ACCRETE - An explicit algorithm to solve kinetically constrained CO 2 -water-rock interactions
|
|
- Clifford Owens
- 5 years ago
- Views:
Transcription
1 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, ACCRETE - An explct algorthm to solve knetcally constraned CO 2 -water-rock nteractons Abstract: HELGE HELLEVANG Department of Earth Scence Unversty of Bergen Allégaten 41, 5007 Bergen NORWAY BJØRN KVAMME Department of Physcs and Technology Unversty of Bergen Allégaten 55, 5007 Bergen NORWAY Increasng atmospherc concentratons of CO 2 are suspected to have caused a gradual warmng of the Earths surface. Underground storage of CO 2 n porous rocks or sedments s one feasble opton for reducng emssons. As CO 2 s njected nto the pore space, t dssolves n the reservor pore waters causng an acd corrosve envronment. Ths leads to dssoluton of the rock or sedment framework and precptaton of new mneral phases. The resultant carbonate mnerals are beleved to be a safe storage host over geologcal tmescales. To understand the magntude of these reactons at long tme scales we need to perform numercal smulatons. 3D reactve transport smulatons are most approprate gven the dynamcs and scales of njecton. Ths nvolves solvng a reacton term that commonly conssts of a stff system of ordnary dfferental equatons (ODE). Such systems can be solved wth mplct schemes lke a backward dfferental formulaton (BDF). Ths paper reports an alternatve explct algorthm to solve knetcally constraned mneral reactons n CO 2 -water-rock systems. The algorthm s used on a comprehensve mneral system that s representatve for a Utsra-lke reservor. Smulatons suggest that alumnum at low concentratons causes numercal nstabltes. By ntegratng the mneral reactons over short tme steps we are able to fnd an ndependent functon or constant for alumnum that facltate the calculatons and stll produces relable results. Usng ths method, a 1000 years sngle-grd smulaton can be completed n a few seconds or less. Ths demonstrates that t s possble to solve the stff ODE systems nvolved n the reactve transport equaton usng a smple explct algorthm. Key-words: CO2 storage, Utsra reservor, Slepner njecton ste, mneral knetcs, ACCRETE, stffness, ODE
2 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, Introducton Measurements of atmospherc CO 2 concentraton durng the last decades have revealed a rapd ncrease, and dfferent strateges have been suggested of how to reduce such emssons. Examples are storage n salne aqufers, storage n abandoned ol- and gas felds, storage n deep unmnable coal seams, and storage combned wth enhanced recovery of hydrocarbon from actve ol and gas felds [1]. The probablty of leakage from a storage ste s dependent on several factors lke hydrodynamc condtons, numbers of wells penetratng the reservor, storage depth, and reservor ntegrty [2]. The probablty s also tme dependent n the sense that CO 2 s mmoblzed wth tme by dssoluton nto formaton waters and by reactons wth the sold rock or sedment framework. Informaton on the reactvty of CO 2 wth formaton water and mnerals, and the way ths affects moblty may be solved by reactve transport smulatons (e.g., [3]). A general reactve transport equaton for aqueous component u can be wrtten as: u t r +, (1) ( vu D u) = R( u) where v s a velocty feld, D s the dffuson tensor, and R s a reacton term dependent on the aqueous chemstry u r. The reacton term on the rght-hand sde of equaton (1) s ntmately connected to the transport operators on the left-hand sde. To ease the calculatons a tme-splt to separate the transport from the source term s usually performed. In ths way the transport operators are dscretszed n space and solved separately from the geochemcal reactons, and the source term becomes a set of ordnary dfferental equatons (ODEs) of the form: du dt r = R. (2) ( u) Reacton (2) covers both equlbrum reactons between aqueous components and between the CO 2 gas or lqud phase and the aqueous phase, as well as mneral reactons constraned by ther reacton rates. Equaton (2) must be solved for each grd pont n the spatal mesh. For large 3D reactve transport smulatons the number of grd ponts may exceed hundreds of thousands. Snce equaton (2) usually s attrbuted to some degree of stffness, the equaton represents a bottleneck n solvng the reactve transport equaton, and effectve algorthms, for solvng equaton (2) s strctly necessary. A common approach for such equatons s backward dfferental formulatons (BDF) whch have proven to be very robust. Ths paper presents the smple explct scheme used n the ACCRETE geochemstry code to solve CO 2 -waterrock nteractons. A 1000 years batch smulaton llustrates the use of the code on a typcal CO 2 storage settng. The ntal mneral composton, aqueous chemstry, and physcal condton resemble those found n the Utsra Reservor at the Slepner West njecton ste n the North Sea [4]. For ths knd of problems nvolvng alumnoslcate stablty coupled va aqueous alumnum and slca, and also carbonate stablty coupled va dssolved carbonate, only aqueous alumnum s shown to cause nstablty n the ODE solver for proper step szes. A soluton to ths specfc nstablty problem s here suggested.
