Introduction to geochemical modeling

Size: px
Start display at page:

Download "Introduction to geochemical modeling"

Transcription

1 Introducton to geochemcal modelng Prof. Dr. Broder J. Merkel Char of Hydrogeology Technsche Unverstät Bergakademe Freberg Germany What determnes the dstrbuton of aquatc speces? Interactons of aquatc speces among themselves (complexaton, redox reactons) of aquatc speces wth gases of aquatc speces wth mneral phases (dssoluton / precptaton, sorpton) Transport processes Decay processes (bologcal degradaton, radoactve decay) 1

2 What determnes the dstrbuton of aquatc speces? Defnton of chemcal reactons thermodynamcal approach mass acton law (MAL) Gbbs free energy knetc approach 2

3 mass acton law aa + bb cc + dd K c d {} C {} D a { A} { B} b mass acton law aa + bb cc + dd cc + dd aa + bb K c d {} C {} D a { A} { B} b a b K* { A} { B} 1 c d {} C {} D K 3

4 Gbbs free energy G H S 0 * T G Gbbs free energy H enthalpy S 0 entropy T temperature Gbbs free energy G 0 G + R T ln c d {} C {} D a { A} { B} b R general gas constant (8.315 J/Kmol) G 0 standard Gbbs free energy at 25 C and 100 kpa 4

5 actvty / concentraton Ionc strenght ( I mol/l ) a f c f onspecfc correcton, < 1 (.e. a < c) I 0.5 m z 2 wth m molalty of a speces z valence of a speces Relatonshp onc strength and actvtycoeffcent f

6 Ion dssocaton theory Debye-Hückel-equaton 2 log(f ) A z I I < mol/kg z valence, A temp.dependng parameter extended Debye-Hückel-equaton A z I log(f ) I < 1 + B a I mol/kg B temp.dependng param., a on spec. param. (dependng on on radus) Güntelberg-equaton 2 I log(f ) 0.5z I < 0.1 mol/kg 1 + 1,4 I Ion dssocaton theory Daves-equaton 2 I log(f ) A z ( 1+ I - 0.3I) I < 0.5mol/kg WATQ-Debye-Hückel-equaton 2 A z I log(f ) + b I I < 1mol/kg 1 + B a I A, B temp.dependng param., a on spec. param. (dependng on on radus) Ion dssocaton theory ends at 1 mol/kg at the latest! 6

7 Specfc Ion Interacton (SIP) model at onc strengths > 1 mol/l (e.g. Ptzer equaton) Ionc strenght mol/l Actvty coeffcent Specff Ion Interacton (SIP) theory onc strenghts > 1 mol/kg e.g. salne waters For comparson: 1 kg water ~ 55.3 mol water Ptzer-equaton Debye-Hückel-equaton + Vral equaton 7

8 Comparson on dssocaton vs specfc on nteracton (SIP Ptzer) theory 1 actvty coeffcent Ptzer DebyeHückel DebyeHückelx ext.debyehückel ext.debyehückelx Güntelberg Güntelbergx Daves Davesx WATQ WATQx Na onc strength [mol/kg] What determnes the dstrbuton of aquatc speces? Interactons of aquatc speces among themselves (complexaton, redox reactons) of aquatc speces wth gases of aquatc speces wth mneral phases (dssoluton / precptaton, sorpton) Transport processes Decay processes (bologcal degradaton, radoactve decay) 8

9 Dssoluton / Precptaton AB A + K { A} { B} { AB} B snce {AB} sold phase 1 Ion actvty product IAP {A} {B} Dependency of the on actvty product temperature partal pressure ph H complex formaton / complex destructon 9

10 Saturaton Index SI SI log(iap) - log (K) log (IAP/K) IAP > K IAP/K > 1 IAP < K IAP/K < 1 Defnes whether a water s over- or under saturated wth respect to a certan mneral Saturaton Index SI SI > 0? Water s super saturated wth respect to a certan mneral. Wll the mneral precptate? Not necessarly, depends on knetcs and boundary condtons SI < 0? Water s under saturated wth respect to certan mneral Wll the mneral dssolve? yes, but dssoluton mght be very slowly 10

11 Autoprotolyss of water H 2 O H + + OH K w + { H }{ OH } { H O} 2 + K W {H } {OH } SATP Standard Ambent Temperature and Pressure ph-value neutral: {H + } {OH - }.e. K W {H + } {OH - } {H + } resp. {H + } 10-7 snce ph -log {H + } -log ph < 7 acd ph > 7 alkalne 11

12 What determnes the dstrbuton of aquatc speces? Interactons of aquatc speces among themselves (complexaton, redox reactons) of aquatc speces wth gases of aquatc speces wth mneral phases (dssoluton / precptaton, sorpton) Transport processes Decay processes (bologcal degradaton, radoactve decay) Henry-Law c K H p xample Ntrogen N 2 : p(n 2 ) 0.78 bar, Henry constant mol/(kg. kpa) at 25 C c mol/kg/kpa kpa 0.5 mmol/kg c 0.5 mmol/kg 2 14 mg/mmol 14 mg/kg temperature [ C] Henry-const. N 2 [ 10-6 mol/kg/kpa] conc. mg/l

13 Henry-Law xample Carbon-Doxde CO 2 Henry constant mol/kg/bar at 25 C (log K H ) 3 Vol% CO 2 n sol gas (0.03 bar) c bar c 1 mmol/kg 44 mg/kg CO 2 rght? CO 2(g) CO 2(aq) CO 2(aq) + H 2 O HCO 3- + H + Ca 2+ + HCO - 3 CaHCO + 3 CO H + HCO - 3 CaCO 3(s) Ca 2+ + CO 2-3 etc. open closed systems open system closed system CO 2 CO 2 CO 2 Wasser Calct Wasser Calct 13

14 What determnes the dstrbuton of aquatc speces? Interactons of aquatc speces among themselves (complexaton, redox reactons) of aquatc speces wth gases of aquatc speces wth mneral phases (dssoluton / precptaton, sorpton) Transport processes Decay processes (bologcal degradaton, radoactve decay) Redox potental - H -value [oxdzed speces] + n[e ] [reduced speces] H 0 + R T [ox] ln n F [red] 0 normal redox potental (V) R general gas constant (8.315 J/K mol) T absolute temperature (K) n number of transfered electrons (e) F FARADAY-constant (96484 C/mol J/V mol) [ox] actvty of oxdzed partners [red] actvty of reduced partners 14

