustion systems operating with blended fuels are susceptible to thermoacoustic instabilities. In this study, we investigate thermoacoustic behaviours and flame morphologies to address three research questions.
-
(i) Recent studies have shown that turbulent combustion systems are not only unstable to the acoustic cavity modes, but can also become unstable to the intrinsic thermoacoustic mode without locking in to one of the acoustic eigenmodes of the combustor. The question then arises as to whether variations in blended fuel composition can influence thermoacoustic mode switching? If so, what are the accompanying nonlinear dynamical states and flame morphologies associated with these transitions?
-
(ii) If the addition of carbon-free fuel can alter the nonlinear dynamical state of the combustion system, what are the specific fuel compositions at which thermoacoustic amplitude is most significantly reduced or amplified? Understanding these conditions is critical to ensuring the stable operation of fuel-flexible combustion systems.
-
(iii) Can a low-order acoustic network model be used to identify and distinguish acoustic cavity modes and intrinsic thermoacoustic modes in combustion systems exhibiting thermoacoustic instability, and to understand the underlying mechanisms driving these instabilities?
The structure of the paper is as follows: § 2 details the experimental set-up and measurement techniques; § 3 presents the experimental results and their discussion; and finally, § 4 summarises the key findings and provides the concluding remarks.
2. Experiments
Experiments are performed on a turbulent, partially premixed swirl-stabilised combustion system. Figure 1(a) shows the set-up, which has four main components: a quartz-tube combustion chamber (inner diameter (ID), 75 mm; length, 500 mm); extension ducts (ID, 75 mm; length, 300 mm), a burner (ID
$_a$
, 28 mm; length, 300 mm) and a plenum (ID. 200 mm; length, 200 mm). A fuel pipe (outer diameter (OD) OD
$_f$
, 12 mm; length, 800 mm) is mounted to pass through the settling chamber and extends to the burner exit. The fuel pipe accommodates a fixed vane swirler (eight tapered vanes inclined at 60
$^{\circ }$
to the axis) to enhance flame stabilisation. At a distance of 5 mm before the swirler, 14 fuel injection holes (ID, 1.7 mm) are placed at equal intervals around the circumference of the fuel pipe. Air is supplied to the burner through the plenum. Air, methane, hydrogen and ammonia are metered with mass flow controllers (Alicat MCR series:
$\pm$
0.2
$\%$
of full scale). The Reynolds number (
$ \textit{Re}$
) in the present study is defined based on the bulk velocity in the burner annulus section
$u_{\kern-2pt B}$
, the hydraulic diameter of the burner annulus
$d = \textit{ID}_a - \textit{OD}_{\kern-1pt f}$
and the kinematic viscosity
$\nu$
of the fuel–air mixture at the operating conditions:
$ \textit{Re} = u_{\kern-2pt B} d / \nu$
. Across the full range of fuel blend compositions and thermal power settings investigated,
$ \textit{Re}$
varies between approximately 3010 and 4700, confirming that the flow is in the fully turbulent regime throughout all experiments. The combustor exit is at ambient conditions. In the present study, we choose a partially premixed, swirl-stabilised configuration because it is representative of practical gas turbine combustion systems, where fully premixed operation is rarely achieved due to the demands of fuel flexibility and the need for flame stabilisation across a range of operating conditions. Moreover, a fully premixed combustion chamber operating in the turbulent regime requires safe handling due to the risks of flashback, explosion and flame-stabilisation difficulties under lean conditions.
(
$a$
) Schematic of the experimental set-up, whose main components include a plenum, a burner, and a combustor made of quartz pipe and stainless steel sections. The flame is stabilised using
$(b)$
a swirler with eight tapered blades at a vane angle of
$60^{\circ }$
, mounted in the annular space between the burner and the fuel injection pipe.
$(c)$
Fuel is injected
$5$
mm upstream of the swirler through
$14$
fuel injection holes. The measurement diagnostics include a pressure transducer for measuring acoustic pressure, a photo-multiplier tube (PMT) for the global CH
$^*$
chemiluminescence from the flame and a high-speed camera for time-resolved flame imaging.

Figure 1. Long description
Panel A: A diagram of the experimental setup showing a plenum connected to a burner, which is attached to a combustor made of quartz pipe and stainless steel sections. The burner includes an acoustic driver and an air supply line. The combustor has a high-speed camera, an acoustic pressure transducer, and extension ducts. Panel B: A close-up view of a 60-degree tapered vane swirler used to stabilize the flame. Panel C: A sectional view of the burner showing the swirler and fuel pipe with air and fuel flow directions indicated.
Pure methane–air combustion experiments are first conducted. For methane–air combustion, the combustion system undergoes a transition from low-amplitude combustion noise (stable operation) to thermoacoustic instability (limit cycle oscillations) via intermittency when the operating conditions (i.e. equivalence ratio and thermal power) are varied. We focus on the self-excited state: a periodic limit cycle. In our combustor, this state can be found at an equivalence ratio of
$\phi$
= 0.85 and thermal power of
$k$
= 4100 W. At this operating condition, the natural frequency of the limit cycle oscillations is
$f_1$
= 179 Hz and the modal structure is a first harmonic standing wave with a pressure antinode near the dump plane of the quartz-tube combustion chamber. The blend ratio of methane, ammonia and hydrogen is varied in the fuel blend to explore their effects on the self-excited limit cycle. The thermal power ratios of hydrogen (
$P_{\textrm{H}_2}$
), ammonia (
$P_{\textrm{NH}_3}$
) and methane (
$P_{\textrm{CH}_4}$
) are changed with a step size of 0.10, while maintaining the total thermal power (
$P_{\textrm{H}_2}+P_{\textrm{NH}_3}+P_{\textrm{CH}_4}$
= 1.0) at a constant value of
$k$
= 4100 W. Experiments under ternary operating conditions are conducted for 66 fuel compositions. Simultaneous measurements of the acoustic pressure and heat release rate are made to quantify the influence of variations in hydrogen, methane and ammonia content in the fuel composition. The acoustic pressure fluctuations are measured with pressure transducers (PCB 103B02) mounted 500 mm downstream of the dump plane. The data are digitally recorded at a sampling rate of 20 480 Hz for 10 s on a 16-bit data acquisition system (NI cDAQ9174). The heat-release rate is measured using a broadband chemiluminescence, which is recorded with a high-speed camera (Photron Nova S12) operating at 2000 frames per second with an image resolution of 560
$\times$
760 pixels. This frame rate is sufficient to identify the time-resolved flame oscillations at the frequency of thermoacoustic instability (
$f_1 =$
179
$\pm$
1.5 Hz). These high-speed images are examined using spectral proper orthogonal decomposition (SPOD) to identify the flame structures at different frequencies.
3. Results and discussions
3.1. Self-excited periodic limit cycle
Before analysing the impact of ammonia and hydrogen enrichment on thermoacoustic instability, we first identify the conditions under which the combustion system operating with pure
${\rm CH}_4$
as a fuel exhibits self-excited limit cycle oscillations. We find that the system becomes self-excited at an equivalence ratio of
$\phi = 0.85$
and a thermal power output of
$k=$
4100 W. This is evidenced by multiple diagnostic indicators: (a) the time trace; (b) the power spectral density (PSD) and (c) the one-sided Poincaré map of the acoustic pressure fluctuations (
$p^\prime$
) in the combustor. The presence of a sharp spectral peak in the PSD (figure 2
b) at
$f_1 = 179 \pm 2$
Hz, combined with the absence of pronounced amplitude modulation in the time trace (figure 2
a), provides strong evidence of limit cycle behaviour (Pikovsky et al. Reference Pikovsky, Rosenblum and Kurths2003). This is further corroborated by the Poincaré map (figure 2
c), where the phase trajectory intercepts form a single cluster of points, indicating that the phase trajectory evolves around a closed repetitive orbit in the phase portrait. This is a hallmark of period-1 limit cycle oscillations (Balanov et al. Reference Balanov, Janson, Postnov and Sosnovtseva2009). The high-speed chemiluminescence images of the flame serve as markers for heat-release-rate oscillations during thermoacoustic instability (Keller & Saito Reference Keller and Saito1987). Figure 3(a) shows phase-resolved images of flame dynamics captured via broadband chemiluminescence imaging at nine different time instants spanning one period of the limit cycle oscillations. The phase-averaged images reveal that the high-intensity heat release rate occurs in the shear layers located downstream of the dump plane. The flame roots anchored at the dump plane exhibit reduced intensity oscillations compared with the tail regions situated between 30 and 60 mm downstream of the dump plane. The flame macrostructures exhibit cyclic variations, where shorter mean flame length in the recirculation zone near the dump plane corresponds to a high-intensity heat release rate. However, as the reaction zone near the recirculation region weakens, the turbulent flame brush thickens downstream, leading to an increased mean flame length with concurrent reduction in heat release rate. Crucially, the dominant peak in the PSD of time-resolved flame images (figure 3
b) closely aligns with that observed in the PSD of
$p'$
, underscoring the strong dynamic coupling between the flame and the acoustic field. In § 3.3.2, using acoustic network modelling, we will demonstrate that the observed mode corresponds to the fourth harmonic of the ITA instability mode, rather than a cavity acoustic mode. This distinction is critical for understanding the fundamental nature of the thermoacoustic feedback mechanisms governing different fuel compositions, as discussed in the subsequent sections.
Thermoacoustic system shows self-excited limit cycle oscillations for pure
${\rm CH}_4$
–air combustion at an equivalence ratio of
$\phi = 0.85$
and thermal power output of
$k =$
4100 W: (
$a$
) time series; (
$b$
) power spectral density (PSD) and (
$c$
) Poincaré map computed from the acoustic pressure (
$p^\prime$
).

Sequence of phase-averaged images of the flame captured from the broadband chemiluminescence images during one time period of the limit cycle at
$f_1=179$
Hz. The high-intensity region of the flame moves closer to the inlet, reducing the mean flame length, and then increases back to form the original flame structure, depicting the cyclic nature of the flame macrostructure in line with the acoustic pressure.