3 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, The ACCRETE algorthm ACCRETE s an acronym for Athena Carbon Capture and storage geochemstry module. The development of the code was ntated as the Athena multphase 3D flow research code, developed at the Unversty of Bergen, was expanded to cover reactve transport smulatons of geologcal storage of CO 2 [5, 6]. ACCRETE s executed as an external module for each Athena tme step and updates the geochemstry accordng to drectves gven by Athena. ACCRETE can also be run as a stand-alone batch geochemstry solver as n the case of ths report. The present ACCRETE verson smulates nteractons between 16 mneral phases, 14 aqueous solutes, H 2 O as a solvent, and CO 2 as a separate gaseous or supercrtcal phase. The CO 2 -water-rock solver s dvded nto two man solvers: (1) the aqueous phase specaton solver; and (2) the mneral solver. The two solvers are presented n the followng sectons. 2.1 Thermodynamcs The standard state adopted n ths study s that of unt actvty for pure mnerals and H 2 O at any temperature and pressure. For aqueous speces other than H 2 O, the standard state s unt actvty of speces n a hypothetcal 1 molal soluton referenced to nfnte dluton at any temperature and pressure. For gases, the standard state s for unt fugacty of a hypothetcal deal gas at 1 bar pressure. Thermodynamc data are extrapolated from data calculated wth the SUPCRT92 program [7] usng the dprons96.dat database. 2.2 Solvng the aqueous specaton Aqueous specaton s constraned by fve equlbrum reactons, and the demand for a mass- and charge balanced system. The frst equlbrum that needs to be satsfed s the dssoluton of gaseous or supercrtcal CO 2 nto the aqueous phase CO 2,g/l CO 2,aq. (3) Ths equlbrum s constraned by the bubblepont of CO 2 calculated from x Pyφ v = exp K H RT b CO P 2 ( 1), (4) where P s pressure, y s fracton CO 2 n the gas phase, φ s the fugacty coeffcent, K H s the Henrys law coeffcent for CO 2, v s the average partal molar volume of CO 2 n water at nfnte dluton, and T s temperature. Wth polynomals for both φ(t,p) and K H (T,salnty), expresson (4) provdes good estmates of CO 2 solublty usng a fast non-teratve procedure [8]. The next four equlbra provdes the specaton of aqueous carbon H 2 O + CO 2,aq HCO H +, (5) HCO 3 - CO H +, (6) and Na + + HCO 3 - NaHCO 3. (7) The two frst (5,6) represents the dssocaton of carbonc acd to bcarbonate and carbonate, whereas (7) s needed to reduce the actvty of bcarbonate and acheve a more accurate ph. The last equlbrum reacton (8) s dssocaton of water nto H + and OH -
4 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, H + + OH - H 2 O. (8) In addton to the equlbrum reactons, the aqueous soluton must be charge balanced H n z n = 0, (9) H where n and z are moles and charge of aqueous speces. The fnal requrement s that the aqueous carbon mass balance s satsfed C ( n + n + n + n ) 0 CO = 2, aq HCO3 CO3 NaHCO3,(10) where C s total dssolved carbon. The aqueous specaton s solved teratvely by the requrement that the dfference between n H gven by expressons (9) and n H estmated from reacton (5) n H K1a a =, (11) a CO2, aq H2O γ HCO3 H s less than a predefned lmt ( 9) ( 11) 2 ( nh nh ) < αvaq, (12) where V aq s volume aqueous phase and α s Solvng mneral reactons The extent ξ of a mneral reacton over one tme step can be calculated from ( Ω ) t t ξ = k S 1, (13) where k and S are the knetc constant and reactve surface area of the reacton respectvely, t s the step sze, and the Ω- 1 term s the affnty of the reacton and provdes the reacton drecton. The affnty s gven by: Q Ω =, (14) K where K s the equlbrum constant and Q s the actvty product of the reacton gven by p Q =. (15) vr a r a v p r p The contrbuton of the mneral reactons to the aqueous components can be expressed as: t1 t 0 n k = n k + ξ ν, k, (16) where v s the stochometrc coeffcent for aqueous component k n mneral reacton. Superscrpts t0 and t1 ndcates the ntegraton tmestep t = t1 t0. The ntegraton s accepted f all k aqueous components at tme t1 have concentratons n t1 k 0. If ths s not the case, the ntegraton tme step s reduced and equaton (16) s solved agan. Because one or more of the equatons n the aqueous phase specaton s always affected by the mneral reactons, the specaton algorthm must be called for each ntegrated tme step n the mneral solver. The system s solved when the sum of all ntegraton tme steps equals the predefned smulaton tme. 3 Results and dscusson To show how the ACCRETE algorthms solve CO 2 -water-rock nteractons, the
5 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, mneralogy, chemstry and physcal condtons from the Slepner West njecton ste were chosen (See Table 1 and 2). Three smulatons are presented here and nclude: (1) smulaton where the mneral reactons are ntegrated over short tme steps to avod nstabltes; (2) smulaton wth larger tme steps to llustrate where the nstablty occur and how t affect the smulated results; and (3) smulaton wth large tme steps wth a problem-spesfc soluton to the nstablty problem. The smulatons are all one-grd sngle-phase batch problems wth an aqueous phase n contact wth an nfnte CO 2 reservor. The smulatons cover 1000 years of CO 2 -water-rock nteractons. Table 1 Intal mneral volume fractons and knetc data for Utsra sand. Mneral nformaton s based on data reported by [4], whereas the knetc data (k and S) s from [5] and [6]. Note that knetc constant for K s lsted here. Ths value s recalculated to the ambent temperature usng an Arrhenus relatonshp. Mneral x Utsra k 298 S (mol/m 2 s) (cm 2 /cm 3 ) Calcte x x10 2 Magneste x x10 2 Sderte x x10 2 Dawsonte x x10 4 Albte x x10 2 Mcroclne x x10 3 Quartz x x10 2 Chalcedony x x10 4 Kaolnte x x10 4 Clnochlore- 14A x x10 4 Daphnte-14A x x104 Muscovte x x10 4 Phlogopte x x10 4 Annte x x10 4 Labradorte x x10 2 Gbbste x x10 3 Porosty Smulated CO 2 storage system The smulated system comprses chemstry, mneralogy and physcal propertes (T, P) that correspond to nformaton publshed from the Slepner CO 2 njecton ste, Norwegan North Sea (see [4]). The mneralogy s lsted n Table 1 together wth data used n the knetc expresson (13). Some mnerals are proxes for smlar mnerals observed n the sedments. The aqueous chemstry s based on data from the Slepner njecton ste presented n [3]. Orgnal data n [3] s slghtly modfed to provde a charge balanced soluton at the startng ph of 7.1 shown n Table 2. Table 2 Intal aqueous chemstry (molefractons). Component X (mol/mol) H + /ph 1.963x10-9 / 7.1 Ca CO 2,aq x HCO x10-5 Na Cl Al x CO x10-8 Mg SO 2,aq 3.514x10-9 K x10-6 Fe x10-5 NaHCO Temporal evoluton of mneral carbonates and aqueous components The frst smulaton ntegrates the mneral reactons over short tme steps to avod nstabltes n the stff mneral solver. Ths smulaton s slow, but provdes relable estmates of the reactvty of the system. Selected mneral data and aqueous chemstry of the smulaton are presented n Fg. 1.
