DEVICE AND METHOD FOR GAS MAINTENANCE IN MICROFEATURES ON A SUBMERGED SURFACE
20180320717 ยท 2018-11-08
Assignee
Inventors
Cpc classification
B81C99/0085
PERFORMING OPERATIONS; TRANSPORTING
C25B5/00
CHEMISTRY; METALLURGY
B29C59/022
PERFORMING OPERATIONS; TRANSPORTING
F15D1/003
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F15D1/0065
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B63B2001/387
PERFORMING OPERATIONS; TRANSPORTING
B63B1/38
PERFORMING OPERATIONS; TRANSPORTING
B81B1/006
PERFORMING OPERATIONS; TRANSPORTING
International classification
F15D1/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B81B1/00
PERFORMING OPERATIONS; TRANSPORTING
B81C99/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A microstructured surface with microfeatures formed thereon and defining spaces between the microfeatures includes least one electrode of an electrode pair in the spaces, wherein electrodes of the pair are electrically connected to one another. The at least one electrode located in the space is configured to generate a gas in between the microfeatures when an electrolyte solution penetrates into the microfeatures. Importantly, the electrodes are not connected to any external power source. Because the microstructured surface is self-powered in replenishing the gas lost in a submerged condition, no additional provision to supply energy or regulate the replenishment is necessary for implementation and use.
Claims
1. A microstructured surface comprising: a plurality of microfeatures disposed on a substrate and defining a space located between inner surfaces of the plurality of microfeatures, wherein the inner surfaces between the plurality of microfeatures are at least partially hydrophobic; a gas generator comprising a first electrode of an electrode pair electrically connected to a second electrode of the electrode pair, the first electrode disposed within the space located between inner surfaces of the plurality of microfeatures and configured to generate a gas by a spontaneous electrochemical reaction when part of the space located between the microfeatures is filled with an electrolyte solution while the microstructured surface is submerged in the electrolyte solution.
2. The microstructured surface of claim 1, wherein the first electrode of the electrode pair is located on the substrate between microfeatures.
3. The microstructured surface of claim 1, wherein the first electrode of the electrode pair is located on the inner surface of at least one of the microfeatures.
4. The microstructured surface of claim 1, wherein the first electrode and the second electrode of the electrode pair have respective standard electrode potentials that generate gas by spontaneous electrochemical reaction when contacted by the electrolyte solution, and the difference between the standard electrode potential of the electrolyte and the standard electrode potential of the second electrode is, in magnitude, larger than an overpotential for gas generation at the first electrode, and wherein the overpotential at the first electrode is, in magnitude, smaller than the overpotential at the second electrode.
5. The microstructured surface of claim 1, wherein the first electrode of the electrode pair comprises one of a trace, track, porous layer, mesh, or wire.
6. The microstructured surface of claim 1, wherein the first electrode comprises nickel and the second electrode comprises magnesium.
7. A microstructured surface comprising: a plurality of microfeatures disposed on a substrate and defining a space located between inner surfaces of the plurality of microfeatures, wherein the inner surfaces between the plurality of microfeatures are at least partially hydrophobic; a gas generator comprising a first electrode and a second electrode of an electrode pair electrically connected to one another, the first electrode and the second electrode disposed within the space located between inner surfaces of the plurality of microfeatures and configured to generate a gas in between the microfeatures by spontaneous electrochemical reaction when part of the space is filled with an electrolyte solution while the microstructured surface is submerged in the electrolyte solution.
8. The microstructured surface of claim 7, wherein the electrode pair is located on the substrate between microfeatures.
9. The microstructured surface of claim 7, wherein the electrode pair is located on the inner surface of at least one of the microfeatures.
10. The microstructured surface of claim 7, wherein the electrodes of the electrode pair have respective standard electrode potentials that generate gas by spontaneous electrochemical reaction when contacted by the electrolyte solution, and the difference between the standard electrode potential of the electrolyte and the standard electrode potential of the second electrode is, in magnitude, larger than an overpotential for gas generation at the first electrode, and wherein the overpotential at the first electrode is, in magnitude, smaller than the overpotential at the second electrode.
