JPH036240B2 - - Google Patents
Info
- Publication number
- JPH036240B2 JPH036240B2 JP11988384A JP11988384A JPH036240B2 JP H036240 B2 JPH036240 B2 JP H036240B2 JP 11988384 A JP11988384 A JP 11988384A JP 11988384 A JP11988384 A JP 11988384A JP H036240 B2 JPH036240 B2 JP H036240B2
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- dissolution
- plating
- shots
- dissolved
- 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
Links
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 45
- 239000011701 zinc Substances 0.000 claims description 40
- 229910052725 zinc Inorganic materials 0.000 claims description 34
- 238000007747 plating Methods 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 19
- VEQPNABPJHWNSG-UHFFFAOYSA-N Nickel(2+) Chemical compound [Ni+2] VEQPNABPJHWNSG-UHFFFAOYSA-N 0.000 claims description 2
- 230000002378 acidificating effect Effects 0.000 claims description 2
- 229910001453 nickel ion Inorganic materials 0.000 claims description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 32
- 238000004090 dissolution Methods 0.000 description 27
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000002184 metal Substances 0.000 description 11
- 229910052759 nickel Inorganic materials 0.000 description 10
- 239000000243 solution Substances 0.000 description 10
- 239000007788 liquid Substances 0.000 description 8
- 238000005246 galvanizing Methods 0.000 description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- 241000080590 Niso Species 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 238000007922 dissolution test Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- QELJHCBNGDEXLD-UHFFFAOYSA-N nickel zinc Chemical compound [Ni].[Zn] QELJHCBNGDEXLD-UHFFFAOYSA-N 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 229910001335 Galvanized steel Inorganic materials 0.000 description 2
- 229910000990 Ni alloy Inorganic materials 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000008397 galvanized steel Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910000978 Pb alloy Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- FMRLDPWIRHBCCC-UHFFFAOYSA-L Zinc carbonate Chemical compound [Zn+2].[O-]C([O-])=O FMRLDPWIRHBCCC-UHFFFAOYSA-L 0.000 description 1
- 229910001297 Zn alloy Inorganic materials 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- 238000010349 cathodic reaction Methods 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 150000003751 zinc Chemical class 0.000 description 1
- 229910000010 zinc carbonate Inorganic materials 0.000 description 1
- 235000004416 zinc carbonate Nutrition 0.000 description 1
- 239000011667 zinc carbonate Substances 0.000 description 1
Landscapes
- Electroplating And Plating Baths Therefor (AREA)
Description
本発明は、電気亜鉛メツキ浴への亜鉛シヨツト
の溶解方法に関するものであり、特には金属亜鉛
溶解速度を上げる為に亜鉛より貴な電位を持ち且
つ水素過電圧の小さな金属であるニツケルを予備
溶存させることを特徴とする亜鉛シヨツト溶解方
法に関する。
鉄鋼材料の防食目的で電気亜鉛メツキが広く実
施されている。近時、自動車、家電製品、建築材
料、プラント材料等の分野での亜鉛メツキ鋼板の
需要増は著しく、特に自動車用途には厚亜鉛メツ
キ材が求められている。こうした需要増に対処す
るべく、従来の可溶性陽極を用いる電気亜鉛メツ
キ法よりも、不溶性陽極を用いて高電流密度下で
メツキを行う高速メツキ法が現在では脚光をあび
ている。不溶性陽極を用いての高速メツキ法で
は、メツキ浴中の亜鉛の消費に伴い亜鉛を補給す
ることが必要とされる。亜鉛補給に当つては、亜
鉛溶解が充分に速いものでなければならない。補
給亜鉛として炭酸亜鉛を用いる場合には迅速な溶
解が保証されるが、コスト増につき、現在では亜
鉛シヨツトを直接メツキ浴中に溶解する方式が考
慮されている。
しかしながら、金属亜鉛シヨツトの電気亜鉛メ
ツキ浴への溶解性は良好ではない。従つて、不溶
性陽極を用いる高速メツキ法を好適に実施する為
には、金属亜鉛シヨツトの溶解性向上のための対
策を確立する必要がある。その対策のためかなり
のコスト増を招くことは、安価な亜鉛シヨツトを
用いることの意義を失わしめる。例えば、液温を
上げることによつて、亜鉛シヨツトの溶解を促進
しうるが、液温の昇降の為のコストがかかり実用
的でない。
こうした事情の下で、本発明は、安価な、電気
亜鉛メツキ浴への亜鉛シヨツト溶解方法の確立を
目的とする。
