AU2007336706B2 - Improved water analysis - Google Patents

Improved water analysis Download PDF

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AU2007336706B2
AU2007336706B2 AU2007336706A AU2007336706A AU2007336706B2 AU 2007336706 B2 AU2007336706 B2 AU 2007336706B2 AU 2007336706 A AU2007336706 A AU 2007336706A AU 2007336706 A AU2007336706 A AU 2007336706A AU 2007336706 B2 AU2007336706 B2 AU 2007336706B2
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electrode
cod
sample
working electrode
light source
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AU2007336706A1 (en
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Shanqing Zhang
Huijun Zhao
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Aqua Diagnostic Pty Ltd
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Aqua Diagnostic Pty Ltd
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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/18Water
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/18Water
    • G01N33/1806Water biological or chemical oxygen demand (BOD or COD)
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/26Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
    • G01N27/28Electrolytic cell components
    • G01N27/30Electrodes, e.g. test electrodes; Half-cells

Description

WO 2008/077191 PCT/AU2007/001987 1 IMPROVED WATER ANALYSIS Field of the Invention This invention relates to a new method for determining oxygen demand of water using photoelectrochemical cells. In particular, the invention relates to an 5 improved direct photoelectrochemical method of determining chemical oxygen demand of water samples using a titanium dioxide nanoparticulate semiconductive electrode. It is particularly adapted to a use in a probe configuration Background to the Invention 10 Nearly all domestic and industrial wastewater effluents contain organic compounds, which can cause detrimental oxygen depletion (or demand) in waterways into which the effluents are released. This demand is due largely to the oxidative biodegradation of organic compounds by naturally occurring microorganisms, which utilize the organic material as a food source. In this 15 process, organic carbon is oxidised to carbon dioxide, while oxygen is consumed and reduced to water. Oxygen demand assay based on photoelectrochemical degradation principles has been previously disclosed in patent specification W02004088305 where the measurement was based on exhaustive degradation principles. 20 It is an object of the present invention to develop an analyzer based on non exhaustive degradation principles. It is another object of this invention to develop a probe type COD analyzer. Brief description of the invention 25 To this end the present invention provides a method of determining chemical oxygen demand (COD) of a water sample, comprising the steps of a) applying a constant potential bias to a photoelectrochemical cell, having a photoactive working electrode and a counter electrode, and containing a supporting electrolyte solution; 30 b) illuminating the working electrode with a light source and recording the background photocurrent produced at the working electrode from the supporting electrolyte solution; c) adding a water sample, to be analysed, to the photoelectrochemical cell; WO 2008/077191 PCT/AU2007/001987 2 d) illuminating the working electrode with a light source and recording the steady state photocurrent produced with the sample; e) determining the chemical oxygen demand of the water sample using the formula 5 [COD ]= 8000 i. FAD where 6 is the Nernst diffusion layer thickness, D is the diffusion coefficient, A is the electrode area, F the Faraday constant and iss the steady state photocurrent. The intensity of the light on the photoelectrode influences the linear range of the instrument. However increasing light intensity to too high a value can lead to 10 stability problems with the instrument either emanating from the light source or from photo corrosion of the electrode. A preferred light intensity is within the range of 3 to 10 W/cm 2 with a value of 6 to 7 W/cm 2 being preferred. Solution pH also affects the signal and an operational pH range of 3 to 10 is preferred. 15 The working electrodes may be regenerated by exposure to UV light and have a useful working life. In addition to the counter electrode it is preferred to also use a reference electrode. The method of this invention is particularly suitable for an analyzer configured as a probe for testing water samples in the field on a discontinuous basis. 20 In another aspect this invention provides a probe for determining water quality comprising a) an electrochemical cell containing a photoactive working electrode, a counter electrode and optionally a reference electrode b) a supporting electrolyte solution chamber; 25 c) a light source to illuminate the working electrode d) sample collection means to provide a volume of sample to the cell e) control means to i) actuate the light source and record the background photocurrent produced at the working electrode from the supporting electrolyte 30 solution; ii) add a water sample, to be analysed, to the photoelectrochemical cell; WO 2008/077191 PCT/AU2007/001987 3 iii) actuate the light source and record the steady state photocurrent produced with the sample; iv) determine the chemical oxygen demand of the water sample using the formula 3 5 [COD ]= x 8000 i FAD where 6 is the Nernst diffusion layer thickness, D is the diffusion coefficient, A is the electrode area, F the Faraday constant and i., the steady state photocurrent. 