[0001] The shaping and surface finishing of metallic substrates has often proven a challenge.
In particular the shaping and surface finishing of metallic substrates obtained from
generative processes such as additive layer manufacturing often exhibit rough surfaces.
The commonly known shaping and surface finishing methods such as abrasive flow machining
are often not applicable to complex surfaces. Furthermore, electrochemical methods
are known, such as electrolytic polishing. The electrolytic polishing effect relies
on a dissolution reaction occurring on a metallic substrate forming part of an electrolytic
cell when a current is applied, wherein the metallic substrate is dissolved into the
electrolyte in form of ions. Without wishing to be bound to by a theory, it is believed
that an electrolytic film is formed on the surface of the metallic substrate and due
to the difference in surface ratio and discharge behaviour peaks are dissolved more
rapidly than plane surfaces resulting in a reduction of surface roughness. However,
state of the art electrolytic polishing processes are often cost and time intensive
or do not result in the desired reduction of surface roughness. Furthermore, it is
often required to apply hazardous chemicals which require a cumbersome disposal. Thus,
it is an object of the present invention to provide an electrolytic polishing process
which does not suffer from the drawbacks indicated above.
[0002] The finding of the present invention is an electrolyte (EL) for the application in
an electrolytic polishing process for metallic substrates, resulting in an excellent
reduction of surface roughness.
[0003] In a first aspect the invention is directed at an electrolyte (EL) for the electrolytic
polishing of a metallic substrate comprising
- (i) at least one acid compound (A),
- (ii) at least one fluoride compound (F), and
- (iii) at least one complexing agent (CA).
[0004] In an embodiment the electrolyte (EL) comprises
- (i) the at least one acid compound (A) in an amount of not more than 20 wt.-%, preferably
in an amount of not more than 15 wt.-%, more preferably in an amount of not more than
10 wt.-%, even more preferably in an amount of not more than 5 wt.-%, like an amount
in the range of 0.05 to 20 wt.-%, preferably an amount in the range of 0.5 to 15 wt.-%,
more preferably an amount in the range of 1 to 10 wt.-%, even more preferably an amount
in the range of 1 to 5 wt.-%, based on the weight of the electrolyte (EL), and/or
- (ii) the at least one fluoride compound (F) in an amount of not more than 40 wt.-%,
preferably in an amount of not more than 30 wt.-%, more preferably in an amount of
not more than 15 wt.-%, even more preferably in an amount of not more than 10 wt.-%,
like an amount in the range of 1 to 40 wt.-%, preferably an amount in the range of
1 to 30 wt.-%, more preferably an amount in the range of 2 to 15 wt.-%, even more
preferably an amount in the range of 4 to 10 wt.-%, based on the weight of the electrolyte
(EL), and/or
- (iii) the at least one complexing agent (CA) in an amount of not more than 30 wt.-%,
preferably in an amount of not more than 20 wt.-%, more preferably in an amount of
not more than 10 wt.-%, even more preferably in an amount of not more than 5 wt.-%,
like an amount in the range of 0.5 to 30 wt.-%, preferably an amount in the range
of 0.5 to 20 wt.-%, more preferably an amount in the range of 0.5 to 10 wt.-%, even
more preferably an amount in the range of 0.5 to 5 wt.-%, yet even more preferably
an amount in the range of 1 to 3 wt.-%, based on the weight of the electrolyte (EL).
[0005] In an embodiment the electrolyte (EL) consists of
- (i) at least one acid compound (A),
- (ii) at least one fluoride compound (F),
- (iii) at least one complexing agent (CA),
- (iv) at least one medium (M), and
- (v) optionally additives (AD).
[0006] In an embodiment the electrolyte (EL) comprises
- (i) the at least one acid compound (A) in an amount of not more than 20 wt.-%, preferably
in an amount of not more than 15 wt.-%, more preferably in an amount of not more than
10 wt.-%, even more preferably in an amount of not more than 5 wt.-%, like an amount
in the range of in the range of 0.05 to 20 wt.-%, preferably an amount in the range
of 0.5 to 15 wt.-%, more preferably an amount in the range of 1 to 10 wt.-%, even
more preferably an amount in the range of 1 to 5 wt.-%, based on the weight of the
electrolyte (EL), and/or
- (ii) the at least one fluoride compound (F) in an amount of not more than 40 wt.-%,
preferably in an amount of not more than 30 wt.-%, more preferably in an amount of
not more than 15 wt.-%, even more preferably in an amount of not more than 10 wt.-%,
like an amount in the range of 1 to 40 wt.-%, preferably an amount in the range of
1 to 30 wt.-%, more preferably an amount in the range of 2 to 15 wt.-%, even more
preferably an amount in the range of 4 to 10 wt.-%, based on the weight of the electrolyte
(EL), and/or
- (iii) the at least one complexing agent (CA) in an amount of not more than 30 wt.-%,
preferably in an amount of not more than 20 wt.-%, more preferably in an amount of
not more than 10 wt.-%, even more preferably in an amount of not more than 5 wt.-%,
like an amount in the range of 0.5 to 30 wt.-%, preferably an amount in the range
of 0.5 to 20 wt.-%, more preferably an amount in the range of 0.5 to 10 wt.-%, even
more preferably an amount in the range of 0.5 to 5 wt.-%, yet even more preferably
an amount in the range of 1 to 3 wt.-%, based on the weight of the electrolyte (EL),
and/or
- (iv) the at least one medium (M) in an amount of at least 10 wt.-%, preferably in
an amount of at least 30 wt.-%, more preferably in an amount of at least 50 wt.-%,
even more preferably in an amount of at least 70 wt.-%, like an amount in the range
of 10 to 98.5 wt.-%, preferably an amount in the range of 30 to 95 wt.-%, more preferably
an amount in the range of 50 to 90 wt.-%, even more preferably an amount in the range
of 70 to 85 wt.-%, based on the weight of the electrolyte (EL), and/or
- (v) the additives (AD) in an amount of not more than 25 wt.-%, preferably in an amount
of not more than 15 wt.-%, more preferably in an amount of not more than 10 wt.-%,
even more preferably in an amount of not more than 5 wt.-%, yet even more preferably
in an amount of not more than 2 wt.-%, like an amount in the range of 0.01 to 25 wt.-%,
preferably an amount in the range of 0.01 to 10 wt.-%, more preferably an amount in
the range of 0.01 to 5 wt.-%, even more preferably an amount in the range of 0.01
to 2 wt.-%, based on the weight of the electrolyte (EL).