6 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, SO 2,aq Reacton (17) s one of several that leads to formaton of Fe-, Mg-, and NaAl(OH)- carbonates. The second part of Fg. 1 shows the temporal evoluton of aqueous components. As expected, ph falls to a steady value around 5.0, and the system reach a steady non-equlbrum state after a few tens of years. Fg. 1. Temporal evoluton of carbonate mnerals (upper) and dssolved aqueous speces (lower) for short tme steps n the ntegraton of mneral reactons. One of the man ssues concerned wth safe long-term storage of CO 2 s to quantfy the amount of stable sold carbonates that form. The mnerals presented n Fg. 1 are those carbonates ncluded n the present smulatons and the total amount of carbon formed. Carbonates form as a consequence of a lowerng of ph as CO 2 s njected, whch n turn trggers dssoluton of prmary mnerals present n the sedment. Ths s llustrated n equaton (17) for the dssoluton of phlogopte and formaton of magneste (MgCO 3 ). Fg. 2. Temporal evoluton of carbonate mnerals (upper) and dssolved aqueous speces (lower) for large tme steps n the ntegraton of mneral reactons. Phl.,s + 10H + + 6HCO 3 - MgCO 3,s + 3CO 2,aq + 9H 2 O + K + + Al 3+ (17)
7 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, Stffness problems caused by Alfluctuatons The second smulaton llustrates stffness problems n the algorthm caused by ntegratng mneral reactons over large tme steps. Ths smulaton s fast but data produced are less relable. Results are presented n Fg. 2 that shows carbonate formaton and aqueous chemstry wth tme. The man dfference between the former smulaton and ths one s that sgnfcantly less sold carbonate forms. The explanaton s found n the aqueous chemstry. Whereas most aqueous components show a temporal evoluton smlar to the frst case, aqueous alumnum fluctuates. The reason for ths can be found by comparng the concentraton of alumnum wth the extent of alumnum-contanng reactons ξ ν, Al η = (18) t0 nal The concentraton of alumnum as a functon of η s presented n Fg. 3. Ths fgure shows that as η approach the lmt - 1 from rght, the alumnum at tme t1 may shft by orders of magntude. Snce 11 of the 16 ncluded reactons that represent a typcal CO 2 -water-rock smulaton, are dependent on the alumnum concentraton, both wth respect to reacton rate and drecton, a rapd change may nduce nstablty. In ths case, several fast reactng mnerals that are close to equlbrum, lke dawsonte, oscllate between saturaton states because of the rapdly changng aqueous alumnum. These rapd changes n saturaton states move the system n the rght drecton wth respect to the global thermodynamc drvng force, but at a slower rate than n a stable system. The reactvty of ndvdual mneral reactons, lke the formaton of dawsonte, are n addton wrongly estmated. Values of η for other aqueous speces are never close to -1, and alumnum s hence the only cause of nstablty n the system. Fg. 3. As η s approached from the rght hand sde the concentraton of alumnum at tme t1 drops rapdly. 3.4 A soluton to the present stffness problem For the present system, whch s representatve for a CO 2 -water-rock system wth a few proxes replacng the natural reservor mnerals, alumnum s dentfed as the cause of a major stffness problem. If we go back to the frst smulaton we notce that alumnum shows some varaton durng the frst 50 to 100 years, and gradually converge towards a steady value. Usng ths nformaton, we can attempt to remove the alumnum as a varable n the system and replace ts temporal evoluton wth an ndependent functon. Snce most of the 1000 years smulated shows constant alumnum concentraton, the frst attempt s to smulate the system usng a constant concentraton. From the frst smulaton we notce that alumnum reach a steady mole fracton of approxmately 2.0x An attempt usng ths value as a constant and ntegratng the mneral reactons over
8 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, the same large tme steps as used n the second smulaton s presented n Fg. 4 and compared to the frst smulaton. The upper part of the fgure shows a drect comparson to the frst smulaton, whereas the lower part plots the dfference between smulated values. It s evdent that t s a very close agreement wth the two smulatons. The frst 100 years dawsonte formaton s overestmated, and also the total carbon formed. Ths corresponds to frst perod of the frst smulaton where alumnum shows most varaton. Durng the last 900 years the two smulatons converges to values that are ndstngushable for all mnerals. An even closer ft would be obtaned f a proper functon s constructed for the frst 100 years. Ths would be trval, but s not necessary f the focus s a long-term reactve system. tmes can probably be decreased further down to sub-seconds. The burden of solvng the reacton term n a large 3D system would then be feasble. For example, the penalty for ncludng the reacton term n the 1944 grds 3D system smulated n [5] and [6] could be less than 30 mnutes. We stll have to keep n mnd however that a mult-grd dynamc system s dfferent than the batch smulatons presented here. For example to fnd one functon approproate for all grds at all tmes may be mpossble. 3.5 Are large reactve transport smulatons possble wth the present algorthm? Wthout a soluton to the stffness caused by aqueous alumnum, a sngle grd smulatons that covers 1000 years of CO 2 - water-rock nteractons, lke the frst smulaton n the present report, requres two or three days of smulaton tme. A 1000 years large-scale reactve transport smulaton s therefore not achevable. On the other hand, by replacng the alumnum varable wth a proper ndependent functon, the runtme may decrease to a few seconds. For example, the executon tme for the thrd smulaton on a standard 32 Bt Lnux archtecture, ncludng extensve formatted reportng, s approxmately 50 seconds. By restrctng the amount of reportng, usng a nonformatted output, and ncreasng the ntegraton step sze further, executon Fg. 4. Comparson between the frst smulaton (R1) and the thrd smulaton (R2), the latter wth the varable alumnum replaced by a constant value.
