US3854881A - Apparatus for determining organic carbon content of polluted liquids - Google Patents
Apparatus for determining organic carbon content of polluted liquids Download PDFInfo
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- US3854881A US3854881A US00179964A US17996471A US3854881A US 3854881 A US3854881 A US 3854881A US 00179964 A US00179964 A US 00179964A US 17996471 A US17996471 A US 17996471A US 3854881 A US3854881 A US 3854881A
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 40
- 239000007788 liquid Substances 0.000 title claims abstract description 18
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 60
- 238000006243 chemical reaction Methods 0.000 claims abstract description 37
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 30
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 28
- 238000012856 packing Methods 0.000 claims description 27
- 239000000463 material Substances 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 8
- 230000001590 oxidative effect Effects 0.000 claims description 6
- 239000010453 quartz Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 230000008016 vaporization Effects 0.000 claims description 5
- 239000003153 chemical reaction reagent Substances 0.000 claims description 2
- 238000005259 measurement Methods 0.000 abstract description 5
- 229960004424 carbon dioxide Drugs 0.000 description 22
- 239000002253 acid Substances 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000507564 Aplanes Species 0.000 description 1
- 101100264195 Caenorhabditis elegans app-1 gene Proteins 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000008246 gaseous mixture Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00389—Controlling the temperature using electric heating or cooling elements
- B01J2208/00407—Controlling the temperature using electric heating or cooling elements outside the reactor bed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T436/00—Chemistry: analytical and immunological testing
- Y10T436/23—Carbon containing
- Y10T436/235—In an aqueous solution [e.g., TOC, etc.]
Definitions
- the invention provides an improved apparatus and a method for performing total organic carbon analyses more efficiently and rapidly than can be done with either the standard laboratory five-day biochemicaloxygen demand test B O D or the two-hour chemical oxygen demand test, C O D I
- a sample stream from the aqueous liquid source to be monitored is continuously fed into a mixing chamber together with sufficient acid to react with and remove as carbon dioxide all of the inorganic carbon content of the sample, i.e. the carbonates in the sample.
- the acidified sample is scrubbed to remove all carbon dioxide produced by the carbonate-acid reaction, and the carbonate-free sample is metered into a reaction chamber.
- the reaction chamber has an inlet through which the sample and air for oxidizing the organic carbon of the sample are introduced; an outlet for the exit of gaseous and vapor products formed from the sample; and a granular packing material inside that is heated by electric resistor elements disposed outside the chamber in surrounding relation thereto.
- This packing material is chemically inert, as for example, crushed quartz, and is heated to a temperature at which the organic carbon in the sample is oxidized to carbon dioxide by the air atmosphere in the chamber.
- the packing material is disposed to define within the reaction chamber an inlet plenum zone communicating with the inlet to accommodate preheating of the sample by the packing material without contact therewith; and an outlet plenum zone.
- the outlet plenum zone is separated from the inlet plenum zone and communicates with the outlet to collect and deliver thereto the gaseous and vapor products of the sample.
- FIG. 1 is a schematic diagram of an organic carbon content analyzer apparatus according to a preferred embodiment of the invention.
- FIG. 2 is an elevation view, partly in section, of the reaction chamber used in the apparatus represented by' FIG. 1, as seen in a typical installation arranged for external heating of the reactionchamber and packing ma-' terial therein.
- FIG. 3. is aplan view of the reaction chamber and heating installation shown in FIG. 2.
- FIG. I there is schematically exemplified an analyzer apparatus 10 constructed in accordance with the invention and which isoperable to measure, on a continuous flow basis, the total organic carbon content in a sample stream taken from an aqueous liquid source 11, such as a body of water to be monitored for'pollution level.
- an aqueous liquid source 11 such as a body of water to be monitored for'pollution level.
- a continuous sample stream from source 11 is deliv-. ered by a metering pump 12 into a mixing chamber 13.
