JPH0241706B2 - - Google Patents
Info
- Publication number
- JPH0241706B2 JPH0241706B2 JP6775781A JP6775781A JPH0241706B2 JP H0241706 B2 JPH0241706 B2 JP H0241706B2 JP 6775781 A JP6775781 A JP 6775781A JP 6775781 A JP6775781 A JP 6775781A JP H0241706 B2 JPH0241706 B2 JP H0241706B2
- Authority
- JP
- Japan
- Prior art keywords
- section
- gas
- acidic
- gas outlet
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000007789 gas Substances 0.000 claims description 74
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 33
- 238000004821 distillation Methods 0.000 claims description 26
- 238000006243 chemical reaction Methods 0.000 claims description 24
- 230000002378 acidificating effect Effects 0.000 claims description 17
- 238000005443 coulometric titration Methods 0.000 claims description 17
- 229910052757 nitrogen Inorganic materials 0.000 claims description 15
- 238000010438 heat treatment Methods 0.000 claims description 14
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 10
- 238000010992 reflux Methods 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 8
- 238000005259 measurement Methods 0.000 claims description 6
- 239000003513 alkali Substances 0.000 claims description 5
- 238000001514 detection method Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 21
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 17
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 239000002253 acid Substances 0.000 description 7
- 229910021529 ammonia Inorganic materials 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 5
- 229910017464 nitrogen compound Inorganic materials 0.000 description 5
- 150000002830 nitrogen compounds Chemical class 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000004448 titration Methods 0.000 description 3
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 239000012159 carrier gas Substances 0.000 description 2
- 238000003869 coulometry Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- 229910000990 Ni alloy Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229940006460 bromide ion Drugs 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- HUAUNKAZQWMVFY-UHFFFAOYSA-M sodium;oxocalcium;hydroxide Chemical compound [OH-].[Na+].[Ca]=O HUAUNKAZQWMVFY-UHFFFAOYSA-M 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N31/00—Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods
- G01N31/002—Determining nitrogen by transformation into ammonia, e.g. KJELDAHL method
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Physics & Mathematics (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
Description
【発明の詳細な説明】
本発明は超微量アンモニア態窒素及び全窒素の
測定装置に関するものである。水質富栄養化現象
を引き起こすといわれている河川、湖沼、海域等
の環境水及び工場排水、プロセス排水、衛生排水
等の排水中の窒素量及び成分が近年大きな問題に
なつてきている。これら水中に含まれる窒素の形
態はアンモニア態、亜硝酸態、硝酸態及び有機態
の4種類に分けられるが、全窒素含量とアンモニ
ア態窒素含量を把握しておくことは排水等の公害
対策上重要である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for measuring ultratrace amounts of ammonia nitrogen and total nitrogen. BACKGROUND ART In recent years, the amount and components of nitrogen in environmental water such as rivers, lakes, sea areas, and wastewater such as industrial wastewater, process wastewater, and sanitary wastewater, which are said to cause water eutrophication, have become a major problem. The form of nitrogen contained in water can be divided into four types: ammonia, nitrite, nitrate, and organic, but it is important to understand the total nitrogen content and ammonia nitrogen content in order to prevent pollution such as wastewater. is important.
従来、超微量のアンモニア態窒素の測定装置と
しては、ヘリウムをキヤリヤーガスとして、反応
管内で試料水中のアンモニア態窒素を臭素イオン
含有反応液で還元して窒素ガスとし、同伴される
水分を完全に除去した後ガスクロマトグラフイー
で定量する装置が提案されている。しかしこの装
置では反応液及び試料水中の溶存窒素ガスを完全
に除去しておかなければならず、また窒素ガスに
還元した後も同伴水分を完全に除去しなければな
らないので、前処理操作に時間を要しかつ操作が
煩雑である欠点がある。 Conventionally, devices for measuring ultratrace amounts of ammonia nitrogen use helium as a carrier gas to reduce the ammonia nitrogen in the sample water with a bromide ion-containing reaction solution in a reaction tube to nitrogen gas, completely removing the entrained moisture. A device has been proposed that uses gas chromatography to quantify the amount of oxidation. However, with this device, dissolved nitrogen gas in the reaction solution and sample water must be completely removed, and entrained moisture must also be completely removed after reduction to nitrogen gas, so pretreatment requires time. The disadvantage is that it requires a lot of time and is complicated to operate.
