Slide film damping in microelectromechanical system devices
Transcription
Slide film damping in microelectromechanical system devices
Original Article Slide film damping in microelectromechanical system devices Proc IMechE Part N: J Nanoengineering and Nanosystems 227(4) 162–170 Ó IMechE 2013 Reprints and permissions: sagepub.co.uk/journalsPermissions.nav DOI: 10.1177/1740349913486097 pin.sagepub.com Weidong Wang, Jianyuan Jia and Jianwen Li Abstract Film damping caused by microfluids has important effects on the dynamic characteristics of moving elements of microelectromechanical system devices. There are two kinds of film damping existing in microelectromechanical system devices, for instance, slide film damping and squeeze film damping. This article presents an overview on the recent research progress on the slide film damping in microelectromechanical system devices. Based on the first slip velocity boundary conditions, this article discusses two kinds of damping models in detail, which commonly used to investigate on the slide film damping. For the convenience of quick reference in future, laterally moving microstructures, adequate important equations and applicable conditions are included in this article. Finally, we proposed two unified models for the analysis and design of laterally moving microstructured devices. Keywords Slide film damping, review, microelectromechanical system, laterally oscillation, microfluids Date received: 14 December 2012; accepted: 18 March 2013 Introduction For these microelectromechanical system (MEMS) devices, especially containing moving elements, it is essential to consider the damping effects of microfluidics produced by the relative motion between the moving elements and the substrates, which have important influence on the dynamic characteristics of MEMS devices.1–3 It has been confirmed by many experiments that the gas behaviors have great effects on the dynamic characteristics that work at an external environment with some certain gas pressures, such as micromachined accelerometers, microgyroscopes, micromirrors and micromotors.2,4–9 The mechanisms of fluid damping that were received by moving elements of MEMS devices can be mainly divided into two categories:9–11 squeeze film damping and slide film damping. The squeeze film damping occurs when two parallel plates are in relative perpendicular motion. The fluid pressure difference above and below the moving microdevices will produce damping forces. The slide film damping occurs when two parallel plates are in relative tangential motion. Viscous energy dissipation in the fluid between the two plates becomes a representative damping mechanism in laterally driven microdevices.5,9 Over the past two decades, the squeeze film damping in MEMS devices has been studied extensively,1–4,6–24 while less attention on slide film damping.5,9,25–31 In 2007, Baoa and Yang17 and Pratap et al.18 have presented a much comprehensive overview about squeeze film air damping in MEMS devices. Moreover, in 2011, Vagia and Tzes22 have also made a literature review on squeezed film damping in modeling and control design for electrostatic microactuators. Herein, we will not investigate on the squeeze film damping, while we will focus on slide film damping and discuss its modeling and application in this article. Two kinds of damping models are commonly used to study the slide film damping, including the Couettetype model and the Stokes-type model, that is, Stokes’ second problem. The Couette-type model shown in Figure 1 can be used either when the gap width between the moving plate and the fixed plate (substrate) is very School of Electrical and Mechanical Engineering, Xidian University, Xi’an, PR China Corresponding author: Weidong Wang, School of Electrical and Mechanical Engineering, Xidian University, P.O. Box183, No. 2 South Taibai Road, Xi’an, Shaanxi 710071, PR China. Email: [email protected] Wang et al. 163 and Couette flows considering the effect of the slip condition due to an oscillating wall, but the solutions are incomplete, and therefore, they did not discuss about them in the application scope of MEMS. Both the Couette-type and the Stokes-type models investigated at microscale in detail will lay a good theoretical foundation for the analysis and design of laterally driven microstructures. Couette-type model Problem solution Figure 1. Microgap shear flow (Couette-type flow). Figure 2. Stokes’ second problem (Stokes-type flow). As shown in Figure 1, a continuum flow is assumed, in which the minimum size of the structure and the thickness of the interstructure fluid film are at least 10 times greater than the mean free path of the gas or the intermolecular distance of the liquid. Neglecting the pressure gradients, the Navier–Stokes equations simplify to equation (1)9,25,32 d2 u =0 dy2 ð1Þ At microscale, the slip velocity boundary conditions should be introduced to solve equation (1) small or when the vibration frequency is very low; otherwise, the Stokes-type model should be used to study the slide film damping.9,25,27 The simplest conceptual configuration finds two infinite, parallel plates separated by a distance h. The top plate translates with a velocity u = u0cosvt, or u = u0sinvt, in its own plane. As shown in Figure 2, it is considered that a laterally oscillating infinite plate is immersed in an incompressible fluid (either a gas or a liquid) with constant transport properties. Due to the liquid viscosity, the plate drives the fluid to oscillate with itself, forming a kind of flow named Stokes flow, that is, Stokes’ second problem. The viscosity damping caused by the relative motion between the fluid and the plate is parallel to the motion of the plate, so-called slide film damping. For the lateral motion of the plate in Figures 1 and 2, the velocity profile is prescribed as u = u0cosvt, where u0 is the velocity oscillation amplitude and v is the oscillation frequency. The phenomenon of velocity slip of fluid on the surface of the plate can be neglected at macroscale, but it plays an important role at microscale. The Stokes-type model has been used by Cho and coworkers25,26 to study the slide film damping received by laterally driven microstructures; nevertheless, the effect of velocity slip has not been considered, which will definitely cause errors in theoretical analysis and structural design. The effect of velocity slip of fluid on laterally driven microstructures has been taken into account by Veijola and Turowski,27 but the Stokes’ second problem has not been studied. Wang et al.30 have given an analytical solution for Stokes’ second problem and have obtained the damping coefficient and spring coefficient. Khaled and Vafai31 have obtained the exact solutions of Stokes u(y, t)jy = 0 = u(0, t) = u0 cos vt + Ls1 u(y, t)jy = h = u(h, t) = Ls2 du j dy y = h du j dy y = 0 ð2Þ ð3Þ where Ls1 and Ls2 are the slip lengths on the moving plate and the substrate (the stationary plate), respectively. Then, the exact solution of velocity in fluid film is u(y, t) = h + Ls2 y u0 cos vt h + Ls1 + Ls2 ð4Þ In the case of gas as fluid, assuming two different tangential momentum accommodation coefficients (TMACs), s1 and s2 of gas molecule on the moving plate and the substrate (stationary plate), respectively, the fluid velocity profile in the gap and shear stress can be deduced as follows h + Ls2 y u0 cos vt h + Ls1 + Ls2 ð5Þ 1 + a2 Kn (y=h) u0 cos vt = 1 + (a1 + a2 )Kn du u0 cos vt u0 cos vt =m = mefc t(y, t) = m dy h + Ls1 + Ls2 h ð6Þ u(y, t) = where Kn is the Knudsen number, Kn = l/h, here l is the mean free path of gas molecule; Ls1 = a1l, Ls2 = a2l, a1 = (2 2s1)/s1, a2 = (2 2s2) /s2, mefc = m/[1 + Kn(a1 + a2)]. Here, mefc is the slip effective viscosity for Couette flow. Therefore, the slide film damping coefficient is 164 Proc IMechE Part N: J Nanoengineering and Nanosystems 227(4) continuity equations result in a one-dimensional diffusion equation9,26,32 ∂u ∂2 u =n 2 ∂t ∂y ð9Þ where n is the kinematic viscosity of the fluid, defined as n = m/r, here r is the density of the fluid. At microscale, the slip boundary conditions can also be introduced u(y, t)jy = 0 = u(0, t) = u0 cos vt + Ls1 u(y, t)jy!