9.4 Determination of the reaction order
|
|
- Angelina Lee
- 5 years ago
- Views:
Transcription
1 0,1 0,2 0,3 r 0,1 r 0,2 r 0,3 t
2 Signifiane r = k [A] [B] [C] One we determine the order of a reation, we an write out the rate equation of the reation and tell the details of the kineti harateristis of the reation aording to the rate equation. Otherwise, the rate equation an provide useful information about the mehanism of the reation. Therefore, determination of the order of the reation is a work of great importane.
3 1) Integration method (1) attempt method (trial-and error ) (2) graphi method Methods for determination of reation order 2) Differential method 3) Partial order method (3) half-life method (1) Graphi method (2) Calulation method 4) Isolation method
4 9.4.1 Integration methods The integration methods are to use the integrated rate equation to determine the order of the reation. (1) The attempt method: C 2 H 5 ONa + C 2 H 5 (CH 3 ) 2 SI NaI + C 2 H 5 O C 2 H 5 + S(CH 3 ) 2 r = k[c 2 H 5 ONa] [C 2 H 5 (CH 3 ) 2 SI] A + B P r = k [A] [B] The values of k an be alulated from the seleted integrated equation from a knowledge of initial onentration ( 0 ) and the onentration at various time intervals (). If the reation is of the seleted order of reation, the k at different intervals thus obtained should be the same.
5 Table 1 kineti data for C 2 H 5 ONa + C 2 H 5 (CH 3 ) 2 SI reation at K t/s 10 2 [A]/ mol dm [B] / mol dm
6 Table2 k of the reation of different order, =0 =1 =0 =2 =0 =1 t k =0 =0 =1 =0 =2 = Therefore, the rate equation is: r = k[c 2 H 5 ONa][C 2 H 5 (CH 3 ) 2 SI]
7 Comment: 9.4 Determination of the reation order 1) It is a rather laborious method 2) For reation without simple order, it is impossible to asertain reation order using this method. 3) the experimental error may ause onfusion sometimes.
8 9.4.1 Integration methods (2) The graphi method The linear relationship of reation with different order is different. order zeroth first seond third Linear relationship ~ t ln ~ t 1/ ~ t 1/ 2 ~ t
9 The rate equation of A P an be expressed as Table 3 kineti data for A P. r = k[a] t / s / mol dm -3 t / s / mol dm
10 C / mol dm ln (C / mol dm -3 ) t / s 100 t / s 1/ C(/ mol dm -3 ) / C t / s t / s For ertain onlusion, the reation should be studied in a wide time range.
11 (3) half-life method the half-life of a reation is proportional to the initial onentration of the reatant t k n ln t ln k (1 n)ln 1 1/ 2 0 1/ 2 0 ln t 1/ lnc 0 Graphi method S = 1 (1 n) = 1, n = 2 Therefore, the reation is of seond order.
12 Calulation method ln t ln k (1 n)ln 1/ 2 0 ln t ' ln k (1 n) ln ' 1/ 2 0 n 1 t ln t ' ln 1/ 2 1/ ' NH 4 OCN CO(NH 2 ) 2 0 /mol dm t 1/2 /h n 1 = 2.051, n 2 = n =
13 9.4.2 differential method Use the differential form of the rate equation to determine the order of the reation. r 9.4 Determination of the reation order d dt n ln ln ln k (1)Graphi method r k n Table 4 deomposition of CH 3 CHO CH 4 +CO. Deomposition % r / Pa min Deomposition % r / Pa min
14 lnr / Pa min Linear fitting results: ln r ln k nln lnc / mol dm -3 ln r = ln Therefore, the order of the reation is 2. Linear orrelation oeffiient: 0.998
15 9.4 Determination of the reation order 0, r 1 r 2 0,2 0,3 r 0,1 r 0,2 r 3 r 4 r 0,3 t 1 t 2 t 3 t 4 t Determination of reation order through one experiment. Reation order with respet to time: n t ln r ln k nln Determination of reation order through several parallel experiments. Reation order with respet to onentration: n C ln r t ln k nln 0 0 The method of initial rates is appliable of a wide variety of reations and is partiularly useful in reations that are ompliated by proesses involving intermediate or produts. t
16 (2) Calulation method ln r ln k nln ln r ' ln r ' ln k nln ' n t ln r ' Deomposition % r / Pa min Deomposition % r / Pa min n C ln ln r r ' ' n t = 2.534; 1.952; 2.327; n t =
17 Table 5 relationship between n C and n t. = n t Both intermediate and produt do not affet the reation n > n t Intermediate or produt atalyze the reation < n t Intermediate or produt inhibit the reation r = k[a] [B] r = k[a] [B] [M] n = + n = + +
18 9.4.3 Partial order method r k a A B C ln r ln k ln ln ln A B C ln r ln k (ln A ln B ln C) To plot lnr versus ln A, if a linear relation an obtained, = 0, = 0. If no linear relation an be observed, adjust the value of and until a line an be obtained. The slope of this line is, and the orresponding value of and an be obtained simultaneously.
