Biomassaperäisen liuoksen fraktiointi membraanisuodatuksella

Työn tavoitteena oli hiilihydraattien ja aminohappojen talteenotto biomassaperäisistä liuoksista erilaisina fraktioina ultra- ja nanosuodattamalla niitä erilaisilla membraaneilla. Työ tehtiin selvitystyönä Senson Oy:lle syystalven 2015 ja kevään 2016 välisenä aikana. Teoriaosassa perehdyttiin nanosuodatukseen ja sen erilaisiin sovelluksiin teollisuudessa, sekä lyhyesti muihin paineavusteisiin membraanisuodatusprosesseihin. Teoriaosassa myös keskityttiin erityisesti nanosuodatuksessa käytettyihin membraaneihin sekä niiden likaantumismekanismeihin. Kokeellisessa osassa keskityttiin hiilihydraattien ja aminohappojen talteenottoon kolmesta biomassaperäisestä liuoksesta. Tutkimuksen osa-alueita olivat ultrasuodatus, ultrasuodatuksen konsentraatin kirkastaminen sekä ultrasuodatuksen permeaatin fraktiointi nanosuodatuksella. Tutkimuksessa kiinnitettiin myös erityistä huomiota suodatuskalvojen likaantumiseen ja peseytyvyyteen sekä kalvojen käytettävyyteen pesujen jälkeen. Ultrasuodatuksessa kaikkien kolmen liuoksen kohdalla tutkittavien hiilihydraattien saanto permeaattiin oli hyvä, noin 90 %. Ultrasuodatuksissa käytettyjen membraanien osalta ei myöskään ollut havaittavissa merkittävää likaantumista. Ultrasuodatuksen konsentraattien kirkastamiskokeissa sameutta aiheuttavat komponentit saatiin poistettua kaikista liuoksista yli 94 %:in tehokkuudella. Nanosuodatuksissa monosakkaridit saatiin erotettua suuremmista hiilihydraattikomponenteista joko täysin tai lähes täysin (97 - 100 %). Nanosuodatuksissa käytettyjen membraanien osalta huomattavaa likaantumista oli havaittavissa vain membraanilla 2. Tulosten perusteella nanosuodatuksen voidaan sanoa olevan tehokas tapa erottaa pienet monosakkaridit suuremmista hiilihydraattiyhdisteistä.

Ultraäänen käyttö ligniinin ja hemiselluloosan ertuksessa puu-uutteesta

Puusta valmistetussa puu-uutteessa on puun polymeerejä, ligniiniä ja hemiselluloosaa, joiden käyttöä halutaan lisätä biojalostamoissa. Polymeerit tulisi erottaa mahdollisimman puhtaasti jatkojalostusta varten. Erotus voidaan tehdä ultrasuodatuksella. Puu-uutetta pitää kuitenkin esikäsitellä, sillä polymeerit ovat lähes samankokoisia. Ultraäänikäsittelyn on osoitettu kasvattavan ligniinin moolimassaa, jolloin myös erotus parantuisi. Ultraäänikäsittely on aikaisemmin käytettyihin esikäsittelymenetelmiin verrattuna ympäristöystävällisempi, sillä sen käytössä ei tarvita erillisiä kemikaaleja. Tämän työn tavoitteena oli selvittää, kuinka ultraäänikäsittely vaikuttaa ligniinin ja hemiselluloosan erotukseen PHWE-puu-uutteesta. Näytteen pH säädettiin emäksiseksi, näyte ultraäänikäsiteltiin eri koeolosuhteissa ja ultrasuodatettiin. Ultraäänikäsiteltyä näytettä verrattiin käsittelemättömään referenssinäytteeseen. Näytteet analysoitiin UV- ja TOC-analyyseillä konsentraattien ligniini- ja hiilipitoisuuksien selvittämiseksi. Lisäksi tarkasteltiin suodatusprosessin parametreja. Tulosten perusteella ultraäänikäsittely paransi ligniinin ja hemiselluloosan erotusta erilleen. Erotus parani eniten pH 12 -näytteessä, joka ultraäänikäsiteltiin 65 °C lämpötilassa, 45 minuutin ajan laiteteholla 175 W.