3.2. Effect of ammonia and hydrogen enrichment on the thermoacoustic instability
Having identified suitable operating conditions for which the combustion system exhibits self-excited limit cycle oscillations, we next examine the dynamical response of the combustor to changes in fuel blend ratios. Specifically, we assess the thermoacoustic response by gradually adjusting the blending ratio of each fuel component (
$P_{\textrm{H}_2}$
,
$P_{\textrm{NH}_3}$
and
$P_{\textrm{CH}_4}$
) from 0 to 1.0 in increments of 0.10, while maintaining a constant equivalence ratio and a constant total thermal power. We employ ternary plots to represent the comprehensive series of fuel blend combinations used to evaluate thermoacoustic behaviour and nonlinear dynamics arising from different
${\rm H}_2$
and
${\rm NH}_3$
enrichment pathways of
${\rm CH}_4$
base fuel. Figure 4 shows two ternary plots for the combustor operating at a thermal power output of 4.1 kW. Both plots are mapped in a parameter space defined by the varying blending ratios of
${\rm CH}_4$
,
${\rm H}_2$
and
${\rm NH}_3$
, with the three vertices corresponding to 100
$\%$
concentration of each fuel component. The ternary plot structure provides a clear visual representation of fuel compositions. Left-leaning diagonal lines (figure 4
a) indicate constant
${\rm CH}_4$
fractions, while right-leaning diagonal lines represent constant
${\rm H}_2$
fractions. Horizontal lines correspond to constant
${\rm NH}_3$
fractions, enabling systematic analysis of fuel composition effects. Figure 4(a) shows the different dynamical states that emerge with various combinations of
${\rm H}_2{-}{\rm NH}_3$
enrichment of
${\rm CH}_4$
fuel, while figure 4(b) displays contours of the response amplitude, measured as the root mean square (r.m.s.) of
$p'$
. A preliminary examination of figure 4(a) reveals that the system exhibits four dynamical states, depending on the fuel blending ratio. To obtain a comprehensive overview of the thermoacoustic response across fuel blend combinations, we employ two systematic enrichment approaches. First, we gradually increase
$P_{\textrm{H}_2}$
while simultaneously decreasing
$P_{\textrm{CH}_4}$
and maintaining a fixed
$P_{\textrm{NH}_3}$
. Second, we increase
$P_{\textrm{NH}_3}$
while simultaneously decreasing
$P_{\textrm{CH}_4}$
and maintaining a fixed
$P_{\textrm{H}_2}$
. Figure 4(b) demonstrates that different blend ratios can either suppress or amplify thermoacoustic oscillations, depending on the enrichment degree and the fuel blending ratio. Notably, the maximum amplification occurs when the thermoacoustic system exhibits quasiperiodic or period-3 oscillations. The emergence of these states is closely linked to
${\rm H}_2$
enrichment in
${\rm CH}_4$
and
${\rm CH}_4{-}{\rm NH}_3$
fuel blends. Figure 4 shows that these quasiperiodic and period-3 dynamical states arise when
$0.2 \lt P_{\textrm{H}_2} \lt 0.6$
, across a wide range of
$P_{\textrm{CH}_4}$
and
$P_{\textrm{NH}_3}$
combinations. However, the thermoacoustic amplitude is substantially suppressed to low values in the range of 20
$-$
50 Pa when
$P_{\textrm{H}_2} \gt 0.6$
, indicating a transition to low-amplitude, aperiodic states at high hydrogen concentrations.
Effect of
${\rm H}_2$
,
${\rm NH}_3$
and
${\rm CH}_4$
on self-excited thermoacoustic instability: ternary plot showing (
$a$
) the fuel compositions at which different nonlinear dynamical states arise and (
$b$
) contours of the root mean square (r.m.s.) of acoustic pressure amplitude (
$P_{\textit{rms}}$
) for
$\phi =$
0.85 and
$k =$
4100 W. In panels (
$a{,}b$
), the grey regions denote no ignition. In panel (
$a$
), P1, one-period limit cycle oscillations; QP, quasiperiodic oscillations; P3, period-3 oscillations; Ch, chaotic oscillations; and NI, no ignition states. The acoustic pressure attains the highest amplitude at quasiperiodic and period-3 states (
$P_{\textrm{H}_2}=$
0.20–0.50).
$P_{\textrm{CH}_4}$
,
$P_{\textrm{H}_2}$
and
$P_{\textrm{NH}_3}$
denote the thermal power ratio of methane, hydrogen and ammonia in the fuel blend, respectively, where
$P_{\textrm{H}_2}+P_{\textrm{NH}_3}+P_{\textrm{CH}_4}$
= 1.0.

Figure 4. Long description
Panel A: A triangular grid plot shows different nonlinear dynamical states arising from various fuel compositions. The grid is color-coded to denote different states: blue for P1 (one-period limit cycle oscillations), green for Ch (chaotic oscillations), orange for QP (quasiperiodic oscillations), red for P3 (period-3 oscillations), and grey for NI (no ignition). The axes are labeled with the thermal power ratios of methane, hydrogen, and ammonia in the fuel blend. Panel B: A triangular contour plot displays the root mean square of acoustic pressure amplitude. The color scale ranges from blue (low amplitude) to red (high amplitude), with grey regions indicating no ignition. The axes are labeled with the thermal power ratios of methane, hydrogen, and ammonia.
Next, we examine the thermoacoustic behaviour for varying degrees of
${\rm H}_2$
enrichment of
${\rm CH}_4{-}{\rm NH}_3$
fuel blends. The emergence of different dynamical states is accompanied by a substantial increase in the thermoacoustic amplitude and a change in the dominant frequency of oscillations, indicative of mode switching.
3.3.
H
$_2$
-driven mode switching: amplification and suppression of thermoacoustic oscillations
Figure 5 shows the response of the thermoacoustic system as the hydrogen concentration in the fuel blend is progressively increased from
$P_{\textrm{H}_2}$
= 0 to 0.7, with a corresponding decrease in
$P_{\textrm{CH}_4}$
, while
$P_{\textrm{NH}_3}$
= 0 is held constant. To characterise the dynamical states that the thermoacoustic system exhibits, we analyse the time trace, PSD and Poincaré map of
$p^\prime$
. We find that the system continues to exhibit self-excited limit cycle oscillations at low
${\rm H}_2$
enrichment levels (
$P_{\textrm{H}_2} \lt 0.10$
). The time trace (figure 5
a) shows peak oscillation amplitudes of approximately 500 Pa for
$p^\prime$
, with no significant amplitude modulation. The PSD plot (figure 5
b) displays a dominant spectral peak at
$f_1$
= 179 Hz, indicating periodic dynamics. The corresponding Poincaré map (figure 5
$c$
) shows a single cluster of points, indicative of period-1 limit cycle oscillations.
Response of the acoustic pressure fluctuations with increasing
$P_{\textrm{H}_2}$
(and decreasing
$P_{\textrm{CH}_4}$
) at fixed
$P_{\textrm{NH}_3} =$
0: (
$a$
) time series; (
$b$
) power spectral density and (
$c$
) Poincaré map of
$p^\prime$
in the combustor. The frequencies at the sharp peaks in the PSD are
$f_1 = 179$
and
$f_2 = 133$
Hz.

Figure 5. Long description
Panel A: Five line graphs show the time series of acoustic pressure fluctuations (p’) in Pascals (Pa) over time (t) in seconds. The graphs are color-coded: green, red, orange (two graphs), and blue. Panel B: Five power spectral density (PSD) graphs display the frequency (f) in Hertz (Hz) on the horizontal axis and PSD in decibels per Hertz (dB Hz^-1) on the vertical axis. The graphs are color-coded similarly to Panel A and show peaks at specific frequencies. Panel C: Five Poincaré maps illustrate the pressure fluctuations (p’) over time (t + τ) for different hydrogen fractions (P_H2). The maps are color-coded to match Panels A and B, with corresponding P_H2 values of 0.7, 0.5, 0.4, 0.3, and 0.
When methane fuel is further enriched with hydrogen by increasing the
${\rm H}_2$
fraction (
$P_{\textrm{H}_2}$
= 0.3) while proportionally reducing
$P_{\textrm{CH}_4}$
and maintaining
$P_{\textrm{NH}_3}$
= 0, the system undergoes an abrupt transition characterised by a marked increase in oscillation amplitudes. The time trace (figure 5
a) shows peak oscillation amplitudes of
$p^\prime$
exceeding 4000 Pa. The PSD (figure 5
b) reveals the emergence of a new dominant spectral peak at
$f_2$
= 133 Hz, along with residual traces of the fourth-harmonic ITA mode around
$f_1$
= 179 Hz. The pronounced amplitude modulations evident in the time trace suggest interactions between multiple incommensurate modes. This is further supported by the appearance of spectral peaks at linear combinations of
$f_1$
and
$f_2$
, which arise through nonlinear resonant three-wave interactions (Schmid, Henningson & Jankowski Reference Schmid, Henningson and Jankowski2002). The emergence of the new peak at
$f_2$
in the PSD indicates a mode-switching event induced by
${\rm H}_2$
enrichment. In the Poincaré map (figure 5
$c$
), the phase trajectory intercepts form a closed continuous ring, indicating that the trajectory in the phase portrait is not closed, but spirals aperiodically on the surface of a stable ergodic two-dimensional
$\mathbb{T}^2$
torus attractor. This behaviour is indicative of quasiperiodic oscillations and the transition from the periodic state to the quasiperiodic state via a Neimark
$-$
Sacker bifurcation. Such quasiperiodic states have been reported in various systems, including a forced self-excited low-density jet (Kushwaha et al. Reference Kushwaha, Worth, Dawson, Gupta and Li2022), a self-excited laminar thermoacoustic system (Kabiraj & Sujith Reference Kabiraj and Suijith2012) and acoustically forced laminar premixed flames (Guan et al. Reference Guan, Gupta, Kashinath and Li2019a
).
As the hydrogen content in the
${\rm CH}_4$
fuel blend is further increased to
$P_{\textrm{H}_2}$
= 0.4, the system continues to exhibit strong oscillations with peak amplitudes exceeding 4000 Pa. The time trace shows amplitude modulation, although it is less pronounced than observed at the lower hydrogen concentrations. The PSD shows a sharp peak at
$f_2$
, alongside the residual peak at
$f_1$
and shallow peaks at their linear combinations, indicating that the system remains in a quasiperiodic regime. The gradual increase in the amplitude of the
$f_2$
mode with concurrent suppression of the
$f_1$
mode indicates the diminishing influence of the fourth-harmonic ITA mode as hydrogen enrichment increases. This trend points to a systematic transition in the instability mechanism from fourth-harmonic-driven to one dominated by first-harmonic ITA dynamics, the physical origin of which we will investigate and demonstrate in detail in § 3.3.2. The Poincaré map (figure 5
$c$
) shows the structural deformation of the ergodic
$\mathbb{T}^2$
torus attractor, indicating the onset of a torus-death bifurcation. Notably, this transition occurs without a significant change in oscillation amplitudes, underscoring the subtle nature of the underlying dynamical transition.
As the hydrogen fraction in the
${\rm CH}_4{-}{\rm H}_2$
fuel blend is further increased to
$P_{\textrm{H}_2}$
= 0.5, the system undergoes a transition from a quasiperiodic state to a new dynamical state characterised by period-3 oscillations. In this state, the system continues to exhibit high-amplitude thermoacoustic oscillations, with the peak amplitude increasing from 4000 Pa to 5000 Pa. A distinguishing feature of this state is the complete suppression of the residual peak at
$f_1$
, which is associated with the fourth harmonic of the ITA mode. The PSD (figure 5
b) reveals sharp spectral peaks at
$f_2$
and its second (
$2f_2$
) and third harmonics (
$3f_2$
), all with comparable amplitudes, indicating the emergence of period-3 dynamics. This behaviour is further confirmed by the Poincaré map (figure 5
c), where the phase trajectory intercepts form three distinct clusters of points. This implies that the system transitions from an infinite period to a three-cycle repeating pattern. The time trace (figure 5
a) shows a waveform repeating every three cycles, a signature feature of period-3 oscillations, which are characterised by three dominant frequencies of comparable amplitudes.
These findings demonstrate that large-amplitude thermoacoustic oscillations are not limited to classical period-1 limit cycle oscillations, but can also arise during quasiperiodic or period-3 states. These findings are particularly significant because most active and passive control methods assume that a thermoacoustic system exhibits a limit cycle with a single dominant frequency and a fixed amplitude, in which the control measures are applied to disrupt the feedback. This assumption implies that such control strategies may not be optimal for suppressing high-amplitude oscillations in multi-fuel systems exhibiting complex nonlinear dynamics. The open-loop control of quasiperiodic and period-3 states, especially when the system is subjected to external acoustic forcing, would require a fundamentally different approach than that used for traditional limit cycle control (Guan et al. Reference Guan, Gupta, Wan and Li2019b ). These findings underscore the need for comprehensive thermoacoustic analysis of fuel blend systems to develop robust control strategies that can effectively suppress the rich spectrum of dynamical states encountered in fuel-flexible combustion systems.
When the
${\rm CH}_4$
fuel is enriched with
${\rm H}_2$
beyond
$P_{\textrm{H}_2}$
= 0.5, the thermoacoustic oscillation amplitudes decrease sharply, marking a transition from a period-3 state to an aperiodic state. The time trace (figure 5
a) demonstrates that the system exhibits aperiodic oscillations with peak pressure fluctuations (
$p^\prime$
) reduced in the range of 20
$-$
40 Pa. The aperiodic behaviour is further confirmed by the PSD (figure 5
b), which shows broadband spectral peaks instead of the distinct peaks at
$f_1$
or
$f_2$
that are characteristic of organised oscillations. The phase trajectory intercepts appear as an irregular structure in the Poincaré map (figure 5
c), indicating non-repetitive phase evolution characteristic of aperiodic oscillations. Such aperiodic oscillations in turbulent swirl combustors arise when turbulence-induced fluctuations dominate the heat release rate, and the flame–acoustic coupling becomes too weak to sustain instabilities. These observations collectively indicate that this state is consistent with stable combustion, often referred to as combustion noise (Strahle Reference Strahle1978), in which random fluctuations dominate organised thermoacoustic feedback mechanisms.
These diverse dynamical states observed in the present study are not limited to the
${\rm CH}_4{-}{\rm H}_2$
fuel blend alone, but are also encountered when the fuel blends are enriched with ammonia up to
$P_{\textrm{NH}_3}\leq 0.2$
. To illustrate this, figures 6 and 7 present data analogous to figure 5, but for ammonia concentrations of
$P_{\textrm{NH}_3}$
= 0.1 and
$P_{\textrm{NH}_3}$
= 0.2, respectively. From figures 6 and 7, it is evident that, as the hydrogen fraction is progressively increased, the system undergoes a similar sequence of dynamical transitions as observed in the previous case. For the
${\rm CH}_4$
–
${\rm NH}_3$
fuel blend with
$P_{\textrm{NH}_3}\leq 0.2$
, the system transitions from limit cycle oscillations at
$P_{\textrm{H}_2} = 0$
to quasiperiodic oscillations as the hydrogen fraction is increased to the range
$P_{\textrm{H}_2}$
= 0.2
$-$
0.3. As observed previously, this quasiperiodic state is marked by the emergence of a new incommensurate mode at
$f_2$
in the PSD, alongside the fourth-harmonic ITA mode,
$f_1$
. At higher hydrogen enrichment levels (
$P_{\textrm{H}_2}$
= 0.5), the system transitions into a period-3 state with a dominant peak at
$f_2$
and its harmonics (2
$f_2$
and
$3f_2$
), a response consistent with the behaviour observed at
$P_{\textrm{NH}_3}$
= 0. As before, this newly emergent
$f_2$
mode remains spectrally distinct from the fourth-harmonic ITA mode
$f_1$
and its harmonics, highlighting a similar shift in the mechanism driving the thermoacoustic instability. When the hydrogen fraction is further increased to
$P_{\textrm{H}_2}\geq 0.6$
, the thermoacoustic oscillation amplitudes decrease drastically and the system transitions to an aperiodic state with peak oscillation amplitudes in the range of 20
$-$
40 Pa. These findings demonstrate that the dynamical transition pathways are robust across different fuel blend compositions, with ammonia enrichment up to 20
$\,\%$
having minimal impact on the hydrogen-induced mode switching behaviour.
Similar to figure 5, but at a slightly higher and fixed ammonia fraction (
$P_{\textrm{NH}_3} = 0.10$
).

