CN102162110B - Methyl sulfonate tinning electrolyte and tinning method of steel strip or steel plate - Google Patents

Methyl sulfonate tinning electrolyte and tinning method of steel strip or steel plate Download PDF

Info

Publication number
CN102162110B
CN102162110B CN2011100330718A CN201110033071A CN102162110B CN 102162110 B CN102162110 B CN 102162110B CN 2011100330718 A CN2011100330718 A CN 2011100330718A CN 201110033071 A CN201110033071 A CN 201110033071A CN 102162110 B CN102162110 B CN 102162110B
Authority
CN
China
Prior art keywords
electrolyte
tin
steel plate
plating
tinning
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.)
Active
Application number
CN2011100330718A
Other languages
Chinese (zh)
Other versions
CN102162110A (en
Inventor
刘子利
徐文龙
王怀涛
徐斌
刘希琴
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhangjiagang Fenghuang Technology Development Co.,Ltd.
Original Assignee
ZHANGJIAGANG NEWGANGXING TECHNOLOGY Co Ltd
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 ZHANGJIAGANG NEWGANGXING TECHNOLOGY Co Ltd filed Critical ZHANGJIAGANG NEWGANGXING TECHNOLOGY Co Ltd
Priority to CN2011100330718A priority Critical patent/CN102162110B/en
Publication of CN102162110A publication Critical patent/CN102162110A/en
Application granted granted Critical
Publication of CN102162110B publication Critical patent/CN102162110B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention discloses methyl sulfonate tinning electrolyte using cerium salt as an additive. The electrolyte comprises the following components: 30 to 120 g/L of stannous methyl sulfonate, 60 to 180 g/L of methylsulfonic acid, 1 to 10 g/L of cerium sulfate, 0.1 to 2 g/L of antioxidant, 5 to 10 g/L of brightening agent and 5 to 10 g/L of surfactant. The invention also discloses a method for tinning a steel strip or a steel plate by adopting the electrolyte. During plating, the cerium salt in the electrolyte lightens the harm degree of 'hydrogen brittleness', and plays roles of the antioxidant and the brightening agent. On the basis of adaptability to the environment, the electrolyte meets the requirements that the process is simple, the solution is stable, the maintenance is easy and the quality of a coating is high.

