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MIL-M-3171C
AL July 19
16 October 1964
MILITARY SPECIFICATION
MAGNESIUM ALLOY, PROCESSES FOR PRETREATMENT AND
PREVENTION OF CORROSION ON
This specification is mandatory for use by all Depart-
ments and Agencies of the Department of Defense.
1. SCOPE
‘ a Scope - This specification covers general requirements
for the apparatus, material, and procedures to be sed im the processing of
magnesium base alloys for the purpose of increasing their corrosion resistance
and by producing surfaces suitable for organic paint finish systems.
1.2 Classification -
‘ ian ‘Types - The magnesium corrosion preventive treatments
shall be of the following types:
Type = Chrome Pickle Treatment
‘Type I~ Dichromate Treatment
‘Type IV - Galvame Anodizing Treatment
‘Type VI. - Chromic Acta Brush-on Treatment
Type VII ~ Fluoride Anodizing Process plus Corrosion
Preventive Treatment
‘Type VIII - Chromate Treatment
2. APPLICABLE DOCUMENTS
+ a1 ‘The following documents of the issue in effect on date of
invitation for bids or request for proposal, form a part of this specification to
the extent specified herein.
FSC_MFFP‘MIL-M-3171¢
SPECIFICATIONS
Miltary
MIL-C-46079 Coating, Epoxy, Baking Type for Magnesium,
Casting
‘MIL-M-46080 Magnesium Castings, Process for Anodic Cleaning
and Surface Sealing of
STANDARDS
Mut
7
MIL- STD-105 Sampling Procedures and Tables for Inspection
by Attributes
(Coptes of specifications and standards required by supphers in connection
with specific procurement functions should be obtained from the procuring activity
or as directed by the contracting officer. )
3. REQUIREMENTS
3. General req
ements ~
BL Materials ~ All matertals used in the cleaning or treating
of magnesium base alloys shall be of good quality and suitable for the purpose
intended. All chemicals used in cleaning and treating shall be free from metallic
impurities such as salts of heavy metals (lead, nickel, zine, arsenic, antimony, ete. ).
a1.2 Workmanship - ‘The treatments covered by this specification
shall be controlled and operated to give a uniform surface conforming to the require-
ments specified herein. ‘The surface shall be free from breaks, discontinuties,
scratches, and other damage. The size and number of contact marks shall be
held at a mimmum,
3.2 Cleaning and pickling operations (sce 3..12)-
3.2.1 Solvent cleaning - Grease or oil shall be removed by
‘means of vapor degreasing, ultrasonic cleaning, organic solvents, or by
‘emulsion cleaning which employs a mmeral oil distillate and an emulsifying
agent. For this cleaning operation, chlorinated solvents, petroleum spirits,
naphtha, lacquer thinners, and similar grease solvents which do not attack,
magnesium may be used. Methyl or wood alchohol (CH;01) 1s specifically
prohibited as a solvent cleaner for magnesium alloys.
2‘MIL;M-3171C
92.2 ‘Mechanical cleaning ~ Mechanical cleaning shall consist
of sand, shot, grit, or vapor blasting, sanding, hard bristle brushing, grinding
and rough polishing, When sand, shot, or grit blasting methods are employed,
there is danger of surface contamination which will greatly increase the initial
corrosion rate of magnesium. In such case, subsequent pickling operations,
as specified in 3.2.4.2, or fluoride anodizing as specified in 3.9.1 shall be
employed
3.2.2.1 ‘New sand castings - New sand castings shall be sand
or grit blasted and then pickled in conformance with 3.2.4,2 or fluoride anodized
as specified in 3.8.1.
3.2.2.2 Discolored or corroded castings ~ Discoloration or corroston
products shall be removed from rough unmachined castings. ‘This operation may
be performed by blasting and subsequent pickling as specified in 3.2.4.2. Machine
parts or sections, which must be held to close dimensional tolerances, may be
cleaned by use of a chromic acid pickle solution conforming to 3.4.1.
32.23 Welding flux - When using flux in the welding operations,
the welded sections shail be thoroughly cleaned Immediately after the operation to
remove all traces of flux. Where possible, hot water and a hard bristle brush
shall be used to insure thorough flux removal. Inaccessible welded sections
shall be washed with a high velocity stream of water (preferably hot). ‘They
shall then be immersed for 1 hour in a 2 to § percent sodium dichromate solution
maintained at 180 to 212" F The parts shall be thoroughly rinsed in cold running
water.
3.2, Alkaline cleaning ~ Cleaning prior to application of treat
ments other than Type I when used for protection during shipment or storage,
shall be done by cleaning the parts in an alkaline cleaner recommended for steel
or ma cleaning solution as specified in 3.3.2. Any alkaline cleaner used shall
have a pH that 1s maintained above 8. Alkaline cleaning, prior to application
of Type I when used for protection during shipment or storage only, may be
omitted provided the parts are free from grease, oll, or other deleterious deposits
at the time of application. Alkaline cleaners containing more than 2 percent
caustic, such as sodium hydroxide will etch ZK60A, ZK60B, and some magnestum-
thium alloys with resultant decrease in dimensions. If euch a dimensional change
1 not desirable, the alkaline cleaners used on these alloys should not contain
more than 2 percent caustic.
3.2.3.1 Graphute lubricant removal. - Graphite base lubricants shall
be removed from hot formed magnesium sheet parts by soaking the parts for
10 to 20 minutes in an aqueous sodium hydroxide (NaOH) bath containing 13 oz/gallon
of NaOH and maintained at 190 to 212° F. This bath shall be maintained at « pHMIL-M-3171C
above 13. One-tenth ounce per gallon of soap or wetting agent may be added to
thie solution if removal of heavy films of mineral oll is required. ‘The parts
shall be thoroughly ringed in cold water and then immersed in a chromic-nitrate
pickle as specified in 3.4.2 for approximately 3 minutes. If complete cleaning
is not obtained the first time, this operation shall be repeated until the parts
are clean. Because of the difficulty of removing graphite from chrome pickled
sheet, such sheet shall not be used for forming unless the chrome pickle coating
has been completely removed as specified in 3.2.3.2.
3.2.3.2 Previously applied chemical finishes - Previously applied
chemical finishes shall be removed. Magnesium base alloys sometimes are
furnished with Type I treatment which provides protection during shipment,
storage, and machining. ‘The coating resulting from Type I treatment remaining
on the unmachined areas will impair the film produced by Type III and Type IV
treatments and consequently, must be removed. This operation may be performed
by use of alkaline cleanera such as the types specified in 3.2.3., If the finish
Is difficult to remove, the part should be immersed in the chromic acid pickle
specified in 3.4.1, Alternate immersion in the alkaline cleaner and chromic
acid pickle may be necessary to remove very old finishes.
3.2.3.2.1 ‘The Type VI treatment may be applied over previously
applied thin film by Type I or Type VI treatments without removing these
finishes (sce 3.8. 1).
3.2.4 ‘Acid plckling -
3.2.4.1 General pickling - General pickling to remove oxide layers,
old chemical finishes, burned-on drawing and forming lubricants, and other
water insoluble or non-emulsifiable substances shall be accomplished, preferably
by using a chromic acid type pickle conforming to 3.4.1 or 3.4.2.
3.2.4.2 Pickling of magnesium sand and permanent mold castings -
Magnesium sand and permanent mold castings which have been subjected to
blasting operations shall be pickled in a sulfuric acid pickle conforming to
3.4.3 or in a sulfuric-nitric acid pickle conforming to 3.4.4. Pickling operations
shall be continued until 0.002 inch of surface has been removed, whenever
dimensional tolerances permit.
3.2.4.3 Pickling of magnesium sheet and plate - Magnesium sheet
and plate up through 0. 500 inch thick shall have the mill ecale removed to insure
aclean surface to which subsequent treatment will be applied. Where dimensional
tolerances permit, 0.0005 inch to 0,001 of metal surface shall be removed. An
acetic-nitrate pickle conforming to 3. 4.7 or equivalent acid pickle shall be used
for this operation.
4MIL-M-3171C
3.2.4.4 Pickling of magnesium die castings - Die castings that are
to be pickled for maximum corrosion resistance and a more uniform surface
for treating shall be pickled in a chromic-nitric HF pickle conforming to 3.4.5
or a phosphoric acid pickle conforming to 3.4.6
3.2.5 Retreatment of wrought and cast parts -
3.2.5.1 Grease and ofl - Grease and oil shall be removed in
conformance with 3.2.1.
3.2.5.2 Paint - Old paint coatings shall be removed, preferably
by the use of an alkaline (caustic) liquid pant remover. Solvent type paint
removers may be used provided the operation is followed by a wash with a
‘wax-free solvent to remove any wax which may have been left on the surface.
