Patent Grant
11105013
The present method relates to an ionic liquid electrolyte and a method to electroplate metal on a substrate using an electrolyte that includes an imidazolium compound, a metal salt, and water. In one embodiment, the imidazolium compound has the general formula (I):
wherein R1, R2, R3, R4, and R5 are each independently selected from an H atom and an organic radical having from 1 to 20 carbon atoms. L− is a compatible anion.
Chromium plating is a surface treatment used in many industrial applications to increase wear resistance, to improve friction coefficient of parts which are treated and to provide a nice surface aspect (decorative application). Currently, this surface treatment is conducted using as an electrolyte aqueous solutions of hexavalent chromium (Cr(VI) as chromium trioxide CrO3, which becomes chromic acid in water). The cathodic reduction of Cr(VI) to metallic chromium Cr(O) takes place under the condition that catalytic products as sulfuric, fluorosilicate, or organosulfonic ions are present in the bath. The thickness of deposits of hard chromium plated parts is a function of the duration of the plating operation and can vary from 0.1 micrometers (decorative application) to several hundred micrometers (functional application).
Unfortunately, hexavalent chromium compounds are considered to be highly toxic and carcinogenic. Thus, even though no hexavalent chromium is present at the surface of the treated parts after electrolytic reduction for chromium plating and even if the process is strictly controlled and managed during application there is a desirability to replace chromium plating using Cr(VI) by other, more environmentally friendly treatments.
Accordingly, the present invention relates to an ionic liquid electrolyte and a method to electroplate a substrate using an ionic liquid electrolyte that includes an imidazolium compound, a metal salt, and water. In one embodiment the imidazolium compound has the general formula (I), below. The substrate may include a metal or a conductive layer on a substrate. The resulting metal layer has a thickness of at least 0.1 μm. The process can be conducted at a temperature between about 20° to about 80° C. and at current densities between about 1 to 200 A/dm2.
In other embodiments, the ionic liquid electrolyte consists essentially of an imidazolium compound, a metal salt, and water. In yet other embodiments, the ionic liquid electrolyte consists of an imidazolium compound, a metal salt, and water.
The imidazolium compound can have the general formula (I):
wherein R1, R2, R3, R4, and R5 are each independently selected from an H atom and an organic radical, which in some embodiments may have from 1 to 20 carbon atoms. L− is a compatible anion.
L− is a compatible anion that can include but is not limited to halide anions, carboxylate anions, oxides, organic sulfite or sulfate, inorganic sulfite or sulfate, sulfonate including organo and alkyl sulfonates such as but not limited to methyl, ethyl, propyl, butyl, sulfonate, sulfamate, carbonate, nitrate, nitrite, thiocyanate, hydroxide, sulfonylimide, phosphates such as hexafluorophosphates, phosphonates, phosphinates, phosphites, phosphonites and phosphinites, borates such as tetrafluoroborate, carboxylates, acetates such as trifluoracetate, triflate and halogenated hydrocarbons. Accordingly, the compatible anion can include, but is not limited to, F−, Cl−, Br−, I−, NO2−, NO3−, the group of sulfates, sulfites and sulfonates (including alkylsulfonates), e.g. SO42−, HSO4−, SO32−, HSO3−, H3COSO3−, H3CSO3−, phenylsulfonate, p-tolylsulfonate, HCO3−, CO32-, the group of alkoxides and aryloxides, e.g. H3CO−, H5C2O−, the group of phosphates, phosphonates, phosphinates, phosphites, phosphonites and phosphinites, e.g. PO43−, HPO42−, H2PO4−, PO33−, HPO32−, H2PO3−, the group of carboxylates, e.g. formate and acetate, and the group of halogenated hydrocarbons, e.g. CF3SO3−, (CF3SO3)2N−, CF3CO2− and CCl3CO2−.
The metal salt can include but are not limited to salts of metals, alkalis, rare earth and other salts such as but not limited to Li, Mg, Ca, Cr, Mn, Fe, Co, Ni, Cu, Zn, Cd, Pb, Bi, La, Ce, Al, Ag, Au, Ga, V, In, Nb, Mo, and W. The anion forming the metal salt can be the same as or different from L−. The metal salt can be unhydrated or hydrated.
