[go: up one dir, main page]

KR940000282B1 - Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White - Google Patents

Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White Download PDF

Info

Publication number
KR940000282B1
KR940000282B1 KR1019910025128A KR910025128A KR940000282B1 KR 940000282 B1 KR940000282 B1 KR 940000282B1 KR 1019910025128 A KR1019910025128 A KR 1019910025128A KR 910025128 A KR910025128 A KR 910025128A KR 940000282 B1 KR940000282 B1 KR 940000282B1
Authority
KR
South Korea
Prior art keywords
plating
steel sheet
zinc
white
manufacturing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
KR1019910025128A
Other languages
Korean (ko)
Other versions
KR930013213A (en
Inventor
김현태
박정렬
신정철
Original Assignee
포항종합제철 주식회사
정명식
재단법인 산업과학기술연구소
백덕현
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 포항종합제철 주식회사, 정명식, 재단법인 산업과학기술연구소, 백덕현 filed Critical 포항종합제철 주식회사
Priority to KR1019910025128A priority Critical patent/KR940000282B1/en
Publication of KR930013213A publication Critical patent/KR930013213A/en
Application granted granted Critical
Publication of KR940000282B1 publication Critical patent/KR940000282B1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/22Electroplating: Baths therefor from solutions of zinc

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating And Plating Baths Therefor (AREA)
  • Electroplating Methods And Accessories (AREA)

Abstract

내용 없음.No content.

Description

광택과 백색이 우수한 아연전기도금강판의 제조방법Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White

제1도는 도금욕에 첨가제의 첨가없이 도금한 시편과 첨가제를 첨가하고 도금한 시편의 도금층 미세 조직을 나타내는 사진FIG. 1 is a photograph showing the plated layer microstructure of the plated specimen and the plated specimen with the additive added without addition of the additive to the plating bath.

본 발명은 아연 전기 도금강판의 제조방법에 관한 것으로서, 보다 상세하게는, 염화물 욕에서 순수 아연 도금의 표면 외관의 백색도 및 광택도가 우수하고 도금층의 도금조직이 미세한 아연 전기 도금강판의 제조방법에 관한 것이다.The present invention relates to a method of manufacturing a zinc electroplated steel sheet, and more particularly, to a method of manufacturing a zinc electroplated steel sheet having excellent whiteness and glossiness of the surface appearance of pure zinc plating in a chloride bath and having a fine plating structure of the plating layer. It is about.

강판의 내식성 향상을 위해서 도금이 발달되었으며 그중에서도 아연전기도금 강판은 자동차용에서 부터 가전제품에 이르기까지 사용의 폭이 넓다. 전기아연도금처리에 사용되는 산성욕으로는 주로 황산아연을 주성분으로 하는 황상물욕과 염화아연을 주로 하는 염화물욕등이 있다. 종래에는 황상물욕을 주로 많이 사용하였으나 황상물욕은 염화물욕에 비하여 전기전도도가 낮아 소정의 도금 전류를 얻기 위하여 높은 전압을 가해야 하므로 전력비용이 많이들고, 또한 허용전류밀도가 낮아서 고속도금을 행하기가 곤란하다. 그러나, 염화물욕은 전기전도도가 양호하여 전력비용이 적게 들고 고속도금에 유리한 반면, 얻어지는 도금층의 표면광택 및 백색이 저하되고 도금층의 미세조직이 커져서 표면이 거칠어지는 결점이 있다. 이러한 경우 도금된 표면외관뿐 아니라 도금후의 공정인 인산염처리나, 크로메이트처리 및 내지문 처리등의 표면이 양호하지 못하며 또한 도장을 행한 후에도 선영섬등에 좋지 못한 영향을 미친다.Plating has been developed to improve the corrosion resistance of steel sheet, and zinc electroplating steel sheet is widely used in automobiles and home appliances. Acidic baths used for electrogalvanizing include sulfuric acid baths mainly composed of zinc sulfate and chloride baths mainly composed of zinc chloride. Conventionally, sulfur-based water baths are mainly used, but sulfur-like water baths have lower electric conductivity than chloride baths, and thus high voltages are required to obtain a predetermined plating current, which leads to high power cost and low allowable current density. Is difficult. However, while the chloride bath has good electrical conductivity and low power cost and is advantageous for high-speed plating, the surface gloss and white of the obtained plating layer are deteriorated and the microstructure of the plating layer is large, resulting in a rough surface. In this case, not only the surface appearance of the plated surface, but also the surface such as phosphate treatment, chromate treatment, and anti-fingerprint process, which is a post-plating process, is not good, and even after coating, the sunscreen is adversely affected.

