JP2000046821A - Method and apparatus for measuring concentration of carbonate in slurry - Google Patents
Method and apparatus for measuring concentration of carbonate in slurryInfo
- Publication number
- JP2000046821A JP2000046821A JP10217592A JP21759298A JP2000046821A JP 2000046821 A JP2000046821 A JP 2000046821A JP 10217592 A JP10217592 A JP 10217592A JP 21759298 A JP21759298 A JP 21759298A JP 2000046821 A JP2000046821 A JP 2000046821A
- Authority
- JP
- Japan
- Prior art keywords
- slurry
- acid
- concentration
- measured
- caco
- 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
Links
- 239000002002 slurry Substances 0.000 title claims abstract description 82
- 238000000034 method Methods 0.000 title claims description 29
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 title claims description 13
- 239000002253 acid Substances 0.000 claims abstract description 70
- 230000003247 decreasing effect Effects 0.000 claims description 5
- 238000001514 detection method Methods 0.000 claims 1
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 abstract description 6
- 229910000019 calcium carbonate Inorganic materials 0.000 abstract description 4
- 235000010216 calcium carbonate Nutrition 0.000 abstract 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 12
- 238000005259 measurement Methods 0.000 description 12
- 238000006477 desulfuration reaction Methods 0.000 description 8
- 230000023556 desulfurization Effects 0.000 description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 230000002745 absorbent Effects 0.000 description 4
- 239000002250 absorbent Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 230000004044 response Effects 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 101100316860 Autographa californica nuclear polyhedrosis virus DA18 gene Proteins 0.000 description 1
- -1 CaCO 3 Chemical compound 0.000 description 1
- 102100032566 Carbonic anhydrase-related protein 10 Human genes 0.000 description 1
- 101000867836 Homo sapiens Carbonic anhydrase-related protein 10 Proteins 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000007850 fluorescent dye Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000001139 pH measurement Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000004043 responsiveness Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
Landscapes
- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、炭酸塩を含むスラ
リ中の炭酸塩濃度を測定する方法、特に自動連続測定方
法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for measuring a carbonate concentration in a slurry containing a carbonate, and more particularly to an automatic continuous measuring method.
【0002】[0002]
【従来の技術】CaCO3などの炭酸塩を含むスラリ中
の炭酸塩濃度を測定する方法としては、JISR910
1に定められている方法が良く知られているが、この方
法は手分析であり、測定にも数十分の時間を必要とす
る。連続測定に関する特許もいくつか出願されている
(例えば特公平3−52826公報、特開平2−195
253公報)。2. Description of the Related Art As a method for measuring a carbonate concentration in a slurry containing a carbonate such as CaCO 3 , JISR910
Although the method defined in No. 1 is well known, this method is a manual analysis and requires several tens of minutes for measurement. Several patents relating to continuous measurement have been filed (for example, Japanese Patent Publication No. 3-52826, Japanese Patent Application Laid-Open No. 2-195).
253 publication).
【0003】前記特許公報に開示されている方法では、
炭酸塩を含むスラリに酸を添加して加熱し、気相中にC
O2を放出させてガス中のCO2を測定することにより
炭酸塩濃度を算出する方法である。しかし、これらの方
法は自動連続分析であるが、気相中にCO2を完全に放
出させるのに時間がかかり、結果として測定時間が長く
なる。[0003] In the method disclosed in the patent publication,
An acid is added to the slurry containing carbonate and heated, and C
This is a method of calculating the carbonate concentration by measuring the CO 2 in the gas by releasing O 2 . However, although these methods are automatic continuous analyses, it takes time to completely release CO 2 into the gas phase, resulting in a longer measurement time.
【0004】CaCO3を含むスラリを使用する分野と
して排煙脱硫装置があるが、これは火力発電所等におい
て、化石燃料の燃焼に伴って発生する排煙中の硫黄酸化
物、中でも特に二酸化硫黄(SO2)をCaCO3を含
む吸収液スラリで吸収除去する装置である。排煙脱硫装
置ではボイラ負荷や使用燃料の性状の変化に応じてCa
CO3の供給量を調整し、吸収液スラリ中のCaCO3
濃度を最適な値(例えば、排ガス量や排ガス中のSO2
濃度が増加すると吸収液スラリ中のCaCO3濃度も高
める)に制御することにより、経済的でかつ高い脱硫性
能を維持する必要がある。A flue gas desulfurization device is used as a field using a slurry containing CaCO 3, which is used in a thermal power plant or the like to generate sulfur oxides in flue gas generated by fossil fuel combustion, especially sulfur dioxide. This is an apparatus for absorbing and removing (SO 2 ) with an absorbent slurry containing CaCO 3 . In flue gas desulfurization equipment, depending on the boiler load and changes in the properties of the fuel used, Ca
The supply amount of CO 3 was adjusted, and CaCO 3 in the absorbent slurry was adjusted.
