Review

Novel designs of thermoelectric generator for automotive waste heat recovery: A review

  • Many worldwide scientists have concentrated on using waste heat recovery technology in automotive applications because of increasingly strict fuel consumption. The thermoelectric generator (TEG) has garnered significant interest in the automobile sector as a viable waste heat recovery solution over the past several decades. A short survey of thermoelectric materials and heat exchangers for TEG systems is initially presented in this paper. To overcome the heat exchanger's current shortcomings, some previous studies designed a variety of the heat exchanger geometry of the TEG system. They suggested concentric cylindrical TEG system utilizes an annular thermoelectric module instead of the traditional square-shaped one. It uses the heat pipe's benefits to improve radial heat transmission. A comparison of the water-inside and gas-inside arrangements indicated that the water-inside concentric cylindrical TEG system provided a greater power output in our simulations to test the performance of the proposed system.

    Citation: Tan Nguyen Tien, Quang Khong Vu, Vinh Nguyen Duy. Novel designs of thermoelectric generator for automotive waste heat recovery: A review[J]. AIMS Energy, 2022, 10(4): 922-942. doi: 10.3934/energy.2022042

    Related Papers:

    [1] He Liu, Chuanjun Dai, Hengguo Yu, Qing Guo, Jianbing Li, Aimin Hao, Jun Kikuchi, Min Zhao . Dynamics induced by environmental stochasticity in a phytoplankton-zooplankton system with toxic phytoplankton. Mathematical Biosciences and Engineering, 2021, 18(4): 4101-4126. doi: 10.3934/mbe.2021206
    [2] Juan Li, Yongzhong Song, Hui Wan, Huaiping Zhu . Dynamical analysis of a toxin-producing phytoplankton-zooplankton model with refuge. Mathematical Biosciences and Engineering, 2017, 14(2): 529-557. doi: 10.3934/mbe.2017032
    [3] Xinyou Meng, Jie Li . Stability and Hopf bifurcation analysis of a delayed phytoplankton-zooplankton model with Allee effect and linear harvesting. Mathematical Biosciences and Engineering, 2020, 17(3): 1973-2002. doi: 10.3934/mbe.2020105
    [4] Jean-Jacques Kengwoung-Keumo . Dynamics of two phytoplankton populations under predation. Mathematical Biosciences and Engineering, 2014, 11(6): 1319-1336. doi: 10.3934/mbe.2014.11.1319
    [5] Dongmei Wu, Hao Wang, Sanling Yuan . Stochastic sensitivity analysis of noise-induced transitions in a predator-prey model with environmental toxins. Mathematical Biosciences and Engineering, 2019, 16(4): 2141-2153. doi: 10.3934/mbe.2019104
    [6] Yueping Dong, Jianlu Ren, Qihua Huang . Dynamics of a toxin-mediated aquatic population model with delayed toxic responses. Mathematical Biosciences and Engineering, 2020, 17(5): 5907-5924. doi: 10.3934/mbe.2020315
    [7] Hong Yang . Global dynamics of a diffusive phytoplankton-zooplankton model with toxic substances effect and delay. Mathematical Biosciences and Engineering, 2022, 19(7): 6712-6730. doi: 10.3934/mbe.2022316
    [8] Xin Zhao, Lijun Wang, Pankaj Kumar Tiwari, He Liu, Yi Wang, Jianbing Li, Min Zhao, Chuanjun Dai, Qing Guo . Investigation of a nutrient-plankton model with stochastic fluctuation and impulsive control. Mathematical Biosciences and Engineering, 2023, 20(8): 15496-15523. doi: 10.3934/mbe.2023692
    [9] Wenjie Yang, Qianqian Zheng, Jianwei Shen, Linan Guan . Bifurcation and pattern dynamics in the nutrient-plankton network. Mathematical Biosciences and Engineering, 2023, 20(12): 21337-21358. doi: 10.3934/mbe.2023944
    [10] Qihua Huang, Hao Wang . A toxin-mediated size-structured population model: Finite difference approximation and well-posedness. Mathematical Biosciences and Engineering, 2016, 13(4): 697-722. doi: 10.3934/mbe.2016015
  • Many worldwide scientists have concentrated on using waste heat recovery technology in automotive applications because of increasingly strict fuel consumption. The thermoelectric generator (TEG) has garnered significant interest in the automobile sector as a viable waste heat recovery solution over the past several decades. A short survey of thermoelectric materials and heat exchangers for TEG systems is initially presented in this paper. To overcome the heat exchanger's current shortcomings, some previous studies designed a variety of the heat exchanger geometry of the TEG system. They suggested concentric cylindrical TEG system utilizes an annular thermoelectric module instead of the traditional square-shaped one. It uses the heat pipe's benefits to improve radial heat transmission. A comparison of the water-inside and gas-inside arrangements indicated that the water-inside concentric cylindrical TEG system provided a greater power output in our simulations to test the performance of the proposed system.



    After the pioneering work of Anderson and May [1], research on predator-prey-parasite system has been explored extensively [2,3,4]. It is now well documented that predator-prey-virus models exhibit more complex and interesting dynamical behaviors than the conventional ecological or epidemiological models [5]. Parasites play a prominent role in trophic interactions and strongly influence the food web characteristics. It can also manipulate the potential of its host and affect the abundance of a predator [6]. A number of studies have demonstrated that the predators tend to forage for prey with high parasite burden [7]. The different factors regulating the intricate planktonic food web are, namely, selective predation [8], nutrient inflow [9], grazing by higher predators [10], etc. Zooplankton are capable of discriminatory feeding [11], and its food selectivity criteria vary to a large extent [12]. Zooplankton can selectively ingest its food depending on a myriad of factors, namely size [13], digestibility [8], toxicity [14], availability [15], and nutrition value [16] of food. A number of studies have documented that Calanoid copepods can discriminate between toxic and nontoxic dinoflagellates [17], noxious and innoxious blue-greens [18], and live and dead algae of the same species [19].

    Marine viruses have been recognized to have a decisive lead in altering the physiological and biochemical compositions of their hosts [20,21]. During viral infection, the host-cell characteristics such as cell size, the diffused infochemicals and the cell lipid membrane properties are changed, which influence the feeding behavior as well as the growth rate of zooplankton [22,23]. Emiliania huxleyi are extremely abundant marine phytoplankton species of the cocolithophore group which are frequently found in most of the marine ecosystems. Under favourable environmental conditions, E. huxleyi outburst into large seasonal blooms [24]. Gaint physcodnaviruses (E. huxleyi viruses, EhVs) are known to infect and lyse E. huxleyi cells and to be highly associated with the regulation of populations and the termination of blooms [25]. It has been documented that the exposure of E. huxleyi to EhVs causes more production of DMS, DMSP compared to normal bloom conditions [26,27]. Some studies have proposed that the infochemicals released from the infected cells act as an activated chemical signal which triggers the selective feeding behavior of the grazer zooplankton [23,28,29,27]. The role of viral infection in the producer trophic level of marine ecosystems has been investigated by several authors [30,31,32,33]. Some model based studies explicitly considered the role of free-viruses in eco-epidemiological system [6,34], assuming that both the healthy and infected phytoplankton are equally preferable for predation.

    Pollutants have a potentially hazardous effect on marine ecosystem. Pollution may arise from different sources, the most well known are influx of domestic sewage, industrial waste, agricultural run-off etc. The environmental toxins affect the plankton communities at different levels abundance, growth strategies, dominance and succession patterns. During predation these toxins are passed onto higher trophic level in the food chain in a cascading manner. The contact rate between environmental toxins and marine organisms is mainly dependent on their distribution pattern and behavioral attributes in the ecosystems [35]. Environmental toxins cause an implicit suppression in the growth of phytoplankton cells among a wide range of phytoplankton population [36,37]. In some recent studies, this growth suppression behavior of environmental toxins have been incorporated mathematically [38,39]. It has been shown that environmental toxin-induced growth suppression of phytoplankton population can lead to a destabilized system. However, the depletion of environmental toxins from the aquatic system plays a crucial role to stabilize the system. Yu et al. [40] have studied a stochastic phytoplankton-zooplankton model by considering toxin-producing phytoplankton and Markov switching in an impulsive polluted environment; they found that environmental fluctuations and exogenous toxicant input have a great influence on the survival fate of plankton.

    Recently, Bairagi and Adak [41] have studied the predator-prey dynamics, where the prey species are susceptible to infection and predators feed upon both the susceptible and infected prey with some preference. Their findings depict that understanding the consequences of predator's selectivity or preference may play a pivotal role to shape the community structure and ecological properties involving parasites. By dividing the entire phytoplankton population of a pelagic ecosystem into preferred and nonpreferred phytoplankton, Bairagi et al. [42] have shown that the selective predation of zooplankton and nutritional value of phytoplankton strongly impact on the complex plankton dynamics, including the bloom phenomenon. In the present investigation, we have captured the idea of selectivity tendency of grazer zooplankton on susceptible phytoplankton cells in the presence of infected ones, for the very first time. The objective of our study is to investigate the role of selectivity behavior on the persistence and dominance of healthy phytoplankton cells. We would also like to investigate the combined effects of free-viruses and environmental toxins on the dynamics of phytoplankton-zooplankton in the system, and how the selectivity behavior of zooplankton regulate the dynamics. The above ecological questions are answered by the model analysis and numerical simulations.

    Pollution of freshwater and marine systems by anthropogenic sources has become a concern over the last several decades. Organic (e.g. triazine herbicides) [43] and inorganic compounds (e.g. heavy metals) [44] both may have harmful effects to the organisms. For example, photosynthesis of the green algae Selenastrum capricornutum is inhibited due to pollutants originating from industrial and recreational sources [45]. In a marine planktonic community comprising mainly diatoms and herbivorous copepods in a low silicate, elevated copper environment [46], copper harms diatoms. At low concentrations, the herbicide triazine also affects primary producers directly by inhibiting photosynthesis, while effects on subsequent trophic levels only would be indirect [46]. Contamination of water bodies with insecticides such as carbaryl, azadirachtin, or cypermetrin increases the death rate of zooplankton.

    In phytoplankton population, viruses are not transmitted from infected phytoplankton to susceptible phytoplankton by contact. Usually, virus particles attach to the host cell and release its genetic material into the cell. The virus then uses the host cells machinery to replicate its own genetic material. Once replication has been completed, the virus particles burst out of the host cell into the extracellular space resulting in the death of the host cell. After escaped from the host cell, virus is ready to infect other susceptible phytoplankton. This kind of transmission converts directly a part of phytoplankton population to an infected class [6]. Moreover, in the absence of viral infection, primary consumers like copepods, access over E. huxleyi and other phytoplankton species at random but in the presence of viral infection zooplankton exhibit some sort of grazing preferences [23,27].

    Let S, I and Z be the concentrations of susceptible phytoplankton, infected phytoplankton and zooplankton in an aquatic ecosystem, and let V and E be the concentrations of free-viruses and environmental toxins in the same system. We have the following assumptions:

    1. In the absence of free-viruses V, environmental toxins E and the grazer zooplankton Z, the susceptible phytoplankton S grow logistically as dSdt=rS(1SK) with r being the intrinsic growth rate and K being the carrying capacity. The environmental toxins E affects the growth rate of S, and it reduces to r1+γγ1SE, where γ is the contact rate of environmental toxins with phytoplankton and zooplankton, and γ1 is the inhibition of the susceptible phytoplankton growth rate due to environmental toxins.

    2. The susceptible phytoplankton S, becomes infected by direct contact with free viruses, V, living in the system following a disc function βSVK1+V with the transmission parameter β and the half saturation constant K1. In the presence of free-viruses, V, the susceptible phytoplankton S is consumed by the zooplankton Z with the rate of αSd+S+θI. The parameter α is the predation rate of the zooplankton Z; d is the half saturation constant; and θ measures the selectivity/preference of the zooplankton to infected phytoplankton over the susceptible one or vice-versa. If θ>1, then zooplankton prefer infected phytoplankton, θ=1 implies equal preference to susceptible and infected phytoplankton, and 0<θ<1 means that zooplankton prefer susceptible phytoplankton.