Light blasting may be used to remove paint from parts of substantial thickness,
‘but only sanding shall be permitted on thin sheets. If sand-blasted, the part shall
be pickled in conformance with 3.2.4.2.
3.2.5.3 Chemical finishes - Chemical finishes shall be removed
as specified in 3.2.3.2 before retreatment.
3.2.5.4 Alkaline cleaning - Parts to be retreated shall be cleaned
in an alkaline cleaning solution as specified in 3.2.3.
3.2.5.5 Corrosion or oxide films - Corrosion products or oxide
films shall be removed, preferably by use of the chromic acid pickle or
chromic-nitrate pickle as specified in 3.4.1 and 3.4.2, respectively.
3.3 Alkaline cleaning solutions -
3.3.1 Alkaline cleaning as required in 3.2.3 may be performed by
using proprietary type cleaners, in which case the operation shall be as specified
by the vendor. in no case will any such cleaner be used that has a pH lower than
8. An alkaline cleaner of the formulation given in Table I may be used quite
satisfactorily. The parts are simply immersed in the solution, or, if direct,
current is available, the parts are made cathodes in the bath and a current
density of 10 to 40 amp/sq. ft. at 6 volts, is applied. When cathodic cleaning
tg employed, the time required for adequate cleaning {s reduced. Parts are
given a thorough rinse in cold running water after alkaline cleaning. Parts shall
be cleaned until no water break occurs im the rinse.
3.3.2 Anodic cleaning employing the work as the anode in the
alkaline cleaning solution is generally not recommended because of the formation
of undesirable oxide films as well ae pitting of magnesium alloy surfaces from
prolonged contact.MIL-M-3171C
TABLE 1
ALKALINE CLEANER SOLUTION AND OPERATION
Ounces per gallon | Operating | Treatment | Tank
Composition (water added to | temperature | time- | construc-
make one gallon) °F minutes | ton
Sodium hydromde (NaOH) 8 190 to 212° | 3to10 | Steel
‘Trisodium phosphate 1-1/3
(NagPO4 121120)
Soluble soap or wetting on
agent
a4 Acid pickling solutions ~
3.4.1 Chromic acid pickle - Chromte acid pickling may be used
where parts with close tolerance limits are to be fimished since this pickle
causes no dimensional change, It can be used in removing old chemical finishes
by alternate immersion in an alkalme cleaner specified in 3.3.2 and the chromic
actd pickle, This pickle 1s satisfactory for removal of surface oxidation,
corrosion products, and for general cleaning of parts. It 1s not satisfactory
for the removal of sand or the effects of blasting and shalll not be used for
parts containing copper based inserts unless masked off. Excessive amounts
of amions, such as chlorides, sulfates, and fluorides must not be allowed to
build up in the solution as these tend to coat or etch the metal rather than clean
the surface Silver mitrate (AgNO3) may be used to precipitate out any chloride
buildup, thus extending the life of the bath, but 1t 1s better to discard the con
taminated solution and replace with a new solution, The solution composition
15 indicated in Table I
3.4.2 Chromic-mitrate pickle - The chromic-nitrate pickle
18 not generally used where surface oxidation or corrosion products are to be
removed but can be substituted for the chromic acid pickle specified in 3.4.1.
It is used, as specified im 3.2.3.1, primarily for removing burned-on graphite
lubricants. It is not satisfactory for the removal of sand or the effects of
blasting and shall not be used for parts containing copper base inserts unle:
masked off. Lack of chemical action and a pH of 1.7 or higher indicates,
depletion of the bath The bath may be controlled by additions of chromic
acid to bring the solution back to the original pH range of 0.5-0.7. Large
tanks may be revivified economically in this manner about 4 times after which
tanks should be drained and refilled with new solution Excessive revivification
6-M-S171C
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results in too great a consumption of chromic acid, excessive etching and
staining of the magnesium. Actual time and temperature used should be regulated
to produce satisfactory results. The solution composition 1s indicated in
‘Table IT
3.4.3 Sulfuric acid pickle - Sulfurie acid pickling 1s used on
‘magnesium sand castings to remove the effects of blasting operations, The
pickle should be applied before any machimng operation, since the amount of
metal removed 18 likely to exceed permissible tolerances, The solution
composition 15 indicated in Table IL
3.4.4 Nitric-sulfurie acid pickle - As an alternate for the
sulfuric acid pickle (see 3. 4.5) the nitric-sulfurie pickle may be used. The
solution composition ts indicated in Table IL
3.4.5 Chromic-nitrie = HF pickle - A chromie-mitric - HF
pickle may be used for pickling of castings, particularly die castings. This
pickle bath removes about 0.0005 inch per mmute per surface. The solution
composition 1s indicated im Table IT
3.4.6 Phosphoric acid pickle - ‘The phosphoric acid pickle
may be used for pickling all types of castings, particularly die castings It
1s espectally effective in removing aluminum segregation from the surfaces
of AZSIA and AZ91B alloys, It has been used for some wrought alloys, such
as HK3IA, prior to plating This pickle bath removes about 0.0005 inch per
minute per surface. The solution composition 1s indicated in Table
34.7 Acetic-nitrate pickle - The acetie-nitrate pickle 1s suitable
for removal of mill scale and other surface contamination from magnesium
sheet to ensure maximum protective finishing. This pickle can be used on other
wrought forms and on solution heat treated magnesium castings. Castings in
the as-cast condition (-F) or in the solution heat-treated and aged condition (-T6)
should not be pickled by dipping in an acctic-nitrate pickle bath as a loose gray
smut 1s formed. Magnesium castings m these conditions should be treated with
a chromte-nitric - HF pichle (see .i.1.5) For most effective results the pickle
should be allowed to remove 0 0005 inch to 1 01 inch metal per surface and
therefore may not be suitable for p.irts requn ing close tolerances. The solution
composition 1s indieated mn Table TL
3.4.8 Glycone-mitrate pickle - In cases where spray piokling
as used or fumes are a problem, the ylcolie-mitrate pickle may be preferred
to the acetie-nitrate pickle (3 4.7) to reduce gerd loss {rom saporization
‘The solution composiinn ry indie ved in table TTMIL-M-3171C
3.4.9 ‘Spot weld chromic-sulphuric pickle ~ A chromic-sulphurie
pickle may be used where parts are to be cleaned prior to spot welding. Parts
are first treated by mmersion in an alkaline cleaner and then given a thorough
rinse in cold running water as specified in 3.3.2. Parts are then immersed in
an alkali neutralizing pickle consisting of an aqueous solution of etther 0.5 to 1
percent of sulphuric acid by volume or a1 to 2 percent solution of sodium
Disulphate (sodium acid sulphate) (weight by volume). Following the neutralizing
dip, the parts are immersed in the chromie-sulphuric acid pickle. This treat-
ment gives a low resistance surface for spot welding. The solution composition
is indicated in Table IL
3.8 ‘Type I treatment ~ Cleaning of parts to receive the Type
Lor chrome pickle treatment shall be in accordance with other requirements of
this specification
3.5.1 Procedures for wrought parts - Wrought magnesium parts
shall be treated in a chrome pickle bath whose solution composition and operation
is stated in Table III. The parts shall be immersed and agitated in the bath for
period of time ranging from 1/2 minute in a solution containing the full quantity
of nitric acid to 2 minutes in a solution i which the mitric acid 18 nearing depletion.
Usually a one minute dip will be sufficient in a properly controlled bath. After
the immersion period, the parts shall be held above the tank for 5 seconds. This
allows the adhering solution to drain off and produce a better colored coating.
‘The parts shall then be washed 1n cold running water followed by a dip in hot
water, to facilitate drying, or by exposure to heated air. Other methods, such
‘as spraying may be used to expose the parts to the chrome pickle solution,
provided the other requirements of ths specification are met.
3.5.2 Procedures for sand, permanent mold, and die castings -
‘Magnesium sand, permanent mold, and die castings shall be treated ina chrome
pickle bath as given in Table III. Die castings and aged sand castings shall be
gaven a 15 to 30 second hot water dip followed immediately by immersion in the
solution specified in Table IIT A 10 second immersion is sufficient if the bath
18 operated at 120 to 140° F. If the bath 1s held at a lower temperature a longer
time 1s needed. Excessive treatment time results in a powdery coating and failure
to pre-heat the castings in hot water may result in no coating. If the bath for
castings 1s not available, the bath for wrought parts may be used for die castings
and aged sand castings. Sand castings in the solution heat treated condition
can be chrome pickled with the solution in Table III at room temperature.
After dipping, parts shall be rinsed as described above in 3.5.1.