Description

The tin plating method of a kind of metilsulfate tin plating electrolyte and steel band or steel plate
Technical field
The present invention relates to electrolytic solution and electro-plating method that the surface of light metal material is handled, refer more particularly to and a kind ofly be the metilsulfate tin plating electrolyte of additive and carry out electric plating method with this metilsulfate tin plating electrolyte with cerium salt.
Background technology
At present, tin plate is cold rolling Low Carbon Steel or the steel band that the two sides is coated with pure tin.It with solidity to corrosion, weldability and attractive in appearance the rolling into one of tin, has advantages such as nontoxic, that ductility good, solidity to corrosion is good with the intensity of steel and formability, and its surface is rich in gloss, the easy coloring printing.Therefore, tin plate is for a long time as the main wrapping material of foodstuffs industry, and is widely used in industries such as medicine, light industry, automobile and household electrical appliances, is one of most popular steel product.
All there is the shortcoming of high pollution (like fluoroborate, phenolsulfonate and halogenide etc.), plating bath unstable (vitriol) in the zinc-plated industry of traditional electrical.Methylsulphonic acid is claimed methylsulfonic acid or methanesulfonic again, is called for short MSA (Methane Sulfonic Acid), and structural formula is CH 3SO 3H is a kind of organic acid, non-oxidizing acid, is widely used as surface-treated leveling agent and brightening agent.Compare with the fluoroborate bath system with vitriol, the MSA bath system is stable in acidity, neutrality and basic soln.In addition, the MSA plating bath can be operated under very high current density, like high speed electrodeposition and continuous electroplating, can improve the solubility of tensio-active agent and other organic additive.The most important thing is that the MSA plating bath has remarkable advantages aspect environmental protection, its toxicity is lower than fluoroboric acid and silicofluoric acid; Can biological degradation, finally generate vitriol and carbonic acid gas, rate capable of circulation reaches 80%, therefore, the zinc-plated system of metilsulfate will become zinc-plated in most widely used technology.
The low oxidation rate of MSA plating bath requires to use some insoluble anodes to replace the used solubility tin anode of halogenation production line to keep the concentration of stannous ion in the plating bath, and current density should be higher than 10A/dm simultaneously 2For preventing Sn 2+Oxidation and hydrolytic precipitation cause the stability of solution to reduce, and free MSA should keep certain content in the plating bath.But too high levels can be dissolved by accelerating anode, makes Sn 2+Mass concentration further rises, and causes coating coarse, increases hydrogen-separating quantity simultaneously, causes electric current to descend; Content is low excessively, and bath stability is reduced, and current density range dwindles.But the key distinction of various MSA plating bath technologies is to comprise the different of additive types such as tensio-active agent, inhibitor, brightening agent and content, so the main still Study on Additive of the tinned research and development of metilsulfate.
People's such as Hu Lixin research document (is electroplated and environmental protection; 2009,29 the 6th phases of volume: 29-32) disclose a kind of methylsulphonic acid eleetrotinplate prescription: stannous methanesulfonate 8~10mL/L, methylsulphonic acid 96~112mL/L with good stability; Resorcinol 1.0~1.5g/L; 2-mercaptobenzimidazole (M) 0.2~0.3g/L, phenolphthalein 1.0~1.6mL/L, OP-10 tensio-active agent 1.0~1.4mL/L.But if temperature too high (>=35 ℃), plating bath stable bad, Sn 2+Be oxidized to Sn easily 4+, make electrolytic solution muddy, and coating is coarse, be difficult on the zinc-plated production line of hot conditions and use this method.Used the basal component of thionamic acid as electrolytic solution in the Russia SU1678094 patent documentation, sulphosalicylic acid and polyoxyethylene glycol sulfuric acid ester are as additive.But this processing parameter is strict, and especially the restriction of electroplating temperature makes this method should not be used for actual production.In addition, it is harmful to environment to contain sulphosalicylic acid in the electrolytic tinning liquid of this preparation, also makes this method be difficult to large-scale promotion and uses.Exploitation can reduce disadvantageous effect, the more excellent additive of performance will be the emphasis of the zinc-plated technology of current metilsulfate.
Turn usefulness into because the brightening agent in the metilsulfate tin plating electrolyte plays resistance to the electrodeposition process of tin, help obtaining careful, the bright coating of crystallization.Owing to constantly consume, when its content during, can not plate out the coating of light, and the resolvent of brightening agent and metallic impurity also can influence the performance of electrolytic solution less than certain value along with electroplating process.Novel brightening agent exploitation in the metilsulfate tin plating electrolyte is the research and development emphasis of the zinc-plated technology of metilsulfate always.
Rare earth has obtained extensive studies and application as electroplating additive.In vitriol and fluoroborate bath system, cerium salt not only can suppress Sn in the acid tank liquor 4+Generation, improved the stability of plating bath; Simultaneously can enlarge the cathode current density scope; Strengthen the covering power of plating bath, widen the bright range of coating, improve the solidity to corrosion of coating and the specific conductivity of coating (Xuan Tianpeng etc. " cerium is to the influence of tinned lead weldability ": " electroplating and finish "; 1993, the 15th volume the 5th phase: 11-13; Yu Jin etc. " cerium salt pair eleetrotinplate parameter and Effect on Performance ": sufacing,, the 33rd the 2nd phase of volume: 62-63) in 2004.In the metilsulfate tin plating electrolyte, do not see the report that adds rare-earth salts at present as yet.
Summary of the invention
Technical problem to be solved by this invention is: taken all factors into consideration on the basis of environmental protection, a kind of good stability is provided, and can improve the metilsulfate tin plating electrolyte of luminance brightness, corrosion resisting property and the welding property of tin coating.
For solving the problems of the technologies described above; The technical scheme that the present invention adopts is: a kind of metilsulfate tin plating electrolyte comprises following composition (g/L): 30~120 stannous methanesulfonates, 60~180 methylsulphonic acids; 1~10 cerous sulfate; 0.1~2 inhibitors, 5~10 brightening agents and 5~15 tensio-active agents, described inhibitor are Resorcino or catechol or both mixtures; Described brightening agent is LUTARALDEHYDE or benzylidene-acetone or both mixtures, and described tensio-active agent is polyoxyethylene octyl phenyl ether or sodium laurylsulfonate or both mixtures.
Another technical problem to be solved by this invention is: a kind of steel band of luminance brightness, corrosion resisting property and the welding property that improves tin coating or the tin plating method of steel plate are provided.
