CN104313602B - The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface - Google Patents

The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface Download PDF

Info

Publication number
CN104313602B
CN104313602B CN201410673616.5A CN201410673616A CN104313602B CN 104313602 B CN104313602 B CN 104313602B CN 201410673616 A CN201410673616 A CN 201410673616A CN 104313602 B CN104313602 B CN 104313602B
Authority
CN
China
Prior art keywords
board surface
solution
polar board
pole plate
temperature
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
CN201410673616.5A
Other languages
Chinese (zh)
Other versions
CN104313602A (en
Inventor
季利宏
刘世宇
董娜
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.)
State Grid Corp of China SGCC
Anyang Power Supply Co of State Grid Henan Electric Power Co Ltd
Original Assignee
Ningxia Cn-Sc Lighting Protection 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 Ningxia Cn-Sc Lighting Protection Co Ltd filed Critical Ningxia Cn-Sc Lighting Protection Co Ltd
Priority to CN201410673616.5A priority Critical patent/CN104313602B/en
Priority claimed from CN201210538399.XA external-priority patent/CN103088350B/en
Publication of CN104313602A publication Critical patent/CN104313602A/en
Application granted granted Critical
Publication of CN104313602B publication Critical patent/CN104313602B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Electroplating Methods And Accessories (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

The present invention relates to a kind of water electrolysis polar board surface processing method, concrete steps include: the polar board surface of carbon steel material is cleaned by A.;B. pole plate is immersed in 8min in the acid etching solution that temperature is 55 DEG C;The nitric acid that composition is 15wt% of described pre-etching solution, the ethanedioic acid of 3wt%, remaining is water;C. pole plate is immersed in 5min in the copper ion solution that temperature is 40 DEG C;D. pole plate is immersed in 8min in the caustic corrosion solution that temperature is 40 DEG C;E. pole plate is put in the strong acid solution of normal temperature and stir, remove the impurity of polar board surface;F., pole plate immersing 12min in the treatment fluid of 35 DEG C, rinses with clear water and dry after taking-up, polar board surface forms corrosion-resisting protective film.