15 15 Redox potental at standard condtons 25 C [ox] [red] log n H [red] [ox] ln F n T R 0 H + [ox] [red] log F n T R H NRNST-potental Redox potental of ph-dependng reactons [ox] [red] log F n T R ph F n T R m H [ox] [red] log F n T R H

16 Redox potental n dependency of temperature H M (T 25 C) Potental varatons at ph-varatons of 1 ph-unt mv be 25 C mv be 20 C mv be 10 C mv be 0 p - concept [oxdzed speces] + n[e ] [reduced speces] log K log [red] [ox] [e - ] n [red] 1 log K log + log n [ox] [e ] log K - log[e ] - [red] log [ox] - n log[e 1 1 [red] logk - log n n [ox] ] - n p - [red] log[e ] logk - log [ox] 1 n log K 1 n log [red] [ox] 16

17 Transformaton pe - H - p - log[e ] F 2.303R T H at standard condtons (25 C) approxmately: p 16.9 H H n Volt measured whth H 2 - probe! at ph : Ranges of H n natural groundwater -400 mv to +800 mv oxdzed condtons partly reduced condtons reduced condtons 17

18 pe-ph-dagram ron (predomnance-dagram) Vald for: The system Fe-H + -OH - Certan onc strenght Certan temeperature Certan ron concentraton 18

Chapter 18, Part 1. Fundamentals of Atmospheric Modeling

Chapter 18, Part 1. Fundamentals of Atmospheric Modeling Overhead Sldes for Chapter 18, Part 1 of Fundamentals of Atmospherc Modelng by Mark Z. Jacobson Department of Cvl & Envronmental Engneerng Stanford Unversty Stanford, CA 94305-4020 January 30, 2002 Types

More information

If two volatile and miscible liquids are combined to form a solution, Raoult s law is not obeyed. Use the experimental data in Table 9.

If two volatile and miscible liquids are combined to form a solution, Raoult s law is not obeyed. Use the experimental data in Table 9. 9.9 Real Solutons Exhbt Devatons from Raoult s Law If two volatle and mscble lquds are combned to form a soluton, Raoult s law s not obeyed. Use the expermental data n Table 9.3: Physcal Chemstry 00 Pearson

More information

Appendix II Summary of Important Equations

Appendix II Summary of Important Equations W. M. Whte Geochemstry Equatons of State: Ideal GasLaw: Coeffcent of Thermal Expanson: Compressblty: Van der Waals Equaton: The Laws of Thermdynamcs: Frst Law: Appendx II Summary of Important Equatons

More information

CHEMISTRY Midterm #2 answer key October 25, 2005

CHEMISTRY Midterm #2 answer key October 25, 2005 CHEMISTRY 123-01 Mdterm #2 answer key October 25, 2005 Statstcs: Average: 70 pts (70%); Hghest: 97 pts (97%); Lowest: 33 pts (33%) Number of students performng at or above average: 62 (63%) Number of students

More information

Electrochemical Equilibrium Electromotive Force

Electrochemical Equilibrium Electromotive Force CHM465/865, 24-3, Lecture 5-7, 2 th Sep., 24 lectrochemcal qulbrum lectromotve Force Relaton between chemcal and electrc drvng forces lectrochemcal system at constant T and p: consder Gbbs free energy

More information

( ) 1/ 2. ( P SO2 )( P O2 ) 1/ 2.

( ) 1/ 2. ( P SO2 )( P O2 ) 1/ 2. Chemstry 360 Dr. Jean M. Standard Problem Set 9 Solutons. The followng chemcal reacton converts sulfur doxde to sulfur troxde. SO ( g) + O ( g) SO 3 ( l). (a.) Wrte the expresson for K eq for ths reacton.

More information

Lecture. Polymer Thermodynamics 0331 L Chemical Potential

Lecture. Polymer Thermodynamics 0331 L Chemical Potential Prof. Dr. rer. nat. habl. S. Enders Faculty III for Process Scence Insttute of Chemcal Engneerng Department of Thermodynamcs Lecture Polymer Thermodynamcs 033 L 337 3. Chemcal Potental Polymer Thermodynamcs

More information

Table 1. Solubility of gypsum and anhydrite adopted in this research and the predicted SI values

Table 1. Solubility of gypsum and anhydrite adopted in this research and the predicted SI values Supporting information: Table 1. Solubility of gypsum and anhydrite adopted in this research and the predicted SI values Sample T ID # ( o C) 16, 65, 74 P NaCl CaSO 4 nh 2 O SI System (psi) (mol/kg H 2

More information

and Statistical Mechanics Material Properties

and Statistical Mechanics Material Properties Statstcal Mechancs and Materal Propertes By Kuno TAKAHASHI Tokyo Insttute of Technology, Tokyo 15-855, JAPA Phone/Fax +81-3-5734-3915 takahak@de.ttech.ac.jp http://www.de.ttech.ac.jp/~kt-lab/ Only for

More information

Mass Transfer Processes

Mass Transfer Processes Mass Transfer Processes S. Majd Hassanzadeh Department of Earth Scences Faculty of Geoscences Utrecht Unversty Outlne: 1. Measures of Concentraton 2. Volatlzaton and Dssoluton 3. Adsorpton Processes 4.

