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JPH01206256A - Method and apparatus for automatic titration of process fluid - Google Patents

Method and apparatus for automatic titration of process fluid

Info

Publication number
JPH01206256A
JPH01206256A JP3051388A JP3051388A JPH01206256A JP H01206256 A JPH01206256 A JP H01206256A JP 3051388 A JP3051388 A JP 3051388A JP 3051388 A JP3051388 A JP 3051388A JP H01206256 A JPH01206256 A JP H01206256A
Authority
JP
Japan
Prior art keywords
titration
reagent
container
process fluid
amount
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.)
Pending
Application number
JP3051388A
Other languages
Japanese (ja)
Inventor
Isao Tanaka
伊佐男 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Kasei Corp
Mitsubishi Chemical Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Kasei Corp, Mitsubishi Chemical Industries Ltd filed Critical Mitsubishi Kasei Corp
Priority to JP3051388A priority Critical patent/JPH01206256A/en
Publication of JPH01206256A publication Critical patent/JPH01206256A/en
Pending legal-status Critical Current

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  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)

Abstract

PURPOSE:To accurately foreknow the replenishing period of a reagent, by taking a definite amount of the reagent in a titration container and subsequently titrating the same by a process fluid to quantity the amount of the substance to be titrated in the process fluid. CONSTITUTION:A dry gas is introduced into a titration container 1 from a gas introducing pipe 7 to dry said container 1 and a predetermined amount of a Kar1 Fischer reagent is introduced into said container 1 from a reagent container 8 by a pump 9 while a predetermined amount of a titration solvent is introduced into the container 1 from a reagent container 1 by a pump 12. Subsequently, a process fluid is introduced into the container 1 from a process fluid source 15' through a pump 16 to advance titration reaction. The advance process of titration is traced by a final point detection mechanism 2 and the liquid feed amount of the pump 16 is adjusted corresponding to the detection signal thereof and, when titration reaches a final point, the moisture content of the process fluid is calculated from the amount of the process fluid used in titration by a calculation/control mechanism 20 to be displayed. Other valve 4 is opened to discharge the liquid in the container 1 to wash said container 1.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明はプロセス流体の自動滴定方法及びそのための装
置に関するものである。特に本発明はプロセス内の流体
を定期的に自動滴定装置により滴定する方法に関するも
ので−ある。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an automatic process fluid titration method and apparatus therefor. In particular, the present invention relates to a method for periodically titrating a process fluid using an automatic titrator.

〈従来の技術〉 プロセス内の流体を定期的に自動滴定装置を用いて滴定
することは広く行なわれている。最も一般的な自動滴定
方法では、プロセス内の流体を一定量滴定容器に取シ入
れ、次いでこれに滴定試薬を滴下して滴定を行ない、こ
の滴定の過程を終点検出機構で追跡して終点に到達した
時点で滴定試薬の滴下を中止し、この時点までに消費し
た試薬量に基づいて被滴定物の量を算出し、且つ滴定容
器内の液体を排出し更に必要に応じて容器内を洗浄して
次回の滴定に備えるという一連の過程を自動的に反復す
る。
<Prior Art> It is widely practiced to periodically titrate a fluid in a process using an automatic titration device. In the most common automatic titration method, a fixed amount of the fluid in the process is introduced into a titration vessel, a titration reagent is then added dropwise to the titration container, and the titration process is tracked by an endpoint detection mechanism to reach the endpoint. At this point, stop dropping the titration reagent, calculate the amount of titrant based on the amount of reagent consumed up to this point, drain the liquid in the titration container, and clean the container as necessary. The process of preparing for the next titration is automatically repeated.

〈発明が解決しようとする課題〉 このような自動滴定方法の問題点は、試薬容器の保守が
煩わしいことである。すなわち毎回の滴定に要する試薬
量が変化するので、試薬容器を時々点検して、試薬が欠
乏しないように常に試薬の補給に気を付けなければなら
ない。
<Problems to be Solved by the Invention> A problem with such an automatic titration method is that maintenance of the reagent container is troublesome. That is, since the amount of reagent required for each titration changes, it is necessary to check the reagent container from time to time and be careful to replenish the reagent at all times so as not to run out of reagent.