10 Description of the drawings Figure 1 is a schematic view of the photoelectrochemical cell used in this invention; Figure 2 is a graph of a typical photocurrent response of 0.1 M NaClO 4 blank 15 solution; Figure 3A shows the quantitative relationship between the net steady state current (iss) and the molar concentration of organic compounds; Figure 3B shows the quantitative relation between the net steady state current (in mA) and nFADC; 20 Figure 4A shows the plot of the theoretical and experimental is, against the theoretical COD values of KHP solution; Figure 4 B shows the plot of experimental iss against the theoretical COD values of KHP and GGA solutions; Figure 5A shows the photoelectrochemical oxidation of glucose under different UV 25 light intensities; Figure 5B shows the effect of potential on iss (a) and blank (o) due to the photoelectrochemical oxidation of 0.2 mM glucose and its blank solution, respectively; Figure 5 C shows the effect of pH on iss (a) and blank (o) due to the 30 photoelectrochemical oxidation of 0.2 mM glucose and its blank solution, respectively; WO 2008/077191 PCT/AU2007/001987 4 Figure 6 shows typical GGA standard addition for the determination of the wastewater from a bakery; Figure 7 shows the correlation between the PECOD and the standard dichromate COD methods for the real sample measurements. 5 Detailed description of the invention Materials and Sample Preparation: Indium Tin Oxide (ITO) conducting glass slides (80/square) were commercially supplied by Delta Technologies Limited. Titanium butoxide (97%, Aldrich), and sodium nitrate were purchased from Aldrich without 10 further treatment prior to use. All other chemicals were of analytical grade and purchased from Aldrich unless otherwise stated. High purity deionised water (Millipore Corp., 18MO cm) was used in the preparation of solutions and the dilution of real wastewater samples. The real samples used in this study were collected within the State of Queensland 15 in Australia from various industrial sites including wastewater treatment plants, sugar plants, brewery manufacturers, cannery manufacturers and dairy production plants. All samples were preserved according to the guidelines of the standard method. When necessary, the samples were diluted to a suitable concentration prior to the analysis. After dilution, the same sample was subject to analysis by 20 both standard COD method and photoelectrochemical COD detector. To the samples for photoelectrochemical determination, NaCIO 4 solid equivalent to 0.1 M was added as supporting electrolyte. Preparation of TiO 2 film electrodes: Same as previously described in the applicant's prior patent application W02004088305. 25 Apparatus and methods All photoelectrochemical experiments were performed at 23 0 C in a three-electrode electrochemical cell with a window for illumination (see Figure 1). A saturated Ag/AgCI electrode and a platinum mesh were used as the reference and the 30 auxiliary electrodes respectively. A voltammograph (CV-27, BAS) was used for application of potential bias in the photoelectrolysis experiments. Potential and current signals were recorded using a computer coupled to a Maclab 400 interface (AD Instruments). Illumination was carried out using a 150W xenon arc lamp light WO 2008/077191 PCT/AU2007/001987 5 source with focusing lenses (HF-200w-95, Beijing Optical Instruments). To avoid the sample solution being heated-up by the infrared light, the light beam was passed through a UV-band pass filters, i.e. UG5 (Avotronics Pty. Limited), prior to illuminating the electrode surface. Standard COD values (dichromate method) of 5 all the samples were measured with a COD analyzer (NOVA 30, Merck). During oxygen dependence experiments, the oxygen concentration was monitored by an oxygen electrode (YSI) and 90 FLMV Microprocessor Field Analyser (from T.P.S. Pty. Ltd.). 10 Analytical Signal Measurement Figures 2A and B show a set of typical photocurrent-time profiles obtained in the presence and absence of organic compounds in the photoelectrochemical cell. Under a constant applied potential of +0.30 V, when the light was switched off, the dark current was approximately zero. Upon illumination, the current increased 15 rapidly before decaying to a steady value. For the blank (dash line), the photocurrent blankn) resulted mainly from the oxidation of water, while photocurrent totala) observed from the sample solution containing organics (solid line) is the total current of two current components, one from the oxidation of water, which was the same as the blank photocurrent ('blank), and the other from photoelectrocatalytic 20 oxidation of organic compounds. The current iss, the diffusion limiting current originated from the oxidation of organics, can be obtained by subtracting the photocurrent of the blank ('blank) in the absence of organic compounds from the total photocurrent in the presence of organic compounds (see Figure 1.2). 