JP2018523128A - Peracid washing inhibitor analyzer and peracid washing analysis method using the same - Google Patents

Peracid washing inhibitor analyzer and peracid washing analysis method using the same Download PDF

Info

Publication number
JP2018523128A
JP2018523128A JP2018506405A JP2018506405A JP2018523128A JP 2018523128 A JP2018523128 A JP 2018523128A JP 2018506405 A JP2018506405 A JP 2018506405A JP 2018506405 A JP2018506405 A JP 2018506405A JP 2018523128 A JP2018523128 A JP 2018523128A
Authority
JP
Japan
Prior art keywords
inhibitor
peracid
solution
agent
ammonia
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.)
Granted
Application number
JP2018506405A
Other languages
Japanese (ja)
Other versions
JP6480084B2 (en
Inventor
シム、ジュ、ヒョン
Original Assignee
ヒュンダイ スチール カンパニー
ヒュンダイ スチール カンパニー
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 ヒュンダイ スチール カンパニー, ヒュンダイ スチール カンパニー filed Critical ヒュンダイ スチール カンパニー
Publication of JP2018523128A publication Critical patent/JP2018523128A/en
Application granted granted Critical
Publication of JP6480084B2 publication Critical patent/JP6480084B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • C23G1/04Cleaning or pickling metallic material with solutions or molten salts with acid solutions using inhibitors
    • C23G1/06Cleaning or pickling metallic material with solutions or molten salts with acid solutions using inhibitors organic inhibitors
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N35/00Automatic analysis not limited to methods or materials provided for in any single one of groups G01N1/00 - G01N33/00; Handling materials therefor
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • C23G1/08Iron or steel
    • C23G1/081Iron or steel solutions containing H2SO4
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • C23G3/02Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • C23G3/02Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
    • C23G3/027Associated apparatus, e.g. for pretreating or after-treating
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N31/00Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods
    • G01N31/16Investigating or analysing non-biological materials by the use of the chemical methods specified in the subgroup; Apparatus specially adapted for such methods using titration

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Metallurgy (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Pathology (AREA)
  • Immunology (AREA)
  • General Physics & Mathematics (AREA)
  • General Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Physics & Mathematics (AREA)
  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
  • Molecular Biology (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

【課題】過酸洗防止剤分析装置およびこれを用いた過酸洗防止剤分析方法に関する発明が開示される。【解決手段】一具体例において、前記過酸洗防止剤分析装置は、第1流入部と、第2流入部と、第3流入部と、第4流入部とが備えられる第1反応部と、第5流入部と、第6流入部と、第7流入部と、pH測定部と、レベル測定部とが備えられる第2反応部と、前記pH測定部およびレベル測定部と電気的に連結される制御演算部とを含む。An invention relating to an apparatus for analyzing an acid pickling inhibitor and a method for analyzing an acid pickling inhibitor using the same is disclosed. In one specific example, the peracid wash inhibitor analyzer includes a first reaction part including a first inflow part, a second inflow part, a third inflow part, and a fourth inflow part. , A fifth inflow part, a sixth inflow part, a seventh inflow part, a second reaction part comprising a pH measurement part and a level measurement part, and electrically connected to the pH measurement part and the level measurement part A control operation unit.

Description

本発明は、過酸洗防止剤分析装置およびこれを用いた過酸洗防止剤分析方法に関する。より詳細には、冷延鋼板の製造時、酸洗圧延工程で使用される過酸洗防止剤に含まれるアミン系化合物の濃度分析装置およびこれを用いた過酸洗防止剤分析方法に関する。   The present invention relates to an apparatus for analyzing an acid pickling inhibitor and a method for analyzing an acid pickling inhibitor using the apparatus. More specifically, the present invention relates to a concentration analysis apparatus for an amine compound contained in a peracid washing inhibitor used in a pickling rolling process at the time of manufacturing a cold-rolled steel sheet, and a peracid washing analysis method using the same.

冷延工程は、常温付近の温度で熱間圧延された鋼材の圧延を行う工程で、表面が美麗で加工性に優れた製品を生産する段階である。冷延工程は、熱延コイルを酸洗圧延設備を経た後、亜鉛めっきまたは冷延めっきなどの設備を経て最終製品を生産する。   The cold rolling process is a process of rolling a steel material that has been hot-rolled at a temperature near room temperature, and is a stage for producing a product with a beautiful surface and excellent workability. In the cold rolling process, the hot rolled coil is subjected to pickling and rolling equipment, and then the final product is produced through equipment such as galvanization or cold rolling.

前記酸洗圧延設備では、前記熱延鋼板の表面に付着した酸化物を酸洗除去した後、常温の条件で所望の厚さに連続圧延して半製品を生産するが、この過程で酸洗のために塩酸が使用される。   In the pickling rolling equipment, the oxide adhering to the surface of the hot-rolled steel sheet is pickled and removed, and then continuously rolled to a desired thickness at room temperature to produce a semi-finished product. Hydrochloric acid is used for the purpose.

本発明に関連する背景技術としては、大韓民国公開特許公報第2004−0017751号(2004年2月27日公開、発明の名称:熱延鋼板の酸洗方法)に開示されている   Background art related to the present invention is disclosed in Korean Patent Publication No. 2004-0017751 (published on February 27, 2004, title of invention: pickling method for hot-rolled steel sheet).

本発明の一実施例によれば、信頼度、正確度および精密度に優れた過酸洗防止剤分析装置を提供する。   According to an embodiment of the present invention, an anti-pickling agent analyzer excellent in reliability, accuracy and precision is provided.

本発明の一実施例によれば、冷延鋼板の過酸洗を防止して、表面不良防止効果に優れた過酸洗防止剤分析装置を提供する。   According to one embodiment of the present invention, there is provided an apparatus for analyzing an anti-pickling agent which prevents cold pickling of a cold-rolled steel sheet and has an excellent surface defect prevention effect.

本発明の一実施例によれば、酸洗工程時の作業効率性を向上させることができる過酸洗防止剤分析装置を提供する。   According to one embodiment of the present invention, there is provided a peracid wash inhibitor analyzer capable of improving the work efficiency during the pickling process.

