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BASICS OF THERMODYNAMICS OF LIVING

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1 BASICS OF THERMODYNAMICS OF LIVING
SYSTEMS

2

3 Thermodynamics deals with mutual conversion of
different types of energy, the direction of physical and chemical processes and of equilibria. It also studies systems composed of many parts. As a system we consider any region of space separated from its surroundings

4 isolated – do not exchange matter or energy with
According to the interaction of the system with its surroundings we discriminate systems: isolated – do not exchange matter or energy with surroundings closed – exchange only energy with surroundings, not matter open – exchange both matter and energy with

5 extensive parameters – characterize thermodynamic
Thermodynamics studies two types of parameters: extensive parameters – characterize thermodynamic system as a whole (mass, volume, total electric charge) intensive parameters – they have different values in different parts of the system (concentration of chemical components, temperature, electrical potential) The studies of the relationship between extensive and intensive parameters create the basis for the formulation of thermodynamic laws.

6 The basic laws of thermodynamics are: law of conservation of mass
I. law of thermodynamics II. law of thermodynamics III. law of thermodynamics

7 I. law of thermodynamics
If a system is doing a work or the surroundings is doing a work on the system, its internal state is changed. E.g. if we compress a gas in a cylinder with a piston the temperature of the gas increases. Similarly, if there is a chemical reaction between the components of the system, its temperature changes. Or, if you consider an iceberg moving on rocky surface, the friction produces heat and the iceberg changes its phase – it melts. The cause producing the change of the state is called energy. Energy can be thus defined as the ability to change given (equilibrium) state of matter.

8 principle of energy conservation.
Initial experimets indicated an equivalence between heat and mechanical work (the work produces heat and heat can be used to do a work) This studies led to the formulation of principle of energy conservation. This principle can be formulated in different ways, e.g.: It is not possible to construct a machine generating energy from nothing. That means it is not possible to produce a perpetuum mobile of the first kind. In a more general formulation: The total energy of isolated system is constant during all processes.

9 the initial and final state of the system, and not on
So we can expres the I. law of thermodynamics in this way The total energy that a system exchanges with surroundings in any process is dependent only on the initial and final state of the system, and not on the way this change was achieved. This means there is an energetic function, whose difference between initial and final state corresponds to energy exchanged between the system and surroundings. This function is called inner energy of the system and is labelled as U. ΔU = U2 - U1 = q - w here q indicates heat accepted by the system from surroundings, w is a work done by the system, indexes 1 a 2 indicate initial and final state of the system

10 The I. law of thermodynamics implies that total heat
released in a chemical reaction will be the same if the reaction proceeds in one step or in more steps. E.g. the amount of heat released during reaction: C + O2 = CO2 equals the sum of heat produced in the following reactions: C + 1/2O2 = CO CO + 1/2O2 = CO2

11 This conclusion is known as the Hess law.
Now we can introduce new thermodynamic function. It is called enthalpy, labeled H, and defined by an equation: H = U + PV where P is pressure and V volume of the system

12 Now we can calculate the amount of heat released in
the system under constant pressure: qP = H2 - H1 = ΔH This expression says that the change of enthalpy in any process is dependent only on the initial and final state of the system. In the case of chemical reaction it is the state of the reactants at the beginning of the reaction and the state of products in the end of the reaction.

13 Reaction heat is the amount of heat exchanged by the
system with surroundings during the chemical reaction. If the heat is released we speak of an exothermic process, if the heat is consumed by the system, it is referred to as endothermic process. If the reaction proceeds under constant volume, the reaction heat corresponds to the change of inner energy of the system. If the reaction proceeds under constant pressure, the reaction heat corresponds to the change of enthalpy.

14 II. law of thermodynamics
By the beginning of 19th century Carnot studied the efficiency of heat machines. He created a concept of cyclically working heat machine, in which the volume in the cylinder was changed by interaction with two heat exchangers having different temperature. Theoretical work out of this concept led to the formulation of the theorem: All the reversible machines working between the same heat exchangers have the same efficiency in spite of the composition of the exchangers.

15 Related formulation was stated by Clausius:
It is not possible to construct an equipment that would do nothing else than transfer heat from the colder body to a warmer body. This implies that it is not possible to create the so called perpetuum mobile of the second kind. These formulations are the expressions of the II. law of thermodynamics

16 The studies of the efficiency of heat engines revealed
the existence of a new state function called entropy labeled S dS = dq/T (4) According to Carnot theorem the efficiency of reversible machine is maximum. Thus, the irreversible machines have always lower efficiency. For the irreversible process we get: dS > dq /T (5)

17 If the system does not exchange heat with surroundings
we get for irreversible process: dS > (6) and for reversible process: dS = (7) It means that entropy is growing under irreversible processes and in equilibrium, when only reversible processes can proceed, it does not change. Entropy can be looked upon as a measure of spontaneousness, as it increases during spontaneous processes.

