linear dependence of balances for non-redox electrolytic...

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American Journal of Analytical Chemistry, 2014, 5, 1285-1289 Published Online December 2014 in SciRes. http://www.scirp.org/journal/ajac http://dx.doi.org/10.4236/ajac.2014.517134 How to cite this paper: Michałowska-Kaczmarczyk, A.M. and Michałowski, T. (2014) Linear Dependence of Balances for Non-Redox Electrolytic Systems. American Journal of Analytical Chemistry, 5, 1285-1289. http://dx.doi.org/10.4236/ajac.2014.517134 Linear Dependence of Balances for Non-Redox Electrolytic Systems Anna M. Michałowska-Kaczmarczyk 1 , Tadeusz Michałowski 2* 1 Department of Oncology, The University Hospital in Cracow, Cracow, Poland 2 Faculty of Engineering and Chemical Technology, Technical University of Cracow, Cracow, Poland Email: * [email protected] Received 12 October 2014; revised 29 November 2014; accepted 11 December 2014 Copyright © 2014 by authors and Scientific Research Publishing Inc. This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/ Abstract Two complex dynamic non-redox systems are considered as examples, providing interdependent linear equations. A simple and efficient linear combination method that leads the system of equa- tions to the identity, 0 = 0, is used for this purpose. These examples are clear confirmations of the general property differentiating non-redox and redox electrolytic systems. This property is in- volved with linear dependence or independence of ( ) ( ) 2 O H f f on charge and elemental/ core balances for elements/cores H, O, where ( ) H f and ( ) O f are elemental balances for H and O, respectively. Keywords Titration, Liebig-Denigès Method, Complexonometric Detemination of Zinc 1. Introduction In numerous examples of electrolytic redox systems presented in our previous papers [1]-[4], it was found that the linear combination ( ) ( ) 2 O H f f of elemental balances: ( ) H f for H and ( ) O f for O jest is linearly independent on charge and elemental/core balances for elements/cores different from H and O. This linear inde- pendence proves that ( ) ( ) 2 O H f f is a new equation, considered as the starting form of the electron bal- ance (GEB) related to the redox system in question. In this way it has been shown, inter alia, that the simplest form of GEB related to a redox system in mixed-solvent media is the same, regardless the solvent composi- tion—assuming that the solutes do not form with solvents other species (except those known from aqueous me- dia) besides solvates [5]-[7]. * Corresponding author.

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Page 1: Linear Dependence of Balances for Non-Redox Electrolytic ...file.scirp.org/pdf/AJAC_2014122511185879.pdf · For non -redox systems, ... linear combination of the relevant equations

American Journal of Analytical Chemistry, 2014, 5, 1285-1289 Published Online December 2014 in SciRes. http://www.scirp.org/journal/ajac http://dx.doi.org/10.4236/ajac.2014.517134

How to cite this paper: Michałowska-Kaczmarczyk, A.M. and Michałowski, T. (2014) Linear Dependence of Balances for Non-Redox Electrolytic Systems. American Journal of Analytical Chemistry, 5, 1285-1289. http://dx.doi.org/10.4236/ajac.2014.517134

Linear Dependence of Balances for Non-Redox Electrolytic Systems Anna M. Michałowska-Kaczmarczyk1, Tadeusz Michałowski2* 1Department of Oncology, The University Hospital in Cracow, Cracow, Poland 2Faculty of Engineering and Chemical Technology, Technical University of Cracow, Cracow, Poland Email: *[email protected] Received 12 October 2014; revised 29 November 2014; accepted 11 December 2014

Copyright © 2014 by authors and Scientific Research Publishing Inc. This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/

Abstract Two complex dynamic non-redox systems are considered as examples, providing interdependent linear equations. A simple and efficient linear combination method that leads the system of equa-tions to the identity, 0 = 0, is used for this purpose. These examples are clear confirmations of the general property differentiating non-redox and redox electrolytic systems. This property is in-volved with linear dependence or independence of ( ) ( )⋅ −2 O Hf f on charge and elemental/

core balances for elements/cores ≠ H, O, where ( )Hf and ( )Of are elemental balances for H and O, respectively.