The technical scheme that the present invention adopts is: the tin plating method of steel band or steel plate has adopted above-mentioned metilsulfate tin plating electrolyte.During plating, the transfer rate of steel band or steel plate is 3~9m/s, and plating temperature is 15~60 ℃, and current density is 6~20A/dm 2
Before plating, steel band or steel plate are carried out degreasing and pickling pre-treatment.
Steel band after the plating or steel plate are carried out soft heat, passivation and tin layer oiling aftertreatment.
The invention has the beneficial effects as follows: contain cerium salt in the electrolytic solution described in the present invention, enlarged the cathode current density scope, strengthen the covering power of plating bath, widen the bright range of coating, improve the solidity to corrosion of coating and the specific conductivity of coating; Brightening agent in this electrolytic solution plays resistance to the electrodeposition process of tin and turns usefulness into; Help obtaining careful, the bright coating of crystallization; And cerium is easy to be adsorbed on the active site of crystal growth; Can effectively suppress crystal growth, make the coating grain refining and surface-brightening is careful, reduce the consumption of the brightening agent in the metilsulfate tin plating electrolyte; Simultaneously, cerium is stronger to the magnetism of electronics, and rare earth forms ion easily in solution, and the specific adsorption of cerium ion makes hydrogen ion stop hydrionic selectivity in raising of negative electrode deposition potential and adsorption film, has alleviated the hazard rating of " hydrogen embrittlement "; Cerous sulfate suppresses Sn as inhibitor in the above-mentioned electrolytic solution 2+Change into Sn 4+, improved the stability of plating bath.
Metilsulfate tin plating electrolyte of the present invention is placed experiment, heated constant temperature oxidation style and H 2O 2The bath stability performance of promote the oxidation experiment is tested, and coating has been carried out binding force of cladding material detection, the detection of high temperature resistance oxidation-resistance, the anti-sulphur corrosion ability experiment of coating and weldability test experience.Experiment proof cerous sulfate additive has improved electrolytic solution stability, has increased the covering power of electrolytic solution, has improved luminance brightness, corrosion resisting property and the welding property of tin coating simultaneously.
Embodiment
Describe the present invention below in conjunction with specific embodiment.
Embodiment 1:
At first; The preplating sample is carried out pre-washing and pickling (according to " Ferrostan (Fei Luositan) " method) pre-treatment; It is zinc-plated that sample after the processing carries out metilsulfate by following condition, and zinc-plated back sample carries out soft heat, Passivation Treatment and tin layer oiling aftertreatment.20 ℃ of electroplating temperatures, current density 6A/dm 2, the speed of negative electrode travelling belt is 3m/s.During electrolyte quota; Clean up coating bath with tap water and deionized water respectively; Then; The deionized water that adds 1/2 volume adds methylsulphonic acid, the inferior tin of methylsulfonic acid, cerous sulfate, Resorcinol, catechol, benzylidene-acetone, LUTARALDEHYDE, OP-10, sodium laurylsulfonate successively by calculated amount; Then, adding deionized water to prescribed volume, is electrodepositable after stirring.The prescription of electrolytic solution is following:
Figure GDA0000158074210000041
Embodiment 2:
25 ℃ of electroplating temperatures, current density 8A/dm 2, the speed of negative electrode travelling belt is 3m/s, other are identical with embodiment 1.The prescription of electrolytic solution is following:
Figure GDA0000158074210000051
Embodiment 3
30 ℃ of electroplating temperatures, current density 10A/dm 2, the speed of negative electrode travelling belt is 3m/s, other are identical with embodiment 1.The prescription of electrolytic solution is following:
Figure GDA0000158074210000052
Embodiment 4
40 ℃ of electroplating temperatures, current density 12A/dm 2, the speed of negative electrode travelling belt is 6m/s, other are identical with embodiment 1.The prescription of electrolytic solution is following:
Figure GDA0000158074210000061
Embodiment 5
50 ℃ of electroplating temperatures, current density 15A/dm 2, the speed of negative electrode travelling belt is 6m/s, other are identical with embodiment 1.The prescription of electrolytic solution is following:
Figure GDA0000158074210000062
Embodiment 6
55 ℃ of electroplating temperatures, current density 20A/dm 2, the speed of negative electrode travelling belt is 9m/s, other are with real
It is identical to execute example 1.The prescription of electrolytic solution is following:
Figure GDA0000158074210000071
For the eleetrotinplate solution that confirms this preparation possesses good stability, carry out following experiment:
Place experiment: get following each 1L of the test solution for preparing, under 20 ℃ temperature, keep the tin anode plate and place test, with the examination bath stability.The result is as shown in table 1 for the experiment gained.
The heated constant temperature oxidation style: below each 50ml of test solution of preparing; Contain respectively in what open wide and have in the graduated small beaker; Place temperature to be controlled at 50 ± 5 ℃ thermostat(t)ed water, under the condition of astigmatism irradiation, observe test solution and become muddy degree; The record test solution begins to become muddy and complete muddy required time, and analyzes respectively with iodimetry,iodometry and to join test solution, test solution Sn in the solution when beginning to become muddy and complete muddiness at present 2+Content.The result is as shown in table 2 for the experiment gained.
H 20 2Promote the oxidation experiment: get following each 50ml of the test solution for preparing, contain respectively in 100ml and have in the graduated beaker, each drips 20 ydrogen peroxide 50, observe phenomena, and drip H with iodimetric analysis 2O 2Sn in the solution of front and back 2+Content.The result is as shown in table 3 for the experiment gained.
Table 1: the test result of placing experiment
Figure GDA0000158074210000072
Table 2: the test result of heated constant temperature oxidation
Figure GDA0000158074210000081
Table 3:H 2O 2The promote the oxidation experimental result
Figure GDA0000158074210000082
Phenomenons such as binding force of cladding material detects: the coating that obtains according to foregoing invention carries out crooked test, and coating do not have bubble, come off; Carry out cut, coating does not all have peeling, explains that binding force of cladding material is good.
The high temperature resistance oxidation-resistance detects and electroplates resulting eleetrotinplate alloy components to electrolytic tinning liquid of the present invention, rack plating and barrel plating person, and through repeatedly toasting 2 hours down at 200 ± 5 ℃, coating surface all keeps original gloss, and non-foaming decortication.Repeatedly in 100 ℃ steam, tested 1 hour the equal no change of coating surface, non-foaming decortication.

