Effect Of Sodium Hypochlorite And Peracetic Acid On The Surface Roughness Of Acrylic Resin Polymerized By Heated Water For Short And Long Cycles.

To evaluate the surface roughness of acrylic resin submitted to chemical disinfection via 1% sodium hypochlorite (NaClO) or 1% peracetic acid (C2H4O3). The disc-shaped resin specimens (30 mm diameter ×4 mm height) were polymerized by heated water using two cycles (short cycle: 1 h at 74°C and 30 min at 100°C; conventional long cycle: 9 h at 74°C). The release of substances by these specimens in water solution was also quantified. Specimens were fabricated, divided into four groups (n = 10) depending on the polymerization time and disinfectant. After polishing, the specimens were stored in distilled deionized water. Specimens were immersed in 1% NaClO or 1% C2H4O3 for 30 min, and then were immersed in distilled deionized water for 20 min. The release of C2H4O3 and NaClO was measured via visual colorimetric analysis. Roughness was measured before and after disinfection. Roughness data were subjected to two-way ANOVA and Tukey's test. There was no interaction between polymerization time and disinfectant in influencing the average surface roughness (Ra, P = 0.957). Considering these factors independently, there were significant differences between short and conventional long cycles (P = 0.012), but no significant difference between the disinfectants hypochlorite and C2H4O3 (P = 0.366). Visual colorimetric analysis did not detect release of substances. It was concluded that there was the difference in surface roughness between short and conventional long cycles, and disinfection at acrylic resins polymerized by heated water using a short cycle modified the properties of roughness.

Antibacterial effectiveness of peracetic acid and conventional endodontic irrigants

Este estudo avaliou, in vitro, a atividade antibacteriana de soluções irrigadoras convencionais e experimentais sobre Enterecoccus faecalis. As seguintes substâncias foram avaliadas por teste de contato direto: hipoclorito de sódio (NaOCl) a 2,5%, clorexidina (CHX) a 2%, ácido peracético a 1%. Após diferentes períodos de contato (30 s, 1, 3 e 10 min), um agente neutralizante foi empregado. Diluições decimais seriadas foram realizadas e semeadas em placas de tryptic soy agar (TSA). O número de unidades formadoras de colônia por mililitro (UFC/mL) foi determinado. Solução salina foi utilizada como controle negativo. Ambos, NaOCl a 2,5% e CHX a 2%, eliminaram E. faecalis após 30 s de contato. O ácido peracético reduziu a contagem bacteriana em 86% após 3 min e eliminou completamente E. faecalis após 10 min. Estes resultados permitem concluir que o ácido peracético a 1% é efetivo sobre E. faecalis, apesar de sua ação mais lenta quando comparado ao NaOCl a 2,5% e CHX a 2%.

Effectiveness of 2% peracetic acid for the disinfection of gutta-percha cones

The aim of this study was to evaluate the effectiveness of 2% peracetic acid for the disinfection of gutta-percha cones contaminated in vitro with Escherichia coli, Staphylococcus aureus, Streptococcus mutans, Candida albicans and Bacillus subtilus (in spore form). Two hundred and twenty-five gutta-percha cones were contaminated with standardized suspensions of each microorganism and incubated at 37 degrees C for 24 h. The cones were divided into 10 experimental groups (n = 15), according to the microorganism tested and disinfection testing times. The disinfection procedure consisted of immersing each cone in a plastic tube containing the substance. The specimens remained in contact with the substance for 1 or 2.5 minutes. Afterwards, each cone was transferred to a 10% sodium thiosulphate solution (Na2S2O3) to neutralize the disinfectant. Microbial biofilms adhering to the cones were dispersed by agitation. Aliquots of 0.1 ml of the suspensions obtained were plated on Sabouraud dextrose agar, or brain and heart infusion agar, and incubated at 37 degrees C for 24 h. The results were expressed in colony forming units (CFU/ml) and the data were submitted to the Wilcoxon Signed Rank Test (level of significance at 0.05). A significant reduction was observed, after 1 minute of exposure, in the test solution for C. albicans (p = 0.0190), S. aureus (p = 0.0001), S. mutans (p = 0.0001), B. subtilis (p = 0.0001), and E. coli (p = 0.0001). After 2.5 minutes of exposure, 100% of the microbial inocula were eliminated. It was concluded that the 2% peracetic acid solution was effective against the biofilms of the tested microorganisms on gutta-percha cones at 1 minute of exposure.