The molar ratio of the imidazolium compound to metal salt can range from about 0.2:1 to about 10:1, or from about 0.5:1 to about 5:1, or from about 1:1 to about 2:1.
An advantage of the materials in accordance with the invention is that when they are used in electrolytic baths, in particular plating or electropolishing baths, hydrogen evolution is significantly reduced, as compared with conventional acidic baths. As a result, reduced hydrogen evolution can improve the safety of the process and reduce the amount of hydrogen embrittlement that may occur in the substrate material during the electrochemical process. The process according to the present invention may also result in plated materials having an improved surface finish.
The present invention relates to an ionic liquid electrolyte and a method to electroplate metal on a substrate using an ionic liquid electrolyte that includes an imidazolium compound, a metal salt, and water. Typically, the substrate is a metal selected from the group consisting of steel, nickel, aluminum, brass, copper and alloys of these metals.
The imidazolium compound can have the general formula (I):
wherein R1, R2, R3, R4, and R5 are each independently selected from an H atom and an organic radical. L− is a compatible anion.
In some embodiments, R1, R2, R3, R4, and R5 are each independently selected from hydrogen and an organic radical having from 1 to 20 carbon atoms and each can be the same or different. In other embodiments, at least one of R1, R2, and R3 are hydrogen and R4 and/or R5 is a C1 to C20 alkyl. Alternatively, R4 and/or R5 is C1 to C8 alkyl. In other embodiments at least two of R1, R2, and R3 are hydrogen and R4 and/or R5 is a C1 to C20 alkyl. In still other embodiments each of R1, R2, and R3 are hydrogen and R4 and/or R5 is a C1 to C20 alkyl.
L− is a compatible anion that can include but is not limited to halide anions, carboxylate anions, oxides, organic sulfite or sulfate, inorganic sulfite or sulfate, sulfonate including organo and alkyl sulfonates such as but not limited to methyl, ethyl, propyl, or butyl sulfonate, sulfamate, carbonate, nitrate, nitrite, thiocyanate, hydroxide, sulfonylimide, phosphates such as hexafluorophosphates, phosphonates, phosphinates, phosphites, phosphonites and phosphinites, borates such as tetrafluoroborate, carboxylates, acetates such as trifluoracetate, triflate and halogenated hydrocarbons. Accordingly, the compatible anion can include, but is not limited to, F−, Cl−, Br, I−, NO2−, NO3−, the group of sulfates, sulfites, sulfonates, alkyl sulfonates, and alkyl sulfamates, e.g. SO42−, HSO4−, SO32−, HSO3−, H3COSO3−, H3CSO3−, phenylsulfonate, p-tolylsulfonate, HCO3−, CO32-, the group of alkoxides and aryloxides, e.g. H3CO−, H5C2O−, the group of phosphates, phosphonates, phosphinates, phosphites, phosphonites and phosphinites, e.g. PO43−, HPO42−, H2PO4−, PO33−, HPO32−, H2PO3−, the group of carboxylates, e.g. formate and acetate, and the group of halogenated hydrocarbons, e.g. CF3SO3−, (CF3SO3)2N−, CF3CO2 and CCl3CO2−. Suitable alkyl sulfonates and sulfamates may include but are not limited to methane, butane, ethane, propane, sulfonates and sulfamates.
Consistent with the above, suitable imidazolium compounds include, but are not limited to the following:
The metal salt can include but is not limited to salts of the metals, alkalis, rare earth and other salts such as, but not limited to, Li, Mg, Ca, Cr, Mn, Fe, Co, Ni, Cu, Zn, Cd, Pb, Bi, La, Ce, Al, Ag, Au, Ga, V, In, Nb, Mo, and W. The anion forming the metal salt can be the same as or different from L. The metal salt can be unhydrated or hydrated. Suitable metal salts include, but are not limited to: ZnCl2.2H2O, CaCl2.6H2O, MgCl2.6H2O, CrCl3.6H2O, CoCl2.6H2O, LaCl3.6H2O, CuCl2.2H2O, LiCl.5H2O, MoCl5, WCl6, Ca(NO3)2.4H2O, Cr(NO3)3.9H2O, Mn(NO3)2.4H2O, Fe(NO3)3.9H2O, Co(NO3)2.6H2O, Ni(NO3)2.6H2O, Cu(NO3)2.3H2O, Li(NO3).H2O, Mg(NO3)2.6H2O, La(NO3)3.6H2O, Cd(NO3)2.4H2O, Ce(NO3)3.6H2O, Bi(NO3)3.5H2O, Zn(NO3)2.4H2O, Cd(OAc)2.2H2O, Pb(OAc)2.3H2O, or Cr2(SO4)3.15H2O.
