J. Nig. Soc. Phys. Sci. 5 (2023) 1137 Journal of the Nigerian Society of Physical Sciences Electrohydrodynamics Convection in Dielectric Rotating Oldroydian Nanofluid in Porous Medium Pushap Lata Sharmaa, Mohini Kapaltaa, Ashok Kumara, Deepak Bainsa, Sumit Guptab, Pankaj Thakurc, aDepartment of Mathematics & Statistics, Himachal Pradesh University, Summer Hill, Shimla, India bRajiv Gandhi Govt college Chaura Maidan, Shimla, India cFaculty of Science and Technology, ICFAI University, Baddi, Solan, India Abstract An electrically conducting nanofluid saturated with a uniform porous medium has been tested to determine how rotation affects thermal convection. Utilizing the Oldroydian model, which incorporates the specific effects of the electric field, Brownian motion, thermophoresis and rheological factors for the distribution of nanoparticles that are top-heavy and bottom-heavy, one may use linear stability theory to ensure stability. Analysis and graphical representation of the effects of the AC electric field Rayleigh number, Taylor number, Lewis number, modified diffusivity ratio, concentration Rayleigh number and medium porosity are provided for both bottom-heavy and top-heavy distribution. DOI:10.46481/jnsps.2023.1231 Keywords: Convection, dielectric, electric field, nanofluid, Oldroydian, porous medium, rotation Article History : Received: 24 November 2022 Received in revised form: 18 January 2023 Accepted for publication: 28 January 2023 Published: 02 March 2023 c© 2023 The Author(s). Published by the Nigerian Society of Physical Sciences under the terms of the Creative Commons Attribution 4.0 International license (https://creativecommons.org/licenses/by/4.0). Further distribution of this work must maintain attribution to the author(s) and the published article’s title, journal citation, and DOI. Communicated by: B. J. Falaye 1. Introduction Nanofluids are fluids that include particles with a diame- ter of less than 100 nm and can stay suspended in them. Choi [1] was the first to coin the term. Nanofluid is a suspension of normal nano-size particles such as metals (Al, Cu), oxides ceramics (Al2O3, CuO), metal carbides (S iC), nitrides and car- bon nanotubes in an aqueous or non-aqueous dispersion me- dia. Because of their unique chemical and physical features, nanofluids are now considered the next-generation heat trans- fer fluid. Nanofluids can be used for a variety of things, in- cluding nanocomposites, electrical cooling, bio-medicine and Email address: pankaj_thakur15@yahoo.co.in (Pankaj Thakur ) nanostructure production transportation because of their capa- bilities. Many researchers have investigated the properties of nanofluids as well as potential application scenarios. Nanoflu- ids are perfect for heat transfer applications since they have better thermal conductivity. Because of their superior thermal conductivity, nanofluids are perfect for transferring heat. The effects of particle size, pH and zeta potential on the thermal conductivity of nanofluids have been the subject of several in- vestigations. In nanofluids with a low concentration of metal oxides, the addition of 4 to 5 percent metal oxides by volume results in an increase in thermal conductivity of between 10 and 20 percent. Several models have been used to estimate the ther- mal conductivity of nanofluids. 