JPH0545138B2 - - Google Patents

Info

Publication number
JPH0545138B2
JPH0545138B2 JP60151697A JP15169785A JPH0545138B2 JP H0545138 B2 JPH0545138 B2 JP H0545138B2 JP 60151697 A JP60151697 A JP 60151697A JP 15169785 A JP15169785 A JP 15169785A JP H0545138 B2 JPH0545138 B2 JP H0545138B2
Authority
JP
Japan
Prior art keywords
black liquor
concentration
organic component
organic
component concentration
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 - Fee Related
Application number
JP60151697A
Other languages
Japanese (ja)
Other versions
JPS6212839A (en
Inventor
Yoshikazu Fukushima
Yohei Shiogoshi
Masaru Nishimura
Yasumitsu Kurosaki
Toshuki Idoko
Shiro Nakabayashi
Kazuyuki Iizuka
Ryuichi Kuwata
Tsugio Kumaki
Itsuo Chikahisa
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.)
Toshiba Corp
Jujo Paper Co Ltd
Kawasaki Heavy Industries Ltd
Kawasaki Motors Ltd
Original Assignee
Toshiba Corp
Jujo Paper Co Ltd
Kawasaki Heavy Industries Ltd
Kawasaki Jukogyo KK
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 Toshiba Corp, Jujo Paper Co Ltd, Kawasaki Heavy Industries Ltd, Kawasaki Jukogyo KK filed Critical Toshiba Corp
Priority to JP15169785A priority Critical patent/JPS6212839A/en
Publication of JPS6212839A publication Critical patent/JPS6212839A/en
Publication of JPH0545138B2 publication Critical patent/JPH0545138B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、チツプ蒸解工程および回収ボイラの
操業管理等に利用する方法および装置に係わり、
特に紙パルプを生産するチツプ蒸解工程の廃液で
ある黒液の有効利用を図るために有機成分濃度を
連続的に推定する黒液の有機成分濃度推定方法お
よびその推定装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method and an apparatus used in a chip cooking process and operation management of a recovery boiler, etc.
In particular, the present invention relates to a method and apparatus for estimating the concentration of organic components in black liquor, which continuously estimates the concentration of organic components in order to effectively utilize black liquor, which is the waste liquid of the chip cooking process for producing paper pulp.

〔従来の技術〕[Conventional technology]

チツプ蒸解工程では、チツプ、薬剤および蒸気
等を用いてパルプを生産するが、このときチツプ
蒸解工程から廃液として希黒液が排出されるの
で、この希黒液を濃縮器で濃縮して濃黒液とした
後、回収ボイラ内へ噴射する。回収ボイラは濃黒
液を浮遊乾燥させてチヤーベツトを形成するとと
もに、このチヤーベツトを燃焼することにより回
収ボイラから蒸気、硫酸ナトリウムを主成分とす
るダストおよびチツプ蒸解用薬剤原料等を回収
し、蒸気は例えばプラントの各種駆動装置の駆動
や自家発電、更にはチツプ蒸解工程等に使用さ
れ、一方、前記回収ダストは前記濃黒液に混合使
用され、また薬剤原料は薬剤としてチツプ蒸解工
程に使用される。
In the chip-cooking process, pulp is produced using chips, chemicals, steam, etc. At this time, dilute black liquor is discharged as waste liquid from the chip-cooking process, so this dilute black liquor is concentrated in a concentrator to produce a thick black liquor. After turning it into a liquid, it is injected into a recovery boiler. The recovery boiler suspends and dries the concentrated black liquor to form a charbet, and by burning this charbet, steam, dust mainly composed of sodium sulfate, raw materials for chips cooking chemicals, etc. are recovered from the recovery boiler, and the steam is For example, it is used to drive various drive devices in plants, in-house power generation, and even in the chip cooking process, etc. On the other hand, the collected dust is mixed with the concentrated black liquor, and the drug raw material is used as a drug in the chip cooking process. .

ところで、前記チツプ蒸解工程から排出される
黒液は有機成分、無機成分および水分により構成
されているが、そのうち有機成分の組成物質とし
てはリグニン・ヒドロキシン酸類などにより構成
され、一方、無機成分は炭酸ナトリウム、硫酸ナ
トリウムおよび硫化ナトリウムなどにより構成さ
れている。
By the way, the black liquor discharged from the chip cooking process is composed of organic components, inorganic components, and water. Of these, the organic components are composed of lignin and hydroxyl acids, while the inorganic components are It is composed of sodium carbonate, sodium sulfate, sodium sulfide, etc.

特に、前記黒液の有機成分濃度は、回収ボイラ
の操業管理やチツプ蒸解工程の操業管理に際して
非常に重要な情報源となつているが、チツプ蒸解
工程で使用されるチツプの材種に基づいて投入さ
れる薬剤の調合、量、蒸解時間などの調整によつ
て黒液性状が変化すると、その変化に伴つて変動
する性質をもつており、また、前記濃縮器の濃縮
程度や濃黒液への混合ダスト量の変化によつて変
動する性質をもつている。このため、黒液の有機
成分濃度測定手段としては、チツプ蒸解工程から
排出される黒液を採取して数日間を要して分析を
行なう直接測定法が最も確実かつ精度よく測定で
きる方法であると考えられるが、前述したように
時々刻々変化する有機成分濃度を即時に連続して
測定することは非常に難しい。一方、測定精度を
ある程度犠牲にしても即時に連続して黒液の有機
成分濃度を知ることがチツプ蒸解工程や回収ボイ
ラの操業管理上からも重要なことである。
In particular, the concentration of organic components in the black liquor is an extremely important source of information for the operational management of recovery boilers and chip cooking processes. When the properties of black liquor change due to adjustments to the formulation, amount, cooking time, etc. of the chemicals to be added, the properties of the black liquor will fluctuate as a result of these changes. It has a property that fluctuates depending on the amount of mixed dust. For this reason, the most reliable and accurate method for measuring the concentration of organic components in black liquor is the direct measurement method, in which the black liquor discharged from the chip cooking process is collected and analyzed over several days. However, as mentioned above, it is extremely difficult to immediately and continuously measure the organic component concentration, which changes from moment to moment. On the other hand, it is important from the standpoint of operational management of the chip cooking process and recovery boiler to know the concentration of organic components in black liquor immediately and continuously even if it sacrifices some measurement accuracy.

