Surface Cleaning Engineering
Transcript of Surface Cleaning Engineering
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Selec A Tade Name
Selec A Applicaion
Selec A Poce
Technical
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MFSA Qualit Metal Finishing Guides
Chemical Surface Preparation For Electroplated and Metallic Coatings
INTRODUCTION
This Quality Metal Finishing Guide deals with pretreatment of surfaces for metallic
coatings. In this context, pretreatment is defined as the process of substrate preparation
specific metallic coating.
Generally, the objective of applying a metallic coating is to provide one or several new pbasis metal. Coatings include decorative finishes such as copper or brass on zinc diecast,
coatings such as hard chrome or electroless nickel on aluminum, or corrosion resistant zi
steel.
Regardless of the function, these coatings all must adhere completely to the basis metal
provide the decorative or functional properties required. Plate adhesion must exceed the
strength of either the substrate or the electroplate. In other words, an attempt to peel t
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caig f he bae hd ee a ae f he bai ea ih eaai
f he bae a he bda. I aig, hi ee f adhei i ibe beee
he bae ad he aed ea.
Whaee he echai, adhei deed he cdii f he face beig aed
heefe, ci f he ciica e ed i he ea f a deiabe caia
iefee ih he ie-aic adhei. Tica caia ae i ch a i, ge
ide ad cae.
Peeae a affec he caig eie. Ee if adhei i eced iiia, b
ig , e i dei, ad faie de hdge ebiee ccig a a
be eaed face eaai.
Peae faie eig f ci ca be aided b efec face ea
cee ceage b he ecified caig. Aie ad he idie e he
aed ce i idig g-e dc-eface aaie.
The ia eeci f a gie eeae ce i dicaed b fac.
1. THE METAL BEING PROCESSED AND THE CLEANING SOLUTION
Geea, ee ad ce ca ihad g aaie ceae (H 10-14), ad aci
50% hdchic acid, ih ie aac f he bai ea. Be ad ba ei
(H 9-13) ad e eeae ee he eecie ea f he ic f he
(deicificai). Zic ad ai eie e ide ihibied aai (H 9-12) ad
Piea fai ae aaiabe ee hee eed.
2. THE TYPE OF SOILS TO BE REMOVED
Si i a bace he face f he ea ha i iefee ih he ea-fiihi
efed. Si a be he e f ieia aicai he ea f a aeia h
ea ig, hadig, ad ee high eeae he ahee.
Geea eaig, he e f i ca be be d i bad caegie: g
igaic.
a. Oganic
OSP Fia Fiih VeificaiPga
Ehe Ai DeieFcci, Maage f e-
Maeig Cicai
Ne Achie
Safe Hab CiaceREACh
C G
C Eecic
Aha
Seicdc
Pacagig
EheA.c
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Saifiabe aia ad egeabe i.
Uaifiabe iea i ad ae.
Miceae caia eihe fed i i (eaic a fed i he b
ihibi f ceai acid icig i edeiig he ea.
b. Inoganic
Scae ad , ide ad eaic eide.Pihig cd, abaie, gidig ad ihig eide gi.
Miceae h d ad deig fe.
Thee ae a fe f he i eceed. Se f he he icde ai, ceai
a ae-i-i ei, figei, ad igaic caig ch a hhae, ch
eeaie.
Ma f he bica, ca ad ci eeie ed da ae be e
i ae be ceaed i a id, -caic-da-caiig aaie ceae a efac, a ae-be bica ca be eed aia b a a ae e-ie,
edcig ceae caiai ad iiiig ceaig be. Paicae ae i
eadi eed b id, -eeae ceaig.
MECHANISMS OF SOIL REMOVAL
M ceaig ad i ea i accihed b e e f he fig echai
1. WETTING
The ce b hich he ceae, hgh he e f face-acie age, e hebd b he diacee f i ad he eig f face ad iefacia ei. We
i he fi eiee f ceaig ied ea.
2. EMULSIFICATION
Oce eig ae ace, he ce f eificai ca cc. Thi i he diei
iicibe iid. Eificai i deede he i eceed ad he chice f
ecdai fac ch a H, eeae ad agiai.
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3.SAPONIFICATION
The eaci f fa acid ih h aai dce be eifiabe a. Ea
aificai f bffig cd ad eaae daig cd.
4. SOLUBILIATION
The ce b hich he bii f a bace (i) i iceaed i a ceai edi,
he e eeci f face acie age. Ma i ed da ae, i fac, ae
5. DEFLOCCULATION
The ce heeb he i i be i e fie aice ad dieed i he cea
i i he aiaied a a diei ad eeed f aggeaig ad eeig
beig ceaed.
6. SEQUESTRATION
The ce i hich deiabe i ch a Ca++ Mg++ ad hea ea ae "ie
deaciaed, heeb eeig he f eacig ih aeia ha a d f
dc. The caic eae i he had ae c fed he a heic de
ed. The c fed i he eaci beee a ad he Ca++ Mg++ i i hahe ae i feed, he Ca++ ad Mg++ i ae "ied " eeeed, eeig
eacig.