Claims (5)

1. metilsulfate tin plating electrolyte; Comprise following composition: 30~120g/L stannous methanesulfonate; 60~180g/L methylsulphonic acid, 1~10g/L cerous sulfate, 0.1~2g/L inhibitor; 5~10g/L brightening agent and 5~15g/L tensio-active agent; Described inhibitor is Resorcino or catechol or both mixtures, and described brightening agent is LUTARALDEHYDE or benzylidene-acetone or both mixtures, and described tensio-active agent is polyoxyethylene octyl phenyl ether or sodium laurylsulfonate or both mixtures.
2. the tin plating method of steel band or steel plate is characterized in that: adopted metilsulfate tin plating electrolyte as claimed in claim 1.
3. the tin plating method described in claim 2, it is characterized in that: during plating, the transfer rate of steel band or steel plate is 3~9m/s, and plating temperature is 15~60 ℃, and current density is 6~20A/dm 2
4. the tin plating method described in claim 2 is characterized in that: before plating, steel band or steel plate are carried out degreasing and pickling pre-treatment.
5. the tin plating method described in claim 2 is characterized in that: steel band after the plating or steel plate are carried out soft heat, passivation and tin layer oiling aftertreatment.
CN2011100330718A 2011-01-31 2011-01-31 Methyl sulfonate tinning electrolyte and tinning method of steel strip or steel plate Active CN102162110B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011100330718A CN102162110B (en) 2011-01-31 2011-01-31 Methyl sulfonate tinning electrolyte and tinning method of steel strip or steel plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011100330718A CN102162110B (en) 2011-01-31 2011-01-31 Methyl sulfonate tinning electrolyte and tinning method of steel strip or steel plate

