A novel mathematical model of formulation design of emulsion explosive

Size: px
Start display at page:

Download "A novel mathematical model of formulation design of emulsion explosive"

Transcription

1 J. Iran. Chem. Res. 1 (008) Journal of the Iranan Chemcal Research IAU-ARAK A novel mathematcal model of formulaton desgn of emulson explosve Mng Lu *, Qfa Lu Chemcal Engneerng College, Nanjng Unversty of Scence and Technology, Nanjng 10094, PR Chna Receved 3 June 008; receved n revsed form 9 September 008; accepted 14 September 008 Abstract A novel mathematcal model has been developed to ad the formulaton of emulson explosves. Ths mathematcal model calculated heat of exploson, oxygen balance and raw materal cost as a functon of explosve ngredents, and the soluton of the mathematcal model was obtaned by a MS Excel program. The effects of the dfferent content of NH 4 NO 3, NaNO 3, H O, and span-80 and composte fuel ol on the heat of exploson and the specfc volume of emulson explosve were dscussed based on the proposed mathematcal model. The results show that (1) wth the ncreasng of the content of NH 4 NO 3, the heat of exploson and the specfc volume ncrease. () The better content of NaNO 3, H O and Span-80 n the formulaton of emulson explosve are 7%~9%, 9%~10%, 1.5%~% respectvely, and ths formulaton results n an oxygen balance of zero or close to zero. Keywords: Mathematcal model, Emulson explosve, Exploson, oxygen balance 1. Introducton The commercal emulson explosves developed n the early 1s [1, ] are very mportant blastng means because of ther hgher detonaton parameters and better water-resstant characterstcs [3, 4]. Ammonum ntrate used n the emulson explosves s the prmary oxdzer and sodum ntrate s frequently added to mprove the propertes of the oxdzer soluton. The ol phase conssts of varous mneral ols, waxes, and even polymers. Explosve propertes are usually prmary consderaton durng the formulaton of emulson explosves. A non-optmum explosve formulaton should result n a poor explosve performance and an ncrease n noxous fumes, all of whch are detrmental to the overall blastng objectves. The object of the present work s to develop a novel mathematcal model to mprove the formulaton desgn of emulson explosves. The contents of ths paper are as follows: 1) a novel computer aded method for the formulaton of emulson explosves; ) the establshment of a mathematcal model for the formulaton of emulson explosves; 3) the computer aded formulaton desgn and optmzaton of emulson explosve and, 4) numerous reasonable formulatons wth an oxygen balance of zero or close to zero.. Mathematcal model * Correspondng author. Tel.: ; fax: E-mal address: lumng30@16.com (M. Lu)

2 M. Lu and Q. Lu / J. Iran. Chem. Res. 1 (008) Explosve propertes are usually prmary consderaton durng the formulaton of ndustral explosves [5]. Because explosve propertes are a functon of the heat of exploson (Qv) of an explosve, the heat of exploson s selected as the prmary fgure of mert for our mathematcal model. Emulson explosves consst of Carbon (C), Hydrogen (H), Oxygen (O), Ntrogen (N) and sodum (Na). The general emprcal formula of emulson explosves s C a H b O c N d Na h. Assumed the specfc emprcal formula s, C a H b O c N d Na h, then the molar mass of component s gven as m and the molar number of component n 1 kg explosve s 10x /m, where x s the percent mass content of component. The equaton for the reacton of an explosve contanng C, H, O, N, Na s gven n equaton (1). C a H b O c N d Na h = n = 1 10x m ( C h b d NaO + H O + N b h + (a c + + ) CO a H b O c N d Na h b + ( c a) CO h ) (1) where a = Σ10a x /m, b = Σ10b x /m, c = Σ10c x /m,and d = Σ10d x /m, h = Σ10h x /m, The mathematcal formula (where the prmary fgure of mert s Heat of Exploson) s shown n equaton (). h b d b + h Qv = H Na ( ) O + H H O + H N + c a H n b h 10 + (a c + + ) H CO x H m = 1 CO () The mathematcal expressons for the other fgures of mert are: Oxygen Balance (OB) = Σa x = 100η Varable Sum (VS) = Σx = 100 Cost Sum (CS) = Σp x = p/10 Lower lmts and upper lmts = s < x <t, where = 1,,, n. In ths mathematcal model the followng defntons are employed: H f Heat of formaton for the ngredents, the entre explosve or explosve products (kj.mol -1 ) g the molar number of the exploson products; the content of component of the explosve; x m the molar mass of component ; a the oxygen balance of component (%); η the oxygen balance of the explosve (%); p raw materal cost of component, RMBy.t -1 ; p raw materal cost of explosve, RMBy.t -1 ; s lower lmt of component ; (%); t upper lmt of component ; (%). 3. Mathematcal expresson for formulatons of emulson explosves 3.1 Ingredents of emulson explosves and ther chemcal parameters The oxdzer of emulson explosves s usually made up of ammonum ntrate and sodum ntrate, and the fuel s a mxture of varous mneral ols and waxes. The formula, molar mass, heat of formaton, oxygen balance and raw materal cost of these components are gven n Table 1 [6-9].