Selluloosamembraanien kehittäminen ja testaus

Tämän työn tavoitteena oli selvittää, kuinka selluloosan lisääminen vaikuttaa polysulfonirunkoisiin membraaneihin. Lisäksi työssä selvitettiin selluloosamembraanien modifiointia kitosaanilla ja bentoniitilla. Työssä muodostettiin membraanit faasi-inversiotekniikalla. Selluloosamembraanien valmistuksessa jauhettu selluloosa liuotettiin ioniseen nesteeseen. Sekä polysulfonista että selluloosasta valmistetuille membraaneille määritettiin puhdasvesivuot ja retentiot. Retention määrittämiseen käytettiin malliaineena dekstraanin vesiliuosta. Lisäksi määriteltiin polysulfonipohjaisten membraanien hydrofiilisyys tutkimalla membraanien pintojen ja vesipisaroiden välisiä kontaktikulmia. Polysulfonimembraaneihin lisätyn selluloosan havaittiin pienentävän puhdasvesivuota ja kasvattavan hydrofiilisyyttä mitä enemmän selluloosaa oli membraanimatriisissa. Kaikkien selluloosalla modifioitujen membraanien retentiot olivat suurempia kuin modifioimattoman polysulfonimembraanin. Kitosaanilla modifioitujen selluloosamembraanien valmistus ei onnistunut johtuen luultavasti kitosaanin liian suuresta partikkelikoosta. Bentoniitilla modifioitujen membraanien vuot olivat merkittävästi suuremmat sekä niiden retentiot pienemmät verrattuna modifioimattomaan selluloosamembraaniin. Tämä johtui luultavasti siitä, että bentoniitin lisääminen aiheutti membraanirakenteeseen reikiä.

Downstream processing of reverse osmosis brine: Characterisation of potential scaling compounds

Reverse osmosis (RO) brine produced at a full-scale coal seam gas (CSG) water treatment facility was characterized with spectroscopic and other analytical techniques. A number of potential scalants including silica, calcium, magnesium, sulphates and carbonates, all of which were present in dissolved and non-dissolved forms, were characterized. The presence of spherical particles with a size range of 10-1000nm and aggregates of 1-10 microns was confirmed by transmission electron microscopy (TEM). Those particulates contained the following metals in decreasing order: K, Si, Sr, Ca, B, Ba, Mg, P, and S. Characterization showed that nearly one-third of the total silicon in the brine was present in the particulates. Further, analysis of the RO brine suggested supersaturation and precipitation of metal carbonates and sulphates during the RO process should take place and could be responsible for subsequently capturing silica in the solid phase. However, the precipitation of crystalline carbonates and sulphates are complex. X-ray diffraction analysis did not confirm the presence of common calcium carbonates or sulphates but instead showed the presence of a suite of complex minerals, to which amorphous silica and/or silica rich compounds could have adhered. A filtration study showed that majority of the siliceous particles were less than 220nm in size, but could still be potentially captured using a low molecular weight ultrafiltration membrane. © 2015 Elsevier Ltd.