1 Sharma et al. / J. Nig. Soc. Phys. Sci. 5 (2023) 1137 2 The first, which relates to the thermal conductivity of par- ticles and fluids was created by Maxwell to ascertain the ther- mal conductivity of colloidal suspension which is analyzed by Nield and Kuznetsov [2]. Sheu [3] has studied the thermal in- stability in a porous medium layer saturated with a viscoelastic nanofluid and demonstrated that oscillatory instability is possi- ble in both bottom-heavy and top-heavy nanoparticle distribu- tions. The results indicate a conflict between the thermophore- sis, Brownian diffusion and viscoelasticity processes, leading to oscillatory rather than stationary modes of convection. Sharma et al. [4] have investigated the onset of thermal convection in an Oldroydian nanofluid layer saturating a porous medium using a Darcy-Brinkman model revolving vertically with a uniform an- gular velocity. Yu and Choi [5] changed the Maxwell model by considering the influence of nanolayers on the electromagnetic field. Another appealing strategy for heat transfer development in industrial systems is the use of porous media in nanofluids. Porous media are normally saturated, hard-open cells that are often filled with fluid to allow fluid to pass through the voids. Porous media improve heat conductivity by increas- ing the contact area between liquid, solid and nanofluid, hence boosting the efficiency of conventional thermal systems. Due to its use in many practical applications such as chemical re- actors, heat exchangers and fluid filters, the increase in ther- mal conductivity of nanofluid with the use of porous media has attracted many researchers for the use of materials with high porosity in the current era for many technological problems. Natural convection in an AC/DC electric field was studied by Jones [6] and Chen et al. [7] for electrically accelerated heat movement in fluids and its applications. Convective heat trans- fer through polarized dielectric liquids was studied by Stiles et al. [8]. They found that the convection pattern identified by the electric field is similar to that of the well-known Bénard cell convection. In their study of the effects of electro-thermal convection on dielectric rotating fluid, Shivakumara et al. [9] discovered that an AC electric field accelerates convection ini- tiation and boosts heat transfer. The dielectric nanofluid may be used for instrument transformers, regulating and converter transformers and other electrical devices. Sharma et al. [10] have researched of heat convection in a dielectric rheological nanofluid layer employed an AC electric field. A Maxwellian model was used to explain the rheology of the nanofluid and it was shown that for bottom-heavy nanopar- ticle distributions, the electric field and the stress relaxation parameter destabilize both stationary and oscillatory modes. Sharma et al. [11] investigation into thermosolutal convection of an elastic-viscous nanofluid in a porous medium with ro- tation and magnetic field led them to the conclusion that sta- tionary convection is stabilized by the magnetic field and the Taylor number, while stationary convection is destabilized by the solutal Rayleigh number, nanoparticle Rayleigh number, thermo-nanofluid Lewis number and modified diffusivity ratio The Rivlin-Ericksen fluid issue in a Darcy-Brinkman porous medium was studied by Sharma et al. [12]. Thermosolutal convection in a porous medium and its rela- tionship to the rotation was examined by Sharma et al. [13]. Kumar et al. [14] researched thermosolutal convection in Jef- frey nanofluid with porous medium