11. The microstructured surface of claim 7, wherein the electrode pair comprise one of a trace, track, porous layer, mesh, or wires.
12. The microstructured surface of claim 7, wherein the first electrode comprises nickel and the second electrode comprises magnesium.
13. A method of forming a microstructured surface comprising: depositing electrodes on a surface of a substrate; securing a mold against the surface of the substrate containing the electrodes so as to form a tight contact between the mold and electrodes, the mold containing a plurality of cavities therein; applying pressure between the mold and the substrate to force material from the substrate into the plurality of cavities to form a plurality of microfeatures; and separating the mold from the substrate.
14. The method of claim 13, wherein pressure is applied at an elevated temperature.
15. The method of claim 13, further comprising removing any substrate material covering the electrodes after separating the mold from the substrate.
16. The method of claim 13, further comprising coating the plurality of microfeatures with a hydrophobic layer.
17. The method of claim 16, wherein the hydrophobic layer comprises polytetrafluoroethylene (PTFE).
18. The method of claim 13, further comprising connecting the electrodes on the substrate to another electrode formed from a different material.
19. A water-borne vehicle or watercraft having the microstructured surface of claim 1 on at least a portion of a water-contacting surface.
20. A water-borne vehicle or watercraft having the microstructured surface of claim 7 on at least a portion of a water-contacting surface.
21. A pipe having the microstructured surface of claim 1 on an interior surface thereof.
22. A pipe having the microstructured surface of claim 7 on an interior surface thereof.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0015]
[0016]
[0017]
[0018]
[0019]
[0020]
[0021]
[0022]
DETAILED DESCRIPTION OF THE ILLUSTRATED EMBODIMENTS
[0023]
[0024] The height of the microfeatures 6 should be high enough such that the sagging meniscus does not touch the substrate 4. This height is also a function of the pitch of the microfeatures 6. It should be understood that a microstructured surface 2 includes a surface that contains microfeatures 6 made of or whose surface is made of a material that water or liquid of interest does not wet, i.e., forms a contact angle larger than 90 on its surface. This means the liquid is not restricted to water and may be of any kind, including water, oil, or solvent, despite the use of hydrophobic as described herein.
[0025] The microfeatures 6 may be formed from the same or different material from the substrate 4. For instance, in some embodiments, the microfeatures 6 may be formed from a polytetrafluoroethylene (PTFE) or the like. The microfeatures 6 may be made mostly from a material that is particularly hydrophobic. Alternatively, at least some portions of the microfeatures 6 may be coated with a hydrophobic material such as PTFE or the like. In some embodiments, the top surfaces of the microfeatures 6 may not be hydrophobic so that only the inner surfaces between the microfeatures 6 are hydrophobic. During typical applications, a fluid of electrolyte 8 that is electrically conductive is disposed on the microstructured surface 2. A typical electrolyte 8 may include seawater or water having dissolved ionic species therein.
[0026] With reference to
[0027] The following criteria set forth the conditions required for the operation of the microstructured surface 2 submerged in electrolyte 8 having a first electrode 12 used for gas generation that is located in the space 13 between microfeatures 6 and a second electrode 14 that may or may not be located in the space 13 as explained herein. Gas generation does not appreciably occur at the second electrode 14 but rather occurs at the first electrode 12 in this description. For the first condition, the SEP of the second electrode 14, denoted SEP.sub.2, should be different from the SEP of electrolyte 8, denoted SEP.sub.3 as seen in Equation 1 below:
SEP.sub.2SEP.sub.3 Eq. 1
[0028] This condition (Equation 1) is required to ensure that there is a reaction between the second electrode 14 and the electrolyte 8.
[0029] The second condition is that the half-reaction of electrolyte 8 should produce gas 10 under standard pressure and temperature. This condition is to ensure that the reaction will generate gas.
[0030] The third condition is that the difference in the theoretical standard cell potentials between the second electrode 14 and electrolyte 8 (SEP.sub.2SEP.sub.3) should be, in magnitude, larger than the overpotential of half-reaction of electrolyte 8 on the first electrode 12, denoted OP.sub.3/1 as seen in Equation 2 below:
|SEP.sub.2SEP.sub.3|>|OP.sub.3/1|Eq. 2
This condition (Equation 2) is to ensure that gas 10 can be generated on the first electrode 12.