The concentration is adjusted to an optimal value (for example, the amount of exhaust gas or SO 2 in exhaust gas).
It is necessary to maintain economical and high desulfurization performance by controlling the concentration of CaCO 3 in the absorbent slurry as the concentration increases.
【0005】しかし、従来の技術では吸収液スラリ中の
CaCO3の測定に長い時間を要し、急なボイラ負荷変
化や使用燃料の性状の変化に対応したCaCO3供給量
の調整が不可能であった。However, in the conventional technique, it takes a long time to measure CaCO 3 in the absorbent slurry, and it is impossible to adjust the supply amount of CaCO 3 in response to a sudden change in boiler load or a change in properties of fuel used. there were.
【0006】このような背景から、本発明者らは短時間
にスラリ中のCaCO3濃度を連続測定する方法を提案
した(特開平9−101296号)。図5に本発明者ら
が提案した前記、出願発明の実施の形態のフローを示
す。[0006] Against this background, the present inventors have proposed a method for continuously measuring the CaCO 3 concentration in a slurry in a short time (Japanese Patent Laid-Open No. 9-101296). FIG. 5 shows a flow of the embodiment of the present invention proposed by the present inventors.
【0007】ライン1からポンプ2により酸添加槽3に
送られたスラリAに、pH計10の指示値に応じて酸添
加槽3内に酸タンク4から酸添加ライン5を通して酸添
加ポンプ12により塩酸Bが添加され、スラリAはライ
ン6の途中に設置されたラインミキサー7により攪拌さ
れた後、測定槽8内に送られる。The slurry A sent from the line 1 to the acid addition tank 3 by the pump 2 is supplied from the acid tank 4 into the acid addition tank 3 through the acid addition line 5 in accordance with the indicated value of the pH meter 10 by the acid addition pump 12. Hydrochloric acid B is added, and the slurry A is sent into the measuring tank 8 after being stirred by the line mixer 7 installed in the middle of the line 6.
【0008】測定槽8では、溶存CO2計9及びpH計
10により、それぞれ溶存CO2濃度及びpHが測定さ
れる。pH計10の測定値が所定の範囲になるように演
算機13により酸添加ポンプ12の流量が調整される。
測定が終了したスラリAはライン11から排出される。
スラリAに酸Bを添加するとスラリA中のCaCO3と
等モルのCO2が発生し、溶解度以下であればCO2は
水に溶解する。このため、スラリA中の溶存CO2濃度
を測定すれば、酸Bを添加する前には同モルのCaCO
3が存在していたことになり、容易にCaCO3濃度を
求めることができる。。In the measuring tank 8, the dissolved CO 2 concentration and pH are measured by a dissolved CO 2 meter 9 and a pH meter 10, respectively. The flow rate of the acid addition pump 12 is adjusted by the calculator 13 so that the measured value of the pH meter 10 falls within a predetermined range.
The slurry A for which the measurement has been completed is discharged from the line 11.
The addition of acid B to the slurry A CaCO 3 and equimolar CO 2 in the slurry A is generated, equal to or less than the solubility CO 2 is dissolved in water. Therefore, if the dissolved CO 2 concentration in the slurry A is measured, the same molar amount of CaCO 2 is added before the acid B is added.
3 was present, and the CaCO 3 concentration can be easily obtained. .
【0009】この方法により排煙脱硫装置で用いる脱硫
スラリA中のCaCO3濃度を測定した結果、ほとんど
の場合でJISR9101に定められている方法と測定
誤差の範囲以内で同じ値が得られた。しかし、スラリA
中のCaCO3濃度が急に変動した場合、酸添加槽3や
測定槽8内のスラリが完全に置換されるのに時間がかか
り、それまでは真のCaCO3濃度が測定されない。As a result of measuring the CaCO 3 concentration in the desulfurization slurry A used in the flue gas desulfurization apparatus according to this method, the same value was obtained in almost all cases within the range of measurement error as in the method specified in JISR9101. However, slurry A
If the CaCO 3 concentration in the medium fluctuates suddenly, it takes time to completely replace the slurry in the acid addition tank 3 and the measurement tank 8, and the true CaCO 3 concentration is not measured until then.
