SlideShare a Scribd company logo
1 of 36
A detailed approach
Presented by
ο‚— Ahmed Asad – CIIT/SP10-BEC-003/LHR

ο‚— Muhammad Usama – CIIT/SP10-BEC-017/LHR

ο‚— Mohammad Abubakar – CIIT/SP10-BEC-022/LHR

ο‚— Noaman Ahmed – CIIT/SP10-BEC-037/LHR

ο‚— Saad Wazir – CIIT/SP10-BEC-043/LHR

ο‚— Saim Khan – CIIT/SP10-BEC-044/LHR

ο‚— Waqar Farooq – CIIT/SP10-BEC-050/LHR
Presentation Outline
ο‚— Restatement of first law of thermodynamics
ο‚— Definition of enthalpy
ο‚— Some common enthalpy changes
ο‚— Enthalpy of vaporization
ο‚— Characteristics of enthalpy of vaporization
ο‚— Physical model for vaporization
ο‚— Experimental determination
ο‚— Sample readings and calculations
ο‚— Applications
First Law of Thermodynamics
ο‚— Energy conservation law


ο‚— Describeschange in         internal   energy    of   a
 thermodynamic system

ο‚— Clausius’ statement: In a thermodynamic process, the
 increment in the internal energy of a system is equal to
 the difference between the increment of heat
 accumulated by the system and the increment of work
 done by it.
First Law of Thermodynamics (contd.)
ο‚— In any incremental process, the change in the internal
 energy is considered due to,

  ο‚— Heat added to the system
  ο‚— Work done by the system


                     dU = dQ - dW
First Law of Thermodynamics (contd.)
ο‚— For a quasistatic process (infinitely slow process),

                         dU = dQ – PdV

ο‚— NO real process is quasistatic

ο‚— A quasistatic process ensures that the system will go
  through a sequence of states that are infinitesimally close
  to equilibrium (so the system remains in quasistatic
  equilibrium), in which case the process is typically
  reversible
Quasistatic and Reversibility
ο‚— Any reversible process is a quasistatic process


ο‚— Any quasistatic process may not be reversible
   ο‚— Due to heat flow
   ο‚— Due to entropy generation


ο‚— Example of an irreversible quasistatic process
   ο‚— Compression against a system with a piston subject to
     friction
Enthalpy
ο‚— Measure of total energy of a thermodynamic system

ο‚— A state function

ο‚— Includes
   ο‚— Internal energy (energy required to create a system)
   ο‚— Amount of energy required to establish system’s pressure and
     volume

                         Ξ”H = Ξ”U + Ξ”(PV)

ο‚— SI Unit – Joule
ο‚— Other conventional units – Btu and Calories
Why Enthalpy is measured?
ο‚— Total enthalpy of a system can’t be measured directly

ο‚— Enthalpy change of a system is measured instead

ο‚— It is measured to,

  ο‚— Calculate β€œuseful work” obtainable from a closed
    thermodynamic system under constant pressure
  ο‚— Determine nature of reaction e.g., exothermic or
    endothermic
Enthalpy is not necessarily heat !!
ο‚— Enthalpy is sometimes described as heat content of a
  system

ο‚— Heat is defined as thermal energy in transit


ο‚— For the description that enthalpy is in-fact heat to be
  valid, no energy exchange must occur with
  environment other than heat or expansion work
Common Enthalpy Changes
ο‚— Enthalpy of reaction

ο‚— Enthalpy of formation

ο‚— Enthalpy of combustion

ο‚— Enthalpy of neutralization

ο‚— Enthalpy of solution

ο‚— Enthalpy of vaporization

ο‚— Enthalpy of sublimation
Vaporization
ο‚— Phase transition from liquid phase to gas phase

ο‚— Two types

  ο‚— Evaporation
    ο‚— Occurs at temperatures below boiling temperature
    ο‚— Usually occurs on surface



  ο‚— Boiling
    ο‚— Occurs at or above boiling temperature
    ο‚— Occurs below the surface
Enthalpy of Vaporization (EOV)
ο‚— Enthalpy change required to completely change the
 state of one mole of substance between liquid and
 gaseous states

ο‚— Energy required to transform a given quantity of a
 substance from a liquid into a gas at a given pressure

ο‚— Usually measured at boiling point of a substance
Characteristics of Enthalpy of
Vaporization
ο‚— It is temperature dependent

ο‚— EOV decreases with increase in temperature

ο‚— EOV diminishes completely at critical temperature
 beyond which liquid and vapor phase no longer co-
 exist

ο‚— Units – J/mol or kJ/mol, kJ/kg, Btu/lb, kcal/mol
Characteristics of Enthalpy of
Vaporization (contd.)
ο‚— Enthalpy of condensation is same as enthalpy of
 vaporization but with opposite sign

ο‚— Enthalpy change of vaporization is always positive


ο‚— Enthalpy change of condensation is always negative
Temperature dependence of EOV
Physical model for vaporization
ο‚— Proposed by professor Jozsef Garai, Florida International
  University, USA

ο‚— Energy required to free an atom from liquid is equivalent to
  energy required to overcome surface resistance of liquid

ο‚— This model states,


Latent heat = (Max. surface area) x (Surface tension) x (No. of
                       atoms in liquid)
Physical model for vaporization
(Diagrammatic representation)
Experimental determination
Apparatus
ο‚— Round bottom boiling flask

ο‚— Distillation condenser or multiple condensers

ο‚— Heat source (a burner or a heating mantle)

ο‚— A vacuum gauge (Bourdon type gauge)

ο‚— Aspirator or trapped vacuum pump

ο‚— Pressure-regulating device (a needle valve that is part of a Bunsen
  burner base)

ο‚— Thermometer
Basic Goal
ο‚— To determine boiling point of the liquid (water) under
 study at different pressure values

ο‚— To determine enthalpy of vaporization using the
 Clausius-Clapeyron relation
Clausius-Clapeyron relation
ο‚— A relation used to characterize a discontinuous phase
  transition between two phases of a single constituent

