An empirical kinetic model for calcium removal from calcium impurity-containing saturated boric acid solution by ion exchange technology using Amberlite IR-120 resin
| dc.authorid | 0000-0003-3962-9255 | en_US |
| dc.contributor.author | Özmetin, Cengiz | |
| dc.contributor.author | Aydın, Özkan | |
| dc.contributor.author | Kocakerim, M. Muhtar | |
| dc.contributor.author | Korkmaz, Mustafa | |
| dc.contributor.author | Özmetin, Elif | |
| dc.date.accessioned | 2019-10-18T08:35:19Z | |
| dc.date.available | 2019-10-18T08:35:19Z | |
| dc.date.issued | 2009 | en_US |
| dc.department | Fakülteler, Mühendislik Fakültesi, Çevre Mühendisliği Bölümü | en_US |
| dc.description | Özmetin, Cengiz (Balikesir Author) | en_US |
| dc.description.abstract | In this study, the use of Amberlite IR-120, a strong acidic cation exchange resin. was investigated to remove calcium impurity from saturated boric acid solutions. Calcium impurity arised from high calcium content of colemanite ore is a very important problem as it increases impurity on the boric acid crystals. Ion exchange experiments were carried out in batch mode as a function of solution pH. resin-to-solution ratio, temperature, and resin contact time. Optimum operation conditions were determined as pH 1.5, resin-to-solution ratio 6.174 g/250 mL, temperature 303 (K), contact time 20 min and, in those conditions maximum calcium removal was about 99%. Also, data calculated by a mass balance equation were employed with the pseudo-first-order and the pseudo-second-order equations. It was determined that the pseudo-second-order equation was the best fitting kinetic equation with a correlation range of 0.991-1. Furthermore, an empirical kinetic model was developed to predict operational conditions of the batch process in the following form; t/q(t), = 6.1452 x (S/L)(0.8903) x [H(+)](-0.00094) x exp(-31.2181/T) x [C(0)](-0.7319) x t(0.9567). | en_US |
| dc.identifier.doi | 10.1016/j.cej.2008.09.021 | |
| dc.identifier.endpage | 424 | en_US |
| dc.identifier.issn | 1385-8947 | |
| dc.identifier.issue | 2-3 | en_US |
| dc.identifier.scopus | 2-s2.0-61649121506 | |
| dc.identifier.scopusquality | Q1 | |
| dc.identifier.startpage | 420 | en_US |
| dc.identifier.uri | https://doi.org/ 10.1016/j.cej.2008.09.021 | |
| dc.identifier.uri | https://hdl.handle.net/20.500.12462/8997 | |
| dc.identifier.volume | 148 | en_US |
| dc.identifier.wos | WOS:000264918900029 | |
| dc.identifier.wosquality | Q1 | |
| dc.indekslendigikaynak | Web of Science | |
| dc.indekslendigikaynak | Scopus | |
| dc.language.iso | en | en_US |
| dc.publisher | Elsevier Science Sa | en_US |
| dc.relation.ispartof | Chemical Engineering Journal | en_US |
| dc.relation.publicationcategory | Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı | en_US |
| dc.rights | info:eu-repo/semantics/openAccess | en_US |
| dc.subject | Boric Acid | en_US |
| dc.subject | Waste Minimization | en_US |
| dc.subject | Calcium Removal | en_US |
| dc.subject | Ion Exchange | en_US |
| dc.subject | Empirical Model | en_US |
| dc.title | An empirical kinetic model for calcium removal from calcium impurity-containing saturated boric acid solution by ion exchange technology using Amberlite IR-120 resin | en_US |
| dc.type | Article | en_US |