本発明の一実施例によれば、前記過酸洗防止剤分析装置を用いた過酸洗防止剤分析方法を提供する。   According to an embodiment of the present invention, there is provided a method for analyzing a peracid washing inhibitor using the peracid washing agent analyzer.

本発明の一つの観点は、過酸洗防止剤分析装置に関する。一具体例において、前記過酸洗防止剤分析装置は、アミン系化合物を含む過酸洗防止剤が流入する第1流入部と、分解剤が流入する第2流入部と、SHST(sodium hydroxide−sodium thiosulfate)溶液が流入する第3流入部と、水が流入する第4流入部とが備えられ、前記過酸洗防止剤に分解剤を添加し加熱して前記過酸洗防止剤を分解し、前記分解された過酸洗防止剤に前記SHST溶液および水を流入し蒸留してアンモニア(NH)を発生する第1反応部と、前記第1反応部で蒸留されたアンモニアが流入する第5流入部と、ホウ酸が流入する第6流入部と、硫酸が流入する第7流入部と、内部のpHを測定するpH測定部と、内部のレベルを測定するレベル測定部とが備えられ、前記流入したアンモニアをホウ酸で捕集して捕集溶液を生成し、前記硫酸を流入して前記捕集溶液を滴定する第2反応部と、前記pH測定部およびレベル測定部と電気的に連結され、前記測定された第2反応部内部のpHおよびレベルデータが送信されて、過酸洗防止剤の濃度を分析する制御演算部とを含む。 One aspect of the present invention relates to a peracid wash inhibitor analyzer. In one specific example, the peracid wash inhibitor analyzer includes a first inflow portion into which a peracid wash inhibitor containing an amine compound flows, a second inflow portion into which a decomposition agent flows, and SHST (sodium hydroxide- a third inflow portion into which a solution of sodium thiosulfate) and a fourth inflow portion into which water flows are provided, and a decomposition agent is added to the peracid wash inhibitor and heated to decompose the peracid wash inhibitor. A first reaction part for flowing the SHST solution and water into the decomposed peracid washing inhibitor to generate ammonia (NH 3 ) by distillation; and an ammonia distilled in the first reaction part 5 inflow parts, a sixth inflow part into which boric acid flows in, a seventh inflow part into which sulfuric acid flows in, a pH measurement part for measuring the internal pH, and a level measurement part for measuring the internal level are provided. Said inflow Ammonia is collected with boric acid to produce a collection solution, and the second reaction unit that flows in the sulfuric acid and titrates the collection solution is electrically connected to the pH measurement unit and the level measurement unit, And a control calculation unit for transmitting the measured pH and level data inside the second reaction unit and analyzing the concentration of the peracid washing inhibitor.

本発明の他の観点は、前記過酸洗防止剤分析装置を用いた過酸洗防止剤分析方法に関する。一具体例において、前記過酸洗防止剤分析方法は、アミン系化合物を含む過酸洗防止剤に分解剤を添加し加熱して分解するステップと、前記分解された過酸洗防止剤にSHST(sodium hydroxide−sodium thiosulfate)溶液および水を添加し蒸留して発生するアンモニア(NH)を収集するステップと、前記収集されたアンモニア(NH)をホウ酸で捕集して、捕集溶液を生成するステップと、前記捕集溶液を硫酸で滴定して、前記アンモニア(NH)に含まれた窒素濃度を導出するステップとを含み、前記分解剤は、硫酸カリウム(KSO)、硫酸銅(CuSO)、硫酸(HSO)および水を混合して製造される。 Another aspect of the present invention relates to a peracid washing inhibitor analysis method using the peracid washing inhibitor analyzer. In one specific example, the method for analyzing a peracid wash inhibitor includes a step of adding a decomposition agent to a peracid wash inhibitor containing an amine compound and decomposing it by heating, and adding SHST to the decomposed peracid wash inhibitor. (Sodium hydride-sodium thiosulfate) solution and adding water and collecting the ammonia (NH 3 ) generated by distillation, collecting the collected ammonia (NH 3 ) with boric acid, collecting the collected solution And deriving the concentration of nitrogen contained in the ammonia (NH 3 ) by titrating the collected solution with sulfuric acid, wherein the decomposition agent is potassium sulfate (K 2 SO 4 ). , Copper sulfate (CuSO 4 ), sulfuric acid (H 2 SO 4 ) and water.

一具体例において、前記加熱は、350℃〜400℃で行われてもよい。   In one specific example, the heating may be performed at 350 ° C to 400 ° C.

一具体例において、前記蒸留は、60℃〜100℃で行われてもよい。   In one embodiment, the distillation may be performed at 60 ° C to 100 ° C.

一具体例において、前記滴定は、前記ホウ酸のpHを測定し、そして、前記捕集溶液に硫酸を投入して、前記捕集溶液のpHを前記測定されたホウ酸のpHまで調節するステップを含んで行われてもよい。   In one embodiment, the titration includes measuring the pH of the boric acid and adding sulfuric acid to the collection solution to adjust the pH of the collection solution to the measured boric acid pH. It may be performed including.

本発明の過酸洗防止剤分析方法を適用する時、過酸洗防止剤に含まれたアミン系化合物の濃度測定の信頼度、正確度および精密度に優れ、冷延鋼板の過酸洗を防止して、表面不良防止効果に優れ、酸洗工程時の作業効率性を向上させることができる。   When applying the method for analyzing a peracid washing inhibitor of the present invention, it is excellent in the reliability, accuracy and precision of the concentration measurement of the amine compound contained in the peracid washing agent, and is suitable for peracid washing of cold-rolled steel sheets. Therefore, it is excellent in the effect of preventing surface defects and can improve the work efficiency during the pickling process.

本発明の一具体例による過酸洗防止剤分析装置を示すものである。1 shows an apparatus for analyzing an anti-pickling agent according to an embodiment of the present invention. 本発明の一具体例による過酸洗防止剤分析方法を示すものである。1 shows a method for analyzing an anti-pickling agent according to an embodiment of the present invention. 調製された過酸洗防止剤および測定された過酸洗防止剤に含まれたアミン系化合物の濃度を比較したグラフである。It is the graph which compared the density | concentration of the amine compound contained in the prepared peracid wash inhibitor and the measured peracid wash inhibitor.