Publications (2)

Publication Number Publication Date
CN102162110A CN102162110A (en) 2011-08-24
CN102162110B true CN102162110B (en) 2012-08-01

Family

ID=44463554

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011100330718A Active CN102162110B (en) 2011-01-31 2011-01-31 Methyl sulfonate tinning electrolyte and tinning method of steel strip or steel plate

Country Status (1)

Country Link
CN (1) CN102162110B (en)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102605392A (en) * 2012-04-18 2012-07-25 吉安市荣泰电讯科技有限公司 Tin plating liquid with rear earth additive
CN103014786B (en) * 2013-01-22 2016-01-20 广州博泉环保材料科技有限公司 Electroplate liquid, its preparation method and apply the tin plating technique of this electroplate liquid
CN104087984A (en) * 2014-06-17 2014-10-08 宁国新博能电子有限公司 Tinning electrolyte of tinned copper wire for electronic component lead wires
CN104099649B (en) * 2014-06-25 2016-08-24 武汉钢铁(集团)公司 Passivator for electrolytic tinplate
CN104060308B (en) * 2014-06-30 2016-09-14 句容市博远电子有限公司 A kind of Pure Tin Plating Process liquid reducing dew copper phenomenon and application thereof
CN104988544A (en) * 2015-06-26 2015-10-21 吕小方 Electrolytic tinning annexing agent
CN105714347A (en) * 2015-09-30 2016-06-29 安徽中盛罐业有限公司 Tin case surface tinning process
CN105821452B (en) * 2016-05-19 2018-08-03 江苏兴达钢帘线股份有限公司 A kind of plating solution and electro-plating method of the Tin plating on copper wire
CN105970216B (en) * 2016-05-23 2019-02-22 江苏固格澜栅防护设施有限公司 The protective fence and preparation method on surface coating tin finishes surface
CN107675217A (en) * 2017-09-26 2018-02-09 安徽金星包装有限公司 A kind of can electroplating surfaces with tin technique
CN109596681B (en) * 2017-09-30 2021-07-09 上海梅山钢铁股份有限公司 Method for detecting uniform plating capacity of tin methanesulfonate electroplating solution
CN108754607A (en) * 2018-06-12 2018-11-06 广东光华科技股份有限公司 A kind of preparation method of electronic-grade sulfuric acid stannous crystal
CN110306213B (en) * 2019-07-08 2020-08-04 广州三孚新材料科技股份有限公司 Tin plating solution for solar cell and preparation method thereof
CN111188068A (en) * 2020-01-17 2020-05-22 肇庆宏旺金属实业有限公司 Black titanium plating method for whole roll of stainless steel
CN111705332B (en) * 2020-05-20 2021-07-20 上海应用技术大学 Simple electrodeposited Co-Ce/NF electrode material and preparation and application thereof
CN111647917A (en) * 2020-05-22 2020-09-11 成都宏明双新科技股份有限公司 Process for preventing tin-plated product from discoloring in high-temperature test
CN113957495A (en) * 2020-07-21 2022-01-21 宝山钢铁股份有限公司 Brightener for PSA (pressure swing adsorption) electrotinning insoluble anode system and application
CN112111763A (en) * 2020-09-30 2020-12-22 首钢集团有限公司 Preparation method of tin plate with high tin plating amount and product thereof
CN114507813A (en) * 2020-11-17 2022-05-17 上海梅山钢铁股份有限公司 Ultralow tin-plating layer cold-rolled electroplated tin steel plate and manufacturing method thereof
CN112538643B (en) * 2020-11-17 2022-05-13 珠海松柏科技有限公司 High-speed tin plating additive and tin plating solution

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7250080B1 (en) * 2006-09-06 2007-07-31 Tronox Llc Process for the manufacture of organosilicon compound-treated pigments
JP2009123463A (en) * 2007-11-14 2009-06-04 Sony Corp Positive electrode for lithium-ion secondary battery, method of manufacturing the same, and lithium-ion secondary battery
CN101608333A (en) * 2008-06-16 2009-12-23 吴昊 Titanium alloy electrochemical oxidation liquid
EP2176366A1 (en) * 2007-08-08 2010-04-21 PPG Industries Ohio, Inc. Electrodepositable coating composition containing a cyclic guanidine