また、全窒素の測定装置としては、水素ガスが
流通されている還元触媒を充填した反応管に試料
を導入して、試料中の窒素をアンモニアに還元
し、得られた反応ガスから酸性ガスを除去した後
電量滴定により定量する装置が市販されている。
しかしこの装置では試料水中の水分が全量水蒸気
の状態でキヤリヤーガスに同伴されて電量滴定槽
に導入されるので、排水中の超微量の全窒素を測
定するために試料水の注入量を多くすると電解液
が希釈され、また温度も上昇し、正確な滴定がで
きなくなるので、試料水の注入量は0.5ml程度が
限度であつた。このため全窒素含量の測定下限は
せいぜい0.2PPm程度であり、更に微量の全窒素
が測定できる装置の開発が望まれていた。 In addition, as a total nitrogen measurement device, a sample is introduced into a reaction tube filled with a reduction catalyst through which hydrogen gas is flowing, the nitrogen in the sample is reduced to ammonia, and acidic gas is extracted from the resulting reaction gas. There are commercially available devices that quantify the amount by coulometric titration after removal.
However, with this device, all of the water in the sample water is introduced into the coulometric titration tank in the form of water vapor, which is accompanied by a carrier gas. The amount of sample water to be injected was limited to about 0.5 ml because the liquid would be diluted and the temperature would rise, making accurate titration impossible. For this reason, the lower limit for measuring total nitrogen content is at most about 0.2 PPm, and there has been a desire to develop an apparatus that can measure even trace amounts of total nitrogen.
本発明はこのような欠点のない超微量アンモニ
ア態窒素及び全窒素の測定装置を提供するもので
あつて、その要旨は、
(1) 下記の測定部及び蒸留部を有することを特徴
とする超微量アンモニア態窒素及び全窒素の測
定装置。 The present invention provides an apparatus for measuring ultratrace ammonia nitrogen and total nitrogen without such drawbacks, and the gist thereof is as follows: Instrument for measuring trace ammonia nitrogen and total nitrogen.
(a) 測定部
一端に試料導入口及び水素ガス導入管を
有し、他端にガス導出口を有する筒状反応
管の内部に還元触媒を充填した反応部、
ガス導入口及びガス導出口を有する容器
の内部に固体アルカリ性物質を充填した酸
性ガス除去部、
反応部及び酸性ガス除去部を加熱するた
めの加熱部、
ガス導入管、ガス導出口、電解電極、終
点検出電極及び電解槽を有する電量滴定
部、
よりなり、反応部及び酸性ガス除去部はそれ
ぞれ加熱部内に収納され、反応部のガス導出
口は酸性ガス除去部のガス導入口と連接さ
れ、酸性ガス除去部のガス導出口は後述する
蒸留槽のガス導入管と連接され、電量滴定部
のガス導入管は電解槽内の底部近くに開口さ
れている。 (a) Measuring section A reaction section consisting of a cylindrical reaction tube having a sample inlet and a hydrogen gas inlet at one end and a gas outlet at the other end filled with a reduction catalyst, a gas inlet and a gas outlet. an acidic gas removal section filled with a solid alkaline substance inside a container, a heating section for heating the reaction section and the acidic gas removal section, a gas introduction pipe, a gas outlet, an electrolytic electrode, an end point detection electrode, and an electrolytic cell. The coulometric titration section consists of a reaction section and an acidic gas removal section each housed in a heating section, a gas outlet of the reaction section is connected to a gas inlet of the acidic gas removal section, and a gas outlet of the acidic gas removal section is connected to a gas inlet of the acidic gas removal section. The gas introduction pipe of the coulometric titration unit is connected to a gas introduction pipe of a distillation tank, which will be described later, and is opened near the bottom of the electrolytic cell.