そこで、従来、黒液の有機成分濃度を連続的に
推定する方法が採用されているが、その測定原理
は異なる2つ以上の濃度計を用いて黒液の有機成
分濃度を推定する方法であり(PULP&PAPER
CANADA VOL,75,NO,12,1974 P83)、そ
の具体例としては光屈折式濃度計とガンマ線式濃
度計を用いて有機成分濃度を推定する方法であ
る。
Therefore, conventional methods have been used to continuously estimate the concentration of organic components in black liquor, but the measurement principle is to estimate the concentration of organic components in black liquor using two or more different densitometers. (PULP & PAPER
CANADA VOL, 75, NO, 12, 1974 P83), a specific example of which is a method of estimating the concentration of organic components using a photorefraction type densitometer and a gamma ray type densitometer.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、この黒液の有機成分濃度推定方法は、
2成分を含む溶液の成分濃度を推定する方法(工
業測定便覧 コロナ社 P789)として一般的な
ものであり、光屈折率の物質による差違と密度の
物質による差違を利用しようとするものである
が、黒液の濃度を精度よく推定したという結果は
未だ得られていない。一方、光屈折式濃度計は、
通常黒液の濃度として第1図に示す溶液A5中の
溶解固形成分A7における無機成分A3−aと有
機成分A2−aの割合が一定であると仮定し、非
溶解成分A6の影響も無視して溶解Aの光屈折率
の変化から黒液A1中の固形分A8の濃度即ち固
形分濃度を推定する装置として用いられている。
この固形分濃度推定装置としての光屈折式濃度計
は黒液の有機成分に対して検出感度が高いと一般
に経験上言われていたが、発明者等の行なつた実
験によると、この光屈折式濃度計のみによつて有
機成分濃度を推定しようとすると、推定値と分析
値の差は標準偏差として推定値の約2.4%も変動
することが確認されている。
However, this method for estimating the concentration of organic components in black liquor is
This is a common method for estimating the component concentration of a solution containing two components (Industrial Measurement Handbook Coronasha P789), and it attempts to utilize the difference in optical refractive index between substances and the difference in density between substances. However, no results have yet been obtained that accurately estimate the concentration of black liquor. On the other hand, a photorefraction type densitometer
It is assumed that the ratio of the inorganic component A3-a and the organic component A2-a in the dissolved solid component A7 in the solution A5 shown in FIG. It is used as a device for estimating the concentration of solid content A8 in black liquor A1, that is, the solid content concentration, from the change in the optical refractive index of dissolved A1.
It has generally been said from experience that the photorefraction type densitometer used as a device for estimating the solid content concentration has a high detection sensitivity for organic components in black liquor; however, according to experiments conducted by the inventors, It has been confirmed that when attempting to estimate the concentration of organic components using only a formula concentration meter, the difference between the estimated value and the analyzed value varies by approximately 2.4% of the estimated value in terms of standard deviation.

従つて、第1の発明は、以上のような点に着目
してなされたもので、黒液の有機成分濃度を即時
に連続的に推定でき、しかも操業管理、燃焼制御
等の使用に充分耐えうる精度の有機成分濃度を推
定し得る黒液の有機成分濃度推定方法を提供する
ことを目的とする。
Therefore, the first invention was made by focusing on the above-mentioned points, and is capable of estimating the organic component concentration of black liquor immediately and continuously, and which is sufficiently durable for use in operational management, combustion control, etc. An object of the present invention is to provide a method for estimating the concentration of organic components in black liquor that can estimate the concentration of organic components with high accuracy.

また、第2の発明の目的とするところは、簡単
な構成で有機成分濃度を連続的かつ高精度に測定
し得、操業管理、燃焼制御等に充分寄与させ得る
黒液の有機成分濃度測定装置を提供することにあ
る。
Further, the object of the second invention is to provide a black liquor organic component concentration measuring device that can continuously and highly accurately measure the organic component concentration with a simple configuration and can sufficiently contribute to operational management, combustion control, etc. Our goal is to provide the following.

〔問題点を解決するための手段〕[Means for solving problems]

第1の発明は、以上のような目的を達成するた
めに、チツプと薬剤を用いてチツプを蒸解するチ
ツプ蒸解工程により排出される黒液の有機成分濃
度を推定する方法において、前記黒液の溶液の屈
折率及び黒液の温度を検知し、これら屈折率及び
温度に基づいて前記チツプ蒸解工程に投入される
前記チツプ材種及び前記薬剤に基づいて得られる
前記黒液性状に対する各有機成分濃度を推定し、
これら有機成分濃度から前記黒液性状に該当する
有機成分濃度を選択するようにした黒液の有機成
分濃度推定方法である。
In order to achieve the above object, a first invention provides a method for estimating the concentration of organic components of black liquor discharged from a chip cooking process in which chips are digested using chips and a chemical. The refractive index of the solution and the temperature of the black liquor are detected, and based on these refractive indexes and temperatures, the concentration of each organic component for the black liquor properties obtained based on the chip material type and the chemical added to the chip cooking process is determined. Estimate
This is a method for estimating the organic component concentration of black liquor, in which an organic component concentration corresponding to the black liquor properties is selected from these organic component concentrations.

一方、第2の発明は、チツプと薬剤を用いてチ
ツプを蒸解するチツプ蒸解工程により排出される
黒液の有機成分濃度を推定する装置において、前
記黒液の溶液の屈折率を検知する濃度計と、前記
黒液の温度を検知する温度計と、前記チツプ蒸解
工程に投入される前記チツプ材種及び前記薬剤に
基づいて定められる黒液性状信号を出力する黒液
性状設定部と、これら濃度計及び温度計により検
知される屈折率及び温度に基づいて前記チツプ材
種及び前記薬剤に基づいて得られる前記黒液性状
に対する各有機成分濃度を推定し、これら有機成
分濃度から前記黒液性状信号に基づいて有機成分
濃度を選択する有機成分濃度推定手段とを備えた
黒液の有機成分濃度推定装置である。
On the other hand, a second invention is a device for estimating the concentration of organic components of black liquor discharged from a chip cooking process in which chips are digested using chips and chemicals, and a concentration meter that detects the refractive index of the black liquor solution. a thermometer that detects the temperature of the black liquor; a black liquor property setting unit that outputs a black liquor property signal determined based on the chip material type and the chemical that are input into the chip cooking process; The concentration of each organic component for the black liquor properties obtained based on the chip material type and the chemical is estimated based on the refractive index and temperature detected by the meter and the thermometer, and the black liquor property signal is calculated from these organic component concentrations. This is an organic component concentration estimating device for black liquor, comprising an organic component concentration estimating means for selecting an organic component concentration based on the organic component concentration.