[0007] In an embodiment the at least one acid compound (A) is selected from the group consisting
of inorganic or organic acids such as sulfuric acid, nitric acid, phosphoric acid,
hydrochloric acid, formic acid, acetic acid propionic acid, or mixtures thereof, preferably
is selected from the group consisting of sulfuric acid, nitric acid, phosphoric acid,
or mixtures thereof, more preferably is sulfuric acid.
[0008] In an embodiment the at least one fluoride compound (F) is selected from the group
consisting of ammonium fluoride, sodium fluoride, potassium fluoride, magnesium fluoride,
calcium fluoride, trifluoracetic acid, or mixtures thereof, preferably is selected
from the group consisting of ammonium fluoride, sodium fluoride, potassium fluoride,
magnesium fluoride, calcium fluoride, or mixtures thereof, more preferably is ammonium
fluoride.
[0009] In an embodiment the at least one complexing agent (CA) is selected from the group
consisting of metylglycindiacetic acid (MGDA), ethylenediaminetetraacetate (EDTA),
diethylenetriaminepentakismethylenephosphonic acid (DTPMP) aminopolycarboxilic acids
(APC) diethylenetriaminepentaacetate (DTPA), nitrilotriacetate (NTA), triphosphate,
1,4,7,10 tetraazacyclododecane-1,4,7,10-tetraacetic acid (DOTA), phosphonate, diethylenetriaminepentakismethylenephosphonic
acid (DTPMP), gluconic acid, β-alaninediactetic acid (ADA), N-bis[2-(1,2 dicarboxy-ethoxy)ethyl]glycine
(BCA5), N-bis[2-(1,2-dicarboxyethoxy)ethyl]aspatic acid (BCA6), tetracis(2-hydroxypropyl)-ethylenediamine
(THPED), N-(Hydroxyethyl)-ethylenediaminetriacetic acid (HEDTA) or mixtures thereof,
preferably is selected from the group consisting of metylglycindiacetic acid (MGDA),
ethylenediaminetetraacetate (EDTA), diethylenetriaminepentakismethylenephosphonic
acid (DTPMP) aminopolycarboxilic acids (APC) diethylenetriaminepentaacetate (DTPA),
diethylenetriaminepentakismethylenephosphonoc acid (DTPMP), tetracis(2-hydroxypropyl)ethylenediamine
(THPED), N-(hydroxyethyl)-ethylenediamine-triacetic acid (HEDTA), or mixtures thereof,
more preferably is metylglycindiacetic acid (MGDA).
[0010] In a second aspect the present invention is directed at a process for the electrolytic
polishing of a metallic substrate comprising the steps of
- (i) providing an electrolyte (EL) as described herein in an electrolytic cell comprising
at least one electrode,
- (ii) disposing a metallic substrate as an anode in the electrolytic cell,
- (iii) applying a current from a power source between the at least one electrode and
the metallic substrate, and
- (iv) immersing the metallic substrate in the electrolyte (EL).
[0011] In an embodiment the current is applied at a voltage of not more than 100 V, preferably
of not more than 80 V, more preferably of not more 50 V, even more preferably of not
more than 20 V, like in the range of 1 to 100 V, preferably in the range of 1 to 80
V, more preferably in the range of 1 to 50 V, even more preferably in the range of
1 to 20 V, yet even more preferably in the range of 5 to 20 V.
[0012] In an embodiment the electrolyte has a temperature in the range of 10 to 95 °C, preferably
a temperature in the range of 40 to 95 °C, more preferably a temperature in the range
of 60 to 95 °C, even more preferably a temperature in the range of 70 to 90 °C, yet
even more preferably a temperature in the range of 75 to 85 °C.
[0013] In an embodiment the current is applied at a current density in the range of 0.05
to 10 A/cm
2, preferably at a current density in the range of 0.05 to 5 A/cm
2, more preferably at a current density in the range of 0.1 to 2.5 A/cm
2, even more preferably at a current density in the range of 0.1 to 2.0 A/cm
2, yet even more preferably at a current density in the range of 0.1 to 1.5 A/cm
2.
[0014] In an embodiment the current is applied for a time in the range of 1 to 240 min,
preferably for a time in the range of 1 to 120 min, more preferably for a time in
the range of 1 to 60 min, even preferably for a time in the range of 1 to 30 min,
yet even more preferably for a time in the range of 2 to 20 min.
[0015] In an embodiment the process comprises at least one additional process step of treating
the metallic substrate with a cleaning composition.
[0016] In a third aspect the present invention is directed at the use of at least one complexing
agent (CA) in an electrolyte to increase the efficiency of surface roughness reduction
in an electrolytic polishing process of a metallic substrate.
[0017] In a fourth aspect the present invention is directed at the use of at least one complexing
agent (CA) in an electrolyte to increase the lifetime of the electrolyte when applied
in an electrolytic polishing process of a metallic substrate.
