HYDROGEN PEROXIDE MONITORING

Abstract: A method and apparatus for determining the hydrogen peroxide content of a fluid. The method includes: (a) contacting the fluid with a catalyst so as to permit decomposition of the hydrogen peroxide present in the fluid to oxygen and water; (b) permitting the oxygen liberated to pass to a gas meter; and (c) measuring the volume of oxygen liberated utilizing the gas meter, wherein the volume of oxygen liberated provides a measure of the hydrogen peroxide content of the fluid.

Description: Hydrocren Peroxide Monitoring The present invention is concerned with a method of monitoring the content of peroxide present m a fluid sample, and apparatus for such a method. Hydrogen peroxide has been used as an oxidant m industrial applications for many years. Hydrogen peroxide is, for example, a stronger oxidant than chlorine or permanganate and has the advantage of non-polluting decomposition products . Hydroxyl radicals (OH * ) are highly oxidising species. The most commonly accepted mechanism for hydroxyl radical production is the photolysis of hydrogen peroxide. Photochemical reduction of Fe 3+ to Fe 2+ (UV/Fentons) m the presence of hydrogen peroxide, increases the generation of OH' radicals and may yield a more effective system for oxidative degradation. A major application of peroxide is m advanced oxidation processes removing recalcitrant organic contaminants, such as herbicides and PCB's (polychloπnated biphenyls). For example, the purification of water containing organic impurities by peroxide (approx 1%) /UV treatment has beer- used since the early 1980 's. In addition, peroxide together with UV and 0 ; , has been used at a field scale to treat ground water contaminated with volatile organic compounds . The partial oxidation of recalcitrant compounds may also be advantageous. It has been shown by Carberry and Benzmg (Water Sci . Tech 23, 1991, 367-376) that two chlorinated aromatics showed enhanced biodegradability after pre- oxidation with peroxide at molar ratios between 2:1 and 6:1, w th an optimum at 4:1. The use of hydrogen peroxide as an oxidant has several advantages over other methods of chemical and photochemical water treatments, namely its thermal stability, the ability to store on-site, its solubility m water, and the lack of mass transfer problems of associated gases. Peroxides are used m the removal of colour, especially as a bleaching agent m the textile industry. In addition, peroxides are used m the manufacture of paper, and during waste paper recycling. Other environmental applications include the oxidation of sulphides for odour control, corrosion control of waste pipes by addition of hydrogen peroxide to waste water, an additional oxygen source for overloaded activated sludge plants and controlling filamentous bulking. It can be seen from the above that the use of hydrogen peroxide m industry has numerous advantages. However, the concentration of peroxide employed m the industrial processes must be carefully controlled and monitored for its efficient and cost effective usage. There are many methods of monitoring hydrogen peroxide known m the art. Standard methods of monitoring hydrogen peroxide include titrimetπc (typically based on the oxidation of hydrogen peroxide with permanganate, followed by the reduction with acidic potassium iodide) , gasometπc, electrochemical colorimetπc , chemiluminescent and acoustic methods. The results of these monitoring methods can then be used to control the process . The methods outlined above can be time consuming, sensitive to interference, and have poor lifetime. They may not be so effective for process monitoring and control . PCT patent specification O98/30884 to BTG Kalle Inventing AB (BTG) discloses a method and device for measuring the content of chemicals (such as hydrogen peroxide) used m connection with bleaching of cellulose fibres. The method includes adding the enzyme catalase to the sample, which is agitated so as to permit the hydrogen peroxide to decompose and oxygen gas to be generated. The resultant oxygen gas pushes out a certain sample volume for the measurement of the sample; the sample volume is then, directly or indirectly, converted to a value representing the amount of hydrogen peroxide present . In addition, the above mentioned patent specification suggests that it is not possible to measure directly the volume of oxygen produced. It is therefore an aim of the present invention to provide a rapid method to monitor hydrogen peroxide over a wide range of concentrations. It is a further aim of the present invention to provide a method for on-line monitoring