CN106092947A - A kind of have multistage except total nitrogen analysis system of water purifying function - Google Patents
A kind of have multistage except total nitrogen analysis system of water purifying function Download PDFInfo
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- CN106092947A CN106092947A CN201610365012.3A CN201610365012A CN106092947A CN 106092947 A CN106092947 A CN 106092947A CN 201610365012 A CN201610365012 A CN 201610365012A CN 106092947 A CN106092947 A CN 106092947A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 178
- 229910001868 water Inorganic materials 0.000 title claims abstract description 178
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title claims abstract description 116
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 57
- 238000004458 analytical method Methods 0.000 title claims abstract description 37
- 239000007789 gas Substances 0.000 claims abstract description 98
- 230000009467 reduction Effects 0.000 claims abstract description 78
- 238000001514 detection method Methods 0.000 claims abstract description 67
- 238000012360 testing method Methods 0.000 claims abstract description 40
- 238000012545 processing Methods 0.000 claims abstract description 22
- 238000013500 data storage Methods 0.000 claims abstract description 10
- 230000002829 reductive effect Effects 0.000 claims abstract description 7
- 230000007246 mechanism Effects 0.000 claims description 152
- 238000000746 purification Methods 0.000 claims description 119
- 238000000034 method Methods 0.000 claims description 43
- 238000001816 cooling Methods 0.000 claims description 34
- 239000003463 adsorbent Substances 0.000 claims description 30
- 238000002485 combustion reaction Methods 0.000 claims description 25
- 239000011521 glass Substances 0.000 claims description 25
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical group O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims description 22
- 230000008569 process Effects 0.000 claims description 21
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Natural products O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 15
- 229910052736 halogen Inorganic materials 0.000 claims description 14
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 11
- 239000001569 carbon dioxide Substances 0.000 claims description 8
- -1 carbon dioxide halogen Chemical class 0.000 claims description 8
- 230000008054 signal transmission Effects 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 5
- 230000005611 electricity Effects 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 238000005303 weighing Methods 0.000 claims description 3
- 230000007812 deficiency Effects 0.000 abstract description 9
- 239000002253 acid Substances 0.000 abstract description 7
- 238000003912 environmental pollution Methods 0.000 abstract description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 abstract description 5
- 238000011017 operating method Methods 0.000 abstract description 5
- 239000012159 carrier gas Substances 0.000 description 13
- 230000008859 change Effects 0.000 description 12
- 230000000694 effects Effects 0.000 description 11
- 239000000047 product Substances 0.000 description 11
- 238000010521 absorption reaction Methods 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 9
- 229910052760 oxygen Inorganic materials 0.000 description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 8
- 210000004027 cell Anatomy 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 239000004065 semiconductor Substances 0.000 description 7
- 229960004424 carbon dioxide Drugs 0.000 description 6
- 150000002367 halogens Chemical class 0.000 description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 238000009833 condensation Methods 0.000 description 5
- 230000005494 condensation Effects 0.000 description 5
- 238000004146 energy storage Methods 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 4
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 239000001307 helium Substances 0.000 description 4
- 229910052734 helium Inorganic materials 0.000 description 4
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 4
- 238000009413 insulation Methods 0.000 description 4
- 239000010410 layer Substances 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 239000011241 protective layer Substances 0.000 description 4
- 230000004888 barrier function Effects 0.000 description 3
- 230000003139 buffering effect Effects 0.000 description 3
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- 238000005057 refrigeration Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000003595 spectral effect Effects 0.000 description 3
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 3
- 229910052721 tungsten Inorganic materials 0.000 description 3
- 239000010937 tungsten Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000000862 absorption spectrum Methods 0.000 description 2
- 150000003863 ammonium salts Chemical class 0.000 description 2
- 238000004380 ashing Methods 0.000 description 2
- 239000004202 carbamide Substances 0.000 description 2
- 235000013877 carbamide Nutrition 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000003818 cinder Substances 0.000 description 2
- 238000012937 correction Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
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- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 230000010355 oscillation Effects 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000004448 titration Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 244000061176 Nicotiana tabacum Species 0.000 description 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 1
- 230000005679 Peltier effect Effects 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 210000005056 cell body Anatomy 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 239000002989 correction material Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000005695 dehalogenation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000007323 disproportionation reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000001795 light effect Effects 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 230000036284 oxygen consumption Effects 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 229910052702 rhenium Inorganic materials 0.000 description 1
- WUAPFZMCVAUBPE-UHFFFAOYSA-N rhenium atom Chemical compound [Re] WUAPFZMCVAUBPE-UHFFFAOYSA-N 0.000 description 1
- 238000002133 sample digestion Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 230000005619 thermoelectricity Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N21/00—Investigating or analysing materials by the use of optical means, i.e. using sub-millimetre waves, infrared, visible or ultraviolet light
- G01N21/17—Systems in which incident light is modified in accordance with the properties of the material investigated
- G01N21/25—Colour; Spectral properties, i.e. comparison of effect of material on the light at two or more different wavelengths or wavelength bands
- G01N21/31—Investigating relative effect of material at wavelengths characteristic of specific elements or molecules, e.g. atomic absorption spectrometry
- G01N21/35—Investigating relative effect of material at wavelengths characteristic of specific elements or molecules, e.g. atomic absorption spectrometry using infrared light
- G01N21/3504—Investigating relative effect of material at wavelengths characteristic of specific elements or molecules, e.g. atomic absorption spectrometry using infrared light for analysing gases, e.g. multi-gas analysis
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/28—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
- G01N1/34—Purifying; Cleaning
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N25/00—Investigating or analyzing materials by the use of thermal means
- G01N25/20—Investigating or analyzing materials by the use of thermal means by investigating the development of heat, i.e. calorimetry, e.g. by measuring specific heat, by measuring thermal conductivity
- G01N25/22—Investigating or analyzing materials by the use of thermal means by investigating the development of heat, i.e. calorimetry, e.g. by measuring specific heat, by measuring thermal conductivity on combustion or catalytic oxidation, e.g. of components of gas mixtures
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/62—Detectors specially adapted therefor
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- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Pathology (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Engineering & Computer Science (AREA)
- Spectroscopy & Molecular Physics (AREA)
- Molecular Biology (AREA)
- Biomedical Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
Abstract
The invention discloses a kind of have multistage except total nitrogen analysis system of water purifying function, including sample introduction processing means；Burner, for the burning of testing sample, and produces mixed gas；Reduction apparatus, described reduction apparatus is connected with described burner so that described mixed gas is reduced in described reduction apparatus；Purifier, described purifier is connected with described reduction apparatus, to purify the mixed gas after reduction；Detection device, described detection device is connected with described purifier, to detect the nitrogen content in purified gas；Data storage, is connected with detection device and described sample introduction processing means, to store data respectively；Display device, is connected with detection device, the data message detected with reception, and shows.The present invention solves technological deficiencies such as using corrosivity soda acid, operating procedure length complicated, time-consuming and environmental pollution serious in prior art.
Description
Technical field
The invention belongs to detection technique field, particularly to a kind of have multistage except total nitrogen analysis system of water purifying function
System.
Background technology
The mensuration of full nitrogen/protein content is widely used in milk product, food, animal feed, corn, fertilizer, Nicotiana tabacum L., plants
The detection of the products such as thing, traditional detection means is Kjeldahl's method, and it as industrial standard executed for many years, but uses corrosion
Property soda acid, operating procedure length complicated, time-consuming and environmental pollution be the most difficult to meet the needs detecting development now.Specifically,
It is under conditions of having catalyst, with concentrated sulphuric acid sample digestion, organic nitrogen is all transformed into inorganic ammonium salt, then at alkalescence bar
Under part, ammonium salt is converted into ammonia, distillates and be the acid solution absorption of excess with steam, then with standard acidometric titration, thus calculate sample
Nitrogen content in product, the process that i.e. predominantly detects for clearing up → distill → titrate.Clear up with titration process the most manually,
Process is tired time-consuming again, and operator requiring, the probability that higher and error produces is bigger.The more important thing is, in digestion process
Strong acid need to be used, the safety of operator be there is also the biggest hidden danger, and time-consumingly length, workload greatly, make detection efficiency relatively low,
The needs of coherent detection unit can not be met far away.