3.53 Precautions - Chrome pickle baths (see Table II) may
remove as much as 0.0006 inch of metal per surface during treatment and, therefore,
cannot be used on machined surfaces unless tolerances will permit or proper
allowances have been made. Magnesium parts containing steel inserts can be
9MIL-M-3171C
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given the Type I treatment. The color, luster, and etch produced by the
‘Type I treatment will vary with age of the solution, with the alloy composition,
‘and with the condition of heat treatment of the alloy. The most desirable paint
base is a matte gray to yellow-red, iridescent coating, which exhibits a net~
work of pebbled etch finish as viewed under magnification. Bright, brassy
coatings, which show a relatively smooth surface with only occasionally rounded
pits when examined with magmfication, shall be unsatisfactory where the treat-
‘ment is used as a paint base, but shall be acceptable for protection during
shipping and storage. This shade indicates an excess of nitric acid or mtrate
salt buildup in the bath.
3.5.4 Brush application - Articles too large to be immersed
shall be carefully brushed with a generous amount of fresh pickle solutions speci-
fied in Table II. The solution shall be allowed to remain on the surface for at least
1 minute while brushing and shall then be washed off immediately with plenty
of cold running water. The coating thus formed is less umform in color than
that produced by immersion but 1s equally good as a paint base. Powdery coatings
are not good as paint bases and indicate poor rinsing or failure to keep the
surface wet with solution during the one minute treatment time by continuous
brushing over the same area. In treating riveted assemblies, care must be
taken to avoid entrapping solution in the jomts. Brush application is suitable for
touchup of all types of treatments which have been damaged. Type I coatings
are best for touchup of base areas before making an electrical bonding joint and
where no primer can be used to seal the treatment.
3.5.4.1 Parts such as tanks which take a long time to fill and
‘empty may be treated with chrome pickle solution for wrought parts diluted
with an equal quantity of water. ‘The time of treatment shall be such as to
produce a complete coating on all areas. Similarly, if a more dilute solution
is required to treat parts by automated time cycle, more water may be used
in the pickle bath.
3.5.5 Control of Type I treatment -
3.5.5.1 Sodium dichromate determination - The sodium dichromate
determination shall be performed as follows, or by recognized analytical
methods:
Pipette 1 ml of the chrome pickle solution into a 250 ml
beaker containing 150 ml of distilled water. Add 5 ml of
concentrated hydrochloric acid (HCl) and 5 gms of potassium
rodide (KI) Allow at least 2 minutes for the reaction
to take place. Next, stir and titrate the liberated fodine
with N/10 sodium thosulphate (NapS,0,) until the
aMIL-M-3171C
yellow color is almost gone. Add several drops of starch
indicator solution, then continue titration with N/10 sodium
thiogulphate (Na28,0;) until the purple starch fodine color
disappears. CAUTION: Do not add starch indicator solution
until the yellowish fodine color is almost gone or incorrect
regults will be obtained. The final solution varies from
pale green to blue in color.
Calculation:
ml N/10 sodium thiosulphate (NayS;03) X 0, 6635=
oz, /gal. sodium dichromate (NayCr207 - 28,0)
3.5.5.2 Nitric acid determination - The nitric acid determination
shall be accomplished as follows:
Pipette 1 ml of the chrome pickle solution into a 250 ml
beaker containing 50 ml of distilled water. Standardize
a glass electrode equipped pH meter with a buffer solution
of approximately 4.0 and immerse the glass electrode
system in the solution. Stir and titrate with N/10
sodium hydroxide (NaOH) to a pH of 4.0 to 4.05.
Calculation:
ml N/10 sodium hydroxide (NaOH) X 0, 8109=
1, oz. /gal. nitric acid
3.5.5.3 Control limits of chrome pickle bath (Table Ill) - Depletion of
the solution is indicated by the paleness of the color, shallowness of etch, and slowness
of action on the metal. ‘The paleness of color should not be confused with that
obtained by insufficient exposure to air between removal from the bath and the
wash in water. The chrome pickle bath shall be revivified only once when non-
aluminum alloys are to be processed. It may be revivified 7 times for other
alloys. The bath may be revivified at the end of each run (the end of the run
{a that point at which the nitric acid has been depleted to or near 8 fl, oz. /gal.)
according to the following schedule.
Chemical Content of Bath
Run Number NagCr207 + 2H,0 HINO (sp gr 1.42)
oz. /gal. fl, o2. /gal.
1 24 24
2 24 a
3 24 18
4to7 24 4
2MIL-M-3171¢
If the chrome pickle solutions are used to produce a protective treatment for
shipment and storage only, it is recommended that they be discarded after
30 to 40 revivifications. Baths from which there is considerable drag out,
necessitating frequent additions of new solution, may be revivified without,
limit provided that the coated articles conform to this specification,
3.5.5.4 rational difficulties and possible explanation -
following operational difficulties may be encountered during chrome pickling:
(@) Brown, non-adherent, powdery coating:
1, The part was in the air too long before rinsing.
‘The air interval shall be as epecified in 3.5.1.
2, The ratio of acid concentration to sodium dichro-
mate content may be too high.
3. The solution may be too hot due to a small quantity
of solution and a large number of parts going
through the bath, Cool the bath or use a larger
quantity of solution.
4, The metal is not properly degreased. Brown
powder will occur at spots where oil exists.
5. Solution has been revivified too many times.
‘The nitrate buildup causes powdery coatings.
(©) Gray, non-adherent, powdery coatings on castings:
1, This may be minimized or virtually eliminated by
treatment with the fluoride modified chrome
treatment bath as specified in Table III.
2, The costing is pyrophoric and may flash violently
upon impact with the rough surfaces of harder
materials auch as steel or concrete, or even
during grinding (see 6.6, 5).
3, The part may have been excessively over-treated
by keeping in the bath too long. Extreme care should
be taken in handling such parts during further treat-
ment. Upon removal the part should be thoroughly
rinsed in cold water, dipped in machine or motor
oil and scrapped. If parts have not been too severely
13MIL-M-3171C
damaged by over-pickling and salvage 1s desirable,
‘the powdery coating may be removed by immersing in
2.10 to 20 percent hydrofluoric acid solution for
5 to 10 minutes. This will remove the powder and
render the part safe to handle.
3.5.6 To give a smoother surface on some alloys after pickling
In the chrome pickle baths, magnesium sulfate may be added to the chrome pickle
solutions specified in Table II] to the extent of 4 ounces per gallon. Such a modi
fication should be used for temporary storage and shipment but not where the coat-
ing will be used as a base for painting. Type I treatment to which magnestum
sulfate has been added leaves a surface which is unfit for organic {imsh systems.
3.6 ‘Type II treatment - The Type III treatment or dichromate
treatment provides satisfactory paint base and protective qualities on all standard
alloys except EK30A, EK41A, HM31A, HM21A, HKSIA, Lal41A and MIA. No
coatings form on these alloys. Properly applied coatings vary from light to
dark brown depending on the alloy. On AZ91C-T6 and AZ92A~-T6 castings, the
coating produced is gray. The treatment causes no appreciable dimension changes
and normally is applied after machining. Castings and other parts contaiming
bearings, stude, and inserts of brass, bronze, cadmium plate, and steel shall
not be treated, although these metals are not affected by the treatment, unless
the dissimilar metal parts are sealed and demonstrated to the procuring activity
that the treatment will not adversely affect the characteristics of the parts.
Aluminum, however, is rapidly attacked during the hydrofluoric acrd dip (see
3.6.1) which is an important step in this treatment, Where aluminum inserts
are used or wrought parts are assembled with aluminum rivets, the acid fluoride
dip (eee 3.6.2) ahall be used in place of the hydrofluoric acid dip. Close control
of the Type III treatment ie essential when applying this treatment to AZ31B-H24,
Acld pickling by the methode specified in 3.4.2, 3.4.7, or 3.4.8 should be used
on magnesium alloy sheet where maximum corrosion resistance 1s required,
On parts that have previously been Type I treated, the Type III treatment will show
the general marking characteristics of the Type I treatment, but with no decrease
m effectiveness.
3.6.1 Hydrofluoric acid treatment - After parts have been cleaned
in accordance with the other requirements of this specification, they shall be
pickled in the hydrofluoric acid treatment. The solution composition and operation
are contained in Table IV. This operation both cleans and activates the magnesium
surface. It is recommended that AZ31B parts be immersed for 30 seconds and
that all other wrought alloys and castings be immersed for 5 minutes, After the
immersion period, the parts shall be thoroughly rinsed m cold running water.
‘Thorough rinsing is important in order to mmmize fluoride carry-over which will
make the dichromate bath inoperative.
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15MIL-M-3171C
3.6.2 Acid fluoride treatment - The acid fluoride treatment shall
be used for all parts containing aluminum inserts, rivets, etc., and may be used
as an alternate treatment for hydrofluorte acid treatment (see 3.6.1). The solu-
tion composition and operation are contamed in Table IV. It 1s preferred for
AZS31B and AZ31C. The acid fluoride treatment may not only be more economical
to operate, it 1s also safer than the hydrofluoric acid treatment. However, the
acid fluoride treatment will not remove the dark smudge which forms on some
castings after sandblasting and pickling. Then the hydrofluoric acid treatment
must be used. After immersion in the solution, the parts shall be thoroughly
rinsed in cold running water. Other acid fluoride solutions may be used upon
approval by the procuring agency.
