This document provides an overview of physical chemistry and its branches, which include thermodynamics, quantum chemistry, statistical mechanics, and kinetics. It discusses various concepts in physical chemistry such as thermodynamic systems and properties, the laws of thermodynamics, entropy, Gibbs free energy, and thermodynamic calculations. Key areas covered are the branches of physical chemistry and why it is important for chemical engineers, as well as explanations of concepts like thermodynamic equilibrium, state functions, and the measurement of temperature.
These slides are especially made to understand the postulates of quantum mechanics or chemistry better. easily simplified and at one place you will find each of relevant details about the 5 postulates. so go through it & trust me it will help you a lot if you are chemistry or a science student.
well done
These slides are especially made to understand the postulates of quantum mechanics or chemistry better. easily simplified and at one place you will find each of relevant details about the 5 postulates. so go through it & trust me it will help you a lot if you are chemistry or a science student.
well done
It shows the basic facts of catalyst along with its importance in industry along with its long last milestone,its characteristics & application in industry its reaction process and preparation of a solid catalyst.
Introductory PPT on Metal Carbonyls having its' classification,structure and applications.This is a basic level PPT specially prepared for UG/PG Chemistry students.
It shows the basic facts of catalyst along with its importance in industry along with its long last milestone,its characteristics & application in industry its reaction process and preparation of a solid catalyst.
Introductory PPT on Metal Carbonyls having its' classification,structure and applications.This is a basic level PPT specially prepared for UG/PG Chemistry students.
This slide will completely describes you about thermodynamics. The basics of thermo is explained in this slide. Intensive and Extensive Propeties are exolained in this properties.
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
Author: Robbie Edward Sayers
Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
Immunizing Image Classifiers Against Localized Adversary Attacksgerogepatton
This paper addresses the vulnerability of deep learning models, particularly convolutional neural networks
(CNN)s, to adversarial attacks and presents a proactive training technique designed to counter them. We
introduce a novel volumization algorithm, which transforms 2D images into 3D volumetric representations.
When combined with 3D convolution and deep curriculum learning optimization (CLO), itsignificantly improves
the immunity of models against localized universal attacks by up to 40%. We evaluate our proposed approach
using contemporary CNN architectures and the modified Canadian Institute for Advanced Research (CIFAR-10
and CIFAR-100) and ImageNet Large Scale Visual Recognition Challenge (ILSVRC12) datasets, showcasing
accuracy improvements over previous techniques. The results indicate that the combination of the volumetric
input and curriculum learning holds significant promise for mitigating adversarial attacks without necessitating
adversary training.
About
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Technical Specifications
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
Key Features
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface
• Compatible with MAFI CCR system
• Copatiable with IDM8000 CCR
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
Application
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
In this month's edition, along with this month's industry news to celebrate the 13 years since the group was created we have articles including
A case study of the used of Advanced Process Control at the Wastewater Treatment works at Lleida in Spain
A look back on an article on smart wastewater networks in order to see how the industry has measured up in the interim around the adoption of Digital Transformation in the Water Industry.
Student information management system project report ii.pdfKamal Acharya
Our project explains about the student management. This project mainly explains the various actions related to student details. This project shows some ease in adding, editing and deleting the student details. It also provides a less time consuming process for viewing, adding, editing and deleting the marks of the students.
2. PHYSICAL CHEMISTRY BRANCHES
• THERMODYNAMICS: MACROSCOPIC SCIENCE THAT STUDIES THE
INTERRELATIONSHIPS OF THE VARIOS EQUILIBRIUM PROPERTIES OF A SYSTEM
AND THEIR CHANGES IN PROCESSES.
• QUANTUM CHEMISTRY: QUANTUM MECHANICS APPLIED TO ATOMIC
STRUCTURE, MOLECULAR BONDING AND SPECTROSCOPY.
• STATISTICAL MECHANICS: RELATES THE MOLECULAR (MICROSCOPIC)
PHENOMENA WITH MACROSCOPIC SCIENCE OF THERMODYNAMIC. (CAUSE-
CONSEQUENCE).
• KINETICS: STUDIES THE RATES OF PROCESSES SUCH AS CHEMICAL REACTIONS,
DIFFUSION, CHARGE FLOW IN AN ELECTROCHEMICAL CELL, ETC.
4. PHYSICAL CHEMISTRY, WHY?
• CHEMICAL ENGINEERS USE THERMODYNAMICS TO PREDICT THE EQUILIBRIUM
COMPOSITION OF REACTION MIXTURES, USE KINETICS TO CALCULATE HOW
FAST PRODUCTS WILL BE FORMED, AND USE PRINCIPLES OF THERMODYNAMIC
PHASE EQUILIBRIA TO DESIGN SEPARATION PROCEDURES SUCH AS FRACTIONAL
DISTILLATION.
5. THERMO
DYNAMICS
• GREEK WORDS FOR HEAT AND POWER
• STUDIES HEAT, WORK AND ENERGY AND THE CHANGES THEY PRODUCE IN THE
STATES OF SYSTEMS. TEMPERATURE IS A KEY PROPERTY.
• SOMETIMES IS DEFINED AS THE RELATION OF TEMPERATURE TO THE
MACROSCOPIC PROPERTIES OF A SYSTEM.
