WO2000047993A1 - Method and device for determining the toc content of aqueous samples - Google Patents
Method and device for determining the toc content of aqueous samples Download PDFInfo
- Publication number
- WO2000047993A1 WO2000047993A1 PCT/EP2000/001066 EP0001066W WO0047993A1 WO 2000047993 A1 WO2000047993 A1 WO 2000047993A1 EP 0001066 W EP0001066 W EP 0001066W WO 0047993 A1 WO0047993 A1 WO 0047993A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- measuring
- ultrapure water
- space
- determining
- conductivity
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/18—Water
- G01N33/1826—Organic contamination in water
- G01N33/1846—Total carbon analysis
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N31/00—Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods
- G01N31/005—Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods investigating the presence of an element by oxidation
Definitions
- the invention relates to a method and a device for determining the total organically bound carbon in aqueous samples according to the preamble of the main claim and the subordinate device claim.
- the generated CO is removed from the solution by acidifying and passing a gas-permeable membrane (gas-liquid separator).
- the C0 2 is passed into a gas cuvette and measured spectroscopically using infrared radiation.
- the measurement solution is passed into a reaction cell.
- the conductivity is measured and the solution is irradiated with UV light until all organic compounds have been destroyed.
- the conductivity is measured continuously, which enables reaction control.
- the TOC content of the solution can be inferred from the conductivity difference determined at the beginning and towards the end of the reaction. Disadvantages here are the impossibility of on-line measurements and the fact that the volume of the reaction solution cannot be varied, which therefore limits the working range of this device to samples with a very low TOC content.
- the disadvantages of the known methods are thus in summary that the use of chemicals can usually not be dispensed with, which results in a relatively high level of maintenance.
- none of the known, commercially available devices enables true on-line monitoring of the TOC content. All known devices for TOC trace analysis also have an extremely limited working range, which severely limits their usability for water samples with higher loads.
- the invention is therefore based on the object of providing a method and a device for determining the TOC content in aqueous samples, in which the use of chemicals can largely be dispensed with and which involves both on-line measurement and measurements allow after the stopped-flow method, whereby water samples with a higher TOC content should be measurable.
- the method according to the invention and the device according to the invention have advantages in particular in that the addition of chemicals and gases can be dispensed with entirely.
- the resulting C0 2 does not have to be separated off and the setting of the C0 2 / HC0 3 " balance in favor of the HC0 3 ⁇ ion is favored by the electrolytic formation of OH " ions.
- the work area can be varied by working in the flow method, which enables true online monitoring or working in the stopped-flow method.
- the analyte is enriched in the stopped-flow method, so that extremely low detection limits are given.
- water samples with a higher TOC content can be measured in online operation.
- the outlay on used chemicals can be reduced to a minimum.
- the modular structure of the device according to the invention also enables a particularly broad spectrum of analytical problems to be dealt with.
- FIG. 1 shows a schematic representation of the device according to the invention with its components
- Figure 2 is a schematic representation of the electrodialysis unit.
- the overall system has an ion exchanger unit 1, for example a mixed bed ion exchanger for removing the inorganic carbon and possibly other inorganic substances, a downstream UV reactor 2, an electrodialysis unit 3, a control and evaluation unit 4 and an ion exchanger 5.
- An option for measuring the conductivity from and after the ion exchanger unit 1 enables the salinity of the sample to be determined.
- the electrodialysis unit 3 shown in FIG. 2 has a cathode space 6 with a cathode 7, in which an anion exchange resin is accommodated. Furthermore, an anode space 8 with anode 9 is provided and a measurement space 10 is arranged between anode space 8 and cathode space 6, an anion exchange membrane 11 being provided at the boundary between measurement space 10 and cathode space 6 and a cation exchange membrane 12 being provided between anode space 8 and measurement space 10.
- the aqueous solution to be measured is fed to the cathode chamber 6 from the UV reactor 2 in accordance with the arrow 13, and the escaping liquid is conducted in accordance with the arrow representation 14 into the anode chamber 8, which it leaves in accordance with the arrow 15.
- Ultrapure water as the measuring medium which, for example, emerges from the ion exchanger 5, is, as indicated by the arrows 16, passed through the measuring chamber in countercurrent to the flow in the cathode chamber 6.
- one conductivity measuring cell 17 is indicated in front of and behind the measuring space 10 by the circuits.
- the aqueous solution to be measured can first be passed through the anode compartment and then through the cathode compartment.
- the aqueous sample is introduced into the unit 1, which is designed in a known manner and in which inorganic carbon compounds are removed or converted.
