Abstract:
The present invention is generally directed to a versatile fluid treatment system which includes: a mobile device; a track system connected to the mobile device; one or more treatment vessels removably attached to the track system, each treatment vessel comprising a treatment material disposed inside the treatment vessel, at least one fluid inlet, and at least one fluid outlet; an input conduit that receives a fluid to be treated, the input conduit in fluid communication with the fluid inlet on the treatment vessel; and an output conduit in fluid communication with the fluid outlet on the treatment vessel, the output conduit receives treated fluid from the treatment vessels via the fluid outlet.
Abstract:
A frustum filter used for separation of cation and anion exchange resins, which is used in condensate water polishing system or apparatus, wherein said frustum filter comprises a microporous filtering net body (1) which is formed by sintering a mixture of silicon carbide grains and a binder, said net body being provided with a plurality of micropores, the diameter of said micropores being in a range of 50-300 micron, said filtering net body (1) being shaped as an inverted truncated cone and its maximum diameter being in a range of 50-200 cm, the angle between a inner tapered face and a horizontal plane being in a range of 15°-30° and the thickness of said filtering net body being in a range of 2 cm-14 cm. Some reinforcing steel bars which have the property of high temperature resistance are embedded in said filtering net body(1) in advance. A steel ring (6) welded at the housing (2) is fixed on the external circumference of said filtering net body (1). This invention has the following advantages: it can distribute evenly water and has high strength; it can not be blocked easily and will not create dead zones when filtration; the product of the invention has high strength and cannot be deformed easily over the prior art; it also has the properties of strong acid fastness, strong alkali fastness, high temperature resistance, oxidation resistance.
Abstract:
By passing an alkali regenerating agent A through a basic anion exchange resin (3), and through a strongly acidic cation exchange resin (4), the basic anion exchange resin can be regenerated while amphoteric organic materials such as the amino acids captured at the strongly acidic cation exchange resin can be desorbed. Then, an acid regenerating agent B is passed through the strongly acidic cation exchange resin to regenerate the strongly acidic cation exchange resin.
Abstract:
THIS INVENTION RELATES TO THE REGENERATION OF ANION EXCHANGE RESINS USED IN MIXED ION EXCHANGE RESIN BED DEMINERALIZERS WHEREIN THE RESINS ARE SEPARATED, THE ANION EXCHANGE RESIN FRACTION REGENERATED WITH AN ALKALI METAL COMPOUND, AND THE REGENERATED RESINS ADMIXED TO REFORM THE MIXED BED. SPECIFICALLY, THE INVENTION COMPRISES TREATMENT OF THE ANION EXCHANGE RESIN FRACTION AFTER REGENERATION TO REPLACE THE ALKALI METAL CATION ASSOCIATED WITH THE CATION EXCHANGE RESIN PRESENT IN THE ANION EXCHANGE RESIN FRACTION WITH AN ALKALINE EARTH METAL CATION SELECTED FROM THE GROUP CONSISTING OF CALCIUM, BARIUM, STONTIUM, AND MIXTURES THEREOF, AND REMOVING THE ALKALI METAL CATION FROM THE FRACTION PRIOR TO ADMIXTURE OF THE RESINS TO REFORM THE MIXED BED.
Abstract translation:1278005离子交换WESTINGHOUSE ELECTRIC CORP 1970年9月30日[1969年10月] 46426/70标题B1J混合床的阴离子和阳离子交换树脂通过将混合床分离成两部分来再生,一部分主要是阴离子交换树脂,另一部分 主要是阳离子交换树脂再生每个级分,阴离子交换树脂级分首先用苛性碱溶液,然后用含有Ca,Sr或Ba阳离子的碱性溶液代替阳离子交换树脂中存在的阳离子交换树脂中的碱金属阳离子 阴离子分数。 混合床然后改革。
Abstract:
THIS PATENT DESCRIBES A PROCESS FOR THE TREATMENT OF AN AQUEOUS STREAM CONTAINING IONIC POLLUTANTS TO REMOVE THE IONS FROM THE STREAM AND RECOVER THE IONS WHICH COMPRIESES: OPTIONALLY COUNTERCURRENTLY PASING SAID AQUEOUS STREAM THROUGH A BED OF MIXED ION EXCHANGE MATERIAL TO REMOVE IONIC POLLUTANTS FROM THE STREAM AND PRODUCE A SUBSTANTIALLY ION-FREE WATER, REMOVING SPENT MIXED ION EXCHANGE MATERIAL FROM SAID BED AND SEPARATING THE SAME INTO ANIONIC AND CATIONIC ION EXCHANGE MATERIAL, REMOVING THE IONIC POLLUTANTS FROM THE SEPARATED SPENT ANIONIC AND CATIONIC ION EXCHANGE MATERIAL WITH ANIONIC AND CATIONIC REGENERANT STREAMS TO REGENERATE THE ANIONIC AND CATIONIC ION EXCHANGE MATERIAL AND TO FORM SPENT ANIONIC AND CATIONIC REGENERANTSTREAMS, RETURING THE REGENERATED
ANIONIC AND CATIONIC EXCHANGE MATERIAL TO SAID BED, TREATING SAID SPENT CATIONIC REGENERANT STREAM WITH A METAL PRECIPITANT TO FORM PRECIPITATED METAL CARBONATES AND RECOVER THE CATIONIC REGENERANT STREAM FOR RECYCLE TO SAID SPENT CTIONIC ION EXCHANGE MATERIAL, AND CONTACTING SAID SPENT ANIONIC REGENERANT STREAM WITH SAID PRECIPITATED METAL CARBONATES AT ELEVATED TEMPERATURES TO PRECIPITATE METAL SALTS AND RECOVER METAL PRECIPITANT FOR RECYCLE TO SAID SPENT CATIONIC REGENERANT STREAM AND ANIONIC COMPLEXING AGENTS FOR RECYCLE TO SAID SPENT ANIONIC ION EXCHANGE MATERIAL.