ο‚— On a P-T diagram, line separating two phases is known
  as coexistence curve

ο‚— This relation gives the slope of the tangents to this
  curve
Clausius-Clapeyron relation (contd.)
ο‚— General form
                        dP/dT = L/TΞ”V
  ο‚— Where
    ο‚— dP/dT is slope of tangent to coexistence curve at any point
    ο‚— L is latent specific heat
    ο‚— T is temperature
    ο‚— Ξ”V is specific volume change of phase transition



ο‚— For transitions between a gas and condensed
 phase, the expression may be rewritten as,
               ln(P) = (-L/R) x (1/T) + C
Procedure
ο‚— Maintain lowest possible pressure by closing bleed
 valve

ο‚— Set water flow to the aspirator at maximum level to
 provide highest vacuum

ο‚— Place few boiling stones in round bottom flask to
 minimize bumping
Procedure (contd.)
ο‚— Temperature increases until boiling starts


ο‚— When boiling occurs, allow the thermometer reading
 to stabilize for 1 to 2 minutes and note the temperature

ο‚— Note the pressure reading on the manometer at this
 temperature
Procedure (contd.)
ο‚— Increase the pressure of the vessel by slightly opening
 the bleed valve

ο‚— Repeat the same procedure as described previously
 and then increase pressure again

ο‚— Take at least five readings and plot a graph between
 reciprocal of temperature and log of pressure
 difference
Sample Readings

Temp (Β°C)   h (mm Hg)    Temp (K)    (1/T) x 103   P (mm Hg)         Log P
                                        (1/K)      (P = 768 –h)

41.5        710         314.5       3.18           58.0           1.77
62.5        610         335.2       2.98           158            2.20
75.0        500         348.0       2.87           268            2.43
86.5        300         359.5       2.78           468            2.67
92.2        220         365.2       2.74           548            2.74
101.0       0           374.0       2.67           768            2.89
Graph between temperature and
pressure
                                Temperature and Log P
        3.5


         3


        2.5


         2
Log P




        1.5


          1


        0.5


         0
              2.6   2.7   2.8          2.9               3   3.1   3.2   3.3
                                             1/T x 103
Calculations
ο‚— Molar latent heat / enthalpy of vaporization can be calculated
  from Clausius-Clapeyron relation as follows,

                       Ξ”Hv = -Rx[d(ln(P))/d(1/T)]]

                          ln(P) = 2.303 log(P)

                      Slope = m = d(ln(P))/d(1/T)

                    Ξ”Hv = -2.303(R)(m) - - - - Eq. (1)
   ο‚— Where R is ideal gas constant = 1.987 cal/K
   ο‚— m is slope of line obtained from graph
Calculations (contd.)
ο‚— Slope (m) can be obtained from linear regression


ο‚— A convenient method is to draw a trend-line on the graph
  and select the option to display an equation of line

ο‚— The equation of line of the sample experiment graph is,


                      y = -2.233x+8.859

ο‚— From equation, value of slope (m) = -2.233
Calculations (contd.)
ο‚— Applying values in equation 1 from previous slide

                   Ξ”Hv = 10.21 cal/mol

ο‚— Accepted value for water is 9.72 cal/mol

ο‚— Deviation is 4.79 %

ο‚— Results  obtained from this experiment seldom
 increase 5% deviation from expected value
Applications
ο‚— Major application in conversion of water into steam

ο‚— Steam is used in

  ο‚— Power generation (steam turbines)
  ο‚— Agriculture
  ο‚— Energy storage
  ο‚— Wood treatment
  ο‚— Cleaning purposes
  ο‚— Sterilization
Applications (contd.)
ο‚— Distillation


ο‚— Vapor Pressure Calculations
References
ο‚— http://en.wikipedia.org/wiki/First_law_of_thermodyn
 amics

ο‚— http://en.wikipedia.org/wiki/Quasistatic_process


ο‚— http://en.wikipedia.org/wiki/Enthalpy


ο‚— http://en.wikipedia.org/wiki/Clausius-
 Clapeyron_relation
References
ο‚— http://en.wikipedia.org/wiki/Enthalpy_of_vaporizatio
 n

ο‚— http://www.sciencedirect.com/science/article/pii/S03
 78381209002180

ο‚— http://www2.selu.edu/Academics/Faculty/delbers/He
 at%20of%20vaporization.htm
QUESTIONS
ARE
WELCOMED !!

More Related Content

What's hot (20)

vapour pressure
vapour pressurevapour pressure
vapour pressure
Β 
Phase Equilibrium
Phase EquilibriumPhase Equilibrium
Phase Equilibrium
Β 
Vapor pressure concept
Vapor pressure conceptVapor pressure concept
Vapor pressure concept
Β 
Phase diagram
Phase diagramPhase diagram
Phase diagram
Β 
Thermodynamics and Heat Transfer
Thermodynamics and Heat TransferThermodynamics and Heat Transfer
Thermodynamics and Heat Transfer
Β 
Zeroth law of thermodynamics
Zeroth law of thermodynamicsZeroth law of thermodynamics
Zeroth law of thermodynamics
Β 
Second law of thermodynamics
Second law of thermodynamicsSecond law of thermodynamics
Second law of thermodynamics
Β 
Thermodynamic notes 2
Thermodynamic notes 2Thermodynamic notes 2
Thermodynamic notes 2
Β 
First law of thermodynamics
First law of thermodynamicsFirst law of thermodynamics
First law of thermodynamics
Β 
Unit 1 thermodynamic process
Unit  1 thermodynamic processUnit  1 thermodynamic process
Unit 1 thermodynamic process
Β 
3.3 the ideal gas
3.3 the ideal gas3.3 the ideal gas
3.3 the ideal gas
Β 
DISTILLATION
DISTILLATIONDISTILLATION
DISTILLATION
Β 
Lecture 4 (b) Reversible and Irreversible processes.pptx
Lecture 4 (b) Reversible and Irreversible processes.pptxLecture 4 (b) Reversible and Irreversible processes.pptx
Lecture 4 (b) Reversible and Irreversible processes.pptx
Β 
Heat Lecture Slides
Heat Lecture SlidesHeat Lecture Slides
Heat Lecture Slides
Β 
Convective mass transfer
Convective mass transferConvective mass transfer
Convective mass transfer
Β 
Thermodynamics
ThermodynamicsThermodynamics
Thermodynamics
Β 
Phase equilibrium
Phase equilibriumPhase equilibrium
Phase equilibrium
Β 
Distillation
DistillationDistillation
Distillation
Β 
Thermodynamic lecture
Thermodynamic lectureThermodynamic lecture
Thermodynamic lecture
Β 
02 part5 energy balance
02 part5 energy balance02 part5 energy balance
02 part5 energy balance
Β 