[0031] For the fourth condition, the overpotential of half-reaction of electrolyte 8 on the first electrode 12, denoted OP.sub.3/1, should be, in magnitude, smaller than the overpotential of half-reaction of electrolyte 8 on the second electrode 14, denoted OP.sub.3/2 as seen in Equation 3 below:
|OP.sub.3/1|<|OP.sub.3/2|Eq. 3
[0032] This condition (Equation 3) is to ensure the gas 10 is generated mainly on the first electrode 12 rather than on the second electrode 14. All four conditions should be satisfied for the gas generation to operate properly.
[0033] Note that the above conditions can be divided into two scenarios, depending on whether the gas generation is by reduction or oxidation reaction. If the gas generation on the first electrode 12 is by reduction reaction (e.g., 2H.sup.++2e.sup..fwdarw.H.sub.2), then the SEP of the second electrode 14, SEP.sub.2, should be smaller than the SEP of the electrolyte, SEP.sub.3 as seen by Equation 4 below.
SEP.sub.2<SEP.sub.3 Eq. 4
[0034] In addition, the half-reaction of the electrolyte 8 should produce the gas under standard pressure and temperature. Further, the theoretical standard electrode potential between the second electrode 14 and the electrolyte 8 (SEP.sub.2SEP.sub.3) should be smaller (i.e., more negative) than the overpotential of half-reaction of the electrolyte 8 on the first electrode 12, OP.sub.3/1 as seen by Equation 5 below.
SEP.sub.2SEP.sub.3<OP.sub.3/1 Eq. 5
[0035] The overpotential of half-reaction of the electrolyte 8 on the first electrode 12, OP.sub.3/1, should be larger (i.e., less negative) than the overpotential of half-reaction of the electrolyte 8 on the second electrode 14 OP.sub.3/2 as seen by Equation 6 below.
OP.sub.3/1>OP.sub.3/2 Eq. 6
[0036] Alternatively, if the gas generation on the first electrode 12 is by oxidation reaction (e.g., 4OH.sup.+4e.sup..fwdarw.O.sub.2+2H.sub.2O), the SEP of the second electrode 14 SEP.sub.2 should be larger than the SEP of the electrolyte 8 SEP.sub.3 as seen by Equation 7 below.
SEP.sub.2>SEP.sub.3 Eq. 7
[0037] The half-reaction of the electrolyte 8 should produce a gas under standard pressure and temperature. The theoretical standard electrode potential electrode potential between the second electrode 14 and the electrolyte 8 (SEP.sub.2SEP.sub.3) should be larger (i.e., more positive) than the overpotential of half-reaction of the electrolyte 8 on the first electrode 12, OP.sub.3/1 as seen by Equation 8 below.
SEP.sub.2SEP.sub.3>OP.sub.3/1 Eq. 8
[0038] The overpotential of half-reaction of the electrolyte 8 on the first electrode 12, OP.sub.3/1, should be smaller (i.e., less positive) than the overpotential of half-reaction of the electrolyte 8 on the second electrode 14 OP.sub.3/2 as seen by Equation 9 below.
OP.sub.3/1<OP.sub.3/2 Eq. 9
[0039] Specifically, according to one embodiment, if the electrolyte 8 is a neutral or alkaline water solution (e.g., seawater), the standard electrode potential is about 0.83 V from 2H.sub.2O+2e.sup.H.sub.2(g)+2OH.sup.. If the electrolyte 8 is an acid water solution, the standard electrode potential is 0 V from 2H.sup.++2e.sup.H.sub.2(g). Once the electrolyte 8 is chosen, possible materials combinations for the first electrode 12 and the second electrode 14 could be obtained, satisfying the constraints stated above regarding standard electrode potential and over-potential. For a specific example, the first electrode 12 may be made from a metal or metal alloy containing nickel, the second electrode 14 may be made from a metal or metal alloy containing magnesium, and the electrolyte 8 may be seawater (although other electrolytes may also be used such as fresh water, acid solutions, basic solutions, and the like). In this case, the gas 10 that is produced is hydrogen at the first electrode 12. Table 1 below lists various materials and SEP and overpotential values that have been tested with successful results.