- the treated aqueous solution is the UV reactor 2 supplied, in which the aqueous solution is irradiated with UV radiation, all organic compounds being oxidized to carbon dioxide.
- the UV oxidation should take place catalytically.
- the sample reaches the cathode space 6 of the electrodialysis unit 3 according to the arrow 13, a variable voltage being applied between the anode 9 and the cathode 7.
- Hybrid formed are OH * at the cathode 7 droxylionen that Genat balance pushes the carbonic acid hydro on the side of HC0 3 ⁇ ions.
- the hydrogen carbonate ions formed are actively transported to the anion exchange membrane 11, since the membrane is positively polarized by the applied voltage. This membrane is permeable to the HC0 3 " ions, so that they reach the measuring chamber in which there is ultrapure water in which an enrichment takes place.
- the connection 14 leads the sample further into the anode chamber 8, the H + -Ions through the cation exchange membrane 12, which due to the applied
- the conductivity of the ultrapure water is measured with the measuring device 17 as the basic value, wherein the temperature can be measured at the same time.
- a second measurement of the ultrapure water enriched with HC0 3 ⁇ is carried out, and the temperature can also be recorded.
- the specific resistance of the solution can be used to determine the TOC, but this is also included in the conductivity measurement.
- the measured values are fed to the control and evaluation unit 4, using the differences the temperature-corrected conductivity measurement of the measuring medium pure water in front of and behind the measuring room the original TOC content of the sample solution is determined.
- the measured values are compared with previously determined values.
- the conductivity measurement is a relative method in which the method or the device is calibrated beforehand with known standard solutions.
- the ultrapure water can be passed continuously through the measuring space 10 to implement on-line monitoring, the difference in the conductivity of the ultrapure water before and after the measuring space being measured continuously. If the quality of the ultrapure water supplied is constant, the continuous measurement of the base value, i.e. the conductivity of the ultrapure water supplied to the measuring space 10 is eliminated and would only have to be checked at certain intervals in a random manner.
- the ultrapure water can, however, also be introduced into the measuring space 10 at intervals (stopped-flow method), it remaining in the measuring space 10 for a predetermined period of time and being drained after this period. Then water is added again.
- the ultrapure water leaving the measuring room, i.e. the water enriched with hydrogen carbonate ions is fed to the mixed bed ion exchanger 5 after the conductivity measurement, in which it is regenerated and used again for the process.
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Medicinal Chemistry (AREA)
- Physics & Mathematics (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
Abstract
Description
Verfahren und Vorrichtung zum Bestimmen des TOC- Gehaltes in wässrigen ProbenMethod and device for determining the TOC content in aqueous samples
Die Erfindung betrifft ein Verfahren und eine Vor- richtung zum Bestimmen des gesamten organisch gebundenen Kohlenstoffs in wässrigen Proben nach dem Oberbegriff des Hauptanspruchs und des nebengeordneten Vorrichtungsanspruchs .The invention relates to a method and a device for determining the total organically bound carbon in aqueous samples according to the preamble of the main claim and the subordinate device claim.
Bei den zur Zeit bekannten Analysensysteme zurIn the currently known analysis systems for
Erfassung des TOC-Gehaltes in wässrigen Proben im unteren Spurenbereich haben sich in den letzten Jahren vor allem zwei Verfahren durchgesetzt. Beiden Verfahren ist die oxidative Zerstörung der organi- sehen Wasserinhaltsstoffe durch Bestrahlung mit UV- Licht gemeinsam. Bei diesem Prozeß werden sämtliche organische Verbindungen bis zum Kohlendioxid oxi- diert. Anorganische KohlenstoffVerbindungen werden bei den meisten Verfahren vor der Photooxidation durch Ansäuern entfernt. Verwendung findet hier zum einen ein einfacher Säurezusatz und zum anderen ein sogenannter solid-phase-acidifier (US 5,672,516). Die Unterscheidung der genannten Verfahren erfolgt hauptsächlich bei der Detektion.Acquisition of the TOC content in aqueous samples in the lower trace range has become the main method in recent years. Both processes have in common the oxidative destruction of the organic water constituents by irradiation with UV light. In this process, all organic compounds are oxidized down to carbon dioxide. Inorganic carbon compounds are removed by acidification in most processes before photo-oxidation. Used here for a simple acid addition and a so-called solid-phase acidifier (US 5,672,516). The differentiation of the above-mentioned methods mainly occurs in the detection.