9 Proceedngs of the 3rd WSEAS Internatonal Conference on Mathematcal Bology and Ecology, Gold Coast, Queensland, Australa, January 17-19, Concluson Solvng reactve transport equatons, lke equaton (1), commonly nvolve a reacton term that can cause some degree of stffness. Ths creates a bottleneck for solvng the reactve transport equatons. Ths work presents a typcal problem that nvolves solvng stff systems of ODE. Ths knd of problems s usually solved by some mplct routne lke a BDF solver. In ths report the ACCRETE geochemstry code attempts to solve the reacton term usng smple explct routnes. The report presents both panstakngly slow calculatons ntegratng the mneral reactons over short tme steps, and fast smulatons wth large tme step szes. By comparng the dfferent smulatons, aqueous alumnum s dentfed as the cause of nstablty for ths system. By replacng the varable alumnum wth an ndependent functon or constant, we can reproduce the long-term reactvty of CO 2 at a low CPU cost. A 1000 years snglegrd batch smulaton becomes possble n a few seconds or even less. Acknowledgements We are grateful to Ncola McLoughln for helpful comments on the language. Ths report was made possble by fnancal support from Norsk Hydro and the Research Councl of Norway through grant /210 and the BIODEEP project. References: [1] Gale, J., Geologcal storage of CO2: What do we know, where are the gaps and what more needs to be done? Energy, Vol. 29, 2004, [2] Bouchard, R., and Delaytermoz, A., Integrated path towards geologcal storage. Energy, Vol. 29, 2004, [3] Johnson, J.W., Ntao, J.J., and Knauss, K.G., Reactve transport modelng of CO 2 storage n salne aqufers to elucdate fundamental processes, trappng mechansms and sequestraton parttonng. In: Banes, S.J., and Worden, R.H. (eds), Geologcal Storage of Carbon Doxde. Geologcal Socety, London, Specal Publcatons, Vol. 233, 2004, [4] Chadwck, R.A., Zwegel, P., Gregersen, U., Krby, G.A., Holloway, S., and Johannessen, P.N., Geologcal reservor characterzaton of a CO 2 storage ste: The Utsra Sand, Slepner, northern North Sea. Energy, Vol. 29, 2004, [5] Hellevang, H., Khattr, S.K., Fladmark, G.E., and Kvamme, B., CO 2 storage n the Utsra Formaton ATHENA 3D reactve transport smulatons. Submtted to Basn Research. [6] Khattr, S.K., Hellevang, H., Fladmark, G.E., and Kvamme, B., Deposton of Green House Gases by Compostonal Smulator: Long Term Reactve Transport of CO 2 n the Sand of Utsra. Submtted to Journal of Transport n Porous Meda. [7] Johnson, J. W., Oelkers, E. H., Helgeson, H. C., SUPCRT92: a software package for calculatng the standard molal thermodynamc propertes of mnerals, gases, aqueous speces, and reactons from 1 to 5000 bar and 0 to 1000 C. Comput. Geosc. Vol. 18, No.7, 1992, [8] Hellevang, H., and Kvamme, B., ACCRETE Geochemstry solver for CO 2 -water-rock nteractons, Paper, GHGT8, Trondhem, Norway, June 19-22, 2006.