Purificação de C-ficocianina e sua incorporação em nanofibras

C-ficocianina (C-FC) é uma ficobiliproteína, de cor natural azul, com diversas aplicações na indústria alimentícia, farmacêutica e biomédica, dependendo do seu grau específico de pureza, que pode variar de 0,7 a 4,0, com respectivo aumento de seu valor comercial. Essa pureza é alcançada através de diversas técnicas de purificação, que podem ser aplicadas em diferentes sequências. Um destes processos de purificação de proteínas baseia-se na cromatografia de troca iônica, que utiliza trocadores que adsorvem as proteínas como resultado de interações iônicas entre a superfície da proteína e o trocador. Resinas e colunas de leito expandido podem ser utilizadas para aumentar a produtividade dessa técnica. É fundamental conhecer o perfil do processo de adsorção, para melhor aplicá-lo como ferramenta para o design e otimização de parâmetros operacionais. Outra tecnologia para o tratamento de biomoléculas é a ultrafiltração. Esta técnica é aplicável em larga escala, apresenta baixa complexidade de aplicação e pode ser realizada em condições brandas, minimizando o dano para o produto. Para aumentar a estabilidade da C-FC, e facilitar a sua aplicação, podem ser avaliadas técnicas recentes, não exploradas para este fim, como as nanofibras obtidas através do processo de electrospinning. Estas fibras possuem uma área superficial específica extremamente elevada devido a seu pequeno diâmetro. O objetivo deste trabalho foi avaliar parâmetros de adsorção e diferentes técnicas para purificação de C-ficocianina de Spirulina platensis e obter nanofibras poliméricas incorporadas de C-ficocianina. O trabalho foi dividido em quatro artigos. No primeiro artigo, foram avaliados os parâmetros e as isotermas de adsorção de C-ficocianina em resina de troca iônica para leito expandido Streamline® DEAE. Verificou-se que o maior coeficiente de partição foi obtido em pH 7,5, nas temperaturas de 15 e 25 °C. As isotermas de adsorção da Cficocianina foram bem representadas pelos modelos de Langmuir, de Freundlich e de Langmuir-Freundlich, sendo os valores estimados para Qm e Kd obtidos pela isoterma de Langmuir foram, respectivamente, 33,92 mg.mL-1 e 0,123 mg.mL-1, respectivamente. No segundo artigo foi avaliada a purificação de C-FC até grau alimentar, utilizando ultrafiltração (UF). Com a membrana de 50 kDa, identificou-se que somente a temperatura e a aplicação de diferentes ciclos de diafiltração (DF) causaram influência significativa sobre a purificação e recuperação da C-ficocianina. Foram então aplicados o aumento gradativo da quantidade de ciclos, e a diafiltração previamente à ultrafiltração (DF/UF), onde obteve-se um extrato de Cficocianina com pureza de 0,95. No terceiro artigo foram propostos processos de purificação, envolvendo a utilização das diferentes técnicas para obtenção de C-FC com diferentes purezas. Determinou-se que a partir de cromatografia de troca iônica em leito fixo seguido de DF/UF, obtém-se C-FC para uso em cosméticos e a partir de precipitação com sulfato de amônio, e DF/UF obtém-se C-FC para uso em biomarcadores. Com uma sequência de precipitação com sulfato de amônio, DF/UF e cromatografia de troca iônica em leito fixo chega-se a C-FC de grau analítico. No último artigo, C-FC foi incorporada a nanofibras de óxido de polietileno (PEO) através de processo de electrospinning. Foram determinadas a condutividade da solução de C-FC/PEO, a estrutura e comportamento termogravimétrico das nanofibras formadas. Soluções de polímeros com concentração de 6 e 8% proporcionaram a formação de nanofibras com diâmetro médio inferior a 800 nm, homogêneas, sem a presença de gotas. A análise termogravimétrica identificou aumento na resistência térmica da C-FC incorporada nas fibras.

Soybean lunasin mediates colon carcinogenesis by inducing apoptosis and preventing outgrowth of metastasis

