U.S. patent application number 10/389836 was filed with the patent office on 2003-09-25 for stainless steel electrolytic coating.
This patent application is currently assigned to United States Steel Corporation. Invention is credited to Paulina, John M., Polinski, Pamela A..
Application Number | 20030178314 10/389836 |
Document ID | / |
Family ID | 28045611 |
Filed Date | 2003-09-25 |
United States Patent
Application |
20030178314 |
Kind Code |
A1 |
Polinski, Pamela A. ; et
al. |
September 25, 2003 |
Stainless steel electrolytic coating
Abstract
Stainless steel coatings are formed on metallic substrates by
employing the metallic substrates as a cathode in an aqueous
electrolyte containing chromium, nickel and iron in specified
concentrations or ratios. A coumarin leveling agent is preferably
used. A product is obtained having a coating comprising, in weight
ratios, weight ratios chromium 6-15:nickel 3-5:iron 32-39; the
product has the appearance and many of the properties of monolithic
stainless steel.
Inventors: |
Polinski, Pamela A.; (North
Huntingdon, PA) ; Paulina, John M.; (Level Green,
PA) |
Correspondence
Address: |
William L. Krayer
Attorney at Law
1771 Helen Drive
Pittsburgh
PA
15216
US
|
Assignee: |
United States Steel
Corporation
|
Family ID: |
28045611 |
Appl. No.: |
10/389836 |
Filed: |
March 17, 2003 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
60366194 |
Mar 21, 2002 |
|
|
|
Current U.S.
Class: |
205/99 ; 205/243;
205/255 |
Current CPC
Class: |
Y10T 428/12965 20150115;
C25D 3/562 20130101 |
Class at
Publication: |
205/99 ; 205/243;
205/255 |
International
Class: |
C25D 003/56 |
Claims
1. Method of forming a coating on a metallic substrate comprising
employing said metallic substrate as a cathode in an aqueous
electrolytic bath comprising 35-65 grams per liter chromium
chloride, 9-15 grams per liter nickel chloride, and 4-8 grams per
liter ferrous chloride, and a leveling agent in an amount effective
to enhance brightness in said coating, and subjecting said bath to
an electric current effective to deposit chromium, nickel and iron
as a coating on said substrate while maintaining said metallic
substrate in turbulent contact with said bath.
2. Method of claim 1 wherein said chromium in said bath is
maintained substantially entirely in the trivalent state.
3. Method of claim 1 wherein said current is 50-500 amperes per
square foot of surface on said substrate.
4. Method of claim 1 wherein said bath is maintained at a pH of 0.8
to 2.0.
5. Method of claim 1 wherein said leveling agent comprises a
coumarin leveling agent.
6. Method of claim 1 wherein said bath includes a stress
reliever.
7. Method of claim 1 wherein said metallic substrate comprises
carbon steel.
8. Method of claim 7 wherein said carbon steel has a precoat
comprising nickel.
9. Method of claim 7 conducted continuously, wherein said carbon
steel is in the form of steel strip, said steel strip is passed
continuously through said aqueous electrolytic bath.
10. Method of claim 9 wherein said chromium chloride, nickel
chloride, and ferrous chloride are replenished continuously or
intermittently to maintain said grams per liter.
11. Method of claim 9 including continuously or intermittently
removing at least one breakdown product of said leveling agent and
continuously or intermittently replenishing said leveling
agent.
12. Method of claim 7 wherein said carbon steel is formed into an
incipient article prior to employing it as the cathode in said
bath.
13. Method of claim 1 wherein said coating comprises 12-30%
chromium, 6-10% nickel, and 64-78% iron.
14. Method of claim 13 wherein said coating comprises 17-20%
chromium, 7-9% nickel, and 71-76% iron.
15. Method of claim 1 followed by removing said metallic substrate
from said bath and heat treating it whereby said metallic substrate
has a corrosion resistance similar to that of stainless steel.
16. Method of claim 9 wherein said bath includes a stress reliever
in an amount effective to inhibit the formation of microcracks in
said coating, followed by forming a three-dimensional steel product
from a portion of said steel strip, said three-dimensional steel
product being substantially free of microcracks.
17. Method of claim 1 wherein the anode in said aqueous
electrolytic bath comprises stainless steel and wherein at least a
portion of said chromium, said nickel, and said iron deposited from
said bath is replenished sacrificially from said stainless steel
anode.