( ) 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 informationChapter 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 informationSupplementary 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 informationIntroduction 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 informationOpen 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 informationNumerical Solution of Ordinary Differential Equations
Numercal Methods (CENG 00) CHAPTER-VI Numercal Soluton of Ordnar Dfferental Equatons 6 Introducton Dfferental equatons are equatons composed of an unknown functon and ts dervatves The followng are examples
More informationmodeling of equilibrium and dynamic multi-component adsorption in a two-layered fixed bed for purification of hydrogen from methane reforming products
modelng of equlbrum and dynamc mult-component adsorpton n a two-layered fxed bed for purfcaton of hydrogen from methane reformng products Mohammad A. Ebrahm, Mahmood R. G. Arsalan, Shohreh Fatem * Laboratory
More informationNAME 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 informationAppendix B. The Finite Difference Scheme
140 APPENDIXES Appendx B. The Fnte Dfference Scheme In ths appendx we present numercal technques whch are used to approxmate solutons of system 3.1 3.3. A comprehensve treatment of theoretcal and mplementaton
More informationNUMERICAL DIFFERENTIATION
NUMERICAL DIFFERENTIATION 1 Introducton Dfferentaton s a method to compute the rate at whch a dependent output y changes wth respect to the change n the ndependent nput x. Ths rate of change s called the
More informationNON-CENTRAL 7-POINT FORMULA IN THE METHOD OF LINES FOR PARABOLIC AND BURGERS' EQUATIONS
IJRRAS 8 (3 September 011 www.arpapress.com/volumes/vol8issue3/ijrras_8_3_08.pdf NON-CENTRAL 7-POINT FORMULA IN THE METHOD OF LINES FOR PARABOLIC AND BURGERS' EQUATIONS H.O. Bakodah Dept. of Mathematc
More informationIf 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(Online First)A Lattice Boltzmann Scheme for Diffusion Equation in Spherical Coordinate
Internatonal Journal of Mathematcs and Systems Scence (018) Volume 1 do:10.494/jmss.v1.815 (Onlne Frst)A Lattce Boltzmann Scheme for Dffuson Equaton n Sphercal Coordnate Debabrata Datta 1 *, T K Pal 1
More informationNumerical Heat and Mass Transfer
Master degree n Mechancal Engneerng Numercal Heat and Mass Transfer 06-Fnte-Dfference Method (One-dmensonal, steady state heat conducton) Fausto Arpno f.arpno@uncas.t Introducton Why we use models and
More informationbetween 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 informationWilbur 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 informationCHAPTER 5 NUMERICAL EVALUATION OF DYNAMIC RESPONSE
CHAPTER 5 NUMERICAL EVALUATION OF DYNAMIC RESPONSE Analytcal soluton s usually not possble when exctaton vares arbtrarly wth tme or f the system s nonlnear. Such problems can be solved by numercal tmesteppng
More informationFormal solvers of the RT equation
Formal solvers of the RT equaton Formal RT solvers Runge- Kutta (reference solver) Pskunov N.: 979, Master Thess Long characterstcs (Feautrer scheme) Cannon C.J.: 970, ApJ 6, 55 Short characterstcs (Hermtan
More information5.68J/10.652J Feb 13, 2003 Numerical Solution to Kinetic Equations Lecture 1
5.68J/10.652J Feb 13, 2003 Numercal Soluton to Knetc Equatons Lecture 1 The Problem We want to solve 1 dn l H = ν r ( T l V dt n, ) Transport of ' ' out of V Eq.(1) Where n s the number of moles of speces,
More information6.3.4 Modified Euler s method of integration
6.3.4 Modfed Euler s method of ntegraton Before dscussng the applcaton of Euler s method for solvng the swng equatons, let us frst revew the basc Euler s method of numercal ntegraton. Let the general from
More informationAdiabatic Sorption of Ammonia-Water System and Depicting in p-t-x Diagram
Adabatc Sorpton of Ammona-Water System and Depctng n p-t-x Dagram J. POSPISIL, Z. SKALA Faculty of Mechancal Engneerng Brno Unversty of Technology Techncka 2, Brno 61669 CZECH REPUBLIC Abstract: - Absorpton
More informationMass 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 informationNote 10. Modeling and Simulation of Dynamic Systems
Lecture Notes of ME 475: Introducton to Mechatroncs Note 0 Modelng and Smulaton of Dynamc Systems Department of Mechancal Engneerng, Unversty Of Saskatchewan, 57 Campus Drve, Saskatoon, SK S7N 5A9, Canada
More informationAdditional Codes using Finite Difference Method. 1 HJB Equation for Consumption-Saving Problem Without Uncertainty
Addtonal Codes usng Fnte Dfference Method Benamn Moll 1 HJB Equaton for Consumpton-Savng Problem Wthout Uncertanty Before consderng the case wth stochastc ncome n http://www.prnceton.edu/~moll/ HACTproect/HACT_Numercal_Appendx.pdf,
More informationOn the correction of the h-index for career length
1 On the correcton of the h-ndex for career length by L. Egghe Unverstet Hasselt (UHasselt), Campus Depenbeek, Agoralaan, B-3590 Depenbeek, Belgum 1 and Unverstet Antwerpen (UA), IBW, Stadscampus, Venusstraat
More informationEnergy, 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 informationDifference Equations
Dfference Equatons c Jan Vrbk 1 Bascs Suppose a sequence of numbers, say a 0,a 1,a,a 3,... s defned by a certan general relatonshp between, say, three consecutve values of the sequence, e.g. a + +3a +1
More informationA Hybrid Variational Iteration Method for Blasius Equation
Avalable at http://pvamu.edu/aam Appl. Appl. Math. ISSN: 1932-9466 Vol. 10, Issue 1 (June 2015), pp. 223-229 Applcatons and Appled Mathematcs: An Internatonal Journal (AAM) A Hybrd Varatonal Iteraton Method
More informationSolutions 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 informationGasometric 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 informationCinChE 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 informationEstimation 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 information3. 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 informationThe Study of Teaching-learning-based Optimization Algorithm
Advanced Scence and Technology Letters Vol. (AST 06), pp.05- http://dx.do.org/0.57/astl.06. The Study of Teachng-learnng-based Optmzaton Algorthm u Sun, Yan fu, Lele Kong, Haolang Q,, Helongang Insttute
More informationNormally, in one phase reservoir simulation we would deal with one of the following fluid systems:
TPG4160 Reservor Smulaton 2017 page 1 of 9 ONE-DIMENSIONAL, ONE-PHASE RESERVOIR SIMULATION Flud systems The term sngle phase apples to any system wth only one phase present n the reservor In some cases
More informationPh.D. Qualifying Examination in Kinetics and Reactor Design
Knetcs and Reactor Desgn Ph.D.Qualfyng Examnaton January 2006 Instructons Ph.D. Qualfyng Examnaton n Knetcs and Reactor Desgn January 2006 Unversty of Texas at Austn Department of Chemcal Engneerng 1.