Toxicity on aquatic organisms exposed to secondary effluent disinfected with chlorine, peracetic acid, ozone and UV radiation

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

Cytotoxicity of peracetic acid in L929 fibroblasts

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Penetration into dentin of sodium hypochlorite associated with acid solutions

Objective. The objective of this study was to evaluate the penetration of 2.5% NaOCl associated with 17.0% EDTA, 1.0% citric acid, and 1.0% peracetic acid into dentin tubules.Study design. The roots of 44 bovine incisors were cross-sectioned and 5-mm-long fragments were produced from their middle thirds. The specimens were instrumented with ProTaper hand files, stained in crystal violet, then sectioned mesiodistally. The buccal fragments were divided into 4 groups (n = 9) and subjected to 2 consecutive 10-minute immersion periods in one of the following acid solutions combined with 2.5% NaOCl: 17.0% EDTA (group 1), 1.0% citric acid (group 2), and 1.0% peracetic acid (group 3). Nine fragments were immersed in 2.5% NaOCl (group 4). The analysis of the penetration of NaOCl solutions into dentin was performed by measuring the depth of crystal violet stain that was bleached using a steromicroscope under x50 magnification. Statistical comparisons were carried out by Kruskal-Wallis and Dunn's tests at the 5% significance level.Results. Group 1 showed less penetration into dentin than group 4 (P < .05). No statistically significant differences were observed among groups 2, 3, and 4 (P > .05).Conclusions. Association of NaOCl with acid solutions did not increase its penetration depth into root dentin. (Oral Surg Oral Med Oral Pathol Oral Radiol Endod 2011;112:e155-e159)

Behavior Of Listeria Monocytogenes In A Multi-species Biofilm With Enterococcus Faecalis And Enterococcus Faecium And Control Through Sanitation Procedures.

The formation of mono-species biofilm (Listeria monocytogenes) and multi-species biofilms (Enterococcus faecium, Enterococcus faecalis, and L. monocytogenes) was evaluated. In addition, the effectiveness of sanitation procedures for the control of the multi-species biofilm also was evaluated. The biofilms were grown on stainless steel coupons at various incubation temperatures (7, 25 and 39°C) and contact times (0, 1, 2, 4, 6 and 8days). In all tests, at 7°C, the microbial counts were below 0.4 log CFU/cm(2) and not characteristic of biofilms. In mono-species biofilm, the counts of L. monocytogenes after 8days of contact were 4.1 and 2.8 log CFU/cm(2) at 25 and 39°C, respectively. In the multi-species biofilms, Enterococcus spp. were present at counts of 8 log CFU/cm(2) at 25 and 39°C after 8days of contact. However, the L. monocytogenes in multi-species biofilms was significantly affected by the presence of Enterococcus spp. and by temperature. At 25°C, the growth of L. monocytogenes biofilms was favored in multi-species cultures, with counts above 6 log CFU/cm(2) after 8days of contact. In contrast, at 39°C, a negative effect was observed for L. monocytogenes biofilm growth in mixed cultures, with a significant reduction in counts over time and values below 0.4 log CFU/cm(2) starting at day 4. Anionic tensioactive cleaning complemented with another procedure (acid cleaning, disinfection or acid cleaning+disinfection) eliminated the multi-species biofilms under all conditions tested (counts of all micro-organisms<0.4 log CFU/cm(2)). Peracetic acid was the most effective disinfectant, eliminating the multi-species biofilms under all tested conditions (counts of the all microorganisms <0.4 log CFU/cm(2)). In contrast, biguanide was the least effective disinfectant, failing to eliminate biofilms under all the test conditions.

Biofilms Of Enterococcus Faecalis And Enterococcus Faecium Isolated From The Processing Of Ricotta And The Control Of These Pathogens Through Cleaning And Sanitization Procedures.

The biofilm formation of Enterococcus faecalis and Enterococcus faecium isolated from the processing of ricotta on stainless steel coupons was evaluated, and the effect of cleaning and sanitization procedures in the control of these biofilms was determined. The formation of biofilms was observed while varying the incubation temperature (7, 25 and 39°C) and time (0, 1, 2, 4, 6 and 8days). At 7°C, the counts of E. faecalis and E. faecium were below 2log10CFU/cm(2). For the temperatures of 25 and 39°C, after 1day, the counts of E. faecalis and E. faecium were 5.75 and 6.07log10CFU/cm(2), respectively, which is characteristic of biofilm formation. The tested sanitation procedures a) acid-anionic tensioactive cleaning, b) anionic tensioactive cleaning+sanitizer and c) acid-anionic tensioactive cleaning+sanitizer were effective in removing the biofilms, reducing the counts to levels below 0.4log10CFU/cm(2). The sanitizer biguanide was the least effective, and peracetic acid was the most effective. These studies revealed the ability of enterococci to form biofilms and the importance of the cleaning step and the type of sanitizer used in sanitation processes for the effective removal of biofilms.

