JPH0315970B2 - - Google Patents
Info
- Publication number
- JPH0315970B2 JPH0315970B2 JP58158957A JP15895783A JPH0315970B2 JP H0315970 B2 JPH0315970 B2 JP H0315970B2 JP 58158957 A JP58158957 A JP 58158957A JP 15895783 A JP15895783 A JP 15895783A JP H0315970 B2 JPH0315970 B2 JP H0315970B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- pickling
- liquid
- sludge
- 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 - Lifetime
Links
- 239000007788 liquid Substances 0.000 claims description 36
- 238000005554 pickling Methods 0.000 claims description 29
- 239000000463 material Substances 0.000 claims description 17
- 238000004448 titration Methods 0.000 claims description 15
- 239000002253 acid Substances 0.000 claims description 11
- 238000005070 sampling Methods 0.000 claims description 9
- 229910000831 Steel Inorganic materials 0.000 claims description 7
- 239000010959 steel Substances 0.000 claims description 7
- 239000010802 sludge Substances 0.000 description 18
- 230000005484 gravity Effects 0.000 description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 11
- 238000005259 measurement Methods 0.000 description 10
- 239000002245 particle Substances 0.000 description 8
- 238000004458 analytical method Methods 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000011449 brick Substances 0.000 description 5
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 2
- 150000002506 iron compounds Chemical class 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000005097 cold rolling Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000010301 surface-oxidation reaction Methods 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/28—Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
- G01N1/40—Concentrating samples
- G01N1/4077—Concentrating samples by other techniques involving separation of suspended solids
Landscapes
- Physics & Mathematics (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Filtration Of Liquid (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Sampling And Sample Adjustment (AREA)
Description
【発明の詳細な説明】
本発明は、鋼帯の連続酸洗設備等における酸洗
液の酸濃度を測定するための酸液サンプリング装
置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an acid liquid sampling device for measuring the acid concentration of a pickling liquid in continuous pickling equipment for steel strips.
一般に、熱間圧延された鋼板の表面部には、
FeO,Fe3O4,Fe2O3等の酸化スケール皮膜が生
成されており、冷間圧延等の次工程に通す前に、
表面酸化スケールを除去する必要がある。一般的
には、塩酸または硫酸等を用いた連続酸洗設備に
よつて鋼帯の表面酸化スケールは連続的に除去さ
れる。この時、酸洗液の濃度により酸洗性能は大
きく左右される。第1図は塩酸濃度の大小による
酸洗時間の変化を、第2図は塩化鉄濃度の大小に
よる酸洗時間の変化を例示している。したがつ
て、これまでの知見から、塩化鉄濃度を適正値に
保ち、酸濃度を上げていくことによつて酸洗性能
を向上し、操業性を上げることができることが知
られている。 Generally, on the surface of hot rolled steel plate,
Oxidized scale films such as FeO, Fe 3 O 4 and Fe 2 O 3 are formed, and before passing through the next process such as cold rolling,
It is necessary to remove surface oxide scale. Generally, surface oxidation scale on the steel strip is continuously removed by continuous pickling equipment using hydrochloric acid, sulfuric acid, or the like. At this time, the pickling performance is greatly influenced by the concentration of the pickling solution. FIG. 1 illustrates changes in pickling time depending on the concentration of hydrochloric acid, and FIG. 2 illustrates changes in pickling time depending on the concentration of iron chloride. Therefore, it is known from past knowledge that pickling performance and operability can be improved by keeping the iron chloride concentration at an appropriate value and increasing the acid concentration.
しかし、酸濃度を必要以上に高めると、酸の蒸
発による酸原単位の悪化および地鉄溶損による歩
止りの悪化をまねくという問題が生ずる。したが
つて、酸濃度は常に測定監視し、操業状況に見合
つた調整および管理をする必要がある。 However, if the acid concentration is increased more than necessary, problems arise in that the acid consumption rate deteriorates due to acid evaporation and the yield rate deteriorates due to erosion of the base metal. Therefore, it is necessary to constantly measure and monitor the acid concentration, and to adjust and manage it in accordance with the operating conditions.