[0018] It is to be understood that the different aspects of the invention and the embodiments
described above and below are interrelated such that the disclosures supplement each
other. For example the electrolyte described according to the first aspect is preferably
applied in the process according to the second aspect and the use according to the
third and fourth aspect.
[0019] In the following the invention is described in more detail:
The invention is directed at an electrolyte (EL) for the electrolytic polishing of
a metallic substrate with excellent long-term stability and efficiency of surface
roughness reduction when applied in an according process.
THE ELECTROLYTE (EL)
[0020] The invention is directed at an electrolyte (EL). The term "electrolyte" as used
according to the present invention is directed at a fluid that can be applied in an
electrolytic cell as conducting medium in which the flow of current is accompanied
by the movement of matter in the form of ions.
[0021] The electrolyte (EL) for the electrolytic polishing of a metallic substrate comprises
at least one acid compound (A), at least one fluoride compound (F), and at least one
complexing agent (CA).
[0022] In a preferred embodiment the electrolyte (EL) does not comprise any other acid compounds,
fluoride compounds and complexing agents beside the at least one acid compound (A),
the at least one fluoride compound (F), and the at least one complexing agent (CA).
[0023] In a preferred embodiment the electrolyte (EL) is acidic. It is appreciated that
the electrolyte has a pH of not more than 6.5, preferably a pH of not more than 6.0,
more preferably a pH of not more than 5.5, like a pH in the range of 0.5 to 6.5, preferably
a pH in the range of 1.0 to 6.0, more preferably a pH in the range of 2.0 to 5.5,
even more preferably a pH in the range of 3.0 to 5.0.
The Acid Compound (A)
[0024] The term "acid compound" as used according to the present invention is directed at
an organic or inorganic compound that can accept a pair of electrons to form a covalent
bond.
[0025] The at least one acid compound (A) is an essential constituent of the electrolyte
(EL). The at least one acid compound (A) increases the conductivity of the electrolyte
and may benefit an electrolytic polishing process as a catalyst depending on the metallic
substrate to be treated.
[0026] Preferably the at least one acid compound (A) is comprised in the electrolyte (EL)
in an amount of not more than 20 wt.-%, preferably in an amount of not more than 15
wt.-%, more preferably in an amount of not more than 10 wt.-%, even more preferably
in an amount of not more than 5 wt.-%, like an amount in the range of in the range
of 0.05 to 20 wt.-%, preferably an amount in the range of 0.5 to 15 wt.-%, more preferably
an amount in the range of 1 to 10 wt.-%, even more preferably an amount in the range
of 1 to 5 wt.-%, based on the weight of the electrolyte (EL).
[0027] It is appreciated that the at least one acid compound (A) is selected from the group
consisting of inorganic or organic acids such as sulfuric acid, nitric acid, phosphoric
acid, hydrochloric acid, formic acid, acetic acid propionic acid, or mixtures thereof,
preferably is selected from the group consisting of sulfuric acid, nitric acid, phosphoric
acid, or mixtures thereof, more preferably is sulfuric acid.
[0028] In a preferred embodiment the at least one acid compound (A) is aqueous sulfuric
acid, wherein sulfuric acid is comprised in an amount in the range of 100 to 20 wt.-%,
preferably in an amount in the range of 98 to 50 wt.-%, more preferably in an amount
in the range of 98 to 80 wt.-%, even more preferably in an amount in the range of
98 to 90 wt.-%, based on the weight of the at least one acid compound (A).
[0029] Thus, it is not required to include toxic acid compounds requiring cumbersome disposal,
such as hydrofluoric acid, which is disclosed as a suitable acid compound for the
electrolytic polishing of metallic substrates in the state of the art.
The Fluoride Compound (F)
[0030] The term "fluoride compound" as used according to the present invention is directed
at a compound that can serve as a source of fluoride ions. Depending on the metallic
substrate to be treated in an electrolytic polishing process fluoride ions may be
required to support the dissolution process, for example by forming stable complexes
with dissolved metal ions.
[0031] Preferably the at least one fluoride compound (F) is comprised in the electrolyte
(EL) in an amount of not more than 40 wt.-%, preferably in an amount of not more than
30 wt.-%, more preferably in an amount of not more than 15 wt.-%, even more preferably
in an amount of not more than 10 wt.-%, like an amount of in the range of 1 to 40
wt.-%, preferably an amount in the range of 1 to 30 wt.-%, more preferably in an amount
the range of 2 to 15 wt.-%, even more preferably an amount in the range of 4 to 10
wt.-%, based on the weight of the electrolyte (EL). It is appreciated that the at
least one fluoride compound (F) is selected from the group consisting of ammonium
fluoride, sodium fluoride, potassium fluoride, magnesium fluoride, calcium fluoride,
trifluoracetic acid, or mixtures thereof, preferably is selected from the group consisting
of ammonium fluoride, sodium fluoride, potassium fluoride, magnesium fluoride, calcium
fluoride, , or mixtures thereof, more preferably is ammonium fluoride.
[0032] It is believed that the application of ammonium fluoride additionally benefits the
process of electrolytic polishing of metallic substrates by providing a cationic wetting
agent (NH
4+) which modifies the polarization of the electrodes.
The Complexing Agent (CA)
[0033] The term "complexing agent" as used according to the present invention is directed
at compounds that form coordinate bonds with a metal atom or ion. Chelating agents
are complexing agents that form a particular type of complex, that involves the formation
or presence of two or more separate coordinate bonds between a polydentate (multiple
bonded) ligand and a multivalent single central atom. Usually these ligands are organic
compounds, and are called chelants, chelators, chelating agents, or sequestering agents.
The term "complexing agent" includes both non-chelating complexing agents and chelating
complexing agents, the latter being preferred.