    3. It is assumed that the infected phytoplankton, I, do not reproduce [47,48], and they are removed by cell lysis before having the capability of reproducing [49]. The infected phytoplankton do not compete for resource with susceptible phytoplankton, S. The infected phytoplankton, I, is consumed by the zooplankton, Z, with the rate of αθId+S+θI. The infected phytoplankton is assumed to die at a constant rate μ with an additional mortality rate γγ2E due to the environmental toxins, E, in the aquatic system.

    4. The zooplankton population increase on consumption of susceptible and infected phytoplankton; experience natural death at a constant rate ν, and additional death due to presence of environmental toxins in the system, γγ3ZE.

    5. Let b be the virus replication factor through the infected phytoplankton I, i.e., lysis of infected phytoplankton, on the average, producing b virus particles (b1). The decay rate of virus is assumed to be constant, δ. The virus is removed through the infection of susceptible phytoplankton at the rate βSVK1+V.

    6. The environmental toxins E has a constant input rate A and a depletion rate of ρ. The additional removal rates are due to being absorbed by both phytoplankton and zooplankton through their contact at a rate γ [38,40].

    The schematic diagram for the interplay among all the considered dynamical variables is depicted in Figure 1. Based on these ecological assumptions, we have the following system of nonlinear differential equations,

    dSdt=rS1+γγ1SE(1SK)βSVK1+VαSZd+S+θI,dIdt=βSVK1+VαθIZd+S+θIγγ2IEμI,dZdt=αZ(λ1S+λ2θI)d+S+θIνZγγ3ZE,dVdt=bμIβSVK1+VδV,dEdt=Aγ(S+I+Z)EρE. (2.1)
    Figure 1.  Schematic diagram of the system (2.1).

    The parameters involved in system (2.1) are positive constants. System (2.1) is to be analyzed with the following initial conditions,

    S(0)>0, I(0)>0, Z(0)>0, V(0)>0, E(0)>0. (2.2)

    We assume 0<λ2λ1<1, i.e., the per capita contribution of infected phytoplankton to the growth of zooplankton never exceeds that of the susceptible phytoplankton. Biological meanings of parameters in the system (2.1) is given in Table 1.

    Table 1.  Biological meanings of parameters in the system (2.1), and their values (hypothetical) used for numerical simulations.
    Parameters Descriptions Values Units
    r Intrinsic growth rate of susceptible phytoplankton 1.2 1/day
    K Carrying capacity of susceptible phytoplankton 10 cells/L
    β Force of infection 0.45 1/day
    K1 Half saturation constant 3 cells/L
    α Capture rate of susceptible phytoplankton 0.18 1/day
    θ Selectivity/preference of the zooplankton 0.15
    d Half saturation constant 5 cells/L
    λ1 Reproductive gain of zooplankton from susceptible phytoplankton 0.75
    λ2 Reproductive gain of zooplankton from infected phytoplankton 0.72
    μ Death rate of infected phytoplankton 0.2 1/day
    ν Mortality rate of zooplankton (natural and due to fish predation) 0.012 1/day
    b Virus replication factor 40
    δ Decay rate of free-virus 0.23 1/day
    A Input rate of environmental toxins in the system 6 μg/L/day
    γ Contact rate between environmental toxins with phytoplankton and zooplankton 0.15 L/cell/day
    γ1 Inhibition of growth rate of susceptible phytoplankton due to environmental toxins 0.1 day L/μg
    γ2 Death rate of infected phytoplankton due to environmental toxins 0.02 cell/μg
    γ3 Death rate of zooplankton due to environmental toxins 0.05 cell/μg
    ρ Depletion rate of environmental toxins 0.25 1/day

     | Show Table
    DownLoad: CSV

    In theoretical ecology, boundedness of a system implies that the system is well behaved. Boundedness of the solutions entails that none of the interacting populations grow exponentially for a long-time interval. The abundance of each population is bounded due to limited resource. Moreover, permanence of a system means the long-term survival of all populations of the system, no matter what the initial populations are. From mathematical point of view, permanence of a system means that strictly positive solutions do not have omega limit points on the boundary of the non-negative cone.

    We have the following theorem.

    Theorem 3.1. Every solution of system (2.1) with initial conditions (2.2) exists and unique in some interval [0,κ), where S(t)>0, I(t)>0, Z(t)>0, V(t)>0, E(t)>0, t0. Further, all non-negative solutions of system (2.1) that start in R5+ are uniformly bounded, and the feasible region for system (2.1) is given by the following set

    Ω={(S,I,Z,V,E): 0S+I+Z+νbμVM, 0EEm}.

    Further, if the following inequalities are satisfied:

    rK1d>(1+γγ1KEm)(βdVm+αK1Zm),βSa>(αθZmd+γγ2Em+μ)Im,α(λ1Sa+λ2θIa)d+K+θIm>ν+γγ3Em, (3.1)

    then system (2.1) is permanent. The quantities M, Em, Sa, Im, Zm and Vm are defined in the proof.

    For proof of this theorem, see Appendix A.

    From the conditions in (3.1), we note that the susceptible phytoplankton may disappear from the aquatic system for very high values of force of infection or its contact rate with environmental toxins; the infected phytoplankton and hence the free-viruses may extinct for very low values of the force of infection or for very high values of its contact rate with environmental toxins; the zooplankton may extinct for very high values of its natural mortality or death rate due to environmental toxins.

    In the absence of free-viruses and environmental toxins, system (2.1) reduces to,

    dSdt=rS(1SK)αSZd+S,dZdt=λ1αSZd+SνZ, (3.2)

    whose dynamics have been well studied [50]. Here, we summarize its dynamics as follows. System (3.2) has the three feasible equilibria.

    1. The plankton-free equilibrium point ˜e0=(0,0) is always a saddle.

    2. If K(λ1αν)<dν, then global stability at the zooplankton-free equilibrium ˜e1=(K,0).

    3. If K(λ1αν)>dν and K<d(λ1α+ν)λ1αν, then global stability at the coexistence equilibrium ˜e=(˜S,˜Z), where

    ˜S=dνλ1αν, ˜Z=λ1rd{K(λ1αν)dν}K(λ1αν)2.

    4. If K(λ1αν)>dν and K>d(λ1α+ν)λ1αν, then globally stable and unique limit cycle around the coexistence equilibrium ˜e=(˜S,˜Z).

    In the absence of free-viruses in the aquatic system, model (2.1) reduces to,

    dSdt=rS1+γγ1SE(1SK)αSZd+S,dZdt=λ1αSZd+SνZγγ3ZE,dEdt=Aγ(S+Z)EρE. (3.3)

    Our model (3.3) differs from the models of [38,39] in the sense that here zooplankton are assumed to be affected by environmental toxins. In [38], the interaction between phytoplankton and zooplankton is assumed to be modified Beddington type. The effect of toxin liberation by phytoplankton on zooplankton and predation of zooplankton by fish are considered in [39]. Yu et al. [40] studied a stochastic model by considering that environmental toxins increase the death rate of phytoplankton as well as zooplankton.

    System (3.3) has the following three non-negative equilibria:

    1. The plankton-free equilibrium ˆe0=(0,0,A/ρ), always feasible.

    2. The zooplankton-free equilibrium ˆe1=(K,0,A/(γK+ρ)), always feasible.

    3. The coexistence equilibrium ˆe=(ˆS,ˆZ,ˆE), where

    ˆZ=1γ[γγ3A(d+ˆS)(λ1αν)ˆSνd(ρ+γˆS)], ˆE=Aρ+γ(ˆS+ˆZ)

    and ˆS is given by positive root of the following equation:

    r1+γγ1SˆE(1SK)αˆZd+S=0. (3.4)

    Regarding local stability of equilibria of the system (3.3), we have the following theorem.

    Theorem 3.2. 1. The equilibrium ˆe0 is always unstable.

    2. The equilibrium ˆe1 is always stable.

    3. The equilibrium ˆe, if feasible, is locally asymptotically stable if and only if the following conditions hold,

    ˆA1>0, ˆA3>0, ˆA1ˆA2ˆA3>0. (3.5)

    For proof of this theorem, see Appendix B.

    In the absence of environmental toxins in the aquatic system, model (2.1) reduces to,

    dSdt=rS(1SK)βSVK1+VαSZd+S+θI,dIdt=βSVK1+VαθIZd+S+θIμI,dZdt=αZ(λ1S+λ2θI)d+S+θIνZ,dVdt=bμIβSVK1+VδV. (3.6)

    In [6], authors assumed that both the healthy and infected phytoplankton are equally preferable for predation. They showed that virus replication factor and half saturation constant of viral infection play an important role in persistence of infection in the system. They also observed that for low infection rate, the virus cannot persist in the system and the system becomes infection-free. If the force of infection increases then above a threshold value, all the species coexist and the system becomes endemic. However, for very large values of force of infection, the zooplankton population extinct from the system. The preference behavior of predator over susceptible prey is considered in [41]; the explicit role of parasites is not taken into account. In [42], the authors showed that the phytoplankton-zooplankton interaction is very complex and the plankton dynamics strongly depends on the selective predation of zooplankton.

    System (3.6) exhibits five non-negative equilibria given as,

    1. The population-free equilibrium ¯e0=(0,0,0,0), which is always feasible.

    2. The equilibrium with only susceptible phytoplankton ¯e1=(K,0,0,0), which is always feasible.

    3. The disease-free equilibrium ¯e2=(¯S2,0,¯Z2,0), where ¯S2=˜S and ¯Z2=˜Z. The equilibrium ¯e2 is feasible provided K(λ1αν)>dν.

    4. The zooplankton-free equilibrium ¯e3=(¯S3,¯I3,0,¯V3), where ¯S3=Kr(rβ¯V3K1+¯V3), ¯I3=Kβ¯V3μr(K1+¯V3)(1β¯V3K1+¯V3) and ¯V3 is positive root of the quadratic,

    ¯a2V2+¯a1V+¯a0=0, (3.7)

    where

    ¯a2=rδ, ¯a1=2rK1δβK(b1)(rβ), ¯a0=rK1{δK1βK(b1)}.

    As ¯a2>0, equation (3.7) has exactly one positive root if ¯a0<0. A necessary condition for ¯S3 to be positive is rK1+(rβ)¯V3>0. Thus, the equilibrium ¯e3 is feasible provided,

    rK1+(rβ)¯V3>0, δK1βK(b1)<0. (3.8)

    In case, the latter is not satisfied, then equation (3.7) has either two or no positive roots.

    5. The coexistence equilibrium ¯e=(¯S,¯I,¯Z,¯V). In equilibrium ¯e, we have

    ¯S=1λ1αν[νdθ(λ2αν)¯V[δ(K1+¯V)(λ1αν)+νdβ¯V]bμ(K1+¯V)(λ1αν)+θβ¯V(λ2αν)],¯I=¯V[δ(K1+¯V)(λ1αν)+νdβ¯V]bμ(K1+¯V)(λ1αν)+θβ¯V(λ2αν), ¯Z=d+¯S+θ¯Iαθ¯I[β¯S¯VK1+¯Vμ¯I] (3.9)

    and ¯V is positive root of the equation

    r(1¯SK)βVK1+Vα¯Zd+¯S+θ¯I=0. (3.10)

    Regarding local stability of equilibria of the system (3.6), we have the following theorem.

    Theorem 3.3. 1. The equilibrium ¯e0 is always unstable.

    2. The equilibrium ¯e1 is locally asymptotically stable if

    δK1βK(b1)>0, Kλ1αν(K+d)<0. (3.11)

    3. The equilibrium ¯e2, if feasible, is locally asymptotically stable if and only if the following conditions are satisfied,

    ¯C1>0, ¯C4>0, ¯C1¯C2¯C3>0, ¯C3(¯C1¯C2¯C3)¯C21¯C4>0. (3.12)

    4. The equilibrium ¯e3, if feasible, is locally asymptotically stable provided,

    ¯B1>0, ¯B3>0, ¯B1¯B2¯B3>0, α(λ1¯S3+λ2θ¯I3)d+¯S3+θ¯I3ν<0. (3.13)

    5. The equilibrium ¯e, if feasible, is locally asymptotically stable if and only if the following conditions are satisfied,

    ¯A1>0, ¯A4>0, ¯A1¯A2¯A3>0, ¯A3(¯A1¯A2¯A3)¯A21¯A4>0. (3.14)

    For proof of this theorem, see Appendix C.

