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Hydrogen economy transition plan: A case study on Ontario

  • # FE and AD contributed equally
  • A shift towards a "hydrogen economy" can reduce carbon emissions, increase penetration of variable renewable power generation into the grid, and improve energy security. The deployment of hydrogen technologies promises major contributions to fulfilling the economy's significant energy needs while also reducing urban pollution emissions and the overall carbon footprint and moving towards a circular economy. Using the Canadian province of Ontario as an example, this paper prioritizes certain recommendations for near-term policy actions, setting the stage for long-term progress to reach the zero-emissions target by 2050. To roll out hydrogen technologies in Ontario, we recommend promptly channeling efforts into deployment through several short-, mid-, and long-term strategies. Hydrogen refueling infrastructure on Highway 401 and 400 Corridors, electrolysis for the industrial sector, rail infrastructure and hydrogen locomotives, and hydrogen infrastructure for energy hubs and microgrids are included in strategies for the near term. With this infrastructure, more Class 8 large and heavy vehicles will be ready to be converted into hydrogen fuel cell power in the mid-term. Long-term actions such as Power-to-Gas, hydrogen-enriched natural gas, hydrogen as feedstock for products (e.g., ammonia and methanol), and seasonal and underground storage of hydrogen will require immediate financial and policy support for research and technology development.

    Citation: Faris Elmanakhly, Andre DaCosta, Brittany Berry, Robert Stasko, Michael Fowler, Xiao-Yu Wu. Hydrogen economy transition plan: A case study on Ontario[J]. AIMS Energy, 2021, 9(4): 775-811. doi: 10.3934/energy.2021036

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  • A shift towards a "hydrogen economy" can reduce carbon emissions, increase penetration of variable renewable power generation into the grid, and improve energy security. The deployment of hydrogen technologies promises major contributions to fulfilling the economy's significant energy needs while also reducing urban pollution emissions and the overall carbon footprint and moving towards a circular economy. Using the Canadian province of Ontario as an example, this paper prioritizes certain recommendations for near-term policy actions, setting the stage for long-term progress to reach the zero-emissions target by 2050. To roll out hydrogen technologies in Ontario, we recommend promptly channeling efforts into deployment through several short-, mid-, and long-term strategies. Hydrogen refueling infrastructure on Highway 401 and 400 Corridors, electrolysis for the industrial sector, rail infrastructure and hydrogen locomotives, and hydrogen infrastructure for energy hubs and microgrids are included in strategies for the near term. With this infrastructure, more Class 8 large and heavy vehicles will be ready to be converted into hydrogen fuel cell power in the mid-term. Long-term actions such as Power-to-Gas, hydrogen-enriched natural gas, hydrogen as feedstock for products (e.g., ammonia and methanol), and seasonal and underground storage of hydrogen will require immediate financial and policy support for research and technology development.



    Jellyfish plays an important role in the marine ecosystems as a keystone species and a potential resource for human consumption [1]. The amount of jellyfish has been significantly increasing in many waters since 1980s [2]. Jellyfish can be found in many regions worldwide such as Japan [3], the China Seas [4], the Mediterranean Sea [5], Taiwan [6], Southampton Water and Horsea Lake, England [7]. It can survive in a wide range of water temperatures $ (0- 36\; ^{\circ}C) $ and salinities $ (3- 36\%) $ [8,9].

    Jellyfish has a complex life history with several different phases: planula, polyp, strobila, ephyra and medusa [10]. The polyp and medusa are two main stages of the life cycle of jellyfish. Medusae are dioecious, the sperm combines with egg to form a planula, which normally settles to the bottom and then occur metamorphosis of planula into tentacles-ring polyp (or scyphistoma) [11]. For Aurelia aurita jellyfish, the scyphistoma produces external outgrowths asexually by budding, the vitally asexual reproduction of polyp ($ 94\% $), stolon ($ 5\% $) and podocysts ($ 1\% $) [3]. The scyphistoma changes into strobila (strobilating polyp) through strobilation, which is asexual reproduction by division into segments developing into ephyra. After liberating from strobila, the ephyra becomes adult medusa. In addition, strobila reverts into the initial scyphistoma [11]. Since jellyfish has a distinct mobility patterns in different phases of its life history, it is interesting to take these facts into account for model formulation.

    Temperature has a great effect on variations of jellyfish populations [12] as the asexual reproduction rate and strobilation rate depend on the functions of temperatures [11]. Global warming has affected the increase of jellyfish populations because it might cause the distribution, growth, and ephyrae production of medusae [13]. The rapid strobilation might be proceeded at the warmer temperature, but the continuous high temperature results in the fewer budding and increased mortality [6]. Hence the population explosions of polyps and medusae might be caused at the appropriate increase of temperature, but rising temperatures lead to the decreased populations.

    Many approaches for jellyfish have been developed to discuss the nature of the correlations between environmental indices and population abundance [6,14]. In particular, mathematical modeling is one of the important tools in analyzing the dynamical properties in aquatic systems. In [15], Oguz et al. presented food web model with an anchovy population and bioenergetics-based weight growth model governed by system of differential equations. In [16], Melica et al. conducted that the dynamics of polyps population by the logistic model. In [11], Xie et al. proposed the following two-dimensional dynamic model of scyphozoan jellyfish:

    $ \begin{equation} \begin{aligned} \frac{dP}{dt} = & \alpha(T)P+s_1\gamma M-d_1P-d_2P-b_1P^2, \\ \frac{dM}{dt} = & s_2\beta(T)nP-d_3M-d_4M-b_2M^2, \end{aligned} \end{equation} $ (1.1)

    where $ P(t) $ and $ M(t) $ are the population sizes of polyps and medusae at time $ t $, respectively. For system (1.1), by using the Bendixson-Dulac's negative criterion and Poincare-Bendixson Theorem, the conditions for the global asymptotical stability of the equilibria $ E_0 $, $ E_1 $ and $ E^* $ are given. The effects of temperature, substrate and predation on the population sizes of scyphozoan were investigated by numerical simulations.

    Although multiple progresses have been seen in the above work of [11], for system (1.1), it is assumed that each population preserves an equal density dependent rate and each individual has the same opportunity to compete for their common resources during the whole life history. Unfortunately, this is not realistic due to the life history of jellyfish which has a diverse mobility body structures in different stages. The immature stages of jellyfish are much weaker than the mature stages and so they cannot compete for their common resources. Jellyfish reaches maturity after surviving the immature stages. Therefore, it is realistic and interesting for us to construct the stage-structured jellyfish model that exhibits a diversity between these different stages.

    Recently, population dynamic models with stage structure and time delays have attracted more attention from authors [17,18,19,20,21,22,23,24]. For instance, Aiello and Freedman proposed a stage-structured model of single species containing of the immature and mature stages and using a discrete time delay taken from birth to maturity [18]. Liu et al. showed that the global stability for the two competitive Lotka-Volterra system with time delay that denotes the time taken from birth to maturity. They proposed that the stage structure is one of the main reasons that cause permanence and extinction for the two competitive system [23]. There have been an increasing interest and progress in the study of the above stage-structured models which assume all individuals are in the same species that require the analogous amount of time to become mature at the same age. Unlike birds and mammals, jellyfish species have the different mobility shapes in the distinctive stages of its life cycle. Thus, the previous methods and techniques cannot be applied exactly to our system because we classify the single species jellyfish into two-stage structure. Mathematically, the proposed model has two delay terms and the equations are matched with each other, which is not similar with the previous models [18,23,24].

    In this paper, we will propose a time-delayed jellyfish model with stage structure and will investigate how the stage structure parameters and temperature affect the dynamical behaviors of system (2.2). Our main purpose is to study the population dynamics of jellyfish for the largest surviving probability as well as for final population numbers. To find the largest surviving probability, we will take the global asymptotical behaviors of the model by applying the monotone dynamical properties (for reference, see [25] and [26,p. 90]).

    This paper is organized as follows: in Section 2, we propose the model and show that the solutions are positiveness and ultimately bounded. The main results of this paper are presented in Section 3. In Section 4, we perform numerical simulations to explore the effects of two delays and temperature on the dynamics. Section 5 is the brief discussion of our results.

    The life history of jellyfish is divided into two main stages; polyp and medusa. The larval stage of polyp is planula and the elementary phase of medusa is ephyra. Let $ P(t) $ and $ M(t) $ be the population size or number of polyps and medusae at time $ t $, respectively. The model is based on the following assumptions and the diagram in Figure 1:

    Figure 1.  Diagram of the model (2.1).

    $ \rm(A1) $ $ \tau_1 $ is the length of the stage from the young polyp to the mature polyp. The immature polyp reproduces asexually at time $ t-\tau_1 $ and surviving from time $ t-\tau_1 $ to $ t $ is $ e^{-(d_1+d_2)\tau_1} $.

    $ \rm(A2) $ $ \tau_2 $ is the time lag taken from the developed polyp to ephyra (incipient medusa), i.e., the developed polyp reaches ephyra after surviving this stage. Denote $ \tau = \max\lbrace{\tau_1, \tau_2}\rbrace $.

    $\rm (A3) $ Its maturity is denoted by $ \tau = \max\lbrace{\tau_1, \tau_2}\rbrace, \tau > 0 $.

    $ \rm(A4) $ Each population competes for their common resources.

    $ \rm(A5) $ Each population has its own natural death rate, the mortality of polyp is varied by the factors of silt coverage or nudibranch consumption while that of medusa is because of different types of predators.

    By the preceding assumptions, we get the following polyp-medusa population with stage structure:

    $ \begin{equation} \begin{array}{rcl} \frac{dP}{dt}& = &\alpha(T)e^{-(d_1+d_2)\tau_1}P(t-\tau_1)+s_1\gamma M-d_1P-d_2P-b_1P^2, \\[6pt] \frac{dM}{dt}& = &s_2\beta(T)ne^{-(d_3+d_4)\tau_2}P(t-\tau_2)-d_3M-d_4M-b_2M^2. \end{array} \end{equation} $ (2.1)

    As pointed out in [11], $ \alpha(T) $ denotes the asexual reproduction rate affected by temperature, involving budding, stolon and podocyst et al., $ s_1 $ is the survival and metamorphosis rate of planula, $ \gamma $ represents the sexual reproduction rate, $ b_1 $ and $ b_2 $ denote the density-dependent rates of polyps and medusae respectively, $ s_2 $ is the survival and development rate of ephyra, $ \beta(T) $ is the strobilation rate affected by temperature and $ n $ is strobilation times. Assuming that the death rate of the immature population is proportional to the existing immature population with proportionality constants $ d_i > 0 $, i = 1, 2, 3, 4. The loss of polyp is either due to natural death rate $ d_1 $ or due to the factors of silt coverage $ d_2 $ and $ \tau_1 $ is the time taken from the immature polyp to the mature one; thus $ e^{-(d_1+d_2)\tau_1} $ is the survival probability of each immature polyp to reach the mature one. The death of medusa is either from natural fatality rate $ d_3 $ or because of the predations $ d_4 $ and $ \tau_2 $ is the time length between the developed polyp and ephyra (incipient medusa); thus $ e^{-(d_3+d_4)\tau_2} $ is the survival rate of each developed polyp to reach the ephyra (incipient medusa) population. As it takes a few days in the larval stage of jellyfish life, the permanence and extinction criteria for the stage structured model are independent in this larval stage.

    For the goal of simplicity, we denote $ a = \alpha(T), $ $ b = s_1\gamma, $ $ d = d_1+d_2 $, $ c = s_2\beta(T)n, $ $ d_* = d_3+d_4 $. Thus the following system can be obtained from system (2.1).

    $ \begin{equation} \begin{array}{ll} \frac{dP}{dt} & = ae^{-\zeta_1}P(t-\tau_1)+bM-dP-b_1P^2, \\[6pt] \frac{dM}{dt} & = ce^{-\zeta_2}P(t-\tau_2)-d_*M-b_2M^2, \end{array} \end{equation} $ (2.2)

    where $ \zeta_1 = d\tau_1 $ and $ \zeta_2 = d_*\tau_2 $. Denote $ \zeta_1 $ and $ \zeta_2 $ the degrees of the stage structure.