7. THERMODYNAMIC SYSTEM
• A SYSTEM COULD BE:
o OPEN/CLOSED
o ISOLATED/NON-ISOLATED
• WALLS CONFINING THE SYSTEM COULD BE:
o RIGID/NON-RIGID (MOVABLE)
o PERMEABLE/IMPERMEABLE
o ADIABATIC/NON-ADIABATIC (THERMALLY CONDUCTING)
9. EQUILIBRIUM
• THE MACROSCOPIC PROPERTIES OF AN ISOLATED SYSTEM REMAIN CONSTANT
WITH TIME.
• THE MACROSCOPIC PROPERTIES OF A NON-ISOLATED SYSTEM
1. REMAIN CONSTANT WITH TIME.
2. REMAIN CONSTANT WHEN THE SYSTEM IS REMOVED FROM CONTACT WITH
ITS SURROUNDINGS.
10. THERMODYNAMIC EQUILIBRIUM
• MECHANICAL EQUILIBRIUM: THERE ARE NO UNBALANCED FORCES APPLIED ON
OR WITHIN THE SYSTEM; THE SYSTEM DOES NOT EXPERIMENT ACCELERATION,
NOR TURBULENCE.
• MATERIAL EQUILIBRIUM: THERE ARE NO CHEMICAL REACTIONS AND SYSTEM
AND THERE IS NO TRANSFER OF MATTER FROM ONE PART OF THE SYSTEM TO
ANOTHER OR BETWEEN IT AND ITS SURROUNDINGS. THE CONCENTRATIONS OF
CHEMICAL SPECIES IN THE VARIOUS PARTS OF THE SYSTEM ARE CONSTANT
WITH TIME
• THERMAL EQUILIBRIUM: THE PROPERTIES OF SYSTEM REMAIN CONSTANT WITH
TIME WHEN THERE IS A NON-ADIABATIC WALL BETWEEN IT AND ANOTHER PART
OR ITS SURROUNDINGS
11. THERMODYNAMIC PROPERTIES
• PROPERTIES THAT CHARACTERIZE A SYSTEM IN EQUILIBRIUM
COMPOSITION
VOLUME
PRESSURE
TEMPERATURE
INTERNAL ENERGY
ENTHALPY
ENTROPY
GIBBS FREE ENERGY
HEMHOLTZ ENERGY (WORK FUNCTION)
12. EXTENSIVE AND INTENSIVE PROPERTIES
• REFRACTIVE INDEX
• MASS
• VOLUME
• MOLAR VOLUME
• SPECIFIC VOLUME
• ENTHALPY
• ENTROPY
• MOLAR ENTHALPY
• SPECIFIC ENTROPY
• TEMPERATURE
• PRESSURE
• DENSITY
• MOLAR FRACTION
• WEIGHT FRACTION
• SPECIFIC GRAVITY (RELATIVE DENSITY)
• SPECIFIC WEIGHT
If you sum the values of a property in every part of the system to obtain the to
of the property in the whole system, then the property is extensive
If all intensive porperties are constant throughout a system, the system is hom
An homogeneous part of as system is called a phase
A system composed of two or more phases is heterogenous
A thermodynamic property is also called a state function because a thermody
has a particular value for each thermodynamic property and the value of a sta
depends on the present state of the system and not on its past history
14. WHAT IS AN STATE?
• A SET OF PROPERTIES OF A GIVEN SYSTEM THAT MAKE IT DIFFERENT FROM ANY
OTHER SYSTEM. WE USE PROPERTIES TO SPECIFY THE STATE OF THE SYSTEM
• STATE POSTULATE:
THE STATE OF SIMPLE COMPRESSIBLE SYSTEM IS COMPLETELY SPECIFIED BY TWO
INDEPENDENT INTENSIVE PROPERTIES.
15. PROCESSES AND CYCLES• ANY PROCESS CAN BE USED TO CHANGE THE SYSTEM STATE TO ANOTHER,
THROUGHOUT A SERIES OF STATES THAT AS A SET ARE CALLED THE PATH.
• A REVERSIBLE OR QUASI-EQUILIBRIUM (QUASI-STATIC) PROCESS IS USED TO
CHANGE THE STATE OF A SYSTEM WITHOUT INHOMOGENEITY OF PROPERTIES
THROUGH THE SYSTEM VOLUME.
• A PROCESS COULD BE:
• ISOTHERMAL
• ISOBARIC
• ISOCHORIC (ISOMETRIC)
• CYCLIC
17. ZEROTH LAW OF THERMODYNAMICS AND
TEMPERATURE
• PRESSURE IS A PROPERTY THAT CAN BE USED TO EVALUATE MECHANICAL
EQUILIBRIUM
• THERMAL EQUILIBRIUM IS EVALUATED WITH A PROPERTY CALLED
TEMPERATURE
• TWO SYSTEMS THAT ARE EACH FOUND IN THERMAL EQUILIBRIUM WITH A
THIRD SYSTEM, THEY WILL BE FOUND TO BE IN THERMAL EQUILIBRIUM WITH
EACH OTHER.