酸濃度の測定方法としては、比色および比重方
式、導電率および比重方式などが従来提案されて
いる。しかし、いずれの方式も間接的測定であ
り、種々の要因によつて影響を受け易く、誤差が
大きい所から、うまく実用化できず、滴定法によ
る手分析による濃度測定を行なつているのが現状
である。しかし、この手分析方法は直接的測定
(滴定法)であるため、測定精度は良好であるが、
次のような欠点を有している。 As methods for measuring acid concentration, colorimetric and specific gravity methods, conductivity and specific gravity methods, and the like have been proposed. However, since both methods are indirect measurements, they are susceptible to various factors and have large errors, making them difficult to put into practical use.Concentration measurements are now performed by manual analysis using the titration method. This is the current situation. However, since this manual analysis method is a direct measurement (titration method), the measurement accuracy is good, but
It has the following drawbacks.
すなわち、(イ)手分析であるため、測定者の個人
差による誤差がある。(ロ)バツチサンプリングで1
回当りの測定時間が長いため、分析回数が多く取
れない。(ニ)酸を直接扱うため危険な作業となる。 That is, (a) since it is a manual analysis, there are errors due to individual differences among the measurers. (b) 1 with batch sampling
Because the measurement time per measurement is long, it is not possible to analyze many times. (d) The work is dangerous as it involves direct handling of acids.
ところが、最近では、自動滴定装置が開発さ
れ、実験等に使用されるようになつてきている。
しかしながら、この種の市販の自動滴定装置を鋼
帯連続酸洗ラインのような操業設備に使用するに
は、下記のような問題点があつた。すなわち、酸
洗液中には、スラツジが含まれており、このスラ
ツジの除去を目的として自動滴定装置の入側に従
来既知の形式の過器を設置しても過材がすぐ
に目詰りしてしまうという問題が、過性能が十
分でない過器では自動滴定装置内の配管が詰ま
つてしまうという問題があつた。 However, recently, automatic titration devices have been developed and are being used for experiments and the like.
However, when this type of commercially available automatic titration device is used in operational equipment such as a continuous pickling line for steel strips, the following problems arise. In other words, the pickling solution contains sludge, and even if a conventionally known type of filtration device is installed on the inlet side of an automatic titration device for the purpose of removing this sludge, the sludge will quickly become clogged. However, there was a problem that the pipes in the automatic titrator would become clogged if the overcapacity was not sufficient.
一般に、酸洗ラインにおける酸洗液中には、
100〜300g/Nm3程度のスラツジが含まれてお
り、さらにこのスラツジは次のような粒度分布を
有している。なお、レンガ屑、ゴム屑は酸洗槽構
成部材の劣化あるいは酸による腐食等によるもの
である。 Generally, the pickling liquid in the pickling line contains:
It contains about 100 to 300 g/Nm 3 of sludge, and this sludge has the following particle size distribution. Note that the brick chips and rubber chips are due to deterioration of the pickling tank components or corrosion due to acid.
粒径1μ以下の鉄化合物(FeCl2またはFeSO4等)
80〜90%
粒径100μ〜1mm程度のレンガ屑 7〜15%
粒径1mm以上のゴム屑 3〜5%
しかるに、一般に使用されている過器の過
材は繊維状のポリプロピレン、グラスウールなど
を布状に編んだもの、あるいは多孔質セラミツク
ス等であるため、前述のようにスラツジの粒径が
大幅に異なり、かつ性質(ゴムは粘性を増し、レ
ンガ、鉄はサラサラした性質を有する)も異なる
ため、上述した構成の従来既知の過器では、目
詰りが激しく(1日〜2日程度でつまる)、実用
上問題があつた。特に、ゴム屑を多く含むスラツ
ジは、粘着性があるため、孔径10μ〜100μ程度の
ものでは、孔をふさいでしまうため、目詰りが激
しく、水、温水、塩酸、空気等により逆洗して
も、除去効果が殆んど上らないという問題があつ
た。Iron compounds (such as FeCl 2 or FeSO 4 ) with a particle size of 1μ or less
80-90% Brick waste with a particle size of about 100 μm to 1 mm 7-15% Rubber waste with a particle size of 1 mm or more 3-5% However, the overmaterial of the commonly used overboard is made of fibrous polypropylene, glass wool, etc. Because the sludge is made of woven material or porous ceramics, the particle size of the sludge differs significantly as mentioned above, and the properties (rubber has increased viscosity, while brick and iron have smooth properties) are also different. In the conventionally known over-container having the above-mentioned configuration, clogging was severe (it clogged within about 1 to 2 days), which caused problems in practical use. In particular, sludge that contains a lot of rubber waste is sticky, so if the sludge has a pore diameter of 10μ to 100μ, it will block the pores and cause severe clogging. However, there was a problem that the removal effect was hardly improved.