3 35 M. Lu and Q. Lu / J. Iran. Chem. Res. 1 (008) Mathematcal expresson for formulaton of emulson explosves Provded that the amount of AN, SN, Water, Span-80, wax and mneral ol are respectvely desgnated as x 1, x, x 3, x 4, x 5 and x 6, then: a=0.561x x x 6 b=0.500x x x x x 6 c=0.375x x x x 4 d=0.50x x h=0.118x and, Formula (3) gves the general formula for Heat of Formaton of emulson explosves. 10x H m f ( ) = x x x x 4 (3) and then the prmary fgure of mert (Maxmum Heat of Exploson) s gven by formula (4). MaxQ v =51.08x x -3.07x x x x 6 (4) Formula (4) s assumed as followng condtons: 0x x 39x4 346x5 346x6 = 100K x 1 + x + x3 + x4 + x5 + x6 = x x + 15x4 + 4x5 + 3x6 P /10 70 x1 8 5 x 15 8 x x4 3 x5 4 1 x6 3 For formula (4), the values η and P may be assumed, n general η 0. Table 1 Physcal chemstry parameters of the raw materals of emulson explosves No. Emprcal MW Hf OB Cost Ingredent formula (g/mole) (kj/mole) (%) (RMBy/t) 1 N O 3 H 4 AN O 3 NNa NA H O water 18 4 C 4 H 44 O 6 Span C 18 H 36 Wax C 1 H 6 mneral ol Computer solutons To arrve at a soluton, a computer was employed. The mathematcal formulas constructed prevously were nputted nto a MS Excel program. The mathematcal soluton vared wth dfferent oxygen balance values (η) and raw materal costs P.

4 4. Results and dscusson M. Lu and Q. Lu / J. Iran. Chem. Res. 1 (008) Effect of formulaton desgn on the heat of exploson and the specfc volume Te heat of exploson s the energetc sources to release the explosve power and the specfc volume s the medum to transfer the power. The heat of exploson calculated based on the aforementoned mathematcal model and here the specfc volume was equal to the total volume produced by all gaseous materals after exploson n standard state. The effects of the dfferent contents of NH 4 NO 3, NaNO 3, H O, and Span-80 and composte fuel ol on the heat of exploson and specfc volume were dscussed by the mathematcal model as follows. 4.. Effect of oxdant Comparson ammonum ntrate wth sodum ntrate Ammonum ntrate (AN) s used as the basc oxdant n the emulson explosves and sodum or calcum ntrate s often added to mprove the propertes of the oxdzer soluton. Oxdant s an mportant ngredent n the emulson explosves that supples oxygen n the exploson reacton and ts oxygen balance values s hgher than zero. For an oxdant, the oxygen balance value only ndcates that how much oxygen t can supply n the exploson reacton, but does not demonstrate how much energy t can offer. Furthermore, the hgher oxygen balance value can not explan the hgher energy was released n the exploson reacton. For example, 1 mol ammonum ntrate can supply 0.5 mol oxygen n the exploson reacton, at the same tme, can offer 17.4 kj energy. However, 1mol sodum ntrate can supply 1.5 mol oxygen but absorb kj energy n the exploson reacton. Therefore the release or absorpton of energy for an oxdant s an mportant characterstc parameter whch s related wth the energetc contrbuton of an oxdant and ammonum ntrate s a good oxdant for the energetc contrbuton of ndustral explosves Effect of ammonum ntrate The effects of the dfferent contents of AN on the heat of exploson and the specfc volume are shown n Fg. 1. As seen from Fg. 1, the heat of exploson and the specfc volume would be mproved when the content of AN was ncreased. Ths was attrbuted to hydrogen, oxygen and ntrogen n AN molecule. After exploson hydrogen and oxygen were transformed nto water havng hgh heat of formaton whch was useful to mprove the heat of exploson, and ntrogen became N whch was, however, help to mprove the specfc volume. Therefore, the AN content may be ncreased reasonably n the formulaton desgn of emulson explosves Heat of explosve X AN / % Fg. 1 The effect of AN content on the heat of exploson and specfc volume

5 Effect of sodum ntrate M. Lu and Q. Lu / J. Iran. Chem. Res. 1 (008) Generally, n order to lower the crystallod pont of oxdant, NaNO 3 was used as another oxdant n emulson explosves. The effects of the dfferent contents of NaNO 3 on the heat of exploson and specfc volume are shown n Fg Heat of explosve X NaNO3 / % Fg. The effect of NaNO 3 content on heat of exploson and specfc volume The heat of exploson and the specfc volume were optmal when the NaNO 3 content was 7% as shown n Fg.. Consderng that ncreasng the content of NaNO 3 would lower the crystallod pont of the mxture of ammonum ntrate and sodum ntrate, whch s benefcal to the safety of the producton process of emulson matrx, the best theoretcal formulaton of emulson explosve conssts of 7% ~ 9% NaNO Effect of water Water was used as a solvent of oxdant n emulson explosve, whch made fuel ol mx wth oxdant fully, and the exploson effcency reach to maxmum. Water was changed nto vapor after the exploson, evaporatve heat was needed n ths process and so the heat of exploson of emulson explosve was lower than that of powder AN explosve. The effects of the dfferent contents of H O on the heat of exploson and specfc volume were dscussed by the mathematcal model. As seen from Fg. 3, the best theoretcal formulaton of emulson explosve conssts of 9% ~ 10% H O Effect of Span-80 The effects of the dfferent emulsfer (Span-80) contents on the heat of exploson and specfc volume were dscussed by the mathematcal model. The results are shown n Fg.4. The best theoretcal formulaton of emulson explosve conssts of 1.5% ~.0% Span Effect of oxygen balance The oxygen balance was nfluenced by the contents of composte fuel ol n emulson explosve. The more the composte fuel ol used was, the more negatve the oxygen balance was. Wth the ncreasng of the weght percent of the composte fuel ol, the heat of exploson decreased and the volume of toxc gases (.e., CO) produced after the exploson ncreased.