【0010】また、酸Bを添加する場所とpHを測定す
る場所が離れているとスラリA中のCaCO3濃度が変
動した場合にpHの値が振動(ハンチング)するため所
定のpHに調整できず、正確なCaCO3濃度が測定さ
れない。特に、排煙脱硫装置ではボイラ負荷や使用燃料
の性状の変化に応じてCaCO3の供給量を調整し、吸
収液スラリA中の濃度を最適な値に制御することにより
経済的でかつ高い脱硫性能を維持する必要があるため、
スラリA中のCaCO3濃度が短時間で増減することが
しばしばであり、従来技術ではこのような状況でCaC
O3濃度を正確に測定することは不可能である。Further, if the place where the acid B is added is far from the place where the pH is measured, the pH value fluctuates (hunts) when the CaCO 3 concentration in the slurry A fluctuates. And an accurate CaCO 3 concentration is not measured. In particular, in a flue gas desulfurization apparatus, the supply amount of CaCO 3 is adjusted according to the change in the boiler load and the properties of the fuel used, and the concentration in the absorption liquid slurry A is controlled to an optimal value, thereby achieving economical and high desulfurization. Because it is necessary to maintain performance,
Often, the CaCO 3 concentration in the slurry A increases and decreases in a short time.
It is not possible to measure the O 3 concentration accurately.
【0011】このような問題を解決する1つの方法とし
て、図6に示すように酸Bをライン1中に添加し、かつ
pH測定槽14(pH計検出器10Aのみが槽内に設置
されるので測定槽8より内容積が小さい)で酸添加後の
pHの値が振動(ハンチング)することを抑制すること
は可能である。しかし、このような方法ではスラリ中の
CaCO3が完全には反応しないまま測定槽8内に送ら
れ、溶存CO2計9により溶存CO2濃度が測定される
ため、誤差を生じる場合があることが判明した。As one method for solving such a problem, as shown in FIG. 6, acid B is added to the line 1 and a pH measuring tank 14 (only the pH meter detector 10A is installed in the tank). Therefore, it is possible to prevent the pH value after the acid addition from oscillating (hunting) in the measuring tank 8). However, in such a method, CaCO 3 in the slurry is sent into the measuring tank 8 without completely reacting, and the dissolved CO 2 concentration is measured by the dissolved CO 2 meter 9, which may cause an error. There was found.
【0012】このように従来技術では、酸Bの添加から
pH測定までのスラリAの容積を小さくするとスラリA
中のCaCO3濃度が変動した場合の応答時間を短くで
き、またpHのハンチングも防止できるが、スラリA中
のCaCO3が完全には反応しないまま測定槽8内に送
られるため誤差を生じるという問題があった。As described above, in the prior art, when the volume of the slurry A from the addition of the acid B to the pH measurement is reduced, the slurry A
Although the response time when the concentration of CaCO 3 in the medium fluctuates can be shortened and the hunting of pH can be prevented, the CaCO 3 in the slurry A is sent into the measuring tank 8 without completely reacting, and an error occurs. There was a problem.
【0013】[0013]
【発明が解決しようとする課題】上記従来技術では、ス
ラリA中のCaCO3濃度が急に変動した場合に真のC
aCO3濃度が検知されるのに時間がかかったり、誤差
を生じるという問題があった。本発明の課題は、上記従
来技術の問題点を解決し、排煙脱硫装置の吸収液スラリ
などのスラリ中のCaCO3濃度が急に変動しても短時
間にスラリ中のCaCO3濃度を正確に測定できる方法
を提案することにある。In the above prior art, when the CaCO 3 concentration in the slurry A suddenly fluctuates, the true C
There has been a problem that it takes time to detect the aCO 3 concentration or an error occurs. The object of the present invention is to solve the above-mentioned problems of the prior art, and to accurately determine the CaCO 3 concentration in a slurry in a short time even if the CaCO 3 concentration in a slurry such as an absorption liquid slurry of a flue gas desulfurization device fluctuates rapidly. It is to propose a method that can be measured.
【0014】[0014]
【課題を解決するための手段】上記本発明の課題は、酸
を添加した後の2カ所以上でのスラリのpHを検出し、
それぞれの測定値及び前記両pH測定値の差に応じて酸
の添加量を変化させること、より好ましくは、該溶存C
O2濃度検出器の前後でのpH値の測定値及び前記両p
H測定値の差に応じて酸の添加量を変化させること、さ
らにより具体的には、前記両pH値の測定値の差がある
設定値より大きい場合は酸の添加量を増加させ、ある設
定値より小さい場合は酸の添加量を減少させることによ
り達成される。The object of the present invention is to detect the pH of a slurry at two or more places after the addition of an acid,
The addition amount of the acid is changed according to each measured value and the difference between the two pH measured values, more preferably, the dissolved C
Measured pH values before and after the O 2 concentration detector
Changing the amount of acid added according to the difference between the measured H values, and even more specifically, increasing the amount of acid added when the difference between the measured values of the two pH values is greater than a certain set value; If it is smaller than the set value, it is achieved by decreasing the amount of acid added.