and Sharma et al. [15] studied electrohydrodynamics convection in dielectric Oldroy- dian nanofluid layer in porous media. For free-free, rigid-free and rigid-rigid boundaries, Poonam et al. [16] looked into the electrohydrodynamic convection in thermal instability of Jef- frey nanofluid in porous media. Shivakumara et al. [17] in- vestigated on the problem Darcy-Brinkman model of electrical convection in a porous dielectric fluid. Chand et al. [18] exam- ined the convection of an electric field saturated by nanofluid in a porous medium. Ramanuja et al. [19] researched MHD SWCNT-blood nanofluid flow through porous medium in the presence of viscous dissipation and radiation effects. Akinpelu et al. [20] studied hydromagnetic double exothermic chemical reactive flow with convective cooling through a porous medium using bimolecular kinetics. This concise survey of the literature shows that research has been done on the current issue, the ini- tiation of thermal convection. 2. Mathematical formulation of problem An infinitely extending electrically conducting horizon- tal layer of an incompressible rotating non-Newtonian Ol- droydian nanofluid of thickness d is taken under gravity g (0, 0, −g) . The rotating vertical angular velocity is Ω(0, 0, Ω) . The temperatures T and volumetric fractions of nanoparticles φ are taken to be T0 and φ0 at z = 0 and T1 and φ1 at z = d (T0 > T1 and φ1 > φ0). This dielectric nanofluid layer is domi- nated by a uniform vertical electric field. Figure 1: Physical Configuration 3. Governing equations The conservation equations for mass and momentum using Boussinesq approximation are ∇.q D = 0, (1) ρ f ε ( 1 + λ ∂ ∂t ) [ ∂ ∂t + 1 ε q D.∇ ] q D = [−∇p + ( φρp + (1 −φ) ρ f {1 −β (T − T1)} ) g + fe + 2ρ ε (Ω× q D)] ( 1 + λ ∂ ∂t ) − µ k1 ( 1 + λ0 ∂ ∂t ) q D , (2) where q D, p,ε,λ,λ0,φ,ρ f ,ρp,β,µ and k1 are the Darcy ve- locity, pressure, porosity, relaxation time, retardation time, 2 Sharma et al. / J. Nig. Soc. Phys. Sci. 5 (2023) 1137 3 nanoparticles volume fraction, the density of the base fluid, the density of nanoparticles, coefficient of volume expansion, coef- ficient of viscosity and medium permeability respectively. fe is the electrical force given by fe = ρe E − 1 2 E2∇K + 1 2 ( ρ ∂K ∂t E2 ) , where ρe is the density of charge, K is the dielectric constant, E is the electric field. The term ρe E is due to the free charge known as Coulomb force. Here, the term ρe E is neglected as compared to the term −12 E 2∇K for most dielectric fluids. The modified pressure term is P = p − 1 2 ( ρ ∂K ∂t E2 ) , (3) where p is the hydrodynamical pressure. Maxwell Equations are ∇. (K E) = 0,∇× E = 0. (4) From equation (4), E can be shown as E = −∇ϕ, (5) where ϕ is a measure of electric potential’s root mean square. It is also assumed that K = K0 [ 1 −γ (T − T1) ] . (6) γ > 0, where, 0 < γ∆T << 1. Thus, the modified equations of motion for rotating Oldroydian nanofluid saturating a porous medium in the presence of an electric field become ρ f ε ( 1 + λ ∂ ∂t ) [ ∂ ∂t + 1 ε q D.∇ ] q D = ( 1 + λ ∂ ∂t ) [−∇p + ( φρp + (1 −φ) ρ f {1 −β (T − T1)} ) g − 1 2 (E.E)∇K + 2ρ ε (Ω× q D)] − µ k1 ( 1 + λ0 ∂ ∂t ) q D . (7) The nanoparticles’ equation of continuity is[ ∂ ∂t + 1 ε (q D.∇) ] φ = DB∇ 2φ + ( DT T1 ) ∇ 2T. (8) A porous medium’s saturating nanofluid’s heat-energy equation is (ρc)m ∂T ∂t + (ρc) f q D.∇T = km∇ 2T + ε(ρc)p [ DB∇φ.∇T + ( DT T1 ) ∇T.