염화물욕 아연제품의 광택을 향상시키기 위한 방법으로는 폴리에틸렌 옥사이드 알킬레이트 술폰화합물을 첨가하는 방법(일본 특허 공보(소) 42-8764호)과 염화물욕에 카드니우무 이온을 함유시키는 방법(일본 특허 공보(소) 46-40402호)이 알려져 있으나, 실도금공정에 적용하는데는 농도의 엄격한 관리가 힘들다는 문제점이 있다.As a method for improving the gloss of a zinc chloride bath product, a method of adding a polyethylene oxide alkylate sulfone compound (Japanese Patent Publication No. 42-8764) and a method of containing cadmium ions in a chloride bath (Japanese Patent) Publication No. 46-40402) is known, but there is a problem that strict control of concentration is difficult to apply to the actual plating process.

또한, 일본 특허 공보(소) 58-48635호 등에는 도금전의 침적에 의하여 광택도를 부여하는 방법이 제시되어 있으나, 이 방법의 경우에는 도금용액이 오염되기 쉽고 침적설비를 설치하는데 비용이 많이들며, 침적용액이 도금원판의 철분의 용출로 인하여 쉽게 오염되어서 사용상에 문제점이 있게 된다.In addition, Japanese Patent Publication No. 58-48635 discloses a method of imparting glossiness by deposition before plating, but in this case, plating solution is contaminated and expensive to install deposition equipment. , The deposition solution is easily contaminated due to the elution of the iron of the plating disc, there is a problem in use.

이에, 본 발명자는 상기와 같은 문제점을 개선하기 위하여 연구와 실험을 행하고, 그 결과에 근거하여 본 발명을 제안하게 된 것으로서, 본 발명은 도금을 행하기 전이나 도금을 행하고 있는 중에 첨가제 포름알데히드와 에틸렌 글리콜을 섞어 일정량 첨가하므로서 표면외관의 백색도 및 광택도가 우수하고 도금층의 도금조직이 미세한 아연 전기 도금강판의 제조방법을 제공하고자 하는데, 그 목적이 있다.Accordingly, the present inventors have conducted research and experiments to improve the above problems, and based on the results, the present invention proposes the present invention, before the plating or during the plating, and the additive formaldehyde and By adding a predetermined amount by mixing ethylene glycol is to provide a method for producing a zinc electroplated steel sheet excellent in the whiteness and gloss of the surface appearance and fine plating structure of the plating layer, the purpose.

이하, 본 발명을 설명한다.Hereinafter, the present invention will be described.

본 발명은 아연의 몰농도 : 0.7~2.0, 및 염소의 몰농도 : 5.0~9.0으로 조성되는 도금액조성과 도금액의 pH : 2.0~5.5, 도금액의 온도 40~75℃, 유속 : 0.5~2.5m sec, 및 전류 밀도 : 30~180 A/dm²의 도금 조건으로 전기도금하여 아연 전기 도금강판을 제조하는 방법에 있어서, 상기 도금액에 첨가제 포름알데히드와 에틸렌 글리콜을 각각 0.1ml/l이상, 그리고 합이 8.0ml/l이하가 되는 범위로 첨가하여 전기도금함으로서 광택과 백색이 우수한 아연전기 도금강판을 제조하는 방법에 관한 것이다.The present invention is a plating liquid composition composed of a molar concentration of zinc: 0.7 to 2.0, and a chlorine concentration of 5.0 to 9.0, pH of the plating liquid: 2.0 to 5.5, temperature of the plating liquid 40 to 75 ℃, flow rate: 0.5 to 2.5 m sec. And Current density: In the method of producing a galvanized steel sheet by electroplating under the plating conditions of 30 ~ 180 A / dm², 0.1ml / l or more of the additive formaldehyde and ethylene glycol in the plating solution, respectively, and the sum 8.0 The present invention relates to a method for producing a galvanized steel sheet having excellent gloss and white color by electroplating by adding in a range of ml / l or less.