〔作用〕 従つて、第1の発明は、以上のような手段とす
ることにより、黒液中に溶解している固形分が温
度によつて大きく変化し、これに伴つて黒液溶液
の屈折率が大きく変化するが、黒液の屈折率及び
温度に基づいて黒液性状に対する各有機成分濃度
を推定し、これら有機成分濃度から黒液性状に該
当する有機成分濃度を選択するようにすれば、黒
液の溶液のみならず、黒液性状に応じて黒液の固
形分に含まれる有機成分濃度をも測定できて精度
高い推定が可能となり、よつて即時に連続しても
操業管理、燃焼管理等の使用に充分たえうる有機
成分濃度を推定できるものである。
[Function] Therefore, the first invention uses the above-described means so that the solid content dissolved in the black liquor changes greatly depending on the temperature, and accordingly, the refraction of the black liquor solution changes. Although the ratio varies greatly, if the concentration of each organic component is estimated for the black liquor properties based on the refractive index and temperature of the black liquor, and the organic component concentration corresponding to the black liquor properties is selected from these organic component concentrations. , it is possible to measure not only the black liquor solution, but also the concentration of organic components contained in the solid content of black liquor depending on the black liquor properties, making it possible to estimate with high accuracy, and thus to improve operational management and combustion even in immediate continuous operation. It is possible to estimate the concentration of organic components that is sufficient for use in management, etc.

又、第2の発明においては、黒液供給ラインに
濃度計と温度計を設けるだけの簡単な構成により
黒液溶液及び黒液の固形分の有機成分濃度を高感
度で検知でき、さらにこれらの濃度計及び温度計
の出力を用いて黒液性状に対する各有機成分濃度
を推定し、これら有機成分濃度から黒液性状に該
当する有機成分濃度を選択するようにすれば、温
度変化に応じて最適な有機成分濃度を連続的かつ
高精度に推定でき、よつて操業管理、燃焼制御等
に充分対処できるものとなる。
In addition, in the second invention, the black liquor solution and the organic component concentration of the solids in the black liquor can be detected with high sensitivity by a simple configuration of just providing a concentration meter and a thermometer in the black liquor supply line. By estimating the concentration of each organic component for the black liquor properties using the output of the densitometer and thermometer, and selecting the organic component concentration corresponding to the black liquor properties from these organic component concentrations, the optimum concentration can be determined according to temperature changes. The concentration of organic components can be estimated continuously and with high precision, and thus it is possible to adequately deal with operational management, combustion control, etc.

〔実施例〕〔Example〕

以下、第1および第2の発明における実施例を
説明するにあたり、先ず、これらの発明の原理に
ついて簡単に説明する。一般に、黒液は第1図に
示すような成分構成を有している。すなわち、黒
液A1は、大きく分けて有機成分A2、無機成分
A3および水分A4によつて構成されており、有
機成分A2、無機成分A3の大部分は水分A4を
伴つた溶液A5となつており、この溶液A5以外
の部分が非溶解成分A6となつている。そして、
溶液A5中の溶液固形成分A7と非溶液成分A6
との和が固形分A8と考えられる。
Below, in describing the embodiments of the first and second inventions, first, the principles of these inventions will be briefly described. Generally, black liquor has a composition as shown in FIG. That is, black liquor A1 is roughly composed of organic component A2, inorganic component A3, and water A4, and most of the organic component A2 and inorganic component A3 are in solution A5 with water A4. , the portion other than this solution A5 is the undissolved component A6. and,
Solution solid component A7 and non-solution component A6 in solution A5
The sum of these is considered to be the solid content A8.

従つて、溶液の屈折率Nは、溶液A5中の水分
A4、溶液固形成分A7の中の有機成分A2−a
および無機成分A3−aの各濃度によつて決り、
一定温度下では近似的に各成分濃度による屈折率
の加重和として表わすことができる。
Therefore, the refractive index N of the solution is determined by the water A4 in the solution A5 and the organic component A2-a in the solution solid component A7.
and each concentration of inorganic component A3-a,
At a constant temperature, it can be approximately expressed as a weighted sum of refractive indexes depending on the concentrations of each component.

N=x1・N1+x2・N2+x3・N3+
NO ……(1) 但し、N:黒液溶液の屈折率、N1:溶解固形
成分中の有機成分A2−aの平均屈折率、x1:
同様の有機成分A2−aの濃度、N2:溶解固形
成分中の無機成分A3−aの平均屈折率、x2:
同様の無機成分A3−aの濃度、N3:水の屈折
率、x3:水の濃度、NO:定数である。上式に
おいてN1の感度はN2,N3に比べて大きく、
溶液中の有機成分濃度x1と屈折率Nとの相関が
比較的強いので、非溶解成分A6が少ない場合に
は溶液中の有機成分濃度X1から黒液A1中の有
機成分A2の濃度である黒液の有機成分を推定す
ることができる。しかし、第2図に示すように温
度が変化すると、固形分A8の溶解度が大きく変
化し、それに伴つて屈折率が変化して有機成分濃
度が大きく変化する。例えば無機成分のみに非溶
解成分が含まれている場合は無機成分溶解成分A
3−aの濃度が高くなり、屈折率としては無機成
分の割合が大きくなり、屈折率は同じ黒液の有機
成分濃度であつても低い値として表われる。
N=x1・N1+x2・N2+x3・N3+
NO...(1) However, N: refractive index of black liquor solution, N1: average refractive index of organic component A2-a in the dissolved solid component, x1:
Concentration of similar organic component A2-a, N2: Average refractive index of inorganic component A3-a in the dissolved solid component, x2:
Concentration of similar inorganic component A3-a, N3: refractive index of water, x3: concentration of water, NO: constant. In the above equation, the sensitivity of N1 is larger than N2 and N3,
Since the correlation between the organic component concentration x1 in the solution and the refractive index N is relatively strong, if the undissolved component A6 is small, the black liquid, which is the concentration of the organic component A2 in the black liquor A1, will change from the organic component concentration X1 in the solution. The organic components of the liquid can be estimated. However, as shown in FIG. 2, when the temperature changes, the solubility of the solid content A8 changes significantly, the refractive index changes accordingly, and the organic component concentration changes greatly. For example, if inorganic components only contain non-dissolved components, inorganic component dissolved component A
As the concentration of 3-a increases, the proportion of inorganic components in the refractive index increases, and the refractive index appears as a low value even if the concentration of organic components in black liquor is the same.