Viewers also liked

Properties of Matter
Properties of MatterProperties of Matter
Properties of Mattermakaberokurota
Β 
Detection and analysis of pesticides pollution
Detection and analysis of pesticides pollutionDetection and analysis of pesticides pollution
Detection and analysis of pesticides pollutionrobinson casimir
Β 
Colligative Properties
Colligative PropertiesColligative Properties
Colligative Propertiesmrsnbrite
Β 
Solutions
SolutionsSolutions
Solutionsprakrsinha
Β 
Chapter 17.1 : Thermochemistry
Chapter 17.1 : ThermochemistryChapter 17.1 : Thermochemistry
Chapter 17.1 : ThermochemistryChris Foltz
Β 
Liquefaction and liquefaction potential
Liquefaction and liquefaction potentialLiquefaction and liquefaction potential
Liquefaction and liquefaction potentialMahesh Raj Bhatt
Β 
Thermochemistry
ThermochemistryThermochemistry
Thermochemistrysweemoi khor
Β 
The Kinetic Molecular Theory
The Kinetic Molecular TheoryThe Kinetic Molecular Theory
The Kinetic Molecular Theorywalt sautter
Β 
SPM Form 4 Physics - Heat
SPM Form 4 Physics - HeatSPM Form 4 Physics - Heat
SPM Form 4 Physics - HeatLoo Carmen
Β 
Colligative properties
Colligative propertiesColligative properties
Colligative propertiesdirksr
Β 
Thermodynamics laws, Brownian motion, Van der Waals equation of state, Entropy
Thermodynamics laws, Brownian motion, Van der Waals equation of state, EntropyThermodynamics laws, Brownian motion, Van der Waals equation of state, Entropy
Thermodynamics laws, Brownian motion, Van der Waals equation of state, EntropyMd Mosharof Hosen
Β 
Thermochemistry Presentation
Thermochemistry PresentationThermochemistry Presentation
Thermochemistry PresentationQ M Muktadir Neal
Β 
Kinetic theory of gases
Kinetic theory of gasesKinetic theory of gases
Kinetic theory of gasesDaya Nandan
Β 
acids and bases
acids and basesacids and bases
acids and basesRosie Leone
Β 

Viewers also liked (20)

Completing the Internal Energy Market
Completing the Internal Energy Market Completing the Internal Energy Market
Completing the Internal Energy Market
Β 
Ap chem unit 6
Ap chem unit 6 Ap chem unit 6
Ap chem unit 6
Β 
Properties of Matter
Properties of MatterProperties of Matter
Properties of Matter
Β 
Detection and analysis of pesticides pollution
Detection and analysis of pesticides pollutionDetection and analysis of pesticides pollution
Detection and analysis of pesticides pollution
Β 
Colligative Properties
Colligative PropertiesColligative Properties
Colligative Properties
Β 
Solutions
SolutionsSolutions
Solutions
Β 
Unit 6 Kinetic Theory of Gases
Unit 6 Kinetic Theory of GasesUnit 6 Kinetic Theory of Gases
Unit 6 Kinetic Theory of Gases
Β 
Chapter 17.1 : Thermochemistry
Chapter 17.1 : ThermochemistryChapter 17.1 : Thermochemistry
Chapter 17.1 : Thermochemistry
Β 
Roultes law
Roultes lawRoultes law
Roultes law
Β 
Liquefaction and liquefaction potential
Liquefaction and liquefaction potentialLiquefaction and liquefaction potential
Liquefaction and liquefaction potential
Β 
Thermochemistry
ThermochemistryThermochemistry
Thermochemistry
Β 
The Kinetic Molecular Theory
The Kinetic Molecular TheoryThe Kinetic Molecular Theory
The Kinetic Molecular Theory
Β 
SPM Form 4 Physics - Heat
SPM Form 4 Physics - HeatSPM Form 4 Physics - Heat
SPM Form 4 Physics - Heat
Β 
Gases
GasesGases
Gases
Β 
Omalgia
OmalgiaOmalgia
Omalgia
Β 
Colligative properties
Colligative propertiesColligative properties
Colligative properties
Β 
Thermodynamics laws, Brownian motion, Van der Waals equation of state, Entropy
Thermodynamics laws, Brownian motion, Van der Waals equation of state, EntropyThermodynamics laws, Brownian motion, Van der Waals equation of state, Entropy
Thermodynamics laws, Brownian motion, Van der Waals equation of state, Entropy
Β 
Thermochemistry Presentation
Thermochemistry PresentationThermochemistry Presentation
Thermochemistry Presentation
Β 
Kinetic theory of gases
Kinetic theory of gasesKinetic theory of gases
Kinetic theory of gases
Β 
acids and bases
acids and basesacids and bases
acids and bases
Β 

