This application pertains to electrochemical gas detectors, which incorporate microelectrodes. More particularly, this application pertains to electrochemical gas detectors, which include an electrode comprised of a catalyst deposited onto a porous surface.
Electrochemical gas sensors using microelectrodes have a number of benefits, such as the ability to use fast scanning voltammetric measurements, utilizing features such as convergent diffusion and potentially being simpler to construct than conventional gas diffusion electrodes. However they also suffer from disadvantages. In particular it is more difficult to achieve a reliable 3-phase region, i.e., a region where gas does not have to diffuse a long distance through the electrolyte before reaching the sensing electrode(s).
The analyte gas can dissolve in the electrolyte and give rise to a background current which remains after the target gas is removed, resulting is slow response times and background current errors.
This issue is normally overcome in conventional gas sensors by ensuring that all of the target gas is consumed by the sensing electrode (e.g., via capillary limitation of flux to a gas diffusion electrode). However the design of gas diffusion electrodes is complex, especially when using non-aqueous electrolytes such as ionic liquids, and the resulting large surface area and hence double layer capacitance means that dynamic electrochemical techniques such as scanning voltammetry are not feasible.
An example of the current state of the art in microband electrodes are those manufactured by Nanoflex® (http://www.nanoflex.com/Products/Product/Platinum_Substrate) which comprise band electrodes within wells of micrometer dimensions. Previously people have also used line electrode devices deposited on ionic conducting substrates (Kirsi Wallgren, PhD thesis 2005, University of Nottingham and references therein). Microband electrodes can be made via sandwich structures using, for example, micromachined silicon layers or line electrodes on the surface of a substrate. These approaches do not address the issue of ensuring easy gas access to the sensing electrode, since it is immersed within the electrolyte (which may be either a solid or liquid).
In accordance herewith, methods and structures are provided for utilizing microelectrodes and particularly microband electrodes in such a way as to ensure rapid gas access to the sensing electrode(s) and/or to compensate or correct the sensor behavior for variations in the degree to which the sensing electrode is wetted. The attached figures illustrate various aspects of embodiments hereof.
The use of non-gas diffusion electrodes in electrochemical gas sensors can alleviate some problematic issues that persist in traditional systems, such as humidity transients, low sensitivity, and slow response times. The novel electrochemical gas sensor described herein includes a sensing electrode fabricated by depositing a catalyst onto a porous support material. The catalyst can be platinum or another noble metal or other catalysts or mixtures thereof known in the art. The porous material can be polytetrafluoroethylene (PTFE) or other porous materials known in the art. This catalyst can be deposited randomly or uniformly. On deposition technique is vacuum sputtering, which when utilized, yields a thin, fully wetted electrode having pores through which a gas can travel. The electrode gives negligible humidity transients when used with an electrolyte such as sulfuric acid, phosphoric acid, ethylmethylimidazolium hydrogen sulfate (EMIM HS) or other known electrolytes or mixtures thereof. The electrode also gives fast response times to hydrogen sulfide gas when used with the above electrolytes.
The electrolyte can be present as a free liquid, absorbed in a wick or separator material, or absorbed in a solid support. The solid support that the electrolyte is absorbed on can be polybenzimidazole film.
This approach requires the shape and location of the electrolyte meniscus to be well defined, which in practice does not always occur—for example changes in temperature and or hydration level of the electrolyte can cause the electrolyte layer to move. By performing measurements such as electrochemical impedance spectroscopy (EIS) on the different electrodes within the structure in
Structures as described above and illustrated by the attached can be fabricated using, for example, screen printing, MEMS fabrication, multilayer printed circuit boards (e.g., with platinum plated copper), or techniques such as those used for making film and foil capacitors or multilayer batteries.
From the foregoing, it will be observed that numerous variations and modifications may be effected without departing from the spirit and scope of the invention. It is to be understood that no limitation with respect to the specific apparatus illustrated herein is intended or should be inferred. It is, of course, intended to cover by the appended claims all such modifications as fall within the scope of the claims.
Further, logic flows depicted in the figures do not require the particular order shown, or sequential order, to achieve desirable results. Other steps may be provided, or steps may be eliminated, from the described flows, and other components may be add to, or removed from the described embodiments.
This application claims priority of U.S. Provisional Application Ser. No. 61/830,392 filed Jun. 3, 2013, whose disclosures are incorporated herein by reference.
Number | Date | Country | |
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61830392 | Jun 2013 | US |