Abstract:
The present invention provides a method of making a fluoropolymer comprising: (i) providing an aqueous dispersion of fluoropolymer particles by polymerizing one or more fluorinated olefins and optionally one or more fluorinated or non-fluorinated comonomers in an aqueous emulsion polymerization whereby the polymerization is initiated in the absence of a fluorinated surfactant and whereby no fluorinated surfactant is added during polymerization; (ii) recovering the fluoropolymer from the aqueous dispersion thereby obtaining said fluoropolymer and waste water; and (iii) contacting said waste water with an anion exchange resin; or alternatively to steps (ii) and (iii), contacting said aqueous dispersion with an anion exchange resin and subsequently separating said anion exchange resin from said aqueous dispersion.
Abstract:
A purification method employs nanofiltration of an aqueous solution containing one or several sugars, multivalent cations, monovalent metal cations, monovalent anions and multivalent inorganic anions and/or organic acid anions. The method includes replacement of at least a part of said multivalent cations and/or said multivalent inorganic anions and organic acid anions respectively by monovalent metal cations and/or monovalent anions to produce a solution. Nanofiltration of the solution is carried out to obtain a retentate, and at least part of the retentate is subject to crystallization.
Abstract:
An improved system of resins comprising a combination of a sulfate-specific strongly basic anion exchange resin and a heterogenous hybrid thermally regenerable salt sorbent (TRSS) resin is provided. The anion exchange resin contains triethylamine and/or tributylamine groups. The TRSS resin comprises a macroporous host copolymer and a crosslinked guest copolymer having, respectively, weak acid groups and weak base groups. The system is used to treat feed water containing dissolved ions, including sulfate ions, and is efficiently regenerated.
Abstract:
A treatment system passes feed water containing a contaminant such as perchlorate through a bed of strong base anion exchange resin that has been placed in a form (e.g., in sulfate form) to selectively capture the contaminant while passing other ions (e.g., nitrate) that may also be present in the water. The bed selectively removes the perchlorate with high efficiency, for example on a stoichiometric basis, until exhaustion. The bed operates robustly without spiking or displacement of more weakly-held or lower affinity ions as composition of the feed varies. The water may be further treated, if necessary, to produce a purified or potable product, in which case downstream processes may remove remaining contaminants and co-ions. Alternatively, the treated stream may be returned to or blended with the source to effect contaminant remediation, e.g., site clean-up. Contaminants such as uranium species, perchlorate or pertechnate may be treated by this method using ordinary (non-specialty) exchange resins. The bed may include a carousel, and the exhausted upstream portion of the resin may efficiently be disposed of by incineration, or may be rotated out for regeneration. Alternatively, the bed or the spent portion thereof may be periodically regenerated transferring perchlorate to a regeneration fluid waste. The concentrated waste may be disposed of by incineration, bioreaction or other suitable disposal process. The concentrated regen waste may also be passed through a smaller, sacrificial bed of ion exchange resin to capture its perchlorate, allowing re-use of the regen fluid and forming a lower-volume solid waste output. This second-bed re-transfer process operates efficiently at the high concentration present in spent regen fluid, and requires only a small fraction of the original bed volume.
Abstract:
Reacting weakly basic anion exchangers bearing tertiary amino groups with ethylene oxide under pH control and addition of acid leads to superior strongly basic anion exchangers.
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 purified fluid product within a container to prevent the subsequent addition of contaminants.
Abstract:
A new method is described to produce large volumes of low cost sterile, Water-for-Injection (WFI) grade water on-line, on-demand from potable water in order to meet the needs of dialysis therapies and other biological applications for sterile, injectable grade water. The source water is processed by a combination of membrane and column chromatographic methods including reverse osmosis, chemical sterilization, reduction of iodine sterilant to iodide, deionization, endotoxin-specific adsorption and polishing filtration in order to reduce contaminant levels below those specified by the US Pharmacopoeia.
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.