本発明を説明するにあたり、かかる公知の技術または構成に関する具体的な説明が本発明の要旨を不必要にあいまいにし得ると判断された場合には、その詳細な説明は省略する。   In describing the present invention, if it is determined that a specific description of the known technique or configuration can unnecessarily obscure the gist of the present invention, the detailed description thereof will be omitted.

そして、後述する用語は、本発明における機能を考慮して定義された用語であって、これは使用者、運用者の意図または慣例などによって異なり得るので、その定義は本発明を説明する本明細書全般にわたる内容に基づいて行われなければならない。   The terms to be described later are defined in consideration of the functions in the present invention, and may be different depending on the intention of the user, the operator, the customs, etc. Must be based on the content of the entire book.

過酸洗防止剤分析装置
本発明の一つの観点は、過酸洗防止剤分析放置に関する。図1は、本発明の一具体例による過酸洗防止剤分析装置1000を示すものである。前記図1を参照すれば、本発明の過酸洗防止剤分析装置1000は、試料貯蔵部201に貯蔵されたアミン系化合物を含む過酸洗防止剤が流入する第1流入部1と、分解剤貯蔵部202に貯蔵された分解剤が流入する第2流入部2と、SHST貯蔵部203に貯蔵されたSHST(sodium hydroxide−sodium thiosulfate)溶液が流入する第3流入部3と、水貯蔵部204に貯蔵された水が流入する第4流入部4とが備えられ、第1流入部1から流入した過酸洗防止剤に第2流入部2から分解剤を流入して添加し加熱して前記過酸洗防止剤を分解し、前記分解された過酸洗防止剤に第3流入部3からSHST溶液および第4流入部4から水を流入し蒸留してアンモニア(NH)を発生する第1反応部101と、第1反応部101で蒸留されたアンモニアが流入する第5流入部5と、ホウ酸貯蔵部205に貯蔵されたホウ酸が流入する第6流入部6と、硫酸貯蔵部206に貯蔵された硫酸が流入する第7流入部7と、内部のpHを測定するpH測定部301と、内部のレベルを測定するレベル測定部302とが備えられ、第5流入部5を通して流入したアンモニアを第6流入部6を通して流入したホウ酸で捕集して捕集溶液を生成し、第7流入部7を通して硫酸を流入して前記捕集溶液を滴定する第2反応部102と、前記pH測定部301およびレベル測定部302と電気的に連結され、前記測定された第2反応部102内部のpHおよびレベルデータが送信されて、過酸洗防止剤の濃度を分析する制御演算部103とを含む。
Peracid Washing Analyzing Device One aspect of the present invention relates to peroxidation preventing agent analysis standing. FIG. 1 shows an anti-pickling agent analyzer 1000 according to an embodiment of the present invention. Referring to FIG. 1, the peracid washing agent analyzer 1000 according to the present invention includes a first inflow part 1 into which a peracid washing inhibitor containing an amine compound stored in the sample storage part 201 flows, and a decomposition. A second inflow part 2 into which the decomposition agent stored in the agent storage part 202 flows in; a third inflow part 3 into which an SHST (sodium hydride-sodium thiosulfate) solution stored in the SHST storage part 203 flows in; and a water storage part And a fourth inflow part 4 into which the water stored in 204 flows in, and a decomposition agent is introduced from the second inflow part 2 to the peracid wash preventing agent that has flowed in from the first inflow part 1 and heated. The peracid washing inhibitor is decomposed, and the SHST solution and water from the fourth inflow part 4 are allowed to flow into the decomposed peracid washing inhibitor and water is distilled from the fourth inflow part 4 to generate ammonia (NH 3 ). First reaction unit 10 1, a fifth inflow part 5 into which ammonia distilled in the first reaction part 101 flows in, a sixth inflow part 6 into which boric acid stored in the boric acid storage part 205 flows, and a sulfuric acid storage part 206. A seventh inflow section 7 into which the sulfuric acid flows in, a pH measurement section 301 for measuring the internal pH, and a level measurement section 302 for measuring the internal level are provided, and the ammonia that has flowed in through the fifth inflow section 5 is provided. A second reaction unit 102 that collects boric acid flowing in through the sixth inflow part 6 to produce a collection solution, and injects sulfuric acid through the seventh inflow part 7 to titrate the collected solution; and the pH measurement A control calculation unit 103 that is electrically connected to the unit 301 and the level measurement unit 302 and transmits the measured pH and level data in the second reaction unit 102 to analyze the concentration of the peracid washing inhibitor. Including.

本発明において、第1反応部101には加熱器(図示せず)が備えられ、前記過酸洗防止剤に分解剤を添加して加熱し、前記SHST溶液および水を投入して蒸留が行われる。また、図示しないが、第1反応部101の一側には廃ガス処理部が備えられ、未反応の廃ガスが排出される。   In the present invention, the first reaction unit 101 is provided with a heater (not shown), and a heating agent (not shown) is added to the decomposition agent and heated, and the SHST solution and water are added to perform distillation. Is called. Moreover, although not shown in figure, the waste gas processing part is provided in the 1st reaction part 101 side, and an unreacted waste gas is discharged | emitted.

前記図1を参照すれば、本発明の一具体例において、第1反応部101および第2反応部102の一側には、それぞれ第1排出部21および第2排出部22が備えられ、第1反応部101および第2反応部102に残っている成分を排出することができる。例えば、サイフォン(siphon)の原理を利用して排出することができる。   Referring to FIG. 1, in one embodiment of the present invention, a first discharge unit 21 and a second discharge unit 22 are provided on one side of the first reaction unit 101 and the second reaction unit 102, respectively. Components remaining in the first reaction unit 101 and the second reaction unit 102 can be discharged. For example, it can be discharged using the principle of siphon.

前記図1を参照すれば、水貯蔵部204に貯蔵された水は、第8流入部8を通して試料貯蔵部201に流入して前記過酸洗防止剤を希釈することができる。前記過酸洗防止剤に含まれるアミン系化合物(HMTA)の濃度が異なり得るので、水の量を試料注入サンプルによって5倍、10倍、20倍、50倍および100倍など希釈可能に注入することができて、最適濃度を換算することができる。   Referring to FIG. 1, the water stored in the water storage unit 204 may flow into the sample storage unit 201 through the eighth inflow unit 8 to dilute the peracid wash inhibitor. Since the concentration of the amine compound (HMTA) contained in the peracid washing inhibitor may be different, the amount of water is injected in a dilutable manner such as 5 times, 10 times, 20 times, 50 times and 100 times depending on the sample injection sample And the optimum concentration can be converted.