本発明は以上の原理に基づいて実現したもので
あつて、以下、第1の発明である黒液の有機成分
濃度推定方法について具体的に説明する。先ず、
チツプ蒸解工程においては、蒸解釜に投入される
木材チツプに対し薬剤および蒸気を加えてパルプ
を生産するが、このとき蒸解釜から廃液として希
黒液が排出されるので、これを濃縮器で濃縮して
濃黒液とし、さらに濃黒液に芒硝および回収ボイ
ラより回収された回収ダストを補給混合して混合
黒液を得る。そして、この混合黒液を適宜な温度
に調整した後、噴射黒液として回収ボイラ内に噴
射し、この回収ボイラから蒸気、ダストおよび薬
剤原料等を回収するものである。
The present invention has been realized based on the above principle, and the method for estimating the organic component concentration of black liquor, which is the first invention, will be specifically described below. First of all,
In the chip cooking process, pulp is produced by adding chemicals and steam to the wood chips that are put into the digester. At this time, dilute black liquor is discharged from the digester as waste liquid, which is concentrated in a concentrator. The concentrated black liquor is further mixed with Glauber's salt and the recovered dust recovered from the recovery boiler to obtain a mixed black liquor. After adjusting this mixed black liquor to an appropriate temperature, it is injected into a recovery boiler as an injection black liquor, and steam, dust, drug raw materials, etc. are recovered from the recovery boiler.

ところで、通常、以上のような構成において黒
液の有機成分濃度は黒液溶液の屈折率Nの関数と
して推定している。しかし、温度が変化すると前
記固形分の溶解度が大きく変化し、それに伴つて
屈折率が変化し、結果として有機成分濃度推定値
が変化する。第2図は温度変化に対する光屈折式
濃度計の濃度(固形分濃度推定値)と有機成分濃
度との関係を示す図であるが、この図からも明ら
かなように同一濃度であつても僅かの温度変化に
よりその有機成分濃度が大きく変化する。
Incidentally, in the above configuration, the organic component concentration of the black liquor is usually estimated as a function of the refractive index N of the black liquor solution. However, when the temperature changes, the solubility of the solid content changes significantly, and the refractive index changes accordingly, resulting in a change in the estimated organic component concentration. Figure 2 shows the relationship between the concentration measured by a photorefraction densitometer (estimated solid content concentration) and the organic component concentration with respect to temperature changes.As is clear from this figure, even at the same concentration, there is a slight The concentration of organic components changes greatly with changes in temperature.

そこで、第1の発明においては、回収ボイラに
供給される噴射黒液の溶液に対して例えば光屈折
手段を用いて固形分濃度推定値を検知し、さらに
黒液の温度を検知する。そして、この固形分濃度
推定値に温度の関数としての補正値を加えること
により、有機成分濃度を推定するものである。従
つて、温度変化の影響を除去することができ、精
度の高い有機成分濃度を推定することができる。
また、黒液溶液の屈折率と黒液の有機成分濃度と
の関係は黒液性状により溶解度の変化、屈折率の
変化が生じるので、予めチツプ蒸解工程に投入さ
れるチツプ材種などに基づいて得られる黒液性状
により複数の有機成分濃度を得、これらの有機成
分濃度の中から前記黒液性状に応じて1つを推定
して出力するようにすれば正確な有機成分濃度を
推定できる。
Therefore, in the first invention, the estimated solid content concentration is detected using, for example, a light refraction means for the injection black liquor solution supplied to the recovery boiler, and the temperature of the black liquor is also detected. Then, by adding a correction value as a function of temperature to this estimated solid content concentration value, the organic component concentration is estimated. Therefore, the influence of temperature changes can be removed, and the organic component concentration can be estimated with high accuracy.
In addition, the relationship between the refractive index of the black liquor solution and the concentration of organic components in the black liquor varies depending on the properties of the black liquor, so the solubility changes and the refractive index changes. Accurate organic component concentration can be estimated by obtaining a plurality of organic component concentrations based on the obtained black liquor properties and estimating and outputting one of these organic component concentrations according to the black liquor properties.

従つて、この発明の実施例の構成によれば、黒
液溶液の屈折率だけでなく、黒液の温度を検知
し、この検知温度に応じて固形分濃度推定値を補
正して有機成分濃度を推定する推定方法をとつて
いるので、即時に連続的に有機成分濃度を推定し
ても操業管理、燃焼制御等の利用に充分耐えうる
精度の有機成分濃度を推定できるものである。
Therefore, according to the configuration of the embodiment of the present invention, not only the refractive index of the black liquor solution but also the temperature of the black liquor is detected, and the estimated solid content concentration is corrected according to the detected temperature to determine the organic component concentration. Since an estimation method is used to estimate the organic component concentration, even if the organic component concentration is estimated continuously immediately, the organic component concentration can be estimated with sufficient accuracy for use in operational management, combustion control, etc.

通常、回収ボイラに投入される噴射黒液粒径を
適正にするために噴射黒液温度の設定値を操作す
ることが行われている。その他の黒液ラインにお
いては黒液温度を所定値に制御する運転はなされ
ていない。従来、かかる状態において黒液を光屈
折式濃度計のみ、または光屈折式濃度計と密度計
から有機成分濃度を推定していたが、上述したよ
うな理由から充分な精度の推定を行うことができ
ない。
Normally, the set value of the jet black liquor temperature is manipulated in order to optimize the jet black liquor droplet diameter that is fed into the recovery boiler. In other black liquor lines, no operation is performed to control the black liquor temperature to a predetermined value. Conventionally, the organic component concentration of black liquor in such conditions has been estimated using only a photorefraction densitometer, or a photorefraction densitometer and a densitometer, but for the reasons mentioned above, it has not been possible to estimate with sufficient accuracy. Can not.

本発明においては、黒液の屈折率のみならず、
温度や黒液性状等の影響を考慮してより精度の高
い有機成分濃度を推定できる。因みに、第2図は
噴射黒液をサンプル分析して得られた黒液の有機
成分濃度およびサンプル時の黒液温度と光屈折式
濃度計の濃度(固形分濃度推定値)との関係につ
いて調べた図であるが、この図から明らかなよう
に濃度計の濃度が同じであつても黒液の温度が±
2℃程度異なれば有機成分濃度は濃度計のみによ
る濃度推定値の約±2%も変化する。本発明にお
いては以上のような温度の変動を捕えて補正する
ので、高精度に有機成分濃度を推定できるもので
ある。
In the present invention, not only the refractive index of black liquor but also
It is possible to estimate the organic component concentration with higher accuracy by taking into account the effects of temperature, black liquor properties, etc. Incidentally, Figure 2 shows the relationship between the black liquor organic component concentration obtained by sample analysis of the jetted black liquor, the black liquor temperature at the time of sampling, and the concentration (estimated solid content concentration) measured by a photorefraction type densitometer. However, as is clear from this figure, even if the concentration measured by the densitometer is the same, the temperature of the black liquor varies between ±
If the temperature differs by about 2°C, the organic component concentration will change by about ±2% of the concentration estimated by the densitometer alone. In the present invention, since the above-described temperature fluctuations are captured and corrected, the organic component concentration can be estimated with high accuracy.

