Abstract: A bike securing apparatus (100) having a vertical member (1), a first engagement member (2), that coupled to the vertical member (1) and comprises a means for attaching to a bicycle pedal (63); and an anti-rotation member (3), that coupled to the vertical member (1) or the first engagement member (2), and has a means for attaching to a bicycle (6). The first engagement member (2) is configured to attach to the bicycle pedal (63) and limit movement of the bicycle pedal (63), and the anti-rotation member (3) is configured to attach to the bicycle (6) at a location other than said bicycle pedal (63) and limit rotation of a said bicycle (6) about the first engagement member (2).
Abstract: A chemical distribution system having improved organic solvent fluid purity and consistency includes a vessel containing ion-exchange media positioned within a fluid flow pathway such that the organic solvent fluid passes through the ion-exchange media, thereby effecting removal of undesired impurities. Different embodiments of the invention position the vessel at varying locations within the fluid flow pathway. The chemical distribution system also preferably includes a return chemical flow pathway that recirculates purified organic solvent fluid through the ion-exchange media-containing vessel and thereby enables the system operator to conduct incremental adjustment of the solvent purity until a desired overall purity is attained.
Abstract: A method of removing inorganic contamination from dielectric condensate precursor fluids and silicate esters, such as tetraethylorthosilicate (TEOS), methyltriethoxyorthosilicate (MTEOS), hydrogen silsesquioxane (HSQ), methyl silsesquioxane (MSQ), polyarylene ether, benzocyclobutene (BCB), or OSG, includes obtaining a commercial grade fluid having up to 10,000 ppb individual metallic contaminants; converting the sodium form of one or more macroporous ion exchange resin beds to a hydrogen form; converting the chloride form of one or more macroporous ion exchange resin beds to a hydroxide form; drying the macroporous ion exchange resin beds to remove substantially all water from the ion exchange resin beds; passing fluids through the ion exchange resin beds one or more times by recirculating all or a portion of the fluid to obtain a purified fluid having less than 1 ppb of individual metallic contaminants, less than 10 ppb of boron contaminants, and less than 1 ppb of chloride contaminants; and collecting the p