More informationCOMPARISON OF SOME RELIABILITY CHARACTERISTICS BETWEEN REDUNDANT SYSTEMS REQUIRING SUPPORTING UNITS FOR THEIR OPERATIONS
Avalable onlne at http://sck.org J. Math. Comput. Sc. 3 (3), No., 6-3 ISSN: 97-537 COMPARISON OF SOME RELIABILITY CHARACTERISTICS BETWEEN REDUNDANT SYSTEMS REQUIRING SUPPORTING UNITS FOR THEIR OPERATIONS
More informationAppendix 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 informationUniversity 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 informationa 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 informationA Robust Method for Calculating the Correlation Coefficient
A Robust Method for Calculatng the Correlaton Coeffcent E.B. Nven and C. V. Deutsch Relatonshps between prmary and secondary data are frequently quantfed usng the correlaton coeffcent; however, the tradtonal
More informationLecture 21: Numerical methods for pricing American type derivatives
Lecture 21: Numercal methods for prcng Amercan type dervatves Xaoguang Wang STAT 598W Aprl 10th, 2014 (STAT 598W) Lecture 21 1 / 26 Outlne 1 Fnte Dfference Method Explct Method Penalty Method (STAT 598W)
More information...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 informationSome modelling aspects for the Matlab implementation of MMA
Some modellng aspects for the Matlab mplementaton of MMA Krster Svanberg krlle@math.kth.se Optmzaton and Systems Theory Department of Mathematcs KTH, SE 10044 Stockholm September 2004 1. Consdered optmzaton
More informationUncertainty and auto-correlation in. Measurement
Uncertanty and auto-correlaton n arxv:1707.03276v2 [physcs.data-an] 30 Dec 2017 Measurement Markus Schebl Federal Offce of Metrology and Surveyng (BEV), 1160 Venna, Austra E-mal: markus.schebl@bev.gv.at
More informationThe 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 informationChapter 5. Solution of System of Linear Equations. Module No. 6. Solution of Inconsistent and Ill Conditioned Systems
Numercal Analyss by Dr. Anta Pal Assstant Professor Department of Mathematcs Natonal Insttute of Technology Durgapur Durgapur-713209 emal: anta.bue@gmal.com 1 . Chapter 5 Soluton of System of Lnear Equatons
More informationDETERMINATION OF TEMPERATURE DISTRIBUTION FOR ANNULAR FINS WITH TEMPERATURE DEPENDENT THERMAL CONDUCTIVITY BY HPM
Ganj, Z. Z., et al.: Determnaton of Temperature Dstrbuton for S111 DETERMINATION OF TEMPERATURE DISTRIBUTION FOR ANNULAR FINS WITH TEMPERATURE DEPENDENT THERMAL CONDUCTIVITY BY HPM by Davood Domr GANJI
More informationIntroduction to geochemical modeling
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
More informationin a horizontal wellbore in a heavy oil reservoir
498 n a horzontal wellbore n a heavy ol reservor L Mngzhong, Wang Ypng and Wang Weyang Abstract: A novel model for dynamc temperature dstrbuton n heavy ol reservors s derved from and axal dfference equatons
More informationMMA and GCMMA two methods for nonlinear optimization
MMA and GCMMA two methods for nonlnear optmzaton Krster Svanberg Optmzaton and Systems Theory, KTH, Stockholm, Sweden. krlle@math.kth.se Ths note descrbes the algorthms used n the author s 2007 mplementatons
More informationThe equation of motion of a dynamical system is given by a set of differential equations. That is (1)
Dynamcal Systems Many engneerng and natural systems are dynamcal systems. For example a pendulum s a dynamcal system. State l The state of the dynamcal system specfes t condtons. For a pendulum n the absence
More informationSolution 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 informationOne-sided finite-difference approximations suitable for use with Richardson extrapolation
Journal of Computatonal Physcs 219 (2006) 13 20 Short note One-sded fnte-dfference approxmatons sutable for use wth Rchardson extrapolaton Kumar Rahul, S.N. Bhattacharyya * Department of Mechancal Engneerng,
More informationLecture 12: Discrete Laplacian
Lecture 12: Dscrete Laplacan Scrbe: Tanye Lu Our goal s to come up wth a dscrete verson of Laplacan operator for trangulated surfaces, so that we can use t n practce to solve related problems We are mostly
More informationELASTIC WAVE PROPAGATION IN A CONTINUOUS MEDIUM
ELASTIC WAVE PROPAGATION IN A CONTINUOUS MEDIUM An elastc wave s a deformaton of the body that travels throughout the body n all drectons. We can examne the deformaton over a perod of tme by fxng our look
More informationLecture Note 3. Eshelby s Inclusion II
ME340B Elastcty of Mcroscopc Structures Stanford Unversty Wnter 004 Lecture Note 3. Eshelby s Incluson II Chrs Wenberger and We Ca c All rghts reserved January 6, 004 Contents 1 Incluson energy n an nfnte
More informationConsistency & Convergence
/9/007 CHE 374 Computatonal Methods n Engneerng Ordnary Dfferental Equatons Consstency, Convergence, Stablty, Stffness and Adaptve and Implct Methods ODE s n MATLAB, etc Consstency & Convergence Consstency
More informationBasic concept of reactive flows. Basic concept of reactive flows Combustion Mixing and reaction in high viscous fluid Application of Chaos
Introducton to Toshhsa Ueda School of Scence for Open and Envronmental Systems Keo Unversty, Japan Combuston Mxng and reacton n hgh vscous flud Applcaton of Chaos Keo Unversty 1 Keo Unversty 2 What s reactve
More informationWorkshop: Approximating energies and wave functions Quantum aspects of physical chemistry
Workshop: Approxmatng energes and wave functons Quantum aspects of physcal chemstry http://quantum.bu.edu/pltl/6/6.pdf Last updated Thursday, November 7, 25 7:9:5-5: Copyrght 25 Dan Dll (dan@bu.edu) Department
More informationTensor Smooth Length for SPH Modelling of High Speed Impact