18. MEASURING TEMPERATURE
• WE NEED A SCALE BASED ON A PROPERTY OF A REFERENCE SYSTEM WE CALL
THERMOMETER
• WE SUPPOUSE FIXED COMPOSITION AND PRESSURE FOR THE REFERENCE SYSTEM
SO THAT A CHANGE IN A THIRD PROPERTY (VOLUME FOR EXAMPLE) WILL MEAN A
CHANGE IN TEMPERATURE. BUT NOT EVERY SUBSTANCE CAN BE USED IN THE
REFERENCE SYSTEM.
• WE SET THE ICE TEMPERATURE AS 0*C AND THE STEAM
TEMPERATURE AS 100*C AND SUPPOSE A LINEAR BEHAVIOR
BETWEEN THE LENGTH OF MERCURY COLUMN AND TEMPERATURE
24. FIRST LAW OF THERMODYNAMICS;
REVERSIBLE P-V
WORK
25. FIRST LAW OF THERMODYNAMICS;
REVERSIBLE P-V
WORK
26. FIRST LAW OF THERMODYNAMICS; HEAT
• TRANSFER OF ENERGY BY USING HEAT BETWEEN TWO BODYS AT DIFFERENT
TEMPERATURES WHERE T2›T1.
27. FIRST LAW OF THERMODYNAMICS; INTERNAL
ENERGY
ENTALPHY AND HEAT CAPACITY• TRANSFER OF ENERGY BY USING HEAT BETWEEN TWO BODYS AT DIFFERENT
TEMPERATURES WHERE T2›T1.
28. SECOND LAW OF THERMODYNAMICS
• KELVIN PLANCK: IT IS IMPOSSIBLE FOR A SYSTEM TO UNDERGO A CYCLIC
PROCESS WHOSE SOLE EFFECTS ARE THE FLOW OF HEAT INTO THE SYSTEM
FROM A HEAT RESERVOIR AND THE PERFORMANCE OF AN EQUIVALENT AMOUNT
OF WORK BY THE SYSTEM ON THE SURROUNDINGS.
• CLAUSIUS STATEMENT: IT IS IMPOSSIBLE FOR A SYSTEM TO UNDERGO A CYCLIC
PROCESS WHOSE SOLE EFFECTS ARE THE FLOW OF HEAT INTO THE SYSTEM
FROM A COLD RESERVOIR AND THE FLOW OF AN EQUAL AMOUNT OF HEAT OUT
OF THE SYSTEM INTO A HOT RESERVOIR.
30. CARNOT CYCLE
• NO HEAT ENGINE CAN BE MORE EFFICIENT THAN A REVERSIBLE HEAT ENGINE
WHEN BOTH ENGINES WORK BETWEEN THE SAME PAIR OF TEMPERATURES TH AND
TC.
31. EXERCISE
• A MODERN STEAM POWER PLANT MIGHT HAVE THE BOILER AT 550°C AND THE
CONDENSER AT 40°C. IF IT OPERATES ON A CARNOT FIND THE EFFICIENCY OF
OPERATION.
33. CALCULATION OF ENTROPY CHANGES
• IDENTIFY THE INITIAL AND FINAL STATES 1 AND 2.
• DEVISE A CONVENIENT REVERSIBLE PATH FROM 1 TO 2.
• CALCULATE S CHANGE.
1. CYCLIC PROCESS
2. ADIABATIC PROCESS
3. REVERSIBLE PHASE CHANGE AT CONSTANT T AND P
34. CALCULATION OF ENTROPY CHANGES
4. REVERSIBLE ISOTHERMAL PROCESS:
5. CONSTANT PRESSURE HEATING WITH NO PHASE CHANGE:
6.REVERSIBLE CHANGE OF STATE OF A PERFECT GAS
35. CALCULATION OF ENTROPY CHANGES
7. MIXING OF DIFFERENT INERT PERFECT GASES AT CONSTANT P AND T.
36. WHAT IS ENTROPY?
• PROBABILITY
• A PROCESS HAPPENS IF THE ENTROPY OF UNIVERSE IS TO BE MAXIMIZED
• FOR A SYSTEM IRREVERSIBLE PROCESS
37. THE GIBBS AND HELMHOLTZ ENERGY
• A=U-TS, CONSTANT VOLUME
• G=H-TS=U+PV-TS, CONSTANT PRESSURE
45. DETERMINATION OF STANDARD ENTHALPIES
OF FORMATION AND REACTION
1. CALCULATE THE ENTHALPY OF FORMATION OF A REAL GAS FROM AN IDEAL
GAS
2. MEASURE THE ENTHALPY FOR MIXING THE PURE ELEMENTS
3. USE TO FIND CHANGE OF ENTHALPY OF
BRINGING THE MIXTURE FROM 1 BAR AND T TO THE EXPERIMENTAL
CONDITIONS
4. USE A CALORIMETER TO MEASURE THE ENTHALPY CHANGE OF REACTION.
5. FOLLOW INVERTED 3 AND 1 STEPS FOR THE COMPOUND FORMED IN STEP 4.
6. SUM ALL THE CHANGE ENTHALPIES INVOLVED FROM 1 TO 5
53. CONVENTIONAL ENTROPIES
• CONVENTIONAL OR RELATIVE ENTROPIES ARE TABULATED INSTEAD OF
ENTROPIES OF FORMATION.
