Eastern Illinois University e Keep Masters eses Student eses & Publications 1977 Stability Constants of NaCO3-, NaSO4- and KCO3- in Water at 25°C Frank Dennis Blum Eastern Illinois University is research is a product of the graduate program in Chemistry at Eastern Illinois University. Find out more about the program. is is brought to you for free and open access by the Student eses & Publications at e Keep. It has been accepted for inclusion in Masters eses by an authorized administrator of e Keep. For more information, please contact [email protected]. Recommended Citation Blum, Frank Dennis, "Stability Constants of NaCO3-, NaSO4- and KCO3- in Water at 25°C" (1977). Masters eses. 3271. hps://thekeep.eiu.edu/theses/3271
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Eastern Illinois UniversityThe Keep
Masters Theses Student Theses & Publications
1977
Stability Constants of NaCO3-, NaSO4- andKCO3- in Water at 25°CFrank Dennis BlumEastern Illinois UniversityThis research is a product of the graduate program in Chemistry at Eastern Illinois University. Find out moreabout the program.
This is brought to you for free and open access by the Student Theses & Publications at The Keep. It has been accepted for inclusion in Masters Thesesby an authorized administrator of The Keep. For more information, please contact [email protected].
Recommended CitationBlum, Frank Dennis, "Stability Constants of NaCO3-, NaSO4- and KCO3- in Water at 25°C" (1977). Masters Theses. 3271.https://thekeep.eiu.edu/theses/3271
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pdm
STABILITY CONSTANTS OF NaCOs-' Naso�--
AND KC03 IN WATER AT 2s0c (TITLE)
BY
FRANK DENNIS BLUM ">
THESIS SUBMlmD IN PARTIAL FULFILLMENT OF THE REQUIREMENTS
FOR THE DEGREE OF
MASTER OF SCIENCE. DEPARTMENT OF CHEMISTRY IN THE GRADUATE SCHOOL, EASTERN ILLINOIS UNIVERSITY
CHARLESTON, ILLINOIS
1977 YEAR
• 1
I HEREBY RECOMMEND THIS THESIS BE ACCEPTED AS FULFILLING
THIS PART OF THE GRADUATE DEGREE CITED ABOVE
�2'1!!7� DATE /
� 2-(/!7'7 DATE /
ABSTRACT
Title of thesis: Stabi l i ty Constants of NaC03- , Naso,.- and KC03-
i n Water at 25°C.
Frank Denni s B lum, Master of Science , 1977
Thesis di rected by: David W . Ebdon , Associate Professor of Chemi stry
A new method for determining ion association constants in aqueous
sol utions usi ng ion selective el ectrodes has been developed. This meth
od has been appl ied to the NaC0 3- , Naso,.- and KC0 3- i on pairs at 25°C.
Association constants for NaC03- and Naso,.- were determined at various
ioni c strengths and ex�rapolated to zero i onic strength to yie l d 2 . 2 ±
0 . 2 for NaC03- and 5 . 3 ±. 0 . 4 for NaSOi.- . Values for the association
constants at an ionic strength near sea water ( I=0 . 70) we1e cal culated
to be 1 . 7 ± 0 . 1 for Naco; and 2 . 1 ± 0 . 2 for Naso,.- . The Kco3- asso-
ciation constant was determi ned to be between zero and one.
Other less d irect methods of determini ng these constants were
tested and evaluated. It was also evident sodi um m-benzenedisul fonate
i s a weakly associ ated electrolyte, which may associate to approximately '
the same extent as sodium carbonate . An Ori on model 94-11 Sodium Ion
Electrode, Orion model 93-19 Potassium Ion Electrode, Sensorex model
S810C03 Carbonate Sensitive El ectrode and Chemtrix model 1015M Sul fate
Electrode were used and compared i n this study.
VITA
Name: Frank Denni s Blum.
Pennanent Address: 400 N. Fairview, Mt . Prospect, I l l inoi s 60056.
Degree and date to be conferred: M .S . , 1977.
Date of bi rth: January 27 , 1955 .
Place of bi rth: Chicago, I l l inoi s .
Secondary education: Lane Techn ical High School , Chicago, " Il l inoi s , 1968-1969. Prospect High School , M� . Prospect , I l l inoi s , 1969-1972.
. .
Col l egi ate institution attended: Date
Univers i ty of I l l inois (Chi cago
Degree Date of Degree
Ci rcle Campus}, Chicago , I l l i nois 1972-1973
Eastern I l l i nois University Charleston , Il l i nois
Eastern I l l i nois Univers ity Charleston , I l l i nois
Major: Physical Chemistry .
1973-1976
1976-1977
B . S . May 1976
M . S . December 1977
Positions hel d: Graduate Assistant, Eastern I l l inois Universi ty , 1976-1977. Teaching Assistant, U�iversity of Minnesota, Mi nneapol i s , Minnesota, Present.
i i i
ACKNOWLEDGMENTS
The author woul d l i ke to express his sincere gratitude to
Professor David W . Ebdon for h is suggestion of thi s project , assi st
ance, gui dance, encouragement and patience during this study.