金属が酸性溶液中に溶解する場合、その陰極反
応として次式の反応による水素の発生が不可欠で
ある。
H++e-=1/2H2
この反応が起こる電位は、反応が起こる電極面
により大きく影響を受ける。このため、水素過電
圧の大きい金属程溶解し難い。亜鉛の水素過電圧
はかなり大きい方に属しており、このため亜鉛シ
ヨツトの電気亜鉛メツキ浴への溶解速度が小さい
ものと考えられる。ちなみに、陰極電流密度=
10-3A/cm2、1N−HCl、室温での亜鉛の過電圧は
0.85であり、SnやCdと並んで非常に高い水準に
ある。従つて、金属亜鉛シヨツトに、Pt、Ni、
Fe等亜鉛より貴な電位を持ち且つ水素過電圧の
小さな金属を接触・共存させることにより、電気
亜鉛メツキ浴への溶解速度を大きくなしうるもの
と期待される。そこで、各種金属について検討を
重ねた。
その結果、亜鉛より貴な金属、特にNiのイオ
ンを微量メツキ浴中に存在させておくことにより
亜鉛シヨツトの溶解を促進しうることを判明し
た。
斯くして、本発明は、酸性電気亜鉛メツキ浴へ
の亜鉛シヨツトの溶解に際して、メツキ浴中に5
〜1000ppmのニツケルイオンを存在させることを
特徴とする亜鉛シヨツト溶解方法を提供する。
以下、本発明を実験例に基いて具体的に説明す
る。
不溶性陽極を用いる高速亜鉛メツキ法は現在の
ところ、
Zn: 100g/
Na2SO4: 30g/
free−H2SO4: 4.9g/
を基本的浴組成とし、ニツケル−亜鉛合金メツキ
の場合にはニツケルが100g/上記に追加され
たものを用いている。浴中のPHは0.8〜3.5程度そ
して浴温は40〜80℃範囲が代表的である。メツキ
浴液は循環使用される。不溶性陽極としては、例
えば、鉛合金、白金族合金等が使用される。
上記電気亜鉛メツキ浴を模擬して次の溶解試験
を行つた。試験においては、亜鉛シヨツト単味
(No.1)、Fe線、Ni片及びPt線を添加したもの
(No.2〜4)、FeSO4・6H2Oを予め溶解したもの
(No.5)及びNiSo4・6H2Oを予め溶解したもの
(No.6)が使用された:
1 溶解液基本条件
液組成 ZnSO4・7H2O:450g/(Zn:
102.4g/)
Na2SO4(無水):30g/
free−H2SO4:4.9g/(Zn当量:3.27
g/)
液温度 55〜60℃
液量 1l
2 供試最純亜鉛シヨツトの性状
粒径 2〜4mm
化学成分 Fe:15ppmPb:10ppmCd:6ppm
投入量 100g
3 試験方法
溶解液1lをビーカーに入れ、これをホツトプ
レートとにより、55〜60℃に保持しながら、こ
こに最純亜鉛シヨツト100gと所定量の添加剤
(金属又は金属塩)を投入し、液PH、free−
H2SO4濃度の経時変化、及び亜鉛シヨツト溶
解量を調べた。
なお、溶解時間は3Hrとし、溶解液は撹拌翼
にて430rpmにて撹拌を行なつた。
4 試験条件
各試験条件を表1にまとめて示す。
The present invention relates to a method for dissolving zinc shots in an electrolytic galvanizing bath, and in particular, in order to increase the dissolution rate of metallic zinc, nickel, a metal which has a nobler potential than zinc and has a small hydrogen overvoltage, is predissolved. The present invention relates to a method for dissolving zinc shots characterized by the following. Electrogalvanizing is widely practiced for the purpose of preventing corrosion of steel materials. In recent years, demand for galvanized steel sheets has increased significantly in the fields of automobiles, home appliances, building materials, plant materials, etc., and thick galvanized steel sheets are particularly required for automobile applications. In order to cope with this increased demand, high-speed plating methods that use insoluble anodes to perform plating under high current density are currently attracting attention rather than conventional electrogalvanizing methods that use soluble anodes. High-speed plating methods using insoluble anodes require replenishment of zinc in the plating bath as it is consumed. When supplementing with zinc, zinc dissolution must be sufficiently rapid. When using zinc carbonate as supplementary zinc, rapid dissolution is guaranteed, but due to the increased cost, methods are currently being considered in which zinc shots are dissolved directly into the plating bath. However, the solubility of metallic zinc shots in electrogalvanizing baths is not good. Therefore, in order to suitably implement a high-speed plating method using an insoluble anode, it is necessary to establish measures to improve the solubility of metallic zinc shots. Incurring a considerable increase in cost as a countermeasure for this eliminates the significance of using inexpensive zinc shots. For example, it is possible to promote the dissolution of zinc shots by increasing the temperature of the liquid, but this is not practical due to the cost associated with raising and lowering the temperature of the liquid. Under these circumstances, the present invention aims to establish an inexpensive method for dissolving zinc shots in an electrogalvanizing bath. When a metal is