- Another metering pump 14 delivers hydrochloric acid from a reservoir 15 into mixing chamber I3 for the purpose of acidifying the liquid sample therein to a pH of approximately 2.0.
- the inorganic carbon present in the sample as carbonates is converted to carbon dioxide by reaction with the acid, and the organic carbon content of the sample is substantially unchanged.
- the acidified samplestream is expediently fed into a conventional gas scrubber l6'that is supplied with air from a pump 17 to purge from the sample whatever carbon dioxide was formed by the acidification reaction.
- This carbon dioxide which corresponds quantitatively to theamount of carbonates in the sample, is by choice vented to a waste zone, but could be delivered to a measuring means not shown should it be desired to measure the amount of inorganic carbon in the sample.
- the carbonate-free sample is fed by a metering pump 18 from scrubber 16 into a heated reaction chamber This hot oxidizing atmosphere rapidly vaporizes the .sample and oxidizes the organic carbon content thereof to carbon dioxide.
- reaction chamber 19 The vapor and gaseous mixture effluent of reaction chamber 19 is delivered to a conventional gas-liquid separator 20 that removes by condensation the vapor component of the mixture and passes the gaseous portion containing the carbon dioxide to an infrared analyzer 21.
- Infrared analyzer 21 is of conventional construction and serves to measure the amount of carbon dioxide formed by oxidation of the organic carbon in the sample.
- The, total quantity of organic carbon originally present in the sample can be readily established by applying a known proportionality factor to the carbon dioxide measurement.
- Analyzer 21 is preferrably of a type which has an electrical analog signal presentation of the carbon dioxide measurement data. ln such case, the carbon dioxide data signal is applied to the input of a compatible moving chart recorder 22 for direct display of the analysis results, either in terms of carbon dioxide quantity or, in terms of equivalent organic carbon, which can be done by suitable calibration of recorder 22 using techniques well known to those skilled in the art.
- the inlet of metering pump 12 can be diverted temporarily from source 11 to another source, not shown of liquid having a known concentration of organic carbon sufficiently constant as to be useable as a standard.
- the gas mixture output of separator 20 can be applied to an oxygen demand analyzer, not shown instead of to the infra-red analyzer 21 where it is desired to measure the oxygen demand level of the sample.
- the reaction chamber 19 has a peripheral wall 23 joined to a top cover 24 andv a bottom cover 25 so as to form-a sealed enclosure.
- Within'chamber 19 is an apertured plate 26 which serves to retain a quantity of crushed quartz material 27.
- Packing material 27 is so disposed as to define within chamber 19' an inlet plenum zone 28 and an outlet plenum zone 29 which is separated from inlet plenum zone 28.
- Plenum zone28 communicates with an inlet.
- Plenum zone 29 thus serves to' collect and deliver to outlet conduit 32 the gaseous and vapor products from the sample for exit from chamber 19.
- Plenum zone 28 is used for preheating the sample by packing 27 without contact therewith.
- Pump 17 is selected and operated so as to deliver into chamber 19 several times the stoichiometric volume of air required for complete oxidation of the maximum anticipated carbon content of the sample.
- a plurality of electric heater elements 33 Disposed outside chamber 19 in surrounding spaced relation thereto are a plurality of electric heater elements 33 that are used to heat the chamber 19 and quartz packing 27 to a temperature of approximately 850C. At such temperature, and with a mass of packing 27 that occupies at least 50 percent of the volume of chamber 19, the sample is preheated to vaporization almost immediately upon entering plenum zone 28, for
- sample feed rates up to about 2 percent per minute of the plenum zone 28 volume.
- plenum zone 28 vaporization of an aqueous sample was achieved at a sample feed rate of 4cc/minute into chamber 19 having a plenum zone 28 volume of 500 cc and a total volume of 2,660 cc of which 1,660 cc was occupied by quartz packing 27.