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7250080B1 (en) * 2006-09-06 2007-07-31 Tronox Llc Process for the manufacture of organosilicon compound-treated pigments
EP2176366A1 (en) * 2007-08-08 2010-04-21 PPG Industries Ohio, Inc. Electrodepositable coating composition containing a cyclic guanidine
JP2009123463A (en) * 2007-11-14 2009-06-04 Sony Corp Positive electrode for lithium-ion secondary battery, method of manufacturing the same, and lithium-ion secondary battery
CN101608333A (en) * 2008-06-16 2009-12-23 吴昊 Titanium alloy electrochemical oxidation liquid

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
于锦等.铈盐对电镀锡参数和性能的影响.《表面技术》.2004,第33卷(第02期),62-63. *
倪光明,严怡芹,戴西林.酸性镀锡液稳定剂的优选.《安徽师范大学学报(自然科学版)》.1995,第18卷(第02期),72-77. *

Also Published As

Publication number Publication date
CN102162110A (en) 2011-08-24

Similar Documents

Publication Publication Date Title
CN102162110B (en) Methyl sulfonate tinning electrolyte and tinning method of steel strip or steel plate
CN102277601B (en) Cyanogen-free silver-plating electroplating liquid containing auxiliary complexing agent
CN102995077B (en) Cyanide-free alkaline bright copper plating solution and preparation method and electroplating process thereof
Jing et al. Effects of additives on nickel electrowinning from sulfate system
CN102758228B (en) A kind of sulfonic acid type semi-bright Pure Tin Plating Process liquid
CA2883815A1 (en) Plating solution and plating process for multi-layer cyanide-free plating copper-tin alloy coating, and coins made by the process
CN103014787B (en) A kind of copper electroplating liquid and electroplating technology thereof
CN102080241A (en) Low-concentration weakly alkaline cyanide-free copper plating and bath solution preparing method
CN102877114A (en) Stripping agent for stainless steel electroplating rack
CN104109885A (en) Weak-alkalinity pyrophosphate solution and technology for electroplating bright tin
CN110760904A (en) Cyanide-free alkaline cuprous copper plating additive
CN104499011A (en) Plating solution
CN105734622A (en) Cyanide-free copper plating solution and preparation method thereof
Abdel-Aziz et al. Electrodeposition of lead and lead-tin alloy on copper using an eco-friendly methanesulfonate plating bath
WO2022170803A1 (en) Electroplating solution for steel substrate direct cyanide-free plating under strong acidic conditions, and preparation method therefor
CN103388172B (en) A kind of method of quick judgement electroplating additive performance
CN102719864A (en) Method for preparing cerium-containing zinc coating
CN108570696A (en) A kind of acidic zinc nickel plating solution of resistance to high current density and its application
CN102383178B (en) Stripping solution for vehicle connector electroplated terminal plating
CN105018981A (en) Weldable gun color electroplating solution and electroplating method thereof
CN103695977A (en) Electroplating method capable of enabling tin coating to be level and preventing tin whisker from growing
CN103046090B (en) Additive capable of preventing copper replacement in cyanide-free alkaline coppering solution and preparation method thereof
CN114164466B (en) Alkaline electrogalvanized ferroalloy additive and electroplating solution
CN103108995B (en) Nickel pH adjustment method and equipment
CN107858712A (en) Water electrolysis pole plate nickel-plating additive

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20220420

Address after: 215000 Shuanglong Village, Fenghuang Town, Zhangjiagang City, Suzhou City, Jiangsu Province

Patentee after: Zhangjiagang Fenghuang Technology Development Co.,Ltd.

Address before: 215613 No. 288, fengma Road, Fenghuang Town, Zhangjiagang City, Suzhou City, Jiangsu Province

Patentee before: ZHANGJIAGANG NEW GANGXING TECHNOLOGY Co.,Ltd.

TR01 Transfer of patent right