19 9.4.4 Isolation method ln r ln k ln ln ln A B C ln r ' ln k ln ln ln ' A B C When B and C were ontrolled Three methods: ln 1) Fixation of onentration method; 2) Exess onentration method; 3) Appliation of stoihiometri ratio r r ' ln ' A A
20 9.4.4 Isolation method (1) Fix the onentration of other reatants Rate equation of 2NO + 2H 2 N 2 + 2H 2 O is r = k[no] [H 2 ]. No. Initial pressure / Pa NO H 2 Initial rate
21 9.4.4 Isolation method (2) Exess onentration C 12 H 22 O 11 + H 2 O C 6 H 12 O 6 + C 6 H 12 O 6 r k[c12h 22O 11][H2O] r k'[c H O ] In exess onentration method, the onentration of B and C is made very muh larger than that of A This tehnique is partiularly useful in determining rate onstants for reations involving water in aqueous solution. Pseudo order reation.
22 9.4.4 Isolation method (3) Using stoihiometri ratio aa + bb P Initial onentration 1 b/a Conversion onentration x bx/a Residual onentration 1-x (b/a)(1-x) r = k[a] [B] = k (b/a) (1-x) + = k(b/a) (1-x) n
23 9.4.5 Other methods: 1) Unit of k 2) Dependene of t 1/2 on 0
24 Mind Mapping MindManager imindmap MindMapper XMind FreeMind NovaMind Inspiration Coggle 思维导图又叫心智图, 是表达发散性思维的有效的图形思维工具
9.4 Determination of the reaction order
0,1 0,2 0,3 r 0,1 r 0,2 r 0,3 t Signifiane r = k [A] [B] [C] One we determine the order of a reation, we an write out the rate equation of the reation and tell the details of the kineti harateristis of
More informationGeneral Equilibrium. What happens to cause a reaction to come to equilibrium?
General Equilibrium Chemial Equilibrium Most hemial reations that are enountered are reversible. In other words, they go fairly easily in either the forward or reverse diretions. The thing to remember
More informationChapter 15 Chemical Equilibrium
Chapter 5 Chemial Equilibrium 5. The Conept of Equilibrium Figure: 3. from Chemistry by MMurray & Fey Figure 3.(a) NO 4( g) NO( g) olorless brown we start with reatant, N O 4, so the solution is olorless
More informationChapter 15 Equilibrium. Reversible Reactions & Equilibrium. Reversible Reactions & Equilibrium. Reversible Reactions & Equilibrium 5/27/2014
Amount of reatant/produt 5/7/01 quilibrium in Chemial Reations Lets look bak at our hypothetial reation from the kinetis hapter. A + B C Chapter 15 quilibrium [A] Why doesn t the onentration of A ever
More informationModule 4 Lesson 2 Exercises Answer Key squared square root
Module Lesson Eerises Answer Key 1. The volume is 1 L so onentrations an be done by inspetion. Just substitute values and solve for K [ CO][ HO] K CO H (0.8)(0.8) (0.55) (0.55) K 0.659. [CH ][HS] K [H
More informationChapter 15 Equilibrium. Reversible Reactions & Equilibrium. Reversible Reactions & Equilibrium. Reversible Reactions & Equilibrium 2/3/2014
Amount of reatant/produt //01 quilibrium in Chemial Reations Lets look bak at our hypothetial reation from the kinetis hapter. A + B C Chapter 15 quilibrium [A] Why doesn t the onentration of A ever go
More informationChapter 14. The Concept of Equilibrium and the Equilibrium Constant. We have for the most part depicted reactions as going one way.
Chapter 14 The Conept of Equilibrium and the Equilibrium Constant In hapter 1 we dealt with Physial Equilibrium Physial Changes HO 2 (l) HO 2 (g) In hapter 14 we will learn about Chemial Equilibrium. We
More informationDetermination of the reaction order
5/7/07 A quote of the wee (or amel of the wee): Apply yourself. Get all the eduation you an, but then... do something. Don't just stand there, mae it happen. Lee Iaoa Physial Chemistry GTM/5 reation order
More informationChapter 15: Chemical Equilibrium
Chapter 5: Chemial Equilibrium ahoot!. At eq, the rate of the forward reation is the rate of the reverse reation. equal to, slower than, faster than, the reverse of. Selet the statement that BEST desribes
More informationChemistry (Physical chemistry) Lecture 10.
