40 research outputs found
Genotoxic Potential of Dentin Bonding Agents
Svrha rada bila je ispitati genotoksiÄno djelovanje pet dentinskih adheziva: Adper Single Bonda, Adper Single Bonda 2, Prompt L-popa, Excitea i OptiBonda Solo Plus. Ispitivanje genotoksiÄnosti provedeno je na humanim limfocitima periferne krvi u uvjetima in vitro, ispitane koncentracije adheziva bile su 0,2, 0,5 i 5 Ī¼g/ml, a testirana vremena eluacije 1 sat, 24 sata i 5 dana. GenotoksiÄnost adheziva ispitivala se citogenetiÄkom metodom - analizom strukturnih aberacija kromosoma, dakle, odreÄivanjem ukupnog broja kromosomskih lomova, kromatidnih lomova i acentriÄnih fragmenata. Rezultati pokazuju genotoksiÄnost OptiBonda Solo Plus veÄ u koncentraciji 0,2 Ī¼g/ml i to nakon 24-satne eluacije, zatim OptiBonda Solo Plus u koncentraciji 0,5 Ī¼g/ml nakon jednosatne eluacije, OptiBonda Solo Plus, Adper Single Bonda 2 i Excitea u koncentraciji 0,5 Ī¼g/ml nakon jednodnevne eluacije. U koncentraciji 5 Ī¼g/ml nakon jednosatne eluacije genotoksiÄnost su pokazali OptiBond Solo Plus, Excite, Adper Single Bond 2 i Adper Single Bond, a nakon jednodnevne eluacije svi su ispitivani adhezivi pokazali genotoksiÄnost. Iz rezultata je jasno da enotoksiÄnost raste s porastom koncentracije adheziva, a smanjuje se s vremenom. NajveÄa genotoksiÄnost zabilježena je nakon 24-satne eluacije.The aim of this study was to examine the genotoxic activity of five dentin bonding agents: Adper Single Bond, Adper Single Bond 2, Prompt L-pop, Excite and Opti-Bond Solo Plus. This in vitro study was performed on human lymphocytes from peripheral blood, and the concentrations of dentin bonding agents tested were 0.2, 0.5 i 5 Ī¼g/ml, and elution times tested were 1 hour, 24 hours and 5 days. Genotoxicity testing was done using the Structural chromosomal aberration analysis cytogenic method , which determined the complete number of chromosome breaks, chromatide breaks and acentric fragments. The results showed genotoxicity of Opti-Bond Solo Plus in the 0.2 Ī¼g/ml concentration after a 24-hour elution period, then OptiBond Solo Plus in the 0.5 Ī¼g/ml concentration after a 1 hour elution period and OptiBond Solo Plus, Adper Single Bond 2 and Excite in the 0.5 Ī¼g/ml concentration after a 1 day elution period. In the 5 Ī¼g/ml concentration after 1 hour of elution, genotoxic potential was observed in cultures with OptiBond Solo Plus, Excite, Adper Single Bond 2 and Adper Single Bond, while all dentin bonding agents showed genotoxicity at that highest concentration but after 1 day of elution. From the results it is obvious that genotoxicity increases with the concentration of the dentin bonding agent, and decreases over time. The highest genotoxicity was observed after a 24-hour-elution period
Multi-fluid model predictions of gas-liquid two-phase flows in vertical tubes
Razvijen je potpun, stabilan, jednodimenzioni viÅ”efluidni model za predviÄanje dvofaznog strujanja u vertikalnim cevima. Model je zasnovan na bilansima održanja mase, koliÄine kretanja i energije, koji su primenjeni na svaku fluidnu struju koja je prisutna u posmatranom obliku dvofaznog strujanja, kao i na odgovarajuÄim konstitutivnim korelacijama za odreÄivanje transportnih procesa na razdelnim povrÅ”inama izmeÄu faza. Bilansne jednaÄine za stacionarno stanje su transformisane u oblik pogodan za direktnu primenu numeriÄke metode za integraciju sistema obiÄnih diferencijalnih jednaÄina. Simulirani su termohidrauliÄki procesi duž celog isparivaÄkog kanala, poÄevÅ”i od strujanja i zagrevanja pothlaÄene teÄnosti na ulazu u strujni kanal pa do zasuÅ”enja teÄnog filma i pojave maglenog toka sa kapima ukljuÄenim u gasnu fazu na kraju kanala. TakoÄe, model je testiran i za uslove nekoliko parcijalnih efekata dvofaznog strujanja.A consistent one-dimensional multi-fluid model is developed for the prediction of two-phase flows in vertical pipes. The model is based on the mass, momentum and energy balance equations for every fluid stream involved in the observed two-phase flow pattern, and corresponding closure laws for interface transfer processes. The steady-state balance equations are transformed in a form suitable for a direct application of the numerical integration method for the system of ordinary differential equations. Thermal-hydraulic processes along the whole length of the boiling channel are simulated, from the flow and heating of sub cooled liquid at the flow channel inlet, and up to the liquid film dry out and gas entrained droplets mist flow at the outlet. Also, the model is tested against several partial effects of two-phase flow
Numerical simulation of condensation induced water hammer