Similar to Enthalpy of vaporization of liquid

Boiler doc 02 principles & heat transfer
Boiler doc 02   principles & heat transferBoiler doc 02   principles & heat transfer
Boiler doc 02 principles & heat transferMars Tsani
Β 
Heat exchanger lab 2
Heat exchanger lab 2Heat exchanger lab 2
Heat exchanger lab 2ANDREW MUNYIVA
Β 
Air conditioning
Air conditioningAir conditioning
Air conditioningsankar murthy
Β 
FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...
FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...
FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...Bishal Bhandari
Β 
Estimate the evaporation rate of water (water loss) for the cooling tower
Estimate the evaporation rate of water (water loss) for the cooling towerEstimate the evaporation rate of water (water loss) for the cooling tower
Estimate the evaporation rate of water (water loss) for the cooling towerBarhm Mohamad
Β 
Predicting and Optimising CT LWT
Predicting and Optimising CT LWTPredicting and Optimising CT LWT
Predicting and Optimising CT LWTRaji Panicker
Β 
Boiling heat transfer
Boiling heat transferBoiling heat transfer
Boiling heat transferashudotkushwaha
Β 
Congelacion de pescado
Congelacion de pescadoCongelacion de pescado
Congelacion de pescadoorlandoes
Β 
Unit1 principle concepts of fluid mechanics
Unit1   principle concepts of fluid mechanicsUnit1   principle concepts of fluid mechanics
Unit1 principle concepts of fluid mechanicsMalaysia
Β 
Steam Power Cycle and Basics of Boiler
Steam Power Cycle and Basics of BoilerSteam Power Cycle and Basics of Boiler
Steam Power Cycle and Basics of BoilerMulugeta Wotango
Β 
marcet boiler
marcet boilermarcet boiler
marcet boilerAree Salah
Β 
HHO driven CCPP
HHO driven CCPPHHO driven CCPP
HHO driven CCPPgabriel galli
Β 
HEAT TRANSFER
HEAT TRANSFER HEAT TRANSFER
HEAT TRANSFER oday hatem
Β 
2. Fluids 2.ppt
2. Fluids 2.ppt2. Fluids 2.ppt
2. Fluids 2.pptBlahBeleh
Β 
Separating and throttling calorimeter for steam
Separating and throttling calorimeter for steamSeparating and throttling calorimeter for steam
Separating and throttling calorimeter for steamSaif al-din ali
Β 
Gas power-09
Gas power-09Gas power-09
Gas power-09UthsoNandy
Β 
volumetric properties.ppt
volumetric properties.pptvolumetric properties.ppt
volumetric properties.pptIyerVasundhara
Β 
types of heat exchangers.pdf
types of heat exchangers.pdftypes of heat exchangers.pdf
types of heat exchangers.pdfhassanzain10
Β 

Similar to Enthalpy of vaporization of liquid (20)

Boiler doc 02 principles & heat transfer
Boiler doc 02   principles & heat transferBoiler doc 02   principles & heat transfer
Boiler doc 02 principles & heat transfer
Β 
Heat exchanger lab 2
Heat exchanger lab 2Heat exchanger lab 2
Heat exchanger lab 2
Β 
Air conditioning
Air conditioningAir conditioning
Air conditioning
Β 
FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...
FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...
FABRICATION OF EXPERIMENTAL SETUP TO EVALUATE CONVECTIVE HEAT TRANSFER COEFFI...
Β 
Estimate the evaporation rate of water (water loss) for the cooling tower
Estimate the evaporation rate of water (water loss) for the cooling towerEstimate the evaporation rate of water (water loss) for the cooling tower
Estimate the evaporation rate of water (water loss) for the cooling tower
Β 
2
22
2
Β 
Predicting and Optimising CT LWT
Predicting and Optimising CT LWTPredicting and Optimising CT LWT
Predicting and Optimising CT LWT
Β 
Boiling heat transfer
Boiling heat transferBoiling heat transfer
Boiling heat transfer
Β 
Congelacion de pescado
Congelacion de pescadoCongelacion de pescado
Congelacion de pescado
Β 
Unit1 principle concepts of fluid mechanics
Unit1   principle concepts of fluid mechanicsUnit1   principle concepts of fluid mechanics
Unit1 principle concepts of fluid mechanics
Β 
Steam Power Cycle and Basics of Boiler
Steam Power Cycle and Basics of BoilerSteam Power Cycle and Basics of Boiler
Steam Power Cycle and Basics of Boiler
Β 
marcet boiler
marcet boilermarcet boiler
marcet boiler
Β 
Unit 2.1 thm
Unit 2.1 thmUnit 2.1 thm
Unit 2.1 thm
Β 
HHO driven CCPP
HHO driven CCPPHHO driven CCPP
HHO driven CCPP
Β 
HEAT TRANSFER
HEAT TRANSFER HEAT TRANSFER
HEAT TRANSFER
Β 
2. Fluids 2.ppt
2. Fluids 2.ppt2. Fluids 2.ppt
2. Fluids 2.ppt
Β 
Separating and throttling calorimeter for steam
Separating and throttling calorimeter for steamSeparating and throttling calorimeter for steam
Separating and throttling calorimeter for steam
Β 
Gas power-09
Gas power-09Gas power-09
Gas power-09
Β 
volumetric properties.ppt
volumetric properties.pptvolumetric properties.ppt
volumetric properties.ppt
Β 
types of heat exchangers.pdf
types of heat exchangers.pdftypes of heat exchangers.pdf
types of heat exchangers.pdf
Β 

More from Noaman Ahmed

Modes of Heat Transfer - An Experimental Approach
Modes of Heat Transfer - An Experimental ApproachModes of Heat Transfer - An Experimental Approach
Modes of Heat Transfer - An Experimental ApproachNoaman Ahmed
Β 
Cooling Towers - An Extensive Approach
Cooling Towers - An Extensive ApproachCooling Towers - An Extensive Approach
Cooling Towers - An Extensive ApproachNoaman Ahmed
Β 
Enhanced oil recovery using steam
Enhanced oil recovery using steamEnhanced oil recovery using steam
Enhanced oil recovery using steamNoaman Ahmed
Β 
Corrosion and its occurence in major environments
Corrosion and its occurence in major environmentsCorrosion and its occurence in major environments
Corrosion and its occurence in major environmentsNoaman Ahmed
Β 
Continuous distillation columns - Characteristics at different operating cond...
Continuous distillation columns - Characteristics at different operating cond...Continuous distillation columns - Characteristics at different operating cond...
Continuous distillation columns - Characteristics at different operating cond...Noaman Ahmed
Β 
Chemicals based on ethylene
Chemicals based on ethyleneChemicals based on ethylene
Chemicals based on ethyleneNoaman Ahmed
Β 
Fuel antioxidants
Fuel antioxidantsFuel antioxidants
Fuel antioxidantsNoaman Ahmed
Β 
Speaking & speaking skills
Speaking & speaking skillsSpeaking & speaking skills
Speaking & speaking skillsNoaman Ahmed
Β 
The Listening Process
The Listening ProcessThe Listening Process
The Listening ProcessNoaman Ahmed
Β 

