Contents 1. Introduction 9. Liquid Handling 2. Fluids 10.Microarrays 3. Physics of Microfluidic Systems 11.Microreactors 12.Analytical Chips 4. Microfabrication Technologies Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 13.Particle-Laden Fluids 5. Flow Control a. Measurement Techniques 6. Micropumps 7. Sensors b. Fundamentals of Biotechnology 8. Ink-Jet Technology c. High-Throughput Screening Microfluidics - Jens Ducrée Fluids: Thermodynamics 1 2. Fluids 1. General Characteristics 2. Dispersions 3. Thermodynamics 4. Transport Phenomena 5. Solutions 6. Surface Tension Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 7. Electrical Properties 8. Optical Properties 9. Biological Fluids Microfluidics - Jens Ducrée Fluids: Thermodynamics 2 2.3. Thermodynamics 1. Heat and Temperature 2. Heat Capacity 3. Chemical Potentials 4. Kinetic Theory of Gases 5. Compressibility 6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 7. Real Gases 8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 3 2.3.1. Heat and Temperature Thermal energy per molecule In thermal equilibrium Number of degrees of freedom f Boltzmann constant Heating 1 mole of ideal gas by 1 K consumes 4.16 J per DoF Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Three translational DoFs Microfluidics - Jens Ducrée Fluids: Thermodynamics 4 2.3.1. Heat and Temperature Mean kinetic energy Combination yields for mean (random, thermal) velocity Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Microfluidics - Jens Ducrée Fluids: Thermodynamics 5 2.3. Thermodynamics 1. Heat and Temperature 2. Heat Capacity 3. Chemical Potentials 4. Kinetic Theory of Gases 5. Compressibility 6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 7. Real Gases 8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 6 2.3.2. Heat Capacity Raising temperature of N particles by T takes energy Heat capacity Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Specific heat capacity Molar heat capacity Microfluidics - Jens Ducrée Fluids: Thermodynamics 7 2.3. Thermodynamics 1. Heat and Temperature 2. Heat Capacity 3. Chemical Potentials 4. Kinetic Theory of Gases 5. Compressibility 6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 7. Real Gases 8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 8 2.3.3. Internal Energy Internal energy U State property Conservation of energy Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Amount of transferred heat Q - Q > 0: heat absorbed by system (Expansion) work W = p V - W > 0: system delivers work, i.e. system spends energy Microfluidics - Jens Ducrée Fluids: Thermodynamics 9 2.3.3. Enthalpy Enthalpy (state property) Chemical reactions normally at constant p Heat energy absorbed or released to system at constant p Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Transferred heat Qp= change in enthalpy No volumetric expansion - Transferred heat = change in internal energy Example: Microfluidics - Jens Ducrée Fluids: Thermodynamics 10 2.3.3. Entropy Entropy Probability Wprob of finding system in given state Entropy of „universe“ Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Entropy of environment Senv Entropy of system under investigation S Stot constantly grows Microfluidics - Jens Ducrée Fluids: Thermodynamics 11 2.3.3. Gibbs Free Enthalpy Processes at constant T and p Typical for chemical reactions Can process occur spontaneously? Gibbs free enthalpy G = H - TS Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el G < 0 for spontaneous process Decrease in enthalpy H Increase in entropy S High temperature T Microfluidics - Jens Ducrée Fluids: Thermodynamics 12 2.3. Thermodynamics 1. Heat and Temperature 2. Heat Capacity 3. Chemical Potentials 4. Kinetic Theory of Gases 5. Compressibility 6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 7. Real Gases 8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 13 2.3.4. Kinetic Theory of Gases Gas Pressure Force perpendicular to surface A Scalar Isotropic Units Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 1 Pa = 1 N m-2 1 Torr (= mm Hg) = 133.4 Pa 1 mbar = 1 hPa 1 psi = 6897 Pa Standard pressure 1 atm = 1013 hPa = 1013 mbar = =760 Torr = 14.7 psi Microfluidics - Jens Ducrée Fluids: Thermodynamics 14 2.3.4. Kinetic Theory of Gases Molecular picture Particle density: N / V Only particles in defined sub-volume (A x v x t ) have chance to hit wall within given time t 1/3 of velocity vectors statistically perpendicular to surface A 1/2 of them pointing towards wall Number of collisions (N / V ) x ( A x v x t ) / 6 Each particle transfers twice its momentum: 2 x mv = F t Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el v t Microfluidics - Jens Ducrée Fluids: Thermodynamics 15 2.3.4. Kinetic Theory of Gases Bernoulli equation By replacing v² with v² (mean square velocity) Substitute v² by thermal velocity Equation of state for ideal gas Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el particles moles # molecules N # moles n Gas constant Rg = 8.31 J K-1 mol-1 Microfluidics - Jens Ducrée Fluids: Thermodynamics 16 2.3.4. Kinetic Theory of Gases (Trivial) conclusions from