6 M. Lu and Q. Lu / J. Iran. Chem. Res. 1 (008) Heat of explosve Fg. 3 The effect of water content on heat of exploson and specfc volume X HO / % Heat of explosve X Span-80 / % Fg. 4 The effect of Span-80 content on heat of exploson and specfc volume However, when oxygen balance value was hgher than zero (η>0)) the volume of toxc gases.e. NO produced after the exploson ncreased. Therefore, t was very mportant that oxygen balance value be zero (or close to zero) n order that formulatons should have hgher heat of exploson and lower toxc gas volumes. The effects of the dfferent oxygen balance values on the heat of exploson and the specfc volume are shown n Fg.5. The best theoretcal formulaton of emulson explosve conssts of 7%~9%NaNO 3, 9%~10%H O, 1.5%~%Span-80 respectvely for hgher heat of exploson, specfc volume and lower toxc gas volume Valdatng the model Some performance of a number of emulson explosves contanng glass mcro-balloons were studed expermentally and theoretcally. For each of the explosves, detonaton velocty and power of explosve were measured, and oxygen balance and heat of exploson were calculated. The nfluence of the content of NH 4 NO 3 NaNO 3, H O, and Span-80 n the emulson matrx respectvely on detonaton velocty and power of explosve was examned.

7 39 M. Lu and Q. Lu / J. Iran. Chem. Res. 1 (008) η / % Heat of explosve 940 Fg. 5 The effect of oxygen balance on theoretc exploson heat and specfc volume The emulson matrx was prepared usng aqueous solutons of the mxture of ammonum ntrate wth sodum ntrate. The contents of other ngredents were unchanged nearly n order to mantan the oxygen balance wthn the range of ±0.5%. The compostons of the emulson matrces are gven n Table. The emulsons were prepared usng a smple faclty consstng of a thermostat and a contaner equpped wth a strrer. The soluton of oxdant was heated to 10 and then slowly added nto the contaner, n whch a preheated (100 ) mxture of fuels (ol and span-80) wth the emulsfer was agtated wth the strrer at a speed of 1440 rpm. After addng the entre amount of the oxdzer, the agtaton was contnued for about two mnutes to obtan fne emulson partcles. The fnal explosve mxtures were prepared by mxng the emulson matrces wth glass mcro-spheres (produced by 3M; mean sze about 80 µm). Mxng was performed carefully (usng the same strrer but at lower speed) untl the dstrbuton of the mcrospheres n the emulson matrx became unform. The mass fracton of mcro-spheres was %~ 3% (above 100%) n all experments. For each explosve, the detonaton velocty and power of explosve were measured. The results obtaned enabled a comparson of the effcency for testng explosve performance. They were also used to analyze the effect of formulaton on the performance of the explosves and to choose the formulatons characterzed by the best detonaton and performance characterstcs. A more quantty of ammonum ntrate, a certan extent of water and an oxygen balance of zero or close to zero are favorable for hgher heat of exploson and exploson strength. Table Formulatons and performance of emulson explosves Mass fracton of components, % AN Fuel SN H O Span ol Oxygen balance / % Calculated heat of exploson / kj kg -1 Power of explosve / ml Detonaton velocty / m s

8 M. Lu and Q. Lu / J. Iran. Chem. Res. 1 (008) Concluson Accordng to thermochemstry of exploson reacton, the mathematcal model for formulaton desgn of emulson explosve was establshed. The computer was used to ad the formulaton desgn and optmzaton of emulson explosve by a MS Excel program. The effects of the dfferent content of NH 4 NO 3, NaNO 3, H O and Span-80 and composte fuel ol on the heat of exploson and the specfc volume were dscussed based on the mathematcal model. The results show that wth the ncreasng of the content of NH 4 NO 3, the heat of exploson and the specfc volume were ncreased. The best theoretcal formulaton of emulson explosve conssts of 7%~9%NaNO 3, 9%~10%H O, 1.5%~%Span-80 respectvely, and an oxygen balance of zero or close to zero for hgher heat of exploson, specfc volume and lower toxc gas volume. References [1] R.S. Egly, A.E. Neckar, US (1964//1/15). [] N.E. Gehrg, US (1965/01/05). [3] J. Lee, P.A. Persson, Propell. Explos. Pyrot. 15 (1990) 08. [4] K. Takahash, K. Murata, Y. Kato, M. Fujta, S. Itoh, J. Mater. Proces. Technol. 85 (1999). [5] M. Lu, C. Lu, Sc. Tech. Energetc Materals 68 (007) 117. [6] M. Lu, C. Lu, J. Chn. Explosve Mat. 8 (1999) 1. [7] Z. Yuan, J. Chn. Explosve Mat. 9 (1) 1. [8] C. Lu, Z. Lu, O. L, Commercal Explosves, Ordnance Industry Press, Bejng, [9] M. Lu, Formulaton desgn of commercal explosves, Ordnance Industry Press, Bejng, 00.

Calculating the Quasi-static Pressures of Confined Explosions Considering Chemical Reactions under the Constant Entropy Assumption

Calculating the Quasi-static Pressures of Confined Explosions Considering Chemical Reactions under the Constant Entropy Assumption Appled Mechancs and Materals Onlne: 202-04-20 ISS: 662-7482, ol. 64, pp 396-400 do:0.4028/www.scentfc.net/amm.64.396 202 Trans Tech Publcatons, Swtzerland Calculatng the Quas-statc Pressures of Confned

More information

modeling of equilibrium and dynamic multi-component adsorption in a two-layered fixed bed for purification of hydrogen from methane reforming products

modeling 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 information

ME 300 Exam 2 November 18, :30 p.m. to 7:30 p.m.

