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A simple chemical engine in steady and dynamic situations

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Języki publikacji
EN
Abstrakty
EN
We transfer to the realm of chemical engines a method of thermodynamic optimization that was developed earlier for thermal machines aimed at maximum production of power. Steady-state model refers to the situation when two reservoirs are infinite, whereas an unsteady model treats a dynamical case with finite upper reservoir and gradually decreasing chemical potential of the active component of fuel. In the considered chemical systems total power output is maximized at constraints which take into account dynamics of mass transport and efficiency of power generation. Methods of dynamic optimization, especially dynamic programming, lead to kinetic limits estimated in form of an optimal function that describes integral power output and extends the reversible chemical work W[rev] to finite rate situations. Optimization results lead to energy limits in chemical systems subject to dissipative effects caused by rates of chemical reaction and transport phenomena. Finite-rate results include irreducible losses caused by mass transfer resistances to the classical work potential. Functions of extremum power, which incorporate a residual minimum of entropy production, are formulated in terms of initial and final states, total duration and (in a discrete process) number of stages.
Rocznik
Strony
57--84
Opis fizyczny
Bibliogr. 16 poz.,Wz., rys., wykr.,
Twórcy
Bibliografia
  • [1] DE VOS, A.: Endoreversible Thermodynamics of Solar Energy Conversion, Clarendon Press, Oxford 1992, 29-51.
  • [2] SIENIUTYCZ S.: Thermodynamic limits for work-assisted and solar assisted mass transfer operations, Archives of Thermodynamics, 22 (2001), 17-36.
  • [3] SIENIUTYCZ S.: Limiting power from imperfect systems with fluid flow, Archives of Thermodynamics 25 (2004) 69-80.
  • [4] SIENIUTYCZ S.: Thermodynamic limits in applications of energy of solar radiation, Drying Technology, 24 (2006) 1139-1146.
  • [5] SIENIUTYCZ S.: Optimal control framework for multistage engines with heat and mass transfer, J. Non-Equilibrium Thermodyn., 24 (1999), 40-74.
  • [6] SIENIUTYCZ S., SZWAST Z.: Practice in Optimization, Wydawnictwa Naukowo Techniczne, Warsaw 1982.
  • [7] SIENIUTYCZ S., FARKAS H.: Variational and Extremum Principles in Macroscopic Systems, Elsevier 2005, 497-522.
  • [8] SIENIUTYCZ S., DE VOS A.: Thermodynamics of Energy Conversion and Transport, Springer N.Y., 2000, 143-172 (Chap.6).
  • [9] SIENIUTYCZ S.: State transformations and Hamiltonian structures for optimal control in discrete systems, Reports on Mathematical Physics, 49, 2006, 289-317.
  • [10] SIENIUTYCZ S.: Nonlinear macrokinetics of heat & mass transfer and chemical or electrochemical reactions, Intern. J. Heat and Mass Transfer, 47 (2004), 515-526.
  • [11] CHEN J., YAN, Z., LIN G, ANDRESEN B.: On the Curzon-Ahlborn efficiency and its connection with the efficiencies of real heat engines, Energy Conversion &; Management, 42 (2001), 173-181.
  • [12] SIENIUTYCZ S.: Hamilton-Jacobi-Bellman equations and dynamic programming for power-maximizing relaxation of radiation, Intern. J. Heat and Mass Transfer, submitted 25 XI 2006, to appear in 2007.
  • [13] SIENIUTYCZ S.: A synthesis of thermodynamic models unifying traditional and work-driven operations with heat and mass exchange, Open Systems & Information Dyn. 10: 31-49, 2003.
  • [14] SIENIUTYCZ S.: Endoreversible modeling and optimization of thermal machines by dynamic programming, Chap. 11 [in:] Recent Advance in Finite Time Thermodynamics (ed. Ch. Wu), Nova Science, New York 1999.
  • [15] SIENIUTYCZ S.: Hamilton-J acobi-Bellman framework for optimal control in multistage energy systems, Physics Reports 326, Elsevier, Amsterdam 2000, 165-285, see Sec.2.3.
  • [16] SIENIUTYCZ S.: Hamilton-Jacobi-Bellman theory of dissipative thermal availability, Physical Review, 56, 1997, 5051-5064.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BGPK-1840-7049
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