なお、本発明は上記実施例に限定されずに種々
変形して実施できる。即ち,黒液の無機成分量の
変化は、溶液として飽和している状態では屈折率
の変化として表われないので黒液の有機成分濃度
の推定に誤差を与えるが、黒液密度の変化として
表らわれる。そこで、黒液の密度を検知して推定
関数に組込むようにして補正を行えば、より高精
度に有機成分濃度を推定することができる。
Note that the present invention is not limited to the above embodiments, and can be implemented with various modifications. In other words, changes in the amount of inorganic components in black liquor do not appear as changes in the refractive index when it is saturated as a solution, causing errors in estimating the concentration of organic components in black liquor, but changes in the amount of inorganic components in black liquor do not appear as changes in black liquor density. I get caught. Therefore, if the density of the black liquor is detected and corrected by incorporating it into the estimation function, the organic component concentration can be estimated with higher accuracy.

次に、第2の発明における実施例について第3
図を参照して説明する。同図において1はチツプ
蒸解工程の一部である蒸解釜であつて、これには
木材チツプ2、薬剤3および蒸気4が供給され、
チツプ2が薬剤3および蒸気4により蒸解されて
パルプ5が生産され、その結果、蒸解釜1から廃
液として希黒液6が排出される。この希黒液6は
濃縮器7によつて濃縮されて濃黒液8とされ、後
段のミキシングタンク9に導入されるようになつ
ている。このミキシングタンク9では濃縮器7の
濃縮液8に回収ボイラ10から回収された回収ダ
スト11と芒硝12が混合されて混合黒液13と
されて出力される。14は黒液ヒータであつて、
ここでは混合黒液13が例えば回収ボイラ10か
ら回収された蒸気15により適宜な温度に調整さ
れて噴射黒液16として回収ボイラ10に送ら
れ、該ボイラ10内で噴射されて燃焼に供され
る。この回収ボイラ10は噴射黒液を乾燥させて
燃焼し、蒸解釜1および黒液ヒータ14等に供給
する蒸気4,15を回収し、またダスト11およ
び薬剤原料3等を回収する機能をもつている。ま
た、黒液ヒータ14と回収ボイラ10の間の噴射
黒液供給ライン17には測定の同時性が損われな
い程度に光屈折式濃度計18および温度計が設け
られている。この光屈折式濃度計18は屈折率の
関数となつている固形分濃度推定値S1を得るも
ので、黒液溶液の屈折率を測定するものであれば
使用される波長帯域上の制約はないものである。
20は有機成分濃度推定演算部であつて、これに
は濃度計18から固形分濃度推定値S1が供給さ
れ、また温度計19から黒液の温度S2が供給さ
れる。この有機成分濃度推定演算部20は後述す
る第(2)式に示す推定演算式により有機成分濃度を
推定するものである。21は黒液性状設定部であ
り、ここではチツプの種類や薬剤3の種類によつ
て予め定められる黒液性状設定信号S4が出力さ
れ、有機成分濃度推定演算部20に供給される。
従つて、この有機成分濃度推定演算部20は黒液
性状信号に基づいて温度および屈折率の関数とし
て複数の有機成分濃度を推定するようになつてい
る。つまり、有機成分濃度演算部20は黒液性状
設定部21から例えばあるチツプ材種の黒液性状
信号が入力されると、そのチツプ材種に応じた有
機成分濃度のみを選択して出力するようになつて
いる。推定関数を選択するのは黒液性状によつて
溶解度および屈折率か変化するためである。な
お、黒液性状によつてある1つの有機成分濃度を
出力する手段としては図示点線に示すように有機
成分濃度推定演算部20の出力端に選択部22を
設け、黒液性状設定部21からの黒液性状信号S
4に応じて前記有機成分濃度推定演算部20から
出力される複数の有機成分濃度の中から1つを選
択して出力する構成であつてもよい。
Next, we will discuss the third embodiment of the second invention.
This will be explained with reference to the figures. In the figure, 1 is a cooking pot which is part of the chip cooking process, to which wood chips 2, chemicals 3 and steam 4 are supplied.
Chips 2 are digested with chemicals 3 and steam 4 to produce pulp 5, and as a result, dilute black liquor 6 is discharged from the digester 1 as waste liquid. This diluted black liquor 6 is concentrated by a concentrator 7 to form a concentrated black liquor 8, which is then introduced into a mixing tank 9 at a subsequent stage. In this mixing tank 9, recovered dust 11 and Glauber's salt 12 recovered from the recovery boiler 10 are mixed with the concentrated liquid 8 of the concentrator 7, and the mixture is output as a mixed black liquor 13. 14 is a black liquor heater,
Here, the mixed black liquor 13 is adjusted to an appropriate temperature by steam 15 recovered from the recovery boiler 10, for example, and sent to the recovery boiler 10 as an injected black liquor 16, where it is injected and combusted. . This recovery boiler 10 has the function of drying and burning the injected black liquor, recovering steam 4, 15 to be supplied to the digester 1, black liquor heater 14, etc., and also recovering dust 11, drug raw materials 3, etc. There is. Further, a photorefraction type densitometer 18 and a thermometer are provided in the injection black liquor supply line 17 between the black liquor heater 14 and the recovery boiler 10 to the extent that the simultaneity of measurement is not impaired. This photorefraction type densitometer 18 obtains the estimated solid concentration value S1 which is a function of the refractive index, and there are no restrictions on the wavelength band used as long as it measures the refractive index of a black liquor solution. It is something.
Reference numeral 20 denotes an organic component concentration estimation calculation unit, to which the estimated solid content concentration value S1 is supplied from the concentration meter 18, and the temperature S2 of the black liquor is supplied from the thermometer 19. The organic component concentration estimation calculation unit 20 estimates the organic component concentration using an estimation calculation formula shown in Equation (2), which will be described later. A black liquor property setting section 21 outputs a black liquor property setting signal S4 predetermined according to the type of chips and the type of medicine 3, and is supplied to the organic component concentration estimation calculation section 20.
Therefore, this organic component concentration estimation calculation unit 20 is designed to estimate a plurality of organic component concentrations as a function of temperature and refractive index based on the black liquor property signal. In other words, when the organic component concentration calculating section 20 receives a black liquor property signal of a certain chip material from the black liquor property setting section 21, for example, it selects and outputs only the organic component concentration corresponding to that chip material. It's getting old. The estimation function is selected because the solubility and refractive index change depending on the properties of the black liquor. As a means for outputting a certain organic component concentration depending on the black liquor properties, a selection section 22 is provided at the output end of the organic component concentration estimation calculation section 20 as shown by the dotted line in the figure, and a selection section 22 is provided at the output end of the organic component concentration estimation calculation section 20. black liquor property signal S
4, one of the plurality of organic component concentrations outputted from the organic component concentration estimation calculating section 20 may be selected and output.