Keywords Titration, Liebig-Denigès Method, Complexonometric Detemination of Zinc

1. Introduction In numerous examples of electrolytic redox systems presented in our previous papers [1]-[4], it was found that the linear combination ( ) ( )2 O Hf f⋅ − of elemental balances: ( )Hf for H and ( )Of for O jest is linearly independent on charge and elemental/core balances for elements/cores different from H and O. This linear inde-pendence proves that ( ) ( )2 O Hf f⋅ − is a new equation, considered as the starting form of the electron bal-ance (GEB) related to the redox system in question. In this way it has been shown, inter alia, that the simplest form of GEB related to a redox system in mixed-solvent media is the same, regardless the solvent composi-tion—assuming that the solutes do not form with solvents other species (except those known from aqueous me-dia) besides solvates [5]-[7].

*Corresponding author.

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For non-redox systems, it was stated that the linear combination ( ) ( )2 O Hf f⋅ − is linearly dependent on charge and elemental/core balances for elements/cores ≠ H, O. This can easily be stated by transformation of the linear combination of the relevant equations to the identity, 0 = 0. In this work, this kind of transformation will be applied to two relatively complex systems involved with 1) determination of cyanide according to Liebig- Denigès method [8] and 2) complexometric titration of zinc with EDTA [9].

2. Liebig-Denigès Method of Cyanide Determination In the system involved with Liebig-Denigès method, V mL of the solution composed of AgNO3 ( ) ( )01 2 02N H O N+ is added into 0V mL of the solution composed of ( ) ( ) ( ) ( )03 04 3 05 2 06NaCN N KI N NH N H O N+ + + ( )2 06H O N . At defined stage of the process, the following species are present in the system:

2H O (N1), H+ (N2), OH− (N3, n3), Na+ (N4, n4), K+ (N5, n5), 3NO− (N6, n6), HCN (N7, n7), CN− (N8, n8), 4NH+ (N9, n9), NH3 (N11, n11), Ag+ (N12, n12), AgOH (N13, n13), ( )2Ag OH − (N14, n14), ( )2

3Ag OH − (N15, n15), ( )2Ag CN − (N16, n16), ( )2

3Ag CN − (N17, n17), ( )34Ag CN −(N18, n18), AgI (N19, n19), 2AgI− (N21, n21), 2

3AgI − (N22, n22), 3

4AgI − (N23, n23), 3AgNH+ (N24, n24), ( )3 2Ag NH + (N25, n25), ( )AgI s (N26, n26), I− (N27, n27).

From the balances: • ( )Hf

( ) ( ) ( ) ( )( ) ( ) ( ) ( )

( ) ( )

1 2 2 3 3 4 4 5 5 6 6 7 7 8 8 9 9

11 11 12 12 13 13 14 14 15 15 16 16 17 17

18 18 19 19 21 21 22 22 23 23 24 24 25 25 26

2N N 1 2n N 1 2n 2N n 2N n 2N n N 1 2n 2N n N 4 2n

N 3 2n 2N n N 1 2n N 2 2n N 3 2n 2N n 2N n

2N n 2N n 2N n 2N n 2N n N 3 2n N 6 2n 2N

+ + + + + + + + + + + +

+ + + + + + + + + + +

+ + + + + + + + + + 26 27 27

02 05 06

n 2N n 2N 3N 2N ,

+

= + +

(1)

• ( )Of

( ) ( )( ) ( ) ( )

1 2 2 3 3 4 4 5 5 6 6 7 7 8 8 9 9 11 11

12 12 13 13 14 14 15 15 16 16 17 17 18 18 19 19

21 21 22 22 23 23 24 24 25 25 26 26 27 27 01 02 06

N N n N 1 n N n N n N 3 n N n N n N n N n

N n N 1 n N 2 n N 3 n N n N n N n N n N n N n N n N n N n N n N n 3N N N ,

+ + + + + + + + + + +

+ + + + + + + + + + +

+ + + + + + + = + +

(2)

we have • ( ) ( )2 O Hf f⋅ −

2 3 6 7 9 11 13 14 15 24 25 01 05N N 6N N 4N 3N N 2N 3N 3N 6N 6N 3N− + + − − − + + + − − = − (3)