• WHAT HAPPENS WITH COMPOUNDS….?
WE HAVE A PROBLEM…
54. THE THIRD LAW OF THERMODYNAMICS
• IN 1900 RICHARDS MADE EXPERIMENTS OF G CHANGE IN FUNCTION OF
TEMPERATURE FOR ELECTROCHEMICAL SYSTEMS
• THEN, NERNST NOTICED THAT THOSE EXPERIMENTS HAD A CLEAR TENDENCY:
59. THERMOCHEMISTRY OF SOLUTIONS
• BONDS ARE BROKEN AND FORMED BETWEEN ATOMS AND MOLECULES DURING DE
SOLUTION FORMATION
• ENERGY IS REQUIRED TO BREAK BONDS AND ENERGY IS RELEASED WHEN BONDS
ARE FORMED
• ENERGY COULD BE TRANSFERRED BETWEEN SYSTEM AND SURROUNDINGS OR
COULD SIMPLY CHANGE DE SYSTEM TEMPERATURE (OR BOTH)
• FOR AN IDEAL MIXTURE:
• HEAT OF SOLUTION (SOLUTES ARE SOLIDS OR GASES) IS EQUIVALENT TO HEAT OF
MIXING (SOLUTES ARE LIQUIDS)
• HEAT OF SOLUTION AT INFINITE DILUTION (SOLVENT IS IN MUCH LARGER
PROPORTION)
60. CALCULUS OF HEAT OF SOLUTION
o WHAT IS THE ENTHALPY CHANGE FOR A PROCESS IN WHICH 2 MOL OF KCN IS
DISSOLVED IN 400 MOL OF WATER AT 18OC?
• THE COMMONLY REPORTED IS DEFINED RELATIVE TO THE PURE
SOLUTE AND SOLVENT AT T.
• WE COULD ALSO CHOICE THE PURE SOLVENT AND AN INFINITELY DILUTE
SOLUTION AT T AS THE REFERENCE CONDITIONS.
o EXAMPLE: CONSIDER A SOLUTION WHERE HCL(G) IS DISSOLVED IN H2O(L) AT 25OC
SO THAT R=10. FIND THE ENTHALPY OF SOLUTION RELATIVE TO H2O(L) AND A
HIGHLY DILUTE SOLUTION
64. THERMODYNAMIC RELATIONS FOR A SYSTEM
IN EQUILIBRIUM
• VOLUME DEPENDENCE OF U
• TEMPERATURE DEPENDENC OF U
• TEMPERATURE DEPENDENCE OF H
• PRESSURE DEPENDENCE OF H
• TEMPERATURE DEPENDENCE OF S
• PRESSURE DEPENDENCE OF S
• TEMPERATURE DEPENDENCE OF G
• PRESSURE DEPENDENCE OF G
67. JOULE EXPERIMENT
• JOULE TRIED TO DETERMINE THE CHANGE OF U IN FUNCTION OF V AT
CONSTANT T BY MEASURING T DURING THE EXPANSION OF A GAS INTO
VACCUM.
• IT IS DEFINED THE JOULE COEFFICIENT AS
• THEN
68. JOULE THOMSON EXPERIMENT
• 10 YEARS LATER JOULE AND THOMSON TRIED TO DETERMINE THE CHANGE OF H
IN FUNCTION OF P AT CONSTANT T BY MEASURING T DURING A CHANGE OF
PRESSURE OF A GAS.
• IT IS DEFINED THE JOULE-THOMSON COEFFICIENT AS
• THEN
69. HEATING AND COOLING BY JOULE-THOMSON
EXPERIMENT
• THE FOR EACH T AND P VALUES IN A JOULE-THOMSON EXPERIMENT, IS
OBTAINED BY FITTING THE EXPERIMENTAL DATA TO AN EXPRESSION OF T IN
FUNCTION OF P CURVE, AND WE FIND THE DERIVATIVE OF THE EXPRESSION IN
POINTS OF INTEREST.