Summary of the invention
The present invention provides a kind of and has multistage except total nitrogen analysis system of water purifying function, solves or part solves existing
There is in technology technological deficiencies such as using corrosivity soda acid, operating procedure length complicated, time-consuming and environmental pollution serious.
According to one aspect of the present invention, it is provided that a kind of have multistage except total nitrogen analysis system of water purifying function, bag
Include: burner, for the burning of testing sample, and produce mixed gas；Water trap, described water trap and described burning
Device connects, for removing the moisture in the mixed gas produced after described burner burns；Wherein, described except water dress
Put and include: one-level water removal body；Two grades of water removal bodies, described one-level water removal body and described two grades of water removal bodies are in parallel, and
One end after parallel connection is connected with described burner, with the mixed gas produced after receiving the burning of described burner；Three grades are removed
Water mechanism, described third class de-watering mechanism with in parallel after described one-level water removal body and described two grades of water removal bodies the other end even
Connect so that described third class de-watering mechanism is in series with described one-level water removal body, two grades of water removal bodies respectively, with by described three
Level water removal body receives the mixed gas after described one-level water removal body and described two grades of water removal bodies process except water；Reduction
Device, described reduction apparatus is connected with described third class de-watering mechanism so that from described third class de-watering mechanism out after gaseous mixture
Body is reduced in described reduction apparatus；Purifier, described purifier is connected with described reduction apparatus, after to reduction
Mixed gas purifies；Wherein, described purifier includes: first class purification mechanism；Secondary purification mechanism；Described first class purification
Mechanism and described secondary purification mechanism are in parallel, and the one end after parallel connection is connected with described reduction apparatus, to receive described reduction
The mixed gas produced after device burning；Three grades of purification mechanisms, described three grades of purification mechanisms with in parallel after described first class purification
The other end of mechanism and described secondary purification mechanism connects so that described three grades of purification mechanisms respectively with described first class purification machine
Structure, secondary purification mechanism are in series, to be received through described first class purification mechanism and described two by described three grades of purification mechanisms
Gas after level purification mechanism purified treatment；Detection device, described detection device is connected with described purifier, after to purifying
Gas in nitrogen content detect；Display device, described display device is connected with described detection device and carries out signal biography
Pass, to receive the data message that described detection device is detected, and described data message is shown；Sample introduction processing means,
Process for described testing sample being entered the sample introduction of early stage；And described burner is fitted vertically and processes in described sample introduction
The top of device so that the described testing sample after the sample introduction of early stage processes, by described sample introduction processing means, is admitted to
Described burner burns；Wherein, described sample introduction processing means at least includes an electronic weigher, to treat test sample to described
Product are weighed；Data storage, described data storage is connected with described detection device and described electronic weigher respectively, makes
The data message that detected of described detection device, described electronic weigher weigh the weight data transmission of gained to described data
Memorizer stores.
Optional: described burner is that temperature controls the combustion furnace at 1100 DEG C；And described combustion furnace includes: body of heater,
Described testing sample is burnt at described furnace interior；Electron electric power device, is connected with described body of heater, for described body of heater
The temperature environment of 1100 DEG C is provided, so that the fully oxidized burning in described body of heater of described testing sample；Heating element heater, described
Heating element heater is arranged on the inwall of described body of heater uniformly, makes the temperature of the inside of described body of heater uniformly divide in described body of heater
Cloth.
Optional: described sample introduction processing means also includes: at least one sampler, takes in vertical direction described in each
Sample device is respectively positioned on the lower section of described burner；The crucible suitable with described sampler quantity, each described crucible is corresponding
Ground is fixed on a described sampler, and is at least placed with described testing sample in a described crucible；Mechanical arm, is arranged
Having the lever arm suitable with described sampler quantity, on each lever arm, correspondence fixes a described sampler, to pass through
The knee-action of described lever arm drives corresponding described sampler to move up and down, and then promotes the most described crucible to enter institute
State in burner；Power source, described power source is connected with described mechanical arm, thinks the fortune of lever arm described in described mechanical arm
Dynamic offer power.
Optional: described reduction apparatus includes: diverter, described diverter connects with described third class de-watering mechanism,
So that the mixed gas transferred out by described third class de-watering mechanism is shunted；Reduction furnace, described reduction furnace respectively with described point
Stream device is connected with described detection device, to reduce the gas after shunting, and the gas after reduction is sent into described detection
Device detects.
Optional: described reduction apparatus also includes: sensor, described sensor is arranged on described reduction furnace and described detection
Between device.
Optional: described first class purification mechanism includes: the first adsorber and the second adsorber；Described first adsorber is respectively
It is connected with described reduction apparatus and described second adsorber；And, described secondary purification mechanism includes: the 3rd adsorber and the 4th is inhaled
Adnexa；Described 3rd adsorber is connected with described reduction apparatus and described 4th adsorber respectively；And, described three grades of purification mechanisms
Including: the 5th adsorber and the 6th adsorber；Described 5th adsorber is connected with described second adsorber respectively, described 4th suction
Adnexa and described 6th adsorber connect, and described 6th adsorber is connected with described detection device.
Optional: described first adsorber is sulfur dioxide/carbon dioxide halogen adsorber；Described second adsorber is water
Adsorber；And/or, described 3rd adsorber is sulfur dioxide/carbon dioxide halogen adsorber；Described 4th adsorber is that water is inhaled
Adnexa；And/or, described 5th adsorber is sulfur dioxide/carbon dioxide halogen adsorber；Described 6th adsorber is water absorption
Device.
Optional: described detection device includes: TCD thermal conductivity detector (TCD)；Mass flowmenter；Wherein, described TCD Thermal Conductivity
Device is connected with described purifier and described mass flowmenter respectively；And described TCD thermal conductivity detector (TCD) and described mass flowmenter
It is connected with described display device respectively, carries out signal transmission.
Optional: described one-level water removal body includes: the first glass physical condenser, the first electronic cooling dehydrater and
One adsorbent；Described first glass physical condenser connects with described burner and described first electronic cooling dehydrater respectively
Connect；Described first adsorbent is connected with described first electronic cooling dehydrater；And, described two grades of water removal bodies include: the second glass
Glass physical cold condenser, the second electronic cooling dehydrater and the second adsorbent；Described second glass physical condenser is respectively with described
Burner and described second electronic cooling dehydrater connect；Described second adsorbent is with described second electronic cooling dehydrater even
Connect；And, described third class de-watering mechanism includes: the 3rd glass physical condenser, the 3rd electronic cooling dehydrater and the 3rd adsorbent；
Described 3rd glass physical condenser removes with described first adsorbent, described second adsorbent and described 3rd electronic cooling respectively
Hydrophone connects；Described 3rd electronic cooling dehydrater and described 3rd adsorbent connect；Described 3rd adsorbent and described reduction
Device connects.
Optional: described display device includes: power supply source；Display end, described display end is connected with described power supply source, with logical
Cross described power supply source described display end is powered in real time, and described display end carries out signal transmission with described detection device.
What the embodiment of the present invention provided a kind of has multistage except total nitrogen analysis system of water purifying function, at least includes sample introduction
Processing means, burner, reduction apparatus, purifier, detection device, data storage and display device.Wherein, enter described in
Sample processing means is connected with described burner, sample to be carried out sample introduction process, and described burner and described reduction apparatus
Connect so that testing sample fully burns in described burner, and produces mixed gas.Reduction apparatus fills with purifying simultaneously
Put connection so that produced mixed gas is purified through a series of control techniquess in purifier.Realize final purification
After gas in comprise only purity nitrogen molecule, and described purifier is connected with described detection device so that in purified gas
The content of nitrogen, is detected by described detection device.Certainly, the present invention by by data storage respectively with sample introduction processing means and
Detection device connects, and to store measured data, and is connected with detection device by display device, with to detection knot
Fruit shows in real time.In the embodiment of the present invention, by least the above device constitute described in have multistage except water purifying function
Total nitrogen analysis system, instead of use corrosivity soda acid, the operating procedure using Kjeldahl's method in conventional art and cause numerous
Multiple, time-consuming long and that environmental pollution is serious technological deficiency.
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to institute in embodiment
The accompanying drawing used is needed to be briefly described, it should be apparent that, the accompanying drawing in describing below is only some enforcements of the present invention
Example, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtains according to these accompanying drawings
Obtain other accompanying drawing.