18 Energy functions F and G
For the case of reversible process we get from the I. law of thermodynamics: dU = dqrev - dwrev For dqrev we substitute from the definition of entropyTdS: dU = TdS - dwrev From this equation we can deduce that work done by the system under reversible conditions can be expressed using basic thermodynamic parameters T, U, S.

19 We can substitute for TdS :
TdS = d(TS) - SdT In the case of a process under constant temperature dT = 0 and TdS = d(TS), and the equation can be rewritten dU - d(TS) = d(U - TS) = -dwrev   For a finite change we get: Δ(U - TS) = -dwrev

20 It is evident there is a state function (U - TS),
the decrease of which indicates maximum (i.e. reversible) work that the system can do under constant temperature. It is known as Helmholtz function and labelled F: F = U - TS

21 dU - d(TS) + d(PV) = d(U - TS + PV) = -dw,rev
We can discern between volume work wvol (wobj = PdV) and an useful work w,rev, comprising all other kinds of work (electrical, transport, etc.) Then we can rewrite the equation: dU = TdS - PdV - dw,rev In the case that in the system proceeds reversible process under constant pressure and temperature, we have: dT = 0, TdS = d(TS) dP = 0, PdV = d(PV) Substituting in the above equation we get: dU - d(TS) + d(PV) = d(U - TS + PV) = -dw,rev

22 And for the finite change:
Δ(U - TS + PV) = -w,rev We can see another state function (U - TS + PV), the decrease of which indicates maximum useful work that can be done by the system under constant pressure and temperature. It is called Gibbs function and labeled G: G = U + PV - TS = H - TS

23 III. law of thermodynamics
The formulation was developing in time. As a definitive version is considered the formulation by Planck from 1912: Entropy of every chemically homogenous condensed phase approaches with decreasing temperature zero.  Another formulation explains it more clearly: It is not possible to cool a physical body to absolute zero in a finite number of steps.

24 Changes of entropy in living systems
For the description of internal processes in the system we consider the states of the system as a whole. Equilibrium state is reached by a system that is isolated from surroundings and let suficient time to evolve until it is not changing any more. This final state will correspond to the most probable arrangement, characterized by the highest degree of disorganization, when entropy reaches its maximum value.

25 Chemical reactions are characterized by equilibrium
constant K, which describes the composition of the reaction mixture under situation when the reaction rate from left to right equals the rate from right to left. For the change of Gibbs function in equilibrium state we obtain: - ΔG = RT ln K.

26 Living systems are open systems. In the living biological
system taken as a whole we can not expect thermodynamic equilibrium, as the system in equilibrium can not do work. However, the ability to do work is essential for the maintenance of living functions. Open systems are able to generate certain stationary state, under which the parameters of the system preserve constant levels of exchange of matter and energy with surroundings.

27 The total entropy of an open system can be changed
either due to exchange with external surroundings deS, or due to internal processes in the system diS: dS = deS + diS For the rate of entropy change we obtain: dS/dt = deS/dt + diS/dt deS/dt corresponds to the exchange of entropy between the system and surroundings and it can reach both positive and negative values, diS/dt is only positive.

28 dS/dt = deS/dt + diS/dt = 0 If we rewrite this equation:
Under stationary state the rate of entropy production is constant, thus dS/dt = 0, and therefore│deS/dt│ = diS/dt dS/dt = deS/dt + diS/dt = 0 If we rewrite this equation: dS/dt + (-deS/dt) = diS/dt We can express it in words: Under stationary state the sum of the rate of entropy production in the system and the rate of emerging entropy from the system equals the rate of entropy production inside the system.

29 Development and growth of organisms is accompanied by
an increase in the complexity of their organization. From the point of view of classical thermodynamics it appears as spontaneous decreasing of entropy of living systems, which is evidently in contradiction with II. law of thermodynamics. However, the decrease of the total entropy of living organisms appears under conditions of  deS/dt < 0 and │deS/dt│ > diS/dt. It means that the decrease in entropy inside the living system runs at the expense of increased entropy in the surroundings.

30 dS = dqrev/T + diS Let us consider open system in equilibrium under
constant temperature and pressure with no irreversible processes running, such as heat transfer etc. In such a system entropy increases only as the result of chemical reactions, mass transfer between phases of the system and generally in processes characterized by a change of chemical potential. We shall consider the heat exchange to proceed only by reversible processes and then we get for entropy change: dS = dqrev/T + diS

31 diS = - dG/T We can calculate the entropy production inside the system
diS = dS - dqrev /T and after aritmetical rearrangement we get: diS = - dG/T That can be expressed in words: The increase in entropy of open system due to internal nonequilibrium processes is proportional to the decrease of the Gibbs function of the system.