18. A product made by the method of claim 15.
19. Steel having a coating comprising 12-30% chromium, 6-10%
nickel, and 64-78% iron, said coating being substantially free of
microcracks, having a brightness similar to monolithic stainless
steel, superior adherence as demonstrated in fold and drop tests,
and a substantially consistent distribution of chromium, nickel and
iron throughout said coating.
20. Steel of claim 19 wherein said coating comprises 16-22%
chromium, 7-9% nickel, and 71-76% iron.
21. Steel of claim 19 wherein said coating is 1-100 micrometers
thick.
22. Steel of claim 19 having an undercoat of nickel.
23. An article made of the steel of claim 19.
24. An aqueous solution useful as an electrolytic bath for
depositing a coating of stainless steel on a metallic substrate
comprising 35-65 grams per liter chromium chloride, 9-15 grams per
liter nickel chloride, and 4-8 grams per liter ferrous chloride,
said solution having a pH of 0.8 to 2.0 and including a small
amount of hydrofluosilicic acid and a small amount of a coumarin
leveling agent.
25. An aqueous solution of claim 24 including at least one of (a)
ammonium chloride in an amount up to 100 g/L, (b) potassium
chloride in an amount up to 60 g/L, and (c) citric acid in an
amount up to 100 g/L.
26. Method of forming a stainless steel coating on a steel
substrate, said stainless steel coating comprising chromium, nickel
and iron within the range of weight ratios chromium 6-15:nickel
3-5:iron 32-39 comprising electrolytically depositing said metals
from an aqueous electrolyte containing chromium, nickel and iron
dissolved in weight ratios of chromium 53.4-79.12:nickel
12.9-31.8:iron 6.4-19.9.
27. Method of claim 26 wherein said aqueous electrolyte also
includes a coumarin leveling agent in an amount effective to
improve brightness of said coating.
28. Method of claim 27 which is continuous and wherein a breakdown
product of said coumarin leveling agent is continuously or
intermittently removed from said aqueous electrolyte.
29. Method of claim 26 wherein said chromium, said nickel, and said
iron are present in said aqueous electrolyte substantially entirely
in the form of chlorides.
30. Method of claim 26 wherein said chromium in said aqueous
electrolyte is substantially entirely trivalent.
Description
RELATED APPLICATION
[0001] This application incorporates in full and claims the full
benefit of provisional application No. 60/366,194 filed Mar. 21,
2002.
TECHNICAL FIELD
[0002] In an electrolytic bath, a metallic substrate is coated with
the constituents of stainless steel. The invention includes steel
and steel articles coated with a stainless steel composition as
well as the process for making it, and the electrolytic bath.
BACKGROUND OF THE INVENTION
[0003] Stainless steel is useful and desirable for many purposes,
but, in a monolithic form, it is expensive. It would be beneficial
for many purposes to have a practical method of providing a less
expensive carbon steel with a coating of a stainless composition.
The carbon steel could be a three-dimensional preform, or in the
form of strip. In either case, the product should be able to
withstand conventional forming techniques and procedures after
coating which might generate microcracks, for example, at points of
stress.
[0004] One of the difficulties in developing an electrolytic
coating process for the deposition of stainless steel coatings is
that formability is generally better without a coating, and
corrosion protection is generally achieved by application of a
coating. A major objective of the present invention therefore is to
achieve a process capable of producing a coated sheet steel product
which can be formed without significantly reducing the corrosion
resistance imparted by the stainless steel coating.
[0005] A coating formed by electrodeposition which does not include
chromium, nickel and iron would not normally be thought of as a
stainless steel coating. Accordingly, various descriptions in the
prior art of the deposition of chromium or chromium and nickel, or
other combinations of metals other than chromium, nickel and iron,
do not achieve the above described objective of making a stainless
steel coated product. The following. U.S. patents describe the
deposition of nickel and/or chromium: Lashmore U.S. Pat. No.
4,461,680, Tajima et al U.S. Pat. No. 4,142,948, Gyllenspitz et al
U.S. Pat. No. 3,954,574, Safranek U.S. Pat. No. 2,990,343, and
Yeshida U.S. Pat. No. 2,766,196.