I would a l so l i ke to thank Ms. Li nda Blum for typing and cor
recting this manuscri pt.
Thi s work was parti ally funded by the Council on Facu lty
Research of Eastern I l l inois University.
I woul d like to dedicate thi s thesi s to the typi st, my wi fe ,
L I ST OF FIGURES dn Plot of Qf versus the radius for univalent i ons
of opposi te ( 1 ) and simi l ar ( 2 ) charge type . . . . .
Di agrams of a sodi um sensit ive sol i d state gl ass el ectrode ( a ) , a potassi um sensitive ion exchange el ectrode (b ) and a single junction reference electrode (c ) . . . . . . . . . . . . . . . . . . . . . . . . •
Di agram of the waterjacketed cel l and experi -menta 1 arrangement . . . . . . . . . . . . . . . . . . . . . . . . . . . . • .
Typi cal cal i bration curve for sodium ion elec-trode at constant i on ic strength . . . . . . . . . . . . . • . .
Plot of Log KA versus IT for NaC03- . . . . . • . . . . . . . . .
Plot of Log KA (Nernstian) versus IT for NaC0 3- . . . .
P lot of Log KA versus If for NaSQ4- • . . . • . . . . . . . . . •
Plot of Log KA(Nernstian) versus IT for NaS04- • • • •
Page
8
27
31
41
45
46
51
52
Figure 9 . Plot of electrode response versus i on ic strength for salts with constant sodium ion concentra-ti on • • • • • • • • • • • • . • • • • • • • . • • • • • • • • . • • • • • . • • • • • • • 56
Figure 10 . Plot of el ectrode response versus Log [Na+] for comparison of Na2BDS and Na2C0 3 . . . . . . . . . . . . . 58
Figure 1 1 . Plot of electrode response versus Log [C03 2- ] using carbonate selective electrode . . . . • . . . . . . . 60
Figure 12 . Plot of electrode response versus pH for sulfate ion selective el ectrode . . . . . . . . . . . . . . . . . . . . . . . . . 62
v i i
LIST OF TABLES
Table 1 . Apparent and Zero Ionic Strength Association Constants for Naco�-
Bol tzman constant (1.381 · 10-16 erg/K); slope from Nernst
equation
KA thermodynami c association constant
K� apparent association constant ·A Kd di ssociation constant
K�el selectiv ity constant of i th i on 1
n1 number of ions with potenti al �i
i x
no total number of ions
r di stance between two ions (cm)
R gas constant 8 . 314 (J/(mol . K) )
T absolute temperature (K) Z; charge of i th ion ( s i�ned)
a degree of di ssociation
r. 1 activi ty coeffi cient of i
y± mean i onic acti vi ty coefficient
e: electronic charge (esu)
A mol ar conductance
Ao molar conductance at zero ionic strength
Pi charge density about ion i
'¥. J potential about ion i
v2 nab l a , l ap laci an operator
[F] concentration of F [F] I i ni ti al concentration of F [F]_T total concentration of F [F] F free i on concentration of F (F) acti vity of species F
x
I . INTRODUCTION
In recent years an increased i nterest in the thermodynamic
characterization of natural water systems has been observed. This
i nterest can be attributed to envi ronmental probl ems , production of
energy-resources and the characterization of the marine envi ronment.
The thermodynami c characterization of natural water systems requi res
knowledge of the pressure, temperature and solution composition .
The species in solution wi l l not only be simple ions , organi c mole
cules , and dissolved gases , but complex ions and i on pai rs . To
determ i ne the concentration of the l atter one needs the ir formation
constants.
A thermodynamic model of sea water has been developed1 and re
fined2 which uti l izes ion association constants to calculate the
free energies of formation of a l l the major and minor ion pai rs
which exist i n sea water. · Then using the el emental composition of
sea water, the total free energy of the system i s i teratively min
imized to achieve equi l i bri um speci ation. The cal culated results
for free ion concentrations and for prediction of precipi tation
agree wel l with experimental resul ts i n ocean ic waters .
Another important aspect of computer mode l i ng i s in oil wel l
brines. Secondary recovery techniques include water-flooding , where
available sources of water ( supply waters ) are pumped i nto the wel l
and the oi l i s displ aced al ong with produced water. Produced water
contains high concentrations of di ssol ved sal ts . This l eads to the
1
·-.
2
production ·of scale, usual ly al kal i ne earth carbonates and sul fate s ,
i n the pi pes and the producing fonnati on , a porous rock. The usual
solution to this problem i s to pul l out the oi l rigging and frac
ture the fonnation wi th explosives . Accurate data and a good com
puter model cou l d predict when sca l i ng wou ld occur and also what
mixtures of supply waters or what compl exing agents could be used
to reduce or prevent scal i ng i n the most economi cal ly feasible way .
In order to improve the re 1 i abi l ity of these computer mode 1 s ,
the present research was undertaken to more accurately detennine
the association constants of sodium carbonate , potassium carbonate
and sodi um sul fate. Carbonate and sul fate are important i n natural
water systems because of the i r effect on precipitation equi l i bria .