    Let $ X = \mathcal{C}([-\tau, 0], \mathbb{R}^2) $ be the Banach space of all continuous function from $ [-\tau, 0] $ to $ \mathbb{R}^2 $ equipped with the supremum norm, where $ \tau = \max\lbrace{\tau_1, \tau_2}\rbrace $. By the standard theory of functional differential equations (see, for example, Hale and Verduyn Lunel [27]), for any $ \psi\in\mathcal{C}([-\tau, 0], \mathbb{R}^2) $, there exists a unique solution $ Y(t, \psi) = (P(t, \psi), M(t, \psi)) $ of system (2.2); which satisfies $ Y_0 = \psi $.

    For system (2.2), we consider the initial conditions to either the positive cone $ X^+ = \{\psi\in X|\mbox{ $\psi_i(\theta)\ge 0$ for all $\theta\in[-\tau, 0]$, $i = 1, 2$ }\} $ or the subset of $ X^+ $ of functions which are strictly positive at zero, $ X_0^+ = \lbrace{\psi\in X^+|\psi_i(0) > 0, i = 1, 2}\rbrace $.

    Lemma 2.1. For equation

    $ \begin{equation} \frac{d\overline{W}}{dt} = ae^{-\zeta_1}\overline{W}(t-\tau_1)+\frac{bce^{-\zeta_2}}{d_*}\overline{W}(t-\tau_2)-\frac{B}{2}\overline{W}^2, \end{equation} $ (2.3)

    where $ a, b, c, d_*, B > 0 $, $ \tau = \max\lbrace{\tau_1, \tau_2}\rbrace, \tau > 0 $ and $ \overline{W}(0) > 0 $ and $ \overline{W}(\theta)\ge 0 $, $ \theta\in[-\tau, 0] $, we have: $ \lim_{t\to\infty}\overline{W}(t) = \frac{2d_*ae^{-\zeta_1}+2bce^{-\zeta_2}}{d_*B} $ if $ d_*ae^{-\zeta_1}+bce^{-\zeta_2} > 0 $.

    Proof. By using the similar argument of Lu et al. [28,Proposition 1], we will prove that $ \overline{W}(t) > 0 $, for all $ t\ge0 $. Otherwise, there exists some constant $ \acute{t}_0 > 0 $ such that $ \min \lbrace{\overline{W}(\acute{t}_0)}\rbrace = 0. $ Let $ t_0 = \inf \lbrace{\acute{t}_0: \overline{W}(\acute{t}_0) = 0}\rbrace. $ Then we have that $ \min \lbrace{\overline{W}(t_0)} = 0\rbrace $ and $ \min \lbrace{\overline{W}(t)}\rbrace > 0 $, $ \forall t \in [0, t_0) $. From system (2.3), we have

    $ \begin{equation} \begin{aligned} \overline{W}(t)& = \overline{W}(0)e^{-\int_0^t \frac{B}{2}\overline{W}(\vartheta)d\vartheta}+ae^{-\zeta_1}\int_0^t \overline{W}(\omega-\tau_1)e^{-\int_\omega^t \frac{B}{2}\overline{W}(\vartheta)d\vartheta}d\omega\\ &+\frac{bce^{-\zeta_2}}{d_*}\int_0^t \overline{W}(\omega-\tau_2)e^{-\int_\omega^t \frac{B}{2}\overline{W}(\vartheta)d\vartheta}d\omega. \end{aligned} \end{equation} $ (2.4)

    Incorporation initial conditions and Eq (2.4), we get $ \overline{W}(t_0) > 0 $, contradicting $ \min \lbrace{\overline{W}(t_0)}\rbrace = 0 $. Consequently, $ \overline{W}(t) > 0 $ for all $ t \ge 0 $.

    Let $ \overline{W}^* = \frac{2d_*ae^{-\zeta_1}+2bce^{-\zeta_2}}{d_*B} $ denotes the unique positive equilibrium of system (2.3). Denote $ u(t) = \overline{W}(t)-\overline{W}^* $, thus system (2.3) takes the form as

    $ \begin{equation} \begin{aligned} \frac{du}{dt} = ae^{-\zeta_1}u(t-\tau_1)+\frac{bce^{-\zeta_2}}{d_*}u(t-\tau_2)-\frac{B}{2}u^2(t)-B\overline{W}^*u(t). \end{aligned} \end{equation} $ (2.5)

    Constructing the Lyapunov functional

    $ \begin{equation*} \begin{aligned} V(u, u_\tau) = \frac{1}{2}u^2(t)+\frac{1}{2}ae^{-\zeta_1}\int_{t-\tau_1}^{t}u^2(s)ds+\frac{1}{2}\frac{bce^{-\zeta_2}}{d_*}\int_{t-\tau_2}^{t}u^2(s)ds, \end{aligned} \end{equation*} $

    we have

    $ \begin{equation*} \begin{aligned} \left.\frac{dV}{dt}\right|_{(2.5)} = &ae^{-\zeta_1}u(t)u(t-\tau_1)+\frac{bce^{-\zeta_2}}{d_*}u(t)u(t-\tau_2)-\frac{B}{2}u^3(t)-B\overline{W}^*u^2(t)+\frac{1}{2}ae^{-\zeta_1}u^2(t)\\ &-\frac{1}{2}ae^{-\zeta_1}u^2(t-\tau_1)+ \frac{1}{2}\frac{bce^{-\zeta_2}}{d_*}u^2(t)-\frac{1}{2}\frac{bce^{-\zeta_2}}{d_*}u^2(t-\tau_2)\\ \le&\frac{1}{2} ae^{-\zeta_1}u^2(t)+\frac{1}{2} ae^{-\zeta_1}u^2(t-\tau_1)+\frac{1}{2}\frac{bce^{-\zeta_2}}{d_*}u^2(t)+\frac{1}{2}\frac{bce^{-\zeta_2}}{d_*}u^2(t-\tau_2)-\frac{B}{2}u^3(t)\\ &-B\overline{W}^*u^2(t)+\frac{1}{2}ae^{-\zeta_1}u^2(t)-\frac{1}{2}ae^{-\zeta_1}u^2(t-\tau_1)+ \frac{1}{2}\frac{bce^{-\zeta_2}}{d_*}u^2(t)-\frac{1}{2}\frac{bce^{-\zeta_2}}{d_*}u^2(t-\tau_2)\\ = &ae^{-\zeta_1}u^2(t)+\frac{bce^{-\zeta_2}}{d_*}u^2(t)-B\overline{W}^*u^2(t)-\frac{B}{2}u^3(t)\\ = &(ae^{-\zeta_1}+\frac{bce^{-\zeta_2}}{d_*}-\frac{B}{2}\overline{W}^*)u^2(t)-(\overline{W}^*+u(t))\frac{B}{2}u^2(t)\\ = &-\frac{B}{2}\overline{W}(t)u^2(t)\le 0, \end{aligned} \end{equation*} $

    which is negative definite and $ \left.\frac{dV}{dt}\right|_{(2.5)} = 0 $ if and only if $ u = 0 $. By Lyapunov-LaSalle invariance principle ([29,Theorem 2.5.3]), we get $ \lim_{t\to\infty}\overline{W}(t) = \overline{W}^* = \frac{2d_*ae^{-\zeta_1}+2bce^{-\zeta_2}}{d_*B} $, this proves Lemma 2.1.

    Lemma 2.2. Given system (2.2), then:

    (I) Under the initial conditions, all the solutions of system (2.2) are positive for all $ t\ge 0 $.

    (II) Solutions of system (2.2) are ultimately bounded.

    Proof. (I) We start with proving the positivity of solutions by using the similar argument of Lu et al. [28,Proposition 1]. We will prove that $ P(t) > 0 $, $ M(t) > 0 $ for $ t\ge 0 $. Otherwise, there exists some constant $ \tilde{t}_0 > 0 $ such that $ \min\lbrace{P(\tilde{t}_0), M(\tilde{t}_0)\rbrace = 0} $. Let $ t_0 = \inf\lbrace{\tilde{t}_0:P(\tilde{t}_0) = 0, M(\tilde{t}_0) = 0}\rbrace $. Then we have that $ \min\lbrace{P(t_0), M(t_0)}\rbrace = 0 $ and $ \min\lbrace{P(t), M(t)}\rbrace > 0 $, $ \forall t\in[0, t_0) $. From system (2.2), we have

    $ \begin{equation} \left\{ \begin{aligned} P(t) = &P(0)e^{-\int_{0}^{t}(d+b_1P(\eta))d\eta}+ae^{-\zeta_1} \int_{0}^{t}P(\kappa-\tau_1)e^{-\int_{\kappa}^{t}(d+b_1P(\eta))d\eta} d\kappa\\ &+b\int_{0}^{t}M(\kappa)e^{-\int_{\kappa}^{t}(d+b_1P(\eta))d\eta} d\kappa, \\ M(t) = &M(0)e^{-\int_{0}^{t}(d_*+b_2M(\eta))d\eta} +ce^{-\zeta_2} \int_{0}^{t}P(\kappa-\tau_2)e^{-\int_{\kappa}^{t}(d_*+b_2M(\eta))d\eta} d\kappa. \end{aligned} \right. \end{equation} $ (2.6)

    Incorporation initial conditions and Eq (2.6), we obtain $ P(t_0) > 0 $ and $ M(t_0) > 0 $, contradicting $ \min\lbrace{P(t_0), M(t_0)}\rbrace = 0 $. Consequently, $ P(t) > 0 $, $ M(t) > 0 $ for all $ t\ge 0 $.

    (II) We show that the boundedness of solutions as follows.

    Let $ W = \frac{d_*}{b}P+M $. By system (2.2), we have

    $ \begin{equation*} \begin{aligned} \left.\frac{dW}{dt}\right|_{(2.2)} = &ae^{-\zeta_1}\frac{d_*}{b}P(t-\tau_1)+ce^{-\zeta_2}P(t-\tau_2)-\frac{dd_*}{b}P-\frac{d_*b_1}{b}P^2-b_2M^2\\ = &ae^{-\zeta_1}[\frac{d_*}{b}P(t-\tau_1)+M(t-\tau_1)]-ae^{-\zeta_1}M(t-\tau_1)+\frac{bce^{-\zeta_2}}{d_*}[\frac{d_*}{b}P(t-\tau_2)+M(t-\tau_2)]\\ &-\frac{bce^{-\zeta_2}}{d_*}M(t-\tau_2)-\frac{dd_*}{b}P-\frac{bb_1}{d_*}(\frac{d_*}{b}P)^2-b_2M^2\\ \le&ae^{-\zeta_1}W(t-\tau_1)+\frac{bce^{-\zeta_2}}{d_*}W(t-\tau_2)-B[(\frac{d_*}{b}P)^2+M^2], \end{aligned} \end{equation*} $

    where $ B: = \min{\{\frac{bb_1}{d_*}, b_2}\} $.

    $ \frac{dW}{dt}\le ae^{-\zeta_1}W(t-\tau_1)+\frac{bce^{-\zeta_2}}{d_*}W(t-\tau_2)-\frac{B}{2}W^2, $

    where $ -2((\frac{d_*}{b}P)^2+M^2)\le -(\frac{d_*}{b}P+M)^2 $.

    Consider the equation

    $ \begin{equation} \frac{d\overline{W}}{dt} = ae^{-\zeta_1}\overline{W}(t-\tau_1)+\frac{bce^{-\zeta_2}}{d_*}\overline{W}(t-\tau_2)-\frac{B}{2}\overline{W}^2. \end{equation} $ (2.7)

    By using Lemma 2.1 and Comparison Theorem, we get

    $ \limsup_{t\to\infty}W(t)\le \frac{2d_*ae^{-\zeta_1}+2bce^{-\zeta_2}}{d_*B} $, which implies $ P(t) $ and $ M(t) $ are ultimately bounded. This completes the proof of Lemma 2.2.