く課題を解決するための手段〉 本発明は滴定容器に一定量の試薬を取り入れ、次いでこ
れをプロセス流体で滴定することにより、プロセス流体
中の被滴定物量を定量するものである。
Means for Solving the Problems> The present invention measures the amount of a titrant in a process fluid by taking a certain amount of a reagent into a titration container and then titrating it with a process fluid.

すなわち、本発明は、流体の存在する系から抜出すプロ
セス流体を滴定により自動的に反復分析する方法を提供
するものであり、この方法によれば、1回の分析は (イ)滴定容器に試薬容器から一定量の試薬を試薬定量
供給機構を介して供給する試薬導入過程 (ロ)滴定容器にプロセス流体を制御した態様で供給し
て滴定容器中の試薬と被滴定物とを反応させる滴定過程 (う 滴定過程の間における試薬と被滴定物との反応を
追跡し、反応終点に達した時点でプロセス流体の供給を
中止する終点検出過程に)滴定容器内の液体を排出して
試薬を供給する前の状態に復帰させる後処理過程 の各過程からなり、試薬導入過程と滴定過程の間に滴定
容器に供給された試薬量とプロセス流体量とから被滴定
物量が算出される。
That is, the present invention provides a method for automatically and repeatedly analyzing a process fluid extracted from a system in which the fluid exists by titration. According to this method, one analysis consists of (a) Reagent introduction process in which a fixed amount of reagent is supplied from a reagent container via a reagent quantitative supply mechanism (b) Titration in which the process fluid is supplied to the titration container in a controlled manner to cause the reagent in the titration container to react with the titrant. During the titration process, the reaction between the reagent and the titrant is tracked and the supply of process fluid is stopped when the end point of the reaction is reached.During the end point detection process, the liquid in the titration vessel is drained and the reagent is removed. It consists of each step of the post-treatment step to return to the state before supply, and the amount of the titrant is calculated from the amount of reagent and process fluid supplied to the titration container between the reagent introduction step and the titration step.

また、本発明は、流体の存在する系から抜出すプロセス
流体を滴定により自動的に反復分析するプロセス分析計
も提供するものであり、この分析計は (イ)滴定過程を追跡して終点を検出する終点検出機構
及び溶液排出機構を備えた滴定容器(ロ)試薬容器、及
び試薬容器と滴定容器とを連絡する導管を備え且つ試薬
定量供給機構を有する試薬供給系 (ハ) プロセス流体の存在する系と滴定容器とを連絡
する導管を備え且つ導管を経て滴定容器にプロセス流体
を制御された態様の下に供給するプロセス流体供給機構
を有するプロセス流体供給系 に) プロセス流体供給機構で測定されたプロセス流体
供給量に基づいてプロセス流体中の被滴定物の量を算出
する計算機構 (ホ)滴定容器への各流体の供給及びこれからの排出を
含め装置全体の作動を制御する制御機、溝の各機構から
成っていて、そのプロセス流体供給機構はプランジャー
型ポンプとこれを駆動するパルスモータ−を備えており
、且つパルスモータ−は終点検出機構からの信号により
制御されるようになっており、ポンプは7回の作動毎に
その吸引したプロセス流体を全量吐出するようになって
いる。
The present invention also provides a process analyzer that automatically and repeatedly analyzes a process fluid extracted from a system in which the fluid exists by titration, and this analyzer (a) tracks the titration process and determines the end point. (b) A reagent supply system comprising a reagent container and a conduit connecting the reagent container and the titration container and a reagent quantitative supply mechanism (c) Presence of process fluid (a process fluid supply system having a process fluid supply system comprising a conduit communicating the titration vessel with the titration vessel and a process fluid supply mechanism for supplying the process fluid to the titration vessel via the conduit in a controlled manner) A calculation mechanism that calculates the amount of the titrant in the process fluid based on the amount of process fluid supplied. The process fluid supply mechanism is equipped with a plunger type pump and a pulse motor that drives it, and the pulse motor is controlled by a signal from an end point detection mechanism. The pump is configured to discharge the entire amount of the sucked process fluid every seven operations.