    System (2.1) exhibits the following five non-negative equilibria:

    1. The equilibrium e0=(0,0,0,0,A/ρ), which is always feasible.

    2. The equilibrium e1=(K,0,0,0,A/(γK+ρ)), which is always feasible.

    3. The equilibrium e2=(S2,0,Z2,0,E2), where S2=ˆS, Z2=ˆZ and E2=ˆE.

    4. The equilibrium e3=(S3,I3,0,V3,E3), where

    I3=1bμ[δV3+βS3V3K1+V3], E3=Aρ+γ{S3+1bμ(δV3+βS3V3K1+V3)},

    S3 and V3 are positive solutions of the following isoclines:

    r(1S/K)[ρ+γ{S+1bμ(δV+βSVK1+V)}]ρ+γ{S+1bμ(δV+βSVK1+V)+Aγ1S}βVK1+V=0,βSVK1+V1bμ(δV+βSVK1+V)[μ+Aγγ2ρ+γ{S+1bμ(δV+βSVK1+V)}]=0.

    5. The equilibrium e=(S,I,Z,V,E), where

    E=1γγ3[α{λ1S+λ2θbμ(δV+βSVK1+V)}d+S+θbμ(δV+βSVK1+V)ν], I=1bμ(δV+βSVK1+V),Z=1γ[γγ3A{d+S+θbμ(δV+βSVK1+V)}S(αλ1ν)νd+θ(αλ2ν)bμ(δV+βSVK1+V)ργ{S+1bμ(δV+βSVK1+V)}],

    S and V are positive solutions of the following isoclines:

    r1+γγ1SE(1SK)βVK1+VαZd+S+θI=0, (3.15)
    βSVK1+VαθIZd+S+θIγγ2IEμI=0. (3.16)

    Regarding local stability of equilibria of the system (2.1), we have the following theorem.

    Theorem 3.4. 1. The equilibrium e0 is always unstable.

    2. The equilibrium e1 is locally asymptotically stable provided,

    ν+γγ3AγK+ρ>αλ1Kd+K, (μ+γγ2AγK+ρ)(δ+βKK1)>bβμKK1. (3.17)

    3. The equilibrium e2, if feasible, is locally asymptotically stable if and only if the following conditions hold,

    A5>0, A1A2A3>0, A3(A1A2A3)A1(A1A4A5)>0,A4{A3(A1A2A3)A1(A1A4A5)}A5{A2(A1A2A3)(A1A4A5)}>0. (3.18)

    4. The equilibrium e3, if feasible, is locally asymptotically stable if and only if the following conditions hold,

    B5>0, B1B2B3>0, B3(B1B2B3)B1(B1B4B5)>0,B4{B3(B1B2B3)B1(B1B4B5)}B5{B2(B1B2B3)(B1B4B5)}>0. (3.19)

    5. The equilibrium e, if feasible, is locally asymptotically stable if and only if the following conditions hold,

    C5>0, C1C2C3>0, C3(C1C2C3)C1(C1C4C5)>0,C4{C3(C1C2C3)C1(C1C4C5)}C5{C2(C1C2C3)(C1C4C5)}>0. (3.20)

    For proof of this theorem, see Appendix D.

    In the context of a biological system, bifurcations describe how the system dynamics may qualitatively drastically change if a parameter varies. A Hopf bifurcation is a critical point where a system's stability switches and a periodic solution arises. We consider here some parameters: selectivity/preference of zooplankton (θ), force of infection (β), growth suppression of susceptible phytoplankton due to environmental toxins (γ1) and carrying capacity of susceptible phytoplankton (K) as bifurcation parameters. Analytically we investigate for the possibility of Hopf bifurcation from the coexistence equilibrium e by taking the selectivity/preference of zooplankton (θ) as bifurcation parameter, keeping other parameters fixed.

    Regarding Hopf bifurcation of the system (2.1) around equilibrium e with respect to the parameter θ, we have the following theorem.

    Theorem 3.5. When the intensity of selectivity (θ) exceeds a critical value, the system (2.1) enters into Hopf-bifurcation around the coexistence equilibrium e. The necessary and sufficient conditions for the occurrence of Hopf bifurcation are that there exists θ=θ such that

    1. ψ(θ){C3(θ)C1(θ)C2(θ)}{C5(θ)C2(θ)C3(θ)C4(θ)}{C5(θ)C1(θ)C4(θ)}2=0.

    2. C1(θ)>0, C1(θ)C2(θ)C3(θ)>0, C3(θ)C1(θ)ω0>0, ω0=C5(θ)C1(θ)C4(θ)C3(θ)C1(θ)C2(θ)>0.

    3. dψ(θ)dθ|θ=θ=0.

    For proof of this theorem, see Appendix E.

    In Table 2, we listed the equilibria of the systems (2.1), (3.2), (3.3) and (3.6), and the conditions for their stability.

    Table 2.  Equilibria and conditions for their stability.
    Models Equilibria Conditions for LAS
    (3.2) ˜e0=(0,0)) Always unstable
    ˜e1=(K,0) K(λ1αν)<dν
    ˜e=(˜S,˜Z) K(λ1αν)>dν, K<d(λ1α+ν)λ1αν
    (3.3) ˆe0=(0,0,A/ρ) Always unstable
    ˆe1=(K,0,A/(γK+ρ)) Always stable
    ˆe=(ˆS,ˆZ,ˆE) Conditions in (3.5)
    (3.6) ¯e0=(0,0,0,0) Always unstable
    ¯e1=(K,0,0,0) Conditions in (3.11)
    ¯e2=(¯S2,0,¯Z2,0) Conditions in (3.12)
    ¯e3=(¯S3,¯I3,0,¯V3) Conditions in (3.13)
    ¯e=(¯S,¯I,¯Z,¯V) Conditions in (3.14)
    (2.1) e0=(0,0,0,0,A/ρ) Always unstable
    e1=(K,0,0,0,A/(γK+ρ)) Conditions in (3.17)
    e2=(S2,0,Z2,0,E2) Conditions in (3.18)
    e3=(S3,I3,0,V3,E3) Conditions in (3.19)
    e=(S,I,Z,V,E) Conditions in (3.20)

     | Show Table
    DownLoad: CSV

    Here, we report the simulations to investigate the behavior of system (2.1), performed using the Matlab variable step Runge-Kutta solver ode45. The set of parameter values are chosen within the range prescribed in various previous literature sources [6,34,38,39,41,42], and are given in Table 1. Unless it is mentioned, the values of parameters used for numerical simulations are the same as in Table 1. In Table 3, we listed the equilibria of the systems (2.1), (3.2), (3.3) and (3.6), and the corresponding eigenvalues of the system's Jacobian. In Table 3, we choose parameter values in such a way that coexistence equilibrium of each system is stable. For system (2.1), we choose parameter values as in Table 1, while for other systems, the changed parameters are: α=0.03 in system (3.2); α=0.057 in system (3.3); α=0.057 and θ=0.15 in system (3.6). From the table, we note that the system (3.3) has two coexistence equilibria: ˆe1 and ˆe2, of which the former is stable and the latter is unstable. Also, the equilibria ˆe1 and ˆe1 are simultaneously stable, thus the system (3.3) shows bistability behavior between these two equilibria. Bistability is a phenomenon where the system can converge to two different equilibria in the same parametric region based on the variation of the initial conditions.

    Table 3.  Equilibria and the corresponding eigenvalues of system's Jacobian.
    Models Equilibria Eigenvalues of the system's Jacobian
    (3.2) ˜e0=(0,0)) 1.1999, 0.0120
    ˜e1=(10,0) 1.1999, 0.0030
    ˜e=(5.7142,183.6734) 0.4043, 0.0071
    (3.3) ˆe0=(0,0,24) 0.2500, 1.1999, 0.1920
    ˆe1=(10,0,3.4285)) 1.7500, 0.7924, 0.0092
    ˆe1=(2.5599,116.9310,0.3301) 0.0066±0.0911i, 18.1762
    ˆe2=(9.6963,7.1492,2.1607) 2.7882, 0.8680, 0.0057
    (3.6) ¯e0=(0,0,0,0) 1.1999, 0.2300, 0.2000, 0.0120
    ¯e1=(10,0,0,0) 1.1999, 2.5825, 4.5125, 0.0165
    ¯e2=(1.9512,0,117.7870,0) 0.0184±0.0894i, 1.0989, 1.9665
    ¯e3=(6.2735,14.0269,0,475.6954) 0.7533, 0.2313, 0.1981, 0.0145
    ¯e=(1.6059,2.4375,70.1090,81.7521) 0.3601, 0.1733, 0.0194±0.0687i
    (2.1) e0=(0,0,0,0,24) 0.2500, 1.1999, 0.1920, 0.2300, 0.2719
    e1=(10,0,0,0,3.4285) 1.7500, 0.7924, 0.0377, 4.5166, 2.5763
    e2=(0.8666,0,35.2363,0,1.0590) 0.0886, 0.0583, 5.6732, 1.3824, 0.6571
    e3=(5.6319,12.2052,0,413.5891,2.0508) 2.9498, 0.6434, 0.2289, 0.1814, 0.0273
    e=(0.8860,1.2285,21.9939,41.1149,1.5518) 3.8772, 0.3882, 0.1071±0.0316i, 0.0290

     | Show Table
    DownLoad: CSV

    First, we investigate the dynamics of the system (2.1) in the absence of free viruses and environmental toxins i.e., subsystem (3.2), Figure 2. We observe that for system (3.2), the coexistence equilibrium ˜e is stable at α=0.03 but the stability is lost on increasing the values of α or K. Moreover, on decreasing the values of λ1, the coexistence equilibrium ˜e losses its stability and the zooplankton-free equilibrium ˜e1 appears in the system. We observe that the system (3.2) is oscillatory at α=0.057, while the introduction of environmental toxins in system (i.e., system (3.3)) makes it stable (Figure 3(a)), but for higher values of input rate of environmental toxins (A=20.5), the system settles to zooplankton-free steady state (Figure 3(b)). Next, we see bistability behavior of the system (3.3) in Figure 4(a). Here, blue region stands for stability domain for the equilibrium ˆe1, and red region stands for stability domain for the equilibria ˆe1 and ˆe1. We observe that the system (3.3) shows bistability between the zooplankton-free equilibrium ˆe1 and the coexistence equilibrium ˆe1 for large input rate of environmental toxins in the aquatic system. Thus, high input rate of environmental toxins leads to extinction of zooplankton or persistence of all the populations depending on the initial conditions. We also plot basin of attractions to confirm bistability behavior of the system. In Figure 4(b), magenta region represents the basin of attraction for the equilibrium ˆe1, and the green region represents the basin of attraction for the equilibrium ˆe1. Next, we observe the dynamics of system (3.6), i.e., the system with free-viruses but without environmental toxins. We observe that the introduction of free-viruses drives the unstable equilibrium of SZ system to stable equilibrium of SIZV system, Figure 5. On increasing the preference of zooplankton on infected phytoplankton, system (3.6) shows limit cycle oscillation around the disease-free equilibrium, ¯e2 (see Figure 6). Next, we observe the behavior of system (3.6) by varying the force of infection, β (see Figure 7). We find that for low values of force of infection, the system is oscillatory around the disease-free equilibrium, but the oscillation is around the coexistence equilibrium on increasing the values of force of infection; further increase in the values of force of infection results in stable coexistence of all the populations.