    The equilibria $ (P, M) $ of system (2.2) satisfies the following system

    $ \begin{equation} \begin{aligned} ae^{-\zeta_1}P+bM-dP-b_1P^2 = 0, \\ ce^{-\zeta_2}P-d_*M-b_2M^2 = 0. \end{aligned} \end{equation} $ (2.8)

    System (2.2) has the equilibria $ E_0 = (0, 0) $ for all parameter values and $ E_1 = (\frac{ae^{-\zeta_1}-d}{b_1}, 0) $ if $ ae^{-\zeta_1}-d > 0 $ and $ c = 0 $.

    Since Eq (2.8) can be rewritten as

    $ \begin{equation} \begin{aligned} (ae^{-\zeta_1}-d-b_1P)P& = -bM, \ \ ce^{-\zeta_2}P& = (d_*+b_2M)M. \end{aligned} \end{equation} $ (2.9)

    When $ PM\neq 0 $, from Eq (2.9) it follows that

    $ \begin{equation} \frac{ae^{-\zeta_1}-d-b_1P}{ce^{-\zeta_2}}+\frac{b}{d_*+b_2M} = 0. \end{equation} $ (2.10)

    Further, substituting $ P = \frac{(d_*+b_2M)M}{ce^{-\zeta_2}} $ into Eq (2.10) and we get

    $ \frac{ae^{-\zeta_1}-d-b_1 \frac{(d_*+b_2M)M}{ce^{-\zeta_2}}}{ce^{-\zeta_2}}+\frac{b}{d_*+b_2M} = 0. $

    Set

    $ F(M): = \frac{ae^{-\zeta_1}-d-b_1 \frac{(d_*+b_2M)M}{ce^{-\zeta_2}}}{ce^{-\zeta_2}}+\frac{b}{d_*+b_2M}, $

    thus $ F(M) $ is a decreasing function of $ M $ for any $ M > 0 $.

    Noting that the continuity and monotonicity of $ F(M) $ and that $ F(+\infty) < 0 $, furthermore since one can get $ F(0) > 0 $ provided that

    $ \begin{equation} (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} > 0, \ \ c\neq 0 \end{equation} $ (2.11)

    hold true, therefore we conclude that system (2.2) admits a unique positive equilibrium given Eq (2.11) is satisfied.

    The purpose of this section is to study the global stability of system (2.2).

    Now we consider the local stability of the equilibria. The characteristic equation of system (2.2) takes the form as follows;

    $ \begin{equation*} \det(\lambda I-G-H_1e^{-\lambda \tau_1}-H_2e^{-\lambda \tau_2}) = 0, \end{equation*} $

    where

    $ \begin{equation*} G = \begin{pmatrix} -d-2b_1P &b\\ 0&-d_*-2b_2M \end{pmatrix}, H_1 = \begin{pmatrix} ae^{-\zeta_1} &0\\ 0&0 \end{pmatrix}, H_2 = \begin{pmatrix} 0 &0\\ ce^{-\zeta_2}&0 \end{pmatrix}. \end{equation*} $

    Lemma 3.1. Suppose that $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} < 0 $, then the equilibrium $ E_0 = (0, 0) $ of system (2.2) is locally asymptotically stable.

    Proof. The characteristic equation of system (2.2) at the equilibrium $ E_0 $ is as follows:

    $ \begin{equation} C(\lambda): = (\lambda+d_*)(\lambda+d-ae^{-\zeta_1-\lambda\tau_1})-bce^{-\zeta_2-\lambda\tau_2} = 0. \end{equation} $ (3.1)

    To show that it is asymptotically stable under assumption $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} < 0 $, we just need to prove that the solutions of the characteristic equation $ C(\lambda) = 0 $ must have negative real parts. Let $ \lambda = u+iv $, where $ u $ and $ v $ are real numbers. Denote

    $ \begin{equation*} \begin{aligned} A_1 = &u+d_*, \qquad &B_1 = &v, \\ A_2 = &u+d-ae^{-\zeta_1-u\tau_1}\cos(v\tau_1), \qquad &B_2 = &v+ae^{-\zeta_1-u\tau_1}\sin(v\tau_1), \\ C_1 = &bce^{-\zeta_2-u\tau_2}\cos(v\tau_2), \qquad &C_2 = &-bce^{-\zeta_2-u\tau_2}\sin(v\tau_2). \end{aligned} \end{equation*} $

    Substituting $ \lambda $ by $ u+iv $ into Eq (3.1)

    $ \begin{equation*} \begin{aligned} A_1A_2-B_1B_2 = C_1, \quad A_1B_2+A_2B_1 = C_2. \end{aligned} \end{equation*} $

    Then

    $ \begin{equation} (A_1A_2)^2+(B_1B_2)^2+(A_1B_2)^2+(A_2B_1)^2 = (C_1)^2+(C_2)^2. \end{equation} $ (3.2)

    Assume that $ u\ge 0 $, then we get

    $ A_1\ge d_* > 0, \quad A_2\ge d-ae^{-\zeta_1} > 0. $

    Hence

    $ \begin{equation} \begin{aligned} (A_1A_2)^2 > ((d-ae^{-\zeta_1})d_*)^2. \end{aligned} \end{equation} $ (3.3)
    $ \begin{equation*} (A_1A_2)^2+(B_1B_2)^2+(A_1B_2)^2+(A_2B_1)^2 \ge (A_1A_2)^2 > ((d-ae^{-\zeta_1})d_*)^2. \end{equation*} $

    From Eq (3.2), we obtain

    $ \begin{equation*} \begin{aligned} (C_1)^2+(C_2)^2&\ge (A_1A_2)^2 > ((d-ae^{-\zeta_1})d_*)^2\\ (bce^{-\zeta_2})^2 (\cos^2(v\tau_2)+\sin^2(v\tau_2))&\ge (A_1A_2)^2 > ((d-ae^{-\zeta_1})d_*)^2\\ (bce^{-\zeta_2})^2&\ge (A_1A_2)^2 > ((d-ae^{-\zeta_1})d_*)^2. \end{aligned} \end{equation*} $

    Hence Eq (3.3) contradicts to the assumption $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} < 0 $, thus $ u < 0 $, which means $ \lambda $ must have negative real parts. This proves Lemma 3.1.

    Lemma 3.2. Suppose that $ ae^{-\zeta_1}-d > 0 $ and $ c = 0 $, then the equilibrium $ E_1 = (\frac{ae^{-\zeta_1}-d}{b_1}, 0) $ of system (2.2) is locally asymptotically stable.

    Proof. The characteristic equation of system (2.2) at the equilibrium $ E_1 $ is

    $ \begin{equation} \begin{aligned} X(\lambda): = (\lambda+d_*)(\lambda-d+2ae^{-\zeta_1}-ae^{-\zeta_1-\lambda\tau_1}) = 0. \end{aligned} \end{equation} $ (3.4)

    Then $ \lambda = -d_* $ is a negative root of the equation $ X(\lambda) = 0 $. Let $ \lambda-d+2ae^{-\zeta_1}-ae^{-\zeta_1-\lambda\tau_1} = 0 $; then if the root is $ \lambda = u+iv $, we have $ u+2ae^{-\zeta_1}-d-ae^{-\zeta_1-u\tau_1}\cos(v\tau_1) = 0 $. Assume that $ u\ge 0 $, then $ u+2ae^{-\zeta_1}-d-ae^{-\zeta_1-u\tau_1}\cos(v\tau_1)\ge ae^{-\zeta_1}-d > 0 $ is a contradiction, hence $ u < 0 $. This shows that all the roots of $ X(\lambda) = 0 $ must have negative real parts, and therefore $ E_1 $ is locally asymptotically stable. This proves Lemma 3.2.

    Lemma 3.3. Suppose that $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} > 0 $ and $ c\neq0 $, then the equilibrium $ E^* = (P^*, M^*) $ of system (2.2) is locally asymptotically stable.

    Proof. The characteristic equation of system (2.2) at the equilibrium $ E^* $ is

    $ \begin{equation*} \begin{aligned} (\lambda+d+2b_1P^*-ae^{-\zeta_1-\lambda\tau_1})(\lambda+d_*+2b_2M^*)-bce^{-\zeta_2-\lambda\tau_2} = 0. \end{aligned} \end{equation*} $

    To show that it is asymptotically stable under $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} > 0 $, we just need to prove that the solutions of the characteristic equation must have negative real parts. Let $ \lambda = u+iv $ where $ u $ and $ v $ are real numbers. Denote

    $ \begin{aligned} D_1 = &u+d+2b_1P^*-ae^{-\zeta_1-u\tau_1}\cos(v\tau_1), &E_1 = &v+ae^{-\zeta_1-u\tau_1}\sin(v\tau_1), \\ D_2 = &u+d_*+2b_2M^*, &E_2 = &v, \\ F_1 = &bce^{-\zeta_2-u\tau_2}\cos(v\tau_2), &F_2 = &-bce^{-\zeta_2-u\tau_2}\sin(v\tau_2). \end{aligned} $

    Substituting $ \lambda $ by $ u+iv $ into the above equation.

    $ \begin{equation*} \begin{aligned} D_1D_2-E_1E_2 = F_1, \quad D_1E_2+D_2E_1 = F_2. \end{aligned} \end{equation*} $

    Then

    $ \begin{equation} \begin{aligned} (D_1D_2)^2+(E_1E_2)^2+(D_1E_2)^2+(D_2E_1)^2 = (F_1)^2+(F_2)^2. \end{aligned} \end{equation} $ (3.5)

    Assume that $ u\ge 0 $, then we get

    $ \begin{equation*} \begin{aligned} D_1&\ge d+2b_1P^*-ae^{-\zeta_1} > d+2b_1 \frac{ae^{-\zeta_1}-d}{b_1}-ae^{-\zeta_1} = ae^{-\zeta_1}-d > 0, \\ D_2&\ge d_*+2b_2M^* = d_*+2b_2\frac{b_1(P^*)^2-(ae^{-\zeta_1}-d)P^*}{b_1}\\ & > d_*+2b_2 \frac {b_1(\frac{ae^{-\zeta_1}-d}{b_1})^2-(ae^{-\zeta_1}-d)(\frac{ae^{-\zeta_1}-d}{b_1})}{b_1} = d_* > 0. \end{aligned} \end{equation*} $

    Hence

    $ \begin{equation*} (D_1D_2)^2 > ((ae^{-\zeta_1}-d)d_*)^2. \end{equation*} $
    $ \begin{equation*} (D_1D_2)^2+(E_1E_2)^2+(D_1E_2)^2+(D_2E_1)^2 \ge (D_1D_2)^2 > ((ae^{-\zeta_1}-d)d_*)^2. \end{equation*} $

    By Eq (3.5), we get

    $ \begin{equation*} \begin{aligned} (F_1)^2+(F_2)^2\ge (D_1D_2)^2 & > ((ae^{-\zeta_1}-d)d_*)^2\\ (bce^{-\zeta_2})^2 (\cos^2(v\tau_2)+\sin^2(v\tau_2))&\ge (D_1D_2)^2 > ((ae^{-\zeta_1}-d)d_*)^2\\ (bce^{-\zeta_2})^2\ge (D_1D_2)^2& > ((ae^{-\zeta_1}-d)d_*)^2. \end{aligned} \end{equation*} $

    By assumption $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} > 0 $, which is a contradiction, thus $ u $ must be negative real parts. This completes the proof of Lemma 3.3.