More from Noaman Ahmed (10)

Modes of Heat Transfer - An Experimental Approach
Modes of Heat Transfer - An Experimental ApproachModes of Heat Transfer - An Experimental Approach
Modes of Heat Transfer - An Experimental Approach
Β 
Cooling Towers - An Extensive Approach
Cooling Towers - An Extensive ApproachCooling Towers - An Extensive Approach
Cooling Towers - An Extensive Approach
Β 
Enhanced oil recovery using steam
Enhanced oil recovery using steamEnhanced oil recovery using steam
Enhanced oil recovery using steam
Β 
Corrosion and its occurence in major environments
Corrosion and its occurence in major environmentsCorrosion and its occurence in major environments
Corrosion and its occurence in major environments
Β 
Continuous distillation columns - Characteristics at different operating cond...
Continuous distillation columns - Characteristics at different operating cond...Continuous distillation columns - Characteristics at different operating cond...
Continuous distillation columns - Characteristics at different operating cond...
Β 
Chemicals based on ethylene
Chemicals based on ethyleneChemicals based on ethylene
Chemicals based on ethylene
Β 
Fuel antioxidants
Fuel antioxidantsFuel antioxidants
Fuel antioxidants
Β 
Preparation
PreparationPreparation
Preparation
Β 
Speaking & speaking skills
Speaking & speaking skillsSpeaking & speaking skills
Speaking & speaking skills
Β 
The Listening Process
The Listening ProcessThe Listening Process
The Listening Process
Β 

Recently uploaded

ROOT CAUSE ANALYSIS PowerPoint Presentation
ROOT CAUSE ANALYSIS PowerPoint PresentationROOT CAUSE ANALYSIS PowerPoint Presentation
ROOT CAUSE ANALYSIS PowerPoint PresentationAadityaSharma884161
Β 
Romantic Opera MUSIC FOR GRADE NINE pptx
Romantic Opera MUSIC FOR GRADE NINE pptxRomantic Opera MUSIC FOR GRADE NINE pptx
Romantic Opera MUSIC FOR GRADE NINE pptxsqpmdrvczh
Β 
AMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdf
AMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdfAMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdf
AMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdfphamnguyenenglishnb
Β 
ENGLISH6-Q4-W3.pptxqurter our high choom
ENGLISH6-Q4-W3.pptxqurter our high choomENGLISH6-Q4-W3.pptxqurter our high choom
ENGLISH6-Q4-W3.pptxqurter our high choomnelietumpap1
Β 
call girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈ
call girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈcall girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈ
call girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈ9953056974 Low Rate Call Girls In Saket, Delhi NCR
Β 
Roles & Responsibilities in Pharmacovigilance
Roles & Responsibilities in PharmacovigilanceRoles & Responsibilities in Pharmacovigilance
Roles & Responsibilities in PharmacovigilanceSamikshaHamane
Β 
What is Model Inheritance in Odoo 17 ERP
What is Model Inheritance in Odoo 17 ERPWhat is Model Inheritance in Odoo 17 ERP
What is Model Inheritance in Odoo 17 ERPCeline George
Β 
Introduction to AI in Higher Education_draft.pptx
Introduction to AI in Higher Education_draft.pptxIntroduction to AI in Higher Education_draft.pptx
Introduction to AI in Higher Education_draft.pptxpboyjonauth
Β 
MULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptx
MULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptxMULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptx
MULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptxAnupkumar Sharma
Β 
ECONOMIC CONTEXT - LONG FORM TV DRAMA - PPT
ECONOMIC CONTEXT - LONG FORM TV DRAMA - PPTECONOMIC CONTEXT - LONG FORM TV DRAMA - PPT
ECONOMIC CONTEXT - LONG FORM TV DRAMA - PPTiammrhaywood
Β 
Alper Gobel In Media Res Media Component
Alper Gobel In Media Res Media ComponentAlper Gobel In Media Res Media Component
Alper Gobel In Media Res Media ComponentInMediaRes1
Β 
Difference Between Search & Browse Methods in Odoo 17
Difference Between Search & Browse Methods in Odoo 17Difference Between Search & Browse Methods in Odoo 17
Difference Between Search & Browse Methods in Odoo 17Celine George
Β 
ECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptx
ECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptxECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptx
ECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptxiammrhaywood
Β 
How to do quick user assign in kanban in Odoo 17 ERP
How to do quick user assign in kanban in Odoo 17 ERPHow to do quick user assign in kanban in Odoo 17 ERP
How to do quick user assign in kanban in Odoo 17 ERPCeline George
Β 
How to Configure Email Server in Odoo 17
How to Configure Email Server in Odoo 17How to Configure Email Server in Odoo 17
How to Configure Email Server in Odoo 17Celine George
Β 
Procuring digital preservation CAN be quick and painless with our new dynamic...
Procuring digital preservation CAN be quick and painless with our new dynamic...Procuring digital preservation CAN be quick and painless with our new dynamic...
Procuring digital preservation CAN be quick and painless with our new dynamic...Jisc
Β 

Recently uploaded (20)