Addition of (3) to charge balance (4) and balances: f(Na) (5), f(K) (6), 5 f(NO3) (7), f(CN) (8), 3f(NH3) (9), f(Ag) (10) and f(I) (11)

2 3 4 5 6 8 9 12 14 15 16 17 18 21 22 23

24 25 27

N N N N N N N N N 2N N 2N 3N N 2N 3N N N N 0,

− + + − − + + − − − − − − − −

+ + − = (4)

03 4N N= (5)

04 5N N= (6)

01 65N 5N= (7)

7 8 16 17 18 03N N 2N 3N 4N N+ + + + = (8)

9 11 24 25 053N 3N 3N 6N 3N+ + + = (9)

01 12 13 14 15 16 17 18 19 21 22 23 24 25 26N N N N N N N N N N N N N N N= + + + + + + + + + + + + + (10)

19 21 22 23 26 27 04N 2N 3N 4N N N N+ + + + + = (11)

gives the identity, 0 = 0, i.e., (3) is not an independent balance in the system. The identity is also valid before crossing the solubility product for AgI(s).

3. Complexometric Titration of Zinc with EDTA Let us consider 0V mL of titrand (D), containing ( ) ( ) ( )4 0 3 1 4 2 2ZnSO C NH C NH Cl C NaH In+ + + (erio T,

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C0In) titrated with V mL of titrant (T) containing EDTA (C). The titrand is composed of N01 molecules of ZnSO4·7H2O (goslarite), N02 molecules of NH3, N03 molecules of

NH4Cl, N04 molecules of NaH2In = C20H12N3O7SNa, N05 molecules of H2O and the titrant is composed of N06 molecules of EDTA = Na2H2L·2H2O = C10H14N2O8Na2·2H2O and N07 molecules of H2O, at defined point of ti-tration (V mL of T added). In the system in question, the following species are formed:

H2O (N1), H+ (N2, n2), OH− (N3, n3), 4HSO− (N4, n4), 24SO − (N5, n5), Cl− (N6, n6), Na+ (N7, n7), 4NH+ (N8, n8),

3NH (N9, n9), Zn2+ (N11, n11), ZnOH+ (N12, n12), soluble complex ( )2Zn OH (N13, n13), ( )3Zn OH − (N14, n14), ( )2

4Zn OH − ( )22H L − (N15, n15), 2

3ZnNH + (N16, n16), ( )23 2

Zn NH + (N17, n17), ( )23 3

Zn NH + (N18, n18), ( )23 4

Zn NH + (N19, n19), ZnCl+ (N21, n21); ZnSO4 (N22, n22), C20H13N3O7S (N23, n23), C20H12N3O7S− (N24, n24), C20H11N3O7S2− (N25, n25), C20H10N3O7S3− (N26, n26), C20H10N3O7SZn− (N27, n27), ( ) 4

20 10 3 7 2C H N O S Zn − (N28, n28), 2

10 18 2 8C H N O + ( )2

6H L + (N29, n29), 10 17 2 8C H N O+ ( )5H L+ (N31, n31), C10H16N2O8 ( )4H L (N32, n32), 10 15 2 8C H N O− ( )13H L− (N33,

n33), 210 14 2 8C H N O − ( )2

2H L − (N34, n34), 310 13 2 8C H N O − ( )3HL − (N35, n35), 4

10 12 2 8C H N O − ( )4L − (N36, n36), 10 13 2 8C H N O Zn− ( )ZnHL− (N37, n37), 2

10 12 2 8C H N O Zn − ( )2ZnL − (N38, n38), 310 13 2 9C H N O Zn − ( )3ZnOHL −

(N39, n39). The complex 3ZnOHL − is formed in reaction between ZnOH+ and 4L − . The species can be arranged in

the following balances: • ( )Hf

( ) ( ) ( ) ( ) ( )( ) ( ) ( ) ( ) ( )

( ) ( ) ( ) ( )