    Figure 2.  System (3.2) shows (a) stable coexistence at α=0.03, (b) limit cycle oscillations at α=0.057, (c) limit cycle oscillations at α=0.03 and K=17, and (d) settles to zooplankton-free equilibrium ˜e1 at α=0.03 and λ1=0.24. Rest of the parameters are at the same value as in Table 1.
    Figure 3.  System (3.3) shows (a) stable focus at α=0.057, and (b) extinction of zooplankton at α=0.057 and A=20.5. Rest of the parameters are at the same value as in Table 1.
    Figure 4.  (a) Bistability region of system (3.3), and (b) basin of attraction. Rest of the parameters are at the same value as in Table 1 except α=0.057. In (a), blue region represents the domain for stability of the equilibrium ˆe1, and red region represents the domain for stability of equilibria ˆe1 and ˆe1. In (b), magenta region represents the basin of attraction for the equilibrium ˆe1, and the green region represents the basin of attraction for the equilibrium ˆe1.
    Figure 5.  System (3.6) shows stable focus at α=0.057 and θ=0.15. Rest of the parameters are at the same value as in Table 1.
    Figure 6.  System (3.6) shows limit cycle oscillation around the disease-free equilibrium ¯e2 at α=0.057 and θ=5.85. Rest of the parameters are at the same value as in Table 1.
    Figure 7.  Bifurcation diagram of the system (3.6) with respect to β. Rest of the parameters are at the same value as in Table 1 except α=0.057. Here, red line represents the upper limit of oscillation cycle and blue line represents the lower limit of oscillation cycle.

    We employed a global sensitivity analysis to assess the impact of uncertainty and the sensitivity of the outcomes of the numerical simulations to variations in each parameter of the model (2.1) using Latin Hypercube Sampling (LHS) and partial rank correlation coefficients (PRCC) [51,52]. To generate the LHS matrices, we assume that all the model parameters are uniformly distributed. We performed PRCC analyses for three different time points in order to investigate which parameters consistently influence free-viruses and environmental toxins in time. Nonlinear and monotone relationships are observed for the free-viruses and environmental toxins with the input parameters of the model (2.1), which is a prerequisite for computing PRCCs. Then, simulations of the model per LHS run were carried out, using the baseline values tabulated in Table 4 and the ranges as 25% from the baseline values (in either direction). The indexes are evaluated at the time points 200,400 and 600 days. For each of the three time points, denoted by 1, 2 and 3, PRCC results are shown in Figs. 8(a) & 8(b) for free-viruses and environmental toxins, respectively. We observe that the PRCC values of free-viruses decrease with time for the parameters, α, d, ν, γ1 and γ3 while for the environmental toxins, the PRCC values decrease for the parameters β and θ, and increases for the parameter A, indicating that these parameters consistently influence free-viruses/environmental toxins in the system; for other parameters there is no trend of either increasing or decreasing in the PRCC's values.

    Table 4.  Baseline values and ranges of variability of the parameters of the system (2.1).
    Parameters Baseline values Minimum values Maximum values
    r 1.2 0.9000 1.5000
    K 10 7.5000 12.5000
    β 0.45 0.3375 0.5626
    K1 3 2.2500 3.7500
    α 0.18 0.1350 0.2250
    θ 0.15 0.1125 0.1875
    d 5 3.7500 6.2500
    λ1 0.75 0.5625 0.9375
    λ2 0.72 0.5400 0.9000
    μ 0.2 0.1500 0.2500
    ν 0.012 0.0090 0.0150
    b 40 30.0000 50.0000
    δ 0.23 0.1725 0.2875
    A 6 4.5000 7.5000
    γ 0.15 0.1125 0.1875
    γ1 0.1 0.0750 0.1250
    γ2 0.02 0.0150 0.0250
    γ3 0.05 0.0375 0.0625
    ρ 0.25 0.1875 0.3125

     | Show Table
    DownLoad: CSV
    Figure 8.  PRCC results showing sensitivity indices of the model parameters with (a) free-viruses, V, and (b) environmental toxins, E, chosen as baseline PRCC analysis variables.

    We discuss the Hopf bifurcation near the coexistence equilibrium e on varying the intensity of selectivity (θ), inhibition of phytoplankton growth due to environmental toxins (γ1), force of infection (β), and carrying capacity of susceptible phytoplankton (K). For the set of parameter values in Table 1, system (2.1) shows stable coexistence of all the populations (see Figure 9) but at θ=1.8, we observe that the system shows limit cycle oscillations around the coexistence equilibrium (see Figure 10). To get a clear view, we vary θ from 0 to 6 and draw bifurcation diagram of system (2.1) with respect to θ, Figure 11. We observe that for low values of θ, the system shows stable coexistence of all the populations, but shows limit cycle oscillations around the coexistence equilibrium e after a critical value of θ; further increase in the values of θ leads to instability of the infection-free equilibrium e2. Next, we draw the bifurcation diagram of the system (2.1) by varying the parameter γ1 in the interval [0, 0.2], Figure 12. We get that for very low values of γ1, the solution trajectories are oscillating around the coexistence equilibrium but the solution trajectories become stable after a threshold value of γ1. Now, we vary the force of infection (β) in the interval [0, 1] and draw bifurcation diagram of the system (2.1), Figure 13. We observe that for very low values of β, the infection-free equilibrium e2 is unstable, but increase in the values of β results in the instability of the coexistence equilibrium, e. The equilibrium e becomes stable for higher values of β. For very large values of force of infection, the system settles to the zooplankton-free steady state. Next, by varying the values of K in the interval $ [5,15] $, we plot bifurcation diagram of the system (2.1), Figure 14. We observe that the stable equilibrium becomes unstable with high-amplitude oscillations with increasing values of K. It is apparent from Figure 15 that for large values of input rate of environmental toxins, the zooplankton-free equilibrium, e3, is stable.

    Figure 9.  System (2.1) shows stable focus for the parameter values in Table 1.
    Figure 10.  System (2.1) shows limit cycle oscillations around the coexistence equilibrium, e, at θ=1.8. Rest of the parameters are at the same value as in Table 1.
    Figure 11.  Bifurcation diagram of the system (2.1) with respect to θ. Rest of the parameters are at the same value as in Table 1. Here, the red line represents the upper limit of the oscillation cycle and the blue line represents the lower limit of the oscillation cycle.
    Figure 12.  Bifurcation diagram of the system (2.1) with respect to γ1. Rest of the parameters are at the same value as in Table 1. Here, the red line represents the upper limit of the oscillation cycle and the blue line represents the lower limit of the oscillation cycle.
    Figure 13.  Bifurcation diagram of the system (2.1) with respect to β. Rest of the parameters are at the same value as in Table 1. Here, the red line represents the upper limit of the oscillation cycle and the blue line represents the lower limit of the oscillation cycle.
    Figure 14.  Bifurcation diagram of the system (2.1) with respect to K. Rest of the parameters are at the same value as in Table 1. Here, the red line represents the upper limit of the oscillation cycle and the blue line represents the lower limit of the oscillation cycle.
    Figure 15.  For the system (2.1), zooplankton-free steady state is achieved at A=20. Rest of the parameters are at the same value as in Table 1.

    Next, we investigate how the stability of the system changes on varying two parameters at a time: (θ,A) and (θ,β), Figure 16. For this reason, we vary θ and A, and plot stability regions in (θ,A) plane, Figure 16(a). Here, regions green, red, blue, black and magenta correspond to zooplankton-free, stable coexistence, unstable coexistence, unstable infection-free, and stable infection-free domain, respectively. For low values of θ (θ<1) and high values of A, we get a zooplankton-free system. By increasing the values of θ, while keeping A at low values, the infection-free equilibrium is unstable while for large values of both θ and A, the infection-free equilibrium is stable. For low values of θ, the coexistence equilibrium is stable while for moderate values of θ, the coexistence equilibrium is unstable. It is apparent from Figure 16(b) that on increasing the values of force of infection, the system becomes zooplankton-free irrespective of the preference of zooplankton for phytoplankton. For low values of β, on increasing θ, the infection-free equilibrium is stable while on increasing the values of θ and moderate values of β, the coexistence equilibrium is stable.

    Figure 16.  Different stability regions of the system (2.1) in (a) (θ,A), and (b) (θ,β) parametric spaces. Regions green, red, blue, black and magenta correspond to zooplankton-free, stable coexistence, unstable coexistence, unstable infection-free, and stable infection-free domains, respectively. Rest of the parameters are at the same value as in Table 1 except in (b) A=19.

    Now, we see the effects of replication factor of free-viruses and input rate of environmental toxins in the aquatic system on the equilibrium abundances of all the densities for the systems (2.1), (3.2), (3.3) and (3.6), Figure 17. The comparisons between equilibrium levels of all the populations for different values of virus replication factor (b) and input rate of environmental toxins (A) are given in Table 5. We observe that the susceptible phytoplankton is at high equilibrium level if there is no viruses in the system and input rate of toxins is very low; while the susceptible phytoplankton is at low level in the absence of toxins but high value of virus replication factor. The infected phytoplankton is at high equilibrium level if virus replication factor is high, and becomes zero in the absence of free-viruses. The zooplankton population is maximum when the system is free of viruses and toxins but becomes very low in their presence. High values of replication factor of viruses and input rate of toxins maintained the high levels of these two environmental degrading agents. Next, we see the effect of two controllable parameters, decay rate of free-viruses and depletion rate of environmental toxins, on the equilibrium levels of variables in system (2.1), Figure 18. We see that zooplankton are at higher density for high values of these two rate parameters in comparison to the case when these parameters are at low values. Opposite situations occur for other variables of the system. Further, we see the percentage increase/decrease in system's variables by varying the decay rate of free-viruses (δ) and depletion rate of environmental toxins (ρ) in the interval [0.01, 0.99], Figure 19. From the figure, it is clear that the concentration of zooplankton changes significantly on increasing the decay rate of free-viruses and depletion rate of environmental toxins; the free-viruses are highly sensitive to its death rate.

    Figure 17.  Effects of the replication factor of free-viruses (b) and the input rate of environmental toxins (A) on the equilibrium values of all the variables of the system (2.1). Rest of the parameters are at the same value as in Table 1 except α=0.03.
    Table 5.  Comparison of equilibrium levels of state variables for systems (2.1), (3.2), (3.3) and (3.6). Rest of the parameter values are same as in Table 1 except α=0.03.
    State variables Comparison
    Susceptible phytoplankton (S) ˆS>˜S>S>¯S
    Infected phytoplankton (I) I>¯I>ˆI=˜I=0
    Zooplankton (Z) ˜Z>ˆZ>¯Z>Z
    Free-viruses (V) V>¯V>ˆV=˜V=0
    Environmental toxins (E) E>˜E>¯E=˜E=0

     | Show Table
    DownLoad: CSV
    Figure 18.  Effects of the decay rate of free-viruses (δ) and the depletion rate of environmental toxins on the equilibrium values of all the variables of the system (2.1). Rest of the parameters are at the same value as in Table 1 except α=0.05.
    Figure 19.  Percentage increase/decrease in the variables of the system (2.1) on varying δ and ρ in the interval [0.01, 0.99]. Rest of the parameter values are same as in Table 1 except α=0.05.

    In this paper, we proposed a model that incorporates zooplankton's selectivity on susceptible phytoplankton in the presence of infective ones, and seen the combined effects of marine viruses and environmental toxins on the dynamics of phytoplankton-zooplankton interactions. We studied the dynamics of full as well as submodels. We observed that in the absence of free-viruses and environmental toxins in the ecosystem, the system is stable for low values of capture rate of susceptible phytoplankton by zooplankton and carrying capacity of susceptible phytoplankton. But, increase in either of these two parameters, drives the system to an oscillatory state. If the reproductive gain of zooplankton on consumption of susceptible phytoplankton is very low, then the system will become zooplankton-free. We got that the introduction of environmental toxins in the system makes it stable if the system with susceptible phytoplankton and zooplankton is already oscillatory. Moreover, high input rate of environmental toxins results in the extinction of zooplankton population, which is not reported in the previous studies [38,39]. The extinction of zooplankton may be due to the fact that environmental toxins increase their death rate. Previously, the destabilizing effects of input rate of environmental toxins and its contact rate with phytoplankton, and the stabilizing effects of depletion rate of environmental toxins have been reported [38,39]. Also, we observed that the presence of free-viruses in the ecosystem can stabilize an unstable equilibrium of the SZ system. But, increase in the preference of zooplankton on infected phytoplankton results in the oscillation of the system around disease-free steady state, which was not obtained in the previous study [6]. We found that for low values of force of infection, the system is oscillatory around the disease-free equilibrium, but the oscillation is around the coexistence equilibrium on increasing the values of force of infection; further increase in the values of force of infection results in stable coexistence of all the populations.