[0006] We are aware, however, of a few workers in the prior art who
used all three metals in an electrolytic bath for coating carbon
steel. See, for example, "Deposition of Stainless Steel from
Chloride Baths" by Larissa Domnikov, Metal Finishing, Feb. 1970, pp
57-63. This article focuses on the addition of aluminum to the
bath. See also U.S. Pat. No. 4,610,763 to Malcolm Law, which
deposits a stainless-like coating on top of a nickel flash. See
also Schiffmann et al U.S. Pat. No. 3,374,156. Larisson Dominikov,
"Iron-Nickel-Chromium Baths" Metal Finishing, March 1964, pp 61-65;
M. Sarojamma and T. L. Rama Char, "Electrodeposition of
Iron-Chromium-Nickel Alloys, Metal Finishing, September 1972, pp
36-42, A. Gowri and B. A. Shenor, "Stress in Chromium-Nickel-Iron
Alloy Deposits", "Metal Finishing, June 1972, pp 30-34;
"Iron-Chromium-Nickel Deposition" by S. Gowri, P. L. Elsie and B.
A. Shenoi, Metal Finishing, December 1967, pp 67-70. A trimetal
coating deposited from a dimethyl formamide/urea bath was heat
treated, as described by M. El-Sarif et al in "Effect of Heat
Treatment in Microstructure of Cr--Ni--Fe Coatings Prepared by
Electrodeposition", Materials Science Forum, vols. 163-165 (1994),
pp 633-638, Trans-Tech Publications; Kagachika et al U.S. Pat. No.
4,673,471; Renton et al U.S. Pat. No. 4,093,521.
[0007] The reader may be interested in the prior art process
described by Schaer in U.S. Pat. No. 2,927,066, which does not use
a leveling agent. Also, where the sources for iron, chromium and
nickel are sulfates, the processes of the prior art tend to be
deficient in terms of coating adhesion and uniformity. See Machu et
al U.S. Pat. No. 3,093,556 and Schiffinan et al U.S. Pat. No.
3,374,156. The percent of chromium in a nickel chromium bath is
controlled with the use of EDTA, in Stromatt et al U.S. Pat. No.
3,888,744.
SUMMARY OF THE INVENTION
[0008] We have invented a method of coating a metallic substrate
with stainless steel. Our method includes employing the metallic
substrate as a cathode in an aqueous electrolytic bath comprising
35-65 grams per liter chromium chloride, 9-15 grams per liter
nickel chloride, and 4-8 grams per liter ferrous chloride, and
subjecting the bath, under agitation, to an electric current
effective to simultaneously deposit chromium, nickel and iron as a
coating on the substrate. The substrate preferably is carbon steel,
which may or may not be precoated with copper or nickel such as by
a nickel flash coating. The electrodeposition is effected by
imposing a current of 50-500, more preferably 100-300, and most
preferably 150-250 amperes per square foot of surface to be coated.
Graphite or other conventional anodes may be used, but a stainless
steel anode is preferred. A stainless steel anode is to an extent
sacrificial and generally helps to maintain the chromium, nickel
and iron contents of the bath within the desired range as they are
deposited on the substrate. Also preferably, the pH is held at 0.8
to 2, more preferably 1-1.5, and a buffering agent is included in
the bath, such as ammonium chloride. We have also found that the
quality of the coating is improved by including one or more
leveling agents, preferably coumarin. Citric acid also helps to
keep the rate of deposition of the metals consistently in the
desired proportions while simultaneously acting as a buffer. A
small amount of hydrofluosilicic acid helps to maintain current
efficiency by contributing to maintaining the chromium ions in the
trivalent state.
[0009] Our process is preferably a continuous one, so a steel strip
can be passed through the electroplating bath. We have found that
if the three metals--chromium, nickel, and iron--are initially
present in certain ranges of ratios, as detailed below, a coating
on the substrate will be formed having the desired, but entirely
different, ranges of ratios similar to stainless steel.
[0010] Our invention also includes a metallic substrate having a
coating comprising, by weight, 12-30% chromium, 6-10% nickel, and
64-78% iron. The three metals are substantially evenly distributed.