Similar to figure 5, but at a slightly higher and fixed ammonia fraction (
$P_{\textrm{NH}_3} = 0.20$
).

Figure 7. Long description
Panel A: Five line graphs show pressure fluctuations over time. The y-axis represents pressure in Pascals, and the x-axis represents time in seconds. The graphs display different pressure fluctuation patterns. Panel B: Five line graphs show power spectral density. The y-axis represents power spectral density in decibels per Hertz, and the x-axis represents frequency in Hertz. The graphs display different spectral density patterns with marked frequencies. Panel C: Four scatter plots show pressure fluctuations in a phase space. Each plot represents different conditions with varying power levels.
3.3.1. Convective scaling of the dominant thermoacoustic modes
We have shown that the thermoacoustic system exhibits distinct modal behaviours that depend critically on fuel composition. With pure
${\rm CH}_4$
fuel, the system exhibits periodic limit cycle oscillations at
$f_1 = 179$
Hz. Progressive hydrogen enrichment triggers the emergence of a different thermoacoustic mode, characterised by a spectral peak at
$f_2=133$
Hz that gradually becomes dominant with increasing
$P_{\textrm{H}_2}$
. The observed frequency reduction
$f_2\lt f_1$
provides crucial insight into the nature of this mode transition. While the addition of
${\rm H}_2$
to the fuel blend raises the hot gas temperature in the combustor, which would typically be expected to raise the acoustic mode frequency, the reduction in frequency from
$f_1$
to
$f_2$
indicates that the
$f_2$
mode does not originate from the cavity acoustic mechanism. Instead, this behaviour suggests a fundamentally different instability mechanism. To investigate this mode switching, we compare the mean flame structures of two representative cases: (i) instability at
$f_1$
for
$P_{\textrm{CH}_4}$
= 1 and
$P_{\textrm{H}_2}$
= 0; and (b) at
$f_2$
for
$P_{\textrm{CH}_4}$
= 0.3,
$P_{\textrm{H}_2}$
= 0.5 and
$P_{\textrm{NH}_3}$
= 0.2. Figure 8 reveals that mode switching is accompanied by dramatic flame morphological changes. The system unstable to the
$f_1$
mode produces a long V-shaped flame structure with its root anchored to the dump plane (figure 8
a). In contrast, the
$f_2$
mode results in a substantially shorter, flatter and more compact flame at the same thermal power (figure 8
b). This transformation is attributed to the higher diffusivity of
${\rm H}_2$
, which enhances the flame speed and modifies the Lewis number, thereby altering the flame propagation characteristics and local strain rates. The integrated heat release rate profiles along the length of the combustor (figure 8
c–d) reveal the upstream migration of peak intensity from
$x=30{-}60$
mm for the pure methane flame to
$x=15{-}45$
mm for the hydrogen-enriched flame (
$P_{\textrm{H}_2}$
= 0.5). This mode-dependent spatial restructuring of flame directly affects the underlying flame–acoustic coupling, modifying the thermoacoustic feedback mechanism.
Mean flame shape with respective integrated heat release rate in
$z$
-direction along the length of the combustor,
$x$
(mm): (
$a$
)
$P_{\textrm{H}_2} =$
0 (
$P_{\textrm{NH}_3} =$
0,
$P_{\textrm{CH}_4} =$
1.0) and (
$b$
)
$P_{\textrm{H}_2} =$
0.50 (
$P_{\textrm{NH}_3} =$
0.20,
$P_{\textrm{CH}_4} =$
0.30). (e) Variation in frequency of thermoacoustic oscillations at
$P_{\textrm{H}_2} =$
0 (
$P_{\textrm{NH}_3} =$
0,
$P_{\textrm{CH}_4} =$
1.0) and
$P_{\textrm{H}_2} =$
0.50 (
$P_{\textrm{NH}_3} =$
0.20,
$P_{\textrm{CH}_4} =$
0.30), as functions of mean flow velocity in the burner section.

To further elucidate the characteristics of the
$f_1$
and
$f_2$
modes, and gain insight into the underlying mode-switching mechanism, we examine their frequency scaling behaviour as a function of mean flow velocity. This approach allows an assessment of the sensitivity of each mode to convective time scales, thereby distinguishing whether the instability is governed by cavity acoustic resonance or by the flame-intrinsic feedback processes. Figure 8(e–f) shows the frequency scaling with mean flow velocity for two representative fuel compositions: (i) pure methane (
$P_{\textrm{CH}_4}$
= 1) and (ii) hydrogen-enriched fuel with
$P_{\textrm{H}_2}$
= 0.5,
$P_{\textrm{CH}_4}$
= 0.30 and
$P_{\textrm{NH}_3}$
= 0.2. It should be noted that an increase in the mean flow velocity at constant equivalence ratio occurs when the thermal power increases. For a combustor operating with pure
${\rm CH}_4$
, increasing thermal power from 2.4 kW to 4.3 kW causes the mean velocity to increase from 1.56 m s
$^{-1}$
to 2.86 m s
$^{-1}$
. Figure 8(e) shows that the dominant frequency increases linearly from 142 to 185 Hz as the mean velocity increases from 1.56 to 2.86 m s
$^{-1}$
. This relationship holds throughout the regime, indicating stable flame anchoring without blowout. Similarly, hydrogen-enriched operation with the fuel blend comprising
$P_{\textrm{CH}_4}$
= 0.30,
$P_{\textrm{H}_2}$
= 0.50 and
$P_{\textrm{NH}_3}$
= 0.30 reveals a consistent scaling trend. When thermal power increases from 3.8 to 4.9 kW, the mean velocity increases from 2.63 to 3.41 m s
$^{-1}$
. Figure 8(f) demonstrates that the dominant frequency varies linearly from 130 to 159 Hz, as the mean velocity progressively increases from 2.63 to 3.41 m s
$^{-1}$
, albeit with a different slope compared with the pure methane case. Regardless of whether the combustor operates with pure
${\rm CH}_4$
or hydrogen-enriched fuel blends, the linear scaling of frequency with the mean flow velocity observed in the two fuel configurations (figure 8
e–f) strongly suggests that the thermoacoustic mode is governed by characteristic time delays intrinsically associated with the flame response. This trend represents a hallmark of the ITA mode of instability. Unlike the acoustic cavity modes, which are eigenfrequencies determined by the combustor geometry, ITA modes arise from flame-intrinsic feedback mechanisms driven by convective time scales and upstream velocity perturbations (Bomberg et al. Reference Bomberg, Emmert and Polifke2015; Emmert et al. Reference Emmert, Bomberg and Polifke2015; Hoeijmakers et al. Reference Hoeijmakers, Kornilov, Arteaga, de Goey and Nijmeijer2016).
To provide a quantitative validation of the convective scaling behaviour, we employ the theoretical framework established by Albayrak et al. (Reference Albayrak, Steinbacher, Komarek and Polifke2018), which relates the ITA mode frequency to
$u_{\kern-2pt B}/L_{\kern-1pt F}$
, the inverse of the characteristic flame time scale, where
$L_{\kern-1pt F}$
is the flame length and
$u_{\kern-2pt B}$
is the mean flow velocity. This scaling is described by (3.1), which enables direct comparison between theoretically predicted and experimentally observed ITA mode frequencies across different operating conditions:
where indices 1 and 2 represent two different thermal power ratings of a combustor.
Figure 9(a–c) shows the mean flame structure at the
$f_2$
mode of instability at three mean flow velocities: (a) 3.1 m s
$^{-1}$
; (b) 3.52 m s
$^{-1}$
and (c) 3.93 m s
$^{-1}$
, corresponding to thermal power levels of 4500, 5100 and 5700 W, respectively. These conditions are associated with dominant spectral peaks in the PSD at 139.5, 148.5 and 159 Hz, respectively. As thermal power increases, the flame exhibits a marked increase in luminosity, indicating an intensified heat release rate, while the overall flame macrostructures remain largely unchanged. This trend is confirmed by the integrated heat release rate profiles shown in figure 9(d), which presents the streamwise distribution of this quantity, showing a clear intensity increase with increasing power input. Figure 9(d) also reveals that flame length, which is defined as the distance from the dump plane to the peak heat release location, increases from 28 to 32 mm as the thermal power rises from 4500 to 5700 W. Using these measured flame lengths
$L_{\kern-1pt F}$
and corresponding mean flow velocities
$u_{\kern-2pt B}$
, we compute the convective time scales (
$\tau _c = L_f/u_{\kern-2pt B}^{0.8}$
) to be approximately 18.8, 17.4, and 15.8 ms for the three operating conditions, respectively. These time scales characterise the intrinsic flame response and will be instrumental in interpreting the network model analysis presented in § 3.3.2. To evaluate whether the observed frequency evolution of the
$f_2$
mode adheres to convective scaling, we apply the relation outlined in (3.1), which links the dominant frequency to the inverse of the flame time scale. Figure 9(e) demonstrates a strong agreement between the theoretically predicted and experimentally observed frequency trends, demonstrating that ITA modes are fundamentally governed by convective transport processes within the flame, thereby distinguishing ITA modes from the acoustic modes.
(
$a$
) Heat release rate integrated in z-direction along the length of the combustor at three different thermal power (i.e. mean flow velocity) conditions (
$P_{\textrm{H}_2}$
= 0.50,
$P_{\textrm{NH}_3}$
= 0.20,
$P_{\textrm{CH}_4}$
= 0.30) and the respective mean flame shapes: (
$b$
)
$k=$
4500 W; (
$c$
)
$k=$
5100 W and (
$d$
)
$k=$
5700 W. (e) Normalised change in the dominant ITA frequency as a function of the bulk flow velocity within the burner for the three thermal powers, the red solid line shows the trend for the model and dotted is from experimental.