More information

Chemistry 163B Free Energy and Equilibrium E&R ( ch 6)

Chemistry 163B Free Energy and Equilibrium E&R ( ch 6) Chemstry 163B Free Energy and Equlbrum E&R ( ch 6) 1 ΔG reacton and equlbrum (frst pass) 1. ΔG < spontaneous ( natural, rreversble) ΔG = equlbrum (reversble) ΔG > spontaneous n reverse drecton. ΔG = ΔHΔS

More information

Open Systems: Chemical Potential and Partial Molar Quantities Chemical Potential

Open Systems: Chemical Potential and Partial Molar Quantities Chemical Potential Open Systems: Chemcal Potental and Partal Molar Quanttes Chemcal Potental For closed systems, we have derved the followng relatonshps: du = TdS pdv dh = TdS + Vdp da = SdT pdv dg = VdP SdT For open systems,

More information

Introduction to Vapor/Liquid Equilibrium, part 2. Raoult s Law:

Introduction to Vapor/Liquid Equilibrium, part 2. Raoult s Law: CE304, Sprng 2004 Lecture 4 Introducton to Vapor/Lqud Equlbrum, part 2 Raoult s Law: The smplest model that allows us do VLE calculatons s obtaned when we assume that the vapor phase s an deal gas, and

More information

between standard Gibbs free energies of formation for products and reactants, ΔG! R = ν i ΔG f,i, we

between standard Gibbs free energies of formation for products and reactants, ΔG! R = ν i ΔG f,i, we hermodynamcs, Statstcal hermodynamcs, and Knetcs 4 th Edton,. Engel & P. ed Ch. 6 Part Answers to Selected Problems Q6.. Q6.4. If ξ =0. mole at equlbrum, the reacton s not ery far along. hus, there would

More information

University of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2014

University of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2014 Lecture 16 8/4/14 Unversty o Washngton Department o Chemstry Chemstry 452/456 Summer Quarter 214. Real Vapors and Fugacty Henry s Law accounts or the propertes o extremely dlute soluton. s shown n Fgure

More information

Be true to your work, your word, and your friend.

Be true to your work, your word, and your friend. Chemstry 13 NT Be true to your work, your word, and your frend. Henry Davd Thoreau 1 Chem 13 NT Chemcal Equlbrum Module Usng the Equlbrum Constant Interpretng the Equlbrum Constant Predctng the Drecton

More information

Chemical Equilibrium. Chapter 6 Spontaneity of Reactive Mixtures (gases) Taking into account there are many types of work that a sysem can perform

Chemical Equilibrium. Chapter 6 Spontaneity of Reactive Mixtures (gases) Taking into account there are many types of work that a sysem can perform Ths chapter deals wth chemcal reactons (system) wth lttle or no consderaton on the surroundngs. Chemcal Equlbrum Chapter 6 Spontanety of eactve Mxtures (gases) eactants generatng products would proceed

More information

4.2 Chemical Driving Force

4.2 Chemical Driving Force 4.2. CHEMICL DRIVING FORCE 103 4.2 Chemcal Drvng Force second effect of a chemcal concentraton gradent on dffuson s to change the nature of the drvng force. Ths s because dffuson changes the bondng n a

More information

CHEMICAL REACTIONS AND DIFFUSION

CHEMICAL REACTIONS AND DIFFUSION CHEMICAL REACTIONS AND DIFFUSION A.K.A. NETWORK THERMODYNAMICS BACKGROUND Classcal thermodynamcs descrbes equlbrum states. Non-equlbrum thermodynamcs descrbes steady states. Network thermodynamcs descrbes

More information

PART I: MULTIPLE CHOICE (32 questions, each multiple choice question has a 2-point value, 64 points total).

PART I: MULTIPLE CHOICE (32 questions, each multiple choice question has a 2-point value, 64 points total). CHEMISTRY 123-07 Mdterm #2 answer key November 04, 2010 Statstcs: Average: 68 p (68%); Hghest: 91 p (91%); Lowest: 37 p (37%) Number of students performng at or above average: 58 (53%) Number of students

More information

Solution Thermodynamics

Solution Thermodynamics CH2351 Chemcal Engneerng Thermodynamcs II Unt I, II www.msubbu.n Soluton Thermodynamcs www.msubbu.n Dr. M. Subramanan Assocate Professor Department of Chemcal Engneerng Sr Svasubramanya Nadar College of

More information

Gasometric Determination of NaHCO 3 in a Mixture

Gasometric Determination of NaHCO 3 in a Mixture 60 50 40 0 0 5 15 25 35 40 Temperature ( o C) 9/28/16 Gasometrc Determnaton of NaHCO 3 n a Mxture apor Pressure (mm Hg) apor Pressure of Water 1 NaHCO 3 (s) + H + (aq) Na + (aq) + H 2 O (l) + CO 2 (g)

More information

Topic 3 : Thermodynamics

Topic 3 : Thermodynamics GEOL360 LECTURE NOTES: T3 : THERMODYNAMICS 1/20 GEOL360 Topc 3 : Thermodynamcs 3.1 Introducton and vocabulary Thermodynamcs deals wth the physcal and chemcal changes of matter due to work and hear flow

More information

Chem 2A Exam 1. First letter of your last name

Chem 2A Exam 1. First letter of your last name Frst letter of your last name NAME: PERM# INSTRUCTIONS: Fll n your name, perm number and frst ntal of your last name above. Be sure to show all of your work for full credt. Use the back of the page f necessary.

More information

Name: SID: Discussion Session:

Name: SID: Discussion Session: Name: SID: Dscusson Sesson: Chemcal Engneerng Thermodynamcs 141 -- Fall 007 Thursday, November 15, 007 Mdterm II SOLUTIONS - 70 mnutes 110 Ponts Total Closed Book and Notes (0 ponts) 1. Evaluate whether

More information

Solution Thermodynamics

Solution Thermodynamics Soluton hermodynamcs usng Wagner Notaton by Stanley. Howard Department of aterals and etallurgcal Engneerng South Dakota School of nes and echnology Rapd Cty, SD 57701 January 7, 001 Soluton hermodynamcs

More information

Energy, Entropy, and Availability Balances Phase Equilibria. Nonideal Thermodynamic Property Models. Selecting an Appropriate Model

Energy, Entropy, and Availability Balances Phase Equilibria. Nonideal Thermodynamic Property Models. Selecting an Appropriate Model Lecture 4. Thermodynamcs [Ch. 2] Energy, Entropy, and Avalablty Balances Phase Equlbra - Fugactes and actvty coeffcents -K-values Nondeal Thermodynamc Property Models - P-v-T equaton-of-state models -

More information

Solutions Review Worksheet

Solutions Review Worksheet Solutons Revew Worksheet NOTE: Namng acds s ntroduced on pages 163-4 and agan on pages 208-9.. You learned ths and were quzzed on t, but snce acd names are n the Data Booklet you wll not be tested on ths

More information

5.60 Thermodynamics & Kinetics Spring 2008

5.60 Thermodynamics & Kinetics Spring 2008 MIT OpenCourseWare http://ocw.mt.edu 5.60 Thermodynamcs & Knetcs Sprng 2008 For nformaton about ctng these materals or our Terms of Use, vst: http://ocw.mt.edu/terms. 5.60 Sprng 2008 Lecture #29 page 1