Preferably the coating will comprise 16-22% chromium, 7-9% nickel,
and 71-76% iron, the coating having excellent brightness, adherence
and levelness. The coating may also include small amounts of other
metals such as copper, but preferably such other metals will not
exceed 2% by weight of the coating. In any case, trivial amounts of
other metals may enter the bath from various sources and be
deposited on the cathodic substrate. Our preferred product is
carbon steel having such a stainless steel coating 1-100,
preferably 2-50, and most preferably 3-25 micrometers thick. Most
preferably the product is in the form of a coated steel strip. Our
coated steel strip is substantially free of microcracks in the
coating. As is known in the art, microcracks are small cracks not
visible to the unaided eye which sometimes form in electroplated
coatings, and can run either vertical with respect to the substrate
or parallel. The coating will preferably also be uniformly
distributed, and the adherence of the coating will also be
superior. Our coated product will exhibit corrosion resistance
comparable to monolithic stainless steel.
BRIEF DESCRIPTION OF THE DRAWINGS
[0011] FIG. 1 is a triangular depiction of metals concentration in
the bath.
[0012] FIG. 2 is a triangular depiction of metals percentages in
the coating.
DETAILED DESCRIPTION OF THE INVENTION
[0013] We have conducted experiments which demonstrate our
invention. In particular, an aqueous bath has been made up having
the following components:
1 Bath A Ingredient Amount CrCl.sub.3 50 g/L NH.sub.4Cl 100 g/L KCl
50 g/L NiCl.sub.2 12 g/L Citric Acid 3 g/L Hydrofluosilicic Acid 2
g/L TRITON X-100.sup.1 1 ml/L Coumarin.sup.2 1 g/L FeCl.sub.2 6 g/L
.sup.1TRITON X-100 is a well-known surfactant.
.sup.21,2-benzopyrone.
[0014] The bath was contained in a reservoir and continuously
pumped through an electrolytic cell where the subject metallic
substrate was retained and connected as the cathode. The anode used
was stainless steel and a current was imposed to provide about 200
Amperes per square foot of surface on the cathode substrate to be
coated. The pH was maintained between 1 and 1.5.
[0015] As a result of various iterations of the use of such a bath,
products were obtained having a coating about 10 microns thick and
a consistent proportion of metals as follows: 16-22% Cr, 64-78%
iron, and 6-10% nickel, having excellent brightness, levelness and
adherence; the product was substantially free of microcracks. Other
thicknesses from 1 to 100 micrometers or more are readily
obtainable with variations of the duration of electrolysis.
[0016] A typical coated carbon steel sample A made in such a bath
was found to have a coating containing, in weight percent, 18
chromium, 74 iron, and 8 nickel. Another coated carbon steel
sample, B, contained 20% chromium, 74% iron, and 6% nickel by
weight in the coating. It was subjected to bend tests at
120.degree. and 180.degree. (the sheet was bent to 120.degree. and
180.degree. with respect to itself). Tape was applied and removed
from the outer surface of the bend. No flaking or powdering of any
sort was observed. The same sample was subjected to drop tests of
120 and 150 inch-pounds and again no powdering or flaking was
observed when a tape was pulled from the impacted area. On a scale
of 0-5, where 0 is the best, "in-house" ratings were awarded as
follows: 120.degree. bend test: 0.0-0.5; 180.degree. bend test:
0.0-0.5; 120 in-lb impact: 0.0-0.5; 150 in-lb impact test: 0.0-0.5.
Brightness of virtually all the products made under various
conditions within the above stated parameters was similar to
monolithic stainless steel or a chrome-plated substrate. No
corrosion was observed after 96 hours in 100% humidity at
100.degree. F.
[0017] Conversion of the chromium in the bath to the hexavalent
state should be minimized; if a significant portion of the chromium
is allowed to convert, the desired form of chromium may become
quickly depleted and a consistent product will not be made.
Moreover, hexavalent chromium is environmentally undesirable, and
reduces the efficiency of the electrodeposition process. A major
factor in maintaining the chromium in the trivalent state is the
use of turbulence in the bath and particularly where the bath
contacts the cathode. In the absence of agitation, drifting of the
cathodic potential may result in a buildup of Cr.sup.++. In the
case of a preformed, three-dimensional workpiece, the agitation
should be provided by a pump or agitator; in the case of steel
strip, passing the strip through the bath may be sufficient, or the
agitation may be augmented by additional turbulent motion of the
bath provided by a pump.
[0018] Maintenance of the Metal Contents and Ratios
[0019] The chromium, nickel and iron contents of the bath are
established primarily by the initial concentrations, as indicated
above. The rate of deposition of the coating is the main factor in
the rates of depletion of the chromium, nickel and iron in the
bath, but they are deposited at different rates with respect to
each other.--that is, the three metals are deposited at rates and
ratios quite different from the ratios of the metals in the bath.