[0034] The at least one complexing agent (CA) is an essential constituent of the electrolyte
(EL). The at least one complexing agent (CA) benefits the long-term stability of the
electrolyte (EL) and increases the efficiency of surface roughness reduction achieved
by electrolytic polishing of a metallic substrate.
[0035] Preferably the at least one complexing agent (CA) is comprised in the electrolyte
(EL) in an amount of not more than 30 wt.-%, preferably in an amount of not more than
20 wt.-%, more preferably in an amount of not more than 10 wt.-%, even more preferably
in an amount of not more than 5 wt.-%, like an amount in the range of 0.5 to 30 wt.-%,
preferably an amount in the range of 0.5 to 20 wt.-%, more preferably an amount in
the range of 0.5 to 10 wt.-%, even more preferably an amount in the range of 0.5 to
5 wt.-%, yet even more preferably an amount in the range of 1 to 3 wt.-%, based on
the weight of the electrolyte (EL)
[0036] It is appreciated that the at least one complexing agent (CA) is selected from the
group consisting of metylglycindiacetic acid (MGDA), ethylenediaminetetraacetate (EDTA),
diethylenetriaminepentakismethylenephosphonic acid (DTPMP) aminopolycarboxilic acids
(APC) diethylenetriaminepentaacetate (DTPA), nitrilotriacetate (NTA), triphosphate,
1,4,7,10 tetraazacyclododecane-1,4,7,10-tetraacetic acid (DOTA), phosphonate, diethylenetriaminepentakismethylene-phosphonic
acid (DTPMP), gluconic acid, β-alaninediactetic acid (ADA), N-bis[2-(1,2 dicarboxy-ethoxy)ethyl]glycine
(BCA5), N-bis[2-(1,2-dicarboxyethoxy)ethyl]-aspatic acid (BCA6), tetracis(2-hydroxypropyl)ethylenediamine
(THPED), N-(hydroxyethyl)-ethylenediaminetriacetic acid (HEDTA) or mixtures thereof,
preferably is selected from the group consisting of metylglycindiacetic acid (MGDA),
ethylenediaminetetraacetate (EDTA), diethylenetriamine-pentakismethylenephosphonic
acid (DTPMP) aminopolycarboxilic acids (APC) diethylenetriaminepentaacetate (DTPA),
diethylenetriaminepentakismethylene-phosphonoc acid (DTPMP), tetracis(2-hydroxypropyl)ethylenediamine
(THPED), N-(hydroxyethyl)-ethylenediaminetriacetic acid (HEDTA), or mixtures thereof,
more preferably is metylglycindiacetic acid (MGDA).
The Medium (M)
[0037] The electrolyte (EL) may comprise at least one medium (M). The term "medium" as used
according to the present invention is directed at any organic or inorganic compound
suitable for providing a medium wherein the electrolytic polishing of metallic substrates
can be conducted. Preferably the at least one medium (M) benefits the process of electrolytic
polishing of metallic substrates, for example by increasing the conductivity of the
electrolytic cell, by stabilizing the complexes formed by the at least one complexing
agent (CA) and/or by providing a sufficient solubility with respect to the compounds
comprised in the electrolyte (EL).
[0038] Preferably the at least one medium (M) is comprised in the electrolyte (EL) in an
amount of at least 10 wt.-%, preferably in an amount of at least 30 wt.-%, more preferably
in an amount of at least 50 wt.-%, even more preferably in an amount of at least 70
wt.-%, like an amount in the range of 10 to 98.5 wt.-%, preferably an amount in the
range of 30 to 95 wt.-%, more preferably an amount in the range of 50 to 90 wt.-%,
even more preferably an amount in the range of 70 to 85 wt.-%, based on the weight
of the electrolyte (EL).
[0039] It is appreciated that the at least one medium (M) is selected from the group consisting
of water, alcohols, ethers, esters, carboxylic acids, and mixtures thereof, like C
1 to C
8 aliphatic alcohols, C
1 to C
8 aliphatic ethers, C
1 to C
8 aliphatic esters, C1 to C8 aliphatic carboxylic acids, and mixtures thereof, preferably
from the group consisting of water, alcohols, ethers, and mixtures thereof, like C
1 to C
8 aliphatic alcohols, C
1 to C
8 aliphatic ethers, and mixtures thereof. In a preferred embodiment the at least one
medium (M) is water.
[0040] In a preferred embodiment the term "water" is directed at deionized water.
[0041] In an embodiment the at least one medium (M) is an electrolyte which is compounded
with the at least one acid compound (A), the at least one fluoride compound (F), the
at least one complexing agent (CA) and optionally additives (AD) to form the electrolyte
(EL). In a preferred embodiment the at least one medium (M) is water which is compounded
with the at least one acid compound (A), the at least one fluoride compound (F), the
at least one complexing agent (CA) and optionally additives (AD) to form the electrolyte
(EL). In other words in a preferred embodiment the electrolyte (EL) is an aqueous
electrolyte comprising the at least one acid compound (A), the at least one fluoride
compound (F) and the at least one complexing agent (CA).
The Additives (AD)
[0042] The electrolyte (EL) may comprise additional additives (AD) that are applied in the
electrolytic polishing of metallic substrates to benefit the process. Typical additives
are known to a person skilled in the art of electrolytic polishing of metallic substrates
and are applied according to needs. Typical additives for the electrolytic polishing
of metallic substrates are for example surfactants, polyvalent alcohols, silicates,
thickeners, and the like.
[0043] It is appreciated that the additives (AD) are present in the electrolyte (EL) in
an amount of not more than 25 wt.-%, preferably in an amount of not more than 15 wt.-%,
more preferably in an amount of not more than 10 wt.-%, even more preferably in an
amount of not more than 5 wt.-%, yet even more preferably in an amount of not more
than 2 wt.-%, like an amount in the range of 0.01 to 25 wt.-%, preferably an amount
in the range of 0.01 to 10 wt.-%, more preferably an amount in the range of 0.01 to
5 wt.-%, even more preferably an amount in the range of 0.01 to 2 wt.-%, based on
the weight of the electrolyte (EL).