Carbonate i s a l so important because of i ts effect on the pH of these
systems . Even though the concentrations of carbonate and sul fate
are sma l l and the equi l i brium constants are also smal l , the effect
on i on pairing in respect to the concentrations of these anions i s
significant due to the relatively l arge concentrations of sodium
i on i n sea water and i n most bri nes .
3
I I . HISTORICAL REVIEW
. To und�rstand how the concept of i on pai ring relates to other
ionic solution processes , a bri ef summary of historical developments
leading to an understanding of ionic interactions in solution i s
appropriate. The concept of an ion, o r charged parti cle which could
carry electric ity, was proposed by Faraday i n 1833. C laus i us sug
gested i n 1857 that ions were produced by the breaking of chemical
bonds . This process occurred when an electrolyte dissolved in a
solvent. Arrheni us; 3 however, suggested that electrolytes were
only partially di ssoci ated i nto ions. The degree of di ssociation ,
a, can be detennined by the ratio of the molar conductance, A, at
concentration C to the molar conductance at i nfi nite di l ution, Ao,
or
a= A/Ao ( 1 )
Thi s concept works very wel l when appl ied to weak el ectrolytes .
The di ssociation i n general for a weak aci d , HA, can be expressed
usi�g the l aw of mass action as
= [H+] [A-] Kd [HA]
At equi l ibrium , [H+] =[A-] = cxC and.[HA]= ( 1-cx )C , where C i s the
( 2 )
stoichiometric concentration of HA . Substituting the rel ationships
i nto equation ( 2 ) we have
A2C K - ---...-d - Ao(Ao-A) ( 3 )
or rearranging,
1 _ 1 + .,.._.CA_.,.._. A - Ao KdA�
4
(3a )
Thi s equation, known as the Ostwa ld Dilution Law, describes the dis-
sociation of weak aci ds , such as acetic aci d , at l ow concentrations .
However i t breaks down when appl ied to the conductance of a "strong
electrolyte" , such as sodi um chloride .
This di l emma was partia l ly cl arified i n 1906 by Bjerrum4 from
research on hexaaquochromium ( I I I ) sal ts . He proposed that not
only these sal ts, but al l strong el ectrolytes dissoci ate completely
i nto i ons . This fact was l ater verified by x-ray crystal studies,
which showed that "strong electrolytes" in the sol i d state were
composed of discrete ions . "Weak el ectrolytes " such as acetic aci d ,
were shown to exist as undissociated neutral molecules .
The modern theory of el ectrolytes dates from the classic work
of Debye and Huckel5 i n 1923 . They assumed that a strong electrolyte
was completely dissociated i nto i ons i n aqueous sol utions and took .
as the ir model a rig id charged sphere i n a diel ectric continuum.6 A
Maxwel l -Bol tzmann distribution of i ons was assumed with the potential
due only to the electrical energy between a "centra l " ion and a l l
the other i ons in sol ution:
(4)
Here ni i s the number of i ons with a gi ven potential �j wi th re
spect to the jth ion, n0 i s the total number of i ons and e:, k and
T are the electron charge , Bol tzmann constant and absolute tempera-
5
ture, respect ively.
This di stribution was then used to calculate the charge densi ty ,
p, which coul d · be used in the Poisson Equation ,
( 5 )
where 'V� i s the l ap lac ian operator and D i s the diel ectric constant
of the sol vent. With proper simpl ifi cation and truncation of an
exponential series,equation ( 5 ) reduces to a simple second order
differential equation. The simpl i fi cation i nvolves assuming that
the i nterel ectronic potential for very di l ute solutions wi l l be much
less than the mean thennal energy . Therefore the second and higher
order tenns in 1/kT can be assumed neg l i gib le . The di fferential
equation when solved yields the el ectri c potenti al, which can be
rel ated to the chemical potenti al of the system. II The Debye-Huckel result for the mean ionic activity coeffi cient
can be stated as:
where Z 1,Z 2 are the charges of ions 1 and 2 ,
-y± i s the mean i on ic acti v ity coeffi ci ent,
a i s the di stance of cl osest approach of the i ons ,
I i s the ionic strength (=!zI:c.Z.2} , 1 1
and A and B are defined constants .
(6 )
This equation i s of great importance because i t can describe the
behavior of a strong electrolyte i n a di l ute solution wi thout the
use of an arbi trary constant. It agrees wel l with experimental re
sul ts for 1-1 el ectrolytes to an ionic strength of about O . lM . " There have been many attempts to extend the Debye-Huckel theory.