dissolved in an acidic solution, it is essential that hydrogen be generated by the following reaction as a cathodic reaction. H + +e - = 1/2H 2 The potential at which this reaction occurs is greatly influenced by the electrode surface where the reaction occurs. Therefore, metals with larger hydrogen overvoltages are more difficult to dissolve. The hydrogen overpotential of zinc is on the rather large side, and it is therefore thought that the rate of dissolution of the zinc shot into the electrolytic galvanizing bath is low. By the way, cathode current density =
The overpotential of zinc at 10 -3 A/cm 2 , 1N−HCl, and room temperature is
It is 0.85, which is at a very high level along with Sn and Cd. Therefore, metal zinc shots include Pt, Ni,
It is expected that the rate of dissolution into the electrolytic galvanizing bath can be increased by bringing metals such as Fe, which have a nobler potential than zinc and have a small hydrogen overvoltage, into contact with and coexist with them. Therefore, various metals were investigated. As a result, it was found that the dissolution of zinc shots could be promoted by allowing a trace amount of ions of metals nobler than zinc, especially Ni, to be present in the plating bath. Thus, the present invention provides a method for dissolving zinc shot in an acidic electrogalvanizing bath.
Provided is a method for dissolving zinc shots characterized by the presence of ~1000 ppm of nickel ions. Hereinafter, the present invention will be specifically explained based on experimental examples. At present, the basic bath composition of the high-speed galvanizing method using an insoluble anode is Zn: 100g/Na 2 SO 4 : 30g/free-H 2 SO 4 : 4.9g/, and in the case of nickel-zinc alloy plating, 100g of nickel is used in addition to the above. The pH in the bath is typically about 0.8 to 3.5, and the bath temperature is typically in the range of 40 to 80°C. Metsuki bath liquid is used in circulation. As the insoluble anode, for example, a lead alloy, a platinum group alloy, or the like is used. The following dissolution test was conducted simulating the electrogalvanizing bath described above. In the test, zinc shot alone (No. 1), one with Fe wire, Ni piece and Pt wire added (No. 2 to 4), and one with FeSO 4 6H 2 O dissolved in advance (No. 5). and NiSo 4・6H 2 O dissolved in advance (No. 6) were used: 1 Basic conditions of solution liquid composition ZnSO 4・7H 2 O: 450 g/(Zn:
102.4g/) Na 2 SO 4 (anhydrous): 30g/ free-H 2 SO 4 : 4.9g/(Zn equivalent: 3.27
g/) Liquid temperature 55-60℃ Liquid volume 1l 2 Properties of the purest zinc shot tested Particle size 2-4mm Chemical composition Fe: 15ppmPb: 10ppmCd: 6ppm Input amount 100g 3 Test method Pour 1l of the solution into a beaker and 100g of the purest zinc shot and a predetermined amount of additives (metals or metal salts) were added thereto while maintaining it at 55 to 60℃ using a hot plate, and the liquid pH was adjusted to 55~60℃.
Changes in H 2 SO 4 concentration over time and the amount of zinc shot dissolved were investigated. The dissolution time was 3 hours, and the solution was stirred with a stirring blade at 430 rpm. 4 Test Conditions Table 1 summarizes each test condition.
【表】
こうして為された溶解試験の結果を示す。次の
表2はNo.1−6における溶解時間3時間後の亜鉛
溶解量の実測値を示す。[Table] Shows the results of the dissolution test thus conducted. The following Table 2 shows the actual measured values of the amount of zinc dissolved after 3 hours of dissolution time in Nos. 1-6.