∇T ] . (9) The boundary conditions appropriate to the problem are w = 0, ∂ϕ ∂z = 0, T = T0, φ = φ0 at z = 0 w = 0, ∂ϕ ∂z = 0, T = T1, φ = φ1 at z = d } . (10) Using the non-dimensional variables (x∗, y∗, z∗) = (x,y,z)d , t ∗ = t αm σ d2 , q ∗ D = q D d αm , p∗ = pk1 µαm ,φ∗ = φ−φ0 φ1−φ0 ,ϕ∗ = ϕ γE0 ∆T d , T∗ = T−T1T0 −T1 , E ∗ = E γE0 ∆T d , K∗ = KK0 , where σ = (ρc)m(ρc) f and αm = km (ρc) f . The non-dimensional forms of equations (1) and (5) - (9) are (asterisk is removed for convenience): ∇.q D = 0, (11) 1 Va ( 1 + λ1 ∂ ∂t ) [ 1 σ ∂ ∂t + 1 ε q D.∇ ] q D = ( 1 + λ1 ∂ ∂t ) [−∇p − Rnφêz − Rmêz + RaT êz + ReT êz −Re ∂ϕ ∂z + √ Ta(vêx − uêy)] − ( 1 + λ2 ∂ ∂t ) q D , (12) 1 σ ∂φ ∂t + 1 ε q D.∇φ = 1 Le ∇ 2φ + NA Le ∇ 2T, (13) ∂T ∂t + q D.∇T = ∇2T + NB Le ∇φ.∇T + NA NB Le ∇T.∇T, (14) E = −∇ϕ, (15) K = [ 1 −γT (T0 − T1) ] , (16) where the non-dimensional parameters are λ1 = λαm σd2 is the Deborah number, λ2 = λ0αm σd2 is the Strain-Retardation time pa- rameter, Pr = µ ρ f αm is the Prandtl number, Dr = k1 d2 is the Darcy number, Va = εPr Dr is the Vadasz number, Le = αm DB is the Lewis number, Ra = ρ f gβdk1 ( T 0−T1 ) µαm is the thermal Darcy- Rayleigh number, Rm = [φ0ρp +(1−φ0 )ρ f ]gdk1 µαm is the basic density Rayleigh number, Rn = (ρp−ρ f )(φ1−φ0 )gdk1 µαm is the concentration Rayleigh number, NA = DT ( T 0−T1 ) DB T 1 (φ1−φ0 ) is the modified diffusivity ratio, NB = ε(ρc)p (φ1−φ0 ) (ρc) f is the modified particle-density incre- ment, √ Ta = 2Ωρk1 εµ is Taylor number and Re = Kγ2 E20 (T0−T1 ) 2 k1 d2 µαm is the AC electric Rayleigh number. In terms of non-dimensional form, boundary conditions (10) transform to w = 0, ∂ϕ ∂z = 0, T = 1, φ = 0 at z = 0 w = 0, ∂ϕ ∂z = 0, T = 0, φ = 1 at z = 1 } . (17) 4. Basic state solution The basic state is stated as{ q D = (u, v, w) = (0, 0, 0) , p = pb (z) , T = Tb (z) , φ = φb (z) , K = Kb (z) , E = Eb (z) , ϕ = ϕb (z) . (18) When there is no motion, equations (13) and (14) require the temperature and the volumetric fraction of nanoparticles to sat- isfy the equations d2φb dz2 + NA d2Tb dz2 = 0, (19) d2Tb dz2 + NB Le dφb dz dTb dz + NA NB Le dTb dz dTb dz = 0. (20) Using the boundary conditions (17), equation (19) can be inte- grated to give φb (z) = −NATb + (1 − NA) z + NA. (21) 3 Sharma et al. / J. Nig. Soc. Phys. Sci. 5 (2023) 1137 4 Substituting φb from equation (21) into equation (20), we get d2Tb dz2 + (1 − N A)NB Le dTb dz = 0. (22) Equation (22) along with the boundary condition (14) gives the solution as Tb = e −(1− N A )NB z/Le ( 1 − e−(1−NA )NB (1−z)/Le 1 − e−(1−NA )NB/Le ) . (23) The terms of second and higher order in the expansion of an exponential function in equation (23) are neglected as they are small and so one gets the best approximate initial stationary state solutions as{ Tb = 1 − z, φb = z, Kb = 1 + γ∆T z, Eb = E0 γ∆T (1+γ∆T z) , ϕb = − E0 (γ∆T )2 log (1 + γ∆T ) , (24) where, E0 = −γ∆Tϕ log(1+γ∆T ) at z = 0. 5. The formulae for perturbations By adding minute disturbances to the state variables, we can gently perturb the initial condition indicated by equation (24) so that q D = (0, 0, 0) + q ′ D (u ′, v′, w′) , T = Tb + T ′, φ = φb + φ ′, p = pb + p′, K = Kb + K′, E = Eb + E′,ϕ = ϕb + ϕ′. (25) Using these perturbations given by equation (25) and neglecting the terms of higher powers and products of perturbations (i.e., applying linear stability theory) in equations (11) - (16), the resulting linearized non-dimensional perturbed equations are: (( 1 + λ2 ∂ ∂t ) + 1 σVa ( 1 + λ1 ∂ ∂t ) ∂ ∂t )2 ∇ 2 + Ta ( 1 + λ1 ∂ ∂t )2 ∂2 ∂z2 