Description

The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface
The application is divisional application, the invention and created name of original application: water electrolysis polar board surface processing method, application number: 201210538399.X, the applying date: 2012-12-13
Technical field
The present invention relates to a kind of surface to carbon steel pole plate carry out corrosion treatmentCorrosion Science and form the process of diaphragm, belong to field of metal surface treatment technology.
Background technology
Water electrolysis is to make water decomposite hydrogen or oxygen under galvanic effect.In a whole set of water electrolysis equipment, electrolytic cell is one of its most crucial device.Industrial conventional water electrolyser is laminated by rule by dozens of to up to a hundred electrolytic chamber as required and constitutes.Each electrolytic chamber is made up of positive plate, oxygen catalysis electrode, choke barrier film, insulated enclosure pad, hydrogen catalysis electrode, minus plate etc..Positive plate and minus plate generally use carbon steel steel plate to make.
Owing to the electrolyte of Strong acidic electrolyte composition has strong corrosivity to metal, so the electrolyte of the electrolytic cell potassium hydroxide that typically uses concentration to be 25% to 30% or sodium hydroxide solution.Under the effect of electric field, potassium ion or sodium ion move to negative pole, and hydroxide ion moves to positive pole, thus separate out hydrogen and oxygen.In order to reduce overpotential, reducing power consumption, the operating temperature of electrolytic cell is generally 85 DEG C to 90 DEG C.Carbon steel steel plate is easily caused alkaline etching by such alkali concn and temperature, so positive plate and minus plate must be carried out preservative treatment.Owing to the caustic corrosion resistance performance of pure nickel is the most excellent, at present, water electrolysis industry generally uses the carbon steel steel plate cathode-anode plate as water electrolyser of nickel plating.
Show, owing to the carbon steel pole plate of nickel plating actually and can not be completely coated with by plated nickel dam, nickel coating inevitably has micropore according to result of study.In pole plate is in the electrolyte that harmful ion is formed, these harmful ions can enter in the micropore of nickel coating, and is enriched with in micropore, with iron ion generation hydrolysis, forms the acid that corrosivity is extremely strong, persistently corrodes pole plate.Additionally, due to nickel coating is the coating of a kind of cathodic, the standard electrode potential of nickel is-0.25V, and the standard electrode potential of iron is-0.44V, and nickel coating and plain steel can form a pair galvanic couple, and electrochemical reaction will occur in they are simultaneously exposed to electrolyte.Iron in micropore is anode, loses electronics and is dissolved;Nickel outside is negative electrode, obtains electronics, and water electrolysis is released hydrogen.It follows that the possibility that the nickel plating carbon steel pole plate using general technology to make is corroded is very big.Once pole plate occurs that serious corrosion can cause hydrogen or oxygen gas to be gone here and there mutually, leak alkali and electrical short, it is more likely that set off an explosion, and threatens personnel and the safety of equipment.
Summary of the invention
The technical problem to be solved in the present invention is, proposes a kind of surface to carbon steel pole plate and carries out corrosion treatmentCorrosion Science and form diaphragm, can be effectively improved the water electrolysis polar board surface processing method of the corrosion resistance after pole plate nickel plating.
The present invention solves that the technical scheme that above-mentioned technical problem proposes is: a kind of water electrolysis polar board surface processing method, comprise the following steps:
A. the polar board surface of carbon steel material is cleaned;
B. pole plate being immersed in 5min to 15min in acid etching solution, polar board surface carries out acid corrosion, the composition of described acid etching solution is the nitric acid of 8wt% to 15wt%, the ethanedioic acid of 2wt% to 8wt%, and remaining is water;
C. pole plate is immersed in 3min to 8min in copper ion solution, iron and copper ion generation displacement reaction;
D., pole plate being immersed in 5min to 15min in caustic corrosion solution, polar board surface carries out caustic corrosion, described caustic corrosion solution is mixed by the sodium hydroxide solution of 10g/L to 30g/L and the sodium nitrate solution of 10g/L to 30g/L;
E. pole plate is put in the strong acid solution that concentration is more than or equal to 30%, remove the impurity of polar board surface;
F. pole plate is immersed in 10min to 20min in treatment fluid; diaphragm is formed at polar board surface; the composition of described treatment fluid is the complexon I of 5wt% to 12wt%; the complexing agent of 0.5wt% to 3wt%; the corrosion inhibiter of 0.2wt% to 2wt%; the surfactant of 0.1wt% to 0.5wt, the pH adjusting agent of 0.02wt% to 2wt%, remaining is water;The pH value of described treatment fluid is 3 to 6.
Above-mentioned complexing agent is one or more in sodium citrate, sodium lactate, natrium malicum.
Above-mentioned corrosion inhibiter is one or more in BTA, KI, methylbenzotrazole.
Above-mentioned surfactant is one or more in lauryl sodium sulfate, neopelex or n-octyl sodium sulphate.
Above-mentioned pH adjusting agent is one or both in triethanolamine, triethylamine.
Above-mentioned copper ion solution is copper-bath or the copper chloride solution of 150mg/L to 500mg/L.
Above-mentioned strong acid solution be temperature be salpeter solution, hydrochloric acid solution or the sulfuric acid solution of 25 DEG C to 50 DEG C.
The temperature of above-mentioned acid etching solution is 40 DEG C to 60 DEG C, and the temperature of described copper ion solution is 30 DEG C to 45 DEG C, and the temperature of described caustic corrosion solution is 30 DEG C to 45 DEG C.
The temperature of above-mentioned treatment fluid is 25 DEG C to 45 DEG C, and pole plate rinses with clear water after taking out from treatment fluid and dries, and drying temperature is 80 DEG C to 150 DEG C.
The present invention has positive effect: the water electrolysis polar board surface processing method of the present invention is first pole plate to be carried out corrosion treatmentCorrosion Science; diaphragm is formed again at polar board surface; corrosion treatmentCorrosion Science makes the micropore that the Surface Creation of pole plate is tiny, and surface becomes coarse, and beneficially diaphragm is preferably compounded on pole plate.During corrosion treatmentCorrosion Science; first carry out sour corrosion and generate micropore at polar board surface; carry out alkaline corrosion again in polar board surface and micropore, generate more tiny micropore; so that micropore is positioned at the position of deeper; the partial alkaline corrosive effect that displacement reaction occurs is more weak; so that the distribution of micropore more disperses, be conducive to increasing roughness, improve the composite effect of diaphragm.Treatment fluid, using complexon I as main component, using complexing agent, corrosion inhibiter, surfactant as auxiliary element, can form the diaphragm of densification, be effectively isolated iron and contact with nickel coating, effectively promote the corrosion resistance of pole plate on the surface of pole plate.Complexon I is made two by three carboxyls by respective oxygen and nitrogen can form complex compound with iron ion coordinating to four-coordination, and sequestering power is extremely strong;Addition complexing agent and corrosion inhibiter can improve the corrosion resistance of diaphragm further, and addition surfactant can significantly improve the surface tension of diaphragm and make pole plate diaphragm finer and close.The treatment fluid of the present invention does not use passivator, uses complexing agent, corrosion inhibiter the most too much, but use complexon I with low cost in a large number, production cost can be substantially reduced, be with a wide range of applications on the premise of ensureing quality of forming film.