本発明は、上述した問題に鑑みなされたもの
で、鋼帯の連続酸洗槽から酸洗液を自動滴定装置
に供給する管路に設けられる過器がスラツジに
よる目詰りを生じないような構成とすることによ
つて、従来困難とされていた鋼帯の連続酸洗ライ
ンにおける酸洗液の濃度測定を自動的に行うこと
を可能にする酸洗液サンプリング装置を提供しよ
うとするものである。 The present invention has been made in view of the above-mentioned problems, and has a structure that prevents clogging with sludge of a filter installed in a pipe line that supplies pickling liquid from a continuous steel strip pickling tank to an automatic titration device. By doing so, the present invention aims to provide a pickling liquid sampling device that makes it possible to automatically measure the concentration of pickling liquid in a continuous pickling line for steel strips, which has been considered difficult in the past. .
以下、本発明を図面に示す実施例につき説明す
る。第3図は滴定装置に供給する酸洗液中のスラ
ツジ分により、滴定装置内で、目詰まりが発生し
ないレベルまで酸洗液中のスラツジ分を滴定装置
の入側にて除去するようにした本発明による構成
を示す。図面において、1はサンプリング液の供
給配管であり、酸洗槽等(図示せず)に連結され
ている。2は1次過器、3はポンプである。4
a,4bは2次過器、5は流量計である。また
6は自動滴定装置である。7は濃度測定後の酸洗
液戻り配管であり、8は純水を自動滴定装置6に
供給する配管である。更に9〜19は各バルブを
示している。 The present invention will be described below with reference to embodiments shown in the drawings. Figure 3 shows a system in which the sludge in the pickling liquid supplied to the titration device is removed at the inlet side of the titration device to a level that does not cause clogging. 1 shows a configuration according to the present invention. In the drawing, 1 is a sampling liquid supply pipe, which is connected to a pickling tank or the like (not shown). 2 is a primary filter, and 3 is a pump. 4
a, 4b are secondary filters, and 5 is a flow meter. Further, 6 is an automatic titration device. 7 is a pickling liquid return pipe after concentration measurement, and 8 is a pipe for supplying pure water to the automatic titration device 6. Further, numerals 9 to 19 indicate respective valves.
次に上記2次過器4a,4bについて第4〜
6図に基ずいて述べる。 Next, regarding the secondary filters 4a and 4b, the fourth to
The explanation will be based on Figure 6.
41は過器本体、42は過材、43は液入
口、44は液出口である。また、45はドレン排
出口である。尚、46は過材42を挿入、保持
するためのガイド、47は過材42の交換及び
内部点検用のフランジである。 41 is a filter body, 42 is a filter material, 43 is a liquid inlet, and 44 is a liquid outlet. Further, 45 is a drain outlet. In addition, 46 is a guide for inserting and holding the overfill material 42, and 47 is a flange for replacing the overfill material 42 and inspecting the inside.
過材は第4図に示すようなガイド46により
過器本体41内部に差込んで取付固定されてい
るため、容易に交換可能であり、上部から作業が
できるため過材の交換に際し、内部の塩酸等を
ぬき取る必要がなく安全である。 The overfill material is inserted into the inside of the overboard body 41 and fixed by a guide 46 as shown in Fig. 4, so it can be easily replaced, and since the work can be done from the top, when replacing the overfill material, it is necessary to It is safe as there is no need to remove hydrochloric acid, etc.
過材42の詳細は第6図のように過材をほ
ぼ上、中、下に3等分し、上部は直径1mm〜5mm
の孔50をあけておき、比重の軽いゴム屑を捕捉
することを目的とする。 The details of the overfill material 42 are as shown in Figure 6, where the overfill material is roughly divided into three equal parts, top, middle, and bottom, and the top has a diameter of 1 mm to 5 mm.
The purpose of this hole 50 is to trap rubber debris with a light specific gravity.
中部は直径100μ〜1mmの孔51をあけておき、
比重が中程度のレンガ屑を主に捕捉する。それぞ
れの孔の数は機械加工が可能なかぎり多くして
過効率の向上をはかる。 A hole 51 with a diameter of 100μ to 1mm is opened in the middle part.
Mainly captures brick debris with medium specific gravity. The number of holes in each hole is increased as much as possible by machining in order to improve overefficiency.
下部42aでは全く孔がなく、この部分ではサ
ンプル液は滞溜し、比重の重い鉄分が沈澱し、堆
積する。 There are no holes in the lower part 42a, and the sample liquid stagnates in this part, and iron with a heavy specific gravity precipitates and accumulates there.