w′ = [( 1 + λ2 ∂ ∂t ) + 1 σVa ( 1 + λ1 ∂ ∂t ) ∂ ∂t ] ( 1 + λ1 ∂ ∂t )[ −Rn∇2Hφ ′ + (Ra + Re)∇2H T ′ − Re∇2H ∂ϕ′ ∂z ] , (26) 1 σ ∂φ′ ∂t + w′ ε = 1 Le ∇ 2φ′ + NA Le ∇ 2T′, (27) (28) ∂T′ ∂z −∇ 2ϕ′ = 0. (29) The boundary conditions (17) for the infinitesimal perturba- tions become w′ = 0, ∂ 2 w′ ∂z2 = 0, ∂ϕ ′ ∂z = 0, T ′ = 1, φ′ = 0 at z = 0 w′ = 0, ∂ 2 w′ ∂z2 = 0, ∂ϕ ′ ∂z = 0, T ′ = 0, φ′ = 1 at z = 1 . (30) 6. The normal mode analysis For the system of equations (26) - (29), the analysis can be made in terms of two-dimensional periodic waves of assigned wave numbers. Thus, we assign the quantities describing the dependence on x, y, t of the form exp ( ikx x + iky x + st ) , where kx and ky are the wave numbers in x-direction and y- direction, respectively and a2 = k2x + k 2 x is the resultant wave number, s is the growth rate, which is a complex constant. The above consideration allows us to suppose (w′, T′,φ′,ϕ′) = (W, Θ, Φ, Ψ ) exp ( ikx x + ikyy + st ) . (31) Using expression (31), the equations (26) - (29), reduces to ( (1 + λ2 s) + 1 σVa (1 + λ1 s) s )2 ( D2 − a2 ) + Ta(1 + λ1 s) 2 D2 W = ( (1 + λ2 s) + 1 σVa (1 + λ1 s) s ) (1 + λ1 s)( a2RnΦ − a2 (Ra + Re) Θ + a2Re DΨ ) , (32) s σ Φ + W ε = 1 Le ( D2 − a2 ) Φ + NA Le ( D2 − a2 ) Θ, (33) sΘ − W = ( D2 − a2 ) Θ + NB Le (DΘ − DΦ) − 2NA NB Le DΘ, (34) DΘ − ( D2 − a2 ) Ψ = 0, (35) where a = √ k2x + k2y. The equations (30) for a free-free boundary are: W = D2W = Θ = Φ = DΨ = 0 at z = 0 and z = 1. (36) Therefore{ W = A1sinπz, Θ = A2sinπz, Φ = A3sinπz, Ψ = A4cosπz, (37) where A1, A2, A3 and A4 are the constants. Substituting (37) in equations (32) - (35) and using the boundary conditions (36), we get A B C D 1 −J − s 0 0 1 ε NA J Le J Le + s σ 0 0 −π 0 −J A1 A2 A3 A4 = 0 0 0 0 , (38) where A = M2 J + π2Ta(1 + λ1 s)2, B = −a2 (1 + λ1 s) M(Ra + Re), C = a2(1 + λ1 s) MRn, D = −a2π(1 + λ1 s) MRe, J = ( π2 + a2 ) , and M = ( (1 + λ2 s) + 1 σVa (1 + λ1 s) s ) . where, the thermal Darcy-Rayleigh number, Ra = − a2 π2 +a2 Re − σLe σ(π2 +a2)+sLe [ π2 +a2 +s ε + (π2 +a2)NA Le ] Rn + π2 +a2 +s a2 [ π 2 +a2 1+λ1 s ( (1 + λ2 s) + 1 σVa (1 + λ1 s) s ) + σVaπ2 σVa (1+λ2 s)+(1+λ1 s)s (1 + λ1 s) Ta] . (39) 4 Sharma et al. / J. Nig. Soc. Phys. Sci. 5 (2023) 1137 5 7. Stationary Convection For the validity of the principle of exchange of stabilities (i.e., steady case), we have s = 0 ( s = r + iω = 0 ⇒ r = ω = 0 ) at the marginal stability. Putting s = 0 in equation (39), we get the thermal Darcy- Rayleigh number at which marginally stable steady mode ex- ists, as Ra = (π2 +a2)2 a2 − a2 π2 +a2 Re − ( Le ε + NA ) Rn + π2(π2 +a2) a2 Ta , (40) which expresses the stationary thermal Darcy-Rayleigh number Ra as a function of the dimensionless wave number a, electric Rayleigh number Re, Taylor number Ta, nanofluid Lewis num- ber Le, modified diffusivity ratio NA, concentration Rayleigh number Rn and medium porosity ε. It is clear from the equation (40) that Ra is independent of stress relaxation time λ1, strain retardation time λ1 for stationary modes since these vanish with the vanishing of s (growth rate). The minimum value of Ra is obtained by putting ∂Ra ∂a2 = 0 and which on simplification implies that{ (ac) 8 + 2π2(ac) 6 − ( π2Re + π2Ta ) (ac) 4 −2π2 (1 + Ta) (ac) 2 −π2 (1 + Ta) } = 0. (41) Therefore, the critical wave number ac shows a substantial increase when the electric Rayleigh number Re increases and is independent of nanoparticles. To obtain the critical wave number we substitute the