    For system (2.1), we observed that for low values of preference of zooplankton on infected phytoplankton, the coexistence equilibrium is stable, but the coexistence equilibrium becomes unstable after a threshold value of preference of zooplankton; further increase in the values of preference of zooplankton on infected phytoplankton leads to instability of the infection-free equilibrium. Note that selectivity behavior of zooplankton was not considered in the previous study [6]. On increasing the values of the parameter related to inhibition of growth rate of susceptible phytoplankton due to environmental toxins, the system get stabilized. It is noted that for very low values of force of infection, the infection-free equilibrium is unstable but increase in the values of force of infection leads to the instability of the coexistence equilibrium; for higher values of force of infection a stable coexistence of all the populations is observed. Moreover, the ecosystem becomes zooplankton-free for very high values of force of infection. We observed that the stable equilibrium becomes unstable with increasing the carrying capacity of susceptible phytoplankton, i.e., increasing nutrient supply, which supports the existing hypothesis of the paradox of enrichment [53].

    The results of sensitivity analysis suggest that a strategy that reduces the parameters having positive PRCC values with either free-viruses or environmental toxins will adequately reduce the density of phytoplankton in the system. Furthermore, a strategy that increases the parameters having negative PRCC values with free-viruses (environmental toxins) will be effective in curtailing free-viruses (environmental toxins) in the system. Identification of these key parameters is important to the formulation of effective control strategies necessary for combating free-viruses and environmental toxins in the aquatic system. Comparison of the equilibrium values of variables in full and subsystems shows that the replication factor of free-viruses and input rate of environmental toxins in the ecosystems can be used as biological controls to combat the reductions in zooplankton and healthy phytoplankton populations. As different parameters show important effects in reducing the concentration of zooplankton, from modeling and analysis perspective, we can conclude that the concentration of zooplankton can be maintained by increasing the decay rate of free-viruses and depletion rate of environmental toxins. For the control of infected phytoplankton in the system, it is imperative to decrease free-viruses from that system by using antiviral reagents [54,55]. Bioremediation technology could be very useful to convert the toxigenic compounds to nontoxic products without further disruption to the local environment, which will enhance the persistence and stability of the populations [56]. Although environmental toxins are thought not to be entering marine ecosystems in large quantities yet, experimental evidence reveals the fact that phytoplankton populations are highly vulnerable to damage from environmental toxins [57]. Sometimes, for high concentration of environmental toxins, complete growth inhibition in phytoplankton was observed [58]. So, there might be a possibility of the population crash. But, it can be controlled through the higher depletion rate of environmental toxins. Regulating the depletion rate of environmental toxins could be an effective control strategy to prevent the crash of the aquatic food web system, which could be achieved with suitable human activities such as safe use of pesticides, chemical toxins, awareness among human etc.

    The authors thank the associate editor and the anonymous reviewers for valuable comments, which contributed to the improvement in the presentation of the paper. The research work of Saswati Biswas is supported by Council of Scientific and Industrial Research, Government of India, New Delhi in the form of Senior Research Fellowship (Ref. No. 20/12/2015(ⅱ)EU-V). Pankaj Kumar Tiwari is thankful to University Grants Commissions, New Delhi, India for providing financial support in form of D. S. Kothari post-doctoral fellowship (No.F.4-2/2006 (BSR)/MA/17-18/0021). The work of Yun Kang is partially supported by NSF-DMS (1313312 & 1716802); NSF-IOS/DMS (1558127), DARPA (ASC-SIM Ⅱ), and The James S. McDonnell Foundation 21st Century Science Initiative in Studying Complex Systems Scholar Award (UHC Scholar Award 220020472).

    The authors declare that there is no conflict of interest in this paper.