- the sample is converted to a mixture of vapor and suspended solids which then pass the inert packing 27 in heat exchange flow contact therewith, and the organic carbon content of the mixture is completely oxidized to carbon dioxide before passing through plate 26 into the outlet plenum zone 29 at the opposite-end of chamber 19.
- thermocouple well 34 into which can be inserted a standard thermocouple, not shown
- an analytical apparatus for determining the total quantity. of organic carbon as a pollutant in anaqueous stream by vaporizing a sample taken from the stream and oxidizing to carbon dioxide the total organic cardisposed to deliver into said mixing chamber a continuous flow of liquid reagent for reaction therein with the sample to remove the inorganic carbr on content thereof as carbon dioxide; a reaction chamber, means connected to said mixing chamber and to said reaction chamber to deliver from said mixing chamber into said reaction chamber a continuous flow aqueous sample to be analyzed and which is substantially free of inorganic carbon and carbon dioxide, said reaction chamber having an inlet for introducing the aqueous sample to be analyzed andan outlet for the exitof gaseous and vapor products formed from such sample, means for introducing air into said reaction chamber to establish an oxidizing atmosphere therein, a packing material disposed within said reaction chamber for heating the sample introduced, and means for heating said packing material to a temperature at which the organic carbon in the sample is oxidized to carbon dioxide by said atmosphere, said packing material being
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- Physics & Mathematics (AREA)
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- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
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Abstract
Apparatus for determining the organic carbon content of a liquid sample whereby the sample is acidified and scrubbed to remove its inorganic carbon content, and then vaporized in a reaction chamber having an air atmosphere which oxidizes to carbon dioxide the total organic carbon content of the sample. Measurement of the amount of carbon dioxide formed from the organic carbon is effected by an infrared analyzer.
Description
United States Patent Cohen Dec. 17, 1974 APPARATUS FOR DETERMINING ORGANIC CARBON CONTENT OF POLLUTED LIQUIDS Alfred Cohen, 71 Joyce Ln., Woodbury, N.Y. 11797 [22] Filed: Sept. 13, 1971 [21] App1.No.: 179,964
[76] Inventor:
3,205,045 9/1965 Von Lossberg 23/230 PC X 3,296,435 1/1967 Teal et a1 23/230 PC X 3,322,504 5/1967 Capuano 23/230 PC 3,523,763 8/1970 Van Driesen et al 23/284 X 3,607,071 9/1971 Staffin et a1. 7. 23/230 PC Primary ExaminerRobert M. Reese 57 ABSTRACT Apparatus for determining the organic carbon content of a liquid sample whereby the sample is acidified and scrubbed to remove its inorganic carbon content, andthen vaporized in a reaction chamber having an air atmosphere which oxidizes to carbon dioxide the total organic carbon content of the sample. Measurement of the amount of carbon dioxide formed from the organic carbon is effected by an infrared analyzer.
5 Claims, 3 Drawing Figures HYDROCHLORIC r ACID E PSQ 15 REsERvoIR LIQUID METERING MIXING Il SOURCE PUMP CHAMBER CO2 VIiNT GAS A1R\ 1O SCRUBBER AIR METERING I71 55% PUMP Ia REAcTIoN CHAMBER -19 22\ 21\ gxgfi INFRARED GAs-LlQllg R A A RECORDER ANALYZE GAS SEP R T sum 1 a; 2
METERING PUMP METERING PUMP ACID RESERVOIR LHYDROCHLORIC GAS SCRUBBER AIR METERING PUMP REAcTloN CHAMBER 1 CO2 VENT AIR GAS-LIQUID (3A5 SEPARATOR INFRARED ANALYZER MOVING CHART RECORDER INVENTOR. ,Alfred Cohen AT T O RNE Y APPARATUS FOR DETERMINING ORGANIC CARBON CONTENT OF POLLUTED LIQUIDS BACKGROUND AND SUMMARY OF THE INVENTION In the measurement of pollution levels in aqueous systems, the amount of organic carbon in a sample taken from the liquid source to be monitored is an imp'ortant index of the existing pollution level.