electric field i.e., Re = 0 and we get ac 2 = π2 √ 1 + Ta, (42) which is the critical wave number for stationary Rayleigh num- ber in the absence of AC electric Rayleigh number Re. 8. Results and discussion To study Re, Ta, Le, NA, Rn,ε on the stationary convection, we examine the behavior ∂Ra ∂Re , ∂Ra ∂Ta , ∂Ra ∂Le , ∂Ra ∂NA , ∂Ra ∂Rn and ∂Ra ∂ε analyt- ically. From equation (40) we obtain ∂Ra ∂Re = − a2( π2 + a2 ), (43) which is always negative for all wave numbers. Thus, AC elec- tric field has destabilizing effect for both bottom-heavy and top- heavy distribution. Equation (40) gives ∂Ra ∂Ta = π2 ( π2 + a2 ) a2 , (44) which is always positive for all wave numbers. Thus, the Taylor number has stabilizing effect for both bottom-heavy and top- heavy distribution in the system. Equation (40) further yields ∂Ra ∂Le = − Rn ε , ∂Ra ∂NA = −Rn. (45) It is clear from equation (45), the nanofluid Lewis number Le and the modified diffusivity ratio NA enhance the stationary convection if Rn < 0 and postpone the stationary convection if Rn > 0. Equation (40) also depicts that ∂Ra ∂Rn = − ( Le ε + NA ) , (46) which is always negative for ( Le ε + NA ) > 0. The nanoparticle Rayleigh number postpones the stationary convection for both bottom-heavy and top-heavy configurations. ∂Ra ∂ε = LeRn ε2 . (47) If Rn < 0, thus the medium porosity delays the stationary convection for bottom-heavy configuration and if Rn > 0 the medium porosity advances the stationary convection. 9. Numerical discussion The variation of thermal Darcy-Rayleigh number with re- spect to wave number has been plotted using equation (40) for stationary case, whereas the experimental values and the fixed permissible values of the dimensionless parameters are Re = 100, Ta = 100, Le = 200, NA = −5 and NA = 5, Rn = −0.1 and Rn = 0.1 and ε = 0.6 . The stationary ther- mal Rayleigh number does not depend upon stress relaxation time and strain retardation time, since it vanishes with the van- ishing of s (growth rate). Thus, the Oldroydian nanofluid acts like a Newtonian nanofluid. Figures 2 and 3 show the variation of Ra for stationary con- vection with respect to the non-dimensional wave number for three different values of Re = 100, 300, 500 for bottom-heavy and top-heavy distribution and fixed permissible values. The graph indicates that the value of Ra drops as Re rises, indicating that Re has a destabilizing influence on both bottom-heavy and top-heavy configurations. Figure 2: Variations of Ra for distinct values of the Re for bottom-heavy distribution Figures 4 and 5 show that Ra increases with an increase in Ta which implies that Ta has a stabilizing effect on stationary 5 Sharma et al. / J. Nig. Soc. Phys. Sci. 5 (2023) 1137 6 Figure 3: Variations of Ra for distinct values of Re for top-heavy distri- bution Figure 4: Variations of Ra for distinct values of Ta for bottom-heavy arrangement Figure 5: Variations of Ra for distinct values of Ta for top-heavy ar- rangement convection for both bottom-heavy and top-heavy pattern of the system. From figures 6 and 7, It is found from the graphs that with an increase in the values of Le, Ra increases for bottom-heavy distribution, whereas Ra decreases for top-heavy configuration with increase in the values of the Lewis number. Hence, Ra stabilizes the bottom-heavy arrangement and destabilizes the top-heavy arrangement. Figures 8 and 9 show that Ra increases slightly with increase in NA for bottom-heavy arrangement and Ra