A suitable molar ratio of the imidazolium compound to the metal salt may be from about 0.1:4, to about 200:1, or from about 0.5:1 to about 100:1, or from about 1:1 to about 10:1, from about 1:1 to about 6:1, from about 1:1 to about 5:1, from about 2:1 to about 4:1, from about 2:1 to about 3:1 and in some embodiments about 2:1.
Surprisingly and unexpectedly, it has been found that the electrolyte should include an amount of water to achieve the formation of desired metal deposits that are thick, hard, and/or provide a shiny silvery metallic appearance. The amount or concentration of water (related to 1 M metallic salt concentration) to be included in the electrolyte is from about 0.1 M to about 55 M, from about 0.1 M to about 40 M, from about 1 M to about 30 M, from about 2 M to about 20 M, from about 2 M to about 10 M, or from about 1 M to about 55 M, or about 2 M to about 50 M, or from about 4 M to about 30 M, or from about 6 M to about 20 M.
The water for the electrolyte is provided by added water. In other words, the water included in the electrolyte is in addition to any water that is present or provided by the hydrated metal salt. Put another way, it has been found that any water that may be present from the hydrated metal salt (or the imidazolium compound) is not sufficient to produce the desired metal deposits. Accordingly, the electrolyte of the present invention must include added water.
The electrolytes according to the invention may be prepared by mixing together the imidazolium compound, the metal salt, and the added water. It is contemplated that the imidazolium compound and the metal salt are mixed together and, after mixed, water is added. The mixing may be carried out by heating, for example to about 70° C. or more. The resulting mixture remains a liquid, even generally at room temperature.
In one embodiment, it has been found that a suitable electrolyte includes an amount of alkyl imidazolium salt and chromium salt to provide a molar ratio of alkyl Imidazolium salt to chromium salt of about 2:1.
Electrodepositing
Plating equipment is well known and typically includes an electroplating tank that holds the electrolyte and is made of a suitable material inert to the electrolytic plating solution. The tank may have any suitable shape. The cathode substrate and anode are electrically connected by wiring and, respectively, to a rectifier (power supply). The cathode substrate for direct or pulse current has a net negative charge so that metal ions in the solution are reduced at the cathode substrate forming plated metal on the cathode surface. An oxidation reaction takes place at the anode.
Substrates are electroplated by contacting the substrate with the electrolyte of the present invention. The substrate typically functions as the cathode. An anode, which may be soluble or insoluble, is located within the electrolyte. Optionally, the cathode and anode may be separated by a membrane. Potential is typically applied between the anode and the cathode. Sufficient current density is applied and plating is performed for a period of time sufficient to deposit a metal layer, such as a chromium layer, having a desired thickness on the substrate.
Suitable current densities, include, but are not limited to, the range of about 1 to about 200 A/dm2, or from about 1 to about 150 A/dm2, or from about 2 to about 150 A/dm2, or from about 5 to about 150 A/dm2. Typically, the current density is in the range of about 5 to about 100 A/dm2 when used to deposit chromium on a metal substrate. The applied current may be a direct current (DC), a pulse current (PC), a pulse reverse current (PRC) or other suitable current.
The electrolyte may be at a temperature in the range of about 20° to about 100° C. It is generally desirable that the temperature of the electrolyte be less than the boiling point of the electrolyte and generally be less than about 100° or 200°, or 300° C. so that evaporation of the added water does not occur or is minimized. In this regard, it may be suitable if the electrolyte is at a temperature between about 20° C. and 70° C.
In some embodiments, it may desirable to measure and/or to control the conductivity of the electrolyte. However, the conductivity will vary with the temperature of the electrolyte as well as the amount of added water. Nevertheless, the conductivity of the electrolyte should be within the range of about 1 to about 30 mS/cm.
The time to achieve the desired metal thickness can range from 10 seconds to 60 minutes or longer depending on the current density and other operating conditions. The thickness of the deposited metal is at least 0.1 μm, and in some embodiments the thickness can range from about 1 μm to about 500 μm, or from about 5 μm to about 100 μm, or from about 10 μm to about 50 μm, or from about 10 μm to about 20 μm.