이하, 상기 수치한정 이유등에 대하여 상세히 설명한다.Hereinafter, the numerical limitation reason and the like will be described in detail.

상기 도금액중의 아연의 몰농도가 0.7이하인 경우에는 표면외관이 검고 유속방향으로의 줄 무늬가 심하게 일어나고 표면에 분말형태의 도금이 되며, 아연의 몰농도가 2.0이상인 경우에는 표면이 거칠고 비용이 증가되므로, 도금액중의 아연 몰농도는 0.7~2.0으로 제한하는 것이 바람직하다.When the molar concentration of zinc in the plating solution is 0.7 or less, the surface appearance is black and streaks in the flow direction are severe and the powder is plated on the surface, and when the molar concentration of zinc is 2.0 or more, the surface is rough and the cost increases. Therefore, the zinc molar concentration in the plating liquid is preferably limited to 0.7 to 2.0.

상기 염소의 농도는 전기도금에서 전도도 향상을 위하여 첨가하지만, 그 함량이 9.0몰농도 이상에서는 정해진 온도에서 과포화로 인하여 도금표면의 박리 현상을 일으키고, 5.0몰농도 이하에서는 전도도가 낮아서 도금전압의 상승으로 표면외관이 검게 그을리는 형상을 유발하게 되므로, 염소의 농도는 5.0~9.0몰농도로 제한하는 것이 바람직하다.The concentration of chlorine is added to improve the conductivity in electroplating, but the content of the above chlorine causes a delamination of the plating surface due to supersaturation at a predetermined temperature above 9.0 molar concentration, and the conductivity of the chlorine is lower than 5.0 molar concentration, resulting in an increase in plating voltage. Since the surface appearance causes a blackened shape, it is preferable to limit the concentration of chlorine to 5.0 to 9.0 molar concentration.

상기 도금액의 온도는 40℃이하에서 전도도가 감소하고 도금층 표면에 분말형태나 줄무늬의 긁힌 상태를 유발하게 되고, 75℃이상에서는 표면이 어두워지고 노오란 색으로 표면이 변화되므로, 도금액의 온도는 40~75℃로 제한하는 것이 바람직하다.The temperature of the plating liquid is reduced in conductivity below 40 ℃ and cause a scratched state of powder or streaks on the surface of the plating layer, the surface is darkened and the surface is changed to a yellow color above 75 ℃, the temperature of the plating solution is 40 ~ It is preferable to limit to 75 ° C.

상기 도금액의 pH는 2.0이하에서는 장치의 부식을 유발하여 불순물을 증가시키고 도금층 표면의 색을 어둡게 하며, 5.5이상에서는 표면에 색상이 노랗게 변화되므로, 도금액의 pH는 2.0~5.5롤 제한하는 것이 바람직하다.The pH of the plating liquid is less than 2.0, causing the corrosion of the device to increase impurities and darken the color of the surface of the plating layer, the color of the surface is changed to yellow above 5.5, the pH of the plating liquid is preferably limited to 2.0 ~ 5.5 rolls .

상기 첨가제 포름알데히드와 에틸렌 글리콜의 첨가량이 각각 0.1ml/l이하이거나 전체 첨가량이 0.2ml/l이하인 경우에는 표면의 색상을 백색으로 변화시키고, 광택을 증가시키는 효과가 없으므로, 광택과 백색이 우수한 전기 아연 도금층 표면을 확보하기 위해서는 도금액중에 첨가되는 첨가제 포름알데히드와 에틸렌 글리콜의 첨가량의 합은 0.2ml/l이상 확보되어야 하고 이들 각각의 첨가량은 0.1ml/l이상이 되어야 한다.When the amount of the additive formaldehyde and ethylene glycol added is 0.1ml / l or less or the total addition amount is 0.2ml / l or less, the color of the surface is changed to white and there is no effect of increasing the gloss. In order to secure the surface of the galvanized layer, the sum of the addition amounts of the additive formaldehyde and the ethylene glycol added in the plating solution should be secured at least 0.2 ml / l, and each addition should be at least 0.1 ml / l.

한편, 상기 첨가제 포름알데히드와 에틸렌 글리콜의 첨가량의 합이 8.0ml/l이상인 경우에는 도금층의 밀착성이 불량하게 되므로, 그 첨가량의 합은 8.0ml/l이하가 되도록 제한하는 것이 바람직하다.On the other hand, when the sum of the addition amount of the additive formaldehyde and ethylene glycol is 8.0 ml / l or more, the adhesion of the plating layer is poor, so the sum of the addition amount is preferably limited to 8.0 ml / l or less.