The structural representation frame with multistage total nitrogen analysis system except water purifying function that Fig. 1 provides for the embodiment of the present invention
Figure one；
The structural representation frame with multistage total nitrogen analysis system except water purifying function that Fig. 2 provides for the embodiment of the present invention
Figure two；
The structural representation frame with multistage total nitrogen analysis system except water purifying function that Fig. 3 provides for the embodiment of the present invention
Figure three；
Fig. 4 is the structural schematic block diagram of the burner in Fig. 2；
Fig. 5 is the structural schematic block diagram of the sampling processing means in Fig. 2；
Fig. 6 is the structural schematic block diagram of the water trap in Fig. 2；
Fig. 7 is the structural schematic block diagram of the reduction apparatus in Fig. 2；
Fig. 8 is the structural schematic block diagram of the purifier in Fig. 2；
Fig. 9 is the structural schematic block diagram of the detection device in Fig. 2；
Figure 10 is for inventing the schematic flow sheet one of the method measuring nitrogen content that another embodiment provides；
Figure 11 is for inventing the schematic flow sheet two of the method measuring nitrogen content that another embodiment provides；
Figure 12 is the schematic flow sheet of water removal phase in Figure 11；
Figure 13 is the schematic flow sheet of purifying step in Figure 11；
Figure 14 is the schematic flow sheet of reduction step in Figure 11；
The overall structure with multistage total nitrogen analysis system except water purifying function that Figure 15 provides for the embodiment of the present invention
Schematic diagram.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Describe, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments wholely.Based on
Embodiment in the present invention, the every other embodiment that those of ordinary skill in the art are obtained, broadly fall into present invention protection
Scope；Wherein involved in this enforcement "and/or" key word, represent and or two kinds of situations, in other words, the present invention implements
A and/or B mentioned by example, illustrates A and B, two kinds of situations of A or B, describes three kinds of states existing for A Yu B, such as A and/or
B, represents: only include A and do not include B；Only include B and do not include A；Including A and B.
Meanwhile, in the embodiment of the present invention, when assembly is referred to as " being fixed on " another assembly, and it can be directly at another
On assembly or assembly placed in the middle can also be there is.When an assembly is considered as " connection " another assembly, and it can be direct
It is connected to another assembly or may be simultaneously present assembly placed in the middle.When an assembly is considered as " being arranged at " another group
Part, it can be to be set directly on another assembly or may be simultaneously present assembly placed in the middle.The embodiment of the present invention is made
Term " vertical ", " level ", "left", "right" and similar statement be merely for purposes of illustration, be not intended to
Limit the present invention.
Specifically refer to Fig. 1, embodiments provide a kind of have multistage except total nitrogen analysis system of water purifying function
System, at least includes burner 200, reduction apparatus 400, purifier 500 and detection device 600.Wherein, described burner
200 are connected with described reduction apparatus 400 so that testing sample fully burns in described burner 200, and produces gaseous mixture
Body.Reduction apparatus 400 is connected with purifier 500 simultaneously so that produced mixed gas in purifier 500 through one
Series control techniques is purified.Realize the gas after final purification comprises only purity nitrogen molecule, and described purifier 500 and institute
State detection device 600 to connect so that the content of nitrogen in purified gas, detected by described detection device.The present invention implements
In example, constitute described tool by least the above burner 200, reduction apparatus 400, purifier 500 and detection device 600
Have multistage except total nitrogen analysis system of water purifying function, instead of the use using Kjeldahl's method in conventional art and cause rotten
The technological deficiency that erosion property soda acid, operating procedure length complicated, time-consuming and environmental pollution are serious.
Multistage elaborate except total nitrogen analysis system of water purifying function in order to embodiment of the present invention offer is had,
Respectively below in conjunction with Fig. 2-9 burner 200, reduction apparatus 400, purifier 500 and detection device 600 are done and explain in detail
State, to support the technical problem to be solved further.
For burner 200,
Owing to the temperature range of burning and the Temperature Distribution in stove all have vital effect to test result.
Therefore, the burner 200 described in the embodiment of the present invention is 1100 DEG C of combustion furnaces, and is uniform constant temperature.
Specifically, referring to Fig. 4, described 1100 DEG C of combustion furnaces at least include: body of heater 201, for automatic constant temperature temperature control
Power electronic equipment 202 and heating element heater 203.Wherein, described power electronic equipment 202 is used for maintaining body of heater 201 internal
The high temperature of 1100 DEG C, to ensure testing sample fully oxidized burning in described body of heater 201, thus eliminates due in body of heater 201
The temperature in portion is on the low side and described testing sample can not be made to clear up oxidation the most uniformly, and causes unnecessary the doing of test experiments
Disturb, and then improve the accuracy of test result.Meanwhile, heating element heater 203 is evenly provided on the surrounding of body of heater 201 inwall, makes
The high temperature of furnace interior is uniformly distributed, so that testing sample thermally equivalent, it is ensured that sample is uniform decomposition in combustion furnace, thus
Further obviate the even technological deficiency brought of the temperature distributing disproportionation within body of heater 201.It should be noted that this enforcement
Heating element heater 203 described in example can be arranged on the inwall of body of heater 201 uniformly, naturally it is also possible to is arranged on outside body of heater 201
Wall, when being arranged on the outer wall of body of heater 201, it is also possible to arranges one layer of overcoat in the periphery of described heating element heater 203, with to place
Heating element heater 203 in body of heater 201 outer wall protects.This overcoat can be made up of heat insulation layer and protective layer two parts.
Its heat insulation layer is filled by adiabator and is constituted, and protective layer is fixed on the outside of insulating barrier, so that insulating barrier is positioned at body of heater 201 outer wall
And between protective layer.Protective layer outside insulating barrier can be cancellated sheetmetal plate or insulation board, to prevent foreign objects
Body collision or friction heat insulation layer.
As preferably, described combustion furnace can be a kind of circulating combustion furnace, also has the combustion furnace sample introduction blowback system of uniqueness
System, it is ensured that all nitrogen component complete oxidations, to eliminate the interference of environmental factors, beneficially low content sample detection, thus realize
Analyze more accurately, it is ensured that the reliability of result.
As a preferred embodiment, above-mentioned power electronic equipment 202 can be an applying electronic pipe higher-order of oscillation electricity
The automatic constant temperature controller on road, wherein, the energy storage coil of described electron tube high-frequency oscillating circuits is suitable due to coupling electrical storage device
Coordinate, a certain frequency of oscillation can be secured to；Energy storage coil has constant temperature index, and has large-scale thermocouple thermometer, bright
Really indicate the temperature of high temperature furnace；Meanwhile, the pointer of energy storage coil has a metal penoncel, when furnace temperature is raised to required temperature, temperature
When the penoncel of degree index is coupled with energy storage coil, oscillating current stops at random, and electron tube plate current therefore changes, and makes it grasp
A vertical relay the sensitiveest, then control a strength relay to cut off the electric current of heating wire with this, make temperature no longer increase,
Upon a drop in temperature, the penoncel of pointer loses with energy storage coil and couples, and electron tube recovers again vibration, controlled strength relay
Recovering the electric current by high temperature furnace, furnace temperature can edge up again the most simultaneously.So interrupted, to reach automatically to keep a constant temperature because of electric current
The purpose of degree.
Same, as a preferred embodiment, above-mentioned heating element heater 203 can be high-quality Tercod；
It should be noted that in embodiments of the present invention, before testing sample enters burner 200, it is also possible to pass through
Sample introduction processing means 100 carries out the physical treatment of early stage.Wherein, the early stage physical treatment of described testing sample can be divided into following two
Kind of situation: testing sample, if testing sample is the solid sample of anisotropic, was pulverized and sieved process before claiming sample by (1)；
(2) if testing sample is liquid and beans class sample, then can directly claim in crucible.Wherein, institute in embodiments of the present invention
State crucible reusable, to reach the technique effect without consumptive material.Meanwhile, the crucible required for the embodiment of the present invention can be such as
One in lower crucible: quartz, pottery, steel, nickel, platinum etc., to reach to be suitable for the purpose of various testing sample.Thus overcome
When using other Instrumental Analysis, sample must pressing mold molding and with tinfoil parcel just can sample introduction analysis, sample preparation complexity, tin can
For the technological deficiency that medical disposable material, operating cost height, combustion-supporting gas and carrier gas consumption are more.Further, real due to the present invention
Execute example and process the chemical reagent such as digestion and toxicity without any extra sample chemical, thus eliminate tradition Kjeldahl's method
Operation complexity, digestion time length, environmental pollution is serious, safety coefficient is low technological deficiency.