    Before the details, we will present the notion from the literature [25]. We define

    $ x_t\in\mathcal{C}([-\tau, 0], \mathbb{R}^2), $

    by $ x_t(\theta) = x(t+\theta), \forall \theta\in[-\tau, 0] $. Consider a delay system

    $ \begin{equation} \begin{aligned} x'(t) = f(x_t), \end{aligned} \end{equation} $ (3.6)

    for which uniqueness of solutions is assumed, $ x(t, \psi) $ designates the solution of Eq (3.6) with initial condition $ x_0 = \psi $ $ (\psi\in\mathcal{C}) $.

    A non-negative equilibrium $ v = (v_p, v_m)\in \mathbb{R}^2 $ of system (2.2) is said to be globally attractive if $ Y(t)\to v $ as $ t\to\infty $, for all admissible solutions $ Y(t) $ of system (2.2). We say that $ v $ is globally asymptotically stable if it is stable and globally attractive.

    System (2.2) is written as Eq (3.6),

    $ \begin{equation} \begin{aligned} f_1(\psi) = &\psi_1(0)[-d-b_1\psi_1(0)]+ae^{-\zeta_1}\psi_1(-\tau_1)+b\psi_2(0), \\ f_2(\psi) = &\psi_2(0)[-d_*-b_2\psi_2(0)]+ce^{-\zeta_2}\psi_1(-\tau_2). \end{aligned} \end{equation} $ (3.7)

    Observe that system (2.2) is cooperative, i.e., $ Df_i(\psi)\varphi\ge 0 $, for all $ \psi, \varphi\in X^+ $ with $ \varphi_i(0) = 0, i = 1, 2 $. This implies that $ f $ satisfies quasi-monotonicity condition [26,p. 78]. Typically, in population dynamics the stability of equilibria is closely related to the algebraic properties of some kinds of competition matrix of the community. Denote

    $ \begin{equation*} A = \begin{pmatrix} ae^{-\zeta_1}-d&0\\ 0&-d_* \end{pmatrix}, \quad D = \begin{pmatrix} 0&b\\ ce^{-\zeta_2}&0 \end{pmatrix}. \end{equation*} $

    For convenience, we shall refer to $ N = A+D $ as the (linear) community matrix:

    $ \begin{equation} N = \begin{pmatrix} ae^{-\zeta_1}-d&b\\ ce^{-\zeta_2}&-d_* \end{pmatrix}. \end{equation} $ (3.8)

    Since $ D\ge 0 $, the matrix $ N $ in Eq (3.8) is called cooperative. If $ D $ is irreducible, then the matrix $ N $ in Eq (3.8) is also irreducible; in this case, system (2.2) is called an irreducible system [26,p. 88], and the semiflow $ \psi\mapsto Y_t(\psi) $ is eventually strongly monotone. $ f = (f_1, f_2)^T:\mathbb{R}^2 \to \mathbb{R}^2 $ is strictly sublinear, i.e., for any $ P\gg 0, M\gg 0 $ and any $ \alpha\in(0, 1), $

    $ \begin{equation*} \begin{aligned} f_1(\alpha P, \alpha M) = &\alpha P[-d-b_1\alpha P]+ae^{-\zeta_1}\alpha P(t-\tau_1)+b\alpha M\\ > & \alpha [P(-d-b_1P)+ae^{-\zeta_1} P(t-\tau_1)+b M] = \alpha f_1(P, M), \\ f_2(\alpha P, \alpha M) = &\alpha M[-d_*-b_2\alpha M]+ce^{-\zeta_2}\alpha P(t-\tau_2)\\ > &\alpha [M(-d_*-b_2M)+ce^{-\zeta_2}P(t-\tau_2)] = \alpha f_2(P, M). \end{aligned} \end{equation*} $

    Cooperative $ DDEs $ satisfying these sublinearity conditions have significant properties [30,Proposition 4.3].

    Recall that the stability modulus of square matrix $ N $ in Eq (3.8), denoted by $ s(N) $, is defined by $ s(N) = \max \{Re \lambda:\mbox{ $\lambda$ is an eigenvalue of $N$ }\rbrace $. If the matrix $ N $ in Eq (3.8) has nonnegative off diagonal elements and is irreducible, then $ s(N) $ is a simple eigenvalue of the matrix $ N $ with a (componentwise) positive eigenvector (see, e.g., [31,Theorem A.5]).

    The matrix $ N $ in Eq (3.8) is

    $ \begin{equation*} N = \begin{pmatrix} ae^{-\zeta_1}-d&b\\ ce^{-\zeta_2}&-d_* \end{pmatrix}, \end{equation*} $

    then we can easily get the following:

    $ s(N) > 0 $ if and only if $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} > 0 $ and $ s(N) < 0 $ if and only if $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} < 0 $.

    Definition 3.4. [32] A square matrix $ A = [a_{ij}] $ with non-positive off diagonal entries, i.e., $ a_{ij}\le 0 $ for all $ i\neq j $, is said to be an M-matrix if all the eigenvalues of $ A $ have a non-negative real part, or equivalently, if all its principal minors are non-negative, and $ A $ is said to be a non singular M-matrix if all the eigenvalues of $ A $ have positive real part, or, equivalently, if all its principal minors are positive.

    Theorem 3.5. Suppose that $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} < 0 $, then the equilibrium $ E_0 $ of system (2.2) is globally asymptotically stable.

    Proof. Let $ P(t, l) $, $ M(t, k) $ be the solutions of system (2.2) with $ P(0+\theta, l) = l $, $ M(0+\theta, k) = k $ for $ \theta\in[-\tau, 0] $. Note that $ f_1(l) = l[-d+b+ae^{-\zeta_1}-b_1l] < 0 $ for $ l > 0 $ sufficiently large and $ f_2(k) = k[-d_*+ce^{-\zeta_2}-b_2k] < 0 $ for $ k > 0 $ sufficiently large. Hence we can easily conclude that all admissible solutions of system (2.2) are bounded [26,Corollary 5.2.2]. We have $ s(N) < 0 $ if and only if $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} < 0 $. By the assumption $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} < 0 $, we observed that it is equivalent to having $ -N $ a non singular M-matrix. Since matrix $ -N $ is a non singular M-matrix, there exists the equilibrium $ v = (v_p, v_m)\in \mathbb{R}^2, v > 0, $ such that $ Nv < 0 $, hence we get

    $ \begin{equation} \begin{aligned} ae^{-\zeta_1}v_p-dv_p+bv_m < 0, \\ ce^{-\zeta_2}v_p-d_*v_m < 0. \end{aligned} \end{equation} $ (3.9)

    Let $ P(t)\ge 0 $, $ M(t)\ge 0 $ be solutions of system (2.2). Denote $ y_p(t) = \frac{P(t)}{v_p} $ and $ y_m(t) = \frac{M(t)}{v_m} $, thus system (2.2) takes the form as

    $ \begin{equation} \begin{aligned} y_p'(t) = &y_p(t)[-d-b_1y_p(t)v_p]+ae^{-\zeta_1}y_p(t-\tau_1)+\frac{bv_m}{v_p}y_m(t), \\ y_m'(t) = &y_m(t)[-d_*-b_2y_m(t)v_m]+ce^{-\zeta_2}\frac{v_p}{v_m}y_p(t-\tau_2). \end{aligned} \end{equation} $ (3.10)

    It suffices to prove that $ (L_p, L_m): = \limsup_{t\to\infty} (y_p(t), y_m(t)) = (0, 0) $. Let $ L_p: = \limsup\lbrace{y_p(t)}\rbrace $, $ L_m: = \limsup\lbrace{y_m(t)}\rbrace $, $ \tilde{L}: = \max\lbrace{L_p, L_m}\rbrace $ and suppose that $ \tilde{L} > 0 $. From Eq (3.9), we can choose $ \varepsilon > 0 $ such that

    $ \begin{equation*} \begin{aligned} \tilde{L}[-d-b_1\tilde{L}v_p+ae^{-\zeta_1}+\frac{bv_m}{v_p}]+\varepsilon[ae^{-\zeta_1}+\frac{bv_m}{v_p}] = :\gamma_p < 0, \\ \tilde{L}[-d_*-b_2\tilde{L}v_m+ce^{-\zeta_2}\frac{v_p}{v_m}]+\varepsilon[ce^{-\zeta_2}\frac{v_p}{v_m}] = :\gamma_m < 0. \end{aligned} \end{equation*} $

    Let $ T > 0 $ be such that $ y_p(t)\le \tilde{L}+\varepsilon $, $ y_m(t)\le \tilde{L}+\varepsilon $ for all $ t > T-\tau $ and the cases of $ y_p(t) $ and $ y_m(t) $ are separated as eventually monotone and not eventually monotone. By [26,Proposition 5.4.2], if $ y_p(t) $ and $ y_m(t) $ are eventually monotone, then $ y_p(t)\to \tilde{L} $ and $ y_m(t)\to \tilde{L} $ as $ t\to \infty $ for $ t\ge T $ and we obtain

    $ \begin{equation} \begin{aligned} y'_p(t)&\le y_p(t)[-d-b_1y_p(t)v_p]+ae^{-\zeta_1}(\tilde{L}+\varepsilon)+(\tilde{L}+\varepsilon)\frac{bv_m}{v_p}\to \gamma_p, \\ y'_m(t)&\le y_m(t)[-d_*-b_2y_m(t)v_m]+ce^{-\zeta_2}\frac{v_p}{v_m}(\tilde{L}+\varepsilon)\to \gamma_m \text{ as } t\to\infty. \end{aligned} \end{equation} $ (3.11)

    Since $ \gamma_p < 0 $ and $ \gamma_m < 0 $, these imply that $ \lim_{t\to \infty} (y_p(t), y_m(t)) = -\infty $, which is impossible. By using the similar argument of Aiello and Freedman [18,Theorem 2], if $ y_p(t) $ and $ y_m(t) $ are not eventually monotone, there is a sequence $ t_n\to\infty $ such that $ y_p(t_n)\to \tilde{L}, $ $ y'_p(t_n) = 0 $ and $ y_m(t_n)\to \tilde{L}, $ $ y'_m(t_n) = 0 $. We obtain (3.11) with $ t $ replaced by $ t_n $, again a contradiction. This proves $ \lim_{t\to \infty} (y_p(t), y_m(t)) = (0, 0) $. Using Lemma 3.1, we complete the proof of Theorem 3.5.

    Theorem 3.6. Suppose that $ ae^{-\zeta_1}-d > 0 $ and $ c = 0 $, then the equilibrium $ E_1 $ of system (2.2) is globally asymptotically stable.

    Proof. If $ c = 0 $, the second equation of system (2.2) becomes

    $ \begin{equation} M'(t) = -d_*M-b_2M^2, \end{equation} $ (3.12)

    For the independent subsystem (3.12), it is obvious that $ \lim_{t\to \infty} M(t) = 0 $.

    Then the first equation of system (2.2) becomes

    $ \begin{equation} P'(t) = ae^{-\zeta_1}P(t-\tau_1)-dP(t)-b_1P^2(t). \end{equation} $ (3.13)

    Let $ \varepsilon > 0 $ be sufficiently small and $ L > 0 $ be sufficiently large such that $ \varepsilon\le P(t)\le L $, $ t\in[-\tau, 0] $, and

    $ ae^{-\zeta_1}\varepsilon-d\varepsilon-b_1\varepsilon^2 > 0, \quad ae^{-\zeta_1}L-dL-b_1L^2 < 0. $

    Let $ P_\varepsilon(t) $ and $ P_L(t) $ be the solutions of Eq (3.13) with $ P_\varepsilon(t) = \varepsilon $ and $ P_L(t) = L $ for $ t\in[-\tau, 0] $. From the monotone properties of the equation [26], the function $ P_\varepsilon(t) $ is increasing and $ P_L(t) $ is decreasing for $ t\ge 0 $ and

    $ P_\varepsilon(t)\le P(t)\le P_L(t), t\ge 0. $

    It therefore follows that

    $ \begin{equation*} \begin{aligned} \frac{ae^{-\zeta_1}-d}{b_1} = \lim\limits_{t\to\infty} P(t)\le \lim\limits_{t\to\infty} P_L(t) = \frac{ae^{-\zeta_1}-d}{b_1} \end{aligned} \end{equation*} $

    because the only equilibrium of the equation between $ \varepsilon $ and $ L $ is $ \frac{ae^{-\zeta_1}-d}{b_1} $. Using Lemma 3.2, we complete the proof of Theorem 3.6.