25 is = total - blank (1.1) It has been proved that all organics transported to the TiO 2 electrode surface can be indiscriminately and fully oxidised. Therefore, the net current (i..) is directly proportional to the rate of electron transfer (the number of electrons transferred per unit of time). As COD is defined as the amount of oxygen required for complete 30 oxidation of organic compounds, subsequently, the net current (iss) can be used to quantify the COD value of a sample. Analytical Signal Quantification WO 2008/077191 PCT/AU2007/001987 6 Under the non-exhaustive photocatalytic oxidation model, the quantitative relationship between the iss and COD of the sample is developed according to the following postulates: (i) the bulk solution concentration remains essentially constant before and after the experiment (non-exhaustive degradation); (ii) all 5 organic compounds at the electrode surface are stoichiometrically oxidized to their highest oxidation state (fully oxidised); (iii) the overall photocatalytic oxidation rate is controlled by the transport of organics to the electrode surface and can reach a steady-state within a reasonable time frame (steady-state mass transfer limited process); (iv) the applied potential bias is sufficient to remove all photoelectrons 10 generated from the photocatalytic oxidation of organics (100% photoelectron collection efficiency). The rate of steady state mass transfer (dN/dt) to the electrode can be given by a well-known semi-empirical treatment of Steady-State Mass Transfer model: -N [C' - C, (X = 0)] (1.2) dtd D 15 where, Cb and Cs refer to the concentrations of analyte in the bulk solution and at the electrode surface respectively. D and 5 are the diffusion coefficient and the Nernst diffusion layer thickness respectively. Under the steady-state mass transfer limited conditions (Postulate (iii)), the rate of overall reaction equals: 20 Rate = Cb (1.3) According to the postulates (ii) and (iv), the number of electrons transferred (n) during photoelectrochemical degradation is a constant for a given analyte and the steady-state photocurrent (i 5 s) can, therefore, be used to represent the rate of reaction: 25 is -nFAD Gb (1.4) where A and F refer to electrode area and Faraday constant respectively. Equation 1.4 defines the quantitative relationship between the steady-state photocurrent and the concentration of analyte. Converting the molar concentration into the equivalent COD concentration (mg/L of 02), we have: WO 2008/077191 PCT/AU2007/001987 7 FAD x [COD ] (1.5a) 8, 8000 8 [COD]= x8000ji (1.5b) FAD Equation 1.5b is valid for the determination of COD in a sample which contains a single organic compound. The COD of a sample containing more than one 5 organic species can be represented as: 8 [COD] x 8000 is, (1.6) FAD Where 5 is the collective Nernst diffusion layer thickness, which has been proved to be a constant and independent of the type of organics, under diffusion controlled conditions, D is the composite diffusion coefficient that depends on the sample 10 composition and is a constant for a given sample. Validation of Analytical Principle Figure 3A shows the plots of steady-state photocurrents against the molar concentrations of organic compounds. Linear relationships between iss and C, as 15 predicted by Equation 1.5, were obtained for all compounds investigated. Further processing of the data in Figure 3A gives Figure 3B. Note that all data in Figure 3B fit into one linear curve of slope = 0.0531 and R 2 = 0.995. As the slope of the curve equals 6-, it can be concluded that, under these experimental conditions, a stagnant diffusion layer thickness (6 =1.86x10 3 cm) exists and that this is 20 independent of concentration and type of organic compound. This finding also confirms that the theoretical slope given by Equation 1.5 represents the slope of the curve for each compound in Figure 1.3a. In fact, we would be not able to obtain the linear line in Figure 3B unless all of the four above postulates are ratified. 25 Theoretically, Equation 1.6 should be valid under the same conditions, as required by Equation 1.4. Thus Figures 4A and 4B show the plot of iss against the theoretical COD value of the synthetic samples ([COD] theoretical) prepared with KHP, a test compound for the standard COD method. As predicted by Equation 1.5, a linear relationship between iss and [COD]theoretical was obtained. The slope of the WO 2008/077191 PCT/AU2007/001987 8 experimental curve obtained was 2.8x10 3 mA (mg/L of 02) with R 2 =0.9985. The theoretical curve calculated from Equation 1.5 was also given in the Figure 4A (solid line) for comparison. When n=30e-, D=6.96x10 3 cm 2 s 1 [ref] and 6=1.86x10~ 3 cm were used, the theoretical slope calculated according to Equation 1.5 was 5 2.9x10 3 mA (mg/L of 02)1. These almost identical theoretical and experimental slope values prove the applicability of Equation 1.5 for COD determination. The applicability of Equation 1.6 was examined using a GGA synthetic sample. The GGA synthetic sample is a mixture of glucose and glutamic acid, which has 10 typically has been used as a standard test solution for BOD analysis. As predicted by Equation 1.6, the steady-state photocurrent, is, is directly proportional to the sample [COD] (see Figure 1.4b). However, application of Equation 1.6 for real samples requires calibration, since the composite diffusion coefficient, D , is not known. Unlike other analyses, the definition of a calibration 15 standard for COD analysis is difficult since COD is an aggregative quantity. In practice, a COD calibration standard can only be selected by experimental means. Two essential criteria should be satisfied by the selected calibration standard: (i) the calibration standard should possess an equiivalent D value to the original sample and (ii), it can be fully oxidized. These criteria reflect the experimental 20 observation that the added calibration standard causes a steady-state photocurrent change which follows the same slope of the original sample. Optimisation