More information

II. Equilibrium Thermodynamics. Lecture 8: The Nernst Equation

II. Equilibrium Thermodynamics. Lecture 8: The Nernst Equation II. Equlbrum Thermodynamcs Lecture 8: The Nernst Equaton Notes by MIT Student, re-wrtten by MZB 2014 February 27, 2014 1 Chemcal Actvty The fundamental thermodynamc quantty controllng transport and reactons

More information

Phase equilibria for the oxygen-water system up to elevated temperatures and pressures

Phase equilibria for the oxygen-water system up to elevated temperatures and pressures Phase equlbra for the oxygen-water system up to elevated temperatures and pressures Xaoyan J 1, 2, Xaohua Lu 2, Jnyue Yan 1,3* 1 Department of Chemcal Engneerng and Technology / Energy Processes, Royal

More information

3. Be able to derive the chemical equilibrium constants from statistical mechanics.

3. Be able to derive the chemical equilibrium constants from statistical mechanics. Lecture #17 1 Lecture 17 Objectves: 1. Notaton of chemcal reactons 2. General equlbrum 3. Be able to derve the chemcal equlbrum constants from statstcal mechancs. 4. Identfy how nondeal behavor can be

More information

Environmental Chemodynamics

Environmental Chemodynamics Envronmental Chemodynamcs Instructor: Gregory Möller, Ph.D. Unversty of Idaho Learnng Objectves Lst the thermodynamc functons used to descrbe the energy status of molecules n an envronmental system. Understand

More information

3) Thermodynamic equation to characterize interfaces

3) Thermodynamic equation to characterize interfaces 3) Thermodynamc equaton to characterze nterfaces 3.1) Gbbs Model Realty: rapd contnuous change of chemcal and thermodynamc propertes Replaced by model (constant propertes up to the surface) uv bulk uv

More information

Lecture # 9. Chapter 8. Activity and Systematic Treatment of Equilibrium. K = [Fe(SCN) 2+ ] [Fe 3+ ] [SCN - ] Fe 3+ + SCN - Fe(SCN) 2+

Lecture # 9. Chapter 8. Activity and Systematic Treatment of Equilibrium. K = [Fe(SCN) 2+ ] [Fe 3+ ] [SCN - ] Fe 3+ + SCN - Fe(SCN) 2+ Lecture # 9 Chapter 8 Activity and Systematic Treatment of Equilibrium K = [Fe(SCN) ] [Fe 3 ] [SCN ] Fe 3 SCN Fe(SCN) CaCO 3 (s) Ca (aq) CO K sp =.5 x 10 9 CaCO 3 (s) CO H O Ca HCO 3 CaCO 3 (s) Ca (aq)

More information

EXAM I Comparative Animal Physiology ZOO 424 Fall 2002

EXAM I Comparative Animal Physiology ZOO 424 Fall 2002 EXAM I Comparatve Anmal Physology ZOO 424 Fall 2002 V Eq = RT X o. ln( [ zf [ X ) RT p K[K o pna[na o pcl[cl V = m ln F pk[k pna[na pcl[cl o I = g(v m V eq. ) Q = C m V m Drvng Force = V m V eq. Ionc Speces

More information

CinChE Problem-Solving Strategy Chapter 4 Development of a Mathematical Model. formulation. procedure

CinChE Problem-Solving Strategy Chapter 4 Development of a Mathematical Model. formulation. procedure nhe roblem-solvng Strategy hapter 4 Transformaton rocess onceptual Model formulaton procedure Mathematcal Model The mathematcal model s an abstracton that represents the engneerng phenomena occurrng n

More information

V T for n & P = constant

V T for n & P = constant Pchem 365: hermodynamcs -SUMMARY- Uwe Burghaus, Fargo, 5 9 Mnmum requrements for underneath of your pllow. However, wrte your own summary! You need to know the story behnd the equatons : Pressure : olume

More information

Determination of Structure and Formation Conditions of Gas Hydrate by Using TPD Method and Flash Calculations

Determination of Structure and Formation Conditions of Gas Hydrate by Using TPD Method and Flash Calculations nd atonal Iranan Conference on Gas Hydrate (ICGH) Semnan Unersty Determnaton of Structure and Formaton Condtons of Gas Hydrate by Usng TPD Method and Flash Calculatons H. Behat Rad, F. Varamnan* Department

More information

Available online at Energy Procedia 4 (2011) Energy Procedia 00 (2010) GHGT-10

Available online at   Energy Procedia 4 (2011) Energy Procedia 00 (2010) GHGT-10 Avalable onlne at www.scencedrect.com Energy Proceda 4 (011) 179 186 Energy Proceda 00 (010) 000 000 Energy Proceda www.elsever.com/locate/xxx www.elsever.com/locate/proceda GHGT10 Solublty of Carbon Doxde

More information

A Modulated Hydrothermal (MHT) Approach for the Facile. Synthesis of UiO-66-Type MOFs

A Modulated Hydrothermal (MHT) Approach for the Facile. Synthesis of UiO-66-Type MOFs Supplementary Informaton A Modulated Hydrothermal (MHT) Approach for the Facle Synthess of UO-66-Type MOFs Zhgang Hu, Yongwu Peng, Zx Kang, Yuhong Qan, and Dan Zhao * Department of Chemcal and Bomolecular

More information

Chapter 3 Thermochemistry of Fuel Air Mixtures

Chapter 3 Thermochemistry of Fuel Air Mixtures Chapter 3 Thermochemstry of Fuel Ar Mxtures 3-1 Thermochemstry 3- Ideal Gas Model 3-3 Composton of Ar and Fuels 3-4 Combuston Stochometry t 3-5 The1 st Law of Thermodynamcs and Combuston 3-6 Thermal converson

More information

Outline. Unit Eight Calculations with Entropy. The Second Law. Second Law Notes. Uses of Entropy. Entropy is a Property.