TABLE-US-00001 TABLE 1 |OP| (H.sub.2 evolution Name Material Half reaction SEP at 25 C.) First Nickel N/A (inert) N/A 0.28 V Electrode Second Magnesium Mg.sup.2+(aq) + 2e.sup. .Math. Mg(s) 2.372 V ~1 V Electrode Electrolyte Seawater 2H.sub.2O(l) + 2e.sup. .Math. H.sub.2(g) + 2OH.sup.(aq) 0.8277 V N/A
[0040] Where and when at least a portion of the space between microfeatures 6 are filled with the electrolyte 8 and contact the gas generating electrode, gas 10 (e.g., hydrogen) is automatically generated by the spontaneous electrochemical reaction (i.e., galvanic reaction) that takes place. The microfeatures 6 are designed and spaced such that the gas 10 that is generated on the electrode 12 is trapped and grows within the localized space, gap, or well 13 formed between adjacent microfeatures 6. Once the volume of generated gas 10 has grown in size to the top (e.g., upper surface) of the microfeatures 6 the gas 10 proceeds to extend laterally in between the microfeatures 6 across the microstructured surface 2. In this regard, the microstructured surface 2 can be restored from a partially or fully wetted state back into a non-wetted state. In one embodiment, the first electrode 12 is disposed on or embedded in the substrate 4.
[0041] The gas 10 that is generated by the first electrode 12 is trapped and grows in the localized space or well 13 formed between adjacent microfeatures 6. It should be noted that gas generation is self-regulated in this embodiment. In particular, the electrochemical circuit is closed and gas generation occurs only if the microstructured surface 2 becomes partially or fully wetted. Once the electrolyte 8 invades the space 13 between adjacent microfeatures 6 the circuit is closed between the first electrode 12 and the second electrode 14 and the electrochemical reaction proceeds, thereby liberating gas 10 within the spaces 13 located between the microfeatures 6. After sufficient gas generation, the electrochemical circuit then becomes open and the electrochemical reaction stops. This feature is particularly advantageous because there is no need for any sensing and controlling circuitry to switch the gas generator (i.e., electrode) on or off; in other words, the gas generation is self-regulated to respond to presence of electrolyte 8 in between the microfeatures 6.
[0042] The gas generation occurs spontaneously without connecting the microstructured surface 2 to any external power source (e.g., battery); in other words, the gas generation is self-sufficient. However, since the gas generation is the product of an electrochemical reaction (i.e., powered electrically albeit using internal energy) rather than pure chemical reaction (i.e., no electric power involved), one may call the disclosed method of gas generation not only self-sufficient but also self-powered. In addition and related to the above difference, it is worth noting that the gas generator (i.e., electrode) located in between the microfeatures 6 is not a reactant in the current self-powered, electrochemical reaction. Self-powering and self-regulating the gas generation, the microstructured surface 2 has the built-in ability to maintain the gas 10 trapped in between its microfeatures 6.
[0043]
[0044]
[0045]
[0046]
[0047] An important aspect for the disclosed fabrication method is how to realize the electrodes (e.g., electrodes 12, 14) exposed or almost exposed in between microfeatures 6 while forming microfeatures 6 by embossing/imprinting. As shown in
[0048]
[0049]
[0050] The microstructured surfaces 2 described herein may be used on an exterior surface of a water-borne vehicle or watercraft (e.g., boat, ship, or the like) that comes into contact with the water. In one particular embodiment, the choice of materials for electrodes 12, 14 is selected for particularly suitability for use in salt-water contact applications (e.g., for water-borne vehicles or watercraft that travel in seawater). The microstructured surfaces 2 may also be used in other applications. For example, the microstructured surfaces 2 may be located on the inner surface of a pipe or conduit.
[0051] While embodiments have been shown and described, various modifications may be made without departing from the scope of the inventive concepts disclosed herein. The invention(s), therefore, should not be limited, except to the following claims, and their equivalents.