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master's thesis
Utjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova
diplomski rad
2018. urn:nbn:hr:167:101811
Miljak, Zrinka
University of Split
Faculty of Chemistry and Technology
Division of Engineering and Chemistry

Cite this document

Miljak, Z. (2018). Utjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova : diplomski rad (Master's thesis). Split: University of Split, Faculty of Chemistry and Technology. Retrieved from https://urn.nsk.hr/urn:nbn:hr:167:101811

Miljak, Zrinka. "Utjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova : diplomski rad." Master's thesis, University of Split, Faculty of Chemistry and Technology, 2018. https://urn.nsk.hr/urn:nbn:hr:167:101811

Miljak, Zrinka. "Utjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova : diplomski rad." Master's thesis, University of Split, Faculty of Chemistry and Technology, 2018. https://urn.nsk.hr/urn:nbn:hr:167:101811

Miljak, Z. (2018). 'Utjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova : diplomski rad', Master's thesis, University of Split, Faculty of Chemistry and Technology, accessed 16 November 2024, https://urn.nsk.hr/urn:nbn:hr:167:101811

Miljak Z. Utjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova : diplomski rad [Master's thesis]. Split: University of Split, Faculty of Chemistry and Technology; 2018 [cited 2024 November 16] Available at: https://urn.nsk.hr/urn:nbn:hr:167:101811

Z. Miljak, "Utjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova : diplomski rad", Master's thesis, University of Split, Faculty of Chemistry and Technology, Split, 2018. Available at: https://urn.nsk.hr/urn:nbn:hr:167:101811