THE PROCESS FOR THE ELECTROLYTIC POLISHING OF A METALLIC SUBSTRATE
[0044] The invention is further directed at a process for the electrolytic polishing of
a metallic substrate.
[0045] A process for the electrolytic polishing of a metallic substrate is described comprising
the steps of
- (i) providing an electrolyte (EL) as described herein in an electrolytic cell comprising
at least one electrode,
- (ii) disposing a metallic substrate as an anode in the electrolytic cell,
- (iii) applying a current from a power source between the at least one electrode and
the metallic substrate, and
- (iv) immersing the metallic substrate in the electrolyte (EL).
[0046] The term "electrolytic cell" as used according to the present invention is directed
at an electrochemical cell that undergoes a redox reaction when electrical energy
is applied. In particular an electrochemical cell containing an electrolyte through
which an externally generated electric current is passed by a system of electrodes
in order to produce an electrochemical reaction. The electrolytic cell can be used
to decompose a metallic substrate, in a process called electrolysis.
[0047] In accordance with the present invention the electrolyte (EL) is provided in an electrolytic
cell which also contains a suitable cathode. In a preferred embodiment the electrolytic
cell comprises a container receiving the electrolyte wherein the container is made
the cathode of the electrolytic cell. However, it is also possible that at least one
separate electrode is present in the electrolytic cell which is made the cathode of
the electrolytic cell. Furthermore, it is also possible that the electrolytic cell
comprises a container receiving the electrolyte and at least one separate electrode,
wherein both container and the at least one separate electrode are made the cathode
of the electrolytic cell. The cathode material is not critical and suitable materials
include copper, nickel, mild steel, stainless steel, graphite, carbon and the like.
[0048] In a preferred embodiment the surface of the cathode and the surface of the anode
have a surface ratio of at least 10:1, preferably a surface ratio of at least 12:1,
even more preferably a surface ratio of at least 15:1, like a surface ratio in the
range of 10:1 to 100:1, preferably a surface ratio in the range of 12:1 to 100:1,
more preferably a surface ratio in the range of 12:1 to 50:1, even more preferably
a surface ratio in the range of 12:1 to 20:1.
[0049] In a preferred embodiment the current from a power source is applied between the
at least one electrode and the metallic substrate, i.e. between the cathode and the
anode of the electrolytic cell before the metallic substrate is immersed in the electrolyte
(EL). In other words in a preferred embodiment process step (iii) is conducted before
process step (iv). However, it is also possible that the current from a power source
is applied between the at least one electrode and the metallic substrate, i.e. between
the cathode and the anode of the electrolytic cell after the metallic substrate has
been immersed in the electrolyte (EL). In other words in a further embodiment process
step (iii) is conducted after process step (iv).
[0050] The composition of the electrolyte (EL) is critical. It is to be understood that
the information provided above and below with respect to the electrolyte (EL) mutually
applies to the inventive process for the electrolytic polishing of a metallic substrate
in presence of the electrolyte (EL). Thus, the electrolyte (EL) for the electrolytic
polishing of a metallic substrate comprises at least one acid compound (A), at least
one fluoride compound (F), and at least one complexing agent (CA).
[0051] In a preferred embodiment the electrolyte (EL) for the electrolytic polishing of
a metallic substrate consists of at least one acid compound (A), at least one fluoride
compound (F), at least one complexing agent (CA), at least one medium (M), and optionally
additives (AD).
[0052] It is to be understood that the information provided above and below with respect
to the at least one acid compound (A), the at least one fluoride compound (F), the
at least one complexing agent (CA), the at least one medium (M) and optionally additives
(AD) mutually applies to the inventive process for the electrolytic polishing of a
metallic substrate in presence of at least one acid compound (A), at least one fluoride
compound (F), at least one complexing agent (CA), at least one medium (M) and/or optionally
additives (AD).
[0053] It is an advantage of the present invention that the process for the electrolytic
polishing of a metallic substrate can inter alia be applied to metallic substrates
with complex surfaces. Thus, the metallic substrate may be in any form such as, for
example, bars, plates, flat sheets, sheets of expanded metal, cuboids, or complex
structures.
[0054] The term "metallic substrate" as used herein is meant to encompass substrates comprising
at least one conductive metal or metal alloy. Preferably the metallic substrate consists
of at least one conductive metal or metal alloy. It is appreciated that the metallic
substrate comprises, preferably consists of, metals selected from the group consisting
of aluminium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper,
niobium, molybdenum, silver, hafnium, tungsten, platinum, gold, steel and combinations
thereof, such as alloys, preferably selected from the group consisting of aluminium,
titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, niobium, molybdenum,
steel and combinations thereof, such as alloys, more preferably selected from the
group consisting of aluminium, titanium and vanadium, and combinations thereof, such
as alloys. In a preferred embodiment the metal substrate is selected from the group
consisting of Ti-6Al-4V, AlSi
10Mg, AlSi
7, Inconel 718, AIMgSc, and combinations thereof.
[0055] It has been found that the process results in an excellent reduction of surface roughness
both at high voltages and at low voltages.
[0056] It is appreciated that the current is applied at a voltage of not more than 100 V,
preferably of not more than 80 V, more preferably of not more 50 V, even more preferably
of not more than 20 V, like in the range of 1 to 100 V, preferably in the range of
1 to 80 V, more preferably in the range of 1 to 50 V, even more preferably in the
range of 1 to 20 V, yet even more preferably in the range of 5 to 20 V.