3.6.3 Dichromate treatment - After the parts have been given the
fluoride treatment in the solution specified in either 3.6.1 or 3.6.2, they shall
be borled for 30 manutes in the bath whose solution composition is listed in Table TV.
Properly applied coatings vary from light to dark brown depending upon alloy.
After the immersion period, the parts shall be rinsed in cold running water
followed by a hot water dip, to facilitate drymg, or by exposure to heated air.
‘The specified paint coatmg shall be applied as soon as practical after the treated
parts are thoroughly dry. Because ZK60A takes the dichromate treatment faster,
15 minute boul of ZK60A parts 1s equivalent to 30 minutes on other alloys.
3.6.4 Control for Type III treatment ~
3.6.4.1 ‘Hydrofluorie acid determination - The hydrofluoric acid
bath 1s depleted very slowly in use. It shall not be allowed to go below 10 percent
HF as determined by titration for free acid with 1N.NaOH and phenolphthalein
indicator. A solution weaker than 10 percent will attack magnesium quite severely.
Hydrofluorie acid shall be added to the batch as needed to maintain the titration
between 10 and 20 ml of 1N.NaOH per 2 ml of sample. This corresponds
approximately to 10 and 20 percent HF by weight. A pipette for obtaming a bath
sample may be made by hning a small (3 or 4 ml) glass pipette with parafin
wax and calibrating to a 2 ml volume. To avoid error by reaction of the HF with
glass, the sample shall be discharged mto at least 100 ml of distilled water in
the vessel used for titration, and titration shall be done immediately.
3.6.4.2 Bifluoride determination - If bifluoride (acid fluoride)
1s used instead of the hydrofluoric acid, 1t shall be controlled by titration with
caustic. The bifluoride content shall be maintained so that a 100 ml sample
requires 45 to 55 ml of IN. NaOH to produce pink color with phenolphthalein
indicator.
3.6.4.3 Control of dichromate bath - The sodium dichromate deter-
‘mination shall be performed as specified in 3.5.5.1. The dichromate content of
the bath will be maintained within the limits of 16 to 24 ounces per gallon.
16MIL-M-3171C
‘The pH of the dichromate bath must be controlled carefully within the limits
of 4.1 to 5.5 by the addition of chromic acid, However, in the treatment of
AZS1B parte, the pH of the bath must be held within 4.1 - 5.2. Chromic
acid is conveniently added to the bath as 2 10 percent solution. ‘The pH deter-
mination shall be made as follows:
Standardize a glass electrode equipped pH meter with a
buffer solution of approximately 4.0 and check the pH
of the dichromate bath. The pH of the bath is brought
back to 4.1 with chromic acid, Close contro! of this
factor is required when treating parts of large surface
area. Low aluminum-containing alloys shall be processed
on the low side of the pH range to obtain a good coating.
3.6.4.4 Operational difficulties and possible explanation - The
following operational difficulties may be encountered during the application of the
‘Type II treatment:
(@) Abnormally heavy and loose powdery coatings:
1, The hydrofluoric acid or acid fluoride bath 18
too dilute. Concentration of free HF shall be
controlled as described in 3.6, 4,1 and 3.6.4.2.
2, The pH of the dichromate bath is too low. It
should not fall below 4.1. ‘The pH is adjusted
by additions of NaOH.
3, Treatment of oxidized, corroded, or flux con-
taminated parts result in gray to yellow coatings
of a loose nature, Parts shall be cleaned as
specified in 3.2.
4. Powdery costings may form when the work contacts
the tank or is in an electrical circuit with the
tonk through metal holding bars, baskets, or other
pieces of equipment which contact the tank.
5. Prolonged treatment in the dichromate bath.
(©) Failure to coat or nonuniform coatings:
1, The pH of the dichromate bath is too high. This is
very important when HF is used as a pre-dip on low
aluminum-containing alloys such as the AZ31B.
a7MIL-M-3171C
18
3.
5
6.
Adjust the pif back to 4.1 by addition of chromic
acid. The pH change ts quite raptd from the
lower limit and frequent checks are necessary.
‘The dichromate concentration is too low in the
bath, The dichromate concentration should not
fall below 16 oz, /gal. (12 percent by weight).
Oily matter has not been properly removed, resulting
{In a spotted coating where some areas are coated
and others are not. Insuffictent cleaning alone may
not be at fault. Properly cleaned parts may become
contaminated by oily matter existing as a film on the
fluoride or dichromate bath. This oily film builds up
due to inadequate rinsing after alkaline cleaning and
perhaps other reasons such as oil in the atmosphere
or dropping from overhead equipment, etc.
Previous chrome pickle coating was not completely
removed. Use of etther solution specified in 3.4.1
or 3.4.2 to supplement the alkaline cleaning may be
required.
‘The part was not fluoride treated.
Alloy treated is one as stated in 3.6 where the Type I
treatment {¢ not suitable for coating deposit.
Too long an HF dip with alloys such as AZ31B produces
1 fluoride film that does not break down evenly in the
normal time, producing a spotty coating. For these
alloys trestment time should be 30 eeconds to 1 minute,
‘The bath was not kept boiling during the treating period.
‘This is particularly tmportant when processing AZ31B.
‘Minimum bath temperature is 200° F.
Improper rinsing after the HF dip. No coating forms
{f the amount of the HF or maximum soluble fluoride
carried over into the dichromate bath exceeds 0.2 percent,
Streaked coatings will be observed before this point 18
reached. A 0,2 percent solution of calcium chromate
(CaCr0,) can be added to the bath to precipitate the
excess fluoride out as insoluble calctum fluoride (CaF).
‘When this addition ts made, the bath need not be discarded.‘MIL-M-3171¢
3.7 ‘Type IV treatment - The Type IV treatment or galvanic
anodizing treatment may be applied to all alloys. It 1s also used specifically for
those alloys which do not react to give a protective film with the Type II treatment,
It causes no dimensional change and may be applied after machining operations.
After the parts have been cleaned in accordance with the other requirements of this
specification, they shall be treated in the hydrofluoric acid pickle as specified in
3.6.1 or in the acid fluoride pickle as specified in 3.6.2.
3.7.4 Galvanic anodizing eolution - After the treatment in a
fluoride solution, the work shall be galvanically anodized for at least 10 minutes
and for as long a8 30 minutes in the solution whose composition is specified in
Table V. The steel tank shall be the cathode. If the tank i made of nonmetallic
material, steel cathode plates shall be used, ‘The magnestum parts must have
good electrical connection with the tank or the cathode plates, care being taken
that the work does not make contact with the tank except by an external connection.
‘An ammeter and rheostat shall be in the electric circuit, ‘The current density shall
not exceed 10 amps per square foot of anode area at any time. A minimum of 70
ampere-minutes per square foot of anode shall be maintained to secure a uniform
coating. Ordinarily 70 to 150 ampere-minutes per square foot will be suffictent.
When the area of work is large, in respect to tank size, the anode may fall below
2 amperes per square foot, resulting in a poor coating being obtained. In this case,
an external source of current should be used to maintain the anode current density
with the required range. After the immersion period the parts shall be rinsed in
cold running water, followed by a hot water dip, to facilitate drying, or by exposure
to heated air. ‘The specified paint coating shall be applied as soon as practical after
the treated parts are thoroughly dry.
3.7.2 Control of the Type IV treatment - The determination of
hydrofluoric acid and the acid fluoride solutions shall be performed as specified in
3.6.4, 1 and 3.6.4.2 respectively. The sulfate-dichromate-hydroxide bath used
for galvanic anodizing shall be controlled by maintaining the pH between 5.6 and 6.0
with additions of a solution containing 5 percent by weight each of chromic acid
(CrOg) and concentrated sulfuric acid (H2804). A properly applied Type IV treatment
usually produces a coating that is uniformly dark brown to black. Time of treatment,
condition of bath, and composition of the alloy influence the color of the coating.
Gray and nonuniform coatings indicate that articles were not properly cleaned before
treatment or that the solution was depleted. Non-adherent coatings are usually
‘caused by too high a current density, too prolonged a treatment, or by too low a
bath pH. An increase in time required to secure a uniform coating also indicates
a depletion of the solution. Parts must be racked firmly for the proper galvanic
action to take place. Monel, stainless steel, or phosphor bronze racks may be
used.
19MIL-M-3171C
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20MIL-M-3171C
3.8 ‘Type VI treatment - The Type VI treatment or chromic
acid brush-on treatment can be applied to magnestum parts that require touchup.