ROOT CAUSE ANALYSIS PowerPoint Presentation
ROOT CAUSE ANALYSIS PowerPoint PresentationROOT CAUSE ANALYSIS PowerPoint Presentation
ROOT CAUSE ANALYSIS PowerPoint Presentation
Β 
Romantic Opera MUSIC FOR GRADE NINE pptx
Romantic Opera MUSIC FOR GRADE NINE pptxRomantic Opera MUSIC FOR GRADE NINE pptx
Romantic Opera MUSIC FOR GRADE NINE pptx
Β 
AMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdf
AMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdfAMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdf
AMERICAN LANGUAGE HUB_Level2_Student'sBook_Answerkey.pdf
Β 
Model Call Girl in Bikash Puri Delhi reach out to us at πŸ”9953056974πŸ”
Model Call Girl in Bikash Puri  Delhi reach out to us at πŸ”9953056974πŸ”Model Call Girl in Bikash Puri  Delhi reach out to us at πŸ”9953056974πŸ”
Model Call Girl in Bikash Puri Delhi reach out to us at πŸ”9953056974πŸ”
Β 
ENGLISH6-Q4-W3.pptxqurter our high choom
ENGLISH6-Q4-W3.pptxqurter our high choomENGLISH6-Q4-W3.pptxqurter our high choom
ENGLISH6-Q4-W3.pptxqurter our high choom
Β 
call girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈ
call girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈcall girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈ
call girls in Kamla Market (DELHI) πŸ” >ΰΌ’9953330565πŸ” genuine Escort Service πŸ”βœ”οΈβœ”οΈ
Β 
Roles & Responsibilities in Pharmacovigilance
Roles & Responsibilities in PharmacovigilanceRoles & Responsibilities in Pharmacovigilance
Roles & Responsibilities in Pharmacovigilance
Β 
What is Model Inheritance in Odoo 17 ERP
What is Model Inheritance in Odoo 17 ERPWhat is Model Inheritance in Odoo 17 ERP
What is Model Inheritance in Odoo 17 ERP
Β 
Introduction to AI in Higher Education_draft.pptx
Introduction to AI in Higher Education_draft.pptxIntroduction to AI in Higher Education_draft.pptx
Introduction to AI in Higher Education_draft.pptx
Β 
MULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptx
MULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptxMULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptx
MULTIDISCIPLINRY NATURE OF THE ENVIRONMENTAL STUDIES.pptx
Β 
OS-operating systems- ch04 (Threads) ...
OS-operating systems- ch04 (Threads) ...OS-operating systems- ch04 (Threads) ...
OS-operating systems- ch04 (Threads) ...
Β 
ECONOMIC CONTEXT - LONG FORM TV DRAMA - PPT
ECONOMIC CONTEXT - LONG FORM TV DRAMA - PPTECONOMIC CONTEXT - LONG FORM TV DRAMA - PPT
ECONOMIC CONTEXT - LONG FORM TV DRAMA - PPT
Β 
Alper Gobel In Media Res Media Component
Alper Gobel In Media Res Media ComponentAlper Gobel In Media Res Media Component
Alper Gobel In Media Res Media Component
Β 
TataKelola dan KamSiber Kecerdasan Buatan v022.pdf
TataKelola dan KamSiber Kecerdasan Buatan v022.pdfTataKelola dan KamSiber Kecerdasan Buatan v022.pdf
TataKelola dan KamSiber Kecerdasan Buatan v022.pdf
Β 
Rapple "Scholarly Communications and the Sustainable Development Goals"
Rapple "Scholarly Communications and the Sustainable Development Goals"Rapple "Scholarly Communications and the Sustainable Development Goals"
Rapple "Scholarly Communications and the Sustainable Development Goals"
Β 
Difference Between Search & Browse Methods in Odoo 17
Difference Between Search & Browse Methods in Odoo 17Difference Between Search & Browse Methods in Odoo 17
Difference Between Search & Browse Methods in Odoo 17
Β 
ECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptx
ECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptxECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptx
ECONOMIC CONTEXT - PAPER 1 Q3: NEWSPAPERS.pptx
Β 
How to do quick user assign in kanban in Odoo 17 ERP
How to do quick user assign in kanban in Odoo 17 ERPHow to do quick user assign in kanban in Odoo 17 ERP
How to do quick user assign in kanban in Odoo 17 ERP
Β 
How to Configure Email Server in Odoo 17
How to Configure Email Server in Odoo 17How to Configure Email Server in Odoo 17
How to Configure Email Server in Odoo 17
Β 
Procuring digital preservation CAN be quick and painless with our new dynamic...
Procuring digital preservation CAN be quick and painless with our new dynamic...Procuring digital preservation CAN be quick and painless with our new dynamic...
Procuring digital preservation CAN be quick and painless with our new dynamic...
Β 