‘ = u(‘, t) = 0 t(0, t) A A = mefc u0 cos vt h ð7Þ where A is shear area. At macroscale, the slip lengths Ls1 and Ls2 can be treated as 0, so that the velocity profile without slip boundary conditions can be simplified from equation (2) u(y) = hy u0 cos vt h ð10Þ ð11Þ where Ls1 is the slip length on the moving plates. Based on the separation of variables and the integral transform methods, the steady-state velocity profile, u(y,t), in the fluid field can be obtained by integrating twice and solving for the constants using the boundary conditions,9,28 Figure 3. Effects of the Knudsen number on the velocity profile (Couette flow). CCout = du j dy y = 0 ð8Þ u(y, t) = bu0 exp( ky) cos½vt (ky + u) ð12Þ pffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi where b = 1= 2g 2p+ 2g + 1, u = arctan[g/(1 + g)], ffiffiffiffiffiffiffiffiffiffiffi g = kLs1 and k = v=2n. Then the shear stress obtained by the moving plate is given by pffiffiffi du(y, t) jy = 0 = 2kbu0 m cos (vt + p=4 u) t w =m dy pffiffiffi = 2kbu0 m½cos vt cos (p=4 u) sin vt sin (p=4 u) ð13Þ Discussion Here, it is assumed that s1 = s2 = 1, a1 = a2 = 1 and then Ls1 = Ls2 = hKn. Figure 3 shows the effect of the Knudsen number on the steady periodic velocity profile. As can be seen, for a certain Kn, the velocity profile of u/u0(cosvt) was keeping straight with a constant slope at any moment t. Also, the slopes of the velocity profiles will increase with the increase in the Knudsen number. For Kn = 0, this situation corresponds to the case at macroscale, that is, the slip length Ls2 = 0. It can be found from Figure 3 that the velocity near the substrate would increase with the increase in the Knudsen number; moreover, the slip length Ls2 has the same trend according to Kn. Therefore, one can conclude that due to the slip velocity boundary conditions at microscale, great changes will happen to the velocity profile, which will have effects on other mechanical properties, for instance, sheer stress and damping coefficient. Stokes-type model Typical Stokes’ second problem Problem solution. As shown in Figure 2, neglecting the pressure gradient, the Navier–Stokes equations and It is obvious that the damping force has two components. The phase of the first component is same with the velocity phase, and the phase of the second component is same with the phase of the displacement. Therefore, we define the damping coefficient and spring coefficient shown as follows pffiffiffi CStok = vnbmA cos(p4 u) ð14aÞ pvffiffiffi p KStok = v n bmA sin( 4 u) ð14bÞ Similar to equation (5), when Ls1 equals to 0 at macroscale, the velocity profiles of Stokes flow can be reduced to equation (15) from equation (12), which agrees with the expression presented by Wang.9 u(y, t) = u0 exp(ky) cos (vt ky) ð15Þ Discussion. The velocity profiles of the typical Stokes’ second problem are shown in Figure 4. Here, the dotted lines are given for the Stokes flow with no slip condition, and the solid lines are for the flow with slip condition, that is, g = kLs1 = 0.215. It is noted that all of the velocities of the Stokes flow will decay to 0 when Y is large enough, that is to say, the moving plate would have little effects on the liquid when the distance Wang et al. 165 Figure 5. Cosine excitation for finite gap height. Figure 4. Velocity profiles of the Stokes flow at different times. is larger than some certain values. In order to illustrate the extent to which the effects of viscosity penetrate into the fluid film, a concept of penetration depth is imported. Generally, a penetration depth dp is defined as the characteristic thickness of a fluid layer over which the velocity amplitude has dropped to 1% of its maximum value u0, that is u = b exp (kdp )u0 = 0:01u0 ∂u ∂2 u =n 2 ∂t ∂§ ð17Þ u(§, t)j§ = h = u(h, t) = u0 cos vt Ls1 u(§, t)j§ = 0 = u(0, t) = Ls2 du j d§ § = h du j d§ § = 0 ð18aÞ ð18bÞ Equation (17) can be solved in the frequency domain for a steady-state cosine velocity excitation, and the solution can be written as follows Therefore, dp can be written as follows dp = For solving conveniently, a variable § was introduced here, § = h2y. Then equations (2), (3) and (9) can be written in the following forms 1 ln 100b = 4:605 ln 2g2 + 2g + 1 =k k u(§, t) = u0 exp (ivt)½C1 sinh (q§) + C2 cosh (q§) ð16Þ It is noted that the penetration depth will decrease with the increase in the oscillation frequency. Finite height of fluid gap The above problem focuses on the typical Stokes flow with infinite fluid film. However, in practical MEMS devices, the thickness of the fluid film cannot be infinite, the analytical results above are not suitable for actual devices. Therefore, the case that has finite height of fluid gap will be investigated in the following. Problem solution. There are two kinds of velocity excitations, including cosine and sine, according to the different velocity phases. (1) For cosine velocity excitation. As shown in Figure 5, the governing equation is same with that of the typical Stokes’ second problem expressed by equation (9), while the velocity boundary conditions are different from theirs, that is, equations (10) and (11). The boundary conditions given by equations (2) and (3) should be introduced here. ð19Þ pffiffiffiffiffiffiffiffiffiffi where q is a complex frequency variable, q = iv=n. The constants C1 and C2 are determined from the boundary conditions of equations (18a) and (18b). Then the velocity function u(§, t) can be obtained as follows u(§, t) = sinh (q§) + qLs2 cosh (q§) u0 exp(ivt) (1 + q2 Ls1 Ls2 ) sinh (qh) + q(Ls1 + Ls2 ) cosh (qh) ð20Þ When Ls1 = Ls2 = l, the velocity function in equation (20) agrees with the expression presented by Veijola and Turowski.27 The velocity profile u(§,t) is the real part of u(§, t). The shear force acting on the moving plate at § = h, with a surface area of A, is given as follows d u(§, t) d§ mAq½1 + qLs2 tanh (q§) u0 exp (ivt) = q(Ls1 + Ls2 ) + (1 + q2 Ls1 Ls2 ) tanh (qh) t (§, t) = mA ð21Þ The damping admittance can be obtained from the velocity 166 Proc IMechE Part N: J Nanoengineering and Nanosystems 227(4) CStok (§, t) = mAq½1 + qLs2 tanh (qh) q(Ls1 + Ls2 ) + (1 + q2 Ls1 Ls2 ) tanh (qh) ð22Þ So the damping coefficient Cstok2 is the real part of the admittance, and the spring coefficient Kstok2 is the imaginary part In case of the same slip length on both the moving plate and the substrate, that is, Ls1 = Ls2 in equations (2) and (3), this above problem with a sinusoidal velocity excitation was solved in the frequency domain through the Laplace transformation based on the theory of residues,31 and a steady periodic velocity is obtained as expressed in equation (24) U(Y, T) (M1 M3 + M2 M4 )½f1 (Y) sin (T) + f2 (Y) cos (t) (M1 M4 M2 M3 )½f2 (Y) sin (T) f1 (Y) cos (T) = U0 M23 + M24 M23 + M24 (M3 M5 + M4 M6 )½f3 (Y) sin (T) + f4 (Y) cos (T) (M3 M6 M4 M5 )½f3 (Y) cos (T) f4 (Y) sin (T) + + M23 + M24 M23 + M24 Cstok2 = Re½CStok (§, t) Kstok2 = Im½CStok (§, t) ð23aÞ ð23bÞ If Ls1 = Ls2, equations (20)–(22) can be simplified as follows u(§, t) = sinh (q§) + qLs1 cosh (q§) u0 exp (ivt) (1 + q2 L2s1 ) sinh (qh) + 2qLs1 cosh (qh) t (z, t) = mAq½1 + qLs1 tanh (qz) m exp (ivt) 2qLs1 + (1 + q2 L2s1 ) tanh (qh) 0 CStok (§, t) = ð24Þ where U = u/(hv), U0 = u0/(hv), Y = y/h, T = vt and R = h2v/n; the functions f1, f2, f3 and f4 are defined as follows qffiffiffi qffiffiffi 8 R R > > f (Y) = sinh 4 Y cos 1 > 2 2Y > > > qffiffiffi qffiffiffi > > > R R > < f2 (Y) = cosh 2 Y sin 2Y qffiffiffi qffiffiffi ð25Þ > R R > > f3 (Y) = cosh Y cos Y > 2 2 > > qffiffiffi qffiffiffi > > > > R R : f4 (Y) = sinh 2 Y sin 2Y mAq½1 + qLs2 tanh (qh) q(Ls1 + Ls2 ) + (1 + q2 Ls1 Ls2 ) tanh (qh) The constants M1, M2, M3, M4, M5 and M6 are calculated from the following qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi 8 R R R R R R > ) cos ( ) + a sinh ( ) cos ( ) a cosh ( ) sin ( ) M = cosh ( > 1 2 2 2 2 2 > > qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffi2ffi > > R R R R R R > > M2 = sinh ( 2 ) sin ( 2 ) + a cosh ( 2 ) sin ( 2 ) + a sinh ( 2 ) cos ( 2 ) > > qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi > > > < M3 = sinh ( R) cos ( R) + 2a cosh ( R) cos ( R) 2a2 cosh ( R) sin ( R) 2a sinh ( R) sin ( R) q2ffiffiffi qffiffi2ffi q2ffiffiffi q2ffiffiffi qffiffi2ffi qffiffiffi2 qffiffi2ffi q2ffiffiffi ð26Þ > R R 2 R R R R R R > ) sin ( ) + 2a ) cos ( ) + 2a sinh ( ) sin ( ) + 2a cosh ( ) cos ( ) M = cosh ( sinh ( 4 > 2 2 > > qffiffi2ffi qffiffi2ffi qffiffiffi 2 qffiffiffi 2 qffiffiffi 2 qffiffiffi 2 > > R R R R R R > M5 = sinh ( 2 ) cos ( 2 ) + a cosh ( 2 ) cos ( 2 ) a sinh ( 2 ) sin ( 2 ) > > > qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi qffiffiffi > > : M = cosh ( R) sin ( R) + a sinh ( R) sin ( R) + a cosh ( R) cos ( R) 6 2 2 2 2 2 2 qffiffiffi where a = Lhs1 R2 . (2) For sinusoidal velocity excitation. As shown in Figure 6, the governing equation is same with equation Discussion. As shown in Figures 5 and 6, a laterally (9), while the velocity boundary conditions are different oscillating plate is immersed in an incompressible fluid, from equations (10) and (11). The boundary conditions assuming the parameters given in Table 1. Figure 7 shows the fluid velocity profiles at different of equations (2) and (3) should also be introduced here. times under the above two kinds of velocity excitation. It is found that the velocity curves for cosine excitation, at times T = 