Tensor Smooth Length for SPH Modellng of Hgh Speed Impact Roman Cherepanov and Alexander Gerasmov Insttute of Appled mathematcs and mechancs, Tomsk State Unversty 634050, Lenna av. 36, Tomsk, Russa RCherepanov82@gmal.com,Ger@npmm.tsu.ru
More informationCHEM 112 Exam 3 Practice Test Solutions
CHEM 11 Exam 3 Practce Test Solutons 1A No matter what temperature the reacton takes place, the product of [OH-] x [H+] wll always equal the value of w. Therefore, f you take the square root of the gven
More informationTransfer Functions. Convenient representation of a linear, dynamic model. A transfer function (TF) relates one input and one output: ( ) system
Transfer Functons Convenent representaton of a lnear, dynamc model. A transfer functon (TF) relates one nput and one output: x t X s y t system Y s The followng termnology s used: x y nput output forcng
More informationNovember 5, 2002 SE 180: Earthquake Engineering SE 180. Final Project
SE 8 Fnal Project Story Shear Frame u m Gven: u m L L m L L EI ω ω Solve for m Story Bendng Beam u u m L m L Gven: m L L EI ω ω Solve for m 3 3 Story Shear Frame u 3 m 3 Gven: L 3 m m L L L 3 EI ω ω ω
More informationElectrochemical 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 informationDesign Equations. ν ij r i V R. ν ij r i. Q n components. = Q f c jf Qc j + Continuous Stirred Tank Reactor (steady-state and constant phase)
Desgn Equatons Batch Reactor d(v R c j ) dt = ν j r V R n dt dt = UA(T a T) r H R V R ncomponents V R c j C pj j Plug Flow Reactor d(qc j ) dv = ν j r 2 dt dv = R U(T a T) n r H R Q n components j c j
More informationThermo-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 informationPhysics 5153 Classical Mechanics. D Alembert s Principle and The Lagrangian-1
P. Guterrez Physcs 5153 Classcal Mechancs D Alembert s Prncple and The Lagrangan 1 Introducton The prncple of vrtual work provdes a method of solvng problems of statc equlbrum wthout havng to consder the
More informationEntropy 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 informationLecture 12. Transport in Membranes (2)
Lecture 12. Transport n embranes (2) odule Flow Patterns - Perfect mxng - Countercurrent flow - Cocurrent flow - Crossflow embrane Cascades External ass-transfer Resstances Concentraton Polarzaton and
More information(1) The saturation vapor pressure as a function of temperature, often given by the Antoine equation:
CE304, Sprng 2004 Lecture 22 Lecture 22: Topcs n Phase Equlbra, part : For the remander of the course, we wll return to the subject of vapor/lqud equlbrum and ntroduce other phase equlbrum calculatons
More informationResearch Article Green s Theorem for Sign Data
Internatonal Scholarly Research Network ISRN Appled Mathematcs Volume 2012, Artcle ID 539359, 10 pages do:10.5402/2012/539359 Research Artcle Green s Theorem for Sgn Data Lous M. Houston The Unversty of
More informationSecond Order Analysis
Second Order Analyss In the prevous classes we looked at a method that determnes the load correspondng to a state of bfurcaton equlbrum of a perfect frame by egenvalye analyss The system was assumed to
More informationLecture 7: Boltzmann distribution & Thermodynamics of mixing
Prof. Tbbtt Lecture 7 etworks & Gels Lecture 7: Boltzmann dstrbuton & Thermodynamcs of mxng 1 Suggested readng Prof. Mark W. Tbbtt ETH Zürch 13 März 018 Molecular Drvng Forces Dll and Bromberg: Chapters
More informationA new Approach for Solving Linear Ordinary Differential Equations
, ISSN 974-57X (Onlne), ISSN 974-5718 (Prnt), Vol. ; Issue No. 1; Year 14, Copyrght 13-14 by CESER PUBLICATIONS A new Approach for Solvng Lnear Ordnary Dfferental Equatons Fawz Abdelwahd Department of
More informationSMOOTHED PARTICLE HYDRODYNAMICS MODEL FOR REACTIVE TRANSPORT AND MINERAL PRECIPITATION
CMWRXVI SMOOTHED PARTICLE HYDRODYNAMICS MODEL FOR REACTIVE TRANSPORT AND MINERAL PRECIPITATION A. TARTAKOVSKY 1, T. SCHEIBE 1, G. REDDEN 2, P. MEAKIN 2, Y. FANG 1. 1 Pacfc Northwest Natonal Laboratory,
More informationHigh resolution entropy stable scheme for shallow water equations
Internatonal Symposum on Computers & Informatcs (ISCI 05) Hgh resoluton entropy stable scheme for shallow water equatons Xaohan Cheng,a, Yufeng Ne,b, Department of Appled Mathematcs, Northwestern Polytechncal
More informationLecture 10 Support Vector Machines II
Lecture 10 Support Vector Machnes II 22 February 2016 Taylor B. Arnold Yale Statstcs STAT 365/665 1/28 Notes: Problem 3 s posted and due ths upcomng Frday There was an early bug n the fake-test data; fxed
More informationSTUDY ON TWO PHASE FLOW IN MICRO CHANNEL BASED ON EXPERI- MENTS AND NUMERICAL EXAMINATIONS
Blucher Mechancal Engneerng Proceedngs May 0, vol., num. www.proceedngs.blucher.com.br/evento/0wccm STUDY ON TWO PHASE FLOW IN MICRO CHANNEL BASED ON EXPERI- MENTS AND NUMERICAL EXAMINATIONS Takahko Kurahash,
More informationProblem adapted reduced models based on Reaction-Diffusion Manifolds (REDIMs)
Problem adapted reduced models based on Reacton-Dffuson Manfolds (REDIMs) V Bykov, U Maas Thrty-Second Internatonal Symposum on ombuston, Montreal, anada, 3-8 August, 8 Problem Statement: Smulaton of reactng
More informationNon-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 informationTurbulence classification of load data by the frequency and severity of wind gusts. Oscar Moñux, DEWI GmbH Kevin Bleibler, DEWI GmbH
Turbulence classfcaton of load data by the frequency and severty of wnd gusts Introducton Oscar Moñux, DEWI GmbH Kevn Blebler, DEWI GmbH Durng the wnd turbne developng process, one of the most mportant
More informationA PROCEDURE FOR SIMULATING THE NONLINEAR CONDUCTION HEAT TRANSFER IN A BODY WITH TEMPERATURE DEPENDENT THERMAL CONDUCTIVITY.