Guggenheim7 ( for 1-1 el ectrolytes) and Davies0 ( for 1-1 and 2-1
electrolytes ) have made the more successful attempts to calculate II acti vity coefficients� priori , based on the Debye-Huckel model and
assumed parameters . II
The Oebye-Huckel theory does have several l imitations . One
major problem i s that for smal l i ons , i ons of large charge type or
sol vents of low dielectric constant the electrical potential energy
i s not negl igi ble compared to the thermal energy . The Bjer�Jm9
treatment attempts to solve thi s problem. The treatment of Bjerrum
fi rst assumes that there i s a Bol tzmann di stribution of i ons in
solution and that the only energy that is important is the elec
troni c potenti al between two close ions . Therefore;
(-Z 1Z2£2 \ dn = n exp \ DrkT ) dV (7 )
where r i s the distance between ions 1 and 2 with charges of Z1 and
6
Z2 respecti vely, and the other variables are as previously defined.
With the assumption of spherical symmetry the equation can be simpl i
fied by replacing dV with 4�r2dr, yielding;
dn = n4�r2exp(-Z1Z2£�) dr DrkT
(8 )
Thi·s equation is pl otted i n figure ( 1 ) for charges of the same and
opposite charge types . For charges of opposite s ign there exists a
7
mi nimum which can be calcul ated by di fferentiating dn/dr with respect
to r, setting the result equal to zero and solving for r. Thi s proc
ess yiel ds a resu lt for the value of the radius rmin ' where the po
tential energy i s a minimum,
IZ1Z2le:2 rmin = 2 DkT (9 )
The distance rmin (3.sA for a 1-1 electrolyte) i s the "Bjerrum
Distance" which Bjerrum used to define an i on pai r. · Two ions of
opposite s ign within a di stance of rmin or less were said to be
paired. This equation can be rearranged to
IZ1Z2!e:2 2kT = ---Dr mi n
(9a)
Note that at rmin the electronic potenti al energy i s twice the mean
thennal energy. This contradicts the Debye-Huckel assumption that
the interelectronic energy i s negl igible compared to the thennal
energy.
I t should be noted here t.hat the Bjerrum treatment defi ni ti on
i s somewhat arbitrary and has been described as a mathematical
fiction!0 However the concept of an i on pai r i s important. It can
be thought of as a neutral di pole (for symmetrical electrolytes )
or a charged species ( for unsymmetrical el ectrolytes) th'e presence
of .whi ch wi l l alter the properties of solution� such as conductiv ity
and activi ty .
There have been many developments in the study of i on associa
tion. Conductiv ity measurements have been successful in d�tennining
.·
dn dr
1
0 5 10 15 20
Radius (�)
Figure 1 . Plot of �� versus the radius for univalent
i ons of opposite ( 1 ) and simi lar ( 2 ) charge type.
8
25
9
association constants. However, conductiv ity only works wel l when
the association constants are l arge , as i s the general case for 2-2
or 3-3 electrolytes . Another problem i s that conducti vity i s not a
"speci fic" technique but rel i es on the measurement of a bulk property
and .on the ion- i n-a-continuum model for detennination of association
constants.
A general l imitation of any thennodynami c method i s that it
can only separate a simple i on i nto two categories: free i ons and
ion pai rs . The constitution of the 11 thennodynamic11 ion pai r has
been the subject of debate for severa 1 years . The . Bjerrum theory
counts ions pai red i f they are closer than the arbitrary rmin value .
Some authors11 have suggested that only ions in di rect contact should
be counted as paired. Since then kineti c studies by Eigen and co
workers have shown that ion pair fonnation appears to take pl ace
through a step-wise mechani sm .12 This was further veri fied by
ultrasonic measurements of MnS04 1 3 and MgSQ4 . 1.4 The association
of MS04 i s bel ieved to take pl ace i n three steps , each of which has
characteri stic rate constants and equi l ibrium constant. Step I i s
assumed to be a diffusion control l ed process of free completely sol
vated i ons fanning an i on pai r separated by two water molecules . In
step I I the sulfate can l ose a water molecule to fonn an ion pai r
separated by one water molecule which can be l o�t i n step I I I to
fonn a contact ion p�i r . This process can be represented as
M2+(aq) + S042- ( aq} : M(WW)S04 : M(W}S04 ! MS04 KI KI I KIII
where W represents a water molecule between the ion pai r . This
..
· ..
10
model is i nstructive because i t considers speci fic ion-sol vent inter
actions rather than merely 11bul k11 sol vent properties . It a l so sug
gests that the contact ion pai r i s not necessari ly the most stable
.fonn of an i on pai r . The overa l l association constant for MgSO�
from .ul trasonics 15 agrees wel l with that determined by conductance . 16
Raman spectra , NMR , pol argraphy and kinetics have a lso been
.,used to study i on pai ring and these methods have been sunmarized
... by Davi es . 1 7 Most of these methods , howeve-r , do not work we 11
·when the . . association constant is sma 11 . A thermodynamic method
which i s both sensitive and specific i s the measurement of ion ac-
··. tivi ty by i on selective electrodes . With a mi nimum of assumpti oll$ ,
such measurements can yiel d precise values of i on association con
stants even when the magnitude of the constant i s not l arge. It i s
this method which wi l l be used in the present study.
II I . STATEMENT OF PROBLEM
The purpose of this study i s to detennine the apparent and
thennodynamic association constants for NaC03- , NaS04- and KC03-
11
ion pairs in aqueous soluti ons at 25° using i on selective electrodes .