    [1] Amar AB, Kouki AB, Cao H (2015) Power approaches for implantable medical devices. Sensors (Switzerland) 15: 28889–28914. https://doi.org/10.3390/s151128889 doi: 10.3390/s151128889
    [2] Jaziri N, Boughamoura A, Müller J, et al. (2020) A comprehensive review of thermoelectric generators: Technologies and common applications. Energy Rep 6: 264–287. https://doi.org/10.1016/j.egyr.2019.12.011 doi: 10.1016/j.egyr.2019.12.011
    [3] Bombarda P, Invernizzi CM, Pietra C (2010) Heat recovery from diesel engines: A thermodynamic comparison between Kalina and ORC cycles. Appl Therm Eng 30: 212–219. https://doi.org/10.1016/j.applthermaleng.2009.08.006 doi: 10.1016/j.applthermaleng.2009.08.006
    [4] Crane D, Jackson G, Holloway D (2001) Towards optimization of automotive waste heat recovery using thermoelectrics. SAE Tech Pap 1: 1–13. https://doi.org/10.4271/2001-01-1021 doi: 10.4271/2001-01-1021
    [5] Jaziri N, Boughamoura A, Müller J, et al. (2020) A comprehensive review of Thermoelectric generators: Technologies and common applications. Energy Rep 6: 264–287. https://doi.org/10.1016/j.egyr.2019.12.011 doi: 10.1016/j.egyr.2019.12.011
    [6] Karvonen M, Kapoor R, Uusitalo A, et al. (2016) Technology competition in the internal combustion engine waste heat recovery: A patent landscape analysis. J Clean Prod 112: 3735–3743. https://doi.org/10.1016/j.jclepro.2015.06.031 doi: 10.1016/j.jclepro.2015.06.031
    [7] Jia N, Cao J, Tan XY, et al. (2021) Thermoelectric materials and transport physics. Mater Today Phys 21: 100519. https://doi.org/10.1016/j.mtphys.2021.100519 doi: 10.1016/j.mtphys.2021.100519
    [8] Knecht W (2008) Diesel engine development in view of reduced emission standards. Energy 33: 264–271. https://doi.org/10.1016/j.energy.2007.10.003 doi: 10.1016/j.energy.2007.10.003
    [9] Saqr KM, Mansour MK, Musa MN (2008) Thermal design of automobile exhaust based Thermoelectric generators: Objectives and challenges. Int J Automot Technol 9: 155160. https://doi.org/10.1007/s12239-008-0020-y doi: 10.1007/s12239-008-0020-y
    [10] Zhang X, Chau KT, Chan CC (2008) Overview of Thermoelectric generation for hybrid vehicles. J Asian Electr Veh 6: 1119–1124. https://doi.org/10.4130/jaev.6.1119 doi: 10.4130/jaev.6.1119
    [11] Abedin MJ, Masjuki HH, Kalam MA, et al. (2013) Energy balance of internal combustion engines using alternative fuels. Renewable Sustainable Energy Rev 26: 20–33. https://doi.org/10.1016/j.rser.2013.05.049 doi: 10.1016/j.rser.2013.05.049
    [12] Yüksel F, Ceviz MA (2003) Thermal balance of a four stroke SI engine operating on hydrogen as a supplementary fuel. Energy 28: 1069–1080. https://doi.org/10.1016/S0360-5442(03)00090-2 doi: 10.1016/S0360-5442(03)00090-2
    [13] Durgun O, Şahin Z (2009) Theoretical investigation of heat balance in direct injection (DI) diesel engines for neat diesel fuel and gasoline fumigation. Energy Convers Manage 50: 43–51. https://doi.org/10.1016/j.enconman.2008.09.007 doi: 10.1016/j.enconman.2008.09.007
    [14] Özcan H, Söylemez MS (2006) Thermal balance of a LPG fuelled, four stroke SI engine with water addition. Energy Convers Manage 47: 570–581. https://doi.org/10.1016/j.enconman.2005.05.019 doi: 10.1016/j.enconman.2005.05.019
    [15] Mukai K, Iijima T, Miyazaki H, et al. (2005) The effects of design factors of the combustion chamber on heat balance in a gasoline engine. SAE Tech Pap 1: 1–9. https://doi.org/10.4271/2005-01-2021 doi: 10.4271/2005-01-2021
    [16] Rakopoulos CD, Giakoumis EG (2006) Second-law analyses applied to internal combustion engines operation. Prog Energy Combust Sci 32: 2–47. https://doi.org/10.1016/j.pecs.2005.10.001 doi: 10.1016/j.pecs.2005.10.001
    [17] Şahin Z, Durgun O (2007) Theoretical investigation of effects of light fuel fumigation on diesel engine performance and emissions. Energy Convers Manage 48: 1952–1964. https://doi.org/10.1016/j.enconman.2007.01.027 doi: 10.1016/j.enconman.2007.01.027
    [18] Ramadhas AS, Jayaraj S, Muraleedharan C (2006) Theoretical modeling and experimental studies on biodiesel-fueled engine. Renewable Energy 31: 1813–1826. https://doi.org/10.1016/j.renene.2005.09.011 doi: 10.1016/j.renene.2005.09.011
    [19] Liu Y, Reitz RD (1998) Modeling of heat conduction within chamber walls for multidimensional internal combustion engine simulations. Int J Heat Mass Transf 41: 859–869.
    [20] Lounici MS, Loubar K, Balistrou M, et al. (2011) Investigation on heat transfer evaluation for a more efficient two-zone combustion model in the case of natural gas SI engines. Appl Therm Eng 31: 319–328. https://doi.org/10.1016/j.applthermaleng.2010.09.012 doi: 10.1016/j.applthermaleng.2010.09.012
    [21] Dado B, Gelbstein Y, Dariel MP (2010) Nucleation of nanosize particles following the spinodal decomposition in the pseudo-ternary Ge0.6Sn0.1Pb0.3Te compound. Scr Mater 62: 89–92. https://doi.org/10.1016/j.scriptamat.2009.09.029 doi: 10.1016/j.scriptamat.2009.09.029
    [22] Komisarchik G, Gelbstein Y, Fuks D (2017) Solubility of Ti in thermoelectric PbTe compound. Intermetallics 89: 16–21. https://doi.org/10.1016/j.intermet.2017.05.016 doi: 10.1016/j.intermet.2017.05.016
    [23] Meroz O, Gelbstein Y (2018) Thermoelectric Bi2Te3-xSex alloys for efficient thermal to electrical energy conversion. Phys Chem Chem Phys 20: 4092–4099.
    [24] Sadia Y, Elegrably M, Ben-Nun O, et al. (2013) Submicron features in higher manganese silicide. J Nanomater 2013: 5–10. https://doi.org/10.1155/2013/701268 doi: 10.1155/2013/701268
    [25] Zilber T, Cohen S, Fuks D, et al. (2019) TiNiSn half-Heusler crystals grown from metallic flux for thermoelectric applications. J Alloys Comp 781: 1132–1138. https://doi.org/10.1016/j.jallcom.2018.12.165 doi: 10.1016/j.jallcom.2018.12.165
    [26] Suwardi A, Cao J, Hu L, et al. (2020) Tailoring the phase transition temperature to achieve high-performance cubic GeTe-based thermoelectrics. J Mater Chem A 8: 18880–18890. https://doi.org/10.1039/D0TA06013E doi: 10.1039/D0TA06013E
    [27] Suwardi A, Cao J, Zhao Y, et al. (2020) Achieving high thermoelectric quality factor toward high figure of merit in GeTe. Mater Today Phys 14: 100239. https://doi.org/10.1016/j.mtphys.2020.100239 doi: 10.1016/j.mtphys.2020.100239
    [28] Chen X, Dai W, Wu T, et al. (2018) Thin film thermoelectric materials: Classification, characterization, and potential for wearable applications. Coatings 8: 1–16. https://doi.org/10.3390/coatings8070244 doi: 10.3390/coatings8070244
    [29] Ren P, Liu Y, He J, et al. (2018) Recent advances in inorganic material thermoelectrics. Inorg Chem Front 5: 2380–2398. https://doi.org/10.1039/C8QI00366A doi: 10.1039/C8QI00366A
    [30] Wong-Ng W, Yan Y, Otani M, et al. (2015) High throughput screening tools for thermoelectric materials. J Electron Mater 44: 1688–1696. https://doi.org/10.1007/s11664-014-3519-1 doi: 10.1007/s11664-014-3519-1
    [31] Bhattacharya S, Madsen GKH (2015) High-throughput exploration of alloying as design strategy for thermoelectrics. Phys Rev B: Condens Matter Mater Phys 92: 1–9. https://doi.org/10.48550/arXiv.1508.03477 doi: 10.48550/arXiv.1508.03477
    [32] Gibbs ZM, Ricci F, Li G, et al. (2017) Effective mass and Fermi surface complexity factor from ab initio band structure calculations. Npj Comput Mater 3: 1–6. https://doi.org/10.1038/s41524-017-0013-3 doi: 10.1038/s41524-017-0013-3
    [33] Liu R, Chen H, Zhao K, et al. (2017) Entropy as a gene-like performance indicator promoting thermoelectric materials. Adv Mater 29: 1–7. https://doi.org/10.1002/adma.201702712 doi: 10.1002/adma.201702712
    [34] Fan Z, Wang H, Wu Y, et al. (2017) Thermoelectric performance of PbSnTeSe high-entropy alloys. Mater Res Lett 5: 187–194. https://doi.org/10.1080/21663831.2016.1244116 doi: 10.1080/21663831.2016.1244116
    [35] Fan Z, Wang H, Wu Y, et al. (2016) Thermoelectric high-entropy alloys with low lattice thermal conductivity. RSC Adv 6: 52164–52170. https://doi.org/10.1039/C5RA28088E doi: 10.1039/C5RA28088E
    [36] Zhu Q, Wang S, Wang X, et al. (2021) Bottom-up engineering strategies for high-performance thermoelectric materials. Nano-Micro Letters 13: 1–38. Available from: https://link.springer.com/article/10.1007/s40820-021-00637-z.
    [37] Kinsella CE, O'Shaughnessy SM, Deasy MJ, et al. (2014) Battery charging considerations in small scale electricity generation from a thermoelectric module. Appl Energy 114: 80–90. https://doi.org/10.1016/j.apenergy.2013.09.025 doi: 10.1016/j.apenergy.2013.09.025
    [38] Kawajiri K, Kishita Y, Shinohara Y (2021) Life cycle assessment of thermoelectric generators (TEGs) in an automobile application. Sustainability 13: 1–13. https://doi.org/10.3390/su132413630 doi: 10.3390/su132413630
    [39] Karri MA, Thacher EF, Helenbrook BT (2011) Exhaust energy conversion by thermoelectric generator: Two case studies. Energy Convers Manage 52: 1596–1611. https://doi.org/10.1016/j.enconman.2010.10.013 doi: 10.1016/j.enconman.2010.10.013
    [40] Liu X, Deng YD, Li Z, et al. (2015) Performance analysis of a waste heat recovery thermoelectric generation system for automotive application. Energy Convers Manage 90: 121–127. https://doi.org/10.1016/j.enconman.2014.11.015 doi: 10.1016/j.enconman.2014.11.015
    [41] Wang Y, Dai C, Wang S (2013) Theoretical analysis of a thermoelectric generator using exhaust gas of vehicles as heat source. Appl Energy 112: 1171–1180. https://doi.org/10.1016/j.apenergy.2013.01.018 doi: 10.1016/j.apenergy.2013.01.018
    [42] Liu X, Li C, Deng YD, et al. (2015) An energy-harvesting system using thermoelectric power generation for automotive application. Int J Electr Power Energy Syst 67: 510–516. https://doi.org/10.1016/j.ijepes.2014.12.045 doi: 10.1016/j.ijepes.2014.12.045
    [43] Wang P, Ji C, Tang B, et al. (2010) Effect of common rail system on vehicle engine combustion performance. Proc-2010 Int Conf Optoelectron Image Process ICOIP 2010 1: 464–467. https://doi.org/10.1109/CCIENG.2011.6007975 doi: 10.1109/CCIENG.2011.6007975
    [44] Huang K, Chang H, Qin J, et al. (2011) The exploration of HCCI combustion in the high-power direct-injection diesel engine. CCIE 2011-Proc 2011 IEEE 2nd Int Conf Comput Control Ind Eng 1: 133–135. https://doi.org/10.1109/CCIENG.2011.6007975 doi: 10.1109/CCIENG.2011.6007975
    [45] Arsie I, Cricchio A, Pianese C, et al. (2014) A comprehensive powertrain model to evaluate the benefits of electric turbo compound (ETC) in reducing CO2 emissions from small diesel passenger cars. SAE Tech Pap 1. https://doi.org/10.4271/2014-01-1650 doi: 10.4271/2014-01-1650
    [46] Hatami M, Ganji DD, Gorji-Bandpy M (2014) A review of different heat exchangers designs for increasing the diesel exhaust waste heat recovery. Renewable Sustainable Energy Rev 37: 168–181. https://doi.org/10.1016/j.rser.2014.05.004 doi: 10.1016/j.rser.2014.05.004
    [47] Thomas J (2014) Drive cycle powertrain efficiencies and trends derived from EPA vehicle dynamometer results. SAE Int J Passeng Cars-Mech Syst 7: 1374–1384. https://doi.org/10.4271/2014-01-2562 doi: 10.4271/2014-01-2562
    [48] Liming F, Wenzhi G, Hao Q, et al. (2010) Heat recovery from internal combustion engine with Rankine cycle. Asia-Pacific Power Energy Eng Conf APPEEC 1: 2–5. https://doi.org/10.1109/APPEEC.2010.5448861 doi: 10.1109/APPEEC.2010.5448861
    [49] Mingshan W, Jinli F, Chaochen M, et al. (2011) Waste heat recovery from heavy-duty diesel engine exhaust gases by medium temperature ORC system. Sci China Technol Sci 54: 2746–2753. https://doi.org/10.1007/s11431-011-4547-1 doi: 10.1007/s11431-011-4547-1
    [50] Amicabile S, Lee JI, Kum D (2015) A comprehensive design methodology of organic Rankine cycles for the waste heat recovery of automotive heavy-duty diesel engines. Appl Therm Eng 87: 574–585. https://doi.org/10.1016/j.applthermaleng.2015.04.034 doi: 10.1016/j.applthermaleng.2015.04.034
    [51] Kobayashi H, Yaji K, Yamasaki S, et al. (2021) Topology design of two-fluid heat exchange. Struct Multidiscip Optim 63: 821–834. https://doi.org/10.48550/arXiv.2005.08870 doi: 10.48550/arXiv.2005.08870
    [52] Li J, Zhou L, Pan K, et al. (1995) Evaluation of the thermodynamic process of indirect injection diesel engines by the first and second law. SAE Tech Pap: 09: 1–13. https://doi.org/10.4271/952055 doi: 10.4271/952055
    [53] Ghazikhani M, Feyz ME, Joharchi A (2010) Experimental investigation of the exhaust gas recirculation effects on irreversibility and brake specific fuel consumption of indirect injection diesel engines. Appl Therm Eng 30: 1711–1718. https://doi.org/10.1016/j.applthermaleng.2010.03.030 doi: 10.1016/j.applthermaleng.2010.03.030
    [54] Ozcan H (2010) Hydrogen enrichment effects on the second law analysis of a lean burn natural gas engine. Int J Hydrogen Energy 35: 1443–1452. https://doi.org/10.1016/j.ijhydene.2009.11.039 doi: 10.1016/j.ijhydene.2009.11.039
    [55] Rakopoulos CD, Kyritsis DC (2001) Comparative second-law analysis of internal combustion enginge operation for methane, methanol, and dodecane fuels. Energy 26: 705–722. https://doi.org/10.1016/S0360-5442(01)00027-5 doi: 10.1016/S0360-5442(01)00027-5
    [56] Saidur R, Rezaei M, Muzammil WK, et al. (2012) Technologies to recover exhaust heat from internal combustion engines. Renewable Sustainable Energy Rev 16: 5649–5659. https://doi.org/10.1016/j.rser.2012.05.018 doi: 10.1016/j.rser.2012.05.018
    [57] Duparchy A, Leduc P, Bourhis G, et al. (2009) Heat recovery for next generation of hybrid vehicles: Simulation and design of a Rankine cycle system. 24th Int Batter Hybrid Fuel Cell Electr Veh Symp Exhib 2009, EVS 24. 2: 1408–1424. https://doi.org/10.3390/wevj3030440 doi: 10.3390/wevj3030440
    [58] Conklin JC, Szybist JP (2010) A highly efficient six-stroke internal combustion engine cycle with water injection for in-cylinder exhaust heat recovery. Energy 35: 1658–1664. https://doi.org/10.1016/j.energy.2009.12.012 doi: 10.1016/j.energy.2009.12.012
    [59] Hosseini MJ, Ranjbar AA, Sedighi K, et al. (2012) A combined experimental and computational study on the melting behavior of a medium temperature phase change storage material inside shell and tube heat exchanger. Int Commun Heat Mass Transf 39: 1416–1424. https://doi.org/10.1016/j.icheatmasstransfer.2012.07.028 doi: 10.1016/j.icheatmasstransfer.2012.07.028
    [60] Jamshidi N, Farhadi M, Ganji DD, et al. (2013) Experimental analysis of heat transfer enhancement in shell and helical tube heat exchangers. Appl Therm Eng 51: 644–652. https://doi.org/10.1016/j.applthermaleng.2012.10.008 doi: 10.1016/j.applthermaleng.2012.10.008
    [61] Xu HJ, Xing ZB, Wang FQ, et al. (2019) Review on heat conduction, heat convection, thermal radiation and phase change heat transfer of nanofluids in porous media: Fundamentals and applications. Chem Eng Sci 195: 462–483. https://doi.org/10.1016/j.ces.2018.09.045 doi: 10.1016/j.ces.2018.09.045
    [62] Xu HJ, Gong L, Zhao CY, et al. (2015) Analytical considerations of local thermal non-equilibrium conditions for thermal transport in metal foams. Int J Therm Sci 95: 73–87. https://doi.org/10.1016/j.ijthermalsci.2015.04.007 doi: 10.1016/j.ijthermalsci.2015.04.007
    [63] Boomsma K, Poulikakos D (2011) Erratum: On the effective thermal conductivity of a three-dimensionally structured fluid-saturated metal foam. Int J Heat Mass Transf 54: 746–748. https://doi.org/10.1016/S0017-9310(00)00123-X doi: 10.1016/S0017-9310(00)00123-X
    [64] Brinkman HC (1952) The viscosity of concentrated suspensions and solutions. J Chem Phys 20: 571. https://doi.org/10.1063/1.1700493 doi: 10.1063/1.1700493
    [65] Buongiorno J (2006) Convective transport in nanofluids. J Heat Transfer 128: 240–250. https://doi.org/10.1115/1.2150834 doi: 10.1115/1.2150834
    [66] Calmidi VV, Mahajan RL (1999) The effective thermal conductivity of high porosity fibrous metal foams. J Heat Transfer 121: 466–471. https://doi.org/10.1115/1.2826001 doi: 10.1115/1.2826001
    [67] Das SK, Putra N, Thiesen P, et al. (2003) Temperature dependence of thermal conductivity enhancement for nanofluids. J Heat Transfer 125: 567–574. https://doi.org/10.1115/1.1571080 doi: 10.1115/1.1571080