A better understanding of the present invention may be obtained through the following examples that are set forth to illustrate, but are not to be construed as limiting.
An electrolyte solution was prepared by mixing: 0.5 M of Cr(NO3)3.9H2O and 1 M of anhydrous EMIM Nitrate, which was poured into a Hull cell, a schematic of which is shown in
Brass plates were prepared before plating by degreasing (acetone) and then activated with abrasive sand paper (grit 600) to eliminate surface oxidation. The brass plate was placed in the Hull cell along edge C. An insoluble anode type titanium mixed metal oxide (“TiMMO”) anode was placed in the Hull cell along edge A. The brass plate and the TiMMO were connected to the negative and positive terminals respectively of a rectifier.
The temperature, current density (Intensity), and duration were varied as shown in Table 1 below. Table 1 presents the results.
No deposition of metallic chromium occurred on the Brass plate whatever the temperature and the cathodic current density were.
An electrolyte solution was prepared according to Comparative Example 1 except water was added so that the electrolyte solution contained 11.2 moles of water. Results obtained are presented in Table 2.
An electrolyte solution was prepared according to Comparative Example 1 except water was added so that the electrolyte solution contained 17.3 moles of water. Results obtained are presented in Table 3.
An electrolyte solution was prepared by mixing: 1 M of Cr(NO3)3.9H2O and 1 M of EMIM Nitrate, which was poured into a Hull cell, a schematic of which is shown in
Brass plates were prepared before plating by degreasing (acetone) and then activated with abrasive sand paper (grit 600) to eliminate surface oxidation. The brass plate was placed in the Hull cell along edge C. An insoluble anode type titanium mixed metal oxide (“TiMMO”) anode was placed in the Hull cell along edge A. The brass plate and the TiMMO were connected to the negative and positive terminals respectively of a rectifier.
The temperature and current density were varied as shown in Table 4 below, which presents the results.
No deposition of metallic chromium occurred on brass plate. For experiment 14, it appears that black stripes were unevenly distributed but were adherent on the plate, 0 and 3-3.5 cm measured on the plate from the higher current density, that correspond to approximately between 100 A/dm2 to 10 A/dm2.
An electrolyte solution was prepared according to Comparative Example 4 except water was added so that the electrolyte solution contained 11.2 moles of water. Results obtained are presented in Table 5.
No deposition of metallic chromium occurred on brass plate.
An electrolyte solution was prepared according to Comparative Example 4 except water was added so that the electrolyte solution contained 17.3 moles of water. Results obtained are presented in Table 6.
No deposition of metallic chromium occurred on brass plate.
An electrolyte solution was prepared by mixing: CrCl3.6H2O and EMIM Nitrate to provide a ratio of CrCl3:EMIM nitrate of 1:2 and was poured into a Hull cell, a schematic of which is shown in
Steel plates were prepared in an HCl wash. The steel plate was placed in the Hull cell along edge C. An insoluble anode type titanium mixed metal oxide (“TiMMO”) anode was placed in the Hull cell along edge A. The steel plate and the insoluble anode were connected to the negative and positive terminals respectively of a rectifier. The temperature was varied from 40° C. to 60° C. and the current density was varied. It was found that there was no metallic deposit on the plate.
A steel plate prepared according to Comparative Example 7 was placed in a Hull cell with an electrolyte solution that was prepared according to Comparative Example 7 except water was added so that the electrolyte solution contained 6 moles of water. The temperature was varied from 40° C. to 60° C. and the current density was varied. It was found that there was no metallic deposit on the plate.
A steel plate prepared according to Comparative Example 7 was placed in a Hull cell with an electrolyte solution prepared according to Comparative Example 7 except water was added so that the solution contained 9 moles of water. The temperature was varied from 40° C. to 60° C. and the current density was varied. It was found that there was no metallic deposit on the plate.
A steel plate prepared according to Comparative Example 7 was placed in a Hull cell with an electrolyte solution prepared according to Comparative Example 7 except water was added so that the solution contained 12 moles of water. The temperature was varied from 40° C. to 60° C. and the current density was varied. It was found that there was no metallic deposit on the plate.