    Lemma 3.7. Suppose there is a positive equilibrium $ (P^*, M^*) $ of system (2.2), and that $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} > 0 $ and $ c\neq 0 $. Then all solutions $ P(t, \psi_1) $, $ M(t, \psi_2) $ of system (2.2) with $ \psi_i\in X_0^+, i = 1, 2 $ satisfy $ \liminf_{t\to\infty}(P(t, \psi_1), M(t, \psi_2))\ge (P^*, M^*) $.

    Proof. For $ (P^*, M^*) $ an equilibrium of system (2.2), we have

    $ \begin{equation} \begin{aligned} ae^{-\zeta_1}-d+b\frac{M^*}{P^*} = b_1P^* > 0, \\ -d_*+ce^{-\zeta_2}\frac{P^*}{M^*} = b_2M^* > 0. \end{aligned} \end{equation} $ (3.14)

    Denote $ \bar{P}(t) = \frac{P(t)}{P^*} $ and $ \bar{M}(t) = \frac{M(t)}{M^*} $ in system (2.2), and dropping the bar for simplicity, we get

    $ \begin{equation} \begin{aligned} P'(t) = &P(t)[-d-b_1P(t)P^*]+ae^{-\zeta_1}P(t-\tau_1)+\frac{bM^*}{P^*}M(t), \\ M'(t) = &M(t)[-d_*-b_2M(t)M^*]+ce^{-\zeta_2}\frac{P^*}{M^*}P(t-\tau_2). \end{aligned} \end{equation} $ (3.15)

    For the solutions $ P(t) = P(t, \psi_1) $ and $ M(t) = M(t, \psi_2) $ of Eq (3.15) with $ \psi_i\in X_0^+ $ for $ i = 1, 2 $, we first claim that $ (l_p, l_m): = \liminf_{t\to\infty}(P(t), M(t)) > (0, 0) $. Otherwise, there exist $ \delta\in(0, 1) $ and $ t_0 > \tau $ such that $ \tilde{l} = \min\lbrace{(P(t), M(t)):t\in[0, t_0]}\rbrace $ and $ \tilde{l} < \delta $. By using Eq (3.14),

    $ \begin{equation*} \begin{aligned} P'(t_0)& = P(t_0)[-d-b_1P(t_0)P^*]+ae^{-\zeta_1}P(t_0-\tau_1)+\frac{bM^*}{P^*}M(t_0)\\ &\ge \tilde{l}[-d-b_1\tilde{l}P^*]+ae^{-\zeta_1}\tilde{l}+\frac{bM^*}{P^*}\tilde{l} \\ & = \tilde{l}(b_1P^*-b_1\tilde{l}P^*) = \tilde{l}b_1P^*(1-\tilde{l}) > 0, \\ M'(t_0)& = M(t_0)[-d_*-b_2M(t_0)M^*]+ce^{-\zeta_2}\frac{P^*}{M^*}P(t_0-\tau_2)\\ &\ge \tilde{l}[-d_*-b_2\tilde{l}M^*]+ce^{-\zeta_2}\frac{P^*}{M^*}\tilde{l} \\ & = \tilde{l}(b_2M^*-b_2\tilde{l}M^*) = \tilde{l}b_2M^*(1-\tilde{l}) > 0. \end{aligned} \end{equation*} $

    But these are not possible. Since the definition of $ t_0 $, $ P'(t_0)\le 0 $ and $ M'(t_0)\le 0 $.

    Next we prove that $ (l_p, l_m)\ge(1, 1) $. Choose $ \tilde{l} = \min \lbrace{l_p, l_m}\rbrace $ and suppose that $ \tilde{l} < 1 $. Let $ T > 0 $ and $ \varepsilon > 0 $ be chosen so that $ P(t)\ge \tilde{l}-\varepsilon $ and $ M(t)\ge \tilde{l}-\varepsilon $ for all $ t > T-\tau $.

    $ \begin{equation*} \begin{aligned} \tilde{l}b_1P^*(1-\tilde{l})-\varepsilon[ae^{-\zeta_1}\tilde{l}+\frac{bM^*}{P^*}] = :n_p > 0, \\ \tilde{l}b_2M^*(1-\tilde{l})-\varepsilon[ce^{-\zeta_2}\frac{P^*}{M^*}] = :n_m > 0. \end{aligned} \end{equation*} $

    By [26,Proposition 5.4.2], if $ P(t) $ and $ M(t) $ are eventually monotone, then $ P(t)\to \tilde{l} $ and $ M(t)\to \tilde{l} $ and for $ t\ge T $, we have

    $ \begin{equation*} \begin{aligned} P'(t)&\ge P(t)[-d-b_1P(t)P^*]+ae^{-\zeta_1}(\tilde{l}-\varepsilon)+(\tilde{l}-\varepsilon)\frac{bM^*}{P^*}\to n_p, \\ M'(t)&\ge M(t)[-d_*-b_2M(t)M^*]+(\tilde{l}-\varepsilon)ce^{-\zeta_2}\frac{P^*}{M^*} \to n_m \text{ as } t\to\infty, \end{aligned} \end{equation*} $

    leading to $ P(t)\to \infty $ and $ M(t)\to \infty $ as $ t\to \infty $, contradicting $ \tilde{l} < 1 $. By using the similar argument of Aiello and Freedman [18,Theorem 2], if $ P(t) $ and $ M(t) $ are not eventually monotone, there is a sequence $ t_n\to \infty $ such that $ P(t_n)\to \tilde{l}, $ $ P'(t_n) = 0 $ and $ M(t_n)\to \tilde{l}, $ $ M'(t_n) = 0 $. For $ t_n\ge T $, we obtain the above inequalities $ t_n $ instead of $ t $, which yield that $ 0 = P'(t_n)\ge n_p $ and $ 0 = M'(t_n)\ge n_m $, again contradicting $ \tilde{l} < 1 $. This proves that $ \tilde{l}\ge 1 $.

    Theorem 3.8. Suppose that $ (ae^{-\zeta_1}-d)d_*+bce^{-\zeta_2} > 0 $ and $ c\neq 0 $, then the equilibrium $ E^* $ of system (2.2) is globally asymptotically stable.

    Proof. For $ (P^*, M^*) $ of system (2.2), after the changes $ P(t)\mapsto \frac{P(t)}{P^*} $ and $ M(t)\mapsto \frac{M(t)}{M^*} $, consider system (3.15) with positive equilibrium $ (1, 1)\in \mathbb{R}^2 $. In view of Lemmas 3.3 and 3.7, we only need to prove that $ (L_p, L_m): = \limsup_{t\to \infty}(P(t), M(t))\le (1, 1) $ and any positive solution $ P(t) $, $ M(t) $ of Eq (3.15).

    For the sake of contradiction, suppose that $ \tilde{L} = \max \lbrace{L_p, L_m}\rbrace > 1 $. Choose $ \varepsilon > 0 $ and $ t > \tau $, such that $ P(t)\le \tilde{L}+\varepsilon $ and $ M(t)\le \tilde{L}+\varepsilon $ for all $ t > T-\tau $ and

    $ \begin{equation*} \begin{aligned} \tilde{L}b_1P^*(1-\tilde{L})+\varepsilon[ae^{-\zeta_1}\tilde{L}+\frac{bM^*}{P^*}] = :&N_p < 0, \\ \tilde{L}b_2M^*(1-\tilde{L})+\varepsilon[ce^{-\zeta_2}\frac{P^*}{M^*}] = :& N_m < 0. \end{aligned} \end{equation*} $

    Separating the cases of $ P(t) $ and $ M(t) $ eventually monotone and not eventually monotone, and reasoning as in the proofs of Theorem 3.5 and Lemma 3.7, we obtain a contradiction, thus $ \tilde{L}\le 1 $. Finally we get $ \lim_{t\to \infty}(P(t), M(t)) = (P^*, M^*) $. Using Lemma 3.3, we complete the proof of Theorem 3.8.

    Remark 1. Note that when $ \tau_1 = \tau_2 = 0 $, system (2.2) becomes system (1.1). Theorems 4–6 in [11] are the corresponding results of Theorems 3.5, 3.6 and 3.8 for system (2.2), respectively. Our main results not only extend the results in [11] but also generalize the related results into the stage-structured system with two delays. But the proof methods of our results are quite different to those in [11].

    In this section, we numerically simulate the dynamics of system (2.2) for a range of parameters which are the same as those in [11]. In this paper, we add the values of two delays $ \tau_1 $ and $ \tau_2 $ from [10,33]. The parameters are given in Table 1.

    Table 1.  Two sets of parameter values used in numerical simulations.
    Parameter Ranges Ref. Unit data 1 data 2
    $ \alpha(T) $ $ 0.03\sim0.15^{a} $ [14] ind $ \cdot $ d$ ^{-1} $ $ P^{-1} $ 0.12 0.15
    $ \beta(T) $ $ 0.065\sim0.139^{a} $ [14] ind $ \cdot $ d$ ^{-1} $time$ ^{-1} $ $ P^{-1} $ 0.108 0.122
    $ \gamma $ $ 19\sim178^{a} $ [33,34] ind $ \cdot $ d$ ^{-1} $ $ M^{-1} $ 100 170
    $ s_1 $ $ 0.001\sim0.3^{b} $ [34,35] no unit 0.008 0.01
    $ s_2 $ $ 0.01\sim0.8^{b} $ [34] no unit 0.2 0.8
    $ n $ $ 1\sim2 $ [14] times 1 1
    $ d_1 $ $ 0\sim0.028^{a, b} $ [6,14] d$ ^{-1} $ 0.0001 0.0001
    $ d_2 $ $ 0.0001\sim0.3^{b} $ [34] d$ ^{-1} $ 0.0001 0.0001
    $ d_3 $ $ 0.004\sim0.02^{a} $ [34,36] d$ ^{-1} $ 0.006 0.004
    $ d_4 $ $ 0.0001\sim0.8^{b} $ [1] d$ ^{-1} $ 0.0001 0.0001
    $ b_1 $ $ 0.00001\sim0.1^{b} $ [3,37] d$ ^{-1} $ind$ ^{-1} $ 0.0012 0.0001
    $ b_2 $ $ 0\sim0.1^{b} $ d$ ^{-1} $ind$ ^{-1} $ 0.0001 0.0001
    $ \tau_1 $ $ 30\sim120^{b} $ [10,33] d 120 120
    $ \tau_2 $ $ 60\sim300^{b} $ [10,33] d 90 150

     | Show Table
    DownLoad: CSV

    Values signatured by $ ^{a} $ are from experimental data with unit innovation and those signatured by $ ^{b} $ are estimated from references.

    The left figure of Figure 2 shows that the positive equilibrium $ E^* $ of system (2.2) is globally asymptotically stable under different initial values. The left figure and right figure of Figure 2 take the parameters data 1 and data 2, respectively. Figure 2 shows that the population sizes change with respect to environmental indices but do not depend on the initial values. The population explosion occurs even though the initial values $ (P = 0, M = 2) $ are small (see the right figure of Figure 2). The numbers of two stages in the right figure of Figure 2 are larger than those in the left figure of Figure 2 because the reproduction is high while the destructions and competitions are low in the right figure of Figure 2. The trajectories of the right figure of Figure 2 finally tend towards a higher population level up to 10–15 times than the trajectories in the left figure of Figure 2 (in the corresponding Figure 3 of [11], the populations of Figure 3(b) is higher 30–50 times than Figure 3(a)) although the initial values $ (0, 2) $ are of equal values.

    Figure 2.  Global stability of $ E^* $ under different initial values and the population sizes for data 1 and data 2, respectively.
    Figure 3.  The effects of delays on the population sizes for data 2.