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Metadata
TitleUtjecaj tipa miješala na ionsku izmjenu u šaržnom reaktoru sa i bez razbijala virova : diplomski rad
Title (english)Effect of impeller type on ion exchange in baffled and unbaffled batch reactor : diploma thesis
AuthorZrinka Miljak
MentorSandra Svilović (mentor)
MBZ: 237630
Committee memberLadislav Vrsalović (predsjednik povjerenstva)
Committee memberIvana Generalić Mekinić (član povjerenstva)
Committee memberSandra Svilović (član povjerenstva)
GranterUniversity of Split
Faculty of Chemistry and Technology
(Division of Engineering and Chemistry)
Split
Defense date and country2018-10-26, Croatia
Scientific / art field,
discipline and subdiscipline		TECHNICAL SCIENCES
Chemical Engineering
Abstract
Mehanička operacija miješanja djeluje vrlo jednostavno, ali utjecaj mnogobrojnih hidrodinamičkih uvjeta na procese koji se odvijaju unutar reaktorskog prostora potrebno je detaljno istražiti. U ovom diplomskom radu ispitan je utjecaj tipa miješala na ionsku izmjenu bakra na zeolitu NaX. Ispitivanja su provedena u reaktoru s razbijalima virova kao i u reaktoru bez razbijala virova kako bi se dobio uvid na sveukupni utjecaj stvorenih hidrodinamičkih uvjeta na već spomenuti proces ionske izmjene. Eksperimenti su izvedeni pojedinačnom primjenom triju miješala: turbinskog miješala s ravnim lopaticama (SBT), turbinskog miješala s lopaticama nagnutim pod kutom od 45° (PBT) i turbinskog miješala s diskom i ravnim lopaticama (Rushtonova turbina, RT). Ispitivanja su provedena sa česticama zeolita promjera d p <0,050mm, a početna koncentracija otopine bakrova(II) nitrata bila je 7,04 mmol L -1 . U cilju dobivanja boljeg uvida u utjecaj ispitivanih parametara određena je minimalna brzina vrtnje miješala potrebna za postizanje stanja potpune suspenzije (N JS ) primjenom Zwieteringovog vizualnog kriterija „1s“, kao i utrošak snage miješala (P JS ). Dobiveni rezultati pokazali su da se prilikom rada u reaktoru s pregradama troši više energije na cjelokupan proces. Iz rezultata ispitivanja utjecaja hidrodinamičkih uvjeta stvorenih SBT, PBT i RT miješalom u reaktoru sa ili bez razbijala virova, može se zaključiti da je proces ionske izmjene općenito brži u reaktoru s razbijalima virova. U isto vrijeme vrijednosti N JS i utroška snage miješala (P JS ) također su veće u reaktoru s razbijalima virova. Provedena je i kinetička analiza procesa kojom se pokazalo da količina izmijenjenog bakra u početnoj fazi eksperimenta naglo raste nakon čega dolazi do uspostave ravnoteže. Dobiveni rezultati obrađeni su metodom nelinearne i linearne regresije korištenjem Ritchievog i Weber-Morrisovog modela i statističkim pokazateljem ocjenjeno je njihovo slaganje s eksperimentalnim podacima. Pokazalo se da brzina kemijske reakcije ovisi o tipu miješala i da je općenito veća u reaktoru s razbijalima virova u odnosu na reaktor bez razbijala virova. Brzina reakcije je najveća kada se koristi RT miješalo u reaktoru s pregradama, a najsporija kod RT miješala u reaktoru bez pregrada.
Abstract (english)
Mixing, as mechanical operation, appears like very simple unit operation, but effects of many hydrodynamic conditions on processes inside of reactor need to be examined in detail. In this work the influence of impeller type on ion exchange of copper on zeolite NaX has been investigated. In order to get a better insight into the effect of hydrodynamic conditions on ion exchange, experiments were conducted in the baffled and unbaffled batch reactor at standard impeller off-bottom clearance (C/H=0,33). Three impeller types were used- straight blade turbine (SBT) which produced radial flow, pitch blade turbine (PBT) that produced dominantly axial flow and Rushton turbine (RT) which also produced radial flow. To avoid the effect of intraparticle diffusion, in all experiments the same zeolite particle size (d p <0,050mm) was used, as well as the same initial concentration of copper solution (c 0 =7,04 mmol/L). In order to get a better insight into the effects of the investigated parameters the minimum impeller speed for complete suspension (N JS ), using visual Zwietering criterion “1s”, and power consumption (P JS ) were found. Results have shown that power consumption (P JS ) is generally higher in baffled batch reactor. From the results of the study of influence of the hydrodynamic conditions generated by SBT, PBT and RT impeller in the reactor with or without baffles, it can be concluded that the difference in maximum amount of exchange is not significant and that the reaction, in generally, is faster in the baffled reactor. But, at the same time, N JS and P JS in a baffled reactor were higher as well. Also, kinetic analysis of the process was conducted, and results have shown that the amount of copper exchanged, at examined conditions, in the initial phase of the experiment was increasing rapidly until equilibrium has been established. The obtained results were processed by the nonlinear and linear analysis using Ritchie and Weber-Morris model. Results have shown that chemical reaction rate depends on the impeller type and that generally is higher in baffled reactor. The reaction rate was the highest using RT impeller in baffled batch reactor, and the lowest using RT impeller in unbaffled batch reactor.
Keywords
Keywords (english)
Languagecroatian
URN:NBNurn:nbn:hr:167:101811
ProjectNumber: 8959
Title: Utjecaj procesnih parametara na kinetiku heterogenih sustava koji se odvijaju u šaržnom reaktoru s miješanjem
Acronym: HETMIX
Leader: Nenad Kuzmanić
Jurisdiction: Croatia
Funder: HRZZ
Study programmeTitle: Chemical Technology; specializations in: Materials, Environmental Protection, Mediteranean Cultures
Course: Materials
Study programme type: university
Study level: graduate
Academic / professional title: magistar/magistra inženjer/inženjerka kemijskog inženjerstva (magistar/magistra inženjer/inženjerka kemijskog inženjerstva)
Type of resourceText
File originBorn digital
Access conditionsOpen access
Embargo expiration date: 2020-10-26
Terms of useLicence In copyright icon
Public noteKljučne riječi doradio knjižničar/ Key words are revised by the librarian.
Created on2018-11-26 12:44:32