Chemistry (Physial hemistry) Leture 0. EPM, semester II by Wojieh Chrzanowsi, PhD, DS Wyłady współfinansowane ze środów Unii Europejsiej w ramah EFS, UDA-POKL 04.0.02.-00-37/-00 Absolwent Wydziału Chemiznego
More informationproperties via a simple hydrolysis-based approach
Eletroni Supplementary Material (ESI) for Journal of Materials Chemistry A This journal is The Royal Soiety of Chemistry 01 Supporting Information Salable synthesis of hollow O nanoubes with unique optial
More informationCEE 670 TRANSPORT PROCESSES IN ENVIRONMENTAL AND WATER RESOURCES ENGINEERING. Kinetics Lecture #1
Updated: 8 Deember 0 Print version CEE 670 TRNSPORT PROCESSES IN ENVIRONMENTL ND WTER RESOURCES ENGINEERING Kinetis Leture # Introdution: Simple Rate Laws Clark, 9.-9.6 Brezonik, pp.-39 Introdution Kinetis
More information2 How far? Equilibrium Answers
How far? Equilibrium Answers ratie: pages 37 39 1 Answer is D. Only a hange in temperature harges the value of the equilibrium onstant. Answer is D. [B] /[A] so [B] [A] or [B] [A] 1/ 3 Answer is B. Amounts
More informationChapter 13, Chemical Equilibrium
Chapter 13, Chemial Equilibrium You may have gotten the impression that when 2 reatants mix, the ensuing rxn goes to ompletion. In other words, reatants are onverted ompletely to produts. We will now learn
More informationController Design Based on Transient Response Criteria. Chapter 12 1
Controller Design Based on Transient Response Criteria Chapter 12 1 Desirable Controller Features 0. Stable 1. Quik responding 2. Adequate disturbane rejetion 3. Insensitive to model, measurement errors
More informationJF Physical Chemistry JF CH 1101: Introduction to Physical Chemistry.
JF Physial Chemistry 010-011. JF CH 1101: Introdution to Physial Chemistry. Dr Mike Lyons. Shool of Chemistry Trinity College Dublin. melyons@td.ie A ompendium of past examination questions set on Physial
More informationImprovements in the Modeling of the Self-ignition of Tetrafluoroethylene
Exerpt from the Proeedings of the OMSOL onferene 010 Paris Improvements in the Modeling of the Self-ignition of Tetrafluoroethylene M. Bekmann-Kluge 1 *,. errero 1, V. Shröder 1, A. Aikalin and J. Steinbah
More informationAnswer: Easiest way to determine equilibrium concentrations is to set up a table as follows: 2 SO 2 + O 2 2 SO 3 initial conc change
Problem #1 6 mol of SO and 4 mol of O are plaed into a 1 L flask at temperature, T. The equilibrium onentration of SO is found to be 4 mol/l. Determine K. SO (g) + O (g) SO (g) K = [SO ] / [SO ] [O ] Answer:
More information2. Mass transfer takes place in the two contacting phases as in extraction and absorption.
PRT 11- CONVECTIVE MSS TRNSFER 2.1 Introdution 2.2 Convetive Mass Transfer oeffiient 2.3 Signifiant parameters in onvetive mass transfer 2.4 The appliation of dimensional analysis to Mass Transfer 2.4.1
More information23.1 Tuning controllers, in the large view Quoting from Section 16.7:
Lesson 23. Tuning a real ontroller - modeling, proess identifiation, fine tuning 23.0 Context We have learned to view proesses as dynami systems, taking are to identify their input, intermediate, and output
More information13.4 REDOX STOICHIOMETRY
(d) In a double-blind study, randomly seleted ontrol and experimental groups of 500 volunteers are studied for hanges whih affet their irulatory system. The ontrol group gets an ordinary braelet (plaebo)
More informationHankel Optimal Model Order Reduction 1
Massahusetts Institute of Tehnology Department of Eletrial Engineering and Computer Siene 6.245: MULTIVARIABLE CONTROL SYSTEMS by A. Megretski Hankel Optimal Model Order Redution 1 This leture overs both
More informationHomework Set 4. gas B open end
Homework Set 4 (1). A steady-state Arnold ell is used to determine the diffusivity of toluene (speies A) in air (speies B) at 298 K and 1 atm. If the diffusivity is DAB = 0.0844 m 2 /s = 8.44 x 10-6 m
More informationModelling and Simulation. Study Support. Zora Jančíková
