4.3 COSTOS PARA LA IMPLEMENTACIÓN DE LA RED
4.3.3 PRECIO ESTIMADO DE LA RED WiMAX Wi-Fi A SER
10.0 Introduction
The overall aim o f this European Union project is to develop a quantitative
Aquatic Passive Sampler (APS) that will measure time-integrated concentrations of
pollutants in environmental waters.* In turn, the motivation for this individual Ph.D.
thesis was brought about by the need to investigate and understand the physico
chemical interactions involved in the retention of pollutants on a Cig solid-phase
extraction (SPE) disk, which has been completed successfully in Chapters 7, 8 and 9.
The disk consists of a PTFE microfibril network embedded with silica-bonded
octadecyl sorbent phase and is taken as the receiving phase in the European Union’s
Aquatic Passive Sampler, which is described in full in Chapter 3. In Chapter 7, it is
shown how the equilibrium constant (Keq) and the uptake rate constant (kup) for the
partitioning of pollutants between water and the Cig SPE disk in a closed system can
be determined by experiment. The findings in Chapter 7 as well as Chapters 8 and 9
show that a novel experimental procedure utilising on-line ultra-violet (UV)
spectroscopy, is a viable method for studying the thermodynamic and kinetic
partitioning of compounds between these two condensed phases.
The successful characterisation of the water-Cig SPE disk system (Chapter 9)
enables one to predict log K@q for the retention o f any compound on the receiving
phase provided the Abraham solute descriptors are known. It is therefore of particular
importance to ascertain if the log Keq values obtained for compounds partitioning
between the water-naked Cig disk system are applicable to a water-APS system too. In
the Aquatic Passive Sampler a rate-limiting membrane (R-LM) forms a physical
barrier between the water and the receiving phase in an attempt to control the rate of
diffusion of pollutants to the surface of the receiving phase/ It is expected that the R-
LM will not ^ffect the physico-chemical interactions involved in retention of
V pollutants onto the Cig disk but may well fe^fect the uptake rate constant, log kup. In
addition to this it is essential to determine if the physical constants determined for a
‘closed’ water-Ci8 disk or -APS system are applicable to an ‘open’ water-Cig disk or -
APS system. The reason being that the APS’s intended use is to monitor time-
integrated pollutant concentrations in environmental waters such as lakes, rivers etc.
These are denoted as ‘open’ systems and are different to the ‘closed’ system used to
obtain Keq and kup in this work. To ensure clarity between the two, ‘closed’ and ‘open’
partitioning systems in this work are defined as follows:
Closed system - water (Vw) and receiving phase ( Vd) volumes are known.
The concentration of pollutant in water ([A]w) decreases
with time as it partitions into the disk / APS.
Open system - receiving phase volume is known but volume of water is
unknown or infinitely large compared to Vq. The
concentration of pollutant in water is constant with time.
!
In this chapter several preliminary experiments are carried out to obtain^ log K^q and
log kup by the UV spectroscopy method detailed in Chapter 7.5 for the partitioning of
diuron between water and the APS. The constants obtained are viewed along side
those for a ‘closed’ water-Cig disk system (from Chapter 7) as well as additional
determine the concentration of diuron in water and the receiving phase during various
partition experiments in both closed and open water-APS systems.^ The R-LM used
for these C3q)eriments is the polysulphone membrane selected for the time-integrated
measurement of relatively polar pollutants by J. Kingston.^ The receiving phase is a
Cl8 sohd-phase extraction disk used in experimental work throughout this thesis. The
idea of the preliminary experiments is to obtain an indication of the values of log Keq
and log kup for a water-APS system and not to quantitatively determine these two
constants. This would be the type of work to be carried out in the future.
10.1 Calculating the Equilibrium Constant
Keq for a closed system (partitioning is followed by recording the change of
pollutant concentration in the waterl is calculated in exactly the same way as
previously defined by equation 7.2:
K e q = [ A ] o e q / [ A ] w e q = X [ A ] w ° ” [ A ] w e q ) / [ A ] w e q (7.2)
Where [ A J o e q and [ A ] w e q are the concentration of pollutant in the disk and the water at
equilibrium respectively, [ A ] w ° is the initial concentration in the water (all in mo 1.1'^)
an d /is the phase ratio (f= VwA^d where Vd and Vw are the volumes of the disk and
water respectively (litres)). For the sake of completion, Keq in an open system is
simply given as (where the change of concentration in the disk is usually recorded
when following the partition process):
K e q = [ A J o e q / [ A ] w e q (5.19)
[ A ] w e q is constant throughout the whole experiment and [ A ] o e q can be determined
directly by various analytical techniques, GC-MS in Kingston’s case.
10.2 Calculating the Uptake Rate Constant
kup is determined by fitting the partitioning data to equation 7.16 in the case of
absorbance data obtained by UV spectroscopy, to obtain constant c which in turn
gives kup from equation 7.17
Abs = sM + (Abs° - eM ) exp’*'"*’^ ^ (7.16)
Z K e q V D Z K e q V D
c = -kupZ (7.17)
where Abs° and Abs are the UV initial absorbance and absorbance at time t for the
pollutant in water. M is the total number of moles in the system, e is the extinction
coefficient for the pollutant under investigation and Z = 1 + Vw / Keq.Vo. In the case
of data collected by any other analytical technique, equation 7.15 is needed instead to
obtain constant c:
[A]w = M + ([A]w° - J y D e x p ^ ' (7.15)
ZKeqVo ZKeq Vo
It is worth pointing out that equation 7.15, 7.16 and 7.17 can not be used to determine
10.3 Results
10.3.1 Data obtained by Kingston
Experimental partition data obtained by Kingston that is comparable to that
obtained in the current work is described for the two scenarios below.^ Kingston uses
GC-MS to quantify either the concentration in water or the Cig disk.
Scenario 1: The concentration in water ([A]w in mo 1.1'*) is obtained for diuron
partitioning between a ‘closed’ water-APS system, 11°C, lOOOrpm.
Scenario 2: The concentration in the disk ([A]d in mo 1.1'*) is obtained for diuron
offloading from a pre-loaded disk, in an ‘open’ water-APS system,
11°C, slow stirring, over 15 days.^
10.3.2 Data obtained in the current work
Two separate experiments carried out in this work utilise the UV spectroscopy
procedure outlined in Chapter 10.7 Details are given below:
Scenario 3: The concentration in water ([A]w in moll'*) is obtained for diuron
partitioning between a ‘closed’ water-APS system, 23°C, 4G0rpm.
Scenario 4: The concentration in water ([A]w in mol.l'*) is obtained for diuron
partitioning between a ‘closed’ water-APS system, 23°C, 200rpm.
Log Keq and log kup for scenarios 1, 3 and 4 are given in Table 10.1. The offloading
rate constant log koff is obtained indirectly from log Keq and log kyp via equation 7.21
for scenarios 1,3 and 4.