(b) 蒸留部
試料導入口、ガス導入管、及びガス導出
口を有し、かつ耐アルカリ性の材質からな
る蒸留槽
還流コンデンサー
よりなり、ガス導入管は蒸留槽内の底部近
くに開口し、還流コンデンサーの下端は蒸
留槽のガス導出口に連接され、上端は前記
電量滴定部のガス導入管と連接されてい
る。 (b) Distillation section A distillation tank that has a sample inlet, a gas inlet pipe, and a gas outlet, and is made of alkali-resistant material.It consists of a reflux condenser, and the gas inlet pipe opens near the bottom of the distillation tank, and the reflux The lower end of the condenser is connected to the gas outlet of the distillation tank, and the upper end is connected to the gas inlet pipe of the coulometric titration section.
に存する。 exists in
以下、本発明を図面と共に説明する。第1図は
本発明に係る装置の一例の説明図である。図中1
は測定部、2は蒸留部、3は制御部、12は蒸留
槽、18は電量滴定部、21,24は加熱部、2
2は酸性ガス除去部、25は反応部である。 The present invention will be explained below with reference to the drawings. FIG. 1 is an explanatory diagram of an example of a device according to the present invention. 1 in the diagram
2 is a measuring section, 2 is a distillation section, 3 is a control section, 12 is a distillation tank, 18 is a coulometric titration section, 21 and 24 are heating sections, 2
2 is an acidic gas removal section, and 25 is a reaction section.
測定部1は試料中の窒素化合物を還元してアン
モニアに転換するための反応部25、転換された
ガス中の酸性ガスを除去するための酸性ガス除去
部22、及びアンモニアを定量するための電量滴
定部18より構成される。 The measurement unit 1 includes a reaction unit 25 for reducing nitrogen compounds in a sample and converting them into ammonia, an acid gas removal unit 22 for removing acid gas from the converted gas, and a coulometric unit for quantifying ammonia. It is composed of a titration section 18.
反応部25は、一端に試料導入口4及び水素ガ
ス導入管26を有し、他端にガス導出口を有する
筒状の反応管の内部に、例えばニツケル、銅等の
金属粒子、または軽石、アルミナ等の不活性粒子
の表面をこれらの金属で被覆した金属触媒を充填
したものである。触媒粒子の大きさは反応管の大
きさにもよるが、通常0.5〜15mm程度のものが用
いられる。触媒は石英、アスベスト、アルミナ等
の耐熱性不活性物質を触媒粒子と混合して充填す
るのが好ましい。反応部25は例えば電熱線を内
蔵した電気炉等の加熱部24内に収納され、300
〜600℃程度の高温に保持される。 The reaction section 25 has a cylindrical reaction tube having a sample inlet 4 and a hydrogen gas inlet tube 26 at one end and a gas outlet at the other end. It is filled with a metal catalyst made by coating the surface of inert particles such as alumina with these metals. Although the size of the catalyst particles depends on the size of the reaction tube, catalyst particles of about 0.5 to 15 mm are usually used. The catalyst is preferably filled with a heat-resistant inert material such as quartz, asbestos, alumina, etc. mixed with catalyst particles. The reaction section 25 is housed in a heating section 24 such as an electric furnace having a built-in heating wire, and
It is maintained at a high temperature of ~600℃.