equation of state Law of Boyle-Mariotte Law of Gay-Lussac Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Law of Charles Microfluidics - Jens Ducrée Fluids: Thermodynamics 17 2.3.4. CV and Cp for Gases Heat capacity of gases At constant volume - CV = ½ f N kB At constant pressure - Volumetric expansion associated with mechanical work Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el heat mech. work Equivalence of thermal and mechanical energy 1 cal = 4.18 J 1842: Robert Mayer and J. P. Joule Microfluidics - Jens Ducrée Fluids: Thermodynamics 18 2.3.4. Adiabatic Change of Condition Adiabatic process No exchange of thermal energy Q = 0 E.g., under thermal insulation U = – W Complete conversion (internal) heat pneumatic work Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Insertion of equation of state and CV CV = ½ f N kB Microfluidics - Jens Ducrée Fluids: Thermodynamics 19 2.3.4. Adiabatic Change of Condition Relationship for adiabatic process „non-adiabatic“ gas laws Adiabatic coefficient Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Poisson equations Compare to „non-adiabatic“ gas laws Microfluidics - Jens Ducrée Fluids: Thermodynamics 20 2.3.4. Mean Free Path Collisional cross section for given gas Mean free path scales with Inverse of particle density Inverse of collisional cross-section of particles Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el thermal motion of targets Example: H2 at p = 1013 hPa lmfp = 270 nm Microfluidics - Jens Ducrée Fluids: Thermodynamics 21 2.3. Thermodynamics 2.3.1. Heat and Temperature 2.3.2. Heat Capacity 2.3.3. Chemical Potentials 2.3.4. Kinetic Theory of Gases 2.3.5. Compressibility 2.3.6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 2.3.7. Real Gases 2.3.8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 22 2.3.5. Compressibility Compressibility of fluids Isothermal compressibility for ideal gas Bulk modulus Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el p V = const. Differentiation of modified (adiabatic) law of Boyle-Mariotte Adiabatic compressibility Microfluidics - Jens Ducrée Fluids: Thermodynamics 23 2.3.5. Compressibility Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Microfluidics - Jens Ducrée Fluids: Thermodynamics 24 2.3. Thermodynamics 2.3.1. Heat and Temperature 2.3.2. Heat Capacity 2.3.3. Chemical Potentials 2.3.4. Kinetic Theory of Gases 2.3.5. Compressibility 2.3.6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 2.3.7. Real Gases 2.3.8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 25 2.3.6. Thermal Expansion Thermal expansion coefficient Derivation from equation of state for (ideal) gases Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Expansion of cube Linear approximation Microfluidics - Jens Ducrée Fluids: Thermodynamics 26 2.3.6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Microfluidics - Jens Ducrée Fluids: Thermodynamics 27 2.3. Thermodynamics 2.3.1. Heat and Temperature 2.3.2. Heat Capacity 2.3.3. Chemical Potentials 2.3.4. Kinetic Theory of Gases 2.3.5. Compressibility 2.3.6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 2.3.7. Real Gases 2.3.8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 28 2.3.7. Real Gases Van-der-Waals equation Volume per mole Vn „Internal pressure“ a/Vn² - Attractive forces between molecules Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Parameter for strength of interaction a Covolume b - Spatial extension of molecules subtracted from overall volume - At low pressures negligible due to large volume per mole Vn Joule-Thomson effect Change in temperature during rapid expansion Work against intermolecular forces Microfluidics - Jens Ducrée Fluids: Thermodynamics 29 2.3. Thermodynamics 2.3.1. Heat and Temperature 2.3.2. Heat Capacity 2.3.3. Chemical Potentials 2.3.4. Kinetic Theory of Gases 2.3.5. Compressibility 2.3.6. Thermal Expansion Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el 2.3.7. Real Gases 2.3.8. Vapor Pressure Microfluidics - Jens Ducrée Fluids: Thermodynamics 30 2.3.8. Vapor Pressure Coexistence of liquid and gaseous state Closed vessel Vapor forms above liquid Saturated vapor pressure Boiling Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Standard Pressure Temperature dependence Boiling Microfluidics - Jens Ducrée Fluids: Thermodynamics 31 2.3.8. Vapor Pressure Vapor pressure curve Coexistence of liquid and vapor Restricted to 1-dimensional curve - Above only vapor - Below only liquid Critical point Phases „converge“ Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Microfluidics - Jens Ducrée Fluids: Thermodynamics 32 2.3.8. Vapor Pressure Absolute humidity abs Concentration of mass, measured in g / m3 Relation to partial pressure of water pwater - Mass of water molecule mwater Relative humidity rel referred to abs at saturation Pr isbexa ispel: Ausar beitun gspha Au tsarbei ungde rStand ard-Ze el Heat of vaporization E per mass to „escape“ liquid phase Equation of Clausius and Clapeyron Temperature T Derivative of vapor pressure curve dp / dT Difference between specific volumes Vm Microfluidics - Jens Ducrée Fluids: Thermodynamics 33