Antibacterial efficacy of endodontic irrigating solutions and their combinations in root canals contaminated with Enterococcus faecalis

Objective. The objective of this study was to evaluate the antibacterial efficacy of irrigating solutions and their combinations against Enterococcus faecalis. Study design. One hundred ten single-rooted human teeth were inoculated with E. faecalis and incubated for 21 days. Teeth were divided according to the irrigant: Group I (GI), 2.5% sodium hypochlorite solution (NaOCl); GII, 2.5% NaOCl + 10% citric acid; GIII, 2.5% NaOCl + apple cider vinegar; GIV, apple cider vinegar; GV, 2% chlorhexidine solution; GVI, 1% peracetic acid; GVII, saline solution. Microbiological samples were taken after root canal preparation and 7 days later. Data were submitted to ANOVA (5%). Results. All solutions promoted reduction of E. faecalis after instrumentation, but bacterial counts were higher in the final sample. GI, GV, and GVI had lower bacterial counts than the other groups. Conclusions. The irrigating solutions may present activity but do not eradicate E. faecalis in the root canal system. (Oral Surg Oral Med Oral Pathol Oral Radiol Endod 2011; 112:396-400)

Citotoxicidade do ácido peracético: avaliação metabólica, estrutural e de morte em fibroblastos L929

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Cost efficient extractive removal of birch pulp

Tämän diplomityön tarkoituksena oli selvittää kustannustehokkaita keinoja uuteaineiden vähentämiseksi koivusulfaattimassasta. Uuteaineet voivat aiheuttaa ongelmia muodostaessaan saostumia prosessilaitteisiin. Saostumat aiheuttavat tukkeumia ja mittaushäiriöitä, mutta irrotessaan ne myös huonontavat sellun laatua. Lopputuotteeseen joutuessaan ne voivat lisäksi aiheuttaa haju- ja makuhaittoja, joilla on erityistä merkitystä esimerkiksi valmistettaessa elintarvikekartonkeja. Tämä työ tehtiin Stora Enson sellutehtaalla, Enocell Oy:llä, Uimaharjussa. Teoriaosassa käsiteltiin uuteaineiden koostumusta ja niiden aiheuttamia ongelmia sellu– ja paperitehtaissa. Lisäksi koottiin aikaisempien tehdaskokeiden fysikaalisia ja kemiallisia keinoja vähentää koivu-uutetta. Tarkastelualueina olivat puunkäsittely, keitto, pesemö ja valkaisu. Kokeellisessa osassa suoritettiin esikokeita laboratorio- ja tehdasmittakaavassa, jotta saavutettaisiin käytännöllistä tietoa itse lopuksi tehtävää tehdasmittakaavan koetta varten. Laboratoriokokeissa tutkittiin mm. keiton kappaluvun, lisäaineiden ja hartsisaippuan vaikutusta koivu-uutteeseen. Lisäksi suoritettiin myös happo- (A) ja peretikkahappovaiheen (Paa) laboratoriokokeet. Tehdasmittakaavassa tarkasteltiin mm. keiton kappaluvun, pesemön lämpötilan, A-vaiheen, valkaisun peroksidi- ja Paa-vaiheen vaikutusta koivu-uutteeseen. Uutteenpoistotehokkuutta eri menetelmien välillä vertailtiin niin määrällisesti kuin rahallisesti. Uutteenpoistotehokkuudella mitattuna vertailuvaihe oli tehokkain pesemön loppuvaiheessa ja valkaisun alkuvaiheessa. Pesemön loppuvaiheessa uutteenpoistoreduktiot olivat noin 30 % ja valkaisun alkuvaiheessa 40 %. Peroksidivaihe oli tehokkain käytettynä valkaisun loppuvaiheessa noin 40 % reduktiolla. Kustannustehokkuudella mitattuna tehokkaimmaksi osoittautui A-vaihe yhdessä peroksidivaiheen kanssa. Säästöt vertailujaksoon verrattuna olivat noin 0.3 €/ADt. Lisäksi kyseinen yhdistelmä osoittautui hyväksi keinoksi säilyttää uutetaso alle maksimirajan kuitulinja 2:lla, kun kuitulinjalla 1 tuotettiin samanaikaisesti armeeraussellua.