本発明の一実施態様を第1図に基づいて説明すれば、(
1)は滴定容器、(2)は滴定終点を電気的に検出する
終点検出機構、(3)は同じく滴定終点を光学的に検出
する終点検出機構である。終点検出機構としては、プロ
セス流体の種類と滴定反応に応じて(2)と(3)との
いずれか一方を備えていれば良い。(4)は滴定容器の
底部に設けた排液弁、(5)は滴定容器の上部に設けた
オーツく−フロー管であり、滴定終了時に滴定容器内に
存在すると想定される溶液の液面よりも高い位置に開口
している。(6)は攪拌機、(7)は乾燥ガス導入管で
ある。(8)は第1の試薬容器、(9)は第1の定量ポ
ンプ、叫は第1の試薬導管である。(11)、CIの、
αJはそれぞれ第ユの試薬容器、定量ポンプ、試薬導管
である。滴定の種類によっては試薬容器等は一方のみで
良いことは勿論である。また定量ポンプは予じめ定めら
れた一定量の試薬を精度よく送出できるものであればよ
い。αゆはプロセス流体の流れている管路などのプロセ
ス流体源であシ、α$、αe′及び(1γ′はプロセス
流体をプロセス流体源から滴定容器(1)に導く導管、
αQはこの導管の途中に設けられた定量ポンプ、α〃及
びα〃′はプロセス流体源を切替える為の弁である。定
量ポンプαQは送出量を精度よく任意の量に制御し、か
つ計測できるものでなければならず、例えば電気化学計
器(掬製のPPZ−P//型のようなパルスモータ−で
、駆動されるプランジャー型ポンプが用いられる。
One embodiment of the present invention will be described based on FIG.
1) is a titration container, (2) is an end point detection mechanism that electrically detects the titration end point, and (3) is an end point detection mechanism that also optically detects the titration end point. The end point detection mechanism may include either (2) or (3) depending on the type of process fluid and the titration reaction. (4) is a drain valve installed at the bottom of the titration container, and (5) is an automatic flow tube installed at the top of the titration container. It opens at a higher position. (6) is a stirrer, and (7) is a dry gas introduction pipe. (8) is a first reagent container, (9) is a first metering pump, and (9) is a first reagent conduit. (11), CI's,
αJ are the first reagent container, metering pump, and reagent conduit, respectively. Of course, depending on the type of titration, only one reagent container may be used. Further, the metering pump may be of any type as long as it can accurately deliver a predetermined amount of reagent. αyu is the process fluid source, such as a conduit through which the process fluid is flowing; α$, αe' and (1γ' are the conduits leading the process fluid from the process fluid source to the titration vessel (1);
αQ is a metering pump provided in the middle of this conduit, and α〃 and α〃' are valves for switching the process fluid source. The metering pump αQ must be capable of controlling and measuring the delivery amount to any desired amount with high precision; A plunger type pump is used.

本発明の好ましい実施態様にあっては、7回の滴定で必
要とすると考えられるプロセス流体量よシも1回の吐出
容量の小さいポンプを用い、1回の滴定の間に複数回に
わ′fc!llプロセス流体源からプロセス流体をポン
プに吸引するようにする。特に好ましくは、ポンプを作
動する毎にプロセス流体源からプロセス流体を吸引し、
且つその全量を滴定容器に吐出するようにする。
In a preferred embodiment of the present invention, a pump with a discharge capacity smaller than the amount of process fluid considered necessary for seven titrations is used, and multiple titrations are performed during one titration. fc! Process fluid is drawn into the pump from a process fluid source. Particularly preferably, each actuation of the pump draws process fluid from a process fluid source;
And the entire amount is discharged into the titration container.