Enthalpy of vaporization of liquid

  • 2. Presented by ο‚— Ahmed Asad – CIIT/SP10-BEC-003/LHR ο‚— Muhammad Usama – CIIT/SP10-BEC-017/LHR ο‚— Mohammad Abubakar – CIIT/SP10-BEC-022/LHR ο‚— Noaman Ahmed – CIIT/SP10-BEC-037/LHR ο‚— Saad Wazir – CIIT/SP10-BEC-043/LHR ο‚— Saim Khan – CIIT/SP10-BEC-044/LHR ο‚— Waqar Farooq – CIIT/SP10-BEC-050/LHR
  • 3. Presentation Outline ο‚— Restatement of first law of thermodynamics ο‚— Definition of enthalpy ο‚— Some common enthalpy changes ο‚— Enthalpy of vaporization ο‚— Characteristics of enthalpy of vaporization ο‚— Physical model for vaporization ο‚— Experimental determination ο‚— Sample readings and calculations ο‚— Applications
  • 4. First Law of Thermodynamics ο‚— Energy conservation law ο‚— Describeschange in internal energy of a thermodynamic system ο‚— Clausius’ statement: In a thermodynamic process, the increment in the internal energy of a system is equal to the difference between the increment of heat accumulated by the system and the increment of work done by it.
  • 5. First Law of Thermodynamics (contd.) ο‚— In any incremental process, the change in the internal energy is considered due to, ο‚— Heat added to the system ο‚— Work done by the system dU = dQ - dW
  • 6. First Law of Thermodynamics (contd.) ο‚— For a quasistatic process (infinitely slow process), dU = dQ – PdV ο‚— NO real process is quasistatic ο‚— A quasistatic process ensures that the system will go through a sequence of states that are infinitesimally close to equilibrium (so the system remains in quasistatic equilibrium), in which case the process is typically reversible
  • 7. Quasistatic and Reversibility ο‚— Any reversible process is a quasistatic process ο‚— Any quasistatic process may not be reversible ο‚— Due to heat flow ο‚— Due to entropy generation ο‚— Example of an irreversible quasistatic process ο‚— Compression against a system with a piston subject to friction
  • 8. Enthalpy ο‚— Measure of total energy of a thermodynamic system ο‚— A state function ο‚— Includes ο‚— Internal energy (energy required to create a system) ο‚— Amount of energy required to establish system’s pressure and volume Ξ”H = Ξ”U + Ξ”(PV) ο‚— SI Unit – Joule ο‚— Other conventional units – Btu and Calories
  • 9. Why Enthalpy is measured? ο‚— Total enthalpy of a system can’t be measured directly ο‚— Enthalpy change of a system is measured instead ο‚— It is measured to, ο‚— Calculate β€œuseful work” obtainable from a closed thermodynamic system under constant pressure ο‚— Determine nature of reaction e.g., exothermic or endothermic
  • 10. Enthalpy is not necessarily heat !! ο‚— Enthalpy is sometimes described as heat content of a system ο‚— Heat is defined as thermal energy in transit ο‚— For the description that enthalpy is in-fact heat to be valid, no energy exchange must occur with environment other than heat or expansion work
  • 11. Common Enthalpy Changes ο‚— Enthalpy of reaction ο‚— Enthalpy of formation ο‚— Enthalpy of combustion ο‚— Enthalpy of neutralization ο‚— Enthalpy of solution ο‚— Enthalpy of vaporization ο‚— Enthalpy of sublimation
  • 12. Vaporization ο‚— Phase transition from liquid phase to gas phase ο‚— Two types ο‚— Evaporation ο‚— Occurs at temperatures below boiling temperature ο‚— Usually occurs on surface ο‚— Boiling ο‚— Occurs at or above boiling temperature ο‚— Occurs below the surface
  • 13. Enthalpy of Vaporization (EOV) ο‚— Enthalpy change required to completely change the state of one mole of substance between liquid and gaseous states ο‚— Energy required to transform a given quantity of a substance from a liquid into a gas at a given pressure ο‚— Usually measured at boiling point of a substance
  • 14. Characteristics of Enthalpy of Vaporization ο‚— It is temperature dependent ο‚— EOV decreases with increase in temperature ο‚— EOV diminishes completely at critical temperature beyond which liquid and vapor phase no longer co- exist ο‚— Units – J/mol or kJ/mol, kJ/kg, Btu/lb, kcal/mol
  • 15. Characteristics of Enthalpy of Vaporization (contd.) ο‚— Enthalpy of condensation is same as enthalpy of vaporization but with opposite sign ο‚— Enthalpy change of vaporization is always positive ο‚— Enthalpy change of condensation is always negative
  • 17. Physical model for vaporization ο‚— Proposed by professor Jozsef Garai, Florida International University, USA ο‚— Energy required to free an atom from liquid is equivalent to energy required to overcome surface resistance of liquid ο‚— This model states, Latent heat = (Max. surface area) x (Surface tension) x (No. of atoms in liquid)
  • 18. Physical model for vaporization (Diagrammatic representation)
  • 20. Apparatus ο‚— Round bottom boiling flask ο‚— Distillation condenser or multiple condensers ο‚— Heat source (a burner or a heating mantle) ο‚— A vacuum gauge (Bourdon type gauge) ο‚— Aspirator or trapped vacuum pump ο‚— Pressure-regulating device (a needle valve that is part of a Bunsen burner base) ο‚— Thermometer
  • 21. Basic Goal ο‚— To determine boiling point of the liquid (water) under study at different pressure values ο‚— To determine enthalpy of vaporization using the Clausius-Clapeyron relation
  • 22. Clausius-Clapeyron relation ο‚— A relation used to characterize a discontinuous phase transition between two phases of a single constituent ο‚— On a P-T diagram, line separating two phases is known as coexistence curve ο‚— This relation gives the slope of the tangents to this curve
  • 23. Clausius-Clapeyron relation (contd.) ο‚— General form dP/dT = L/TΞ”V ο‚— Where ο‚— dP/dT is slope of tangent to coexistence curve at any point ο‚— L is latent specific heat ο‚— T is temperature ο‚— Ξ”V is specific volume change of phase transition ο‚— For transitions between a gas and condensed phase, the expression may be rewritten as, ln(P) = (-L/R) x (1/T) + C
  • 24. Procedure ο‚— Maintain lowest possible pressure by closing bleed valve ο‚— Set water flow to the aspirator at maximum level to provide highest vacuum ο‚— Place few boiling stones in round bottom flask to minimize bumping
  • 25. Procedure (contd.) ο‚— Temperature increases until boiling starts ο‚— When boiling occurs, allow the thermometer reading to stabilize for 1 to 2 minutes and note the temperature ο‚— Note the pressure reading on the manometer at this temperature
  • 26. Procedure (contd.) ο‚— Increase the pressure of the vessel by slightly opening the bleed valve ο‚— Repeat the same procedure as described previously and then increase pressure again ο‚— Take at least five readings and plot a graph between reciprocal of temperature and log of pressure difference
  • 27. Sample Readings Temp (Β°C) h (mm Hg) Temp (K) (1/T) x 103 P (mm Hg) Log P (1/K) (P = 768 –h) 41.5 710 314.5 3.18 58.0 1.77 62.5 610 335.2 2.98 158 2.20 75.0 500 348.0 2.87 268 2.43 86.5 300 359.5 2.78 468 2.67 92.2 220 365.2 2.74 548 2.74 101.0 0 374.0 2.67 768 2.89
  • 28. Graph between temperature and pressure Temperature and Log P 3.5 3 2.5 2 Log P 1.5 1 0.5 0 2.6 2.7 2.8 2.9 3 3.1 3.2 3.3 1/T x 103
  • 29. Calculations ο‚— Molar latent heat / enthalpy of vaporization can be calculated from Clausius-Clapeyron relation as follows, Ξ”Hv = -Rx[d(ln(P))/d(1/T)]] ln(P) = 2.303 log(P) Slope = m = d(ln(P))/d(1/T) Ξ”Hv = -2.303(R)(m) - - - - Eq. (1) ο‚— Where R is ideal gas constant = 1.987 cal/K ο‚— m is slope of line obtained from graph
  • 30. Calculations (contd.) ο‚— Slope (m) can be obtained from linear regression ο‚— A convenient method is to draw a trend-line on the graph and select the option to display an equation of line ο‚— The equation of line of the sample experiment graph is, y = -2.233x+8.859 ο‚— From equation, value of slope (m) = -2.233
  • 31. Calculations (contd.) ο‚— Applying values in equation 1 from previous slide Ξ”Hv = 10.21 cal/mol ο‚— Accepted value for water is 9.72 cal/mol ο‚— Deviation is 4.79 % ο‚— Results obtained from this experiment seldom increase 5% deviation from expected value
  • 32. Applications ο‚— Major application in conversion of water into steam ο‚— Steam is used in ο‚— Power generation (steam turbines) ο‚— Agriculture ο‚— Energy storage ο‚— Wood treatment ο‚— Cleaning purposes ο‚— Sterilization
  • 34. References ο‚— http://en.wikipedia.org/wiki/First_law_of_thermodyn amics ο‚— http://en.wikipedia.org/wiki/Quasistatic_process ο‚— http://en.wikipedia.org/wiki/Enthalpy ο‚— http://en.wikipedia.org/wiki/Clausius- Clapeyron_relation
  • 35. References ο‚— http://en.wikipedia.org/wiki/Enthalpy_of_vaporizatio n ο‚— http://www.sciencedirect.com/science/article/pii/S03 78381209002180 ο‚— http://www2.selu.edu/Academics/Faculty/delbers/He at%20of%20vaporization.htm