【0015】なお、スラリ中の溶存CO2濃度を測定す
る方法としては、(a)気体透過膜によってスラリと隔
離された熱伝導度検出素子を利用した方法、(b)気体
透過膜によってスラリと隔離された蛍光色素溶液中にス
ラリ中のCO2が溶け込むことにより蛍光強度が変化す
る現象を利用した方法、又は(c)気体透過膜によって
スラリと隔離された溶液中にスラリ中のCO2が溶け込
むことにより溶液のpHが変化する現象を利用した方法
など既知のあらゆる方法を用いることができる。The method of measuring the concentration of dissolved CO 2 in the slurry is as follows: (a) a method using a thermal conductivity detecting element separated from the slurry by a gas permeable membrane; A method using a phenomenon in which the fluorescence intensity is changed by dissolving CO 2 in the slurry into the isolated fluorescent dye solution, or (c) CO 2 in the slurry is separated from the slurry by a gas-permeable membrane. Any known method such as a method utilizing a phenomenon in which the pH of a solution changes by dissolution can be used.
【0016】[0016]
【作用】CaCO3に塩酸を添加した時の反応により下
記(1)式に示すように、CaCO3と等モルのCO2
が発生する。CO2は水に溶解するので、溶解度以下で
あれば溶存したCO2濃度を測定することによりスラリ
中のCaCO3濃度を求めることができる。例えば、溶
存したCO2濃度がX(g/L)であれば、CO 2の分
子量は44であるのでスラリ中のCaCO3濃度はX/
44(mol/L)になる。[Action] CaCO3Due to the reaction when hydrochloric acid is added to
As shown in equation (1), CaCO3And equimolar CO2
Occurs. CO2Is soluble in water.
If there is dissolved CO2Slurry by measuring concentration
CaCO in3The concentration can be determined. For example,
Existed CO2If the concentration is X (g / L), CO 2Minute
Since the amount of particles is 44, CaCO in the slurry3The concentration is X /
44 (mol / L).
【0017】 CaCO3+2HCl=CaCl2+CO2+H2O (1) スラリ中の正確なCaCO3濃度を求めるにはスラリ中
のすべてのCaCO3を酸と反応させる必要があるが、
スラリ中のCaCO3が完全には反応しないまま測定槽
8内に送られ、溶存CO2計9により溶存CO2濃度が
測定されるため、誤差を生じる場合があるので、必要な
塩酸の量はスラリのpHを測定しながら調整する必要が
ある。CaCO 3 + 2HCl = CaCl 2 + CO 2 + H 2 O (1) In order to obtain an accurate CaCO 3 concentration in the slurry, it is necessary to react all CaCO 3 in the slurry with an acid.
The CaCO 3 in the slurry is sent into the measuring tank 8 without completely reacting, and the dissolved CO 2 concentration is measured by the dissolved CO 2 meter 9, which may cause an error. It is necessary to adjust while measuring the pH of the slurry.
【0018】適切なpHの値は、例えば石灰石(主成C
aCO3)粒子の粒径や反応性(不純物の量や粒子表面
の付着物)、さらには酸を添加した後の攪拌状態や測定
までの時間などによっても異なる。本発明者らの研究に
より、通常はpHが2〜4程度になるように酸を添加す
ることが好ましいことが分かった。pHは2以下でも測
定精度には問題はないが、酸の添加量が増加して経済的
でない。Suitable pH values include, for example, limestone (C
It varies depending on the particle size and reactivity of the (aCO 3 ) particles (the amount of impurities and deposits on the particle surface), and also the stirring state after the addition of the acid and the time until measurement. According to the study of the present inventors, it has been found that it is usually preferable to add an acid so that the pH becomes about 2 to 4. If the pH is 2 or less, there is no problem in the measurement accuracy, but it is not economical because the amount of acid added increases.