Outline. Unit Eight Calculations with Entropy. The Second Law. Second Law Notes. Uses of Entropy. Entropy is a Property. Unt Eght Calculatons wth Entropy Mechancal Engneerng 370 Thermodynamcs Larry Caretto October 6, 010 Outlne Quz Seven Solutons Second law revew Goals for unt eght Usng entropy to calculate the maxmum work

More information

j) = 1 (note sigma notation) ii. Continuous random variable (e.g. Normal distribution) 1. density function: f ( x) 0 and f ( x) dx = 1

j) = 1 (note sigma notation) ii. Continuous random variable (e.g. Normal distribution) 1. density function: f ( x) 0 and f ( x) dx = 1 Random varables Measure of central tendences and varablty (means and varances) Jont densty functons and ndependence Measures of assocaton (covarance and correlaton) Interestng result Condtonal dstrbutons

More information

Electrochemistry Thermodynamics

Electrochemistry Thermodynamics CHEM 51 Analytcal Electrochemstry Chapter Oct 5, 016 Electrochemstry Thermodynamcs Bo Zhang Department of Chemstry Unversty of Washngton Seattle, WA 98195 Former SEAC presdent Andy Ewng sellng T-shrts

More information

Supplementary Notes for Chapter 9 Mixture Thermodynamics

Supplementary Notes for Chapter 9 Mixture Thermodynamics Supplementary Notes for Chapter 9 Mxture Thermodynamcs Key ponts Nne major topcs of Chapter 9 are revewed below: 1. Notaton and operatonal equatons for mxtures 2. PVTN EOSs for mxtures 3. General effects

More information

Thermo-Calc Software. Modelling Multicomponent Precipitation Kinetics with CALPHAD-Based Tools. EUROMAT2013, September 8-13, 2013 Sevilla, Spain

Thermo-Calc Software. Modelling Multicomponent Precipitation Kinetics with CALPHAD-Based Tools. EUROMAT2013, September 8-13, 2013 Sevilla, Spain Modellng Multcomponent Precptaton Knetcs wth CALPHAD-Based Tools Kasheng Wu 1, Gustaf Sterner 2, Qng Chen 2, Åke Jansson 2, Paul Mason 1, Johan Bratberg 2 and Anders Engström 2 1 Inc., 2 AB EUROMAT2013,

More information

a for save as PDF Chemistry 163B Introduction to Multicomponent Systems and Partial Molar Quantities

a for save as PDF Chemistry 163B Introduction to Multicomponent Systems and Partial Molar Quantities a for save as PDF Chemstry 163B Introducton to Multcomponent Systems and Partal Molar Quanttes 1 the problem of partal mmolar quanttes mx: 10 moles ethanol C 2 H 5 OH (580 ml) wth 1 mole water H 2 O (18

More information

CHAPTER 7 ENERGY BALANCES SYSTEM SYSTEM. * What is energy? * Forms of Energy. - Kinetic energy (KE) - Potential energy (PE) PE = mgz

CHAPTER 7 ENERGY BALANCES SYSTEM SYSTEM. * What is energy? * Forms of Energy. - Kinetic energy (KE) - Potential energy (PE) PE = mgz SYSTM CHAPTR 7 NRGY BALANCS 1 7.1-7. SYSTM nergy & 1st Law of Thermodynamcs * What s energy? * Forms of nergy - Knetc energy (K) K 1 mv - Potental energy (P) P mgz - Internal energy (U) * Total nergy,

More information

Lecture 8. Chapter 7. - Thermodynamic Web - Departure Functions - Review Equations of state (chapter 4, briefly)

Lecture 8. Chapter 7. - Thermodynamic Web - Departure Functions - Review Equations of state (chapter 4, briefly) Lecture 8 Chapter 5 - Thermodynamc Web - Departure Functons - Revew Equatons of state (chapter 4, brefly) Chapter 6 - Equlbrum (chemcal potental) * Pure Component * Mxtures Chapter 7 - Fugacty (chemcal

More information

Groundwater chemistry

Groundwater chemistry Read: Ch. 3, sections 1, 2, 3, 5, 7, 9; Ch. 7, sections 2, 3 PART 14 Groundwater chemistry Introduction Matter present in water can be divided into three categories: (1) Suspended solids (finest among

More information

The ChemSep Book. Harry A. Kooijman Consultant. Ross Taylor Clarkson University, Potsdam, New York University of Twente, Enschede, The Netherlands

The ChemSep Book. Harry A. Kooijman Consultant. Ross Taylor Clarkson University, Potsdam, New York University of Twente, Enschede, The Netherlands The ChemSep Book Harry A. Koojman Consultant Ross Taylor Clarkson Unversty, Potsdam, New York Unversty of Twente, Enschede, The Netherlands Lbr Books on Demand www.bod.de Copyrght c 2000 by H.A. Koojman

More information

Introductory Inorganic Chemistry

Introductory Inorganic Chemistry Introductory Inorganic Chemistry What is Inorganic Chemistry? As: 1s 2 2s 2 2p 6 3s 2 3p 6 4s 2 3d 10 4p 3 Classes of Inorganic Substances Elements Ionic Compounds Covalent Compounds Atomic/Molecular

More information

Chapter 2: Equilibrium Thermodynamics and Kinetics

Chapter 2: Equilibrium Thermodynamics and Kinetics Chapter 2: Equilibrium Thermodynamics and Kinetics Equilibrium Thermodynamics: predicts the concentrations (or more precisely, activities) of various species and phases if a reaction reaches equilibrium.

More information

General Thermodynamics for Process Simulation. Dr. Jungho Cho, Professor Department of Chemical Engineering Dong Yang University

General Thermodynamics for Process Simulation. Dr. Jungho Cho, Professor Department of Chemical Engineering Dong Yang University General Thermodynamcs for Process Smulaton Dr. Jungho Cho, Professor Department of Chemcal Engneerng Dong Yang Unversty Four Crtera for Equlbra μ = μ v Stuaton α T = T β α β P = P l μ = μ l1 l 2 Thermal

More information

Electrical double layer: revisit based on boundary conditions

Electrical double layer: revisit based on boundary conditions Electrcal double layer: revst based on boundary condtons Jong U. Km Department of Electrcal and Computer Engneerng, Texas A&M Unversty College Staton, TX 77843-318, USA Abstract The electrcal double layer

More information

Chapter 2. Electrode/electrolyte interface: ----Structure and properties

Chapter 2. Electrode/electrolyte interface: ----Structure and properties Chapter 2 Electrode/electrolyte nterface: ----Structure and propertes Electrochemcal reactons are nterfacal reactons, the structure and propertes of electrode / electrolytc soluton nterface greatly nfluences