Figure 9. Long description
The image contains multiple graphs depicting heat release rates and flame shapes at different thermal power conditions and the normalized change in dominant frequency as a function of bulk flow velocity. Panel A: A heat map showing the heat release rate integrated in the z-direction along the length of the combustor at 4500 W. The x-axis represents the distance in millimeters, and the y-axis represents the height in millimeters. The color scale indicates the intensity of the heat release rate, ranging from 0 to 1. Panel B: A heat map showing the heat release rate at 5100 W. The axes and color scale are the same as in Panel A. Panel C: A heat map showing the heat release rate at 5700 W. The axes and color scale are the same as in Panels A and B. Panel D: A line graph showing the heat release rate as a function of distance along the combustor for three different thermal power conditions (4500 W, 5100 W, and 5700 W). The x-axis represents the distance in millimeters, and the y-axis represents the heat release rate. The graph includes three lines, each representing a different thermal power condition, with corresponding frequencies labeled. Panel E: A scatter plot showing the normalized change in the dominant intrinsic thermoacoustic (ITA) frequency as a function of the bulk flow velocity within the burner for the three thermal powers. The x-axis represents the bulk flow velocity in meters per second, and the y-axis represents the normalized change in the dominant ITA frequency. The plot includes data points and trend lines for both the model and experimental results.
3.3.2. Acoustic network approach for thermoacoustic mode prediction
Next, we use an acoustic network model to identify unstable eigenmodes and characterise flame-acoustic interactions within the combustor (detailed methodology provided in Appendix A). This approach enables systematic differentiation between acoustic cavity modes and intrinsic thermoacoustic (ITA) modes through eigenfrequency analysis in the complex plane. We represent the thermoacoustic system as a network of three interconnected acoustic elements: a plenum, a burner and a combustion chamber, within which one-dimensional acoustic wave propagation is assumed. The model assumes uniform cold flow properties (
$T_u$
= 293 K) in the plenum and burner sections, while the combustion chamber temperature is set to
$T_d$
= 1600 K to reflect realistic operating conditions. The geometric parameters corresponding to the experimental configuration are summarised in table 1. We model the flame as a compact heat source located at the combustion chamber inlet, characterising its unsteady dynamics with the
$n{-}\tau$
model:
$\digamma (s) = ne^{-s\tau }$
, where
$n \geqslant 0$
represents the interaction index that quantifies flame–acoustic coupling strength, and
$\tau \geqslant 0$
denotes the time delay between acoustic perturbations and heat-release-rate oscillations (Silva, Yong & Magri Reference Silva, Yong and Magri2019). To assess the stability characteristics of the system, we solve the eigenvalue problem numerically using the taX acoustic simulation software (Emmert Reference Emmert2016), computing eigenfrequencies across a wide range of flame interaction indices (
$n$
) and time delays (
$\tau$
). This parametric sweep enables the identification of different thermoacoustic modes and their dependence on flame response parameters (Silva Reference Silva2023).
Parameters for the acoustic network model. Thermodynamic properties are
$\bar {p} = 101325$
Pa and
$\gamma = 1.4$
.

Table 1. Long description
A table with three rows and three columns. The columns are labeled Section and Parameters. The rows list the sections as Plenum, Burner, and Combustor. For each section, the table provides the length, diameter, and temperature. Row 1: Section, Plenum; Parameters, Length, l 0 equals 0.2 meters; Diameter, d 0 equals 0.2 meters; T u equals 293 K. Row 2: Section, Burner; Parameters, Length, l 1 equals 0.3 meters; Diameter, d 1 equals 0.028 meters; T u equals 293 K. Row 3: Section, Combustor; Parameters, Length, l 2 equals 0.8 meters; Diameter, d 2 equals 0.075 meters; T d equals 1600 K.
Figure 10(a) presents a thermoacoustic stability map for
${\rm CH}_4$
combustion, displaying eigenfrequency loci in the complex plane defined by frequency (
$f$
) and growth rate (
$\sigma$
) coordinates. The analysis encompasses interaction indices
$n \in$
[0.05, 4] and time delays
$\tau \in$
[25, 27.8] ms, where
$\tau$
values are estimated from experimental measurements of pure
${\rm CH}_4$
flames. The thermoacoustic map reveals distinct eigenfrequency trajectories originating from three fundamental instability mechanisms: (i) the plenum Helmholtz mode at frequency
$f_H$
; (ii) the cavity acoustic mode at frequency
$f_{acoustic}$
and (iii) the intrinsic thermoacoustic (ITA) mode at frequency
$f_{\textit{ITA}}$
. Each mechanism exhibits characteristic behaviour that enables definitive mode identification. Cavity acoustic modes typically manifest as star-shaped spiral trajectories centred around specific frequencies, converging to natural eigenfrequencies of passive acoustic modes in the limit
$n\rightarrow 0$
(Silva & Polifke Reference Silva and Polifke2019; Orchini et al. Reference Orchini, Silva, Mensah and Moeck2020; Silva Reference Silva2023). Figure 10(a) shows that trajectories around
$f_{acoustic}$
approach 244 Hz, with large negative growth rates as
$n\rightarrow 0$
, regardless of variations in
$\tau$
. This behaviour indicates strongly damped cavity acoustic modes across the investigated parameter ranges. The stability map also reveals groups of clustered quasi-vertical trajectories characteristic of ITA modes. In the limit of
$n\rightarrow 0$
, the eigenfrequencies associated with these quasi-vertical trajectories exhibit highly negative growth rates, reflecting strong damping under weak flame–acoustic coupling conditions. This behaviour constitutes a defining characteristic of intrinsic thermoacoustic modes (Silva et al. Reference Silva, Yong and Magri2019; Silva Reference Silva2023). For non-zero values of
$n$
and
$\tau$
, the network model predicts an infinite number of intrinsic modes (Mukherjee & Shrira Reference Mukherjee and Shrira2017; Albayrak et al. Reference Albayrak, Steinbacher, Komarek and Polifke2018). In the present study, we show only the first nine intrinsic modes in the stability map for visual clarity. Each trajectory cluster represents a different harmonic of
$f_{\textit{ITA}}$
, with the flame-intrinsic frequencies given by
$f = (2n_m+1)/2\tau$
, where
$n_m$
denotes the mode number. Along a given trajectory,
$n$
varies while
$\tau$
remains constant. Figure 10(a) demonstrates that these ITA modes become unstable when
$n$
exceeds a critical threshold within the time delay range
$\tau \in$
[25, 27.8] ms. Variation in
$\tau$
causes progressive horizontal shifts in ITA trajectories. Specifically, increasing
$\tau$
decreases the eigenfrequency of ITA modes, consistent with the inverse relationship prescribed by the intrinsic frequency formula. When convective time delays derived from pure
${\rm CH}_4$
combustion are used, the predicted frequencies spanning 155 to 185 Hz (see figure 8
e), corresponding to the fourth harmonic of the ITA mode, demonstrate remarkable agreement with experimental observations. To validate this mode identification, figure 10(b) presents the experimentally observed dominant frequency
$f_1$
(open circular markers) as a function of
$\tau$
estimated from the pure
${\rm CH}_4$
flame. Theoretical modal lines (grey solid lines) represent the relationship
$f = (2n_m+1)/2\tau$
, linking ITA eigenfrequencies with mode number
$n_m$
and time delay
$\tau$
. The experimental dominant frequency closely follows the modal grid line corresponding to the fourth harmonic, providing compelling evidence for the intrinsic nature of the observed modes.
(a) Eigenfrequencies of the system with a wide range of flame interaction index (
$n=[0.05 {-} 4]$
) and the time delay (
$\tau = [25{-}27.8]$
ms) computed using taX software. A closed inlet (R
$_{in}$
= 1) and an open outlet (R
$_{out}$
= −1) are considered. (b) Theoretical flame instrinsic thermoacoustic frequency
$f_{\textit{ITA}}$
as functions of
$\tau$
for different mode number, with
$f_{\textit{ITA}}$
given by
$ (2n_m+1)/2\tau$
. The time delay values are determined from
$\tau = L/u_{\kern-2pt B}^{0.8}$
, accounting for variations in flame length
$L$
and bulk velocity
$u_{\kern-2pt B}$
for pure
${\rm CH}_4$
flame, as demonstrated in figure 8(e).