【0019】スラリ中のCaCO3濃度が変動した場
合、酸の添加量は変化する。例えば、スラリ中のCaC
O3濃度が急に変動した場合、pH計での測定値が上昇
したことを検知した後に酸の添加量を増加させるため、
図5に示した従来技術では正確なCaCO3濃度を検知
するまでに時間がかかる。また、図6に示した従来技術
では、スラリ中のCaCO3が酸と完全には反応しない
まま測定槽8内に送られ、溶存CO2計9により溶存C
O2濃度が測定されるため、誤差を生じる(真CaCO
3濃度より低い値を検出する)場合がある。When the CaCO 3 concentration in the slurry fluctuates, the amount of acid added changes. For example, CaC in slurry
When the O 3 concentration fluctuates suddenly, the amount of acid added is increased after detecting that the value measured by the pH meter has increased,
In the prior art shown in FIG. 5, it takes time to detect an accurate CaCO 3 concentration. In the prior art shown in FIG. 6, CaCO 3 in the slurry is sent to the measuring tank 8 without completely reacting with the acid, and the dissolved C 2 is measured by the dissolved CO 2 meter 9.
Since the O 2 concentration is measured, an error occurs (true CaCO 2).
3 values lower than the density).
【0020】これに対して、本発明の方法では、スラリ
中のCaCO3濃度が変動した場合には上流側のpH計
でより早く酸添加量を増減し、さらに下流側のpH計と
の差からスラリ中のCaCO3が酸と完全に反応したか
否かが判定できるため、スラリ中のCaCO3濃度が急
に変動した場合でも短時間で正確なCaCO3濃度を求
めることが可能になる。On the other hand, in the method of the present invention, when the CaCO 3 concentration in the slurry fluctuates, the amount of acid added is increased or decreased more quickly by the pH meter on the upstream side, and the difference from the pH meter on the downstream side is further increased. Thus, it can be determined whether or not CaCO 3 in the slurry has completely reacted with the acid. Therefore, even when the CaCO 3 concentration in the slurry fluctuates suddenly, it is possible to obtain an accurate CaCO 3 concentration in a short time.
【0021】これは、酸の添加量が十分でスラリ中のC
aCO3が酸と完全に反応した場合、上記(1)式に示
した反応はこれ以上進行しないため、上流側と下流側と
のpH計の指示値の差は小さい。このため、スラリ中の
CaCO3が酸と完全に反応したか否かが分かる。酸の
添加量が極めて少なく、上記(1)式の反応が短時間に
終了した場合でも上流側と下流側とのpH計の指示値の
差は小さくなるが、この場合はpH指示値の絶対値が高
く(pH4.0以上)なるため、スラリ中のCaCO3
が酸と完全には反応していないことが分かる。This is because the amount of acid added is sufficient and the C
When aCO 3 completely reacts with the acid, the reaction shown in the above formula (1) does not proceed any more, and the difference between the indicated values of the pH meter between the upstream side and the downstream side is small. Thus, it can be seen whether CaCO 3 in the slurry has completely reacted with the acid. Even when the amount of acid added is extremely small and the reaction of the above formula (1) is completed in a short time, the difference between the indicated values of the pH meter between the upstream side and the downstream side becomes small. Value (pH 4.0 or higher), CaCO 3 in the slurry
Is not completely reacted with the acid.
【0022】[0022]
【発明の実施の形態】本発明は、下記の実施の形態によ
って、さらに詳細に説明されるが、下記の例で制限され
るものではない。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in more detail by the following embodiments, but is not limited by the following examples.
【0023】実施例1 本発明による実施の形態の例を図1に示す。図5、図6
に示す従来技術と同様、酸添加槽3,酸タンク4,ライ
ンミキサー7,測定槽8,溶存CO2計9及びpH計1
0により構成されるが、図1に示す例では、さらに溶存
CO2計9の前後にpH計10及び10’を備え、pH
測定値及び溶存CO2測定値の差に応じて演算機13及
び酸添加物ポンプ12により酸の添加量を変化させるこ
とができる。Embodiment 1 FIG. 1 shows an embodiment of the present invention. 5 and 6
As in the prior art shown in FIG. 1, an acid addition tank 3, an acid tank 4, a line mixer 7, a measuring tank 8, a dissolved CO 2 meter 9 and a pH meter 1
However, in the example shown in FIG. 1, pH meters 10 and 10 ′ are further provided before and after the dissolved CO 2
The amount of acid to be added can be changed by the calculator 13 and the acid additive pump 12 according to the difference between the measured value and the dissolved CO 2 measured value.