次に、以上のように構成された装置の動作を説
明する。チツプ蒸解工程としての蒸解釜1にはチ
ツプ2の外、回収ボイラ10から薬剤原料3およ
び蒸気4等が供給され、ここでチツプ2が薬剤3
および蒸気4によつて蒸解されてパルプ5を生産
するとともに、該蒸解釜1から廃液として希黒液
6が排出される。この希黒液6は濃縮器7に送ら
れ、ここで濃縮されて濃黒液8を得た後、ミキシ
ングタンク9に導入される。このミキシングタン
ク9では濃縮器7からの濃黒液8に前記回収ボイ
ラ10からのダスト11と芒硝12とを混合して
混合黒液13を得、更に後段の黒液ヒータ14に
送り、ここで蒸気15の熱で適宜な温度に調整し
て回収ボイラ10に供給し、回収ボイラ内に噴射
黒液16として噴射するものである。
Next, the operation of the apparatus configured as above will be explained. In addition to chips 2, a chemical raw material 3 and steam 4 are supplied from a recovery boiler 10 to a digester 1 used for the chip cooking process.
and steam 4 to produce pulp 5, and at the same time, dilute black liquor 6 is discharged from the digester 1 as waste liquid. This diluted black liquor 6 is sent to a concentrator 7, where it is concentrated to obtain a concentrated black liquor 8, which is then introduced into a mixing tank 9. In this mixing tank 9, the dust 11 and Glauber's salt 12 from the recovery boiler 10 are mixed with the concentrated black liquor 8 from the concentrator 7 to obtain a mixed black liquor 13, which is further sent to the subsequent black liquor heater 14, where it is The temperature is adjusted to an appropriate temperature using the heat of the steam 15 and then supplied to the recovery boiler 10, where it is injected as black liquor 16 into the recovery boiler.

このとき、噴射黒液供給ライン17に光屈折式
濃度計18および温度計19が設置され、これら
の計器18,19により固形分濃度推定値S1、
黒液の温度S2が検知され、有機成分濃度演算部
20に供給される。この有機成分濃度演算部20
はチツプ2の材種や薬剤3の種類等によつて異な
る黒液性状に対する有機成分濃度S5−1〜S5
−nが計算され、黒液性状設定部21によつて設
定される黒液性状信号S4によつて該当する有機
成分濃度を選択し、有機成分濃度推定値S5とし
て出力する。
At this time, a photorefraction type concentration meter 18 and a thermometer 19 are installed in the injection black liquor supply line 17, and these meters 18 and 19 measure the estimated solid content concentration S1,
The temperature S2 of the black liquor is detected and supplied to the organic component concentration calculation section 20. This organic component concentration calculation section 20
are the organic component concentrations S5-1 to S5 for the black liquor properties, which vary depending on the type of chip 2, the type of chemical 3, etc.
-n is calculated, and the corresponding organic component concentration is selected based on the black liquor property signal S4 set by the black liquor property setting section 21, and outputted as an estimated organic component concentration value S5.

前記有機成分濃度演算部20の推定演算式とし
ては、温度変化範囲および固形分濃度変化範囲が
比較的小さければ,、下式のような簡単な演算式
で充分な精度の推定が可能となる。
As for the estimation calculation formula of the organic component concentration calculation section 20, if the temperature change range and the solid content concentration change range are relatively small, a simple calculation formula such as the following formula can be used to estimate with sufficient accuracy.

S5=α1S1+β1S2 +δ1(S4=1の時) αiS1+βiS2+δi(S4=iの時) αnS1+βnS2+δn(S4=nの時) …(2) ここで、αi,βi,δi(i=1、2、…n)は定
数、濃度計18から出力される固定分濃度推定値
S1は第(1)式に示す黒液溶液の屈折率Nとの関数
として推定されるので、S1=f(n)で表わせ
る。S2は温度計19の検知温度である。なお、
温度変化範囲や固形分濃度変化範囲が大きけれ
ば、更に複雑な演算式により精度よく有機成分濃
度S5を推定できる。
S5=α1S1+β1S2 +δ1 (when S4=1) αiS1+βiS2+δi (when S4=i) αnS1+βnS2+δn (when S4=n)...(2) Here, αi, βi, δi (i=1, 2,...n) are The fixed concentration estimated value S1 output from the constant concentration meter 18 is estimated as a function of the refractive index N of the black liquor solution shown in equation (1), so it can be expressed as S1=f(n). S2 is the temperature detected by the thermometer 19. In addition,
If the temperature change range and solid content concentration change range are large, the organic component concentration S5 can be estimated with high accuracy using a more complicated calculation formula.

従つて、以上のような第2の発明の実施例の構
成によれば、噴射黒液供給ライン17に光屈折式濃
度計18の外に温度計19を設け、屈折率の関数と
なつている固形分濃度推定値S1に屈折率の変動
要因である黒液の温度を補正値として考慮し、有
機成分濃度を推定するようにしているので、簡単
な構成で即時に連続的に有機成分濃度を推定でき
る。しかも、黒液性状設定部21で予めチツプ材種
や薬剤3の種類によつて黒液性状信号を設定し、
この黒液性状信号ごとに第(2)式に示すように複数
の有機成分濃度を定め、黒液性状信号に応じて複
数の有機成分濃度の中から1つを選択して有機成
分濃度と推定して出力する構成としているので、
温度のみならず、黒液性状の変化によつて生じる
推定誤差をも除去し得、高精度に有機成分濃度を
推定でき、チツプ蒸解工程や回収ボイラを適切に
操業管理、燃焼制御等を行い得るものである。
Therefore, according to the configuration of the embodiment of the second invention as described above, a thermometer 19 is provided in the injection black liquor supply line 17 in addition to the photorefraction type densitometer 18, and the temperature is a function of the refractive index. The temperature of the black liquor, which is a factor in the fluctuation of the refractive index, is considered as a correction value for the estimated solid content concentration value S1, and the organic component concentration is estimated. It can be estimated. Moreover, the black liquor property setting section 21 sets the black liquor property signal in advance according to the chip material type and the type of chemical 3,
For each black liquor property signal, multiple organic component concentrations are determined as shown in equation (2), and one of the multiple organic component concentrations is selected according to the black liquor property signal to estimate the organic component concentration. Since it is configured to output as follows,
Estimation errors caused not only by temperature but also by changes in black liquor properties can be removed, organic component concentrations can be estimated with high accuracy, and chip cooking processes and recovery boilers can be appropriately managed and combustion controlled. It is something.