Next, we perform the network analysis to predict the thermoacoustic eigenfrequencies and identify mode-switching behaviour during hydrogen-enriched combustion. As shown previously (figure 8), hydrogen enrichment substantially reduces the flame length from 51 mm (for pure
${\rm CH}_4$
) to 28 mm (for
$P_{\textrm{H}_2}$
= 0.5), causing time delays to decrease from approximately
$\tau$
= 25 ms to 11 ms. This reduction in characteristic time scales fundamentally alters the thermoacoustic behaviour. Figure 11(a) shows a thermoacoustic stability map obtained from the network analysis. The same interaction indices
$n \in$
[0.05, 4] are used as before, but with updated time delays
$\tau \in$
[10.7, 12.8] ms, estimated from experimental measurements of
${\rm H}_2$
-enriched fuel combustion. When this physically appropriate convective time delay is used in the network analysis, the model reliably identifies the ITA mode characteristics under these modified conditions. As before, the stability map shows quasi-vertical trajectories in the complex plane with highly negative growth rates in the limit
$n\rightarrow 0$
, reflecting strong damping under weak flame–acoustic coupling conditions. When
$n$
exceeds a threshold value, the eigenfrequency trajectory intersects the neutral stability axis at specific frequencies given by
$f = (2n_m+1)/2\tau$
. A comparison between the thermoacoustic map (figure 11
a) and the experimentally observed frequencies (figure 11
b) reveals remarkable agreement. The eigenfrequencies of the first harmonic of the ITA mode demonstrate excellent correspondence with the experimentally observed dominant frequencies. Specifically, ITA mode trajectories approach neutral stability at discrete frequencies
$f_2$
= 130–160 Hz (see figure 8
f) in the thermoacoustic map for convective time delays
$\tau _c \in$
[10.7–12.8] ms, which are the first harmonics of the ITA mode as seen in figure 11(b). This systematic frequency–time-delay relationship is consistent with the flame-intrinsic feedback mechanism that endows ITA modes with four distinctive characteristics that differentiate them from acoustic cavity modes: (i) their frequencies do not depend on the acoustic eigenfrequencies of the combustor (Silva Reference Silva2023); (ii) they become more unstable as acoustic losses increase (Silva et al. Reference Silva, Merk, Komarek and Polifke2017; Wildemans et al. Reference Wildemans, Kornilov, de Goey and Lopez Arteaga2023); (iii) the phase of the flame transfer function at ITA frequencies is close to
$-\pi$
(Xu et al. Reference Xu, Zheng, Wang, Feng, Tian, Li and Qi2021); (iv) and their frequencies scale with the convective time delay upstream of the flame,
$\tau$
(Albayrak et al. Reference Albayrak, Steinbacher, Komarek and Polifke2018). These characteristics have been confirmed across a wide range of configurations, from theoretical studies of simple configurations (Bomberg et al. Reference Bomberg, Emmert and Polifke2015; Emmert et al. Reference Emmert, Bomberg and Polifke2015; Hoeijmakers et al. Reference Hoeijmakers, Kornilov, Arteaga, de Goey and Nijmeijer2014) to experimental studies of laminar premixed flames (Hoeijmakers et al. Reference Hoeijmakers, Kornilov, Arteaga, de Goey and Nijmeijer2014; Wildemans et al. Reference Wildemans, Kornilov, de Goey and Lopez Arteaga2023), turbulent premixed swirl-stabilised combustors (Albayrak et al. Reference Albayrak, Steinbacher, Komarek and Polifke2018; Xu et al. Reference Xu, Zheng, Wang, Feng, Tian, Li and Qi2021) and partially premixed configurations (Murugesan et al. Reference Murugesan, Singaravelu, Kushwaha and Mariappan2018). The presence of the same essential ITA characteristics across both premixed and partially premixed configurations indicates that the underlying physics governing ITA modes is not tied to a specific premixing arrangement. The agreement with eigenfrequency, along with the convective scaling behaviour confirmed here, provides compelling evidence of
${\rm H}_2$
-driven mode switching. Collectively, these results indicate that hydrogen enrichment shifts the ITA eigenfrequency from the fourth harmonic (under pure
${\rm CH}_4$
conditions) to the first harmonic under
${\rm H}_2$
-enriched conditions with
$P_{\textrm{H}_2}$
= 0.5). This harmonic shift represents a fundamental change in the dominant instability mechanism rather than a simple frequency adjustment. The mode switching coincides with substantial changes in the flame macrostructure, which reduce the characteristic time scale and alter the thermoacoustic feedback mechanism. This correspondence between predicted eigenfrequency shifts and observed flame structure modifications provides corroborative evidence that flame time scales govern the intrinsic thermoacoustic feedback mechanism (Albayrak et al. Reference Albayrak, Steinbacher, Komarek and Polifke2018).
(a) Network analysis results for
${\rm H}_2$
-enriched conditions, analogous to figure 10(a) but for
${\rm H}_2$
enriched conditions, with time delay varied over the range
$\tau = [10.7{-}12.8]$
ms. (
$b$
) Theoretical flame instrinsic thermoacoustic frequency
$f_{\textit{ITA}}$
as a function of time delay
$\tau$
for different mode numbers
$n_m$
, where
$f_{\textit{ITA}}$
=
$ (2n_m+1)/2\tau$
. The time delay values are determined from
$\tau = L/u_{\kern-2pt B}^{0.8}$
, accounting for variations in flame length
$L$
and bulk velocity
$u_{\kern-2pt B}$
with
${\rm H}_2$
enrichment, as demonstrated in figure 8(f).

Figure 11. Long description
Panel A: A scatter plot shows the network analysis results for enriched conditions. The horizontal axis represents frequency (f) in Hertz, ranging from 0 to 350. The vertical axis represents sigma (σ), ranging from -200 to 50. The plot includes multiple data points colored from red to yellow, indicating different time delays (τ) in milliseconds. Key frequencies such as f_H, f_2, and f_acoustic are marked. Panel B: A line graph displays the theoretical flame intrinsic thermoacoustic frequency as a function of time delay (τ) in seconds. The horizontal axis ranges from 0 to 50 seconds, and the vertical axis ranges from 120 to 200 Hertz. The graph includes multiple lines representing different mode numbers (n_m) and red circles indicating experimental data points.
The network analysis thus successfully captures the physical basis for hydrogen-induced mode transitions through the systematic relationship between fuel composition, flame characteristics and eigenfrequency behaviour. The identification of harmonic shifts as the mechanism for mode switching provides crucial insights into the control of thermoacoustic instability. Unlike cavity acoustic modes that depend on combustor dimensions, ITA modes scale with flame properties and can be controlled through fuel composition modifications, offering new strategies for control of thermoacoustic instability in alternative fuel applications. In this subsection, we have shown that variation in the hydrogen content causes the thermoacoustic system to undergo nonlinear dynamical transitions accompanied by mode switching. Next, we examine the effects of ammonia addition on self-excited thermoacoustic instability.
3.3.3. Impact of
$\textit{NH}_{\it 3}$
enrichment in
$\textit{CH}_{\it 4}{-}\textit{H}_{\it 2}$
blends on thermoacoustic dynamics
As previously established, the thermoacoustic system operating with pure
${\rm CH}_4$
exhibits limit cycle oscillations with a dominant frequency of
$f_1$
= 179 Hz and peak amplitudes of approximately 500 Pa. When
${\rm CH}_4$
is enriched with
${\rm NH}_3$
by incrementally increasing the ammonia fraction from
$P_{\textrm{NH}_3}$
= 0–0.4 while simultaneously decreasing the methane fraction from
$P_{\textrm{CH}_4}$
= 1 to 0.6, while
$P_{\textrm{H}_2}$
is held constant at 0, the system continues to exhibit periodic oscillations, but with reduced oscillation amplitudes. This behaviour is evident from the time trace of
$p'$
(figure 12
a), which shows no significant amplitude modulation, and from the PSD (figure 12
d) where the dominant peaks remain at approximately 179 Hz. However, when
$P_{\textrm{NH}_3}$
is increased further to 0.6 with proportionally decreasing
$P_{\textrm{CH}_4}$
while keeping
$P_{\textrm{H}_2}$
fixed at 0, the oscillation amplitude decreases substantially to approximately 40 Pa and the signal becomes aperiodic, as evidenced by the time trace in figure 12(a). The corresponding PSD (figure 12
d) shows a shallow spectral peak, indicating the suppression of thermoacoustic instability. These findings demonstrate that while enrichment of
${\rm CH}_4$
with
${\rm NH}_3$
does not alter the nonlinear dynamical state, it can reduce the oscillation amplitudes. For
$P_{\textrm{NH}_3} \gt 0.70$
, the combustor fails to ignite, marking the combustion stability limit associated with high
${\rm NH}_3$
content.
(
$a{,}b{,}c$
) Time series and (
$d{,}e{,}f$
) power spectral density of
$p^\prime$
in the combustor at (
$a{,}d$
) limit cycle (
$P_{\textrm{H}_2} =$
0), (
$b{,}e$
) quasiperiodic (
$P_{\textrm{H}_2} =$
0.30) and (
$c{,}f$
) period-3 states (
$P_{\textrm{H}_2} =$
0.50) with increasing
$P_{\textrm{NH}_3}$
(and decreasing
$P_{\textrm{CH}_4}$
).

Figure 12. Long description
Panel A: Three line graphs show the time series of pressure oscillations in Pascals over time in seconds at different ammonia concentrations. The concentrations are 0.6, 0.4, 0.3, and 0 percent. Panel B: Three line graphs display the time series of pressure oscillations in Pascals over time in seconds at different ammonia concentrations. The concentrations are 0.6, 0.4, 0.3, and 0 percent. Panel C: Three line graphs illustrate the time series of pressure oscillations in Pascals over time in seconds at different ammonia concentrations. The concentrations are 0.5, 0.4, 0.3, and 0 percent. Panel D: Four line graphs present the power spectral density in decibels per Hertz against frequency in Hertz at different ammonia concentrations. The concentrations are 0.6, 0.4, 0.3, and 0 percent. Panel E: Four line graphs show the power spectral density in decibels per Hertz against frequency in Hertz at different ammonia concentrations. The concentrations are 0.6, 0.4, 0.3, and 0 percent. Panel F: Four line graphs depict the power spectral density in decibels per Hertz against frequency in Hertz at different ammonia concentrations. The concentrations are 0.5, 0.4, 0.3, and 0 percent.
Next, we examine the thermoacoustic behaviour when
${\rm NH}_3$
is introduced into the fuel blends containing a relatively high hydrogen fraction, specifically
$P_{\textrm{H}_2}$
= 0.3. Figure 12(b) shows that when the
${\rm CH}_4{-}{\rm H}_2$
fuel blend is enriched with
${\rm NH}_3$
at
$P_{\textrm{NH}_3}$
= 0.3, the system exhibits quasiperiodic oscillations
$-$
a continuation of the dynamical trend observed at lower
${\rm NH}_3$
fraction (
$P_{\textrm{NH}_3}$
= 0.1 and 0.2, as seen in figures 6 and 7). The time trace of
$p'$
(figure 12
b) shows more pronounced amplitude modulation than in the
${\rm NH}_3$
free fuel blend of
${\rm CH}_4{-}{\rm H}_2$
. This behaviour is corroborated by the PSD (figure 12
e), which reveals sharp peaks at
$f_1$
and
$f_2$
, and several additional peaks at their linear combinations, all of which are characteristic of quasiperiodic dynamics. As the
${\rm NH}_3$
fraction is further increased in the
${\rm CH}_4{-}{\rm H}_2$
fuel blend up to
$P_{\textrm{NH}_3}$
= 0.4, while
$P_{\textrm{H}_2}$
is held at 0.3, the system continues to exhibit quasiperiodic oscillations. While the oscillation amplitudes decrease slightly, the spectral amplitude at
$f_2$
remains strong, whereas that at
$f_1$
weakens considerably, as evidenced by the PSD in figure 12(e). This selective suppression suggests that
${\rm NH}_3$
enrichment preferentially suppresses the fourth-harmonic ITA mode
$f_1$
, while leaving the first-harmonic ITA mode relatively unaffected.
The dynamics of quasiperiodic oscillations are also clearly reflected in the phase-resolved chemiluminescence images shown in figure 13(a). These images depict one full cycle of the dominant low-frequency mode (
$\approx$
12 Hz) for a fuel blend of
$P_{\textrm{CH}_4}$
= 0.4,
$P_{\textrm{H}_2}$
= 0.3 and
$P_{\textrm{NH}_3}$
= 0.3. This frequency corresponds to
$|f_2-f_1|$
, as demonstrated by the PSD of time-resolved flame images in figure 13(b). Over the course of this cycle, a compact flame initially anchored near the dump plane undergoes contraction and reaches its minimum length before gradually elongating to its maximum extent. This cyclic variation in the flame length represents a process occurring on a slow time scale during which the flame undergoes near-quenching followed by re-ignition events. The coexistence of dynamics occurring on both slow and fast time scales during quasiperiodicity stands in stark contrast to the more stationary flame structure observed during limit cycle oscillations at
$P_{\textrm{CH}_4}$
= 1, where the mean flame shape remains largely unchanged. Similar flame dynamics, marked by transitions between near-extinction and full combustion, flame elongation, and pinch-off, have been reported in other thermoacoustic systems, including both laminar and turbulent premixed combustors (Kabiraj & Sujith Reference Kabiraj and Suijith2012; Liu et al. Reference Liu, Yang, Ruan, Yu, Nan, Li and Lu2024). When the
${\rm CH}_4{-}{\rm H}_2$
fuel blend is further enriched with
${\rm NH}_3$
at
$P_{\textrm{NH}_3}$
= 0.6, the system transitions from a quasiperiodic state to a periodic state, as evidenced by the time trace (figure 12
b). Figure 12(e) shows sharp spectral peaks at the
$f_2$
and its harmonics without any trace of the
$f_1$
mode in the PSD. This transition marks a shift from quasiperiodic to periodic oscillations, now governed by the first harmonic of the ITA mode. These results demonstrate that
${\rm NH}_3$
enrichment selectively suppresses the fourth-harmonic ITA mode while leaving the first-harmonic ITA mode largely unaffected. This selective suppression mechanism reveals fundamental differences in how fuel composition affects different harmonic modes within the ITA family. The oscillation amplitudes, however, remain considerably higher than those observed during the periodic state driven by the fourth-harmonic ITA mode, as seen in pure
${\rm CH}_4$
or
${\rm CH}_4{-}{\rm NH}_3$
combustion.
Sequence of phase-averaged flame images during one time period of the first dominant mode in quasiperiodic oscillations. The flame length shrinks to the minimum at
$t/T = 2/9$
and grows through re-ignition events at
$t/T = 3/9$
and
$t/T = 4/9$
. Flame length exhibits the highest variation at the slow time scale. This time period corresponds to the beating frequency of the amplitude modulations at quasiperiodicity.