ME 300 Exam 2 November 18, :30 p.m. to 7:30 p.m. CICLE YOU LECTUE BELOW: Frst Name Last Name 1:3 a.m. 1:3 p.m. Nak Gore ME 3 Exam November 18, 14 6:3 p.m. to 7:3 p.m. INSTUCTIONS 1. Ths s a closed book and closed notes examnaton. You are provded wth

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

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

SAMPLE ANALYSIS REQUEST FORM

SAMPLE ANALYSIS REQUEST FORM SAMPLE ANALYSIS REQUEST FORM Please complete ths Sample Analyss Request Form (one request per sample) and send t to CILAS wth the Samples and the Safety Datasheet Please complete page 2 and 3 for another

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

By Dr. Erkan KARACABEY 1 Dr. Cem BALTACIOĞLU 2 and Dr. Erdoğan KÜÇÜÖNER 1

By Dr. Erkan KARACABEY 1 Dr. Cem BALTACIOĞLU 2 and Dr. Erdoğan KÜÇÜÖNER 1 Optmzaton of ol uptake of predred and deep-fat-fred fred carrot slces as a functon of process condtons By Dr. Erkan KARACABEY 1 Dr. Cem BALTACIOĞLU 2 and Dr. Erdoğan KÜÇÜÖNER 1 1 Food Engneerng Deparment,

More information

A study on the effect of ball diameter on breakage properties of clinker and limestone

A study on the effect of ball diameter on breakage properties of clinker and limestone Indan Journal of Chemcal Technology Vol. 9, May 202, pp. 80-84 A study on the effect of ball dameter on breakage propertes of clnker and lmestone Vedat Denz* Department of Chemcal Engneerng, Htt Unversty,

More information

An identification algorithm of model kinetic parameters of the interfacial layer growth in fiber composites

An 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 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

The Study of Teaching-learning-based Optimization Algorithm

The 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 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

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

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

Air Age Equation Parameterized by Ventilation Grouped Time WU Wen-zhong

Air Age Equation Parameterized by Ventilation Grouped Time WU Wen-zhong Appled Mechancs and Materals Submtted: 2014-05-07 ISSN: 1662-7482, Vols. 587-589, pp 449-452 Accepted: 2014-05-10 do:10.4028/www.scentfc.net/amm.587-589.449 Onlne: 2014-07-04 2014 Trans Tech Publcatons,

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

COMPARISON OF SOME RELIABILITY CHARACTERISTICS BETWEEN REDUNDANT SYSTEMS REQUIRING SUPPORTING UNITS FOR THEIR OPERATIONS

COMPARISON 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 information

DESIGN OPTIMIZATION OF CFRP RECTANGULAR BOX SUBJECTED TO ARBITRARY LOADINGS

DESIGN OPTIMIZATION OF CFRP RECTANGULAR BOX SUBJECTED TO ARBITRARY LOADINGS Munch, Germany, 26-30 th June 2016 1 DESIGN OPTIMIZATION OF CFRP RECTANGULAR BOX SUBJECTED TO ARBITRARY LOADINGS Q.T. Guo 1*, Z.Y. L 1, T. Ohor 1 and J. Takahash 1 1 Department of Systems Innovaton, School

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

Pulse Coded Modulation

Pulse Coded Modulation Pulse Coded Modulaton PCM (Pulse Coded Modulaton) s a voce codng technque defned by the ITU-T G.711 standard and t s used n dgtal telephony to encode the voce sgnal. The frst step n the analog to dgtal

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

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

Influence Of Operating Conditions To The Effectiveness Of Extractive Distillation Columns

Influence Of Operating Conditions To The Effectiveness Of Extractive Distillation Columns Influence Of Operatng Condtons To The Effectveness Of Extractve Dstllaton Columns N.A. Vyazmna Moscov State Unversty Of Envrnmental Engneerng, Department Of Chemcal Engneerng Ul. Staraya Basmannaya 21/4,

More information

A Hybrid Variational Iteration Method for Blasius Equation

A 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 information

Number Average Molar Mass. Mass Average Molar Mass. Z-Average Molar Mass

Number Average Molar Mass. Mass Average Molar Mass. Z-Average Molar Mass 17 Molar mass: There are dfferent ways to report a molar mass lke (a) Number average molar mass, (b) mass average molar mass, (c) Vscosty average molar mass, (d) Z- Average molar mass Number Average Molar

More information

Module 3 LOSSY IMAGE COMPRESSION SYSTEMS. Version 2 ECE IIT, Kharagpur

Module 3 LOSSY IMAGE COMPRESSION SYSTEMS. Version 2 ECE IIT, Kharagpur Module 3 LOSSY IMAGE COMPRESSION SYSTEMS Verson ECE IIT, Kharagpur Lesson 6 Theory of Quantzaton Verson ECE IIT, Kharagpur Instructonal Objectves At the end of ths lesson, the students should be able to:

More information

Turbulence classification of load data by the frequency and severity of wind gusts. Oscar Moñux, DEWI GmbH Kevin Bleibler, DEWI GmbH

Turbulence 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 information

829. An adaptive method for inertia force identification in cantilever under moving mass

829. An adaptive method for inertia force identification in cantilever under moving mass 89. An adaptve method for nerta force dentfcaton n cantlever under movng mass Qang Chen 1, Mnzhuo Wang, Hao Yan 3, Haonan Ye 4, Guola Yang 5 1,, 3, 4 Department of Control and System Engneerng, Nanng Unversty,