【表】
添付第1図は溶解後PHの経時変化を示すグラフ
である。溶解後PHは亜鉛溶解量を反映するもので
ある。
表2及び第1図から分かるように、最純亜鉛単
味溶解の場合に比較して、添加剤を添加した場合
は、いずれの場合も溶解速度が大きくなつている
が、中でもPt線を接触させた場合が最も効果が
大きく、次が、溶解液中に予めNiを溶解させた
場合が効果が大きい。
Niを金属として添加する場合(No.3)とイオ
ンとして添加する場合(No.6)とでは溶解速度は
全く異なる。Niにおいてはイオンとして存在さ
せる方がはるかに高い溶解速度を示すのに対し、
Feにおいては金属として添加する方が高い溶解
速度を示す。このように、Fe、Niという同種に
対してさえも、溶解現象は複雑な様相を呈し、予
知は仲々困難である。
以上の結果より、ZnシヨツトにPtを接触させ
た場合が最もZnの溶解速度が大きくなることが
分かつたが、この方法を実操業化する場合、イニ
シヤルコストが高いこと、またPtの摩耗による
消耗が考えられることから、実用性に乏しい。従
つて、Ptとの接触に準ずる高い溶解速度を示す
Ni予備溶解法が工業的には一番優れた亜鉛シヨ
ツト溶解法と結論づけられる。
表3及び第2図に、各溶解時間におけるZn溶
解量及び溶解液中のNi濃度、free−H2SO4濃度
を示す。
溶解開始後20分程度は、溶解速度は極めて小さ
いようであるが、その後は溶解時間3時間まで溶
解時間とともに、ほぼ直線的に溶解している。[Table] Attached Figure 1 is a graph showing the change in pH after dissolution over time. The pH after dissolution reflects the amount of zinc dissolved. As can be seen from Table 2 and Figure 1, the dissolution rate is higher in all cases when additives are added than in the case of simple dissolution of purest zinc. The effect is the greatest when Ni is allowed to dissolve in the solution, and the second most effective is when Ni is dissolved in the solution in advance. The dissolution rate is completely different when Ni is added as a metal (No. 3) and when it is added as an ion (No. 6). Whereas Ni shows a much higher dissolution rate when it exists as an ion,
Fe exhibits a higher dissolution rate when added as a metal. As described above, even for the same species, Fe and Ni, the dissolution phenomenon exhibits a complex aspect, making prediction difficult. From the above results, it was found that the dissolution rate of Zn is the highest when Pt is brought into contact with the Zn shot, but when this method is put into actual operation, the initial cost is high, and the wear of Pt It is not practical due to the possibility of wear and tear. Therefore, it shows a high dissolution rate similar to that in contact with Pt.
It is concluded that the Ni pre-melting method is industrially the best zinc shot melting method. Table 3 and FIG. 2 show the amount of Zn dissolved, the Ni concentration in the solution, and the free-H 2 SO 4 concentration at each dissolution time. The dissolution rate seems to be extremely slow for about 20 minutes after the start of dissolution, but after that it dissolves almost linearly with the dissolution time until 3 hours.
【表】
試験結果では、予め添加したNi濃度の分析値
はほとんど変化していないがおそらく微細に析出
した微量のNiが水素発生の促進に寄与している
ものと考えられる。またこの方法では、溶解液中
のNiは、電解時にも通常のメツキ条件下の電流
密度では、ほとんど析出しないと考えられ、たと
えわずかに析出したとしてもメツキ皮膜の耐食性
等にはプラスになるものと考えられることから、
何ら障害を呈するものでない。
Niイオンの添加量は5ppm以上存在することが
溶解速度増大効果を奏する上で必要である。添加
量の上限は目的とする電気亜鉛メツキ製品の品質
に悪影響を与えない範囲(例えば、Znめつき板
の化成処理時の外観不良、塗装後の密着性不良を
起こし、さらに、経済的でなくなる。)である
1000ppmまでなら高くなしうる。
電気亜鉛メツキを行うメツキ工場においては、
この亜鉛単独メツキと併せて亜鉛−ニツケル合金
メツキを実施することが多い。亜鉛−ニツケル合
金メツキ浴は亜鉛とほぼ同量のニツケルを含有し
ている。こうした合金メツキ槽排出後の槽内には
ニツケルが必ず微量残留している。従つて、その
後で亜鉛単独メツキを実施することにより残留ニ
ツケルを亜鉛シヨツト溶解促進剤として有効活用
することができる。ニツケル添加の為の別個の手
段を購じる必要がなくなる。
実際のメツキ工場において、先ず合金メツキ液
を溶解調整し、それを次工程に送つた後のメツキ
槽において亜鉛単独メツキ浴を調整したところ10
〜30ppmのニツケルの存在が確認され、その後亜
鉛シヨツトの添加をスムーズに行うことができ
た。
さらに他の実施例として以下の試験を行つた。
メツキ槽につながる溶解槽3m3内に亜鉛メツキ
液(ZnSO4・7H2O450g/、Na2SO430g/
PH液温60℃)を2m3導入し、NiSO4・6H2OをNi
として500ppmを添加した。この上に最純亜鉛シ
ヨツト(約3mmφ)7Kgを徐々に添加し、撹拌翼
で撹拌した。1時間後には亜鉛シヨツトは完全に
溶解した。
また上記方法との比較として、以下の確認試験
をした。
実施例1と同要領で、亜鉛メツキ液にNiSO4・
6H2Oを添加せずに亜鉛シヨツト(約3mmφ)5
Kgを徐々に添加し、撹拌翼で撹拌した。約3時間
経過後でも亜鉛シヨツトは、大部分が溶解してい
なかつた。
以上、本発明は、亜鉛シヨツトの溶解速度を上
げる為のコスト負担の実質ない簡便な方法を提供
するものであり、今後益々需要の増大の予想され
る高速亜鉛メツキに有益な貢献をなすものであ
る。[Table] According to the test results, there was almost no change in the analytical value of the concentration of Ni added in advance, but it is thought that a trace amount of finely precipitated Ni probably contributed to the promotion of hydrogen generation. In addition, with this method, it is thought that almost no Ni in the solution will precipitate at the current density under normal plating conditions during electrolysis, and even if a small amount of Ni precipitates, it will have a positive effect on the corrosion resistance of the plating film. Since it is thought that