Finally, we examine how the system responds when the
${\rm CH}_4{-}{\rm H}_2$
fuel blend with
$P_{\textrm{H}_2}$
= 0.5 is enriched with
${\rm NH}_3$
through incremental increases in
$P_{\textrm{NH}_3}$
. As shown earlier (§ 3.3), the system operating with
${\rm CH}_4{-}{\rm H}_2$
fuel blend at
$P_{\textrm{H}_2}$
= 0.5 exhibits period-3 oscillations, characterised by sharp spectral peaks at
$f_2$
,
$2f_2$
and
$3f_2$
of comparable amplitude in the PSD. Upon the introduction of
${\rm NH}_3$
at
$P_{\textrm{NH}_3}$
= 0.1, the system exhibits notable changes in both the frequency and oscillation amplitude. The dominant spectral peak shifts from 145 to 135 Hz, while the r.m.s. of
$p'$
rises from 2100 to 3000 Pa (not shown here for brevity). Further increases in
$P_{\textrm{NH}_3}$
(up to 0.5) result in minimal changes in the amplitude, indicating that the system enters a saturation regime. However, the dominant frequency gradually shifts back towards 145 Hz, approaching the original value observed in the absence of
${\rm NH}_3$
enrichment.
Figure 14(a) shows phase-averaged flame images at nine time instants spanning one cycle of the dominant mode (135 Hz) under period-3 oscillations. Unlike in the quasiperiodic case, in which the dominant flame frequency differs from that of
$p'$
, the dominant frequency observed in the PSD of time-resolved flame images (figure 14
b) closely matches the dominant peak in the PSD of
$p'$
(figure 12
f), further confirming the period-3 state. The phase-averaged images reveal a flatter and shorter flame with an M-shaped structure, which contrasts markedly with the V-shaped flame observed during period-1 oscillations. This transition of the flame macrostructure from a V-shaped to an M-shaped configuration has been previously observed upon the addition of hydrogen to turbulent swirl flames. This transition coincides with the onset of high-amplitude pressure oscillations (Schefer et al. Reference Schefer, Wicksall and Agrawal2002). While the flame length varies as it evolves through the cycle, the highest heat release rate remains concentrated in a narrow region close to the flame root. This behaviour is characteristic of higher
${\rm H}_2$
enrichment levels due to the greater reactivity of hydrogen. The intense heat release rate generates large-amplitude pressure oscillations, driven by a strong positive feedback coupling between unsteady heat release rate (
$q'$
) and acoustic pressure
$p'$
– a hallmark of robust thermoacoustic instability. This coupling mechanism is further corroborated by the spatially resolved Rayleigh index distribution shown in figure 15(b). This map quantifies the local spatial distribution of thermoacoustic driving and damping by measuring the time-integrated correlation between
$q^\prime$
and
$p^\prime$
at each point in the flame. A positive RI indicates a thermoacoustically active driving region (where
$q^\prime$
and
$p^\prime$
are in phase), while a negative RI indicates a damping region. Figure 15 reveals that the RI map of the
${\rm CH}_4$
flame exhibiting limit cycle oscillations is strikingly different from the
${\rm H}_2$
enriched flame that exhibits period-3 oscillations. Specifically, the spatial location of the driving region differs profoundly. For instance, during limit cycle oscillations, alternating driving and damping regions in the RI map of the pure
${\rm CH}_4$
flame (figure 15
$a$
) are distributed along the shear layer of the elongated V-shaped flame, with the zone of driving located near the flame root. The simultaneous occurrence of alternating in-phase and out-of-phase regions of
$q^\prime$
and
$p^\prime$
along the shear layer results in local cancellation and a moderate net integrated driving, leading to lower-amplitude oscillations (Ahn et al. Reference Ahn, Lee, Jung and Kim2018). In contrast, for the period-3 state (figure 15
$b$
), the positive RI is concentrated in a narrow, intense band close to the dump plane, enclosed by comparatively weak damping regions upstream and downstream. The flat and compact RI map for the
${\rm H}_2$
enriched flame is attributed to the higher reactivity and diffusivity of
${\rm H}_2$
. Furthermore, figure 15 also shows that the magnitude of the Rayleigh index is substantially larger for the period-3 state than for the limit cycle state. This elevated RI reflects the stronger positive feedback between
$p^\prime$
and
$q^\prime$
, leading to large-amplitude oscillations that are approximately one order of magnitude larger than those observed for the pure
${\rm CH}_4$
flame. The fundamental difference between these two states is also visible in the balance between the driving and damping regions of the corresponding RI map. Notably, both positive and negative RI regions are distributed symmetrically for the period-1 limit cycle state, reflecting a near-equilibrium balance between driving and dissipation characteristics. This balance is evidenced by the modest
$p'$
oscillation amplitudes during the limit cycle state. However, during the period-3 state, the positive RI substantially dominates the overall RI map, while the negative RI regions are either spatially confined to a narrow zone close to the flame anchoring location or weakly present at the flame tip. This pronounced asymmetry between driving and damping results in less local cancellation and a high integrated thermoacoustic driving, resulting in significantly large-amplitude thermoacoustic oscillations characteristic of the period-3 state. Furthermore, the RI map corresponding to the period-3 state also exhibits a degree of asymmetry across the constant
$z=0$
line that separates the top and bottom flame regions, suggesting lateral heat release oscillations that can arise due to the excitation of the azimuthal modes of the
${\rm H}_2$
enriched flame. Collectively, these observations highlight that the compact M-shaped flame driven at
$f_2$
of the
${\rm H}_2$
enriched flame is a more efficient thermoacoustic amplifier than the elongated V-shaped flame driven at
$f_1$
of the pure
${\rm CH}_4$
flame. The transition from the
$f_1$
limit cycle to the period-3 state represents not merely a quantitative increase in oscillation amplitude, but a qualitative change in the spatial organisation of thermoacoustic energy exchange.
Phase-averaged images during one time period of the dominant mode (
$f_2 = 133$
Hz) at period-3 cycle. The mean flame has a flat and ’M’ shape at this 50
$\,\%$
${\rm H}_2$
-rich condition.

Rayleigh index for (
$a$
) a limit cycle (
$P_{\textrm{H}_2}$
= 0) and (
$b$
) a period-3 cycle (
$P_{\textrm{H}_2}$
= 0.5), computed from
$p^\prime$
and time-resolved chemiluminescence images oscillating at the dominant frequencies
$f_1 = 179$
and
$f_2 = 133$
Hz, respectively. The Rayleigh index for a period-3 cycle is higher than that of a limit cycle, much like
$p^\prime$
is higher for a period-3 than for a limit cycle.

3.4. Spectral proper orthogonal decomposition
We have shown that the mean flame macrostructure exhibits distinct transitions as the system evolves through different dynamical states, progressing from limit cycle oscillations to quasiperiodicity and eventually to either a period-1 or period-3 state, depending on the degree of
${\rm H}_2$
and
${\rm NH}_3$
enrichment. These morphological changes indicate that flame dynamics play a fundamental role in mediating energy transfer to the acoustic field, thereby linking flame–acoustic coupling to dynamical state transitions in combustors (Schuller, Poinsot & Candel Reference Schuller, Poinsot and Candel2020). To gain deeper insights into how flame dynamics differ across these states, it is essential to analyse not only the time-averaged flame shape, but also the frequency-specific, spatially coherent heat-release-rate structures that drive these oscillations. We therefore employ spectral proper orthogonal decomposition (SPOD) to isolate dynamically dominant modes that are both spatially coherent and frequency-resolved (Towne, Schmidt & Colonius Reference Towne, Schmidt and Colonius2018; Karmarkar et al. Reference Karmarkar, Gupta, Boxx, Hemchandra and O’Connor2022). We prefer SPOD over conventional decomposition techniques such as proper orthogonal decomposition or dynamic mode decomposition because it generates energy-ranked modes that oscillate at a single frequency and maintain orthogonality in both space and time across ensembles (Schmidt et al. Reference Schmidt, Towne, Rigas, Colonius and Brès2018; Schmidt & Colonius Reference Schmidt and Colonius2020). This dual orthogonality is critical for reliably interpreting the evolution of coherent structures in systems exhibiting complex, multi-frequency behaviours, such as quasiperiodicity. We extract spectrally resolved coherent SPOD modes from 4000 time-resolved snapshots, the latter divided into 38 ensembles of 512 snapshots each with 50
$\,\%$
overlap between ensembles. The resulting SPOD modes, which are eigenvectors of a cross-spectral density (CSD) tensor, allow us to capture and quantify spatiotemporal coherence in the time-resolved flame data. These coherent structures provide deeper insights into the dominant structures governing thermoacoustic instability at specific frequencies (Karmarkar et al. Reference Karmarkar, Gupta, Boxx, Hemchandra and O’Connor2022). The SPOD analysis provides quantitative measures of spatial coherence and energy content for each frequency component, enabling systematic comparison of flame dynamics across different fuel compositions and dynamical states. This approach reveals how fuel composition modifications alter the spatial organisation of heat-release-rate fluctuations and their coupling to acoustic perturbations.
3.4.1. Limit cycle
Figure 16(a) shows the SPOD eigenvalue spectra as a function of frequency for the combustor operating with pure
${\rm CH}_4$
fuel (
$P_{\textrm{CH}_4}$
= 1) under limit cycle oscillations. The periodic nature of the thermoacoustic system is evident from the sharp dominant peak at
$f_1$
= 179 Hz in the SPOD spectrum, indicating that most of the energy is concentrated in mode 1, which exerts a greater influence on the flow field compared with other modes. The SPOD spectra also show a second dominant mode at the first harmonic of
$f_1$
, denoted as
$2f_1$
. This finding is consistent with the trend seen in the PSD of
$p'$
(figure 1), confirming the periodic characteristics. Figures 16(b) and 16(c) show the spatial distribution of the leading SPOD modes at
$f_1$
and
$2f_1$
, respectively. These dominant spatial modes manifest as a series of alternating positive and negative convective wavepackets, exhibiting axial oscillatory characteristics. Notably, these wavepackets are localised along the shear layers. The leading mode at
$2f_1$
is similar to the mode at
$f_1$
, particularly in its quasi-symmetric structure along the flame centreline. The wavepackets of both modes display a conical spatial distribution that mirrors the V-shaped flame geometry observed in high-speed chemiluminescence images (figure 2). Despite these similarities, there are also notable differences between the two modes. Specifically, the wavepackets at
$f_1$
are longer and wider than those at
$2f_1$
, reflecting differences in the characteristic length scales of the respective oscillatory patterns. Furthermore, the wavepackets associated with the
$f_1$
mode are energetically more active near the flame root and extend downstream up to
$x \lt 50$
mm. By contrast, the wavepackets corresponding to the
$2f_1$
mode are more energetically dominant in the intermediate downstream region
$15\lt x\lt 30$
mm, while their intensity fluctuations appear significantly reduced near the flame root. This spatial differentiation suggests that the fundamental mode primarily governs flame dynamics in the near-field region, where flame anchoring and initial heat release occur, while the harmonic mode influences flame behaviour in the intermediate downstream region, where flame development and convective processes dominate. These distinct spatial signatures provide insights into the multiscale nature of thermoacoustic coupling in combustion systems operating under periodic limit cycle conditions
SPOD eigenvalue spectra as a function of frequency for (
$a$
) a limit cycle (
$P_{\textrm{H}_2}$
= 0), (
$d$
) a quasiperiodic state (
$P_{\textrm{H}_2}$
= 0.2) and (
$g$
) a period-3 cycle (
$P_{\textrm{H}_2}$
= 0.5). The SPOD mode shapes at first two dominant modes for (
$b{,}c$
) a limit cycle (
$P_{\textrm{H}_2}$
= 0), (
$e{,}f$
) a quasiperiodic state (
$P_{\textrm{H}_2}$
= 0.2) and (
$h{,}i$
) a period-3 cycle (
$P_{\textrm{H}_2}$
= 0.5).