‘This treatment, as well as Type I treatment, is generally used in refinishing
procedures or where parts and assemblies are too large to be immersed. The
‘Type VI treatment is less critical to apply than the Type I treatment by brush
application as detailed in 3.5.4, Also, the Type VI treatment is relatively
inexpensive, not harmful when trapped in faying surfaces and does not present
the toxicity hazards of the Type I treatment. Normal methods for removing oll,
grease, etc., as given in 3.2 are used prior to the treatment. It can be readily
applied to all alloys by brushing, dipping or spraying. ‘The solution composition
and operation are specified in Table VI
TABLE VI
SOLUTION COMPOSITION AND OPERATION FOR TYPE VI TREATMENT
Composition 1/ Operating
temperature | Tank construction
Material 2/ oz. °F
Chromic acid (CrO3) 3/ | 1-1/3 | 70 to 90" | Stainless steel, alumi-
Calerum sulphate 1 ‘num, vinyl polyethylene
(Ca804 + 2120) or rubber lined tanks.
1/ Avotrdupots or flutd ounces per gallon. Water 1s added to make one
gallon, Most tap water or purified water may be used.
2/ Chemicals should be added to the water in the order shown, and then
the solution stirred vigorously, either mechanically or by air agitation
for at least 15 minutes.
3/ Technical grade chromic acid (99.5 percent purity) may be used.
38.1 Brush application - Proper application by the Type VI
treatment requires that the surface of the parts be kept wet with the brush-on
solution for a sufficient time, usually about 1 to 3 minutes, to produce a brown
film. ‘The parts shall then be rinsed in cold running water, and dried, either
in an oven, or by exposure to a blast of hot air. Inno case, should the parts
be rinsed in hot water, Unlike brush application by Type I treatment, the time
‘between the pickling and cold water rinsing is not critical. In fact, where running
water is not feasible, the rinse step can be eliminated without materially altering
the coating effectiveness. The paint base properties are substantially equal
to that of the Type I treatment. The brown color of the coating is not altered
by chemical composition of the magnesium alloys. As with the Type I treatment,
‘Type VI treatment may be applied over previously prepared thin films of all the
‘Type treatments.
2MIL-M-3171¢
3.8.2 Operational explanations - Facilities that use and are
familiar with the Type I treatment may prefer to use this treatment for
touchup application. However, it should be noted in comparing the Types
and VI treatments for brush application, that the Type I solution is more
costly to prepare as well as presenting greater toxicity hazards, and requires
careful rinsing of the retouched part as an essential control factor Coatings
by the Type VI treatment are not adequate for interfaces used in electrical bonding
but are aatiefactory for use on entrapment areas of all magnesium assemblies.
‘Type VI processed coatings require paiting or sealing before exposure to
overnight, outdoor atmospheric conditions. Coatings by the Type VI treatment
can be varied from a brassy iridescence to a dark brown depending upon
treatment time. Up to 1 minute of treatment produces a brassy film and from
2 to 3 minutes a dark brown coating. The brush-on treatment shall not be less
than 30 seconds nor longer than 3 minutes, Prolonged treatment produces
loose powdery coatings similar to those listed in 3,5. 5.4. For best paint
adhesion, the dark brown coatings are preferred,
3.9 ‘Type Vil treatment - The Type VII treatment or the
fluoride anodizing treatment is essentially an anodic treatment followed by a
stripping operation to remove the fluoride coating and then post-treated with
8 corrosion preventative treatment to provide the optimum protection. The
anodizing and stripping portions of the treatment may be applied to all alloys
and forms. ‘The anodizing portion of the treatment is suitable to take the
place of shot or grit blasting as a means of cleaning magnesium alloys from
adherent foundry sand (see 3.2.2 and 3.2.2.1). Subsequent pickling operations
such as specified in 3.2.4.2 will therefore not be necessary. The anodizing
portion of the treatment system removes cathodic impurities at the surface.
3.9.1 Anodic treatment - The anodizing process 18 one step
treatment employing an aqueous ammonium bifluoride bath in which alternating
high voltage current generally produces a uniform clean white or pearly-gray
coating. With QE22A alloy, the coating will have a creamy or yellowish
appearance because of the silver in alloy composition,
3.9.1.1 Application - The anodizing treatment may be applied with
alternating current. Magnesium parts should be anodized by the fluoride treatment
prior to attaching dissimilar metal parts. Where inserts and attachments must
be in place before treatment, they must be adequately shielded. Suitable
masking material such as polyvinyl-butyral may be used for this purpose.
Steel studs may be fitted with rubber or plastic caps. Cast-in steel or copper
tubes may be plugged with rubber bungs. In suitable positions, magnesium
plugs may be fitted or magnesium blanking off plates may be applied to prevent
access of the bath solution to areas where it 18 required to prevent the process
from taking place. Certain chloride containing plasties are known to be harmful,
0 tests shall be performed prior to adopting any material for masking purposes.
22MIL-M-31710
3.9.1.2 ‘Treatment - Parts to be given the anodic treatment
need not usually require cleaning in accordance with other requirements of
this specification. Loosely held sand shovld be removed by knocking or brush-
ing from castings, Any thick layers of grease should be removed by solvent
cleaning (eee 3.2.1) to prevent contamination of the anodizing bath. The mag-
nesium parts to be treated are suspended in the anodizing bath. The work is
fixed in pairs in good electrical contact on electrode bars across the insulated
tank and suspended not less than 9 inches below the surface of the bath. The
work shall be arranged so that approximately equal surface areas are present
‘at each electrode. All parts of the fixed clamps below the bath surface shall be
of magnestum-rich alloy, such as AZ31, AZ63A, AZ91, or EZ33A. Because
of the relatively high voltage used to obtain the coating and the bath's excellent
polarization characteristics, the bath has a strong tendency to clean the magnesium
surface during the application of this coating, This further removes traces of
foretgn matter, graphite, corrosion products and other non-metallic films.
Good electric contact with the work is essential. Anodizing is carried out at
constant current in the bath whose composition ie detailed in Table VIL
‘The voltage is continuously raised to maintain the desired current density
as the resistance increases. The voltage 1s increased progressively until
120 volts are reached. Current flow is usually heavy at first, but diminishes
rapidly as impurities are removed and a coating of unbroken magnesium fluoride
1s formed in thelr place. When this occurs, the treatment may be regarded
a8 complete. After the indicated quantity of electricity has been applied, the
voltage 1s maintained for 10 to 15 minutes or until the current falls to less than
5 amperes per square foot. Parts shall then be removed and rinsed in hot
running water. Parts are then quickly dried by exposure to heated air.
3.9.1.3 Costing characteristics - A thin costing, magnestum
fluoride, less than 0.0001 inch 1s produced. The film itself has no measurable
thickness. The treatment leads to no detectable dimensional loss likely to
cause difficulty even when working to definite fine limits. The fluoride film,
after stripping does not prevent application of other chromate treatments such
as Types I, Il, or IV.
3.9.2 Post anodic treatments -
3.9.2.1 Chromic actd pickle ~ After the parts have been given
the anodizing treatment as specified in 3.9.1, they shall be boiled for 1 to 15
minutes in the chromic actd pickle bath listed in Table II (see 3.4.1) or that
given in Table VII. After the immersion period, the parts shall be rinsed in
cold water.
3.9.2.2 Dichromating treatment - The stripped and rinsed parts
shall then be immersed in a bath for the acid fluoride treatment (see 3. 6. 2)
for § minutes at room temperature, The parts shall then be rinsed and immersed
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4MIL-M-3171C
in the boiling solution specified for the Type III dichromate treatment for 30
minutes (see 3.6.3) After this immersion period, the parts shall be rinsed
in cold running water followed by a hot water dip to facilitate drying, or by
exposure to heated air. Controls for these dichromating treatments shall be
as detailed in 3.6.4.2 and 3.6.4.3. Operational difficulties and possible
explanations are contained 1n 3.6.4.4,
3.9.2.3 Other dichromate treatments - Where s0 specified in
the contract, purchase order or applicable drawing, other dichromate treat-
ments may be used than those detailed in 3.9.2.1 and 3.9.2.2, The dichromate-
nitric acid bath given in Table VII or that of Table III (see 3 5.1) may be used
in place of the boiling chromic acid bath (see 3.9.2.1) to strip the fluoride
film. The dichromate-mitric bath, used cold,leads to some dimensional loss and
should not be used on machined parts where permitted tolerances are small.
Controls and operational difficulties with this bath are detailed in 3.5.5.
A very satisfactory chromate film may also be produced by boiling the part
or component directly after the anodizing treatment (see 3.99. 1) in the dichromate
bath specified in Table VII for 40 to 60 minutes. After the immersion period
by either of the above two treatments the parts shall be rinsed in cold running
water, followed by a hot water dip to facilitate drying or by exposure to heated air.