• TO HEAT A GAS USING THE JOULE THOMSON EXPERIMENT WE HAVE TO WORK IN
T-P REGIONS WHERE IS NEGATIVE
• TO COOL A GAS WE HAVE TO WORK IN REGIONS T-P REGIONS WHERE IS
POSITIVE
70. THE JOULE THOMSON COEFFICIENT IN
FUNCTION OF EASILY MEASURABLE SYSTEM
PROPERTIES
71. CALCULATION OF CHANGES IN STATE
FUNCTIONS IN A PROCESS
• CALCULATION OF ENTROPY CHANGE IN FUNCTION OF T AND P
72. CALCULATION OF CHANGES IN STATE
FUNCTIONS IN A PROCESS
• CALCULATION OF ENTHALPY CHANGE IN FUNCTION OF T AND P
• CALCULATION OF INTERNAL ENERGY CHANGE IN FUNCTION OF T AND P
• CALCULATION OF GIBBS ENERGY CHANGE IN FUNCTION OF T AND P
• CALCULATION OF HELMHOLTZ ENERGY CHANGE IN FUNCTION OF T AND P
73. REAL GASES; COMPRESSION FACTORS
• THE Z COMPRESSION FACTOR IS A MEASURE OF THE IDEALITY DEVIATION
• Z BECOMES 1 WHEN DENSITY IS IN THE LIMIT OF ZERO
74. REAL GASES; EQUATIONS OF STATE
• VAN DER WAALS
• REDLICH-KWONG EQUATION
• VIRIAL EQUATION OF STATE (FROM STATISTICAL MECHANICS)
75. REAL GASES; EQUATIONS OF STATE
• EXAMPLE: WHAT IS THE MOLAR VOLUME OF AR(G) AT 250,00K AND 1,0000ATM
• THE COMPRESSION FACTOR CAN BE EXPRESSED IN TERMS OF ATTRACTION AND
REPULSION FACTORS OF THE VAN DER WAALS EQUATION
b IS APPROXIMATELY THE MOLAR VOLUME OF THE LIQUID
76. REAL GASES; EQUATIONS OF STATE
• B IS APPROXIMATELY THE MOLAR VOLUME OF THE LIQUID SO AND WE
CAN EXPRESS THE FOLLOWING EXPANSION
• COMPARING WITH THE VIRIAL EQUATION OF STATE
• AND Z
77. REAL GASES MIXTURES
• TO RELATE A TWO PARAMETER EQUATION OF STATE WITH A REAL GAS MIXTURE
BEHAVIOR WE HAVE TO USE THE MIXING RULE:
• WE NOW REFER TO THE MEAN MOLAR VOLUME OF THE SYSTEM
• AND FOR THE LOW P VIRIAL EQUATION
• THE MIXING RULE FOR NON SIMILAR GASES
78. CONDENSATION OF GASES AND CRITICAL
PROPERTIES
• THE NORMAL TEMPERATURE BOILING POINT AND THE CRITICAL TEMPERATURE ARE BOTH
DEPENDENT ON INTERMOLECULAR FORCES, THEN, THEY ARE CORRELATED
• REMEMBER THAT THE AVERAGE MOLECULAR KINETIC ENERGY IS
• WHAT IS A FLUID? WHAT IS A LIQUID? WHAT IS A GAS? WHAT IS A SUPERCRITICAL FLUID?
80. CALCULATION OF LIQUID VAPOR EQUILIBRIA
• USING REDLICH-KWONG (EOS)
• The condition of liquid vapor equilibria is that a
molecule being transferred from the vapor to the liquid
phase (or visc.) must not change the Gibbs free energy
of the system.
84. THE LAW OF CORRESPONDING STATES
• THE VALUES OF CERTAIN PHYSICAL PROPERTIES OF A GAS DEPENDS ON THE
PROXIMITY OF THE GAS TO ITS CRITICAL STATE
• FOR HE AND H, ADJUSTED CRITICAL PROPERTIES
MUST BE USED
90. REAL GAS THERMODYNAMIC PROPERTIES
CHANGES RELATIVE TO IDEAL VALUES
• IT IS POSSIBLE TO USE ANY OF THE REAL GAS EQUATIONS OF STATE TO FIND
EXPRESSIONS FOR:
91. CHEMICAL POTENTIAL
• FOR A SYSTEM UNDERGOING A COMPOSITION CHANGE DUE TO AN IRREVERSIBLE
REACTION OR MASS TRANSFER (WITHIN THE PHASES OF THE SYSTEM OR
BETWEEN THE SYSTEM AND SURROUNDINGS) THE GIBBS FREE ENERGY IS ALSO A
FUNCTION OF COMPOSITION.
• NOW WE CAN CONSIDER WHAT HAPPENS WITH THE SYSTEM PROPERTIES DUE TO
THE IRREVERSIBLE CHANGE OF MATTER (REMEMBER THAT A CHANGE IN A STATE
BY AN IRREVERSIBLE PROCESS CAN BE CALCULATED SUPPOSING A REVERSIBLE
PROCESS)
93. CHEMICAL POTENTIAL IN Α PHASE SYSTEMS• THE TOTAL FREE GIBBS ENERGY IS EXPRESSED AS:
• CONSIDERING AN INFINITESIMAL CHANGE IN G IN PHASE Α;
• IT IS POSSIBLE TO WRITE AN INFINITESIMAL CHANGE OF G IN THE SYSTEM AS:
• FINALLY
94. MATERIAL EQUILIBRIUM AND CHEMICAL
POTENTIAL
• MATERIAL EQUILIBRIUM
• REVERSIBLE PROCESS
• REMEMBER THAT WHEN EQUILIBRIUM IS REACHED UNDER CONDITIONS OF
CONSTANT T AND P, THEN G IS MINIMIZED AND WHEN THE SYSTEM REACHES THE
EQUILIBRIUM UNDER CONDITIONS OF CONSTANT T AND V, THEN A IS MINIMIZED.
95. WHAT IS CHEMICAL POTENTIAL?
• IT IS AN INTENSIVE PROPERTY
• IT DEPENDS ON T, P AND NI OR XI.
• THE CHEMICAL POTENTIAL OF SUBSTANCE I EXPRESS HOW IS THE CHANGE OF G
WHEN N MOLES OF I ARE ADDED TO THE SOLUTION.
• CHEMICAL POTENTIAL IS STILL DEFINED FOR A SUBSTANCE THAT IS ABSENT FROM
THE SOLUTION.