In embodiments of the present invention, described testing sample is directly weighed in repeatedly used described crucible, crucible position
On sampler and can Reusability, the weighing of described testing sample can be in the way of using PC end automatization record, that is, enter
Sample processing means 100 can at least include an electronic weigher, and can be weighed in real time by this electronic weigher is positioned at crucible
The quality of interior sample, and the weight data information gathered is transmitted to PC end, generate weight DBMS and also preserve, thus have
Eliminate to effect the recording error caused by manual entry data and/or calculate the technological deficiency of error.
Need exist for explanation, in order to enable that data measured in the embodiment of the present invention are stored and shown.Make
For preferably, continuing with seeing Fig. 2, the embodiment of the present invention is additionally provided with data storage 800 and a display device 700.Wherein,
Described data storage 800 carries out signal transmission with described electronic weigher and described detection device respectively, with to the number received
According to storing.Meanwhile, display device is connected with described detection device and carries out signal transmission, to receive described detection device institute
The data message of detection, and described data message is shown.Certainly, display device here can include a power supply source
701 and a display end 702.Described display end 702 is connected with described power supply source 701, with by described power supply source 701 to described
Display end 702 is powered in real time, and described display end 702 carries out signal transmission with described detection device.It is noted that
Described display end is liquid crystal display.
Further, described sample introduction processing means 100 at least includes: sampler 101, mechanical arm 102, power source 103,
Plus/minus speed mechanism, actuating device and bracket institution etc.；Wherein, described sampler 101 is porous plate disc structure.On it intrinsic
One crucible 104；Mechanical arm 102 is rotationally fixed on described sampler 101, and described power source 103 is mechanical arm 102
Run and power is provided, to drive sampler 101 to move by the motion of mechanical arm 102, and then realize driving crucible 104 to enter
Row motion.Here power source 103 can be selected for motor or servomotor as controlling motor.But as preferred, this
Bright embodiment selects motor as the power source 103 of mechanical arm 102 so that it is have that control mode is flexible, floor space is little,
The advantages such as low price.Meanwhile, plus/minus speed mechanism, actuating device are connected with mechanical arm 102 respectively so that by plus/minus speed machine
The motion of mechanical arm 102 is accelerated or slows down by structure, and bracket institution is to mechanical arm 102, acceleration and deceleration mechanism and/or transmission
Device is supported.And actuating device can be ball screw nut transmission, so make to change the rotary motion of mechanical arm
For linear motion, move equipped with the crucible of testing sample with promotion.Wherein, plus/minus speed mechanism and the machinery of actuating device
Structure and motion principle think prior art, and here is omitted.
In detail, in embodiments of the present invention, 1100 DEG C of combustion furnaces use unique upper furnace structure and from bottom to top
Vertical input mode.That is, body of heater 201 is positioned at the top of sampler 101.
Wherein, the transmission of described sampler 101 uses the vertical input mode of linear type from bottom to top, i.e. by controlling even
The crucible 104 that the mechanical arm 102 being connected to described sampler 101 will be located on sampler 101 heads in body of heater 201 so that sample
After burning completely in combustion furnace, it is transferred on sampler 101 by mechanical arm 102 from top to bottom.Sample after ashing is then protected
Stay in crucible 104, and can after analysis by control sampler 101 will ashing after the automatic interference-free of sample transfer to instrument
Outside device, clean dust without blow-on, need not safeguard；Sample direct injected, need not wrap up with tinfoil, without pressing mold, reaches solid
The test of body, fluid sample all can get result accurately.This design is substantially shorter the detection cycle, and can extend thermal cycle parts
Service life (4-5 times).Thus effectively overcome tradition and determine blood urea/nitrogen analyzer to use the Dumars of the next furnace design determine
Nitrogen instrument sample must pressing mold molding and after wrapping up with tinfoil just can sample introduction analysis, and in cinder catcher, sample ash reaches a certain amount of
After must manual blow-on technological deficiency that the dust in cinder catcher is removed.
The embodiment of the present invention by using unique upper furnace structure and vertical input mode, be possible not only to realize solid,
The quick detection of fluid sample, moreover it is possible to reach the full automation from sample process to assay.Additionally, the load that burning produces
Air-flow can take away sample dust automatically, cleans dust without blow-on, need not safeguard, it is achieved multiple samples detect, and can simultaneously
To circulate sample-adding.This improvement can be greatly promoted automaticity, shortens sample processing time, improves system effectiveness, and can show
Write prolongation system service life.
It should be strongly noted that in embodiments of the present invention, due to described testing sample and at burner 200 internal combustion
The product burnt all contains moisture, therefore from burner 200 gaseous state NOx out need to carry out through water trap 300
Except water processes.Described water trap 300 is connected between described burner 100 and described reduction apparatus 400, specifically can be such as figure
Shown in 2 and 3.
Certainly, it should be noted that in sample introduction processing means 100 here, the quantity of sampler 101 can also be many
Individual, mechanical arm 102 is provided with the multiple lever arms suitable with sampler 101 quantity, and each lever arm is fixed with one
Corresponding sampler, each sampler 101 is fixed with a crucible.Thus so that pass through set by mechanical arm 102
Several samplers 101 are controlled by several lever arms put simultaneously flexibly, i.e. realize selective to sampler
Sample in 101 burns.
Further, referring to shown in Figure 15, water trap 300 described in the embodiment of the present invention includes one-level water removal body
310, two grades of water removal bodies 320 and third class de-watering mechanism 330.Wherein, described one-level water removal body 310 and described two grades of water removing machines
Structure 320 is in parallel, and using the one-level water removal body 310 after parallel connection and described two grades of water removal bodies 320 as one on the whole,
Its one end is connected with described burner, with the mixed gas produced after receiving the burning of described burner；The other end is with described
Third class de-watering mechanism 330 connects so that described third class de-watering mechanism 330 removes water with described one-level water removal body 310, two grades respectively
Mechanism 320 constitutes the structural relation of series connection, to realize being received through described one-level water removing machine by described third class de-watering mechanism 330
Structure 310 and described two grades of water removal bodies 320 are except the mixed gas after water process.
It should be noted that in embodiments of the present invention, why water trap 300 be arranged to multistage water removal body,
On the one hand purpose be mixed gas is carried out multistage except water, to guarantee that the moisture in mixed gas is sufficiently removed.Another
Described one-level water removal body 310 and described two grades of water removal bodies 320 are used the mode being connected in parallel by aspect, so make from combustion
The mixed gas burning device output is mixed at the receiving terminal of described one-level water removal body 310 and described two grades of water removal bodies 320
Close, buffer, be balanced with the airflow rate to the mixed gas exported by burner, it is to avoid the mixed gas air-flow of output
Excessive velocities and cannot obtain fully except water.Simultaneously by the described one-level water removal body 310 after parallel connection and described two grades of water removing machines
Structure 320, the mixed gas exported mixes at the outfan of one-level water removal body 310 and two grades of water removal bodies 320, then at stream
Entering and carry out in third class de-watering mechanism 330 again except water, same principle, this also makes to be removed by one-level water removal body 310 or two grades
The airflow rate of mixed gas of the outfan output of water mechanism 320 obtained effective buffering, balance, it is to avoid the mixing of output
After gas input third class de-watering mechanism, air velocity is too fast and cannot obtain fully except water.
Certainly, in embodiments of the present invention, described one-level water removal body 310 and described two grades of water removal body 320 phases are also
Connection, and using the one-level water removal body 310 after parallel connection and described two grades of water removal bodies 320 as one on the whole, its one end with
Described burner connects, with the mixed gas produced after receiving the burning of described burner；The other end and described third class de-watering
Mechanism 330 connects so that described third class de-watering mechanism 330 respectively with 310, two grades of water removal bodies 320 of described one-level water removal body
Constitute the structural relation of series connection, this kind of connected mode can be defined as the connected mode 1 of water removal body.Certainly, this connection side
Formula 1 is only merely 310, two grades of a kind of connection sides between water removal body 320 and third class de-watering mechanism 330 of one-level water removal body
Formula, the embodiment of the present invention is not limited to.