    Based on data 2, Figure 3 illustrates how time delays affect the population dynamics. In the left figure of Figure 3, we fix the delay $ \tau_2 $ as the best fit value and increase the delay $ \tau_1\in [30,120] $. We find that the populations are slightly fallen over the longer period $ \tau_1 $ (see the left figure of Figure 3). This is because of the lack of needed temperature and resources and so the asexual reproduction period is long, and the results of the population are low. When we fix the delay $ \tau_1 $ and change the delay $ \tau_2 $ from $ 60 $ to $ 300 $, the populations are significantly decreased over the longer period $ \tau_2 $ (see the right figure of Figure 3). Overall, Figure 3 can be seen that the peaks of population abundance occur at the small $ \tau_1 $ and $ \tau_2 $ while the longer maturation periods may be responsible for the lower populations.

    Figure 4 depicts the effect of temperature $ T\in [7,36] $ on the populations. Temperature is the impact factor that affects the asexual reproduction and strobilation of the jellyfish. In [11], Xie et al. presented that

    $ \alpha(T) = \frac{1.9272}{T^3-30.3904T^2+294.7234T-871.29}+0.0378, $
    $ \beta(T) = 0.1430 \text{ exp } \lbrace{-(\frac{T-16.8108}{10.5302})^2}\rbrace. $
    Figure 4.  The effects of temperature on the population sizes for data 1 and data 2, respectively.

    In Figure 4, the numbers of polyp reach a peak at $ 12.5\; ^{\circ}C $, which correlates with the maximum budding rate of experimental data [14] and then gradually declined over the high temperature. From $ 12.5\; ^{\circ}C $ to $ 16.8\; ^{\circ}C $ is the maximum level of the number of medusae which is different from the experimental result $ 15\; ^{\circ}C $ [14]. Figure 4 reveals that an appropriate increase of temperature might cause a large increase in the number of populations but the rise of temperatures would result in the fewer populations. Comparing the corresponding Figure (4d) in [11] with the right figure of Figure 4 in this paper, we find out that we can exactly see the peak populations due to the stage structure and can exactly know the effects of temperature on the population dynamics because the temperature is considered up to $ 36\; ^{\circ}C $ in this paper.

    In this paper, we propose and analyze a delayed jellyfish model with stage structure, which is an extension of ODE model studied by Xie et al. in [11]. We have investigated how the phenomena of budding and strobilation influence the population dynamics of the jellyfish population. $ \tau_1 $ stands the time needed from the stage of the young polyp to the developed polyp and $ \tau_2 $ stands the time taken from the mature polyp to ephyra (incipient medusa). We have developed the systematic analysis of the model in both theoretical and numerical ways.

    We have proved the global stability of the equilibria under suitable conditions. Our results not only extend but also improve some related results of literature [11]. Our Theorems 3.5, 3.6 and 3.8 straightly extend the corresponding Theorems 4–6 in [11], respectively. Comparing the corresponding Theorems 4–6 in [11] for the ODE system (1.1) with Theorem 3.5, 3.6 and 3.8 for system (2.2), we find out that there are two extra terms $ e^{-d\tau_1} $ and $ e^{-d_*\tau_2} $ in our permanence and extinction criteria, i.e., the surviving probability of each immature population to develop into mature, which obtains due to the stage structure. From our results, we find that the jellyfish population will be extinct in the large immature mortality rate $ d, d_* $ or the long maturation $ \tau_1, \tau_2 $. Thus we may suggest that the proper increases of $ d\tau_1 $ and $ d_*\tau_2 $ have a negative effect of jellyfish population.

    Biologically, our results suggest that (i) jellyfish species go extinct if the survival rate of polyp during cloning and the survival rate of the incipient medusa during strobilation are less than their death rates; (ii) polyps will continue and there is no complement from polyp to medusa if the survival rate of polyp during cloning is larger than its death rate and the temperature is not enough to strobilate; (iii) both polyp and medusa will survive in a certain ideal environment and our result converges to the positive constant when the survival rate of polyp during cloning and the survival rate of the incipient medusa during strobilation are larger than their death rates.

    Besides the above systematic theoretical results, we have performed the numerical simulations to support the theoretical results. Our numerical results suggest that the positive equilibrium is globally asymptotically stable under distinctive initial values and the population sizes don't deal with the initial values but they change with respect to environmental factors. In Figures 3 and 4, our results suggest that the abundance in population occurs at the smaller periods $ \tau_1 $ and $ \tau_2 $ whereas the longer periods $ \tau_1 $ and $ \tau_2 $ will lower the peak population of polyp and medusa. In addition to the problem due to increasing $ \tau_1 $ and $ \tau_2 $, the increase of temperatures might cause the outburst of the population dynamics. If there is much higher temperature, the population rate leads to decline. Since temperature has a great impact on jellyfish population, it is interesting for one to consider the populations under the relevance to temperature. We leave this interesting problem as our future work.

    We would like to take this chance to thank the editor and the anonymous referees for their very valuable comments, which led to a significant improvement of our previous versions. The authors would like to thank Dr. Zhanwen Yang for his warm help on the numeric simulations. Z. Win, B. Tian and S. Liu are supported by the Natural Science Foundation of China (NSFC) (No. 11871179, 11771374, 91646106).

    All authors declare no conflicts of interest in this paper.