Bei dem einen Verfahren wird das generierte C0 durch Ansäuern und Vorbeileiten an einer gasmipermeablen Membran (gas-flüssig-Separator) aus der Lösung entfernt. Das C02 wird in eine Gasküvette geleitet und mittels Infrarotstrahlung spektroskopisch gemessen.In one method, the generated CO is removed from the solution by acidifying and passing a gas-permeable membrane (gas-liquid separator). The C0 2 is passed into a gas cuvette and measured spectroscopically using infrared radiation.
Es erfolgt eine Anreicherung in der Gasküvette, deren Dauer sich nach der erwarteten TOC-Konzentration richtet. Die wesentlichen Nachteile dieses Verfahrens sind die Unmöglichkeit einer on-line-Messung bzw. kontinuierlichen Messung (die typische Meßzeit beträgt hier ca. 10 bis 30 min.) und die Tatsache, daß zur Messung Hilfsgase sowie Chemikalien benötigt werden, wodurch die Betriebskosten steigen und eine regelmäßige Wartung erforderlich wird.There is an enrichment in the gas cuvette, the duration of which depends on the expected TOC concentration. The main disadvantages of this method are the impossibility of an on-line measurement or continuous measurement (the typical measurement time here is approximately 10 to 30 minutes) and the fact that auxiliary gases and chemicals are required for the measurement, which increases the operating costs and regular maintenance is required.
Beim zweiten Verfahren wird die Meßlösung in eine Reaktionszelle geleitet. Die Leitfähigkeit wird gemessen und die Lösung mit UV-Licht bestrahlt bis alle organischen Verbindungen zerstört worden sind. Die Leitfähigkeit wird dabei kontinuierlich gemessen, wodurch eine Reaktionskontrolle ermöglicht wird. Aus der ermittelten Leitfähigkeitsdifferenz zu Beginn und gegen Ende der Reaktion läßt sich auf den TOC-Gehalt der Lösung schließen. Nachteile sind hier wiederum die Unmöglichkeit von on-line-Messungen und die Tatsache, daß das Volumen der Reaktionslösung nicht variiert werden kann, was den Arbeitsbereich dieses Gerätes deshalb auf Proben mit sehr geringem TOC-Gehalt begrenzt . Die Nachteile der bekannten Verfahren sind somit in Zusammenfassung, daß auf den Einsatz von Chemikalien meist nicht verzichtet werden kann, was einen relativ hohen Wartungsaufwand zur Folge hat. Außerdem ermög- licht keines der bekannten, kommerziell erhältliche Geräte eine echte on-line-Überwachung des TOC-Gehal- tes. Alle bekannten Geräte zur TOC-Spurenanalytik haben zudem einen äußerst begrenzten Arbeitsbereich, was ihre Einsatzfähigkeit bei stärker belasteten Was- serproben stark einschränkt.In the second method, the measurement solution is passed into a reaction cell. The conductivity is measured and the solution is irradiated with UV light until all organic compounds have been destroyed. The conductivity is measured continuously, which enables reaction control. The TOC content of the solution can be inferred from the conductivity difference determined at the beginning and towards the end of the reaction. Disadvantages here are the impossibility of on-line measurements and the fact that the volume of the reaction solution cannot be varied, which therefore limits the working range of this device to samples with a very low TOC content. The disadvantages of the known methods are thus in summary that the use of chemicals can usually not be dispensed with, which results in a relatively high level of maintenance. In addition, none of the known, commercially available devices enables true on-line monitoring of the TOC content. All known devices for TOC trace analysis also have an extremely limited working range, which severely limits their usability for water samples with higher loads.
Der Erfindung liegt daher die Aufgabe zugrunde, ein Verfahren und eine Vorrichtung zur Bestimmung des TOC-Gehaltes in wässrigen Proben zu schaffen, bei denen weitgehend auf den Einsatz von Chemikalien verzichtet werden kann und die sowohl eine on-line-Mes- sung als auch Messungen nach dem stopped-flow-Verfah- ren gestatten, wobei Wasserproben mit höherem Gehalt am TOC meßbar sein sollen.The invention is therefore based on the object of providing a method and a device for determining the TOC content in aqueous samples, in which the use of chemicals can largely be dispensed with and which involves both on-line measurement and measurements allow after the stopped-flow method, whereby water samples with a higher TOC content should be measurable.
Diese Aufgabe wird erfindungsgemäß durch die Merkmale des Hauptanspruchs und des Nebenanspruchs gelöst.This object is achieved by the features of the main claim and the subclaim.