VYSOKÁ ŠKOLA BÁŇSKÁ TECHNICKÁ UNIVERZITA OSTRAVA FAKULTA METALURGIE A MATERIÁLOVÉHO INŽENÝRSTVÍ Modelling and Simulation Study Support Zora Jančíková Ostrava 5 Title: Modelling and Simulation Code: 638-3/
More informationTemperature Control of Batch Suspension Polyvinyl Chloride Reactors
1285 A publiation of CHEMICAL ENGINEERING TRANSACTIONS VOL. 39, 2014 Guest Editors: Petar Sabev Varbanov, Jiří Jaromír Klemeš, Peng Yen Liew, Jun Yow Yong Copyright 2014, AIDIC Servizi S.r.l., ISBN 978-88-95608-30-3;
More informationRESEARCH ON RANDOM FOURIER WAVE-NUMBER SPECTRUM OF FLUCTUATING WIND SPEED
The Seventh Asia-Paifi Conferene on Wind Engineering, November 8-1, 9, Taipei, Taiwan RESEARCH ON RANDOM FORIER WAVE-NMBER SPECTRM OF FLCTATING WIND SPEED Qi Yan 1, Jie Li 1 Ph D. andidate, Department
More informationMean Activity Coefficients of Peroxodisulfates in Saturated Solutions of the Conversion System 2NH 4. H 2 O at 20 C and 30 C
Mean Ativity Coeffiients of Peroxodisulfates in Saturated Solutions of the Conversion System NH 4 Na S O 8 H O at 0 C and 0 C Jan Balej Heřmanova 5, 170 00 Prague 7, Czeh Republi balejan@seznam.z Abstrat:
More informationReactive Transport & Biodegradation Model (Part I)
Projet no.: 51154 (STREP) SEDBARCAH SEDiment BioBARriers for Chlorinated Aliphati Hydroarbons in ground water reahing surfae water Reative Transport & Biodegradation Model (Part I) Harald Kalka Short Leture
More informationCOPYRIGHTED MATERIAL. Gravimetrics. Key Terms. Key Concepts. Words that can be used as topics in essays: accuracy atomic theory
8684-X Ch02.F 2/9/01 7:49 AM Page 23 Gravimetris Key Terms Words that an be used as topis in essays: auray atomi theory density empirial formula extensive property frational rystallization heterogeneous
More informationMass Transfer (Stoffaustausch) Fall 2012
Mass Transfer (Stoffaustaush) Fall Examination 9. Januar Name: Legi-Nr.: Edition Diffusion by E. L. Cussler: none nd rd Test Duration: minutes The following materials are not permitted at your table and
More information2. Failure to submit this paper in its entirety at the end of the examination may result in disqualification.
Memorial University of Newfoundland St. John s, Newfoundland and Labrador Chemistry 101 Intersession 007 Midterm Exam May 8 th, 007 Time: 0 Minutes Name: MUN #: Dr. Peter Warburton READ THE FOLLOWING CAREFULLY!
More informationSTUDY OF FURFURAL FORMATION USING FORMIC ACID. Kaisa Lamminpää & Juha Tanskanen
STUDY OF FURFURAL FORMATION USING FORMIC ACID Kaisa Lamminpää & Juha Tanskanen Department of Proess and Environmental Engineering, University of Oulu Abstrat: Furfural is produed from hemiellulose-rih
More informationCHAPTERS 8-12 BOOKLET-3
CHEMISTRY XI CHAPTERS 8-1 BKLET- Contents: Page No. Chapter 8 Chemial Equilibrium 181-199 Chapter 9 Redox Reations 00-19 Chapter 10 s & p Blok Elements part 1 0-49 Chapter 11 s & p Blok Elements part 50-77
More informationSample Teaching Sequence (Hong Kong Secondary 4 6 Chemistry)
Revised (1 Sept 009 Sample Teahing Suene (Hong Kong Seondary 4 6 Chemistry Topi: Chemial Equilibrium Teahing Suene Content 1.1 Reversible reations Examples of reversible reation; forward reation; reverse
More informationPossibility of Refuse Derived Fuel Fire Inception by Spontaneous Ignition
Possibility of Refuse Derived Fuel Fire Ineption by Spontaneous Ignition Lijing Gao 1, Takashi Tsuruda 1, Takeshi Suzuki 1, Yoshio Ogawa 1, Chihong Liao 1 and Yuko Saso 1 1 National Researh Institute of
More informationThe reaction whose rate constant we are to find is the forward reaction in the following equilibrium. NH + 4 (aq) + OH (aq) K b.
THE RATES OF CHEMICAL REACTIONS 425 E22.3a The reaction for which pk a is 9.25 is NH + 4 aq + H 2Ol NH 3 aq + H 3 O + aq. The reaction whose rate constant we are to find is the forward reaction in the
More informationCalculation of Desorption Parameters for Mg/Si(111) System
e-journal of Surfae Siene and Nanotehnology 29 August 2009 e-j. Surf. Si. Nanoteh. Vol. 7 (2009) 816-820 Conferene - JSSS-8 - Calulation of Desorption Parameters for Mg/Si(111) System S. A. Dotsenko, N.