이하, 실시예를 통하여 본 발명을 보다 상세히 설명한다.Hereinafter, the present invention will be described in more detail with reference to Examples.

[실시예]EXAMPLE

냉연강판을 소지금속으로 하여 하기 표2에 나타난 도금액 조성 및 도금조건으로 전기 도금을 행한 후, 도금강판의 표면외관의 광택도 및 백색도를 관찰하고, 그 관찰결과를 하기 표 1에 나타내었다.After the cold-rolled steel sheet as a base metal, electroplating was performed under the plating solution composition and plating conditions shown in Table 2, the glossiness and whiteness of the surface appearance of the coated steel sheet were observed, and the results are shown in Table 1 below.

또한, 하기 표 2의 비교재(B) 및 발명재(6)에 대해서는 도금액의 미세조직을 주사전자현미경을 이용하여 관찰하고 그 결과를 제1도에 나타내었다.In addition, about the comparative material (B) and the invention material (6) of Table 2, the microstructure of the plating liquid was observed using a scanning electron microscope, and the results are shown in FIG.

하기 표 2의 광택도는 Glossor Meter(ERICHSEN)에 의하여 입사각 60°로 측정한 값이며, 백색도는 Color and Color Difference Meter C-5120(TOKYO DANSHOKY)에 의해 측정된 값이며, 제1도의 도금층의 미세조직은 도금액을 Stereo Scan CAMBRIDGE 25 MK3의 주사 전자현미경으로 확대한 조직을 나타낸 것이다.The glossiness of Table 2 is a value measured at an incident angle of 60 ° by a Glossor Meter (ERICHSEN), and the whiteness is a value measured by a Color and Color Difference Meter C-5120 (TOKYO DANSHOKY), and the fineness of the plating layer of FIG. Tissues represent tissues in which the plating solution was expanded with a scanning electron microscope of Stereo Scan CAMBRIDGE 25 MK3.

[표 1]TABLE 1

* 첨가제 : 포름 알데히드 + 에틸렌글리콜* Additive: Formaldehyde + Ethylene Glycol

상기 표1에 나타낸 바와같이, 도금액에 첨가제인 포름알데히드와 에틸렌 글리콜을 본 발명의 범위내로 첨가하여 전기 도금한 본 발명재(1-10)가 첨가제인 포름알데히드와 에틸렌 글리콜을 첨가하지 않고 전기도금한 비교재(A-D)에 비하여 광택도 및 백색도에 있어서 매우 우수함을 알 수 있다.As shown in Table 1 above, the present invention material (1-10) electroplated by adding formaldehyde and ethylene glycol as additives to the plating solution within the scope of the present invention is electroplated without adding formaldehyde and ethylene glycol as additives. It can be seen that it is very excellent in glossiness and whiteness as compared to one comparative material (AD).

한편, 도금층의 미세조직을 나타내는 제1도에서 알 수 있는 바와같이, 첨가제인 포름알데히드와 에틸렌글리콜을 도금액에 2.0ml/ℓ 첨가한 발명재(6)의 도금층 [제1도(b)]은 입자들이 판상으로 적층되어 있으며, 첨가제인 포름알데히드와 에틸렌글리콜을 전혀 첨가하지 않고 전류밀도를 100A/d㎡로 하여 전기 도금한 비교재(B)의 도금층[제1도(a)]에 비하여 미세한 도금조직을 나타내고 있다.On the other hand, as can be seen from FIG. 1 showing the microstructure of the plating layer, the plating layer [In Fig. 1 (b)] of the invention material 6, in which 2.0 ml / l of formaldehyde and ethylene glycol as additives were added to the plating solution, The particles are laminated in a plate shape, and are finer than the plating layer [FIG. 1 (a)] of the comparative material (B) which was electroplated at 100 A / dm 2 without adding any additives of formaldehyde and ethylene glycol. The plating structure is shown.

