A General Theory for Coupled Chemo-Electro-Thermo-Mechanical

Total Page:16

File Type:pdf, Size:1020Kb

Load more

Research Article A general theory for coupled chemo‑electro‑thermo‑mechanical heterogeneous system Zhen‑Bang Kuang1 Received: 7 April 2020 / Accepted: 4 November 2020 / Published online: 12 December 2020 © Springer Nature Switzerland AG 2020 Abstract Many transport and rate processes in chemical, physical, mineral, material and biological felds are controlled by the coupled chemo-electro-thermo-mechanical (CETM) process. Though many literatures discussed these coupled problems, but a unifed rigorous theory and a unifed method based on the chemical thermodynamics are lacked. In this paper on the basis of electrochemistry, the non-equilibrium thermodynamics and modern continuum mechanics we modify some previous theories and give a general theory including mass conservation equation, the electric charge conservation equation, complete energy conservation equation, entropy equation, evolution equations and the complete governing equations of these couple CETM systems. An extension of Nernst–Planck equation is derived for the CETM system. This theory gives a theoretical foundation and a universal method to improve and develop engineering theories, especially for the gradual failure components and cells. In appendix we also discuss the interdifusion problems in solids with vacancies shortly as a complement of the continuum difusion. Keywords Energy equation · Chemo-electro-thermo-mechanical systems · Entropy equation and entropy production rate · Gibbs equation · Evolution equation · Governing equation 1 Introduction are for electrically neutral system. However, in engineer- ing a system may be worked under electromagnetic feld, In chemical, physical, material and biological systems, which may be externally imposed or internally created, many transport and rate processes are controlled by the or both. In a thermoelectric material there exist Seebeck, coupled chemo-electro-thermo-mechanical interaction. Peltier and Thomson phenomena [3, 9]. Ionic and mixed We shall abbreviate a system with coupled Chemo-Elec- ionic–electronic devices, such as solid oxide fuel cells, oxy- tro-Thermo-Mechanical interaction as CETM system. Simi- gen pumps and hydrogen production, have gained many larly, a system with coupled Chemo-Thermo-Mechanical applications [10–13]. For expansive media including clays, interaction is a CTM system and a system with coupled shales, polymers gels, corneal endothelium, immature Chemo-Electro-Mechanical interaction is a CEM system. articular cartilage and connective biological tissues, elec- All these systems are complex thermodynamic systems. trochemical interaction are also typical [14–16]. In theories A general theory for CTM system has been discussed in of these chemo-electro-mechanical (CEM) system the tem- papers [1, 2], where a complete energy conservation equa- perature efects are neglected [9–16]. Especially when one tion, an appropriate entropy equation and the govern- discusses the gradual failure of components and cells the ing equation system have been given and modifed the temperature efects may be important. So integrating the previous theories [3–8]. Most of these previous theories efects of the electromagnetic felds into the CTM system * Zhen-Bang Kuang, [email protected] | 1School of Naval Architecture, Ocean and Civil Engineering, Shanghai Jiaotong University, Shanghai 200240, China. SN Applied Sciences (2020) 2:2185 | https://doi.org/10.1007/s42452-020-03842-4 Vol.:(0123456789) Research Article SN Applied Sciences (2020) 2:2185 | https://doi.org/10.1007/s42452-020-03842-4 and integrating the efects of the temperature felds into to denote the serial number of the species and the serial the CEM system are necessary. Though in [3] the CETM number of the chemical reaction and the summation nota- system without chemical reaction had been discussed, tion is written in evidence, as shown in Eq. (1); but the sub- but its results are still left improvement. Therefore the scripts are used to components of a vector or tensor and CETM systems are worth to study. For a CETM system the the summation rule for the repeated indices is used. mass equation, energy equation, entropy equation and Let (k) , c(k) , v(k) , (jk) , �(jk)�̇ (j) and Θ̇ (k) be the partial den- momentum equation can be studied unitedly, but the sity or the apparent density, the mass fraction, the velocity, electric felds are produced due to various reasons and the reaction rate, the mass production rate per volume in jth every case should be researched independently. This situ- chemical reaction and in all chemical reactions of the species ation is analogous to the forces in the mechanical action. k respectively; v = u̇ and u are the barycentric velocity and The complete coupling efects of heat, difusion, chemi- the mechanical displacement vector of a representative ele- cal efect and electromagnetic feld