More informationMillennium Relativity Acceleration Composition. The Relativistic Relationship between Acceleration and Uniform Motion
Millennium Relativity Aeleration Composition he Relativisti Relationship between Aeleration and niform Motion Copyright 003 Joseph A. Rybzyk Abstrat he relativisti priniples developed throughout the six
More information8:30 am 11:30 am 2:30 pm Prof. Memon Prof. Naik Prof. Lucht
1 Last Name First Name CIRCLE YOUR LECTURE BELOW: 8:3 am 11:3 am :3 pm Prof. Memon Prof. Naik Prof. Luht EXAM # 3 INSTRUCTIONS 1. This is a losed book examination. An equation sheet and all needed property
More informationUniversity of Washington Department of Chemistry Chemistry 452/456 Summer Quarter 2011
Homework Assignment #4: Due at 500 pm Monday 8 July,. University of Washington Department of Chemistry Chemistry 45/456 Summer Quarter 0 ) o a very good approximation, ammonia obeys the Bertholet equation
More informationReplacement of gas phase with liquid, for hexamine production
Proeedings of the International Conferene on Ciruits, Systems, Signals Replaement of gas phase with liquid, for hexamine prodution Anita Kovač Kralj¹ Davorin Kralj² Faulty of Chemistry and Chemial Engineering,
More informationThe Effectiveness of the Linear Hull Effect
The Effetiveness of the Linear Hull Effet S. Murphy Tehnial Report RHUL MA 009 9 6 Otober 009 Department of Mathematis Royal Holloway, University of London Egham, Surrey TW0 0EX, England http://www.rhul.a.uk/mathematis/tehreports
More informationCHAPTER 16. Basic Concepts. Basic Concepts. The Equilibrium Constant. Reaction Quotient & Equilibrium Constant. Chemical Equilibrium
Proerties of an Equilibrium System CHAPTER 6 Chemial Equilibrium Equilibrium systems are DYNAMIC (in onstant motion) REVERSIBLE an be aroahed from either diretion Pink to blue Co(H O) 6 Cl ---> > Co(H
More informationHeat exchangers: Heat exchanger types:
Heat exhangers: he proess of heat exhange between two fluids that are at different temperatures and separated by a solid wall ours in many engineering appliations. he devie used to implement this exhange
More information» R ^ " 1 ) A 4 0 JSS MJECT I7K. Nuclear Waste Glass Dissolution: Mechanism, Model and Application. Report to JSS Project Phase IV
» R ^ " 1 ) A 4 0 JSS MJET I7K Nulear Waste Glass Dissolution: Mehanism, Model a Appliation Report to JSS Projet Phase IV Ber Grambow Hahn-Meitner -Institut Berlin GmbH TEHNIAL REPORT A joint Japanese
More informationReview for Exam #2. Specific Heat, Thermal Conductivity, and Thermal Diffusivity. Conduction
Review for Exam # Speifi Heat, Thermal Condutivity, and Thermal Diffusivity Speifi heat ( p ) A measure of how muh energy is required to raise the temperature of an objet Thermal ondutivity (k) A measure
More informationKINETICS OF IRON OXIDE DIRECT REDUCTION BY COAL E.R. ABRIL 1
KINETICS OF IRON OXIDE DIRECT REDUCTION BY COAL E.R. ABRIL 1 CIMM- Av.Velez Sarsfield 1561 C.P.5000 Córdoba, Argentina. aabril@intiemor.gov.ar Abstrat - A new interpretation to the kinetis of iron oxide
More informationIn this problem, we are given the following quantities: We want to find: Equations and basic calculations:
.1 It takes. million tons of oal per year to a 1000-W power plant that operates at a apaity fator of 70%. If the heating value of the oal is 1,000 /lb, alulate the plant s effiieny and the heat rate. In
More informationMC Practice F2 Solubility Equilibrium, Ksp Name
MC Pratie F Solubility Equilibrium, Ksp Name This is pratie - Do NOT heat yourself of finding out what you are apable of doing. Be sure you follow the testing onditions outlined below. DO NOT USE A CALCULATOR.
More informationREVIEW QUESTIONS Chapter 15
hemistry 10 ANSWER EY REVIEW QUESTIONS hapter 15 1. A mixture of 0.10 mol of NO, 0.050 mol of H and 0.10 mol of HO is plaed in a 1.0-L flask and allowed to reah equilibrium as shown below: NO (g) + H (g)
More informationNatural Convection Experiment Measurements from a Vertical Surface
OBJECTIVE Natural Convetion Experiment Measurements from a Vertial Surfae 1. To demonstrate te basi priniples of natural onvetion eat transfer inluding determination of te onvetive eat transfer oeffiient.
More informationImpact of Developer Temperatureon Dissolution Behavior
INTERFACE '97 This paper was published in the proeedings of the Olin Mirolithography Seminar, Interfae '97, pp. 23-212. It is made available as an eletroni reprint with permission of Olin Miroeletroni
More informationStochastic Models for Chemically Reacting Systems Using Polynomial Stochastic Hybrid Systems
Stohasti Models for Chemially Reating Systems Using Polynomial Stohasti Hybrid Systems João Pedro Hespanha and Abhyudai Singh Center for Control Engineering and Computation University of California, Santa
More informationSupporting Information
Supporting Information Olsman and Goentoro 10.1073/pnas.1601791113 SI Materials Analysis of the Sensitivity and Error Funtions. We now define the sensitivity funtion Sð, «0 Þ, whih summarizes the steepness
More informationShrinking core model for the reaction-diffusion problem in thermo-chemical heat storage Lan, S.; Zondag, H.A.; Rindt, C.C.M.
Shrinking ore model for the reation-diffusion problem in thermo-hemial heat storage Lan, S.; Zondag, H.A.; Rindt, C.C.M. Published in: Proeedings of The 13th International Conferene on Energy Storage,
More informationNAME section. BANNER ID N00 MAT 102 LAST EXAM Fall Complete each problem using the answer key general forms file provided.