7. MECHANICAL ACTION
Thi i a eee ia fac i ea ceaig, ice i ca gea iceae he
efficiec f i ea. Mechaica aci ca be accihed b i ee
he ief. Se e f i agiai ae ai, echaica, aic, a a
f eecic ceaig. Ai agiai i a efficie a he he ehd.
CLASSES OF CLEANERS
Ceae fi i hee g - e, ei-ae ad ae.
1. SOLVENT-BASED CLEANERS
Bh a degeaig ad e iei ae beig haed eiced a a e
cce ad eiea egai.
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2. SEMI-AQUEOUS OR DIPHASE CLEANERS
Thee ae ei f ae, gaic e ad eifie. The hae iied aic
ie, ice he eie ecda ae ceaig e.
3. AQUEOUS CLEANERS
Cie he age g ad ca heee be fi i hee caegie: acid, e
ceae:
a. Acid Cleane
Baed cceai f gaic igaic acid ch a ciic ad hhic.
he igh ea ide ae ee. The e f acid ad addiie acage ed deed
ea, e f i ad bee ceig. Aicai f acid ceae icde bff
ba hee ii aac f he face i eaed.
b. Neal cleane (alo called deegen cleane)
Neihe acid aaie baed. The a ci f eeeig age, diea
age ad eig age. High cceai ad eeae ae hei e iie
c. Alkaline cleane
The he f he id. The ae ea e, eaie afe ad ea c.
e feibe ad hae bade eaig ii ha he ceae. Aaie ceae a
cheica ha ide aaie cdiiig, aificai f fa i ad i e
Geneal chemiie ed in alkaline cleane:
Caic alkali - ide he highe ee f aaii, ih eaab c. The
ad he de f aac ie. The ide ecee aaii he ed i e
Cabonae - ide bffeig, ie e ad fe ae b eciiai. Deedig
ide a ide age f aaii. Cabae ca cae caig i had ae aea if
ied ih he ae-feig age.
Silicae - ae ce he caic aai i e f aaii. The ae gd bffe, e
eifie ad he i i edig. Siicae be e ied i acid di
ee ibe i icic acid ge f fig.
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Phophae - ide ae feig, id aaii ad e bffeig. The ae
eig age, ehacig he ea ceaig effec.
ETTING AGENTS (SURFACTANTS)
Weig age ae ciica he fci f ceae. Thee gaic aeia
e f haig ae eeig (hdhbic) ad ae aacig (hdhiic)
ece. Thi aagiic effec a f he eeai f hee aeia a he caia-ea face), ieface, heeb faciiaig ea ad biiai f
C faca ed i ceae ae:
Anionic - hich ide gd deegec. The ae a gd cig age f he
Sa i a eae f a aa deied aiic faca. Aiic faca ae ge
fae.
Nonionic - ae heic aeia ad ae gd eifie. I addii, he ae ed
eed ceae ad f fa c i a ceae. The bii f iic fa
ceaig i deceae ih iceaig eeae ad cceai. Thi i caei. Whe a aaie ceae caiig iic faca i eaed abe he e
eeae ad cceai, he faca bece ae ibe ad begi ac
iei ceae hi i deiea ad ca cae he f he faca hgh
I a a ceae, -cd-i iic faca ae fe ed a defae.
Amphoeic - ae iia aiic faca he ed i aaie ceae. The
abii i g aaie iid. Aheic faca be e ied i
acid, hich i ce he caiic fi fe.
Caionic - faca ae fi fe ad ae ed i ecia aaie ceae ad a i
acid.
ALKALINE DESCALING
Aaie decaig i a ecia e f ceaig ha i deiged ee igh ide a
fe bae. The ceae ae baed high aaii i cbiai ih ce
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chelating agents. Used at 168.8-185F, alkaline descalers are capable of dissolving light
by immersion.
One or more additional cleaning actions as described under Mechanism of Soil Removal
involved in soak cleaning applications. Removal of buffing compounds, for instance, requ
saponification, emulsification and deflocculation. On the other hand, if the emphasis is o
skimming of oils from cleaners, displacement, rather than emulsifying type cleaners are
with chemicals that provide good wetting characteristics.
METHODS OF SURFACE PREPARATION
A total surface preparation process consists of one or several operations. They are carrie
sequence designed to produce an optimum condition for the application of the intended c
steps are typically classified in accordance with their particular cleaning mechanism,
as follows:
1. MECHANICAL CLEANING (spra and ultrasonic)
2. SOAK CLEANING3. ELECTROCLEANING
4. ACID ACTIVATION
While some pretreatment processes call for soak cleaning followed by acid activation, oth
all or most of the above operations.