• FOR THE SIMPLEST SYSTEM:
96. PHASE EQUILIBRIUM
• IN A SEVERAL PHASE SYSTEM THAT IS IN EQUILIBRIUM, WHERE dnJ MOLES OF J ARE
FLOWING FROM PHASE Β TO PHASE Δ THE CONDITION OF PHASE EQUILIBRIUM IS
DEFINED BY:
• SUPPOSE THE SAME PHASE SYSTEM TO BE SPONTANEOUSLY REACHING THE
EQUILIBRIUM AT CONSTANT T AND P:
• ALSO:
97. PHASE EQUILIBRIUM
• IN A SEVERAL PHASE SYSTEM THAT IS IN EQUILIBRIUM, WHERE DNJ MOLES OF ARE
FLOWING FROM PHASE Β TO PHASE Δ THE CONDITION OF PHASE EQUILIBRIUM IS
DEFINED BY:
• SUPPOSE THE SAME PHASE SYSTEM TO BE SPONTANEOUSLY REACHING THE
EQUILIBRIUM AT CONSTANT T AND P:
• ALSO:
98.
99. EXTENT OF REACTION ξ
• FOR ANY REACTION:
• WE DEFINE THE EXTENT OF REACTION Ξ AS THE PROPORTIONALITY CONSTANT
BETWEEN THE STOICHIOMETRIC COEFFICIENTS OF THE REACTION AND CHANGE
IN MOLES OF EACH SUBSTANCE.
101. CHEMICAL POTENTIAL IN IDEAL GASES
• AS PRESSURE GOES TO ZERO, ENTROPY GOES TO INFINITY AND THAT FACT
DEFINES THE BEHAVIOR OF CHEMICAL POTENTIAL IN FUNCTION OF PRESSURE
FOR AN IDEAL GAS.
• AN IDEAL GAS MIXTURE MUST OBEY THE PURE-IDEAL
-GAS CONDITIONS AND ALSO THE LAW OF PARTIAL PRESSURES;
THEY ARE EQUAL TO THE PRESSURES OF PURE GASES AT THE
SAME CONDITIONS:
102. CHEMICAL POTENTIAL IN IDEAL GASES
• AS PRESSURE GOES TO ZERO, ENTROPY GOES TO INFINITY AND THAT FACT
DEFINES THE BEHAVIOR OF CHEMICAL POTENTIAL IN FUNCTION OF PRESSURE
FOR AN IDEAL GAS.
• AN IDEAL GAS MIXTURE MUST OBEY THE PURE-IDEAL
-GAS CONDITIONS AND ALSO THE LAW OF PARTIAL PRESSURES;
THEY ARE EQUAL TO THE PRESSURES OF PURE GASES AT THE
SAME CONDITIONS:
109. PHASE EQUILIBRIUM; THE PHASE RULE
IT MAKE SENSE TO TRY SOLVING THE EQUATIONS THAT RELATE THE INTENSIVE
VARIABLES OF THE SYSTEM TO SPECIFY ITS INTENSIVE THERMODYNAMIC STATE.
IT MEANS TO KNOW ALL THE MOLAR FRACTIONS IN ALL PHASES, T AND P.
THE TOTAL INTENSIVE VARIABLES ARE:
IT IS POSSIBLE TO RELATE THE MOLAR FRACTIONS WITH ONE EQUATION IN EACH
PHASE, EG. SO WE CAN FORGET A NUMBER OF P
VARIABLES BECAUSE THEY ARE DEPENDENT.
IT IS POSSIBLE TO STATE C(P-1) PHASE EQUILIBRIUM CONDITION EQUATIONS, AND
EACH THEM ALLOW US TO FORGET ONE DEPENDENT COMPONENT.
THEN WE HAVE THE GENERAL PHASE RULE THAT LET US TO OBTAIN THE NUMBER
OF INDEPENDENT VARIABLES THAT NEED TO BE FIXED TO SPECIFY THE INTENSIVE
110. PHASE EQUILIBRIUM; THE PHASE RULE
• WHEN THERE IS A REACTION HAPPENING IN THE SYSTEM WE CAN DROP A
NUMBER OF INTENSIVE VARIABLES EQUAL TO THE NUMBER OF CHEMICAL
REACTIONS (R) CONSIDERING THAT EACH OF THEM ALLOWS TO WRITE AN
EQUILIBRIUM CONDITION.
• ALSO WE CAN DROP A NUMBER OF INTENSIVE VARIABLES EQUAL TO SPECIAL
STOICHIOMETRIC OR NEUTRALITY CONDITIONS (A). Independent
Components
111. PHASE EQUILIBRIUM; THE PHASE RULE
• ALSO WE CAN DROP A NUMBER OF INTENSIVE VARIABLES EQUAL TO SPECIAL
STOICHIOMETRIC OR NEUTRALITY CONDITIONS (A).
112. ONE COMPONENT, PHASE EQUILIBRIUM
• ALSO WE CAN DROP A NUMBER OF INTENSIVE VARIABLES EQUAL TO SPECIAL
STOICHIOMETRIC OR NEUTRALITY CONDITIONS (A).