More information

...Thermodynamics. If Clausius Clapeyron fails. l T (v 2 v 1 ) = 0/0 Second order phase transition ( S, v = 0)

...Thermodynamics. If Clausius Clapeyron fails. l T (v 2 v 1 ) = 0/0 Second order phase transition ( S, v = 0) If Clausus Clapeyron fals ( ) dp dt pb =...Thermodynamcs l T (v 2 v 1 ) = 0/0 Second order phase transton ( S, v = 0) ( ) dp = c P,1 c P,2 dt Tv(β 1 β 2 ) Two phases ntermngled Ferromagnet (Excess spn-up

More information

Thermodynamics II. Department of Chemical Engineering. Prof. Kim, Jong Hak

Thermodynamics II. Department of Chemical Engineering. Prof. Kim, Jong Hak Thermodynamcs II Department of Chemcal Engneerng Prof. Km, Jong Hak Soluton Thermodynamcs : theory Obectve : lay the theoretcal foundaton for applcatons of thermodynamcs to gas mxture and lqud soluton

More information

VAPOR LIQUID EQUILIBRIUM DATA GENERATION FOR ACETIC ACID AND p-xylene AT ATMOSPHERIC PRESSURE

VAPOR LIQUID EQUILIBRIUM DATA GENERATION FOR ACETIC ACID AND p-xylene AT ATMOSPHERIC PRESSURE Int. J. Chem. Sc.: 14(3), 2016, 1511-1519 ISSN 0972-768X www.sadgurupublcatons.com VAPOR LIQUID EQUILIBRIUM DATA GENERATION FOR ACETIC ACID AND p-xylene AT ATMOSPHERIC PRESSURE PAWAN KIRAN MALI *,a and

More information

NAME and Section No. it is found that 0.6 mol of O

NAME and Section No. it is found that 0.6 mol of O NAME and Secton No. Chemstry 391 Fall 7 Exam III KEY 1. (3 Ponts) ***Do 5 out of 6***(If 6 are done only the frst 5 wll be graded)*** a). In the reacton 3O O3 t s found that.6 mol of O are consumed. Fnd

More information

Wilbur and Ague 4 WILBUR AND AGUE; APPENDIX DR1. Two-dimensional chemical maps as well as chemical profiles were done at 15 kv using

Wilbur and Ague 4 WILBUR AND AGUE; APPENDIX DR1. Two-dimensional chemical maps as well as chemical profiles were done at 15 kv using DR2006139 Wlbur and Ague 4 WILBUR AND AGUE; APPENDIX DR1 MINERAL ANALYSES Two-dmensonal chemcal maps as well as chemcal profles were done at 15 kv usng the JEOL JXA-8600 electron mcroprobe at Yale Unversty

More information

V. Electrostatics. Lecture 25: Diffuse double layer structure

V. Electrostatics. Lecture 25: Diffuse double layer structure V. Electrostatcs Lecture 5: Dffuse double layer structure MIT Student Last tme we showed that whenever λ D L the electrolyte has a quas-neutral bulk (or outer ) regon at the geometrcal scale L, where there

More information

Diffusion Mass Transfer

Diffusion Mass Transfer Dffuson Mass Transfer General onsderatons Mass transfer refers to mass n transt due to a speces concentraton gradent n a mture. Must have a mture of two or more speces for mass transfer to occur. The speces

More information

Name ID # For relatively dilute aqueous solutions the molality and molarity are approximately equal.

Name ID # For relatively dilute aqueous solutions the molality and molarity are approximately equal. Name ID # 1 CHEMISTRY 212, Lect. Sect. 002 Dr. G. L. Roberts Exam #1/Sprng 2000 Thursday, February 24, 2000 CLOSED BOOK EXM No notes or books allowed. Calculators may be used. tomc masses of nterest are

More information

1st Year Thermodynamic Lectures Dr Mark R. Wormald BIBLIOGRAPHY

1st Year Thermodynamic Lectures Dr Mark R. Wormald BIBLIOGRAPHY M.R.W. -- Thermodynamcs 5 1st Year Thermodynamc Lectures Dr Mark R. Wormald Soluton thermodynamcs :- Lecture 1. Behavour of deal solutons (and solvents). Defnton of dealty. Solvent n dlute solutons, collgatve

More information

Factors that Effect the Rate of Solvation

Factors that Effect the Rate of Solvation Factors that Effect the Rate of Solvation Rate of Solvation there are three ways to increase collisions between the solvent and the solute. agitating the mixture increasing the surface area of the solute

More information

The Dissolution and Transport of Radionuclides from Used Nuclear Fuel in an Underground Repository

The Dissolution and Transport of Radionuclides from Used Nuclear Fuel in an Underground Repository Presented at the COMSOL Conference 2010 Boston The Dssoluton and Transport of adonucldes from Used Nuclear Fuel n an Underground epostory Y A N N I C K B E A U E G A D 1 M A K G O B I E N 2 F A N K G A

More information

Thermodynamics General

Thermodynamics General Thermodynamcs General Lecture 1 Lecture 1 s devoted to establshng buldng blocks for dscussng thermodynamcs. In addton, the equaton of state wll be establshed. I. Buldng blocks for thermodynamcs A. Dmensons,

More information

Vapor-Liquid Equilibria for Water+Hydrochloric Acid+Magnesium Chloride and Water+Hydrochloric Acid+Calcium Chloride Systems at Atmospheric Pressure

Vapor-Liquid Equilibria for Water+Hydrochloric Acid+Magnesium Chloride and Water+Hydrochloric Acid+Calcium Chloride Systems at Atmospheric Pressure Chnese J. Chem. Eng., 4() 76 80 (006) RESEARCH OES Vapor-Lqud Equlbra for Water+Hydrochlorc Acd+Magnesum Chlorde and Water+Hydrochlorc Acd+Calcum Chlorde Systems at Atmospherc Pressure ZHAG Yng( 张颖 ) and

More information

CHEMICAL ENGINEERING

CHEMICAL ENGINEERING Postal Correspondence GATE & PSUs -MT To Buy Postal Correspondence Packages call at 0-9990657855 1 TABLE OF CONTENT S. No. Ttle Page no. 1. Introducton 3 2. Dffuson 10 3. Dryng and Humdfcaton 24 4. Absorpton

More information

Assignment 4. Adsorption Isotherms

Assignment 4. Adsorption Isotherms Insttute of Process Engneerng Assgnment 4. Adsorpton Isotherms Part A: Compettve adsorpton of methane and ethane In large scale adsorpton processes, more than one compound from a mxture of gases get adsorbed,

More information

Redox reactions.