NAME setion BANNER ID N00 MAT 0 LAST EXAM Fall 0 Comlete eah roblem using the answer key general forms file rovided. Chek-list for eah roblem: ) State the Model used: samling distribution of the means,
More informationModel-based mixture discriminant analysis an experimental study
Model-based mixture disriminant analysis an experimental study Zohar Halbe and Mayer Aladjem Department of Eletrial and Computer Engineering, Ben-Gurion University of the Negev P.O.Box 653, Beer-Sheva,
More informationAnalysis of discretization in the direct simulation Monte Carlo
PHYSICS OF FLUIDS VOLUME 1, UMBER 1 OCTOBER Analysis of disretization in the diret simulation Monte Carlo iolas G. Hadjionstantinou a) Department of Mehanial Engineering, Massahusetts Institute of Tehnology,
More informationProcess engineers are often faced with the task of
Fluids and Solids Handling Eliminate Iteration from Flow Problems John D. Barry Middough, In. This artile introdues a novel approah to solving flow and pipe-sizing problems based on two new dimensionless
More informationLecture 24: Spinodal Decomposition: Part 3: kinetics of the
Leture 4: Spinodal Deoposition: Part 3: kinetis of the oposition flutuation Today s topis Diffusion kinetis of spinodal deoposition in ters of the onentration (oposition) flutuation as a funtion of tie:
More informationAn excess of concentrated hydrochloric acid is added to separate aqueous solutions containing [Cu(H 2 O) 6 ] 2 and [Co(H 2 O) 6 ] 2.
1 An exess of a given reagent is added to eah of the following pairs of aqueous metal ions. For eah metal ion, state the initial olour of the solution and the final oservation that you would make. In eah
More informationKinetics. Mary J. Bojan Chem Rate: change that occurs in a given interval of time.
Kinetics Rates of reaction average rates instantaneous rates Dependence of rate on concentration rate constant rate laws order of the reaction Dependence of rate on time First order Second order Half-life
More informationA Stochastic Analysis of Liquid Mixing in Bubble Column
Amerian Journal of Fluid Dynamis 013, 3(3): 75-79 DOI: 193/j.ajfd.0130303.04 A Stohasti Analysis of Liquid Mixing in Bubble Column Rajeev Parmar, Subrata Kumar Majumder * Department of Chemial Engineering,
More informationMachining. Introduction
Mahining Introdution Mahining aims to generate the shape of the workpiee from a solid body, or to improve the toleranes and surfae finish of a previously formed workpiee, by removing exess material in
More informationf 2 f n where m is the total mass of the object. Expression (6a) is plotted in Figure 8 for several values of damping ( ).
F o F o / k A = = 6 k 1 + 1 + n r n n n RESONANCE It is seen in Figure 7 that displaement and stress levels tend to build up greatly when the oring requeny oinides with the natural requeny, the buildup
More informationFinal Exam: know your section, bring your ID!
Chapter 15: Equilibrium Part 1 Read: BLB 15.1 3 HW: BLB 15:13,14, 21 Supplemental 15:1 4 Know: Chemial Equilibrium Catalysts Equilibrium Constant Equilibrium onstant expression Homogeneous/Heterogeneous
More informationPhysical Laws, Absolutes, Relative Absolutes and Relativistic Time Phenomena
Page 1 of 10 Physial Laws, Absolutes, Relative Absolutes and Relativisti Time Phenomena Antonio Ruggeri modexp@iafria.om Sine in the field of knowledge we deal with absolutes, there are absolute laws that
More informationEvaluation of effect of blade internal modes on sensitivity of Advanced LIGO
Evaluation of effet of blade internal modes on sensitivity of Advaned LIGO T0074-00-R Norna A Robertson 5 th Otober 00. Introdution The urrent model used to estimate the isolation ahieved by the quadruple
More informationAP CHEMISTRY NOTES 7-1 KINETICS AND RATE LAW AN INTRODUCTION
AP CHEMISTRY NOTES 7-1 KINETICS AND RATE LAW AN INTRODUCTION CHEMICAL KINETICS the study of rates of chemical reactions and the mechanisms by which they occur FACTORS WHICH AFFECT REACTION RATES 1. Nature
More informationWe consider the nonrelativistic regime so no pair production or annihilation.the hamiltonian for interaction of fields and sources is 1 (p
.. RADIATIVE TRANSITIONS Marh 3, 5 Leture XXIV Quantization of the E-M field. Radiative transitions We onsider the nonrelativisti regime so no pair prodution or annihilation.the hamiltonian for interation
More informationQCLAS Sensor for Purity Monitoring in Medical Gas Supply Lines
