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master's thesis
Utjecaj promjena SBT miješala na kinetiku sorpcije bakra
diplomski rad
2023. urn:nbn:hr:167:744876
Roković, Ivana
University of Split
Faculty of Chemistry and Technology
Division of Engineering and Chemistry

Cite this document

Roković, I. (2023). Utjecaj promjena SBT miješala na kinetiku sorpcije bakra : diplomski rad (Master's thesis). Split: University of Split, Faculty of Chemistry and Technology. Retrieved from https://urn.nsk.hr/urn:nbn:hr:167:744876

Roković, Ivana. "Utjecaj promjena SBT miješala na kinetiku sorpcije bakra : diplomski rad." Master's thesis, University of Split, Faculty of Chemistry and Technology, 2023. https://urn.nsk.hr/urn:nbn:hr:167:744876

Roković, Ivana. "Utjecaj promjena SBT miješala na kinetiku sorpcije bakra : diplomski rad." Master's thesis, University of Split, Faculty of Chemistry and Technology, 2023. https://urn.nsk.hr/urn:nbn:hr:167:744876

Roković, I. (2023). 'Utjecaj promjena SBT miješala na kinetiku sorpcije bakra : diplomski rad', Master's thesis, University of Split, Faculty of Chemistry and Technology, accessed 20 November 2024, https://urn.nsk.hr/urn:nbn:hr:167:744876

Roković I. Utjecaj promjena SBT miješala na kinetiku sorpcije bakra : diplomski rad [Master's thesis]. Split: University of Split, Faculty of Chemistry and Technology; 2023 [cited 2024 November 20] Available at: https://urn.nsk.hr/urn:nbn:hr:167:744876

I. Roković, "Utjecaj promjena SBT miješala na kinetiku sorpcije bakra : diplomski rad", Master's thesis, University of Split, Faculty of Chemistry and Technology, Split, 2023. Available at: https://urn.nsk.hr/urn:nbn:hr:167:744876

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Metadata
TitleUtjecaj promjena SBT miješala na kinetiku sorpcije bakra : diplomski rad
Title (english)Impact of SBT impeller diameter on kinetics of copper sorption : diploma thesis
AuthorIvana Roković
MentorSandra Svilović (mentor)
Committee memberNediljka Vukojević-Medvidović (predsjednik povjerenstva)
Committee memberMario Nikola Mužek (član povjerenstva)
Committee memberSandra Svilović (član povjerenstva)
GranterUniversity of Split
Faculty of Chemistry and Technology
(Division of Engineering and Chemistry)
Split
Defense date and country2023-09-29, Croatia
Scientific / art field,
discipline and subdiscipline		TECHNICAL SCIENCES
Chemical Engineering
Abstract
U ovom diplomskom radu ispitan je utjecaj promjera radijalnog turbinskog miješala s četiri ravne lopatice (SBT miješalo) na proces sorpcije bakra na sintetskom zeolitu u kotlastom reaktoru, s i bez razbijala. Otopina bakra pripravljena otapanjem odgovarajuće mase Cu(NO 3 ) 2 u destiliranoj vodi. U eksperimentima je korišten sintetski zeolit NaX srednjeg promjera čestica 0,0765 mm. Ispitivanja su provedena pri stalnoj temperaturi (25 °C) suspenzije. Utjecaj promjera SBT miješala s četiri lopatice na kinetiku sorpcije ispitan je eksperimentima u kojima su korištena miješala različitih promjera (D/d T = 0,32; 0,46; 0,57; 0,68). Analiza dobivenih kinetičkih eksperimentalnih podataka primjenom Weber-Morrisovog i Blanchardovog modela pokazala je da difuzija ne utječe na ukupnu brzinu procesa, odnosno da ispitivana reakcija prati kinetiku drugoga reda u reaktoru s i bez razbijala virova. Rezultati ispitivanja pokazali su i da se povećanjem D/d T omjera i u reaktoru s i bez razbijala virova smanjuje utrošak snage miješanja.
Abstract (english)
In this diploma thesis, the influence of the diameter of the straight blade turbine (SBT impeller) with four blades on the copper sorption process of synthetic zeolite in a batch reactor with and without baffles was investigated. A copper solution was prepared by dissolving an appropriate amount of Cu(NO 3 ) 2 in distilled water. Synthetic zeolite NaX with an average particle diameter of 0.0765 mm was used in all experiments. The experiments were carried out at a constant temperature (25 °C) of the suspension. The influence of the diameter of SBT impeller with four blades on the kinetics of sorption was investigated by using impellers with different diameters (D/d T = 0.32; 0.46; 0.57; 0.68). The analysis of the obtained experimental kinetic data using the Weber-Morris and Blanchard models showed that diffusion does not affect the overall rate of the process, i.e. that the studied reaction in the reactor with and without baffles follows second order kinetics. The experiments results also showed that by increasing the D/d T ratio in both the reactor with and without baffles, the consumption of mixing power is reduced.
Keywords
Keywords (english)
Languagecroatian
URN:NBNurn:nbn:hr:167:744876
Study programmeTitle: Chemical Technology; specializations in: Materials, Environmental Protection, Mediteranean Cultures, Materials and Environmental protection
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 conditionsClosed access
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Created on2023-12-01 07:24:41