1. MECHANICAL CLEANING
Mechanical cleaning in the context of surface preparation for metal coating encompasses
ultrasonic cleaning. Mass finishing is also used, but is described in detail in a separate Q
Mechanical cleaning relies in great part on mechanical energy in physically removing soilsurface. To assist the removal process, detergents, alkalis or acids, deflocculants and so
Heat also helps, although low to moderate solution temperatures are the norm.
a. Spra Cleaning
This is a very common cleaning technique, often used in dedicated spray machines, or b
within a plating line. Primps deliver cleaning solutions through spray nozzles at pressure
20 to 200 psi. Some high-pressure systems can produce 800 psi or more. The cleaning s
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recirculated through a reservoir, which is usually fitted with heaters, oil skimmers, and l
Spray-cleaning solutions are formulated with low or non-foaming detergents. Since the
relies mostly on the spray-impact energy, the solution concentration is kept relatively lo
temperature. Spray cleaners are designed for specific applications, taking into account th
being processed and types of soils to be removed.
Mild acid or alkaline cleaners are used on nonferrous and highly finished metals, e.g., bu
aluminum. Stronger cleaners, incorporating rust inhibitors, are used on ferrous metals, i
alloys. Typical soils removed by spray cleaners are buffing compounds, heavy oils, drawi
compounds. Parts that benefit from spray cleaning include cabinets and other geometric
deep corners and recesses. For superior cleaning, turbojet nozzles are used inside an im
Parts may be cleaned in stationary positions or on conveyors moving across banks of spr
positioned to reach all areas to be cleaned. Spray cleaning may be single or multiple stat
rinsing, inhibiting and drying or other surface-preparation steps.
b. Ulaonic CleaningUltrasonic cleaning takes place when small vacuum cavities caused by high-frequency so
traveling in a liquid implode against surfaces submerged in the liquid. Transducers attac
or bottoms of cleaning tanks supply the ultrasonic waves to the cleaning solution. Tempe
140-160F should be avoided, as they tend to reduce the ultrasonic efficiency.
When this technique is used with a water-detergent solution, the scrubbing action that r
surface is effective in removing various contaminants, especially insoluble particles, smu
that are difficult to remove by conventional wetting or emulsification. It does not, howev
remove oils, which is why it is used after degreasing.
2. SOAK CLEANING
Cleaning by immersion is intended to remove the bulk of the soils, particularly those tha
mechanically deposited on the surface. Examples of such soils are cutting fluids, grease,
buffing compounds. There are various types of soak cleaners designed for different clean
By saponification of fatty acids such as those encountered in buffing compounds,
and drawing compounds. Saponification relies on the level of alkalinity available i
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ad i ed b high eeae.
B eificai f i, geae, fa acid ad hei deiaie. Thi i acc
he e f ecia faca bed ad ceai aai ch a iicae.
B diacee f i ad geae, hgh he e f ecia faca. Di
he i be eai ied he faca a he ea face, hee he
eeaed a he face f he i. Effecie ie be ed ih c
ee dag f eeaed i he . Thee ceae a eie e
ice he ae eai aaed ih i.
3. ELECROCLEANING
Eecceaig i a ia e i ea-face eaai. I i a eecic
chaaceied b he e f diec ce ad a ecia faed eece. The
ceed a be eecica ceced a he ade, cahde, bh (aeae), de
aicai.
Ahgh eecceaig i a diffee ad diic ehd f face ceaig, i hd
iega a f he eae cce.
Eecceae a decibed hee ae aaie, ad i geea f aaie a ce
ecede acid aciai i he eae cce. Thei baic fci i ee i ha
eed b ie a ceaig degeaig. Eae f ch i ae a f:
Figei, daig cd, ad i die i face i aied
Fie diided aice ch a ihig abaie, eaic fie f gidig
eai, cab ad he aig eee. Ofe hee fie aicae a
efeed a , a be hed he face b ie echaica fce, eec
i a hi i geae ai.Mea idai dc, he e f ee he ahee, a he
a hea eae, fgig, edig, ec.
Ahgh eecceaig a a ee a aica e f i, i cdii
i f eaie ea i he bee e i he cce. F iace, a adhee i
eed egh be ifed i he fig ie a. Sface ide a be edced
e be f be eai died i he acid a.
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a. Electrolsis of Electrocleaners
A ce i aied a eecceae, he fig eeccheica eaci ae
eecig ae. The aai ee a he cdcie edi.
A he Ade: 4[OH]- --> 2H20 + 02 + 4e
A he Cahde: 4H20 + 4e --> 4[OH] + 2H2
A ca be ee, ice a ch hdge i ibeaed a he cahde a ge a he a
b. Tpes of Electrocleaners
Eecceae ae caified he bai f ai ieeaed cieia:
Pai f he i he a.
Te f bae beig eaed.