Das erfindungsgemäße Verfahren und die erfindungsge- mäße Vorrichtung weisen Vorteile insbesondere dahingehend auf, daß vollständig auf den Zusatz von Chemikalien und Gasen verzichtet werden kann. Es muß entstehendes C02 nicht abgetrennt werden und die Einstellung des C02/HC03 "-Gleichgewichtes zugunsten des HC03 ~-Ions wird durch die elektrolytische Bildung von OH"-Ionen begünstigt. Der Arbeitsbereich kann durch Arbeiten im Durchflußverfahren, wodurch eine echte on-line-Überwachung möglich ist oder Arbeiten im stopped-flow-Verfahren sehr weit variiert werden. Im stopped-flow-Verfahren wird der Analyt angereichert, so daß äußerst geringe Nachweisgrenzen gegeben sind. Auf der anderen Seite können im on-line-Betrieb Wasserproben mit einem höheren Gehalt an TOC gemessen werden.The method according to the invention and the device according to the invention have advantages in particular in that the addition of chemicals and gases can be dispensed with entirely. The resulting C0 2 does not have to be separated off and the setting of the C0 2 / HC0 3 " balance in favor of the HC0 3 ~ ion is favored by the electrolytic formation of OH " ions. The work area can be varied by working in the flow method, which enables true online monitoring or working in the stopped-flow method. The analyte is enriched in the stopped-flow method, so that extremely low detection limits are given. On the other hand, water samples with a higher TOC content can be measured in online operation.
Durch die in den Unteransprüchen angegebenen Maßnahmen sind weitere vorteilhafte Weiterbildungen und Verbesserungen möglich.The measures specified in the subclaims make further advantageous developments and improvements possible.
Durch Regeneration des im Prozeß verbrauchten Reinst- wasser mit Hilfe eines Ionenaustauschers läßt sich der Aufwand an Gebrauchschemikalien auf ein Minimum reduzieren.By regenerating the ultrapure water used in the process with the help of an ion exchanger, the outlay on used chemicals can be reduced to a minimum.
Der modulare Aufbau der erfindungsgemäßen Vorrichtung ermöglicht zudem ein besonders breites Spektrum an analytischen Problemstellungen zu bearbeiten.The modular structure of the device according to the invention also enables a particularly broad spectrum of analytical problems to be dealt with.
Ein Ausführungsbeispiel der Erfindung ist in der Zeichnung dargestellt und wird in der nachfolgenden Beschreibung näher erläutert.An embodiment of the invention is shown in the drawing and is explained in more detail in the following description.
Es zeigenShow it
Figur 1 eine schematische Darstellung der erfindungs- gemäßen Vorrichtung mit ihren Bestandteilen,FIG. 1 shows a schematic representation of the device according to the invention with its components,
Figur 2 eine schematische Darstellung der Elektrodialyseeinheit .Figure 2 is a schematic representation of the electrodialysis unit.
In Figur 1 ist das Gesamtsystem zur Analyse von wässrigen Proben bzw. zur Bestimmung des gesamten organisch gebundenen Kohlenstoffs, genannt TOC, in wässrigen Proben. Dabei weist das Gesamtsystem eine Ionentauschereinheit 1 z.B. einen Mischbettionenaus- tauscher zum Entfernen des anorganischen Kohlenstoffs und gegebenenfalls anderer anorganischer Substanzen, einen nachgeschalteten UV-Reaktor 2, eine Elektrodialyseeinheit 3, eine Steuer- und Auswerteeinheit 4 sowie einen Ionenaustauscher 5 auf. Eine Option zur Leitfähigkeitsmessung von und nach der Ionenaustauschereinheit 1 ermöglicht die Bestimmung der Salinität der Probe.1 shows the overall system for the analysis of aqueous samples or for the determination of the total organically bound carbon, called TOC, in aqueous samples. The overall system has an ion exchanger unit 1, for example a mixed bed ion exchanger for removing the inorganic carbon and possibly other inorganic substances, a downstream UV reactor 2, an electrodialysis unit 3, a control and evaluation unit 4 and an ion exchanger 5. An option for measuring the conductivity from and after the ion exchanger unit 1 enables the salinity of the sample to be determined.