Accordingly, there is a need for equipment and methods that enable rapid and accurate determination of the organic carbon content of a liquid on a continuous or quasi-continuous sampling basis. One rather elaborate apparatus for total carbon analysis is described in US. Pat. No. 3,296,435 issued on Jan. 3, 1967 to J. L. Teal et al.
The invention provides an improved apparatus and a method for performing total organic carbon analyses more efficiently and rapidly than can be done with either the standard laboratory five-day biochemicaloxygen demand test B O D or the two-hour chemical oxygen demand test, C O D I In the analytical apparatus of the invention, a sample stream from the aqueous liquid source to be monitored is continuously fed into a mixing chamber together with sufficient acid to react with and remove as carbon dioxide all of the inorganic carbon content of the sample, i.e. the carbonates in the sample. The acidified sample is scrubbed to remove all carbon dioxide produced by the carbonate-acid reaction, and the carbonate-free sample is metered into a reaction chamber. The reaction chamber has an inlet through which the sample and air for oxidizing the organic carbon of the sample are introduced; an outlet for the exit of gaseous and vapor products formed from the sample; and a granular packing material inside that is heated by electric resistor elements disposed outside the chamber in surrounding relation thereto. This packing material is chemically inert, as for example, crushed quartz, and is heated to a temperature at which the organic carbon in the sample is oxidized to carbon dioxide by the air atmosphere in the chamber.
Clogging of the reaction chamber by solids deposited upon the packing material is minimized through a,spe cial arrangement of the packing material-with respect to the chamber boundaries. In accordance with the invention, the packing material is disposed to define within the reaction chamber an inlet plenum zone communicating with the inlet to accommodate preheating of the sample by the packing material without contact therewith; and an outlet plenum zone. The outlet plenum zone is separated from the inlet plenum zone and communicates with the outlet to collect and deliver thereto the gaseous and vapor products of the sample.
- water vapor portion of the reaction chamber effluent is expediently removed by a conventional gas-liquid sepa- BRIEF DESCRIPTION OF THE DRAWING In the drawing:
FIG. 1 is a schematic diagram of an organic carbon content analyzer apparatus according to a preferred embodiment of the invention.
- FIG. 2 is an elevation view, partly in section, of the reaction chamber used in the apparatus represented by' FIG. 1, as seen in a typical installation arranged for external heating of the reactionchamber and packing ma-' terial therein.
FIG. 3. is aplan view of the reaction chamber and heating installation shown in FIG. 2.
DESCRIPTION OF A PREFERRED EMBODIMENT OF THE INVENTION In FIG. I there is schematically exemplified an analyzer apparatus 10 constructed in accordance with the invention and which isoperable to measure, on a continuous flow basis, the total organic carbon content in a sample stream taken from an aqueous liquid source 11, such as a body of water to be monitored for'pollution level.
A continuous sample stream from source 11 is deliv-. ered by a metering pump 12 into a mixing chamber 13. Another metering pump 14 delivers hydrochloric acid from a reservoir 15 into mixing chamber I3 for the purpose of acidifying the liquid sample therein to a pH of approximately 2.0. The inorganic carbon present in the sample as carbonates is converted to carbon dioxide by reaction with the acid, and the organic carbon content of the sample is substantially unchanged.
' The acidified samplestream is expediently fed into a conventional gas scrubber l6'that is supplied with air from a pump 17 to purge from the sample whatever carbon dioxide was formed by the acidification reaction. This carbon dioxide, which corresponds quantitatively to theamount of carbonates in the sample, is by choice vented to a waste zone, but could be delivered to a measuring means not shown should it be desired to measure the amount of inorganic carbon in the sample.
The carbonate-free sample is fed by a metering pump 18 from scrubber 16 into a heated reaction chamber This hot oxidizing atmosphere rapidly vaporizes the .sample and oxidizes the organic carbon content thereof to carbon dioxide.