Anodic ElectrocleaningThe i ceced he iie (ade) ide f he ecifie. Thi ce i a
eecceaig, ice he ai i ie ha i eecaig. A decibed de
ge i ibeaed a he face f he (he ade) he ce i aied. A h
, i ceae a echaica cbbig aci ha e ad if he i.
T he heea a ae ace. A ge bbbe ae fed he face, he
g befe he ie i ci ae. I i beieed ha he aic chage hdig fi
he face i eeaed hgh he ae f bbbe, faciiaig i ea hgh h
aci. Thi hee a aie he he de f eecceaig.
Cheica effec, idai ad d i H a ae ace a he ade face. If ece
idai ca be ee ch ea a ba, ic ad ie, a he dic, ai
ihibied adic eecceae ae aaiabe f ba ad ic.
Whe ice i adica eaed, i i ic aiae ad ee aig i f
eaciaed.
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A iia effec i eeieced ih aie ee. Rega ee ae adee affe
eecceaig, heea high-cab ee ae e eiie ad eie deai.
ice ad ie ae aaced aihed b adic eecceaig.
A ge i ibeaed a he ade, he e H ae ed iceae a he ieface.
be iced ee if a eecceae' aaii i b deig a a e f
aieace. The ee i e aid idied, ad eciiaed i hdide f
Pa eiig he a i hae a eched aeaace, eecia i high-ce-
The iai ca be eadi ecified b iceaig he aaii f he bah b edci
dei be a eaig ee.
Cathodic Electrocleaning
The i ceced he egaie eia (cahde) ide f he ecifie. Thi i a
diec eecceaig. I hi cae, hdge i ibeaed a he cahde. Tice a ch
ge i geeaed. Cee, e cbbig aci ad ceaig abii ae ee
eecceaig, hee, ha fd a ideead e i id f ea:
ab hdge ebiee a a e f ci hdge eeae a he face; aae f chaged iiie f he i he cahdic face. The ae
eceibe he caa bee a he a ei he a, b ead adhei
eecdei. Caia eadig ch adhei faie ae eaic fie, ceai
faca, cid, eaic a ad dagged-i heaae che.
Cahdic ceae, he e cea ad e aiaied, ae ed f ceig bffed
hie ea, ih aihig, ad f eecceaig ice ad high ice ee i
aiai. Whe ed ee ad ce ae adaage f hei ei cb-c
ecda adic eecceae hd f, if ee f a fe ecd. Thi eiiie ha a hae deied he b cahdic aci.
Periodic-Reerse Electrocleaning
Thi ehd f eecceaig f fe ea e a cbiai f bh adic ad
ceaig. A eidic-eee i ( a P.R.) i iaed he ecifie' . Th
ichig echai ha eee he ai a ced ad ied iea. The
ae aeaig adic ad cahdic aiie f he ecified ceaig ie.
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A ica eig i 10 ec. cahdic - 10 ec. adic. B chagig he eig, e cah
a be ed effec ai ceaig. The i ca be gaed ha he a
adic befe he ie eig h ff he ecifie. Thi ee ea f a chage
a hae aed he dig cahdic ceaig.
The ci idai ad edci a he face ce he ide ad cae
be f ha ae iced b caide cheaig age bi i he ceae f
PR ceae eea bece aaed ih died i ide ad be eace
acica, he ca be egeeaed b aig he i cahdica. PR. ceaig i e
decaig ad deig high egh ad ig ee ih he e f decaig acid
heeb cig hdge ebiee. (ASTM B242 dea ecifica ih he a
eceded f he eaai f high cab ee f eecaig iiie hd
ebiee).
c. Operating Parameters and Process Considerations
A eaied eaie, eeci i he ai diig ce i eecceae. The a
eibe f he cbbig aci a he eecde i a fci f he a f chgh he ce. Theefe, hee aaee cig ce hd be cideed:
Solution Conductivit
Thi i i a fci f ceae cceai ad eeae a a gie age. T
cceai ad eeae, a acica ee, he highe he cdcii ad
gaig ad cbbig aci.
Vage Aied-Ce iceae ih age, ahgh he ae i e ai
V. Highe ae ae cae "big" ghe a.
Surface Area Being Cleaned
The face aea beig ceaed eecica ad he a f ce aied e i
ce dei (CD). I i eaed i aee e ae f (af). Ce dei a
efficiec.
Adeae eceded CD age f diffee bai ea ae aied i Tabe I.
ae dce igh agia eecceaig. Highe ae geea ead echi
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f he face.
Ade cahde aea ai f 1:1 ae adeae f aicai. The ai i
he ecified ce deiie ae aiaied.
TABLE I: Recommended Electrocleaning Current Densit-Rack Applications
A/f2 Pai
(A=Adic, C=Ca
See, -cab 47-93 A,C
See high egh 28-47 A
Saie ee 47-74 C
Ce 47-74 A, C
Ba 19-37 A, C (adic ihib
Zic dieca 19-37 A, C (adic ihib
Nice ad i a 19-28 C
Lead ad i a 47-74 C
Sie ad i a 19-28 C
*In barrel applications, a fraction of the above C.D. values should be epected.