[0057] However, it is also possible that the current is applied at a voltage of at least
20 V, preferably of at least 50 V, more preferably of at least 100 V, even more preferably
of at least 200 V, yet even more preferably of at least 250 V, like in the range of
20 to 800 V, preferably a voltage in the range of 50 to 600 V, more preferably a voltage
in the range of 100 to 500 V, even more preferably a voltage in the range of 200 to
400 V, yet even more preferably a voltage in the range of 250 to 350 V.
[0058] Furthermore, it is appreciated that the current is applied at a current density in
the range of 0.05 to 10 A/cm
2, preferably at a current density in the range of 0.05 to 5 A/ cm
2, more preferably at a current density in the range of 0.1 to 2.5 A/cm
2, even more preferably at a current density in the range of 0.1 to 2.0 A/cm
2, yet even more preferably at a current density in the range of 0.1 to 1.5 A/cm
2.
[0059] The temperature does not appear to be a critical parameter. However, an increased
temperature seems to improve the efficiency of the process for the electrolytic polishing
of a metallic substrate. It is appreciated that the temperature of the electrolyte
is at least 10 °C, preferably is at least 40 °C, more preferably is at least 60 °C,
even more preferably is at least 70 °C, yet even more preferably is at least 75 °C,
like a temperature in the range of 10 to 95 °C, preferably a temperature in the range
of 40 to 95 °C, more preferably a temperature in the range of 60 to 95 °C, even more
preferably a temperature in the range of 70 to 90 °C, yet even more preferably a temperature
in the range of 75 to 85 °C.
[0060] The treatment time is generally within the range of 1 to 240 min. However, the treatment
of some metallic substrates may require a shorter or longer treatment for the desired
reduction in surface roughness, depending on factors such as initial surface roughness
and desired surface roughness, surface area, surface geometry and the like. In a preferred
embodiment the current is applied for a time in the range of 1 to 240 min, preferably
for a time in the range of 1 to 120 min, more preferably for a time in the range of
1 to 60 min, even preferably for a time in the range of 1 to 30 min, yet even more
preferably for a time in the range of 2 to 20 min.
[0061] In a preferred embodiment the electrolyte is continuously agitated during the process
for the electrolytic polishing of a metallic substrate. There are various methods
of agitating an electrolyte during electrolytic polishing of a metallic substrate.
The agitation may be achieved by immersing a pressurized gas. Suitable gases for immersion
are for example, nitrogen, hydrogen helium, argon, and combinations thereof. During
immersion the pressurized gas is bubbled through the electrolyte. The pressurized
gas may have a pressure in the range of 0.01 to 1000 kg/cm
2, preferably a pressure in the range of 1 to 1000 kg/cm
2.
[0062] It may be beneficial for the process for the electrolytic polishing of a metallic
substrate if the metallic substrate is subjected to pre- or post-treatment steps,
such as treating the metallic substrate with a cleaning composition. In an embodiment
the process for the electrolytic polishing of a metallic substrate comprises a post-treatment
step of treating the metallic substrate with a cleaning composition, preferably a
post-treatment step of treating the metallic substrate with water, preferably deionized
water.
[0063] The process for the electrolytic polishing of a metallic substrate provides metallic
substrate with reduced surface roughness.
[0064] It is appreciated that the average surface roughness (R
a) of a metallic substrate treated according to the process for the electrolytic polishing
of a metallic substrate described is reduced by at least 0.1 µm, preferably is reduced
by at least 0.5 µm, even more preferably is reduced by at least 1.0 µm, like in the
range of 0.1 to 100 µm, preferably in the range of 0.5 to 10 µm, even more preferably
in the range of 1.0 to 5.0 µm.
[0065] Furthermore, it is appreciated that from the process for the electrolytic polishing
of a metallic substrate described a metallic substrate is obtained with an average
surface roughness (R
a) of not more than 10 µm, preferably of not more than 5 µm, more preferably of not
more than 1 µm, even more preferably of not more than 0.5 µm, yet even more preferably
of not more than 0.1 µm, like an average surface roughness (R
a) in the range of 10 to 0.01 µm, preferably an average surface roughness (R
a) in the range of 5 to 0.01 µm, more preferably an average surface roughness (R
a) in the range of 1 to 0.01 µm, even more preferably an average surface roughness
(R
a) in the range of 0.5 to 0.01 µm, yet even more preferably an average surface roughness
(R
a) in the range of 0.1 to 0.01 µm.
[0066] The electrolyte (EL) is described in more detail above and below in particular in
the section "THE ELECTROLYTE".
USE OF THE COMPLEXING AGENT (CA)
[0067] The electrolyte (EL) can be applied for electrolytic polishing of metallic substrates
comprising metals or metal alloys. It is a finding of the present invention that the
efficiency of surface roughness reduction in an electrolytic polishing process of
a metallic substrate can be improved when providing at least one complexing agent
(CA). In addition hereto it is a finding of the present invention that the lifetime
of an electrolyte can be increased when providing at least one complexing agent (CA).
[0068] The invention is further directed at the use of at least one complexing agent (CA)
in an electrolyte to increase the efficiency of surface roughness reduction in an
electrolytic polishing process of a metallic substrate.
[0069] The invention is further directed at the use of at least one complexing agent (CA)
in an electrolyte to increase the lifetime of the electrolyte when applied in an electrolytic
polishing process of a metallic substrate.
[0070] The at least one complexing agent (CA) is described in more detail above and below,
in particular in the section "The Complexing Agent (CA)".
FIGURES
[0071]
Figure 1 depicts a SEM image of the metallic substrate Ti-6Al-4V before being treated in the
process according to Example 1. The SEM image provides a 100 fold magnification and
has been acquired at a voltage of 15,000 kV and a working distance of 4.5 mm.