, 'The vapor and gaseous mixture effluent of reaction chamber 19 is delivered to a conventional gas-liquid separator 20 that removes by condensation the vapor component of the mixture and passes the gaseous portion containing the carbon dioxide to an infrared analyzer 21.
' For calibration purposes, the inlet of metering pump 12 can be diverted temporarily from source 11 to another source, not shown of liquid having a known concentration of organic carbon sufficiently constant as to be useable as a standard. The gas mixture output of separator 20 can be applied to an oxygen demand analyzer, not shown instead of to the infra-red analyzer 21 where it is desired to measure the oxygen demand level of the sample.
While other means could be employed for effecting oxidation of the organic carbon content to carbon dioxide, the reaction chamber 19, shown in specific detail by FIGS. 2 and 3 offers definite improvements andadvantages over prior art counterparts. The Chamber 19 has a peripheral wall 23 joined to a top cover 24 andv a bottom cover 25 so as to form-a sealed enclosure.
Within'chamber 19 is an apertured plate 26 which serves to retain a quantity of crushed quartz material 27.
Disposed outside chamber 19 in surrounding spaced relation thereto are a plurality of electric heater elements 33 that are used to heat the chamber 19 and quartz packing 27 to a temperature of approximately 850C. At such temperature, and with a mass of packing 27 that occupies at least 50 percent of the volume of chamber 19, the sample is preheated to vaporization almost immediately upon entering plenum zone 28, for
sample feed rates up to about 2 percent per minute of the plenum zone 28 volume.
For example, at a packing 27 temperature of 850C, plenum zone 28 vaporization of an aqueous sample was achieved at a sample feed rate of 4cc/minute into chamber 19 having a plenum zone 28 volume of 500 cc and a total volume of 2,660 cc of which 1,660 cc was occupied by quartz packing 27.
With the plenum zone vaporization afforded by the zation compaction of the packing 27.
In plenum zone 28, the sample is converted to a mixture of vapor and suspended solids which then pass the inert packing 27 in heat exchange flow contact therewith, and the organic carbon content of the mixture is completely oxidized to carbon dioxide before passing through plate 26 into the outlet plenum zone 29 at the opposite-end of chamber 19.
.To aid in controlling the temperature of the packing 27 there is provided in chamber 19 a thermocouple well 34, into which can be inserted a standard thermocouple, not shown From the foregoing description it will become apparent to the artisan that the invention is adaptable to many specific applications where the carbon content of liquids must be monitored, and that obvious changes in the exemplified apparatus can ticular requirements. What is claimedis:
be made to satisfy par- I In an analytical apparatus for determining the total quantity. of organic carbon as a pollutant in anaqueous stream by vaporizing a sample taken from the stream and oxidizing to carbon dioxide the total organic cardisposed to deliver into said mixing chamber a continuous flow of liquid reagent for reaction therein with the sample to remove the inorganic carbr on content thereof as carbon dioxide; a reaction chamber, means connected to said mixing chamber and to said reaction chamber to deliver from said mixing chamber into said reaction chamber a continuous flow aqueous sample to be analyzed and which is substantially free of inorganic carbon and carbon dioxide, said reaction chamber having an inlet for introducing the aqueous sample to be analyzed andan outlet for the exitof gaseous and vapor products formed from such sample, means for introducing air into said reaction chamber to establish an oxidizing atmosphere therein, a packing material disposed within said reaction chamber for heating the sample introduced, and means for heating said packing material to a temperature at which the organic carbon in the sample is oxidized to carbon dioxide by said atmosphere, said packing material being disposed to defor introducing air therethrough along with the sample.
3. The improvement according to claim 1 wherein the means for heating said packing material is disposed v outside the reaction chamber.
4. The improvement according to claim 1 wherein said packing material is crushed quartz and occupies at least 50 percent of the reaction chamber volume.
products of the sample.