なお、この発明は上記実施例に限定されずに
種々変形して実施できるものである。例えば有機
成分濃度推定演算部20に黒液性状設定部21を
含めて構成してもよい。また、第3図に示す点線の
ように噴射黒液供給ライン17に濃度計18、温
度計19の外に、ガンマ線式密度計または振動式
密度計23を設けるようにすれば、無機成分の影
響を補正して推定精度を上げることができる。つ
まり、黒液の無機成分量の変化は前述したように
溶液として飽和している状態では屈折率の変化と
して現われずに黒液の密度変化として現われるの
で、黒液の有機成分濃度の推定値に誤差を生じ
る。そこで、密度計23により黒液の密度S3を検
知し、この密度S3によつて補正するようにすれ
ばその誤差を除去でき、より高精度に有機成分濃
度を推定することができる。この場合、上記(2)式の
各黒液性状信号S4=iごと例えばS4=1の
時、 S5=α1S1+β1S2+γ1S3+δ1に
より有機成分濃度を推定すればよい。S3は検知
密度、γ1は定数である。
Note that the present invention is not limited to the above-mentioned embodiments, and can be implemented with various modifications. For example, the organic component concentration estimation calculation section 20 may include the black liquor property setting section 21. Moreover, if a gamma ray type density meter or a vibration type density meter 23 is installed in the injection black liquor supply line 17 in addition to the concentration meter 18 and thermometer 19 as shown by the dotted line in FIG. can be corrected to improve estimation accuracy. In other words, as mentioned above, when the black liquor is saturated as a solution, changes in the amount of inorganic components do not appear as changes in the refractive index, but as changes in the density of the black liquor. cause an error. Therefore, by detecting the density S3 of the black liquor using the densitometer 23 and correcting it using this density S3, the error can be removed and the organic component concentration can be estimated with higher accuracy. In this case, the organic component concentration may be estimated for each black liquor property signal S4=i in the above equation (2), for example, when S4=1, S5=α1S1+β1S2+γ1S3+δ1. S3 is the detection density and γ1 is a constant.

次に、第4図は本発明方法およびその推定装置
の応用例の1つとして噴射黒液の有機成分濃度推
定値を用いた回収ボイラの燃焼制御を説明する構
成図である。即ち、この装置は、第3図に示す装
置に、新たに黒液の体積流量を検知する体積流量
計31、燃焼空気流量演算部32および下段空気
流量調節計33、中段空気流量調節計34、上段
空気流量調節計35を設けてなる構成である。通
常、回収ボイラ10は噴射黒液16を燃焼するボ
イラであるが、このボイラの燃焼効率を上げるた
めに、有機成分濃度推定値S5、噴射黒液の体積
流量計31により検知される黒液の体積流量S
6、ガンマ線密度S3および黒液性状信号S4等
を燃焼空気流量演算部32に供給し、ここでこれ
らの信号S3〜S6を用いて必要な燃焼空気量で
ある回収ボイラ10の各段へ投入される空気流量
指令値S7〜S9を求め、各段の空気流量調節計
33〜35に供給する。そして、これら各段の空
気流量調節計33〜35にて空気流量指令値S7
〜S9と実空気流量S17〜S19とを比較しそ
の偏差が零となるように回収ボイラ10の下段,
中段および上段の燃焼用流量S27〜S29を
得、回収ボイラ10に供給するものである。従つ
て、本発明の推定方法およびその推定装置を回収
ボイラ10に応用すれば、回収ボイラ10の燃焼
制御を適正に行うことができる。
Next, FIG. 4 is a block diagram illustrating combustion control of a recovery boiler using the estimated value of the organic component concentration of the injected black liquor as one of the application examples of the method and estimation device of the present invention. That is, this device includes, in addition to the device shown in FIG. 3, a volumetric flow meter 31 for detecting the volumetric flow rate of black liquor, a combustion air flow rate calculation section 32, a lower stage air flow controller 33, a middle stage air flow controller 34, This configuration includes an upper stage air flow rate controller 35. Normally, the recovery boiler 10 is a boiler that burns the injected black liquor 16, but in order to increase the combustion efficiency of this boiler, the estimated organic component concentration S5, the black liquor detected by the volumetric flow meter 31 of the injected black liquor are Volumetric flow rate S
6. Supply the gamma ray density S3, black liquor property signal S4, etc. to the combustion air flow rate calculation section 32, and use these signals S3 to S6 to determine the required amount of combustion air to be injected into each stage of the recovery boiler 10. The air flow rate command values S7 to S9 are determined and supplied to the air flow rate controllers 33 to 35 at each stage. Then, the air flow rate command value S7 is determined by the air flow rate controllers 33 to 35 at each stage.
~S9 and the actual air flow rate S17~S19 are compared, and the lower stage of the recovery boiler 10 is adjusted so that the deviation becomes zero.
The middle stage and upper stage combustion flow rates S27 to S29 are obtained and supplied to the recovery boiler 10. Therefore, if the estimation method and estimation device of the present invention are applied to the recovery boiler 10, combustion control of the recovery boiler 10 can be performed appropriately.

〔発明の効果〕〔Effect of the invention〕

以上詳記したように第1の発明によれば、温度
による誤差要因を排除することにより、高精度に
有機成分濃度を推定でき、かつ黒液性状の変化に
よつて生じる推定誤差をも除去でき、よつて即時
に連続的に有機成分濃度を推定しても操業管理、
燃焼管理等の使用に充分耐えうる有機成分濃度を
推定し得る黒液の有機成分濃度推定方法を提供で
きる。
As detailed above, according to the first invention, it is possible to estimate the organic component concentration with high accuracy by eliminating error factors due to temperature, and it is also possible to eliminate estimation errors caused by changes in black liquor properties. Therefore, even if the concentration of organic components is estimated immediately and continuously, operational management,
It is possible to provide a method for estimating the concentration of organic components in black liquor that can estimate the concentration of organic components that can sufficiently withstand use such as combustion control.

又、第2の発明によれば、濃度計と温度計を設
けて黒液溶液の屈折率及び黒液の温度を検知し、
さらに屈折率及び温度の関数として複数の有機成
分濃度を得、これらの有機成分濃度の中から1つ
を推定して出力するようにしたので、簡単な構成
により有機成分濃度を推定でき、かつ黒液性状の
変化によつて生じる推定誤差をも除去でき、よつ
て有機成分濃度を即時に連続的に推定し得、操業
管理、燃焼管理等を適切に行い得る黒液の有機成
分濃度推定装置を提供できる。
Further, according to the second invention, a densitometer and a thermometer are provided to detect the refractive index of the black liquor solution and the temperature of the black liquor,
Furthermore, multiple concentrations of organic components are obtained as a function of refractive index and temperature, and one of these organic component concentrations is estimated and output. Therefore, the concentration of organic components can be estimated with a simple configuration, and black An apparatus for estimating the concentration of organic components in black liquor that can eliminate estimation errors caused by changes in liquid properties, can immediately and continuously estimate the concentration of organic components, and can appropriately perform operational management, combustion management, etc. Can be provided.