Detailed description of the invention
Embodiment 1
The water electrolysis polar board surface processing method of the present embodiment, specifically comprises the following steps that
A. the polar board surface of carbon steel material is cleaned: sequentially pass through oil removing, washing, pickling process, will be attached to the greasy dirt of polar board surface, dust, corrosion etc. and remove.
B. polar board surface is carried out acid corrosion process.Pole plate being immersed in 10min in the acid etching solution that temperature is 60 DEG C so that polar board surface is tentatively corroded, form small pit, the diameter of pit is less than 10 μm.The composition of described acid etching solution is the nitric acid of 10wt%, the ethanedioic acid of 5wt%, and remaining is water.
C. polar board surface is carried out ion exchange process.Pole plate is immersed in 5min in the copper ion solution that temperature is 40 DEG C so that the part iron in polar board surface and pit and copper ion generation displacement reaction, separates out copper.Described copper ion solution is the copper-bath of 250mg/L.
D. polar board surface is carried out caustic corrosion process.Pole plate is immersed in 10min in the caustic corrosion solution that temperature is 30 DEG C so that in polar board surface and pit, form more more tiny pits.Described caustic corrosion solution is mixed by the sodium hydroxide solution of 20g/L and the sodium nitrate solution of 20g/L.
E. polar board surface is carried out de-sludging process.Pole plate is put in the strong acid solution of normal temperature and stir, remove the impurity of polar board surface, be then rinsed with clear water.Described strong acid solution be concentration be the salpeter solution of 30%.
F., pole plate immersing 15min in the treatment fluid of 40 DEG C, rinses with clear water and dry after taking-up, drying temperature is 90 DEG C.Polar board surface forms corrosion-resisting protective film.The composition of described treatment fluid is: the complexon I of 10wt%, the sodium citrate of 3wt%, the BTA of 1wt%, the lauryl sodium sulfate of 0.3wt%, and remaining is water, is 3 by triethanolamine regulation pH value.
Embodiment 2
The water electrolysis polar board surface processing method of the present embodiment, specifically comprises the following steps that
A. the polar board surface of carbon steel material is cleaned: sequentially pass through oil removing, washing, pickling process, will be attached to the greasy dirt of polar board surface, dust, corrosion etc. and remove.
B. polar board surface is carried out acid corrosion process.Pole plate is immersed in 15min in the acid etching solution that temperature is 50 DEG C.The nitric acid that composition is 8wt% of described pre-etching solution, the ethanedioic acid of 8wt%, remaining is water.
C. polar board surface is carried out ion exchange process.Pole plate is immersed in 8min in the copper ion solution that temperature is 40 DEG C so that the part iron in polar board surface and pit and copper ion generation displacement reaction, separates out copper.Described copper ion solution is the copper-bath of 200mg/L.
D. polar board surface is carried out caustic corrosion process.Pole plate is immersed in 5min in the caustic corrosion solution that temperature is 35 DEG C so that in polar board surface and pit, form more more tiny pits.Described caustic corrosion solution is mixed by the sodium hydroxide solution of 10g/L and the sodium nitrate solution of 30g/L.
E. polar board surface is carried out de-sludging process.Pole plate is put in the strong acid solution that temperature is 40 DEG C and stir, remove the impurity of polar board surface, be then rinsed with clear water.Described strong acid solution be concentration be the hydrochloric acid solution of 40%.
F., pole plate immersing 20min in the treatment fluid of 25 DEG C, rinses with clear water and dry after taking-up, drying temperature is 80 DEG C.Polar board surface forms corrosion-resisting protective film.The composition of described treatment fluid is: the complexon I of 8wt%, the sodium lactate of 1wt%, the KI of 0.5wt%, the neopelex of 0.2wt%, and remaining is water, is 4.5 by triethylamine regulation pH value.
Embodiment 3
The water electrolysis polar board surface processing method of the present embodiment, specifically comprises the following steps that
A. the polar board surface of carbon steel material is cleaned: sequentially pass through oil removing, washing, pickling process, will be attached to the greasy dirt of polar board surface, dust, corrosion etc. and remove.
B. polar board surface is carried out acid corrosion process.Pole plate is immersed in 8min in the acid etching solution that temperature is 55 DEG C.The nitric acid that composition is 15wt% of described pre-etching solution, the ethanedioic acid of 3wt%, remaining is water.
C. polar board surface is carried out ion exchange process.Pole plate is immersed in 5min in the copper ion solution that temperature is 40 DEG C so that the part iron in polar board surface and pit and copper ion generation displacement reaction, separates out copper.Described solion is the copper chloride solution of 300mg/L.
D. polar board surface is carried out caustic corrosion process.Pole plate is immersed in 8min in the caustic corrosion solution that temperature is 40 DEG C so that in polar board surface and pit, form more more tiny pits.Described caustic corrosion solution is mixed by the sodium hydroxide solution of 30g/L and the sodium nitrate solution of 15g/L.
E. polar board surface is carried out de-sludging process.Pole plate is put in the strong acid solution of normal temperature and stir, remove the impurity of polar board surface, be then rinsed with clear water.Described strong acid solution be concentration be the salpeter solution of 40%.
F., pole plate immersing 12min in the treatment fluid of 35 DEG C, rinses with clear water and dry after taking-up, drying temperature is 120 DEG C.Polar board surface forms corrosion-resisting protective film.The composition of described treatment fluid is: the complexon I of 12wt%, the natrium malicum of 2wt%, the methylbenzotrazole of 0.5wt%, the n-octyl sodium sulphate of 0.2wt%, and remaining is water, is 4 by triethanolamine regulation pH value.
Use common process to carry out nickel plating on the pole plate of the water electrolysis polar board surface processing method through embodiment 1 to 3, then carry out salt spray test.Sample being put into salt spray test chamber, uses the NaCl solution of 5%, humidity is 70%, and temperature is 50 DEG C, and persistently spray every day 8h, and continuous 10 days, polar board surface was without obvious corrosion phenomenon.

