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US3840341A Expired / Lapsed US ⏱️ 0.0 years remaining

Organic carbon method and analyzer

Assignee: Veolia WTS Systems USA Inc
•
Filing: 1972-03-03
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Granted: 1974-10-08
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Expires: 1992-03-03
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Abstract

Abstract An improved apparatus and method for the automatic determination of total organic carbon in aqueous media. The invention comprises two sample injection valves, two reaction chambers, one for converting all carbon (both organic and inorganic) in the sample to carbon dioxide, the other for converting only the inorganic carbon to carbon dioxide, a methanizer for converting the formed carbon dioxide to methane and a flame ionization detector for measuring the quantity of the methane produced which corresponds to the total and the inorganic carbon content of the sample, the difference between these two values being the organic carbon content.

Inventors

  • 👤 L Rogers

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 08:09
CPC Classifications
G; G01; G01N; G01N33/00; G01N33/18; G01N33/1826; G01N33/1846; Y; Y10; Y10T; Y10T436/00; Y10T436/20; Y10T436/204998; Y10T436/21; Y10T436/214; Y10T436/23; Y10T436/235

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 286 words
APPARATUS FOR THE AUTOMATIC DETERMINATION OF TOTAL ORGANIC CARBON IN AN AQUEOUS SOLUTION COMPRISING IN COMBINATION A CARRIER GAS SUPPLY SOURCE, A HYDROGEN GAS SUPPLY SOURCE A FIRST AUTOMATIC INJECTION MEANS FOR INTRODUCING A FIRST REACTIO OUS SOLUTION SAMPLE AND SAID CARRIER GAS TO A FIRST REACTION CHAMBER CONTAINING A CATALYTICALLY ACTIVE BODY FOR PRODUCING CARBON DIOXIDE FROM THE WATER AND THE TOTAL CARBON CONTENT OF SAID AQUEOUS SOLUTION, SECOND AUTOMATIC INJECTION MEANS FOR INTRODUCING A SECOND AQUEOUS SOLUTION SAMPLE AND SAID CARRIER GAS TO A SECOND REACTION CHAMBER CONTAINING A CATALYTICALLY ACTIVE BODY FOR PRODUCING CARBON DIOXIDE FROM THE WATER AND THE INORGANIC CARBON CONTENT OF SAID AQUEOUS SOLUTION, MEANS FOR HEATING SAID FIRST AND SECOND REACTION CHAMBERS, MEANS FOR SEPARATELY PASSING EACH OF SAID REACTION CHAMBER''S EFFLUENT GASEOUS PRODUCTS AND HYDROGEN GAS INTO A METHANIZER CHAMBER CONTAINING A CATALYTICALLY ACTIVE NICKEL BODY FOR PRODUCING METHANE BY THE REDUCTION OF CARBON DIOXIDE IN THE PRESENCE OF HYDROGEN, HEATING MEANS LOCATED UPSTREAM TO THE ENTRANCE OF SAID METHANIZER CHAMBER FOR PREHEATING EACH OF THE SAID EFFLUENT GASEOUS STREAMS PRIOR TO THEIR ENTERING INTO SAID METHANIZER CHAMBER TO A TEMPERATURE SUFFICIENT TO SUBSTANTIALLY MAINTAIN LIQUID WATER THEREIN IN A VAPOR STATE MEANS FOR HEATING SAID METHANIZER CHAMBER, PASSAGE MEANS FROM SAID METHANIZER CHAMBER TO DETECTION MEANS SENSITIZED TO BE RESPONSIVE TO METHANE AND TO PRODUCE SEPARATE INDICIA REPRESENTATIVE OF THE TOTAL CARBON AND INORGANIC CARBON CONTENT RESPECTIVELY OF SA IS ID FIRST AND SECOND SAMPLES, MEANS TO PROVIDE CONTINUOUS PASSAGE OF FLUIDS THROUGH THE APPARATUS COMPONENTS AND ELECTRONIC MEANS FOR AUTOMATICALLY DETERMINING THE DIFFERENCE BETWEEN SAID TWO SEPARATE CARBON INDICIA TO PRODUCE AN ADDITIONAL INDICIA DIRECTLY REPRESENTATIVE OF THE TOTAL ORGANIC CARBON CONTENT OF SAID AQUEOUS SOLUTION.
Claim 2
Dependent Claim 286 words