【0024】ライン1からポンプ2により酸添加槽3に
送られたスラリAに、演算機13からの信号に応じて酸
添加槽3内に酸タンク4から酸添加ライン5を通して酸
添加ポンプ12により塩酸Bが添加され、スラリAはラ
イン6の途中に設置されたラインミキサー7により攪拌
された後、pH測定槽14でpH計10によりpHが測
定される。The slurry A sent from the line 1 to the acid addition tank 3 by the pump 2 is fed into the acid addition tank 3 from the acid tank 4 through the acid addition line 5 by the acid addition pump 12 in response to a signal from the computer 13. Hydrochloric acid B is added, and the slurry A is stirred by the line mixer 7 installed in the middle of the line 6, and then the pH is measured by the pH meter 10 in the pH measuring tank 14.
【0025】次いで、スラリは測定槽8内に送られ、そ
こで溶存CO2計9により、溶存CO2濃度の測定が行
われ、その後、さらにpH測定槽14’でpH計10’
によりpHが測定される。pH計10の測定値及びpH
計10’での測定値の差が所定の範囲になるように演算
機13により酸添加ポンプ12の流量が調整される。前
記測定が終了したスラリAはライン11から排出され
る。Next, the slurry is sent into the measuring tank 8 where the dissolved CO 2 concentration is measured by the dissolved CO 2 meter 9, and then the pH meter 10 ′ is further measured in the pH measuring tank 14 ′.
Measures the pH. Measured value of pH meter 10 and pH
The flow rate of the acid addition pump 12 is adjusted by the calculator 13 so that the difference between the measured values in the total 10 ′ falls within a predetermined range. The slurry A for which the measurement has been completed is discharged from the line 11.
【0026】具体的には、pH計10の測定値が2.4
〜2.6で、pH計10及び10’での測定値の差が
0.2〜0.3になるように酸添加ポンプ12の流量が
調整された。pH計10の測定値とpH計10及び1
0’での測定値の差のいずれか一方でも設定値より大き
い場合は酸添加ポンプ12の流量を増加させた。Specifically, the measured value of the pH meter 10 is 2.4.
At ~ 2.6, the flow rate of the acid addition pump 12 was adjusted so that the difference between the measured values at the pH meters 10 and 10 'would be 0.2-0.3. Measured value of pH meter 10 and pH meters 10 and 1
When any one of the measured value differences at 0 'was larger than the set value, the flow rate of the acid addition pump 12 was increased.
【0027】図1に示す測定装置を用いて、スラリA中
のCaCO3濃度をステップ状に増減させた際の測定装
置の応答時間を調べた。図2の曲線aにスラリA中のC
aCO3濃度をステップ状に増減させた際の濃度を、曲
線bに図1の測定装置で測定した結果を示す。Using the measuring apparatus shown in FIG. 1, the response time of the measuring apparatus when the CaCO 3 concentration in the slurry A was increased or decreased in a stepwise manner was examined. The curve a in FIG.
A curve b shows the result of measurement of the concentration when the aCO 3 concentration was increased or decreased in a step-like manner, using the measurement apparatus shown in FIG.
【0028】なお、図2の曲線aの値は、スラリAをサ
ンプリングし、JISR9101に定められている手分
析法でCaCO3濃度を測定した結果である。また、縦
軸は溶存CO2計9の検出値からスラリA中のCaCO
3濃度を換算した結果で示した(単位:mmol/
L)。曲線aと曲線bはよく一致し、スラリA中のCa
CO3濃度が変動しても図1の測定装置では時間遅れが
小さいことが分かる。なお、pH計10とpH計10’
での測定値の差が設定値より大きい場合の酸添加ポンプ
12の流量の調整方法は、図7に示したように測定値の
差が大きいほど酸添加ポンプ12の流量の調整を行うこ
とも可能であることはいうまでもない。The value of the curve a in FIG. 2 is a result of sampling the slurry A and measuring the CaCO 3 concentration by the manual analysis method specified in JISR9101. The vertical axis indicates CaCO in slurry A from the detected value of dissolved CO 2 9
3 The result was calculated by converting the concentration (unit: mmol /
L). Curve a and curve b agree well, and Ca in slurry A
It can be seen that even if the CO 3 concentration fluctuates, the measuring device of FIG. 1 has a small time delay. In addition, pH meter 10 and pH meter 10 '
In the method of adjusting the flow rate of the acid addition pump 12 in the case where the difference between the measured values is larger than the set value, as shown in FIG. It goes without saying that it is possible.