DOI.56/sensoren6/P3. QLAS Sensor for Purity Monitoring in Medial Gas Supply Lines Henrik Zimmermann, Mathias Wiese, Alessandro Ragnoni neoplas ontrol GmbH, Walther-Rathenau-Str. 49a, 7489 Greifswald, Germany
More informationThe simulation analysis of the bridge rectifier continuous operation in AC circuit
Computer Appliations in Eletrial Engineering Vol. 4 6 DOI 8/j.8-448.6. The simulation analysis of the bridge retifier ontinuous operation in AC iruit Mirosław Wiślik, Paweł Strząbała Kiele University of
More informationINTERNATIONAL JOURNAL OF CIVIL AND STRUCTURAL ENGINEERING Volume 2, No 4, 2012
INTERNATIONAL JOURNAL OF CIVIL AND STRUCTURAL ENGINEERING Volume, No 4, 01 Copyright 010 All rights reserved Integrated Publishing servies Researh artile ISSN 0976 4399 Strutural Modelling of Stability
More informationEnhanced Energy Harvesting by Concentration. Gradient-Driven Ion Transport in SBA-15 Mesoporous
Eletroni Supplementary aterial (ESI) for ab on a Chip. This journal is The Royal Soiety of Chemistry 016 Eletroni supplementary information (ESI) Enhaned Energy arvesting by Conentration Gradient-Driven
More informationGreen s function for the wave equation
Green s funtion for the wave equation Non-relativisti ase January 2019 1 The wave equations In the Lorentz Gauge, the wave equations for the potentials are (Notes 1 eqns 43 and 44): 1 2 A 2 2 2 A = µ 0
More informationStudy on the leak test technology of spacecraft using ultrasonic
SINCE2013 Singapore International NDT Conferene & Exhibition 2013, 19-20 July 2013 Study on the test tehnology of spaeraft using ultrasoni Yan Rongxin, Li Weidan Beijing Institute of Spaeraft Environment
More informationSeismic dip estimation based on the two-dimensional Hilbert transform and its application in random noise attenuation a
Seismi dip estimation based on the two-dimensional Hilbert transform and its appliation in random noise attenuation a a Published in Applied Geophysis, 1, 55-63 (Marh 015) Cai Liu, Changle Chen, Dian Wang,
More informationSANDING OF FAGUS SILVATICA L. WOOD PERPENDICULARLY TO THE GRAINS
SANDING OF FAGUS SILVATICA L. WOOD PERPENDICULARLY TO THE GRAINS Bolesław Porankiewiz a* and Grzegorz Wieloh b In this paper the dependenies of the degree of surfae burning and intensity during dis sanding
More informationKinetics of Esterification of Ethylene Glycol with Acetic Acid Using Cation Exchange Resin Catalyst
V. P. YADAV et al., Kinetis of Esterifiation of Ethylene Glyol with Aeti Aid, Chem. Biohem. Eng. Q. 5 (3) 359 366 (011) 359 Kinetis of Esterifiation of Ethylene Glyol with Aeti Aid Using Cation Exhange
More informationResearch Article Finding Solvable Units of Variables in Nonlinear ODEs of ECM Degradation Pathway Network
Hindawi Computational and Mathematial Methods in Mediine Volume 2017, Artile ID 5924270, 15 pages https://doi.org/10.1155/2017/5924270 Researh Artile Finding Solvale Units of Variales in Nonlinear ODEs
More informationEffect of magnetization process on levitation force between a superconducting. disk and a permanent magnet
Effet of magnetization proess on levitation fore between a superonduting disk and a permanent magnet L. Liu, Y. Hou, C.Y. He, Z.X. Gao Department of Physis, State Key Laboratory for Artifiial Mirostruture
More informationA Novel Process for the Study of Breakage Energy versus Particle Size
Geomaterials, 2013, 3, 102-110 http://dx.doi.org/10.4236/gm.2013.33013 Published Online July 2013 (http://www.sirp.org/journal/gm) A Novel Proess for the Study of Breakage Energy versus Partile Size Elias
More informationModeling of Threading Dislocation Density Reduction in Heteroepitaxial Layers
A. E. Romanov et al.: Threading Disloation Density Redution in Layers (II) 33 phys. stat. sol. (b) 99, 33 (997) Subjet lassifiation: 6.72.C; 68.55.Ln; S5.; S5.2; S7.; S7.2 Modeling of Threading Disloation
More informationPREDICTION OF CONCRETE COMPRESSIVE STRENGTH
PREDICTION OF CONCRETE COMPRESSIVE STRENGTH Dunja Mikuli (1), Ivan Gabrijel (1) and Bojan Milovanovi (1) (1) Faulty o Civil Engineering, University o Zagreb, Croatia Abstrat A ompressive strength o onrete
More informationGluing Potential Energy Surfaces with Rare Event Simulations
This is an open aess artile published under an ACS AuthorChoie Liense, whih permits opying and redistribution of the artile or any adaptations for non-ommerial purposes. pubs.as.org/jctc Gluing Potential
