2.1. Computational microstructure modeling approach to designing porous materials
The sound absorption and heat conduction phenomena occurring in the solid and fluid phases inside porous materials are formulated using the homogenization method. This section outlines the microstructural design model of such sound absorption phenomenon.
The sound absorption model considers the viscosity of the fluid phase and attenuation due to heat dissipation. Homogenization is applied using asymptotic expansion to directly obtain the equivalent properties necessary to predict the macroscopic properties of the porous sound-absorbing material from its microstructure. These equivalent properties are then applied to a model of porous sound absorbers to determine the macroscopic properties of the material, such as its sound absorption coefficient, as described by Yamamoto et al. [
13].
Consider the porous sound-absorbing material with a periodic microstructure shown in
Figure 2. For the microscale governing equations, the equilibrium, constitutive, and displacement–strain relations of a linear elastic body are applied to the solid phase. The linearized Navier–Stokes equations are applied to the flow field of the fluid phase, which is assumed to exhibit microdisplacement. The temperature field of the fluid phase follows the first law of thermodynamics. Because the specific heat of the solid phase is sufficiently high compared with that of the fluid phase, the temperature field of the solid phase is assumed to be in equilibrium. The law of conservation of mass and an equation of state are considered to be the governing equations. Velocity, vertical stress, and temperature continuity conditions are imposed at the boundary between the solid and fluid phases. Assuming an asymptotically expanded solution and substituting it into the microscale governing equations, we obtain microscale boundary value problems. Macroscopic properties, such as equivalent density, are obtained by volume-averaging the solutions obtained from solving these equations. The macroscale governing equations for the solid and fluid phases are derived by averaging the microscale governing equations. Performance indicators, such as the sound absorption coefficient, are determined by solving these equations.
The microscale governing equations of a porous sound-absorbing material are described. The solid phase is an isotropic linear elastic body, the fluid phase is a viscous fluid with a compressible viscosity coefficient
, and all fluid phases are assumed to be connected. The governing equations for the solid phase are expressed as Equation (1), where
is angular frequency,
is the displacement of the solid phase,
is the mass density,
is the elasticity tensor,
is the distortion, and
is the stress.
The velocity and mass density of the fluid phase are denoted as
and
, respectively. The governing equations for the flow field of the fluid phase are expressed in terms of the linearized Navier–Stokes equations, given that they are of a small amplitude.
The specific heat of the solid phase is sufficiently high compared with that of the fluid phase, so the temperature
can be assumed to be in equilibrium. Then, only the fluid phase needs to be considered for the temperature field, and the governing equation can be expressed as follows according to the first law of thermodynamics:
where
is the temperature variation,
is the constant-volume specific heat,
is the gas constant,
is the heat flow velocity, and
is the thermal conductivity. The law of conservation of mass and equation of state for the fluid phase can be expressed as follows:
The boundary conditions at the boundary
between the solid and fluid phases are written in terms of the continuity of velocity, boundary vertical stress, and temperature as follows:
where
and
are the unit normal vectors of the solid and fluid phases, respectively, outward to the domain at
.
Assuming that the microstructure is periodic, let
be the unit cell and
be the size of the unit cell (
in
Figure 2). The representative macroscale length
is the wavelength of the porous material, and the ratio of the representative microscale length to the representative macroscale length is
. Let
be the macroscale spatial variable and
be the microscale spatial variable. Asymptotic expansion solutions are possible; Gilbert and Mikelić [
14] and Clopeau et al. [
15] applied two-scale convergence theory to a problem of porous materials. For the state quantities
,
,
,
, and
, we assume the asymptotic expansion solution of Sanchez-Palencia [
16] as follows:
where all terms on the right-hand side are periodic with respect to
(
-periodic).
Applying the Galerkin method to a relational expression of the order of
for the solid phase, we obtain the following boundary value problem for the
-periodic characteristic function
:
The characteristic function can be obtained by solving the above equation under the condition to exclude rigid-body displacements.
Consider the relative velocity
of the fluid phase to the solid phase on the order of
and replace
with
. From the relation on the order of
, we obtain the following microscale boundary value problem for the flow field of the fluid phase:
where
and
are the
-periodic characteristic functions of relative velocity and pressure, respectively.
at
.
and
are obtained by implement the condition
to exclude the constant-pressure component.