‘The specified paint coating may be applied as soon as practical after the parts
treated im accordance to 3.9.2.2 or 3.9.2.3 are dried, or the chromated parts
may be sealed as specified in 3.9.3 prior to the painting operation
3.9.2.4 Dichromate treatment effectiveness - The presence of
the fluoride film on the anodized magnesium alloys does not prevent the appli-
cation of the dichromate treatment. The fluoride layer is slowly displaced
by the chromate film unless the fluoride anodized film is first removed by
boiling in chromic acid solution (see 3.9.2) It often happens that after chromat-
ing is complete, the displaced fluoride costing remains on the chromate surface
as a fme impalpable powder or bloom. This is not harmful. It does not interfere
in any way with adhesion of subsequent paint systems. If desired, however, it
can be removed by gently brushing or wiping with a soft cloth. However for
optimum results in the dichromating step, the fluoride should be removed as
there may be conditions where the loose anodized film would be harmful by
retaining moisture.
3.9.3 Surface sealing treatments - Parts receiving the Type VII
treatment should be given a surface sealing treatment to improve corrosion
resistance even if followed by a paint coating system. This is especially
applicable to castings. ‘The work, as soon as possible, after the dichromate
treatment (see 3.9.2 2 and 3.9.2.3) should be heated to approximately
392° F for about 1/2 hour. This effectively dries the surface and furthermore
drives moisture from surface flaws. The casting or work is cooled to about
140° F and dipped into a surface coating resin. After evaporation of the solvent,
25‘MIL-M-3171C
the casting 1s reheated to approximately 392° F for 15 minutes and the treatment
of cooling, dipping and reheating repeated until three coats of the resin have been
applied. Three such costs, suitably applied should total less than 0.001 inch in
‘thickness with a weight increase of less than 1-1/2 ounces per square yard of
surface.
3.9.3.1 ‘The surface sealing treatment may also be applied as
detailed in MIL-M-46080 and the surface coating resin may be in accordance
with the requirements of MIL-C-46079 for a baking type epoxy coating for
castings.
3.9.3.2 ‘The surface sealing can be applied equally to any of
the processes, Type I (see 3.5), Type Ill (see 3.6), Type IV (see 3.7),
‘Type VI (see 3.8), or Type VIII (see 3. 10), after the final drying operation and
prior to painting.
3.9.4 Racks for the Type VII treatment. - Racks made of mag-
nesium alloys such as AZ31B, AZ63A, AZ91C, shall be used in applying the
anodizing portion, Type VII treatment. Rubber, synthetic rubber, or poly-
vinylchloride covered, steel racks may be used. Design of the rack shall
be such as to ensure very firm contacts at the bus bar and to the part, The
portion of the rack connecting the bus bar shall be made of copper, bronze, or
brass which can be bolted to the lower part of the rack. The rack shall make
‘good contact with the magnestum parts. Stee! racks shall be exposed only at
the point where contact 1s made to the parts. The legs of the racks may be
wrapped with a suitable tape such as polyvinylchloride or to fit polyethylene
or rubber sleeves, especially at the "wind and water" line. Since the coating
acts as an insulator, magnesium racks shall be stripped of the coating at
the contact point by sanding prior to each use or by the use of chromic acid
pickle, specified in 3.4.1, or the chrome-pickle, specified in Table III for
‘wrought materials,
3.9.5 Control for Type VII treatment - The Type VII anodizing
treatment bath (see 3.9, 1) depletes slowly for all practical purposes. Depletion
{is indicated by roughness or an etched appearance in the coating. Replentsh-
ment of the bath can be accomplished by adding ammonium bifluoride solution.
Standard analytical methods for testing for fluoride may be used for controlling
‘the bath. The fluoride concentrate 18 not critical provided it exceeds the
minimum concentration,
3.9.6 Operational difficulties and possible explanation - The
following operational difficulties may be encountered during application of the
anodizing portion of Type VII treatment.
26MIL-M-3171C
(@) Castings which have received too short a treatment
will show some areas with a characteristic whitish
or pearl-gray film while other areas may appear
not to have responded,
(b) Castings which are not free from attached foundry
ands will have some areas darker than others. If
obstinate areas of foundry sands still remain after
treatment, or blemishes which are not being cleaned
up quickly as the rest of the observed surface of
the work, mechanical treatment with a stiff wire or
bristle brush may be given at this stage and the work
returned for a further short period of fluoride
anodizing.
(©) Painted parts or components should not be normally
treated until the bulk of the paint has been removed.
Paint films themselves are softened by reaction in
the bath. Nickel and copper electroplates can also
bbe removed by the treatment. Unless these precautions
are taken, contamination of the bath will result,
reducing bath efficiency.
(@) Too low a voltage or too short a time in the bath
will be usually indicated by a very thin sem(trans~
parent film, On machined surfaces or wrought material,
which is initially in good condition, such a thin film
may be acceptable.
(@) In hollow parts or components with re-entrant angles,
dark areas may remain in such recesses and indicate
gas entrapment. In such cases the items should be
turned about once or twice in the bath to ensure
complete contact with the liquid.
® An etched appearance may indicate too hot a bath,
possibly operation at too high a voltage, or a bath
too low in ammontum bifluoride. The strength of the
bath must not be allowed to fall below 10 percent.
A stronger solution will do no harm but is wasteful.
(@) A dense film may indicate the presence of acid radicals
other than fluoride. No foreign metals, organic
matter, salts or acid radicals other than fluoride
should be introduced into the bath. Pitting of the
work surface may also be caused by the presence of
the chloride ton.
arMIL-M-3171C
(h) The bath, during continuous operation must be stirred
well between batches of items with a wooden or plastic
pole to ensure that the upper layers of the liquid
are not depleted of the fluoride or become warmer than
the bulk of the bath. It may be advantageous to arrange
for continuous agitation of the solution by air stream.
A large volume of air should not be blown through
the bath as it promotes heavy current flow which in
turn creates undue heating. Only the mereet trickle,
sufficient to cause a gentle circulation of the liquid
1m the bath, shall be permitted.
() In the progress of operation, if the tendency of the
current to fall away to low values at any voltage
up to about 120 volts does not occur, observations
should be made to see if the anodizing solution, as,
specified in Table VI is too weak; a foreign metal
insert, rivet or other attachment is present; part of
the clamp that 1s not made of magnesium is below the
surface of the bath solution; the clamp, as specified
in 3.9.1.2 18 not of one of the materials detailed,
or the work 1s too severely contaminated. In the
latter case, this may arise from having been heavily
shot-blasted (see 3.2. 2) or from the presence in the
casting of one or more flux inclusions. It will be
found that when the last of the contammants, tron
particles, have been removed, the current during
anodizing will fall normally.
3.10 ‘Type VIII treatment - The Type VIII or chromate treat
ment provides a satisfactory paint base and protective coating on all magnesium
alloys, unlike the restrictive Type HI treatment (see 3.6) The coating may be
applied to the magnesium alloys by dip or brush. Type VIII treatment may be
substituted, when approved by the procuring activity, for the Types I, III or
VI treatments as well as the corrosion preventative treatment of the Type VII
‘The coating deposited 1s somewhat like that of the Type III, being dark brown
to light reddish brown in appearance. ‘The Type VIII treatment causes no
appreciable dimension changes and normally 1s applied after machining.
3.10.1 For alloy containing more than one percent aluminum -
Parts of magnesium alloys containing more than one percent aluminum shall be
cleaned in accordance with other requirements of this specification. For parts
of magnesium alloys with 3 5 percent aluminum or less, such as AZ-31, the
chromic-nitrate pickle (see 3.4.2) shall be used, whereas with those alloys
having an alurmnum content over 3.5 percent, such as AZ-61, AZ-81, and
28MIL-M-s10
AZ-91, the chromic-nitric-HF pickle shall be used (ace 3. 4. 6) following
the alkaline cleaning. If mill pickled stock is to be treated, parts shall be
tmmersed in the acid pickle for 15 to 30 seconds, but if unpickled or cast
materials are used for parts, the immersion time in the acid pickle solution
shall be from 2 to 3 minutes. The parts shall then be rinsed prior to treat
ment in the chromate bath, Solution No. 1. The Solution No. 1 composition
amd operation are contained in Table VIII. After the parts have been treated
with the chromate bath, Solution No. 1 for 15 to 30 seconds, the parts shall
‘be double rinsed in cold running water followed by a hot water dip to facilitate
drying, or by exposure to heated air. Drying temperatures in the range of
160 to 200° F will produce a dark brown coating of increased hardness and
‘reduced solubility.
3.10.2 For alloys containing less than one_percent_alumimum -
Parts of magnesium alloy without or containing less than one percent aluminum
shall be cleaned in accordance with other requirements of this specification.