More informationON THE MOVING BOUNDARY HITTING PROBABILITY FOR THE BROWNIAN MOTION. Dobromir P. Kralchev
Pliska Stud. Math. Bulgar. 8 2007, 83 94 STUDIA MATHEMATICA BULGARICA ON THE MOVING BOUNDARY HITTING PROBABILITY FOR THE BROWNIAN MOTION Dobromir P. Kralhev Consider the probability that the Brownian motion
More informationCOMPUTER METHODS FOR THE DETERMINATION OF THE CRITICAL PARAMETERS OF POLLUTED INSULATORS
COMPUTER METHODS FOR THE DETERMINATION OF THE CRITICAL PARAMETERS OF POLLUTED INSULATORS I. F. GONOS S. A. SUFLIS F. V. TOPALIS I.A. STATHOPULOS NATIONAL TECHNICAL UNIVERSITY OF ATHENS DEPARTMENT OF ELECTRICAL
More informationLine Radiative Transfer
http://www.v.nrao.edu/ourse/astr534/ineradxfer.html ine Radiative Transfer Einstein Coeffiients We used armor's equation to estimate the spontaneous emission oeffiients A U for À reombination lines. A
More informationPart II SECTION I : One or more options correct Type
[1] JEE Advaned 2013/ Paper -2 Part II SECTION I : One or more options orret Type This setion ontains 8 multiple hoie questions. Eah question has four hoies (A), (B), (C) and (D), out of whih ONE or MORE
More informationAnswers to Coursebook questions Chapter J2
Answers to Courseook questions Chapter J 1 a Partiles are produed in ollisions one example out of many is: a ollision of an eletron with a positron in a synhrotron. If we produe a pair of a partile and
More informationCRITICAL EXPONENTS TAKING INTO ACCOUNT DYNAMIC SCALING FOR ADSORPTION ON SMALL-SIZE ONE-DIMENSIONAL CLUSTERS
Russian Physis Journal, Vol. 48, No. 8, 5 CRITICAL EXPONENTS TAKING INTO ACCOUNT DYNAMIC SCALING FOR ADSORPTION ON SMALL-SIZE ONE-DIMENSIONAL CLUSTERS A. N. Taskin, V. N. Udodov, and A. I. Potekaev UDC
More informationPOROUS CARBON PARTICLE COMBUSTION IN AIR
MCS 7 Chia Laguna, Cagliari, Sardinia, taly, 11-15, 11 POOUS CABON PATCLE COMBUSTON N A V. M. Gremyahkin grema@ipmnet.ru nstitute for Problems in Mehanis, AS, Mosow, ussia Abstrat Theoretial investigation
More informationC H E M I C N E S C I
C H E M I C A L K I N E T S C I 4. Chemical Kinetics Introduction Average and instantaneous Rate of a reaction Express the rate of a reaction in terms of change in concentration Elementary and Complex
More informationFast and Robust Algorithm for Compositional Modeling: Part I Stability Analysis Testing
Fast and Robust Algorithm for Compositional odeling: Part I Stability Analysis Testing Abbas Firoozabadi, SPE, and Huanquan Pan, SPE, Reservoir Engineering Researh Inst. (RERI) Summary Given pressure,
More informationOn the Quantum Theory of Radiation.
Physikalishe Zeitshrift, Band 18, Seite 121-128 1917) On the Quantum Theory of Radiation. Albert Einstein The formal similarity between the hromati distribution urve for thermal radiation and the Maxwell
More information1. A dependent variable is also known as a(n). a. explanatory variable b. control variable c. predictor variable d. response variable ANSWER:
1. A epenent variale is also known as a(n). a. explanatory variale. ontrol variale. preitor variale. response variale FEEDBACK: A epenent variale is known as a response variale. Definition of the Simple
More informationEquilibrium 07 M07_CHSL_SB_IBD_9069_U07.indd /07/ :21
07 Equilibrium Essential ideas 7.1 Many reations are reversible. These reations will reah a state of equilibrium when the rates of the forward reation and reverse reation are equal. The position of equilibrium
More informationRobust Flight Control Design for a Turn Coordination System with Parameter Uncertainties
Amerian Journal of Applied Sienes 4 (7): 496-501, 007 ISSN 1546-939 007 Siene Publiations Robust Flight ontrol Design for a urn oordination System with Parameter Unertainties 1 Ari Legowo and Hiroshi Okubo
More informationDYNAMICS OF CAPILLARY FLOW AND TRANSPORT PROPERTIES IN CARBONATE SEDIMENTARY FORMATION BY TIME-CONTROLLED POROSIMETRY
SCA4-44 /5 DYNAMICS OF CAPILLARY FLOW AND TRANSPORT PROPERTIES IN CARBONATE SEDIMENTARY FORMATION BY TIME-CONTROLLED POROSIMETRY A. Cerepi, Institut EGID-Bordeaux 3, Université Mihel de Montaigne,, allée
More informationLOGISTIC REGRESSION IN DEPRESSION CLASSIFICATION
LOGISIC REGRESSIO I DEPRESSIO CLASSIFICAIO J. Kual,. V. ran, M. Bareš KSE, FJFI, CVU v Praze PCP, CS, 3LF UK v Praze Abstrat Well nown logisti regression and the other binary response models an be used
More information