Colorectal cancer (CRC) is the third most common cancer worldwide. Various factors such as age, lifestyle and dietary patterns affect the risk of having CRC. Epidemiological studies showed a chemopreventive effect of soy consumption against CRC. However, which component(s) of soybean is associated with this reduced risk is not yet fully delineated. The objective of this research was to evaluate the anti-colon cancer potential of lunasin isolated from defatted soybean flour using in vitro and in vivo models of CRC. Lunasin was isolated from defatted soybean flour by a combination of different chromatographic and ultrafiltration techniques. The anti-colon cancer potential of lunasin was determined using different human colon cancer cell lines in vitro and a CRC liver metastasis model in vivo. Lunasin caused cytotoxicity to different human colon cancer cells with an IC50 value of 13.0, 21.6, 26.3 and 61.7 µM for KM12L4, RKO, HCT-116 and HT-29 human colon cancer cells, respectively. This cytotoxicity correlated with the expression of the α5 integrin on human colon cancer cells with a correlation coefficient of 0.78. The mechanism involved in the cytotoxic effect of lunasin was through cell cycle arrest and induction of the mitochondrial pathway of apoptosis. In KM12L4 human colon cancer cells, lunasin caused a G2/M phase arrest increasing the percentage of cells at G2/M phase from 12% (PBS-treated) to 24% (treated with 10 µM lunasin). This arrest was attributed to the capability of lunasin to increase the expression of cyclin dependent kinase inhibitors p21 and p27. At 10 µM, lunasin increased the expression of p21 and p27 in KM12L4 colon cancer cells by 2.2- and 2.3-fold, respectively. Flow cytometric analysis showed that lunasin at 10 µM increased the percentage of cells undergoing apoptosis from 13.6% to 24.7%. This is further supported by fluorescence microscopic analysis of KM12L4 cells treated with 10 µM lunasin showing chromatin condensation and DNA fragmentation. The mechanism involved is through modification of proteins involved in the mitochondrial pathway of apoptosis in KM12L4 cells as 10 µM lunasin reduced the expression of the anti-apoptotic Bcl-2 protein by 2-fold and increased the expression of the pro-apoptotic proteins Bax, cytochrome c and nuclear clusterin by 2.2-, 2.1- and 2.3- fold, respectively. This led to increased expression and activity of the executioner of apoptosis, caspase-3 by 1.8- and 2.3-fold, respectively. This pro-apoptotic property of lunasin can be attributed to its capability to internalize into the cytoplasm and nucleus of colon cancer cells 24 h and 72 h after treatment, respectively. In addition, lunasin mediated metastasis of colon cancer cells in vitro by inhibiting the focal adhesion kinase activation thereby reducing expression of extracellular regulated kinase and nuclear factor kappa B and finally inhibiting migration of colon cancer cells. In KM12L4 colon cancer cells, 10 µM lunasin resulted in the reduction of phosphorylation of focal adhesion kinase and extracellular regulated kinase by 2.5-fold, resulting in the reduced nuclear translocation of p50 and p65 NF-κB subunits by 3.8- and 1.4-fold, respectively. In an in vivo model of CRC liver metastasis, daily intraperitoneal administration of lunasin at 4 mg/kg body weight resulted in the inhibition of KM12L4 liver metastasis as shown by the reduction of the number of liver metastases from 28 (PBS-treated) to 14 (lunasin-treated, P = 0.047) and reduction in tumor burden as measured by liver weight/body weight from 0.13 (PBS-treated) to 0.10 (lunasin-treated, P = 0.039). Moreover, lunasin potentiated the anti-metastatic effect of the chemotherapeutic drug oxaliplatin given at 5 mg/kg body weight twice per week. Lunasin and oxaliplatin combination resulted in a more potent inhibition of outgrowth of KM12L4 cell metastases to the liver reducing the number of liver metastases by 6-fold and reducing the tumor burden in the liver by 3-fold when compared to PBS-treated group. This can be attributed by the capability of lunasin and oxaliplatin to reduce expression of proliferating cell nuclear antigen in liver-tumor tissue as measured by immunohistochemical staining. The results of this research for the first time demonstrated the anti-colon cancer potential of lunasin isolated from defatted soybean flour which might contribute to the chemopreventive effect of soybean in CRC as seen in different epidemiological studies. In conclusion, lunasin isolated from defatted soybean flour mediated colon carcinogenesis by inducing apoptosis and preventing outgrowth of metastasis. We suggest that the results of this research serve as a basis for further study on the chemopreventive effect of lunasin against CRC and a possible adjuvant role for lunasin in therapy of patients with metastatic CRC.

Avaliação de Impacto Ambiental, Valorização do Efluente e dos Resíduos Sólidos da Indústria Corticeira