1 2 2 3 3 4 4 5 5 6 6 7 7 8 8 9 9

11 11 12 12 13 13 14 14 15 15 16 16

17 17 18 18 19 19 21 21 22 22 23 23

24

2N N 1 2n N 1 2n N 1 2n 2N n 2N n 2N n N 4 2n N 3 2n

2N n N 1 2n N 2 2n N 3 2n N 4 2n N 3 2n

N 6 2n N 9 2n N 12 2n 2N n 2N n N 13 2n

N 1

+ + + + + + + + + + + + +

+ + + + + + + + + + +

+ + + + + + + + + +

+ ( ) ( ) ( ) ( ) ( ) ( )( ) ( ) ( ) ( ) ( ) ( )( ) ( ) ( )

24 25 25 26 26 27 27 28 28 29 29

31 31 32 32 33 33 34 34 35 35 36 36

37 37 38 38 39 39

01 02 03 04 0

2 2n N 11 2n N 10 2n N 10 2n N 20 2n N 18 2n

N 17 2n N 16 2n N 15 2n N 14 2n N 13 2n N 12 2n

N 13 2n N 12 2n N 13 2n 14N 3N 4N 12N 2N

+ + + + + + + + + + +

+ + + + + + + + + + + +

+ + + + + +

= + + + + 5 06 0718N 2N ,+ +

(12) • ( )Of

( ) ( ) ( )( ) ( ) ( ) ( )

( ) ( ) ( ) ( ) ( )( )

1 2 2 3 3 4 4 5 5 6 6 7 7 8 8 9 9 11 11

12 12 13 13 14 14 15 15 16 16 17 17 18 18

19 19 21 21 22 22 23 23 24 24 25 25 26 26

27 27 28

N N n N 1 n N 4 n N 4 n N n N n N n N n N n

N 1 n N 2 n N 3 n N 4 n N n N n N n

N n N n N 4 n N 7 n N 7 n N 7 n N 7 n

N 7 n N 14 n

+ + + + + + + + + + + +

+ + + + + + + + + + +

+ + + + + + + + + + + +

+ + + +( ) ( ) ( ) ( ) ( )( ) ( ) ( ) ( ) ( ) ( )

28 29 29 31 31 32 32 33 33

34 34 35 35 36 36 37 37 38 38 39 39

01 04 05 06 07

N 8 n N 8 n N 8 n N 8 n

N 8 n N 8 n N 8 n N 8 n N 8 n N 9 n 11N 7N N 10N N ,

+ + + + + + + +

+ + + + + + + + + + + +

= + + + +

(13)

The balance ( ) ( )2 O Hf f⋅ − , obtained from Equations (12) and (13), is as follows

2 3 4 5 8 9 12 13 14 15 16 17

18 19 22 23 24 25 26 27 28 29 31

33 34 35 36 37 38 39 01 02 03 04 06

N N 7N 8N 4N 3N N 2N 3N 4N 3N 6N 9N 12N 8N N 2N 3N 4N 4N 8N 2N N N 2N 3N 4N 3N 4N 5N 8N 3N 4N 2N 2N ,

− + + + − − + + + + − −

− − + + + + + + + − −

+ + + + + + + = − − + +

(14)

Addition of (14) to charge balance (15) and balances for ( )2 Znf⋅ (16), ( )Clf (17), ( )Naf (18), ( )46 SOf⋅ (19), ( )33 NHf⋅ (20), ( )20 10 3 7C H N O Sf (21), and ( )10 12 2 80 C H N Of⋅ (22):

2 3 4 5 6 7 8 11 12 14 15 16 17 18 19 21 24

25 26 27 28 29 31 33 34 35 36 37 38 39

N N N 2N N N N 2N N N 2N 2N 2N 2N 2N N N 2N 3N N 4N 2N N N 2N 3N 4N N 2N 3N 0,

− − − − + + + + − − + + + + + −

− − − − + + − − − − − − − = (15)

01 11 12 13 14 15 16 17 18 19 21 22 27 28

37 38 39

2N 2N 2N 2N 2N 2N 2N 2N 2N 2N 2N 2N 2N 2N 2N 2N 2N ,

= + + + + + + + + + + + +

+ + + (16)

6 21 03N N N+ = (17)

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A. M. Michałowska-Kaczmarczyk, T. Michałowski

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04 06 7N 2N N+ = (18)

01 4 5 226N 6N 6N 6N= + + (19)