Words sentence is talked about, and other for 310, two grades of water removal bodies 320 of one-level water removal body and third class de-watering mechanism 330 connect
Connect mode, as long as can reach, effectively except the technique effect of water, to may also apply to the embodiment of the present invention.Such as, in order to simplify knot
Structure designs, and the embodiment of the present invention can use the connected mode 2 of water removal body, is directly in series by three water removal bodies, i.e. one-level
310, two grades of water removal bodies 320 of water removal body and third class de-watering mechanism 330 are sequentially connected with, or in order to reduce cost, employing removes
The connected mode 3 of water mechanism, removes third class de-watering mechanism, two grades of water removal bodies 320 and one-level water removal body 310 is in series.
Again or in order to further reduce manufacturing cost, use the connected mode 4 of water removal body, only select one-level water removal body 310,
Any one water removal body in two grades of water removal bodies 320 and third class de-watering mechanism 330, and respectively with burner and reduction apparatus
Connect, to reach the technical scheme of the technique effect except water, also within protection scope of the present invention.It should be noted that this
" one-level " in 310, two grades of water removal bodies 320 of one-level water removal body in inventive embodiments and third class de-watering mechanism 330, " two
Level ", " three grades " be only and carry out several water removal bodies encoding label, in order to convenient description, namely the embodiment of the present invention are described
In three water removal bodies identical.
It is to say, in the embodiment of the present invention, described one-level water removal body 310 may include that the first glass physical condensation
Device the 301, first electronic cooling dehydrater 302 and the first adsorbent 303.Described two grades of water removal bodies 320 may include that the second glass
Glass physical cold condenser, the second electronic cooling dehydrater and the second adsorbent；Described three grades of purification mechanisms 330 may include that the 3rd
Glass physical condenser, the 3rd electronic cooling dehydrater and the 3rd adsorbent.
Owing in the embodiment of the present invention, 310, two grades of water removal bodies 320 of one-level water removal body and third class de-watering mechanism 330 are complete
Complete lower same, the most only as a example by the connected mode 4 of above-mentioned water removal body, the present invention is elaborated, be placed in water removal body
The non-detailed portion of connected mode 1,2,3, and two grades of water removal bodies 320, third class de-watering mechanism 330 self structure do not describe portion in detail
Point, see also in water removal body the specific descriptions of one-level water removal body 310 in connected mode 4.
Specifically, refer to Fig. 3, for the one-level water removal body 310 in the connected mode 4 of water removal body, its
Including the first glass physical condenser the 301, first electronic cooling (2 DEG C) dehydrater 302 and the first adsorbent 303.Wherein, in institute
State in water trap 300, first pass through the first glass physical condenser 301 and remove water, then by the first electronic cooling dehydrater 2
DEG C except water, finally by the first adsorbent 303 absorption except water.I.e., first allow after being burnt by the first glass physical condenser 301
Product carry out physics cooling by by steam liquefaction except water, then cooled down further by the first electronic cooling dehydrater 302
Gas to be measured also removes steam again by by steam liquefaction, is fully absorbed by moisture finally by the first adsorbent 303
To reach thoroughly except the purpose of water, to guarantee that described combustion product steam is removed completely, moisture is completely eliminated to nitrogen content
The impact of the accuracy measured.
As preferably, in the water trap 300 that the embodiment of the present invention provides, described first glass physical condenser 301 can
To be third generation double-tee glass condenser, it is rapidly decreased to 2-3 degree Celsius from high temperature, by steam contained in combustion product
Condense into water, then moisture extracted and separate.Complete the first step except water.It is noted that in the embodiment of the present invention
Carrying out first step condensation by the first glass physical condenser 301 is necessary except water, is the most significantly dropped by high-temperature combustion product
Temperature so that it is be reduced to 2-3 DEG C, provides except water condition except water for follow-up electronic cooling dehydrater 302 electronic cooling then.
Further, described first electronic cooling dehydrater 302 can be semiconductor cooler, uses extraordinary quasiconductor material
The P-N junction that material is constituted, formation thermocouple pair, generation Peltier effect (when two kinds of different metals couple together and pass to electric current,
Have a joint heat absorption, another joint heat release), a kind of New Refrigerating method i.e. freezed by unidirectional current.Electronic cooling effect
Producing the principle being through thermoelectricity, be the cooling piece of a monolithic, it is made up of two panels potsherd, has N-type and p-type in the middle of it
Semi-conducting material (Tellurobismuthite .), this semiconductor element on circuit be with cascade connect composition.Semiconductor chilling plate
Operation principle be: when one block of N-type semiconductor material and one block of P-type semiconductor material are coupled to galvanic couple pair, with copper sheet two
Individual quasiconductor couples together.After connecting DC current in this circuit, just can produce the transfer of energy, electric current is by N-type element
The joint flowing to p-type element absorbs heat, becomes cold end, p-type element flow to the joint release heat of N-type element, become heat
End.By various radiating modes, the heat in hot junction being taken away, cold end just can keep lower temperature.The size of heat absorption and heat release is logical
The size of overcurrent and the element logarithm of semi-conducting material N, P determine.By up to a hundred, galvanic couple is unified into inside cooling piece
Thermoelectric pile, to reach to strengthen the effect of refrigeration, when heat load is zero, the strongest refrigeration can reach 80 DEG C of temperature difference.Electronics
The temperature difference amplitude of refrigeration limits, and also further illustrates the condensation of described first step glass physical except the necessity of water.
And then, owing to there being the water removal phase of first two steps, most moisture have been removed by, so having only to
The first a small amount of adsorbent 303 i.e. can reach the effect well eliminating moisture, thus is greatly saved the usage amount of adsorbent,
Overcome tradition azotometer and use the defect that a large amount of adsorbent costs are high.As preferably, the adsorbent in the embodiment of the present invention can
To be silica gel, activated alumina or activated carbon.
Last it should be noted that by above-mentioned one-level water removal body 310, effectively ensure through burner 200
After combustion product steam remove completely, so that moisture impact on the accuracy of nitrogen analysis is completely eliminated and permissible
Direct analysis fluid sample, thus it is substantially reduced the use of adsorbent, reduce operating cost.Certainly, as stated above, herein
The present invention only only includes in water trap 300 as a example by one-level water removal body 310 that the operation principle to water removal body is retouched
State, during actual job, it is possible to 310, two grades of water removal bodies 320 of one-level water removal body and third class de-watering mechanism 330 are pressed
Constituting water trap 300 according to above-mentioned connected mode 1-3 and carry out efficient water-removing, the present invention does not limit to, the most superfluous
State.
Secondly, for reduction apparatus 400,
Described reduction apparatus 400 includes: reduction furnace 402, part flow arrangement 401, non-dispersive IR line (NDIR) sensor
403.Wherein, described part flow arrangement 401 and the direct phase of described electronic cooling (2 DEG C) dehydrater 302 in higher level's water trap 300
Even, it is connected with described reduction furnace 402 subsequently, is sensed by described NDIR between described reduction furnace 402 and described purifier 500
Device 403 is connected.
Specifically, part flow arrangement 401 described in the embodiment of the present invention is the gas diverter of a kind of precision, split ratio
Example is 1/35 or 1/80, enters reduction furnace 402 at gas and reduces front Partial flow dilution gas, thus reaches to save copper reduction stove
The consumption of the reducing agent of 402 and save the purpose of the cost every time measured, meanwhile, built-in membrane disappears deimpurity interference.Specifically
Ground, owing to N (nitrogen element) burning conversion becomes the NOx of substantial amounts of gaseous state, the highest for detector concentration, and carrying out reducing
During can consume substantial amounts of reducing agent, therefore, will be from described burner 200 out and through three by part flow arrangement 401
The condensation of individual condensing unit is except reduction detection after the gaseous sample shunting after water, and remaining gas processes heel row by adsorbent
Remove.