Claims (5)
1. IN AN ANALYTICAL APPARATUS FOR DETERMINING THE TOTAL QUANTITY OF ORGANIC CARBON AS A POLUTAN IN AN AQUEOUS STREAM BY VAPORIZING A SAMPLE TAKEN FROM THE STREAM AND OXIDIZING TO CARBON DIOXIDE THE TOTAL ORGANIC CARBON IN THE SAMPLE, THE DETERMINATION BEI*G ON THE BASIS OF THE MEASURE OF CARBON DIOXIDE FORMED PER UNIT MEASURE OF THE SAMPLE, THE IMPROVEMENT WHICH COMPRISES A MIXING CHAMBER, A FIRST METERING PUMP DISPOSED TO DELIVER INTO SAID MIXING CHAMBER A CONTINUOUS FLOW SAMPLE TAKEN FROM THE STREAM, A SECOND METERING PUMP DISPOSED TO DELIVER INTO SAID MIXING CHAMBER, A CONTINUOUS FLOW OF LIQUID REAGENT FOR REACTION THEREIN WITH THE SAMPLE TO REMOVE THE INORGANIC CARBON CONTENT THEREOF AS CARBON DIOXIDE; A REACTION CHARMBER, MEANS CONNECTED TO SAID MIXING CHAMBER AND TO SAID REACTION CHAMBER TO DELIVER FROM SAID MIXING CHAMBER INTO SAID REACTION CHAMBER A CONTINUOUS FLOW AQUEOUS SAMPLE TO BE ANALYZED AND WHICH IS SUBSTANTIALLY FREE OF INORGANIC CARBON AND CARBON DIOXIDE, SAID REACTION CHAMBER HAVING AN INLET FOR INTRODUCING THE AQUEOUS SAMPLE TO BE ANALYZED AND AN OUTLET FOR THE EXIT OF GASEOUS AND VAPOR PRODUCTS FORMED FROM SUCH SAMPLE, MEANS FOR INTRODUCING AIR INTO SAID REACTION CHAMBER TO ESTABLISH AN OXIDIZING ATMOSPHERE THEREIN, A PACKING MTERIAL DISPOSED WITHIN SAID REACTION CHAMBER FOR HEATING THE SAMPLE INTRODUCED, AND MEANS FOR HEATING SAID PACKING MATERIAL TO A TEMPERATURE AT WHICH THE ORGANIC CARBON IN THE SAMPLE IS OXIDIZED TO CARBON DIOXIDE BY SAID ATMOSPHERE, SAID PACKING MATERIAL BEING DISPOSED TO DEFINE WITHIN THE EACTION CHAMBER AN INLET PLENUM ZONE
2. The improvement according to claim 1 including a conduit extending outside the reaction chamber and communicating with an air supply means and said inlet for introducing air therethrough along with the sample.
3. The improvement according to claim 1 wherein the means for heating said packing material is disposed outside the reaction chamber.
4. The improvement according to claim 1 wherein said packing material is crushed quartz and occupies at least 50 percent of the reaction chamber volume.