상술한 바와같이, 본 발명은 도금욕에 첨가제인 포름알데히드와 에틸렌글리콜을 적정량 첨가하여 전기도금함으로써, 도금강판 표면외관의 백색도 및 광택도가 우수하고 도금층의 도금조직이 미세한 아연 전기 도금강판을 제공할 수 있는 효과가 있는 것이다.As described above, the present invention is electroplated by adding a proper amount of formaldehyde and ethylene glycol additives to the plating bath, thereby providing a zinc electroplated steel sheet having excellent whiteness and glossiness of the surface appearance of the plated steel plate and fine plating structure of the plated layer. There is an effect that can be done.

Claims (1)

아연의 몰농도 : 0.7~2.0, 및 염소의 몰농도 : 5.0~9.0로 조성되는 도금액 조성과 도금액의 pH : 2.0~5.5, 도금액의 온도 : 40-75℃, 유속 : 0.5~2.5m/sec, 및 전류밀도 : 30-180A/d㎡의 도금조건으로 전기도금하여 아연 전기도금강판을 제조하는 방법에 있어서, 상기 도금액에 첨가제 포름알데히드와 에틸렌 글리콜을 각각 0.1ml/ℓ이상, 그리고 그 첨가량의 합이 8.0ml/ℓ이하가 되는 범위로 첨가하여 전기도금하는 것을 특징으로 하는 광택과 백색이 우수한 아연전기도금강판의 제조방법.Plating liquid composition with zinc molarity: 0.7-2.0, and chlorine molarity: 5.0-9.0, pH of the plating liquid: 2.0-5.5, temperature of plating liquid: 40-75 ° C., flow rate: 0.5-2.5 m / sec, And a current density of 30-180 A / dm < 2 > for electroplating zinc plated galvanized steel sheet, wherein the additives formaldehyde and ethylene glycol in an amount of at least 0.1 ml / l and the sum of the added amounts. A method for producing a zinc electroplated steel sheet having excellent gloss and whiteness, which is added in an amount of not more than 8.0 ml / l and electroplated.
KR1019910025128A 1991-12-30 1991-12-30 Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White Expired - Fee Related KR940000282B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019910025128A KR940000282B1 (en) 1991-12-30 1991-12-30 Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019910025128A KR940000282B1 (en) 1991-12-30 1991-12-30 Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White

Publications (2)

Publication Number Publication Date
KR930013213A KR930013213A (en) 1993-07-21
KR940000282B1 true KR940000282B1 (en) 1994-01-14

Family

ID=19326642

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019910025128A Expired - Fee Related KR940000282B1 (en) 1991-12-30 1991-12-30 Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White

Country Status (1)

Country Link
KR (1) KR940000282B1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100256427B1 (en) * 1995-12-27 2000-05-15 이구택 Method of making znic electroplating with excellent surface

Also Published As

Publication number Publication date
KR930013213A (en) 1993-07-21

Similar Documents

Publication Publication Date Title
Kumar et al. Factor effecting electro-deposition process
DE3784416T2 (en) SURFACE TREATED BLACK STEEL SHEET AND METHOD FOR PRODUCING THE SAME.
DE4019964C2 (en)
Takahashi et al. Effect of SiO2 Colloid on the Electrodeposition of Zinc‐Iron Group Metal Alloy Composites
EP0140564A2 (en) Electroplated product and method
US6365031B1 (en) High current density zinc sulfate electrogalvanizing process and composition
US5871631A (en) Acidic tin-plating bath and additive therefor
KR940000282B1 (en) Manufacturing Method of Zinc Electroplated Steel Sheet with Excellent Gloss and White
KR0136173B1 (en) Additives of chloride type electro zinc plating solution and plating solution containing same
KR100321374B1 (en) Manufacturing method of zinc-iron alloy plated steel sheet with good plating adhesion, surface roughness and surface appearance
US4806226A (en) Process for electrolytically coloring aluminum material
KR19980050699A (en) Manufacturing method of electro-galvanized steel sheet with good adhesion, surface appearance and roughness
KR100419658B1 (en) An additive for chloride zn-fe alloy electrodeposite and chloride zn-fe alloy electrodeposite solution containg the same
KR0143502B1 (en) Manufacturing method of zinc electric plated steel plate
CN113957495A (en) Brightener for PSA (pressure swing adsorption) electrotinning insoluble anode system and application
KR0128121B1 (en) Additives of chloride-based zinc-iron alloy electroplating solutions and plating solutions containing them
US4804444A (en) Method of producing a both-side electrogalvanized steel strip in a chloride bath
KR100370569B1 (en) Solution for Zinc-Iron Alloy Electroplating with Additive and Method for Manufacturing Plated Steel Sheet Using the Same
KR100417615B1 (en) Method for making Zn electrodeposit additive
KR100979047B1 (en) Additives for electro zinc plating useful for excellent plating adhesion, flatness and surface appearance, manufacturing method thereof and plating method using the same
KR100578214B1 (en) Manufacturing method of zinc-magnesium electroplated steel sheet
KR100349141B1 (en) Method for manufacturing electro galvanized steel sheet with good appearance
KR100723176B1 (en) Sulfide-based galvanized plating solution with excellent surface appearance and hardness, and electro-galvanized steel plate plated using the same
KR960008154B1 (en) Manufacturing method of galvanized steel sheet with excellent surface gloss
JPS5826438B2 (en) Manufacturing method for electrogalvanized steel sheets with excellent gloss