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

第1図ないし第3図は本発明方法およびその装
置を説明するために示したもので、第1図は本発
明方法およびその装置を実現するための原理説明
図、第2図は黒液温度の変化に対する濃度計出力
と有機成分濃度の関係図、第3図は第2の発明の
一実施例を説明するための構成図、第4図は本発
明方法およびその装置を応用した回収ボイラの燃
焼制御を説明する構成図である。 1……蒸解釜、7……濃縮器、9……ミキシン
グタンク、10……回収ボイラ、14……黒液ヒ
ータ、18……光屈折式濃度計、19……温度
計、20……有機成分濃度推定演算部、21……
黒液性状設定部、22……選択部、23……ガン
マ線式密度計。
Figures 1 to 3 are shown to explain the method and apparatus of the present invention. Figure 1 is an explanatory diagram of the principle for realizing the method and apparatus of the present invention, and Figure 2 is the black liquor temperature. 3 is a diagram showing the configuration of an embodiment of the second invention, and FIG. 4 is a diagram showing the relationship between the densitometer output and the organic component concentration with respect to changes in It is a block diagram explaining combustion control. 1... Digester, 7... Concentrator, 9... Mixing tank, 10... Recovery boiler, 14... Black liquor heater, 18... Light refraction type densitometer, 19... Thermometer, 20... Organic Component concentration estimation calculation section, 21...
Black liquor property setting section, 22... selection section, 23... gamma ray density meter.

Claims (1)

【特許請求の範囲】 1 チツプと薬剤を用いて前記チツプを蒸解する
チツプ蒸解工程により排出される黒液の有機成分
濃度を推定する方法において、 前記黒液の溶液の屈折率及び前記黒液の温度を
検知し、これら屈折率及び温度に基づき、前記チ
ツプ蒸解工程に投入される前記チツプ材種及び前
記薬剤に基づいて得られる前記黒液性状に対する
各有機成分濃度を推定し、これら有機成分濃度か
ら該当する前記黒液性状の有機成分濃度を選択す
ることを特徴とする黒液の有機成分濃度推定方
法。 2 黒液の有機成分濃度を推定する手段は、前記
屈折率より求めた有機成分濃度を前記温度によつ
て補正して推定するものである特許請求の範囲第
1項記載の黒液の有機成分濃度推定方法。 3 チツプと薬剤を用いて前記チツプを蒸解する
チツプ蒸解工程により排出される黒液の有機成分
濃度を推定する装置において、 前記黒液の溶液の屈折率を検知する濃度計と、
前記黒液の温度を検知する温度計と、前記チツプ
蒸解工程に投入される前記チツプ材種及び前記薬
剤に基づいて定められる黒液性状信号を出力する
黒液性状設定部と、前記濃度計及び前記温度計に
より検知される屈折率及び温度に基づいて、前記
チツプ材種及び前記薬剤に基づいて得られる前記
黒液性状に対する各有機成分濃度を推定し、これ
ら有機成分濃度から前記黒液性状信号に基づいて
有機成分濃度を選択する有機成分濃度推定手段と
を備えたことを特徴とする黒液の有機成分濃度推
定装置。 4 黒液の有機成分濃度推定手段は、前記屈折率
より求めた有機成分濃度を前記温度によつて補正
して推定するものである特許請求の範囲第3項記
載の黒液の有機成分濃度推定装置。
[Scope of Claims] 1. A method for estimating the concentration of organic components in black liquor discharged from a chip cooking process in which the chips are digested using chips and a chemical, comprising: the refractive index of the black liquor solution; Detect the temperature, and based on these refractive index and temperature, estimate the concentration of each organic component for the black liquor properties obtained based on the chip material type and the chemical added to the chip cooking process, and calculate the concentration of these organic components. A method for estimating the concentration of organic components in black liquor, characterized in that the concentration of organic components in the corresponding black liquor properties is selected from the following. 2. The organic component concentration of the black liquor according to claim 1, wherein the means for estimating the organic component concentration of the black liquor estimates the organic component concentration determined from the refractive index by correcting it by the temperature. Concentration estimation method. 3. In an apparatus for estimating the concentration of organic components of black liquor discharged from a chip cooking process in which the chips are digested using chips and a chemical, a densitometer that detects the refractive index of the black liquor solution;
a thermometer that detects the temperature of the black liquor; a black liquor property setting unit that outputs a black liquor property signal determined based on the chip material type and the chemical that are input into the chip cooking process; the densitometer; Based on the refractive index and temperature detected by the thermometer, the concentration of each organic component for the black liquor properties obtained based on the chip material type and the drug is estimated, and the black liquor property signal is determined from these organic component concentrations. 1. An organic component concentration estimating device for black liquor, comprising an organic component concentration estimating means for selecting an organic component concentration based on the organic component concentration. 4. Estimating the organic component concentration of black liquor according to claim 3, wherein the black liquor organic component concentration estimating means estimates the organic component concentration determined from the refractive index by correcting it based on the temperature. Device.
JP15169785A 1985-07-10 1985-07-10 Method and apparatus for estimating concentration of organic component in black liquor Granted JPS6212839A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15169785A JPS6212839A (en) 1985-07-10 1985-07-10 Method and apparatus for estimating concentration of organic component in black liquor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15169785A JPS6212839A (en) 1985-07-10 1985-07-10 Method and apparatus for estimating concentration of organic component in black liquor

Publications (2)

Publication Number Publication Date
JPS6212839A JPS6212839A (en) 1987-01-21
JPH0545138B2 true JPH0545138B2 (en) 1993-07-08

Family

ID=15524283

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15169785A Granted JPS6212839A (en) 1985-07-10 1985-07-10 Method and apparatus for estimating concentration of organic component in black liquor

Country Status (1)

Country Link
JP (1) JPS6212839A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5223393A (en) * 1975-08-18 1977-02-22 Nippon Kokan Kk <Nkk> Method of measuring concentration of tempering fluid for skin-pass rol ling mills
JPS56392A (en) * 1979-06-12 1981-01-06 Katayama Chemical Works Co Prevention of pitch obstacle

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5223393A (en) * 1975-08-18 1977-02-22 Nippon Kokan Kk <Nkk> Method of measuring concentration of tempering fluid for skin-pass rol ling mills
JPS56392A (en) * 1979-06-12 1981-01-06 Katayama Chemical Works Co Prevention of pitch obstacle

Also Published As

Publication number Publication date
JPS6212839A (en) 1987-01-21

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