Die in Figur 2 dargestellte Elektrodialyseeinheit 3 weist einen Kathodenraum 6 mit Kathode 7 auf, in dem ein Anionenaustauscherharz aufgenommen ist. Weiterhin ist ein Anodenraum 8 mit Anode 9 vorgesehen und zwischen Anodenraum 8 und Kathodenraum 6 ist ein Meßraum 10 angeordnet, wobei an der Grenze zwischen Meßraum 10 und Kathodenraum 6 eine Anionenaustau- schermembran 11 und zwischen Anodenraum 8 und Meßraum 10 eine Kationenaustauschermembran 12 vorgesehen sind. Die zu messende wässrige Lösung wird dem Kathodenraum 6 aus dem UV-Reaktor 2 entsprechend dem Pfeil 13 zugeführt, die austretende Flüssigkeit wird ent- sprechend der Pfeildarstellung 14 in den Anodenraum 8 geleitet, den sie entsprechend dem Pfeil 15 verläßt. Reinstwasser als Meßmedium, das beispielsweise aus dem Ionenaustauscher 5 austritt, wird, wie die Pfeile 16 andeuten, im Gegenstrom zur Strömung im Kathoden- räum 6 durch den Meßraum geleitet. Jeweils eine Leitfähigkeitmeßzelle 17 ist vor und hinter dem Meßraum 10 durch die Schaltkreise angedeutet. In einem anderen Ausführungsbeispiel kann die zu messende wässrige Lösung zuerst durch den Anodenraum und dann durch den Kathodenraum geleitet werden.The electrodialysis unit 3 shown in FIG. 2 has a cathode space 6 with a cathode 7, in which an anion exchange resin is accommodated. Furthermore, an anode space 8 with anode 9 is provided and a measurement space 10 is arranged between anode space 8 and cathode space 6, an anion exchange membrane 11 being provided at the boundary between measurement space 10 and cathode space 6 and a cation exchange membrane 12 being provided between anode space 8 and measurement space 10. The aqueous solution to be measured is fed to the cathode chamber 6 from the UV reactor 2 in accordance with the arrow 13, and the escaping liquid is conducted in accordance with the arrow representation 14 into the anode chamber 8, which it leaves in accordance with the arrow 15. Ultrapure water as the measuring medium, which, for example, emerges from the ion exchanger 5, is, as indicated by the arrows 16, passed through the measuring chamber in countercurrent to the flow in the cathode chamber 6. In each case one conductivity measuring cell 17 is indicated in front of and behind the measuring space 10 by the circuits. In another embodiment, the aqueous solution to be measured can first be passed through the anode compartment and then through the cathode compartment.
Die wässrige Probe, deren TOC-Gehalt bestimmt werden soll, wird in die Einheit 1 eingeleitet, die in bekannter Weise ausgeführt ist und in der anorganische Kohlenstoff erbindungen entfernt bzw. umgewandelt werden. Die so behandelte wässrige Lösung wird dem UV-Reaktor 2 zugeführt, in dem die wässrige Lösung mit UV-Strahlung bestrahlt wird, wobei sämtliche organische Verbindungen bis zum Kohlendioxid oxidiert werden. Dabei sollte die UV-Oxidation katalytisch ab- laufen. Die Probe gelangt entsprechend dem Pfeil 13 in den Kathodenraum 6 der Elektrodialyseeinheit 3, wobei eine variable Spannung zwischen Anode 9 und Kathode 7 angelegt ist. An der Kathode 7 werden Hy- droxylionen OH* gebildet, die das Kohlensäure-Hydro- genat-Gleichgewicht auf die Seite der HC03 ~ Ionen schiebt. Die entstandenen Hydrogencarbonationen werden aktiv zur Anionenaustauschermembran 11 transportiert, da die Membran durch die anliegende Spannung positiv polarisiert ist. Diese Membran ist für die HC03 "-Ionen durchlässig, so daß sie in den Meßraum gelangen, in dem sich Reinstwasser befindet, in dem eine Anreicherung stattfindet. Über die Verbindung 14 wird die Probe weiter in den Anodenraum 8 geleitet, wobei die H+-Ionen durch die Kationenaus- tauschermembran 12, die aufgrund der angelegtenThe aqueous sample, the TOC content of which is to be determined, is introduced into the unit 1, which is designed in a known manner and in which inorganic carbon compounds are removed or converted. The treated aqueous solution is the UV reactor 2 supplied, in which the aqueous solution is irradiated with UV radiation, all organic compounds being oxidized to carbon dioxide. The UV oxidation should take place catalytically. The sample reaches the cathode space 6 of the electrodialysis unit 3 according to the arrow 13, a variable voltage being applied between the anode 9 and the cathode 7. Hybrid formed are OH * at the cathode 7 droxylionen that Genat balance pushes the carbonic acid hydro on the side of HC0 3 ~ ions. The hydrogen carbonate ions formed are actively transported to the anion exchange membrane 11, since the membrane is positively polarized by the applied voltage. This membrane is permeable to the HC0 3 " ions, so that they reach the measuring chamber in which there is ultrapure water in which an enrichment takes place. The connection 14 leads the sample further into the anode chamber 8, the H + -Ions through the cation exchange membrane 12, which due to the applied
Spannung negativ polarisiert ist, gleichfalls in das im Meßraum 10 vorhandene Reinstwasser gelangen.Voltage is polarized negatively, also get into the ultrapure water present in the measuring room 10.