of hydrogen peroxide which utilizes direct measurement of the oxygen gas produced m the decomposition of hydrogen peroxide. It is yet a further aim of the present invention to provide a monitor which is capable of monitoring hydrogen peroxide m "dirty" and "high solid content" environments such as industrial process streams and effluents without fouling or interference which is one of the major drawbacks of currently available instruments. Therefore, according to the present invention there is provided a method of determining the hydrogen peroxide content of a fluid, which method includes; (a) contacting the fluid with a catalyst so as to permit decomposition of the hydrogen peroxide present m the fluid to oxygen and water; (b) permitting the oxygen liberated to pass to a gas meter; and (c) measuring the volume of oxygen liberated utilizing the gas meter, wherein the volume of oxygen liberated provides a measure of the hydrogen peroxide content of the fluid. The term "fluid" is a term generally used m the art for any material whicn can be pumped. Non- limiting examples of such fluids are solutions, slurries, pulps, gravel, etc. It is preferred that the gas meter is arranged to measure low and irregular gas flows with a low back pressure. Typically, the gas meter is a low flow gas meter, such as the meter described m "On-line low flow high precision gas metering systems", Wat. Res, vol 29, page 977-979 (1995), the disclosure of which is incorporated by reference. The volume may be measured as an absolute volume, or as a rate of evolution (m other words, the volume evolved m a It is preferred that the volume of oxygen liberated m step (b) is measured directly. It is preferred that the catalyst is an enzyme, such as catalase, which may be either soluble or immobilised. However other suitable catalysts may be used. Preferably, the catalase is Hydrogen peroxide: hydrogen peroxide oxidoreductase, EC 1.11.1.6. The catalase catalyses the decomposition of hydrogen peroxide to water and oxygen gas. Typically, the amount of catalase present m step (a) is predetermined. It is also preferred that the catalase is present m an amount excess relative to the hydrogen peroxide . It is preferred that the mixing and catalysed release of oxygen m step (a) is carried out for sufficient time to decompose substantially all of the hydrogen peroxide present in the fluid. The temperature of the process may be kept at a predetermined temperature, for example, m the range from 20°C to 40°C. Preferably, the oxygen liberated may be measured using a pressure transducer or the like, such as a low-flow gas meter. Thus, the hydrogen peroxide content of the sample at any given time may be determined, for example, m a continuous treatment process. Preferably, the measurements by the gas meter of the oxygen liberated from the sample are passed to a data acquisition system for processing, where, advantageously, the information may be calibrated to produce an accurate reading of the hydrogen peroxide present m the sample. Advantageously, when it is required to measure small amounts of hydrogen peroxide, such as about 25-500 mg.l "1 , the fluid sample is aerated prior to contacting with the catalyst. The method according to the invention may be used m a wide range of industrial applications, for example, m paper processing, textile processes, steel industry and water treatment. Accordmg to a second aspect of the present invention, there is provided apparatus for determining the hydrogen peroxiαe content of a fluid, which apparatus includes: (a) a first receptacle arranged to (1) receive the fluid and a catalyst, and (n) to permit decomposition of the hydrogen peroxide present to oxygen and water; (b) a gas meter arranged to measure the oxygen evolved. It is preferred that the flow of fluid and the catalyst are controlled using at least one suitable peristaltic pump and/or at least one centrifugal pump. In a first embodiment of the second aspect of the present invention, the apparatus is suitable for use m continuous measurements. In this embodiment, the fluid m the receptacle is maintained at a volume of about 15-60cm 3 , preferably about 50cm 3 . The volume may be advantageously controlled using a manometer. The apparatus preferably includes aeration means when it is required to measure small amounts of hydrogen peroxide, such as about 25-500 mg.l 1 . In a second embodiment of the second aspect of the present invention, the apparatus is suitable for use m batch measurements. In this embodiment, the fluid m the receptacle is maintained at about 25-2000cm 3 , preferably about 1000cm 3 . According to a third