A steel plate prepared according to Comparative Example 7 was placed in a Hull cell with an electrolyte solution prepared according to Comparative Example 7 except water was added so that the solution contained 18 moles of water. The temperature was varied from 40° C. to 60° C. and the current density was varied. It was found that there was no metallic deposit on the plate.
An electrolyte solution was prepared by mixing: CrCl3.6H2O and BMIM Chloride to provide a ratio of CrCl3:BMIM chloride of 1:2 and was poured into a Hull cell, a schematic of which is shown in
Brass plates were prepared by degreasing (acetone) and then activated with abrasive sand paper (grit 600) to eliminate surface oxidation. The brass plate was placed in the Hull cell along edge C. An insoluble anode type titanium mixed metal oxide (“TiMMO”) anode was placed in the Hull cell along edge A. The brass plate and the insoluble anode were connected to the negative and positive terminals respectively of a rectifier.
The temperature and current density (Intensity) were varied as shown in Table 7 below, which presents the results.
No deposition of real metallic chromium occurs on the plate whatever have been the temperature, and the cathodic current density. However, persistent black stripes and a violet coloration suggest that reduction reaction of chromium ions is present at cathodic surface.
An electrolyte solution was prepared according to Comparative Example 12 except water was added so that the electrolyte solution contained 6 moles of water. The temperature was varied from 40° C. to 70° C. and the current density was varied. Results obtained are presented in Table 8.
On each plate, deposition of good metallic chromium appears. Pictures of each plate are provided at
An electrolyte solution was prepared according to Comparative Example 12 except water was added so that the electrolyte solution contained 9 moles of water. The temperature was varied from 40° C. to 70° C. and the current density was varied. Results obtained are presented in Table 9.
On each plate, deposition of good metallic chromium appears. Pictures of each plate are provided at
An electrolyte solution was prepared according to Comparative Example 12 except water was added so that the electrolyte solution contained 12 moles of water. The temperature was varied from 40° C. to 70° C. and the current density was varied. Results obtained are presented in Table 10.
On each plate, deposition of good metallic chromium appears. Pictures of each plate are provided at
An electrolyte solution was prepared according to Comparative Example 12 except water was added so that the solution contained 18 moles of water. The temperature was varied from 40° C. to 70° C. and the current density was varied. Results obtained are presented in Table 11.
On each plate, deposition of good metallic chromium appears. Pictures of each plate are provided at
An electrolyte solution was prepared by mixing: CrCl3.6H2O and EMIM Chloride to provide a ratio of CrCl3:EMIM chloride of 1:2 and was poured into a Hull cell, a schematic of which is shown in
Brass plates were prepared before plating by degreasing (acetone) and then activated with abrasive sand paper (grit 600) to eliminate surface oxidation. The brass plate was placed in the Hull cell along edge C. An insoluble anode type titanium mixed metal oxide (“TiMMO”) anode was placed in the Hull cell along edge A. The brass plate and the insoluble anode were connected to the negative and positive terminals respectively of a rectifier.
The temperature, current density (Intensity) and amount of water were varied as shown in Table 12 below, which presents the results.
The experiments of Example 5 demonstrate that metallic chromium deposition was achieved with the described electrolyte.
An electrolyte solution was prepared by mixing: CrCl3.6H2O and HMIM Chloride to provide a ratio of CrCl3:HMIM chloride of 1:2 and was poured into a Hull cell, a schematic of which is shown in
Brass plates were prepared before plating by degreasing (acetone) and then activated with abrasive sand paper (grit 600) to eliminate surface oxidation. The brass plate was placed in the Hull cell along edge C. A DSA was placed in the Hull cell along edge A. The brass plate and the DSA were connected to the negative and positive terminals respectively of a rectifier.
The temperature, current density (Intensity) and amount of water were varied as shown in Table 13 below, which presents the results.
The experiments of Example 6 demonstrate the efficacy of deposition of metallic chromium and black chromium with the tested electrolyte. The black chromium deposition which is present on certain plates (e.g. plates 34-39) may be useful for black chromium deposition applications such are solar application (photons absorber), decorative application (automotive industry), furnishing, army (decreasing reflection on firearm parts, etc.).