This is illustrated in FIGS. 1 and 2. While the original makeup of
the bath is preferably stated in terms of the concentrations of the
chlorides,--that is, 60-83% of the metals source is chromium (III)
chloride, 11-27.7% of the metals source is nickel chloride, and
4.7-15.4% of the metals source is ferrous chloride--the particular
source of each metal is not as important as the metals themselves
in the bath. These percentages of metal chlorides (weight
percentages of the total metal chlorides) are converted in FIG. 1
to percentages of the total of the three metals dissolved in the
bath. Thus, when the total of the metal sources in the bath is
60-83% CrCl.sub.3.6H.sub.2O, and the other two metal sources are
within the ranges stated herein, chromium is 53.4% to 79.12% of the
total metals in the bath; 11% to 27.7% of the total metal sources
is NiCl.sub.2.6H.sub.2O and nickel is 12.9% to 31.8% of the total
of the three metals in the bath, and iron, derived from 4.7% to
15.4% FeCl.sub.2.4H.sub.2O, is 6.4% to 19.9% by weight of the total
of the three metals in the bath. The shaded area A represents the
various combinations of percentages of the three metals in the
bath. Other halides and/or even other anions may be used in place
of the chlorides where it is found they have no harmful
effects.
[0020] When the three metals are present in the bath in the ratios
illustrated in FIG. 1 and the other conditions described herein are
observed, the metal cathode acquires a coating of metals having
stainless steel composition illustrated in FIG. 2 and described
elsewhere herein. Specifically, FIG. 2 shows a shaded area B
representing the coating composition wherein the chromium content
is 12% to 30% by weight, the nickel content is 6% to 10% by weight,
and the iron content is 64% to 78% by weight. Thus our invention
includes a method of forming a stainless steel coating on a steel
substrate, where the stainless steel coating comprises chromium,
nickel and iron within the range of weight ratios chromium
6-15:nickel 3-5:iron 32-39 comprising electrolytically depositing
the three metals from an aqueous electrolyte containing chromium,
nickel and iron dissolved in weight ratios of chromium
53.4-79.12:nickel 12.9-31.8:iron 6.4-19.9. Similar coatings may be
deposited on other metal cathodes.
[0021] The two shaded areas A and B of FIGS. 1 and 2 are clearly
far removed from each other, reflecting the different rates of
deposition of the three metals. Ideally, the metals are deposited
in the ratios illustrated in FIG. 2 and in amounts calculable from
the coating weights and areas, but in practice depletion of the
metals in the bath may vary from facility to facility, as a
function of the applied current, with the concentrations of the
dissolved metals, and with their ratios to each other within area
A. Therefore the preferred method of maintaining effective
concentrations and ratios of the metals to each other is to take
samples periodically, analyze for the metals, and replenish the
bath incrementally--that is, remove a portion of the used bath and
replace it with the same amount of new solution containing
concentrations and ratios of the three metals calculated to replace
the deposited metals. Where a stainless steel anode is employed,
some dissolution of the anode may be expected, contributing metals
to the bath at rates generally in accord with the anode's
composition, but which may vary somewhat over time. Over a long
period, experience will enable persons skilled in the art to
construct models of the process so that the bath may be replenished
more or less continuously, whether or not a stainless steel anode
is used. Also, it may be useful to design an anode specifically as
a sacrificial anode to continuously and entirely replace the metals
in the bath in the amounts and proportions they are deposited, thus
avoiding or minimizing the need to use new solution for replacing
the metals.
[0022] While any stainless steel composition may be used for the
anode, it may be useful to design an anode specifically as a
sacrificial anode to continuously substantially replace the metals
in the bath in the proportions and amounts they are deposited on
the cathode, thus avoiding or minimizing the necessity of
replenishing the dissolved metals by removing and replacing bath
solution.