113. ONE COMPONENT, PHASE EQUILIBRIUM
• ALSO WE CAN DROP A NUMBER OF INTENSIVE VARIABLES EQUAL TO SPECIAL
STOICHIOMETRIC OR NEUTRALITY CONDITIONS (A).
114. ONE COMPONENT, PHASE EQUILIBRIUM
• ALSO WE CAN DROP A NUMBER OF INTENSIVE VARIABLES EQUAL TO SPECIAL
STOICHIOMETRIC OR NEUTRALITY CONDITIONS (A).
115. ONE COMPONENT, PHASE EQUILIBRIUM
• OA AND AC SHOW THE BEHAVIOR OF SOLID VAPOR PRESSURE AND LIQUID VAPOR
PRESSURE IN FUNCTION OF TEMPERATURE
116. ENTHALPIES AND ENTROPIES OF PHASE
CHANGES
• STARTING FROM LIQUID VAPOR EQUILIBRIUM, BY LOWERING PRESSURES THE
VAPOR PHASE BECOMES MORE STABLE BECAUSE OF ITS GREAT DECREASING OF
GIBBS FREE ENERGY.
• INCREASING TEMPERATURE FAVORS THE ENTROPY CONTRIBUTION TO THE
MOLAR GIBBS FREE ENERGY AND GAS PHASE IS FAVORED.
• DECREASING TEMPERATURE FAVORS THE ENTHALPY CONTRIBUTION TO THE
MOLAR GIBBS FREE ENERGY AND LIQUID PHASE IS FAVORED.
• THE TROUTON’S RULE
• THE TROUTONS-HILDEBRAND-EVERETT’S RULE
117. ENTHALPIES AND ENTROPIES OF PHASE
CHANGES
• THE TROUTON’S RULE
• THE TROUTONS-HILDEBRAND-EVERETT’S RULE
118. THE CLAPEYRON EQUATION
• THE CLAPEYRON EQUATION PREDICTS THE BEHAVIOR OF THE SLOPE OF PHASE
EQUILIBRIA LINES.
121. THE ANTOINE EQUATION
• THE ANTOINE EQUATION IS AN EMPIRICAL EXPRESSION THAT WORKS VERY WELL
BETWEEN 10 AND 1500 TORR AND RELATES THE VAPOR PRESSURE OF A
SUBSTANCE WITH TEMPERATURE.
123. SOLUTIONS; PARTIAL MOLAR QUANTITIES
• A START ABOVE A PROPERTY MEANS THE PROPERTY OF A PURE SUBSTANCE OR THE
PROPERTY OF A COLLECTION OF PURE SUBSTANCES.
• BUT IN GENERAL THE PROPERTY OF A SOLUTION IS DIFFERENT TO THE PURE
SUBSTANCE PROPERTY SUM
• SO… WE KNOW THAT ALL PROPERTIES OF A SYSTEM ARE FUNCTIONS OF T, P AND NI:
• AND WE DEFINE THE PARTIAL MOLAR VOLUME OF J AS
124. SOLUTIONS; PARTIAL MOLAR QUANTITIES
• REMEMBER THAT FOR A PURE SUBSTANCE SYSTEM, Μ=GM. IN SIMILAR WAY BUT
IT DOES NOT MEANS THAT THE PARTIAL MOLAR VOLUME OF COMPONENT IN A
SOLUTION IS EQUAL TO THE MOLAR VOLUME OF PURE J.
• IF ALL INTENSIVE PROPERTIES ARE FIXED:
DIFFERENTIATION:
AND WE KNOW THAT: OR
SO OR
127. RELATIONS BETWEEN PARTIAL MOLAR
QUANTITIES
• WE KNOW THAT G=H-TS SO:
• ALSO , THEN:
• IN SIMILAR WAY: AND
128. IMPORTANCE OF CHEMICAL POTENTIAL
• CHEMICAL POTENTIAL IS USED TO DEFINE REACTION AND PHASE EQUILIBRIA, BUT
ALSO IS USED TO FIND ALL OTHER PARTIAL MOLAR PROPERTIES AND ALL
THERMODYNAMIC PROPERTIES.
129. MIXING QUANTITIES
• IN MOST CASES WHEN YOU MAKE A SOLUTION, THERE IS DIFFERENCE BETWEEN THE
SUM OF THE PURE COMPONENT PROPERTIES AND THE REAL VALUE OF THE PROPERTY.
WE CALL SUCH A DIFFERENCE MIXING QUANTITIES.