APPARATUS FOR THE AUTOMATIC DETERMINATION OF TOTAL ORGANIC CARBON IN AN AQUEOUS SOLUTION COMPRISING IN COMBINATION A CARRIER GAS SUPPLY SOURCE, A HYDROGEN GAS SUPPLY SOURCE A FIRST AUTOMATIC INJECTION MEANS FOR INTRODUCING A FIRST REACTIO OUS SOLUTION SAMPLE AND SAID CARRIER GAS TO A FIRST REACTION CHAMBER CONTAINING A CATALYTICALLY ACTIVE BODY FOR PRODUCING CARBON DIOXIDE FROM THE WATER AND THE TOTAL CARBON CONTENT OF SAID AQUEOUS SOLUTION, SECOND AUTOMATIC INJECTION MEANS FOR INTRODUCING A SECOND AQUEOUS SOLUTION SAMPLE AND SAID CARRIER GAS TO A SECOND REACTION CHAMBER CONTAINING A CATALYTICALLY ACTIVE BODY FOR PRODUCING CARBON DIOXIDE FROM THE WATER AND THE INORGANIC CARBON CONTENT OF SAID AQUEOUS SOLUTION, MEANS FOR HEATING SAID FIRST AND SECOND REACTION CHAMBERS, MEANS FOR SEPARATELY PASSING EACH OF SAID REACTION CHAMBER''S EFFLUENT GASEOUS PRODUCTS AND HYDROGEN GAS INTO A METHANIZER CHAMBER CONTAINING A CATALYTICALLY ACTIVE NICKEL BODY FOR PRODUCING METHANE BY THE REDUCTION OF CARBON DIOXIDE IN THE PRESENCE OF HYDROGEN, HEATING MEANS LOCATED UPSTREAM TO THE ENTRANCE OF SAID METHANIZER CHAMBER FOR PREHEATING EACH OF THE SAID EFFLUENT GASEOUS STREAMS PRIOR TO THEIR ENTERING INTO SAID METHANIZER CHAMBER TO A TEMPERATURE SUFFICIENT TO SUBSTANTIALLY MAINTAIN LIQUID WATER THEREIN IN A VAPOR STATE MEANS FOR HEATING SAID METHANIZER CHAMBER, PASSAGE MEANS FROM SAID METHANIZER CHAMBER TO DETECTION MEANS SENSITIZED TO BE RESPONSIVE TO METHANE AND TO PRODUCE SEPARATE INDICIA REPRESENTATIVE OF THE TOTAL CARBON AND INORGANIC CARBON CONTENT RESPECTIVELY OF SA IS ID FIRST AND SECOND SAMPLES, MEANS TO PROVIDE CONTINUOUS PASSAGE OF FLUIDS THROUGH THE APPARATUS COMPONENTS AND ELECTRONIC MEANS FOR AUTOMATICALLY DETERMINING THE DIFFERENCE BETWEEN SAID TWO SEPARATE CARBON INDICIA TO PRODUCE AN ADDITIONAL INDICIA DIRECTLY REPRESENTATIVE OF THE TOTAL ORGANIC CARBON CONTENT OF SAID AQUEOUS SOLUTION.
Claim 3
Dependent Claim 84 words
The apparatus according to claim 1 wherein said heating means located upstream of the entrance of the said methanizer chamber comprises heat exchange tubing carrying the gaseous stream to be heated, said tubing being in close proximity to an oven employed as the heating means for any of said reaction chambers whereby the heat from said oven is sufficient to substantially maintain any water in said heat exchange tubing in a vapor state prior to passage of the gaseous stream into said methanizer chamber.
Claim 4
Dependent Claim 14 words
Apparatus according to claim 1 wherein the detection means comprises a flame ionization detector.
Claim 5
Dependent Claim 37 words
Apparatus according to claim 1 wherein means are provided for the removal of condensated liquids from the gaseous products of said first or second reaction chamber prior to the entrance of said gases into said methanizer chamber.
Claim 6
Dependent Claim 35 words
Apparatus according to claim 1 wherein the catalytic active body in said second reaction chamber comprises a particulate solid having an acidic coAting thereon and wherein flushing means are provided for replenishing said acidic coating.
Claim 7
Independent Claim 262 words
A method for the automatic determination of total organic carbon in an aqueous solution comprising the combination of steps of introducing a first aqueous sample to be analyzed into a confined stream of a carrier gas, directing the resulting mixture of said first aqueous sample and carrier gas to contact a first reaction chamber heated catalytic active body capable of producing carbon dioxide from the water and total carbon content in said first aqueous sample, introducing a second aqueous sample to be analyzed into a confined stream of carrier gas, directing the resulting mixture of said second aqueous sample and carrier gas to contact a second reaction chamber heated catalytic active body capable of producing carbon dioxide from the water and inorganic carbon content in said second aqueous sample, separately directing the gaseous mixture of the products of