are fully considered ment respectively, J(k) is the mass difusion fow of the species on a unifed thermodynamic foundation and a theoretical k . The mass conservation equation of the species k is [1–4]: frame of governing equations are given. An appropriate ⋅ d() �() complete governing equation system is the foundation for �ċ (k) = −∇ ⋅ J(k) + Θ̇ (k), () = = + v ⋅ ∇() solving engineering problems. The electrochemistry, the dt �t ��(k) non-equilibrium thermodynamics and modern continuum = −∇ ⋅ �(k)v(k) + Θ̇ (k); ̇� + �∇ ⋅ v = 0 mechanics allow us to construct an efcient theory for this �t N N coupling problems. �(k) c(k) = , � = �(k), c(k) = 1 We discuss an open system consisted of N (charged � k=1 k=1 (2) M or uncharged) species with total mass , total volume N N V and total density . According to the engineering cus- J(k) = �(k) v(k) − v , �v = �(k)v(k), J(k) = 0 tom we use the partial density or the mass concentration k=1 k=1 (k) (k) = M ∕V of a species k , rather than the molar con- L N (k) (k) (k) (k) (k) ̇ (k) (jk) ̇ (j) ̇ (k) centration C = ∕MM , where M and MM , are the Θ = � � , Θ = 0; k = 1, 2, ⋅⋅⋅, N total mass in V and the molecular weight of the species j=1 k=1 k respectively. where ∇ is the Eulerian gradient operator. Equation (2) shows that the mass fraction rate ċ , the mass fow J(k) and ̇ (k) 2 The mass and electric charge conservation the total mass production rate Θ of species k subject to equations the equation N N N 2.1 The mass conservation equation ċ (k) = 0, J(k) = 0, Θ̇ (k) = 0 (3) k=1 k=1 k=1 The mass conservation equation of the species k is the In the appendix, one will see that the interdifusion in same for CETM and CTM systems because the macroscopic noncontinuum solids with vacancies [21, 22] has diferent mass is independent to the electromagnetic feld. For easy mechanism with the above theory and discussed shortly to read the mass conservation equation given in literatures as the complement of the difusion phenomena in con- [1–4] is repeated here. tinuum media. Let a CETM system be consisted of N = N1 + N2 species N N M with 1 reactants and 2 products, the total mass , total 2.2 The electric charge conservation equation volume V , total density and chemical reaction number L . The jth chemical reaction equation can be written as [1, According to literature [3] one defne 2, 17–20] N N N I = (k)z(k)v(k) = I + i; I = zv, i = z(k)J(k) (jk)B(k) = 0, j = 1, 2 … , L 0 0 (1) k=1 k=1 k=1 (4) N N −1 (k) (k) (k) (k) where B(k) is the chemical formula of species k , (jk) is the z = z = c z k=1 k=1 stoichiometric constant of a species k in the chemical reac- tion j , which is positive if species k is a product and nega- where z(k) is the charge per mass of component k , z is the (m) th tive if k is a reactant. If B is not appear in the j chemical total charge per mass of the system, I is the total electric reaction, then (jm) = 0 . In this paper, we use superscript Vol:.(1234567890) SN Applied Sciences (2020) 2:2185 | https://doi.org/10.1007/s42452-020-03842-4 Research Article current density, I0 is the convective current density and i From Eq. (9) it is known that a part of electromagnetic is the conductive current density. Using Eq. (2) the electric work, zE ⋅ v − i ⋅ (v × B) , is changed to the kinetic energy. charge conservation equation is According to the Maxwell equation the balance law of electromagnetic energy [3, 23–26] is N N N (k) (k) ⋅ (k) ̇ (k) (k) ⋅ ̇ (k) (k) �ż = � ċ z = −∇ J + Θ z = −∇ i + Θ z Φ D B k=1 k=1 k=1 = E ⋅ + H ⋅ = −∇ ⋅ (E × H) − I ⋅ E (10) (5) t t t where Φ is the energy density stored in the electro-mag- netic feld, E × H is the Poynting vector of energy fow, I ⋅ E 3 The momentum and energy conservation is the work on matter supplied by the electro-magnetic equations in a CETM open system feld. In I ⋅ E the part i ⋅ E produced by conductive current i is changed to Joule heat [26] and constitutes a part of the 3.1 The momentum conservation equation internal energy, but the part I0 ⋅ E , produced by convective current I0 which moves with the Centroid of medium, is The electromagnetic force f (em) applied on a moving not related to internal energy or Joule heat, but is changed charge is given by Lorentz force law, so the momentum to the kinetic energy of the system (see Eq. 9). equation in CETM system is [23–26] The energy equation in a CETM open system for a vis- cous fuid is ∇ ⋅ + � f (m) + f (em) = �v̇ = �ü , U̇ + K̇ = Ẇ + Q̇ + �̇ + �̇ N (6) (em) (k) (k) (k) 1 ⋅ �f = � z E + v × B = �zE + I × B U̇ = �udV̇ , K̇ = � (v ⋅ v) dV k=1 V V 2 where (k)z(k) E + v(k) × B is the Lorentz force per volume Ẇ = � f (m) + f (em) ⋅ vdV + p ⋅ vda acting on species k , f (m) is the mechanical body force per V a volume, is the stress tensor of a representative element, Q̇ =− q ⋅ nda + (i ⋅ E)dV + −�̇ dV (11) E is electric feld intensity, B is the magnetic induction.
Recommended publications
  • Fundamental Governing Equations of Motion in Consistent Continuum Mechanics