Mixing properties relations
130. DETERMINATION OF MIXING QUANTITIES
• WE CAN FIND THE MIXING VOLUME BY MEASURING THE DEINSITIES OF THE SOLUTION
AND THE PURE COMPONENTS AT P, T AND X. OR WE CAN DIRECTLY MEASURE THE
CHANGE IN VOLUME WHEN A COMPONENT IS ADDED AT CONSTANT T. THE MIXING
ENTHALPY CAN BE FOUND WITH A CONSTANT PRESSURE CALORIMETER
• FOR MIXING GIBBS FREE ENERGY WE HAVE:
135. IDEAL SOLUTIONS
• SOME OF THE MIXTURES THAT CAN BE CONSIDERED IDEAL ARE
• ISOTOPIC MIXTURE
• BENZENE-TOLUENE
•
•
•
136. THERMODYNAMIC FUNCTIONS OF IDEAL
SOLUTIONS
• MIXING GIBBS FREE ENERGY
CYCLOHEXANE-CYCLOPENTANE
BENZENE-DEUTERATED BENZENE
• MIXING ENTROPY
137. CHEMICAL POTENTIAL OF IDEAL SOLUTIONS
• AS NOTED EARLIER
AND WE CAN WRITE
SO
THAT HOLDS ONLY IF
• NOTE THAT ΜI INCREASES AS XI INCREASES
• IN SUMMARY
138. CHEMICAL POTENTIAL OF IDEAL SOLUTIONS
• AS NOTED EARLIER
AND WE CAN WRITE
SO
THAT HOLDS ONLY IF
• NOTE THAT ΜI INCREASES AS XI INCREASES
• IN SUMMARY
139. VAPOR PRESSURE OF IDEAL SOLUTIONS
(RAOULT’S LAW)
• THE CONDITION OF PHASE EQUILIBRIUM IS:
• SUPPOSING A PURE SUBSTANCE SYSTEM:
• USING THE SECOND AND THIRD EQUATIONS:
• REMEMBER THAT THE PROPERTIES OF A LIQUID VARY SLOWLY WITH PRESSURE, SO:
• AND THE RAOULT’S LAW:
140. VAPOR PRESSURE OF IDEAL SOLUTIONS
(RAOULT’S LAW)
• OTHER USEFUL FORM OF THE ROULT’S LAW IS:
• AND FOR TWO COMPONENTS:
• THE LAST FORM MEANS THAT
THE TOTAL VAPOR PRESSURE OF
AN IDEAL SOLUTION VARIES
LINEARLY WITH THE MOLE
FRACTION OF A COMPONENT
IN A TWO COMPONENTS SYSTEM.
141. VAPOR PRESSURE OF IDEAL SOLUTIONS
(RAOULT’S LAW)
• OTHER USEFUL FORM OF THE ROULT’S LAW IS:
• AND FOR TWO COMPONENTS:
• THE LAST FORM MEANS THAT
THE TOTAL VAPOR PRESSURE OF
AN IDEAL SOLUTION VARIES
LINEARLY WITH THE MOLE
FRACTION OF A COMPONENT
IN A TWO COMPONENTS SYSTEM.
Note that an ideal gas mixtu
Is an ideal solution, so:
142. IDEALLY DILUTE SOLUTIONS
• IN AN IDEALLY DILUTE SOLUTIONS, SOLUTE MOLECULES INTERACT ESSENTIALLY
ONLY WITH SOLVENT MOLECULES BECAUSE OF THE HIGH DILUTION OF SOLUTES
At low
concentrations
143. VAPOR PRESSURE IN IDEALLY DILUTE
SOLUTIONS (HENRY’S LAW)
• IN AN IDEALLY DILUTE SOLUTIONS, SOLUTE MOLECULES INTERACT ESSENTIALLY
ONLY WITH SOLVENT MOLECULES BECAUSE OF THE HIGH DILUTION OF SOLUTES
144. VAPOR PRESSURE IN IDEALLY DILUTE
SOLUTIONS (HENRY’S LAW)
• SOLVENTS OBEY RAOULT’S LAW AND SOLUTES HENRY’S LAW
145. SOLUBILITY OF GASES IN LIQUIDS
• FOR GASES THAT ARE SOLUBLE IN A GIVEN LIQUID THE CONCENTRATION OF THE
GAS IS LOW ENOUGH TO CONSIDER THE SOLUTION AS IDEALLY DILUTED. SO HENRY
LAW HOLDS WELL
At low concentrations
146. SOLUBILITY OF GASES IN LIQUIDS
• FOR GASES THAT ARE SOLUBLE IN A GIVEN LIQUID THE CONCENTRATION OF THE
GAS IS LOW ENOUGH TO CONSIDER THE SOLUTION AS IDEALLY DILUTED. SO HENRY
LAW HOLDS WELL
At low concentrations
147. SOLUBILITY OF GASES IN LIQUIDS
• FOR GASES THAT ARE SOLUBLE IN A GIVEN LIQUID THE CONCENTRATION OF THE
GAS IS LOW ENOUGH TO CONSIDER THE SOLUTION AS IDEALLY DILUTED. SO HENRY
LAW HOLDS WELL
At low concentrations
148. VAPOR PRESSURE LOWERING
• IT HOLDS IN SOLUTIONS WHERE THE SOLUTES ARE NON-VOLATILE (SOLID SOLUTES)
Equal to 1 for ideally diluted solutions
Elevation of boling point
150. OSMOTIC PRESSURE
• CHEMICAL POTENTIAL IS LOWER IN THE SOLUTION SO SOLVENT TENDS TO FLOW
THROUGH THE SEMIPERMEABLE MEMBRANE TO EQUATE THE CHEMICAL POTENTIALS
151. OSMOTIC PRESSURE
• CHEMICAL POTENTIAL IS LOWER IN THE SOLUTION SO SOLVENT TENDS TO FLOW
THROUGH THE SEMIPERMEABLE MEMBRANE TO EQUATE THE CHEMICAL POTENTIALS