decrease slightly Figure 6: Variations of stationary Ra for different values of Le for bottom-heavy distribution Figure 7: Variations of Ra for different values of Le for top-heavy dis- tribution with increase in the modified diffusivity ratio for top-heavy ar- rangement. Hence NA stabilize the system for bottom-heavy arrangement and destabilize the system for top-heavy arrange- ment. Figure 8: Variations of Ra for different values of NA for bottom-heavy arrangement Figures 10 and 11 show the variation of Ra for stationary convection with respect to the non-dimensional wave number for different values of Rn. It is depicted from the graphs that for the cases of bottom-heavy and top-heavy configuration, Ra decreases with the increase in Rn which causes the destabilizing 6 Sharma et al. / J. Nig. Soc. Phys. Sci. 5 (2023) 1137 7 Figure 9: Variations of Ra for different values of NA for top-heavy ar- rangement effect on the system. Figure 10: Variations of Ra for different values of Rn for bottom-heavy arrangement Figure 11: Variations of Ra for different values of Rn for top-heavy ar- rangement The effect of the medium porosity ε on Ra is displayed in figures 12 and 13. It is found that with an increase in the ε, Ra decreases and increases, respectively for bottom-heavy and top- heavy configurations. Thus, a porous medium destabilizes the system for the bottom-heavy pattern and stabilizes the system for the top-heavy pattern. Figure 12: Variations of Ra for three different values of ε bottom-heavy distribution Figure 13: Variations of Ra for three different values of ε top-heavy distribution 10. Conclusions The effect of rotation on thermal convection in an electri- cally conducting nanofluid saturated by porous medium has been studied using linear stability theory by employing an Ol- droydian model which incorporates the effects of the electric field, Brownian motion, thermophoresis and rheological param- eters for bottom-heavy and top-heavy distribution of nanoparti- cles. The conclusions of the present study are given below: 1. AC electric field has destabilizing for both bottom-heavy and top-heavy distribution of nanoparticles. 2. The Taylor number Ta has stabilizing for both bottom- heavy and top-heavy distribution of nanoparticles. 3. The effect of Lewis number (non-dimensional parameter accounting for Brownian motion parameter DB) tends to stabilize the stationary convection for bottom-heavy dis- tribution and destabilizes for top-heavy configuration. 4. Modified diffusivity ratio has stabilized the system for bottom-heavy and destabilized the system for top-heavy configuration. 5. The concentration Rayleigh number postpones the sta- tionary convection for both bottom-heavy and top-heavy distribution. 7 Sharma et al. / J. Nig. Soc. Phys. Sci. 5 (2023) 1137 8 6. Medium porosity has destabilizing effect for bottom- heavy distribution and stabilizing effect for top-heavy distribution on stationary convection. Acknowledgments The third author gratefully acknowledges the financial as- sistance of CSIR-HRDG for JRF. References [1] S. U. S. Choi, “Enhancing thermal conductivity of fluids with nanoparti- cles”, Siginer, D. A., Wang, H. P. (eds.) Developments and Applications of Non-Newtonian Flows 66 (1995) 99. [2] D. A. Nield & A. V. Kuznetsov, “The onset of convection in a horizontal nanofluid layer of finite depth”, European Journal of Mechanics-B/fluids 29 (2010) 217. [3] L. J. Sheu, “Thermal instability in a porous