酸性ガス除去部22は反応部導出ガス中に含ま
れて来る硫化水素等の酸性ガスを除去するための
ものであり、通常ガス導入口及びガス導出口を有
する容器に、アルカリ金属又はアルカリ土類金属
の酸化物又は水酸化物の1種又は2種以上の混合
物を1〜7mm程度の粒状にしたアルカリ吸収剤を
充填したものである。アルカリ吸収剤の具体例と
しては、水酸化ナトリウムと酸化カルシウムとの
混合物(ソーダライム)、水酸化カルシウムと酸
化カシウムとの混合物、水酸化ナトリウムとα−
アルミナとの混合物、水酸化ナトリウムと炭酸カ
リウムとアスベストとの混合物等が挙げられる。
酸性ガス除去部22は、加熱部24と同様の加熱
部21内に収納され、室温(20℃)〜300℃程度
の温度に保持される。 The acid gas removal section 22 is for removing acid gases such as hydrogen sulfide contained in the gas discharged from the reaction section. It is filled with an alkali absorbent in which one or a mixture of two or more metal oxides or hydroxides is made into particles of about 1 to 7 mm. Specific examples of alkaline absorbents include a mixture of sodium hydroxide and calcium oxide (soda lime), a mixture of calcium hydroxide and calcium oxide, and a mixture of sodium hydroxide and α-
Examples include a mixture with alumina, a mixture of sodium hydroxide, potassium carbonate, and asbestos.
The acid gas removal section 22 is housed in the heating section 21 similar to the heating section 24, and is maintained at a temperature of about room temperature (20°C) to 300°C.
電量適定部18は、後述する蒸留部導出ガス中
のアンモニアを定量するためのものであり、摺合
せ蓋付の電解槽19と核槽内に設置された電解電
極16、検出電極17、ガス導入管15及びガス
導出管14より構成される。各電極16,17及
びガス導入管15は、下端が電解液中に埋没する
位置に設置される。 The coulometric adjustment unit 18 is for quantifying ammonia in the gas discharged from the distillation unit, which will be described later, and includes an electrolytic tank 19 with a sliding lid, an electrolytic electrode 16 installed in the nuclear tank, a detection electrode 17, and a gas. It is composed of an inlet pipe 15 and a gas outlet pipe 14. Each electrode 16, 17 and gas introduction pipe 15 are installed at a position where the lower end is submerged in the electrolyte.
蒸留部2は、試料中のアンモニア態窒素をアン
モニアガスとして追出すためとの前記酸性ガス除
去部22より導出されるガス中の水分を吸収除去
するためのものであり、試料導入口11、ガス導
入管10及びガス導出口を有する蒸留槽12、還
流コンデンサー6、及び加熱器13より構成され
る。ガス導入管10は一端が前記酸性ガス除去部
22のガス導出管20に連接され、他端が蒸留槽
12内の底部近くに開口されるが、開口端に多孔
板を取付けておくのが好ましい。蒸留槽12はそ
の内部に水酸化ナトリウム、水酸化カリウム等の
強アルカリの20〜50wt%、好ましくは20〜40wt
%の水溶液が入れられるので耐アルカリ性の材
質、例えば、高いニツケル合金鋼、セラミツク等
からなることが望ましい。還流コンデンサー6は
ミストの揮散を避け得るように、ガス流路に障害
物のあるものが好ましく、通常蛇管のものが用い
られるが、直管の場合は充填物を入れて用いれば
よい。還流コンデンサー6の下端開口は蒸留槽1
2のガス導出口に連通され、上端開口は導管5に
より前記電量滴定部18のガス導入管15に連接
される。蒸留槽12は加熱部13により70℃〜液
の沸騰温度、好ましくは100℃〜液の沸騰温度に
加熱される。 The distillation section 2 is for removing ammonia nitrogen in the sample as ammonia gas and for absorbing and removing moisture in the gas derived from the acidic gas removal section 22. It is composed of a distillation tank 12 having an inlet pipe 10 and a gas outlet, a reflux condenser 6, and a heater 13. One end of the gas introduction pipe 10 is connected to the gas discharge pipe 20 of the acidic gas removal section 22, and the other end is opened near the bottom of the distillation tank 12, but it is preferable to attach a perforated plate to the open end. . The distillation tank 12 contains 20 to 50 wt%, preferably 20 to 40 wt%, of a strong alkali such as sodium hydroxide or potassium hydroxide.