なお過材は正しく3等分する必要はなく、サ
ンプル液中のスラツジの粒径の比により、上部を
大きくしたり、中部を大きくしたりすることは自
由である。 Note that it is not necessary to divide the filtration material into three equal parts, and it is possible to make the upper part larger or the middle part larger depending on the ratio of the particle sizes of the sludge in the sample liquid.
このように一枚の過材に数種類の異なる寸法
の過孔を加工し、スラツジの液との比重差を利
用して過するよう、比重別毎の粒子径に見合う
寸法の過孔を比重の大きいものから小さいもの
に対応するよう、過材の下から上にあければよ
い。なお比重差によるスラツジ除去効果を高める
ため、サンプル液の単位時間あたりの流入量はで
きるだけ少量がよい。 In this way, several types of holes with different sizes are machined in a single sheet of overfill material, and in order to take advantage of the difference in specific gravity with the sludge liquid, we create holes with a size that corresponds to the particle diameter of each specific gravity. You can open the holes from the bottom to the top of the overfill so that it corresponds to the largest to the smallest. In order to enhance the sludge removal effect due to the difference in specific gravity, it is preferable that the inflow amount of the sample liquid per unit time be as small as possible.
過器本体の大きさは反対に大きい程良いがサ
ンプル液の遅れ時間があまり大きいのは実用上問
題がある。おおむね流入量に対し、過器内部で
の滞溜時間を1分〜3分とするのがよい。 On the contrary, the larger the size of the filter body, the better, but it is a practical problem if the delay time of the sample liquid is too long. It is preferable that the residence time inside the filter is approximately 1 to 3 minutes relative to the inflow amount.
過器内部に堆積したスラツジは逆洗液を液出
口44から流してドレン排出口45より排出する
ことができる。この場合、液入口43は閉じてお
く、一般にはこのバルブの切換を定期的に自動又
は手動で行ない、逆洗用液体の圧力は2〜5Kg/
cm2が利用される。 The sludge accumulated inside the filter can be discharged from the drain outlet 45 by flowing the backwashing liquid through the liquid outlet 44. In this case, the liquid inlet 43 is kept closed. Generally, this valve is switched automatically or manually periodically, and the pressure of the backwash liquid is 2 to 5 kg/kg.
cm2 is used.
次に、第3図に基いて動作について述べる。ポ
ンプ3を起動すると、分析用サンプル液が酸洗槽
(図示せず)から吸引され、1次過器2により
大きなゴミなどが除去される。ここで、ポンプ3
は前述したように、2次過器4a,4bが比重
差を利用してスラツジを除去するため精確な設定
が必要となる。したがつて、定量ポンプが望まし
い。このポンプ3により吸引されたサンプル液は
2次過器4a、あるいは4bに送られ、前述の
原理によりスラツジが除去される。すなわち、比
重の重い鉄化合物は、過材の下部には孔がない
ため、沈澱する。比重が中程度のレンガクズに対
して過材の中段にあけられた孔により捕捉し、
さらに最も比重の小さいゴム屑は上段の孔にて捕
捉する。なお第3図では2個の過器4a,4b
が設けられているが、勿論1個の過器だけでも
よい。しかし、図示のように2個の過器を設け
ることによつてバルブ9a,9b,10a,10
bを開閉制御して、交互に使用できるので2次
過器のメンテナンスに便利である。 Next, the operation will be described based on FIG. When the pump 3 is started, a sample liquid for analysis is sucked from a pickling tank (not shown), and large particles and the like are removed by the primary filter 2. Here, pump 3
As described above, since the secondary filters 4a and 4b remove sludge using the difference in specific gravity, accurate settings are required. Therefore, metering pumps are preferred. The sample liquid sucked by the pump 3 is sent to the secondary filter 4a or 4b, and sludge is removed according to the above-mentioned principle. That is, iron compounds with heavy specific gravity precipitate because there are no pores in the lower part of the overfill material. Brick waste with medium specific gravity is captured by the holes drilled in the middle of the overfill material.
Furthermore, rubber debris with the lowest specific gravity is captured in the upper hole. In addition, in Fig. 3, there are two overpass units 4a and 4b.
is provided, but of course only one overpass may be used. However, by providing two overflow devices as shown in the figure, the valves 9a, 9b, 10a, 10
b can be used alternately by controlling opening and closing, which is convenient for maintenance of the secondary filter.