Figure 2 depicts a SEM image of the metallic substrate Ti-6Al-4V after being treated in the
process according to Example 1. The SEM image provides a 100 fold magnification and
has been acquired at a voltage of 15,000 kV and a working distance of 8.9 mm.
Figure 3 depicts a SEM image of the metallic substrate Ti-6Al-4V after being treated in the
process according to Example 1. The SEM image provides a 10,000 fold magnification
and has been acquired at a voltage of 15,000 kV and a working distance of 5.4 mm.
Figure 4 depicts a SEM image of a metallic substrate Ti-6Al-4V after being treated in the
process according to Example 2. The SEM image provides a 100 fold magnification and
has been acquired at a voltage of 15,000 kV and a working distance of 10.4 mm.
Figure 5 depicts a SEM image of a metallic substrate Ti-6Al-4V after being treated in the
process according to Example 2. The SEM image provides a 10,000 fold magnification
and has been acquired at a voltage of 15,000 kV and a working distance of 10.4 mm.
EXAMPLES
Definitions and Measuring Methods
[0072] The
average surface roughness (Ra) is determined according to DIN EN 4287:1998-10 using the tactile incision technique
according to DIN EN ISO 3274 (Hommel Tester T1000 Wave of Jenoptik, tipradius 5µm,
taper angle 90°)
The pH is determined according to DIN 19261:2005-6.
Example 1
[0073] A metallic substrate in form of a 32 mm x 16 mm x 30 mm metal plate of Ti-6Al-4V
with an initial average surface roughness of R
a = 16.0 µm is disposed as an anode in an electrolytic cell comprising a stainless
steel cathode. A current of 20 V is applied from a direct current power source between
the cathode and the metallic substrate. The metallic substrate is immersed in an electrolyte
consisting of 6 wt.-% NH
4F, 4 wt.-% H
2SO
4 and 1 wt.-% MGDA. The electrolyte has a pH of 3.5. The metallic substrate is treated
for 10 min. A final average surface roughness of R
a = 0.9 µm is achieved.
Example 2
[0074] A metallic substrate in form of a 116 mm x 25 mm x 30 mm metal plate of Ti-6Al-4V
with an initial averaged surface roughness of R
a = 16.0 µm is disposed as an anode in an electrolytic cell comprising a stainless
steel cathode. A current of 20 V is applied from a direct current power source between
the cathode and the metallic substrate. The metallic substrate is immersed in an electrolyte
consisting of 6 wt.-% NH
4F and 1 wt.-% H
2SO
4. The electrolyte has a pH of 3.5. The metallic substrate is treated for 10 min. A
final average surface roughness of R
a = 9.3 µm is achieved. The building of oxide layers can be partially be observed on
the surface.
Example 3
[0075] A metallic substrate in form of a 50 mm x 10 mm x 20 mm metal plate of AlSi
10Mg with an initial averaged surface roughness of R
a = 16.4 µm is disposed as an anode in an electrolytic cell comprising a stainless
steel cathode. A current of 20 V is applied from a direct current power source between
the cathode and the metallic substrate. The metallic substrate is immersed in an electrolyte
consisting of 6 wt.-% NH
4F, 4 wt.-% H
2SO
4 and 1 wt.-% MGDA. The electrolyte has a pH of 3.5. The metallic substrate is treated
for 10 min. A final average surface roughness of R
a = 4.5 µm is achieved.
1. Electrolyte (EL) for the electrolytic polishing of a metallic substrate comprising
(i) at least one acid compound (A),
(ii) at least one fluoride compound (F), and
(iii) at least one complexing agent (CA).
2. Electrolyte (EL) according to claim 1, consisting of
(i) at least one acid compound (A),
(ii) at least one fluoride compound (F),
(iii) at least one complexing agent (CA),
(iv) at least one medium (M), and
(v) optionally additives (AD).
3. Electrolyte (EL) according to any one of previous claims 1 or 2, wherein
(i) the at least one acid compound (A) is comprised in an amount of not more than
20 wt.-%, preferably in an amount of not more than 15 wt.-%, more preferably in an
amount of not more than 10 wt.-%, even more preferably in an amount of not more than
5 wt.-%, like an amount in the range of in the range of 0.05 to 20 wt.-%, preferably
in the range of 0.5 to 15 wt.-%" more preferably in the range of 1 to 10 wt.-%, even
more preferably in the range of 1 to 5 wt.-%,
and/or
(ii) the at least one fluoride compound (F) is comprised in an amount of not more
than 40 wt.-%, preferably in an amount of not more than 30 wt.-%, more preferably
in an amount of not more than 15 wt.-%, even more preferably in an amount of not more
than 10 wt.-%, like an amount in the range of in the range of 1 to 40 wt.-%, preferably
in the range of 1 to 30 wt.-%" more preferably in the range of 2 to 15 wt.-%, even
more preferably in the range of 4 to 10 wt.-%,
and/or
(iii) the at least one complexing agent (CA) is comprised in an amount of not more
than 30 wt.-%, preferably in an amount of not more than 20 wt.-%, more preferably
in an amount of not more than 10 wt.-%, even more preferably in an amount of not more
than 5 wt.-%, like an amount in the range of in the range of 0.5 to 30 wt.-%, preferably
in the range of 0.5 to 20 wt.-%" more preferably in the range of 0.5 to 10 wt.-%,
even more preferably in the range of 0.5 to 5 wt.-%, yet even more preferably in the
range of 1 to 3 wt.-%,
and/or
(iv) the at least one medium (M) in an amount of at least 10 wt.-%, preferably in
an amount of at least 30 wt.-%, more preferably in an amount of at least 50 wt.-%,
even more preferably in an amount of at least 70 wt.-%, like an amount in the range
of 10 to 98.5 wt.-%, preferably in the range of 30 to 95 wt.-%, more preferably in
the range of 50 to 90 wt.-%, even more preferably in the range of 70 to 85 wt.-%,
and/or
(v) additives (AD) in an amount of not more than 25 wt.-%, preferably in an amount
of not more than 15 wt.-%, more preferably in an amount of not more than 10 wt.-%,
even more preferably in an amount of not more than 5 wt.-%, yet even more preferably
in an amount of not more than 2 wt.-%, like an amount in the range of 0.01 to 25 wt.-%,
preferably in the range of 0.01 to 10 wt.-%, more preferably in the range of 0.01
to 5 wt.-%, even more preferably in the range of 0.01 to 2 wt.-%, based on the weight
of the electrolyte (EL),
based on the weight of the electrolyte (EL).