5. The improvement according to claim 1 wherein said inlet plenum zone is at one end of the reaction chamber and said outlet plenum zone is at the opposite end of the reaction chamber, and said packing material contains voids accommodating the flow therethrough to the outlet plenum zone of the gaseous and vapor products of the sample.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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US00179964A US3854881A (en) | 1971-09-13 | 1971-09-13 | Apparatus for determining organic carbon content of polluted liquids |
US05/533,247 US4023932A (en) | 1971-09-13 | 1974-12-16 | Reactor for analysis of polluted liquids |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US00179964A US3854881A (en) | 1971-09-13 | 1971-09-13 | Apparatus for determining organic carbon content of polluted liquids |
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US05/533,247 Continuation-In-Part US4023932A (en) | 1971-09-13 | 1974-12-16 | Reactor for analysis of polluted liquids |
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US00179964A Expired - Lifetime US3854881A (en) | 1971-09-13 | 1971-09-13 | Apparatus for determining organic carbon content of polluted liquids |
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Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2287042A1 (en) * | 1974-10-04 | 1976-04-30 | Envirotech Corp | GAS SPRAYING DEVICE FOR DETERMINING THE ORGANIC CARBON CONTENT |
US3964868A (en) * | 1974-05-24 | 1976-06-22 | Raytheon Company | Organic carbon analyzer system |
US4032296A (en) * | 1973-12-17 | 1977-06-28 | Purdue Research Foundation | Electrolytic conductivity detector system |
US4078894A (en) * | 1976-11-12 | 1978-03-14 | Raytheon Company | Analyzer system with salt extractor |
US4273558A (en) * | 1980-03-07 | 1981-06-16 | Envirotech Corporation | Determination of total organic carbon in an aqueous sample containing halide ion |
US4288229A (en) * | 1980-03-07 | 1981-09-08 | Envirotech Corporation | Determination of total organic carbon in a plurality of aqueous samples containing halide ion |
EP0046178A2 (en) * | 1980-08-20 | 1982-02-24 | The Perkin-Elmer Corporation | Apparatus useful in determining organic carbon content of a sample |
US4529427A (en) * | 1977-05-19 | 1985-07-16 | At&T Bell Laboratories | Method for making low-loss optical waveguides on an industrial scale |
DE3511687A1 (en) * | 1984-03-30 | 1985-10-03 | Hitachi, Ltd., Tokio/Tokyo | Apparatus and method for determining organic carbon in water |
US4775634A (en) * | 1986-08-06 | 1988-10-04 | Servomex Company | Method and apparatus for measuring dissolved organic carbon in a water sample |
EP0401648A1 (en) * | 1989-06-05 | 1990-12-12 | CARLO ERBA STRUMENTAZIONE S.p.A. | Process and equipment for the determination of organic carbon content in complex matrixes |
US5194814A (en) * | 1991-05-22 | 1993-03-16 | Tremetrics, Inc. | Electrolytic conductivity detector |
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US20200173968A1 (en) * | 2018-11-29 | 2020-06-04 | Nanjing University | Organic Carbon Detector for Liquid Chromatography and Use Thereof |
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US4032296A (en) * | 1973-12-17 | 1977-06-28 | Purdue Research Foundation | Electrolytic conductivity detector system |
US3964868A (en) * | 1974-05-24 | 1976-06-22 | Raytheon Company | Organic carbon analyzer system |
US4095951A (en) * | 1974-05-24 | 1978-06-20 | Raytheon Company | Organic carbon analyzer system |
FR2287042A1 (en) * | 1974-10-04 | 1976-04-30 | Envirotech Corp | GAS SPRAYING DEVICE FOR DETERMINING THE ORGANIC CARBON CONTENT |
US4078894A (en) * | 1976-11-12 | 1978-03-14 | Raytheon Company | Analyzer system with salt extractor |
US4529427A (en) * | 1977-05-19 | 1985-07-16 | At&T Bell Laboratories | Method for making low-loss optical waveguides on an industrial scale |
US4288229A (en) * | 1980-03-07 | 1981-09-08 | Envirotech Corporation | Determination of total organic carbon in a plurality of aqueous samples containing halide ion |