0, p/2, p and 3p/2, are in good agreement with those curves for sinusoidal excitation, at times T = p/2, p, 3p/2 and 0, respectively. That is to say, there is a lagging phase p/2 of the velocity profile under sinusoidal excitation with respect to that under cosine excitation, which is obvious due to the phase difference between cosine and sinusoidal excitation. Herein in the following, the case of cosine excitation is utilized to explain the characteristics of the Stokes flow with finite height of fluid gap. Figure 6. Sinusoidal excitation for finite gap height. (1) Effects of oscillation frequency. The oscillation frequency is changed from 10 Hz to 10 kHz, and Wang et al. 167 Table 1. Parameters for the laterally oscillating plate. h (mm) u0 (m/s) v (Hz) l (mm) Ls1 (mm) Ls2 (mm) n (m2/s) 1000 10 1000 68 68 68 531025 Figure 7. Fluid velocity profiles at different times under cosine and sinusoidal excitation. Figure 9. Fluid velocity profiles with different distances (T = 0). frequencies, the fluid velocities near the substrate are near 0 as the penetration depths become shorter than the distance between the moving plate and the substrate. Figure 8. Fluid velocity profiles at different oscillation frequencies (T = 0). other parameters remain unchanged (Figure 8). It is found that at different frequencies, the fluid velocities near the substrate (i.e., the fixed wall) are also different. It is found that all the fluid velocities near the moving plate are less than the velocity oscillation amplitude u0. At low frequencies, for instance, 10, 100 and 200 Hz, because of the viscous effect of the fluid on the fixed wall and the slip conditions, their velocities near the substrate are not 0. It is noted that at very low frequency, such as 10 Hz, the velocity profile is of high linearity, which is in good agreement with the Couette flow. However, at high (2) Effects of the distance. Maintaining other parameters unchanged in Table 1, we only change the distance h between the moving plate and the substrate from 10 to 1000 mm. Figure 9 shows the velocity profiles with different heights of the fluid gap at time T = 0. Because of the slip conditions, all the fluid velocities near the moving plate are not equal to 0. Supposing the slip lengths Ls1 and Ls2 are equal to 0, then all the velocities near the moving plate would become 0. Except the case of h = 2000 mm, most of the velocities near the fixed wall are not equal to 0 because of the viscous effect of the fluid. However, it can be predicted that if the distance h is greater than 2000 mm or the oscillation frequency v is higher than 1 kHz, then the velocities near the fixed wall (the substrate) will become 0. For small distance h, including 10, 100 and 200 mm, the fluid velocity profiles are of high linearity, which agree well with the Couette flow. We will discuss these phenomena in the following section. It is noted that for the smallest distance of h = 10 mm, the fluid velocity profile is close to a parallel line, that is to say, the velocity is of little variation between h = 0 and 10 mm. We think that this phenomenon stems from a large slip length, Ls1 = Ls2 = 68 mm, and a large Knudsen number, Kn = 6.8. In Figure 9, the hollow square symbols denotes the fluid velocity profile at a small slip length, Ls1 = Ls2 = 0.68 mm, and a small Knudsen number, Kn = 0.068. 168 Figure 10. Fluid velocity profiles for the typical Stokes’ second problem and the Stokes flow with finite height of fluid gap (T = 0, v = 10 kHz). Figure 11. Fluid velocity profiles for the Couette flow and the Stokes flow with finite height of fluid gap (T = 0, v = 1 kHz). Comparison analysis In this section, we will compare the above models to find out the relationships among them, which will lay a good theoretical foundation for future use. (1) Typical Stokes’ second problem and Stokes flow with finite height of fluid gap. For the typical Stokes’ second problem, without a fixed wall (the substrate), the moving plate is immersed in an incompressible fluid. From the above analysis in section ‘‘Typical Stokes’ second problem,’’ it is found that for the typical Stokes’ second problem, if the distance is longer than the penetration depth dp, the fluid velocity can be considered as 0, that is to say, the moving plate has little effects on the fluid once the distance exceeds dp. In practical application, the substrate (the fixed