Kalvosuodatusprosessin tehostaminen paperiteollisuuden sovelluksissa

Tässä diplomityössä tutkittiin kalvosuodatuksen esikäsittelymenetelmiä ja kalvonpesua. Työn kirjallisuusosassa käsitellään vuon alenemiseen vaikuttavia tekijöitä, esikäsittelymenetelmiä ja kalvonpesua. Kokeellisessa osassa tutkittiin kemiallisten esikäsittelyjen vaikutusta vuon alenemiseen paperitehtaan happaman kiertoveden kirkkaan suodoksen kalvosuodatuksessa. Esikäsittelykemikaalit olivat ympäristöystävällisiä ja paperinvalmistusprosessiin soveltuvia. Lisäksi tutkittiin kalvonpesuaineiden pesutehokkuuksia. Tutkitut esikäsittelyaineet olivat mikrokiteinen kitosaani, karboksimetyyliselluloosa, selluloosa- ja puukuitu sekä kaupallinen antiskalantti. Pesuaineista tutkittiin kolmea kaupallista kalvonpesuainetta, yhtä kalvopesun tehostusainetta sekä peretikkahappoa. Kokeet tehtiin kahdella laboratoriomittakaavaisella kalvosuodattimella. Kalvoina käytettiin kahta nanosuodatus- ja yhtä ultrasuodatuskalvoa. Vuon alenemista tutkittiin suodatuksen aikaisena alenemisena ja vesivuohon verrattavana alenemisena. Esikäsittelyjen vaikutusta erotustehokkuuteen tutkittiin ioni-, johtokyky-, orgaanisen hiilen kokonaispitoisuus-, sokeri-, sameus- ja ligniinireduktioilla. Lisäksi määritettiin kalvon likaantuminen suodatuksen aikana vesivuon määrityksillä ennen ja jälkeen suodatuksen. Pesutehokkuus määritettiin vesivuon määrityksillä suodatuksen jälkeen ja pesun jälkeen. Kitosaani- ja karboksimetyyliselluloosakäsittelyillä oli vuon alenemista estävä vaikutus hydrofiilisellä nanosuodatuskalvolla suodatettaessa. Kitosaanikäsittelyn 5 g/dm3:n ja karboksimetyyliselluloosakäsittelyn 2 g/ dm3:n annostuksella vuot alentuivat suodatuksen aikana 8 %-yksikköä vähemmän kuin ilman esikäsittelyä. Puukuitukäsittely stabiloi 0,1 g/dm3:n annostuksella saman kalvon vuota, kun kiintoainetta ei poistettu syötöstä. Hydrofobisen nanosuodatuskalvon vuon alenemista ehkäisivät puu- ja selluloosakuitukäsittelyt sekä karboksimetyyliselluloosakäsittely. Karboksimetyyliselluloosakäsittely vähensi vuon alenemista 25 %-yksikköä ja puukuitukäsittely 13 %-yksikköä. Hydrofiilisellä ultrasuodatuskalvolla vuon aleneminen oli pientä ilman esikäsittelyä. Reduktioihin esikäsittelyt vaikuttivat parhaiten ultrasuodatuskalvolla. Kitosaanikäsittely nosti 1 g/dm3:n annostuksella alumiinireduktion 50 %:sta 96 %:iin ja 5 g/dm3:n annostuksella rautareduktion 30 %:sta 55 %:iin. Karboksyylimetyyliselluloosakäsittelyt vaikuttivat parantavasti mangaanin, magnesiumin, raudan ja kalsiumin reduktioihin. Optimi karboksyylimetyyliselluloosa-annostus oli 2 g/dm3. Merkittävin reduktion nousu oli kalsiumilla, jonka reduktio nousi esikäsittelyllä 4 %:sta 57 %:iin. Reduktiota nostava mekanismi oli kalvon pinnalle muodostuva sekundaarikerros. Pesuaineista tehokkain oli entsyymiä sisältävä kalvonpesuaine. Suurin vaikutus sillä oli hydrofobisen nanosuodatuskalvon pesussa. Optimiannostuksella (0,5 %) kalvon vesivuo pesun jälkeen oli 114 % pesua edeltäneestä vesivuosta. Muut kaupalliset pesuaneet oli tehokkaita hydrofiilisille kalvoille. Peretikkahappo oli yksittäisenä pesuaineena heikkotehoinen.