【0029】比較例1 図5に示した従来技術に基づく測定装置で、図1に示す
装置と同じ条件で同一スラリA中のCaCO3濃度を測
定した。その結果を図2の曲線cに示す。図1に示す装
置と比較してスラリAが相対的にCaCO3濃度が変動
した際の時間遅れが大きい。特に、CaCO3濃度が急
に低下した場合の応答性が悪い。これは、酸添加層3や
測定槽8内の相対的にCaCO3濃度が高いスラリAが
相対的にCaCO3濃度が低いスラリAで置換されるの
に時間がかかるためである。Comparative Example 1 The concentration of CaCO 3 in the same slurry A was measured with the measuring device based on the prior art shown in FIG. 5 under the same conditions as the device shown in FIG. The result is shown by curve c in FIG. The time lag when the CaCO 3 concentration of the slurry A fluctuates relatively is larger than that of the apparatus shown in FIG. In particular, the responsiveness when the CaCO 3 concentration suddenly decreases is poor. This is because it takes time for the slurry A having a relatively high CaCO 3 concentration in the acid addition layer 3 and the measuring tank 8 to be replaced with the slurry A having a relatively low CaCO 3 concentration.
【0030】比較例2 図6に示した従来技術に基づく測定装置で図1と同じ条
件で同一スラリA中のCaCO3濃度を測定した。その
結果を図3の曲線dに示す。比較例1と比べると、時間
遅れは小さくなっているが、測定値が振動(ハンチン
グ)している。Comparative Example 2 The CaCO 3 concentration in the same slurry A was measured under the same conditions as in FIG. 1 using a measuring device based on the prior art shown in FIG. The result is shown by a curve d in FIG. Although the time delay is smaller than that of Comparative Example 1, the measured value is oscillating (hunting).
【0031】上記図1又は図5、図6の装置では酸とし
て塩酸Bを用いているが、塩酸以外でもCaCO3と反
応する硫酸など他の酸を用いることができることはいう
までもない。In the apparatus shown in FIG. 1, FIG. 5, and FIG. 6, hydrochloric acid B is used as the acid, but it goes without saying that other acids such as sulfuric acid that reacts with CaCO 3 can be used other than hydrochloric acid.
【0032】図1に示す例では溶存CO2計9の前後で
のpHを測定しているが、図4に示すように溶存CO2
計9の前に2台pH計10、10’を設置することも可
能である。ただし、溶存CO2計9の前後でのpHを測
定する方が好ましい。[0032] In the example shown in FIG. 1 measures the pH of the before and after of dissolved CO 2 meter 9, dissolved CO 2 as shown in FIG. 4
It is also possible to install two pH meters 10, 10 'before the total 9. However, it is more preferable to measure the pH before and after the dissolved CO 2 measurement.
【0033】[0033]
【発明の効果】本発明によれば、スラリ中のCaCO3
濃度が急に変動しても短時間にスラリ中のCaCO3濃
度を正確に測定することができる。According to the present invention, CaCO 3 in the slurry
Even if the concentration fluctuates suddenly, the CaCO 3 concentration in the slurry can be accurately measured in a short time.
【図1】 本発明の実施の形態におけるCaCO3濃度
の測定装置のフロー図である。FIG. 1 is a flowchart of a CaCO 3 concentration measuring device according to an embodiment of the present invention.
【図2】 図1のCaCO3濃度の測定装置と比較例1
の実験データである。FIG. 2 shows a CaCO 3 concentration measuring apparatus shown in FIG. 1 and Comparative Example 1
Is experimental data.
【図3】 図1のCaCO3濃度の測定装置と比較例2
の実験データである。FIG. 3 shows a CaCO 3 concentration measuring apparatus shown in FIG. 1 and Comparative Example 2
Is experimental data.
【図4】 本発明の実施の形態におけるCaCO3濃度
測定装置のフロー図である。FIG. 4 is a flowchart of a CaCO 3 concentration measuring device according to an embodiment of the present invention.
【図5】 従来技術におけるCaCO3濃度測定装置の
フロー図である。FIG. 5 is a flow chart of a CaCO 3 concentration measuring device in a conventional technique.
【図6】 従来技術におけるCaCO3濃度測定装置の
フロー図である。FIG. 6 is a flow chart of a CaCO 3 concentration measuring device in the prior art.
【図7】 酸添加ポンプの運転方法の一例である。FIG. 7 is an example of an operation method of an acid addition pump.