    Fundamental Governing Equations of Motion in Consistent Continuum Mechanics

    Fundamental governing equations of motion in consistent continuum mechanics Ali R. Hadjesfandiari, Gary F. Dargush Department of Mechanical and Aerospace Engineering University at Buffalo, The State University of New York, Buffalo, NY 14260 USA [email protected], [email protected] October 1, 2018 Abstract We investigate the consistency of the fundamental governing equations of motion in continuum mechanics. In the first step, we examine the governing equations for a system of particles, which can be considered as the discrete analog of the continuum. Based on Newton’s third law of action and reaction, there are two vectorial governing equations of motion for a system of particles, the force and moment equations. As is well known, these equations provide the governing equations of motion for infinitesimal elements of matter at each point, consisting of three force equations for translation, and three moment equations for rotation. We also examine the character of other first and second moment equations, which result in non-physical governing equations violating Newton’s third law of action and reaction. Finally, we derive the consistent governing equations of motion in continuum mechanics within the framework of couple stress theory. For completeness, the original couple stress theory and its evolution toward consistent couple stress theory are presented in true tensorial forms. Keywords: Governing equations of motion, Higher moment equations, Couple stress theory, Third order tensors, Newton’s third law of action and reaction 1 1. Introduction The governing equations of motion in continuum mechanics are based on the governing equations for systems of particles, in which the effect of internal forces are cancelled based on Newton’s third law of action and reaction.
  • Hypersonic-Flow Governing Equations with Electromagnetic Fields