The nitrogen oxides that burning generates, after the gas diverter of described precision shunts, spreads using helium as carrier gas
Sending, described nitrogen oxides is completely reduced as dinitrogen in 600 DEG C of copper reduction stoves, and the oxygen of excess is combined into oxidation by copper simultaneously
Copper.Using non-dispersive IR line (NDIR) sensor to be used for the amount of oxygen controlled needed for best combustion, this can ensure that oxygen
Minimum with the consumption of copper, the highest save 95% oxygen consumption.
(non-dispersive IR line) sensor 403 used in the embodiment of the present invention can measure different gas in mixed gas
The concentration of body.Asymmetric double atom and polyatomic gas have selection absorbability to infrared energy.This character is infrared
A kind of character that active substance itself has, has uniqueness, and such as the DNA of human body, everyone DNA is different, and not
Can change because of any environmental factors or the change of condition, therefore according to this character, material can be carried out qualitative and quantitative point
Analysis.Different gas has different absorption spectrums, and absorption spectrum is made up of the spectral line in the range of certain frequency, has certain
Broadband, in broadband, the absorption intensity of each Frequency point is different.If infrared radiating light spectral limit includes tested gas
Absorption bands, when infra-red radiation by be full of tested gas air chamber time, at the energy intensity quilt of corresponding frequencies infra-red radiation
GAS ABSORPTION and cause the decay of energy, and gas concentration is the biggest, and energy attenuation is the most severe, gets final product inverting by analyzing attenuation
Go out the concentration of gas to be measured.
The detection method of described non-dispersive IR line (NDIR) principle sensor 403 can use spectral absorption calculus of finite differences
Detection.Being sent infrared light through divided beams by light source, after reference channel and tested passage air chamber absorb, optical signal is detected
Device carries out processing and amplifying after being converted into the signal of telecommunication.Because of the change of such environmental effects and the infrared light effect phase to two paths of signals
With, difference detecting method eliminates the impact of these unstable factors, can truly reflect tested gas concentration information.
Again, for purifier 500,
Continuing with seeing Figure 15, purifier 500 described in the embodiment of the present invention includes 510, two grades of first class purification mechanism
Purification mechanism 520 and three grades of purification mechanisms 530.Wherein, described first class purification mechanism 510 and described secondary purification mechanism 520 phase
Parallel connection, and using the first class purification mechanism 510 after parallel connection and described secondary purification mechanism 520 as one on the whole, its one end
It is connected with described reduction apparatus 400, with the gas produced after receiving the reduction of described reduction apparatus；The other end and described three grades of purifications
Mechanism 530 connects so that described three grades of purification mechanisms 530 respectively with described first class purification mechanism 510, secondary purification mechanism 520
Constitute the structural relation of series connection, to realize being received through described first class purification mechanism 510 He by described three grades of purification mechanisms 530
Gas after described secondary purification mechanism 520 purified treatment.
It should be noted that in embodiments of the present invention, why purifier 500 be arranged to multistage purification mechanism,
On the one hand purpose is to be gas is carried out multistage purification, to guarantee that mixed gas is sufficiently purified.On the other hand by described one
Level purification mechanism 510 and described secondary purification mechanism 520 use the mode being connected in parallel, and so make from reduction apparatus 400 defeated
The mixed gas gone out carries out mixing, buffering at the receiving terminal of described first class purification mechanism 510 and described secondary purification mechanism 520,
It is balanced with the airflow rate to the mixed gas exported by reduction apparatus 400, it is to avoid the mixed gas air velocity of output
Too fast and cannot be fully purified.Simultaneously by the described first class purification mechanism 510 after parallel connection and described secondary purification mechanism
520, the mixed gas exported mixes at the outfan of first class purification mechanism 510 and secondary purification mechanism 520, is then flowing into
Again purifying in three grades of purification mechanisms 530, same principle, this also makes by first class purification mechanism 510 or secondary purification
The airflow rate of mixed gas of the outfan output of mechanism 520 obtained effective buffering, balance, it is to avoid the gaseous mixture of output
After body three grades of purification mechanisms 530 of input, air velocity is too fast and cannot be fully purified.
Certainly, in embodiments of the present invention, described first class purification mechanism 510 and described secondary purification mechanism 520 are in parallel,
And using the first class purification mechanism 510 after parallel connection and described secondary purification mechanism 520 as one on the whole, its one end is with described
Reduction apparatus 400 connects；The other end is connected with described three grades of purification mechanisms 530 so that described three grades of purification mechanisms 530 respectively with
Described first class purification mechanism 510, secondary purification mechanism 520 constitute the structural relation of series connection, can be by this kind of connected mode definition
Connected mode 1 for purification mechanism.Certainly, this connected mode 1 is only merely first class purification mechanism 510, secondary purification mechanism 520
And a kind of connected mode between three grades of purification mechanisms 530, the embodiment of the present invention is not limited to.
Words sentence is talked about, and other for first class purification mechanism 510, secondary purification mechanism 520 and three grades of purification mechanisms 530 connect
Connect mode, as long as the technique effect effectively purified can be reached, may also apply to the embodiment of the present invention.Such as, in order to simplify knot
Structure designs, and the embodiment of the present invention can use the connected mode 2 of purification mechanism, is directly in series by three purification mechanisms, i.e. one-level
Purification mechanism 510, secondary purification mechanism 520 and three grades of purification mechanisms 530 are sequentially connected with, or in order to reduce cost, use clean
Change the connected mode 3 of mechanism, remove three grades of purification mechanisms, secondary purification mechanism 520 and first class purification mechanism 510 are in series.
Again or in order to further reduce manufacturing cost, use the connected mode 4 of purification mechanism, only select first class purification mechanism 510,
Any one purification mechanism in secondary purification mechanism 520 and three grades of purification mechanisms 530, and respectively with reduction apparatus and detection device
Connect, to reach the technical scheme of the technique effect purified, also within protection scope of the present invention.It should be noted that this
" one-level " in first class purification mechanism 510, secondary purification mechanism 520 and three grades of purification mechanisms 530 in inventive embodiments, " two
Level ", " three grades " be only and carry out several purification mechanisms encoding label, in order to convenient description, namely the embodiment of the present invention are described
In three purification mechanisms identical.
It is to say, in the embodiment of the present invention, described first class purification mechanism 510 may include that the first adsorber 501 and
Two adsorbers 502.Described secondary purification mechanism 520 may include that the 3rd adsorber and the 4th adsorber.Described three grades of clearing machines
Structure 530 may include that the 5th adsorber and the 6th adsorber.
Owing in the embodiment of the present invention, first class purification mechanism 510, secondary purification mechanism 520 and three grades of purification mechanisms 530 are complete
Complete lower same, the most only as a example by the connected mode 4 in above-mentioned purification mechanism, the present invention is elaborated, be placed in clearing machine
The non-detailed portion of connected mode 1,2,3 of structure, and 520, three grades of purification mechanism 530 self structure of secondary purification mechanism do not describe in detail
Part, sees also in purification mechanism the specific descriptions of first class purification mechanism 510 in connected mode 4.
Specifically, continuing with seeing Fig. 3, for the first class purification mechanism 510 in the connected mode 4 of water purification mechanism
Speech, it includes the first adsorber 501 and the second adsorber 502, wherein, described first adsorber 501 directly with described non-dispersive
Property infrared ray sensor 403 be connected, described second adsorber 502 is connected with detected device 600.Specifically, through reduction
After process, except nitrogen molecular in air-flow, possibly together with other impurity, it is therefore desirable to removed in reducing gas by purifier
CO2/SO2, water and halogen, it is ensured that the degree of purity of nitrogen molecular, and then ensure the accurate reliability of test.Gas after reduction passes through
Described first adsorber 501, can remove CO2/SO2 and halogen；Further, then by described second adsorber 502, permissible
Remove moisture removal.By two step adsorption processes, the removal of impurity can be reached, purify the purpose of gas nitrogen to be detected.Wherein, described
First adsorber 501 possesses dehalogenation function, it is possible to eliminate halogen, effectively prevents halogen from entering the detection device described in subordinate and making
Become infringement, thus reach to protect the purpose of described detection device.As preferably, described first adsorber 501 is sulfur dioxide/bis-
Carbonoxide halogen adsorber；And/or, described second adsorber 502 is water adsorber.Certainly, as stated above, herein this
The bright operation principle only only included in purifier 500 as a example by first class purification mechanism 510 purification mechanism is described,
During actual job, it is possible to by first class purification mechanism 510, secondary purification mechanism 520 and three grades of purification mechanisms 530 according to above-mentioned
Connected mode 1-3 constitute purifier 500 carry out high-efficient purification, the present invention does not limit to, and the most also repeats no more.