medium layer saturated with a viscoelastic nanofluid”, Transport in Porous Media 88 (2011) 461. [4] V. Sharma, R. Kumari & S. Garga, “Overstable convection in rotating Oldroydian nanofluid layer saturated a Darcy-Brinkman porous medium embedded by dust particle”, Recent Trends in Algebra and Mechanics 18 (2014) 149. [5] W. Yu & S. U. S. Choi, “The role of interfacial layers in the enhanced ther- mal conductivity of nanofluids: A renovated Maxwell model”, Journal of Nanoparticle Research 5 (2003) 167. [6] T. B. Jones, “Electrohydrodynamically enhanced heat transfer in liquids - a review”, Advances in Heat Transfer 14 (1978) 107. [7] X. Chen, J. Cheng & X. Yin, “Advances and applications of electro hy- drodynamics”, Chinese Science Bulletin 48 (2003) 1055. [8] P. J. Stiles, F. Lin & P. J. Blennerhassett, Convective heat transfer through polarized dielectric liquids, Physics of Fluids, 5 (1993) 3273. [9] I. S. Shivakumara, J. Lee, K. Vajravelu & M. Akkanagamma, “Electro- thermal convection in a rotating dielectric fluid layer: Effect of velocity and temperature boundary conditions”, International Journal of Heat and Mass Transfer 55 (2012) 2984. [10] V. Sharma, A. Chowdhary & U. Gupta, “Electrothermal convection in di- electric Maxwellian nanofluid layer”, Journal of Applied Fluid Mechan- ics11, (2018) 765. [11] P. L. Sharma, Deepak & A. Kumar, “Effects of rotation and magnetic Field on thermosolutal convection in elastico-viscous Walters’ (model B’) nanofluid with porous medium”, Stochastic Modeling & Applications 26 (2022) 21. [12] P. L. Sharma, A. Kumar & G. C. Rana, “On the principle of exchange of stabilities in a Darcy Brinkman porous medium for a Rivlin-Ericksen fluid permeated with suspended particles using positive operator method”, Stochastic Modeling & Applications, 26 (2022) 47. [13] P. L. Sharma, Deepak, A. Kumar & P. Thakur, “Effects of rotation on ther- mosolutal convection in Jeffrey nanofluid with porous medium”, Struc- tural Integrity and Life (2022). [14] A. Kumar, P. L. Sharma, Deepak & P. Thakur, “Thermosolutal convection in Jeffrey nanofluid with porous medium”, Structural Integrity and Life (2022). [15] P. L. Sharma, M. Kapalta, Deepak, A. Kumar, V. Sharma & P. Thakur, “Electrohydrodynamics convection in dielectric Oldroydian nanofluid layer in a porous medium”, Structural integrity and life (2022). [16] P. K. Gautam, G. C. Rana & H. Saxena, “Stationary convection in the electrohydrodynamics thermal instability of Jeffrey nanofluid layer satu- rating a porous medium: free-free, rigid-free and rigid-rigid”, Journal of Porous Media 23 (2020) 1043. [17] I. S. Shivakumara, N. Rudraiah, J. Lee & K. Hemalatha, “The onset of Darcy-Brinkman electroconvection in a dielectric fluid saturated porous layer”, Transport in Porous Media 90 (2011) 509. [18] R. Chand, G. C. Rana & D. Yadav, “Electrothermo convection in a porous medium saturated by nanofluid”, Journal of Applied Fluid Mechanics 9 (2016) 1081. [19] M. Ramanuja, J. Kavitha, A.Sudhakar & N. Radhika, “Study of MHD SWCNT-Blood Nanofluid Flow in Presence of Viscous Dissipation and Radiation Effects through Porous Medium”, Journal of the Nigerian So- ciety of Physical Sciences 5 (2023) 1054. [20] F.O. Akinpelu, R.A. Oderinu & A.D. Ohaegbue, “Analysis of Hydromag- netic Double Exothermic Chemical Reactive Flow with Convective Cool- ing through a Porous Medium under Bimolecular Kinetics”. Journal of the Nigerian Society of Physical Sciences 4 (2022) 130. 8