[0023] The Leveling Agents
[0024] Leveling agents and brighteners are desirable to enhance the
product quality. A leveling agent is an additive for the bath which
influences the rate of deposition and thickness of the deposited
metals over large and small areas, generally assuring that the
deposition is evenly conducted especially over areas which might
include microscopic pits or peaks. In the absence of a leveling
agent, stress is built in to the coating, resulting in a rough
surface. In our preferred process and bath, we use both citric acid
and coumarin as leveling agents, but if only one is to be used, we
prefer coumarin. In addition to functioning as a leveling agent,
coumarin is a brightener. Brighteners provide a more even, shiny,
or bright surface. The leveling effect of a leveling agent is
substantially similar to the brightening effect of a brightener;
the two terms and effects may be used interchangeably, and where we
refer herein to brighteners or brightening we intend equivalence to
leveling agents and leveling effects. While coumarin
(1,2-benzopyrone) is preferred, related compounds and isomers may
be used, such as 2,1-benzopyrone, 1,4-benzopyrone,
3-chlorocoumarin, 3-bromocoumarin, 3-acetylcoumarin,
7-hydroxxyethyl coumarin, 6-chlorocoumarin, 4,8-dimethyl coumarin,
8-methoxycoumarin, 7-ethoxycoumarin, 6-propargoxy coumarin, and
6-acetamido coumarin. These and other coumarin derivatives are
described as leveling agents in the following U.S. patents: Faust
et al U.S. Pat. No. 2,840,517, Tomaszewski et al U.S. Pat. No.
3,268,307, Du Rose et al U.S. Pat. No. 3,414,491, Klein et al U.S.
Pat. No. 3,719,568 and U.S. Pat. No. 3,795,592, and Tremmel U.S.
Pat. No. 4,441,969. Coumarin and the coumarin derivatives listed
above and any others described as effective leveling agents in
electrolytic baths are defined as, and may be called herein,
"coumarin leveling agents." Coumarin leveling agents may be used in
small amounts effective in our aqueous electrolytic bath to
brighten the coating and/or distribute the metals substantially
level over a metallic surface which might not be substantially
level microscopically.
[0025] As is indicated in the above patents, coumarin may be
expected to break down in the bath to melilotic acid, also known as
3-(2-hydroxyphenyl) propionic acid, which can have adverse color
effects on the product. Accordingly, we may continuously or
intermittently pass at least part of the bath through a filter or
absorbent to remove the melilotic acid; we prefer to use a bed of
activated carbon, but an ion exchange resin such as Amberlite may
be useful in some facilities to remove melilotic acid from the
solution. Where a coumarin leveling agent other than coumarin is
used, breakdown products other than melilotic acid may be produced;
we do not intend to be limited to the removal of melilotic acid by
filtration, adsorption, or otherwise. Also, the filter, absorbent,
or resin may remove some of the coumarin as well as the melilotic
acid. Whether or not undegraded coumarin is removed in the
filtering or adsorption process, the converted or removed coumarin
may be replenished continuously or intermittently either in the
same solution used to replenish the metals or in a separate
addition. Various additives have been used in electrolytic baths to
complement the action of the coumarin leveling agent and/or to
ameliorate its breakdown. Such additives include water soluble
acetylenic compounds (U.S. Pat. Nos. 3,111,466 and 3,414,491),
propylene oxide adducts of propargyl alcohol (U.S. Pat. No.
3,719,568), butyne diol, formaldehyde, and chloral hydrate (U.S.
Pat. No. 4,441,969). Such additives may be called coumarin
complements; they are compatible with, and may be useful in, our
process.
[0026] Other constituents of the bath are not consumed at
significant rates in the process, but should nevertheless be
monitored occasionally in a continuous process.
[0027] The pH of the bath may be maintained by the citric acid and
to a lesser extent the ammonium chloride. Little adjustment of the
pH, if any, will be required, but, any conventional method of
maintaining a desired acid pH in a plating bath may be used if
necessary.
[0028] The hydrofluosilicic acid improves the deposition of
chromium and contributes to the enhanced shininess of the product
attainable by our process. The "Triton X-100" is a stress
reliever--that is, it inhibits the formation of microcracks in the
coating as it builds, thereby alleviating the potential for
corrosion. Other surfactants may perform in much the same manner.
Other stress relievers include formates, acetates, and salicylic
acid. Many surfactants and other stress relievers also have the
property of alleviating the undesirable tendency, sometimes
noticeable, of the coumarin leveling agent to induce tensile stress
or brittleness in the coating. Where a stress reliever is used, the
concentration of brightener (coumarin leveling agent) may be
reduced.
[0029] Our coated metal products may be used in many applications
in place of conventional stainless steel; for example they are
ideal for architectural uses, appliances, automotive parts, and
anywhere steel is used, where corrosion resistance is important,
and/or especially where an attractive, readily polished appearance
is desired without the necessity of painting.
* * * * *