Estimates of the fonnation constant of NaC0 3- from various exper
imental procedures are generally not i n agreement . I t i s hoped
that thi s more direct method wi l l yi el d a more accurate value for
this constant. The constant for Kco 3- is expected to be very smal l
and often has been assumed to be negl ig ib le . Values for NaS04- are
known from conductance and other methods which can serve as a veri
fication of our method.
Another area to be studied i s the association of the meta
benzenedi sul fonate ion with the sodi um ion . There i s some evi dence
from solution conducti vity that meta-benzenedi sul fonates ei ther do
not associate or associate to a very l imited degree . If these salts
do not associate they can be used as a standard for 2-1 el ectrolytes
just as sodi um chloride and potassium chloride are for 1-1 electrolytes.
In this study we wi l l attempt to calcul ate the equ i l i bri um con-· � stants and examine methods of detennining the constants with the use
of ion selective el ectrodes which respond only to the activity of
the free ion. I t is assumed that a paired i on cannot .affect th�
electrode potential .
I V . THEORY
A . I on Association
When a "weak electrolyte" (AaBb) dissolves in a solvent, an
e�u i l i brium. i s establ i shed between the di ssociated ions AX+, sYand the undi ssociated molecules AaBb . This equ i l ibrium can be
written as
A B ! aAX+ + bBYa b
where ax = by,and the corresponding equ i l i brium expression as
( 10 )
( 11 )
12
where the parentheses represent the activities of the various species
and Kd i s the thennodynamic di ssociation constant.
For a strong electrolyte an equ i l i brium i s establ i shed between
the free ions and ion pai rs . Simi l arly thi s equi l i brium can be ex
pressed by
CX+ + [)Y- ! CX+[)Y- ( i on pair )
with the equi l i brium expression
( cx+(}Y-) K = ----A ( cX+)([}Y-)
( 12 )
(13 )
where KA i s the thermodynamic association constant. The thermody
namic association constant should be a constant at any i onic strength .
However i t i s often convenient to use the apparent or stoichiometric
constant , KA , where the activities are replaced by the stoichiometric
conce_11t rations:
K"' = A
·[CX+()Y-]
ccx+JcoY-J (14)
13
Note �hat the stoichiometric equi l i brium constant can be converted
to the thermodynami c constant by mul ti plying by the appropriate ac-• .I
�i v i ty coeffi cients to obtain .•
( 15 }
where the y's represent the act iv ity coefficients of the species
i nd.i ca ted . '
The fonnation of an ion pai r resul ts in the fonnation of a
species which no l onger has the properties of the free i ons. For
example i t wi l l reduce the conductiv ity of a solution , produce an
u l trasoni c absorption or not respond to an ion selective electrode .
Formation of the ion pai r wi l l reduce the concentration and activity
of the free i ons .
Si nce the association constants for the alkali metal sul fates
and carbonates are smal l , conductiv ity or ultrasonics may not be
the best method for determining these constants . A better method of
determining these constants i s by means of ion selective el ectrodes .
I n theory the ion selective electrode responds only to the act iv ity
of free ions. Therefore i f free ions exist i n equi l ibrium with i on '
pai rs , the measured activity of the free i ons wi l l be l ess than that
calculated assuming complete di ssociati on . If we can then attribute
..
14
thi s decrease sol ely to the fonnation of ion pai rs , we can calcul ate
the concentration of i on pai rs . Using the l aw of mass action and
the free ion and i on pai r concentrations , we can calcul ate the equi
l i bri um constant.
B . Ion Selective El ectrodes
Recently qua l i ty el ectrodes of high selecti vity for certain
i ons have been developed. A sol i d state sodi um gl ass el ectrode,
potassium ion exchange electrode and precipi tate electrodes selec
tive to carbonate and sul fate wi l l be di scussed.
Consi der a glass specifi c ion and reference el ectrode i n con-tact with a solution of interest. This set-up can be represented as:
i nternal I internal I gl ass I solution I reference electrode solution
. membrane
1of i nterest .electrode
v EI E EM Eref
where EIE' EM and Eref are the potentials of the i nternal electrode,
membrane and reference el ectrode, respecti vely. For a gi ven tem
perature and pressure the potential E1E i s expected to be constant
because the el ectrode i s sealed and. the composition of the i nternal
sol ution can not be a ltered. For most electrodes the Eref wi l l be
constant or nearly constant for a given temperature and pressure.
ine glass membrane potential , EM , how=ver wi l l not be a constant
i f the sol ution of interest i s changed. Thi s potential depends on
the potentia l s at the gl ass- l iquid boundries and possibly a di ffu
s i on potential. Us i ng the Nernst equation and the selecti vi ty
15
constants for various interfering i ons one can arrive at the fol l ow-i ng equation;1 8'19
. RT E = E0 + - l n M . M nF
{16)
where a1 and a2 refer to the acti vities of the specific ion in the
internal or external sol utions , respecti vely,
K�el i s the selectiv ity constant for the i th i nterfering ion ,
ani represents the act ivi ty of the ith i on i n the i nternal
{n=l) or external {n=2 ) sol ution ,
and EM i s the glass membrane standard potenti al .