% aqueous solution, it is preferable to use an alkali-resistant material such as high nickel alloy steel or ceramic. The reflux condenser 6 is preferably one with an obstruction in the gas flow path so as to avoid volatilization of the mist, and a coiled pipe is usually used, but if it is a straight pipe, it may be filled with a filler. The bottom opening of the reflux condenser 6 is the distillation tank 1.
The upper end opening is connected to the gas introduction pipe 15 of the coulometric titration section 18 through a conduit 5. The distillation tank 12 is heated by the heating unit 13 to 70° C. to the boiling temperature of the liquid, preferably 100° C. to the boiling temperature of the liquid.
制御部3は、通常電量滴定制御装置7、温度制
御装置8及びガス流量制御装置9より構成され
る。電量滴定制御装置7に於いては、検出電極1
7より得られる水素イオン濃度に対応した電気信
号を増巾し、終点PH値からの偏差に見合つて比例
する電流出力に変換して電解電極16に電解電流
が供給される。一方、この電解電流は必要があれ
ばブランク電流を差引いた電流となし、分析値単
位換算、採取試料に対する割合を示すための試料
採取量係数等の補正演算を行なつた後積算され、
電気量に見合つた分析の直読値で表示される。 The control unit 3 usually includes a coulometric titration control device 7, a temperature control device 8, and a gas flow rate control device 9. In the coulometric titration control device 7, the detection electrode 1
The electric signal corresponding to the hydrogen ion concentration obtained from step 7 is amplified, converted into a current output proportional to the deviation from the end point PH value, and an electrolytic current is supplied to the electrolytic electrode 16. On the other hand, if necessary, this electrolytic current is calculated as a current after subtracting the blank current, and is integrated after performing correction calculations such as analysis value unit conversion and sampling amount coefficient to indicate the ratio to the collected sample.
It is displayed as a direct reading of analysis that corresponds to the amount of electricity.
温度制御装置8は、加熱部21,24及び加熱
器13の温度を所定の温度に調節するためのもの
である。 The temperature control device 8 is for adjusting the temperatures of the heating sections 21 and 24 and the heater 13 to a predetermined temperature.
ガス流量制御装置9は水素ガス導入管26から
導入される水素ガスの流量を所定の量に調節する
ためのものである。これらガスの流量は通常200
〜700ml/分、好ましくは400〜500ml/分の範囲
から選ばれる。 The gas flow rate control device 9 is for adjusting the flow rate of hydrogen gas introduced from the hydrogen gas introduction pipe 26 to a predetermined amount. The flow rate of these gases is typically 200
~700ml/min, preferably 400-500ml/min.
次にこのように構成された本発明装置を用いて
超微量の窒素化合物を含有する水の分析を行なう
場合について説明する。まず全窒素量の測定は、
試料水の所定量を測定部1の試料導入口4より注
入する。注入された試料水は水素ガス導入管26
より導入される水素ガスに同伴され、反応部25
で全ての窒素化合物がアンモニアに還元される。
生成したアンモニアガスは水素ガスと共に導管2
3より酸性ガス除去部22に導入され、共存する
酸性ガスが除去される。次いで導管20及び10
を経て蒸留槽12へ導入される。ガス中の水分は
蒸留槽12中のアルカリ液に吸収されることによ
り一部除去され、還流コンデンサー6で残余の水
分の大部分を除去された後、導管5及び15を経
て電解槽19へ導入され、電解槽19内に予じめ
入れられている例えば1%硫酸ナトリウム水溶液
等の電解液に吸収され、電量滴定が行なわれる。
滴定結果は電量滴定制御装置7に表示される。試
料水の注入量は含有される窒素化合物の量によつ
て異なるが、通常5μ〜5ml程度である。1回
の測定は4〜8分程度で終了する。 Next, a case will be described in which water containing an ultratrace amount of nitrogen compounds is analyzed using the apparatus of the present invention configured as described above. First, to measure the total nitrogen amount,
A predetermined amount of sample water is injected through the sample inlet 4 of the measuring section 1. The injected sample water is passed through the hydrogen gas introduction pipe 26.