また、水貯蔵部204に貯蔵された水は、第9流入部9を通して第2反応部102に流入して、前記捕集溶液の濃度を調節したり、第2反応部102の内部を洗浄することができる。   Further, the water stored in the water storage unit 204 flows into the second reaction unit 102 through the ninth inflow unit 9 to adjust the concentration of the collected solution or to wash the inside of the second reaction unit 102. be able to.

一具体例において、pH測定部301は、ホウ酸貯蔵部205から第6流入部6を通して第2反応部102に流入したホウ酸のpHを測定し、前記ホウ酸に第5流入部5を通して流入したアンモニアが捕集されて生成された捕集溶液に、前記第7流入部7を通して硫酸を投入して、前記捕集溶液のpHを測定することができる。   In one specific example, the pH measurement unit 301 measures the pH of boric acid flowing from the boric acid storage unit 205 through the sixth inflow unit 6 into the second reaction unit 102 and flows into the boric acid through the fifth inflow unit 5. Sulfuric acid can be introduced into the collection solution generated by collecting the collected ammonia through the seventh inflow portion 7 to measure the pH of the collection solution.

レベル測定部302は、ホウ酸貯蔵部205から第6流入部6を通して第2反応部102に流入したホウ酸のレベルを測定し、前記ホウ酸に前記アンモニアが捕集されて生成された捕集溶液のレベルと、前記硫酸を投入して滴定される前記捕集溶液のレベルを測定することができる。   The level measuring unit 302 measures the level of boric acid that has flowed into the second reaction unit 102 from the boric acid storage unit 205 through the sixth inflow unit 6, and collected by collecting the ammonia in the boric acid. It is possible to measure the level of the solution and the level of the collection solution that is titrated by adding the sulfuric acid.

制御演算部103は、pH測定部301のpHデータ、およびレベル測定部302で測定されたレベルデータを用いて、過酸洗防止剤に含まれた窒素の濃度を導出することができる。 The control calculation unit 103 can derive the concentration of nitrogen contained in the peracid washing preventing agent using the pH data of the pH measurement unit 301 and the level data measured by the level measurement unit 302.

一具体例において、第1流入部〜第9流入部は、それぞれポンプが備えられてもよいし、前記ポンプは、制御演算部103と電気的に連結されて制御可能である。   In one specific example, each of the first to ninth inflow portions may be provided with a pump, and the pump is electrically connected to the control calculation unit 103 and can be controlled.

過酸洗防止剤分析方法
本発明の他の観点は、前記過酸洗防止剤分析装置を用いた過酸洗防止剤分析方法に関する。図2は、本発明の一具体例による過酸洗防止剤分析方法を示すものである。前記図2を参照すれば、前記過酸洗防止剤分析方法は、(s101)過酸洗防止剤分解ステップと、(s102)アンモニア収集ステップと、(s103)捕集溶液製造ステップと、(s104)滴定ステップとを含む。
Method for Analyzing Peracid Washing Agent Another aspect of the present invention relates to a method for analyzing an acid pickling inhibitor using the peracid washing agent analyzer. FIG. 2 shows a method for analyzing a peracid washing inhibitor according to an embodiment of the present invention. Referring to FIG. 2, the method for analyzing a peracid wash inhibitor includes (s101) a peracid wash decomposition step, (s102) an ammonia collection step, (s103) a collected solution manufacturing step, and (s104). ) A titration step.

より具体的には、前記過酸洗防止剤分析方法は、(s101)アミン系化合物を含む過酸洗防止剤に分解剤を添加し加熱して分解するステップと、(s102)前記分解された過酸洗防止剤にSHST(sodium hydroxide−sodium thiosulfate)溶液および水を添加し蒸留して発生するアンモニア(NH)を収集するステップと、(s103)前記収集されたアンモニア(NH)をホウ酸で捕集して、捕集溶液を生成するステップと、(s104)前記捕集溶液を硫酸で滴定して、前記アンモニア(NH)に含まれた窒素濃度を導出するステップとを含む。 More specifically, the method for analyzing an anti-pickling agent comprises: (s101) a step of adding a decomposing agent to an anti-pickling agent containing an amine compound and heating to decompose; and (s102) the decomposition. A step of adding SHST (sodium hydride-sodium thiosulfate) solution and water to the peracid pickling inhibitor and collecting ammonia (NH 3 ) generated by distillation; (s103) boring the collected ammonia (NH 3 ) Collecting with an acid to produce a collected solution; and (s104) titrating the collected solution with sulfuric acid to derive a concentration of nitrogen contained in the ammonia (NH 3 ).

以下、本発明に係る過酸洗防止剤分析方法をステップ別に詳細に説明する。   Hereinafter, the method for analyzing an acid pickling agent according to the present invention will be described in detail step by step.

(s101)過酸洗防止剤加熱ステップ
前記ステップは、アミン系化合物を含む過酸洗防止剤に分解剤を添加し加熱して分解するステップである。前記ステップで前記過酸洗防止剤と分解剤とが反応して、分解、酸化および還元反応が発生する。
酸洗工程で使用される酸濃度によって発生する未酸洗および過酸洗の直接的原因となる酸タンクの酸濃度の制御が要求されており、過酸洗を防止するために過酸洗防止剤が使用される。
(S101) Peracid wash preventing agent heating step The above step is a step of adding a decomposing agent to the peracid wash preventing agent containing the amine compound and heating to decompose. In the step, the peracid washing inhibitor and the decomposition agent react to generate decomposition, oxidation, and reduction reactions.
It is required to control the acid concentration of the acid tank, which is the direct cause of unpickling and over-pickling that occurs depending on the concentration of acid used in the pickling process, and over-pickling prevention is required to prevent over-pickling. Agent is used.

本発明の一具体例において、前記過酸洗防止剤に含まれるアミン系化合物は、通常のものを使用することができる。例えば、ヘキサメチレンテトラアミン(hexamethylenetetraamine、HMTA)であってもよい。   In one specific example of the present invention, a normal compound can be used as the amine compound contained in the peracid washing inhibitor. For example, hexamethylenetetraamine (HMTA) may be used.