Claims (1)

1. a water electrolysis polar board surface processing method, comprises the following steps that
A. the polar board surface of carbon steel material is cleaned;
B. pole plate is immersed in 8min in the acid etching solution that temperature is 55 DEG C;The composition of described acid etching solution is the nitric acid of 15wt%, the ethanedioic acid of 3wt%, and remaining is water;
C. pole plate is immersed in 5min in the copper ion solution that temperature is 40 DEG C so that the part iron in polar board surface and pit and copper ion generation displacement reaction, separates out copper;Described copper ion solution is the copper chloride solution of 300mg/L;
D. pole plate is immersed in 8min in the caustic corrosion solution that temperature is 40 DEG C, polar board surface is carried out caustic corrosion;Described caustic corrosion solution is mixed by the sodium hydroxide solution of 30g/L and the sodium nitrate solution of 15g/L;
E. pole plate is put in the strong acid solution of normal temperature and stir, remove the impurity of polar board surface, be then rinsed with clear water;Described strong acid solution be concentration be the salpeter solution of 40%;
F., pole plate immersing 12min in the treatment fluid of 35 DEG C, rinses with clear water and dry after taking-up, polar board surface forms corrosion-resisting protective film;The composition of described treatment fluid is: the complexon I of 12wt%, the natrium malicum of 2wt%, the methylbenzotrazole of 0.5wt%, the n-octyl sodium sulphate of 0.2wt%, and remaining is water, is 4 by triethanolamine regulation pH value.
CN201410673616.5A 2012-12-13 2012-12-13 The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface Expired - Fee Related CN104313602B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410673616.5A CN104313602B (en) 2012-12-13 2012-12-13 The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201410673616.5A CN104313602B (en) 2012-12-13 2012-12-13 The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface
CN201210538399.XA CN103088350B (en) 2012-12-13 2012-12-13 Water electrolysis pole plate surface treatment method

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CN201210538399.XA Division CN103088350B (en) 2012-12-13 2012-12-13 Water electrolysis pole plate surface treatment method

Publications (2)

Publication Number Publication Date
CN104313602A CN104313602A (en) 2015-01-28
CN104313602B true CN104313602B (en) 2016-08-24

Family

ID=52368907

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410673616.5A Expired - Fee Related CN104313602B (en) 2012-12-13 2012-12-13 The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface

Country Status (1)

Country Link
CN (1) CN104313602B (en)