このようにすることにより、7回の滴定の間に滴定容器
に供給されるプロセス流体を、その間におけるプロセス
流体源のプロセス流体の平均値に近いものとすることが
できる。その結果プロセス流体源に何らかの原因で一時
的ないし局所的な変化が生じても、それが測定結果に大
きな影響を及ぼすのを避けることができる。なお、導管
(1*、α9′及びα→″の容量は、7回の滴定に必要
とすると考えられるプロセス流体量よりも十分に小さく
しておくことは勿論である。0→は標準溶液の容器、α
つはポンプαQの吸入端をこの容器α団に切替えるため
の弁である。標準溶液は試薬の力価を検定する為のもの
であり、試薬が保存安定性の良いものである場合には不
必要である。00は装置全体の作動を制御し、かつ滴定
結果を算出して表示する計算・制御機構で、その主たる
制御機能は予じめ定められたタイム・スケジュールに従
って順次ポンプ及び弁を作動させること、及び終点検出
機構からの滴定の進行過程を示す信号に応じてポンプα
Qの作動を制御し滴定の終点が正確に検出できるように
することにある。
By doing so, the process fluid supplied to the titration vessel during the seven titrations can be close to the average value of the process fluid of the process fluid source during that period. As a result, even if a temporary or local change occurs in the process fluid source for some reason, it can be avoided from greatly affecting the measurement results. It goes without saying that the capacity of the conduits (1*, α9' and α→'' should be sufficiently smaller than the amount of process fluid considered necessary for seven titrations. 0→ is the volume of the standard solution. container, α
One is a valve for switching the suction end of pump αQ to this container α group. The standard solution is used to test the potency of the reagent, and is unnecessary if the reagent has good storage stability. 00 is a calculation/control mechanism that controls the operation of the entire device and calculates and displays titration results. Its main control functions are to sequentially operate the pumps and valves according to a predetermined time schedule, and Pump α responds to the signal indicating the progress of titration from the end point detection mechanism.
The purpose is to control the operation of Q so that the end point of titration can be accurately detected.

く作 用〉 本発明に従い、石油化学工業等における有機液体中の微
量水分全カール・フィシャー試薬を用いて滴定する場合
について説明する。
Effect> A case will be described in which, according to the present invention, a trace amount of water in an organic liquid in the petrochemical industry is titrated using a Karl-Fischer reagent.

先ず内部を十分に洗浄したのちガス導入管(7)から乾
燥ガスを導入してよく乾燥させた滴定容器+11に、試
薬容器(8)からカール・フィシャー試薬、試薬容器α
υから滴定用溶媒を、それぞれポンプL9L 142 
f経て所定量づつ導入する。次いでプロセス流体源07
から、プロセス流体をポンプ(IQを経て滴定容器[1
1に導入して滴定反応を進行させる。滴定の進行過程は
終点検出機構(2)で追跡し、その検出信号に応じてポ
ンプαQの送液量を調節する。終点検出機、構(2)及
び検出信号に応じてのポンプ送液量の調節方式としては
、市販のカール・フィシャー容量滴定装置で用いられて
いるものを準用することができる。滴定が終点に達した
ならば、計算・制御機構−で滴定に用いたプロセス流体
量からその甲の水分量を算出して表示する。他方では弁
(4)を開放して滴定容器(1)内の液を排出し、次い
で弁(4)f、閉じたのち、次回に滴定すべきプロセス
流体を抜出すプロセス流体源(19″からポンプOQに
よりプロセス流体を滴定容器(1)内に導入してオーバ
ーフロー管(5)から流出させて容器内を洗浄したのち
、弁(4)を開放して排液する。更に乾燥ガス導入管(
力から乾燥ガスを導入して容器内を十分に乾燥して次回
の滴定に備える。
First, after thoroughly cleaning the inside, drying gas was introduced from the gas introduction pipe (7) and the Karl Fischer reagent and reagent container α were added from the reagent container (8) to the titration container +11, which was thoroughly dried.
Pump the titration solvent from υ to each pump L9L 142
A predetermined amount is introduced after f. Then process fluid source 07
from the titration vessel [1
1 to proceed with the titration reaction. The progress of the titration is tracked by an end point detection mechanism (2), and the amount of liquid fed by the pump αQ is adjusted in accordance with the detection signal. As the end point detector, the mechanism (2), and the method of adjusting the amount of liquid pumped according to the detection signal, those used in a commercially available Karl Fischer volumetric titration device can be applied mutatis mutandis. When the titration reaches the end point, the calculation/control mechanism calculates and displays the moisture content of the instep from the amount of process fluid used in the titration. On the other hand, the valve (4) is opened to drain the liquid in the titration vessel (1), and then the valve (4) f is closed and the process fluid source (19'') is opened from which the process fluid to be titrated next time is drawn out. The process fluid is introduced into the titration container (1) by the pump OQ and flows out from the overflow pipe (5) to clean the inside of the container, and then the valve (4) is opened to drain the liquid.
Introduce drying gas to thoroughly dry the inside of the container in preparation for the next titration.