For detection device 600,
Described detection device 600 includes: TCD thermal conductivity detector (TCD) 601, mass flowmenter 602.Wherein, described TCD thermal conductance inspection
Surveying device 601 to be directly connected with the second adsorber 502 described in upper level purifier 500, described mass flowmenter 602 directly connects
After being connected on described TCD thermal conductivity detector (TCD) 601, it it is last device link of sample detection.
Use described TCD thermal conductivity detector (TCD) 601 to detect remaining nitrogen in carrier gas stream.TCD thermal conductivity detector (TCD) 601 is also known as warm
Lead pond or heated filament and examine hot device, be the most frequently used a kind of detector of gas chromatography.The operation principle of described thermal conductivity detector (TCD) is base
Having different thermal conductivities in gas with various, the sensing element of described detector is heated filament, such as tungsten filament, platinum filament, rhenium silk, and by heat
Silk composition electric bridge, in the thermal conductivity detector (TCD) of described novel azotometer, uses tungsten filament, also replaces tungsten filament with other heated filament
Can, heated filament has the characteristic that resistance varies with temperature.When there being a constant dc by described thermal conductivity detector (TCD), heated filament is added
Heat.Owing to the conduction of heat of carrier gas makes a part of heat of heated filament be taken away by carrier gas, a part passes to cell body.When heated filament produces
When raw heat and dissipated heat reach balance, hot-wire temperature is the most stable in certain numerical value.Now, heated filament resistance is also stabilized in one
Fixed number value.Be passed through due to reference cell and measuring cell is all pure carrier gas, same carrier gas has an identical thermal conductivity, therefore two-arm
Resistance value is identical, bridge balance, and no signal exports, and record system record is straight line.When there being sample to enter detector,
Pure carrier gas flows through reference cell, and carrier gas carries component air-flow through measuring cell, due to carrier gas and component binary mixture to be measured
Thermal conductivity different with the thermal conductivity of pure carrier gas, heat dispersal situations in measuring cell thus change, make reference cell and measuring cell hole
Creating difference, electric bridge disequilibrium between middle heater resistance value, detector has voltage signal to export, and monitor draws respective sets
The chromatographic peak divided.In carrier gas, the concentration of component to be measured is the biggest, and in measuring cell, heat conductivity of gas changes the most notable, temperature and resistance
Value changes the most notable, and voltage signal is the strongest.The voltage signal now exported is directly proportional to the concentration of sample, this thermal conductance just
The quantitative basis of detector.
Therefore, when using described novel azotometer to measure total nitrogen content, in described thermal conductivity detector (TCD), N2 volume content
Cause a kind of electronic measurement signal, by it, then the independence correction through material, the meter the most automatically of the nitrogen content in sample
Calculate, print and store.Specifically, described standard correction material uses EDTA or carbamide, and has only to regular calibration, nothing
Must start shooting every time make blank and standard correction.Possesses feature simple to operate, widely used.
Described TCD thermal conductivity detector (TCD) 601 does not destroy the collection of monitored component, beneficially sample during detection, or
With other Instrument crosslinkings.Described TCD thermal conductivity detector (TCD) 601 can meet the requirement that in Industrial Analysis, peak height is quantitative, is suitable for factory
Control analysis.Meanwhile, TCD thermal conductivity detector (TCD) 601 has the working range of broadness, can measure and cover as little as ppm rank, up to
The analysis of the total nitrogen/protein of percentage concentration content.
Described mass flowmenter 602 uses thermal measuring method, i.e. how many by molecular mass that split molecule is taken away
Thus measure flow.Because be with thermal measure, so will not because of gas temperature, the change of pressure thus have influence on survey
The result of amount.Mass flowmenter 602 be one more accurately, quickly, reliable, efficiently, stable, flow measurement instrument flexibly.
Mass flowmenter 602 can not control flow, and it can only detect the mass flow of liquid or gas, by analog voltage, electricity
Stream or serial communication output stream value.
It should be added that, in embodiments of the present invention, the concentration of the combustion gas oxygen being passed through is 99.995%,
The concentration of the carrier gas stream helium being passed through is 99.99%, and the flow of the oxygen that is passed through and helium is by quality flow control
Device automatically controls.Wherein, described mass flowmenter 602, is a kind of instrument simultaneously can be able to being controlled again in detection.Matter
Amount effusion meter 602 itself is except measuring part, and also with a solenoid valve or piezo electric valve, such mass flow controls this
Body constitutes a closed loop system, for controlling the mass flow of fluid.The setting value of mass flowmenter 602 can be by simulation electricity
Pressure, analog current, or computer, PLC offer.
Need further exist for supplementary notes, in embodiments of the present invention, also need to described have multistage except Water warfare merit
Built-in 40 DEG C ± 0.1 DEG C Thermotank device in total nitrogen analysis system of energy, to guarantee system detector, diverter, gas collection
The temperature constant state of the devices such as system, gas circuit control, it is to avoid owing to the change of ambient temperature causes the change of gas flow path stability,
Improve analysis precision and accuracy.
To sum up, described testing sample is after the physical treatment and automatic Weighing of early stage, at described vertical mechanical sample introduction
Enter from described sampler under the effect of arm in described 1100 DEG C of homogeneous combustion furnaces of high temperature, fully burn with oxygen, then pass through
Combustion product and impurity are carried out cooling de-watering, then are shunted by described gas diverter precision by described " three step condensations " device
Gaseous sample to be measured after burning, then it is passed through the helium current-carrying gas as the gaseous sample being diverted, send into described together
600 DEG C of copper reduction stoves, by nitrogen molecular Restore All out, meanwhile, use NDIR sensor to control the oxygen needed for best combustion
Amount, this can ensure that the consumption of oxygen and copper is minimum, then passes through described first adsorber and the second adsorber removes CO2/
SO2, halogen and water, be then passed through pure nitrogen in described TCD thermal conductivity detector (TCD), the concentration of detection nitrogen, finally by
Described mass flowmenter, the mass flow of detection nitrogen, in conjunction with the nitrogen gas concn surveyed, automatically calculated by software for calculation
Total nitrogen content in described testing sample.
The device embodiment provided based on above-described embodiment, refers to Figure 10-14, and another embodiment of the present invention also provides for
A kind of embodiment of the method corresponding with device embodiment, specific as follows:
Another embodiment of the present invention provides a kind of method measuring nitrogen content, specifically includes as follows: step 1000, combustion
Burn step, for testing sample being burnt by burner, and produce mixed gas, in described combustion step, described
The ignition temperature of burner is 1100 DEG C, and is constant temperature；Step 2000, reduction step, it is used for by reduction apparatus described
Mixed gas is reduced, and in described reduction step, the reduction temperature of described reduction apparatus is 600 DEG C, and is constant temperature；Step
3000, purifying step, for the mixed gas after reduction being purified by purifier, go the removal of impurity, it is thus achieved that residue gas
Body；Wherein, described impurity at least include following in one: water, carbon dioxide or halogen；Step 4000, detecting step, use
In by detection device, the nitrogen content in described remaining gas being detected.
Further, another embodiment of the present invention also includes；Step 5000, sampling procedure, for processing by sample introduction
Device is sampled, it is thus achieved that described testing sample, and described testing sample is sent in the way of vertical sample introduction described burning dress
Burn in putting.Step 6000, water removal phase, for carrying out except water through mixed gas produced by described combustion step
Process, to remove the moisture in described mixed gas.
Wherein, described water removal phase 6000 also includes following sub-step: step 6001, first removes water sub-step, by described
Mixed gas is sent into glass physical condenser and is carried out once except water；Step 6002, second removes water sub-step, will be through once except water
After mixed gas send in electronic cooling dehydrater and carry out secondary except water；Step 6003 the 3rd, will be through two except water sub-step
Secondary feeding except the mixed gas after water carries out three times except water in adsorbent.