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61276982A (en) * 1985-05-30 1986-12-06 Nec Corp Plating method for magnesium alloy
JP3192003B2 (en) * 1992-10-02 2001-07-23 三井金属鉱業株式会社 High corrosion resistance coating method for magne-based alloy
CN100398700C (en) * 2004-06-24 2008-07-02 侯文清 Surface cladding treatment of ferro-manganese aluminium alloy
CN100408725C (en) * 2005-12-30 2008-08-06 东北大学 Process for compound surface sheilding of metal magnesium and magnesium alloy
CN102021552A (en) * 2009-09-21 2011-04-20 邵阳市创捷化工有限公司 Modifier for black metal surface matrix and production method thereof

Also Published As

Publication number Publication date
CN104313602A (en) 2015-01-28

Similar Documents

Publication Publication Date Title
CN103088333B (en) Water electrolysis pole plate surface treatment liquid
Lei et al. A study of chromium-free pickling process before electroless Ni–P plating on magnesium alloys
CN102234800A (en) Aluminum alloy rare earth passivating liquid taking chlorine salt as accelerator and use method thereof
CN103088375B (en) Water electrolysis pole plate nickel plating additive
CN103147112B (en) A kind of electrolytic solution and for the preparation of the purposes of nuclear fuel rod zirconium alloy cladding micro-arc oxidation films and method
CN103088358B (en) Surface treatment method before water electrolysis pole plate plating
CN104313601B (en) Water electrolysis polar board surface processing method
CN104313602B (en) The water electrolysis polar board surface processing method of diaphragm can be formed at polar board surface
CN104451724B (en) The water electrolysis polar board surface processing method of the corrosion resistance after pole plate nickel plating can be improved
CN104451707B (en) The water electrolysis polar board surface processing method of protecting film can be formed
CN104451687B (en) Polar board surface processing method
CN104451647B (en) Lower-cost water electrolysis polar board surface processing method
CN104404535B (en) The water electrolysis polar board surface processing method of corrosion resistance can be improved
CN104694937B (en) A kind of micro- alkalization transitional period heat exchanger electrochemistry induction filming method of recirculated cooling water
CN107190288A (en) A kind of preparation method of HEDP copper facing imporosity thin layer
CN104532266B (en) Corrosion resistant water electrolysis polar board surface processing method
CN103088350B (en) Water electrolysis pole plate surface treatment method
CN104532267A (en) Surface treatment method for electrode plate
CN103046051B (en) Surface corrosion processing method before water electrolysis pole plate plating
CN100336143C (en) Method for removing residual copper of aluminium corroding foil surface of negative electrode for aluminium electrolytic capacitor
CN104087985A (en) Copper coating method of metal part
CN108796583B (en) A kind of preparation method of the super-hydrophobic passivating film of Pure Iron Surface corrosion resistance
CN111719144A (en) Preparation method of zirconate passivation film
CN110468400A (en) A kind of aluminum alloy surface environmental protection passivating method
CN102242367A (en) Multifunctional novel ethylene diamine tetraacetic acid (EDTA) cleaning corrosion inhibitor

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
C41 Transfer of patent application or patent right or utility model
CB03 Change of inventor or designer information

Inventor after: Gao Xiaogang

Inventor after: Ji Lihong

Inventor after: Liu Shiyu

Inventor after: Dong Na

Inventor before: The inventor has waived the right to be mentioned

COR Change of bibliographic data
GR01 Patent grant
TA01 Transfer of patent application right

Effective date of registration: 20160801

Address after: 750002 the Ningxia Hui Autonomous Region Jinfeng District of Yinchuan city Ning Street No. 490 Yinchuan IBI incubation center two building 6 room 1401

Applicant after: NINGXIA CN-SC LIGHTING PROTECTION CO., LTD.

Address before: 213022 Jiangsu Province, Changzhou New District No. -701 26- Ding Long Jin Lu BaiCaoYuan

Applicant before: Wu Xiaozai

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20181017

Address after: 100032 West Chang'an Avenue, Xicheng District, Xicheng District, Beijing

Co-patentee after: ANYANG POWER SUPPLY COMPANY, STATE GRID HENAN ELECTRIC POWER CO., LTD.

Patentee after: State Grid Corporation of China

Address before: 750002 Yinchuan, the Ningxia Hui Autonomous Region, Jinfeng District, Ning'an Street 490, Yinchuan IBI breeding center two phase 6 Building 1401 room.

Patentee before: NINGXIA CN-SC LIGHTING PROTECTION CO., LTD.

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160824

Termination date: 20181213

CF01 Termination of patent right due to non-payment of annual fee