4. Electrolyte (EL) according to any one of previous claims 1 to 3, wherein the at least
one acid compound (A) is selected from the group consisting of inorganic or organic
acids such as sulfuric acid, nitric acid, phosphoric acid, hydrochloric acid, formic
acid, acetic acid propionic acid, or mixtures thereof, preferably is selected from
the group consisting of sulfuric acid, nitric acid, phosphoric acid, or mixtures thereof,
more preferably is sulfuric acid.
5. Electrolyte according to any one of previous claims 1 to 4, wherein the at least one
fluoride compound (F) is selected from the group consisting of ammonium fluoride,
sodium fluoride, potassium fluoride, magnesium fluoride, calcium fluoride, trifluoracetic
acid, or mixtures thereof, preferably is selected from the group consisting of ammonium
fluoride, sodium fluoride, potassium fluoride, magnesium fluoride, calcium fluoride,
or mixtures thereof, more preferably is ammonium fluoride.
6. Electrolyte according to any one of previous claims 1 to 5, wherein the at least one
complexing agent (CA) is selected from the group consisting of metylglycindiacetic
acid (MGDA), ethylenediaminetetraacetate (EDTA), diethylenetriaminepentakismethylenephosphonic
acid (DTPMP) aminopolycarboxilic acids (APC) diethylenetriaminepentaacetate (DTPA),
nitrilotriacetate (NTA), triphosphate, 1,4,7,10 tetraazacyclododecane-1,4,7,10-tetraacetic
acid (DOTA), phosphonate, diethylenetriaminepentakismethylenephosphonoc acid (DTPMP),
gluconic acid, β-alaninediactetic acid (ADA), N-bis[2-(1,2 dicarboxy-ethoxy)ethyl]glycine
(BCA5), N-bis[2-(1,2-dicarboxyethoxy)ethyl]aspatic acid (BCA6), tetracis(2-hydroxypropyl)ethylenediamine
(THPED), N-(Hydroxyethyl)-ethylenediaminetriacetic acid (HEDTA) or mixtures thereof,
preferably is selected from the group consisting of metylglycindiacetic acid (MGDA),
ethylenediaminetetraacetate (EDTA), diethylenetriaminepentakismethylenephosphonic
acid (DTPMP) aminopolycarboxilic acids (APC) diethylenetriaminepentaacetate (DTPA),
diethylenetriaminepentakismethylenephosphonoc acid (DTPMP), tetracis(2-hydroxypropyl)ethylenediamine
(THPED), N-(hydroxyethyl)-ethylenediaminetriacetic acid (HEDTA), or mixtures thereof,
more preferably is metylglycindiacetic acid (MGDA).
7. Process for the electrolytic polishing of a metallic substrate comprising the steps
of
(i) providing an electrolyte (EL) according to any of previous claims 1 to 6 in an
electrolytic cell comprising at least one electrode,
(ii) disposing a metallic substrate as an anode in the electrolytic cell,
(iii) applying a current from a power source between the at least one electrode and
the metallic substrate, and
(iv) immersing the metallic substrate in the electrolyte (EL).
8. Process according to claim 7, wherein the current is applied at a voltage of not more
than 100 V, preferably of not more than 80 V, more preferably of not more 50 V, even
more preferably of not more than 20 V, like in the range of 1 to 100 V, preferably
in the range of 1 to 80 V, more preferably in the range of 1 to 50 V, even more preferably
in the range of 1 to 20 V, yet even more preferably in the range of 5 to 20 V.
9. Process according to any one of previous claims 7 or 8, wherein the electrolyte has
a temperature in the range of 10 to 95 °C, preferably in the range of 40 to 95 °C,
more preferably in the range of 60 to 95 °C, even more preferably in the range of
70 to 90 °C, yet even more preferably in the range of 75 to 85 °C.
10. Process according to any one of previous claims 7 to 9, wherein the current is applied
at a current density in the range of 0.05 to 10 A/cm2, preferably at a current density in the range of 0.05 to 5 A/cm2, more preferably at a current density in the range of 0.1 to 2.5 A/ cm2, even more preferably at a current density in the range of 0.1 to 2.0 A/ cm2, yet even more preferably at a current density in the range of 0.1 to 1.5 A/ cm2.
11. Process according to any one of previous claims 7 to 9, wherein the current is applied
for a time in the range of 1 to 240 min, preferably in the range of 1 to 120 min,
more preferably in the range of 1 to 60 min, even preferably in the range of 1 to
30 min, yet even more preferably in the range of 2 to 20 min.
12. Use of at least one complexing agent (CA) in an electrolyte to increase the efficiency
of surface roughness reduction in an electrolytic polishing process of a metallic
substrate.
13. Use of at least one complexing agent (CA) in an electrolyte to increase the lifetime
of the electrolyte when applied in an electrolytic polishing process of a metallic
substrate.