A preocupação com o meio ambiente, nomeadamente na descarga de águas residuais, consumo de água excessivo e produção de resíduos industriais, está cada vez mais presente no quotidiano. Devido a estas problemáticas, efetuou-se a avaliação de impacte ambiental (AIA) do processo produtivo das rolhas de cortiça naturais, tratamento das águas de cozedura da cortiça (estudo da possível reutilização do efluente tratado) e valorização de subprodutos – resíduo sólido (raspa de cortiça), sendo estes os objetivos propostos para a realização da presente dissertação. Na AIA, efetuada no decorrer das fases da Análise do Ciclo de Vida (ACV), foram selecionadas 8 categorias de impacte – aquecimento global, acidificação, dessecação, toxicidade e ecotoxicidade, eutrofização, consumo de recursos não renováveis e oxidação foto-química. A água de cozedura caracterizou-se por uma elevada carga poluente, apresentando elevada concentração de cor, Carência Química de Oxigénio (CQO), taninos e lenhina e Sólidos Suspensos Totais (SST). O processo de tratamento proposto consistiu num pré-tratamento por ultrafiltração (UF), com membranas de 30.000 e 20.000 MWCO, seguido de adsorção por carvão ativado (comercial e produzido a partir de raspa de cortiça). No tratamento por UF, utilizando uma membrana de 30.000 MWCO, foram obtidas percentagens de remoção para a primeira amostra de água de cozedura de 74,8 % para a cor, 33,1 % para a CQO e para a segunda amostra de 85,2 % para a cor e 41,8 % para a CQO. Posteriormente, apenas para a segunda amostra de água de cozedura e com uma membrana de 20.000 MWCO, as percentagens de remoção obtidas foram superiores, de 93% para a cor, 68,9 % para a CQO, 88,4 % para taninos e lenhina e 43,0 % para azoto total. No tratamento por adsorção com carvão ativado estudou-se o tempo de equilíbrio do carvão ativado comercial e do carvão ativado produzido a partir de aparas de cortiça, seguindo-se o estudo das isotérmicas de adsorção, no qual foram analisados os parâmetros da cor e CQO para cada solução. Os ajustes dos modelos teóricos aos pontos experimentais demonstraram que ambos os modelos (Langmuir e Freundlich) poderiam ser considerados, uma vez que apresentaram ajustes idênticos. Relativamente ao tratamento de adsorção em contínuo do permeado, obtido por UF com membrana de 20.000 MWCO, constatou-se que ambos os carvões ativados (comercial e produzido) não ficaram saturados, tendo em consideração os tempos de saturação estimados pela capacidade máxima de adsorção (determinada para a isotérmica de Langmuir) e as representações gráficas dos valores experimentais obtidos para cada ensaio. No ensaio de adsorção com carvão ativado comercial verificou-se que o efluente tratado poderia ser descarregado no meio hídrico ou reutilizado no processo industrial (considerando os parâmetros analisados), uma vez que até aos 11 minutos de ensaio a concentração da solução à saída foi de 111,50 mg/L O2, para a CQO, e incolor, numa diluição de 1:20. Em relação à adsorção em contínuo com carvão ativado produzido verificou-se no ensaio 4 que o efluente resultante apresentou uma concentração de CQO de 134,5 mg/L O2 e cor não visível, numa diluição de 1:20, ao fim de 1h22 min de ensaio. Assim, concluiu-se que os valores obtidos são inferiores aos valores limite de emissão (VLE) presentes no Decreto-Lei n.º 236/98 de 1 de Agosto. O carvão ativado produzido apresentou elevada área superficial específica, com 870 m2/g, comparativamente ao carvão comercial que foi de 661 m2/g. O processo de extração da suberina a partir de raspa de cortiça isenta de extraíveis, efetuado através da metanólise alcalina, apresentou percentagens de extração superiores aos restantes métodos. No processo efetuado em scale-up, por hidrólise alcalina, obteve-se uma extração de 3,76 % de suberina. A aplicação da suberina no couro demonstrou que esta cera apresenta enormes potencialidades, uma vez que a sua aplicação confere ao couro um aspeto sedoso, com mais brilho e um efeito de “pull-up”.