1、6、11 ライン 2 ポンプ 3 酸添加槽 4 酸タンク 5 酸添加ライン 7 ラインミキ
サー 8 測定槽 9 溶存CO2
計 10、10’ pH計 12 酸添加物
ポンプ 13 演算機 14 pH測定
槽 A スラリ B 塩酸1, 6, 11 line 2 pump 3 acid addition tank 4 acid tank 5 acid addition line 7 line mixer 8 measuring tank 9 dissolved CO 2
Total 10, 10 'pH meter 12 Acid additive pump 13 Computer 14 pH measuring tank A Slurry B Hydrochloric acid
───────────────────────────────────────────────────── フロントページの続き (72)発明者 高本 成仁 広島県呉市宝町3番36号 バブコック日立 株式会社呉研究所内 (72)発明者 野沢 滋 広島県呉市宝町6番9号 バブコック日立 株式会社呉工場内 Fターム(参考) 2G042 AA01 BB03 BB05 CA10 CB04 FA01 HA07 4D002 AA02 BA02 DA05 DA16 GA02 GB08 GB09 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Seiji Takamoto 3-36 Takara-cho, Kure-shi, Hiroshima Pref. Inside the Kure Research Laboratory, Babcock Hitachi Co., Ltd. (72) Inventor Shigeru Nozawa 6-9 Takara-cho, Kure-shi, Hiroshima Pref. F-term in the Kure factory (reference) 2G042 AA01 BB03 BB05 CA10 CB04 FA01 HA07 4D002 AA02 BA02 DA05 DA16 GA02 GB08 GB09
Claims (4)
酸を添加した後、スラリ中の溶存CO2濃度を測定する
ことにより、該スラリ中に存在していた炭酸塩濃度を測
定する方法において、 酸を添加した後流側の2カ所以上のスラリ流れの中でス
ラリのpHを検出し、それぞれの測定値及び前記両pH
測定値の差に応じて酸の添加量を変化させることを特徴
とするスラリ中の炭酸塩濃度の測定法。1. A method for measuring the concentration of carbonate present in a slurry by adding an acid while flowing a slurry containing a carbonate through a cell and then measuring the concentration of dissolved CO 2 in the slurry. The pH of the slurry is detected in two or more slurry streams on the downstream side after adding the acid, and the respective measured values and both pH values are measured.
A method for measuring a carbonate concentration in a slurry, wherein an amount of an acid added is changed according to a difference between measured values.
リ流れでのpH値の測定値及び前記両pH測定値の差に
応じて酸の添加量を変化させることを特徴とする請求項
1記載のスラリ中の炭酸塩濃度の測定法。2. The method according to claim 1, wherein the addition amount of the acid is changed according to the measured value of the pH value in the slurry flow before and after the dissolved CO 2 concentration detection site and the difference between the measured pH values. A method for measuring the concentration of carbonate in the slurry described.
より大きい場合は酸の添加量を増加させ、ある設定値よ
り小さい場合は酸の添加量を減少させることを特徴とす
る請求項1または2記載のスラリ中の炭酸塩濃度の測定
法。3. The method according to claim 1, wherein when the difference between the measured values of the two pH values is larger than a certain set value, the amount of acid added is increased, and when the difference is smaller than a certain set value, the added amount of acid is decreased. Item 3. The method for measuring a carbonate concentration in a slurry according to Item 1 or 2.
ルに酸を添加する酸添加手段と、酸添加後のスラリ中の
溶存CO2濃度を測定する溶存CO2計と、酸を添加し
た部位より後流側の2カ所以上のセル内のスラリのpH
を検出するpH計と、前記各pH計の測定値及び前記両
pH測定値の差を計算する演算機と、該演算機の測定値
及び前記両pH測定値の差に応じて酸の添加量を変化さ
せるポンプとを備えたことを特徴とするスラリ中の炭酸
塩濃度の測定装置。Added 4. A cell flowing slurry containing carbonate, an acid adding means for adding an acid to the cell, and the dissolved CO 2 meter for measuring the dissolved CO 2 concentration in the slurry after acid addition, the acid PH of the slurry in two or more cells downstream of the site
And a calculator for calculating the difference between the measured value of each of the pH meters and the measured pH value, and the amount of the acid added according to the measured value of the calculator and the difference between the measured pH values. And a pump for changing the pressure of the slurry.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10217592A JP2000046821A (en) | 1998-07-31 | 1998-07-31 | Method and apparatus for measuring concentration of carbonate in slurry |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10217592A JP2000046821A (en) | 1998-07-31 | 1998-07-31 | Method and apparatus for measuring concentration of carbonate in slurry |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000046821A true JP2000046821A (en) | 2000-02-18 |
Family
ID=16706719
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10217592A Pending JP2000046821A (en) | 1998-07-31 | 1998-07-31 | Method and apparatus for measuring concentration of carbonate in slurry |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2000046821A (en) |
-
1998
- 1998-07-31 JP JP10217592A patent/JP2000046821A/en active Pending
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