8 9 16 17 18 19 02 033N 3N 3N 6N 9N 12N 3N 3N+ + + + + = + (20)

04 23 24 25 26 27 28N N N N N N 2N= + + + + + (21)

29 31 32 33 34 35 36 37 38 39 060 N 0 N 0 N 0 N 0 N 0 N 0 N 0 N 0 N 0 N 0 N⋅ + ⋅ + ⋅ + ⋅ + ⋅ + ⋅ + ⋅ + ⋅ + ⋅ + ⋅ = ⋅ (22)

gives the identity, 0 = 0, that testifies about linear dependence between the balances, i.e., Equation (14) is li-nearly dependent on other balances in the system. Note that the Equations (19)-(22) are specified separately, ac-cording to different “cores”: SO4, NH3, C20H10N3O7S, C10H12N2O8. Note that N enters the compounds and spe-cies in Equations (20)-(22); S enters the compounds and species in Equations (19) and (21); C enters the com-pounds and species in Equations (21) and (22). However, none transformations occur between the “cores” of the species that belong to different concentration balances. Generalizing, for any non-redox system, there are some numbers/multipliers for the relevant equations that reduce the sum received to the identity.

Referring again to Equation (21), related to the species involved with erio T, one can write the elemental balances:

23 24 25 26 27 28 0420N 20N 20N 20N 20N 40N 20N+ + + + + = (for C),

23 24 25 26 273N 3N 3N 3N 3N+ + + + 28 046N 3N+ = (for N), 23 24 25 26 27 28 04N N N N N 2N N+ + + + + = (for S),

and

23 24 25 267N 7N 7N 7N+ + + 27 28 047N 14N 7N+ + = (for O).

All the equations are identical and equivalent to Equation (21), because the “core” C20H10N3O7S is unchanged in reactions occurred during the titration. Similarly, the species involved with EDTA, see Equation (22), fulfill the relations:

29 31 32 33 34 35 36 3710N 10N 10N 10N 10N 10N 10N 10N+ + + + + + + 38 39 0610N 10N 10N+ + = (for C),

and

29 31 32 33 34 35 36 37 38 393N 3N 3N 3N 3N 3N 3N 3N 3N 3N+ + + + + + + + + = 063N (for N).

Both equations are equivalent to ( )10 12 2 8C H N Of .

4. Final Comments Checking of linear dependence or independence of algebraic equations [10] is not a mathematical problem of the highest order. However, it requires an additional knowledge of the user, concerning the properties of the matrix

ija = A ( 1, ,i m= ; 1, ,j n= ; n m> ) of coefficients ija in the matrix equation =Ax b , where

11 1 1 1

1

, , n

m mn n m

a a x b

a a x b

= = =

A x b (23)

with vectors of variables, x , and vector of constant terms, b . For explaining these properties, some abstract terms such as (dimension of) vector space, (matrix, kolumn, row) ranks, are used.

It should be noted, however, that the coefficients ija and ib used in purely algebraic equations

11 1 1 1

1 1

n n

m mn n m

a x a x b

a x a x b

+ + =

+ + =

(24)

do not have specific physical or chemical connotations. Assuming the charge balance as the second of the bal-ances (24) considered for this purpose, we state that the coefficients 2 ja in this balance are involved with ex-ternal charges of the species in the system in question and 2 0b = in the vector b . The coefficients ija in the elemental/core balances are involved with the number of elements/cores in the related species. The coefficients

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in ( ) ( )2 O Hf f⋅ − depend on the form of equations for ( )Hf and ( )Of . In this paper, the linear relationship between the balance ( ) ( )2 O Hf f⋅ − and charge + elemental/core bal-

ances for elements/cores ≠ H, O was checked in extremely simple way (indicated in [4]) and proved on exam-ples of two electrolytic non-redox systems, of analytical importance, known from titrimetric analyses. Full com-plexity of these systems, known from preliminary physicochemical data, is involved in the related balances, ex-pressed in terms of numbers of entities of particular components and species iz

iX . The related balances can also be expressed in terms of molar concentrations: iz

iX ( ) 30 i A10 N NV V+ = × for the species iz

iX (NA― Avogadro’s number) and analogous relationships for components forming the titrand (D) and titrant (T) in the related D + T system. It should be recalled and emphasized that a linear relationship between ( ) ( )2 O Hf f⋅ − and charge + elemental/core balances for elements/cores ≠ H, O does not occur for redox systems, and the re-sulting balance is the basis of formulation of GEB for these systems, obtained according to Approach II to GEB [1]-[7] [11].