The EM shou ld be the same on both g lass surfaces and therefore be I
zero. ' However because s i des of the glass can have di fferent environ-
ments {one surface i s always i n contact with the i nternal surface
whi l e the other i s conti nua l ly bei ng changed) the potential i s often
. not zero. Thi s has been tenned the asymmetry potential and mainly
depends on the hi story of the gl ass . Because of this asymmetry
potential the electrode must be "cal i brated" before use.
Si nce the i nternal solution i s of constant composi tion the
activi ties of the i ons i n equation ( 16 ) wi l l be constant and ca·n
be grouped w�th the asynvnetry potential to yield
E, RT l EM = M + n F n . a 2 { 17 ).
where
EM� = E 0 - RT l n a 1 (18) M nF
(Note that the K�el ai tenns have been omitted for simpl icity . I n
our experimental work the effects of possible interfering ions are
neg l ig ible . )
I t i s possible to write the overal l voltage for the cel l as
or by substi tuting and combining constants as
RT E = E0 + � ln a2 nF
(19)
( 20 )
where E0 is the col l ection of constants and a2 i s the activity of
16
the specific ion i n the external solution. Therefore i n theory an
ion selective el ectrode is responsive to the activity of the selected
ion in the absence of any i nterfering ions . The same bas i c equa
tion (20) wi l l al so hol d for an ion exchange or precipitate electrode.
The main di fference i s that i nstead of a g lass membrane the ion ex
ch�nge el ectrode has an ion exchange reservoi r i n contact with the
internal solution , which exchanges the outer solution through a
porous membrane. The precipitate electrode has a membrane composed
of an insoluble salt of the ion of i nterest pressed into a pel let ,
precipitated on the electrode surface or impregnated into a s i l i con
or pl astic matrix . A more compl ete treatment of these electrodes
·-�
17
can be found i n the l i terature. 18�20
It i s important to note here that due to the asymmetry potenti a l s
i t i s very diffi cul t to relate the electrode readings of two solu
tions taken at different times. One solution to the problem i s to use
a reference solution of constant i on activity and make alternate read
ings i n the reference and unknown solutions. The unknown solution
vol tage can then be corrected for electrode "drift . " Another method
of avoiding this problem wi l l be di scussed i n the fol l owing section.
C . Detenni nation of Association Constants
The formation of an ion pair (NaC0 3- for example ) can be repre
sented by;
(21 )
From the laws of mass balance i t i s possib l e to express the total
concentration of sodium ion , [Na+]T as the amount of free sodium ion,
[Na+] F p lus the amount of ion pai r, [NaC0 3-] or
(22)
Simi larly ,
(23 )
Since [Na+ ]T and [C032-1T are known, i t would be possible to express
the concentration of the ion pai r and hence the association constant
i f the free ion concentration of ei ther the carbonate or the sodium
I
18
ion i s known . The free ion concentrations can be calcul ated through
the use of an ion selective el ectrode .
In theory the electrode shou l d obey the Nernst equation. From
equation (20) we have
or
E = E0 + RT l n a nF
E = E0 + 0 . 05915 log a
(20)
for a singly charged i on such as sodium i on where a represents the
"free i on" activity. The Nernstian sl ope for a doubly charged ion
shoul d be 0 . 05915/2. The s lope however i s not always Nernstian but
varies with el ectrode composition and must be experimentally deter
mined . Equation (20) wi l l then become
E = E 0 + k l og a ( 25)
where k is the experimentally determined s lope . The activity of the
ion can also be rewri tten as a = ye where Y i s the acti vity coeffi-'� cient and c i s the concentration (moles/l i ter) of the free ion .
The acti vity coeffi cient shoul d be a function of ionic strength.
Si nce the act·ivi ty coeffi cient wi l l be constant at constant ionic
stre.ngth and the E0 term wi l l be invariant , the d ifference between
two vol�age readings taken at constant i onic strength wi l l be due
to a dffference i n the concentration of the free ion. We can express
the voltage at a concentration C as
19
E = E0.+ k l og C + k l og Y ( 26)
and for a concentration c·' at the same i onic strength
E' = E0 + k. log C' + k. l og Y ( 26a)
Then the di fference can be g iven by
E - E' = k .1 og C - k l og C' = k. l og .�, ( 27)
A change in voltage can then be di rectly related to a change i n
concentration of the free i on .
Two types of measurements w'il 1 be done. F i rst , a run where the
concentration of the sodium ion i s varied at constant i oni c strength
in the absence of any signifi cant complexing ions . This wi l l al l ow
us to calculate k , the slope, by
E - E' k = ----
1 og (c:/c ') (27a)
Once the sl ope is known the results of the second run can be i nter
preted. To a sol ution of sodi um chlori de (where al l Na+ i s i n the
free i on) a solution of sodium i on and tetramethyl ammonium carbonate
i s added. This sol ution has the same sodium i on concentration and
ionic strength.