Vor dem Erreichen des Meßraums 10 wird die Leitfähig- keit des Reinstwassers mit der Meßvorrichtung 17 als Grundwert gemessen, wobei gleichzeitig die Temperatur gemessen werden kann. Nach dem Verlassen des Meßraums 10 wird eine zweite Messung des mit HC03 ~ angereicherten Reinstwassers durchgeführt, wobei ebenfalls die Temperatur mit erfaßt werden kann. Alternativ läßt sich der spezifische Widerstand der Lösung zur TOC-Bestimmung heranziehen, der jedoch auch in der Leitfähigkeitsmessung enthalten ist.Before the measuring space 10 is reached, the conductivity of the ultrapure water is measured with the measuring device 17 as the basic value, wherein the temperature can be measured at the same time. After leaving the measuring room 10, a second measurement of the ultrapure water enriched with HC0 3 ~ is carried out, and the temperature can also be recorded. Alternatively, the specific resistance of the solution can be used to determine the TOC, but this is also included in the conductivity measurement.
Die Meßwerte werden der Steuer- und Auswerteeinheit 4 zugeführt, in der unter Verwendung der Unterschiede der temperaturkorrigierten Leitfähigkeitsmessung des Meßmediums Reinsrwasser vor und hinter dem Meßraum der ursprüngliche TOC-Gehalt der Probenlösung bestimmt wird. Dabei werden die Meßwerte mit vorher bestimmten Werten verglichen. Es handelt sich bei der Leitfähigkeitsmessung in diesem Zusammenhang um ein Relativverfahren, bei dem das Verfahren bzw. die Vorrichtung vorher mit bekannten Standardlösungen kalibriert werden.The measured values are fed to the control and evaluation unit 4, using the differences the temperature-corrected conductivity measurement of the measuring medium pure water in front of and behind the measuring room the original TOC content of the sample solution is determined. The measured values are compared with previously determined values. In this context, the conductivity measurement is a relative method in which the method or the device is calibrated beforehand with known standard solutions.
Das Reinstwasser kann zur Realisierung einer on-line- Überwachung kontinuierlich durch den Meßraum 10 geleitet werden, wobei kontinuierlich die Differenz der Leitfähigkeit des Reinstwassers vor und nach dem Meß- räum gemessen wird. Bei Konstanz der Qualität des zugeführten Reinstwassers könnte die kontinuierliche Messung des Basiswertes, d.h. die Leitfähigkeit des dem Meßraum 10 zugeführten Reinstwassers entfallen und müßte nur stichprobenartig in bestimmten Inter- vallen überprüft werden.The ultrapure water can be passed continuously through the measuring space 10 to implement on-line monitoring, the difference in the conductivity of the ultrapure water before and after the measuring space being measured continuously. If the quality of the ultrapure water supplied is constant, the continuous measurement of the base value, i.e. the conductivity of the ultrapure water supplied to the measuring space 10 is eliminated and would only have to be checked at certain intervals in a random manner.
Das Reinstwasser kann aber auch intervallartig in den Meßraum 10 eingeleitet werden (stopped-flow-Verfahren) , wobei es einen vorgegebenen Zeitraum im Meßraum 10 verbleibt und nach diesem Zeitraum abgelassen wird. Danach wird erneut Wasser zugeführt. Das den Meßraum verlassende Reinstwasser, d.h. das mit Hydrogenkarbonationen angereicherte Wasser wird nach der Leitfähigkeitsmessung dem Mischbettionenaustauscher 5 zugeführt, in dem es regeneriert wird und erneut für den Prozeß verwendet wird.The ultrapure water can, however, also be introduced into the measuring space 10 at intervals (stopped-flow method), it remaining in the measuring space 10 for a predetermined period of time and being drained after this period. Then water is added again. The ultrapure water leaving the measuring room, i.e. the water enriched with hydrogen carbonate ions is fed to the mixed bed ion exchanger 5 after the conductivity measurement, in which it is regenerated and used again for the process.