一具体例において、前記分解剤(digestion)は、硫酸カリウム(KSO)、硫酸銅(CuSO)、硫酸(HSO)および水を混合して製造できる。一具体例において、前記分解剤は、134gの硫酸カリウム(KSO)および7.3gの硫酸銅(CuSO)を800mLの水に溶解した後、90%硫酸134mLを加えて、再び1Lに希釈して製造することができる。 In one embodiment, the digestion may be prepared by mixing potassium sulfate (K 2 SO 4 ), copper sulfate (CuSO 4 ), sulfuric acid (H 2 SO 4 ), and water. In one embodiment, the decomposition agent is prepared by dissolving 134 g of potassium sulfate (K 2 SO 4 ) and 7.3 g of copper sulfate (CuSO 4 ) in 800 mL of water, and then adding 134 mL of 90% sulfuric acid, It can be manufactured by diluting.

この時、前記硫酸カリウムは、硫酸に溶解して沸点を上昇させ、分解を促進する役割を果たす。   At this time, the potassium sulfate serves to promote decomposition by dissolving in sulfuric acid to raise the boiling point.

前記加熱温度は、350℃〜400℃であってもよい。前記範囲で加熱する時、前記過酸洗防止剤に含まれた窒素の熱分解を防止しながら、前記過酸洗防止剤の分解が容易に進行できる。例えば、380℃〜400℃であってもよい。   The heating temperature may be 350 ° C to 400 ° C. When heating in the above range, decomposition of the peracid washing inhibitor can easily proceed while preventing thermal decomposition of nitrogen contained in the peracid washing inhibitor. For example, it may be 380 ° C to 400 ° C.

前記過酸洗防止剤に含まれる窒素成分は、前記分解剤と反応してアンモニア(NH)が生成され、前記アンモニアは、前記分解剤の硫酸(HSO)と反応して硫酸アンモニウム((NHSO)が生成される。 The nitrogen component contained in the peracid washing inhibitor reacts with the decomposition agent to produce ammonia (NH 3 ), and the ammonia reacts with the decomposition agent sulfuric acid (H 2 SO 4 ) to produce ammonium sulfate ( (NH 4 ) 2 SO 4 ) is produced.

(s102)アンモニア収集ステップ
前記ステップは、前記分解された過酸洗防止剤にSHST(sodium hydroxide−sodium thiosulfate)溶液および水を添加し蒸留して発生するアンモニア(NH)気体を収集するステップである。
(S102) Ammonia collection step The step is a step of collecting an ammonia (NH 3 ) gas generated by adding an SHST (sodium hydride-sodium thiosulfate) solution and water to the decomposed peracid washing inhibitor and distilling. is there.

前記SHST(sodium hydroxide−sodium thiosulfate、NaOH)溶液は、水酸化ナトリウム(sodium hydroxide)およびチオ硫酸ナトリウム(sodium thiosulfate、Na・5HO)を含む。 The solution of SHST (sodium hydroxide-sodium thiosulfate, NaOH) contains sodium hydroxide and sodium thiosulfate (Na 2 S 2 O 3 .5H 2 O).

一具体例において、前記SHST溶液は、前記水酸化ナトリウム(NaOH)500gおよび前記チオ硫酸ナトリウム(Na・5HO)25gを水に溶解させ、水を添加して1Lに希釈させて製造することができる。 In one embodiment, the SHST solution is prepared by dissolving 500 g of the sodium hydroxide (NaOH) and 25 g of the sodium thiosulfate (Na 2 S 2 O 3 · 5H 2 O) in water and adding water to dilute to 1 L. Can be manufactured.

前記蒸留は、通常の方法を利用して実施することができる。前記蒸留は、60℃〜100℃で行われてもよい。前記温度で蒸留する時、アンモニア(NH)気体の収集効果に優れることができる。 The distillation can be performed using a normal method. The distillation may be performed at 60 ° C to 100 ° C. When distilling at the above temperature, the ammonia (NH 3 ) gas collecting effect can be excellent.

(s103)捕集溶液製造ステップ
前記ステップは、前記収集されたアンモニア(NH)をホウ酸で捕集して、捕集溶液を生成するステップである。前記ホウ酸を用いる時、前記アンモニアの容易な捕集が可能で、前記過酸洗防止剤に含まれた窒素量の分析が容易であり得る。
(S103) Collection Solution Production Step The step is a step of collecting the collected ammonia (NH 3 ) with boric acid to generate a collection solution. When the boric acid is used, the ammonia can be easily collected, and the amount of nitrogen contained in the peracid washing inhibitor can be easily analyzed.

(s104)滴定ステップ
前記ステップは、前記捕集溶液を硫酸で滴定して、前記アンモニア(NH)に含まれた窒素濃度を導出するステップである。例えば、前記滴定時に消費された硫酸の量から、捕集されたアンモニアに含まれた窒素量を計算することができる。
(S104) Titration step The step is a step of deriving the concentration of nitrogen contained in the ammonia (NH 3 ) by titrating the collected solution with sulfuric acid. For example, the amount of nitrogen contained in the collected ammonia can be calculated from the amount of sulfuric acid consumed during the titration.

一具体例において、前記硫酸は、希硫酸を使用することができる。例えば、0.01N〜0.05N(normality)の硫酸を使用することができる。   In one embodiment, dilute sulfuric acid can be used as the sulfuric acid. For example, 0.01 N to 0.05 N (normality) sulfuric acid can be used.

一具体例において、前記滴定は、前記ホウ酸のpHを測定し、そして、前記捕集溶液に硫酸を投入して、前記捕集溶液のpHを前記測定されたホウ酸のpHまで調節するステップを含んで行われてもよい。   In one embodiment, the titration includes measuring the pH of the boric acid and adding sulfuric acid to the collection solution to adjust the pH of the collection solution to the measured boric acid pH. It may be performed including.