このようにして清澄になつたサンプル液は流量
計5を通り、自動滴定装置6に供給される。分析
されたサンプル液は配管7を通り系外に排出され
る。また配管8からは純水が自動滴定装置6に供
給される。 The sample liquid thus clarified passes through a flowmeter 5 and is supplied to an automatic titration device 6. The analyzed sample liquid passes through piping 7 and is discharged to the outside of the system. Further, pure water is supplied from the pipe 8 to the automatic titration device 6 .
以上においては、バルブ11,12,13,1
5,19は開、バルブ14,16,17,18
a,18bは閉である。また、バルブ9aと10
a及び9bと10bはどちらかのペアが開、他が
閉となつている。尚、バルブ17を開にし、一定
量流すようにしてもよい。これにより、ポンプ保
護が出来る。 In the above, valves 11, 12, 13, 1
5, 19 are open, valves 14, 16, 17, 18
a, 18b are closed. Also, valves 9a and 10
One pair of a, 9b, and 10b is open, and the other is closed. Note that the valve 17 may be opened to allow a certain amount of water to flow. This protects the pump.
予め、設定された回数の測定が完了すれば、ポ
ンプ3を停止し、バルブ16を開にし、配管中の
サンプル液を系外に排出するとともに2次過器
あるいは配管中に堆積したスラツジを除去するの
である。さらに、サンプル液が抜けた時点で、ポ
ンプ3を運転すれば、吐出圧によりさらに除去さ
れるので有効である。このように所定の時間上記
作業を行つたのち、再びサンプリングを開始する
のである。 When the preset number of measurements are completed, the pump 3 is stopped, the valve 16 is opened, and the sample liquid in the piping is discharged to the outside of the system, and the sludge that has accumulated in the secondary filter or the piping is removed. That's what I do. Furthermore, it is effective to operate the pump 3 once the sample liquid has drained, since the discharge pressure will further remove the sample liquid. After performing the above operation for a predetermined period of time, sampling is started again.
このようなサンプリングを繰返し、過器が汚
れてくれば、以下の手順で逆洗を行なう。すなわ
ち、まず、バルブ11を閉にし、バルブ12,1
3,14,15を開にし、自動滴定装置6の内部
の洗浄を行ない、次に、バルブ12,13,19
を閉にし、バルブ11,17を開にして、逆洗を
行なう。 If such sampling is repeated and the filter becomes dirty, perform backwashing using the following procedure. That is, first, valve 11 is closed, and valves 12 and 1 are closed.
3, 14, and 15 to clean the inside of the automatic titration device 6, and then open the valves 12, 13, and 19.
Close the valve, open the valves 11 and 17, and perform backwashing.
以上の動作をシーケンサーにより制御すること
により、自動的に酸洗液のサンプリングと濃度測
定を行なうことができる。 By controlling the above operations with a sequencer, it is possible to automatically sample and measure the concentration of the pickling solution.
次に、塩酸により酸洗する場合の実施例につい
て述べる。2次過器の内容積は1.6で、サン
プル液の流入量は1/minとした。また、過
材の材質はポリプロピレンを用いたが、サンプル
液に腐食されないものであれば任意の材質の過
材を用いることができる。 Next, an example of pickling with hydrochloric acid will be described. The internal volume of the secondary filter was 1.6, and the inflow rate of the sample liquid was 1/min. Further, although polypropylene was used as the material for the overfill, any overfill material may be used as long as it is not corroded by the sample liquid.
第7図に本発明による装置により自動分析して
いる状況を示す。これにより、従来手分析では1
回/4〜5時間の割合で測定していたが、1回/
15分の割合で分析できるようになつたため、この
結果を逐次、酸洗液の濃度調整装置にフイードバ
ツク可能となり、濃度変化を±0.5%の範囲にす
ることができた。尚、従来は±2.0%程度であつ
た。 FIG. 7 shows a situation in which automatic analysis is performed using the apparatus according to the present invention. As a result, conventional manual analysis
Measurement was performed at a rate of 4 to 5 hours per time, but once per hour.
Since analysis can now be performed at a rate of 15 minutes, the results can be fed back to the pickling solution concentration adjustment device, making it possible to keep concentration changes within ±0.5%. Note that conventionally it was about ±2.0%.
尚、2次過器の逆洗を行なうため、第8図に
示すように専用の逆洗液入口52を設けてもよ
い。 In order to backwash the secondary filter, a dedicated backwash liquid inlet 52 may be provided as shown in FIG.