wall) always exists, so that the Stokes flow with finite height of fluid gap should be used to study it. Proc IMechE Part N: J Nanoengineering and Nanosystems 227(4) According to equation (16), the penetration depth of the typical Stokes’ second problem is about 400 mm at the oscillation frequency of 10 kHz. Figure 10 shows the fluid velocity profiles of the above two models at a varying distance, from 100 to 1000 mm. It is obvious that once the distances exceed 400 mm, the fluid velocity profiles of the Stokes flow with finite gap height agree well with those of the typical Stokes’ second problem. At small distances, for instance, 100 and 200 mm, the fluid velocity profiles of the Stokes flow with finite gap distance do not match with the correspondent velocity profiles of the typical Stokes’ second problem. Especially for 100 mm, the corresponding velocity profiles take on a discrete state. It can be drawn a conclusion that as long as the distance is equal or greater than the penetration depth, the solutions of the typical Stokes’ second problem can be applied to the Stokes flow with finite height of fluid gap. However, it needs a precondition for the above conclusion that the slip lengths on both the moving plate and the substrate are equal, that is, Ls1 = Ls2. (2) Couette flow and Stokes flow with finite height of fluid gap. According to equations (5) and (20), Figure 11 illustrates the fluid velocity profiles of the Couette flow and the Stokes flow with finite gap height. It is found that at the oscillation frequency of v = 10 kHz, only for the case of h = 100 mm, the velocity profile of Couette flow fits well with that of the Stokes flow; for other cases, such as h = 200, 400 and 1000 mm, their velocity profiles take on discrete states between the above two models. Meanwhile, the longer the distance, the higher the discrete degree. Through a large amount of calculation results, it is also found that the higher the oscillation frequency, the higher the discrete degree. It should be noted that the Stokes-type model is more suitable than the Couette-type model for describing the fluid velocity profiles at high oscillation frequencies and larger distances. In other words, the Couette-type model is fit for illustrating the fluid velocity profile at low frequencies and with small distances. In the following, it is assumed that a laterally oscillating plate is parallel to a substrate, and both of them are immersed in an incompressible fluid. How to deal with this problem? Or, how to model it? Based on the above analysis, two unified models can be used to describe this problem, as shown in Figure 12. At low frequency and with small distance, the model shown in Figure 12(a) should be utilized. The fluid between the moving plate and the substrate can be described by the Couette-type model, and the fluid above the moving plate can be modeled through the Stokes-type model. At high frequency and with large distance, the model shown in Figure 12(b) should be utilized. All of the fluid can be modeled through the Stokes-type model. Wang et al. 169 Figure 12. Unified models for laterally oscillating plate: (a) at low frequency and with small distance and (b) at high frequency and with large distance. Summary First, the article presents an overview and reports the recent progress of research on slide film air damping in MEMS. Then the analytical solutions are discussed in detail for the Couette-type and Stokes-type models. Especially for Stokes flow, two kinds of excitation of the moving plate were investigated in detail. Next, the simulation of slide film air damping is analyzed. For quick reference in future MEMS research, abundant important equations on slide film damping are included in this article. Finally, some comparison analyses on both the Couette-type model and the Stokes-type model are carried out and then two unified models are proposed for the analysis and design of laterally moving microstructured devices. In order to use the above formulae appropriately, we proposed two unified models for the design and analysis of MEMS devices, as shown in Figure 12. 2. Acknowledgements 7. The authors thank the reviewers for their comments and their kind suggestions for this article. 3. 4. 5. 6. 8. Declaration of conflicting interests The authors declare that there is no conflict of interest. 9. 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