本発明の過酸洗防止剤分析方法を適用する時、アミンに含まれた窒素を測定分析する方法を適用して、定量限界が低く、酸溶液ベースに分析対象試料が存在する場合にも、検出可能であるという利点があり、過酸洗防止剤の濃度測定の信頼度、正確度および精密度に優れ、冷延鋼板の過酸洗を防止して、表面不良防止効果に優れ、酸洗工程時の作業効率性を向上させることができる。   When applying the method for analyzing the peracid wash inhibitor of the present invention, applying a method for measuring and analyzing nitrogen contained in amines, the quantitation limit is low, and even when the sample to be analyzed is based on an acid solution, It has the advantage that it can be detected, has excellent reliability, accuracy, and precision in the concentration measurement of the per-acid pickling agent. Work efficiency during the process can be improved.

以下、本発明の好ましい実施例を通じて本発明の構成および作用をより詳細に説明する。ただし、これは本発明の好ましい例として提示されたものであり、いかなる意味でもこれによって本発明が制限されると解釈されない。   Hereinafter, the configuration and operation of the present invention will be described in more detail through preferred embodiments of the present invention. However, this is presented as a preferred example of the present invention and should not be construed as limiting the invention in any way.

実施例
図1のような過酸洗防止剤分析装置を用いて過酸洗防止剤の窒素濃度を分析した。
EXAMPLE The nitrogen concentration of the peracid washing inhibitor was analyzed using a peracid washing inhibitor analyzer as shown in FIG.

試料貯蔵部201に貯蔵されたヘキサメチレンテトラアミン(hexamethylenetetraamine、HMTA)を含む過酸洗防止剤試料5mlを第1流入部1を通して第1反応部101に流入した。この時、第1反応部101の第1排出部21は閉じており、ガス流出部分は、廃ガス処理部(図示せず)を通して排出した。   5 ml of a peracid washing inhibitor sample containing hexamethylenetetraamine (HMTA) stored in the sample storage unit 201 was introduced into the first reaction unit 101 through the first inflow unit 1. At this time, the first discharge part 21 of the first reaction part 101 was closed, and the gas outflow part was discharged through a waste gas treatment part (not shown).

また、134gの硫酸カリウム(KSO)および7.3gの硫酸銅(CuSO)を800mLの水に溶解した後、90%硫酸134mLを加えて、再び水で1Lに希釈して分解剤を用意し、前記水酸化ナトリウム(NaOH)500gおよび前記チオ硫酸ナトリウム(Na・5HO)25gを水に溶解させ、水を添加して1Lに希釈させてSHST溶液を用意した。 In addition, 134 g of potassium sulfate (K 2 SO 4 ) and 7.3 g of copper sulfate (CuSO 4 ) were dissolved in 800 mL of water, and then 134% of 90% sulfuric acid was added and diluted to 1 L with water again to decompose the solution. Prepare a SHST solution by dissolving 500 g of the sodium hydroxide (NaOH) and 25 g of the sodium thiosulfate (Na 2 S 2 O 3 .5H 2 O) in water and adding water to dilute to 1 L. did.

次に、分解剤貯蔵部202に貯蔵された分解剤を第2流入部2を通して第1反応部101に5mL流入した。以後、加熱器を作動して、第1反応部101の内部を390℃に10分加熱後、5分間冷やした。ホウ酸貯蔵部205に貯蔵されたホウ酸を第2反応部102に5mLを入れて、pH測定部301によりホウ酸のpHを測定した。第1反応部101に、水貯蔵部204に貯蔵された蒸留水を第4流入部4を通して30mLを流入し、SHST溶液貯蔵部203に貯蔵されたSHST溶液を第3流入部3を通して5mL入れた後、100℃に加熱し蒸発して、発生するアンモニア(NH)を第5流入部5を通して収集して第2反応部102の内部に流入し、ホウ酸で捕集して、捕集溶液を生成した。レベル測定部302で測定した第2反応部102内部のレベルが20mLになると、前記加熱器の作動を中止した。 Next, 5 mL of the decomposition agent stored in the decomposition agent storage unit 202 flowed into the first reaction unit 101 through the second inflow unit 2. Thereafter, the heater was operated, and the inside of the first reaction unit 101 was heated to 390 ° C. for 10 minutes and then cooled for 5 minutes. 5 mL of boric acid stored in the boric acid storage unit 205 was added to the second reaction unit 102, and the pH of the boric acid was measured by the pH measurement unit 301. 30 mL of distilled water stored in the water storage unit 204 flows into the first reaction unit 101 through the fourth inflow unit 4, and 5 mL of the SHST solution stored in the SHST solution storage unit 203 enters through the third inflow unit 3. After that, it is heated to 100 ° C. and evaporated, and the generated ammonia (NH 3 ) is collected through the fifth inflow part 5 and flows into the second reaction part 102, and is collected with boric acid. Was generated. When the level inside the second reaction unit 102 measured by the level measurement unit 302 reached 20 mL, the operation of the heater was stopped.

次に、前記捕集溶液に硫酸貯蔵部206に貯蔵された硫酸を第7流入部7を通して流入して、前記捕集溶液のpHを前記測定されたホウ酸のpHまで調節して滴定した。   Next, sulfuric acid stored in the sulfuric acid storage unit 206 was introduced into the collection solution through the seventh inflow unit 7, and the pH of the collection solution was adjusted to the pH of the measured boric acid and titrated.

この時、pH測定部301およびレベル測定部302では、滴定済み捕集溶液のpHおよびレベルを測定して、前記pH測定部301およびレベル測定部302と電気的に連結された制御演算部103に送信した。   At this time, the pH measurement unit 301 and the level measurement unit 302 measure the pH and level of the titrated collection solution, and the control calculation unit 103 electrically connected to the pH measurement unit 301 and the level measurement unit 302 sent.

前記制御演算部103で、pH測定部301で測定された捕集溶液のpHデータ、およびレベル測定部302で測定された滴定済み捕集溶液のレベルデータを用いて、過酸洗防止剤に含まれた総窒素の濃度を導出して、下記表1に示した。   Included in the peracid wash inhibitor using the pH data of the collected solution measured by the pH measuring unit 301 and the level data of the titrated collected solution measured by the level measuring unit 302 in the control calculation unit 103 The total nitrogen concentration was derived and shown in Table 1 below.

前記実施例のように分析した結果を用いて単位換算して、アミン系化合物の濃度に変換して結果値を導出して、下記表1に示した。   Using the results analyzed as in the above Examples, the results were derived by converting the units into amine compound concentrations and are shown in Table 1 below.