When a l iquots of the carbonate solution are added the voltage
wi l l be l owered even though the total sodium i on concentration has
not changed. It i s proposed that thi s decrease i n el ectrode response
20
and the corresponding decrease in the free sodium i on concentration
is due to the fonnation of the i on pai r , NaC0 3- . The el ectrode
response can be compared to the known voltage and concentration of
the i ni tial sodium chloride solution to yield the free sodium i on
concentrati on . Rearrangi ng equation (27) we have
(27b)
where [Na+] F is the free sodium ion concentration with an el ectrode
response of E; and [Na+]1 i s the initial sodi um i on concentration
with a voltage of E. Then using equation (27b) the free carbonate
ion concentration can be calculated.
· Once the free i on and ion pair concentrations are known i t i s
possible to express the apparent equi l i brium constant , KA,from equa
tion ( 14 )
[NaCO 3- ] K; = -----
A [Na+] [CO 3 �-] (28)
As noted previously the apparent constant, KA. can be converted to
the ·thennodynami c constant by mul tipl i cation of the proper activity
coefficients , equation ( 15 ) . The activity coefficients for the sodi um
carbonate ion pair and the sodium i on can be estimated at l ow ioni c
strengths using the Davies equation . 17 However, si nce both are of the
same charge typ� i t-can be·expected that i n d i l ute so1utjons both wi l l
have approximately the same acti vity coeffi cient so that equation (15 )
'
21
becomes
·:: (29)
The thennodynamic association constant can be calcul ated by
�taking the logari thm of both s ides of equation (29) yiel ding
logKA = logKA - l ogYCO 2-3 (30)
'The logYc032- can be estimated by pl otting the . l ogKA versus the
square root of the ionic strength or by the use of
If l ogY = -o .sz2 ---
1 + all - bl ( 3 1 )
··which i s the functional fonn of the Davies equation where a and b
are detennined constants . A plot of l ogKA + 0 . 5Z 2 If versus 1 + all
I woul d have an intercept of l ogKA (at zero i on ic strength) and a
s l ope of 0 . 5Z 2b . Davies has suggested that the parameters of a=l
and b=0 . 3 work best for most sal ts .
> V . EXPERIMENTAL
! A . Reagents
The fol l owing chemical s used were reagent grade and dried
over.night at approximately 100° i n a vacuum oven and stored i n a
desi ccator before usage: NaCl , KCl , Na2C0 3 , K2C0 3 , Na2S04 and
K2S04 .
22
Tetramethylammonium chloride , (CH3)4NCl . (97%, Al drich Tl ,952-6)
A stock so lution of tetramethyl anmonium chloride (usual ly l-2M) was
prepared. The salt was not weighed di r�ctly because of i ts hygro
scopic nature . The stock solution was analyzed by passing a known
volume of the solution through a col umn of Dowex SOW-XB·cation ex
changer charged with H+ . The HCl produced was then ti trated with
a standardized base to a phenolphthalein endpoint .
Tetramethylammonium carbonate , [(CH 3 ) 4NJ2C03• A Dowex 50W-X8
cation exchange column i n the aci d fonn was charged with tetra
metnylammonium i on . At least a five fold excess of tetramethyl
a1T1noniu� chloride was passed through the column and the effluent
solution was tested wi th pHydrion paper unti l there was no further
evidence of hydrogen i on being displaced from the column. Then a
sma l l amount of tetramethylammonium hydroxide ( 20% in a methanol
solution , Aldrich Tl , 954-2 ) was passed through the column to el im
i nate any residual amounts of acid present. A weighed amount of
sodium carbonate was passed through the column and the tetramethyl
ammonium carbonate was col l ected and used . A second method of
23
preparation was also used . A Dowex l-X8 anion exchange col umn was
changed from. the chlori de fonn to the carbonate fonn using potassium
carbonate ( ca . 4M) . The charg ing continued unt i l the effluent solu
tion contained no chloride. A known volume of a r.ecently standard
ized. tetramethyl ammoni um chloride solution was passed thr�ugh the
column and the tetramethyl ammoni um carbonate was col l ected and used.
Tetramethyl ammonium sul fate, [{CH3)3N]2S04 . A Dowex l-X8 anion
exchange column was charged with hydroxide (�. 4M) ion and a known
amount of tetramethylammonium was passed through the column. The
tetramethylammonium hydroxide solution was immediately titrated with
standardized sulfuric aci d to a pH 7 endpoint using a pH electrode.
A second method of preparation involved charging a Dowex 1-X8 column
di rectly wi th su lfuric acid (4M) and sodium sul fate. The sodium
sulfate (�. 2M) was used unt i l the pH of the effluent solution was
neutral . A known amount of tetramethyl ammonium chlori de solution was
passed through the column. The tetramethylammonium sul fate was . col
lected and used . The col umn charging with sul fate ion seemed to be
the fastest most efficient process whi l e charg ing with hydroxide ,
tetramethylamnonium o r carbonate ions took a l ong time and used a
much l arger excess of these i ons .