embodiment of the present invention, there is provided a gas flow meter for use m the measurement of oxygen which is liberated as a result of the decomposition of hydrogen peroxide, the decomposition being a result of contacting the hydrogen peroxide with a catalyst . It is preferred that the gas meter comprises a three way solenoid valve, a sensitive differential pressure transducer and a ballast chamber. The pressure transducer is preferably based on a steel diaphragm wnich advantageously is not significantly affected by temperature changes and is resistant to corrosion by water-saturated gases. Preferably, the solenoid valve comprises a dry paddle solenoid valve, typically made from a material which is resistant to corrosive gases. Such a valve is advantageously corrosion resistant . The output from the differential pressure transducer may, m some embodiments, be smoothed, typically by an RC circuit or other conventional methods. The present invention will now be illustrated, by way of example only, with reference to Figure 1 of the accompanying drawings, which represents an embodiment of apparatus according to the present invention for measurement of hydrogen peroxide. Standard hydrogen peroxide solutions were prepared from a 30% solution. The catalase, commercially available from Biocatalysts Limited, UK was produced from a selected stram of Aspergill us niger (this catalase is heat stable, active in a broad pK range and less susceptible to the deactivating effects of hydrogen peroxide when compared with bovine sources) . Various dilutions of the catalase supplied was used m the experiments outlined below: Continuous Experiments Referring to Figure 1, the continuous experiments were carried out in a hydrogen peroxide monitor 1 consisting of an acrylic reaction chamber 2 (26cm 3 total volume) , with a working liquid volume 3 of 17cm 3 (the working liquid volume 3 is maintained at 17cm 3 by manometer 9) ; the contents were mixed by a magnetic stirrer bar 4. The chamber was housed in a SI 60 D variable temperature controlled incubator (Stuart Scientific Co. UK) supplied by Fisher Scientific UK (not shown) . The chamber was connected to a LFM100 gas meter (G H Zeal Ltd) . The gas meter 5 comprises a solenoid valve 10, a ballast chamber 11, a sensitive pressure transducer 12 and a control circuit and acquisition system 13. Data from the monitor was logged on a PC with a interface card (DAQ 700) using LabVIEW (a trade mark of National Instruments, Newbury, UK) . The Virtual instrument (VI) was configured to sample the output from the monitor at 1 minute intervals and download to "Microsoft Excel" (both being trade marks) for off-line processing. The standard hydrogen peroxide 14 was introduced into reaction chamber 2 using a 5 Q 5u peristaltic pump 6 (Watson-Marlow Ltd, Poole, UK) w th an 8-roller multi -channel pump nead at a rate of 2.2cm 3 mm -. Similarly, the 1% catalase solution 8 was introduced into reaction chamber 2 using a 505μ peristaltic pump 7 (Watson-Marlow Ltd, Poole, UK) with an 8-roller multi-channel pump nead at a rate of 0.075cm 3 mm 1 . Duplicate runs of each hydrogen peroxide solution were performed at three different temperatures of 30, 25 and 45°C. The oxygen production rate for each run was calculated as the average of at least 25 minutes of steady state gas production. Figures 2 and 3 show examples of results obtained for measurements carried out m these experiments. Experiments in Batch Mode In one set of experiments the hydrogen peroxide monitor was similar m construction to that depicted m Figure 1. It consisted of an acrylic reaction chamber having 70cm 3 total volume. The liquid temperature was controlled using a water jacket and a Grant FH15 (Cambridge, UK) flow heater. The chamber was connected to a LFMlOO gas meter (G H Zeal Ltd, UK) . Data from the monitor was logged on a PC with an interface card (DAQ 700) using LabVIEW (a trade mark of National Instruments, Newbury, UK) . The Virtual instrument was configured to sample the output from the monitor at 1 minute intervals and download to "Microsoft Excel" (both trade marks) for off line processing. A 25cm 3 sample of hydrogen peroxide was pipetted into the chamber, which was then sealed. A 1% solution of the catalase was then pumped into reaction chamber using a 505μ peristaltic at a rate of 0.075cm 3 mm 1 (Watson & Marlow Ltd., Poole, UK) . The catalase was continuously pumped into the reaction chamber until all the hydrogen peroxide had completely degraded and gas evolution had ceased, the total oxygen production was than calculated taking into account the displacement caused by introduction of