    Hypersonic-Flow Governing Equations with Electromagnetic Fields

    Hypersonic-FlowGoverningEquationswith ElectromagneticFields D. Giordano 1 European Space Research & Technology Center P.O. Box 299, 2200 AG Noordwijk, The Netherlands Abstract The paper deals with the formulation of a consistent set of governing equations apt to de- scribe the physical phenomenology comprising the hypersonic flow field of an ionized gas mixture and the electromagnetic field. The governing equations of the flow field and those of the electromagnetic field are revisited in sequence and differences or similarities with past treatments are pointed out and discussed. The equations governing the flow field hinge on the customary balance of masses, momenta and energies. The equations governing the electromagnetic field are introduced both directly in terms of the Maxwell equations and by recourse to the scalar and vector potentials. The theory of linear irreversible thermody- namics based on the entropy-balance equation is also revisited for the purpose of obtaining, consistently with the presence of the electromagnetic field, the phenomenological relations required to bring the governing equations into a mathematically closed form. Old problems, such as the influence of the medium compressibility on chemical-relaxation rates or the im- portance of cross effects among generalized fluxes and forces, are re-discussed; additional problems, such as the necessity to consider the tensorial nature of the transport properties because of the presence of the magnetic field, are pointed out. A non-conventional choice of first-tensorial-order generalized forces and corresponding fluxes is proposed which ap- pears to offer more simplicity and better convenience from a conceptual point of view when compared to alternative definitions customarily used in the literature.
  • Numerical Models of Groundwater Flow and Transport

    Numerical Models of Groundwater Flow and Transport

    4 USE OF NUMERICAL MODELS TO SIMULATE GROUNDWATER FLOW AND TRANSPORT L.F. KONIKOW1 US Geological Survey, Reston, Virginia, USA 4.1 INTRODUCTION In the past, the main driving force for hydrogeologic studies has been the need to assess the water-supply potential of aquifers. During the past 20 years, however, the emphasis has shifted from water-supply problems to water-quality problems. This has driven a need to predict the movement of contaminants through the subsurface environment. One consequence of the change in emphasis has been a shift in perceived priorities for scientific research and data collection. Formerly, the focus was on developing methods to assess and measure the water-yielding properties of high-permeability aquifers. The focus is now largely on transport and dispersion processes, retardation and degradation of chemical contaminants, the effects of heterogeneity on flow paths and travel times, and the ability of low-permeability materials to contain contaminated groundwater. The past 20 years or so have also seen some major technological breakthroughs in groundwater hydrology. One technological growth area has been in the development and use of deterministic, distributed-parameter, computer simulation models for analysing flow and solute transport in groundwater systems. These developments have somewhat paralleled the development and widespread availability of faster, larger memory, more capable, yet less expensive computer systems. Another major technological growth area has been in the application of isotopic analyses to groundwater hydrology, wherein isotopic measurements are being used to help interpret and define groundwater flow paths, ages, recharge areas, leakage, and interactions with surface water (Coplen 1993). Because isotopes move through groundwater systems under the same driving forces and by the same processes as do dissolved chemicals, it is natural that the groundwater flow and solute-transport models applied to groundwater contamination problems be linked to and integrated with isotopic measurements and interpretations.
  • Two-Fluid Formulation of the Cloud-Top Mixing Layer for Direct Numerical

    Two-Fluid Formulation of the Cloud-Top Mixing Layer for Direct Numerical

    Theor. Comput. Fluid Dyn. (2010) 24:511–536 DOI 10.1007/s00162-010-0182-x ORIGINAL ARTICLE Juan Pedro Mellado · Bjorn Stevens · Heiko Schmidt · Norbert Peters Two-fluid formulation of the cloud-top mixing layer for direct numerical simulation Received: 2 April 2009 / Accepted: 19 November 2009 / Published online: 2 February 2010 © The Author(s) 2010. This article is published with open access at Springerlink.com Abstract A mixture fraction formulation to perform direct numerical simulations of a disperse and dilute two-phase system consisting of water liquid and vapor in air in local thermodynamic equilibrium using a two- fluid model is derived and discussed. The goal is to understand the assumptions intrinsic to this simplified but commonly employed approach for the study of two-layer buoyancy reversing systems like the cloud-top mix- ing layer. Emphasis is placed on molecular transport phenomena. In particular, a formulation is proposed that recovers the actual nondiffusive liquid-phase continuum as a limiting case of differential diffusion. High-order numerical schemes suitable for direct numerical simulations in the compressible and Boussinesq limits are described, and simulations are presented to validate the incompressible approach. As expected, the Boussinesq approximation provides an accurate and efficient description of the flow on the scales (of the order of meters) that are considered. Keywords Stratocumulus clouds · Multiphase · Free convection · Free turbulent flows 1 Introduction Phase transition at the cloud boundaries often compounds the difficulty in understanding turbulent entrain- ment [15,21]. There are many different aspects of the problem, which can be considered. One of them, the role of buoyancy reversal due to the evaporative cooling that is promoted by the evaporation of the droplets under certain mixing conditions, has been long debated using theory, field and laboratory measurements, and numerical simulations [7,14,25,28,29,36,46,51,54,61].
  • Theoretical and Numerical Aspects of Modelling Geological Carbon Storage with Application to Muographic Monitoring