US4273558A (en) * | 1980-03-07 | 1981-06-16 | Envirotech Corporation | Determination of total organic carbon in an aqueous sample containing halide ion |
EP0046178A2 (en) * | 1980-08-20 | 1982-02-24 | The Perkin-Elmer Corporation | Apparatus useful in determining organic carbon content of a sample |
EP0046178A3 (en) * | 1980-08-20 | 1984-07-04 | The Perkin-Elmer Corporation | Apparatus useful in determining organic carbon content of a sample |
DE3511687A1 (en) * | 1984-03-30 | 1985-10-03 | Hitachi, Ltd., Tokio/Tokyo | Apparatus and method for determining organic carbon in water |
US4775634A (en) * | 1986-08-06 | 1988-10-04 | Servomex Company | Method and apparatus for measuring dissolved organic carbon in a water sample |
US5473162A (en) * | 1987-10-26 | 1995-12-05 | Baylor University | Infrared emission detection of a gas |
US5246868A (en) * | 1987-10-26 | 1993-09-21 | Research Corporation Technologies, Inc. | Infrared emission detection |
EP0401648A1 (en) * | 1989-06-05 | 1990-12-12 | CARLO ERBA STRUMENTAZIONE S.p.A. | Process and equipment for the determination of organic carbon content in complex matrixes |
US5443991A (en) * | 1990-03-02 | 1995-08-22 | Sievers Instruments, Inc. | Method for the determination of dissolved carbon in water |
US5194814A (en) * | 1991-05-22 | 1993-03-16 | Tremetrics, Inc. | Electrolytic conductivity detector |
US5312756A (en) * | 1991-07-15 | 1994-05-17 | Umpqua Research Company | Total organic carbon (TOC) and total inorganic carbon (TIC) calibration system |
US5476637A (en) * | 1992-04-09 | 1995-12-19 | Hans-Dieter Schultz | Method and device for the, measurement of impurities in a liquid more particularly water |
US6149880A (en) * | 1996-06-04 | 2000-11-21 | Ebara Corporation | Method and apparatus for treating aqueous medium containing organic matter |
US20020020113A1 (en) * | 1997-12-01 | 2002-02-21 | The Board Of Trustees Of The University Of | Superadiabatic generation of hydrogen and hydrocarbons |
US6653142B1 (en) | 1998-05-09 | 2003-11-25 | Henkel Kommanditgesellschaft Auf Aktien (Henkel Kgaa) | Automatic determination of the contamination of aqueous cleaning solutions with carbonaceous compounds |
WO1999058969A3 (en) * | 1998-05-09 | 2001-10-11 | Henkel Kgaa | Automatic determination of the contamination of aqueous cleaning solutions with carbonaceous compounds |
WO1999058969A2 (en) * | 1998-05-09 | 1999-11-18 | Henkel Kommanditgesellschaft Auf Aktien | Automatic determination of the contamination of aqueous cleaning solutions with carbonaceous compounds |
US20030049854A1 (en) * | 2001-09-11 | 2003-03-13 | Rhodes John R. | Method and apparatus for the on-stream analysis of total sulfur and/or nitrogen in petroleum products |
US6830730B2 (en) * | 2001-09-11 | 2004-12-14 | Spectrolanalytical Instruments | Method and apparatus for the on-stream analysis of total sulfur and/or nitrogen in petroleum products |
WO2012129734A1 (en) * | 2011-04-01 | 2012-10-04 | General Electric Company | Method and apparatus for carbon dioxide removal in aqueous sample by in-vial sparging for toc measurement |
CN110621991A (en) * | 2017-07-29 | 2019-12-27 | 哈希公司 | SP3 substituted carbon electrode TOC analysis using metal catalysts |
US10724984B2 (en) * | 2017-07-29 | 2020-07-28 | Hach Company | SP3 substituted carbon electrode TOC analysis using metallic catalyst |
EP3615927B1 (en) * | 2017-07-29 | 2020-12-16 | Hach Company | Sp3 substituted carbon electrode toc analysis using metallic catalyst |
EP3809129A3 (en) * | 2017-07-29 | 2021-05-19 | Hach Company | A total organic carbon analyzer |
US20200173968A1 (en) * | 2018-11-29 | 2020-06-04 | Nanjing University | Organic Carbon Detector for Liquid Chromatography and Use Thereof |
US11567043B2 (en) * | 2018-11-29 | 2023-01-31 | Nanjing University | Organic carbon detector for liquid chromatography and use thereof |
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