‘The chromic-nitrate solution (see 3. 4.2) may be used for acid pickle under the
same conditions for stock as recommended in 3.10.1. After the rinsing,
following the pickling treatment, the parts shall be treated in the chromate
bath, Solution No. 2. The Solution No. 2 composition and operation are contained
in Table VII. Further treatment is as detailed in 3.10.1
3.10.3 Control of the Type VIII treatment - The solution baths
used for the chromate treatment shall be controlled by maintaining the pH
between 0,2 and 0.6 for Solution No. 1 and between 0.6 and 1.0 for Solution
No. 2 by adding the chromate salts and hydrochloric acid in the original pro-
Portions. The wetter detergent should be controlled by adding 0.034 ounce of
the detergent for every 5 ounces of the chromate salts when the solution bath
is in constant use. When the solution bath has been allowed to stand for a week
or more, and a thin foam layer does not form during treatment, 0.034 ounce
of the wetter detergent shall be added for every gallon of the bath so as to
provide a thin blanket of foam during the processing. Scratch Type VIII treat-
‘ment coatings can easily be touched up by swabbing with the solution used for
working the part and rinsed with flowing water.
3.10.4 Bath life ~ Repeated replenishment additions may be made
‘until satisfactory coatings are no longer obtained (even though the chromate
solution is within its correct operating limits). ‘The solution should not require
dumping until the total replenishment additions are approximately one and a half
‘to double the original make-up amounts, and the amount of work treated is
equivalent to spproximately 175 square feet of alloy surface per gallon of the
working bath.
3.10.5 ational difficulties and possible explanations -
following operational difficulties may be encountered during chromate treatment:
29‘MIL-M-3171C
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MIL-M-3171C
Failure to form coatings:
1. The pH of the solution 18 too high. Solutions:
should be as spectfied in 3.10.3.
2. The solution may be too cold. The solution
temperature shall be as specified in Table VIII.
3, The metal is not properly degreased and cleaned.
The part was not pickled prior to treatment in
the chromate solution.
4, ‘The ratio of the acid concentration to the chromate
salts may be too low by using the improper amount
of acid or strength.
Non-adherent powdery coatings:
1, The part may have been of magnesium alloys
containing less than 1 percent aluminum and
the improper chromate Solution No. 1 used on
the part. This can be eliminated by treatment
with the bath ae specified in 3.10.2 and
Table VI
2. ‘The pl of the solution 1s too low. Solutions
should be as specified in 3.10.3.
3. ‘The metal 1s not properly degreased and cleaned.
‘The part was not pickled prior to treatment in
the chromate solution.
4, The ratio of the acid concentration to the chromate
salts may be too high by using improper amount
of acid or strength
Excessive smut on parts:
1. The parts may have excessive aluminum smut
on aluminum-bearing alloys by being kept in
the bath too long. This may be minumized or
virtually elimmated by proper treatment time
as specified in Table VII
aMIL-M-3171C
3.11 Other treatments - Other treatments may be substituted
for the specified treatments when approved by the procuring agency. (See 6.8.)
3.12 General - The sequence of the operations to be used for
the application of treatments specified herein shall be in accordance with
Figures 1 and 2. Treated articles shall be primed as soon as practical after
thorough drying. Parts which are handled or processed after sealing or remain
unprimed for extended periods shall be cleaned prior to painting. Other methods
of exposing the parts to the treatment solution than by immersion may be used
provided the other requirements of the specification are met. Other types of
tank construction other than those specified may be used provided they do not
have an adverse effect on the solutions to be contained.
3.13 Dimensional changes - Unless otherwise specified, the
dimensional changes resulting from treatment shall comply with the requirements
stated in Table IX when tested in accordance with 4.4.5. The indicated dimen-
sional changes do not include those resulting from the various cleaning processes.
‘It should be noted that the maximum corrosion resistance can be achieved even
with the minimum value of the range for each type. No significant advantages
are gnined by deposits heavier than the specified range.
TABLE IX
DIMENSIONAL CHANGE REQUIREMENTS OF COATINGS IN MILS
Process min. | Max. | Typical 1/
‘Type - Chrome pickle 0.6 | 1.0 oe
Type Ill - Dichromate : - 2
Type IV ~ Galvanic . - 7
‘Type VI - Chromic acid brush-on : - 2
Type VII - Fluoride anodizing : - xy
Type VIM - Chromate - - 2
1/ On AZ31B magnesium alloy.
2/ No appreciable dimension changes.
3/ No appreciable dimension changes with chromic acid pickle and Type HI
process
3.14 yecial requirements In addition to the requirements
specified above, coating shall conform ta any special requirements specified
in the contract or purchase v1 sles
32MIL-M-3171C
FIGURE 1. FLOW SHEET FOR CLEANING CYCLESMIL-M-3171C
FIGURE 2. FLOW SHEET FOR TREATMENT CYCLES.MIL-M-3171C
4. QUALITY ASSURANCE PROVISIONS
4 Responsibility for inspection - Unless otherwise specified
in the contract or purchase order, the supplier is responsible for the performance
of all inspection requirements as specified herein. Except as otherwise specified,
the supplier may utilize his own facilities or any commercial laboratory acceptable
to the Government. The Government reserves the right to perform any of the
inspections set forth in the specification where such inspections are deemed
necessary to assure supplies and services conform to prescribed requirements.
4.2 Lot - A lot shall consist of all processed and treated
parts of the same type produced or completed within a period of time specified
by the procuring activity with no change in process. Lot size may also be
determined by the procuring activity as a number of square feet of material
surface processed per umt volume of the treatment bath.
4.3 Sampling -
4.3.1 Visual examination - Random sampling for visual examina-
tion and workmanship shall be conducted in accordance with MIL-STD-105,
Inspection Level If, and with an AQL of 1. 5 percent defective.
4.3.2 For determination of dimension change - A number of
pieces corresponding to Inspection Level S-4 of MIL-STD-105 shall be selected
from the lot prior to treatment; provided however that the sample shall consist
of not less than ten articles, or of the entire lot, whichever is smaller. ‘The
AQL shall be 1,5 percent unless otherwise specified.
4.3.3 Concurrently anodized specimens - When the use of
‘a sample of anodized items for the determitiation of the dimensional change
is impracticable, suitable specimens composed of the same basis metal and
processed concurrently with the lot which they represent may be used for the
dimensional change determination.
44 Examinatio
4.4.1 General ~ Examination of equipment, process and treated
parts shall be made to ascertain compliance with this specification. The continued
effectiveness of equipment and procedures, after approval by the government,
is the responsibility of the supplier.
4.4.2 Materials - In case of doubt, the supplier may be required
to furnish satisfactory evidence of compliance of materials used in processing
with the requirements of this specification.
38MIL-M-3171¢
443 ‘Treatment examination -
44.3.1 ‘Treatment examination shall consist of the observation of
time of treatment, operating temperature, current density, voltage, and all
other pertinent treatment conditions.
44.3.2 ‘The process shall be examined for compliance with the
‘requirements of this specification at the beginning of each prodaction run
and at the beginning of the reuse of any equipment following any period of
one week or longer during which the equipment is not used for production in
accordance with this specification. In addition, sufficient periodic inspections
of the process shall be made to ensure compliance with the requirements of
this specification.
4.4.3.3 ‘The supplier shall maintain a permanent record of the
history of each processing bath, showing all additions of chemicals to the bath,
the results of all analyses performed and the quality of parts of each kind
Processed in the bath. This record shall be available to the Government at
all times.
aad Product examination - The samples of treated parts
selected im accordance with 4.3.1 shall be visually examined to determine
conformance with the requirements of this specification in regards to workman-
ship, quality of the treated surface and any other requirements specified by the
procuring activity. A visual examination of the processed surface shall be
‘made for complete and uniform coverage. Surfaces shall be examined for the
coloring and general characteristics, described herein, peculiar to the type
treatment being examined, which shall be an indication of satisfactory time of
treatment and condition of solution. The color shall be a reasonable close
approximation to that of a sample consisting of a treated piece or pieces agreed
‘upoa as a standard by the supplier and the procuring activity, if 90 agreed won
oF specified in the contract or order.
445 Dimension determination -
4.4.5.1 ‘Measurement - The thickness of each piece selected prior
to treatment shall be determined by measuring with a micrometer which reads
accarately to 0.0001 inch. ‘The pieces shall then be processed concurrently
‘with the remainder of the lot. The pieces shall be distributed throughout
the various batches during processing #0 as to be representative of the entire
lot. The thickness of each piece shall be determined after treatment by
measuring the same location as before. The dimensional changes of each
piece shall be determined from the difference of the two measurements.MIL-M-3171
4.4.6 Other tests - Treated pieces shall be tested for con-
formance with any special requirements specified in the contract or order.
‘The tests shall be performed according to the methods specified therein.