References [1] Michałowski, T. (2010) The Generalized Approach to Electrolytic Systems: I. Physicochemical and Analytical Impli-

cations. Critical Reviews in Analytical Chemistry, 40, 2-16. http://dx.doi.org/10.1080/10408340903001292 [2] Michałowski, T., Toporek, M., Michałowska-Kaczmarczyk, A.M. and Asuero, A.G. (2013) New Trends in Studies on

Electrolytic Redox Systems. Electrochimica Acta, 109, 519-531. http://www.sciencedirect.com/science/article/pii/S0013468613013947 http://dx.doi.org/10.1016/j.electacta.2013.07.125

[3] Michałowski, T., Michałowska-Kaczmarczyk, A.M. and Toporek, M. (2013) Formulation of General Criterion Distin- guishing between Non-Redox and Redox Systems. Electrochimica Acta, 112, 199-211 http://www.sciencedirect.com/science/article/pii/S0013468613016836 http://dx.doi.org/10.1016/j.electacta.2013.08.153

[4] Michałowska-Kaczmarczyk, A.M. and Michałowski, T. (2013) Comparative Balancing of Non-Redox and Redox Electro- lytic Systems and Its Consequences. American Journal of Analytical Chemistry, 4, 46-53. http://www.scirp.org/journal/PaperInformation.aspx?paperID=38569#.VGObL2dvHFw http://dx.doi.org/10.4236/ajac.2013.410A1006

[5] Michałowski, T., Pilarski, B., Asuero, A.G. and Michałowska-Kaczmarczyk, A.M. (2014) Chapter 9.4: Modeling of Acid- Base Properties in Binary-Solvent Systems. In: Wypych, G., Ed., Handbook of Solvents, Volume 1, Properties, 2nd Edi- tion, ChemTec Publishing, Toronto, 623-648. http://store.elsevier.com/Handbook-of-Solvents-Volume-1/isbn-9781895198645/

[6] Michałowska-Kaczmarczyk, A.M. and Michałowski, T. (2014) Compact Formulation of Redox Systems According to GATES/GEB Principles. Journal of Analytical Sciences, Methods and Instrumentation, 4, 39-45. http://www.scirp.org/journal/PaperInformation.aspx?PaperID=46335#.VGm1Tmfpt74

[7] Michałowska-Kaczmarczyk, A.M. and Michałowski, T. (2014) Generalized Electron Balance for Dynamic Redox Sys- tems in Mixed-Solvent Media. Journal of Analytical Sciences, Methods and Instrumentation, 4, 102-109. http://www.scirp.org/Journal/PaperInformation.aspx?PaperID=52018#.VIfpeMkdqUR

[8] Michałowski, T., Asuero, A.G., Ponikvar-Svet, M., Toporek, M., Pietrzyk, A. and Rymanowski, M. (2012) Principles of Computer Programming Applied to Simulated pH-Static Titration of Cyanide According to a MODIFIED Liebig- Denigès Method. Journal of Solution Chemistry, 41, 1224-1239. http://dx.doi.org/10.1007/s10953-012-9864-x

[9] Michałowski, T. (2001) Calculations in Analytical Chemistry with Elements of Computer Programming (in Polish), PK, Cracow. http://suw.biblos.pk.edu.pl/resourceDetails&rId=3974

[10] http://en.wikipedia.org/wiki/System_of_linear_equations [11] Michałowski, T. (2011) Application of GATES and MATLAB for Resolution of Equilibrium, Metastable and Non-

Equilibrium Electrolytic Systems, In: Michałowski, T., Ed., Applications of MATLAB in Science and Engineering, In- Tech—Open Access Publisher in the Fields of Science, Technology and Medicine, Rijeka, Chapter 1, 1-34. http://www.intechopen.com/books/show/title/applications-of-matlab-in-science-and-engineering

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