More information

A Robust Method for Calculating the Correlation Coefficient

A 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 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

Design and Optimization of Fuzzy Controller for Inverse Pendulum System Using Genetic Algorithm

Design and Optimization of Fuzzy Controller for Inverse Pendulum System Using Genetic Algorithm Desgn and Optmzaton of Fuzzy Controller for Inverse Pendulum System Usng Genetc Algorthm H. Mehraban A. Ashoor Unversty of Tehran Unversty of Tehran h.mehraban@ece.ut.ac.r a.ashoor@ece.ut.ac.r Abstract:

More information

DUE: WEDS FEB 21ST 2018

DUE: WEDS FEB 21ST 2018 HOMEWORK # 1: FINITE DIFFERENCES IN ONE DIMENSION DUE: WEDS FEB 21ST 2018 1. Theory Beam bendng s a classcal engneerng analyss. The tradtonal soluton technque makes smplfyng assumptons such as a constant

More information

A Fast Computer Aided Design Method for Filters

A Fast Computer Aided Design Method for Filters 2017 Asa-Pacfc Engneerng and Technology Conference (APETC 2017) ISBN: 978-1-60595-443-1 A Fast Computer Aded Desgn Method for Flters Gang L ABSTRACT *Ths paper presents a fast computer aded desgn method

More information

Grand canonical Monte Carlo simulations of bulk electrolytes and calcium channels

Grand canonical Monte Carlo simulations of bulk electrolytes and calcium channels Grand canoncal Monte Carlo smulatons of bulk electrolytes and calcum channels Thess of Ph.D. dssertaton Prepared by: Attla Malascs M.Sc. n Chemstry Supervsor: Dr. Dezső Boda Unversty of Pannona Insttute

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

Prediction of Ultrasonic Velocity in Binary Mixtures of a Nuclear Extractant and Monocarboxylic Acids using Several Theoretical Models

Prediction of Ultrasonic Velocity in Binary Mixtures of a Nuclear Extractant and Monocarboxylic Acids using Several Theoretical Models Predcton of ltrasonc Velocty n Bnary Mxtures of a Nuclear Extractant and Monocarboxylc Acds usng Several Theoretcal Models R. K. Mshra 1, B. Dala 1*, N. Swan 2 and S.K. Dash 3 1 BSH, Gandh Insttute of

More information

PERFORMANCE OF HEAVY-DUTY PLANETARY GEARS

PERFORMANCE OF HEAVY-DUTY PLANETARY GEARS THE INTERNATIONAL CONFERENCE OF THE CARPATHIAN EURO-REGION SPECIALISTS IN INDUSTRIAL SYSTEMS 6 th edton PERFORMANCE OF HEAVY-DUTY PLANETARY GEARS Attla Csobán, Mhály Kozma 1, 1 Professor PhD., Eng. Budapest

More information

THE VIBRATIONS OF MOLECULES II THE CARBON DIOXIDE MOLECULE Student Instructions

THE VIBRATIONS OF MOLECULES II THE CARBON DIOXIDE MOLECULE Student Instructions THE VIBRATIONS OF MOLECULES II THE CARBON DIOXIDE MOLECULE Student Instructons by George Hardgrove Chemstry Department St. Olaf College Northfeld, MN 55057 hardgrov@lars.acc.stolaf.edu Copyrght George

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

is the calculated value of the dependent variable at point i. The best parameters have values that minimize the squares of the errors

is the calculated value of the dependent variable at point i. The best parameters have values that minimize the squares of the errors Multple Lnear and Polynomal Regresson wth Statstcal Analyss Gven a set of data of measured (or observed) values of a dependent varable: y versus n ndependent varables x 1, x, x n, multple lnear regresson

More information

Adiabatic Sorption of Ammonia-Water System and Depicting in p-t-x Diagram

Adiabatic 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 information

Back Analysis of Self-Compacting Concrete Rheological Parameters Based on H-B Model

Back Analysis of Self-Compacting Concrete Rheological Parameters Based on H-B Model Internatonal Conference on Archtectural, Cvl and Hydraulcs Engneerng (ICACHE 2015) Back Analyss of Self-Compactng Concrete Rheologcal Parameters Based on H-B Model Shua Zeng1, a, Janjun Sh1,b, Wenqang

More information

EVALUATION OF THE VISCO-ELASTIC PROPERTIES IN ASPHALT RUBBER AND CONVENTIONAL MIXES

EVALUATION OF THE VISCO-ELASTIC PROPERTIES IN ASPHALT RUBBER AND CONVENTIONAL MIXES EVALUATION OF THE VISCO-ELASTIC PROPERTIES IN ASPHALT RUBBER AND CONVENTIONAL MIXES Manuel J. C. Mnhoto Polytechnc Insttute of Bragança, Bragança, Portugal E-mal: mnhoto@pb.pt Paulo A. A. Perera and Jorge

More information

Module 2. Random Processes. Version 2 ECE IIT, Kharagpur

Module 2. Random Processes. Version 2 ECE IIT, Kharagpur Module Random Processes Lesson 6 Functons of Random Varables After readng ths lesson, ou wll learn about cdf of functon of a random varable. Formula for determnng the pdf of a random varable. Let, X be