図3は、調製された過酸洗防止剤および測定された過酸洗防止剤に含まれたアミン系化合物の濃度を比較したグラフである。前記表1および図3を参照すれば、実際のデータ分析の結果、92%の正確度を示しており、精密度は3%以内で測定され、本発明の過酸洗防止剤分析装置を用いた分析方法を適用する時、過酸洗防止剤に含まれたアミン化合物の濃度の分析時、精密度および正確度に優れていることが分かった。   FIG. 3 is a graph comparing the concentrations of amine compounds contained in the prepared peracid wash inhibitor and the measured peracid wash inhibitor. Referring to Table 1 and FIG. 3, the result of actual data analysis shows an accuracy of 92%, the accuracy is measured within 3%, and the peracid wash inhibitor analyzer of the present invention is used. It was found that when the analysis method used was applied, the precision and accuracy were excellent when analyzing the concentration of the amine compound contained in the peracid washing inhibitor.

本発明の単純な変形乃至変更は、当該分野における通常の知識を有する者によって容易に実施可能であり、このような変形や変更はすべて本発明の領域に含まれると見なすことができる。   Simple variations and modifications of the present invention can be easily implemented by those having ordinary knowledge in the art, and all such modifications and changes can be considered to be included in the scope of the present invention.

Claims (5)

アミン系化合物を含む過酸洗防止剤が流入する第1流入部と、分解剤が流入する第2流入部と、SHST(sodium hydroxide−sodium thiosulfate)溶液が流入する第3流入部と、水が流入する第4流入部とが備えられ、前記過酸洗防止剤に分解剤を添加し加熱して前記過酸洗防止剤を分解し、前記分解された過酸洗防止剤に前記SHST溶液および水を流入し蒸留してアンモニア(NH)を発生する第1反応部と、
前記第1反応部で蒸留されたアンモニアが流入する第5流入部と、ホウ酸が流入する第6流入部と、硫酸が流入する第7流入部と、内部のpHを測定するpH測定部と、内部のレベルを測定するレベル測定部とが備えられ、前記流入したアンモニアをホウ酸で捕集して捕集溶液を生成し、前記硫酸を流入して前記捕集溶液を滴定する第2反応部と、
前記pH測定部およびレベル測定部と電気的に連結され、前記測定された第2反応部内部のpHおよびレベルデータが送信されて、過酸洗防止剤の濃度を分析する制御演算部とを含むことを特徴とする過酸洗防止剤分析装置。
A first inflow portion into which an anti-pickling agent containing an amine compound flows, a second inflow portion into which a decomposition agent flows, a third inflow portion into which an SHST (sodium hydroxide-sodium thiosulfate) solution flows, and water And a fourth inflow part that flows in. A decomposition agent is added to the peracid washing inhibitor and heated to decompose the peracid washing inhibitor, and the decomposed peracid washing agent includes the SHST solution and A first reaction section for flowing water and distilling to generate ammonia (NH 3 );
A fifth inflow portion into which ammonia distilled in the first reaction portion flows, a sixth inflow portion into which boric acid flows, a seventh inflow portion into which sulfuric acid flows, and a pH measurement portion that measures the internal pH; And a level measuring unit for measuring the internal level, collecting the inflowed ammonia with boric acid to form a collected solution, and flowing in the sulfuric acid to titrate the collected solution. And
A control operation unit that is electrically connected to the pH measurement unit and the level measurement unit, and that transmits the measured pH and level data inside the second reaction unit and analyzes the concentration of the peracid wash inhibitor. An anti-pickling agent analyzer characterized by the above.
アミン系化合物を含む過酸洗防止剤に分解剤を添加し加熱して分解するステップと、
前記分解された過酸洗防止剤にSHST(sodium hydroxide−sodium thiosulfate)溶液および水を添加し蒸留して発生するアンモニア(NH)を収集するステップと、
前記収集されたアンモニア(NH)をホウ酸で捕集して、捕集溶液を生成するステップと、
前記捕集溶液を硫酸で滴定して、前記アンモニア(NH)に含まれた窒素濃度を導出するステップとを含み、
前記分解剤は、硫酸カリウム(KSO)、硫酸銅(CuSO)、硫酸(HSO)および水を混合して製造されることを特徴とする過酸洗防止剤分析方法。
Adding a decomposing agent to the peracid wash inhibitor containing an amine compound and heating to decompose,
Adding ammonia (NH 3 ) generated by adding SHST (sodium hydroxide-sodium thiosulfate) solution and water to the decomposed peracid wash inhibitor and distilling;
Collecting the collected ammonia (NH 3 ) with boric acid to produce a collected solution;
Titrating the collected solution with sulfuric acid to derive a concentration of nitrogen contained in the ammonia (NH 3 ),
The method according to claim 1, wherein the decomposition agent is produced by mixing potassium sulfate (K 2 SO 4 ), copper sulfate (CuSO 4 ), sulfuric acid (H 2 SO 4 ) and water.
前記加熱は、350℃〜400℃で行われることを特徴とする請求項2に記載の過酸洗防止剤分析方法。   The method for analyzing an anti-pickling agent according to claim 2, wherein the heating is performed at 350C to 400C. 前記蒸留は、65℃〜100℃で行われることを特徴とする請求項2に記載の過酸洗防止剤分析方法。   The method for analyzing an anti-pickling agent according to claim 2, wherein the distillation is performed at 65 to 100 ° C. 前記滴定は、前記ホウ酸のpHを測定し、そして、
前記捕集溶液に硫酸を投入して、前記捕集溶液のpHを前記測定されたホウ酸のpHまで調節するステップを含んで行われることを特徴とする請求項2に記載の過酸洗防止剤分析方法。
The titration measures the pH of the boric acid, and
The method according to claim 2, further comprising the step of adding sulfuric acid to the collection solution to adjust the pH of the collection solution to the pH of the measured boric acid. Agent analysis method.
JP2018506405A 2015-08-19 2016-06-22 Peracid washing inhibitor analyzer and peracid washing analysis method using the same Active JP6480084B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
KR1020150116784A KR101777916B1 (en) 2015-08-19 2015-08-19 Analyzing apparatus for pickling inhibitor and analyzing method for pickling inhibitor using the same
KR10-2015-0116784 2015-08-19
PCT/KR2016/006622 WO2017030282A1 (en) 2015-08-19 2016-06-22 Over-descaling preventive agent analyzing apparatus and over-descaling preventive agent analyzing method using same