Razvijen je numeriÄki model za simulaciju i analizu hidrauliÄkog udara koji je zasnovan na jednodimenzionalnom homogenom modelu dvofaznog strujanja praÄenju razdelne povrÅ”ine stuba teÄnosti i parnog mehura i modeliranju direktne kondenzacije pare na pothlaÄenoj teÄnosti. Sistem bilansnih jednaÄina je reÅ”en primenom metode karakteristika. Integracija je vrÅ”ena duž tri karakteristiÄna pravca: dva pravca odreÄena su pravcem prostiranja talasa pritiska a treÄi prostiranjem fluidnog deliÄa. PraÄenje fluidnog deliÄa i razdelne povrÅ”ine vode i pare izvrÅ”eno je reÅ”avanjem energetske jednaÄine u prostoru sa taÄnoÅ”Äu treÄeg reda. KoliÄina toplote koju para preda teÄnosti pri kondenzaciji odreÄena je integracijom povrÅ”inskog toplotnog fluksa po razdelnoj povrÅ”ini parne i teÄne faze na mestu kontakta pare i pothlaÄene teÄnosti. Model je primenjen na simulaciju i analizu hidrauliÄkog udara izazvanog u nekoliko eksperimentalih aparatura.A numerical model for the simulation and analysis of the water hammer in the pipe two-phase flow is developed. The modeling is based on one-dimensional homogeneous model of two-phase flow, tracking of the interface between steam volume and water column and modeling of the direct condensation of steam on sub cooled liquid. The mass, momentum and energy conservation equations are solved by the method of characteristics. For these three equations, there are three characteristic directions: two of them are determined by the pressure wave propagation and the third one by the fluid particle propagation. The fluid particle and the steam-water interface tracking are obtained through the energy conservation equation solving in space, with the accuracy of the third degree. The value of thermodynamic quality is used to determine whether the observed computational region is filled with water, two-phase mixture or steam. The term in the energy conservation equation, which contains information about the heat exchanged between steam and liquid phase through condensation, is determined by integration of superficial heat flux over steam-water interface. The model is applied to the simulation and analysis of the air-water interface propagation in the experimental apparatus of oscillating manometer and the condensation induced water hammer in a vertical pipe for draining of steam into the pool filled with sub cooled water
Numerical simulation of condensation induced water hammer
Razvijen je numeriÄki model za simulaciju i analizu hidrauliÄkog udara koji je zasnovan na jednodimenzionalnom homogenom modelu dvofaznog strujanja praÄenju razdelne povrÅ”ine stuba teÄnosti i parnog mehura i modeliranju direktne kondenzacije pare na pothlaÄenoj teÄnosti. Sistem bilansnih jednaÄina je reÅ”en primenom metode karakteristika. Integracija je vrÅ”ena duž tri karakteristiÄna pravca: dva pravca odreÄena su pravcem prostiranja talasa pritiska a treÄi prostiranjem fluidnog deliÄa. PraÄenje fluidnog deliÄa i razdelne povrÅ”ine vode i pare izvrÅ”eno je reÅ”avanjem energetske jednaÄine u prostoru sa taÄnoÅ”Äu treÄeg reda. KoliÄina toplote koju para preda teÄnosti pri kondenzaciji odreÄena je integracijom povrÅ”inskog toplotnog fluksa po razdelnoj povrÅ”ini parne i teÄne faze na mestu kontakta pare i pothlaÄene teÄnosti. Model je primenjen na simulaciju i analizu hidrauliÄkog udara izazvanog u nekoliko eksperimentalih aparatura.A numerical model for the simulation and analysis of the water hammer in the pipe two-phase flow is developed. The modeling is based on one-dimensional homogeneous model of two-phase flow, tracking of the interface between steam volume and water column and modeling of the direct condensation of steam on sub cooled liquid. The mass, momentum and energy conservation equations are solved by the method of characteristics. For these three equations, there are three characteristic directions: two of them are determined by the pressure wave propagation and the third one by the fluid particle propagation. The fluid particle and the steam-water interface tracking are obtained through the energy conservation equation solving in space, with the accuracy of the third degree. The value of thermodynamic quality is used to determine whether the observed computational region is filled with water, two-phase mixture or steam. The term in the energy conservation equation, which contains information about the heat exchanged between steam and liquid phase through condensation, is determined by integration of superficial heat flux over steam-water interface. The model is applied to the simulation and analysis of the air-water interface propagation in the experimental apparatus of oscillating manometer and the condensation induced water hammer in a vertical pipe for draining of steam into the pool filled with sub cooled water
Multi-fluid model predictions of gas-liquid two-phase flows in vertical tubes