Encapsulation of Local Anesthetic Bupivacaine in Biodegradable Poly(DL-lactide-co-glycolide) Nanospheres: Factorial Design, Characterization and Cytotoxicity Studies

Local anesthetic agents cause temporary blockade of nerve impulses productiong insensitivity to painful stimuli in the area supplied by that nerve. Bupivacaine (BVC) is an amide-type local anesthetic widely used in surgery and obstetrics for sustained peripheral and central nerve blockade. in this study, we prepared and characterized nanosphere formulations containing BVC. To achieve these goals, BVC loaded poly(DL-lactide-co-glycolide) (PLGA) nanospheres (NS) were prepared by nanopreciptation and characterized with regard to size distribution, drug loading and cytotoxicity assays. The 2(3-1) factorial experimental design was used to study the influence of three different independent variables on nanoparticle drug loading. BVC was assayed by HPLC, the particle size and zeta potential were determined by dynamic light scattering. BVC was determined using a combined ultrafiltration-centrifugation technique. The results of optimized formulations showed a narrow size distribution with a polydispersivity of 0.05%, an average diameter of 236.7 +/- 2.6 nm and the zeta potential -2.93 +/- 1,10 mV. In toxicity studies with fibroblast 3T3 cells, BVC loaded-PLGA-NS increased cell viability, in comparison with the effect produced by free BVC. In this way, BVC-loaded PLGA-NS decreased BVC toxicity. The development of BVC formulations in carriers such as nanospheres could offer the possibility of controlling drug delivery in biological systems, prolonging the anesthetic effect and reducing toxicity.

Characterization of the Interactions between Endocrine Disruptors and Aquatic Humic Substances from Tropical Rivers

Interactions between two endocrine disruptors (ED) and aquatic humic substances (AHS) from tropical rivers were studied using an ultrafiltration system equipped with a 1 kDa cut-off cellulose membrane to separate free ED from the fraction bound in the AHS. Quantification of 17 alpha-ethynylestradiol and bisphenol A was performed using gas chromatography-mass spectrometry (GC-MS). The times required for establishment of equilibrium between the AHS and the ED were ca. 30 min, and complexation capacities for 17 alpha-ethynylestradiol and bisphenol A were 18.53 and 2.07 mg g(-1) TOC, respectively. The greater interaction of AHS with 17 alpha-ethynylestradiol, compared to bisphenol A, was due to the presence of hydrogen in the structure of 17 alpha-ethynylestradiol, which could interact with ionized oxygenated groups of the AHS. The results indicate that AHS can strongly influence the transport and reactivity of endocrine disruptors in aquatic systems.

Anaerobic bio-digestion of concentrate obtained in the process of ultra filtration of effluents from tilapia processing unit

The objective of the present study was to evaluate the efficiency of the process of biodigestion of the protein concentrate resulting from the ultrafiltration of the effluent from a slaughterhouse freezer of Nile tilapia. Bench digesters were used with excrements and water (control) in comparison with a mixture of cattle manure and effluent from the stages of filleting and bleeding of tilapias. The effluent obtained in the continuous process (bleeding + filleting) was the one with highest accumulated population from the 37th day, as well as greatest daily production. Gases composition did not differ between the protein concentrates, but the gas obtained with the use of the effluent from the filleting stage presented highest methane gas average (78.05%) in comparison with those obtained in the bleeding stage (69.95%) and in the continuous process (70.02%) or by the control method (68.59%).

Asymptomatic intradialytic hypotension: the need for pre-emptive intervention

Intradialytic hypotension (IDH) remains the most common severe side effect of hemodialysis despite numerous technological advancements. Recent evidence emphasises the significance of asymptomatic hypotensive episodes, as well as the hypoperfusive consequences of both relative blood pressure drops and repetitive, symptomatic events. This article reviews the physiological importance of rapid blood pressure decrease during hemodialysis, and highlights the pathological consequences of repeated asymptomatic and symptomatic hypoperfusive episodes. In proposing a view concerned with asymptomatic IDH, a practicalpre-emptive intervention is offered to improve the long-term outcomes of patients on hemodialysis. Ongoing monitoring of individual patient's mean arterial pressure (MAP) throughout the dialysis treatment can facilitate the identification of an asymptomatic hypotensive episode. A brief pause in ultrafiltration enables vascular refill and subsequent increase in MAP, allowing resumption of safe fluid removal. Such enhanced assessment results in a reduction off patient risk, allowing safe and optimal fluid removal.