Zur Untersuchung von Reinstwasserproben bei denen eine sehr präzise Bestimmung des TOC-Gehaltes not- wendig ist und mit anorganischen Verbindungen nicht gerechnet werden muß, kann ein Entfernen von anorga- nischen Verbindungen komplett entfallen. Bei stärker verunreinigten Probenlösungen, in denen mit anorganischen Substanzen gerechnet werden muß, ist eine Entfernung dieser durch einen Mischbettionenaustauscher 1 vorgesehen. For the analysis of ultrapure water samples where a very precise determination of the TOC content is necessary and inorganic compounds do not have to be expected, the removal of inorganic African connections are completely eliminated. In the case of more contaminated sample solutions in which inorganic substances have to be expected, removal of these by a mixed bed ion exchanger 1 is provided.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19906151.3 | 1999-02-10 | ||
| DE1999106151 DE19906151A1 (en) | 1999-02-10 | 1999-02-10 | Method and device for determining the TOC content in aqueous samples |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2000047993A1 true WO2000047993A1 (en) | 2000-08-17 |
Family
ID=7897478
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2000/001066 Ceased WO2000047993A1 (en) | 1999-02-10 | 2000-02-09 | Method and device for determining the toc content of aqueous samples |
Country Status (2)
| Country | Link |
|---|---|
| DE (1) | DE19906151A1 (en) |
| WO (1) | WO2000047993A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011041378A1 (en) * | 2009-10-02 | 2011-04-07 | Hach Company | Total organic carbon (toc) fluid sensor |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4112360B2 (en) * | 2000-10-16 | 2008-07-02 | シーヴァーズ インスツルメンツ,インク. | Pulse flow total organic carbon analyzer |
| DE102004038607B4 (en) * | 2004-06-09 | 2007-07-12 | Dr. Bruno Lange Gmbh & Co. Kg | Method for determining the organically bound carbon (TOC) and test kit for carrying out the method |
| EP1983340A1 (en) | 2007-04-19 | 2008-10-22 | Hach Lange GmbH | Method for determining the concentration of analytes |
| FR2951272B1 (en) * | 2009-10-09 | 2011-12-09 | Millipore Corp | METHOD OF CALIBRATING A DEVICE FOR MEASURING THE TOTAL ORGANIC CARBON CONTENT |
| DE102016111466A1 (en) | 2016-06-22 | 2017-12-28 | Axagarius Gmbh & Co. Kg | Apparatus and method for removing the Inorganically Bonded Carbon (TIC) in a sample |
| DE102024116918A1 (en) * | 2024-06-17 | 2025-12-18 | Endress+Hauser Conducta Gmbh+Co. Kg | Method and apparatus for measuring the TOC content of a sample |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3909381A (en) * | 1974-11-18 | 1975-09-30 | Raymond John L | Purification of chromium plating solutions by electrodialysis |
| US4018563A (en) * | 1974-08-21 | 1977-04-19 | Aktiebolaget Atomenergi | Analysis of low ion contents |
| DE3223167A1 (en) * | 1982-06-22 | 1983-12-22 | Chemische Werke Hüls AG, 4370 Marl | Method of examining water containing decomposable carbon compounds |
| DE3830623A1 (en) * | 1987-09-15 | 1989-05-03 | Bbc Brown Boveri & Cie | Method for the determination of the total organic carbon content in water |
| EP0570681A1 (en) * | 1992-05-20 | 1993-11-24 | Hüls Aktiengesellschaft | Method for identifying decomposable organic compounds in water |
| US5512608A (en) * | 1993-03-05 | 1996-04-30 | Dymax Corporation | Method for producing an adherent deposit using a chemically activated multi-part, solvent-free composition |
| WO1997003354A1 (en) * | 1995-07-12 | 1997-01-30 | Sievers Instruments, Inc. | Method and apparatus for the measurement of dissolved carbon |
| US5798271A (en) * | 1990-03-02 | 1998-08-25 | Sievers Instruments, Inc. | Apparatus for the measurement of dissolved carbon in deionized water |
| WO1999000178A1 (en) * | 1997-06-30 | 1999-01-07 | Electrosynthesis Company, Inc. | Electrochemical methods for recovery of ascorbic acid |
-
1999
- 1999-02-10 DE DE1999106151 patent/DE19906151A1/en not_active Withdrawn
-
2000
- 2000-02-09 WO PCT/EP2000/001066 patent/WO2000047993A1/en not_active Ceased
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4018563A (en) * | 1974-08-21 | 1977-04-19 | Aktiebolaget Atomenergi | Analysis of low ion contents |
| US3909381A (en) * | 1974-11-18 | 1975-09-30 | Raymond John L | Purification of chromium plating solutions by electrodialysis |