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

A PROBABILITY-DRIVEN SEARCH ALGORITHM FOR SOLVING MULTI-OBJECTIVE OPTIMIZATION PROBLEMS

A PROBABILITY-DRIVEN SEARCH ALGORITHM FOR SOLVING MULTI-OBJECTIVE OPTIMIZATION PROBLEMS HCMC Unversty of Pedagogy Thong Nguyen Huu et al. A PROBABILITY-DRIVEN SEARCH ALGORITHM FOR SOLVING MULTI-OBJECTIVE OPTIMIZATION PROBLEMS Thong Nguyen Huu and Hao Tran Van Department of mathematcs-nformaton,

More information

COMPOSITE BEAM WITH WEAK SHEAR CONNECTION SUBJECTED TO THERMAL LOAD

COMPOSITE BEAM WITH WEAK SHEAR CONNECTION SUBJECTED TO THERMAL LOAD COMPOSITE BEAM WITH WEAK SHEAR CONNECTION SUBJECTED TO THERMAL LOAD Ákos Jósef Lengyel, István Ecsed Assstant Lecturer, Professor of Mechancs, Insttute of Appled Mechancs, Unversty of Mskolc, Mskolc-Egyetemváros,

More information

Formulas for the Determinant

Formulas for the Determinant page 224 224 CHAPTER 3 Determnants e t te t e 2t 38 A = e t 2te t e 2t e t te t 2e 2t 39 If 123 A = 345, 456 compute the matrx product A adj(a) What can you conclude about det(a)? For Problems 40 43, use

More information

Relationship between Refractive Index and Molar Concentration of Multi-Component Solutions Zhu Xingyu 1, a, Mai Tiancheng 2, b and Zhao Zilong 2, c

Relationship between Refractive Index and Molar Concentration of Multi-Component Solutions Zhu Xingyu 1, a, Mai Tiancheng 2, b and Zhao Zilong 2, c Advances n Computer Scence Research, volume 71 4th Internatonal Conference on Machnery, Materals and Informaton Technology Applcatons (ICMMITA 2016) Relatonshp between Refractve Index and Molar Concentraton

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

System in Weibull Distribution

System in Weibull Distribution Internatonal Matheatcal Foru 4 9 no. 9 94-95 Relablty Equvalence Factors of a Seres-Parallel Syste n Webull Dstrbuton M. A. El-Dacese Matheatcs Departent Faculty of Scence Tanta Unversty Tanta Egypt eldacese@yahoo.co

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

ELASTIC WAVE PROPAGATION IN A CONTINUOUS MEDIUM

ELASTIC 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 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

Annexes. EC.1. Cycle-base move illustration. EC.2. Problem Instances

Annexes. EC.1. Cycle-base move illustration. EC.2. Problem Instances ec Annexes Ths Annex frst llustrates a cycle-based move n the dynamc-block generaton tabu search. It then dsplays the characterstcs of the nstance sets, followed by detaled results of the parametercalbraton

More information

KINETICS OF GAS HYDRATE FORMATION FROM PYROLYSIS GAS IN WATER-IN-OIL EMULSION SYSTEM

KINETICS OF GAS HYDRATE FORMATION FROM PYROLYSIS GAS IN WATER-IN-OIL EMULSION SYSTEM Proceedngs of the 7th Internatonal Conference on Gas Hydrates (ICGH 211), Ednburgh, Scotland, Unted Kngdom, July 17-21, 211. KINETICS OF GAS HYDRATE FORMATION FROM PYROLYSIS GAS IN WATER-IN-OIL EMULSION

More information

OFF-AXIS MECHANICAL PROPERTIES OF FRP COMPOSITES

OFF-AXIS MECHANICAL PROPERTIES OF FRP COMPOSITES ICAMS 204 5 th Internatonal Conference on Advanced Materals and Systems OFF-AXIS MECHANICAL PROPERTIES OF FRP COMPOSITES VLAD LUPĂŞTEANU, NICOLAE ŢĂRANU, RALUCA HOHAN, PAUL CIOBANU Gh. Asach Techncal Unversty

More information

Army Ants Tunneling for Classical Simulations

Army Ants Tunneling for Classical Simulations Electronc Supplementary Materal (ESI) for Chemcal Scence. Ths journal s The Royal Socety of Chemstry 2014 electronc supplementary nformaton (ESI) for Chemcal Scence Army Ants Tunnelng for Classcal Smulatons

More information

Structure and Drive Paul A. Jensen Copyright July 20, 2003

Structure and Drive Paul A. Jensen Copyright July 20, 2003 Structure and Drve Paul A. Jensen Copyrght July 20, 2003 A system s made up of several operatons wth flow passng between them. The structure of the system descrbes the flow paths from nputs to outputs.

More information

AGC Introduction

AGC Introduction . Introducton AGC 3 The prmary controller response to a load/generaton mbalance results n generaton adjustment so as to mantan load/generaton balance. However, due to droop, t also results n a non-zero

More information

REAL TIME OPTIMIZATION OF a FCC REACTOR USING LSM DYNAMIC IDENTIFIED MODELS IN LLT PREDICTIVE CONTROL ALGORITHM

REAL TIME OPTIMIZATION OF a FCC REACTOR USING LSM DYNAMIC IDENTIFIED MODELS IN LLT PREDICTIVE CONTROL ALGORITHM REAL TIME OTIMIZATION OF a FCC REACTOR USING LSM DYNAMIC IDENTIFIED MODELS IN LLT REDICTIVE CONTROL ALGORITHM Durask, R. G.; Fernandes,. R. B.; Trerweler, J. O. Secch; A. R. federal unversty of Ro Grande