第1図は塩酸濃度と脱スケール時間との関係を
示すグラフ、第2図は酸化鉄濃度と脱スケール時
間との関係を示すグラフ、第3図は本発明による
サンプリング装置の概略線図、第4図は過器の
平面図、第5図は過器の側面図、第6図は過
材の斜視図、第7図はHCl,FeCl2濃度連続測定
図、第8図は過器の他の実施例を示す側面図で
ある。
1……サンプリング液の供給配管、2……1次
過器、3……ポンプ、4a,4b……2次過
器、5……流量計、6……自動滴定装置、7……
酸洗液戻り管路、41……過器本体、42……
過材、43……液入口、43……液出口、45
……ドレン排出口、46……ガイド、50,51
……過孔、52……逆洗液入口。
FIG. 1 is a graph showing the relationship between hydrochloric acid concentration and descaling time, FIG. 2 is a graph showing the relationship between iron oxide concentration and descaling time, and FIG. 3 is a schematic diagram of the sampling device according to the present invention. Figure 4 is a plan view of the filter, Figure 5 is a side view of the filter, Figure 6 is a perspective view of the filter, Figure 7 is a continuous measurement of HCl and FeCl 2 concentrations, and Figure 8 is the other FIG. 1... Sampling liquid supply piping, 2... Primary filter, 3... Pump, 4a, 4b... Secondary filter, 5... Flow meter, 6... Automatic titration device, 7...
Pickling liquid return pipe, 41... Filter unit body, 42...
Overmaterial, 43...liquid inlet, 43...liquid outlet, 45
...Drain outlet, 46...Guide, 50, 51
...Perforation, 52...Backwash liquid inlet.
Claims (1)
置に供給する管路に濾過器が設けられ、この濾過
器の本体内が実質的に直立の板状濾過材により入
口側室と出口側室とに分けられ、前記濾過材の上
方部分に濾過孔を設け、上方部分の上部における
濾過孔の孔径を下部における濾過孔の孔径より大
きくしたことを特徴とする酸濃度測定用酸洗液サ
ンプリング装置。1 A filter is installed in the pipe line that supplies pickling liquid from a continuous pickling tank for steel strips, etc. to an automatic titration device, and the main body of the filter is divided into an inlet side chamber and an outlet by a substantially upright plate-shaped filter material. A pickling solution sampling for measuring acid concentration, characterized in that the filter material is divided into a side chamber, and a filter hole is provided in the upper part of the filter material, and the diameter of the filter hole in the upper part of the upper part is larger than that of the filter hole in the lower part. Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58158957A JPS6052737A (en) | 1983-09-01 | 1983-09-01 | Pickling liquid sampling device for measurement of acid concentration |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58158957A JPS6052737A (en) | 1983-09-01 | 1983-09-01 | Pickling liquid sampling device for measurement of acid concentration |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6052737A JPS6052737A (en) | 1985-03-26 |
JPH0315970B2 true JPH0315970B2 (en) | 1991-03-04 |
Family
ID=15683035
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58158957A Granted JPS6052737A (en) | 1983-09-01 | 1983-09-01 | Pickling liquid sampling device for measurement of acid concentration |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6052737A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2898286B2 (en) * | 1988-03-15 | 1999-05-31 | 大同特殊鋼株式会社 | Stainless steel pickling equipment |
KR100896646B1 (en) * | 2002-08-21 | 2009-05-08 | 주식회사 포스코 | An apparatus for automatically sampling acid in a pickling tank by using strip lifter |
KR100854373B1 (en) | 2006-12-29 | 2008-09-02 | 주식회사 포스코 | Acid cleaning solution sampling apparatus of the acid solution tank |
JP5729211B2 (en) * | 2010-08-31 | 2015-06-03 | Jfeスチール株式会社 | Cold rolled steel sheet manufacturing method, cold rolled steel sheet and automobile member |
JP5919920B2 (en) * | 2011-03-28 | 2016-05-18 | Jfeスチール株式会社 | Method and apparatus for producing Si-containing cold-rolled steel sheet |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4836298U (en) * | 1971-09-06 | 1973-05-01 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51155557U (en) * | 1975-06-05 | 1976-12-11 |
-
1983
- 1983-09-01 JP JP58158957A patent/JPS6052737A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4836298U (en) * | 1971-09-06 | 1973-05-01 |
Also Published As
Publication number | Publication date |
---|---|
JPS6052737A (en) | 1985-03-26 |
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