Selection and Use of Electrocleaners - Thee ae geea cideai i he eeci
e f eecceae:
Formulation - Seea iea fai ae aaiabe, ceig a ide age f
Thee fai hd ide he fig eie:
A iabe degee f aaii f he ea ceed, e.g., high aaii f e
ad ba.
A e ai f hdide iicae ee ibe iicae fi f adhe
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and affecting plate adhesion.
TABLE II: Tpical Operating Conditions for Electrocleaners
Steel and Copper Brass Zinc Ni
Alkalinity, g/L
(as NaOH)
50-100 15-20 15-20 30-
Temperature F 140-195 120-160 120-160 120
Time, seconds 1-5 1-3 1-3 1-5
The above are typical average operating conditions. Suppliers of proprietary electroclean
specify optimum operating parameters for specific applications. Alkalinity expressed as N
represent from 20 to 80% of the total product formulation.
Equipment Maintenance and Operation-Corrugated or mesh steel can be used as anodes
provide optimum surface area and solution circulation. Periodic cleaning of the anode/canecessary to remove plated-on smut, oxides and other charged particles. Using the tank
cathode is not recommended, as it leads to uneven current distribution and provides a s
current. Many electrocleaning problems, such as under- and over-cleaning, have been tr
such a practice.
Solid polypropylene or plastic-lined steel tanks are recommended for alkaline electroclea
should be fitted with steel, stainless steel or Teflon heaters. Recirculating pumps are rec
provide solution recirculation, overall homogeneity, and to prevent stratification. It shou
solution inlets and outlets must be located at two opposite diagonal top and bottom corn
for efficient solution movement.
TABLE III: Most Common Electrocleaning Problems
Problem Probable Causes
Etching, tarnishing
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Too high C.D.
Cleane non-inhibied fo nonfeo
Wong polai
Tempeae oo high fo nonfeo
Eceie oil in olion
Roghne Cleane oo eak, caing bn o
C.D.
In anodic cleaning: plling alloing
face
In cahodic cleaning: depoiing ch
and m on face
Incomplee ining of elecocleane
Hae nde plaeCleane empeae oo high, ca
film.
Cleane oo eak
Incomplee ining afe cleaning
Inefficien oak o pecleaning pioelecocleaning
Heaalen chome conaminaion
Poo adheion, blie, piing of plaeCleane oo eak
C.D. oo lo o oo high
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Cleaning ime oo lo o oo high
Reee of inended polai
Heaalen chome conaminaion
Infficien ining afe cleaning
Eceie oil, geae in cleane
4. ACID ACTIATION
Acid aciaion i ed o aciae he face of a meal afe alkaline pa, oak, o el
ch, he acid nealie eidal alkalini a ell a objecionable oide, and epoe
eadil plaeable face.
Thi poce i ed o emoe chemicall fomed oil fom he meal face. Tpicallmeal oide and hei al. The fom a a el of epoe o high empeae, o
amophee. Eample ae hea-eaing oide and cale, foging and caing cale,
oidaion.
Alhogh ome of hee oide ae plaeable, he lead o poo plae adheion and coo
Oide emoal i geneall caied o b acid eamen.
The acid ae eleced accoding o he meal being poceed, o ha limied o no aa
meal occ.
Thee ae hee majo pe of acid aciao:
Oganic and Mild Mineal Acid- Eample ae glconic, phophoic, and ciic acid.picall ed o aciae highl polihed o eniie meal ch a alminm, ba an
diecaing, and ome polihed eel.
Sfacan and eing agen ma be ed o edce he face enion and impoe
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Mineal Acid - Hdchic ad fic acid ae eae f g iea acid. Th
geea ed decae ad aciae ee ad e aie ee.
Niic acid b ief i cbiai ih fic ad hdfic i ed de a
ai ad i a.
Fbic ad hdchic ae ed eaded ee ad eaded ba. Cbiai f
ad hdchic ae eie ed i decaig ad bigh diig ce ad ba, a
geeae hea ige ide fe ad be haded ih eee cae. Secia
ad ihibi a be ed ih hee acid diee i geae eide, ie
face aciai, ad f iiiig aac f he bai ea.
Acid Sal - Acid a ae ica f he fae e, baed aia eaied
eaiig hdge i i he a ide fficie acidi aciae ea face.
Adaage f acid a icde afe hadig ad he feibii cd he ih
faca ad ihibi dce a ide age f ecia acia.
Cd acid a a, f eae, icde fide ad ihibi ha ae e effe
ad ea f fe ea, e ihibi aac f bai ea. The ae gee
ad e cie a eie.
The e f acid acia f caef cideai. The eeced acid
aac he ea beig ceaed, a hi a gie ie fai, iig ad g
bee caig.