catalase. Duplicate runs of each hydrogen peroxide solution were performed at 25°C. Figures 4 and 5 show examples of results of experiments carried out with this monitor measuring from 0.25 to 1.5% hydrogen peroxide solutions m sodium dihydrogen orthophosphate buffer at pH7. In a further set of experiments, the hydrogen peroxide monitor consisted of an acrylic chamber with a working volume of 1 litre. The reaction chamber was located m a temperature controlled enclosure to maintain the temperature of the reaction. The contents of the reaction chamber were mixed by recirculation of the reactor contents by means of a centrifugal pump. The reaction chamber was connected to a low flow gas meter, the technology as described previously. A data logger recorded output from the gas flow meter at predefined intervals and this was downloaded via an RS232 port using "Easy Log" software onto a PC where the data was processed off-line using "Microsoft Excel", both being trade marks. For measurement, the chamber was filled with pre-aerated sample to the predefined volume. The chamber was then sealed shut. A known volume of catalase reagent was then added. The gas flow due to injection of the reagent is known and compensated for. As catalyst was injected, a compensating volume was removed from the reaction chamber. The reaction was allowed to continue until all oxygen evolved was measured. The oxygen evolved passed to the gas flow meter where its passage through the meter was registered electronically m the data logger as a voltage. The hydrogen peroxide concentration could be calculated and was proportional to the total measured evolved oxygen registered as a cumulative voltage. The following equation can be used to determine the volume of oxygen based on the voltage measurement. 1 mol 0 2 = 25.41L (273.15 K, 0°C) 1 mol 0 2 = 25 . 29L ( 308 . 15 K, 37°C) [p*V = n*R*T ; V x /V 2 = Υ T 2 ] 1 mol H 2 0 2 = 0 . 5 mole 0 2 = 12 . GA S L 1 mL 0 2 = 0 . 1 V C = reaction volume m litres Equation: 1 mg/L* (34.01 mg/mmol) - χ *12.65mL/mmol*0.1 V/mL*C=lppm H 2 0 2 — y [ppm H 2 0 2 ] = 0.037 V/L*C The chamber was emptied before repeating the process. Duplicate runs were performed using hydrogen peroxide solutions with the reaction chamber incubated at 37°C. Figures 6 to 9 show examples of results of various experiments carried out with this monitor for concentrations of peroxide between 0 - 300 ppm m solutions of water, (Figures 6 and 7), paper pulp filtrates filtered through a 500um mesh adjusted to pHIO using NaOH, (Figure 8) and samples m water using different concentrations of catalase reagent, 1, 5 and 10%, (Figure 9) . Results : The results of the experiments outlined above are given m the accompanying figures, wherein: Figure 2 is a graph of the oxygen produced from hydrogen peroxide standards using a continuous operated hydrogen peroxide monitoring method; Figure 3 is a graph representing the correlation of oxygen produced against peroxide standards using a continuous operated hydrogen peroxide monitoring method; Figure 4 is a graph of the oxygen produced from hydrogen peroxide standards using a batch operated hydrogen peroxide monitoring method; and Figure 5 is a graph representing the correlation of oxygen produced against hydrogen peroxide standards using a batch operated hydrogen peroxide monitoring method. Figure 6 shows oxygen evolution profiles for concentrations of hydrogen peroxide of 75, 100, 150, 200 and 300 ppm m water obtained by dosing of 10% catalase using a batch operated peroxide monitoring method; Figure 7 shows the correlation of oxygen evolved against samples of known peroxide concentration m water from 0-300 ppm obtained by dosing of 10% catalase using a batcn operated peroxide monitoring method; Figure 8 shows the correlation of oxygen evolved against samples of known peroxide concentration (0-300 ppm) prepared from paper pulp filtrates, pH adjusted to 10, obtained by dosing of 10% catalase using a batch operated peroxide monitoring method; Figure 9 shows the correlation of oxygen evolved for samples of known peroxide concentration m water (0-300 ppm) with dosing of different concentrations of catalase reagent into the chamber, 1,5 and 10%, using a batch operated peroxide monitoring method; The method according to the invention may provide rapid measurement of peroxide m sample sizes of 20ml or above. The method is more rapid than the existing titrimetric and colorimetric methods, and is not generally subject to interferences. The method can therefore also be used offline to replace existing methods for peroxide determination both for industrial and research purposes.