More information

STUDY OF A THREE-AXIS PIEZORESISTIVE ACCELEROMETER WITH UNIFORM AXIAL SENSITIVITIES

STUDY OF A THREE-AXIS PIEZORESISTIVE ACCELEROMETER WITH UNIFORM AXIAL SENSITIVITIES STUDY OF A THREE-AXIS PIEZORESISTIVE ACCELEROMETER WITH UNIFORM AXIAL SENSITIVITIES Abdelkader Benchou, PhD Canddate Nasreddne Benmoussa, PhD Kherreddne Ghaffour, PhD Unversty of Tlemcen/Unt of Materals

More information

The Quadratic Trigonometric Bézier Curve with Single Shape Parameter

The Quadratic Trigonometric Bézier Curve with Single Shape Parameter J. Basc. Appl. Sc. Res., (3541-546, 01 01, TextRoad Publcaton ISSN 090-4304 Journal of Basc and Appled Scentfc Research www.textroad.com The Quadratc Trgonometrc Bézer Curve wth Sngle Shape Parameter Uzma

More information

STAT 511 FINAL EXAM NAME Spring 2001

STAT 511 FINAL EXAM NAME Spring 2001 STAT 5 FINAL EXAM NAME Sprng Instructons: Ths s a closed book exam. No notes or books are allowed. ou may use a calculator but you are not allowed to store notes or formulas n the calculator. Please wrte

More information

Uncertainty in measurements of power and energy on power networks

Uncertainty 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 information

Assessment of Site Amplification Effect from Input Energy Spectra of Strong Ground Motion

Assessment of Site Amplification Effect from Input Energy Spectra of Strong Ground Motion Assessment of Ste Amplfcaton Effect from Input Energy Spectra of Strong Ground Moton M.S. Gong & L.L Xe Key Laboratory of Earthquake Engneerng and Engneerng Vbraton,Insttute of Engneerng Mechancs, CEA,

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

NON-CENTRAL 7-POINT FORMULA IN THE METHOD OF LINES FOR PARABOLIC AND BURGERS' EQUATIONS

NON-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 information

CHARACTERISTICS OF COMPLEX SEPARATION SCHEMES AND AN ERROR OF SEPARATION PRODUCTS OUTPUT DETERMINATION

CHARACTERISTICS OF COMPLEX SEPARATION SCHEMES AND AN ERROR OF SEPARATION PRODUCTS OUTPUT DETERMINATION Górnctwo Geonżynera Rok 0 Zeszyt / 006 Igor Konstantnovch Mladetskj * Petr Ivanovch Plov * Ekaterna Nkolaevna Kobets * Tasya Igorevna Markova * CHARACTERISTICS OF COMPLEX SEPARATION SCHEMES AND AN ERROR

More information

Module 9. Lecture 6. Duality in Assignment Problems

Module 9. Lecture 6. Duality in Assignment Problems Module 9 1 Lecture 6 Dualty n Assgnment Problems In ths lecture we attempt to answer few other mportant questons posed n earler lecture for (AP) and see how some of them can be explaned through the concept

More information

Relationship between fiber degradation and residence time distribution in the processing of long fiber reinforced thermoplastics

Relationship between fiber degradation and residence time distribution in the processing of long fiber reinforced thermoplastics express Polymer Letters Vol.2, No.8 (28) 56 568 Avalable onlne at www.expresspolymlett.com DOI: 1.3144/expresspolymlett.28.68 Relatonshp between fber degradaton and resdence tme dstrbuton n the processng

More information

CS-433: Simulation and Modeling Modeling and Probability Review

CS-433: Simulation and Modeling Modeling and Probability Review CS-433: Smulaton and Modelng Modelng and Probablty Revew Exercse 1. (Probablty of Smple Events) Exercse 1.1 The owner of a camera shop receves a shpment of fve cameras from a camera manufacturer. Unknown

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

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

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

Ph.D. Qualifying Examination in Kinetics and Reactor Design

Ph.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 information

LNG CARGO TRANSFER CALCULATION METHODS AND ROUNDING-OFFS

LNG CARGO TRANSFER CALCULATION METHODS AND ROUNDING-OFFS CARGO TRANSFER CALCULATION METHODS AND ROUNDING-OFFS CONTENTS 1. Method for determnng transferred energy durng cargo transfer. Calculatng the transferred energy.1 Calculatng the gross transferred energy.1.1

More information

Lecture 3. Ax x i a i. i i

Lecture 3. Ax x i a i. i i 18.409 The Behavor of Algorthms n Practce 2/14/2 Lecturer: Dan Spelman Lecture 3 Scrbe: Arvnd Sankar 1 Largest sngular value In order to bound the condton number, we need an upper bound on the largest

More information

Chapter 11: Simple Linear Regression and Correlation

Chapter 11: Simple Linear Regression and Correlation Chapter 11: Smple Lnear Regresson and Correlaton 11-1 Emprcal Models 11-2 Smple Lnear Regresson 11-3 Propertes of the Least Squares Estmators 11-4 Hypothess Test n Smple Lnear Regresson 11-4.1 Use of t-tests

More information

NUMERICAL DIFFERENTIATION

NUMERICAL 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 information

FUZZY GOAL PROGRAMMING VS ORDINARY FUZZY PROGRAMMING APPROACH FOR MULTI OBJECTIVE PROGRAMMING PROBLEM

FUZZY GOAL PROGRAMMING VS ORDINARY FUZZY PROGRAMMING APPROACH FOR MULTI OBJECTIVE PROGRAMMING PROBLEM Internatonal Conference on Ceramcs, Bkaner, Inda Internatonal Journal of Modern Physcs: Conference Seres Vol. 22 (2013) 757 761 World Scentfc Publshng Company DOI: 10.1142/S2010194513010982 FUZZY GOAL