Benzyltriethylammoni um chlori de , C6HsCH2N(C2H5 ) 3Cl . (97% ,
Aldrich 14 ,655-2) A stock solution of ben�yl triethylammonium chlo
ri de was prepared and analyzed by the same method described for
Figure 9 . Plot of Electrode Response Versus Ionic
Strength for Salts with Constant Sodium Ion Concentration
( • NaCl with (CH 3 ) i.NCl , A Na2C0 3 with (CH 3 ) t.NCl ,ANa2C0 3 with [ (CH3 ) ..N] 2BDS and CJ Na2BDS with [ (CH 3) ..N] 2BDS)
;JV
--'
0
57
);.
i s ·hiQher than the concentration of NaC0 3- i n the Na2C0 3 solutions . ' "' �!'·" ... Thjs suggests that the sodium and m-benzenedisul fonate ions wi l l
pai r to a signifi cant degree, perhaps as much as NaC03- . Thi s seems
a bit surpri s ing because the charge in the BOS i on is spread out
over a much l arger framework than in either carbonate or sulfate.
4. Comparison of Sal ts Method
The resul ts of the compari son of salts method are shown in
figure ( 10) for a typical run . It was noted that the sl opes deter
mined by this method are cl ose to Nernstian (54 to 52) , whi ch i s
good consi dering we are plotting l ogarithm of concentrations and not ;
acti vities . This method i s not acceptable for determining constants
becaµ,5€ the l i nes for Na2C03 and Na2BDS are almost co-l i near. Ei ther ' .
thi s· ·i s due to experimenta 1 error or the fact that Na2BOS i s not
a good standard. Perhaps BOS ion pairs with sodium ion to almost
the same extent as carbonate. This wou l d explain the curve crossing
i n · figure ( 9 ) and the co-l i near behavior i n figure ( 10) .
B . Other Electrode Methods
1 . Potassi um Ion El ectrode
The potassium ion el ectrode was unable to g i ve stable readi ngs
for any of the solutions tested. Electrode i nstabi l i ty of ±2 mV/5min
was noted which cou l d mask any sma l l change in the free i on concen
tration of potass i um. It i s possib le that the tetramethyl ammonium
9. N. Bjenum, Klg. Danske Videnskab. Selskab., ]_, 2 (1926).
10 . R. M. Fuoss and F. Accascina, Electrolvtic Conductance, Interscience, New York, 1959, Chapter XVI.
11. J. T. Denison and J. B. Ramsey, J. Amer. Chern Soc., 77, 2615 (1955). --
12. ~1. E·i gen and K. Tamm, z. El ektrochem., 66, 93' 107 (1962).
13. G. Atkinson and S. K. Kor, J. Phys. Chern. , 69, 128 (1965).
14. G. Atkinson and S. Petrucci, ibid. ' 70, 3122 (1966).
15. H. s. Dunsmore ·. and J. c. James, J. Chern, Soc., 2925 (1951).
16. G. Atkinson and S. Petrucci, J. Phys. Chern. 5 70, 3122 (1966).
17. C. H. Davies, Ion Association , Butterworths, London, 1962.
18. G. Eisman, Ed ~ , Gla~_?___!_lectrodes for Hydrogen and O~her Cations, Marcel Dekker, Inc., New York, 1967, Chapter 6.
19. J. Koryta, Ion Selective Electrodes, Cambridge University Press, New York, 1975.
20. R.A. Durst, ed., Ion-Selective Electrodes, National Bureau of Standards Special Publication 312, U.S. Government Printing Office, Washington, D.C., 1969.
23. H. B. Herman and G. A. Rechnitz, Anal. Chim. Acta., 76, 155 (1975).
24. M. S. Mohan and G. A. Rechnitz, Anal. Chern., 45 1323 (1973).
25. A. C. Walker, U. B. Bray and J. Johnston, J. Amer. Chern. Soc., 49, 1935 (1927).
26. F. S. Nakayama, J. Phys. Chern., 1!!._, 2726 {1970).
27. C. Lin and G. Atkinson, Chemistry and Physics of Aqueous Gas Solutions, W. A. Adams, et. · ~., ed., The Electrochemical Society, Inc., Princeton, N.J., 1975.
28. J. N. Butler and R. Huston, J. Phys. Chern., ]4, 2976 (1970).
29. J. E. Hawley, Ph.D. Thesis, Oregon State University, Corvallis, Oregon, .. 1973.
30. I. L. Jenkins and C. B. Monk, J. Amer. Chern. Soc., 72, 2695 (1950).
31. F. H. Fisher and A. P. Fox, J. Solution Chern., 5_, 225 ( 1975 ).
32. E. J. Reardon, Ph.D. Thesis, The Penn ~ylvania State University, University Park, Pennsylvania, 1974.
33. M. M. Santos et ~·, J. Solution Chern., 5_, 1 (1975).
34. D. R. Kester and R. M. Pytkowicz, Lim~ol. Oceanogr., 14_, 686 (1969) .
35. R. Fernandez-Prini and J. E. Prue, J. Phys. Chern., 69, 2793 (1965).