It does not present any problem. It is necessary for the amount of Ni ions added to be 5 ppm or more in order to achieve the effect of increasing the dissolution rate. The upper limit of the amount added is within the range that does not adversely affect the quality of the intended electrogalvanized product (for example, it may cause poor appearance during chemical conversion treatment of Zn-plated plates, poor adhesion after painting, and become uneconomical. ).
It can be as high as 1000ppm. At the Metsuki factory, which performs electrogalvanizing,
Zinc-nickel alloy plating is often carried out in conjunction with this zinc single plating. Zinc-nickel alloy plating baths contain approximately the same amount of nickel as zinc. After the alloy plating tank is discharged, a small amount of nickel always remains in the tank. Therefore, by subsequently plating with zinc alone, the residual nickel can be effectively utilized as a zinc shot dissolution promoter. There is no need to purchase separate means for nickel addition. In an actual plating factory, the alloy plating solution was first dissolved and adjusted, and after it was sent to the next process, a zinc-only plating bath was prepared in the plating tank10.
The presence of ~30ppm of nickel was confirmed, and zinc shots could then be added smoothly. Furthermore, the following test was conducted as another example. Galvanizing solution (ZnSO 4 7H 2 O 450g /, Na 2 SO 4 30g/
Introduce 2 m 3 of PH liquid temperature 60℃) and add NiSO 4 6H 2 O to Ni
500ppm was added. 7 kg of the purest zinc shot (approximately 3 mmφ) was gradually added thereto and stirred with a stirring blade. After one hour, the zinc shot was completely dissolved. In addition, as a comparison with the above method, the following confirmation test was conducted. In the same manner as in Example 1, add NiSO 4 to the galvanizing solution.
Zinc shot (approximately 3 mmφ) 5 without adding 6H 2 O
Kg was gradually added and stirred with a stirring blade. Even after about 3 hours, most of the zinc shots remained undissolved. As described above, the present invention provides a simple and cost-free method for increasing the dissolution rate of zinc shot, and will make a useful contribution to high-speed galvanizing, the demand of which is expected to increase in the future. be.
第1図は溶解試験No.1〜6における溶解後PHの
経時変化を示すグラフであり、第2図はニツケル
を予備溶解されたNo.6における亜鉛溶解量の経時
変化を示すグラフである。
FIG. 1 is a graph showing the change over time in the pH after dissolution in dissolution test Nos. 1 to 6, and FIG. 2 is a graph showing the change over time in the amount of zinc dissolved in No. 6 in which nickel was pre-dissolved.
Claims (1)
解に際して、メツキ浴中に5〜1000ppmのニツケ
ルイオンを存在させることを特徴とする亜鉛シヨ
ツト溶解方法。1. A method for dissolving zinc shots, which comprises causing 5 to 1000 ppm of nickel ions to be present in the plating bath when dissolving the zinc shots in an acidic electrolytic zinc plating bath.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11988384A JPS61600A (en) | 1984-06-13 | 1984-06-13 | Dissolving method of zinc shot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11988384A JPS61600A (en) | 1984-06-13 | 1984-06-13 | Dissolving method of zinc shot |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61600A JPS61600A (en) | 1986-01-06 |
| JPH036240B2 true JPH036240B2 (en) | 1991-01-29 |
Family
ID=14772592
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11988384A Granted JPS61600A (en) | 1984-06-13 | 1984-06-13 | Dissolving method of zinc shot |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61600A (en) |
-
1984
- 1984-06-13 JP JP11988384A patent/JPS61600A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61600A (en) | 1986-01-06 |
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