Towards enhanced performance thin-film composite membranes via surface plasma modification

Advancing the design of thin-film composite membrane surfaces is one of the most promising pathways to deal with treating varying water qualities and increase their long-term stability and permeability. Although plasma technologies have been explored for surface modification of bulk micro and ultrafiltration membrane materials, the modification of thin film composite membranes is yet to be systematically investigated. Here, the performance of commercial thin-film composite desalination membranes has been significantly enhanced by rapid and facile, low pressure, argon plasma activation. Pressure driven water desalination tests showed that at low power density, flux was improved by 22% without compromising salt rejection. Various plasma durations and excitation powers have been systematically evaluated to assess the impact of plasma glow reactions on the physico-chemical properties of these materials associated with permeability. With increasing power density, plasma treatment enhanced the hydrophilicity of the surfaces, where water contact angles decreasing by 70% were strongly correlated with increased negative charge and smooth uniform surface morphology. These results highlight a versatile chemical modification technique for post-treatment of commercial membrane products that provides uniform morphology and chemically altered surface properties.

Effect of gamma-irradiation on total organic carbon and trihalomethane formation potential

This research was conducted to study the use of radiation in water treatment as an alternative to chlorination which has caused health concerns due to the formation of harmful disinfection by-products. Groundwater solutions from the Biscayne aquifer were radiated with Cobalt-60 gamma radiation and studied for changes in dissolved organic carbon (DOC), UV absorbance at 254 nm (UV254), fluorescence and trihalomethane formation potential (THMFP). Molecular fractionations were conducted by ultrafiltration. Effect of the combination of radiation/peroxide was studied for DOC and UV254. Radiation showed significant removal in DOC and THMFP. Similar results were seen in the fluorescence and UV absorbance experiments. Radiation/peroxide did not improve the DOC removal. Radiation of the groundwater samples broke the larger molecular weight fractions in to smaller fractions.

Étude comparative de deux méthodes de fabrication de yogourt grec à échelle pilote utilisant l’ultrafiltration comme technique de concentration - Étude basée sur la méthode d’Analyse de Cycle de Vie

Le yogourt grec, pouvant être obtenu par concentration du yogourt traditionnel par ultrafiltration (UF), connaît une croissance exceptionnelle en Amérique du Nord (+100% depuis 2012), et représente le premier segment de marché des produits laitiers fermentés en 2014. Cependant, d’un point de vue environnemental, la production du yogourt grec fait face à plusieurs enjeux et défis. Son élaboration nécessite trois fois plus de lait que le yogourt traditionnel de par l’étape de concentration nécessaire à l’atteinte de la concentration protéique cible. De plus, l’étape d’UF du yogourt génère un perméat acide (coproduit du yogourt) difficilement valorisable. Néanmoins, une alternative consistant à effectuer l’étape d’UF sur le lait avant sa fermentation permet d’éliminer la production du perméat acide, et génère un perméat de lactosérum doux déprotéiné dont les voies de valorisation sont davantage connues. Cette stratégie pourrait donc potentiellement réduire l’impact environnemental du procédé et générer des coproduits plus facilement valorisables, améliorant ainsi l’écoefficience du procédé de fabrication de yogourt grec. Dans cette optique, ce projet de recherche visait à comparer l’impact environnemental sur l’ensemble du cycle de vie de la production de yogourt grec selon deux procédés : en effectuant l’étape de concentration par UF avant l’étape de fermentation (UF LAIT), ou après (UF YOG) comme utilisé dans l’industrie. Ainsi, des expérimentations à échelle pilote ont été réalisées dans le but de comparer ces deux procédés. Le nouveau procédé (UF LAIT) permettrait une réduction des consommations d’énergie à l’étape de transformation étant donné que l’UF du lait avant fermentation permet de réduire la quantité de matière première à transformer d’environ un tiers. Cependant l’Analyse du Cycle de Vie (ACV) des deux procédés donne comme résultat un bilan environnemental défavorable à (UF LAIT) comparativement au procédé traditionnel (UF YOG) à cause d’une plus grande consommation de lait, qui est responsable d’environ 80% des impacts sur le cycle de vie du yogourt grec. Cet impact majeur pour UF LAIT l’est encore même lorsque dans une analyse de sensibilité le perméat doux de UF LAIT est alloué à l’étape d’UF contrairement au perméat acide de UF YOG qui est considéré comme un déchet non valorisable.