なお、カール・フィシャー試薬の力価を検定する際は、
プロセス流体の代シに標準溶液容器α樽内の水−メタノ
ール標準液を用いて滴定容器(1)の洗浄及び滴定を行
なえばよい(洗浄に水−メタノール標準液を用いるのは
、ポンプal19及ヒ導管a5内の液の置換のためであ
る)。
When testing the potency of Karl Fischer reagent,
The water-methanol standard solution in the standard solution container α barrel can be used instead of the process fluid for cleaning and titration of the titration container (1). This is for replacing the liquid in the conduit a5).

〈効 果〉 本発明によれば一回の滴定に消費する試薬量は一定なの
で、滴定の周期に応じて試薬の補給時期を正確に予知す
ることができる。また、−回の滴定に際し、流体源から
複数回にわたりプロセス流体を抜出して滴定に用いるこ
とにより、プロセス流体源の一時的ないし局所的変動の
影響を軽減することができる。
<Effects> According to the present invention, since the amount of reagent consumed in one titration is constant, the time to replenish the reagent can be accurately predicted according to the titration cycle. Furthermore, by extracting the process fluid from the fluid source multiple times and using it for the titration during the second titration, it is possible to reduce the influence of temporary or local fluctuations in the process fluid source.

更に、本発明は、カール・フィシャー試薬と滴定溶媒の
ように、2種以上の試薬をその場で混合して使用する場
合には特に有利である。何故ならば、本発明によれば混
合後の滴定に供する状態の試薬の力価を標準液で検定で
きるからである。若し常法のようにプロセス流体の一定
量を滴定容器にと9、これを試薬で滴定しようとすれば
、一種以上の試薬を一定比率で、且つ送液量を制御しつ
つ、送液する機構が必要であシ、その機、溝は本発明で
必要とするものよりも複雑とならざるを得ない。
Furthermore, the present invention is particularly advantageous when two or more reagents are used as a mixture on the spot, such as a Karl Fischer reagent and a titration solvent. This is because, according to the present invention, the titer of a reagent ready for titration after mixing can be assayed using a standard solution. If you want to titrate a certain amount of process fluid into a titration container9 with a reagent as in the conventional method, one or more reagents must be fed at a fixed ratio and while controlling the amount of liquid fed. A mechanism is required, and the machine and groove are more complicated than those required by the present invention.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明を実施する装置の7例の模式/:滴定容
器1.2:終点検出機構(電気式)、3:終点検出機構
(光学式)、tl:排液弁、Sニオ−バーフロー管、6
:攪拌機、7:乾燥ガス導入管、g、ii:試薬容器、
ワ、/2=試薬ポンプ、10. /、? :試薬導管、
/ILt= プロセス流体源、/S%/3’、ls″:
プロセス流体導管、lA:  プロセス流体ポンプ、7
7′、/7”:プロセス流体の切替用弁、7g:標準浴
液容器、/ヲ:標準溶液の切替弁1.2o:計算、制御
機構特許出願人 三菱化成工業株式会社 代 理 人 弁理士 長谷用   − ほか/名
FIG. 1 is a schematic diagram of seven examples of apparatus for carrying out the present invention. Bar flow tube, 6
: Stirrer, 7: Dry gas introduction tube, g, ii: Reagent container,
wa, /2=reagent pump, 10. /,? : Reagent conduit,
/ILt=process fluid source, /S%/3',ls'':
Process fluid conduit, lA: Process fluid pump, 7
7′, /7”: Process fluid switching valve, 7g: Standard bath liquid container, /wo: Standard solution switching valve 1.2o: Calculation, control mechanism Patent applicant Mitsubishi Chemical Industries, Ltd. Representative Patent attorney For Hase - Others/Names