Razvijen je potpun, stabilan, jednodimenzioni viÅ”efluidni model za predviÄanje dvofaznog strujanja u vertikalnim cevima. Model je zasnovan na bilansima održanja mase, koliÄine kretanja i energije, koji su primenjeni na svaku fluidnu struju koja je prisutna u posmatranom obliku dvofaznog strujanja, kao i na odgovarajuÄim konstitutivnim korelacijama za odreÄivanje transportnih procesa na razdelnim povrÅ”inama izmeÄu faza. Bilansne jednaÄine za stacionarno stanje su transformisane u oblik pogodan za direktnu primenu numeriÄke metode za integraciju sistema obiÄnih diferencijalnih jednaÄina. Simulirani su termohidrauliÄki procesi duž celog isparivaÄkog kanala, poÄevÅ”i od strujanja i zagrevanja pothlaÄene teÄnosti na ulazu u strujni kanal pa do zasuÅ”enja teÄnog filma i pojave maglenog toka sa kapima ukljuÄenim u gasnu fazu na kraju kanala. TakoÄe, model je testiran i za uslove nekoliko parcijalnih efekata dvofaznog strujanja.A consistent one-dimensional multi-fluid model is developed for the prediction of two-phase flows in vertical pipes. The model is based on the mass, momentum and energy balance equations for every fluid stream involved in the observed two-phase flow pattern, and corresponding closure laws for interface transfer processes. The steady-state balance equations are transformed in a form suitable for a direct application of the numerical integration method for the system of ordinary differential equations. Thermal-hydraulic processes along the whole length of the boiling channel are simulated, from the flow and heating of sub cooled liquid at the flow channel inlet, and up to the liquid film dry out and gas entrained droplets mist flow at the outlet. Also, the model is tested against several partial effects of two-phase flow
Adsorption kinetics and mechanism analysis of cyan printing dye on polyethylene microplastics
Printing on polymer materials might result with generation of coloured wastewater, enriched with a certain amount of microplastics in a form of polyethylene or polypropylene. In that way, microplastics may acquire the function of carriers of synthetic dyes, heavy metals and other polluting substances. In this paper, kinetics and adsorption mechanism of printing Cyan dye on polyethylene (powdered and granulated), as one of the most common types of microplastics, were investigated. The experiments were performed in a batch mode, in laboratory conditions. Based on the obtained results, a similar adsorption rate degree of selected printing dye was determined on granulated (adsorbed amount was 48.04 Āµg/g) and powdered material (adsorbed amount was 44.32 Āµg/g). The adsorption data were fitted well by pseudo-second-order kinetics, while isotherm studies were evaluated using two models: Langmuir and Freundlich. Freundlich and Langmuir equations showed similar performances to fit the solid/liquid distribution of Cyan dye on powdered polyethylene (R2 = 0.987), whereas Langmuir equation showed slightly better performances for granulated polyethylene than Freundlich equation
Zastupljenost oganohlornih pesticida u filetima osliÄa
Organohlorni pesticidi (OCP) su grupa jedinjenja Å”iroko zastupljena u prirodi a samim tim i u hrani koju konzumiramo. Da bismo za proizvod rekli da je bezbedan za upotrebu neophodno je da sadržaj OCP-a u njemu bude manji od maksimalno dozvoljenih vrednosti koje su propisane važeÄim Pravilnikom. Identifikacija ove grupe jedinjenja se vrÅ”i gasnom hromatografijom sa masenim detektorom. Priprema uzoraka za analizu sa brzom QuECHERS metodom obezbeÄuje da za kratko vreme, pouzdano ekstrahujemo analite od interesa. U naÅ”oj studiji ispitivali smo sadžaj 19 organohlornih pesticida u filetima osliÄa, ribljem proizvodu popularnom u naÅ”oj zemlji. Ispitivanja su pokazala da se koncentracija OCP-ova u ovim proizvodima nalazi znatno ispod maksimalno dozvoljenih koncentracija. Organohlorni pesticidi se akumuliraju u hrani i okruženju Å”to izaziva zabrinutost zbog potencijalnih rizika po ljudsko zdravlje kao i zbog naruÅ”avanja ekoloÅ”ke ravnoteže (Kartalovic et al, 2015). U predhodnim decenijama organohlorni pesticidi su se koristili Å”irom sveta kako bi unapredili poljoprivrednu proizvodnju. Globalna upotreba ove grupe jedinjenja je od 1950. godine dovela je do poveÄanja njihove potroÅ”nje i do pedeset puta, paralelno sa rastom stanovniÅ”tva (Nath, 2013). U naÅ”oj studiji ispitivali smo sluÄajno izabrane uzorke iz marketa. Uzorci su do ispitivanja Äuvani u orginalnom pakovanju u skladu sa preporukom proizvoÄaÄa. Na osnovu ispitivanja 18 uzoraka zakljuÄeno je da je sadržaj organohlornih pesticida znatno niži od maksimalno dozvoljenih koncentracija u ribi, koje su propisane važeÄim Pravilnikom Republike Srbije. Opseg koncentracija OCP-a se kretao od 0.0065-0.0097 mg/kg.