of Analytical Signal The effect of light intensity on the steady-state photocurrent was examined (see 25 Figure 5A). It is notable that the change of the light intensities has a dramatic influence on the linear range. An increase in the light intensity leads to an increase in linear range. The is deviations from the linear relationship relate to the rate of the photocatalytic oxidation being slower than that of mass transfer to the electrode. Increasing light intensity leads to an increase in the rate of photohole 30 generation, which, in effect, increases the rate of photocatalytic oxidation. That is, a high light intensity can sustain the overall process under the mass transfer controlled conditions at higher concentrations. Thus, to provide a wide linear range and good operating conditions,, a relatively low (but sufficient) light intensity WO 2008/077191 PCT/AU2007/001987 9 (6.6mW/cm 2 ) was employed. For a particulate TiO 2 semiconductor electrode, the applied potential bias serves the function of collecting the electrons made available by the interfacial photocatalytic reactions. 100% photoelectron collection efficiency (Postulate (iv) 5 see Analytical Signal Quantification section) can be achieved only when the applied potential bias is sufficient. Figure 5B shows the effect of potential bias on both i, and iblank. It reveals that both is, and blank becomes constant when the applied potential bias is more positive than -0.05V vs Ag/AgCI indicating 100% photoelectron collection efficiency. To ensure the selected potential bias is 10 applicable under various conditions and at the same time, to avoid direct electrochemical reaction, a standard potential bias of +0.30V vs Ag/AgCI was selected. It is well known that the solution pH affects the flat band and the band edge potentials of TiO 2 semiconductors in a Nernstian fashion. The solution pH also 15 affects the speciation of both surface functional groups of the semiconductor electrode and the chemical forms of organic compounds in the solution . These pH dependent factors may affect the analytical signal. Figure 5C shows the effect of pH on both iss and blank. Within the pH range of 2 to 3, both iss and blank increased slightly as the solution pH was increased. Within the pH range of 3 to 20 10, both iss and blank were insensitive to the solution pH change. When the solution pH was above 10, the is, observed was relatively insensitive to the pH change, but a sharp increase in the blank with the solution pH was observed due to the rate of water oxidation was greatly enhanced at high pH. The sensitivity of blank towards the solution pH may cause problems for accurate measurement of is. Therefore, a 25 solution pH range from 3 to 10 is preferred. This pH range is suitable for most of the environmental samples (pH 3-10) that can be used without the needs for pH adjustment. Real Sample Analyses 30 The analysis of real samples was conducted. These real samples were collected from various industrial sites. The pH of the real samples tested in this paper was in the range of 6-8, i.e., in the pH independent region. For the analysis of very high COD samples, dilution with NaClO 4 or NaNO 3 solution will normally bring the WO 2008/077191 PCT/AU2007/001987 10 pH in the range of 5-8 and the 02 concentration in the range of 5-9.5 mgL 1 . To minimize any matrix effect, if required, the standard addition method can be used for the photoelectrochemical determination of COD value of real samples and so ensure that the D value is constant and consistent during the calibration and 5 measurement. The results shown in Figure 6 confirm that Equation 1.6 can be used to determine COD values of real samples. Figure 7 shows the correlation between the experimental COD values and standard COD values. The standard COD value was determined with the conventional COD method (dichromate method). Where valid, the Pearson 10 Correlation coefficient was used as a measure of the intensity of association between the values obtained from the photoelectrochemical COD method and the conventional COD method. A highly significant correlation (r=0.988, P=0.000, n=1 8) between the two methods was obtained indicating the two methods agreed very well. The slope of the graph was 1.02. This near unity slope indicates that 15 both methods were accurately measuring the same COD value. Given a 95% confidence interval, this slope was between 0.96 and 1.11, which implies a 95% confidence level that the true slope lies between these two values. Considering that there are analytical errors associated with both the photoelectrochemical COD and the standard method measurements, and that these errors contribute to 20 scatter on both axes, the strong correlation and slope obtained provides compelling support for the suitability of the photoelectrochemical COD method for measuring Chemical Oxygen Demand. It is found that the detection limit of 0.8 mgL 1 COD with linear range up to 70 mgL I COD can be achieved under the above optimised experimental conditions. The 25 detection range may be extended by proper dilution as aforementioned. A reproducibility of 2.2% RSD was obtained from 19 analyses of 50 pM KHP. From the above, it can be seen that this invention provides an improved method and a probe for use in conducting non-exhaustive COD analyses of water samples. 30 Those skilled in the art will realize that this invention may be implemented in embodiments other than those described without departing from the core teachings of the invention.