Legal Events

Date Code Title Description
A201 Request for examination
PA0109 Patent application

St.27 status event code: A-0-1-A10-A12-nap-PA0109

PA0201 Request for examination

St.27 status event code: A-1-2-D10-D11-exm-PA0201

R17-X000 Change to representative recorded

St.27 status event code: A-3-3-R10-R17-oth-X000

E902 Notification of reason for refusal
PE0902 Notice of grounds for rejection

St.27 status event code: A-1-2-D10-D21-exm-PE0902

PG1501 Laying open of application

St.27 status event code: A-1-1-Q10-Q12-nap-PG1501

T11-X000 Administrative time limit extension requested

St.27 status event code: U-3-3-T10-T11-oth-X000

P11-X000 Amendment of application requested

St.27 status event code: A-2-2-P10-P11-nap-X000

P13-X000 Application amended

St.27 status event code: A-2-2-P10-P13-nap-X000

G160 Decision to publish patent application
PG1605 Publication of application before grant of patent

St.27 status event code: A-2-2-Q10-Q13-nap-PG1605

E701 Decision to grant or registration of patent right
PE0701 Decision of registration

St.27 status event code: A-1-2-D10-D22-exm-PE0701

GRNT Written decision to grant
PR0701 Registration of establishment

St.27 status event code: A-2-4-F10-F11-exm-PR0701

PR1002 Payment of registration fee

St.27 status event code: A-2-2-U10-U11-oth-PR1002

Fee payment year number: 1

PR1001 Payment of annual fee

St.27 status event code: A-4-4-U10-U11-oth-PR1001

Fee payment year number: 4

PR1001 Payment of annual fee

St.27 status event code: A-4-4-U10-U11-oth-PR1001

Fee payment year number: 5

FPAY Annual fee payment

Payment date: 19981221

Year of fee payment: 6

PR1001 Payment of annual fee

St.27 status event code: A-4-4-U10-U11-oth-PR1001

Fee payment year number: 6

LAPS Lapse due to unpaid annual fee
PC1903 Unpaid annual fee

St.27 status event code: A-4-4-U10-U13-oth-PC1903

Not in force date: 20000115

Payment event data comment text: Termination Category : DEFAULT_OF_REGISTRATION_FEE

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

PC1903 Unpaid annual fee

St.27 status event code: N-4-6-H10-H13-oth-PC1903

Ip right cessation event data comment text: Termination Category : DEFAULT_OF_REGISTRATION_FEE

Not in force date: 20000115

PN2301 Change of applicant

St.27 status event code: A-5-5-R10-R13-asn-PN2301

St.27 status event code: A-5-5-R10-R11-asn-PN2301

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

PN2301 Change of applicant

St.27 status event code: A-5-5-R10-R13-asn-PN2301

St.27 status event code: A-5-5-R10-R11-asn-PN2301

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

PN2301 Change of applicant

St.27 status event code: A-5-5-R10-R13-asn-PN2301

St.27 status event code: A-5-5-R10-R11-asn-PN2301

PN2301 Change of applicant

St.27 status event code: A-5-5-R10-R13-asn-PN2301

St.27 status event code: A-5-5-R10-R11-asn-PN2301

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

P22-X000 Classification modified

St.27 status event code: A-4-4-P10-P22-nap-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000

R18-X000 Changes to party contact information recorded

St.27 status event code: A-5-5-R10-R18-oth-X000