Claims: Claims ; 1. A method of determining the hydrogen peroxide of a fluid, which method includes: (a) contacting the fluid with a catalyst so as to permit decomposition of the hydrogen peroxide present in the fluid to oxygen and water; (b) permitting the oxygen liberated to pass to a gas meter; and (c) measuring the volume of oxygen liberated utilizing the gas meter, wherein the volume of oxygen liberated provides a measure of the hydrogen peroxide content of the fluid. 2. A method according to claim 1, characterised in that the gas meter is arranged to measure low and irregular gas flows with a low back pressure. 3. A method according to claims 1 or 2 , characterised in that the gas meter is a low flow gas meter. 4. A method according to any preceding claim, characterised in that the volume of oxygen liberated in step (b) is measured directly. A method according to any preceding claim, characterised in that the catalyst is an enzyme. 6. A method according to claim 5, characterised m that the enzyme is catalase. 7. A method according to claim 6, characterised m that the catalase is hydrogen peroxide: hydrogen peroxide oxidoreductase , ECl.11.1.6. 8. A method according to any preceding claim, characterised m that the catalyst is soluble or immobilised. 9. A method according to any preceding claim, characterised m that the amount of catalyst present m step (a) is predetermined. 10. A method according to any preceding claim, characterised in that step (a) is carried out for sufficient time to decompose substantially all of the hydrogen peroxide present m the fluid. 11. A method according to any preceding claim, wherein the fluid which is maintained m a predetermined temperature range. 12. A method according to claim 11, characterised in that the range is from about 20°C to 40°C 13. A method according to any preceding claim, characterised in that a parameter corresponding to volume of oxygen liberated is passed to a data acquisition system for processing. 14 A method according to any preceding claim, characterised in that the fluid sample is aerated prior to contacting the catalyst . 15. Apparatus for determining the hydrogen peroxide content of a fluid, which apparatus includes: (a) a first receptacle arranged to (I) receive the fluid and a catalyst, and (n) to permit decomposition of the hydrogen peroxide present to oxygen and water; and (b) a gas meter arranged to measure the oxygen evolved m step (a) . 16. Apparatus according to claim 15, characterised m that the apparatus further includes at least one peristaltic pump and/or at least one centrifugal pump. 17. Apparatus according to claim 15 or 16, which includes a manometer for controlling the fluid m the first receptacle . 18. Apparatus according to any of claims 15 to 17, characterised in that the apparatus further includes means for aerating the fluid. 19. A gas flow meter for use m the measurement of oxygen which is liberated as a result of the decomposition of hydrogen peroxide, said decomposition being a result of contacting the hydrogen peroxide with a catalyst. 20. A gas flow meter according to claim 19, which includes a three way solenoid valve, a differential pressure transducer and a ballast chamber. 21. A gas meter according to claim 20, characterised in that the pressure transducer is based on a steel diaphragm. 22. A gas meter according to claims 20 or 21, characterised m that the solenoid valve comprises a dry paddle solenoid valve. 23. A gas meter according to any of claims 20 to 22, characterised m that the pressure transducer produces an output which is smoothed by a RC circuit.

Inventors: CUNNAH PHILIP JEFFREY, DINSDALE RICHARD, GUWY ALAN, HAWKES DENNIS, HAWKES FREDA, CUNNAH, PHILIP, JEFFREY, DINSDALE, RICHARD, GUWY, ALAN, HAWKES, DENNIS, HAWKES, FREDA
Applicants: BIOCATALYSTS LTD, CUNNAH PHILIP JEFFREY, DINSDALE RICHARD, GUWY ALAN, HAWKES DENNIS, HAWKES FREDA, BIOCATALYSTS LIMITED, CUNNAH, PHILIP, JEFFREY, DINSDALE, RICHARD, GUWY, ALAN, HAWKES, DENNIS, HAWKES, FREDA
Application year: 2000
Main classification: C12Q1
IPC codes: C12Q1, G01N7, G01N31