each of the reaction chambers and hydrogen to contact a reduction chamber heated catalytic nickel body capable of producing methane by the reduction of carbon dioxide in the presence of hydrogen, each of said gaseous mixtures being heated prior to entering said reduction chamber to a temperature sufficient to substantially maintain liquid water therein in a vapor state, by flame ionization analyzing for the said methane content of each gaseous mixture and in so doing produce separate indicia representative of the total carbon present in the said first sample and the inorganic carbon present in the said second sample and thereafter automatically determining the difference between the total carbon and inorganic carbon to directly obtain the total organic carbon content of said aqueous solution.
Claim 8
Independent Claim 262 words
A method for the automatic determination of total organic carbon in an aqueous solution comprising the combination of steps of introducing a first aqueous sample to be analyzed into a confined stream of a carrier gas, directing the resulting mixture of said first aqueous sample and carrier gas to contact a first reaction chamber heated catalytic active body capable of producing carbon dioxide from the water and total carbon content in said first aqueous sample, introducing a second aqueous sample to be analyzed into a confined stream of carrier gas, directing the resulting mixture of said second aqueous sample and carrier gas to contact a second reaction chamber heated catalytic active body capable of producing carbon dioxide from the water and inorganic carbon content in said second aqueous sample, separately directing the gaseous mixture of the products of each of the reaction chambers and hydrogen to contact a reduction chamber heated catalytic nickel body capable of producing methane by the reduction of carbon dioxide in the presence of hydrogen, each of said gaseous mixtures being heated prior to entering said reduction chamber to a temperature sufficient to substantially maintain liquid water therein in a vapor state, by flame ionization analyzing for the said methane content of each gaseous mixture and in so doing produce separate indicia representative of the total carbon present in the said first sample and the inorganic carbon present in the said second sample and thereafter automatically determining the difference between the total carbon and inorganic carbon to directly obtain the total organic carbon content of said aqueous solution.
Claim 9
Dependent Claim 21 words
A method according to claim 6 wherein the carrier gas is selected from the group consisting of nitrogen, helium and argon.
Claim 10
Dependent Claim 32 words
A method according to claim 6 wherein the catalytic body in the reduction chamber is nickel adsorbed on fire brick and heated to a temperature between about 275* C. to 400* C.
Claim 11
Dependent Claim 45 words
A method according to claim 8 wherein the nickel catalyst is prevented from contacting liquid water by heating the said gaseous mixture stream prior to its entering said reduction chamber to a temperature sufficient to maintain any water of said stream in a vapor state.
Claim 12
Dependent Claim 23 words
A method according to claim 6 wherein an acidic washing fluid is employed for rinsing the said second reaction chamber''s heated catalytic body.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-10-07 1978-04-08 1978-10-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-10-07 1982-04-08 1982-10-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-10-07 1986-04-08 1986-10-08 $7700.00 Window Closed / Lapsed

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