A utilização de perácidos na deslignificação e no branqueamento de polpas celulósicas

Peracids are strong oxidant species and their use is being largely studied in the delignification and cellulose pulp bleaching. Some of them has already an industrial application, specially in non-conventional bleaching sequences like ECF (Elemental chlorine free) and TCF (Totally chlorine free). This review presents the main aspects of the structure, properties, preparation and reaction of peracids (peracetic acid, peroxymonosulfuric acid and their mixture) with lignin, specially for peracetic acid. Information about bleaching and delignification of wood pulps with peracids and the factors affecting its efficiency are also presented.

Water circulations for effective bleaching of high-brightness mechanical pulps

The amount of water available is usually restricted, which leads to a situation where a complete understanding of the process, including water circulations and the influence of water components, is essential. The main aim of this thesis was to clarify the possibilities for the efficient use of residual peroxide by means of water circulation rearrangements. Rearranging water circulations and the reduction of water usage may cause new problems, such as metal induced peroxide decomposition that needs to be addressed. This thesis introduces theoretical methods of water circulations to combine two variables; effective utilization of residual peroxide and avoiding manganese in the alkaline peroxide bleaching stage. Results are mainly based on laboratory and mill site experiments concerning the utilization of residual peroxide. A simulation model (BALAS) was used to evaluate the manganese contents and residual peroxide doses. It was shown that with optimum recirculation of residual peroxide the brightness can be improved or chemical costs can be decreased. From the scientific perspective, it was also very important to discover that recycled peroxide was more effective pre-bleaching agent compared to fresh peroxide. This can be due to the organic acids i.e. per acetic acid in wash press filtrate that have been formed in alkaline bleaching stage. Even short retention time was adequate and the activation of residual peroxide using sodium hydroxide was not necessary. There are several possibilities for using residual peroxide in practice regarding bleaching. A typical modern mechanical pulping process line consist of defibering, screening, a disc filter, a bleach press, high consistency (HC) peroxide bleaching and a wash press. Furthermore there usually is not a particular medium consistency (MC) pre-bleaching stage that includes additional thickening equipment. The most advisable way to utilize residual peroxide in this kind of process is to recycle the wash press filtrate to the dilution of disc filter pulp (low MC pre-bleaching stage). An arrangement such as this would be beneficial in terms of the reduced convection of manganese to the alkaline bleaching stage. Manganese originates from wood material and will be removed to the water phase already in the early stages of the process. Recycling residual peroxide prior to the disc filter is not recommended because of low consistencies. Regarding water circulations, the novel point of view is that, it would be beneficial to divide water circulations into two sections and the critical location for the division is the disc filter. Both of these two sections have their own priority. Section one before the disc filter: manganese removal. Section two after the disc filter: brightening of pulp. This division can be carried out if the disc filter pulp is diluted only by wash press filtrate before the MC storage tower. The situation is even better if there is an additional press after the disc filter, which will improve the consistency of the pulp. This has a significant effect on the peroxide concentration in the MC pre-bleaching stage. In terms of manganese content, it is essential to avoid the use of disc filter filtrate in the bleach press and wash press showers. An additional cut-off press would also be beneficial for manganese removal. As a combination of higher initial brightness and lower manganese content, the typical brightness increase varies between approximately 0.5 and 1% ISO units after the alkaline peroxide bleaching stage. This improvement does not seem to be remarkable, but as it is generally known, the final brightness unit is the most expensive and difficult to achieve. The estimation of cost savings is not unambiguous. For example in GW/TMP mill case 0.6% ISO units higher final brightness gave 10% savings in the costs of bleaching chemicals. With an hypothetical 200 000 ton annual production, this means that the mill could save in the costs of bleaching chemicals more than 400 000 euros per year. In general, it can be said that there were no differences between the behavior of different types of processes (GW, PGW, TMP and BCTMP). The enhancement of recycling gave a similar response in all cases. However, we have to remember that the utilization of residual peroxide in older mills depends a great deal on the process equipment, the amount of water available and existing pipeline connections. In summary, it can be said that processes are individual and the same solutions cannot be applied to all cases.