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

Lab 2e Thermal System Response and Effective Heat Transfer Coefficient

Lab 2e Thermal System Response and Effective Heat Transfer Coefficient 58:080 Expermental Engneerng 1 OBJECTIVE Lab 2e Thermal System Response and Effectve Heat Transfer Coeffcent Warnng: though the experment has educatonal objectves (to learn about bolng heat transfer, etc.),

More information

More metrics on cartesian products

More metrics on cartesian products More metrcs on cartesan products If (X, d ) are metrc spaces for 1 n, then n Secton II4 of the lecture notes we defned three metrcs on X whose underlyng topologes are the product topology The purpose of

More information

International Journal of Engineering Research and Modern Education (IJERME) Impact Factor: 7.018, ISSN (Online): (

International Journal of Engineering Research and Modern Education (IJERME) Impact Factor: 7.018, ISSN (Online): ( CONSTRUCTION AND SELECTION OF CHAIN SAMPLING PLAN WITH ZERO INFLATED POISSON DISTRIBUTION A. Palansamy* & M. Latha** * Research Scholar, Department of Statstcs, Government Arts College, Udumalpet, Tamlnadu

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

Lecture Notes on Linear Regression

Lecture Notes on Linear Regression Lecture Notes on Lnear Regresson Feng L fl@sdueducn Shandong Unversty, Chna Lnear Regresson Problem In regresson problem, we am at predct a contnuous target value gven an nput feature vector We assume

More information

Study on Active Micro-vibration Isolation System with Linear Motor Actuator. Gong-yu PAN, Wen-yan GU and Dong LI

Study on Active Micro-vibration Isolation System with Linear Motor Actuator. Gong-yu PAN, Wen-yan GU and Dong LI 2017 2nd Internatonal Conference on Electrcal and Electroncs: echnques and Applcatons (EEA 2017) ISBN: 978-1-60595-416-5 Study on Actve Mcro-vbraton Isolaton System wth Lnear Motor Actuator Gong-yu PAN,

More information

CHAPTER IV RESEARCH FINDING AND DISCUSSIONS

CHAPTER IV RESEARCH FINDING AND DISCUSSIONS CHAPTER IV RESEARCH FINDING AND DISCUSSIONS A. Descrpton of Research Fndng. The Implementaton of Learnng Havng ganed the whole needed data, the researcher then dd analyss whch refers to the statstcal data

More information

Color Rendering Uncertainty

Color Rendering Uncertainty Australan Journal of Basc and Appled Scences 4(10): 4601-4608 010 ISSN 1991-8178 Color Renderng Uncertanty 1 A.el Bally M.M. El-Ganany 3 A. Al-amel 1 Physcs Department Photometry department- NIS Abstract:

More information

UNR Joint Economics Working Paper Series Working Paper No Further Analysis of the Zipf Law: Does the Rank-Size Rule Really Exist?

UNR Joint Economics Working Paper Series Working Paper No Further Analysis of the Zipf Law: Does the Rank-Size Rule Really Exist? UNR Jont Economcs Workng Paper Seres Workng Paper No. 08-005 Further Analyss of the Zpf Law: Does the Rank-Sze Rule Really Exst? Fungsa Nota and Shunfeng Song Department of Economcs /030 Unversty of Nevada,

More information

The Order Relation and Trace Inequalities for. Hermitian Operators

The Order Relation and Trace Inequalities for. Hermitian Operators Internatonal Mathematcal Forum, Vol 3, 08, no, 507-57 HIKARI Ltd, wwwm-hkarcom https://doorg/0988/mf088055 The Order Relaton and Trace Inequaltes for Hermtan Operators Y Huang School of Informaton Scence

More information

Lecture Note 3. Eshelby s Inclusion II

Lecture 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 information

Supporting Information

Supporting Information Supportng Informaton Water structure at the ar-aqueous nterface of dvalent caton and ntrate solutons Man Xu, Rck Spnney, Heather C. Allen* allen@chemstry.oho-state.edu Fresnel factors and spectra normalzaton

More information

The Minimum Universal Cost Flow in an Infeasible Flow Network

The Minimum Universal Cost Flow in an Infeasible Flow Network Journal of Scences, Islamc Republc of Iran 17(2): 175-180 (2006) Unversty of Tehran, ISSN 1016-1104 http://jscencesutacr The Mnmum Unversal Cost Flow n an Infeasble Flow Network H Saleh Fathabad * M Bagheran

More information

Ttle Cs-trans somerzaton of malec a pressure Author(s) Kyama, Ryo; Mnomura, Shgeru Ctaton The Revew of Physcal Chemstry of ssue Date 1952 URL http://hdl.handle.net/2433/46672 Rght Type Departmental Bulletn

More information

Similar Constructing Method for Solving the Boundary Value Problem of the Compound Kummer Equation

Similar Constructing Method for Solving the Boundary Value Problem of the Compound Kummer Equation Amercan Journal of Mathematcal Analyss, 05, Vol. 3, No., 39-43 Avalable onlne at http://pubs.scepub.com/ajma/3//3 Scence and Educaton Publshng DOI:0.69/ajma-3--3 Smlar Constructng Method for Solvng the

More information

Statistics Chapter 4

Statistics Chapter 4 Statstcs Chapter 4 "There are three knds of les: les, damned les, and statstcs." Benjamn Dsrael, 1895 (Brtsh statesman) Gaussan Dstrbuton, 4-1 If a measurement s repeated many tmes a statstcal treatment

More information

Note 10. Modeling and Simulation of Dynamic Systems

Note 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 information