Claims (6)

1. A method of determining chemical oxygen demand (COD) of a water sample, comprising the steps of a) applying a constant potential bias to a photoelectrochemical cell, having 5 a photoactive working electrode and a counter electrode, and containing a supporting electrolyte solution; b) illuminating the working electrode with a light source and recording the background photocurrent produced at the working electrode from the supporting electrolyte solution; 10 c) adding a water sample, to be analysed, to the photoelectrochemical cell; d) illuminating the working electrode with a light source and recording the steady state photocurrent produced with the sample; e) determining the chemical oxygen demand of the water sample using the formula 15 [COD]= x 8000 i,, FAD where 6 is the Nernst diffusion layer thickness, D is the diffusion coefficient, A is the electrode area, F the Faraday constant and iss the steady state photocurrent. 20
2. A method as claimed in claim 1 wherein the pH of the water sample is within the range of 3 to 10. 25
3. A method as claimed in claim 1,2 or 3 wherein the photo electrode is a titanium dioxide nanoparticulate photo electrode. 30 WO 2008/077191 PCT/AU2007/001987 12
4. A probe for determining water quality comprising a) an electrochemical cell containing a a photoactive working electrode and a counter electrode, b) a supporting electrolyte solution chamber; 5 c) a light source to illuminate the working electrode d) sample collection means to provide a volume of sample to the cell e) control means to i) actuate the light source and record the background photocurrent produced at the working electrode from the supporting 10 electrolyte solution; ii) add a water sample, to be analysed, to the photoelectrochemical cell; iii) actuate the light source and record the steady state photocurrent produced with the sample; 15 iv) determine the chemical oxygen demand of the water sample using the formula [COD ]= x 8000 i FAD where 5 is the Nernst diffusion layer thickness, D is the 20 diffusion coefficient, A is the electrode area, F the Faraday constant and iss the steady state photocurrent;
5. A probe as claimed in claim 4 wherein the photo electrode is a titanium dioxide nanoparticulate photo electrode. 25
6. A probe as claimed in claim 4 or 5 in which the light intensity is from 3 to 10 W/cm 2 30
AU2007336706A 2006-12-22 2007-12-21 Improved water analysis Ceased AU2007336706B2 (en)

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CN102331447A (en) * 2011-04-27 2012-01-25 河北先河环保科技股份有限公司 Method and equipment for measuring chemical oxygen demand by photocatalytic oxidation process
RU2555774C2 (en) * 2013-11-28 2015-07-10 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Омский государственный университет им. Ф.М. Достоевского" Water state indication method
TWM496760U (en) * 2014-11-05 2015-03-01 Univ Chaoyang Technology Chemical oxygen demand inspection device
KR101639616B1 (en) * 2014-12-15 2016-07-15 한국기계연구원 Photo-electorde for tandem structure photoelectrochemical cell comprising metal ultra-thin layer and photoelectrochemical cell comprising the same
CN105044180B (en) * 2015-06-29 2017-11-17 江苏大学 A kind of preparation method and purposes of heterojunction photovoltaic pole
CN105116040B (en) * 2015-08-25 2018-05-08 广西壮族自治区农业科学院农产品质量安全与检测技术研究所 Optical electro-chemistry reaction tank
CN105203527B (en) * 2015-09-11 2018-03-23 山东师范大学 The optical electro-chemistry detection means and its application method of a kind of double detection cells
CN106970131B (en) * 2017-03-28 2019-01-18 北京北大明德科技发展有限公司 A kind of photoelectrocatalysis type water-soluble organic compound concentration sensor and preparation method
CN108845004B (en) * 2018-06-15 2020-10-13 浙江大学 Photocurrent carbon dioxide sensor

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HUIJUN ZHAO ET AL:"DEVELOPMENT OF A DIRECT PHOTOELECTROCHEMICAL METHOD FOR DETERMINATION OF CHEMICAL OXYGEN DEMAND" Analytical Chemistry, vo1.76, no.1, 1 January 2004, p.155-160. *

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