The rates of adsorption of hydrochloric acid by 16 weakly basic ion-exchange resins have been measured, together with the rates of adsorption of sodium hydroxide by 16 weakly acidic ion-exchange resins. The results obtained for the weakly basic resin "Amberlite IRA-93" confirm that the adsorption ra
Further studies on the weak electrolyte ion exchange resin desalination process (Desal Process)
โ Scribed by Robert Kunin
- Publisher
- Elsevier Science
- Year
- 1968
- Tongue
- English
- Weight
- 650 KB
- Volume
- 4
- Category
- Article
- ISSN
- 0011-9164
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โฆ Synopsis
Studies on the bw?3k clectrolytc ion cxcbangc resin daaiination process, DESAL m wcrc continual in conjunction with field tri315. The r:udics ~zrc conducted on brackish waters, 3cid mine drainage waras emanating from coal mines, and szwagc dflucnts. TLu DESAL pta;tss inu&es tltc following steps: (l) CarbGnation -a~nversion of wrak bare anion cxdt3agc resin to bicarbonate tait. Of Afkafiiion -anion exctrangc cooversion of salinity to atkaiinity. ~3) D4lrrttization -c&ion cxchangc removal ofc3tMrrr and txpulsien of liberated CO,. Variatiollt in the dcsaiination prrxr~s have baa dcvciopcd that permit one te t&e adv3nt3ge of varying water armpositions and specific water quality requirements. These innovatim include a uwbinarion of the first stage of the DESAL Process (3lMitation) with cold-Iimc s&'&sting. Tbc reuits indirate that one may desalinate economically bmckish waters, magc efftuents. and acid mine daaiw wdtcrs with a weak ek~rolytc ion exchange r&n tilination process using. at hi& cf6&&es. such cheap regcncrants as NHJ. NaOH. N32CO3, or CaO for the anion cxetlangc resin and H-$0&. SOa. or CO2 for the cation cxcbange resin. A p!3xX instaliation has been operating in the U.S. sucessfttlfy for the fest nine months at rated cRp3city dud without difficulty.
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