    [68] Gao L, Zhou XF (2006) Differential effective medium theory for thermal conductivity in nanofluids. Phys Lett Sect A Gen At Solid State Phys 348: 355–360. https://doi.org/10.1016/j.physleta.2005.08.069 doi: 10.1016/j.physleta.2005.08.069
    [69] Manohara R, Harinath MA (2019) Application of Taguchi method for optimization of process parameters in drilling operation. Int J Trend Sci Res Dev 3: 1052–1057. https://doi.org/10.31142/ijtsrd24003 doi: 10.31142/ijtsrd24003
    [70] Alkidas AC, Battiston PA, Kapparos DJ (2004) Thermal studies in the exhaust system of a diesel-powered light-duty vehicle. SAE Tech Pap 1: 1–21. https://doi.org/10.4271/2004-01-0050 doi: 10.4271/2004-01-0050
    [71] Kishore RA, Kumar P, Priya S (2018) A comprehensive optimization study on Bi2Te3 -based thermoelectric generators using the Taguchi method. Sustainable Energy Fuels 2: 175–190. https://doi.org/10.1039/C7SE00437K doi: 10.1039/C7SE00437K
    [72] Kang CC, Yamauchi KA, Vlassakis J, et al. (2016) Single cell-resolution western blotting. Nat Protoc 11: 1508–1530. https://doi.org/10.1038/nprot.2016.089 doi: 10.1038/nprot.2016.089
    [73] Silaipillayarputhur K, Idem S (2013) A general matrix approach to model steady-state performance of crossflow heat exchangers. Heat Transf Eng 34: 338–348. https://doi.org/10.1080/01457632.2013.716347 doi: 10.1080/01457632.2013.716347
    [74] Silaipillayarputhur K, Al Mughanam T (2018) Performance charts for multi-pass parallel crossflow heat exchangers. Int J Mech Eng Robot Res 7: 478–482. https://doi.org/10.18178/ijmerr.7.5.478-482 doi: 10.18178/ijmerr.7.5.478-482
    [75] Romie FE (1983) Transient response of gas-to-gas crossflow heat exchangers with neither gas mixed. J Heat Transfer 105: 563–570. https://doi.org/10.1016/0017-9310(91)90249-E doi: 10.1016/0017-9310(91)90249-E
    [76] Gao T, Geer J, Sammakia B (2014) Nonuniform temperature boundary condition effects on data center cross flow heat exchanger dynamic performance. Int J Heat Mass Transf 79: 1048–1058. https://doi.org/10.1016/j.ijheatmasstransfer.2014.09.011 doi: 10.1016/j.ijheatmasstransfer.2014.09.011
    [77] Gao T, Sammakia BG, Geer FJ, et al. (2014) Dynamic analysis of cross flow heat exchangers in data centers using transient effectiveness method. IEEE Trans Components, Packag Manuf Technol 4: 1925–1935. https://doi.org/10.1109/TCPMT.2014.2369256 doi: 10.1109/TCPMT.2014.2369256
    [78] Yuan P (2003) Effect of inlet flow maldistribution on the thermal performance of a three-fluid crossflow heat exchanger. Int J Heat Mass Transf 46: 3777–3787. https://doi.org/10.1016/S0017-9310(03)00196-0 doi: 10.1016/S0017-9310(03)00196-0
    [79] Mishra M, Das PK, Sarangi S (2008) Effect of temperature and flow nonuniformity on transient behaviour of crossflow heat exchanger. Int J Heat Mass Transf 51: 2583–2592. https://doi.org/10.1016/j.ijheatmasstransfer.2007.07.054 doi: 10.1016/j.ijheatmasstransfer.2007.07.054
    [80] Guo D, Gao J, Yu YJ, et al. (2014) Design and modeling of a fluid-based micro-scale electrocaloric refrigeration system. Int J Heat Mass Transf 72: 559–564. https://doi.org/10.1016/j.ijheatmasstransfer.2014.01.043 doi: 10.1016/j.ijheatmasstransfer.2014.01.043
    [81] Jia Y, Sungtaek Ju Y (2012) A solid-state refrigerator based on the electrocaloric effect. Appl Phys Lett 100. https://doi.org/10.1063/1.4729038 doi: 10.1063/1.4729038
    [82] Ossmer H, Wendler F, Gueltig M, et al. (2016) Energy-efficient miniature-scale heat pumping based on shape memory alloys. Smart Mater Struct 25: 1–13. Avaiable from: https://iopscience.iop.org/article/10.1088/0964-1726/25/8/085037.
    [83] Park SIl (1996) Performance analysis of a moving-bed heat exchanger in vertical pipes. Energy 21: 911–918. https://doi.org/10.1016/0360-5442(96)00027-8 doi: 10.1016/0360-5442(96)00027-8
    [84] Rahimi A, Niksiar A (2013) A general model for moving-bed reactors with multiple chemical reactions part Ⅰ: Model formulation. Int J Miner Process 124: 58–66. https://doi.org/10.1016/j.minpro.2013.02.015 doi: 10.1016/j.minpro.2013.02.015
    [85] García-Triñanes P, Seville JPK, Ansart R, et al. (2018) Particle motion and heat transfer in an upward-flowing dense particle suspension: Application in solar receivers. Chem Eng Sci 177: 313–322. https://doi.org/10.1016/j.ces.2017.11.041 doi: 10.1016/j.ces.2017.11.041
    [86] Yusuf R, Melaaen MC, Mathiesen V (2005) Convective heat and mass transfer modeling in gas-fluidized beds. Chem Eng Technol 28: 13–24. https://doi.org/10.1002/ceat.200407014 doi: 10.1002/ceat.200407014
    [87] Zhang Y, Jiang C, Yang Z, et al. (2016) Numerical study on heat transfer enhancement in capsule-type plate heat exchangers. Appl Therm Eng 108: 1237–1242. https://doi.org/10.1016/j.applthermaleng.2016.08.033 doi: 10.1016/j.applthermaleng.2016.08.033
    [88] Song JW, Wang F, Cheng L (2012) Experimental study and analysis of a novel multi-media plate heat exchanger. Sci China Technol Sci 55: 2157–2162. https://doi.org/10.1007/s11431-012-4931-5 doi: 10.1007/s11431-012-4931-5
    [89] Villanueva HHS, de Mello PEB (2015) Heat transfer and pressure drop correlations for finned plate ceramic heat exchangers. Energy 88: 118–125. https://doi.org/10.1016/j.energy.2015.04.017 doi: 10.1016/j.energy.2015.04.017
    [90] Kim M, Baik YJ, Park SR, et al. (2010) Experimental study on corrugated crossflow air-cooled plate heat exchangers. Exp Therm Fluid Sci 34: 1265–1272. https://doi.org/10.1016/j.expthermflusci.2010.05.007 doi: 10.1016/j.expthermflusci.2010.05.007
    [91] Zhang L, Che D (2011) Influence of corrugation profile on the thermalhydraulic performance of cross-corrugated plates. Numer Heat Transf Part A Appl 59: 267–296. https://doi.org/10.1080/10407782.2011.540963 doi: 10.1080/10407782.2011.540963
    [92] Gulenoglu C, Akturk F, Aradag S, et al. (2014) Experimental comparison of performances of three different plates for gasketed plate heat exchangers. Int J Therm Sci 75: 249–256. https://doi.org/10.1016/j.ijthermalsci.2013.06.012 doi: 10.1016/j.ijthermalsci.2013.06.012
    [93] Yang J, Jacobi A, Liu W (2017) Heat transfer correlations for single-phase flow in plate heat exchangers based on experimental data. Appl Therm Eng 113: 1547–1557. https://doi.org/10.1016/j.applthermaleng.2016.10.147 doi: 10.1016/j.applthermaleng.2016.10.147
    [94] Durmuş A, Benli H, Kurtbaş I, et al. (2009) Investigation of heat transfer and pressure drop in plate heat exchangers having different surface profiles. Int J Heat Mass Transf 52: 1451–1457. https://doi.org/10.1016/j.ijheatmasstransfer.2008.07.052 doi: 10.1016/j.ijheatmasstransfer.2008.07.052
    [95] Seo JW, Kim YH, Kim D, et al. (2015) Heat transfer and pressure drop characteristics in straight microchannel of printed circuit heat exchangers. Entropy 17: 3438–3457. https://doi.org/10.3390/e17053438 doi: 10.3390/e17053438
    [96] Gao T, Sammakia BG, Geer J, et al. (2014) Dynamic analysis of cross flow heat exchangers in data centers using transient effectiveness Method. IEEE Trans Components, Packag Manuf Technol 4: 1925–1935. Avaiable from: https://ieeexplore.ieee.org/document/6963402.
    [97] Vintrou S, Bougeard D, Russeil S, et al. (2013) Quantitative infrared investigation of local heat transfer in a circular finned tube heat exchanger assembly. Int J Heat Fluid Flow 44: 197–207. https://doi.org/10.1016/j.ijheatfluidflow.2013.05.019 doi: 10.1016/j.ijheatfluidflow.2013.05.019
    [98] Monteiro DB, de Mello PEB (2012) Thermal performance and pressure drop in a ceramic heat exchanger evaluated using CFD simulations. Energy 45: 489–496. https://doi.org/10.1016/j.energy.2012.02.012 doi: 10.1016/j.energy.2012.02.012
    [99] Zhang C, Wang D, Han Y, et al. (2017) Experimental and numerical investigation on the exergy and entransy performance of a novel plate heat exchanger. Exp Heat Transf 30: 162–177. https://doi.org/10.1080/08916152.2016.1179358 doi: 10.1080/08916152.2016.1179358
    [100] Doo JH, Ha MY, Min JK, et al. (2012) An investigation of cross-corrugated heat exchanger primary surfaces for advanced intercooled-cycle aero engines (Part-Ⅰ: Novel geometry of primary surface). Int J Heat Mass Transf 55: 5256–5267. https://doi.org/10.1016/j.ijheatmasstransfer.2013.01.084 doi: 10.1016/j.ijheatmasstransfer.2013.01.084
    [101] Lee JM, Kwan PW, Son CM, et al. (2015) Characterizations of aerothermal performance of novel cross-corrugated plate heat exchangers for advanced cycle aero-engines. Int J Heat Mass Transf 85: 166–180. https://doi.org/10.1016/j.ijheatmasstransfer.2013.01.084 doi: 10.1016/j.ijheatmasstransfer.2013.01.084
    [102] Nilpueng K, Wongwises S (2015) Experimental study of single-phase heat transfer and pressure drop inside a plate heat exchanger with a rough surface. Exp Therm Fluid Sci 68: 268–275. https://doi.org/10.1016/j.expthermflusci.2015.04.009 doi: 10.1016/j.expthermflusci.2015.04.009
    [103] Kundu B (2015) Beneficial design of unbaffled shell-and-tube heat exchangers for attachment of longitudinal fins with trapezoidal profile. Case Stud Therm Eng 5: 104–112. https://doi.org/10.1016/j.csite.2015.03.001 doi: 10.1016/j.csite.2015.03.001
    [104] Parikshit B, Spandana KR, Krishna V, et al. (2015) A simple method to calculate shell side fluid pressure drop in a shell and tube heat exchanger. Int J Heat Mass Transf 84: 700–712. https://doi.org/10.1016/j.ijheatmasstransfer.2015.01.068 doi: 10.1016/j.ijheatmasstransfer.2015.01.068
    [105] Chang TB, Yu LY (2015) Optimal nozzle spray cone angle for triangular-pitch shell-and-tube interior spray evaporator. Int J Heat Mass Transf 85: 463–472. https://doi.org/10.1016/j.ijheatmasstransfer.2015.01.123 doi: 10.1016/j.ijheatmasstransfer.2015.01.123
    [106] Alimoradi A, Veysi F (2017) Optimal and critical values of geometrical parameters of shell and helically coiled tube heat exchangers. Case Stud Therm Eng 10: 73–78. https://doi.org/10.1016/j.csite.2017.03.003 doi: 10.1016/j.csite.2017.03.003
    [107] Raja BD, Jhala RL, Patel V (2017) Many-objective optimization of shell and tube heat exchanger. Therm Sci Eng Prog 2: 87–101. https://doi.org/10.1016/j.tsep.2017.05.003 doi: 10.1016/j.tsep.2017.05.003
    [108] Gao B, Bi Q, Nie Z, et al. (2015) Experimental study of effects of baffle helix angle on shell-side performance of shell-and-tube heat exchangers with discontinuous helical baffles. Exp Therm Fluid Sci 68: 48–57. https://doi.org/10.1016/j.expthermflusci.2015.04.011 doi: 10.1016/j.expthermflusci.2015.04.011
    [109] Salahuddin U, Bilal M, Ejaz H (2015) A review of the advancements made in helical baffles used in shell and tube heat exchangers. Int Commun Heat Mass Transf 67: 104–108. https://doi.org/10.1016/j.icheatmasstransfer.2015.07.005 doi: 10.1016/j.icheatmasstransfer.2015.07.005
    [110] Yang JF, Zeng M, Wang QW (2015) Numerical investigation on combined single shell-pass shell-and-tube heat exchanger with two-layer continuous helical baffles. Int J Heat Mass Transf 84: 103–113. https://doi.org/10.1016/j.ijheatmasstransfer.2014.12.042 doi: 10.1016/j.ijheatmasstransfer.2014.12.042
    [111] Zhou GY, Xiao J, Zhu L, et al. (2015) A Numerical Study on the Shell-Side Turbulent Heat Transfer Enhancement of Shell-and-Tube Heat Exchanger with Trefoil-Hole Baffles. Energy Procedia 75: 3174–3179. https://doi.org/10.1016/j.egypro.2015.07.656 doi: 10.1016/j.egypro.2015.07.656
    [112] Wen J, Yang H, Jian G, et al. (2016) Energy and cost optimization of shell and tube heat exchanger with helical baffles using Kriging metamodel based on MOGA. Int J Heat Mass Transf 98: 29–39. https://doi.org/10.1016/j.ijheatmasstransfer.2016.02.084 doi: 10.1016/j.ijheatmasstransfer.2016.02.084
    [113] Du BC, He YL, Wang K, et al. (2017) Convective heat transfer of molten salt in the shell-and-tube heat exchanger with segmental baffles. Int J Heat Mass Transf 113: 456–465. https://doi.org/10.1016/j.ijheatmasstransfer.2017.05.075 doi: 10.1016/j.ijheatmasstransfer.2017.05.075
    [114] Wen J, Yang H, Wang S, et al. (2017) PIV experimental investigation on shell-side flow patterns of shell and tube heat exchanger with different helical baffles. Int J Heat Mass Transf 104: 247–259. https://doi.org/10.1016/j.ijheatmasstransfer.2016.08.048 doi: 10.1016/j.ijheatmasstransfer.2016.08.048
    [115] Crane D, Lagrandeur J, Jovovic V, et al. (2013) TEG on-vehicle performance and model validation and what it means for further teg development. J Electron Mater 42: 1582–1591. https://doi.org/10.1007/s11664-012-2327-8 doi: 10.1007/s11664-012-2327-8
    [116] Mori M, Yamagami T, Sorazawa M, et al. (2011) Simulation of fuel economy effectiveness of exhaust heat recovery system using thermoelectric generator in a series hybrid. SAE Int J Mater Manuf 4: 1268–1276. https://doi.org/10.4271/2011-01-1335 doi: 10.4271/2011-01-1335
    [117] Hussain QE, Brigham DR, Maranville CW (2009) Thermoelectric exhaust heat recovery for hybrid vehicles. SAE Tech Pap 2: 1132–1142. https://doi.org/10.4271/2009-01-1327 doi: 10.4271/2009-01-1327
    [118] Espinosa N, Lazard M, Aixala L, et al. (2010) Modeling a thermoelectric generator applied to diesel automotive heat recovery. J Electron Mater 39: 1446–1455. https://doi.org/10.1007/s11664-010-1305-2 doi: 10.1007/s11664-010-1305-2
    [119] Gonçalves VM, Maia CA, Hardouin L (2012) On the solution of Max-plus linear equations with application on the control of TEGs. IFAC Proc 45: 91–97. https://doi.org/10.3182/20121003-3-MX-4033.00018 doi: 10.3182/20121003-3-MX-4033.00018
    [120] Brito FP, Goncalves LM, Martins J, et al. (2013) Influence of heat pipe operating temperature on exhaust heat thermoelectric generation. SAE Int J Passeng Cars-Mech Syst 6: 652–664. https://doi.org/10.4271/2013-01-0559 doi: 10.4271/2013-01-0559
    [121] Martins J, Goncalves LM, Antunes J, et al. (2011) Thermoelectric exhaust energy recovery with temperature control through heat pipes. SAE 2011 World Congr Exhib 1: 1–16. Avaiable from: https://core.ac.uk/download/pdf/55616825.pdf.
    [122] Jang JC, Chi RG, Rhi SH, et al. (2015) Heat pipe-assisted thermoelectric power generation technology for waste heat recovery. J Electron Mater 44: 2039–2047. https://doi.org/10.1007/s11664-015-3653-4 doi: 10.1007/s11664-015-3653-4
    [123] Lan S, Yang Z, Chen R, et al. (2018) A dynamic model for thermoelectric generator applied to vehicle waste heat recovery. Appl Energy 210: 327–338. https://doi.org/10.1016/j.apenergy.2017.11.004 doi: 10.1016/j.apenergy.2017.11.004
    [124] Tang ZB, Deng YD, Su CQ, et al. (2015) A research on thermoelectric generator's electrical performance under temperature mismatch conditions for automotive waste heat recovery system. Case Stud Therm Eng 5: 143–150. https://doi.org/10.1016/j.csite.2015.03.006 doi: 10.1016/j.csite.2015.03.006
    [125] Orr B, Akbarzadeh A (2017) Prospects of waste heat recovery and power generation using thermoelectric generators. Energy Procedia 110: 250–255. https://doi.org/10.1016/j.egypro.2017.03.135 doi: 10.1016/j.egypro.2017.03.135
    [126] He W, Wang S, Yue L (2017) High net power output analysis with changes in exhaust temperature in a thermoelectric generator system. Appl Energy 196: 259–267. https://doi.org/10.1016/j.apenergy.2016.12.078 doi: 10.1016/j.apenergy.2016.12.078
    [127] Fankai M, Lingen Ch, Sun FR (2012) Effects of temperature dependence of thermoelectric properties on the power and efficiency of a multielement thermoelectric generator. Int J Energy Environ Eng 3: 137–150. Available from: https://www.ijee.ieefoundation.org/vol3/issue1/IJEE_14_v3n1.pdf.
    [128] Gou X, Yang S, Xiao H, et al. (2013) A dynamic model for thermoelectric generator applied in waste heat recovery. Energy 52: 201–209. https://doi.org/10.1016/j.apenergy.2017.11.004 doi: 10.1016/j.apenergy.2017.11.004
    [129] Meng JH, Zhang XX, Wang XD (2014) Dynamic response characteristics of thermoelectric generator predicted by a three-dimensional heat-electricity coupled model. J Power Sources 245: 262–269. https://doi.org/10.1016/j.jpowsour.2013.06.127 doi: 10.1016/j.jpowsour.2013.06.127
    [130] Hsu CT, Huang GY, Chu HS, et al. (2011) An effective Seebeck coefficient obtained by experimental results of a thermoelectric generator module. Appl Energy 88: 5173–5179. https://doi.org/10.1016/j.apenergy.2011.07.033 doi: 10.1016/j.apenergy.2011.07.033
  • This article has been cited by:

    1. Arindam Mandal, Pankaj Kumar Tiwari, Samares Pal, Impact of awareness on environmental toxins affecting plankton dynamics: a mathematical implication, 2020, 1598-5865, 10.1007/s12190-020-01441-5
    2. Arindam Mandal, Saswati Biswas, Samares Pal, Toxicity-mediated regime shifts in a contaminated nutrient–plankton system, 2023, 33, 1054-1500, 023106, 10.1063/5.0122206
    3. Saswati Biswas, Pankaj Kumar Tiwari, Samares Pal, Effects of toxicity and zooplankton selectivity on plankton dynamics under seasonal patterns of viruses with time delay, 2022, 45, 0170-4214, 585, 10.1002/mma.7799
    4. Vladimir G. Dvoretsky, Marina P. Venger, Anastasya V. Vashchenko, Tatyana M. Maksimovskaya, Tatyana G. Ishkulova, Veronika V. Vodopianova, Pelagic Bacteria and Viruses in a High Arctic Region: Environmental Control in the Autumn Period, 2022, 11, 2079-7737, 845, 10.3390/biology11060845
    5. Sourav Kumar Sasmal, Yasuhiro Takeuchi, Editorial: Mathematical Modeling to Solve the Problems in Life Sciences, 2020, 17, 1551-0018, 2967, 10.3934/mbe.2020167
    6. Xiaomei Feng, Yuan Miao, Shulin Sun, Lei Wang, Dynamic Behaviors of a Stochastic Eco-Epidemiological Model for Viral Infection in the Toxin-Producing Phytoplankton and Zooplankton System, 2022, 10, 2227-7390, 1218, 10.3390/math10081218
    7. SASANKA SHEKHAR MAITY, PANKAJ KUMAR TIWARI, SAMARES PAL, AN ECOEPIDEMIC SEASONALLY FORCED MODEL FOR THE COMBINED EFFECTS OF FEAR, ADDITIONAL FOODS AND SELECTIVE PREDATION, 2022, 30, 0218-3390, 285, 10.1142/S0218339022500103
    8. Vikas Kumar, Bulti Pramanick, Impact of nanoparticles on the dynamics of a Crowley–Martin type phytoplankton–zooplankton interaction model, 2022, 8, 26667207, 100139, 10.1016/j.rico.2022.100139
    9. Subarna Roy, Pankaj Kumar Tiwari, Himadri Nayak, Maia Martcheva, Effects of fear, refuge and hunting cooperation in a seasonally forced eco-epidemic model with selective predation, 2022, 137, 2190-5444, 10.1140/epjp/s13360-022-02751-2
    10. SASANKA SHEKHAR MAITY, PANKAJ KUMAR TIWARI, ZHISHENG SHUAI, SAMARES PAL, ROLE OF SPACE IN AN ECO-EPIDEMIC PREDATOR-PREY SYSTEM WITH THE EFFECT OF FEAR AND SELECTIVE PREDATION, 2023, 31, 0218-3390, 883, 10.1142/S0218339023500316
    11. Sasanka Shekhar Maity, Pankaj Kumar Tiwari, Samares Pal, Comprehensive Analysis of Deterministic and Stochastic Eco-Epidemic Models Incorporating Fear, Refuge, Supplementary Resources, and Selective Predation Effects, 2024, 191, 0167-8019, 10.1007/s10440-024-00654-1
    12. Saswati Biswas, Arindam Mandal, Samares Pal, Catastrophic and noncatastrophic population crashes in a bitrophic system with dynamic additional food provision to cooperative predators, 2024, 109, 2470-0045, 10.1103/PhysRevE.109.024224
    13. Sasanka Shekhar Maity, Pankaj Kumar Tiwari, Nanda Das, Samares Pal, 2023, Chapter 12, 978-3-031-33049-0, 197, 10.1007/978-3-031-33050-6_12
    14. Arindam Mandal, Nazmul Sk, Saswati Biswas, Nutrient enrichment and phytoplankton toxicity influence a diversity of complex dynamics in a fear-induced plankton-fish model, 2024, 578, 00225193, 111698, 10.1016/j.jtbi.2023.111698
    15. Tiancai Liao, Stochastic dynamics of a plankton model with zooplankton selectivity and nutritional value of phytoplankton, 2024, 70, 1598-5865, 251, 10.1007/s12190-023-01959-4
    16. Arindam Mandal, Saswati Biswas, Pankaj Kumar Tiwari, Samares Pal, Seasonal refuge patterns of phytoplankton trigger irregular bloom events in a contaminated environment, 2024, 14, 2045-2322, 10.1038/s41598-024-66578-w
    17. Conghui Zhang, Jin Lu, Maoxing Liu, Hanzhi Zhang, Stable patterns with jump-discontinuity for a phytoplankton–zooplankton system with both Allee and fear effect, 2025, 472, 01672789, 134481, 10.1016/j.physd.2024.134481
    18. Soumita Sen, Suddhyashil Sarkar, Samares Pal, Comparative studies on a zooplankton-fish model subjected to infection in zooplankton with varying rates of disease transmission, 2024, 27731863, 100194, 10.1016/j.fraope.2024.100194
    19. Ravikant Singh, Archana Ojha, Pankaj Kumar Tiwari, Nilesh Kumar Thakur, Yun Kang, Impact of time delay in a plankton–fish system with nonlinear harvesting and external toxicity, 2025, 18, 1793-5245, 10.1142/S1793524523500961
    20. Nada A. Almuallem, Miled El Hajji, How Can Viruses Affect the Growth of Zooplankton on Phytoplankton in a Chemostat?, 2025, 13, 2227-7390, 1192, 10.3390/math13071192
  • Reader Comments
  • © 2022 the Author(s), licensee AIMS Press. This is an open access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/4.0)
通讯作者: 陈斌, bchen63@163.com
  • 1. 

    沈阳化工大学材料科学与工程学院 沈阳 110142

  1. 本站搜索
  2. 百度学术搜索
  3. 万方数据库搜索
  4. CNKI搜索

Metrics

Article views(4318) PDF downloads(292) Cited by(3)

Figures and Tables

Figures(2)

Other Articles By Authors

/

DownLoad:  Full-Size Img  PowerPoint
Return
Return

Catalog