3.4.2. Quasiperiodicity
We now analyse the SPOD spectrum and coherent flame structures during the quasiperiodic oscillations that emerge with increasing hydrogen enrichment in the range
$0.3\lt P_{\textrm{H}_2}\lt 0.5$
. Figure 16(d–f) show results analogous to figure 16(a–c), but for the quasiperiodic state. The SPOD spectrum in figure 16(d) for the quasiperiodic state (for
$P_{\textrm{H}_2} =$
0.3,
$P_{\textrm{NH}_3}$
= 0.2 and
$P_{\textrm{CH}_4}$
= 0.5) shows a dominant peak at 11 Hz, identified as beating frequency
$f_B = |f_2-f_1|$
. Subsequent energetic modes appear at
$f_1$
,
$f_2$
and several other frequencies that are linear combinations of
$f_1$
and
$f_2$
, a trend consistent with those observed in the PSD of
$p^\prime$
. Notably, the spectral amplitude of the SPOD mode at
$f_2$
exceeds that at
$f_1$
, reflecting the increasing dominance of the first-harmonic ITA mode with
${\rm H}_2$
enrichment. The significant difference in eigenvalues between the SPOD mode at
$f_B$
and those at
$f_1$
or
$f_2$
signifies that the
$f_B$
mode is the most energetically dominant mode during quasiperiodicity, governing the low-frequency quasiperiodic dynamics. Figure 16(e–f) shows the spatial distribution of coherent flame structures for SPOD modes at
$f_B$
and
$f_2$
, respectively. The convective wavepackets corresponding to the
$f_B$
mode (figure 16
e) extend downstream up to
$x=80$
mm, nearly spanning the entire combustor length
$L=80$
mm and exhibiting characteristics of lateral oscillations. These coherent structures indicate that the zone of pronounced heat-release-rate oscillations occurs near the downstream end of the combustor. This spatial distribution indicates that the elongated flame structure observed in figure 13 is linked to the beating frequency
$f_B$
, with oscillation dynamics governed by a slow-time-scale process. In contrast, figure 16(f) shows that the wavepacket corresponding to the
$f_2$
mode does not extend to the entire combustor length; instead, it remains confined to the downstream region
$x\lt 60$
mm. The alternating positive and negative wavepackets observed for the
$f_2$
mode are characteristic of dominant axial oscillations. However, traces of low-amplitude lateral oscillations are also observed around
$x\approx 20$
mm. While wavepackets near the flame root appear conical and symmetric about the flame centreline, those located farther downstream become increasingly asymmetric. This asymmetric distribution indicates non-uniform heat-release-rate oscillations around the centreline during quasiperiodic oscillations, reflecting the complex three-dimensional flame dynamics that emerge from the interaction between multiple incommensurate frequencies.
3.4.3. Period-3 cycle
Figure 16(g–i) shows the SPOD eigenvalue spectra and coherent flame structures of the two leading SPOD modes for a combustor exhibiting period-3 oscillations. This corresponds to a condition in which the combustor operates with a fuel blend of methane (
${\rm CH}_4$
) enriched with a sufficiently higher hydrogen concentration but a lower ammonia concentration:
$P_{\textrm{H}_2}$
= 0.5,
$P_{\textrm{NH}_3}$
= 0.2 and
$P_{\textrm{CH}_4}$
= 0.3. The SPOD spectra reveal that the two dominant peaks occur at
$f_2$
and its harmonics
$2f_2$
, and additional peaks correspond to its higher-order harmonics of
$f_2$
, indicating periodic dynamics. Figure 16(e–f) shows that the leading SPOD modes at
$f_2$
and
$2f_2$
share several key characteristics with those observed in the periodically oscillating combustor operating with pure
${\rm CH}_4$
fuel. These similarities include symmetrically distributed wavepackets along the flame centreline, and the presence of alternating positive and negative wavepackets for both leading SPOD modes at
$f_2$
and
$2f_2$
, suggesting the dominance of axial oscillations. Furthermore, the convective wavepackets corresponding to
$2f_2$
are shorter than those at
$f_2$
, consistent with the trend observed for their counterparts from the periodic state of figure 16(b,c). However, there are also notable disparities in the spatial distribution of coherent flame structures between these two different periodic states. Most prominently, the convective wavepackets corresponding to both
$f_2$
and
$2f_2$
appear substantially flatter, markedly different from the V-shaped spatial distribution of wavepackets observed for the periodic case operating with pure
${\rm CH}_4$
, as seen in figure 16(a–c). The flatter wavepacket geometry is consistent with the compact M-shaped flame observed in phase-averaged chemiluminescence images and indicates fundamental changes in the spatial organisation of heat-release-rate fluctuations. Furthermore, the presence of both positive and negative wavepackets along the lateral direction near the flame root for both SPOD modes, as seen in figure 16(g–h), suggests the occurrence of lateral oscillations in the heat-release-rate near the flame base. The inverted U-shaped wavepackets in the leading SPOD mode at
$f_2$
indicate a complex interaction between axially and laterally oscillating coherent flame structures arising during the period-3 dynamical state, which further distinguishes this state from the purely periodic case. Notably, the SPOD eigenvalue spectra do not show a dominant second harmonic of
$f_2$
(at 3
$f_2$
) with a comparable amplitude to that of
$f_2$
or
$2f_2$
. This is because the period-3 dynamics are damped by the
${\rm NH}_3$
enrichment, as evident from the time trace in figures 6 and 7.
In summary, we have shown that hydrogen enrichment not only significantly modifies the thermoacoustic behaviour, but also fundamentally alters the coherent flame structures. These changes fundamentally alter the spatial distribution of the heat release rate within the combustor, with direct consequences for the thermoacoustic feedback mechanism. We also find that the convective wavepackets associated with the flame morphology can exhibit distinct characteristics even between ostensibly similar periodic states, depending on the underlying instability mechanism.
4. Conclusions
In this study, we have experimentally explored the nonlinear thermoacoustic behaviour of a turbulent swirl-stabilised combustor operating with various ternary fuel blends of methane (
${\rm CH}_4$
), hydrogen (
${\rm H}_2$
) and ammonia (
${\rm NH}_3$
). By adopting a dynamical systems approach, we have systematically examined how fuel composition affects the emergence of different instability modes and associated flame morphologies. Our findings directly address the key research questions posed in § 1.4 and are summarised now.
-
(i) Can variation in blended fuel composition influence the thermoacoustic mode switching? If so, what are the accompanying nonlinear dynamical states and flame morphology associated with these transitions?
We have demonstrated that variations in fuel composition strongly influence the nature of thermoacoustic instability modes. When operating on pure methane fuel, the combustor exhibits limit-cycle oscillations associated with the fourth-harmonic ITA mode of instability (
$f_1$
). However, when methane or methane–ammonia fuel blends are progressively enriched with hydrogen, the system transitions from limit cycle states to quasiperiodic states at
$P_{\textrm{H}_2}\lt 0.3$
and eventually to a period-3 state at
$P_{\textrm{H}_2}\gt 0.4$
. This transition is marked by the emergence of a new frequency
$f_2$
, which becomes the dominant frequency at higher
$P_{\textrm{H}_2}$
values. Crucially, we have shown that the emergent
$f_2$
mode corresponds to the first harmonic of the ITA mode, distinct from the fourth-harmonic ITA mode observed during pure methane combustion. Both frequencies scale with the mean flow velocity rather than the acoustic eigenfrequencies of the combustion chamber, confirming their flame-intrinsic thermoacoustic nature. This represents a systematic mode-switching within the ITA mode family, driven by fuel composition variations. Furthermore, we have demonstrated that this mode-switching is accompanied by distinct changes in the flame morphology. Specifically, flame structures undergo a transition from elongated, V-shaped configurations during fourth-harmonic ITA mode instability to compact, flat M-shaped flames observed during first-harmonic ITA instability. This morphological transition directly correlates with the redistribution of heat release and the enhanced flame-acoustic coupling mechanisms. -
(ii) If the addition of carbon-free fuel can alter the nonlinear dynamical state of the combustion system, what are the specific fuel compositions at which thermoacoustic amplitude is most significantly reduced or amplified?
The ternary plots mapping the
${\rm CH}_4{-}{\rm H}_2{-}{\rm NH}_3$
blend space have revealed critical regions where thermoacoustic instabilities are either amplified or suppressed. These maps demonstrate that the impact of carbon-free fuels (
${\rm NH}_3$
and
${\rm H}_2$
) on thermoacoustic instability is strongly dependent on the fuel blend ratio. We have identified critical fuel compositions that can amplify or suppress thermoacoustic oscillations. Specifically, we have found that hydrogen enrichment of up to
$50\,\%$
leads to significant amplification of thermoacoustic instability and triggers a systematic transition within the ITA mode family. Pure methane operation exhibits ITA mode instability at the fourth harmonic, while progressive hydrogen enrichment shifts the dominant instability to the first harmonic of the ITA mode, accompanied by a significant increase in the amplitude. Conversely, ammonia enrichment of pure methane fuel acts as a stabilising mechanism, effectively suppressing thermoacoustic oscillation associated with the fourth-harmonic ITA mode. This stabilising effect demonstrates the potential of ammonia as a natural damping mechanism for controlling intrinsic thermoacoustic instabilities. However, at high hydrogen concentrations (
$P_{\textrm{H}_2} \approx 0.50$
) where the first-harmonic ITA mode dominates, oscillation amplitudes remain largely unaffected by further ammonia enrichment, indicating that the stabilising mechanism is specific to the fourth-harmonic mode. Moreover, at excessive ammonia concentrations (
$P_{\textrm{NH}_3} \gt 0.70$
), the system fails to sustain stable combustion, thereby defining practical operability boundaries for fuel-blend compositions. These insights are critical for designing fuel-flexible combustion systems that can mitigate thermoacoustic instability risks. -
(iii) Can a low-order acoustic network model be used to identify and distinguish acoustic cavity modes and intrinsic thermoacoustic modes in combustion systems exhibiting thermoacoustic instability, and to understand the underlying mechanisms driving these instabilities?
We have demonstrated that a low-order acoustic network model coupled with an
$n{-}\tau$
flame response function, which captures a generalised flame response to acoustic perturbations, offers a robust framework for identifying and classifying thermoacoustic instability modes. We have shown that the eigenfrequency loci produced by the network model form two distinct classes of trajectories in the complex frequency plane: star-shaped spirals and quasi-vertical branches. These eigenfrequency loci serve as definitive markers for differentiating between the cavity acoustic mode and the ITA mode. Specifically, cavity acoustic modes are identified by frequency trajectories that spiral around fixed centre points, whereas ITA modes are characterised by trajectories that diverge towards highly negative growth rates as
$n\rightarrow 0$
, reflecting their strongly damped nature in the absence of flame–acoustic coupling. Furthermore, using a semiempirical relation, we have shown that the ITA mode exhibits convective time scaling, with its frequency dependent on the bulk velocity and the characteristic flame time scale. In contrast, the acoustic cavity mode exhibits weak sensitivity to flow or flame properties. The classification of these two modes reveals the underlying physics of flame–acoustic interactions and the thermoacoustic mode selection mechanism.
Regarding the future works, several important directions emerge. First, flame transfer function (FTF) measurements across different fuel-blend compositions deserve attention to pursue and quantify the time delays, and gain characteristics governing the observed instability mechanisms. Such measurements will provide deeper insight into the fundamental coupling among fuel composition, flame dynamics and thermoacoustic feedback, enabling predictive modelling of mode transitions in multi-fuel combustion systems. Our next step is to explore the influence of acoustic boundary conditions on ITA mode dynamics by systematically varying the combustor exit area ratio, thereby modifying the acoustic reflectivity at the downstream boundary, and assessing its effect on ITA harmonic switching and nonlinear dynamical transitions. Extending these findings to elevated operating pressures relevant to practical gas turbine applications will be essential for assessing the robustness of the identified ITA mode switching mechanism under industrially relevant conditions. Finally, developing active control strategies tailored to ITA-driven instabilities in multi-fuel systems, particularly those exhibiting quasiperiodic and period-3 dynamics, represents a further important avenue for investigation.
Funding
M.M would like to acknowledge the financial support from the Science and Engineering Research Board, Department of Science and Technology, India (project number: CRG/2023/001277). A.R.S. is very grateful for the Prime Minister Research Fellowship (PMRF), India.
Declaration of interests
The authors report no conflict of interest.
Declaration of generative AI and AI-assisted technologies in the writing process
During the preparation of this work, the author(s) used CLAUDE.AI to improve the language and readability of the manuscript. After using this tool/service, the author(s) reviewed and edited the content as needed and take(s) full responsibility for the content of the publication.
Appendix A. Acoustic network model
We consider a one-dimensional acoustic network model of the experimental combustor to investigate the axial thermoacoustic modes (Poinsot & Veynante Reference Poinsot and Veynante2005; Polifke & Schram Reference Polifke and Schram2010). The system is composed of three duct elements: a plenum, a burner and a combustion chamber, as shown in figure 17. We employ the linearised Euler equations (LEEs) to describe the acoustic plane-wave propagation within each duct element, assuming one-dimensional wave propagation and neglecting viscous and thermal losses.
Acoustic network model of the thermoacoustic system under investigation.