32 If we will study the changes of the state parameters in
chemical reactions, when changes in the number of moles appear, we obtain expressions for the chemical potential μ: (dU/dni)S,V = (μi)S,V (dH/dni)S,P = (μi)S,P (dG/dni)T,P = (μi)T,P (dF/dni)T,V = (μi)T,V Concomitantly: (μi)S,V = (μi)S,P = (μi)T,P = (μi)T,V = μi

33 The relationship between entropy increase, decrease of
Gibbs energy, change in composition and in chemical potentials in open system can be expressed like this: diS = - dG/T = - 1/T Σ μidni diS/dt = - 1/T (dG/dt) = - 1/T Σ μi (dni/dt)

34 The reaction rate is given: v = 1/ υi (dni/dt)
dni = υi dλ and dλ = 1/ υi dni The reaction rate is given: v = 1/ υi (dni/dt) After substituting for dni we get: v = dλ/dt For the change of mols of reacting substance we get: dni/dt = υi v = υi (dλ/dt)

35 diS/dt = - 1/T Σ μi υi (dλ/dt) = - 1/T Σ μi υi v
And we obtain expression for the increase of entropy in the system: diS/dt = - 1/T Σ μi υi (dλ/dt) = - 1/T Σ μi υi v As the reaction rate is equal for all components i, we get: diS/dt = - 1/T (v) Σ μi υi we introduce: W = - Σ μi υi = (dG/ dλ)T,P which represents work done by the system after all reactions run through

36 and for the rate of entropy production we get:
diS/dt = Wv/T This can be expressed in words: the rate of entropy production in open system under constant temperature and pressure is given by product of reaction rate and the work done by the system.

37 Now we introduce expression for the rate of entropy
production in unit volume: Θ = 1/V (dS/dt) and function Ψ: Ψ = T Θ The functionΨ is proportional to the rate of entropy in unit volume and is called dissipative function

38 We can rewrite it in general expression:
Ψ = T Θ = Σ Ji Xi > 0 where Ji rate of flux of the process Xi driving force of the process Ψ depends on the rate of flux and driving force of the process, which are time-dependent parameters, therefore Ψ is also a function of time: Ψ(t) = Σ Ji(t) Xi(t)

39 In equilibrium X equals J, as it holds under equilibrium
that X = 0, J = 0. We can thus assume that close to equilibrium there is a linear relationship between fluxes and forces and flux is a function of force: J = J(X) and it holds: J(X) = L(X) This equation represents linear phenomenological relationship between the parameters of generalized fluxes and forces, and the coefficient L is called linear phenomenological coefficient

40 If we have a linear system close to equlibrium, we can write
expression for the rate of entropy production in the system: diS/dt = 1/T Σ Jj Xj > 0 In agreement with II. law of thermodynamics this change must be positive. Although the overall sum must be positive, inside system can proceed one ore more processes for which we can write: diS'/dt = 1/T Σ Jk Xk ≤ 0 i.e. there are processes during which the entropy of the system decreases

41 These conclusions in such a simple form holds true
only for linear relationships close to equilibrium. Living systems, however, are nonlinear systems far from equilibrium, in which irreversible processes proceed.

42 In agreement with II. law of thermodynamics any
irreversible process is accompanied by heat of dissipation. In open system it is possible that this heat leaves the system and the total entropy of the system stayes constant, or even decreases. We can write for the rate of entropy production in non- linear systems: dS/dt = deS/dt + diSn/dt + diSd/dt where diSn/dt part of entropy production bound in the system diSd/dt part of entropy production crossing the boundaries of the system

43 Analogicaly with the preceding situation we have
function Ψ: Ψ = Ψn + Ψd where Ψn function of bound dissipation Ψd function of outer dissipation According to the principle of the least outer dissipation of energy: In the stationary state of any thermodynamics system, the function of outer dissipation reaches the least possible values. 

44 Physiology has been using long time the term, which is very close to the concept of the stationary state in the thermodynamics of irreversible processes. It is basal metabolism. Basal metabolism measured as the rate of heat production or breathing represents the lowest metabolism of an animal in rest. It is thus characterized by minimal rate of heat production (minimum of the function of outer dissipation of energy), that corresponds the concept of stationary state.

45 The stationary state of living systems differs from the
stationary state of sipmple physical-chemical systems. This difference consists in the fact, that in the simple systems the stationary state is given by the outer parameters and stayes stable only under maintained outer conditions. On the other hand, living systems are able to resist the changes of the outer environment by means of regulation and control of the inner processes. Thus to describe the stationary state of living systems it is more appropriate to use the term homeostasis, introduced by Cannon.

46 As homeostasis we describe the ability of living organisms
to maintain the stability of inner medium during occurence of random changes in the outer environment. Living organisms are, from the point of view of thermodynamics, open systems far away from thermodynamic equilibrium. They are controlled and regulated. Exact thermodynamic theory of such systems has not been created yet.


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