An electrolyte solution was prepared by mixing: CrCl3.6H2O and BMIM Chloride and was poured into a Hull cell, a schematic of which is shown in
Brass plates were prepared before plating by degreasing (acetone) and then activated with abrasive sand paper (grit 600) to eliminate surface oxidation. The brass plate was placed in the Hull cell along edge C. An insoluble anode type titanium mixed metal oxide (“TiMMO”) anode was placed in the Hull cell along edge A. The brass plate and the insoluble anode were connected to the negative and positive terminals respectively of a rectifier.
The temperature, current density (Intensity) and amount of water were varied as shown in Table 14 below, which presents the results.
The experiments of Example 7 demonstrate that metallic chromium deposition was achieved with the described electrolyte.
Deposition on two steel rods (1 and 2) was investigated. Each were prepared by degreasing in ethyl alcohol, water and acetone, thereafter activation (dipped) in HCl solution (¼ HCl+water), surface abrasion using abrasive paper (grid 600), Anodic etching in Sulfuric acid/water solution: 30 A/dm2, with titanium MMO plate cathode for about 1 min., and rinsed in deionized water. Steel rod 1 had a diameter of 0.25 in. and steel rod 2 had a diameter of 0.5 in.
The treated steel rods (Cathodes) were placed in the middle of the Titanium MMO (Mixed Metal Oxide) basket used as an insoluble anode, and the anode and cathode were immersed in the electrolytic solution contained in a beaker. An electrolyte solution was prepared by mixing: CrCl3.6H2O and BMIM Chloride to provide a ratio of CrCl3:BMIM chloride of 1:2.
Deposition was conducted at an average current density of 15-20 A/dm2, at a temperature of 40 to 48° C. The period of deposition for steel rod 1 was about 15 and the period of deposition for steel rod 2 was about 21 minutes. The thickness of the deposited metal was about 15 μm for steel rod 1 and about 20 μm for steel rod 2.
Steel rods were prepared by turning of the rod. The treated steel rods (Cathodes) were placed in the middle of the Titanium MMO (Mixed Metal Oxide) basket used as an insoluble anode and, the anode and cathode were immersed in the electrolytic solution contained in a beaker. An electrolyte solution was prepared by mixing: CrCl3.6H2O and BMIM Chloride to provide a ratio of CrCl3:BMIM chloride of 1:2.
Deposition was conducted at an average current density of 15-20 A/dm2, at a temperature of 35 to 45° C. for about 15 minutes. The thickness of the deposited metal was about 10 μm. Deposition was also conducted at an average current density of 15-20 A/dm2, at a temperature of 40 to 48° C. for about 21 minutes. The thickness of the deposited metal was about 20 μm.
Accordingly, it has been found that the use of the above-described ionic liquid electrolyte and method for depositing metals provides a silvery, metallic, bright, shiny lustrous surface appearance (not black and dull, matte, appearance) with a desired hardness.
It is therefore intended that the foregoing detailed description be regarded as illustrative rather than limiting, and that it be understood that it is the following claims, including all equivalents, that are intended to define the spirit and scope of this invention.
This application claims priority to U.S. Provisional Patent Application No. 61/979,705 filed on Apr. 15, 2014, the entire contents of which are incorporated herein by reference.
This invention was made with government support under IIP1237829 awarded by the National Science Foundation. The government has certain rights in the invention.
| Number | Name | Date | Kind |
|---|---|---|---|
| 3910774 | Krienke | Oct 1975 | A |
| 4906342 | Takahashi | Mar 1990 | A |
| 20130264222 | Bae | Oct 2013 | A1 |
| 20160369418 | Goto | Dec 2016 | A1 |
| Number | Date | Country |
|---|---|---|
| 1884622 | Dec 2006 | CN |
| 101054698 | Oct 2007 | CN |
| 101555608 | Oct 2009 | CN |
| 101629312 | Jan 2010 | CN |
| 102433575 | May 2012 | CN |
| 102766891 | Nov 2012 | CN |
| 102912380 | Feb 2013 | CN |
| 103046081 | Apr 2013 | CN |
| 103046082 | Apr 2013 | CN |
| WO 201109878 | Sep 2011 | WO |
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| Number | Date | Country | |
|---|---|---|---|
| 20150292098 A1 | Oct 2015 | US |
| Number | Date | Country | |
|---|---|---|---|
| 61979705 | Apr 2014 | US |