Redox reactions. Redox reactions http://eps.mcgill.ca/~courses/c220/ Redox reactions In a similar way that acids and bases have been defined as proton donors and proton acceptors, reductants and oxidants are defined as

More information

ACCRETE - An explicit algorithm to solve kinetically constrained CO 2 -water-rock interactions

ACCRETE - An explicit algorithm to solve kinetically constrained CO 2 -water-rock interactions Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, 2007 67 ACCRETE - An explct algorthm to solve knetcally constraned

More information

GEOL 414/514 ACTIVITY COEFFICIENTS OF DISSOLVED SPECIES

GEOL 414/514 ACTIVITY COEFFICIENTS OF DISSOLVED SPECIES GEOL 414/514 ACTIVITY COEFFICIENTS OF DISSOLVED SPECIES Chapter 4 LANGMUIR ACTIVITY & ACTIVITY COEFFICIENTS Earlier we studied common ion effect on decreasing the solubility CaCO 3 Ca +2 + CO 3 Add Ca

More information

Tutorials : Corrosion Part 1: Theory and basics

Tutorials : Corrosion Part 1: Theory and basics Tutorials : Corrosion Part 1: Theory and basics Outline A. Definition and effects of corrosion B. General thermodynamics and kinetics in electrochemistry C. Thermodynamics and kinetics in corrosion 2 2/21

More information

Homework Chapter 21 Solutions!!

Homework Chapter 21 Solutions!! Homework Chapter 1 Solutons 1.7 1.13 1.17 1.19 1.6 1.33 1.45 1.51 1.71 page 1 Problem 1.7 A mole sample of oxygen gas s confned to a 5 lter vessel at a pressure of 8 atm. Fnd the average translatonal knetc

More information

Learning Outcomes: At the end of this assignment, students will be able to:

Learning Outcomes: At the end of this assignment, students will be able to: Chemical Equilibria & Sample Preparation Purpose: The purpose of this assignment is to predict how solute concentrations are controlled by chemical equilibria, understand the chemistry involved with sample

More information

Computers&Concrete, An International Journal, Vo. 4, No. 4, August 2007 MECHANISMS OF SULFATE IONIC DIFFUSION IN POROUS CEMENT BASED COMPOSITES

Computers&Concrete, An International Journal, Vo. 4, No. 4, August 2007 MECHANISMS OF SULFATE IONIC DIFFUSION IN POROUS CEMENT BASED COMPOSITES Computers&Concrete, An Internatonal Journal, Vo. 4, No. 4, August 27 MECHANISMS OF SULFATE IONIC DIFFUSION IN POROUS CEMENT BASED COMPOSITES P. Gospodnov, M. Mronova 2, R. Kaandjev * Insttute of Mechancs,

More information

Introduction to Interfacial Segregation. Xiaozhe Zhang 10/02/2015

Introduction to Interfacial Segregation. Xiaozhe Zhang 10/02/2015 Introducton to Interfacal Segregaton Xaozhe Zhang 10/02/2015 Interfacal egregaton Segregaton n materal refer to the enrchment of a materal conttuent at a free urface or an nternal nterface of a materal.

More information

SUPPLEMENTARY INFORMATION

SUPPLEMENTARY INFORMATION Hghly monodsperse core-shell partcles created by sold-state reactons Supplementary Materals Velmr Radmlovc 1,2, Coln Ophus 1,, Emmanuelle A Marqus 3, Marta D Rossell 4, Alfredo Tolley 1,5, Abhay Gautam

More information

Entropy generation in a chemical reaction

Entropy generation in a chemical reaction Entropy generaton n a chemcal reacton E Mranda Área de Cencas Exactas COICET CCT Mendoza 5500 Mendoza, rgentna and Departamento de Físca Unversdad aconal de San Lus 5700 San Lus, rgentna bstract: Entropy

More information

Estimation of the composition of the liquid and vapor streams exiting a flash unit with a supercritical component

Estimation of the composition of the liquid and vapor streams exiting a flash unit with a supercritical component Department of Energ oltecnco d Mlano Va Lambruschn - 05 MILANO Eercses of Fundamentals of Chemcal rocesses rof. Ganpero Gropp Eercse 8 Estmaton of the composton of the lqud and vapor streams etng a unt

More information

( ) Phase equilibrium Some basic principles for phase calculations

( ) Phase equilibrium Some basic principles for phase calculations Chapter From Fundamentals to Propertes 6 Table. Total propertes from an excess approach V U H A G S Pure component Real mxture Ideal mxture Mxng contrbuton Excess property = * v + 0 + * v v (.0) = * u

More information

Numerical Analysis on Si Deoxidation of Molten Ni and Ni Cu Alloy by Quadratic Formalism

Numerical Analysis on Si Deoxidation of Molten Ni and Ni Cu Alloy by Quadratic Formalism Materals ransactons, Vol. 44, No. 9 (2003) pp. 1817 to 1823 #2003 he Japan Insttute of Metals Numercal Analyss on S Deoxdaton of Molten N and N Cu Alloy by Quadratc Formalsm akahro Mk, Fuo Ish and Mtsutaka

More information

Modeling the binding of fulvic acid by goethite: The speciation of adsorbed FA molecules

Modeling the binding of fulvic acid by goethite: The speciation of adsorbed FA molecules Pergamon PII S0016-7037(02)01042-6 Geochmca et Cosmochmca Acta, Vol. 67, No. 8, pp. 1463 1474, 2003 Copyrght 2003 Elsever Scence Ltd Prnted n the USA. All rghts reserved 0016-7037/03 $30.00.00 Modelng

More information

I wish to publish my paper on The International Journal of Thermophysics. A Practical Method to Calculate Partial Properties from Equation of State