The reaction part 25 is entrained by the hydrogen gas introduced from
All nitrogen compounds are reduced to ammonia.
The generated ammonia gas is sent to conduit 2 along with hydrogen gas.
3 into the acid gas removal section 22, where the coexisting acid gas is removed. Then conduits 20 and 10
It is introduced into the distillation tank 12 through the. A portion of the water in the gas is removed by being absorbed by the alkaline liquid in the distillation tank 12, and most of the remaining water is removed in the reflux condenser 6, after which it is introduced into the electrolytic tank 19 via conduits 5 and 15. The sample is absorbed into an electrolytic solution, such as a 1% aqueous sodium sulfate solution, which has been placed in advance in the electrolytic cell 19, and coulometric titration is performed.
The titration results are displayed on the coulometric titration control device 7. The amount of sample water to be injected varies depending on the amount of nitrogen compounds contained, but is usually about 5 μ to 5 ml. One measurement is completed in about 4 to 8 minutes.
次にアンモニア態窒素の測定は次のようにして
行なう。試料水の所定量を蒸留部2の試料導入口
11より注入する。注入された試料水中のアンモ
ニア態窒素はアンモニアガスとなり、ガス導入管
10から導入される水素ガスに同伴され、還流コ
ンデンサー6で同伴される水分の大部分を除去さ
れた後導管5及び15を経て電量滴定部18の電
解槽19に導入され、前記した方法に従つて電量
滴定される。試料水の注入量は含有される窒素化
合物の量によつて異なるが、通常5μ〜5ml程
度である。1回の測定は6〜8分程度で終了す
る。 Next, ammonia nitrogen is measured as follows. A predetermined amount of sample water is injected from the sample inlet 11 of the distillation section 2. The ammonia nitrogen in the injected sample water becomes ammonia gas, which is entrained by the hydrogen gas introduced from the gas introduction pipe 10, and after most of the entrained water is removed by the reflux condenser 6, it is passed through the conduits 5 and 15. It is introduced into the electrolytic cell 19 of the coulometric titration section 18 and subjected to coulometric titration according to the method described above. The amount of sample water to be injected varies depending on the amount of nitrogen compounds contained, but is usually about 5 μ to 5 ml. One measurement is completed in about 6 to 8 minutes.
以上詳述したように、本発明装置は水の影響の
ない蒸留部2を測定部1と組合して構成している
ので、試料の採取量を変えることにより、
0.005PPm程度の超微量の範囲迄の全窒素量及び
アンモニア態窒素量を精度よく、しかも短時間で
測定することができるので、環境水、排水、農
業、食品、医薬品関係の全窒素分析及びアンモニ
ア態窒素分析用として極めて有用である。 As described in detail above, since the device of the present invention is configured by combining the distillation section 2, which is not affected by water, with the measurement section 1, by changing the amount of sample collected,
It is possible to measure total nitrogen and ammonia nitrogen in ultra-trace amounts of around 0.005PPm with high precision and in a short time, making it ideal for total nitrogen analysis and ammonia analysis in environmental water, wastewater, agriculture, food, and pharmaceuticals. It is extremely useful for nitrogen analysis.