    Theoretical and Numerical Aspects of Modelling Geological Carbon Storage with Application to Muographic Monitoring

    Theoretical and Numerical Aspects of Modelling Geological Carbon Storage with Application to Muographic Monitoring Darren L. Lincoln This thesis is submitted for partial consideration towards the degree of Doctor of Philosophy at the The Department of Civil and Structural Engineering at the University of Sheffield December 2015 No flow system is an island. A. Bejan Abstract The storage of waste carbon dioxide (CO2) from fossil fuel combustion in deep geological forma- tions is a strategy component for mitigating harmfully increasing atmospheric concentrations to within safe limits. This is to help prolong the security of fossil fuel based energy systems while cleaner and more sustainable technologies are developed. The work of this thesis is carried out as part of a multi-disciplinary project advancing knowledge on the modelling and monitoring of geological carbon storage/sequestration (GCS). The underlying principles for mathematically describing the multi-physics of multiphase multi- component behaviour in porous media are reviewed with particular interest on their application to modelling GCS. A fully coupled non-isothermal multiphase Biot-type double-porosity formu- lation is derived, where emphasis during derivation is on capturing the coupled hydro-thermo- mechanical (HTM) processes for the purposes of study. The formulated system of governing field equations is discretised in space by considering the standard Galerkin finite element procedure and its spatial refinement in the context of capturing coupled HTM processes within a GCS system. This presents a coupled set of nonlinear first-order ordinary differential equations in time. The system is discretised temporally and solved using an embedded finite difference method which is schemed with control theoretical techniques and an accelerated fixed-point-type procedure.
  • The Heat Transfer Module User's Guide

    The Heat Transfer Module User's Guide

    Heat Transfer Module User’s Guide Heat Transfer Module User’s Guide © 1998–2018 COMSOL Protected by patents listed on www.comsol.com/patents, and U.S. Patents 7,519,518; 7,596,474; 7,623,991; 8,457,932; 8,954,302; 9,098,106; 9,146,652; 9,323,503; 9,372,673; and 9,454,625. Patents pending. This Documentation and the Programs described herein are furnished under the COMSOL Software License Agreement (www.comsol.com/comsol-license-agreement) and may be used or copied only under the terms of the license agreement. COMSOL, the COMSOL logo, COMSOL Multiphysics, COMSOL Desktop, COMSOL Server, and LiveLink are either registered trademarks or trademarks of COMSOL AB. All other trademarks are the property of their respective owners, and COMSOL AB and its subsidiaries and products are not affiliated with, endorsed by, sponsored by, or supported by those trademark owners. For a list of such trademark owners, see www.comsol.com/trademarks. Version: COMSOL 5.4 Contact Information Visit the Contact COMSOL page at www.comsol.com/contact to submit general inquiries, contact Technical Support, or search for an address and phone number. You can also visit the Worldwide Sales Offices page at www.comsol.com/contact/offices for address and contact information. If you need to contact Support, an online request form is located at the COMSOL Access page at www.comsol.com/support/case. Other useful links include: • Support Center: www.comsol.com/support • Product Download: www.comsol.com/product-download • Product Updates: www.comsol.com/support/updates • COMSOL Blog: www.comsol.com/blogs • Discussion Forum: www.comsol.com/community • Events: www.comsol.com/events • COMSOL Video Gallery: www.comsol.com/video • Support Knowledge Base: www.comsol.com/support/knowledgebase Part number: CM020801 Contents Chapter 1: Introduction About the Heat Transfer Module 20 Why Heat Transfer is Important to Modeling .