Proceedngs of the th Brazlan Congress of Thermal Scences and Engneerng -- ENCIT 006 Braz. Soc. of Mechancal Scences and Engneerng -- ABCM, Curtba, Brazl,- Dec. 5-8, 006 A PROCEDURE FOR SIMULATING THE NONLINEAR
More informationChapter - 2. Distribution System Power Flow Analysis
Chapter - 2 Dstrbuton System Power Flow Analyss CHAPTER - 2 Radal Dstrbuton System Load Flow 2.1 Introducton Load flow s an mportant tool [66] for analyzng electrcal power system network performance. Load
More informationCHEMICAL 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 informationName 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 informationAn identification algorithm of model kinetic parameters of the interfacial layer growth in fiber composites
IOP Conference Seres: Materals Scence and Engneerng PAPER OPE ACCESS An dentfcaton algorthm of model knetc parameters of the nterfacal layer growth n fber compostes o cte ths artcle: V Zubov et al 216
More informationConstitutive Modelling of Superplastic AA-5083
TECHNISCHE MECHANIK, 3, -5, (01, 1-6 submtted: September 19, 011 Consttutve Modellng of Superplastc AA-5083 G. Gulano In ths study a fast procedure for determnng the constants of superplastc 5083 Al alloy
More informationCollege of Computer & Information Science Fall 2009 Northeastern University 20 October 2009
College of Computer & Informaton Scence Fall 2009 Northeastern Unversty 20 October 2009 CS7880: Algorthmc Power Tools Scrbe: Jan Wen and Laura Poplawsk Lecture Outlne: Prmal-dual schema Network Desgn:
More informationLeast squares cubic splines without B-splines S.K. Lucas
Least squares cubc splnes wthout B-splnes S.K. Lucas School of Mathematcs and Statstcs, Unversty of South Australa, Mawson Lakes SA 595 e-mal: stephen.lucas@unsa.edu.au Submtted to the Gazette of the Australan
More informationAvailable 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 informationChapter 13: Multiple Regression
Chapter 13: Multple Regresson 13.1 Developng the multple-regresson Model The general model can be descrbed as: It smplfes for two ndependent varables: The sample ft parameter b 0, b 1, and b are used to
More informationFinite Element Modelling of truss/cable structures
Pet Schreurs Endhoven Unversty of echnology Department of Mechancal Engneerng Materals echnology November 3, 214 Fnte Element Modellng of truss/cable structures 1 Fnte Element Analyss of prestressed structures
More informationUncertainty in measurements of power and energy on power networks
Uncertanty n measurements of power and energy on power networks E. Manov, N. Kolev Department of Measurement and Instrumentaton, Techncal Unversty Sofa, bul. Klment Ohrdsk No8, bl., 000 Sofa, Bulgara Tel./fax:
More informationElectrical 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 informationAPPENDIX 2 FITTING A STRAIGHT LINE TO OBSERVATIONS
Unversty of Oulu Student Laboratory n Physcs Laboratory Exercses n Physcs 1 1 APPEDIX FITTIG A STRAIGHT LIE TO OBSERVATIOS In the physcal measurements we often make a seres of measurements of the dependent
More informationFTCS Solution to the Heat Equation
FTCS Soluton to the Heat Equaton ME 448/548 Notes Gerald Recktenwald Portland State Unversty Department of Mechancal Engneerng gerry@pdx.edu ME 448/548: FTCS Soluton to the Heat Equaton Overvew 1. Use
More informationProcess Modeling. Improving or understanding chemical process operation is a major objective for developing a dynamic process model
Process Modelng Improvng or understandng chemcal process operaton s a major objectve for developng a dynamc process model Balance equatons Steady-state balance equatons mass or energy mass or energy enterng
More informationResource Allocation with a Budget Constraint for Computing Independent Tasks in the Cloud
Resource Allocaton wth a Budget Constrant for Computng Independent Tasks n the Cloud Wemng Sh and Bo Hong School of Electrcal and Computer Engneerng Georga Insttute of Technology, USA 2nd IEEE Internatonal
More informationSimulated Power of the Discrete Cramér-von Mises Goodness-of-Fit Tests
Smulated of the Cramér-von Mses Goodness-of-Ft Tests Steele, M., Chaselng, J. and 3 Hurst, C. School of Mathematcal and Physcal Scences, James Cook Unversty, Australan School of Envronmental Studes, Grffth
More information