From the relation for the temperature
of the fluid phase on the order of
, we obtain the following boundary value problem:
where
is a
-periodic characteristic function with respect to temperature; the isothermal condition
is satisfied at
.
The characteristic function
in unit cell
, obtained by solving the corresponding boundary value problem, is volume averaged. The homogenized elastic tensor
of the solid phase is obtained using the following formula:
where
is the volume of the unit cell
of the porous material.
The equivalent density
of the fluid phase is obtained by volume averaging the
of the fluid phase
in the unit cell.
where
is the volume of the fluid phase
in the unit cell and
is the volume average of
.
The equivalent volumetric modulus of elasticity
of the fluid phase is obtained by volume averaging the
of the fluid phase
in the unit cell as follows:
The obtained macroscopic properties are then used to derive the macroscale governing equations for the solid and fluid phases respectively as follows [
17]:
where
is the potential function, defined as
;
is the stress in the solid phase without considering its coupling with the fluid phase;
is the porosity; and
is the average mass density of the porous material,
.
,
, and
are the homogenized macro properties of the solid phase (homogenized elastic tensors).
,
, and
are the homogenized macro properties of the fluid phase.
The vertical-incidence sound absorption coefficient is derived through Equation (21) using the acoustic tube model shown in
Figure 3 and by formulating the porous sound-absorbing material using the homogenized macroscopic properties (
,
,
,
,
, and
) and the macroscale governing equations (Equations (17) and (18)).
where
is the frequency of air.
and
are the sound pressures at distances
and
, respectively, from the surface of the porous sound-absorbing material in the acoustic tube.
2.3. Preparation of porous materials and performance evaluation methods
A prototype porous composite material consisted of PMS xerogel and CNFs was fabricated to resemble the microstructure and Young's modulus of the porous sound absorber model calculated in
Section 3.1. The fabrication procedure accorded with Kanamori et al. [
18] and Yamasaki et al. [
19].
The vertical-incidence sound absorption coefficients of the prepared xerogel specimens were measured using a WinZacMTX (Nihon Onkyo Engineering Co., Ltd.; per JIS A 1405-2 and ISO 10534-2). The inner diameter of the acoustic tube was 40 mm, and the measurement frequency range was 200–4,800 Hz.
The flow resistance per unit thickness was measured using an AirReSys (Nihon Onkyo Engineering Co., Ltd.; per ISO 9053). The differential pressure before and after the specimen was read when air flowed through the specimen at a velocity of 0.5 mm/s. The results were normalized using the flow velocity and specimen thickness.
Young’s modulus and the loss modulus were measured using a modulus measurement system (Nihon Onkyo Engineering Co., Ltd.). The specimen was placed on the base plate of a shaker, and a mass plate was placed on top of the specimen to construct a spring–mass system in the thickness direction. Resonance was generated by vibrating the base plate, and Young’s modulus was calculated using the resonance frequency and the thickness of the specimen. The loss factor was calculated using the full width at half maximum of the peak near the resonance frequency.
The pore size distribution was determined using an AutoPore IV 9500 mercury intrusion porosimeter (Micromeritics Instruments Corporation). A measurement specimen sized approximately 0.03–0.04 g was placed in a sealed glass container for measurement. The mercury intrusion pressure ranged from approximately 1 kPa to 400 MPa, and the measurement mode was pressure boosting.
Thermal conductivity was measured in a room under standard conditions using a simple measurement apparatus equipped with a heat flux sensor, thermocouples, an electric heater, and a thermal insulator, as shown in
Figure 5. The heat flux sensor and a thermocouple were placed on the heater, which supplied a constant heat quantity. The test specimen, which was covered with an insulation material with a thermal conductivity of 0.0313 W/(m·K), was placed on the heater and the thermocouple, and a thermocouple and a 1 mm–thick resin plate was placed on the test specimen for measurement. Thermal conductivity was derived from the measured heat flux and the temperatures above and below the specimen. The thermal conductivity of the thermal-insulating material was 0.0313 W/(m·K) according to a steady-state thermal conductivity measurement system (HFM436/3/1 Lambda, NETZSCH-Gerätebau GmbH; per JIS A 1412-2 and ISO 8301) and 0.0469 W/(m·K) according to this simple measurement apparatus. Therefore, as a reference value, a calibrated value of thermal conductivity was also calculated assuming a constant percentage of heat flowing out of this simple system for the measurement of thermal conductivity.