Publications (2)

Publication Number Publication Date
JP2018523128A true JP2018523128A (en) 2018-08-16
JP6480084B2 JP6480084B2 (en) 2019-03-06

Family

ID=58052087

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2018506405A Active JP6480084B2 (en) 2015-08-19 2016-06-22 Peracid washing inhibitor analyzer and peracid washing analysis method using the same

Country Status (5)

Country Link
JP (1) JP6480084B2 (en)
KR (1) KR101777916B1 (en)
CN (1) CN107923894A (en)
DE (1) DE112016003741T5 (en)
WO (1) WO2017030282A1 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63286763A (en) * 1987-05-19 1988-11-24 Chemo Sero Therapeut Res Inst Kjeldahl nitrogen determination device
US6329206B1 (en) * 1999-06-22 2001-12-11 Henkel Corporation Method of determining inhibitor concentrations in inhibited acidic pickling solutions
JP2003003280A (en) * 2001-06-25 2003-01-08 Nippon Steel Corp Plated steel having excellent rust preventability in edge side
JP2014234469A (en) * 2013-06-04 2014-12-15 株式会社ブリヂストン Rubber composition and tire prepared using the same

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR950005527Y1 (en) * 1993-03-29 1995-07-13 포항종합제철 주식회사 Additive device of an inhibitor
JP2003090836A (en) 2001-09-19 2003-03-28 Horiba Ltd Method and device for measuring nitrogenous compound
KR100899687B1 (en) 2002-08-23 2009-05-28 주식회사 포스코 Descaling method of hot coil
KR100805727B1 (en) * 2006-08-22 2008-02-21 주식회사 포스코 Agent for inhibiting stain and rust of pickling steel strip
CN100573111C (en) * 2007-04-27 2009-12-23 李立华 A kind of computer full-automatic Kjeldahl determination device
KR101125199B1 (en) * 2009-11-17 2012-03-20 강태영 A Total Nitrogen and Total Phosphorous Measuring Apparatus with A Multi Cracking Bath
CN201611342U (en) * 2010-02-03 2010-10-20 济南精密科学仪器仪表有限公司 Automatic sample introduction Kjeldahl nitrogen determination apparatus
KR101057970B1 (en) * 2011-04-18 2011-08-19 길주형 The analyzer of inorganic compounds nitrogen into the water
CN103018236B (en) * 2012-11-30 2014-10-29 济南海能仪器股份有限公司 Nitrogen content titration device by using titration apparatus
CN203405437U (en) * 2013-08-31 2014-01-22 李中 Azotometer for measuring content of Kjeldahl nitrogen through concentration method
CN203720189U (en) * 2014-02-28 2014-07-16 张笑言 Full-automatic Kjeldahl apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63286763A (en) * 1987-05-19 1988-11-24 Chemo Sero Therapeut Res Inst Kjeldahl nitrogen determination device
US6329206B1 (en) * 1999-06-22 2001-12-11 Henkel Corporation Method of determining inhibitor concentrations in inhibited acidic pickling solutions
JP2003003280A (en) * 2001-06-25 2003-01-08 Nippon Steel Corp Plated steel having excellent rust preventability in edge side
JP2014234469A (en) * 2013-06-04 2014-12-15 株式会社ブリヂストン Rubber composition and tire prepared using the same

Also Published As

Publication number Publication date
DE112016003741T5 (en) 2018-04-26
JP6480084B2 (en) 2019-03-06
KR101777916B1 (en) 2017-09-26
WO2017030282A1 (en) 2017-02-23
CN107923894A (en) 2018-04-17
KR20170022153A (en) 2017-03-02

Similar Documents

Publication Publication Date Title
JP2013509566A (en) Analysis and detection method of calcium element in ore
US6537822B1 (en) Method for analyzing free fluorine in solutions containing hydrofluoric acid solution, and apparatus for practicing the method
CN104833674A (en) Measuring method for cyanides in cyanide-containing wastewater of gold mine
CN102288727A (en) Method for measuring vanadium in vanadium-nitrogen alloy
CN103091450A (en) Method for rapidly determining content of total iron in nitrided ferrovanadium
JP6480084B2 (en) Peracid washing inhibitor analyzer and peracid washing analysis method using the same
CN103604799A (en) Method for determining elements such as chromium, iron, manganese, nickel and copper in glycerol aqueous solution
JP2008275537A (en) Method of analyzing nitric acid in mixed acid liquid
CN103487550A (en) Method for determining content of nitric acid in titanium plate pickling solution
CN108918761A (en) The analyzing detecting method of element in the detection method and VN alloy of content of nitrogen in vanadium-nitrogen alloy
CN105203488A (en) Method for testing permanganate index though gas phase molecular absorption spectroscopy
CN106093294A (en) A kind of analysis method of Caddy (Cleary) in acid non-cyanide plating cadmium solution
JP4248606B2 (en) Nitrogen determination method
JPH11142387A (en) Method for separating determining quadrivalent selenium from hexavalent selenium in solution
JP2013205104A (en) Method for analyzing chlorine
US20060121622A1 (en) Method for determination of organic hydroperoxides
CN102628848A (en) Method for measuring content of iron in silicon steel surface oxidation layer
CN105510394A (en) Method for detecting content of total organic matters in water in microgravity environment
Lambert et al. Flowsheet Testing for Strip Effluent to Slurry Mix Evaporator Modifications at the Defense Waste Processing Facility
Roy et al. On the development of thermo-kinetic Eh-pH diagrams
JP2009222427A (en) Alloy composition analysis method and composition analyzer
WO2013107293A1 (en) Method for treating leather by using leather production wastewater and method for producing leather
JP2019034279A (en) Treatment method of cyanide waste liquid
JP2010078456A (en) Method for quantifying free hydrochloric acid in ferric chloride solution
Nelson Hydrogen-bonded complexes of iso-cyanic acid: Infrared spectra and thermodynamic measurements

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20180207

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20181214

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20190111

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20190206

R150 Certificate of patent or registration of utility model

Ref document number: 6480084

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250