| DE3223167A1 (en) * | 1982-06-22 | 1983-12-22 | Chemische Werke Hüls AG, 4370 Marl | Method of examining water containing decomposable carbon compounds |
| DE3830623A1 (en) * | 1987-09-15 | 1989-05-03 | Bbc Brown Boveri & Cie | Method for the determination of the total organic carbon content in water |
| US5798271A (en) * | 1990-03-02 | 1998-08-25 | Sievers Instruments, Inc. | Apparatus for the measurement of dissolved carbon in deionized water |
| EP0570681A1 (en) * | 1992-05-20 | 1993-11-24 | Hüls Aktiengesellschaft | Method for identifying decomposable organic compounds in water |
| US5512608A (en) * | 1993-03-05 | 1996-04-30 | Dymax Corporation | Method for producing an adherent deposit using a chemically activated multi-part, solvent-free composition |
| WO1997003354A1 (en) * | 1995-07-12 | 1997-01-30 | Sievers Instruments, Inc. | Method and apparatus for the measurement of dissolved carbon |
| WO1999000178A1 (en) * | 1997-06-30 | 1999-01-07 | Electrosynthesis Company, Inc. | Electrochemical methods for recovery of ascorbic acid |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011041378A1 (en) * | 2009-10-02 | 2011-04-07 | Hach Company | Total organic carbon (toc) fluid sensor |
Also Published As
| Publication number | Publication date |
|---|---|
| DE19906151A1 (en) | 2000-09-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE69133288T2 (en) | METHOD AND APPARATUS FOR DETERMINING LOSS OF CARBON IN WATER | |
| EP0428514B1 (en) | Process and device for determining oxidable substances contained in the water of an aqueous sample liquid | |
| DE2823587C3 (en) | Method and device for determining the content of organically bound carbon in water with a high salt content and water containing organic substances | |
| EP3045221A1 (en) | Checking the integrity of a membrane using at least one membrane of an electrolyzer | |
| DE10393273T5 (en) | Excretion of inorganic carbon | |
| DE19780491B4 (en) | CO gas sensor and method for measuring the concentration of CO gas | |
| DE3223167C2 (en) | Method for examining water containing decomposable carbon compounds | |
| WO2000047993A1 (en) | Method and device for determining the toc content of aqueous samples | |
| AT523373B1 (en) | Sensor device for a fuel cell system | |
| EP0282441B1 (en) | Method for determining the chemical oxygen demand of water | |
| DE3546409A1 (en) | Method and appliance for the automatic calibration of chemical sensors | |
| CH659327A5 (en) | Method and apparatus for determining the organic carbon content of water or of an aqueous solution | |
| DE2553756B1 (en) | USE OF THE CONTINUOUS BOTTOM GAS ANALYSIS FOR MONITORING AND REGULATING THE FURNACE AND DEVICE FOR IT | |
| DE19615061C2 (en) | Procedure for measuring the spread of pollutants in groundwater and analysis arrangement for carrying out the procedure | |
| DE3942229C2 (en) | ||
| DE3511687C2 (en) | Method and device for determining organic carbon in water | |
| EP3450976B1 (en) | Method and device for determining chemical oxygen requirements with thermal sample decomposition | |
| DE102019120415A1 (en) | Method for determining a chemical absorption capacity of a process medium in a measuring point and also measuring point for determining a chemical absorption capacity of a process medium | |
| EP0570681B1 (en) | Method for identifying decomposable organic compounds in water | |
| DE3937635C2 (en) | ||
| EP0603751A2 (en) | Method for detecting compounds which are present in a liquid phase | |
| EP1293778B1 (en) | Apparatus for concentration monitoring in fluids | |
| DE102019120442A1 (en) | Method for calibrating an analytical measuring device and measuring point for analyzing a process medium and for calibrating an analytical measuring device | |
| DE2348090C2 (en) | Process for the continuous transfer of gas components dissolved in a liquid into a carrier gas | |
| DE102019120420A1 (en) | Method for calibrating an analytical measuring device and measuring point for analyzing a process medium and for calibrating an analytical measuring device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Kind code of ref document: A1 Designated state(s): JP US |
|
| AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
| DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
| 122 | Ep: pct application non-entry in european phase |