The e f acid ed a be caibe ih he aig ce. Hdchic acid
be ed i acid ce aig. Chide caiai ca ei affecha aig bah. Lieie, fic acid i eceded f ead eaded a, a
ibe ead fae he face f a.
Ue f g iea, ihibied acid hd be eiced ig- ad high-cab
eaci ih ch acid ead hdge ebiee.
Acid acia i eae cce a be ed b ie di iei, eecic
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he ea beig eaed. Geea eecic acid aciai i ed fe ad
a. The a ae a ceced cahdica (egaie chaged) i he a. Le
ade ae ed. Ceai ea ch a aie ee ae adica (iie) chag
aciaed ide ei adhei f he aed caig.
Nice ad ice aed a ae acid aciaed eecica ee he aie fi
fhe aig. I hi cae, he ice i ceced cahdica. The aie fi, ice
edced a he cahde.
Seciaied bicai ad ecedai f ie ae gd ce f ifa
ad efficie e f acid acia.
SURFACE PREPARATION OF ALUMINUM AND ITS ALLOS
Sface eaai f ai f aig i diffee f ha f fe ad he
diffeece i caed b he high degee f ai eacii. O ee ai, a
aid ad ce he face f ai. Thi ae ee diec bdig ih he
Ahe be i he diffeece i icce beee diffee ai a a
bgh ab b hea eae f he ae a. The e i a age f eec
eie eiig diffee eeae ad aciai echie. A ih he e
face i ch a i, geae, bffig cd, figei, ec. a a be ee
eed. A geea cce a fed eea ai i a f:
1. DEGREASING
2. OIDE REMOVAL
3. SURFACE CONDITIONING TO PREVENT REOIDATION
4. PLATE
1. DEGREASING
The e f degeaig i ee echaica deied i he face, e.g.
bffig cd, figei, ec.
Geea, a aac f he face a hi i d be ee, eig i a bch
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cdii. The degeaig e, heefe, hd be deiged ee hee i ih
bai ea. Mid aai, deege, ad e aied ih ih aic ae
e.
Aaie -ech ceae ae ide ed i hi e. Thee ceae a a
a a f hei cii. Siicae ae ecee degeaig age, b a high cce
eeae i f ibe ai iicae fi he face. T be eed e
fi eie he e f fide addiie i bee acid dee.
Siicae-fee -ech ceae e gd faca ad defccaig age deg
ih eaig ihibiig fi.
Se ece deee hae ade i ibe cbie a high degee f deegec
iae echig eie. Thee fai ae iied ea f igh i,
caef ied, ice he ech ae a be affeced b i adig i he i.
2. OIDE REMOVAL
A eaied eaie, a ide ae i ee ee ai face. The ae' hhade deed aig eee, afacig echie ad hea eae.
ide ae i a ciica e i he eae cce. Oide ea ca be achieed b ai
aaie eae.
High aaie i caiig di hdide ffe a high ae f aac f ai
e effecie i ide ea.
Died ai eai i i a aiae a g a fficie fee aaii
he bah. A be f addiie ae ed c ech ae, ech ae gai ie,
he fai f hdaed ai ide cae ad heae ad a a.
Rea f ide b aaie echig, hee, eae behid a eide f aig di
eee ha ae aaie be. Thi eide, decibed a , a cai iic
agei, ec. deedig he a cii. Theefe a deig e f
echig.
Acid echa ae a aaiabe. The ae ed hee aggeie aaie echig i
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. A .
D ,
. T IV . T
. A ( , , )
.
E , ,
, , . H- , , " " . T
,
. R
), -
3. FACE CONDIIONING
A ,
. A
. T , , .., , , , , .
T , . A
,
. N
. T
. T
. T .
T , , . T
.
A . D
. T
, .
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Addiional ncleaion ie deelop, eling in a moe nifom, een and adheen inc
lae peen eoidaion of he face, making anfe ime pio o plaing le cii
Anohe feae of allo incae i hei capabili o poec edge and hap cone of
in bael o blk fom being on, a common poblem leading o blie in bael plain
TABLE IV: Tpical Desmutting and Acid-Deoidiing Solution
For 1XXX and 2XXX Allos
Niic acid 30-70% /
Wae Balance
For 2XXX and 4XXX Containing Silicon and Most Castings
Niic acid 30-50% /
Floide 60-100 g/L
Wae Balance
For 5XXX Containing Magnesium (Ma also be used as all-purpose desmutter)
Niic acid 30-50% /
Slfic acid 20-30%
Floide 60-100 g/L
Wae Balance
For Copper Magnesium Allos (Fluoride ma be added for silicon-containing allo
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Sulfuric 5-10% v/v
Hdrogen Peroide 3-5%
Water Balance
Proprietar, nonfuming, stable-acid desmutters are also available for most applications.