Generalno, svi pesticidi su toksiÄne supstance dizajnirane da ubiju Å”tetoÄine sa svojim otrovnim ili Å”tetnim efektima. Direktno ili indirektno pesticidi mogu uÄi u ljudsko telo kroz lanac ishrane i konaÄno, mogu prouzrokovati razliÄite efekte na ljudsko zdravlje, poput alergijskih reakcija ukljuÄujuÄi i sterilitet i kancer. ZagaÄivanje hrane sa ovim supstancama se smatra jednim od najopasnijih aspekata u poslednjih nekoliko godina. Riba i riblji proizvodi mogu biti kontaminirani sa hloriovanim ostacima kroz razliÄite izvore. Ovi kvaliteti ih Äine najopasnijom grupom hemikalija kojima prirodni sistemi mogu biti izloženi i funkcioniÅ”u kao hemijski indikatori antropogenog pritiska i zagaÄenja (Baiarri i dr., 2001; Storelli et al.,2004). Zbog Äinjenice da su OCP ipak prisutni u ovim proizodima neophodno je iste izloziti stalnom monitoringu s ciljem obezbeÄivanja plasmana samo bezbednih proizvoda na naÅ”e trziÅ”te
Numerical simulation of dynamic loads at the steam pipe line of the thermal power plant 'Nikola Tesla Bā
OdreÄivanje dinamiÄkih sila kojima nestacionarna struja fluida deluje na cevovod je neophodno u cilju sagledavanja maksimalnih naprezanja koja deluju na strukturu, spojeve i oslonce, odnosno u cilju dobijanja podloga za projektovanje ovih elemenata na maksimalna dinamiÄka naprezanja. U radu su prikazani metodologija i rezultati raÄunarske simulacije nestacionarnih gasodinamiÄkih sila koje deluju na parovod tople meÄupregrejane pare termoelektrane āNikola Tesla Bā. Nestacionarne gasodinamiÄke sile nastaju usled nestacionarnog strujanja radnog fluida pri delovanju sigurnosno-zaÅ”titnih sistema. Zatvaranje pregradnih ventila ispred tur bine srednjeg pritiska zaustavlja protok pare i dovodi do porasta pritiska ispred pregradnih ventila, i prostiranja i superponiranja talasa pritiska duž parovoda, Å”to izaziva dopunska dinamiÄka optereÄenja parovoda. OdreÄivanje dinamiÄkih fluidnih sila se vrÅ”i zajedno sa simulacijom nestacionarnog strujanja pare. Simulacija strujanja i odreÄivanje fluidnih dinamiÄkih sila su sprovedeni pomoÄu raÄunarskog programa TEA razvijenog na MaÅ”inskom fakultetu u Beogradu. Dobijeni rezultati su koriÅ”Äeni u okviru revizije inostranog projekta rekonstrukcije (zamene) parovoda meÄupregrejane pare na termoelektrani āNikola Tesla Bā. Rezultati proraÄuna dobijeni programom TEA su uporeÄeni sa rezultatima inostranog raÄunarskog programa SHOCK i dobijeno je prihvatljivo slaganje.Prediction of the transient fluid dynamic forces that act on the pipe line structure, junctions and supports are important in order to predict the maximum design loads. The paper presents the methodology and results of the fluid dynamic forces prediction for the reheated steam pipe line at the Thermal Power Plant āNikola Tesla Bā. The dynamic forces are induced by fluid transient flow caused by the action of the plant safety system. Closure of the isolation valves in front of the intermediate pressure turbine stops the steam flow and leads to the in crease of pres sure in front of the isolation valves, pressure waves propagation and super position along the pipe line, which cause additional dynamic loading of the pipe line structure. Prediction of the fluid dynamic forces is performed simultaneously with the simulation of the transient fluid flow. Transient simulation of fluid flow and calculation of fluid-dynamic forces are performed with the computer code TEA (Transient Evaluation Analyses), which is developed at the Faculty of Mechanical Engineering in Belgrade. Obtained results are used for the review of a foreign project on the reconstruction (replacement) of steam pipeline in Thermal Power Plant āNikola Tesla Bā. Results obtained with the computer code TEA are compared with results of foreign computer code SHOCK. Acceptably agreement is achieved