Claims (4)

【特許請求の範囲】[Claims] (1)流体の存在する系から抜出すプロセス流体を滴定
により自動的に反復分析する方法であって、1回の分析
が (イ)滴定容器に試薬容器から一定量の試薬を試薬定量
供給機構を介して供給する試薬導 入過程 (ロ)滴定容器にプロセス流体を制御した態様で供給し
て滴定容器中の試薬と被滴定物と を反応させる滴定過程 (ハ)滴定過程の間における試薬と被滴定物との反応を
追跡し、反応終点に達した時点で プロセス流体の供給を中止する終点検出過 程 (ニ)滴定容器内の液体を排出して容器を試薬を供給す
る前の状態に復帰させる後処理過 程 から成り、試薬導入過程と滴定過程の間に滴定容器に供
給された試薬量とプロセス流体量とから被滴定物量を算
出することを特徴とする自動滴定方法。
(1) A method in which a process fluid extracted from a system in which the fluid is present is automatically and repeatedly analyzed by titration, in which one analysis consists of (a) a reagent quantitative supply mechanism that supplies a fixed amount of reagent from a reagent container to a titration container; (b) A titration process in which the process fluid is supplied to the titration vessel in a controlled manner to cause the reagent in the titration vessel to react with the titrant. (c) The process of introducing the reagent and the titrant during the titration process. An end point detection process in which the reaction with the titrant is tracked and the supply of process fluid is stopped when the reaction end point is reached. (d) The liquid in the titration container is drained to return the container to the state before supplying the reagent. An automatic titration method comprising a post-treatment process and characterized in that the amount of the substance to be titrated is calculated from the amount of reagent supplied to the titration container and the amount of process fluid between the reagent introduction process and the titration process.
(2)流体の存在する系から抜出すプロセス流体中の水
分を、カール・フィシャー試薬を用いて自動的に反復し
て分析する方法であって、1回分の分析が (イ)滴定容器に、カール・フィシャー試薬及びカール
・フィシャー滴定用溶媒を、それ ぞれの容器から一定量づつ供給する試薬導 入過程 (ロ)滴定容器に、プロセス流体をその量を制御しつつ
供給して滴定容器中のカール・フ ィシャー試薬と反応させる滴定過程 (ハ)滴定過程の間におけるカール・フィシャー試薬と
水分との反応を追跡し、反応終点 に達した時点でプロセス流体の供給を中止 する終点検出過程 (ニ)滴定容器内の液体を排出して、カール・フィシャ
ー試薬を供給する前の状態に復帰 させる後処理過程 から成り、試薬導入過程と滴定過程の間に滴定容器に供
給された試薬量とプロセス流体量とからプロセス流体中
の水分量を算出することを特徴とする自動滴定方法。
(2) A method of automatically and repeatedly analyzing water in a process fluid extracted from a system in which the fluid exists, using a Karl Fischer reagent, in which one analysis is performed by (a) placing a titration vessel in a titration vessel; Reagent introduction process in which Karl Fischer reagent and Karl Fischer titration solvent are supplied in fixed amounts from each container (b) The process fluid is supplied to the titration container while controlling its amount, and the Karl Fischer titration in the titration container is Titration process of reacting with Fischer reagent (c) End point detection process of tracking the reaction between Karl Fischer reagent and water during the titration process and stopping the supply of process fluid when the reaction end point is reached (d) Titration vessel It consists of a post-treatment process in which the liquid in the titration vessel is drained to return the state to the state before supplying the Karl Fischer reagent, and the amount of reagent and process fluid supplied to the titration vessel between the reagent introduction process and the titration process are An automatic titration method characterized by calculating the amount of water in a process fluid.
(3)請求項(1)又は(2)記載の自動滴定方法にお
いて、滴定過程においてプロセス流体の存在する系から
複数回にわたりプロセス流体を抜出しこれを滴定容器に
供給することを特徴とする方法。
(3) The automatic titration method according to claim (1) or (2), characterized in that during the titration process, the process fluid is extracted from the system where the process fluid is present multiple times and supplied to the titration vessel.
(4)流体の存在する系から抜出すプロセス流体を滴定
により自動的に反復分析するための装置であって、 (イ)滴定過程を追跡して終点を検出する終点検出機構
及び溶液排出機構を備えた滴定容 器 (ロ)試薬容器、及び試薬容器と滴定容器とを連絡する
導管を備え且つ試薬定量供給機構 を有する試薬供給系 (ハ)プロセス流体の存在する系と滴定容器とを連絡す
る導管を備え且つ導管を経て滴定 容器にプロセス流体を制御された態様の下 に供給するプロセス流体供給機構を有する プロセス流体供給系 (ニ)プロセス流体供給機構で測定されたプロセス流体
量に基づいてプロセス流体中の被 滴定物の量を算出する計算機構 (ホ)滴定容器への各流体の供給及びこれからの排出を
含め装置全体の作動を制御する制 御機構の各機構から成っており、且つその プロセス流体供給機構は、プランジャー型 ポンプとこれを駆動するパルスモーターを 備えており、且つパルスモーターは終点検 出機構からの信号により制御されるように なっており、ポンプは1回の作動毎にその 吸引したプロセス流体を全量吐出するよう になっていることを特徴とする装置。
(4) An apparatus for automatically and repeatedly analyzing a process fluid extracted from a system in which the fluid exists, by titration, which includes (a) an end point detection mechanism for tracking the titration process and detecting the end point, and a solution discharge mechanism. (b) A reagent supply system comprising a reagent container and a conduit connecting the reagent container and the titration container and having a reagent quantitative supply mechanism (c) A conduit connecting the system in which the process fluid exists and the titration container. and having a process fluid supply mechanism for supplying the process fluid to the titration vessel via a conduit in a controlled manner. It consists of a calculation mechanism that calculates the amount of the titrant in the titration container (e) and a control mechanism that controls the operation of the entire device, including the supply and discharge of each fluid to the titration container, and the process fluid The supply mechanism is equipped with a plunger type pump and a pulse motor that drives the plunger type pump.The pulse motor is controlled by a signal from the end point detection mechanism, and the pump performs suction every time it is operated. 1. A device characterized in that the device is configured to discharge the entire amount of process fluid.
JP3051388A 1988-02-12 1988-02-12 Method and apparatus for automatic titration of process fluid Pending JPH01206256A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3051388A JPH01206256A (en) 1988-02-12 1988-02-12 Method and apparatus for automatic titration of process fluid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3051388A JPH01206256A (en) 1988-02-12 1988-02-12 Method and apparatus for automatic titration of process fluid