Wherein, described purifying step also includes following sub-step: step 3001, first purifies sub-step, after reduction
Mixed gas is sent into sulfur dioxide/carbon dioxide halogen adsorber and is carried out primary purification；Step 3002, second purifies sub-step,
Mixed gas after primary purification is sent in adsorbent and carries out double purification.
Wherein, described reduction step also includes following sub-step: step 2001, shunting sub-step, for filling by shunting
Put and mixed gas is shunted, so that described mixed gas is diluted；Step 2002, goes back atomic step, after shunting
Gas reduces in reduction furnace；Step 2003 flow control sub-step, for carrying out the flow of the oxygen in described reduction furnace
Control.
The method measuring nitrogen content provided due to another embodiment of the present invention, relative with above-mentioned device embodiment
Should, the most herein to the most too much the repeating of embodiment of the method, in embodiment of the method, non-detailed portion see device enforcement
Example.
Although preferred embodiments of the present invention have been described, but those skilled in the art once know basic creation
Property concept, then can make other change and amendment to these embodiments.So, claims are intended to be construed to include excellent
Select embodiment and fall into all changes and the amendment of the scope of the invention.
Obviously, those skilled in the art can carry out various change and the modification essence without deviating from the present invention to the present invention
God and scope.So, if these amendments of the present invention and modification belong to the scope of the claims in the present invention and equivalent technologies thereof
Within, then the present invention is also intended to comprise these change and modification.
Claims (10)
1. one kind has multistage except total nitrogen analysis system of water purifying function, it is characterised in that including:
Burner, for the burning of testing sample, and produces mixed gas；
Water trap, described water trap is connected with described burner, produces after described burner burns for removing
The raw moisture in mixed gas；Wherein, described water trap includes:
One-level water removal body；
Two grades of water removal bodies, described one-level water removal body and described two grades of water removal bodies are in parallel, and the one end after parallel connection and institute
State burner to connect, with the mixed gas produced after receiving the burning of described burner；
Third class de-watering mechanism, described third class de-watering mechanism with in parallel after described one-level water removal body and described two grades of water removal bodies
The other end connect so that described third class de-watering mechanism is in series with described one-level water removal body, two grades of water removal bodies respectively, with
By described third class de-watering authorities mixing after described one-level water removal body and described two grades of water removal bodies process except water
Close gas；
Reduction apparatus, described reduction apparatus is connected with described third class de-watering mechanism so that from described third class de-watering mechanism out after
Mixed gas be reduced in described reduction apparatus；
Purifier, described purifier is connected with described reduction apparatus, to purify the mixed gas after reduction；Its
In, described purifier includes:
First class purification mechanism；
Secondary purification mechanism；Described first class purification mechanism and described secondary purification mechanism are in parallel, and the one end after parallel connection and institute
State reduction apparatus to connect, with the mixed gas produced after receiving the burning of described reduction apparatus；
Three grades of purification mechanisms, described three grades of purification mechanisms with in parallel after described first class purification mechanism and described secondary purification mechanism
The other end connect so that described three grades of purification mechanisms are in series with described first class purification mechanism, secondary purification mechanism respectively, with
The gas after described first class purification mechanism and described secondary purification mechanism purified treatment is received by described three grades of purification mechanisms
Body；
Detection device, described detection device is connected with described purifier, to examine the nitrogen content in purified gas
Survey；
Display device, described display device is connected with described detection device and carries out signal transmission, to receive described detection device
The data message detected, and described data message is shown；
Sample introduction processing means, processes for described testing sample enters the sample introduction of early stage；And described burner is vertically
Be fixed on the top of described sample introduction processing means so that through early stage sample introduction process after described testing sample pass through described in enter
Sample processing means, is admitted in described burner burning；Wherein, described sample introduction processing means at least includes an electronic-weighing
Device, to weigh to described testing sample；
Data storage, described data storage is connected with described detection device and described electronic weigher respectively so that described
The detection data message that detected of device, described electronic weigher weigh the weight data transmission of gained to described data storage
Store.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 1, it is characterised in that:
Described burner is that temperature controls the combustion furnace at 1100 DEG C；
And described combustion furnace includes:
Body of heater so that described testing sample burns at described furnace interior；
Electron electric power device, is connected with described body of heater, for providing the temperature environment of 1100 DEG C to described body of heater so that described in treat
Test sample product are fully oxidized burning in described body of heater；
Heating element heater, described heating element heater is arranged on the inwall of described body of heater uniformly, makes the temperature of the inside of described body of heater
It is uniformly distributed in described body of heater.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 1, it is characterised in that described sample introduction
Processing means also includes:
At least one sampler, each described sampler is respectively positioned on the lower section of described burner in vertical direction；
The crucible suitable with described sampler quantity, each described crucible is fixed on a described sampler accordingly,
And at least it is placed with described testing sample in a described crucible；
Mechanical arm, is provided with the lever arm suitable with described sampler quantity, and on each lever arm, correspondence fixes an institute
State sampler, to drive corresponding described sampler to move up and down by the knee-action of described lever arm, then promote correspondence
The described crucible in ground enters in described burner；
Power source, described power source is connected with described mechanical arm, thinks that the motion of lever arm described in described mechanical arm provides dynamic
Power.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 1, it is characterised in that described reduction
Device includes:
Diverter, described diverter is connected with described third class de-watering mechanism, with mixed to transferred out by described third class de-watering mechanism
Close gas to shunt；
Reduction furnace, described reduction furnace is connected with described diverter and described detection device respectively, to carry out the gas after shunting
Reduction, and will the gas described detection device of feeding after reduction detect.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 4, it is characterised in that described reduction
Device also includes:
Sensor, described sensor is arranged between described reduction furnace and described detection device.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 1, it is characterised in that
Described first class purification mechanism includes: the first adsorber and the second adsorber；Described first adsorber respectively with described reduction
Device and described second adsorber connect；
And,
Described secondary purification mechanism includes: the 3rd adsorber and the 4th adsorber；Described 3rd adsorber respectively with described reduction
Device and described 4th adsorber connect；
And,
Described three grades of purification mechanisms include: the 5th adsorber and the 6th adsorber；Described 5th adsorber is respectively with described second
Adsorber connection, described 4th adsorber and described 6th adsorber connect, and described 6th adsorber is with described detection device even
Connect.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 6, it is characterised in that
Described first adsorber is sulfur dioxide/carbon dioxide halogen adsorber；Described second adsorber is water adsorber；
And/or,
Described 3rd adsorber is sulfur dioxide/carbon dioxide halogen adsorber；Described 4th adsorber is water adsorber；
And/or,
Described 5th adsorber is sulfur dioxide/carbon dioxide halogen adsorber；Described 6th adsorber is water adsorber.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 1, it is characterised in that described detection
Device includes:
TCD thermal conductivity detector (TCD)；
Mass flowmenter；
Wherein, described TCD thermal conductivity detector (TCD) is connected with described purifier and described mass flowmenter respectively；And described TCD heat
Lead detector and described mass flowmenter is connected with described display device respectively, carry out signal transmission.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 1, it is characterised in that；
Described one-level water removal body includes: the first glass physical condenser, the first electronic cooling dehydrater and the first adsorbent；Institute
State the first glass physical condenser to be connected with described burner and described first electronic cooling dehydrater respectively；Described first inhales
Attached dose is connected with described first electronic cooling dehydrater；
And,
Described two grades of water removal bodies include: the second glass physical condenser, the second electronic cooling dehydrater and the second adsorbent；Institute
State the second glass physical condenser to be connected with described burner and described second electronic cooling dehydrater respectively；Described second inhales
Attached dose is connected with described second electronic cooling dehydrater；
And,
Described third class de-watering mechanism includes: the 3rd glass physical condenser, the 3rd electronic cooling dehydrater and the 3rd adsorbent；Institute
State the 3rd glass physical condenser and remove water with described first adsorbent, described second adsorbent and described 3rd electronic cooling respectively
Device connects；Described 3rd electronic cooling dehydrater and described 3rd adsorbent connect；Described 3rd adsorbent is the most original-pack with described
Put connection.
Have multistage except total nitrogen analysis system of water purifying function the most as claimed in claim 1, it is characterised in that described aobvious
Showing device includes:
Power supply source；
Display end, described display end is connected with described power supply source, to be supplied described display end in real time by described power supply source
Electricity, and described display end and described detection device carry out signal transmission.
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