Numerical simulation of dynamic loads at the steam pipe line of the thermal power plant 'Nikola Tesla Bā
OdreÄivanje dinamiÄkih sila kojima nestacionarna struja fluida deluje na cevovod je neophodno u cilju sagledavanja maksimalnih naprezanja koja deluju na strukturu, spojeve i oslonce, odnosno u cilju dobijanja podloga za projektovanje ovih elemenata na maksimalna dinamiÄka naprezanja. U radu su prikazani metodologija i rezultati raÄunarske simulacije nestacionarnih gasodinamiÄkih sila koje deluju na parovod tople meÄupregrejane pare termoelektrane āNikola Tesla Bā. Nestacionarne gasodinamiÄke sile nastaju usled nestacionarnog strujanja radnog fluida pri delovanju sigurnosno-zaÅ”titnih sistema. Zatvaranje pregradnih ventila ispred tur bine srednjeg pritiska zaustavlja protok pare i dovodi do porasta pritiska ispred pregradnih ventila, i prostiranja i superponiranja talasa pritiska duž parovoda, Å”to izaziva dopunska dinamiÄka optereÄenja parovoda. OdreÄivanje dinamiÄkih fluidnih sila se vrÅ”i zajedno sa simulacijom nestacionarnog strujanja pare. Simulacija strujanja i odreÄivanje fluidnih dinamiÄkih sila su sprovedeni pomoÄu raÄunarskog programa TEA razvijenog na MaÅ”inskom fakultetu u Beogradu. Dobijeni rezultati su koriÅ”Äeni u okviru revizije inostranog projekta rekonstrukcije (zamene) parovoda meÄupregrejane pare na termoelektrani āNikola Tesla Bā. Rezultati proraÄuna dobijeni programom TEA su uporeÄeni sa rezultatima inostranog raÄunarskog programa SHOCK i dobijeno je prihvatljivo slaganje.Prediction of the transient fluid dynamic forces that act on the pipe line structure, junctions and supports are important in order to predict the maximum design loads. The paper presents the methodology and results of the fluid dynamic forces prediction for the reheated steam pipe line at the Thermal Power Plant āNikola Tesla Bā. The dynamic forces are induced by fluid transient flow caused by the action of the plant safety system. Closure of the isolation valves in front of the intermediate pressure turbine stops the steam flow and leads to the in crease of pres sure in front of the isolation valves, pressure waves propagation and super position along the pipe line, which cause additional dynamic loading of the pipe line structure. Prediction of the fluid dynamic forces is performed simultaneously with the simulation of the transient fluid flow. Transient simulation of fluid flow and calculation of fluid-dynamic forces are performed with the computer code TEA (Transient Evaluation Analyses), which is developed at the Faculty of Mechanical Engineering in Belgrade. Obtained results are used for the review of a foreign project on the reconstruction (replacement) of steam pipeline in Thermal Power Plant āNikola Tesla Bā. Results obtained with the computer code TEA are compared with results of foreign computer code SHOCK. Acceptably agreement is achieved
Experimental design of photo-Fenton process decolorization of Reactive Red 120 by using mathematical statistics models
A statistical design of experiments was used to evaluate the potential use of clay catalyst (CuOFeB) during photo-Fenton process in which the concentration of hydrogen peroxide (H2O2), catalyst loading and pH values were selected as effective experimental factors in the process of dye decolorization. The photo-Fenton oxidation of Reactive Red 120 (RR120) has been investigated using a concentrating solar parabolic reactor with constant solar radiation of 950 W/m2 during summer period of the year. Under the optimal reaction conditions catalyst showed good catalytic activity in the processes with dye removal over 90%. Also, experiment confirmed that decolorization efficiency depends on the pH and concentration of H2O2 , wherein better results were achieved under lower pH values and higher concentration of H2O2