Publications (1)

Publication Number Publication Date
JPH01206256A true JPH01206256A (en) 1989-08-18

Family

ID=12305892

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3051388A Pending JPH01206256A (en) 1988-02-12 1988-02-12 Method and apparatus for automatic titration of process fluid

Country Status (1)

Country Link
JP (1) JPH01206256A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS597938A (en) * 1982-07-06 1984-01-17 Ricoh Co Ltd thermal copy machine
JPS5987350A (en) * 1982-11-11 1984-05-19 Sumitomo Chem Co Ltd Method and apparatus for performing full automatic titration analysis of sample
JPS6051459B2 (en) * 1978-03-24 1985-11-14 ウイリアム・エイチ・ロウラ−・インコ−ポレ−テツド amidinourea
JPS6330513A (en) * 1986-07-25 1988-02-09 Dainippon Ink & Chem Inc Aqueous polymer dispersion

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6051459B2 (en) * 1978-03-24 1985-11-14 ウイリアム・エイチ・ロウラ−・インコ−ポレ−テツド amidinourea
JPS597938A (en) * 1982-07-06 1984-01-17 Ricoh Co Ltd thermal copy machine
JPS5987350A (en) * 1982-11-11 1984-05-19 Sumitomo Chem Co Ltd Method and apparatus for performing full automatic titration analysis of sample
JPS6330513A (en) * 1986-07-25 1988-02-09 Dainippon Ink & Chem Inc Aqueous polymer dispersion

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