4.5 Rejection ~
4.5.1 For nonconformance of process - Fatlure to conform
to any of the requirements of this specification pertaining to treatment con-
ditions shall be cause for rejection of the process. In the event unsatisfactory
quality 1s indicated by mspection, the contractor shall be promptly notified,
and all work which 1s readily obtainable and which was processed under
doubtful conditions, shall be rejected unless the contractor demonstrates
its suitability for aircraft use to the satisfaction of the procuring activity.
In addition, no further work will be accepted until the contractor demon-
strates to the satisfaction of the procuring activity that the necessary
improvements in the processing have been accomplished.
4.5.2 For nonconformance of coating - If a sample of coated
part or article fatls to conform to the requirements of this specification,
including any special requirements of the contract or purchase order, the
lot represented by the sample shall be rejected. Rejected lots may be
submitted for acceptance after the lot has been reprocessed or subjected
to 100 percent inspection by the contractor in order to remove any defective
tems and after any deviations from the specified process conditions
responsible for the failure of the coating shall have been corrected by
the contractor.
5. PREPARATION FOR DELIVERY
5.1 This section 18 not applicable to this specification.
NOTES
6.1 Intended use -
6.1.1 ‘Type 1 Chrome pickle treatment - For temporary
storage, domestic shipment, electrical bonding, touching up of previously
treated work, and brush application when permitted. Applicable to all
alloys when close dimensional tolerances are not required. Parts pro-
cessed by this treatment are not to be subjected to temperatures above
450° F,
61.2 ‘Type II - Dichromate treatment - For general long
‘time protection of all alloys except EK30A, EK41A, HM21A, HM31A, Lal4iA,
HKS1A and MIA, including work for which close dimensional tolerances
are required. Parts processed by this treatment are not to be subjected
to temperatures above 550° F.
37MIL-M-3171C
6.1.3 ‘Type IV - Galvame anodizing treatment - For general
long time protection of all alloys when close dimensional tolerances are required.
Parts processed by this treatment are not to be subjected to temperatures
above 550° F
6.14 ‘Type VI - Chromic-acid brush-on treatment - For temporary
storage, protective touchup of previously treated work, and brush application
where parts and assemblies are too large to be immersed. Applicable to all
alloys when close dimensional tolerances are not required. Parts processed
by this treatment are not to be subjected to temperatures above 450° F.
6.1.5 ‘Type VII - Fluoride anodizing treatment ~ For cleaning
of magnesium alloys asa substitute for shot or grit blasting, by providing a
relatively inert film when close dimensional tolerances are required and a
good base favorable for the other type treatments, such as the Type III.
6.1.6 ‘Type VIII - Chromate treatment - For general long
time protection of all alloys where close dimensional tolerances are required.
Parts processed by this treatment are not to be subjected to temperatures above
550° F,
62 Ordering data - Invitation for bids, contract or orders
should specify the following:
a, Title, number, and date of this specification.
b, Treatment type required (see 1.2.1)
© Special requirements, if applicable (see 3 13)
. Availability of treatment records (see 4.4.
© Other tests, if applicable (see 4.4.6)
£ Other treatments, if approved (see 6 4)
6.3 Post treatment - The term "post-treatment" means
any treatment used after anodizing Because all anodic coatings are more or
less porous, it 18 advisable to follow the anodize treatment with a post treat-
‘ment of chromate and/or an impregnation of a suitable clear baked epoxy
resin, Several specially developed epoxy resin formulations are commercially
available for impregnation treatment (see 3 9 3)
64 Other treatments ~
38MIL-M-3171C
6.4.1 Chemical conversion coatings ~ In addition to the
chemical conversion coatings detailed in this specification (Types I, HI, VI,
and VIII) there are others such as the half-hour RAE, chrome manganese
and the selenious acid. Coatings produced from these treatments range in
color from brown to black. Each has its own advantages and disadvantages.
For example, the RAE requires 30 minutes in the bath and the pH of the
solution is critical (5.90 to 6.18) However it exhibits the maximum corroston
protection and 1s an excellent paint base. ‘The chrome-manganese treatment
has excellent abrasion resistance, but 1s improved by baking at 356° F for
30 minutes. The range of pH tolerance of the chrome-manganese bath
(4.0 to 6.0) makes easy control. The selenate coatings are used to repair
damaged chromate type coatings but are not suitable as a base for paint systems
In addition, selenates are more toxic than the chromates.
6.4.2 Anodic coatings - In addition to the anodic coatings
detailed in this specification (Types IV and VII), MIL-M-45202 details several
treatments most often used with magnestum, namely the Dow 17, the HAE
and CR-22, Anodic coatings on magnesiumare much softer,lese dense and
less protective than they are on aluminum. Usually, anodic coatings on
‘magnesium require an additional treatment with an organic finish or an
morganic sealant. In addition to the coatings detailed in MIL-M-45202, the
‘Manodyz process 1s often used for an anodic coating. The coating produced
1s one of excellent wear resistant with good dielectric properties
6.4.3 Other coating systems - The stannate protective coating
for magnesium consists partly of a magnesium-tin-hydroxide and partly of
metallic tin, This type coating has some of the properties of a chemical
conversion coating and some of the properties of a metallic coating. The
film, formed from a stannate bath, provides good corrosion resistance and
can be used as a base for paint systems.
6.5 o ‘eferences - The correlation between the types
used in this specification, the previous designations and the common commercial
designations for the magnesium alloy processes are indicated in Table X.
6.6 Caution - Due consideration should be given by con-
tractors to the occupational health hazards associated with the processes
covered by this specification.
6.6.1 Among the special precautions indicated for the more
significant hazards are: the use of protective clothing; the avoidance of skin
contact with organic solvents, as well as avoidance of the inhalation of their
vapors; protection during sandblasting operations; avotdance of skin contact
‘and protection against the mhalation of alkali fumes or mists; the avoidance
of skin contact with nitric, sulfuric, phosphoric, and hydrofluoric acids,MIL-M-3171C
TABLE X
CORRELATION OF TREATMENT TYPES
treatment | mtiew-sinic | auit-m-eime | Motem-siria| — Sommercial
rome Prekie Type Type typet [Bow no. 1
MACroning 101
eatea Chrome | aeteted | detetea typem | pow No. 10
Piokle
prchromate tyem | tyem | typem | dow wo. 7
MACrohiag D-7
caivanic awe | tye | type | pow No. 3
Anedeing MACroNag D-9
cavone deleted | deleted type v | pow No 12
‘anodizing
rome Acta tye | Tye wl : Dow No. 18,
Brushon MACroMag D-19
iuoride ype va ; Magnesium Elektron
Anodizing
Jcoromate ype VI : Inlte No. 18
protection of the eyes by proper safety goggles, and the avoidance of the nhala-
tion of their vapors or fumes; and protection against skin contact and inhalation
of chromium compounds.
6.6.2 Storage and treating tanks should be provided with such
hoods and other ventilating equipment as 1s necessary to prevent atmospheric
contamination,
6.6.3 In the handling of acids or alkalies, rubber gloves and
protective clothing should be worn. Accidental contact should be followed by
speedy removal of the excess acid or alkali by blotting with clean mechanics
waste, or a similar agent, after removal of the soiled clothing and shoes.
Profuse irrigation of the surfaces mvolved should then be done with large
quantities of water. Special care should be taken to avoid all skin contact
with hydrofluoric acid.
6.64 A physician should be consulted 1n all cases of contamina-
tion of the skin with any of these acids and also in cases where inhalation of
vapors or fumes causes respiratory distress
40MIL-M-3171C
6.6.5 Acid pickling of castings sometimes results in formation
of a gray powder layer which can spark or ignite easily thus presenting a
defimte safety hazard. Although this powder is usually associated with chromate
type coating, particularly Type I, it may also occur on castings treated in such acid
pickles as sulfuric (see 3.4.3), nitric-sulfuric (see 3.4.4), etc., that are free
of chromates. This powder results from excessive treatment time and can be
elimmated by good production practices (see 3.5. 5. 4).
6.7 Changes from previous issue - The outside margins of
this specification have been marked "#" to indicate where changes (deletions,
additions, etc ) from the previous issue have been made. This has been
done as a convenience only and the Government assumes no liability whatsoever
for any inaccuracies in those notations. Bidders and contractors are cautioned
to evaluate the requirements of this document based on the entire content as
written irrespective of the marginal notations and relationship to the last previous
issue.
Custodians Preparing activity:
Army - MR Navy - AS
Navy - AS (Project No. MFFP-0001)
‘Air Force - 11
Review activities:
‘Army - MR, MI, MU, WC
Navy - AS, OS
Aur Force - 11, 69
User activities
Army - EL, GL.
Navy ~ SH, ES
Air Force ~ None
Review/user information is correct as of date of this document. For future
coordination of changes to this document, draft circulation should be based
on the information in the current DODISS.
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