    [1] Butterworth S, Hill N, Kallamthodi S (2005) Feasibility Study Into The Use Of Hydrogen Fuel. Rail Safety & Standards Board.
    [2] Ellen MacArthur Foundation, What is a circular economy? Ellen MacArthur Foundation, 2019. Available from: https://www.ellenmacarthurfoundation.org/circular-economy/concept.
    [3] Kirchherr J, Piscicelli L, Bour R, et al. (2018) Barriers to the circular economy: Evidence from the European Union (EU). Ecol Econ 150: 264-272. doi: 10.1016/j.ecolecon.2018.04.028
    [4] Falcone PM (2019) Tourism-Based circular economy in Salento (South Italy): A SWOT-ANP Analysis. Soc Sci, 8.
    [5] Bartolacci F, Paolini A, Quaranta AG, et al. (2018) Assessing factors that influence waste management financial sustainability. Waste Manag 79: 571-579. doi: 10.1016/j.wasman.2018.07.050
    [6] De Gioannis G, Muntoni A, Polettini A, et al. (2013) A review of dark fermentative hydrogen production from biodegradable municipal waste fractions. Waste Manag 33: 1345-1361. doi: 10.1016/j.wasman.2013.02.019
    [7] Wu C, Williams PT (2010) Pyrolysis-gasification of post-consumer municipal solid plastic waste for hydrogen production. Int J Hydrogen Energy 35: 949-957. doi: 10.1016/j.ijhydene.2009.11.045
    [8] Andika R, Nandiyanto ABD, Putra ZA, et al. (2018) Co-electrolysis for power-to-methanol applications. Renew Sustain Energy Rev 95: 227-241. doi: 10.1016/j.rser.2018.07.030
    [9] Ranisau J, Barbouti M, Trainor A, et al. (2017) Power-to-gas implementation for a polygeneration system in southwestern ontario. Sustainability, 9.
    [10] Valente A, Iribarren D, Dufour J (2019) End of life of fuel cells and hydrogen products: From technologies to strategies. Int J Hydrogen Energy 44: 20965-20977. doi: 10.1016/j.ijhydene.2019.01.110
    [11] United Nations, The 17 Goals. United Nations Department of Economic and Social Affairs, 2018. Available from: https://sdgs.un.org/goals.
    [12] Falcone PM, Hiete M, Sapio A (2021) Hydrogen economy and sustainable development goals: Review and policy insights. Curr Opin Green Sustain Chem 31: 100506. doi: 10.1016/j.cogsc.2021.100506
    [13] Australian Government Department of Industry, Science, Energy, and Resources, Australia's National Hydrogen Strategy. COAG Energy Council Hydrogen Working Group, 2019. Available from: https://www.industry.gov.au/sites/default/files/2019-11/australias-national-hydrogen-strategy.pdf.
    [14] Deutsche Energie-Agentur, The role of clean hydrogen in the future energy systems of Japan and Germany. Jensterle M, Narita J, Piria R, et al., 2019. Available from: https://www.dena.de/fileadmin/dena/Publikationen/PDFs/2019/The_role_of_clean_hydrogen_in_the_future_energy_systems.pdf.
    [15] Climate Change Act 2008, c. 27. 2008. Available from: https://www.legislation.gov.uk/ukpga/2008/27/contents.
    [16] Climate Change Committee, Hydrogen in a low-carbon economy. Joffe D, Livermore S, Hemsley M, et al., 2018. Available from: https://www.theccc.org.uk/wp-content/uploads/2018/11/Hydrogen-in-a-low-carbon-economy.pdf.
    [17] Energy Independence Now, Renewable Hydrogen Roadmap, 2018. Available from: https://einow.org/rh2roadmap.
    [18] Government of Canada, 2019 Hydrogen Pathways—Enabling a clean growth future for Canadians. Natural Resources Canada, 2019. Available from: https://www.nrcan.gc.ca/energy-efficiency/transportation-alternative-fuels/resource-library/2019-hydrogen-pathways-enabling-clean-growth-future-for-canadians/21961.
    [19] Natural Resources Canada, Hydrogen strategy for Canada: Seizing the opportunities for hydrogen. Natural Resources Canada, 2020. Available from: https://www.nrcan.gc.ca/sites/www.nrcan.gc.ca/files/environment/hydrogen/NRCan_Hydrogen-Strategy-Canada-na-en-v3.pdf.
    [20] Independent Electricity System Operator, 2020 Year in Review. IESO, 2020. Available from: https://www.ieso.ca/en/Corporate-IESO/Media/Year-End-Data.
    [21] Orecchini F, Naso V (2012) Energy systems in the era of energy vectors, Springer US.
    [22] Zhao W, Stasko R (2019) The Present Status of Hydrogen Technologies and Project Deployments in Ontario and Canada with an Overview of Global H2 Activities.
    [23] Shamsi H, Tran M-K, Akbarpour S, et al. (2021) Macro-Level optimization of hydrogen infrastructure and supply chain for zero-emission vehicles on a canadian corridor. J Clean Prod 289: 125163. doi: 10.1016/j.jclepro.2020.125163
    [24] Maroufmashat A, Fowler M (2017) Low-carbon transportation pathways through power-to-gas. 2017 5th IEEE Int Conf Smart Energy Grid Eng SEGE 2017, 353-356.
    [25] Wu XY, Luo Y, Hess F, et al. (2021) Editorial: Sustainable Hydrogen for energy, fuel and commodity applications. Front Energy Res 9: 231.
    [26] Ludwig M, Haberstroh C, Hesse U (2015) Exergy and cost analyses of hydrogen-based energy storage pathways for residual load management. Int J Hydrogen Energy 40: 11348-11355. doi: 10.1016/j.ijhydene.2015.03.018
    [27] Mukherjee U, Elsholkami M, Walker S, et al. (2015) Optimal sizing of an electrolytic hydrogen production system using an existing natural gas infrastructure. Int J Hydrogen Energy 40: 9760-9772. doi: 10.1016/j.ijhydene.2015.05.102
    [28] National Renewable Energy Laboratory, Blending Hydrogen into Natural Gas Pipeline Networks: A Review of Key Issues. Melaina M, Antonia O, Penev M, 2013. Available from: https://www.nrel.gov/docs/fy13osti/51995.pdf.
    [29] Ramachandran R, Menon RK (1998) An overview of industrial uses of hydrogen. Int J Hydrogen Energy 23: 593-598. doi: 10.1016/S0360-3199(97)00112-2
    [30] Maroufmashat A, Fowler M (2017) Transition of future energy system infrastructure; through power-to-gas pathways. Energies, 10.
    [31] Luo Y, Wu XY, Shi Y, et al. (2018) Exergy analysis of an integrated solid oxide electrolysis cell-methanation reactor for renewable energy storage. Appl Energy 215: 371-383. doi: 10.1016/j.apenergy.2018.02.022
    [32] Yao Y, Sempuga BC, Liu X, et al. (2020) Production of Fuels and Chemicals from a CO2/H2 Mixture. Reactions 1: 130-146. doi: 10.3390/reactions1020011
    [33] Statista, Natural gas consumption worldwide from 1998 to 2019 (in billion cubic meters). Sö nnichsen N, 2021. Available from: https://www.statista.com/statistics/282717/global-natural-gas-consumption/.
    [34] Washington Post, Global greenhouse gas emissions will hit yet another record high this year, experts project. Dennis B, Mooney C, 2019. Available from: https://www.washingtonpost.com/climate-environment/2019/12/03/global-greenhouse-gas-emissions-will-hit-yet-another-record-high-this-year-experts-project/.
    [35] Pembina Institute, Hydrogen on the path to net-zero emissions Costs and climate benefits. Ewing M, Israel B, Jutt T, et al., 2020. Available from: https://www.pembina.org/reports/hydrogen-climate-primer-2020.pdf.
    [36] Alberta, Natural Gas Vision and Strategy. Alberta Energy, 2020. Available from: https://www.alberta.ca/natural-gas-vision-and-strategy.aspx.
    [37] Koumi Ngoh S, Njomo D (2012) An overview of hydrogen gas production from solar energy. Renew Sustain Energy Rev 16: 6782-6792. doi: 10.1016/j.rser.2012.07.027
    [38] IEA, The clean hydrogen future has already begun. van Hulst, 2019. Available from: https://www.iea.org/commentaries/the-clean-hydrogen-future-has-already-begun.
    [39] Wu XY, Ghoniem AF (2019) Mixed ionic-electronic conducting (MIEC) membranes for thermochemical reduction of CO2: A review. Prog Energy Combust Sci 74: 1-30. doi: 10.1016/j.pecs.2019.04.003
    [40] Soltani R, Rosen MA, Dincer I (2014) Assessment of CO2 capture options from various points in steam methane reforming for hydrogen production. Int J Hydrogen Energy 39: 20266-20275. doi: 10.1016/j.ijhydene.2014.09.161
    [41] Government of the Netherlands, Government Strategy on Hydrogen. Ministry of Economic Affairs and Climate Policy, 2020. Available from: https://www.government.nl/documents/publications/2020/04/06/government-strategy-on-hydrogen.
    [42] Yan J (2018) Negative-emissions hydrogen energy. Nat Clim Chang 8: 560-561. doi: 10.1038/s41558-018-0215-9
    [43] Noussan M, Raimondi PP, Scita R, et al. (2021) The role of green and blue hydrogen in the energy transition—a technological and geopolitical perspective. Sustainability 13: 1-26.
    [44] Naterer GF, Suppiah S, Stolberg L, et al. (2011) Clean hydrogen production with the Cu-Cl cycle-Progress of international consortium, I: Experimental unit operations. Int J Hydrogen Energy 36: 15472-15485. doi: 10.1016/j.ijhydene.2011.08.012
    [45] Walker SB, Mukherjee U, Fowler M, et al. (2016) Benchmarking and selection of Power-to-Gas utilizing electrolytic hydrogen as an energy storage alternative. Int J Hydrogen Energy 41: 7717-7731. doi: 10.1016/j.ijhydene.2015.09.008
    [46] Buttler A, Spliethoff H (2018) Current status of water electrolysis for energy storage, grid balancing and sector coupling via power-to-gas and power-to-liquids: A review. Renew Sustain Energy Rev 82: 2440-2454. doi: 10.1016/j.rser.2017.09.003
    [47] Carmo M, Fritz DL, Mergel J, et al. (2013) A comprehensive review on PEM water electrolysis. Int J Hydrogen Energy 38: 4901-4934. doi: 10.1016/j.ijhydene.2013.01.151
    [48] Barbir F (2005) PEM electrolysis for production of hydrogen from renewable energy sources. Sol Energy 78: 661-669. doi: 10.1016/j.solener.2004.09.003
    [49] United States Department of Energy, 2017 DOE Hydrogen and Fuel Cells Program Review: Renewable Electrolysis Integrated System Development & Testing. Peters M, Harrison K, Dinh H, et al., 2017. Available from: https://www.hydrogen.energy.gov/pdfs/review17/pd031_peters_2017_o.pdf.
    [50] Cummins, In its second year, North America's first multi-megawatt power-to-gas facility shows hydrogen's potential. Cummins Inc., 2020. Available from: https://www.cummins.com/news/2020/11/12/its-second-year-north-americas-first-multi-megawatt-power-gas-facility-shows.
    [51] Hubert M, Laurencin J, Cloetens P, et al. (2018) Impact of Nickel agglomeration on Solid Oxide Cell operated in fuel cell and electrolysis modes. J Power Sources 397: 240-251. doi: 10.1016/j.jpowsour.2018.06.097
    [52] Hossain E, Faruque HMR, Sunny MSH, et al. (2020) A comprehensive review on energy storage systems: Types, comparison, current scenario, applications, barriers, and potential solutions, policies, and future prospects. Energies 13: 1-127.
    [53] Boudghene Stambouli A, Traversa E (2002) Fuel cells, an alternative to standard sources of energy. Renew Sustain Energy Rev 6: 295-304. doi: 10.1016/S1364-0321(01)00015-6
    [54] Chen M, Sun X, Chatzichristodoulou C, et al. (2017) Thermoneutral operation of solid oxide electrolysis cells in potentiostatic mode. ECS Trans 78: 3077-3088. doi: 10.1149/07801.3077ecst
    [55] Schefold J, Brisse A, Poepke H (2015) Long-term steam electrolysis with electrolyte-supported solid oxide cells. Electrochim Acta 179: 161-168. doi: 10.1016/j.electacta.2015.04.141
    [56] Al-Subaie A, Maroufmashat A, Elkamel A, et al. (2017) Presenting the implementation of power-to-gas to an oil refinery as a way to reduce carbon intensity of petroleum fuels. Int J Hydrogen Energy 42: 19376-19388. doi: 10.1016/j.ijhydene.2017.06.067
    [57] United States Department of Energy, Hydrogen Production: Natural Gas Reforming. Office of Energy Efficiency and Renewable Energy, 2016. Available from: https://www.energy.gov/eere/fuelcells/hydrogen-production-natural-gas-reforming.
    [58] United States Department of Energy, Hydrogen Production: Coal Gasification. Office of Energy Efficiency and Renewable Energy, 2016. Available from: https://www.energy.gov/eere/fuelcells/hydrogen-production-coal-gasification.
    [59] Ghazvini M, Sadeghzadeh M, Ahmadi MH, et al. (2019) Geothermal energy use in hydrogen production: A review. Int J Energy Res 43: 7823-7851.
    [60] Chen L, Qi Z, Zhang S, et al. (2020) Catalytic hydrogen production from methane: A review on recent progress and prospect. Catalysts 10.
    [61] Rethwisch DG, Dumesic JA (1986) The effects of metal-oxygen bond strength on properties of oxides: Ⅱ. Water-gas shift over bulk oxides. Appl Catal 21: 97-109.
    [62] Grenoble DC, Estadt MM, Ollis DF (1981) The chemistry and catalysis of the water gas shift reaction: 1. The kinetics over supported metal catalysts. J Catal 67: 90-102.
    [63] Boudjemaa A, Auroux A, Boumaza S, et al. (2009) Hydrogen production on iron-magnesium oxide in the high-temperature water-gas shift reaction. React Kinet Catal Lett 98: 319-325. doi: 10.1007/s11144-009-0084-3
    [64] Amadeo NE, Laborde MA (1995) Hydrogen production from the low-temperature water-gas shift reaction: Kinetics and simulation of the industrial reactor. Int J Hydrogen Energy 20: 949-956. doi: 10.1016/0360-3199(94)00130-R
    [65] Bouarab R, Bennici S, Mirodatos C, et al. (2014) Hydrogen Production from the Water-Gas Shift Reaction on Iron Oxide Catalysts. J Catal 2014: 1-6. doi: 10.1155/2014/612575
    [66] Yamashita K, Barreto L (2005) Energyplexes for the 21st century: Coal gasification for co-producing hydrogen, electricity and liquid fuels. Energy 30: 2453-2473. doi: 10.1016/j.energy.2004.12.002
    [67] Higman C, Tam S (2014) Advances in coal gasification, hydrogenation, and gas treating for the production of chemicals and fuels. Chem Rev 114: 1673-1708. doi: 10.1021/cr400202m