I wish to publish my paper on The International Journal of Thermophysics. A Practical Method to Calculate Partial Properties from Equation of State I wsh to publsh my paper on The Internatonal Journal of Thermophyscs. Ttle: A Practcal Method to Calculate Partal Propertes from Equaton of State Authors: Ryo Akasaka (correspondng author) 1 and Takehro

More information

CHEMISTRY Topic #2: Thermochemistry and Electrochemistry What Makes Reactions Go? Fall 2018 Dr. Susan Findlay See Exercises in Topic 8

CHEMISTRY Topic #2: Thermochemistry and Electrochemistry What Makes Reactions Go? Fall 2018 Dr. Susan Findlay See Exercises in Topic 8 CHEMISTRY 2000 Topic #2: Thermochemistry and Electrochemistry What Makes Reactions Go? Fall 208 Dr. Susan Findlay See Exercises in Topic 8 Vapour Pressure of Pure Substances When you leave wet dishes on

More information

First Law: A body at rest remains at rest, a body in motion continues to move at constant velocity, unless acted upon by an external force.

First Law: A body at rest remains at rest, a body in motion continues to move at constant velocity, unless acted upon by an external force. Secton 1. Dynamcs (Newton s Laws of Moton) Two approaches: 1) Gven all the forces actng on a body, predct the subsequent (changes n) moton. 2) Gven the (changes n) moton of a body, nfer what forces act

More information

1. Mathematical models of the chromatographic process

1. Mathematical models of the chromatographic process 1. athematcal models of the chromatographc process - What determnes retenton tme n L? - What causes pea broadenng n L? - Why are the L peas often asymmetrc? - Why s partton chromatography much more popular

More information

Using Spectrophotometric Methods to Determine an Equilibrium Constant Prelab

Using Spectrophotometric Methods to Determine an Equilibrium Constant Prelab Usng Spectrophotometrc Methods to Determne an Equlbrum Constant Prelab 1. What s the purpose of ths experment? 2. Wll the absorbance of the ulbrum mxture (at 447 nm) ncrease or decrease as Fe soluton s

More information

1) Silicon oxide has a typical surface potential in an aqueous medium of ϕ,0

1) Silicon oxide has a typical surface potential in an aqueous medium of ϕ,0 1) Slcon oxde has a typcal surface potental n an aqueous medum of ϕ, = 7 mv n 5 mm l at ph 9. Whch concentraton of catons do you roughly expect close to the surface? What s the average dstance between

More information

Andrzej Anderko OLI Systems Inc. 108 American Road Morris Plains, NJ ABSTRACT

Andrzej Anderko OLI Systems Inc. 108 American Road Morris Plains, NJ ABSTRACT SIMULATION OF CO 3 / S SCALE FORMATION USING TERMODYNAMIC AND ELECTROCEMICAL MODELS Andrzej Anderko OLI Systems Inc. 18 Amercan Road Morrs Plans, NJ 795 ABSTRACT A comprehensve model has been developed

More information

CALCULATION OF DIFFUSION COEFFICIENT OF ION IN MULTICOMPONENT SOLUTION FOR ION MOVEMENT IN CONCRETE

CALCULATION OF DIFFUSION COEFFICIENT OF ION IN MULTICOMPONENT SOLUTION FOR ION MOVEMENT IN CONCRETE CALCULATION OF DIFFUSION COEFFICIENT OF ION IN MULTICOMPONENT SOLUTION FOR ION MOVEMENT IN CONCRETE Worapatt RITTHICHAUY *1, Takafum SUGIYAMA * and Yukkazu TSUJI *3 ABSTRACT: A method for calculatng the

More information

Non-Ideality Through Fugacity and Activity

Non-Ideality Through Fugacity and Activity Non-Idealty Through Fugacty and Actvty S. Patel Deartment of Chemstry and Bochemstry, Unversty of Delaware, Newark, Delaware 19716, USA Corresondng author. E-mal: saatel@udel.edu 1 I. FUGACITY In ths dscusson,

More information

Problem Set #6 solution, Chem 340, Fall 2013 Due Friday, Oct 11, 2013 Please show all work for credit

Problem Set #6 solution, Chem 340, Fall 2013 Due Friday, Oct 11, 2013 Please show all work for credit Problem Set #6 soluton, Chem 340, Fall 2013 Due Frday, Oct 11, 2013 Please show all work for credt To hand n: Atkns Chap 3 Exercses: 3.3(b), 3.8(b), 3.13(b), 3.15(b) Problems: 3.1, 3.12, 3.36, 3.43 Engel

More information

Properties of the living organism. Interaction between living organism and the enviroment. Processing informations. Definitions

Properties of the living organism. Interaction between living organism and the enviroment. Processing informations. Definitions thermodynamcs energy materal Interacton between lvng organsm and the envroment Propertes of the lvng organsm Separaton from the envroment: Strctly controlled energy and materal transport. Changng n the

More information

Chemistry 2000 Lecture 12: Temperature dependence of the equilibrium constant

Chemistry 2000 Lecture 12: Temperature dependence of the equilibrium constant Chemistry 2000 Lecture 12: Temperature dependence of the equilibrium constant Marc R. Roussel February 12, 2019 Marc R. Roussel Temperature dependence of equilibrium February 12, 2019 1 / 15 Temperature

More information

ON A DETERMINATION OF THE INITIAL FUNCTIONS FROM THE OBSERVED VALUES OF THE BOUNDARY FUNCTIONS FOR THE SECOND-ORDER HYPERBOLIC EQUATION

ON A DETERMINATION OF THE INITIAL FUNCTIONS FROM THE OBSERVED VALUES OF THE BOUNDARY FUNCTIONS FOR THE SECOND-ORDER HYPERBOLIC EQUATION Advanced Mathematcal Models & Applcatons Vol.3, No.3, 2018, pp.215-222 ON A DETERMINATION OF THE INITIAL FUNCTIONS FROM THE OBSERVED VALUES OF THE BOUNDARY FUNCTIONS FOR THE SECOND-ORDER HYPERBOLIC EUATION

More information

Oxidation-reduction (redox) reactions

Oxidation-reduction (redox) reactions Oxidation-reduction (redox) reactions Reactions in which there are changes in oxidation state (oxidation number) between reactants and products 2 MnO 4- + 10 Br - + 16 H + 2 Mn 2+ + 5 Br 2 + 8 H 2 O One

More information