TABLE V: Tpical Preparation Ccles
1. For Simple Allos and Castings:
Non-etch soak
Etch
Desmut
Zincate
Plate
2. For Heat Treated Allos:
Non-etch soak
Deoidie
Etch clean
Desmut
Zincate
Plate
3. For Magnesium and Heat Treated Allos:
Non-etch soak
Etch
Desmut
Zincate
Strip (50% nitric acid)
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Zincate
Plate
Rining
The chemistries of the different steps could vary substantially from tank to tank in a giv
preparation process. Types and degrees of alkalinity or acidity, surfactants, etc. may not
among the different solutions. Such cross contamination can create a general drop in cle
and cause objectionable residues to form on the surface being prepared. Sil icate residue,
contact with acids will precipitate insoluble silica acid on the metal surface, leading to ha
loss of adhesion when parts are plated. Rinsing is therefore considered an important and
the surface-preparation process.
Adequate rinsing should provide a flow rate adequate to remove residues from the previ
the given rinse time, taking into account the extent that a maximum level of that residu
Flow controllers, conductivity meters and counter-current-flow rinse techniques are tool
optimize quantity and quality of water used.
Rinse-water temperature is a factor often ignored in preplate cycles. Temperatures beloinadequate in rinsing off alkalis and surfactant residues. This is a problem often encount
weather, with incoming rinse water at 40-50F. Optimum temperature for efficient solub
cleaners and salts is 70-90F. Higher temperatures are effective but may induce flash ru
Air agitation and spray rinsing greatly improve rinsing efficiency and are often used whe
Reclaimed water for reuse in rinsing is generally acceptable in preplate cycles as long as
are compatible with the different chemistries used in the process. A fraction of fresh wat
used to prevent an increase in residual content.
Poce ConolControl of cleaners is usually done by titration of the acid or alkali contents. Maintenanc
replenish the basic constituents as well as surfactants and other components included in
Suppliers of proprietary cleaners provide complete control procedures and kits that allow
means to control and maintain the solutions at optimum operating conditions.
Although the essential components can be maintained, contaminants build up and event
O
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. O ,
,
G . I .
- . H
T .
S , ,
H , -
. C .
,
. T ,
.
Cleanline Cieia
T . M, ,
. T UV ,
UV- , , , .
T W B T. T
. T
. T -
, -- . T
, -
- . S
ASTM B320-60, ,
. T
C . H
. ASTM B-3
W B T. A 30
, .
Adheion Teing
Since surface preparation has a direct impact on adhesion of the plate adhesion testing i
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Since surface preparation has a direct impact on adhesion of the plate, adhesion testing i
performed to measure the adequacy of the preplate process. There are several adhesion
as a form of production control. The choice of a particular test is limited by the type of p
intended use.
For example, if a part is expected to be exposed to high temperature, a heat-and-quench
relevant. Bending would be an adequate test for post-plate forming operations. ASTM B-
the following tests in detail. One or more may be specified for a particular application. In
coating is expected to remain intact, with no signs of peeling or flaking off the substrate.
a. Bend Test
Bending of parts at a 90 angle around a mandrel, or back and forth through 180 until
basis metal occurs. Cracks in the metal without lifting of the deposit do not constitute a
b. Chisel-Knife Test
An attempt is made to undercut and lift the coating with a sharp chisel or knife. Not reco
soft or thin deposits.
c. Burnish Test
Rubbing and applying pressure on the plate with a smooth-ended tool, producing a burni
no peeling or blistering. Not satisfactory for thick deposits.
d. File Test
The cross section of the part is filed with a coarse file at a 45 angle so that the substrat
leaving the edge of the plate protruding. The plate should not lift or peel when pulled.
e. Grind-Sa Test
Grind or saw the plated article in the direction that favors separation of the plate.
f. Heat-Quench Test
Articles are heated in an inert or reducing atmosphere, then quenched in water. The tem
different basis and plated metals are specified in ASTM B57. Appearance of blisters may
deposit cannot be peeled off the substrate in areas around the blisters, it is not an adhes
g. Impact Test
A hammer or an impact device is used to strike and deform the plated part
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A hammer or an impact device is used to strike and deform the plated part.
h. Peel Test
A strip of steel or brass is soldered or secured by a heat cured adhesive to the plate. The
90 to the surface.
i. Push Test
A blind hold is drilled through the substrate on one side of the part, short of reaching th
other side. A punch is pushed through the hole against the supported part until a buttonNo exfoliation or peeling in the punched area should occur.