where
$u'$
,
$p'$
and
$\dot {q}'$
represent the velocity, pressure and heat-release-rate fluctuations, respectively, while
$A$
,
$\bar {\rho }$
,
$c$
and
$\gamma$
denote the cross-sectional area, mean density, speed of sound and specific heat ratio, respectively. We assume that the interfaces at the junctions between the plenum and burner, the burner and combustion chamber, and the unsteady flame are acoustically compact. Under this assumption, the LEEs are integrated across each compact element to derive the acoustic jump conditions, which relate the complex amplitudes of the acoustic pressure and velocity upstream (
$\hat {p}_u$
,
$\hat {u}_u$
) and downstream (
$\hat {p}_d$
,
$\hat {u}_d$
) of each compact element. These jump conditions are expressed as
where
$\hat {\dot {Q}'}$
denotes the total heat release rate fluctuation from the flame. To solve the resulting system, we assume harmonic fluctuations of the form
$p' (x,t) = \textrm{Re}\, (\hat {p}(x) \exp (st))$
and
$u' (x,t)$
, where the Laplace variable
$s = \sigma + i\omega$
contains the growth rate
$\sigma$
and frequency
$\omega$
of the fluctuations. Under this assumption, the amplitudes of the upstream- and downstream-travelling waves are defined by (Rienstra & Hirschberg Reference Rienstra and Hirschberg1992)
The acoustic waves propagating in the plenum, the burner and the combustion chamber are represented in terms of the travelling wave amplitudes (
$f$
) and (
$g$
), and their respective transfer matrices as follows:
\begin{align} \begin{bmatrix} f_{{uc}} \\ g_{{uc}} \end{bmatrix} = \underbrace { \begin{bmatrix} e^{-sl_0/c_u} & 0 \\ 0 & e^{sl_0/c_u} \end{bmatrix} }_{T_p(s)} \begin{bmatrix} f_{{in}} \\ g_{{in}} \end{bmatrix}, \\[-28pt] \nonumber \end{align}
\begin{align} \begin{bmatrix} f_{{u}} \\ g_{{u}} \end{bmatrix} = \underbrace { \begin{bmatrix} e^{-sl_1/c_u} & 0 \\ 0 & e^{sl_1/c_u} \end{bmatrix} }_{T_b(s)} \begin{bmatrix} f_{{dc}} \\ g_{{dc}} \end{bmatrix}, \\[-28pt] \nonumber \end{align}
\begin{align} \begin{bmatrix} f_{{out}} \\ g_{{out}} \end{bmatrix} = \underbrace { \begin{bmatrix} e^{-sl_2/c_d} & 0 \\ 0 & e^{sl_2/c_d} \end{bmatrix} }_{T_{cc}(s)} \begin{bmatrix} f_{{d}} \\ g_{{d}} \end{bmatrix}. \\[-12pt] \nonumber\end{align}
Here,
$l_0$
,
$l_1$
and
$l_2$
denote the lengths of the plenum, the burner and the combustion chamber, respectively. The transfer matrix
$T_C$
accounts for the sudden area change at the junction between the plenum and the burner. Similarly, an equivalent transfer matrix is applied at the junction between the burner and the combustion chamber,
\begin{align} \begin{bmatrix} f_{dc} \\ g_{dc} \end{bmatrix} = \frac {1}{2} \underbrace { \begin{bmatrix} 1 + A_0/A_1 & 1 - A_0/A_1 \\[4pt] 1 - A_0/A_1 & 1 + A_0/A_1 \end{bmatrix} }_{T_C(s)} \begin{bmatrix} f_{uc} \\[4pt] g_{uc} \end{bmatrix}. \end{align}
The unsteady heat release from the flame is modelled as a compact source at the combustion chamber inlet, with its acoustic response characterised by the
$n{-}\tau$
flame transfer function introduced in § 3.3.2,
\begin{align} \digamma (s) = \frac {\hat {\dot {Q}'}/\bar {\dot {Q}'}}{\hat {u'}/\bar {u'}} = ne^{-s\tau }, \end{align}
where
$n$
and
$\tau$
denote the interaction index and the time delay of the flame, respectively. The jump conditions at the junction between the burner and the combustion chamber are derived by combining four key parameters: the flame response (
$\digamma (s)$
), the area ratio (
$A_1/A_2$
), the ratio of the specific acoustic impedances (
$\xi = \bar {\rho _u}c_u/\bar {\rho _d}c_d$
) and the temperature ratio across the flame (
$\theta = \bar {T}_d/\bar {T}_u - 1$
), which represents the normalised temperature rise from the cold reactants to the hot combustion products. Together, these parameters fully characterise the acoustic boundary conditions at the flame interface and govern the thermoacoustic coupling within the network model,
\begin{align} \begin{bmatrix} f_d \\[4pt] g_d \end{bmatrix} = \frac {1}{2} \underbrace { \begin{bmatrix} \xi + A_1/A_2 + A_1/A_2 \theta \digamma (s) & \xi - A_1/A_2 - A_1/A_2 \theta \digamma (s) \\[4pt] \xi - A_1/A_2 - A_1/A_2 \theta \digamma (s) & \xi + A_1/A_2 + A_1/A_2 \theta \digamma (s) \end{bmatrix} }_{T_F(s)} \begin{bmatrix} f_u \\[4pt] g_u \end{bmatrix} .\end{align}
The overall system transfer matrix
$T$
is assembled by multiplying the individual element transfer matrices in sequence, incorporating the acoustic boundary conditions at the plenum inlet and the combustor exit. The non-trivial solutions of the eigenvalue problem for the complex eigenfrequency
$s$
are obtained, which yield the thermoacoustic eigenfrequencies that characterise the stability behaviour of the complete thermoacoustic system,
\begin{align} \underbrace { \begin{bmatrix} 1 & -R_{t{in}} & 0 & 0 \\[4pt] 0 & 0 & -R_{{out}} & 1 \\[4pt] T_{11}(s) & T_{12}(s) & -1 & 0 \\[4pt] T_{21}(s) & T_{22}(s) & 0 & -1 \end{bmatrix} }_{M(s)} \begin{bmatrix} f_{{in}} \\[4pt] g_{{in}} \\[4pt] f_{{out}} \\[4pt] g_{{out}} \end{bmatrix} = \begin{bmatrix} 0 \\[4pt] 0 \\[4pt] 0 \\[4pt] 0 \end{bmatrix}, \\[0pt] \nonumber \end{align}
where
indicate the acoustic reflection coefficient at the inlet and outlet, respectively.



















a
(b)
60∘
(c)
5
14
∗
CH4
ϕ=0.85
k=
a
b
c
p′
f1=179
H2
NH3
CH4
a
b
Prms
ϕ=
k=
a,b
a
PH2=
PCH4
PH2
PNH3
PH2+PNH3+PCH4
PH2
PCH4
PNH3=
a
b
c
p′
f1=179
f2=133
PNH3=0.10
PNH3=0.20
z
x
a
PH2=
PNH3=
PCH4=
b
PH2=
PNH3=
PCH4=
PH2=
PNH3=
PCH4=
PH2=
PNH3=
PCH4=
a
PH2
PNH3
PCH4
b
k=
c
k=
d
k=
p¯=101325
γ=1.4
n=[0.05−4]
τ=[25−27.8]
in
out
fITA
τ
fITA
(2nm+1)/2τ
τ=L/uB0.8
L
uB
CH4
H2
H2
τ=[10.7−12.8]
b
fITA
τ
nm
fITA
(2nm+1)/2τ
τ=L/uB0.8
L
uB
H2
a,b,c
d,e,f
p′
a,d
PH2=
b,e
PH2=
c,f
PH2=
PNH3
PCH4
t/T=2/9
t/T=3/9
t/T=4/9
f2=133
%
H2
a
PH2
b
PH2
p′
f1=179
f2=133
p′
a
PH2
d
PH2
g
PH2
b,c
PH2
e,f
PH2
h,i
PH2