    [68] Rezaee P, Naeij HR (2020) A new approach to separate hydrogen from carbon dioxide using graphdiyne-like membrane. Sci Rep 10: 1-13. doi: 10.1038/s41598-020-69933-9
    [69] Wu XY, Cai L, Zhu X, et al. (2020) A high-efficiency novel IGCC-OTM carbon capture power plant design. J Adv Manuf Process 2: e10059.
    [70] Cai L, Wu XY, Zhu X, et al. (2020) High-performance oxygen transport membrane reactors integrated with IGCC for carbon capture. AIChE J 66.
    [71] Locatelli G, Mancini M, Todeschini N (2013) Generation IV nuclear reactors: Current status and future prospects. Energy Policy 61: 1503-1520. doi: 10.1016/j.enpol.2013.06.101
    [72] Lewis MA, Masin JG (2009) The evaluation of alternative thermochemical cycles—Part Ⅱ: The down-selection process. Int J Hydrogen Energy 34: 4125-4135. doi: 10.1016/j.ijhydene.2008.07.085
    [73] Naterer GF, Suppiah S, Stolberg L, et al. (2013) Progress of international hydrogen production network for the thermochemical Cu-Cl cycle. Int J Hydrogen Energy 38: 740-759. doi: 10.1016/j.ijhydene.2012.10.023
    [74] Nikolaidis P, Poullikkas A (2017) A comparative overview of hydrogen production processes. Renew Sustain Energy Rev 67: 597-611. doi: 10.1016/j.rser.2016.09.044
    [75] Bartels JR, Pate MB, Olson NK (2010) An economic survey of hydrogen production from conventional and alternative energy sources. Int J Hydrogen Energy 35: 8371-8384. doi: 10.1016/j.ijhydene.2010.04.035
    [76] Orhan MF, Dincer I, Naterer GF (2008) Cost analysis of a thermochemical Cu-Cl pilot plant for nuclear-based hydrogen production. Int J Hydrogen Energy 33: 6006-6020. doi: 10.1016/j.ijhydene.2008.05.038
    [77] Cetinkaya E, Dincer I, Naterer GF (2012) Life cycle assessment of various hydrogen production methods. Int J Hydrogen Energy 37: 2071-2080. doi: 10.1016/j.ijhydene.2011.10.064
    [78] Tarkowski R (2019) Underground hydrogen storage: Characteristics and prospects. Renew Sustain Energy Rev 105: 86-94. doi: 10.1016/j.rser.2019.01.051
    [79] Lemieux A, Sharp K, Shkarupin A (2019) Preliminary assessment of underground hydrogen storage sites in Ontario, Canada. Int J Hydrogen Energy 44: 15193-15204. doi: 10.1016/j.ijhydene.2019.04.113
    [80] Haghi E, Kong Q, Fowler M, et al. (2019) Assessing the potential of surplus clean power in reducing GHG emissions in the building sector using game theory; a case study of Ontario, Canada. IET Energy Syst Integr 1: 184-193. doi: 10.1049/iet-esi.2019.0019
    [81] United States Department of Energy, Hydrogen Storage. Office of Energy Efficiency and Renewable Energy, 2020. Available from: https://www.energy.gov/eere/fuelcells/hydrogen-storage.
    [82] Olabi AG, Wilberforce T, Sayed ET, et al. (2020) Prospects of fuel cell combined heat and power systems. Energies, 13.
    [83] The Canadian Hydrogen and Fuel Cell Association, Fuel Cells - The Sustainable Power Source. Canadian Hydrogen and Fuel Cell Association, 2016. Available from: http://www.chfca.ca/fuel-cells-hydrogen/about-fuel-cells/.
    [84] Fuel Cell Store, Direct Methanol Fuel Cell Improvements. Spiegel C, 2018. Available from: https://www.fuelcellstore.com/blog-section/direct-methanol-fuel-cell-improvements.
    [85] Joghee P, Malik JN, Pylypenko S, et al. (2015) A review on direct methanol fuel cells—In the perspective of energy and sustainability. MRS Energy Sustain 2: E3.
    [86] NBC News, US Nissan plant to use methanol to cut costs. Poovey B, 2009. Available from: https://www.nbcnews.com/id/wbna32553892.
    [87] Sammes N, Bove R, Stahl K (2004) Phosphoric acid fuel cells: Fundamentals and applications. Curr Opin Solid State Mater Sci 8: 372-378. doi: 10.1016/j.cossms.2005.01.001
    [88] Leo T (2012) Molten carbonate fuel cells: theory and application. Comprehensive Renewable Energy, 247-259.
    [89] Dwivedi S (2020) Solid oxide fuel cell: Materials for anode, cathode and electrolyte. Int J Hydrogen Energy 45: 23988-24013. doi: 10.1016/j.ijhydene.2019.11.234
    [90] Abdelkareem MA, Elsaid K, Wilberforce T, et al. (2021) Environmental aspects of fuel cells: A review. Sci Total Environ 752: 141803. doi: 10.1016/j.scitotenv.2020.141803
    [91] Kirubakaran A, Jain S, Nema RK (2009) A review on fuel cell technologies and power electronic interface. Renew Sustain Energy Rev 13: 2430-2440. doi: 10.1016/j.rser.2009.04.004
    [92] Bagotskii VS, Skundin AM, Volfkovich YM (2014) Electrochemical Power Sources—Batteries, Fuel Cells, and Supercapacitors—18. Proton-Exchange Membrane Fuel Cells (PEMFC), John Wiley & Sons, Ltd.
    [93] Government of Canada, Canadian Environmental Sustainability Indicators: Greenhouse gas emissions. Environment and Climate Change Canada, 2020. Available from: www.canada.ca/en/environment-climate-change/services/environmental-indicators/greenhouse-gas-emissions.html.
    [94] United States Environmental Protection Agency, National Air Quality: Status and Trends Through 2007. U.S. Environmental Protection Agency, Office of Air Quality Planning and Standards, Air Quality Assessment Division, 2008. Available from: epa.gov/sites/production/files/2017-11/documents/trends_brochure_2007.pdf.
    [95] Government of Canada, Air pollution from cars, trucks, vans and SUVs. Environment and Climate Change Canada, 2017. Available from: https://www.canada.ca/en/environment-climate-change/services/air-pollution/sources/transportation/cars-trucks-vans-suvs.html.
    [96] Government of Canadian Environmental Sustainability Indicators: Air pollutant emissions. Environment and Climate Change Canada, 2019. Available from: https://www.canada.ca/en/environment-climate-change/services/environmental-indicators/air-pollutant-emissions.html.
    [97] City of Toronto, Path To Healthier Air: Toronto Air Pollution Burden of Illness Update. Toronto Public Health, 2014. Available from: https://www.toronto.ca/wp-content/uploads/2017/11/9190-tph-Air-Pollution-Burden-of-Illness-2014.pdf.
    [98] Mohankumar S, Senthilkumar P (2017) Particulate matter formation and its control methodologies for diesel engine: A comprehensive review. Renew Sustain Energy Rev 80: 1227-1238. doi: 10.1016/j.rser.2017.05.133
    [99] Canada Energy Regulator, Provincial and Territorial Energy Profiles—Ontario. Canada Energy Regulator, 2020. Available from: https://www.cer-rec.gc.ca/en/data-analysis/energy-markets/provincial-territorial-energy-profiles/provincial-territorial-energy-profiles-ontario.html.
    [100] Office of the Auditor General of Ontario, 2015 Annual Report—3.05 Electricity Power System Planning. Office of the Auditor General of Ontario, 2015. Available from: https://www.auditor.on.ca/en/content/annualreports/arbyyear/ar2015.html.
    [101] Green Ribbon Panel, 2020 Green Ribbon Panel Report: Clean Air, Climate Change and Practical, Innovative Solutions—Policy Enabled Competitive Advantages Tuned for Growth. Green Ribbon Panel, 2020. Available from: http://www.greenribbonpanel.com/reports-and-publications/.
    [102] Bruce Power, History: 2010s. Available from: https://www.brucepower.com/about-us/history/#twentyten.
    [103] Probe International, Power Exports at What Cost? How Ontario Electricity Customers Are Paying More to Dump the Province's Excess Power. Yauch B, Mitchnick S, 2016. Available from: http://probeinternational.org/library/wp-content/uploads/2016/09/power-exports-at-what-cost.pdf.
    [104] Bird L, Cochran J, Wang X (2014) Wind and solar energy curtailment: Experience and practices in the United States. Natl Renew Energy Lab 58.
    [105] Rose S, Apt J (2014) The cost of curtailing wind turbines for secondary frequency regulation capacity. Energy Syst 5: 407-422. doi: 10.1007/s12667-013-0093-1
    [106] Independent Electricity System Operator, 2019 Year in Review. IESO, 2019. Available from: https://www.ieso.ca/en/Sector-Participants/IESO-News/2020/01/2019-year-in-review.
    [107] Ontario Society of Professional Engineers, Ontario Wasted More Than $1 Billion Worth of Clean Energy in 2016. OSPE, 2017. Available from: https://ospe.on.ca/advocacy/ontario-wasted-more-than-1-billion-worth-of-clean-energy-in-2016-enough-to-power-760000-homes/.
    [108] Fraser Institute, Auditor general report sheds more light on Ontario's soaring electricity costs. Eisen B, Jackson T, 2015. Available from: https://www.fraserinstitute.org/blogs/auditor-general-report-sheds-more-light-on-ontarios-soaring-electricity-costs.
    [109] Mukherjee U, Walker S, Maroufmashat A, et al. (2016) Power-to-gas to meet transportation demand while providing ancillary services to the electrical grid. 2016 4th IEEE Int Conf Smart Energy Grid Eng SEGE 2016, 221-225.
    [110] Sperling D (1988) New transportation fuels: a strategic approach to technological change, Berkeley: University of California Press.
    [111] Canadian Urban Transit Research & Innovation Consortium, Pan-Canadian Hydrogen Fuel Cell Electric Bus Demonstration and Integration Trial. CUTRIC, 2020. Available from: https://cutric-crituc.org/project/pan-canadian-hydrogen-fuel-cell-vehicle-demonstration-integration-trial.
    [112] Al-Subaie A, Elkamel A, Mukherjee U, et al. (2017) Exploring the potential of power-to-gas concept to meet Ontario's industrial demand of hydrogen. 2017 5th IEEE Int Conf Smart Energy Grid Eng SEGE 2017, 336-340.
    [113] The Essential Chemical Industry - online, Hydrogen. Lazonby J, Waddington D, 2016. Available from: https://www.essentialchemicalindustry.org/chemicals/hydrogen.html.
    [114] Akhoundzadeh MH, Raahemifar K, Panchal S, et al. (2019) A conceptualized hydrail powertrain: A case study of the Union Pearson Express route. World Electr Veh J 10: 1-14. doi: 10.3390/wevj10010001
    [115] Metrolinx, Hydrail Feasibility Study: Fact Sheet. Metrolinx, 2018. Available from: http://www.metrolinx.com/en/news/announcements/hydrail-resources/HydrailFactsheet_Feb21.pdf.
    [116] Mukherjee U, Maroufmashat A, Ranisau J, et al. (2017) Techno-economic, environmental, and safety assessment of hydrogen powered community microgrids; case study in Canada. Int J Hydrogen Energy 42: 14333-14349. doi: 10.1016/j.ijhydene.2017.03.083
    [117] Ontario Power Generation, Community micro grid project now online. Ontario Power Generation, 2019. Available from: https://www.opg.com/media_release/community-micro-grid-project-now-online/.
    [118] Maroufmashat A, Fowler M, Sattari Khavas S, et al. (2016) Mixed integer linear programing based approach for optimal planning and operation of a smart urban energy network to support the hydrogen economy. Int J Hydrogen Energy 41: 7700-7716. doi: 10.1016/j.ijhydene.2015.08.038
    [119] Government of Canada, Businesses—Canadian Industry Statistics. Statistics Canada, 2019. Available from: https://www.ic.gc.ca/app/scr/app/cis/businesses-entreprises/48-49.
    [120] van Lanen D, Walker SB, Fowler M, et al. (2016) Market mechanisms in power-to-gas systems. Int J Environ Stud 73: 379-389. doi: 10.1080/00207233.2016.1165475
    [121] Thiel GP, Stark AK (2021) To decarbonize industry, we must decarbonize heat. Joule.
    [122] Enbridge Gas, Enbridge Gas announces a $5.2M Hydrogen Blending Pilot Project to further explore greening of the natural gas grid. Enbridge Gas Inc., 2020. Available from: https://www.newswire.ca/news-releases/enbridge-gas-announces-a-5-2m-hydrogen-blending-pilot-project-to-further-explore-greening-of-the-natural-gas-grid-849137548.html.
    [123] Nicita A, Maggio G, Andaloro APF, et al. (2020) Green hydrogen as feedstock: Financial analysis of a photovoltaic-powered electrolysis plant. Int J Hydrogen Energy 45: 11395-11408. doi: 10.1016/j.ijhydene.2020.02.062
    [124] Eliezer D, Eliaz N, Senkov ON, et al. (2000) Positive effects of hydrogen in metals. Mater Sci Eng A 280: 220-224. doi: 10.1016/S0921-5093(99)00670-X
    [125] Gielen D, Saygin D, Taibi E, et al. (2020) Renewables-based decarbonization and relocation of iron and steel making: A case study. J Ind Ecol 24: 1113-1125. doi: 10.1111/jiec.12997
    [126] Ikäheimo J, Kiviluoma J, Weiss R, et al. (2018) Power-to-ammonia in future North European 100 % renewable power and heat system. Int J Hydrogen Energy 43: 17295-17308. doi: 10.1016/j.ijhydene.2018.06.121
    [127] Valera-Medina A, Xiao H, Owen-Jones M, et al. (2018) Ammonia for power. Prog Energy Combust Sci 69: 63-102. doi: 10.1016/j.pecs.2018.07.001
    [128] Hogerwaard J, Dincer I (2016) Comparative efficiency and environmental impact assessments of a hydrogen assisted hybrid locomotive. Int J Hydrogen Energy 41: 6894-6904. doi: 10.1016/j.ijhydene.2016.01.118
    [129] Dalena F, Senatore A, Marino A, et al. (2018) Methanol Production and Applications: An Overview. Methanol Sci Eng, 3-28.
    [130] Steynberg AP (2004) Chapter 1 - Introduction to Fischer-Tropsch Technology, In: Steynberg A, Dry MBT-S in SS and C (Eds.), Fischer-Tropsch Technology, Elsevier, 1-63.
    [131] Xu H, Maroto-Valer MM, Ni M, et al. (2019) Low carbon fuel production from combined solid oxide CO2 co-electrolysis and Fischer-Tropsch synthesis system: A modelling study. Appl Energy 242: 911-918. doi: 10.1016/j.apenergy.2019.03.145
    [132] Peng DD, Fowler M, Elkamel A, et al. (2016) Enabling utility-scale electrical energy storage by a power-to-gas energy hub and underground storage of hydrogen and natural gas. J Nat Gas Sci Eng 35: 1180-1199. doi: 10.1016/j.jngse.2016.09.045
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