Editor's Notes

  1. Noaman StartThe first law of thermodynamics is a specialized version of law of conservation of energy for thermodynamicsThe first explicit statement of this law was given by Rudolf Clausius in 1850, and in terms of internal energy the statement was (SLIDE)
  2. where dQand dW are infinitesimal amounts of heat supplied to the system and work done by the system, respectively. Note that the minus sign in front of indicates that a positive amount of work done by the system leads to energy being lost from the system. This is the sign convention used in many textbooks on physics.(An alternate sign convention is to consider the work performed on the system by its surroundings. This leads to a change in sign of the work, so that . This is the convention adopted by many modern textbooks of physical chemistry, such as those by Peter Atkins and Ira Levine.)
  3. In practice, such processes can only be approximated by performing them infinitesimally slowly.A quasistatic process ensures that the system will go through a sequence of states that are infinitesimally close to equilibrium (so the system remains in quasistatic equilibrium), in which case the process is typically reversible.
  4. Any reversible process is necessarily a quasistatic one. However, some quasistatic processes are irreversible, if there is heat flowing (in or out of the system) or if entropy is being created in some other way. An example of a quasistatic process that is not reversible is a compression against a system with a piston subject to friction β€” Although the system is always in thermal equilibrium, the friction ensures the generation of dissipative entropy, which directly goes against the definition of reversible.
  5. Muhammad Usama Start
  6. The total enthalpy of a system cannot be measured directly; the enthalpy change of a system is measured instead.
  7. Adding or removing energy through heat is one of only two ways to change the enthalpyEnthalpy is nothing more than heat "stored" by the system, provided the given restrictions are adhered toEnthalpy also changes when the pressure of the environment is altered, even if no energy is exchanged as heatEnthalpy changes when energy is transferred into or out of the system through a means other than heat or expansion work, such as through external fields or stirring
  8. Enthalpy of reaction, defined as the enthalpy change observed in a constituent of a thermodynamic system when one mole of substance reacts completely. Enthalpy of formation, defined as the enthalpy change observed in a constituent of a thermodynamic system when, one mole of a compound is formed from its elementary antecedents. Enthalpy of combustion, defined as the enthalpy change observed in a constituent of a thermodynamic system, when one mole of a substance combusts completely with oxygen.Enthalpy of neutralization, defined as the enthalpy change observed in a constituent of a thermodynamic system, when one mole of water is produced when an acid and a base react.Enthalpy of solution, defined as the enthalpy change observed in a constituent of a thermodynamic system, when one mole of an solute is dissolved completely in an excess of solvent.Enthalpy of vaporization, defined as the enthalpy change required to completely change the state of one mole of substance between liquid and gaseous states. Enthalpy of sublimation, defined as the enthalpy change required to completely change the state of one mole of substance between solid and gaseous states.
  9. Vaporization is a phase transition from a liquid phase to a gas phase
  10. Saad Wazir Start
  11. The enthalpy of condensation is by definition equal to the enthalpy of vaporization with the opposite sign: Enthalpy changes of vaporization are always positive becauseheat is absorbed by the substance, whereas enthalpy changes of condensation are always negative because heat is released by the substance.
  12. Ahmed Asad start
  13. A simple physical model for the liquid-gas phase transformation has been proposed recently by Jozsef Garai, a professor in the Department of Mechanical and Materials Engineering, Florida International University, United States.The model suggests that the energy required to free an atom from the liquid is equivalent to the energy needed to overcome the surface resistance of the liquid. The model allows calculating the latent heat by multiplying the maximum surface area covering an atom with the surface tension and the number of atoms in the liquid. The calculated latent heat of vaporization values for the investigated 45 elements agrees well with experiments.
  14. Mohammad Abubakar StartBallast is usedto hold water – The water ballast is placed because when the drop condenses in the condenser, it may be sucked by the vacuum pump due to its small size and weight. The water trap doesn’t allow the water drop to pass on to the pump which otherwise may cause cavitations
  15. This is the apparatus that we are going to use,
  16. For a liquid-gas transition, L is the specific latent heat (or specific enthalpy) of vaporization, whereas for a solid-gas transition, L is the specific latent heat of sublimation. If the latent heat is known, then knowledge of one point on the coexistence curve determines the rest of the curve. Conversely, the relationship between lnP and 1/T is linear, and so linear regression may be used to estimate the latent heat.Where C is constant of integration. This is removed when boundary conditions are given
  17. Waqar Farooq Start
  18. Atmospheric Pressure is 768 mm Hg
  19. Saim Khan Start
  20. In statistics, linear regression is an approach to modeling the relationship between a scalar dependent variabley and one or more explanatory variables denoted X.
  21. Distillation is one of the most practical methods for separation and purification of chemical compounds. The heat of vaporization is the fundamental quantity that determines the experimental conditions at which an industrial or laboratory-scale distillation should be run.The concentration of a gas is given by its vapor pressure.Knowledge of the heat of vaporization permits the control of vapor pressure by setting the temperature of the liquid being vaporized.