j. Scribe-Grid Test
This is a commonly used test in which the surface is scribed with a sharp blade in a grid
special adhesive tape is applied to the scribed area, then pulled off rapidly. No peeling sh
TABLE VI: Tpical Cleaning Ccles
Substrate Alkalinitgm/l of
NaOH
Tpical Cleaner Condition
COLD ROLLED STEEL
Soak clean high 80-100
Electroclean 50-100 20-100 ASF Anodic or Cathodic followed by An
Rinse
Acid Activate n/a no current or 15-25 ASF Cathodic
Rinse
Electroclean 50-100 20-100 ASF Anodic
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Rinse
Mild acid dip plate n/a 3-5% HCI
STAINLESS STEEL
Compound remover 5-15 used if parts are polished soak or Ultrasonic
Soak clean 20-100 8 oz/gal, 4 min, 160F
Electroclean 50-100 20-50 ASF Anodic
Rinse
Acid activate or
Plate
50%Hcl 15-25 ASF Anodic
INC DIE CAST
Compound remover 5-15 Soak or Ultrasonic
Soak clean
moderate
low, 5-15
Electroclean 10-20 10-15 ASF Anodic
Rinse
Acid dip plate n/a
COPPER
Soak clean high 20-100
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Soak clean high 20 100
Electroclean 20-100 20-50 Anodic
Rinse
Acid actiate n/a
BRASS
Soak clean
moderate
5-15
Electroclean 10-20 10-15 ASF Anodic or Anodic
Rinse
Acid dip n/a
TUNGSTEN
Soak clean high 20-100
Acid dip n/a
Rinse
Anodic etch plate 20-100 100-300 ASF Anodic
anodic
TPICAL ALKALINIT RANGE
High 20-100
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High 20 100
Moderate 10-20
Low 5-15 (May not contain free Hydroxides)
Temperature and time vary depending on supplier recommendations and process used.
1. LIQID CLEANERS
Traditional cleaning products were dry powdered materials. Though liquid cleaners were
early as the 1970s, they were not accepted, for a variety of reasons. The most commonl
were that liquid cleaners were not concentrated, as were powders, had narrower operati
that the user was "paying to ship water." Advances in surfactant technology and the wid
potassium salts have enabled chemical manufacturers to overcome these perceived probl
another way, liquid cleaners are not powdered cleaners pre-dissolved in water. Liquid cle
chemically different than powders in the use of potassium salts, safe solvents, surfactant
carbonates and other fillers. A final factor in the acceptance of liquid cleaners is the inhe
they imply to the user, some of which are:
Improved safety, no risk of splashback.
Automatic control and replenishment-hands-off operation, consistent bath chemis
fewer defects. They are more suitable for SPC.
Less down time for make up - less sludge generated, less demand on the waste-tr
Effective and economical cleaning.
Cleaner filtration is gaining in popularity, with the aim of prolonging the bath life betwee
Several filtration techniques have been proposed, ranging from simple bag filtration to cof soil skimmers, coalescers and ultrafiltration. Since the cost of such systems varies app
feasibility study must be undertaken before adopting a particular system. In general, ho
been reported that any type of filtration does increase the bath life by at least 20%, and
or more.
Recent developments in preplate products promote the use of environmentally acceptabl
Substituting effective biodegradable surfactants for hard chelates and use of safer solven
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g g
emulsifiers in place of chlorinated solvents are examples.
Emphasis on simplified water treatment is another aspect of newer cleaning technologies
developments allow oil separation from process cleaner. While water treatment is made
cleaner solution life is extended and its performance maintained at optimum longer. Sep
reclaimed and reused.
SAFET AND HANDLINGThe majority of people who operate cleaner and acid tanks pay only minor attention to t
important subject. Many serious accidents, such as chemical burns, respiratory problems
can be avoided. This information is given to the user by the suppliers, including specific i
handling process chemicals. The following safety tips should help inexperienced personn
injuries.
When making up acid-dip tanks, never add water to the concentrated acid, always
the water, with constant stirring to avoid spattering. Sulfuric acid is a good exam
react violently if not handled properly.Never add dry cleaner (alkaline) directly to a hot tank above 120F. Violent erupt
large quantities of dry cleaner are added directly to the tank. Instead, add dry pro
continuous agitation.
Avoid breathing fumes from acids and cleaners. Otherwise respiratory problems c
Avoid skin and eye contract when handling chemicals. Wear protective clothes, gl
goggles and other protective equipment. A fume hood should be used when an an
involves the liberation of hazardous fumes.
In case of injury, contact a physician immediately. Give first aid and see MSDS sh
If a spill occurs, clean up the spill as soon as possible and prevent the spill from a
other chemicals, to prevent reaction. Maintain your own safety first, secure the ar
Do not allow personnel to work over hot solution without adequate precautions. N
in an area where chemicals are in use.
Provide professional training to those involved in handling chemicals.
Check appropriate MSDS sheets prior to the handling or use of all chemicals.
Good laboratory safety practice requires that incompatible chemicals be stored, transpor
of in ways that will prevent their coming together in the event of an accident. Tanks sho
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y p g g
labeled and identified by type of chemical used, hazard classification and safety informati
The preceding material has been reproduced
from the MFSA Qualit Metal Finishing Guide,
Volume 1, No. 1-P
"Chemical Surface Preparation for Electroplated Metallic Coatings"
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