第1図は本発明に係る装置の一例の説明図であ
る。
1:測定部、2:蒸留槽、3:制御部、12:
蒸留槽、18:電量滴定部、21,24:加熱
部、22:酸性ガス除去部、25:反応部。
FIG. 1 is an explanatory diagram of an example of a device according to the present invention. 1: Measuring section, 2: Distillation tank, 3: Control section, 12:
Distillation tank, 18: coulometric titration section, 21, 24: heating section, 22: acidic gas removal section, 25: reaction section.
Claims (1)
とする超微量アンモニア態窒素及び全窒素の測定
装置。 (a) 測定部 一端に試料導入口及び水素ガス導入管を有
し、他端にガス導出口を有する筒状反応管の
内部に還元触媒を充填した反応部、 ガス導入口及びガス導出口を有する容器の
内部に固体アルカリ性物質を充填した酸性ガ
ス除去部、 反応部及び酸性ガス除去部を加熱するため
の加熱部、 ガス導入管、ガス導出口、電解電極、終点
検出電極及び電解槽を有する電量滴定部、 よりなり、反応部及び酸性ガス除去部はそれぞ
れ加熱部内に収納され、反応部のガス導出口は
酸性ガス除去部のガス導入口と連接され、酸性
ガス除去部のガス導出口は後述する蒸留槽のガ
ス導入管と連接され、電量滴定部のガス導入管
は電解槽内の底部近くに開口されている。 (b) 蒸留部 試料導入口、ガス導入管、及びガス導出口
を有し、かつ耐アルカリ性の材質からなる蒸
留槽 還流コンデンサー よりなり、ガス導入管は蒸留槽内の底部近くに
開口し、還流コンデンサーの下端は蒸留槽のガ
ス導出口に連接され、上端は前記電量滴定部の
ガス導入管と連接されている。[Scope of Claims] 1. An apparatus for measuring ultratrace ammonia nitrogen and total nitrogen, characterized by having the following measurement section and distillation section. (a) Measuring section A reaction section consisting of a cylindrical reaction tube having a sample inlet and a hydrogen gas inlet at one end and a gas outlet at the other end filled with a reduction catalyst, a gas inlet and a gas outlet. an acidic gas removal section filled with a solid alkaline substance inside a container, a heating section for heating the reaction section and the acidic gas removal section, a gas introduction pipe, a gas outlet, an electrolytic electrode, an end point detection electrode, and an electrolytic cell. The coulometric titration section consists of a reaction section and an acidic gas removal section each housed in a heating section, a gas outlet of the reaction section is connected to a gas inlet of the acidic gas removal section, and a gas outlet of the acidic gas removal section is connected to a gas inlet of the acidic gas removal section. The gas introduction pipe of the coulometric titration unit is connected to a gas introduction pipe of a distillation tank, which will be described later, and is opened near the bottom of the electrolytic cell. (b) Distillation section A distillation tank that has a sample inlet, a gas inlet pipe, and a gas outlet, and is made of alkali-resistant material.It consists of a reflux condenser, and the gas inlet pipe opens near the bottom of the distillation tank, and the reflux The lower end of the condenser is connected to the gas outlet of the distillation tank, and the upper end is connected to the gas inlet pipe of the coulometric titration section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6775781A JPS57182647A (en) | 1981-05-06 | 1981-05-06 | Measuring apparatus of infinitesimal ammoniacal nitrogen and total nitrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6775781A JPS57182647A (en) | 1981-05-06 | 1981-05-06 | Measuring apparatus of infinitesimal ammoniacal nitrogen and total nitrogen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57182647A JPS57182647A (en) | 1982-11-10 |
| JPH0241706B2 true JPH0241706B2 (en) | 1990-09-19 |
Family
ID=13354124
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6775781A Granted JPS57182647A (en) | 1981-05-06 | 1981-05-06 | Measuring apparatus of infinitesimal ammoniacal nitrogen and total nitrogen |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57182647A (en) |
-
1981
- 1981-05-06 JP JP6775781A patent/JPS57182647A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57182647A (en) | 1982-11-10 |
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